TW200418520A - Dry powder inhale system for pulmonary administration - Google Patents

Dry powder inhale system for pulmonary administration Download PDF

Info

Publication number
TW200418520A
TW200418520A TW092135122A TW92135122A TW200418520A TW 200418520 A TW200418520 A TW 200418520A TW 092135122 A TW092135122 A TW 092135122A TW 92135122 A TW92135122 A TW 92135122A TW 200418520 A TW200418520 A TW 200418520A
Authority
TW
Taiwan
Prior art keywords
air
composition
container
freeze
flow path
Prior art date
Application number
TW092135122A
Other languages
Chinese (zh)
Other versions
TWI327073B (en
Inventor
Chikamasa Yamashita
Akitsuna Akagi
Yuichiro Fukunaga
Original Assignee
Otsuka Pharma Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Otsuka Pharma Co Ltd filed Critical Otsuka Pharma Co Ltd
Publication of TW200418520A publication Critical patent/TW200418520A/en
Application granted granted Critical
Publication of TWI327073B publication Critical patent/TWI327073B/en

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Medicinal Preparation (AREA)
  • Medical Preparation Storing Or Oral Administration Devices (AREA)

Abstract

This invention provides a dry powder inhale system for pulmonary administration combined of: (1) a container for receiving freeze-drying composition for pulmonary administration, which is formulated by freeze-drying the liquid containing non-soluble state, and the following (i) to (iii) properties, (i) being in non-powder cake state, (ii) distinguish index is over 0.05, (iii) forming micro particles having average particle radius (particle radius of air mechanics) is over 10 μm or effective particles ratio is over10% by receiving air punch having air speed at least 1 m/sec and air flow at least 17 ml/sec; (2) a device having means for producing above punch to the freeze-drying composition in above container means for discharging the micro particles powder of the freeze-drying composition.

Description

200418520 坎、發明說明 [發明所屬之技術領域] 本發明係關於適於經肺投與之新穎齡 、子己辟粉末吸入系 、、’。更詳言之,本發明係關於在使用收容於A^ 、人 、奋為所提供之 Q凍乾燥組成物時,藉由微粒化可調製成 、 刹h 衣战通於經肺投盥夕 製蜊形態,並可以該形態直接吸入投與 /、 粉末吸入系統。 -肺投與用乾燥200418520, Description of the invention [Technical field to which the invention belongs] The present invention relates to a novel age, Zijipi powder inhalation system suitable for pulmonary administration. In more detail, the present invention relates to the use of Q freeze-dried compositions contained in A ^, Ren, and Fenwei, which can be made by micronization and adjustable, and the garments can be made through the lung. Clam form, and in this form can be directly inhaled for administration and / or powder inhalation system. -Dry for lung administration

幵有,本發 % π興…、、工/,τ认六汁J百―π lx · 此χ 一⑺孝乙燥粉末吸入糸 御之下述技術。具體…此等技術例如為使用時二 以凋製成適於經肺投與之微粒粉末C經肺投與“ 製幻之冷隸燥組成物,該經肺投_乾朴2粉末 i生古、土 处也 知柄末製劑之製 :,使用上述冷耗燥組成物之吸人或經肺投與方Yes, the hair% π… ,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,-,-,-,-,-,-,-,-,-,-,-,-,-,-,-,-,-,-dry-powder-inhaled-powder Specifically ... These techniques are, for example, used in the preparation of micropowder powder suitable for transpulmonary administration in the lungs, and "cold and dry composition for making fantasy", the transpulmonary administration_ 乾 朴 2 粉 i 生 古The Department of Earth also knows the preparation of stalk preparations: using the above-mentioned cold-drying composition for inhalation or pulmonary administration

'以及在使用經肺投與用乾燥粉末製劑時用以製造之人 康乾燥組成物的使用等。 σ Q 」意指不論形狀為 ’只要具有微細形 又,以下在本說明書中所謂「微粒 粉末(微粉末)狀、針狀、板狀或纖維狀 狀者皆包括在内。 [先前技術] ’…’已知經肺投與之時,#由將醫藥品所含之 之平均粒徑製成10微米以下,較佳5微米以下, 是.=!:”分效率良奸地到達肺部。因此,目前的狀況 疋·先刖之經肺投盥田口β λ w ^ ν. ^ μ 刎,為了預先將醫藥品原料製 = 徑,料乾法及仙磨法等調製成i ^ 、仃加工處理,然後將其填入吸入裝置來提供。 315314 6 200418520 具體而言,一直以來,已知乾燥粉末吸入劑有三種: (1)將只由藥物微粒組成之粉末狀組成物充填於適當容器 而成之製劑;(2)將藥物微粒輕輕地造粒成較大粒徑並將其 形成之粉末狀組成物充填於適當容器而成之製劑;以及(3) 將藥物微粒與比該藥物微粒之粒徑大之賦形劑粒子(乳糖 等)均一地混合並將所得混合粒子組成之粉末狀組成物充 填於適當容器而成之製劑(例如參照日本專利特開平^ _ 171760號公報等)。在此等文獻中記載有:若將此等乾燥 粉末吸入劑投與至呼吸道内,則顯示有下列之舉動:(” 組成物中之該藥物微粒將到達並沉著於氣管及支氣管等下 呼吸這;(2)造粒之藥物飛行於氣道内時解離成微粒,且生 成之藥物微粒將到達並沉著於氣管及支氣管等下呼吸道; (3)賦形劑沉著於口腔内、咽頭或喉頭,而只有藥物微粒到 達並沉著於氣管及支氣管等下呼吸道。 如上述,先前之經肺投與用乾燥粉末吸入劑,係預先 將吸入成分製造成期望之微粒後,或者將該微粒用任合方 法加工後,充填於吸入裝置中,然後經肺投與。 通常,為了將低分子藥物微粒化,可以使用喷乾法(例 1 1.1 71760 2001-1 5 1673號公報等)等。其中所用之喷射磨法,係將以 1000 L/=ln以上之空氣流量且經由音速以上之空氣速度生 成之空氣衝擊賦舆低分子藥物並將該藥物微粒化之方法, 但對於以低空氣衝擊將藥物微粒化之方法則尚未知悉。 另一方面,關於肽及蛋白質等高分子藥物,已知有例 315314 7 200418520 如將包含添加劑之醫藥原液之噴霧溶 驟做成平均粒捏為5微米以下之微粒,並將1 二“…步 裝置之方法(噴I將其充填於吸入 .例如 w〇95/3 1479 質與添加劑一起A#、p 、),將肽及蛋白 等微粒化並充填於吸入 ‘物用喷射磨 法;例如W〇91/16〇38號等)。方法^東乾燥-噴射磨 肺』:乾:二==噴乾法或噴射磨法調製之先前經 又用秌私末吸入劑,尤其是 子藥物而言,未必是# # a # 、肽及蛋白質等高分 未必疋理想的製劑。舉 W095/31479觫由餅々# j 3之,如在 唬中所&己载之於喷乾步 活,若藉由喑弘土 -r W τ干棱素約25%失 :由育乾法’可以預知在製造步驟中蛋 活以及樂物活性之降低。又’對於古“胃荨之失 低分子荜物相 ^ ^ 、问刀子樂物而言,亦與 _刀于市物相同,無法得悉藉由低空 方法。 乳衝犟進行微粒化之 再者,無論對於喷乾法或冷凌 掣夕艸4八士 W + ▲ 木乾4 -贺射磨法,其將調 衣之被粉末從喷乾裝置或噴射 、, 竹门 填於容哭中# 、置回收亚分成小部分充 L也::Γ 因此,伴隨該操作,不可避 免地3產生因回收及充填耗損造 而來之&太μ 4 ^ + 战之调製收率下降及隨之 而耒之成本上彳,以及夾雜物 ^ ^ . ν , 衣d寺問4。又,一般 而§ ,將粉末在微量下精確地 因此,對於必須在粉末狀態以微量t:分充填頗有困難。 法及喷射磨法而言,高精確度刀θ成小部分充填之喷乾 妙右立ν Φ 古 之彳政夏粉末充填法之確立當 然有其必要。事實上,例如在 口南八如士 、國專利公報第5,826,633 號么報中,對於將微粉末進行 丁知末充填之系統、裝置及方 315314 8 200418520 法均有詳細之記載。 [發明内容] 本發明之目的儀為結 ,ρ φχ - β ,—、、、解決關於上述先前經肺投與用乾 秌叔末吸入劑之各種問 供-種可用於經肺㈣之新;:::,本發明之目的為提 /、之新碩製劑系統及投與系統,其中 將收谷於容器内之洽秦# 東乾燥組成物在該容器中微粒化成適 方;!肺投與之粒徑並直接吸入。 本’X月者為達成該目的,曰夜反覆深入 到地發現將做為右对士、八# ^ ^ ^ _ ”、、 >成刀之藥理活性物質充填於容器中並 :,Γ東乾燥法所調製而成之非粉末狀態之冷綠燥組成 ’精由較低之空氣衝擊,可將直接收納於容器中者予以 微粒化。基於該見解’本發明者進一步反覆研究,發現藉 由將以非粉末狀態收容於容器内之冷;東乾燥組成物,血呈 備=賦與該組成物㈣之空氣衝擊,將特定速度及流量 之空氣導人容器内之手段及將微粒化之粉末組成物從容器 ο出之手奴之I置組合使用,使用者於使用時(尤其是吸 入時)將可簡單地將冷凍乾燥之非粉末製劑調製成適於經 肺投與之微粒狀態,因此藉由將該微粒直接吸入服用,將 可達成經肺投與。再者,本發明者發現以液態充填於容器 之含藥理活性物質組成液,不限於其中之添加成分(尤其是 為有效成份之藥理活性物質)澄明地溶於溶媒或澄明地混 k情,’縱使此等添加成分以未溶於溶媒或非溶解狀態 存在,藉由特定之空氣衝擊,仍可調製成適於經肺投與之 微粒之冷埭乾燥組成物。因此,本發明者則肯定若藉由該 315314 9 200418520 經肺投與用乾燥斗分太 坏扣末吸入糸統,可以完全解決上述先前經 肺投與用乾燥粉末吸人劑之相關問題。 亦即,若依照本發明之經肺投與系統,由於盔 直 他裝置進行微粒化後再分成小部分充填於容器中,因此沒 題,可以應用於經肺投與。又,若依照本發明 梦:牛:乾燥粉末吸入系統’由於不像藉由噴乾法之 ;::為_分之蛋白質及胜肽等須暴露於高溫 :★不會有因高溫暴露而造成藥理活性降低之問題。 對於為高價藥物之胜肽及蛋白質等藥理活性物質而 -’可以降低製劑製造成本,亦即本發明之 從經濟觀點而言亦為有用。 …手一充 命田私p 右依—本發明之經肺投 人用乾餘粉末吸入系統,可以$ ^ ^ ^ ^ ^ ^ ^ !達肺之幻,可以有效率地將藥物送到達肺部。 本發明之經肺投與用乾燥粉末 包含有效成分之非溶系統,其特徵為將 八士 解狀心組成液經冷凍乾燥及調製成非 鳥末之塊狀形態之冷滚乾焊 , 祀;木、、且成物做為經肺投與用製劑。 將如此調製之塊狀形態之冷東 7不牦/木組成物應用於乾燥 吸入用裝置所形成之本發明乾 / 卞寸刀禾 二 y、‘末吸入系統,與依昭先 丽乾燥粉末吸入劑所採用 …、 子η## μ b 育射磨法或贺乾法預先將粒 子破粒化成所要大小以適於經 又Η之粉末狀製劑應用於 本㈣之編末吸入褒置之情況相 之有效粒子比率。因此,本 上:者- 定位為高性能經肺投與系統。“知末吸入糸統可以 本發明係基於以該見解而问 解而開發者,其包含下述形態。 315314 10 200418520 (第1項)一種經肺投與用之人 〃用< ~凍乾燥組成物,係將包含非 溶解狀態之添加成分之έ且点、'右μ、人土 风刀之、、且成液經冷凍乾燥而調製成,且具 有下述⑴至(iii)之特性·· (i) 具有非粉末之塊狀形態; (ii) 衰變指數為〇·〇5以上;以及 ㈣藉由:受具有至少lm/sec之空氣速度及至少制_ 之空氣流量之空氣衝擊,可成為平均粒徑在i0微米以 下或有效粒子比率在10%以上之微粒。 (第2項)如第1項之冷漁齡 東乾知組成物,係包含做為有效成 分之高分子藥物。 (第3項)一種經肺投盥用乾 仅礼你枱末製劑之製造方法,包含 在收各下述冷;東乾燥组成物夕六 、、成物之办态中,使用可將下述空氣 衝擊賦與該容器内之冷;東乾焊 ▽果钇炼組成物之裝置,導入具備該 空氣衝擊能力之空翕,益+你π 一 乳错此使传上述冷凍乾燥組成物形成 平均粒桎纟ίο微米以下或有效粒子比率在以上之微 粒;其卞該冷來乾燥組成物藉由將包含非溶解狀態之添加 成分之組成液經冷;東乾燥而調製成,且具有下 之特性: (1)具有非粉末之塊狀形態, (ii)衰變指數為0·〇5以上,以及 (111)精:具有至少1油“之空氣速度及至少17ml/seC 之空乳流$之空氣衝擊,可成為平均粒徑在1 〇微米以 下或有效粒子比率在1〇%以上之微粒。 (第4員)如第3項之經肺投與用乾燥粉末製劑之製造方 315314 11 200418520 藥物Γ中’ 5亥冷;東乾燥組成物包含做為有效成份之高分子 L第,5:頁中)如,第3項之經肺投與用乾燥粉末製劑之製造方 置做為:置:=Γ卿記載之乾燥粉… 將々凍乾耜组成物微粒化. (Α)經肺投與用乾燥 容;Α #、將以非粉末狀態收 •:寻=乾燥組成物微粒化並使被驗者吸入 >所付U粒用之裝i,其特徵為具備·· =二氣喷射流路之針部,具有排出流路之針部,在上 段,H工Μ射流路中輸送空氣用之空氣麼送手 〃上述針部之排出流路連通 且構成為: 及入口, 2 = :::入供密封上述容器之口栓以將空氣喷射 Γ排出流路與上述容器内部連通,並用上述空氣芦 送手#又使空氣經由上 4 ^ 内,藉由該喷射M m 上述容器 化,且得到之述冷;東乾燥組成物微粒 者 丨之U粒經由上述排出流路從吸入口排出丨或 ⑻經肺投與用乾燥粉末吸入裝置,其係將以非 容於容器中之冷束乾燥組成: 得到之微粒用之裝置,其特徵為具備:冑“者吸入 具有吸引流路之針部,具 上述吸引流路連通之吸入口; &之針部以及與 且構成為: 315314 12 200418520 2述針部扎人供密封上述容器之口栓之狀態,藉由使 :者之吸氣壓從上述吸入口吸入上述容器内之空氣,同 日ΤΓ使空氣經由上流允今道 、 “由上述工乳導入流路流入已成為負壓之容 '由流入之空氣衝擊將上述冷束乾燥組成物微粒 ’且付到之微粒經由上述吸引流路從吸入口排出。 (第6項)-種經肺投與用乾燥粉末吸人系統,係將下述⑴ 及(2 )組合使用: ⑴收容具有冷凍乾燥組成物之容器,該冷滚乾燥組成物係 將已3非办解狀悲之添加成分之組成液經冷滚乾燥而 調製成,且具有下述⑴至Gii)之特性·· (1)具有非粉末之塊狀形態, (ii)哀變指數為〇·〇5以上,以及 (出)藉由承受具有至少! m/sec之空氣速度及至少! 7ιηΐ/_ 之空氣流量之空氣衝擊,可成為平均粒徑在1〇微米以 下或有效粒子比率在10%以上之微粒; 可將上述空乱衝擊賦與於上述容器内之冷滚乾燥 組成物之手&以及排出經微粒化之粉末狀冷滚乾燥組 成物之手段之裝置。 (第7項)如帛6項之經肺投與用乾燥粉末吸入系統,其 [在吸入時將上述容器與上述裝置組合使用。 (第8項)如帛6項之經肺投與用乾燥粉末吸入系統,其 中,該冷凌乾燥組成物係包含做為有效成份之高分子藥 物。 (第9項)如帛6項之經肺投與用乾燥粉末吸人系統,其 315314 13 中,使用下述(A)或(B)做為裝置: (A)=!與用乾燥粉末吸入裝置,係將以非粉末狀態收容 於谷器中之A洁# β 7東乾燥組成物經微粒化並使使用者吸入 所侍微粒用之裝置’係具備: 2^氣噴射流路之針部,具有排出流路之針部,在上 二::Ρ之空氣噴射流路中輸送空氣用之空氣壓送手 又以及與上述針部之排出流路連通之吸入口· 且構成為: ’ 使上述針部札入供宓 六口口 流路及排出流路二、 口栓以將空氣喷射 :/、述谷益内部連通,並用上述空氣壓 —又二轧經由上述空氣喷射流路噴射於上述容哭 空氣之衝擊使上述冷來乾燥組成物經微 仔到之微粒經由上述排出流路從吸入; 或者 (Β)=Γ:粉末吸入裝置,其係將《非粉末狀態收 &之~凍乾燥組成物經微粒化並使被驗者吸 侍彳之微粒用之裝置,係具備·· it:::路之針部,具有空氣導入流路之針部以及與 ^ 引流路連通之吸入口 ; 且構成為: 針部札入供密封上述容器之口拾之狀態,藉由被 日:二軋麼從上述吸入口吸入上述容器内之空氣,同 f:由上述空氣導入流路流入已成為負屢之容 -内’精由流入之空氣衝擊將上述冷; 東乾燥組成物經微 315314 14 200418520 / 粒化,且得到之微粒經由上述吸引流路從吸入口排出。 (第1 〇項)一種經肺投與方法,包 ^ ^ ^ 便用々凍乾刼組成物, ㈣成物係將包含非溶解狀態之添 液經冷,東乾燥而調製成,具有下述特性: (1)具有非粉末之塊狀形態, (ii) 衰變指數為0·05以上,以及 (iii) 藉由承受具有至少lm/sec 扣 工乳迷度及至少17ml/sec :氣流量之空氣衝擊’可成為平均粒徑在ι〇微米以 下或有效粒子比率在1〇%以上之微粒; 物1吏I時’藉由將上述空氣衝擊賦與該冷;東乾燥組成 物,形,平均粒…0微米以下或有效粒子比率在1〇% ϋ之’然後藉由令使用者吸人該經微粒化之粉末而 投與。 、如¥ 1G項之經肺投與方法,其中,該冷康乾谓 收容於容器内,以及該經微粒化之粉末係用具偉 下置調製而成:可將上述空氣衝擊賦與該容器内 :::乾燥組成物之手段以及可從容器中排出經微粒化之 粉末狀冷凍乾燥組成物之手段。 (弟12項)如第10項之經肺投與方法,其中,該冷凍乾 t組成物係包含做為有效成份之高分子藥物。 、::、員)如第11項之經肺投與方法,其中,使用在下 述(A)或(B)中記載之乾燥粉末吸入裝置做為裝置: (A)經肺投與用乾燥粉末吸入裝置,係將以非粉末狀態收容 方t 哭由 之4 ’東乾無組成物經微粒化並使使用者吸入 15 315314 418520 所得微粒用之裝置,係具備: 具有空氣噴射流路之針部,具有排出流路之針部,在上 :針部之空氣喷射流路中輸送空氣用之空氣壓送手 奴以及與上述針部之排出流路連通之吸入口; 且構成為: ’ 使上述針部扎入供宓 & π 流路及排出流路心述容Μ: : ί以將空氣噴射 … 一迚奋内邛連通,亚用上述空氣壓 达X使空氣經由上述空氣喷射流路嘴射於上述容哭 射空氣之衝擊使上述冷純燥組成物經: " 且侍到之微粒經由上述排出流路從吸入口排出; 或者 ’ (Β)::=用乾燥粉末吸入裝置’係將以非粉末狀態收容 之冷凍乾燥組成物經微粒化並使被驗者吸入 付到之微粒用之裝置’係具備: 具有Μ流路之針部,具有空氣導人流路 上述吸引流路連通之吸入口; 及/、 且構成為: 2 供密封上述容器之口栓之狀態,藉由被 虱垒攸上述吸入口吸入上述容器内之空氣,同 ^吏空氣經由上述空氣導入流路流入已成為負壓之容 :内’:由之空氣衝擊將上述冷滚乾燥組成物經微 /侍到之微粒經由上述吸引流路從吸入口排出。 (弟14項);種冷凍乾燥組成物在吸入式經肺投與之使 用’其中’該冷’東乾燥组成物係將包含非溶解狀態之添加 315314 16 200418520 成分之組成液經冷凍乾燥而調製成,且具有下述特性·· ⑴具有非粉末之塊狀形態, (ii)衰變指數為〇·〇5以上,以及 (m)藉由承受具有至少lm/sec之空氣速度及至少pmi/sec 之空氣流量之空氣衝擊,可成為平均粒徑在ι〇微米以 下或有效粒子比率在10%以上之微粒;並且 將該冷凍乾燥組成物粉末化使成為具有上述平均粒徑 或有效粒子比率之微粒來使用,。 (弟15項)14項之冷凍乾燥組成物在經肺投與之使 :,其中,該冷康乾燥組成物被收容於容器内,以及該經 微粒化之粉末係用具備可將上述空氣衝 冷康乾燥組成物之手段以及可從六哭由姑山彡谷μ内 、 丁仅从及J攸谷為、中排出經微粒化之粉 末—狀冷康乾燥組成物之手段之裝置調製而成。 (_ 第1=項)如第丨4項之冷凍乾燥組成物在經肺投與之使 用,其中,言亥冷滚乾燥組成物係包含做為有效成份之高分 子藥物。 (第1 7項) —&、人、土上 〇 、 種東乾燥組成物在製造吸入式經肺投與之 車乙粉末製齋丨^^ # _ 灸用中’該冷凍乾燥組成物具有下述 特性: :匕3非〉谷解狀態之添加成分之組成液經 調製成, ⑴)具有非粉末之塊狀形態, (iii) 衰變指數為0·05以上,以及 (iv) 错由承香呈古 又/、有至少lm/sec之空氣速度及至少17mi/sec 315314 200418520 之空氣流量之空氣衝擊, 可成為平均粒徑在1 0微米以 下或有效粒子比率在10%以上之微粒;並且 、使用日可將凍乾燥組成物經微粒化使成為且有 上述平均粒徑或上述有效粒子比率。 (:二8項)如弟17項之冷凍乾燥組成物在製造經肺投鱼 用乾紐粉末製劑之使用,复中 ^ 、中该冷凍乾燥組成物係包含 做為有效成份之高分子藥物。 (用V9項)如第17項之冷康乾燥組成物在製造經肺投盘 用之乾燥粉末製劑之使用,其 ’ ^ ^ ^ 0 /、 M Q凍乾餘組成物係收 谷於合裔内,以及該經微粒化 > a Μ <知末係用具備可將上述空 乳衝擊賦與該容器内之冷凍 „ . ? 尽钇4組成物之手段以及可從容 調製而成。 東乾U組成物之手段之裝置 (第20項)一種包含非溶解狀能之 m 心之添加成分之組成液之使 用’係用於製造供調製經肺投盥 P ψ仅Μ用乾燥粉末製劑用之冷凍 呆、、且成物,該冷純燥組成物具有下述特性: (1)具有非粉末之塊狀形態, (π)衰變指數為0 05以上,以及 (⑴)藉由承受具有至少lm/sec 工礼逑度及至少1 7ml/sec'And the use of human dried compositions for the manufacture of dry powder formulations for pulmonary administration. "σ Q" means that regardless of the shape, as long as it has a fine shape, what is called "fine particle (fine powder), needle, plate, or fibrous shape" in the present specification is included. [Prior Art] ' … 'When it is known to be administered via the lungs, # the average particle size contained in the medicine is made below 10 micrometers, preferably below 5 micrometers, and it is. = !: "It reaches the lungs with good efficiency. Therefore, the current situation is 疋 · 刖 口 through the lungs to wash the mouth Taguchi β λ w ^ ν. ^ Μ 为了, in order to prepare the pharmaceutical raw material = diameter, material dry method and fairy grinding method into i ^, 仃 processing Process, then fill it into the inhalation device to provide. 315314 6 200418520 Specifically, there have been three known dry powder inhalants: (1) a preparation prepared by filling a powdery composition consisting only of drug particles in an appropriate container; (2) lightly mixing drug particles A preparation prepared by granulating into a larger particle size and filling the resulting powdery composition in an appropriate container; and (3) drug particles and excipient particles (lactose, etc.) larger than the particle size of the drug particles ) A preparation prepared by uniformly mixing and filling a powdery composition composed of the obtained mixed particles into an appropriate container (for example, refer to Japanese Patent Laid-Open No. ^ _171760). It is described in these documents that if these dry powder inhalants are administered into the respiratory tract, the following actions are shown: ("The drug particles in the composition will reach and settle down in the trachea and bronchus, etc. (2) the granulated drug dissociates into particles when flying in the airway, and the generated drug particles will reach and settle in the lower respiratory tract such as the trachea and bronchus; (3) the excipient is settled in the mouth, throat or throat, and Only the drug particles reach and settle in the lower respiratory tract such as the trachea and bronchi. As mentioned above, the previous dry powder inhalants for pulmonary administration are prepared in advance by inhaling the ingredients into desired particles, or the particles are processed by any method Then, it is filled in an inhalation device and then administered through the lungs. Generally, in order to micronize low-molecular-weight drugs, a spray-drying method (Example 1 1.1 71760 2001-1 5 1673, etc.) can be used. The jet mill used therein Method is a method in which a low-molecular-weight drug is impregnated with an air flow of 1000 L / = ln or more and an air impact generated by an air speed above the speed of sound, and the drug is micronized, but The method of micronizing a drug with a low air impact is not known. On the other hand, as for peptides, proteins, and other high-molecular-weight drugs, there is an example of 315314 7 200418520. For example, spraying and dissolving a pharmaceutical stock solution containing additives into an average particle Pinch the particles below 5 microns, and fill the inhalation method with a 12-step device (spray I to fill inhalation. For example, w095 / 3 1479 together with additives A #, p,), use peptide and protein particles And inject it into the inhaled material using a jet mill method; for example, WO91 / 16〇38, etc.). Method ^ East Dry-Jet Grinding Lung ": Dry: Two == Spray dry or jet mill method previously used inhaler, especially for sub-drugs, may not be # # a #, peptide and High scores such as protein may not be ideal. For example, W095 / 31479 觫 由 饼 々 # j 3 of it, as already described in Bluff & already contained in the spray-drying step, if about 25% is lost by 藉 洪 土 -r W τ dry edge: by Yugan method 'It is foreseeable that the egg activity and the reduction of the fun activity in the manufacturing step are reduced. And 'for the ancient "stomach of the low-molecular-weight tritium phase ^ ^, asked the knife fun, is also the same as _ knife in the city, can not know the low-altitude method. The milk is washed into micronization and then Regardless of the spray-drying method or the cold-blowing method, it will be 48 + W ▲ Mugan 4-He-shot grinding method, which will adjust the powder of the dressing from the spray-drying device or spray, and the bamboo door is filled in the rong cry # The recycling sub-segment is also filled with a small portion of charge L :: Γ Therefore, with this operation, it is inevitable that 3 will result from the recovery and filling loss & too μ 4 ^ + The modulation yield of the war will decrease and follow The cost of 彳, and the inclusions ^ ^. Ν, Yi d Temple 4. And, generally, §, the powder is precisely in a small amount. Therefore, it is difficult to fill the powder with a small amount of t: minute. As for the spraying method and the jet grinding method, it is of course necessary to establish the spray-drying method of the high-precision knife θ filled in a small portion ν Φ Guzheng Zhengxia powder filling method. In fact, for example No. 5,826,633 of the National Patent Gazette, a system for filling fine powder with Dingzhi powder , Device and formula 315314 8 200418520 method are all described in detail. [Summary of the invention] The purpose of the present invention is to solve the above problems, ρ φχ-β,-, ... Various kinds of questions-new ones that can be used for trans-pulmonary dysfunction; ::: The purpose of the present invention is to provide a new master preparation system and an administration system, in which the valley is harvested in a container. In this container, the particles are micronized into a suitable formula; the particle size of the lungs is administered and directly inhaled. In order to achieve this purpose, the person who has been in the night will go deeper and deeper and discover that it will be used as a right pair, eight # ^ ^ ^ _ ",, > The pharmacologically active substance into the knife is filled in the container and :, the non-powdered cold green dry composition prepared by the Γ-dong drying method is composed of lower air impact, and can be directly stored in the Those in the container are micronized. Based on this insight, the present inventors further researched repeatedly and found that by drying the composition in a non-powdered state in a container; drying the composition, preparing blood = the impact of air given to the composition, the specific speed and flow rate The method of introducing air into the container and the combination of the hand and the slave device of the micronized powder composition from the container are used in combination, and the user can simply freeze-dry the non-powder during use (especially when inhaled). The preparation is prepared into a particulate state suitable for pulmonary administration, and therefore, pulmonary administration can be achieved by directly inhaling the microparticles. Furthermore, the inventors have discovered that the pharmacologically active substance-containing liquid filled in the container in a liquid state is not limited to the added ingredients (especially the pharmacologically active substance that is an effective ingredient) that are clearly dissolved in the solvent or mixed clearly, Even if these added ingredients exist in an undissolved solvent or in an undissolved state, they can be adjusted into a cold-dried dry composition suitable for pulmonary administration of particles by specific air impact. Therefore, the present inventor is certain that if the 315314 9 200418520 is used to administer the dry inhalation system through the dry bucket for pulmonary administration, the problems related to the previous dry powder inhaler for pulmonary administration can be completely solved. That is, according to the pulmonary administration system according to the present invention, since the helmet is micronized by other devices and then divided into small portions and filled in a container, it is not a problem and can be applied to pulmonary administration. In addition, if the dream according to the present invention: cattle: dry powder inhalation system 'because unlike the spray drying method; :: protein and peptides must be exposed to high temperature: ★ will not be caused by high temperature exposure The problem of reduced pharmacological activity. For pharmacologically active substances such as peptides and proteins of high-priced drugs,-'can reduce the manufacturing cost of the preparation, that is, the present invention is also useful from an economic point of view. … The first hand fills the life field private right right—the dry-powder powder inhalation system of the present invention for injecting into the lungs, can reach the lung's magic, and can efficiently deliver drugs to the lungs . The dry powder for pulmonary administration of the present invention contains an insoluble system of active ingredients, which is characterized by freeze-drying and preparing cold-roll dry-welding of Baishi solution-like heart composition liquid into a non-bird-like block form; The wood and the product are used as preparations for transpulmonary administration. The thus prepared block-shaped cold Dong 7 牦 / wood composition was applied to the dry inhalation device of the present invention, which was formed by a dry inhalation device, and the inhalation system of the present invention was used to inhale with the dry powder of Ezhao Xianli The agent used ..., η ## μ b The blasting method or the dry method is used to break the particles into granules of the desired size in advance, which is suitable for the use of the powdered preparations in the preparation of the inhalation device. Effective particle ratio. Therefore, this:-is positioned as a high-performance transpulmonary administration system. "The terminal inhalation system can be developed by the present invention based on an inquiry based on this knowledge, and includes the following forms. 315314 10 200418520 (item 1) An application for humans for pulmonary administration < ~ lyophilization The composition is prepared by adding the ingredients in a non-dissolved state, 'right μ, human soil wind knife, and freeze-drying the prepared liquid, and has the following characteristics ⑴ to (iii) · · (I) has a non-powder morphology; (ii) the decay index is greater than or equal to 0.05; and ㈣ by: being impacted by air having an air velocity of at least lm / sec and an air flow of at least _ Microparticles with an average particle size of less than 0 micron or an effective particle ratio of 10% or more. (Item 2) The composition of the cold fish age Dongganzhi as described in Item 1 contains a polymer drug as an active ingredient. Item 3) A method for preparing the end-of-the-table preparations by using the lungs for lavatory, including the following cold and dry ingredients, and using the following air in the state of the product: Shock imparts coldness in the container; equipment for dry welding ▽ yttrium smelting, introduction To prepare for the air impact ability, you will benefit from the above-mentioned freeze-dried composition to form particles with an average particle size of less than micrometers or an effective particle ratio of more than one; it should be cooled to dry the composition. It is prepared by cooling the composition liquid containing the added components in a non-dissolved state and drying it, and has the following characteristics: (1) it has a non-powder morphology, and (ii) the decay index is greater than 0 · 05, (111) Essence: Air impact with an air velocity of at least 1 oil and an empty milk flow of at least 17 ml / seC can become particles having an average particle size of 10 microns or less and an effective particle ratio of 10% or more. (4th member) The manufacturer of the dry powder preparation for pulmonary administration as described in item 3, 315314 11 200418520, the drug Γ in the 50% cold; the dry composition contains a polymer L as an effective ingredient, page 5: Middle) For example, the manufacturer of the dry powder preparation for pulmonary administration in item 3 is set as follows: Set: = Dry powder described in Γ Qing ... The lyophilized lyophilized mash composition is micronized. (Α) Pulmonary administration Use dry capacity; Α #, will be collected in a non-powder state :: Xun = dry composition into particles and inhaled by the subject > equipment for U tablets paid, characterized by: The needle part of the road has a needle part for discharging the flow path. In the upper stage, the air for conveying air in the H & M jet flow path is sent by hand. The discharge flow path of the needle part is connected and configured as: and the inlet, 2 = :: : The mouth plug for sealing the above container is used to inject air to the exhaust flow path and communicate with the inside of the above container, and the above air lu sends a hand # to pass air through the upper 4 ^, and the above container is formed by the injection M m, and The obtained cold; U particles of the dried composition particles 丨 U particles are discharged from the suction port through the above discharge flow path 丨 or ⑻ The dry powder inhalation device for pulmonary administration is composed of a cold beam drying device not contained in a container. The obtained device for particles is characterized by having the following features: The suction port connected to the suction channel; & the needle portion and the structure are as follows: 315314 12 200418520 2 The state where the needle portion is pierced to seal the mouth plug of the container, and the suction pressure of the container is taken from the suction mouth Inhaled the air in the container, and on the same day, TΓ caused the air to flow through the upper flow path, and "the inflow from the above-mentioned working milk introduction flow path has become a negative pressure." The fine particles are discharged from the suction port through the suction flow path. (Item 6)-A dry powder inhalation system for pulmonary administration, which uses the following ⑴ and (2) in combination: ⑴ Contains a container with a freeze-dried composition. The composition liquid of the non-solvent additive ingredients is prepared by cold-rolling drying, and has the following characteristics: ⑴ to Gii) (1) It has a non-powder-like morphology, and (ii) the sadness index is 〇 · 〇5 or more, and (out) by bearing at least! m / sec air speed and at least! The air impact of the air flow of 7ιηΐ / _ can become fine particles with an average particle size of less than 10 microns or an effective particle ratio of more than 10%; the above-mentioned random impact can be imparted to the cold-rolled dry composition in the container. Hand & and means for discharging the powdered cold-roll-dried composition. (Item 7) The dry powder inhalation system for pulmonary administration according to item 6, [the above-mentioned container is used in combination with the above-mentioned device during inhalation. (Item 8) The dry powder inhalation system for pulmonary administration according to item 6, wherein the cold-dried dry composition contains a polymer drug as an active ingredient. (Item 9) If the dry powder inhalation system for pulmonary administration in item 6 of item 315314 13, the following (A) or (B) is used as the device: (A) =! And inhalation with dry powder The device is a device for storing A clean # β 7 East dry composition in a non-powder state in a grain container and making the user inhale the particles provided by the user '. The device is provided with: 2 ^ the needle portion of the air jet flow path A needle part having a discharge flow path, an air pressure hand for conveying air in the air jet flow path of the second 2 :: P, and an suction port communicating with the discharge flow path of the needle part, and is constituted as: The needle part is inserted into the six-pass mouth flow path and the discharge flow path. Two, the mouth plug is used to spray the air: //, Shu Guyi is connected internally, and the above-mentioned air pressure is used-and the second roll is sprayed on the above through the air spray flow path. The impact of crying air causes the particles from the cold-dried composition to pass through the above-mentioned exhaust flow path to be sucked in through the above-mentioned exhaust flow path; or (B) = Γ: powder inhalation device, which collects & Apparatus and device for micronizing dry composition and allowing subject to suck particles ·: It ::: Needle section of the road, having a needle section for the air introduction flow path and a suction port communicating with the ^ drainage path; and the structure is: the needle part is inserted into a state for sealing the mouth of the container, and is Day: Two rolling mills inhale the air in the container from the above suction port, the same as f: the inflow from the air introduction flow path has become a negative capacity-the inner 'fine' is cooled by the impact of the inflowing air; Micro 315314 14 200418520 / Granulated, and the obtained particles are discharged from the suction port through the above suction flow path. (Item 10) A method for administration via the lungs, including ^ ^ ^ lyophilizing the hydrazone composition, and the resulting system is prepared by cold and drying the additive solution containing the undissolved state, and has the following Characteristics: (1) has a non-powdered morphology, (ii) has a decay index of 0.05 or more, and (iii) by withstanding at least lm / sec milking degree and at least 17ml / sec: Air impact can become particles with an average particle size of less than 10 microns or an effective particle ratio of more than 10%; at the time of the object, the air impact is imparted to the cold; the dry composition, shape, average Granules: 0 micrometers or less, or an effective particle ratio of 10%, and then administered by inhaling the user to the micronized powder. 1. The method for administration via lung according to item ¥ 1G, wherein the Lengkanggan is contained in a container, and the micronized powder system is prepared underneath: the above-mentioned air impact can be imparted to the container ::: Means for drying the composition and means for discharging the micronized powdered freeze-dried composition from the container. (12th item) The method for pulmonary administration according to item 10, wherein the freeze-dried t composition comprises a polymer drug as an active ingredient. (::, member) The method for pulmonary administration according to item 11, wherein the dry powder inhalation device described in (A) or (B) below is used as the device: (A) Dry powder for pulmonary administration The inhalation device is a device that will contain the powder in a non-powder state. 4 'Donggan No composition is atomized and the user inhales the particles obtained by 15 315314 418520. It is equipped with: a needle with an air jet flow path A needle part having a discharge flow path, on the upper part of the air jet flow path of the needle part, an air pressure hand slave for conveying air, and an suction port communicating with the discharge flow path of the needle part; and is configured as: 'the above The needle is inserted into the supply and discharge flow path. M:: ί to inject air ... Connected internally, and the air pressure X is used to pass the air through the nozzle of the air flow path. The impact of the above-mentioned crying air causes the cold and dry composition to pass through: " and the served particles are discharged from the suction port through the above-mentioned discharge flow path; or '(Β): == Dry powder inhalation device' system The freeze-dried composition contained in a non-powdered state is The device for changing the particulates inhaled by the subject is provided with: a needle portion having an M flow path, and an air inlet through which the air flow path communicates with the suction flow path; and / or, and is configured as: 2 for sealing In the state of the mouth plug of the container, the air in the container is sucked through the suction port of the lice, and the air flows into the negative pressure capacity through the above-mentioned air introduction flow path: inside ': the air impact will The cold / rolled dry composition is discharged from the suction port through the suction flow path through the micro / served particles. (Brother 14 item); a freeze-dried composition is used for inhaled pulmonary administration, where 'the cold' east-dried composition is prepared by freeze-drying a composition liquid containing the addition of 315314 16 200418520 ingredients in an undissolved state It has the following characteristics ... It has a non-powdered morphology, (ii) a decay index of 0.05 or more, and (m) by withstanding an air velocity of at least lm / sec and at least pmi / sec The air impact of the air flow can become fine particles with an average particle size of less than 10 microns or an effective particle ratio of 10% or more; and the freeze-dried composition is powdered to become fine particles with the above average particle size or effective particle ratio To use ,. (15th item) The freeze-dried composition of item 14 is administered via the lung: wherein the cold-knock-dried composition is contained in a container, and the micronized powder is provided with a device capable of flushing the above air. Means of Lengkang drying the composition and means capable of discharging the micronized powder-like form of Lengkang dry composition from Gushan Yangu μ, Ding only and J Yougu from Liuliu . (_ Item 1 =) The freeze-dried composition according to item 丨 4 is used for pulmonary administration, in which the Yan Hai cold-rolled and dried composition contains a high molecular weight drug as an active ingredient. (Item 17) — &, human, soil 〇, seed dry composition in the manufacture of inhaled pulmonary administration Che Yi powder made Zhai 丨 ^^ # _ moxibustion 'The freeze-dried composition has The following characteristics:: The composition liquid of the additive components that are not in the cleavage state is prepared, ⑴) has a non-powder morphology, (iii) the decay index is greater than or equal to 0.05, and The fragrance is ancient and / or has air impact with an air velocity of at least lm / sec and an air flow of at least 17mi / sec 315314 200418520, which can become particles with an average particle size of less than 10 microns or an effective particle ratio of more than 10%; and 2. On the day of use, the freeze-dried composition can be micronized to have the average particle diameter or the effective particle ratio. (: 2: 8) If the freeze-dried composition of item 17 is used in the production of dried button powder preparations for fish for lung administration, the compound ^, the freeze-dried composition contains a polymer drug as an active ingredient. (Use item V9) The use of the Lengkang dry composition as described in item 17 in the manufacture of pulmonary powder-dried dry powder preparations, its' ^ ^ ^ 0 /, MQ lyophilized residue composition is collected in Hezu , And the micronized > a Μ < Zhi Mo is made with the means which can impart the impact of the above-mentioned empty milk to the freezing in the container.... Device for means of composition (item 20) A use of a composition liquid containing non-dissolved energy and an additive component of the heart is used for the manufacture of frozen powder preparations for the preparation of P ψ only for use in pulmonary administration The cold and dry composition has the following characteristics: (1) it has a non-powdered morphology, (π) a decay index of 0 05 or more, and (ii) has at least lm / sec salute degree and at least 17ml / sec

之空氣流量之空氣衝擊,可成A j成為千均粒徑在1 0微米以 下或有效粒子比率在10%以上之微粒; 並且於使用時經微粒化為上述 ^ η述十均粒控或上述有效粒 卞比毕。 (第21項)如第20項之包含非溶解 解狀恶之添加成分之組 315314 18 200418520 成液之使用,纟中,該冷;東乾燥組成物係包含做為有效成 份之高分子藥物。 (弟22項)如第2G項之包含非溶解狀態之添加成分之組 成液之使用,其中,該冷凍乾燥組成物被收容於容器内, =該經微粒化之粉末係、用具備可將上述空氣衝擊賦與該 合态内之冷凍乾燥組成物之手段以及可從容器中排出經微 粒化之粉末狀冷凍乾燥組成物之手段之裝置調製而 [實施方式] 最佳 (1)冷凍乾燥組成物 、本1明之冷4乾燥組成物,係藉由將包含非溶解狀態 ,添加成分之組成m態充填於容器並直接將其 :而調製成之非粉末之乾燥狀態組成物。其較佳為將包: =欠或數次投與有效量(以包含單次投與份之有效量為特 之東乾燥組成物。 本發明之冷凍乾燥組成物,藉由選擇及調製上述组 ==且成(有效成分,以及與有效成分併用之載劑之種類及 用里)以使冷,東乾燥處理所得之非粉末組成物之衰變指數 ,〇.〇5以上,將可藉著被導入(流入)容器内之空氣衝擊 =擊、嘴射壓),瞬間或快速地微粒化成適於經肺投與: 其中 组成物, ’在本發明中所謂之衰變指數,係對於冷康乾燥 依照下述方法測得之該冷凍乾燥組成物之固有 315314 19 200418520 值: <衰變指數> 在筒徨㈣酿或筒徑023mm之 填0.2至〇.5ml组成液 以液恶充 成物…含有以構成冷柬乾燥组 成物為“的之成份)线其冷;東乾燥。繼而,在得到 末狀冷凍乾燥組成物中,經由容 1 ml。將1认。 土秤蛘地滴入正己烷i .〇 ml將其於3〇⑽rpm攪拌約1〇秒 真! m 所仔之混合液投入光路 >長1 mm,光路寬【0 mm之uv 、、則定名、*且 快速地用分光光度計 ::… 0 nm之濁度。將所得濁度除以構成冷凍r 餘組成物之成份之總量(重量 乾 數。 1重里)其所得之值定義為衰變指 其中,本發明之冷滚乾燥組成物所具有之衰變 下限值為上述之0 · 0 5,其理相依床LV Λ 012Λ, ν 里心依序以。別、。,、。」、。·"、 ϋ·12馮佳,又以〇 13為最佳。 又,關於本發明之冷康乾燥組成物之上限值 別限疋,f以U為較佳,其理想依序以0.9、 Ο.?:別π 0.5為最佳。本發明之冷;東乾 :上為限度,期望具有在從上述者任意選出之下二 舁上限值構成之範圍内之衰變 辦而士,々丨4Α 數衣交指數之範圍,呈 …例如為〇.〇5至〗·5’0.08〜 ;、 至 0·:’0·10 至 °·8,至。.7,至。.6 及。·〗至。:·1 本發明之冷凍乾燥組成物 U·5。 粉末之塊狀形能去.'精由/々凍乾燥調製成非 知末之塊狀“者。在本發明中所謂非粉末 組成物意指將含有效成分夕知Λ、— 果乾4 成刀之組成液經冷凌乾燥所得之乾燥 315314 20 固體’通常被稱為冷凍乾 之處理中,塊體產生裂痕二=:東⑽驟或其後 分破損成為粉狀者,。要…成為數個大塊者、以及部 y、聲不損及本發明之钕罢,比 明所針對之非粉末狀冷凍 5 % ;:木組成物,亦即皆 非粉末之塊狀形態之冷仏燥組成物中。 在具有 之Γ 組成物,為將上述包含非溶解狀態 I添加成分之組成液奴入 ^ 0 μ 、'?凍乾燥而調製成者,其特徵為具 ==衰變指數以及非粉末之塊狀形態,而且基於 由二=數表現之該冷;東乾燥組成物之固有性質,藉 々>lm/sec之空氣速度及至少滿ec之空 =之空氣衝擊,可以形成為平均粒徑為1〇微米以下或 有效粒子比率為10%以上之微粒。 衝擊就=之冷凍乾燥組成物而纟,藉由承受上述空氣之 =’,二如可以形成平均粒徑為1〇微米以下(較佳5微米 賦與冷凍乾燥組成物之空氣衝擊,若藉由具有夏 以上之空氣速度及17 ml/sec以上之空氣流量之空氣 產生之衝擊’則無特別限制。具體而f,上述之空氣衝擊 例如為藉由1 m/see以上,較佳S 2 m/sec以上,更佳為5 = SeC以上’最佳為1 0 m/sec以上之空氣速度生成之衝擊。 其中,關於空氣速度之上限,雖無特別限制,但通常為3〇〇 較佳為250 m/sec以上,更佳為200 m/sec以上, 取仏為1 50 m/sec以上。又,空氣速度,只要在從上述中 灶’者有效粒子比率為10%以上(較佳20。/。以上,更 土 25/。以上’最佳3〇%以上,特佳训以上)之微粒。 315314 21 200418520 任意選f之下限及上限所構成之範圍内,則無特別限制。 具體而言,為 1 至 300 m/sec,i 至 25〇 m/sec,2 至 25〇 m/sec,5 至 25〇 m/sec,5 至 200 m/sec,1〇 至 2〇〇 , 1 〇至1 50 m/sec之範圍。 二又,上述之空氣衝擊,例如通常藉由丨7 ml/sec以上, 4 〇 ml/sec以上’更佳25 mi/sec以上之空氣流量產生 之衝擊H空氣流量之上限,雖無特別限制,例如可 為 900 L/min,依序以 15L/sec、1〇L/sec 5L/s“、礼〜c 為佳’又以3L/Sec為最佳。具體而言,空氣流量只要在上 2中任f選出之下限及上限所構成之範圍内,則無特別限 1。该耗圍例如為 17 ml/sec 至 15 L/sec,20 ml/sec 至 1〇 ,20 ml/sec 至 5 L/sec,2〇 ιώ1/_ 至 4 L〜c,2〇 ⑽ 至 3 L/Sec,25 ml/sec 至 3 L/sec。 在本發明中所使用之有效成分,原則上只要可作為經 :投與用乾燥粉末吸入劑之成份之具有任何藥理活性之物 :(藥理活性物質:以下亦可簡稱為藥物),則無特別限 :子!體而言,例如可為低分子藥物及高分子藥物。又高 二:物包含所謂「酵素、激素及抗體等蛋白質(包含胜肽 及夕狀)以及DlSiAe ρχτλ々々丨△ 生理活性成分。RNA寻核酸(包含基因及侧入)」之 又,做為藥物之對象疾 及局部療法二種。 病者,視情況 可為全身療法 者 醇 做為低分子藥物 c〇rtisone)、去氫可體 例如為皮質醇(hydro-(prednisolone)、去炎松 315314 22 200418520 (tiiamcinolone) 地基米松(dexamethasone)、倍他米松 (betamethasone)、倍氯米松(becl〇methas〇ne)、氟提卡松 (fluticasone) 莫美他松(mometasone)、可滅喘 (budesonide) ◊ 丁胺醇(salbutamol)、沙美特羅 (salmeterol)丙卡特羅(procaterol)、鹽酸丁丙諾非 (bUPren〇rphine hydr〇chl〇dde)、阿噗嗎啡(apomorphin°e)、 紫杉醇(taxol)及妥布黴素(t〇bramycin)等抗生物質。 做為高分子藥物(蛋白質類及核酸等生理活性成分) 者,例如干擾素(α,万,7)、間白素(例如間白素_卜2、 3 4 5、6、7、8、9、10、11、12、13、14、15、16、17、 18等)、抗間白素]α抗體、間白素」受體、間白素受體 拮抗劑、間白素-4受體、抗間白素·2抗體、抗間白素-& 受體抗體、間白素-4拮抗劑、間白素_6•拮抗劑、抗間白素 -8抗體、化學趨素受體拮抗劑、抗間白素_ 7受體、抗間白 素-7抗體、抗間白素_5抗體、間白素_5受體、抗間白素_ 9抗體、間白素-9受體、抗間白素_1〇抗體、間白素_ι〇'受 體、抗間白素-1 4抗體、間白素_丨4受體、抗間白素_ 1 $抗 體、間白素-15受體、間白素_18受體、抗間白素_18抗體^ 紅血球生成素(ΕΡ0)、紅血球生成素衍生物、顆粒球群落 刺激因子(G-CSF)、顆粒球巨噬細胞·群落刺激因子 CSF)、巨噬細胞·群落刺激因子(M-CSF)、降鈣素、胰离 素、胰島素衍生物(LisPro、N〇VORapid、h〇E901、NN-3〇4 等)、促胰島素激素、類胰島素生長因子 '升糖素、生長抑 素(somatostatin)或其之類似物、血管升壓素(vas〇pressi^ 315314 23 200418520 或其之類似物、月請粉樣酵素(amylin)、人類 :體,成激素釋出激素、㈣刺激激素、成長激_出因 ,,、田”狀腺激素、血管内皮細胞成長因子、血小板 增殖因子、角質細胞成長因子、上皮細胞成長因子、纖丁维 、來自腦之神經營養因子、毛樣體神經營 :口”瘤壞死因子(TNF)、TNF受體、TNF抑制劑、 子⑽、因子⑽F)、肝細胞成長因子(HGF)、神經成長因 血液幹細胞成長因子、血小板增殖因子、鈉利 水胜肽、血液凝固因子、血液肝細胞成長因子(S_CSF)、 FLT3配位體、抗血小板凝聚抑制單株抗體、組織.纖维蛋 白溶酶原•活化因子或其之衍生物、超級歧化氧化酶、反 =樂、免疫抑制劑(例如環孢素、塔可羅利姆斯…⑽ :合物等)、癌抑制基因p53、囊胞性纖維症膜貫通型調節 α白⑽TR)基因、RNA干擾素(RNAi)、架橋核酸(BNA)、 血“胰蛋白酶 '促血小板生成素(thrombopoietin, TPO)、 催I成抑制素(metastasin)、去氧核糖核酸酶(DNAase)、 性礼激素、催產素、促甲狀腺激素釋放激素(TRH)、殺菌 卢,過^増加蛋白質(BPI)以及流行性感冒疫苗、愛滋病 1田輪狀病毋疫苗、癔疾疫苗以及Mtb72f等結核疫苗等 疫苗製劑等。 i此等有效成分可以使用單獨一種,或組合使用2種以 夕 上述各種脞肽類亦包含天然型多肽、基因重組型 夕肽、藉由化學合成之多肽等。 又,此等有效成分,可以使用本身游離態或鹽狀態者。 24 315314 200418520 又可以使用被保持為任意之 體,若為可使有效成分(例如包含者。關::保持 藥物及合成低分子藥物)以任 及核酸寺南分子 包、包接、離子結合等)保持者=存在形態(吸著、内 脂質膜構造體、微膠囊、環糊精、樹狀 二^ 微米球粒、奈米膠囊及奈米球粒等。x,其中脂質^ 體包含單層膜脂質體及多 、、 層月日貝體寺脂質體、o/w型或 w/o/w型乳液、球狀膠體粒子、細帶狀膠體粒子及層狀構 造物等。 又’所謂「樹狀分子」,一般而言,為分子之鏈依據一 定之規則,從中心向外方三次元地形成規則擴大之形狀之 分子。樹狀分子具有球狀構造,在其之内部具有攝入藥物 之工間,並有做為奈米膠囊之機能。為了在樹狀分子内部 中保持藥物,已知有下述方法:1}利用樹狀分子内部與藥 物之相互作用(疏水性相互作用及靜電相互作用等),或 在樹狀分子表面形成緻密胞室構造,物理性地捕集藥物等 (文獻·河野健司:Drug Delivery System,17-6,462-470 (2002))。又,實施例所使用之Superfect係由具有一定形 狀之活性型樹狀分子形成(文獻· T a n g, Μ · X,R e d e m a η η, C.T.以及 Szoka, Jr. F.C : In vitro gene delivery by degraded polyami do amine dendrimers. Bioconjugate Chem. 7,703 (1996))。此等分子從中心分枝,藉由在終端具有带正電荷 之胺基,並與核酸之磷酸基(带負電)交互作用而構成。又, SuperFect為了容易將DNA及RNA導入細胞中,具有將 25 315314 200418520 DNA及RNA凝縮成緻密形態之性質。 • 做為較佳之保持體者,可例舉如:脂質體、樹狀分子、 .反錄病毒載體、腺病毒載體、腺病毒-伴隨病毒、慢病毒 (lentiVlrus)、單純疱疹病毒載體、HVJ(仙台病毒卜脂質體 (例如HVJ外套載體套組等)。 ’、中月曰貝膜構造體及樹狀分子等之保持體,由於可將 外來基因導入細胞内,所以比先前應用廣泛。在本發明中, _可同樣地使用基因導人用脂質體及基因導人用樹狀分子。 又’此等可從商業上獲得。 、、又,保持體之粒徑(幾何學之平均粒徑:用動態光散射 法或雷射折射及散射法測定),若在1〇微米以下,則無特 制、。較佳為5微米以下。例如脂質體及乳液,粒徑(幾 何干之平均粒徑)為5〇⑴力至數#以,球狀膠體粒徑為$至 50 nm ° #〜又,關於幾何學之平均粒徑之測定方法,一般而言, =衣數十奈米領域之粒子之粒度分布,可使用動態光散射 射及Γ於數十微米以上之粒子之粒度分布,可使用雷射折 • 射法測疋,其間數百奈米與數微米領域之粒子之粒 度分布測定,皆可使用任一測定方法。 限制關於有效成分在此等保持體中之保持形態,雖無特別 •體之膜例如在知質膜構造體之情況,例如有在脂質膜構造 中、表面、内部、脂質層中或脂質層表面任意附著/ 伟在之形態。 關於形成該保持形態之方法,例如為在脂質膜構造體 315314 26 200418520 桩 與有效成分(基因等)之混合乾燥物中添加水系 某,然後用均質器等乳化機乳化或懸浮之方法 …合 膜構造體等保持體溶於有機溶媒後,餘去、容婵二質 燥物中,再添加勺人I门 去,合媒所仔到之乾 分,於k 基因之水系溶媒以乳化之方法;在已 有:文:媒之脂質膜構造體等保持體中,再添加包含 =::Γ:等)之水系溶媒之方法;將脂質膜構造二 Ζ體以於水“媒後乾㈣得之乾燥物添 效成分(基因等)之水系、、定姐夕古、土C 匕s有 公報)。 某之方法(苓照特開2001-2592號 大小(粒徑)之情況,使用孔徑相同之膜式 壓下進行押出過濾之方法,或使用加壓型整 ^之方法(茶照例如特開平6_238j42號公報)。 本發明之冷; 東乾燥組成物之特徵之—係將包含非溶解 恶之添加成分之組成液經冷;東乾燥而調製成。其中所气 非溶解狀態意指添加成分在構成組成液之溶媒中無法以澄 =之狀態溶解或者以澄明之狀態混合之狀態。該非溶解狀 恶’包含在溶媒中固形物以可用任意手段檢測出之狀態存 在。具體而言,例如在溶媒中,具有〇〇…以上,較 佳 0.05 # m 以上,f 估 〇 ! 门 1 0·1#111以上,再更佳0.2// m以上, 最佳〇 ·5 // m以上之幾、知風、τ,认,/ <成何學平均粒徑(用動態光散射法或雷 射折射及政射法測定)之固形物之存在可以檢測之情況。若 可以達成本發明之目的,此等固形物之幾何學平均粒徑⑺ 動心光政射纟或雷射折射及散射〉去測定)之i限雖無特別 限制,但通常纟20…下,較佳15”以下,更佳1〇 27 315314 200418520 μ m。更具體而言,本發明中所謂之「非溶解狀態」包含 ^溶媒中,幾何學平均粒徑(用動態光散射法或雷射折射及 散射法測定)在0·01至20"m、0.05至15/zm、(U至15 以 m、0.2 至 15 “mu 至 16 “m'oou 1〇 “瓜、〇1 至1〇 "m、〇·2至10 或〇·5至10//m之範圍内之固 :物以可用任意手段檢測出之狀態存在之狀態。關於該非 、解狀怨之具體形態,例如為添加成分不斷地溶於溶媒中 成為飽和以上之狀態’以及添加成不溶於溶媒之狀態,亦 即=於溶媒為非溶解性或難溶解性之有效成分懸浮或混濁 二岭媒中之狀態。又’具體評價非溶解狀態之方法,測定 =之濁度雖為—般之方法’但可以使用以粒度分布測定 衣士敎不溶解物之粒度分布之方法。後者之方法,具體 ::丄错由將做為對象之非溶解狀態之組成液用蒸 =食鹽液稀釋成適於粒徑測定之濃度後,裝入小室中: 在之粒子之粒徑而實施^置測疋在所得稀釋液中存 =其巾所謂「添加成分為非詩狀態」意、 二有二成夕下述载劑本身在溶劑中為非溶解狀態“ 况亦包含上述脂質體、微膠夤 持體中所保持之有兮点八/展、展糊精、樹狀分子等保 熊,伯t所、、 > 刀在保持狀態雖為溶於溶媒之狀 :、二月曰質體等保持體為非溶解狀態之情況。 成分限定為有效成分,=4將該非溶解狀態之添加 之保持體或其他任意成分(下組成液 ^/又有特別限制。 315314 28 200418520 對知與添加成分同時構成組成液之溶媒,並益 別限制,伯^ … ^ 仁T例如為水及生理食鹽液等等張液、培養基或 制 寺。又,在該溶媒中可包含有機溶媒,但以最終調 衣物(鉍肺投與用冷凍乾燥組成物)不會對人體產生 塑為PP a ^ ^ " 该有機溶媒例如為甲醇、乙醇、異丙醇、丙酮及 乙二醇等。 ^ ^明之冷凍乾燥組成物,只要最終調製物之上述衰 :^ ^足夠,將可為單獨之上述有效成分或有效成分與保 、、亦、且口而成者,或添加適當載劑者α在有效成分中加入 載Ί it况’使用之載劑之種類及量,若可使包含其與有 :=刀之非溶解狀態之組成液藉由冷凍乾燥所調製成之最 終~凍乾燥組成物滿足下述⑴至(iii)之特性: (0具有非粉末之塊狀形態, (ii)衰變指數為〇·〇5以上,以及 ⑽藉受具有至少lm/sec之空氣速度及至少17義。 工氧极1之空氣衝擊,可成為平均粒徑在1 〇微米以 下或有效粒子比率在i0%以上之微粒, 並且可以達成本發明之效果者,則無特別限制,可以 任意使用先前冷凍乾燥所使用之載劑或期望量。 做為该載劑者,具體而言,例如纈胺酸、白胺酸、異 白胺酸及苯基丙賴等疏水性胺基,或彼等之鹽或醯胺:、 甘胺I、脯胺酸、丙胺酸、精胺酸、榖胺酸等親水性胺基 酸或此等鹽或醯胺;胺基酸之衍生物;具有2個以上相同 或相異之上述胺基酸之二肽、三肽或者彼等之鹽或醯胺。 315314 29 200418520 可將彼等1縣。Μ、 或2種以上組合使用。其中,做為胺基酸或 胜月太之踏去 J 、 列如為鈉及鉀等驗金屬及妈等驗土金屬類金 屬之鹽;與磷酸及鹽酸等無機酸以及磺酸等有機酸形成之 力口 感 $ · 、 ' ,做為聽胺者,例如為L· _白胺it胺鹽酸鹽。 又,做為載劑者,可以添加α _胺基酸以外之胺基酸,該等 月女基酉义例如為冷-丙胺酸、r -胺基丁酸、高絲胺酸及牛碏 酸等。 … • 再者,做為其他載劑者,例如為葡萄糖等單糖類;蔗 糖、麥芽糖、乳糖及海藻糖等雙糖類;甘露醇等糖醇;環 糊精等养糖類;葡聚糖40及聚三葡萄糖等多糖類;聚乙二 醇等多元醇;以及癸酸鈉等脂肪酸鈉等。又此等載劑,可 以添加單獨一種,或添加二種以上之組合。 其中,關於可使有效成份效率良好地到達肺部之載 劑,具體而言,為異白胺酸、纈胺酸、白胺酸、苯基丙胺 酸等疏水性胺基酸或者彼等之鹽或醯胺;白胺醯基-纈胺 _酸、白胺醯基-苯基丙胺酸及苯基丙胺醯基_異白胺酸等疏 水性二肽等;以及白胺醯基_白胺醯基_白胺酸,白胺醯基_ 白胺醯基-纈胺酸等疏水性三肽等。此等亦可以一種單獨添 加’亦可以2種以上之組合添加。 又,干擾素_r之情況,從微粉末化及製劑安定性之觀 點言之,較佳除上述疏水性胺基酸或其之鹽或醯胺、疏水 性一肽及疏水性二肽之外,可以組合使用鹼性胺基酸或彼 等之鹽或醯胺、驗性二肽及驗性三狀。其中,做為驗性胺 基酸者,例如為精胺酸、離胺酸、組胺酸及其之趟。 土 卞人I 土 315314 30 200418520 為本基丙胺酸與鹽酸精胺酸之組合、苯基丙胺酸、白 與鹽酸精胺酸之組合。 卜~凍乾燥組成物所包含之有效成分(藥物)之含有比率 热:別限制,該含量例如為20mg以下,較佳10mg以下, 叫以下’再更佳2 mg以下,特佳1 mg以下。 物“ ’上述載劑之添加比率,若可使最終冷康乾燥組成 ,滿f上述⑴至㈣之特性,則無特別限制。雖然沒^ 节比】I個標準為當冷編組成物定為100重量%時, 该比率為0.1至不到丨 了 較佳,以1〇至不糾 夏以1至不到100重量%為 不到1 0 0重量0/0為更佳 重量%為特佳。 勹灵仫以20至不到1〇〇 又’本發明做為對象 述⑴至㈣之特性且不會損==、、且成物只要能滿足上 乾燥前之組成液中之有效」日之效果’為了使冷凌 安定化及防止有1 刀女疋化、乾燥後之有效成分 丨々此有效成分吸著於宏哭 各種添加劑。舉例茸-可在上述成分中添加 白、無機鹽、界可包含人類血清白蛋 若為通常適用於醫藥品 、關於界面活性劑, 面活性劑、陽離 、:活性劑’則不論陰離子性界 均可廣為應用。例如宜為 非續子性界面活性劑, (例如Tween型界 〃、耗乙烯山梨糖醇酐脂肪酸酯 性界面活性齊卜㈣)及山,梨醇肝三油酸醋等非離子 又,將該包含有效成分及任八 耜之方法則無特別限制, :―:之組成液經冷凍乾 —般製造冷凍乾燥製劑 315314 31 200418520 (:令凍乾燥組成物),如用時溶解型注射劑 乾無法。雖無限制,但視情況,調 =之冷床 速地冷凍乾燥。 條件,可急 本發明之冷;東乾燥組成物,藉由賦與 擊、,可以形成達到適於經肺投與之微粒。因此,太t氣衝 "凍乾燥組成物係適於調製經肺投與 1:, 供做為經肺投與粉末製劑之前調製物上二: 製劑調製用之冷康乾燥組成物)。 …又料末 樣:又,本發明之冷康乾燥組成物包含下文揭示之具體態 &、'"肺U之冷/東乾燥組成物’係將包含非溶解 悲之添加成分之組成液經冷凍乾燥而調製成者,且具有 下述(1)至(iii)之特性: (i) 具有非粉末之塊狀形態; (ii) 衰變指數為〇·〇5以上;以及 (iii) 藉由承受具有至少1 / sec之工氣速度及至少17ml/sec 之空氣流量之空氣衝擊’可成為平均粒徑在10微米以 下或有效粒子比率在10%以上之微粒。 1 0 2 ·如態樣1 ο 1項記葡入 、 戟之々凍乾燥組成物,其中,衰 變指數為0.05至1.5。 1 03 ·如態樣1 〇 1項記載 ^ 我~ /果乾燥組成物,其中,猎 由承受具有至少2 m/sec之处备、由由 乳速度及至少17ml/sec之空 氣流量之空氣衝擊,可成為平灼4 乂句十均粒杈在1 0微米以下或有效 粒子比率在1 0 %以上之微粒。 315314 32 200418520 104·如態樣101項記截 / 々’東乾無組成物,其中,藉 由承受1至300 m/sec範圍之*今 礼图之空乳速度及至少n mi/sec之 空氣流量之空氣衝擊,可成Λ 风马十均粒杈在1 〇微米以下或有 效粒子比率在10%以上之微粒。 1 0 5.如態樣1 〇 1項記葡、入 東乾無組成物,其中,藉 由承受具有至少1 m/sec之*气冻命Ώ ^ 工乳速度及至少20 ml/sec之空 氣流ΐ之空氣衝擊,可成為求 斤 為千均粒徑在1 〇微米以下或有效 粒子比率在1 〇 %以上之微粒。 1 0 6 ·如態樣1 〇 1項記葡、人 戰之/々康乾_組成物,其中,藉 由承受具有至少1 m/sec之*巧 <工乳速度及至少17 ml/sec至 15L/sec之空氣流量之空氧 孔衝^ 可成為平均粒徑在1 0微 米以下或有效粒子比率纟10%以上之微粒。 1 0 7 ·如態樣1 〇 1項記恭 丄/ 貝。己載之冷凍乾燥組成物,其中,藉 由承受空氣之衝擊,可成一 成為千均粒偟在5微米以下或有效 粒子比率在20%以上之微粒。 係包含做 108·如態樣ι〇1項記截 、 只 < 戰之冷凍乾燥組成物 為有效成分之低分子藥物。 係包含做 1 0 9 ·如態樣1 〇丨項記截 、 貝尤戟之冷凍乾燥組成物 為有效成分之蛋白質類及核酸等高分子藥物。 係具有做 110·如態樣109項記載之冷滚乾燥組成物 為有效成分之呈保持於保持體散態之核酸。 係含有做 ⑴·、如態樣⑽項記載之冷康乾燥娜一 一 為有效成分之低分子藥物以及載劑’肖載劑為至少一種選 自胺基酸、二肽、三肽及糖類組成之群者。 315314 33 200418520 112·如態樣1〇9項記載之冷凍乾燥組成物,係含有做 為有效成分之蛋白質類及核酸等高分子藥物以及載劑,該 載劑為至少-種選自胺基酸、二肽、三肽及糖類組成之群 者0 113.如態樣m項記載之冷凍乾燥組成物,係含有做 為有效成分之低分子藥物以及載劑,該載劑為至少一種選 自疏水性胺基酸、疏水性二肽及疏水性三肽組成之群者。 114·如態樣112項記載之冷朿乾燥組成物,係含有做 為有效成分之蛋白質類及核酸等高分子藥物以及載劑,該 載劑為至少-種選自疏水性胺基酸、疏水性二肽及疏水性 三肽組成之群者。 115·如態樣101項記載之冷凍乾燥組成物,係為水溶 性組成物。 116·如態樣1G1項記載之冷;東乾燥組成物,係含有上 次投與量之有效成分。 117·如態樣101項記載之冷來乾燥組成物,係將包含 非溶解狀態之添加成分之組成液經冷凍乾燥而調製成,且 具有下述⑴至(iii)之特性: (i) 具有非粉末之塊狀形態; (ii) 衰變指數為0.05至1.5 ;以及 (iii) 藉由承受1至300 m/sec範圍之空氣速度及17ml/sec 至1 5 L/sec之空翁流晉之介与& 土 工轧抓里之二虱衝擊,可成為平均粒徑 在10微米以下或有效粒子比率在1〇%以上之微粒。 118.如態樣117項記載之冷康乾燥組成物,1中,* 315314 34 200418520 氣速度為1至250 m/sec。 •如恶樣11 7項記載之冷凍乾燥組成物,其中,办 氣流量為2〇ml/se(^ 1〇1^咖。 王 (2)經肺投與用乾燥粉*製劑之製造方法 、人、a本&明係關於藉由將以非粉末狀態收容於容器内 口之冷康乾燥組成物在該容器内微粒化,製造具有適於藉由 " 肺杈與之粒徑之乾燥粉末製劑(經肺投與用乾燥粉 ^ 4劑)之方法。該方法可藉由對於以非粉末狀態收容於容 态内:冷凍乾燥組成物賦與特定空氣衝擊而實施。 /、-而σ本叙明之經肺投與用乾燥粉末製劑之製造 =去’經上述⑴所詳述之包含非溶解狀態之添加成分之植 成液經冷隸燥,調製成具有G.G5以上衰變指數之本發明 非粉,狀冷;東乾燥組成物,然後對其賦與具有至少i ‘二速度及至夕17 mi/sec之空氣流量之空氣衝擊而實 藉此可將,亥非粉末狀之冷;東乾燥組成物調製成具有平 均粒徑為丨〇微米以下(較佳5微米以下)或者有效粒子比率 為10%以上(較佳20%以上,更佳2S%以上,還要更佳3〇〇/。 乂上’特佳35。/。以上)之微粒形態之乾燥粉末製劑。 又,在本發明中所謂之微粒之平均粒徑意指在吸入劑 相關產業中通常所採用之平均粒徑,具體而言,非為幾何 學之粒徑,而係表*空氣力學之平均粒徑(MMad)。該空 氣力學之平均粒徑可以藉由習用方法求得。具體而言:: 氣力學之平均粒徑,例如用安裝人工肺型空氣呼吸器之: 315314 35 200418520The air impact of the air flow can become A j into particles with a thousand-average particle size of less than 10 microns or an effective particle ratio of more than 10%; Effective capsule ratio. (Item 21) As in item 20, it contains the group of non-dissolving and dissolving added ingredients. 315314 18 200418520 The use of liquid, in the cold, the cold; the dry composition contains the polymer drug as an effective ingredient. (Item 22) The use of a composition liquid containing non-dissolved added ingredients as described in item 2G, wherein the freeze-dried composition is contained in a container, = the micronized powder system can be used for the above The means for imparting air freeze to the freeze-dried composition in the combined state and the means for discharging the micronized powdery freeze-dried composition from the container are prepared. [Embodiment] The best (1) freeze-dried composition The cold and dry composition of the present invention is a non-powder dry composition prepared by filling the container with the composition m state containing the insoluble state and the added ingredients and directly filling it in the container. It is better to pack: = owed or several times the effective amount (Effective amount including a single dose is the East dry composition. The freeze-dried composition of the present invention, by selecting and preparing the above group == The decay index of the non-powder composition obtained by the cold and eastern drying treatment (the type and use of the active ingredient and the carrier used in combination with the active ingredient), which is more than 0.05, can be used by The air introduced into the container (impact = blow, mouth ejection pressure), instantly or quickly micronized into suitable for pulmonary administration: where the composition, 'the so-called decay index in the present invention, The inherent 315314 19 200418520 value of the freeze-dried composition measured by the following method: < Decay Index > Filling 0.2 to 0.5 ml of the composition solution with a liquid evil filling in a tube or a tube diameter of 023 mm ... The components that make up the dry composition of cold Cambodia are "the ingredients", which are cold and dry in the east. Then, in the final freeze-dried composition, the volume is 1 ml. The volume is dropped into n-hexane i 〇ml, stir it at 30 rpm for about 10 seconds. m Put the mixed solution into the light path> 1 mm long, the width of the light path [0 mm uv, then name, * and quickly use a spectrophotometer:… 0 nm turbidity. Divide the obtained turbidity by the composition The total amount of the components of the frozen r composition (dry weight. 1 mile). The value obtained is defined as the decay. The lower limit of the decay of the cold-roll drying composition of the present invention is the above-mentioned 0 · 0 5 , Its rational phase depends on the bed LV Λ 012Λ, ν The heart is in order. Do n’t ... · &Quot;, ϋ · 12 Feng Jia, and 13 is the best. In addition, regarding the upper limit of the cold-kang dry composition of the present invention, f is preferably U, and its ideal order is preferably 0.9, 0.?: Π 0.5 is the best. The cold of the present invention; Donggan: The upper limit is the expectation, and it is expected to have a decay within the range composed of the lower limit of the upper limit of the two selected arbitrarily. It is from 0.05 to 5'0.08 ~; to 0 ·: '0 · 10 to ° · 8, to. .7, to. .6 and. ·〗to. : · 1 Freeze-dried composition U · 5 of the present invention. The block shape of the powder can be removed. 'Fine is prepared by lyophilization / freeze-drying to form a block of non-knowledge.' In the present invention, a non-powder composition means that the active ingredient contains Xizhi Λ, — dried fruit 40% Drying of the composition liquid of the knife by freeze-drying 315314 20 Solid 'commonly referred to as freeze-drying, cracks in the block 2 =: East ⑽ ⑽ or its subsequent breakage to become powdery. To ... become several A large piece, as well as a part y, does not damage the neodymium of the present invention, than the non-powder-free frozen 5% targeted by Ming; wood composition, that is, a cold-drying composition that is not a powder-like block. The Γ composition has a composition of Γ, which is prepared by adding the above-mentioned composition liquid containing non-dissolved state I added ingredients to ^ 0 μ, '? Freeze-dried, and is characterized by == decay index and non-powder. Block-like morphology, and based on the inherent properties of the cold dry composition represented by two = number, can be formed into an average particle size by the air velocity of lm & sec and air impact at least full ec =. Particles below 10 microns or effective particle ratio above 10%. Impact = cold Dry the composition, and withstand the above-mentioned air = ', if you can form an average particle size of 10 microns or less (preferably 5 microns to impart air impact to the freeze-dried composition, if the air with more than summer There is no particular restriction on the impact of air at a speed and an air flow rate of 17 ml / sec or more. Specifically, f, the above air impact is, for example, 1 m / see or more, preferably S 2 m / sec or more, and more preferably 5 = SeC or higher, preferably an impact generated by an air speed of 10 m / sec or more. Among them, the upper limit of the air speed is not particularly limited, but is usually 300, preferably 250 m / sec or more. More preferably, it is 200 m / sec or more, and 仏 is more than 1 50 m / sec. In addition, as long as the effective air particle rate is 10% or more (preferably 20% or more) from the above range, it is more soil. 25 /. Above 'best 30% or more, special training above) 315314 21 200418520 There is no particular restriction on the range of the lower and upper limits of f. Specifically, it is 1 to 300 m / sec, i to 25m / sec, 2 to 25m / sec, 5 to 25m / sec 5 to 200 m / sec, 10 to 200, 10 to 150 m / sec. Second, the above-mentioned air impact, for example, usually by 7 ml / sec or more, 40 ml / sec or more 'Although the upper limit of the impact H air flow caused by an air flow of more than 25 mi / sec is not particularly limited, for example, it may be 900 L / min, in order of 15 L / sec, 10 L / sec 5 L / s ", Li ~ c is better 'and 3L / Sec is the best. Specifically, the air flow rate is not particularly limited as long as it falls within a range formed by the lower limit and the upper limit selected by any of the above 2 f. The consumption range is, for example, 17 ml / sec to 15 L / sec, 20 ml / sec to 10, 20 ml / sec to 5 L / sec, 2ml / _ to 4 L ~ c, and 20 to 3 L. / Sec, 25 ml / sec to 3 L / sec. The effective ingredients used in the present invention are, in principle, as long as they can be used as ingredients of any dry powder inhalant for administration: (pharmacologically active substances: hereinafter also referred to as drugs), there is no special Limit: Son! For example, it can be a low-molecular drug and a high-molecular drug. Another second year: The substance contains so-called "enzymes, hormones, and antibodies such as proteins (including peptides and peptides) and DlSiAe ρχτλ々々 丨 △ physiologically active components. RNA nucleic acid search (including genes and side entry)" as drugs The target disease and local therapy are two kinds. Patients, as the case may be systemic therapy alcohol as low molecular drug cortisone), dehydrocorticoids such as cortisol (hydro- (prednisolone), triamcinolone 315314 22 200418520 (tiiamcinolone) dexamethasone) Betamethasone, beclomethasone, fluticasone, mometasone, budesonide, salbutamol, salbutamol Salmeterol, procaterol, buprenorphine hydrochlodde, apomorphin ° e, taxol, and tobramycin Antibiotics. As polymer drugs (proteins and nucleic acids and other physiologically active components), such as interferon (α, 10,000, 7), interleukin (such as interleukin_bu 2, 3 4 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, etc.), anti-interleukin] α antibodies, interleukin "receptors, interleukin receptor antagonists, inter Interleukin-4 receptor, anti-interleukin-2 antibody, anti-interleukin- & receptor antibody, interleukin-4 antagonist, Interleukin-6 antagonist, anti-interleukin-8 antibody, chemokine receptor antagonist, anti-interleukin-7 receptor, anti-interleukin-7 antibody, anti-interleukin-5 antibody, Interleukin-5 receptor, anti-interleukin-9 antibody, interleukin-9 receptor, anti-interleukin-10 antibody, interleukin_ι〇 'receptor, anti-interleukin-1 4 Antibody, interleukin-4 receptor, anti-interleukin-1 antibody, interleukin-15 receptor, interleukin-18 receptor, anti-interleukin-18 antibody ^ Erythropoietin (EPO) , Erythropoietin derivatives, granulocyte community stimulating factor (G-CSF), granulocyte macrophage · community stimulating factor (CSF), macrophage · community stimulating factor (M-CSF), calcitonin, selin , Insulin derivatives (LisPro, NVORapid, HOE901, NN-3〇4, etc.), insulinotropic hormones, insulin-like growth factor 'glucagon, somatostatin or its analogs, vascular Vaspressin (vasopressi ^ 315314 23 200418520 or its analogue, amylin, human: body, hormone release hormone, 激素 stimulating hormone, growth stimulus, cause, and field " Adrenal hormones, vascular endothelial cell growth factor, platelet proliferation factor, keratinocyte growth factor, epithelial cell growth factor, fibrin, neurotrophic factor from the brain, hairy body god management: mouth "tumor necrosis factor (TNF), TNF Receptor, TNF inhibitor, daughter ⑽, factor ⑽F), hepatocyte growth factor (HGF), nerve growth factor blood stem cell growth factor, platelet proliferation factor, natriuretic peptide, blood coagulation factor, blood hepatocyte growth factor (S_CSF ), FLT3 ligands, anti-platelet aggregation inhibitory monoclonal antibodies, tissues, plasminogen • activating factor or derivatives thereof, super disproportionation oxidase, trans = Le, immunosuppressants (such as cyclosporine, Taco Rolims ... ⑽: compounds, etc.), cancer suppressor gene p53, cystic fibrosis membrane penetrating regulatory α white ⑽ TR) gene, RNA interferon (RNAi), bridging nucleic acid (BNA), blood "trypsin 'Thrombopoietin (TPO), metastasin, DNAase, sex hormones, oxytocin, thyroid-stimulating hormone-releasing hormone TRH), bactericidal Lu, too ^ to increase in protein (BPI), and influenza vaccines, AIDS-like disease no wheel 1 vaccine field, hysteria and other disease vaccines and tuberculosis vaccines such as Mtb72f preparations. These active ingredients may be used singly or in combination of two or more kinds. The aforementioned various peptides also include natural peptides, genetically recombinant peptides, and chemically synthesized peptides. These active ingredients can be used in a free state or in a salt state. 24 315314 200418520 It can also be used as an arbitrary body. If it is an active ingredient (for example, include it. Off: keep the drug and synthesize a low-molecular drug), it can also be used for nucleic acid package, inclusion, ion binding, etc. Holder = Existing morphology (adsorption, internal lipid membrane constructs, microcapsules, cyclodextrin, dendritic microspheres, nanocapsules, and nanospheres, etc. x, where the liposomes include a monolayer membrane Liposomes and multi-layered, multi-layered, sun-shelled beetle liposomes, o / w or w / o / w emulsions, spherical colloidal particles, thin band colloidal particles, and layered structures, etc. "Molecular molecules" are generally molecules whose molecular chains form a three-dimensionally expanded shape from the center to the outside according to a certain rule. The dendrimers have a spherical structure and have drugs inside them. It also has the function as a nanocapsule. In order to maintain the drug in the inside of the dendrimer, the following methods are known: 1} Using the interaction between the inside of the dendrimer and the drug (hydrophobic interaction and electrostatic interaction) Role, etc.), or in the tree A dense cell structure is formed on the sub-surface, and medicines are physically collected (Document · Keno Kono: Drug Delivery System, 17-6, 462-470 (2002)). The Superfect used in the examples has a certain shape. Formation of active dendrimers (Tang, M.X., Reedema η, CT, and Szoka, Jr. FC: In vitro gene delivery by degraded polyami do amine dendrimers. Bioconjugate Chem. 7,703 (1996)). These molecules branch from the center and are formed by having a positively charged amine group at the terminal and interacting with a phosphate group (negatively charged) of a nucleic acid. In addition, in order to easily introduce DNA and RNA into cells, SuperFect has the 25 315314 200418520 The nature of DNA and RNA condensing into a dense form. • As a preferred holder, examples include: liposomes, dendrimers, retrovirus vectors, adenovirus vectors, adenovirus-associated viruses, Lentivirus (lentiVlrus), herpes simplex virus vector, HVJ (Sendai virus liposomes (such as HVJ coat vector kits, etc.). ', The retainer of the shell structure and dendrimers, etc. Since a foreign gene can be introduced into a cell, it is more widely used than before. In the present invention, a gene-derived liposome and a gene-derived dendrimer can be used in the same way. These are also commercially available. The particle diameter of the retainer (geometric average particle diameter: measured by dynamic light scattering method or laser refraction and scattering method), if it is less than 10 microns, there is no special. It is preferably 5 μm or less. For example, for liposomes and emulsions, the particle size (average particle size of the geometric stem) is 50 to tens of millimeters, and the particle size of the spherical colloid is $ to 50 nm ° # ~ Also, the measurement of the average particle diameter of the geometry Method, in general, the particle size distribution of particles in the field of tens of nanometers can use dynamic light scattering and particle size distribution of particles above tens of microns, and can be measured by laser refraction method. The particle size distribution of particles in the hundreds of nanometers and several micrometers can be measured by any method. Regarding the retention form of the active ingredient in these retainers, although there is no special case in which the membrane of the body is, for example, a plasma membrane structure, for example, in the lipid membrane structure, the surface, the interior, the lipid layer, or the surface of the lipid layer Arbitrary attachment / significant form. The method of forming the holding form is, for example, a method of adding a water system to a mixed and dried substance of a lipid membrane structure 315314 26 200418520 and an active ingredient (gene, etc.), and then emulsifying or suspending with an emulsifier such as a homogenizer ... After the structure and other retainers are dissolved in the organic solvent, the remaining dry matter is stored, and the second dry substance is added, and then the human I is added, and the dry matter obtained by the medium is emulsified in the aqueous solution of the k gene. A method of adding an aqueous solvent containing = :: Γ :, etc. to a retainer such as a lipid membrane structure of the medium, and the existing method: the lipid membrane structure of the body is dried after the medium is dried. Aqueous systems for adding effective ingredients (genes, etc.) to dry matter, Dingjiexigu, and soil C. There is a bulletin. A certain method (in the case of the size (particle size) of Lingzhao JP 2001-2592, use the same pore size The method of extruding and filtering under a membrane type, or a method of using a pressurized type (a tea photo, for example, Japanese Patent Application Laid-Open No. 6_238j42). The characteristics of the present invention are cold; the characteristics of the dried composition-will include non-dissolving evil The composition liquid of the added ingredients is cooled; The non-dissolved state means that the added components cannot be dissolved or mixed in a clear state in the solvent constituting the composition liquid. The non-dissolved solids are contained in the solvent and can be used at any time. The state detected by the means exists. Specifically, for example, in the solvent, it has 〇〇… or more, preferably 0.05 # m or more, f estimate 〇! Door 1 0 · 1 # 111 or more, and even more preferably 0.2 // m or more. , The best 0.5 · m / m or more, know the wind, τ, recognize, < the average particle size of Cheng Hexue (measured by dynamic light scattering method or laser refraction and political radiation method) Conditions that can be detected. If the purpose of the present invention can be achieved, the geometric mean particle diameter of these solids (attentional optical government or laser refraction and scattering> to determine) Although the i limit is not particularly limited, it is usually 纟 20 ..., preferably 15 "or less, and more preferably 1027 315314 200418520 μm. More specifically, the so-called "non-dissolved state" in the present invention includes in the solvent, the geometric average particle diameter (measured by dynamic light scattering method or laser refraction and scattering method) is between 0.01 and 20 " m, 0.05 To 15 / zm, (U to 15 to m, 0.2 to 15 "mu to 16" m'oou 1〇 "melon, 〇1 to 1〇 " m, 0.2 to 10, or 0.5 to 10 // The solid within the range of m: the state where the substance exists in a state that can be detected by any means. The specific form of the non-resolving complaint is, for example, that the added ingredients are constantly dissolved in the solvent to become more than saturated, and that the added is insoluble. In the state of the solvent, that is, the state in which the active ingredient in which the solvent is insoluble or hardly soluble is suspended or turbid in the Erling medium. It is also a method of specifically evaluating the insoluble state. Method ', but you can use the particle size distribution method to determine the particle size distribution of E. indica insoluble matter. The latter method, specifically :: the wrong solution is the target non-dissolved state of the composition solution is diluted with steam = table salt solution After the concentration suitable for particle size measurement, put it into the chamber: Measure the particle size of the sample and place it in the obtained diluent = the so-called "additional ingredients are in a non-poetic state" means that the following carrier itself is in a non-dissolved state in the solvent. The above-mentioned liposomes and microcapsule holders can be kept in the solvent, such as Xidianba / Zhan, Zhandextrin, and dendrimers, etc. Although the knife is in a dissolved state in the maintenance state: In February, the body such as the plastid is in an undissolved state. The ingredients are limited to effective ingredients, = 4 The added insoluble state of the retainer or other arbitrary components (the lower composition liquid ^ / has special restrictions. 315314 28 200418520 The solvent that constitutes the composition liquid at the same time as the known and added ingredients is restricted separately. The ren T is, for example, water, physiological salt solution, and other liquids, culture media, or temples. In addition, the solvent may include organic Solvent, but the final adjustment of clothing (freeze-dried composition for bismuth lung administration) does not produce PP to the human body. The organic solvent is, for example, methanol, ethanol, isopropanol, acetone, and ethylene glycol. ^ ^ Mingzhi freeze-dried composition, as long as The above-mentioned decay of the final preparation: ^ ^ is enough, it will be the above-mentioned active ingredient or the active ingredient alone, and the oral, or the addition of an appropriate carrier α added to the active ingredient. 'If the type and amount of the carrier used are such that the composition liquid containing non-dissolved state with: = knife can be prepared by freeze drying, the final freeze-dried composition satisfies the following ⑴ to (iii) Characteristics: (0 has a non-powdered morphology, (ii) the decay index is greater than 0.05, and ⑽ is subject to an air velocity of at least lm / sec and at least 17 ohms. The air impact of the working oxygen electrode 1 can be Those particles having an average particle diameter of 10 micrometers or less or an effective particle ratio of i0% or more and achieving the effects of the present invention are not particularly limited, and a carrier or a desired amount previously used for freeze-drying can be arbitrarily used. As the carrier, specifically, for example, hydrophobic amines such as valine, leucine, isoleucine, and phenylpropane, or their salts or amidines: glycine I, candied Hydrophilic amino acids, such as amino acids, alanine, arginine, amidine, or these salts or amidoamines; derivatives of amino acids; dipeptides having two or more of the above amino acids that are the same or different , Tripeptides, or their salts or amidines. 315314 29 200418520 They can be counted as 1 county. M, or a combination of two or more. Among them, it is used as amino acid or Katsuyuki Taito to go to J, and is listed as a salt of metal such as sodium and potassium and a metal of metal such as soil; it is formed with inorganic acids such as phosphoric acid and hydrochloric acid and organic acids such as sulfonic acid. The strength of the mouthfeel $,, ', as the amine listener, for example, L · _ white amine it amine hydrochloride. In addition, as a carrier, amino acids other than α-amino acids can be added. Examples of such hydrazines include cold-alanine, r-aminobutyric acid, homoserine, and taurine. . … • Furthermore, as other carriers, for example, monosaccharides such as glucose; disaccharides such as sucrose, maltose, lactose, and trehalose; sugar alcohols such as mannitol; saccharides such as cyclodextrin; dextran 40 and polysaccharides Polysaccharides such as triglucose; polyols such as polyethylene glycol; and sodium fatty acids such as sodium caprate. These carriers may be added singly or in combination of two or more kinds. Among them, the carrier that allows the effective ingredients to reach the lungs efficiently is specifically a hydrophobic amino acid such as isoleucine, valine, leucine, and phenylalanine, or their salts Or ammonium; hydrophobic dipeptides such as leukoamido-valine_acid, leukoamido-phenylalanine, and phenylpropylamine_isoleucine; and leukoamido_leucine Hydrophobic tripeptides such as amino_leucine, leukoamido_ leukoamido-valine, and the like. These may be added singly or in combination of two or more. In the case of interferon_r, from the standpoint of micronization and formulation stability, it is preferable to exclude the above-mentioned hydrophobic amino acid or its salt or amidine, hydrophobic monopeptide, and hydrophobic dipeptide. You can use basic amino acids or their salts or amidines, dipeptides, and triads in combination. Among them, those who test amino acids are, for example, arginine, lysine, histidine and their trips. Soil 卞 人 I Soil 315314 30 200418520 is a combination of benzyl alanine and arginine hydrochloride, a combination of phenylalanine, white and arginine hydrochloride. The content ratio of the active ingredient (drug) contained in the freeze-dried composition. Heat: Don't limit it. For example, the content is 20 mg or less, preferably 10 mg or less, and it is more preferably 2 mg or less, particularly preferably 1 mg or less. If the addition ratio of the above-mentioned carrier is to make the final cold-kang dry composition, the above characteristics of ⑴ to ㈣ are not particularly limited. Although there is no ^ section ratio, one criterion is when the cold-knitted composition is determined as When the content is 100% by weight, the ratio is preferably 0.1 to less than 1, preferably 10 to 100%, and less than 100% by weight, less than 100% by weight, and more preferably 0% by weight.勹 仫 仫 仫 20 to less than 100 'and the present invention as the object to describe the characteristics of ⑴ to 不会 and will not damage ==, and the product as long as it can meet the effectiveness of the composition liquid before drying' 'day The effect 'In order to stabilize the cold ling and prevent the active ingredient after drying and drying, this active ingredient is absorbed in various additives. For example, white and inorganic salts can be added to the above ingredients, and human serum albumin can include human serum albumin. If it is generally applicable to pharmaceuticals, as for surfactants, surfactants, cations, and active agents, regardless of the anionic boundary Can be widely used. For example, it is preferably a non-facial interfacial surfactant (such as Tween-type boundary 〃, ethylene-consuming sorbitan fatty acid ester-based interface active zibu ㈣), and non-ionic such as mountain sorbitol trioleate, etc. The method containing the active ingredients and any of the ingredients is not particularly limited. ——: The composition solution is freeze-dried to produce a freeze-dried preparation 315314 31 200418520 (: make the freeze-dried composition dry). . Although there are no restrictions, depending on the situation, the cooling bed can be quickly freeze-dried. The conditions can be urgent. The dry composition of the present invention can be formed into particles suitable for pulmonary administration by applying a blow. Therefore, Taiqiqiong " freeze-dried composition is suitable for preparation via pulmonary administration 1: for preparation before pulmonary administration of powder preparations on the second: cold health dry composition for preparation preparation). … Again: the cold health dry composition of the present invention includes the specific states disclosed below &, " Lung U Cold / East Dry Composition 'is a composition liquid that contains non-dissolved additives It is prepared by freeze-drying and has the following characteristics (1) to (iii): (i) it has a non-powdered morphology; (ii) its decay index is above 0.05; and (iii) borrows By being subjected to air impact with a working gas velocity of at least 1 / sec and an air flow rate of at least 17ml / sec, it can become fine particles with an average particle size of less than 10 microns or an effective particle ratio of more than 10%. 1 0 2 · As in item 1 ο 1 item, the composition is freeze-dried, and the decay index is 0.05 to 1.5. 1 03 · As described in Item 1 〇 ^ ~~ Fruit dry composition, in which the hunting force is subjected to the impact of air having a place of at least 2 m / sec, the speed of milk and the air flow of at least 17 ml / sec. It can become fine particles with flat average 4 haiku ten uniform grains below 10 microns or effective particle ratio above 10%. 315314 32 200418520 104 · Scenario 101 item / 々'Donggan without composition, in which, by withstanding the milk speed of the present chart and air of at least n mi / sec in the range of 1 to 300 m / sec The impact of the flow of air can form particles of Λ wind horse ten average grain branches below 10 microns or effective particle ratio of more than 10%. 1 0 5. As described in Item 10, there is no composition in Portugal and Jindonggan, in which, by withstanding * air freezing life of at least 1 m / sec, ^ working milk speed and air of at least 20 ml / sec The impact of flowing air can become fine particles with a weight average particle size of 10 microns or less or an effective particle ratio of 10% or more. 1 0 6 · As in Item 10, the composition of the Portuguese, human warfare, and human health composition, in which, by bearing a speed of at least 1 m / sec < working milk speed and at least 17 ml / sec Air pore punching with an air flow rate of up to 15 L / sec ^ can become fine particles with an average particle size of less than 10 microns or an effective particle ratio of more than 10%. 1 0 7 · As the appearance 1 〇 1 note Christine 丄 / shell. The already-laid freeze-dried composition can be made into particles with a thousand-average particle size below 5 microns or an effective particle ratio of 20% or more by withstanding the impact of air. It is a low-molecular-weight drug that contains 108. As described in the description of morphology, only < and freeze-dried composition of war. It contains high molecular weight drugs such as protein and nucleic acid, which are made as the effective ingredients of the 109 · item 1 〇 丨 record, the freeze-dried composition of Beyouji. It is a nucleic acid having a cold rolling dry composition as described in item 110 and item 109 as an active ingredient, which is maintained in a bulk state. It is a low-molecular-weight drug that contains Lengkang Dry Na, which is described in the above item, as an active ingredient, and a carrier. The carrier is at least one selected from amino acids, dipeptides, tripeptides, and sugars Group of people. 315314 33 200418520 112. The freeze-dried composition according to item 10, which contains high-molecular-weight drugs such as proteins and nucleic acids as active ingredients and a carrier, and the carrier is at least one species selected from amino acids. The group consisting of dipeptide, tripeptide and carbohydrate 0 113. The freeze-dried composition according to item m, which contains a low-molecular-weight drug as an active ingredient and a carrier, the carrier being at least one selected from hydrophobic A group consisting of amino acid, hydrophobic dipeptide and hydrophobic tripeptide. 114. The cold-dried dry composition according to item 112, which contains high-molecular-weight drugs such as proteins and nucleic acids as active ingredients and a carrier, and the carrier is at least one selected from hydrophobic amino acids, hydrophobic A group of sexual dipeptides and hydrophobic tripeptides. 115. The freeze-dried composition according to item 101, which is a water-soluble composition. 116. Cold as described in item 1G1; the dried composition contains the active ingredient in the last dose. 117. The composition for cold-drying as described in item 101 is prepared by freeze-drying a composition liquid containing an additive component in a non-dissolved state, and has the following characteristics (i) to (iii): (i) has Non-powdered morphology; (ii) a decay index of 0.05 to 1.5; and (iii) by being able to withstand air speeds in the range of 1 to 300 m / sec and airspace of 17 ml / sec to 15 L / sec The impact of the two lice in the & geogrinding can become fine particles with an average particle size of less than 10 microns or an effective particle ratio of more than 10%. 118. The cold-kang dry composition as described in item 117, 1 * 315314 34 200418520 The gas velocity is 1 to 250 m / sec. • The freeze-dried composition according to item 11 in item 17, wherein the gas flow rate is 20 ml / se (^ 101). Wang (2) Manufacturing method of dry powder for pulmonary administration * Preparation, Humans, humans, and humans are concerned with the production of a dry particle having a particle size suitable for " lung branches by pulverizing a cold-killed dry composition contained in a non-powder state in the inside of the container into the container. Method for powder preparation (dry powder for pulmonary administration). This method can be implemented by containing a non-powdered state in a container: freeze-drying the composition by applying a specific air impact. /,-And σ Manufacture of dry powder preparation for pulmonary administration described in this description = to 'the planting solution containing non-dissolved added ingredients as detailed in the above paragraph is cold-dried and prepared to have a G.G5 or higher decay index Invented non-powdered, cold; East dried the composition, and then imparted an air impact with an air flow of at least i 'two speeds and 17 mi / sec to the evening, so that the non-powdered cold; The dry composition is prepared to have an average particle size of 0 μm or less (preferably 5 μm or less) ) Or a dry powder preparation in the form of particles with an effective particle ratio of 10% or more (preferably 20% or more, more preferably 2S% or more, and more preferably 300 /. 乂 上 '特 佳 35. or more). In addition, the average particle diameter of the microparticles in the present invention means an average particle diameter generally used in the inhaler-related industry, and specifically, it is not a geometric particle diameter, but refers to the average particle diameter of aerodynamics. Diameter (MMad). The average particle size of aerodynamics can be obtained by conventional methods. Specifically: The average particle size of aerodynamics, for example, with an artificial lung air respirator: 315314 35 200418520

式粒度分佈計(美國Amberst Process Instrument,Inc·公司 製)、二段式塵埃測定器(G.W. Hallworth and D.GParticle size distribution meter (Amberst Process Instrument, Inc., USA), two-stage dust meter (G.W. Hallworth and D.G.

Westmoreland: J· pharm· Pharmacol·,39,966-972 (1972), 美國專利公報第6 1 5 3 2 2 4號)、多段硬式塵埃測定器、大理 石磨衝擊為、安德森多段衝擊器等測定。又,B. Olsson等 人報口卩返著空氣力學之平均粒徑在5 // m以下之粒子之比 率增加,對肺之輸送增加(B· 〇lss〇n et a][: Respirat〇ry Di,吨Westmoreland: J. Pharm. Pharmacol., 39, 966-972 (1972), U.S. Patent Publication No. 6 1 5 3 2 2 4), multi-stage hard dust tester, Dali stone mill impact test, Anderson multi-stage impactor, etc. In addition, B. Olsson et al. Reported that the ratio of particles with an average aerodynamic diameter below 5 // m increased, and the transport to the lungs increased (B · 〇lss〇n et a] [: Respirat〇ry Di, tons

DellVeiy V,273_281 (1996)。像這樣推定可輸送至肺之量 之方法,例如為用乾式粒度分佈計、二段式塵埃測定器、 多&硬式塵埃測定器、大理石磨衝擊器或安德森多段衝擊 器等測定所得之有效粒子比率及細粒量等。 、、發明之製造方法,較佳係藉由將包含非溶解狀態之 丄成Si::成液收容於容器中,藉由在該狀態冷凍乾燥 a ~凍乾燥組成物,繼而藉著將空氣導入收容該 組成物之容器内, 斜 〆Dell Veiy V, 273_281 (1996). A method for estimating the amount that can be delivered to the lungs in this way is, for example, effective particle size measured by a dry particle size distribution meter, a two-stage dust tester, a multiple & hard dust tester, a marble mill impactor or an Anderson multi-stage impactor Ratio and fines. The manufacturing method of the invention is preferably by containing the insoluble Si :: forming solution in a container, freeze-drying a ~ freeze-dried composition in this state, and then introducing air by Inside the container containing the composition, obliquely

衝丨於“凌乾燥組成物賦與上述空氣 衝擎而貫施。方兮卜主 Tki 可利用… 月 由於乾燥處理及粉末製劑化處理 =用:-谷器實因此不會因分成小份 失及污染之問體。 厅°月才貝 對於將上述空氣衝擊賦盥於人 段,雖益特別限制Y ά 一 '述々凍乾燥組成物之手 床…%另J限制,但較佳係使用、 粉末吸入裝置。 ()中說明之乾燥 本發明之經肺投與用乾制 為,使用經肺投盘用…刀衣知之袅造方法之一特徵 時),可以將收4 ㈣劑之患者於自行使用時(吸入 4 了以將收谷於容器令 及入 钇秌組成物調製成適於經 315314 36 200418520 肺投與之粒徑之粉末製劑。 又,本發明之經肺投與用乾燥 含下文揭#之具體態# : ,衣^之製造方法包 2〇 1 ·經肺投與用乾燥粉製,制生 包含右韭、〜妒社处々、夭4丄^ 衣k方法’該製劑係將 成,且呈之、,且成液經冷滚乾燥調製而 容器中: 注之冷凍乾燥組成物收容於 ⑴具有非粉末之塊狀形態, (ii)衰變指數為〇·〇5至1.5,以及 (m)藉由承受具有至少im/sec之 ★…产 乱迷度及至少17ml/sec 之空氣流量之空氣衝擊,可成兔 , 』成為千均粒徑在10微米以 或有效粒子比率在丨0%以上之微粒; 藉由使用對於上述容器内之入 , ~,東乾燥組成物可賦與上 述空氣衝擊之裝置,將具有該办 、另邊工虱衝擊之空氣導入,· 藉此將上述冷凍乾燥組成物 w初该粒化成平均粒徑在1 〇 被米以下或有效粒子比率在10%以上。 生202.如態樣201項記載之經肺投與用乾燥粉製劑之製 以方法,其中,收容於容器内之冷凌乾燥組成物含有卜欠 投與量之有效成分。 2 0 3 ·如態樣2 0 1項記葡之奴< 疏4 貝忒戟之經肺投與用乾燥粉末製劑之 製造方法,其中,調製成之料# J衣风怠U粒之千均粒徑在5微米以下 或有效粒子比率在20%以上。 制、2G4.如態樣201項記載之經肺投與用乾燥粉末製劑之 衣l方法《中’ 4冷;東乾燥組成物之衰變指數在⑴至 315314 37 200418520 1 · 5之範圍内。 205.如態樣2G1項記载之經 製造方法,其t,該冷滚乾燥組成物包末製劑之 低分子藥物。 U為有效成分之 2 0 6.如悲樣2 〇 1項記恭 制 、載之經肺投與用乾烽+八士制十丨 製造方法,其中,該冷凌i λ 钇秌粉末製劑之 蛋白質類及核酸等高分子藥物。 :、、、有效成分之 2〇7·如態樣201項記載之 製造方法,直中,兮、入$弘 一用乾無粉末製劑之 力宏”干δ亥冷凍乾燥組成物 呈保持於保持體狀態之核酸。 為有效成分之 208. 如態樣2G5項記載之 製造方法,其中,該冷;東乾焊,且成物粉末製劑之 低分子藥物以及載劑,該載劑為至少:種效:分之 肽、三肽及糖類組成之群者。 ""胺基酸、一 209. 如態樣2G6項記載之 製造方法,豆中,^、入# 又^用乾垛粉末製劑之 、中5亥冷凍乾燥組成物含有做Rinse and apply in the "Ling dry composition given the above-mentioned air flushing engine. Fang Xibu master Tki can use ... Month due to drying treatment and powder preparation treatment = use:-cereal device so it will not be lost due to small portions. The problem of pollution and contamination. Hall ° Because the above-mentioned air impact is given to humans, although it is particularly restricted, it is recommended that the hand-drying composition of the freeze-dried composition ...% is also limited, but it is preferably used. (Powder inhalation device.) The drying method described in () for the pulmonary administration of the present invention is to use the method of using the pulmonary discs (a feature of the manufacturing method known as knife clothing), and the patient receiving 4 tinctures At the time of self-use (inhalation 4 is used to prepare the grains in a container and the yttrium-yttrium composition is prepared into a powder preparation having a particle size suitable for lung administration by 315314 36 200418520. In addition, the invention is dried for lung administration Contains the following disclosure # 的 specific state # :, the manufacturing method of the clothes ^ 001 · made by using dry powder for pulmonary administration, the production method includes the right lee, ~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~ The preparation is prepared, and it is, and the prepared liquid is prepared by cold rolling and drying in a container: The freeze-dried composition is contained in a non-powdered morphology, (ii) the decay index is from 0.05 to 1.5, and (m) by withstanding at least im / sec ★ ... promiscuous degree and at least 17ml The air impact of air flow per second can become a rabbit, and it becomes a particle with a thousand-average particle size of 10 microns or an effective particle ratio of more than 0%. By using the above composition, The object can be applied to the above-mentioned air impact device, and the air having the impact of the lice on the other side is introduced, so that the freeze-dried composition can be granulated to an average particle size of less than 10 meters or effective particles. The ratio is above 10%. Health 202. The method for preparing a dry powder preparation for pulmonary administration as described in item 201, wherein the cold-dried dry composition contained in the container contains an active ingredient in an insufficient amount. 2 0 3 · As in the case of item 201, a method for manufacturing a dry powder preparation for the administration of Pulmonaria pulcherrima by pulmonary administration, wherein the prepared material # J 衣 风 闲 U 粒 的Thousand average particle size is less than 5 microns or the effective particle ratio is more than 20%. System, 2G4. As described in item 201, the method for drying powder preparations for pulmonary administration by the method "Medium '4 cold; the decay index of the east dry composition is in the range of ⑴ to 315314 37 200418520 1 · 5. 205. Such a state According to the manufacturing method described in item 2G1, t, the low-molecular-weight drug of the cold-rolled and dried composition package preparation. U is the active ingredient 2 0 6. As described in the sad article 2 01, it is made by the lungs. Dosage for administration + Yashiba ten 丨 Manufacturing method, wherein the cold Ling i λ yttrium ytterbium powder preparation is a protein and a nucleic acid polymer drug. 207, the active ingredient 207, such as aspect 201 According to the manufacturing method described in the above item, Li Zhonghong, Li Hongyi uses dry powder-free formulations of Lihong "Dry Delta Hai freeze-dried composition is a nucleic acid maintained in a retainer state. The active ingredient is 208. The manufacturing method described in item 2G5, wherein the cold; dry welding, and low-molecular-weight drugs of the powder preparation and the carrier, the carrier is at least: seed effect: fraction of peptide , Tripeptides and carbohydrates. " " Amino acid, a 209. The manufacturing method described in item 2G6, in the bean, ^, 入 # and ^ using the dry stack powder preparation of the, lyophilized composition containing

蛋白質類及核酸等高分子藥物以及載劑,W 種選自胺基酸、二肽、m播… 4刮為至少- 一肽及糖類組成之群者。 2 1 0 ·如態樣 2 0 8 Jp 蕾—a » 製迭方、本ιφ *…载肺投與用乾燥粉末製劑之 二° / 冷凍乾燥組成物含有做為有效成分之 低分子藥物以及載劑,該#丨 酸详μ “少一種選自疏水性胺基 、^水性一肽及疏水性三肽組成之群者。 211.如態樣209項記載之肺 製造方法,其巾m ^^粉末製劑之 札“組成物含有做為有效成分之 315314 38 200418520 蛋白質類及核酸等高分子藥物以及載劑,該載劑為至小 :選自疏水性胺基酸、疏水性二肽及疏水性三肽組成:鮮 212.如態樣201項記載之經肺投與用乾燥粉末製k 製造方法’其中,該冷;東乾燥組成物為水溶性叙成物月 213·如態樣加項記載之經肺投與用乾燥粉 製造方法,係在容量為〇 2至so 1 π d之 勹」至50刎之容器内 組成物微粒化之方法。 7 H @ 2 1 4 ·如態樣2 0 1項記載之奴始 „ 戰之紅肺投與用乾燥粉末製劑之 製造方法,其中,藉由使用具有 J之 成物賦與具有至少2 m/sec之空氣速 乾無、、且 工孔逑度及至少l7ml/ 空氣流量之空氣產生衝擊之手段 之 手〈于奴之I置,並將具備 衝擊之空氣導入收容冷凍 二虱 果钇々卞組成物之容器而進行。 2 1 5 ·如態樣2 0 1項$恭々γ叫 ^ ^ …载之經肺投與用乾燥粉末萝判 之製造方法,*中’藉由使用具有可對容器内之冷= 組成物賦與具有1至3_〜空氣速度及至少17= 之空氣流量之空氣產生衝擊之 sec 』于又 &lt; 忒置,亚將具備兮处 氣衝擊之空氣導入收容冷凍乾 脊忒二 ▽果钇‘組成物之容器而進 216·如態樣201項印哉+ γ 之μ 肺投㈣㈣粉末製劑 “方法,其中,猎由.使用具有可對容器内之 組成物賦與具有至少i m/s 乾秌 乂〜 工耽迷度及至少20 11ι1/ςρρ 之二氣流量之空氣產生衝擊之 、, 氣衝擊之空氣導入收容、… 衣置,亚將具備該空 虱涂收今冷凍乾燥組成物之容器而進行。 2 1 7 ·如態樣2 0 1項記恭&gt; 貝己载之經肺投與用乾燥粉末製劑 315314 39 200418520 之製造方法,其中,藉由使用具有可對容器内之冷凍乾燥 組成物賦與具有至少lm/sec之空氣速度及17ml/sec至 WL/sec之空氣流量之空氣產生衝擊之手段之装置,並將具 備該空氣衝擊之空氣導人收容冷;東乾燥組成物之容器而進 行0 2 18.如悲樣201項記載之經肺投與用乾燥粉末製劑之 製造方法’其中,使用後述(3)乾燥粉末吸入裝置中‘載之 態樣3〇1或302項之乾燥粉末吸入裝置做為裝置,將冷 乾燥組成物微粒化。 … 制、:如=218項記載之經肺投與用乾燥粉末製劑之 心方法,其中’使用乾燥粉末吸入裝置後述⑺ 載之態樣309項之乾燥粉末吸入裝置做 : 燥組成物微粒化。 时~ /東乾 ι/ο.如« 218項記載之經肺投與用乾燥粉末 衣k方法,係使用後述(3)章乾燥粉末吸入 — 之態樣3G1項之乾燥粉末吸入用裝置將Μ㈣m己載 粒化之乾燥粉末製劑之製造方法,直 1钇坧、、且成物微 之每次空氣喷射量為5 i 100 ml。 4 I置對容器内 21如態樣218項記載之經肺投與w 製造方法’係使用後述(3)章之乾燥粉末吸入&quot;衣劑之 態樣302項之乾燥粉末吸入裝置將冷 、、中§己栽之 之乾燥粉末製劑之製造方法, 、、且成物Μ粒化 流量為5至30〇L/min。 口之空氣 222+如態樣201項記載之經肺投與用乾燥粉末製劑之 315314 40 200418520 衣造方法’包含將為非溶解狀怨之添加成分之組成液經冷 束乾燥調製而成之具有下述⑴至(π〇之特性之冷康乾燥: 成物收容於容器中: ⑴具有非粉末之塊狀形態, 氣速度及17 ml/sec ⑴)具有0.05至1.5之衰變指數,以及 (iii)藉由承受具有1至300 m/sec之空 至15L/sec之空氣流量之空氣衝擊, J手 可成為平均粒徑 在10微米以下或有效粒子比率在1〇%以上之微粒; 藉由使用對於上述容器内之冷凍乾燁έΒ 士 n丄t γ +祀知組成物可賦與上 述空氣衝擊之裝置,並將具有該空氣衝擊之空氣導入; 藉此使上述冷凍乾燥組成物形成平均粒徑在1〇微米 以下或有效粒子比率在1 〇%以上之微粒。 告223.如態樣222項記載之經肺投與用乾燥粉末製劑之 製造方法,其巾,收容於容器内之冷凍乾燥組成物含有i 次投與量之有效成分。 224.如態樣222項記載之經肺投與用乾燥粉末製劑之 製造方法,其中,空氣速度為1至25〇 。 ,225·如恶樣222項記載之經肺投與用乾燥粉末製劑之 製造方法,其中,空氣流量為2〇 ml/sec至。 (3)乾燥粉末吸入裝置 製造上述本發明之經肺投與用乾燥粉末製劑時適合 使用之乾燥粉末吸人裝置’係不僅可將以非粉末狀態收容 於容器内之冷凍乾燥製劑(冷凍乾燥組成物)在該容器内微 315314 200418520 粒化,且該經微粒化之乾燥粉末製劑 个衣^亦可供使用者吸入服 用之裝置。該裝置藉由具備(1)對於非 ,^ ) 了万、非粉末狀之冷凍乾燥組 二物可賦與能將其微粒化之空氣衝擊之手段,以及⑺可將 ,微粒化之粉末狀冷涞乾燥組成物藉由吸入投與至使用者 mu㈣f施冷;東㈣組成物之微粒化 之吸入投與二者。又,上述(1)之 者 ι J之予奴亦可謂「將具備上述 工氣衝擊之空氣導入收容冷康乾燥組成物之容器内手 段」。又,上述⑺之手段亦可謂「將在容器内經微粒化之 =劑從容器中排出之手段」。在本發明中,若為具備此 、奴者,將可使用先财公知者或未來開發者中之任一裳 置。 ^ 、⑴之手段,具體而言,藉由將可對收容於容器内之冷 凍乾燥組成物賦與上述空氣衝擊之空氣導入該容器之手段 而貝現。又’该(1)之手段可為將具有至少丨m/see之空氣 速度及至少17ml/sec之空氣流量之空氣衝擊賦與容器内 之冷凌乾I组成物之手段。藉由⑺之手段或經由該手段, 可將調製成適於經肺投與之形態之乾燥粉末製劑吸入投與 :患者等使用者。X,可將⑺之手段例如工作室及流路:、 設計成組成物可進一步微粒化或分散。 。該乾燥粉末吸入裝置包含在下述(a)中揭示之喷射型 乾媒粉末吸人裝置,以及在(b)中揭示之自己吸人型乾燥粉 末吸入裝置。 喷射型裝置(active powder inhaler) (a-i)乾燥粉末吸入裝置,其係將以非粉末狀態收容於 315314 42 200418520 並供吸入用之裝置,其具 容器中之冷凍乾燥組成物微粒化 備·· 有空氣嘴射流路之針部, 士 百排出/瓜路之針部,在上述 ’’十口P之空氣噴射流路中輸送 j &lt;工矾用之空虱壓送手段,以及 與該排出流路連通之吸入口 ; 且構成為: 上述針部扎入供密封上述容器之口栓並將空氣喷射流 :及排f流路與上述容器内部連通,#由上述空氣壓送手 段使空,從上述空氣喷射流路噴射於上述容器β,藉由該 貪射工氣之衝擊使上述冷康乾燥組成物 粒經由上述排出流路從吸人口排出。 (a-2)如(α_υ記載之乾燥粉末吸入裝置,其中,上述空 氣I达手段為手動式,其具備設有吸入閥之吸進口及設有 =出閥之吐出口之風箱體,且構成為在關閉吸進閥之狀 〜藉由壓縮忒風箱體並開放吐出閥,可將上述風箱體内 之空氣經由連通於吐出口之針部之空氣噴射流路壓送至容 為内,在關閉上述吐出閥及打開吸進閥之狀態,藉由彈性 復原力使上述風箱體擴張,及將空氣導入風箱體内。 (a 3)如上述(a_i)或(a-2)記載之乾燥粉末吸入裝置,其 中’將上述空氣喷射流路及上述排出流路形成在一根針部 中0 (b)自己吸入型裝置(passive p〇wder inhaler) (b-1)乾燥粉末吸入裝置,係將以非粉末狀態收容於容 裔中之冷凍乾燥組成物微粒化並供吸入用之裝置,其具 43 315314 200418520 備: /、啕及引&amp;路之針部,具有空氣導入流路之針部以及 與上述吸引流路連通之吸入口; 且構成為: 在上述針部礼入供密封上述容器之口检之狀態 使用者之吸氣壓從上述吸入口吸入上述容器内之空氣; 時使空氣經由上述空氣導入流路流入已成為負 — 内,f由流人之空氣之衝擊將上述冷純燥組:物= 化,付到之微粒經由上述吸引流路從吸入口排出。广 (2)士(b 1 ) D己載之乾燥粉末吸入 使用者之一次吸入,將上诚、人&amp; 係構成為糟由 肝上述冷凍乾燥組成物 化並從吸入口排出β 人^分微粒 (b-3)如(b-1)或(b_2)記載之乾燥粉末吸 述吸引流路及上述空U邕 &amp;置,其將上 义工虱^入流路形成在一 將空氣導入容器内之手 、十4中。 常壓下可從外部導入空氣之^ &amp; ,L(1)之手段)’係只要在 等之壓縮空氣。又,Si卜部導二?無:特別使用噴射磨 例如上述喷射型乾燥粉二札之手段無特別限制, 1刀木吸入裝置軎 地將外部空氣喷射導 ',可以採用人為 π八奋态内之手與· q 乾燥粉末吸入裝置之彳主 Μ 自己吸入型之 月况’错由使用各+ 之容器内負壓化,可以採用將 “ D人服用所伴隨Proteins, nucleic acids and other high-molecular drugs and carriers, W are selected from amino acids, dipeptides, m… ... 4 is a group consisting of at least one peptide and carbohydrates. 2 1 0 · Like appearance 2 0 8 Jp lei—a »Preparation of formula, Ben ι φ * ... 2nd dry powder preparation for pulmonary administration ° / Freeze-dried composition contains low-molecular-weight drugs as active ingredients and Agent, the # 丨 酸 Detail μ "less one selected from the group consisting of a hydrophobic amine group, an aqueous monopeptide and a hydrophobic tripeptide. 211. The method for producing a lung according to item 209, the towel m ^^ The powder formulation contains "315314 38 200418520 as an active ingredient, high molecular drugs such as proteins and nucleic acids, and a carrier, the carrier is small: selected from hydrophobic amino acids, hydrophobic dipeptides and hydrophobic Tri-peptide composition: Fresh 212. Manufacturing method of dry powder for pulmonary administration via pulmonary administration as described in item 201, wherein the cold; east-dried composition is a water-soluble compound, as described in item 213. The method for producing dry powder for pulmonary administration is a method of micronizing the composition in a container having a capacity of 0 to 50 Å to 50 Å so 1 π d. 7 H @ 2 1 4 · The manufacturing method of the dry powder preparation for the administration of red lungs of war, as described in Item 2 01 of the aspect, wherein a product having a minimum of 2 m / The air of sec is quick-drying, and the hole diameter and the air of at least 17ml / air flow are the means of impact. <I place it in the slave, and the air with the impact is introduced into the refrigerated diode fruit yttrium. 2 1 5 · As the appearance of the item 2 0 $ 1 々 叫 called ^ ^… contained in the manufacturing method of dry powder for pulmonary administration, the method of * zhong 'can be used by the container The cold inside = the composition imparts the impact of air with an air velocity of 1 to 3_ ~ and an air flow rate of at least 17 = sec ”于 & 忒, the air with the air impact is introduced into the containment freeze-dried ridge忒 二 ▽ Fruit yttrium 'composition into the container 216 · As the state 201 item seal + γ μ lung injection ㈣㈣ powder preparation "method, in which the hunting. The use of the composition in the container can be provided with At least im / s dryness ~ work delay and at least 20 11ι1 / ςρρ ,, impact of the gas shock generating gas introducing air storage, home clothes ..., the sub-blank will have received this lice coating composition of the freeze-dried composition of the container is performed. 2 1 7 · As in aspect 2 01, respectfully, a method for producing Beijizai's dry powder preparation for pulmonary administration 315314 39 200418520, wherein a freeze-dried composition in a container can be used by using the method Means for generating impact with air having an air velocity of at least lm / sec and an air flow rate of 17ml / sec to WL / sec, and guiding the air provided with the air impact to a cold storage container; 0 2 18. The method for producing a dry powder preparation for pulmonary administration as described in item 201, wherein the dry powder inhalation of item 301 or 302 as described in (3) Dry powder inhalation device described later is used. The device was used as a device to atomize the cold-dried composition. … Preparation: If the method described in item 218 of the dry powder preparation for pulmonary administration is described in the following, ‘the dry powder inhalation device of item 309 described below is used as the dry powder inhalation device, and the dry composition is micronized.时 ~ / 东 乾 ι / ο. As described in «218, dry powder coating for pulmonary administration using the method described below, using the dry powder inhalation method described in Chapter (3) below-the 3G1 dry powder inhalation device will be used for The manufacturing method of the granulated dry powder preparation is 1 yttrium europium, and the amount of air spray per product is 5 i 100 ml. 4 I placed in the container 21 The method of pulmonary administration w as described in item 218 of the manufacturing method is to use the dry powder inhalation device of the dry powder inhalation method of item 302 in the (3) section described below to draw cold, The production method of the dried powder preparation that has been planted in the above §, and the granulation flow rate of the product M is 5 to 300 L / min. Mouth air 222 + Dry powder preparation for pulmonary administration as described in item 201 315314 40 200418520 Clothing manufacturing method 'Contains the composition solution of the non-dissolved additive ingredients by cold beam drying and preparation The following ⑴ to (cold dryness of π〇: the product is contained in a container: ⑴ has a non-powder morphology, gas velocity and 17 ml / sec ⑴) has a decay index of 0.05 to 1.5, and (iii ) By withstanding the air impact with air flow from 1 to 300 m / sec to 15 L / sec, J hand can become particles with an average particle size of 10 microns or less or an effective particle ratio of 10% or more; by using It is known that the freeze-dried material 丄 n 丄 t γ + in the container can be applied to the air impact device, and the air having the air impact is introduced; thereby, the freeze-dried composition has an average particle size. Particles below 10 microns or effective particle ratio above 10%. Report 223. The method for producing a dry powder preparation for pulmonary administration as described in item 222, wherein the freeze-dried composition of the towel and the container is contained in the container in an amount of i dose of the active ingredient. 224. The method for producing a dry powder preparation for pulmonary administration according to item 222, wherein the air velocity is 1 to 25 °. 225. The method for producing a dry powder preparation for pulmonary administration according to item 222, wherein the air flow rate is 20 ml / sec. (3) Dry powder inhalation device The dry powder inhalation device suitable for the production of the dry powder preparation for pulmonary administration of the present invention is not only a freeze-dried preparation (freeze-dried composition) that can be stored in a container in a non-powder state. Material) in the container are 315314 200418520 granulated, and the micronized dry powder preparation is also a device for users to inhale. The device is equipped with (1) non-powdered, non-powdered freeze-dried components that can impart the impact of air that can be atomized, and can cool the micronized powder.涞 The dry composition is administered to the user mu 施 f by inhalation to cool; the micronized composition of the dong ㈣ composition is administered to both. In addition, the slave of J in the above (1) can also be referred to as "the method of introducing the air with the impact of the industrial gas into the container containing the cold and dry composition". In addition, the above-mentioned method of tadpoles can also be referred to as "means for discharging a micronized agent in a container from a container". In the present invention, if there is such a slave, it is possible to use any one of the fortune-tellers or future developers. ^ And ⑴ means, specifically, means by introducing into the container the air which can impinge the above-mentioned air impact on the lyophilized composition contained in the container. The method of (1) may be a method of imparting an air impact having an air velocity of at least 1 m / see and an air flow rate of at least 17 ml / sec to the cold-dried dry I composition in the container. The dry powder preparation prepared into a form suitable for pulmonary administration can be inhaled and administered to a user such as a patient by or through this method. X. It is possible to design a method such as a working room and a flow path :, the composition can be further micronized or dispersed. . The dry powder inhalation device includes a spray type dry medium powder inhalation device disclosed in (a) below, and a self-inhalation type dry powder inhalation device disclosed in (b). Active powder inhaler (ai) dry powder inhalation device, which is a device for inhalation in a non-powdered state in 315314 42 200418520, and has a freeze-dried composition in a container. The needle part of the air nozzle jet flow path, the needle ejection / melon needle part, conveying j &lt; air lice pressure feeding means for industrial aluminum in the air jet flow path of the above ten ports, and And the suction port is connected with the road; and the structure is: the needle portion is inserted into the mouth plug for sealing the container and the air jet flow is communicated with the inside of the container; The air jet flow path is sprayed onto the container β, and the cold and dry composition particles are discharged from the suction population through the discharge flow path by the impact of the spitting working gas. (a-2) The dry powder inhalation device described in (α_υ), wherein the above-mentioned means of air I is a manual type, which has a suction inlet provided with a suction valve and a wind box provided with a spout outlet of a valve; and It is configured to close the suction valve ~ By compressing the air box and opening the discharge valve, the air in the air box can be pressure-fed to the inside through the air jet flow path of the needle part connected to the discharge port. When the discharge valve is closed and the suction valve is opened, the air box is expanded by the elastic restoring force, and air is introduced into the air box. (A 3) As described in (a_i) or (a-2) above The dry powder inhalation device according to the description, wherein the air jet flow path and the discharge flow path are formed in one needle part. 0 (b) Self-inhalation type device (passive p0wder inhaler) (b-1) Dry powder inhalation The device is a device for micronizing the freeze-dried composition contained in a non-powdered state and for inhalation. The device has 43 315314 200418520. The needle part of the road and the suction port communicating with the suction flow path; And the structure is: in the state where the needle portion is provided for the oral inspection of the sealed container, the user's suction pressure sucks the air in the container from the suction port; when the air flows in through the air introduction flow path, it becomes negative , F The above-mentioned cold and dry group is changed by the impact of the flowing air. The particles paid are discharged from the suction port through the above-mentioned suction flow path. (2) ± (b 1) D dry powder inhaled Once inhaled by the user, the Shangcheng, human &amp; system is constituted by the above-mentioned freeze-dried composition of the liver, and β-human particles (b-3) are described in (b-1) or (b_2) from the inhalation port. The dry powder absorbs the suction flow path and the above-mentioned empty U 邕 &amp; device, which forms the upper volunteer lice into the flow path in a hand that introduces air into the container, ten 4. Under normal pressure, air can be introduced from the outside ^ &amp;, L (1) means) 'means just waiting for compressed air. Also, Si Bu Budao 2? None: There are no special restrictions on the use of jet mills, such as the above-mentioned spray-type dry powder. The 1-knife inhalation device squirts out the external air, and can use artificial π eight-strength hand and q dry powder to inhale. The main condition of the device is the self-inhalation type of the month, which is caused by the negative pressure in the container of each +.

器内之手段。又,A二土 °工氣自然地吸引導· λ A 于奴又在別者噴射型乾 及,¥入容 將外部空氣人為地噴射 末吸入裝置之情況, 可為使用任意之機械自動進一 之方法,可為手動,亦 仃之方法。 315314 44 200418520 Θ白本發明所使用之乾㈣末吸人裝置,無論是喷射型還 是自己吸入型,均可益士m, ^ 六1 k 了猎由用上述空氣導入(流入)手段導入 谷态内之外部空痛嘉&amp; 哭肉“礼產生之衝擊,將以非粉末狀態、收容於容 °。内之々凍乾燥製劑微粒化。 對於:-關方、其中所使用之容器,只要可供冷凍乾燥者, m Λ ㈣將無㈣限制。舉例言之,就材質而言, :如=聚乙_、聚丙稀及聚苯乙稀等聚稀烴系為主二 恥,玻璃及鋁等。又,就來抑品丄 β王之塑 狀、:角柱狀而…列如可為圓筒狀、杯 角柱(二角錐)、正方柱(正方錐)、六 八角柱(八角錐)等多角柱(多角錐)。 角、隹)、 成你為了可以效率良好地得到該效果,就收容冷凍m 成物之容器之容量言之,可以 ”東乾燦組 ^丨為較佳’以^^丨為. ml’以〇·2至 徑)言之中使用” ,就容器之筒經(内 功主使用0 2至1〇〇 mm, 佳,以2至50_為更佳。 至75㈣為較 又,收容於該容器内之冷凍乾燥袓成物之θ 包含單位投與量(1 ^旦、卞叙 成物之!’較佳為 投鱼旦士 扠與里)或數次(具體而言2至3 A、 杈舁里之有效成分之量。更佳A 至3次) 量)之有效成八夕曰 包含早位投與量U次投盥 3欢烕分之量。又,冷凍齡护 似一、 洗乾燥組成物所包含之有攻成八之具體量’視冷 為從可吸入量中二種類及添加量而異,若 以下,較佳為20擇者,將無特別限定,通常為3〇mg 以下。為〇叫以下’更佳為1〇叫以下,特佳為^ 又,藉由導入容器内之外部空氣所產生之空氣衝擊, 315314 45 200418520 係由至少人類1次或數次 之空氣流量及其所產生之:::::!成,流入容器内 器之耐久性之限度内,導 疋导然,只要在容 ^ v入之外部办今如 及空氣速度超過上述者並未受到^具有之空氣流量 之空氣流量通常為5至300L/分, j人類1次吸入 分。又,在噴射型之鈔枵4、士 D 、,'田舌之為10至200 L/ 1次空氣之啫射晉盔&lt; r κ〖月况,可以使用 工孔I赁射里為5至J 〇〇 ml 者。較件士用敕^ 父心^為1 Θ至5 0 m 1 季又佺凋整成對於充填於容器内 表面造成相當於至少lm/ 々凍乾燥組成物之 田 夕1 m/sec之空翕诘疮立 擊。更佳之空氣衝擊為至少2m/s ^度產生之空氣衝 朝偷躲既击处 WseC之空氣速度產生之空 乳衝擊,再更佳至少5 m/see it ^ P ^ „ I 1 η 工巩連度產生之空氣衝擊, 逖要更彳土至少1 〇 m/sec之空痛 乱逮度產生之空氣衝擊。其中Inside the device. In addition, the working air of A two degrees ° naturally attracts the guide. Λ A Yu Nu is sprayed by others and the air-injection of the external air into the device artificially can be done automatically by using any machine. The method can be manual or not. 315314 44 200418520 ΘWhite The dry end suction device used in the present invention, whether it is a spray type or a self-inhalation type, can be used for m, ^ 6 1k The hunting is introduced into the valley state by the above-mentioned air introduction (inflow) means. Inside and outside the empty pain Jia & Crying Meat "The impact of the ceremony will be stored in a non-powdered state. The lyophilized preparation inside will be micronized. For:-Guan Fang, the container used in it, as long as it can For freeze-drying, m Λ ㈣ will have no limit. For example, as far as the material is concerned, such as: Polyethylene, Polypropylene, Polystyrene, etc. Polyolefins are the main two, as well as glass and aluminum. . Also, let's suppress the shape of β King's plastic shape: angular column and ... columns can be cylindrical, cup corner column (diagonal pyramid), square column (square pyramid), six-octagonal column (octagonal pyramid), etc. Polygonal column (polygonal cone). In order to obtain this effect efficiently, the capacity of the container containing the frozen m product can be said as "Donggancan group ^ 丨 is better" to ^ ^ 丨 is. Ml 'to use in the language of 0.2. ”, The tube of the container (the internal power master uses 0 2 It is better to 100mm, and more preferably 2 to 50mm. To 75mm is more, the θ of the freeze-dried product contained in the container includes the unit administration amount (1 旦, the product of the product! 'Preferably, it is the amount of the active ingredient in the fish fork and fork) or several times (specifically, 2 to 3 A, the amount of the active ingredient in the branch. More preferably, A to 3 times). The amount administered is 3 times as much as the amount of the U-throw. Also, the freezing age protection is the same as that of the washing and drying composition, which has a specific amount of 8%. The amount varies, but if it is below, it is preferably 20, but it is not particularly limited, but it is usually 30 mg or less. It is less than or equal to 0, more preferably less than or equal to 10, and particularly preferably ^. The air impact generated by the external air, 315314 45 200418520 is caused by at least one or several times the air flow of human beings and its generated :::::!, Into the container within the limit of the durability of the container, As a matter of fact, as long as the air flow is outside the capacity and the air speed exceeds the above, the air flow is not affected by the air flow It is usually 5 to 300 L / min, j human inhalation once. In addition, in the jet type banknote 4, 士 D ,, 'Tian Tong Zhi is 10 to 200 L / 1 time of air shot Jin helmet &lt; r κ 〖Monthly condition, you can use the hole I rent in the range of 5 to J 〇ml. For the person who uses it, 敕 ^ Father's heart ^ is 1 Θ to 50 m 1 The season is again filled and filled into the container The surface causes an air scab that is equivalent to at least 1 m / sec of Tian Xi at least 1 lm / 々 of freeze-dried composition. A better air impact is at least 2 m / s. The air generated is rushed towards the WseC where it was hiding. The air impact caused by air velocity is better at least 5 m / see it ^ P ^ „I 1 η The air impact produced by the industrial continuity should be more than the air pain caused by air at least 10 m / sec. Air impact. among them

關於空氣衝擊之上限,則I 、…、知' 別限制,例如為300 m/sec 之空氣速度產生之衝擊。關於兮 #關於5亥上限,較佳為250 m/sec 之工孔速度產生之空氣衝擊,更佳為2〇〇 之空氣速 度產生之空氣衝擊,特佳為150 m/sec之空氣速度產生之 空氣衝擊。 空氣衝擊,若為藉由具備在從上述任一者選出之下限 及上限構成之範圍内之空氣速度之空氣產生者,則無特別 限制’例如在 1 至 300 m/sec,1 至 250 m/sec,2 至 250 m/sec ’ 5 至 250 m/sec,5 至 200 m/sec,10 至 200 m/sec, 1 0至1 50 m/sec之範圍内之空氣產生之衝擊。 X ’其中賦與於冷凍乾燥組成物之空氣之速度可如下述 ’則定。亦即’在下述之實施形態例1中所示之喷射型乾燥 46 315314 200418520 粉末吸入裝置中,採用將蓄積於風箱體1 0中之空氣從空氣 喷射流路3強制地導入充填於容器内之冷凍乾燥組成物 (塊狀之冷凍乾燥組成物:以下亦稱為「冷凍乾燥塊」)上, 以賦與空氣衝擊,結果生成之微粒從排出流路4排出之機 構。此時,流經空氣喷射流路3之空氣流量藉由蓄積於風 箱體1 0之空氣量除以將該空氣送進容器之時間而算出。繼 而藉由將該空氣流量除以將空氣導入容器之流路諸如空氣 喷射流路3等之截面積,可以算出對於冷凍乾燥組成物(冷 凍乾燥塊)賦與衝擊之空氣速度。 空氣速度(cm/sec)=空氣流量(ml = cm3/sec)+空氣導入流路 之截面積(cm2) 具體而言,例如在設計成空氣喷射流路3之孔徑為必 1.2 mm,排出流路之孔徑為0 1 · 8 mm及蓄積於風箱體1 0 之空氣量為約20 ml之喷射型乾燥粉末吸入裝置之情況, 當將蓄積於風箱體10之約20 ml之空氣量以約0.5秒從空 氣喷射流路3強制地導入容器内之冷凍乾燥組成物時,空 氣流量成為約40 ml/sec。其中若將該值除以空氣導入流路 (空氣噴射流路)之截面積(〇.〇6x 0.06x 3.14 = 0.0113cm2) 時,將成為3540 cm/sec,即空氣速度為約35 m/sec。 又,在下述之實施形態例2、3及4所示之自己吸入型 乾燥粉末吸入裝置中,由於採用從空氣導入流路1 7流入之 空氣賦與冷凍乾燥塊衝擊後,生成之微粒從吸引流路1 6 排出之機構,因此由空氣導入流路1 7及吸引流路1 6之孔 徑來規定流經該流路之空氣流量。因此,帶給收容於容器 47 315314 200418520 内之冷凍乾燥組成物之空氣速度,可藉由測定流經空氣導 入流路1 7之空氣流量,並將其除以空氣導入流路1 7之喷 嘴之截面積而算出。 空氣速度(cm/sec)=空氣流量(ml = cm3/sec)+空氣導入流路 17之截面積(cm2) 具體而言,將包含容器之吸入裝置安裝於在歐洲藥局 方(European Pharmacopoeia,Third Edition Supplement _ 2001,pi 13-115)中記載之裝置a(裝置A)(二段式塵埃測定 器··英國Copley公司製)之截面部分,使用流量計(K〇FL〇c DPM-3)測定流經空氣導入流路I?之空氣流量。 例如’在設計成空氣導入流路1 7之孔徑為0 1.99 mm 且吸引流路之孔徑為0丨·99 mm之自己吸入型乾燥粉末吸 入裝置中,用流量計(K〇FL〇C DPM-3)測得之流經空氣導 入流路17之空氣流量為n 7 L/min(亦即295 ml/sec)之情 況’空氣速度可藉由將該值除以空氣導入流路之截面積 ❿(0·0995χ 〇·〇995χ 3.14 = 〇.〇311cm2)而得到(9486 cm/sec,即 9 5 m/sec) 〇 又,關於帶給充填於容器内部之冷凍乾燥組成物之空 氣’L Ϊ例如至少為丨7 。空氣之流量較佳為至少μ ml/sec ’更佳為至少25 ml/s“。纟中,關於空氣流量之上 限無特別限制,例如為900 L/min。該上限較佳為15 以似’更佳為10 L/sec,再更佳為5 L/sec,還要更佳為4 L/sec,特佳為3 L/sec。具體而言,空氣流量只要在從上 述者中任意選出之下限及上限構成之範圍内,將無特別限 315314 48 200418520 制。該範圍例如為1 7 m / sec 至 15 L/sec,20 ml/sec 至 1 〇 L/sec,20 ml/sec 至 5 T / s。τ / Sec’ 20 ml/sec 至 4 L/sec,20 ml/sec 至 3L/SeC,25ml/咐至 3L/sec。 又’本發明所使用 ^ ^粉末吸入裝置,可具備將空 乳以接近收谷於容器启 .,.^ °卩之4凍乾燥組成物之狀態從流路 之吐出口(較佳具備細孔 峪 .^ ^ y , 之土出口)吐出空氣之手段,諸如 在貫施例中詳述之具備处 ^ '&quot;軋V入路或空氣喷射流路之針 :二:為提高從外部導入之空氣衝擊壓之手段。又,該 會變動,所隨著容器之大小等,其較佳範圍 ;:Γ別限制,直徑“在〇.3至、,較 丨土 υ·:)至5 mm,更佳〇 8昼 内。 〇.8至5 ,特佳1至4mm之範圍 藉由將空氣導入該容哭肉,叮、 於衮哭允人 ^ 可以將以非粉末狀態收容 若点炎4 风物^粒化。其中微粒化之程度, 成為適於經肺投與之粒徑即 以下,較佳5…下。 fi如平均粒徑在1 一 _又’在本發明中所使用之乾燥粉末吸入裝 揭7^之具體態樣物: 下文 3〇〇·經肺投與用之乾燥粉末吸 墼W斗 衣置’係藉由空教衝 擊从非粉末狀態收容於容器.内之冷 孔 驗者吸入所得微粒。 成物,並使受 3 0〗·如態樣3 00項記載之經肺投鱼 置,甘〆 /、用乾無粉末吸入裝 其係將以非粉末狀態收容於容哭中 微^匕並將得到之微粒供被驗者吸東乾燥組成物 芝衣置,其具備: 315314 49 200418520 、、具有空氣噴射流路之針部,具有排出流路之 上述針部之空氣噴射流路中 T鞠达空乳用之空氣壓送 以及與上述針部之排出流路連通之吸入口; 且構成為: 上述針部扎入供密封上述容器之口检以使空 路及排出流路與上述容器内部連通,#由上述空氣壓送: ^吏空氣經由上述空氣噴射流路噴射於上述容器内^由 ^贺射^氣之衝擊使上述冷;東乾難成物微粒化,得狀 被粒經由上述排出流路從吸入口排出。 302.如態樣項記載之經肺投與用乾燥粉末吸入f 二,其係將以非粉末狀態收容於容器中之冷涂乾燥組成物 Μ粒化並將得到之微粒供被驗者吸入用之裝置,其具備: 具有吸引流路之針部,具有空氣導入流路之針部以及 與上述吸引流路連通之吸入口; 且構成為: 在上述針部扎入供密封上述容器之口检之狀態,Η 被驗者之吸氣壓從上述吸入口吸入上述容器内之空氣,同 時使空氣經由上I空氣導人流路流人已成為負屢之容哭 内,藉由流入之空氣衝擊將上述冷來乾燥組成物微粒化, 得到之微粒經由上述吸引流路從吸入口排出。 303·如態樣301 員記載之經肺投與用乾燥粉末吸入裴 置,係構成為藉由將空氣喷射至上述容器内一次,使得上 述冷;東乾無組成物經微粒化並從上述吸入口排出。 304·如態樣301項記載之經肺投與用乾燥粉末吸入裝 315314 50 200418520 置,係構成為藉由將空氣喷射至上述容 / 東乾燥組成物經微粒化成平均粒徑在使得上述冷 粒子比率在10%以上,並從上述吸入口排出一&quot;或有效 305.如態樣3()1項記载之經肺投 置,其為將上述空氣f $ 、 L紅粉末吸入裝 針部中之形態。 出机路形成在一根 306·如態樣3()2項記載之經肺投 置,係構成為藉由被驗者 A ^乾‘叔末吸入裝 物經微粒化並從上述吸入口排出。 述9凍乾燥組成 307·如態樣3〇2項 置,其被構成為藉由被驗者之\ :與用乾燥粉末吸入裝 成物經微粒化成平均粒徑:V:::下:術燥組 在1 0%以上,並從卜、+、 或有效粒子比率 亚攸上述吸入口排出。 308·如態樣302項記載 置,其為將上述吸引产踗“ ”用“粉末吸入裝 針部中之形態。 34空氣導入流路形成在-根 309·如態樣3〇8項 置,係呈備下”载 肺投與用乾燥粉末吸入裝 置係具備下列構件之乾燥粉末吸入裝置: 保持容器用之保持部,1 擊以進行微粒化之非粉末^ “收各待接受空氣衝 用口栓密封;以及 塊狀形態之冷束乾燥組成物,且 賦與該容器内之上沭Α&amp; 之上述々凍乾燥組成物空氣衝擊,並從 上述谷态内吸引藉由空翁 攸 組成物之手段; ’、~#而微粒化之粉末狀冷来乾燥 315314 51 200418520 其具備: &amp;具#供從上述容器吸引上述冷;東乾燥組成物 …流路以及供將外部氣體導入上述容器内之空氣導入 流路, 與上述針部之吸引流路連通之吸引口部, 將上述保持部導向上述針部之軸線方向之引導部, 保:部運轉部’其具有將上述容器保持於上述保持部 述^尖^容器向該針部之針尖前進並使容器之口检被上 針尖:機二或從上述針尖後退而將容器之口栓拉離上述 。卩’以及操作該機構部之操作體,且該機構部 被構t為可用比使上述針部札入容器之口栓所需要之力為 小之力操作上述操作體,以&amp; *要之力為 上if # p+ 13卩且U上述吸引σ部、上述引導部及 上述保持部運轉部之外殼;而且 !、...述針。卩扎入上述口拴以使上述針部之吸引流路 1Γ!:導入流路舆上述容器内連通,同時將上述冷凍乾p 組成物定位成在空氣導入流路之前端之狀態東泫 被驗者之爾從上述吸引口部吸入上述容器内二氣用 亚使空乳經由空氣導入流路流入上述容器内,可對上述容 益内之冷凍乾燥組成物賦與空氣衝擊。 谷 3 1 0.如態樣3 〇9 置,其係構成為:㈣投與用乾燥粉末吸入裳 該外殼形成為筒狀, 端,在該外殼内心二 部形成在該外殼之前 由上述保持部形成供收容上述容器之收 315314 52 200418520 至,將上述針部以針尖朝向上述收納室之方 述外殼内,將與上述針部之 a《方式配設在上 氣用之導入口 項¥入〜路連通並供導入外 置在上述外殼之壁部;並且 藉由上述保持部運轉部, 中以上述外殼之述保持#在上述收納室 之軸線方向丽進及後退。 置::::::1°項記載之經肺投與用乾燥粉… 器之=:外::;述:持部後退之位置形成有上述容 之上述出入口Γ 以及用絞鍵連結於上述外殼本體Regarding the upper limit of air impact, I, ..., and other specific limits, for example, an impact generated by an air velocity of 300 m / sec. About Xi # About the upper limit of 5 Hai, the air impact generated by the hole speed of 250 m / sec is preferred, the air impact generated by the air speed of 200 is more preferred, and the air impact generated by the air speed of 150 m / sec is particularly preferred. Air impact. The air impact is not particularly limited if it is an air generator having an air velocity within a range consisting of a lower limit and an upper limit selected from any of the above, such as 1 to 300 m / sec, 1 to 250 m / sec, 2 to 250 m / sec, 5 to 250 m / sec, 5 to 200 m / sec, 10 to 200 m / sec, and air impact in the range of 10 to 150 m / sec. X 'wherein the speed of the air imparted to the freeze-dried composition can be determined as described below. That is, in the spray-type drying 46 shown in the first embodiment below 46 315314 200418520 powder suction device, the air stored in the wind box 10 is forcedly introduced into the container from the air jet flow path 3 and filled in the container. A mechanism that freezes and dries the composition (block-shaped freeze-dried composition: also referred to as "freeze-dried block" hereinafter) to impinge air, and the generated particles are discharged from the discharge channel 4. At this time, the air flow rate flowing through the air jet flow path 3 is calculated by dividing the amount of air stored in the air box 10 by the time for which the air is sent to the container. Then, by dividing the air flow rate by the cross-sectional area of the flow path that introduces air into the container, such as the air jet flow path 3, it is possible to calculate the air velocity that imparts an impact to the freeze-dried composition (freeze-dried block). Air velocity (cm / sec) = air flow rate (ml = cm3 / sec) + cross-sectional area of the air introduction flow path (cm2) Specifically, for example, when the diameter of the air jet flow path 3 is designed to be 1.2 mm, the discharge flow In the case of a spray-type dry powder inhalation device with a hole diameter of 0 1 · 8 mm and an air volume of about 20 ml stored in the air box 10, the air volume of about 20 ml stored in the air box 10 is less than When the freeze-dried composition was forcibly introduced into the container from the air jet flow path 3 for about 0.5 seconds, the air flow rate was about 40 ml / sec. If this value is divided by the cross-sectional area of the air introduction flow path (air jet flow path) (0.06x 0.06x 3.14 = 0.0113 cm2), it will become 3540 cm / sec, that is, the air velocity is about 35 m / sec. . Further, in the self-suction dry powder inhalation device shown in the following embodiment examples 2, 3, and 4, since the air flowing from the air introduction channel 17 is used to impinge on the freeze-dried block, the generated particles are attracted from The mechanism that the flow path 16 is discharged, therefore, the air flow rate through the flow path is regulated by the diameter of the air introduction flow path 17 and the suction flow path 16. Therefore, the air velocity of the freeze-dried composition contained in the container 47 315314 200418520 can be measured by measuring the air flow rate flowing through the air introduction channel 17 and dividing it by the nozzle of the air introduction channel 17 The cross-sectional area is calculated. Air velocity (cm / sec) = air flow rate (ml = cm3 / sec) + cross-sectional area (cm2) of the air introduction channel 17 Specifically, the inhalation device including the container is installed at the European Pharmacopoeia, The third section Supplement _ 2001, pi 13-115) of the cross section of the device a (device A) (two-stage dust measuring instrument · made by Copley, UK) uses a flow meter (KOFLOc DPM-3 ) Measure the air flow through the air introduction channel I ?. For example, 'In a self-inhalation type dry powder inhalation device designed with an air introduction flow path 17 having a hole diameter of 0 1.99 mm and a suction flow path having a diameter of 0 丨 99 mm, a flow meter (KOFLOC DPM- 3) In the case where the measured air flow through the air introduction flow path 17 is n 7 L / min (that is, 295 ml / sec), the air velocity can be divided by the cross-sectional area of the air introduction flow path. (0 · 0955 × 〇 · 9955 × 3.14 = 〇.〇311cm2) to obtain (9486 cm / sec, that is, 95 m / sec) 〇 Also, regarding the air 'L 带 to the freeze-dried composition filled in the container For example, at least 丨 7. The air flow rate is preferably at least μ ml / sec 'more preferably at least 25 ml / s.' In the above description, there is no particular limitation on the upper limit of the air flow rate, for example, 900 L / min. The upper limit is preferably 15 or more. It is more preferably 10 L / sec, still more preferably 5 L / sec, still more preferably 4 L / sec, and particularly preferably 3 L / sec. Specifically, the air flow rate is only required to be arbitrarily selected from the above. Within the range of the lower limit and the upper limit, there will be no special limit 315314 48 200418520. The range is, for example, 17 m / sec to 15 L / sec, 20 ml / sec to 10 L / sec, 20 ml / sec to 5 T / s.τ / Sec '20 ml / sec to 4 L / sec, 20 ml / sec to 3 L / SeC, 25 ml / command to 3 L / sec. Also, the powder inhalation device used in the present invention can be provided with a vacuum Milk is in a state close to the bottom of the container, and the freeze-dried composition of ^ ° 卩 4 freeze-dried composition is used to spit air from the outlet of the flow path (preferably with a fine hole 峪. ^ ^ Y, the soil outlet), such as In the implementation examples, the details are provided with a ^ '&V; rolling V channel or air jet flow needle: two: means to increase the impact pressure of air introduced from the outside. Also, this will change, with The size of the device, with its preferred range;: Γ particularly limited, a diameter ",, compared to the 〇.3 Shu soil υ · :) to 5 mm, more preferably within 8 square day. 〇.8 to 5, especially good range of 1 to 4mm. By introducing air into the crying meat, bite, cry, and let people cry ^ Can be stored in a non-powder state. Among them, the degree of micronization is a particle size suitable for pulmonary administration, i.e., 5 or less. The specific particle size of fi is as follows: the dry powder inhalation device used in the present invention has a specific appearance of 7 ^: the following 300. The dry powder for pulmonary administration is sucked into a bucket. 'The particles are inhaled from a cold-hole examiner contained in a container in a non-powder state by air impact. The result is 30% of the total amount, as indicated in item 3 of the article, and it is placed in a dry powder-free inhalation container. It will be contained in a non-powdered state. The obtained particles were used by the subject to absorb the dried composition, and the article was provided with: 315314 49 200418520, a needle portion having an air jet flow path, and an air jet flow path having the above-mentioned needle portion of the discharge flow path. The air pressure feed for the empty milk and the suction port communicating with the discharge path of the needle part; and the structure is: the needle part is inserted into the mouth for sealing the container so that the empty path and the discharge flow path communicate with the inside of the container , #Pressurized by the above air: ^ Official air is sprayed into the container through the air jet flow path ^ He shot ^ the impact of the gas to make the above cold; Donggan difficult particles become micronized, and the shaped particles are discharged through the above The flow path is discharged from the suction port. 302. The dry powder for inhalation through pulmonary administration as described in the sample item f2, which is to granulate the cold-coated dry composition M stored in a container in a non-powder state, and obtain the obtained particles for inhalation by the subject. A device comprising: a needle portion having a suction flow path, a needle portion having an air introduction flow path, and an suction port communicating with the suction flow path; In this state, the subject ’s inspiratory pressure sucks the air in the container from the suction port, and at the same time, the air flows through the upper air-conducting flow path. It has become a common problem. The above-mentioned air impacts the air The composition is made into particles by cooling and drying, and the obtained particles are discharged from the suction port through the suction flow path. 303. The dry powder for inhalation through pulmonary administration as described by the member 301 is inhaled into the container by spraying air into the container once to make the above cold; Donggan-free composition is micronized and inhaled from the above Mouth drains. 304. The dry powder inhalation device for pulmonary administration as described in item 301 315314 50 200418520, which is constituted by spraying air to the above-mentioned container / dong. The ratio is above 10%, and it is discharged from the above-mentioned suction port. "Effective" 305. As described in aspect 3 () 1, the pulmonary injection is to inhale the above-mentioned air f $ and L red powder into the needle loading part. In the form. The exit path is formed by a 306 · transplantation via lung as described in item 3 (2), which is constituted by the subject A's dry uncle's inhaled contents which are micronized and discharged from the above-mentioned inhalation port. . The 9 freeze-dried composition 307. As shown in item 302, it is constituted by the subject's \: and the inhalation of the dry powder into an average particle size: V ::: under: surgery The dry group is above 10%, and is discharged from the above-mentioned inhalation port of Bu, +, or effective particle ratio. 308 · As described in item 302, it is a form in which the above-mentioned suction powder "" is sucked into the needle loading portion. 34 The air introduction flow path is formed at -root 309 · As in item 308, The "Dry Powder Inhalation Device for Lung Delivery" is a dry powder inhalation device equipped with the following components: Holder for holding a container, 1-shot non-powder for micronization ^ "Close each port to receive air for flushing A plug seal; and a cold beam dried composition in the form of a block, which imposes air impact on the above-mentioned freeze-dried composition of 沭 Α &amp; in the container, and attracts the air-borne composition from the above-mentioned valley state. Means; ', ~ # and micronized powder cold to dry 315314 51 200418520 It has: &amp; 具 # for attracting the above cold from the container; east drying composition ... flow path and for introducing external air into the container An air introduction flow path, a suction port portion communicating with the suction flow path of the needle portion, and a guide portion that guides the holding portion to the axial direction of the needle portion. Description ^ tip ^ The container is advanced toward the needle point of the needle and the mouth of the container is inspected by the needle point: machine two or retracted from the needle point to pull the mouth of the container away from the above. 卩 'and the operating body that operates the mechanism And the mechanism is configured to operate the above-mentioned operation body with a force smaller than the force required for the needle to be inserted into the mouthpiece of the container, with the &amp; * required force as above if # p + 13 卩 and U The casing of the suction σ part, the guide part, and the holding part operation part; and!, ... the needle. 卩 pierce into the mouth to make the suction flow path 1Γ of the needle part into the flow path to the container The internally connected, and at the same time, the freeze-dried p composition is positioned at the front end of the air introduction flow path. The test subject is sucked into the container from the suction port, and the sub-gas is used to pass the empty milk through the air introduction flow path. It can flow into the container to impinge the air on the freeze-dried composition in the container. Valley 3 1 0. As in aspect 3 009, the structure is as follows: the dry powder is sucked into the casing with dry powder. It is cylindrical, with two ends formed at the inner part of the outer shell. Before the shell is formed by the above-mentioned holding portion for receiving the container 315314 52 200418520 to, the needle portion is directed to the above-mentioned storage room with the needle tip facing the storage room, and is arranged in the same manner as the above-mentioned needle portion in a gas form. The inlet port is connected to the entrance and is externally provided on the wall portion of the casing; and through the holding portion operating portion, the holding # of the casing is used to advance and retreat in the axial direction of the storage room. ::::::: 1 ° Dry powder for pulmonary administration according to item 1 ... of the device =: outside :: ;; description: The above-mentioned entrance and exit Γ is formed at the position where the holding part is retracted, and it is connected to the above-mentioned casing with a twist key. Ontology

迷出入口之蓋子而形成H 保持部運轉部,具備在蓋上上述¥ 閉之時,使上述保持部向著 :^出入口關 述蓋子使上述出入口打開之時,且在拉起上 尖後退之上述機構部,且上述 做:持4從針部之針 作體。 上子兼做為上述機構部之操 (4)經肺投與用乾燥粉末吸入系統 本發明之經肺投與用乾燥粉末吸入 燥组成物與具備特定丰 '、、,係將兮凍乾 中,… 手段之吸入裝置組合而成之系統,1 中省々凍乾燥組成物所且有之έ旧 ^ 與在容器内經冷編且;二::成,係在將空氣衝擊賦 存在之…η Τ粉碎處理之以非粉末狀態 丨丁你&lt; ~ ’果乾紐組成物 微半W… 内可形成平均粒徑在10 脉机纟 羊在10 / 乂上之微粒者。依昭嗜紉 禾及入糸、統,使用者於使用(吸入)以非粉 315314 53 200418520 末狀態提供之冷凉乾燥組成物 投與之劑型,即由平均粒徑在 自仃5周衣成適於經肺 ‘在咖以上之微粒組成之二^以下或有效粒子比率 .用)。 &amp;之乾u末製劑’且可自行投與(服 ϋ為、II有效率地得到料投與用乾操粉末吸人“之 等頗為重要。 斷組成,吸入裝置及容器 •、容解=該冷滚乾燥組成物者,較佳係使用藉由將包含非 有=恶之添加成分之組成液經冷;東乾燥而調製成,且且 有下述特性之冷凍乾燥組成物: 〃 (〇具有非粉末之塊狀形態; (η)衰變指數為〇·05以上;以及 (m)藉由承受具有至少lm/sec之 .^ ^ ^ 礼迷度及至少17ml/sec 量之空氣衝擊,可成為平均粒徑在1〇微米以 下或有效粒子比率在10%以上之微粒。 關於該冷凍乾燥組成物之組成 , 及其之調製方法,可 以棱用在上述(1)章中詳述之内容。 收4:乾燥組成物’係在容器内經冷凌乾燥處理且被 奋灰孩谷态内。被收容於容器内 # ^ ^ ^~凍乾燥組成物之量 二 投與量(1次投與量)或數次(具體而言2至3 -人)杈與夏之有效成分之量。更佳為 你旦、丄 ~ G 3早位投與量(1次投 入里)之有效成分之量。收容於容器内 呈卿旦 &lt; ~ /果乾燥組成物之 視鳴燥組成物所包含之有效成分之種類及添 口里而異’若為從可吸入量中適當選擇則無特別限定,通 315314 54 200418520 常為3〇mg以下,較佳為2〇mg以下,更佳為l〇mg以下, 斗寸佳為5 mg以下。 另一方面’做為乾燥粉末吸入裝置者,較佳係採用具 有下述特徵之乾燥粉末裝置:具備(1)空氣衝擊賦與手段 (或工軋導入手段)及(2)微粒排出手段(或吸入投與手段), 藉由上返(1)空氣衝擊賦與手段,將空氣導入(流入)收容非 粉末狀態之冷凍乾燥組成物之容器内,利用導入(流入)之 工氣衝名(噴射壓)’將該冷凍乾燥組成物微粒化,再者藉 由上述(2)微粒排出手段,使被⑴之手段微粒化之乾燥於末 組成物從容器中排出,且可以直接以吸入法投與至:用 者0 置之-例’例如為在上述(3)章中詳述之乾燥粉末 亦即,本發明之適當經肺投與用乾燥粉末吸入系統, 至少於使用時,為組合使用 y、’ ,.^ ^ . 更用收今上述本發明之冷;東乾燥組 成物之合為以及上述乾燥粉末 L 衣直之糸統。亦即太菸 明之經肺投與用乾燥粉末 又 +次八糸統至少於吸入使用 備收谷上述本發明之冷凌齡丨品 八 〜 v /果乾“組成物之容器以 粉末吸入裝置。 工返I乙^ 若依照本發明之兮έ ^/ 猎由使用上述乾燥粉末吸入 :氣¥入收容本發明之冷滚乾燥組成物之容器 中’以對存在於其β部之冷純 - —之空氣速度及至少17ml/s她武與具有至少1 土夕i /ml/sec之介勻4曰&amp; 擊,可以碉掣忐亘I π # 二乳▲置之空氣衝 月衣成具備可错吸入經肺投與之粒徑或可有效用 315314 55 200418520 於藉吸入經肺投與之有效粒子比率 干 &lt; 钆軔粉末製劑。 關於可藉吸入經肺投與之粒徑,例 ^ ^ , ^ ^ 如平均粒徑(具體而 曰,工氣力學之平均粒徑,MMAD)為 n ^ r; _ 1 〇微米以下較佳5 u未以下。又,關於可有效用於藉 ...ν μ 八經肺投與之有效粒 千比率,例如10%以上,較佳2〇% $ ^ 更佳25%以上, 再更佳30%以上,特佳35%以上。 又若依照該系統,可以將調製得之乾 鲁經肺投與(藉由吸入)至使用者。此表示衣诗接 用乾燥粉末吸入系統可謂r適於藉 二:之[肺技與 #古制π ^ 、、稭甶及入經肺投與之乾燥 叔末製劑之製造系統,同時為將該 了 /私^粉末製劑經肺投與 至使用者之投與系統」。 又,本發明之經肺投與用乾燥粉末吸入系統包含下文 揭不之具體形態·· 40 1 · —種經肺投與用乾燥 Τ刀不及入糸統,係將下述(1) 及(2)組合使用: _ (1)收容冷凍乾燥組成物之容器,該;人;# Ρ t , —、 成~,東乾燥組成物係將包 含非溶解狀態之添加成分之έ 、 、、且成液經冷凍乾燥而調製 成’且具有下述⑴至(iii)之特性: (I) 具有非粉末之塊狀形態; (II) 衰變指數為〇 〇5以上;以及 (⑴)藉由承受具有至少lm/sec之空氣速度及至少 之空氣流量4空氣衝擊,可成為平均粒徑纟1〇微米以 下或有效粒子比率在1〇%以上之微粒; ⑺具借可將上述空氣衝擊賦與上述容器内之冷滚乾燥組 315314 56 200418520 成物之手段以及排出 物之手段之裝置。 經微粒化之粉末狀 冷凍乾燥組成 402.如態樣4〇1項記載之經肺投與 統,其中收容冷凍乾燥組成物之容器, 與量之有效成分之冷凍乾燥組成物之容 用乾燥粉末吸入系 為收容含有1次投 4 0 3 ·如態樣4 0 1項記載 統,其於吸入時為組合使用 4 0 4 ·如態樣4 0 1項記載 統,其中,冷;東乾燥組成物 圍内。 器。 之經肺投與用乾燥粉末吸入系 上述容器與上述裝置之形態。 之經肺投與用乾燥粉末吸入系 之衰變指數在0.05至15之範 、。0執 &lt; 經肺投與用乾燥粉末吸入 統,其中,綱中記載之空氣衝擊係藉由具有至少2m/s 空氣速度及至少17 ml/sec之*巧义曰 之I乳流量之空氣產生 態樣4 0 1 j音却^ _ 之 偏.如態樣項記載之經肺投與用乾燥粉。入 統’其中’在㈣中記载之空氣衝擊係藉由呈彳3 m/sec之空氣速度及至少17 ml/sec之空氣流量之空氣 生0 407. 如恶樣4〇1項記載之經肺投與用乾燥粉末吸入系 統,其中,在㈣中記載之空氣衝擊係藉由*有至少 之空氣速度及至少胸sec之空氣流量之空氣產生。 408. 如態樣40&quot;員記載之經肺投與用乾燥粉末吸入系 統,其中’在中記载之空氣衝擊係藉由具有至少一 之空氣速度及蘭se…5L/sec之空氣流量之空氣』 支0 315314 57 200418520 4 09·如態樣4〇1工苜々#β t 員兄載之、左肺杈與用乾燥粉末吸入系 統其中’該冷决乾燥組成物具有承受空氣衝擊時’可成 為平均粒徑在5微米以 七古 下或有效粒子比率在20%以上之微 粒之特性。 4 1 0 ·如態樣4 〇 1 Jg ~沿ί &gt; t 、5己載之!肺投與用乾燥粉末吸入系 、、先,其中,該冷凍乾燥組成 藥物。 匕3 1义馮有效成分之低分子 4 11 ·如態樣4 〇 1工盲士發 統,其中,該冷康乾二 與用乾燥粉末吸入系 類及核酸等高分子藥物。一為有效成分之蛋白質 412.如態樣401項 統,其中,該冷束乾烤电…:一嶋粉末吸入系 於保持體狀態之核酸。 ’、、、 成刀之呈保持 4U,如態樣41〇項記載 統,其中,該冷凍 杈共用乾煉粉末吸入系 果乾無組成物包含彳於 、 藥物以及載劑,該载劑為 μ有效成分之低分子 d I 為至夕一種選自月# I而分 rtr 肽及糖類組成之群者。 、目胺基酸、二肽、三 4U.如態樣411項記载之 統,其中,該冷凍乾 广、用乾煉粉末吸入系 碩及核酸等高分子藥物 勹有效成刀之蛋白質 胺基酸、二狀、二狀刀4載㈣,該载劑為至少一種選自 肽—肽及糖類組成之群 4 1 5 ·如態樣4 1 3項記. 統,其中,該冷凍乾二…/投與用乾燥粉末吸入系 藥物以及載劑,”:;:包含做為有效成分之低分子 载制為至少-種選自疏水性胺基酸、疏 315314 58 200418520 水性二肽及疏水性三肽組成之群者。 4 1 6 ·如態樣4 1 4頊汴恭十么一 ^ ..^ . 、°載之!肺投與用乾燥粉末吸A &amp; 統,其中,該冷滚乾燥組成物包含 :末及入糸 類及核酸等高分子藥物以及載劑,刀之蛋白質 疏水性胺基酸、疏水性 至少-種選自 虹如態樣仙項三肽組成之群者。 緣# . + 員載之經肺投與用乾燥粉末吸入系 統,其中,f冷凌乾燥組成物為水溶性組成物。糸 4 1 8·如態樣4〇 1頊9哉 緣# , 、。己载之、、坐肺投與用乾燥粉末吸人系 統’其中,該裝置係採用下列〇及屮. 末及入糸 μ肺投與用乾燥粉末吸入裝置,其係 谷於容器中之冷凌乾 知末狀恶收 供被矜㈣入田 微粒化並將得到之微粒 仏破驗者吸入用之裝置,其具備: 具有空氣噴射流路之針部,且 上述針部之空氣嗆鼾a々+ ,、有排出〜路之針部,在 以及盘m ^氣用之空w送手段, 以及與上述針部之排出流路連通之吸人口,·、乎&amp; 且被構成為: 上述針部扎入供贫抖 路及排出流路愈上二匕述谷…栓以將空氣喷射流 段使”婉由:μ内#連通’藉由上述空氣壓送手 仅1文工乳經由上诚处今 該噴射空氣之衝;==噴射於上述容器内,藉* 献經由上述排出流路從吸入口排出。 〗 Π)經肺投與用㈣粉末吸人裝置 &amp; 於&amp;哭由々、人 知將以非粉末狀態收容 被^ 〜凍乾燥組成物經微粒化並將得到之微粒供 被驗者吸入用之裝置,其具備: 315314 59 200418520 ’、有吸引*路之針部,具有空氣導 與上述吸引流路連通之吸入口; 路之針部以及 且構成為: 在上述針部札入供密封上述容器之口 姆之吸氣壓從上述吸入口吸入上述二藉由 時使空氣經由上述介_ °。内之工氣,同 内乳導入流路流入已成為負壓之 内,精由流入之空氣衝擊將上述冷滚乾 物〜 得到之微粒經由上述 …成物破粒化, 义次引/爪路從吸入口排出。 4 1 9 ·如態樣 4 1 8 # 員ό己载之經肺投與 統,其中,該裝置係採用經肺投與用之乾末吸入系 其係具備下列構件之乾燥粉末吸入裝置入褒置’ 保持容器用之保持部,其中該容器收容待承〜^ 擊以進行微粒化之非粉末塊狀 =風衝 用口栓密封,以及 來釔秌組成物,且 賦與該容器内之上述冷凌 上述容器内吸引夢由μ ^ 衝擊,並從 組成物之手段;μ 而微粒化之粉末狀冷凌乾燥 其具備: 之吸ϋ路具有供從上述容11吸引上述冷隸燥組成物用 ^引*路以及供將外部氣體導人上述容器内之空氣導入 與上述針部之吸引流路連通之吸引口部, 將上述保持部導向上述針部之軸線方向之引導部, 保持部運轉部,其具有將上述容器保持於上述保持部 315314 60 200418520 之時,使該容器向該針部之斜尘俞, … |又針大别進亚使容器之口栓被上 述針尖扎入,及從上述針尖後退 k阳將奋為之口栓拉離上述 針尖用之機構部,以及摔作兮撼;4蓉仓 鈿作该機構部之操作體,且該機構 部被構成為可用比使上述針部扎入容器之口 為小之力操作上述操作體,以及 支持上述針部且供設置上诚 迷及引口部、上述引導部及 上述保持部運轉部之外殼;而且 於上述針部扎入上述口栓佶 彺M便上述針部之吸引流路及 空氣導入流路與上述容器内連通, 。路及 ,.^ y ^ ^ rj捋將上述冷凍乾燥組 成物疋位成在空氣導入流路之前端 ^ ^〆 引而之狀悲時,藉由利用被 驗者之吸氣壓從上述吸引口部吸 抑 |叹八上述谷裔内之空氣,並 使空氣經由空氣導入流路流入上述 谷為内,可對上述容器 内之冷凍乾燥組成物賦與空氣衝擊。 420·如態樣401項記載之經肺投盘 &quot;又一用乾紐粉末吸入系 、、死,其中,組合使用下列⑴及(2): ⑴::冷繼組成物之容器’該冷,東乾燥组成物係將包 :非溶解狀態之添加成分之組成液經冷康乾燥而調製 成,且具有下述⑴至(iii)之特性: (1)具有非粉末之塊狀形態; (η)衰變指數在〇.〇5至15之範圍内;以及 ㈣:由承受具有1至3〇〇m/sec之空氣速度及i7mi/sec 主l5L/sec之空氣流量之空氣衝擊, 」成為平均粒徑 10微米以下或有效粒子比率在1〇%以上 以及 ’ 315314 61 200418520 (2)具備可將上述线衝擊賦與上述容器 ,手段以及排出經微粒化之粉末狀冷;Ϊ = 物之手段之裝置。 7 /來乾燥組成 ⑵·如態樣420項記載之經肺投 統,其中,收容該冷庾款r ζ , 祀&amp;心末吸入系 叹合3 ~床乾紐組成物之容哭, 次投與量之有效成分之A $ # p 為收谷含有1 喇风刀~凍乾燥組成物之容器。 422.如態樣42G項記栽之經肺投細乾燥 統,其中,該空氣速度為i至25〇m/sec。习 入糸 :23·如態樣項記載之經肺投與用乾燥粉末 、、充’其中,該空氣流量為20ml/se^咖如。 、 (5)經肺投與方法 ^者’本發明係關於經肺投與方法,其包含在使 =非粉末狀態之冷; 東乾燥組成物時,調製成可經肺投與之 =之狀態,並吸入該微粒形態之乾燥粉末製劑。該經肺 =方法可藉由使用在(4)章中詳述之本發明經肺投與用 &gt; %末吸入系統進行’該系統宜為由收容⑴章中詳述之 Γ包含非溶解狀態之添加成分之組成液經冷凍乾燥所調製 ^ ^本發明冷凍乾燥組成物之容器,以及在(3)章中詳述之 乾燥粉末吸入裝置組成之經肺投與用乾燥粉末吸入系統組 成0 樣: 本發明之經肺投與方法包含在下文中揭示之具體態 501 · —種經肺投與方法,包含使用冷凍乾燥組成物, 315314 62 200418520 該冷珠乾燥組成物係將包含非溶解狀態之添加成分之組成 液經冷凍乾燥而調製成,且具有下述特性·· (i) 具有非粉末之塊狀形態; (ii) 衰變指數為〇·〇5以上;以及 剛由承受具有至少lm/sec之空氣速度及至少η — 之空氣流量之空氣衝擊,可成為平均粒徑在ι 〇微米以 下或有效粒子比率在10%以上之微粒; 使用時,猎由將上述空氣衝擊賦與於該冷;東乾燥組成 物,形成平均粒徑纟10微米以下或有效粒子比率在⑽ 以上之微粒,然後藉由令使用者吸入該微粒化之粉末而投0 5〇2·如怨樣501項記載之經肺投與方法,其中,1、令 凍乾燥組成物含有1次投與量之有效成分。 一 503·如態樣501項記載之經肺投與方法,其中,該冷 康乾燥組成物被收容於容器1,以及被微粒化之粉末係= -備對於谷杰内之該冷;東乾燥組成物可賦與上述空氣衝擊 之手I又以及將經微粒化之粉末狀冷床乾燥組成物從容 排出之手段之裝置調製而成。 口口 、504·如怨樣501項記載之經肺投與方法,其中,該冷 凍乾燥組成物之衰變指數在0.05至1.5之範圍内。^ ^ 5〇5 ·如怨樣503項記載之經肺投與方法,其中,在(iH) 中:載之空氣衝擊係藉由具有至少、2 m/sec之空氣速度及 17ml/sec之空氣流量之空氣產生。 5〇6·如態樣503項記載之經肺投與方法,其中,在(iii) 63 315314 200418520 中記載之空氣衝擊係 承错由具有1至300 m/sec之空氣速度The H holding part running part is formed by being covered with the cover of the entrance and exiting. When the cover is closed, the holding part is directed toward: ^ When the door is closed to open the entrance and exit, and the upper part is pulled back to retract And do the above: Hold the needle from the needle part as the body. Shangzi doubles as the operation of the above-mentioned mechanism. (4) Dry powder inhalation system for pulmonary administration. The dry powder inhalation composition for lung administration of the present invention is provided with a specific enrichment. , ... A system composed of means of inhalation devices, 1 in the province of lyophilized composition, and the old one ^ and cold knitting in the container ;; 2 :: Cheng, which is caused by the impact of air ... η Τ pulverized in a non-powder state. Dingyou &lt; ~ 'Dried fruit composition has micro-half W ... can form particles with an average particle size of 10 pulse machine lambs on 10 / 乂. According to Zhao Zhileihe, and the system, the user will use (inhale) the non-powder 315314 53 200418520 to provide the cool and dry composition of the dosage form, that is, from the average particle size within 5 weeks of clothing. Applicable to the lungs, the composition of the particles above the coffee is less than 2 ^ or effective particle ratio. &amp; of dry preparations and can be administered on their own (the service is, II to get the material to be efficiently administered with dry powder to suck people "etc. is very important. Composition, inhalation device and container •, solution = The cold-rolled dry composition is preferably a freeze-dried composition prepared by cold-drying a composition liquid containing non- = evil added ingredients and having the following characteristics: 〃 ( 〇 has a non-powder morphology; (η) a decay index of 0.05 or more; and (m) by being subjected to air impact having a degree of at least lm / sec of ^ ^ ^ and at least 17 ml / sec, It can be fine particles with an average particle size of less than 10 microns or an effective particle ratio of more than 10%. Regarding the composition of the freeze-dried composition and its preparation method, it can be used in detail in Chapter (1) above. 4: Dry composition 'is in a container that has been subjected to cold-blood drying treatment and is in the valley state of Fenhui. It is contained in a container # ^ ^ ^ ~ freeze-dried composition amount two doses (one dose) ) Or several times (specifically 2 to 3-person) and the amount of active ingredients in summer. Better for you, 丄~ G 3 The amount of effective ingredients in the early administration amount (into 1 shot). The contents of the active ingredients contained in the visually-drying composition contained in the container are clear and dry. It varies according to the mouth, and it is not particularly limited if it is appropriately selected from the inhalable amount. 315314 54 200418520 is usually 30 mg or less, preferably 20 mg or less, more preferably 10 mg or less. 5 mg or less. On the other hand, as a dry powder inhalation device, it is preferable to use a dry powder device having the following characteristics: (1) air impact imparting means (or rolling introduction means) and (2) particles Evacuation means (or inhalation and administration means), the air is introduced (inflowed) into the container containing the non-powder freeze-dried composition by means of the upward return (1) air impact application means, and the working gas introduced (inflowed) is used Redemption (jetting pressure) 'This freeze-dried composition is made into micronized particles, and the above-mentioned (2) particle ejection means is used to pulverize and dry the micronized composition and discharged from the container. Administration by inhalation: user 0 -Example 'is, for example, the dry powder detailed in Chapter (3) above, that is, the dry powder inhalation system suitable for pulmonary administration of the present invention, and at least when used, it is used in combination with y,',. ^ ^. The combination of the above-mentioned present invention; the combination of the East dry composition and the above-mentioned dry powder L. The direct system. That is, the dry powder for lung administration for Taiyanming plus + eight-time system is at least used for inhalation to prepare the harvest valley. The above-mentioned cold lingling of the present invention 丨 product 8 ~ v / dried fruit "composition container with powder inhalation device. Rework I B ^ If in accordance with the present invention ^ / hunting by using the above dry powder inhalation: gas ¥ into In the container containing the cold-rolled and dried composition of the present invention, the air velocity and the air velocity of at least 17 ml / s and the air temperature of at least 17 ml / s and the uniformity of at least 1 soil i / ml / sec in the β portion of the β Said &amp; strike, you can 碉 忐 亘 I π # 二 乳 ▲ Place the air to the moon garment to have a particle size that can be mistakenly inhaled and administered by the lung or effective 315314 55 200418520 Effective by inhalation by the lung Particle ratio dry &lt; 钆 轫 powder formulation. Regarding the particle size that can be administered by inhalation through the lung, for example, ^ ^, ^ ^ If the average particle size (specifically, the average particle size of industrial pneumatics, MMAD) is n ^ r; _ 10 μm or less preferably 5 u is below. In addition, regarding the ratio of effective granules that can be effectively used for borrowing ν μ by eight lungs, such as 10% or more, preferably 20% $ ^ 25% or more, 30% or more, especially Better than 35%. According to this system, the prepared stem can be administered (by inhalation) to the user via the lungs. This means that the dry powder inhalation system used by Yi Shi can be described as suitable for borrowing two: the [pulmonary technology and # 古 制 π ^ ,, straw, and the manufacturing system of dry tertiary preparations administered through the lung, and at the same time The powder / powder formulation is administered to the user's delivery system via the lung. " In addition, the dry powder inhalation system for pulmonary administration according to the present invention includes the following specific forms that are not disclosed below. · 40 1 · A type of dry T-knife for pulmonary administration is less than the system. The following (1) and ( 2) Combined use: _ (1) A container containing a freeze-dried composition, the person; # Ρ t, —, Cheng ~, East drying composition will contain the non-dissolved state of the added ingredients, and The liquid is prepared by freeze-drying and has the following characteristics (i) to (iii): (I) it has a non-powdered morphology; (II) its decay index is above 0.05; and (ii) it has The air velocity of at least lm / sec and the air flow of at least 4 air impact, can become particles with an average particle size of less than 10 microns or an effective particle ratio of more than 10%; The cold rolling and drying group inside 315314 56 200418520 means for forming and discharging means. Micronized powder freeze-dried composition 402. The pulmonary administration system as described in item 401, wherein the container containing the freeze-dried composition and the amount of the active ingredient of the freeze-dried composition are contained in a dry powder. The inhalation system contains one dose of 403 for each injection. · As described in item 401, it is used in combination when inhaled. · As in item 401, it is cold; Within the fence. Device. The dry powder inhalation for pulmonary administration is in the form of the container and the device described above. The decay index of the dry powder inhalation system for pulmonary administration is in the range of 0.05 to 15. 0 &lt; Dry powder inhalation system for pulmonary administration, wherein the air impact described in the outline is produced by air having a milk flow rate of at least 2 m / s and at least 17 ml / sec. Ecological sample 4 0 1 j sound but ^ _ partial. As described in the state sample, dry powder for pulmonary administration. The air impact recorded in "Where" is generated by air at an air velocity of 3 m / sec and an air flow of at least 17 ml / sec. A dry powder inhalation system for pulmonary administration, wherein the air impact described in the urn is generated by air having at least an air velocity and an air flow rate of at least chest sec. 408. The dry powder inhalation system for pulmonary administration as described in Aspect 40, in which the air impulse described in the above is by air having an air velocity of at least one and an air flow rate of 5 L / sec. 』Support 0 315314 57 200418520 4 09 · As the appearance 4〇1 工 杏 々 # β t The brother, the left lung branch and the inhalation system with dry powder, where 'the cold-determined dry composition has the ability to withstand air impact' can be It has the characteristics of fine particles with an average particle size of 5 micrometers or less, or an effective particle ratio of 20% or more. 4 1 0 · Like aspect 4 〇 1 Jg ~ Yan ί &gt; t, 5 has been contained! Dry powder inhalation system for pulmonary administration, first, and first, wherein the freeze-dried composition of the drug. The low molecular weight of the active ingredients of Yifeng 4 11 • Such as the situation of 401 industrial blinds system, in which the cold Kanggan II and dry powder inhalation system and nucleic acid and other polymer drugs. One is the protein of the active ingredient 412. The system of item 401, wherein the cold-beam dry roasting is performed by electricity: a pile of powder is sucked into the nucleic acid which is in the state of the body. ',,, and the knife remain 4U, as described in item 40, wherein the frozen branch shares a dry powder inhalation system, and the dried fruit contains no drug, a drug, and a carrier, and the carrier is μ The low molecular weight d I of the active ingredient is a group consisting of rtr peptides and carbohydrates selected from month #I. , Amino acid, dipeptide, tri 4U. As described in item 411, wherein the freeze-dried, inhaled polymer powder such as system and nucleic acid with dry powder is used to effectively form the protein amine group of the knife. The acid, bimorph, and bimorph knives are contained in 4 carriers, and the carrier is at least one member selected from the group consisting of peptide-peptides and carbohydrates. 4 1 5 · As for aspect 4 1 3, the system, wherein the freeze-dried ... / Dry powder inhalation drug and carrier for administration, "::: contains low-molecular-weight carrier as an active ingredient at least-selected from the group consisting of hydrophobic amino acids, 315314 58 200418520 aqueous dipeptides and hydrophobic three Groups of peptides. 4 1 6 · Like aspect 4 1 4 顼 汴 contend ^ ^ .. ^., ° Load it! Lung administration with dry powder suction A &amp; system, where the cold rolling dry The composition includes: macromolecules, macromolecules, nucleic acids, and other high-molecular drugs and carriers; the protein of the knife is hydrophobic amino acid, and at least hydrophobic-a group selected from the group consisting of rainbow-like triseptides. 缘 # + Dry powder inhalation system for intrapulmonary administration, in which the frigid dry composition is a water-soluble composition. 糸 4 1 8 · Such as the aspect 4〇1 顼 9 哉 缘 #,,... Has been contained, the dry powder suction system for sitting lung administration. Among them, the device uses the following 0 and 屮. 末 and 糸 μ pulmonary administration The dry powder inhalation device is a device for inhalation of cold chilled and dry powder in a container for inhalation, which is inhaled into the field to be atomized and the obtained particles are broken by the examiner for inhalation. The device includes: an air jet flow path; Needles, and the air 呛 鼾 a々 + of the needles, needles that have a way to discharge ~, air delivery means for the disk m ^ air, and the suction population that communicates with the discharge flow path of the needles And, it is constituted as follows: The above-mentioned needle part is pierced into the poor shaking path and the exhaust flow path, and the upper and lower valleys are tied ... to tie the air jet flow section so that "wanyou: μ 内 # 通通" by The above-mentioned air pressure feeding hand only has 1 milk of the milk sprayed by Shangcheng to spray the air; == is sprayed into the container, and is discharged from the suction port through the above-mentioned discharge flow path. 〖Π) Pulmonary powder inhalation device for pulmonary administration &amp; Yu &amp; Crying by 々, known to be contained in a non-powdered state ^ ~ The freeze-dried composition is micronized and the resulting particles are used by the subject for inhalation The device includes: 315314 59 200418520 ', a needle part having a suction path, an air inlet which communicates with the suction flow path; a needle part of the path, and is configured to be inserted into the needle part for sealing the above The suction pressure of the mouth of the container is sucked into the two through the suction port, and the air is passed through the above medium. The internal working gas flows into the negative milk flow path with the internal milk introduction flow path, and the cold rolled dry matter is finely impacted by the inflowing air. The obtained particles are broken into particles through the above-mentioned ... The suction port is discharged. 4 1 9 · 如 势 样 4 1 8 # The member has a pulmonary administration system, in which the device is a dry powder inhalation system for pulmonary administration, which is a dry powder inhalation device with the following components: The holding portion for holding a container, wherein the container contains a non-powdered block to be subjected to pulverization = air impulse is sealed with a spigot, and a yttrium-rhenium composition is provided to the above-mentioned container. Lengling in the above container attracts dreams by μ ^ impact and from the composition means; μ and the micronized powder cold leng drying has: The suction path has for the above-mentioned container 11 to attract the above-mentioned cold-drying composition ^ Introduction channel and suction port for introducing external air into the container into the suction port communicating with the suction flow path of the needle portion, guiding the holding portion to the guide portion in the axial direction of the needle portion, and holding portion operation portion When the container is held in the holding portion 315314 60 200418520, the container is tilted toward the needle portion, and the needle is inserted into the mouth of the container by the needle point, and The needle tip retreats The mouth bolt is pulled away from the mechanism part for the above-mentioned needle tip, and it is shaken; 4 Rongcang is used as the operating body of the mechanism part, and the mechanism part is configured to be usable smaller than the mouth of the needle part into the container Operate the operating body with force, and a housing that supports the needle portion and is provided with a fan and mouth portion, the guide portion and the holding portion operation portion; and the mouth pin 佶 彺 M is inserted into the needle portion, and the above The suction flow path and air introduction flow path of the needle part communicate with the inside of the container. Lu and. ^ Y ^ ^ rj 时 When the above freeze-dried composition is positioned at the front end of the air introduction flow path ^ ^ 悲, the air is drawn from the suction port by using the suction pressure of the subject Suck the air in the valley and let the air flow into the valley through the air introduction channel, which can impinge the air on the freeze-dried composition in the container. 420. As described in item 401, the trans-pulmonary tray &quot; another inhalation system with dry button powder, and die, wherein the following ⑴ and (2) are used in combination: ⑴ :: a container for cold relay composition 'The cold The dry composition is prepared by cold-drying the composition liquid of the additive components in a non-dissolved state, and has the following characteristics (i) to (iii): (1) it has a non-powder morphology; ( η) the decay index is in the range of 0.05 to 15; and ㈣: from the impact of air with an air velocity of 1 to 300 m / sec and an air flow of 15 l / sec at an i7mi / sec, "" becomes an average The particle size is less than 10 microns or the effective particle ratio is more than 10% and '315314 61 200418520 (2) Equipped with the means for imparting the above-mentioned linear impact to the container and means for discharging the powdered cold powder; Ϊ = means of material Device. 7 / Coming to dry 干燥 · As described in item 420 through the lung system, which contains the cold 庾 section r ζ, worship &amp; end of heart inhalation sigh 3 ~ bed dry button composition, cry, The effective amount of the administered ingredient A $ # p is a container containing 1 Lafeng knife ~ freeze-dried composition. 422. The lung-draining fine drying system described in item 42G, wherein the air velocity is i to 25 m / sec. Learning: 23. The dry powder for pulmonary administration as described in the aspect described above, wherein the air flow rate is 20ml / se ^ Caru. (5) Method for pulmonary administration ^ The present invention relates to a method for pulmonary administration, which includes cooling in a non-powder state; when the composition is dried, it is prepared into a state that can be administered by lungs = And inhaled the dry powder preparation in the form of particles. The transpulmonary method can be performed by using the transpulmonary administration &gt;% inhalation system of the present invention detailed in Chapter (4). The system is preferably composed of Γ containing non-dissolved added ingredients detailed in the containment chapter. The composition liquid is prepared by freeze-drying ^ ^ The container of the freeze-dried composition of the present invention, and the dry powder inhalation system for pulmonary administration composed of the dry powder inhalation device detailed in Chapter (3) The method of administration includes the specific state 501 disclosed below. A method of pulmonary administration, including the use of a freeze-dried composition, 315314 62 200418520 The cold-bead-dried composition is a composition liquid containing non-dissolved added ingredients frozen It is prepared by drying and has the following characteristics ... (i) It has a non-powdered morphology; (ii) The decay index is greater than or equal to 0.05; and it has been subjected to an air velocity of at least lm / sec and at least η. — The air impact of air flow can become particles with an average particle size of less than ι 0 μm or an effective particle ratio of more than 10%; in use, the above-mentioned air impact is imparted to Cold; dry the composition to form particles with an average particle size of 纟 10 microns or less, or an effective particle ratio of ⑽ or more. Then, the user inhales the micronized powder and throws it in. 0502. As recorded in Item 501 The method for administration via the lungs, wherein: 1. The freeze-dried composition contains the active ingredient in a single administration amount. A 503. The method of pulmonary administration as described in item 501, wherein the cold-kang dry composition is contained in the container 1 and the micronized powder system =-prepare the cold for Gu Jie; The composition can be prepared by means of a means for imparting the above-mentioned air impacting hand I and a means for calmly discharging the micronized powdery cold-bed drying composition. Mouth mouth, 504. The pulmonary administration method as described in item 501, wherein the freeze-dried composition has a decay index in the range of 0.05 to 1.5. ^ ^ 5〇5. The method of pulmonary administration as described in Item 503, wherein in (iH): the air impact of the load is by an air velocity of at least 2 m / sec and 17 ml / sec. A flow of air is generated. 506. The method of pulmonary administration as described in item 503, wherein the air impact system described in (iii) 63 315314 200418520 has an error rate of 1 to 300 m / sec.

及至少1 7 ml/sec之空汽 曰 M 工虱流置之空氣產生。 507.如態樣5〇3 上 負汜載之經肺投與方法,其中,在(iii) 中記載之空氣衝擊係盐 ’、错由具有至少1 m/sec之空氣速度及 至少 20ml/sec 之^? * 二氣 量之空氣產生。 5 0 8 ·如態樣5 〇 3馆^And at least 17 ml / sec of air vapour. 507. The method of pulmonary administration with a negative load on aspect 503, wherein the air impact salt described in (iii) has an air velocity of at least 1 m / sec and at least 20 ml / sec. Zhi ^? * Two air volumes are generated. 5 0 8 · Like appearance 5 03 Hall ^

貝汜載之經肺投與方法,其中,在(iii) 中記載之空氣衝擊係M 赢^ 咏错由具有至少1 m/sec之空氣速度及 響 17ml/sec 至 15L/Sec + … 之二氣流量之空氣產生。 509·如態樣5〇3 貝屺載之經肺投與方法,其中,該冷 康乾纟呆組成物包含傲 文為有效成分之低分子藥物。 5 10·如態樣 5〇3 二 負圮載之經肺投與方法,其中,該冷 凍乾燥組成物包含傲失 2 ^ 马有效成分之蛋白質類及核酸等高分 子樂物。Bei Yingzai's method of pulmonary administration, wherein the air impact system described in (iii) M wins ^ Wrong from having an air speed of at least 1 m / sec and a sound of 17ml / sec to 15L / Sec +… bis Air flow is generated by air. 509. The method for administration via lung according to aspect 503, wherein the composition of Lengkang dry dementia comprises a low-molecular-weight drug with Aowen as an active ingredient. 5 10 · Such as aspect 503, a method for administering lung cancer via a negative load, wherein the freeze-dried composition includes proteins and nucleic acids such as active ingredients of horses.

5 11·如態樣503 〉東乾纟呆組成物包含做 核酸。 項記載之經肺投與方法,其中,該冷 為有效成分之呈保持於保持體狀態之 5 12.如態樣509項 凍乾燥組成物包含做為 该載劑為至少一種選自 群者。 記載之經肺投與方法,其中,該冷 有效成分之低分子藥物以及載劑, 胺基酸、二肽、三肽及糖類組成之 513.如態樣 51〇 Jg a 土、 . 、6己載之經肺投與方法,其中,該冷 凍乾燥組成物包含做為 ^ ^ 馮有效成刀之蛋白質類及核酸等高分 子樂物以及載劑,該番丄 ϋΛ載劑為至少一種選自胺基酸、二肽、 三肽及糖類組成之群者。 、 315314 64 200418520 5 1 4 ·如態樣 5 ] 7 ts _ 項記載之經肺投與方法,中,該;人 凍乾燥組成物包含做 ” 7 9 θ i 、有效成7刀之低分子藥物以及載劑, 石亥載劑為至少一稽准ώ丄 枓一日+ 、自&amp;水性胺基酸、疏水性二肽及疏水 性二肽組成之群者。 ^5.如悲、樣513工員記載之經肺投與方法,纟中,該冷 ^ m 4 、 〜、有效成为之蛋白質類及核酸等高分 子条物以及載劑,該載 # he - pi 戟…為至^種璉自疏水性胺基酸、 肢水性二肽及疏水性三肽組成之群者。 態# 5〇3項記載之經肺投與方法,其中,該冷 凍乾燥組成物為水溶性組成物。 志卓 H 5G3項記載之經肺投與方法,其係'微粒化 成平均粒徑在5檄半,、;π + + , 未以下或有效粒子比率在20%以上之微 粒之投與方法。 5 1 8.如悲樣5 〇 3項印恭夕么7姑_ 4rL彳 貝。己載之經肺投與方法,其中,該裝 置係採用(3)乾燥粉末吸入穿 , 夂八衣置之早中纪载之形態項301或 3 〇2之乾燥粉末吸入裝置。 =9·如態m 518項記載之經肺投與方法,其中,該裝 置4用(3)乾燥粉末吸入裝置之章中記載之形態項谓之 乾燥粉末吸入裝置。 …520·如態樣503項記載之經肺投與方法,其中,冷床 乾燥組成物係將包含非溶 1 f狀心之冰加成分之組成液經冷 凍乾燥而調製成,且具有下述特性者: 具有非粉末之塊狀形態; (1〇衰婕指數在0.05至15之範圍内;以及 315314 65 200418520 (iii)藉由承受具有1至300 m/sec 工孔逑度及17 ml/sec 至 15L/sec之空氣流|夕允名 孔伽·里之I軋衝擊,可成為平均粒徑 在10微米以下或有效粒子 干牡1 υ /❹以上之微粒; 經微粒化之粉末,係使用具備可將 、 每J肘上逑空虱衝擊賦與容器 内之上述冷/東乾燥組成物之手段以 攸谷為排出經微粒化 之粉末狀冷凍乾燥組成物之手段之裝置調製而成。 52L如態樣52G項記載之經肺投與方法,其中該空氣 速度為1至250 m/sec。 旦522.如態| 520項記載之經肺投與方法,其中該空氣 流量為 20 ml/sec 至 l〇L/sec。 (6)冷凍乾燥組成物在吸入式經肺投與之使用 再者’本發明係關於非粉末狀態之冷凍乾燥組成物在 吸入式經肺投與上之使用。該㈣包含在 體態樣: … 601 ·冷凍乾燥組成物在吸入式經肺投與之使用,其 中’、該冷康乾燥組成物係將包含非溶解狀態之添加成分之 組成液經冷凍乾燥而調製成,且具有下述特性: (I) 具有非粉末之塊狀形態; (II) 衰變指數為〇 〇5以上;以及 (iii)=承受具有至少im/sec之空氣速度及至少17ml/sec 二氣/瓜置之空氣衝擊’可成為平均粒徑在1 〇微米以 下或有政粒子比率在1 〇%以上之微粒; Q凍乾燥組成物係粉末化成具有上述平均粒徑或有 315314 66 200418520 效粒子比率之微粒來使用。 6〇2·如態樣601項記恭夕、人、土 ± m ^ 、 々凍乾燥組成物在經肺投與 有效成分者。 成物為含有丄次投與量之 上之Γ用如601項記載之冷;東乾燥組成物在經肺投與 „^ 7凍乾挺組成物被收容於容器内,以 及經微粒化之粉末係用。 円 物可肼钿、+、# 有對衣谷态内之該冷凍乾燥組成 ^ 于奴以及將經微粒化之粉末狀a 凍乾無組成物從容器中排 飞 徘出之手段之裝置調製而成。 604·如態樣603項記恭々、人、土 + 上之梯爾甘士 .、。 々凍乾燥組成物在經肺投與 1 5 ^ - pr βπ …、且成物之哀變指數在0.05至 丄·〕&lt;粑圍内。 605·如態樣603項記恭令、人、土 + m # 、 々凍乾燥組成物在經肺投與 工I便用,其中,該;入淹# 9 / V東乾無組成物係藉由承受具有至少 2 m/sec之空氣速度及至少 ^ 擊,可渺&amp; $ ml/sec之空氣流量之空氣衝 # 了形成平均粒徑在1 〇微 以上之微粒者。 …下或有效粒子比率在⑽ 上之6Q3項記载之冷;東乾燥組成物在經肺投與 上之使用,其中,該冷凍乾 + 本、、且成物係猎由承受具有1至 3〇〇m/sec之空氣速度及至少 #τ « , ^ /Sec之空氣流量之空氣 丁#,可形成平均粒徑在i 〇 u木以下或有效粒子比率在 1 〇 /。以上之微粒者。 6〇7·如態樣6〇3項記载之人査 秋&lt; ~ /果乾燥組成物在經肺投與 上之使用’其中,該冷凌齡枵 也“組成物係藉由承受具有至少 315314 67 200418520 之空氣速度及至少2Gml/see之空氣流量之空氣衝 擊,形成平均粒徑| 10微米以下或有效粒子比率在10% 以上之微粒者。 8 ·如匕、樣603工員έ己載之冷滚乾燥組成物纟經肺投與 使用其中’ s亥冷凍乾燥組成物係藉由承受具有至少 l:’sec之空氣速度及17nU/sec至说/…之空氣流量之空 錢擊,形成平均粒徑纟1G微米以下或有效粒子比率在 1 0 %以上之微粒者。 609·如態樣603項記恭夕、人、占⑺ 戟之々凍乾爍組成物在經肺投盘 上之使用,其中,該冷;東乾燥組成物為藉由承受空氣衝擊了 =成^粒徑在5微米以τ或有效粒子比率在2 之微粒者。 6:.:態請項記載之冷來乾燥組 之使用’以,該冷來乾燥組成物 。 低分子藥物者。 ^做為有效成分之 6 11 ·如態樣603項記載之;人壶 之使用,#中,該冷;東㈣㈣物=、、且成物在經肺投與 白質類及核酸等高分子藥物。 頁效成刀之蛋 之使6用1:樣項'己载之冷;東乾燥組成物在經肺投金 之使用,/、中’心錢燥組成物包含、 保持於保持體狀態之核酸。 -有效成为之呈 613·如態樣61〇項記載 分子藥物以及載劑’該載劑為至少1選自:基效酸::低 315314 68 200418520 三肽及糖類組成之群者。 614·如態樣611項記 之使用,其巾,u 組成物在經肺投與 °次〜/來刼組成物#么 白質類及核酸等高分子藥物 ”、、有效成分之蛋 選自胺基酸、-肽、一:!载劑,該载劑為至少一種 \ —肽二肽及糖類組成之群者。 6 1 5 ·如態樣6 1 3項記载之A洁 7東乾文呆組成物在經肺投與 之使用,其中,該冷凍乾燥組成物 yv ^ Μ λ, c. ^ ^ 3做為有效成分之低 刀子樂物以及載劑,該載劑 舻始P^ 種選自疏水性胺基 酉文、馭水性一肽及疏水性三肽組成之群者。 616·如態樣614項記載之冷洁 少你田甘士 , 7東乾無組成物在經肺投與 之使用’其中’該冷;東乾燥έθ Λ' AL·. λ, ^ ^ 木組成物包含做為有效成分之蛋 白貝類及核酸等高分子藥物以 J该載劑為至少一種 k自&amp;水性胺基酸、疏水性-肢 肽及疏水性三肽組成之群 者0 成物在經肺投與 性組成物。 成物在經肺投與 燥粉末吸入裝置 入裝置。 成物在經肺投與 燥粉末吸入裝置 〇 成物在經肺投與 含非溶解狀態之 6 17.如態樣603項記載之冷凍乾燥組 之使用,其中,該冷凍乾燥組成物為水溶 61 8·如態樣603項記載之冷凍乾燥組 之使用,其中,該裝置係採用前述(3)章乾 中記載之態樣301或302項之乾燥粉末吸 619·如態樣618項記載之冷凍乾燥組 之使用’其中’該裝置係採用前述(3)章乾 中記載之態樣309項之乾燥粉末吸入褒置 620·如態樣603項記載之冷凍乾燥組 之使用’其中,該冷凍乾燥組成物係將包 315314 69 200418520 添加成分之組成液經冷凍乾燥而調製成,且具有下述特性 者: ⑴具有非粉末之塊狀形態; (ii)衰變指數在0.05至1.5之範圍内;以及 (in)藉由承受具有!至3〇〇m/sec之空氣速度及i7mi/sec 至15L/sec之空氣流量之空氣衝擊,可成為平均粒徑 在10微米以下或有效粒子比率在1〇%以上之微粒; 經微粒化之粉末’係使用具備可將上述空氣衝擊賦與 容器内之上述冷凍乾燥組成物之手段以及從容器排出經微 粒化之粉末狀冷滚乾燥組成物之手段之裝置調製而成。 ⑶.如態樣㈣項記載之冷;東乾燥組成物在經肺投與 之使用’其中,該空氣流量為1至25〇 m/sec。 622.如恶樣620項記載之冷凍乾燥組成物在經肺投盥 之使用,其中’該空氣流量為2〇ml/seU肌/㈣。”5 11 · Such as state 503> The composition of Dongganduolen contains nucleic acid. The method for pulmonary administration according to item 5, wherein the cold active ingredient is maintained in the state of the retainer 5 12. Item 509, the freeze-dried composition contains as a carrier the at least one member selected from the group. The documented method of pulmonary administration, wherein the low-molecular-weight drug and carrier of the cold active ingredient, amino acid, dipeptide, tripeptide, and carbohydrates are composed of 513. Such as 5101 Jg a soil, ..., 6 The method for administering via the lung, wherein the freeze-dried composition comprises ^ ^ Feng Xiaocheng's proteins and nucleic acid polymers and carriers, and the Panyu Λ carrier is at least one selected from amines. A group of amino acids, dipeptides, tripeptides and sugars. , 315314 64 200418520 5 1 4 · As in aspect 5] The method of pulmonary administration described in item 7 ts _, in which, the human freeze-dried composition contains "7 9 θ i, which is a low-molecular-weight drug that is effective to 7 knives As well as the carrier, the Shihai carrier is a group consisting of at least one day +, self-amplified water-based amino acid, hydrophobic dipeptide, and hydrophobic dipeptide. ^ 5. 如 忧 、 样 513 According to the method of pulmonary administration given by the workers, the cold m 4, ~, polymer strips such as proteins and nucleic acids and carriers that are effectively formed, and the carrier # he-pi… ... are up to ^ species A group consisting of a hydrophobic amino acid, a limbic dipeptide, and a hydrophobic tripeptide. The pulmonary administration method described in item # 503, wherein the freeze-dried composition is a water-soluble composition. Zhizhuo H The method of pulmonary administration described in item 5G3 is a method of administering microparticles into microparticles with an average particle size of 5 1/2, π + +, or less, or an effective particle ratio of 20% or more. 5 1 8. As sad as 5 〇3 Indian Gong Xi Mo 7 Gu _ 4rL 彳 shellfish. The method of pulmonary administration has been included, in which the device uses (3) dry powder Inhalation wear, dry powder inhalation device in the form of item 301 or 3 002 in the middle and early stages of the set of clothes. = 9 · The method of pulmonary administration as described in item 518 of item m, in which the device 4 is used (3 ) The dry powder inhalation device described in the form described in the chapter of the dry powder inhalation device ... 520 · The method of pulmonary administration as described in item 503, wherein the cold-bed drying composition will contain insoluble 1 f form The composition solution of the heart's ice plus ingredients is prepared by freeze-drying, and has the following characteristics: It has a non-powder morphology; (10 The index of decay is in the range of 0.05 to 15; and 315314 65 200418520 (iii ) By withstanding 1 to 300 m / sec working hole angle and 17 ml / sec to 15 L / sec air flow Effective particles: dry particles of 1 υ / ❹ or more; micronized powder, using the above-mentioned cold / easy-dried composition in a container, which can impart the impact of air lice on each elbow to the container. Prepared by a device that discharges the powdered freeze-dried composition 52L The method of pulmonary administration according to item 52G, wherein the air velocity is 1 to 250 m / sec. 522. The state of pulmonary administration according to item 520, wherein the air flow rate is 20 ml / sec to 10 L / sec. (6) Use of freeze-dried composition for inhaled pulmonary administration. Further, the present invention relates to use of freeze-dried composition in a non-powder state for inhaled pulmonary administration. The body contains: 601 · Freeze-dried composition is administered by inhalation through the lungs, where ', this cold health dry composition is prepared by freeze-drying a composition liquid containing non-dissolved added components by freeze-drying And has the following characteristics: (I) has a non-powdered morphology; (II) has a decay index of more than 0.05; and (iii) = withstands an air velocity of at least im / sec and at least 17 ml / sec. The air impact of the air / melon can be made into particles with an average particle size of less than 10 microns or a ratio of active particles of more than 10%; Q freeze-dried composition is powdered to have the above average particle size or have 315314 66 200418520 effect Particle ratio of fine particles to use. 602. If item 601 is described in terms of Gong Xi, Human, Soil ± m ^, and lyophilized composition, the active ingredient is administered via the lungs. The finished product contains Γ above the amount of administration, and is used as described in item 601. The east-dried composition is administered through the lungs. 7 The freeze-dried composition is contained in a container, and the powder is micronized.用 物 可 hydrazine 钿, +, # have the freeze-dried composition in the glutinous state ^ Yu slave and the means of lyophilizing the micronized powder a without composition from the container The device is prepared by 604. 603 items such as respect, human, soil, and Tirgans on the ground. 々 The freeze-dried composition is administered by the lung 1 5 ^-pr βπ ... The mourning index is within the range of 0.05 to 丄〕 & 粑. 605. Such as the 603 item, the order of congratulations, people, soil + m #, 々 lyophilized composition is used in lung administration, where The inundation # 9 / V Donggan-free composition is formed by withstanding an air velocity of at least 2 m / sec and at least ^ strikes, and the air flow of the air flow of $ ml / sec is average. Particles with a particle size of 10 micrometers or more.… Or as described in item 6Q3 of the effective particle ratio above ⑽; the use of East dry composition for pulmonary administration, its The freeze-dried + original, and the finished product is made of air Ding # bearing an air velocity of 1 to 300 m / sec and an air flow of at least # τ «, ^ / Sec, which can form an average particle size in Those with a particle size of less than or equal to 10% or more and an effective particle ratio of more than 10%. 6007. The person described in item 603, Chaqiu &lt; ~ / fruit dried composition on the pulmonary administration The use of the 'Ling Ling Ling' also "composition is formed by withstanding air impact with an air velocity of at least 315314 67 200418520 and an air flow of at least 2Gml / see to form an average particle size | 10 microns or less or effective particle ratio Particles above 10%. 8 · As a dagger, sample 603 workers carry the cold-rolled dry composition, which is administered by the lungs. The freeze-dried composition is used to withstand an air speed of at least 1: sec and 17 nU / sec. / ... The air flow of the air strikes to form particles with an average particle size of less than 1G microns or an effective particle ratio of more than 10%. 609 · As in 603 items, the use of freeze-dried composition of Gong Xi, Ren, and Zhan Zhi on the transpulmonary platter. Among them, the cold and dry composition is subjected to air impact. ^ Particles with a particle size of 5 microns and τ or an effective particle ratio of 2. 6:.: The use of the cold-drying group described in the item 'is used to dry the composition. Low molecular drugs. ^ As an active ingredient, 6 11 · As described in item 603; Use of human pot, # 中 , 此 冷; ㈣㈣ 物 =, and the product is administered to the high molecular weight drugs such as white matter and nucleic acid through the lung . The effect of the egg of the knife is 6 uses 1: sample 'self-loaded cold; the use of eastern dry composition in the lung investment, /,' heart and dry composition 'contains and maintains the nucleic acid in the state of the body . -Effectively become 613. The molecular drug and carrier as described in item 61. The carrier is at least 1 selected from the group consisting of: base acid :: low 315314 68 200418520 tripeptide and carbohydrate. 614. If used as described in item 611, the towel, the composition of which is administered through the lungs times // 来 刼 组合 物 #molecular substances and nucleic acid polymers, and the egg of the active ingredient is selected from amines Base, -peptide, 1: carrier, the carrier is a group consisting of at least one peptide dipeptide and saccharides. 6 1 5 · A Jie 7 Donggan Wen as described in item 6 1 3 The composition is used for pulmonary administration, in which the freeze-dried composition yv ^ Μ λ, c. ^ ^ 3 is used as a low-knife fun and carrier for the active ingredient. A group consisting of self-hydrophobic amine scriptures, water-soluble monopeptides, and hydrophobic tripeptides. 616 · Leng Jie Shao Tian Tian Shi Shi according to item 614, 7 Donggan No composition is administered via the lung The use of 'where' the cold; Dong drying θ Λ 'AL ·. Λ, ^ ^ wood composition contains protein shellfish and nucleic acids as active ingredients of high-molecular-weight drugs, and the carrier is at least one kind of k &amp; water A group consisting of amino acid, hydrophobic-limb peptide, and hydrophobic tripeptide 0 The composition is administered to the lung through the lung. The composition is administered to the lung through the dry powder inhalation device. The product is administered in the lung through a dry powder inhalation device. The product is administered in the lung including a non-dissolved state. 6. 17. The use of the freeze-drying group according to item 603, wherein the freeze-dried composition is Water soluble 61 8 · The use of freeze-drying group as described in item 603, in which the device uses the dry powder of item 301 or 302 described in Chapter (3) above, and 619 · as the item 618 The use of the freeze-drying group 'wherein' the device is the use of the dry powder inhalation device 620 in the state described in Chapter (3) of the dry state, and the use of the freeze-drying group in the state 603 'wherein the unit The freeze-dried composition is prepared by freeze-drying the composition liquid containing the added ingredients 315314 69 200418520 and having the following characteristics: ⑴ It has a non-powder morphology; (ii) The decay index is in the range of 0.05 to 1.5 ; And (in) By withstanding air impact with an air velocity of! To 300 m / sec and an air flow rate of i7mi / sec to 15 L / sec, the average particle diameter can be less than 10 microns or the effective particle ratio is 1 〇% of particles; The 'granulated powder' is prepared by using a device having a means for imparting the above-mentioned air impact to the freeze-dried composition in a container and a means for discharging the micronized powdery cold-roll-dried composition from the container. ⑶. Cold as described in item ;; Dong drying composition used in pulmonary administration ', where the air flow rate is 1 to 25 m / sec. 622. Freeze-dried composition described in item 620 in The use of pulmonary toilets, where 'the air flow is 20 ml / seU muscle / ㈣. "

(7)冷凍乾燥組成物在 劑之使用 製造吸入式經肺投與用乾燥粉末製 之冷凍乾燥組成物在 上之使用。該使用包 再者,本發明係關於非粉末狀態 製造吸入式經肺投與用乾燥粉末製劑 含在下文中揭示之具體態樣: …7凍乾秌組成物在製造吸入式經肺投與用乾燥粉 末衣d之使用’ 5亥冷凍乾燥組成物具有下述特性·· (i)係將包含非溶解狀能 &gt;、、夭 Λ 心之斗加成刀之組成液經冷凌乾焊 而調製成, 木 315314 70 200418520 (π)具有非粉末之塊狀形態, (^)衰變指數為〇·05以上,以及(7) Use of freeze-dried composition In the preparation of a freeze-dried composition made of dry powder for inhaled pulmonary administration, it is used. In addition, the present invention relates to the production of dry powder preparations for inhaled transpulmonary administration in a non-powder state, which contains the specific aspects disclosed below: ... The use of powder coating d. The freeze-dried composition has the following characteristics: (i) The composition liquid containing insoluble energy &gt;, 夭 Λ heart bucket addition knife is prepared by cold-drying dry welding Cheng, wood 315314 70 200418520 (π) has a non-powdered morphology, (^) decay index is above 0.05, and

Gv)猎由承受旦有至小 . 夕1 m/sec之空氣速度及至少i7 之空氣流量之空氣衝擊,可成為平均粒徑在Μ ㈣以下或有效粒子比率在」〇%以上之微粒;以及 :使:時,將該冷滚乾燥組成物經微粒化成具有上述平均 粒從或上述有效粒子比率。 7 0 2 ·如態樣7 〇 1項印都夕、人、杰 員。己載之冷束乾燥組成物之使用’其 中忒々凍乾燥組成物為含有丨次γ &amp;曰&gt; + , π 3 , 1人奴與1之有效成分者。 /(J3·如態樣701項却都夕、人、击从LO 投盥用耖p 、載之々凍乾紐組成物在製造經肺 〇用乾燥粉末製劑上之使用, 之妄傲% Ύ 為冷凍乾燥組成物 又、交才日數在〇·〇5至1·5之範圍内。 704·如態樣7〇1項記葡夕、入唾 投盥用# 、載♦凍乾燦組成物在製造經肺 技與用乾燥粉末製劑之使用,i 藉由承受且有至小2 / 、 5亥々凍乾燥組成物係 …旦 &quot;2m/sec之空氣速度及至少17m&quot;sec之 二“L里之空氣衝擊’可形成平均粒 效粒子比率在10%以上之微粒者。 心以下或有 705.如態樣7〇1項記載之 措彻田私β , 木也^木組成物在製造經肺 杈一用乾爍粉末製劑之使用,其 藉由承為且右Ί 、 4 &amp;凍乾燥組成物係 之”::至3〇°m/SeC之空氣速度及至少17—c 足工虱流$之空氣衝擊,可形成平 7〇6·如態樣701項記載之; 7東乾無組成物在製造妳肺 才又鉍用乾燥粉末製劑之使用,其 、、、工 /、 4々凍乾燥組成物係 315314 71 200418520 藉由承受具有至少lm/sec 空氣流量之空氣衝擊,可形成二=至少2一之 ^ , 取十均粒徑在1 〇微米以下哎右 效粒子比率在10%以上之微粒者。 次有 於广.如態樣701項記載之冷滚乾燥組成物在_肺 才又與用乾燥粉末製劑之使用 肺 夢由承-Μ 令,該冷;東乾燥組成物係 1…至少1m/sec之空氣速度及—至Gv) Hunting is capable of withstanding air impact of 1 m / sec and air impact of at least i7, and can become particles with an average particle size below M Μ or an effective particle ratio of "0% or more; and : At this time, the cold-roll dried composition is micronized to have the average particle size or the effective particle ratio. 7 0 2 · Such as the situation 〇 1 item India Du Xi, Ren, Jijie. The use of the cold-beam-dried composition which has already been loaded ', wherein the freeze-dried composition is one containing γ times & + &gt; +, π 3, 1 slave and 1 active ingredient. / (J3 · If the state 701 items are du Xi, people, hit the LO from the toilet, 载 p, lyophilized button composition used in the manufacture of dry powder preparation for pulmonary use,% arrogance% Ύ It is a freeze-dried composition, and the number of days for delivery is in the range of 0.05 to 1.5. 704. As the state 701, remember the evening of the night, enter the saliva, use #, and lyophilize the composition In the manufacture of transpulmonary techniques and the use of dry powder formulations, i can withstand freeze-drying compositions with a minimum of 2 /, 50 hrs ... once the air speed of 2m / sec and at least 17m sec bis "Air impact in L 'can form particles with an average particle-effect particle ratio of 10% or more. Below the heart or there may be 705. As described in Item 701, measures such as the private wood, wood also The use of dry powder formulations for the manufacture of transpulmonary branches is performed by the following methods: lyophilized composition, and lyophilized composition :: to an air velocity of 30 ° m / SeC and at least 17-c feet The air impact of the lice flow can form flat 706 · As described in item 701; 7 Donggan-free composition is used in the manufacture of your lungs and bismuth dry powder preparations, which 、、 工 / 、 4 Freeze-dried composition system 315314 71 200418520 By withstanding air impact with an air flow of at least lm / sec, it can form two = at least 2 to ^, take ten average particle size below 10 microns. Those with a right-effect particle ratio of more than 10%. Secondly, it is more extensive. As described in item 701, the cold-rolled dry composition described in item _ Lung Cai and the use of dry powder preparation Lung Meng You Cheng-M Order, the Cold; East dry composition system 1 ... at least 1m / sec air velocity and-to

以下或有效粒子比率在10%以上之微粒者。 U 708.如態樣701項記載之人 投與用乾燥粉末製劑之使用,::乾無組成物在製造經肺 猎由承受空氣衝擊,可形成平均粒徑在…、 為 粒子比率在2G%以上之微粒者。 …、以下$有致 投與用乾燥粉t二項:己載之冷;東乾燥組成物在製造經肺 包含做為有效成=二、=f + ’該冷;東乾燥組成物為 ~另双成分之低分子藥物者。 投與7用二項記載之冷滚乾燥組 含做為有二 用,其中’該冷;東乾燥組成物包 文為有效成分之蛋白質類及核酸等高分子華物。 投7G1項記載之冷;東乾燥、组成物在製造經肺 含做製劑之使用’其中,該冷滚乾燥組成物包 ’’’、成刀之呈保持於保持體狀態之核酸。 投與用乾= :之::乾燥組成物在製造經肺 為有效成分之低分子藥物以及裁劑,該載劑為至少— 315314 72 200418520 種込自胺基酸、二肽、三肽及糖類組成之群者。 投盘樣710項記載之冷床乾燥組成物在製造經肺 做 丈用 J a 東乾燥組成物包 :、有效成分之蛋白質類及核酸等高分子藥物以 W ’该載劑為至少一種 成之群者。 種、自胺基…肽、三肽及糖類組 投血7用:7=:12項記載之冷;東乾燥組成物在製造經^ 含做製劑之使用,其中’該峨燥組成物包 為有效成刀之低分子藥物 m is ό ^ 入執片j邊戟劑為至少一 種、自疏水性胺基酸、 者。 性一肽及疏水性三肽組成之群 7 1 5 .如態樣7彳q 投與用乾燥粉末制、δ之&amp;凍乾燥組成物在製造經肺 含做為有效成八Γ1之使用’其中’該冷;東乾燥組成物包 文成刀之蛋白質類及核 劑,該载劑為i小從 ^夂寺同么子樂物以及载 戟d馮至少一種選自 疏水性三肽組成之群者。&quot;^基酸m肽及 71 6·如態樣701項記葡夕、人、占士 投與用乾烊粉末制π 、° ~凍乾燥組成物在製造經肺 子乙/木知末製劑之使用,1 水溶性組成物。 /、 遠々凌乾燥組成物為 717.如態樣701項記載之冷 投與用乾焊於丈制 乾秌組成物在製造經肺 祀知和末製劑之使用,1 末製劑之肖# &gt; Τ /、Υ ’達經肺投與用,乾燥粉 d 粒之平均粒徑為5微 子比率為20%以上。 、乂下,或微粒之有效粒 71 8·如態樣701項記裁之、人、占 、 —凍乾燥組成物在製造經肺 315314 73 200418520 投與用乾燥粉末製劑之使用,其中 收容於衮% m ~凍乾紐組成物被 叹办万、谷态内,以及經微粒化之 内之A ;秦# r 4 1 末係用具備對於該容器 微粒化之粉Mm,/ 衝擊之手段以及將經 置$制乾燦組成物從容器中排出之手段之裝 置凋製而成。 丁 f又心衣 投與樣718項記載之冷滚乾燥組成物在製造經肺 粉:吸之使用,其中,該裝置係採用(3)乾燥 吸入裝置:早中§己載之形態項3。丨或3。2之乾燥粉末 投/用719項記載之冷;東乾燥組成物在製造經肺 ^ ^ A ^ ^ 亥衣置係採用(3)乾燥粉 :及入衣置之章t記載之形態項309之乾燥粉末吸入裳 721.如態樣7G1項記載之冷康乾燥組成物在製造 才又與用乾燥粉末製劑之使用,其中 來乾燥組成物: +使用具有下迷特性之冷 (二二:成包含非溶解狀態之添加成分之組成液經冷康乾 ^1)具有非粉末之塊狀形態; (111)衰變指數在〇 〇5至1·5之範圍内;以及 (⑴)藉由承受具有丨至300 m/sec之空氣速度及17_… 至15L/sec之空氣流量之空氣衝擊,可成為平均粒徑 在1 〇微米以下或有效粒子比率在丨〇%以上之微粒。 722·如態樣721項記載之冷凍乾燥組成物在製造經肺 315314 74 ZUU4l^520 投與用乾燥粉末製劑之使用 W / S 6 c ° 其中該空氣速度為】至250 組成物在製造經肺 氣流量為2 0 m I / s e c ^ 723.如態樣721項記載之冷凍乾燥 投與用乾燥粉末製劑之使用,其中該* 至 l〇L/sec 〇 〆二 (8)添加成分非溶解組成 末製劑戶彳+ # ^ ± 在製以5周製經肺投與用乾燥粉 衣片丨所而之令凍乾燥組成物之使用。 者本备明係關於—種添力σ成分非、、# # 使用。…:,粉末製劑所需之冷凌乾燥組成物之 溶解組成液,“St燥組成物時使用之添加成分非 調製方法,以及二凌”,使用彼等之冷康乾燥組成物之 燥粉末製劑之$制+ 勿之使用方法(經肺投與用乾 衣J之5周製方法)係如前述。 以下,列舉實施例具 於此等實施例。 且D月本务明,但本發明並不限 又,在以下之實施例中, 燥組成物(冷凍乾 务明之非粉末狀之冷凍乾 評價經微粉末化/仏 衷變指數以及有效粒子比率(係 述方法計算出f粉末製劑對送達肺之指標)依照下 &lt;农變指數之計算&gt; 在調製之非粉末 _ 中,經由容器之辟#之冷凍乾燥組成物(冷凍乾燥塊) ’商入1 ·〇 ml正己烷。將其用自動 315314 75 200418520 貝驗至/匕合器NS-8(Pasolina公司製)於3000 rpm約授拌 秒。將得到之混合溶液投入光路長 1 mm,光路寬1 〇 mm 之UV至(島津glc公司製)中,並快速地用分光光度計 (UV 240 ’島津製作所製)於測定波長5〇〇 nm測定該混合液 之濁度。將得到之濁度除以總處方量(有效成分與載劑之總 量(重量))所得之值做為衰變指數。 &lt;有效粒子比率之算出&gt; 鲁 將充填有調製之非粉末狀冷凍乾燥組成物之容器安裝 於乾燥粉末吸入裝置中。將使用該裝置並賦與特定之空氣 衝擊所微粉末化而得之粉末製劑於歐洲藥局方(Εύορκη Pharmacopoeia, Third Edition Supplement 200 15 pll3-ll5) 中記載之裝置A(二段式塵埃測定器··英國c〇pley公司製) 中直接排出。之後,分別回收裝入該裝置之第丨段及第2 之’谷媒藉由生物測疋法及HPLC等適於測定冷康乾燥 組成物中之有效成分之方法,定量第丨段及第2段之各溶 •媒中所包含之有效成分[Lucas #人之報告(pharm Res, 15(4),562_569(1998))及飯田等人之報 叫又可以期待送達肺之部分為^ 段(在該部分中所回收之空氣力學之粒徑為6·4 # m以 下)’通常達到其之第2段所回收之有效成分之比率稱為有 效粒子比率(可期待達到肺之量,即細粒比率),其被做為 评價經肺投與用之吸入劑之適用性之基準。 在下述之實施例及比較例中,定量第丨段及第2段各 含之有效成分之重量,並將得到之第2段中有效成分之重 315314 76 200418520 里除以被喷射之有效成分之總重量(第工段及第2段所含之 有效成刀之‘、重夏:以下稱為「第工段+第2段」),以得 到之值做為有效粒子比率(%)。又,原則上,在歐洲藥局方 中使用二段式塵埃測定器(英國Copley公司製)之情況,由 於規定空氣之吸弓丨流量為6〇L/min(即况㈣,因此下述 之實施例及比較例亦比照此。 i β幵八、邊』乾燥粉末吸入裝置(喷射型!) 本^月所用之噴射型乾燥粉末吸入裝置之一實施形態 用第1圖說明。 “米刀末吸入裝置’係將收容於容器】之底部之非粉 末性之單,或數次投與量之冷凍乾燥組成物2予以微粒化 並送達肺器官之处有疮红 二轧唷射型器具’其具備設有空氣喷射流 =⑽出流路4之針部5,有吸…且裝設在針部5 之基立而之吸氣構件7, H ^ ^ ^ w 圍4針邛5且兼具容器丨之保持 同狀女全罩8以及空氣壓送手段9。 空氣壓送年J5:q 、七土上 在風箱體1〇上設置附有為沒手隹動式且具備筒狀之風箱體10, 她3之吐出=有吸進間&quot;之吸進口 12以及附有吐 射流路3之吐出口 14設置在於針部5之空氣噴 3連通 而形成之接續口 15 ’並與空氣嘴射流路 且’在關閉吸進閥U之狀能,蕤士 於風箱體10使之收…山 狀心肖由施加壓縮力 一 二軋贺射流路3排出至容器1内。另 方面,若解除壓縮力,藉由 另 體10將伸茫I山 π相肢10之弹性復原力風箱 、吐出閥13成為關閉狀態且吸入閥丨丨打開, 315314 77 农疋空氣被導入風箱體1 0中。 使用遠乾燥粉末吸入裝置時, 1褒入筒狀安全罩8中,使針 目所示,將容器 並使空氣嘴射流路3及排出流路之口栓部h 在該狀態,若使空氣厂塑送手段9之風箱 ' 之内部連通。 從吐出口 該空氣將經由;:喷,^^ =前端朝向容以之冷“燥組絲^路3從針部5 厂令凌乾燥組成物2將成為微粒_針::該空氣衝 路4從吸氣構件7之吸 、、,由針七5之排出流 吸氣構件7之吸 。使用者(患者)藉由從 微粒可送達,者…吸入該微粒’冷凌乾燥組成物2之 器之口栓之材質並⑼, 對於本發明所使用之容 膠或紹等通常做為:容=化:如可任意選爾、塑 之材質。 市物及化合物之容器之口栓所使用 在該喷射型之明λ # 及入衣置中,設定成空氣喷射量為約20 如’容器之容量為的ς ι 、 〃 1 5 ml,空氣喷射流路3之孔徑(直徑) 為約丨^1&quot;111以及排出流路4之孔徑(直徑)為約丨.8 mm。 卜仁疋非限疋於此,空氣喷射流路3及排出流路4之孔 ^由方、視谷為之大小等較佳範圍而變動,所以並無特別限 制直彳二可彳文0·3至10 llm,較佳〇·3至7 mm,更佳0.5 至之範圍内適當選擇。 又,空氣壓送手段9,藉由調整風箱體10之壓縮速度, 可以凋即吸入投與所需要之微粒之排出量,又藉由該空氣 嘴射可以調整成使冷凍乾燥組成物2之大部分微粒化。 315314 78 200418520 實施见態复1乾燥粉末吸入裝置(自己吸入型 本發明所用之自己吸入型乾燥粉末 n 、衣置之一眘大&amp; 形態(其υ用第2圖說明。第2圖所 貝把 子乙/木粉末揭人梦 置,具備有吸引流路16及空氣導入流 、 ^ /之針部5、筒 狀安全盍8、以及有與吸引流路1 6連诵 &lt;及入口 18之吸 氣構件1 9,吸氣構件! 9與針部5 連結。 之及引机路16之基端側 使用乾燥粉末吸入裝置時,如第2圖所示,將容器丄Particles with a particle size below 10% or more. U 708. The use of dry powder preparations for human administration as described in item 701 :: Dry composition without the impact of air in the manufacture of lung hunting, can form an average particle size in the ratio of 2G% The above particles. …, The following two items have two types of dry powder for administration: cold already loaded; east dry composition is included in the manufacture of lungs as effective ingredients = two, = f + 'this cold; east dry composition is ~ another double Ingredients of low molecular drugs. The cold-rolling drying group described in the 7th item of administration 7 contains the dual-purpose, among which, the cold-drying composition includes the active ingredients such as proteins and nucleic acids and other macromolecules. Put the cold as described in item 7G1; the dryness of the composition, the use of the composition in the preparation of transpulmonary preparations', among which the cold-rolled and dried composition contains the nucleic acid that is maintained in the state of the holder. Dry for administration = :::: Dry composition is used in the manufacture of low-molecular-weight drugs and cut-offs that are active ingredients through the lungs. The carrier is at least — 315314 72 200418520 kinds of amidines, dipeptides, tripeptides, and sugars. Group of people. The cold-bed dried composition described in item 710 of the casting plate is used to manufacture the jaw-dried dry composition package for the lungs: active ingredients such as proteins and nucleic acids, and high molecular drugs. Group of people. Species, self-amino groups ... Peptide, tripeptide and carbohydrate groups 7 blood injection: 7 =: cold as described in item 12; Dong drying composition is used in the manufacture of preparations, where 'The Egan composition package is The effective low-molecular-weight drug that can be used as a knife is at least one self-hydrophobic amino acid. The group consisting of sex monopeptides and hydrophobic tripeptides 7 1 5. As in the case of 7 彳 q administration is made from dry powder, δ's & freeze-dried composition is used in the manufacture of transpulmonary as effective use of Γ'1 ' Wherein, the cold; the dried and dried composition includes the protein and the core agent of the knife, and the carrier is i Xiao Cong 夂 Lu Si Tong Mu Zi Le Wu and Feng Ji Feng, at least one selected from the group consisting of hydrophobic tripeptides By. &quot; ^ Methyl-peptide and 71 6 · As described in item 701, xi, ren, and james do π, ° ~ freeze-dried composition made from dried powder for the preparation of Lung Zi B / Zhi Zhi preparations For use, 1 water-soluble composition. The dry composition of Yuanling Ling is 717. As described in item 701, the cold injection and dry welding of the dried stem ingredients are used in the manufacture of lung preparations and final preparations. ; Τ /, Υ 'for menstrual administration, the average particle size of dry powder d particles is 5 neutrinos ratio is more than 20%. , His Majesty, or Effective Particles of Microparticles 71 8 · As stated in Item 701, Human, Occupation, and Use of Freeze-Dried Compositions for the Preparation of Dry Powder Preparations for Lung 315314 73 200418520 for Administration, Contained in 衮% M ~ The composition of freeze-dried button is smashed into the grain, in the valley state, and in the micronized A; Qin # r 4 1 Finally, it is provided with means to impact the micronized powder of the container, and It is made by means of a device for putting the dry-can composition out of the container. Ding Yiyi The cold-rolled and dried composition described in item 718 is used in the manufacture of transpulmonary powder: suction. Among them, the device adopts (3) drying. Inhalation device: as described in § 3 of the form already included.丨 or 3.2 The dry powder is put in / use the cold recorded in item 719; the east dry composition is used in the manufacture of lungs ^ ^ A ^ ^ Haiyizhi adopts (3) dry powder: and described in chapter t of the clothing into The dry powder of the form item 309 is sucked into the dress 721. The cold health dry composition described in item 7G1 is used in the manufacture and the use of the dry powder preparation, in order to dry the composition: + Use the cold (two 2: Constituting the composition liquid containing the added ingredients in a non-dissolved state through cold lyophilization ^ 1) It has a non-powdered morphology; (111) The decay index is in the range of 0.05 to 1.5; and (ii) borrow By being subjected to air impact with an air speed of ˜300 m / sec and an air flow of 17… to 15 L / sec, it can become particles with an average particle size of 10 microns or less or an effective particle ratio of 丨 0% or more. 722 · The freeze-dried composition described in item 721 is used in the manufacture of transpulmonary lungs 315314 74 ZUU4l ^ 520 The use of dry powder preparations for administration W / S 6 c ° Where the air velocity is] to 250 The composition is used in the manufacture of transpulmonary The air flow rate is 20 m I / sec ^ 723. The use of the dry powder preparation for freeze-drying administration as described in item 721, wherein the * to 10 L / sec. (8) added components non-dissolved composition Use of the final formulation household 彳 + # ^ ± freeze-dried composition of the dry powder-coated tablets for pulmonary administration for 5 weeks. This book is about the use of a kind of tianli σ component non-, # #. …: The dissolving composition solution of the cold-dried dry composition required for powder preparations, "the non-modulating method of the additive ingredients used in the St-drying of the composition, and Erling", using their dry-kang dry-dried powder preparations The method of $ system + don't use method (5 week system of drying clothes J for lung administration) is as described above. Examples are given below as examples. In the following example, the present invention is not limited, but the present invention is not limited. In the following examples, the dry composition (freeze-drying of non-powdered freeze-dried evaluation of freeze-dried resin is micronized / coated index and effective particle ratio. (Calculate the index of the powder preparation to the lungs by the method described below) According to the following calculation of the "agricultural index", in the prepared non-powder_, the freeze-dried composition (freeze-dried block) passed through the container No. ## Quoted 1.0 ml of n-hexane. It was stirred for about 2 seconds at 3000 rpm using automatic 315314 75 200418520 shell inspection / combiner NS-8 (manufactured by Pasolina). The resulting mixed solution was put into the optical path 1 mm in length, With a light path width of 10 mm from UV to (made by Shimadzu glc), the turbidity of the mixed solution was quickly measured with a spectrophotometer (UV 240 'made by Shimadzu Corporation) at a measurement wavelength of 500 nm. The obtained turbidity The value obtained by dividing the total prescription amount (the total amount (weight) of the active ingredient and the carrier) is used as the decay index. &Lt; Calculation of the effective particle ratio &gt; Filled with the prepared non-powder freeze-dried composition Container for dry powder suction Into the device. The powder preparation obtained by using the device and given a specific air impact to be micronized is described in the device A (second stage) described in the European Pharmacy Bureau (Εύορκη Pharmacopoeia, Third Edition Supplement 200 15 pll3-ll5) Type dust measuring instrument ·· made by Copley Co., Ltd. in the United Kingdom). After that, they were collected in the first and second stages of the device, and the second cereal grain was suitable for the measurement of Lengkang by bioassay and HPLC. Method for drying the active ingredients in the composition, quantifying the active ingredients contained in the solvents and media of paragraphs 丨 and 2 [Lucas # 人 的 报告 (pharm Res, 15 (4), 562_569 (1998)) and The report by Iida et al. Can also be expected to be delivered to the lungs in section ^ (the aerodynamic particle size recovered in this section is below 6.4 # m) 'usually reaches the active ingredient recovered in section 2 The ratio is called the effective particle ratio (the amount that can be expected to reach the lung, that is, the ratio of fine particles), and it is used as a criterion for evaluating the applicability of inhalants for pulmonary administration. In the following examples and comparative examples, , Quantify the effective results contained in paragraphs 丨 and 2 respectively Weight divided by the weight of the active ingredient in the second paragraph 315314 76 200418520 divided by the total weight of the active ingredient being sprayed (the effective knife included in paragraphs 2 and 2 ', heavy summer: the following (Referred to as "the first stage + the second stage"), and the obtained value is taken as the effective particle ratio (%). In addition, in principle, a two-stage dust detector (manufactured by Copley, UK) is used in the European Pharmacy Agency. In some cases, the flow rate of the suction bow of the air is 60 L / min (that is, the condition), so the following examples and comparative examples follow this. i β 幵 八, "side" dry powder inhalation device (jet type!) One embodiment of the spray type dry powder inhalation device used this month is described with reference to the first figure. "The rice knife powder inhalation device 'is a non-powder sheet or a freeze-dried composition 2 dosed in several doses, which is contained in the bottom of the container, and is micronized and delivered to the lungs. Type device ', which is provided with a needle part 5 provided with an air jet flow = ⑽out flow path 4, and has a suction member 7 which is installed on the base of the needle part 5, H ^ ^ ^ w surrounds 4 needles 邛5 It also has a container 丨 the same shape female full cover 8 and the air pressure feeding means 9. The air pressure feeding year J5: q, seven soils are provided on the wind box body 10 and are equipped with a no-hand movement type and have The cylindrical wind box 10, the discharge of her 3 = the suction inlet 12 with the suction chamber &quot; and the discharge outlet 14 with the discharge jet flow path 3 are provided at the spout 15 formed by the air jet 3 of the needle 5 communicating with each other 'And with the air nozzle jet flow path', when the suction valve U is closed, the warrior closes it in the wind box 10 ... The mountain-shaped heart is discharged into the container 1 by applying a compression force to the roller flow path 3 On the other hand, if the compressive force is released, the elastic restoring force bellows and the ejection valve 13 of the π-phase limb 10 extending over the mountain I will be closed by the other body 10 and the suction valve丨 Open, 315314 77 The agricultural air is introduced into the air box 10. When using the remote dry powder inhalation device, 1 into the cylindrical safety cover 8 so that the needle and eye are shown, the container and the air nozzle jet path 3 and In this state, if the outlet h of the outlet channel h is connected, if the inside of the air box of the air plant plastic conveying means 9 is communicated, the air will pass through the outlet;: spray, ^^ = the front end is cold and dry. The assembly thread 3 passes from the needle 5 to the factory, and the dry composition 2 becomes particles. Needle: The air rush path 4 is sucked from the suction member 7 and discharged from the needle 7 5 by the suction member 7 Suck. The user (patient) can be delivered from the particles, or ... inhale the particles and the material of the mouth plug of the device of the cold-drying composition 2 is combined. For the gelatin or plastic used in the present invention, it is usually as follows: = Chemical: If you choose any material, plastic. The mouth plug of the container of the city and the compound is used in the spray type of Ming λ # and the clothes set, and the air spray volume is set to about 20, such as' the capacity of the container is ς, 1 5 ml, air spray The diameter (diameter) of the flow path 3 is about ^^ 1 &quot; 111 and the diameter (diameter) of the discharge path 4 is about 1.8 mm. Brenzi is not limited to this. The holes ^ of the air jet flow path 3 and the discharge flow path 4 are changed by the preferred range such as the square and the size of the valley, so there are no special restrictions. It is appropriately selected within a range of 3 to 10 llm, preferably 0.3 to 7 mm, more preferably 0.5 to. In addition, the air pressure feeding means 9 can adjust the compression speed of the air box 10 to inhale and discharge the amount of particles required for administration, and the air nozzle can be adjusted to make the freeze-dried composition 2 Mostly micronized. 315314 78 200418520 Implementation of the compound 1 dry powder inhalation device (self-inhalation type self-inhalation type dry powder n used in the present invention, one of the clothes is cautious &amp; form (the υ is illustrated in Fig. 2). The ziyi / wood powder is exposed to dreams, and has a suction flow path 16 and an air introduction flow, a needle part 5 ^, a cylindrical safety tube 8, and a continuous recitation 16 &lt; and an entrance 18 for the suction flow path. The suction member 19, the suction member! 9 are connected to the needle portion 5. When the dry powder suction device is used on the base end side of the lead-in path 16, as shown in Fig. 2, the container 丄

裝入筒狀安全蓋8中,使針部5扎入容器 谷J 〜1 a並使 吸引流路16及空氣導入流路17與容器丨之内部連通。在 該=,藉患者之吸氣壓從吸入口 18經由吸引流二卜及 引容1§ 1内之空氣,同時使外氣從空氣導入流路1 7攻入因 此成為負壓之容器Μ。此時,#由作用於冷;東乾:組成 物2之空氣衝擊,將冷;東乾燥組成物2微粒化,調製得之 微粒經由吸引流路16從吸入口 18送達患者之肺器官内。 又,該乾燥粉末吸入裝置被設定成藉由患者之丨次吸 入,冷凍乾燥組成物2之大部分可微粒化並從吸入口 i 8 排出。又,雖然患者之;!次吸入之空氣流量為5至 分’以10至200 L/分為較佳,以1〇至1〇〇L/分為更佳, 不過,本發明之自己吸入型乾燥粉末吸入裝置可依照使用 之患者之呼吸能力而適當地變更設計。第2圖所示之吸入 裝置,係依照某患者之呼吸能力設定成容器之容量為約ι〇 ml’空氣導入流路17及吸引流路16之孔徑(直徑)為約15 賴者。藉此設定成藉由患者&lt; !次吸入,冷;東乾燥組成 315314 79 200418520 :2可大致热殘留地完全微粒化並從吸入口 1 8排出。 丄乾燥粉末吸入裝置(自己吸入型2) 本發明所用之自己吸入型乾燥粉末吸入裝置之一實施 形態(其2)用第3 m %日日 — 圖-兄月。弟3圖所示之乾燥粉末吸入裝 置’與第1圖所示之噴射型乾燥粉末吸入裝置從接續口 15 取下用方、壓达空氣之風箱體1 〇時之形態相同;又第1圖之 噴射型乾燥粉末吸入裝置之排出流路4相當於吸引流路 16 ’空氣噴射流路3相當於空氣導入流路17,有吸入口 6 之吸氣構件7 4目#於有吸人口 18之吸氣構件19。 卜口此使用s亥自己吸入型乾燥粉末吸入裝置時,以與 第2圖所示之乾燥粉末吸人裝置相同之要領,#患者之吸 氣職吸入口 18經由吸引流路16吸引容器1内之空氣, 同打,外氣仗$氣導入流路i 7流入藉此成為負壓之容器工 内藉由伴§亥空氣流入所產生之空氣衝擊,將冷柬乾燥 組成,2微粒化。之後,所得之微粒從吸人口 18送達患者 肺-S内X ’如上述患者之】次吸入之空氣流量為5 至3〇〇L/分,不過,第3圖所示之% m π &lt; 患者之呼吸能力設定成容器之容量為約5 mi,空氣導入流 路17之孔徑(直徑)為約丨.2職,以及吸引流路丨6之孔徑 (直徑)為約1.8 mm者。藉此設定成藉由患者之i次吸入, 冷滚乾燥組成物2之大部分經微粒化並從吸入口 18排出。 若構成此種自己吸入型之乾燥粉末吸入裝置,藉由將 風箱體10等空氣壓送手段9以裝卸自如之方式安裝在接續 口 15上,可將該自己吸入型之吸入裝置變更為喷射型。藉 315314 80 200418520 此’對同一個乾燥粉末吸入裝置,可按照所需適宜選擇自 己吸入型及喷射型之任一形態來使用。 以上之本發明之乾燥粉末吸入裝置可為自己吸入型或 噴射型之任一型,冷凍乾燥組成物可被構成為藉由選擇設 定空氣衝擊之大小,而形成平均粒徑為丨0微米以下(較佳5 微米以下)之微粒且大體無殘留之飛散。 81 200418520 入 32 :口 25之蓋子27。蓋子27以絞鏈21A連結於外殼本體 又’在盖子27上設置供確認容器!之裝填之窗μ。 在外殼21之壁部設置導入外氣用之導入口 29,在導 2”裝設逆止閥30。又,在外殼21之前部安裝咬嘴 夂嘴32,於不使用本乾燥粉末吸入裝 31用蓋子32a塞住。 ’將吸引口 、在針部5之基端部形成凸緣狀之隔壁部3 3,* 5 方Γ。又端:::W33内並開口 之吸引二延:隔壁部33之外周緣朝向… 31 I伸,错由將隔壁部33嵌進外 可將針部5忠驻卢从4 r八又2 1之W端部 十口&quot;女裝在外殼21内。藉由該安裝 、、泉方向與針部5之輛線方向_致。 A 1之軸 在保持部22中安裝供將容器ι從 起取出之取出體35,在該取出體%成。=底隸 之控制桿3 6。 ^成拉起谷器1用 保持部運轉部24 向往復移動用之機構使保持部22在外殼21之軸線方 機構部37具傷連結^ 7、#作機構部37之操作控制桿。 結在保持部22上,Π”。連結體39之-端用絞鏈40連 子27上。蓋子27 ' 之另一端用絞鏈41連結在蓋 之開關操作,使得保^為上述操作控制桿。藉由蓋子27 放下蓋子27之力部22沿著引導部23前進及後退。 點。亦即,從絞鏈2lA之作用點為第7圖之箭頭C所示之 絞鏈41之長度長,藉至/亥作用點之長度比從絞鏈21A至 曰由「槓桿原理」可以比針部5扎入容 82 200418520 器1之口栓U所需之力A丨 桿)27。 為小之力操作蓋子(操作控制 又,如第6圖所示,&lt; 、_ 末吸入裝置之第2導’、^成將空氣補助性地導入乾燥粉 冷凍乾燥組成物時,々— 在由及鳴3 2吸引粉末化之 嘴32之吸引口 31:」氣經由該第2導入路42流入直接咬 以無負擔地使用該袭:#活里低之患者或兒童患者可 導入路42。 〆乙、々末吸入裝置。X,可以省略第2 第2導入路42 隔壁部”,將導入溝4二:導入溝❿裝設在針部5之 進針部5之周壁部厂在周壁部34並將咬嘴32嵌 形成者。 #34,而由咬嘴U以及導入溝42a及仙 在咬嘴3 2與外Μ 9 1々日日 42之一 外双21之間形成小間隙43,第2導入路 之一 % 44經由間隙43 叉 山 王外口卜,弟2導入路42之 另一鳊45開口於咬嘴32之吸引口 31。 辟/ ’如第6圖所示’在吸引口 31設置有通氣孔46之 土 7。因此,縱使藉由吸引力不足等賦與冷凍乾燥組成物 八之空氣衝擊力變小’冷;東乾燥組成物2之_部分產生非 知末部分之情況,該非粉末部分通過壁47之通氣孔Μ之 時可以粉末化。 又,如第6(a)圖所示,針部5之空氣導入流路17之前 端口 17a比吸引流路16之前端口 16a更靠近冷束乾燥組成 物2。藉此,可儘可能地壓抑從空氣導入流路丨7之前端口 Ha流入容器丨内之空氣之流速降低’而可有效地將空氣 315314 83 200418520 衝擊賦與冷凍乾燥組成物2。又,由於針部5之吸引流路 1 6之鈾端口 1 6a比空氣導入流路1 7之前端口 1 7a遠離冷 束乾燥組成物2,在針部5之吸引流路16中進行吸引之 別’在容器1内可儘可能地將冷凍乾燥組成物2微粉末化。 因此’乾烯粉末吸入裝置係如下述使用。首先,如第 7圖所示,藉由拉起蓋子27並打開外殼21之出入口 25, 使保持部22後退靠近至外殼2 1之出入口 25。繼而將容器The cylindrical safety cap 8 is inserted, and the needle portion 5 is inserted into the container valley J to 1a, and the suction flow path 16 and the air introduction flow path 17 are communicated with the inside of the container 丨. At this time, the patient's inspiratory pressure is used to draw air from the suction port 18 through the suction flow 2 and the volume 1§1, and at the same time, the external air is introduced into the container M with negative pressure from the air introduction channel 17. At this time, # is caused by the air that acts on the cold; Donggan: the composition 2 is impacted by the air, and the cold; Donggan composition 2 is micronized, and the prepared particles are sent from the suction port 18 to the lung organ of the patient through the suction flow path 16. In addition, the dry powder inhalation device is set such that a large part of the freeze-dried composition 2 can be micronized by the patient's inhalation and discharged from the inhalation port i 8. Also, although the patient's! The air flow rate for each inhalation is 5 minutes to 10's to 200 L / minutes, and more preferably to 10 to 100L's minutes. However, the self-inhalation type dry powder inhalation device of the present invention can be used in accordance with Design the patient's breathing capacity appropriately. The inhalation device shown in FIG. 2 is set according to a patient's breathing capacity so that the volume of the container is about ιιml ml, and the diameter (diameter) of the air introduction flow path 17 and the suction flow path 16 is about 15 mm. With this setting, the patient &lt;! Inhalation, cold; east dry composition 315314 79 200418520: 2 can be completely particulated with approximately heat remaining and discharged from the inhalation port 18.丄 Dry powder inhalation device (self-inhalation type 2) One embodiment of the self-inhalation type dry powder inhalation device used in the present invention (the second) uses the 3m% day-to-day-figure-brother month. The dry powder inhalation device shown in Fig. 3 is the same as that when the spray-type dry powder inhalation device shown in Fig. 1 is removed from the connection port 15 and the compressed air box with air pressure of 10; The discharge flow path 4 of the spray-type dry powder inhalation device shown in the figure is equivalent to the suction flow path 16 ′ The air spray flow path 3 is equivalent to the air introduction flow path 17, and the suction member 7 having a suction port 6 Of the suction member 19. When using the dry powder inhalation device of the self-inhalation type, the same method as that of the dry powder inhalation device shown in FIG. 2 is used. The suction port 18 of the patient is sucked into the container 1 through the suction flow path 16 The air, the same air, and the external air are introduced into the flow path i 7 and flow into the container worker which becomes a negative pressure. The air is generated by the air inflow with the air inflow, and the cold card is dried to form 2 particles. After that, the obtained particles are delivered from the inhalation population 18 to the lungs of the patient X ′, and the air flow rate of the inhalation of the patient as described above is 5 to 300 L / min. However, the% m π shown in FIG. 3 &lt; The patient's breathing capacity is set to a container capacity of about 5 mi, the pore diameter (diameter) of the air introduction channel 17 is about 丨 2, and the pore diameter (diameter) of the suction channel 丨 6 is about 1.8 mm. As a result, it is set that the majority of the cold-roll-dried composition 2 is micronized by the patient's i inhalation and discharged from the inhalation port 18. If such a self-inhalation type dry powder inhalation device is constituted, the self-inhalation type inhalation device can be changed to a jet by attaching the air pressure feeding means 9 such as the air box 10 to the connection port 15 in a detachable manner. type. By 315314 80 200418520, the same dry powder inhalation device can be used in accordance with the needs of the user to choose one of the inhalation type and spray type. The above-mentioned dry powder inhalation device of the present invention can be any one of self-inhalation type or spray type, and the freeze-dried composition can be configured to form an average particle size of 0 micrometer or less by selecting and setting the size of air impact ( 5 micron or less particles are preferred and there is almost no residual scattering. 81 200418520 Access 32: Cap 27 of port 25. The lid 27 is connected to the case body with a hinge 21A. A container for confirming is provided on the lid 27! The loading window μ. An introduction port 29 for introducing outside air is provided on the wall portion of the casing 21, and a check valve 30 is installed on the guide 2 ". A mouthpiece 32 is installed on the front portion of the casing 21, and the dry powder inhalation device 31 is used without using the dry powder. Close it with the lid 32a. 'The suction opening, a flange-shaped partition wall portion 3 3, * 5 square Γ is formed at the base end portion of the needle portion 5. Another end: :: W33 and the opening of the second attraction opening: partition wall portion The outer edge of 33 faces ... 31 I extends, and the wrong part is to insert the next part 33 into the outer part, and the needle part 5 can be lodged from 4 to eight and 21 to the W end ten mouths &quot; women's clothing in the housing 21. Borrow Due to the mounting direction, the spring direction and the thread direction of the needle portion 5. The A 1 shaft is installed in the holding portion 22 to take out the extraction body 35 from which the container ι is lifted. The control lever 3 6. The mechanism for pulling up the holding device for the trough 1 is 24. The mechanism for reciprocating the holding part 22 on the axis of the housing 21 is 37, and the connecting part 37 is broken. Operate the joystick. Attach to the holder 22, Π ". The -end of the connecting member 39 is connected to the connector 27 with a hinge 40. The other end of the cover 27 'is connected to the cover with a hinge 41 to operate the switch, so that the above-mentioned operation control lever is maintained. The force portion 22 of the cover 27 is lowered by the cover 27 to advance and retreat along the guide portion 23. point. That is, the action point of the hinge 21A is the length of the hinge 41 shown by the arrow C in FIG. 7, and the length of the borrow point / interaction point is greater than that from the hinge 21A to the "lever principle". The part 5 is inserted into the volume 82 200418520 and the force required by the mouth bolt U of the device 1 is 27). Operate the lid for small force (Operation control, as shown in Fig. 6, &lt;, _ 2nd end of the inhalation device), when introducing air supplementally into the dry powder freeze-dried composition, 々— 在Youming 31 attracts the suction mouth 31 of the powdered mouth 32: "The gas flows into this bite via the second introduction path 42 to bite directly to use the attack without burden: #patients or children with low living conditions can be introduced into the path 42. 〆B and inhalation device. X, you can omit the 2nd and 2nd introduction channel 42 next wall ", the introduction groove 42: the introduction groove is installed in the needle wall 5 of the needle inlet 5 and the peripheral wall of the needle factory is in the peripheral wall 34 and the mouthpiece 32 is embedded in the formation. # 34, and a small gap 43 is formed between the mouthpiece 32 and the outer double 21 by the mouthpiece 32 and the outer M 9 1 the next day 42 by the mouthpiece U and the introduction groove 42a and the immortal. One of the second introduction paths 44 is via the gap 43. Fork of the King of the Fork, the other one of the second introduction path 42 is opened at the suction port 31 of the mouthpiece 32. / / 'as shown in Figure 6' at the suction port 31 is provided with the soil 7 of the vent hole 46. Therefore, even if the freeze-dried composition Ya is given an air impact force by the lack of attractive force, etc. In the case where the _ part of the product 2 is a non-known part, the non-powder part can be powdered when it passes through the vent hole M of the wall 47. As shown in FIG. 6 (a), the air of the needle part 5 is introduced into the flow path. The port 17a before 17 is closer to the cold beam drying composition 2 than the port 16a before the suction flow path 16. This can suppress as much as possible the flow velocity of the air flowing into the container from the port Ha before the flow path 丨 7. It can effectively apply air 315314 83 200418520 shock to freeze-dried composition 2. In addition, the uranium port 16a of the suction flow path 16 of the needle 5 is farther from the cold beam drying than the port 17a before the air introduction flow path 17 The object 2 is sucked in the suction flow path 16 of the needle part 5 'The freeze-dried composition 2 can be powdered as much as possible in the container 1. Therefore, the' dryene powder inhalation device is used as follows. First, As shown in FIG. 7, by pulling up the lid 27 and opening the entrance 25 of the casing 21, the holding portion 22 is moved backward to approach the entrance 25 of the casing 21. Then, the container

1以口栓1 a向前之方式安裝在保持部22中。接下來如第8 圖所不’藉由放下蓋子以關閉外殼2 1之出入口 2 5,利用 連、、、。體39將保持部22朝針部5之方向壓入並使針部5之 础立而扎入容器1之口栓丨a,以使針部5之吸引流路丨6及 工氣導入流路1 7與容器1之内部連通。接下來,藉由患者 之吸氣壓從咬嘴32之吸引口 31經由針部5之吸引流路Η 吸引谷态1内之空氣。此時容器j内成為負壓且逆止閥% 打開,外氣經由針部5之空氣導入流路17流入容器丨内。 猎此,在容器1内產生空氣衝擊,冷凍乾燥組成物2經微 步化6周製之微粒經由吸引流路1 6從吸引口 3 1送至串者1 is installed in the holding portion 22 in a manner such that the spigot 1 a is forward. Next, as shown in Fig. 8, by closing the lid to close the entrance 2 5 of the housing 21, use the connection ,,,, and so on. The body 39 presses the holding portion 22 in the direction of the needle portion 5 and puts the foundation of the needle portion 5 into the mouth bolt of the container 1 丨 a so that the suction flow path of the needle portion 5 and the working gas are introduced into the flow path 1 7 communicates with the inside of the container 1. Next, the air in the valley state 1 is sucked by the suction pressure of the patient from the suction port 31 of the mouthpiece 32 through the suction flow path Η of the needle part 5. At this time, the inside of the container j becomes a negative pressure and the check valve% is opened, and the outside air flows into the container 丨 through the air introduction flow path 17 of the needle portion 5. In this case, air impact is generated in the container 1, and the freeze-dried composition 2 is fine-grained for 6 weeks, and the particles are sent from the suction port 3 1 to the stringer through the suction flow path 16

之肺器官内。使用後,拉起蓋子且保持部22靠近外嗖U 之出入口 2 5後,用控制桿3 6拉起取出體3 5並將^抑 從保持部22取出。 、各裔1 另一方面,縱使從咬嘴32之吸引口 3 1將介* 口口 工乳吹進容 器1内,微粒化之冷凍乾燥組成物2向外部之排 ^ $將舍香 到逆止閥3 0擋住。 又’雖然如上述患者之1次吸入之空氣流量通常在 315314 84Inside the lung organs. After use, the cover is pulled up and the holding portion 22 is close to the entrance and exit 25 of the outer sleeve U. Then, the lever 35 is used to pull up the take-out body 35 and remove it from the holding portion 22. On the other hand, even if the suction mouth 3 1 from the mouthpiece 32 is blown into the container 1, the micronized freeze-dried composition 2 is discharged to the outside ^ $ 将 香香 至 逆The check valve 30 is blocked. Also, although the air flow rate of a patient's inhalation is usually 315 314 84

O JZ.U 至300 L/分鐘之範圍内,但 裝置可依照患者之呼吸^ 0至第10圖所示之吸入 -1,空氣導入流路17之 設定成容器之容量為約5 路W之口徑(直捏)為約;直徑)為約2.5mm,吸引流 吸入,冷凍乾燥組成物 猎由心者之1次 3 1排出。 大部分將經微粒化並從吸引口 乾燥粉末吸入裝置(自 第11圖至第13圖所示。 入聖)之其他實施形態例如 第Π圖所示之乾 箭頭所示,將操作體48 ‘轉:::置(自己吸入型4),如 方向。未圖示出之保持 口土设置在外殼21之圓周 其扣合之隨動構件,葬±4。轉邛之機構部具有螺旋溝及與 持部22變換為向針部9 5之卡作版48之回轉運動,可以將保 48之迴轉角度為、約18() ^轴線方向直線運動。又,操作體 又,第12圖及第13 吸入型5),係將環 不之乾燥粉末吸入裝置(自己 21中,未圖示出之 *體49迴轉自如地安裝在外殼 藉由操作體49之问絲、運轉部之機構部具有送料螺旋, 之軸線方向直線運動。 將保持部22變換為向針部5 後部自由取出者。 ”、一 22係形成為可從外殼2 1之O JZ.U to 300 L / min, but the device can breathe according to the patient's breath ^ 0 to the inhalation shown in Figure 10-1, the air introduction channel 17 is set to a capacity of about 5 channels W The caliber (straight pinch) is about 2.5mm; the diameter is about 2.5mm. The suction stream is sucked in, and the freeze-dried composition is hunted by the heart person once and discharged. Most of the other embodiments of the powder inhalation device (shown from FIG. 11 to FIG. 13) which are powdered and dried from the suction port are shown in the dry arrow shown in FIG. Turn ::: Set (self-inhalation type 4), such as direction. The holding hole (not shown) is provided on the circumference of the casing 21, and the follower member which is fastened is buried by ± 4. The turning mechanism part has a spiral groove and a turning motion that is converted to the card making plate 48 to the needle part 95 by the holding part 22, and the turning angle of the turning 48 can be linearly moved about 18 () ^ axis direction. In addition, the operating body, FIG. 12 and 13 suction type 5), is an inhaling device for sucking dry powder (not shown in the figure 21). The body 49 is rotatably mounted on the housing and is operated by the operating body 49. The mechanism part of the wire and operation part has a feeding screw, and the axis direction moves linearly. The holding part 22 is transformed into a person who can freely take out the back part of the needle part 5. ", 22 is formed to be able to be

將為基因I n ^入用Ik性脂質俨 (inVitr〇gen 公 、版之 Llp〇fectAMjrNE 2〇〇( J衣)72 // g及為 入与貝體DNA之pEGFp_C2 315314 85 200418520 (Clontech公司製)24 //g添加至為細胞培養液之〇ρτι_ MEM I無血清培養基(Invitr〇gen公司製,伊格氏最少必須 培養基之改良培養基)1200 //丨中,並懸浮混合,在該培養 液存在下形成複合體。該複合體之幾何學平均粒徑用動態 光散射光度計(ELS-8000,大塚電子公司製)測定。接下來, 將包含該複合體之懸浮液各100//1分別添加混合於1〇個 容器(筒徑0 18mm)中(檢體數:1〇),其中各容器預先收容 L-白胺酸溶於水之水溶液(5 mg/ml)4〇〇 #丨。之後,使用棚 狀冷凍乾燥機(LY〇VAC GT-4,LEYB〇LD公司製)進行冷 凍乾燥,對於得到之非粉末狀冷凍乾燥組成物(冷凍乾燥 塊)’计异出衰變指數。接下來,將含有得到之非粉末狀冷 凍乾燥組成物(冷凍乾燥塊)之容器安裝在被設計成空氣噴 射流路3之孔徑為0 12 mm,排出流路4之孔徑為必18 之喷射型乾燥粉末吸入裝置(具有可供給空氣量約2〇ml2 風箱體10 ’參照實施形態例1,第1圖)中。 確認藉由將空氣量約20ml從吸入裝置導入容器内(賦 與由空氣速度約35m/sec及空氣流量約4〇ml/seCi空氣所 產生之衝雀)’可將谷裔内之非粉末狀之冷凍乾燥塊微粒 化,並瞬間從容器經由微粒排出流路4噴射排出。使用安 裝有為人工肺型空氣呼吸器(美國Amherst Pr〇cess Instrument公司製,R.W.川彻:抑關心㈣…Techn〇i〇gy, 72-78( 1 993))(測定條件,呼吸速率·· 6〇L/min;呼吸體積: L加速19)之粒度为布什(氣膠分析儀(aer〇sizer):美國 Amherest Process Instrument 公司製,Rw Niven 315314 86 200418520The gene I n ^ Ik sex lipid (inVitrogen, public version of LlpfectfectjjrNE 2〇〇 (J clothing) 72 // g and pEGFp_C2 315314 85 200418520 (made by Clontech) ) 24 // g is added to 〇ρτι_ MEM I serum-free medium (manufactured by Invitrogen, an improved medium for Igor's minimum required medium) 1200 // 丨, which is a cell culture medium, and suspended and mixed. A complex is formed in the presence of the complex. The geometric average particle diameter of the complex is measured with a dynamic light scattering photometer (ELS-8000, manufactured by Otsuka Electronics Co., Ltd.). Next, each of the suspensions containing the complex is 100 // 1. 10 containers (diameter: 0 18 mm) (sample number: 10) were added and mixed, and each container contained an aqueous solution of L-leucine dissolved in water (5 mg / ml) 400 # in advance. Then, freeze drying was performed using a shed-type freeze dryer (LYOCV GT-4, manufactured by LEYBOLD), and the obtained non-powder freeze-dried composition (freeze-dried block) was used to calculate an abnormal decay index. Next , Containing the obtained non-powder freeze-dried composition (cold Freeze-drying block) The container is installed in a spray-type dry powder inhalation device (with an air supply volume of about 20ml2) designed to have an air jet flow path 3 with a hole diameter of 0 12 mm and a discharge path 4 with a required 18 hole diameter. For the cabinet 10 ', refer to Embodiment Example 1, FIG. 1). Confirm that about 20 ml of air is introduced into the container from the inhalation device (apply air at a speed of about 35 m / sec and an air flow rate of about 40 ml / seCi. The generated punching bird) 'can granulate non-powder freeze-dried blocks in the descent, and instantly eject them from the container through the particle discharge flow path 4. Use an artificial lung-type air respirator (Amherst Pr, USA) 〇cess Instrument Co., Ltd., RW Kawasawa: Suppression of concern ... Technology, 72-78 (1 993)) (Measurement conditions, respiration rate · 60L / min; respiration volume: L acceleration 19) Particle size is Bush (aerosizer): manufactured by Amherest Process Instrument, USA, Rw Niven 315314 86 200418520

Pharmaceuticai Techn〇1〇gy,72_78(i993))將其回收,測定經 U粒化之粒子之粒度分佈,並從其算出空氣力學平均粒徑 (// m± SD)。將以非溶解狀態存在於懸浮液中之粒子之幾 何子平均粒後,及各冷凍乾燥組成物之衰變指數,及從該 衣置噴射之粒子之空氣力學平均粒徑加土 5〇)示於表工 中。 &lt;表1&gt; 冷;東乾無組成物 幾何學之平衰變指數 均粒控(μηι)Pharmaceuticai Technology, 72-78 (i993)) was collected, and the particle size distribution of the U-granulated particles was measured, and the aerodynamic mean particle size (// m ± SD) was calculated therefrom. The geometric mean particle size of the particles existing in the suspension in an undissolved state, the decay index of each freeze-dried composition, and the aerodynamic mean particle size of the particles sprayed from the clothes are shown in Figure 5). Watchmaker. &lt; Table 1 &gt;Cold; Donggan no composition Geometric flat decay index Uniform particle control (μηι)

LipofectAMINE2 000+PEGFP-C2 + 白胺酸 0.827 空氣力學之平 均粒徑(μηι土SD, MMAD) °·1 86 1.726 士 1.491 。士表1所不’頒不衰變指數為〇 · j %之非粉末狀冷; 乾塊,肖由空氣速度約35111/咖及空氣流量約偏&quot;μ 之空,所產生之衝擊而衰,變,形成為空氣力學之平均粒; 為5微米以下之適於經肺投與之微粒狀乾燥粉末製劑。^ ^較在冷㈣燥前之試料為非溶解狀態(在其中為^ :怨),精由在本發明中所規定之特定空氣衝擊,可以㈣ 能調製適於經肺投與之微粒化乾燥粉末之冷 : 物,亦即顯示縱使在冷凍乾燥前-太&amp; BB ^ K忒枓為非溶解狀態,4 本兔明之經肺投與用乾燥粉末吸入系統中亦適 叮 效地經肺投與。又,藉由使用癌抑制劑基因吻^ 纖維症膜貫通型調節蛋白(cftr)&amp; 展匕- 使用之質體腿(卿叫可將能得^^實果^ 315314 87 200418520 或反義分子等藉由經肺投與導入體内。所以本發明之經肺 才又a用乾秌粉末吸入系統被認為可有效地利用做為基因治 療。 。 Α施例2、比毯例1 將為基口 $入用㈣性脂質體之Lip〇fectAM;[NE 2000 (Invitrogen公司製)72“及〇Ug〇冰να ι〇“(大塚製藥 公司製)1〇 Vg,於opti_MEMi無血清培養基(invitMga 丨公司製,伊格氏最少必須培養基之改良培養基)存在下混合 懸浮,以形成複合體。該複合體之幾何學平均粒徑用動^ 光散射光度計(ELS-8000,大塚電子公司製)測定。接下來, ^包含該複合體之懸浮液各1〇〇//1分別添加混合於⑺個 容器(筒徑0 18 mm)中,其中各容器預先加入^白胺酸溶 於水調製而成之L-白胺酸水溶液(5 mg/ml) 4〇〇 #卜調製得 冷凍乾燥用試料(實施例2)。又,關於比較例,用葡聚糖 4〇之水溶液(5mg/ml)400 代替上述卩白胺酸水溶液, 並同樣地調製冷凍乾燥用試料(〗〇個)(比較例丨)。 之後,各個試料用棚狀冷凍乾燥機(LY〇VAc gT-4, leybold公司製)進行冷;東乾燥,對於得到之非粉末狀冷 凍乾燥組成物(冷凍乾燥塊)計算出衰變指數。接下來,將 含有非粉末狀冷凍乾燥組成物(冷凍乾燥塊)之容器安裝在 被设計成空氣噴射流路3之孔徑為0 i ·2 _,排出流路4 之孔徑為0 1 ·8 之喷射型乾燥粉末吸入裝置(具有可供 給空氣量約20 ml之風箱體1〇,參照實施形態例1,第工 圖)中。 315314 88 200418520 …:果,對於實施例2之冷,東乾燥組成物,確認藉由 將空氣量約20ml從吸人裝置導μ器内(賦與由空氣速度 約3 5m/sec及空氣流量約4〇ml/sec之空氣所產生之衝擊), 可將容器内之非粉末狀之冷;東乾燥塊微粒化,並瞬間從容 益經由微粒排出流路4噴射排出。與實施合&quot;同樣地,使 用安裝空氣呼吸器(美目Amherst〜咖-加咖公司 衣)(測疋ir、件,呼吸速率:飢/他;呼吸體積:况;加 ^ 19)之粒度分布計(氣膠分析儀(aerosizer):美國LipofectAMINE2 000 + PEGFP-C2 + Leucine 0.827 The average aerodynamic particle size (μηι SD, MMAD) ° · 1 86 1.726 ± 1.491. The non-powder-like cold of dry sheet 1 with a non-decay index of 0 · j% is awarded by the air table, which is caused by the impact of the air velocity of about 35111 / ca and the air flow rate of about μ. Change into an aerodynamic average particle; a granular dry powder formulation suitable for pulmonary administration of less than 5 microns. ^ ^ Compared with the sample before cold dehydration, it is in a non-dissolved state (where ^: grudge). It is precisely impinged by the specific air specified in the present invention, and can be adjusted to be micronized and dried suitable for pulmonary administration. The powder is cold: it shows that even before freeze-drying-too & BB ^ K 忒 枓 is in a non-dissolved state, the rabbit powder is administered through the lung in the dry powder inhalation system. versus. In addition, by using the cancer suppressor gene to kiss the fibrosis membrane penetrating regulatory protein (cftr) &amp; spreading dagger-the plastid legs used (Qing Jiao will be able to get ^ ^ fruit ^ 314 314 87 200418520 or antisense molecules It is introduced into the body by pulmonary administration. Therefore, the dried powder inhalation system of the present invention is considered to be effectively used as gene therapy. A Example 2 is more basic than blanket example 1. LipasefectAM for liposomes for liposome; [NE 2000 (manufactured by Invitrogen) 72 "and 〇Ug〇 冰 ναι〇" (manufactured by Otsuka Pharmaceutical Co., Ltd.) 10Vg, in opti_MEMi serum-free medium (invitMga 丨Co., Ltd., a modified medium with at least Iggler's medium) in the presence of a suspension to form a complex. The geometric mean particle size of the complex is measured with a light scattering photometer (ELS-8000, manufactured by Otsuka Electronics Co., Ltd.) Next, ^ 100 // 1 each of the suspension containing the complex is added and mixed into a container (tube diameter 0 18 mm), wherein each container is prepared by adding ^ amino acid in water L-leucine aqueous solution (5 mg / ml) 4〇〇 # prepared cold A sample for drying (Example 2). For the comparative example, an aqueous solution of dextran 40 (5 mg / ml) 400 was used in place of the above-mentioned leucine acid aqueous solution, and freeze-drying samples (0) were prepared in the same manner. (Comparative Example 丨) Then, each sample was cooled with a shed-type freeze dryer (LYOVAC gT-4, manufactured by leybold); dried in the east, and calculated for the obtained non-powder freeze-dried composition (freeze-dried block). The decay index is obtained. Next, a container containing a non-powder freeze-dried composition (freeze-dried block) is installed in an air jet flow path 3 having a hole diameter of 0 i · 2 _ and a discharge flow path 4 having a hole diameter of 0 1 · 8 in a spray-type dry powder inhalation device (with a wind box 10 capable of supplying about 20 ml of air, refer to Embodiment 1 and the drawing). 315314 88 200418520…: For Example 2, Cool and dry the composition. Confirm that the impact caused by air with an air volume of about 35 m / sec and air flow of about 40 ml / sec is introduced by introducing 20 ml of air from the suction device into the μ device. ), Can be the non-powdered cold in the container The Dong dry block is atomized and ejected from Rongyi via the particle exhaust flow path 4 instantly. As with the implementation, an air respirator (Meme Amherst ~ Ka-Ka Coffee Co., Ltd.) is used. Pieces, breathing rate: hunger / he; breathing volume: condition; plus ^ 19) particle size distribution meter (aerosizer): United States

Amherest i&gt;r〇cess化价職⑽公司製㈣其回收測定經微 粒化之粒子之粒度分佈,並從其算出空氣力學平均粒徑U m士 SD)。 另方面’比較例1之冷凍乾燥組成物,藉由空氣速 度約 3 5 rn / s e c乃处与、六曰/ l 4 久工軋流直約40ml/sec之空氣所產生之衝 ^兀王未分散,因此無法測定空氣力學之平均粒徑。 將以非〉谷解狀態存在於各懸浮液中之粒子之幾何學平 均粒徑,各冷;φ p z L t v果乾燥組成物(實施例2、比較例1)之衰變指 數,及從該裝晋+ &amp;夏f射之粒子之空氣力學平均粒徑(# m土 SD) 示於表2中。 89 315314 200418520 &lt;表2&gt; 組成 1勿幾 均粒徑(μπι) 均粒徑(pm:tSD, 實施例2) 1.19 LipofectAMINE2 000 + Olig〇_RNA + 白胺酸 ^ ^ 1)1.19 LipofectAMINE2 000 + Olig〇-RNA + _葡聚糖40 __MMAD) , °· 165 「^η士 1·4—96—^ 〇·002 法測定 如表2所示,顯示衰變指數為〇165之非粉末狀冷凍 乾燥塊(實施例2)’與實施例1同樣地,縱使在冷凍乾燥前 之試料為非溶解狀態(在其中為懸浮狀態),藉由空氣逮度 約35m/sec及空氣流量約4〇mi/sec之空氣所產生之衝擊而 朋壞,形成為空氣力學之平均粒徑為5微米以下之適於經 肺投與之微粒狀乾燥粉末製劑。 、^ 相對於此,顯示衰變指數為〇.〇〇2之非粉末狀冷束乾 鲁燥塊(比較例υ,藉由上述衝擊,完全未分散及微粒化,不 適於η周製成為經肺投與用之乾燥粉末製劑。 實施例3至5、比較例2 將為基因導入用活性型樹狀分子(陽性聚合物)之 Superfect (Qiagen 公司製)36〇# g 及 〇Hg〇 RNA(大塚製藥 公司製)5 // g (實施例3,比較例2)或為質體dna之 PEGFP-C2 (Clontech 公司製)24/z g(實施例 4 及 5),於 OPTI-MEM 12G(^1存在下混合懸浮,以形成複合體。該 315314 90 200418520 複合體之幾何學平均粒徑用動態光散射光度計作ls_ _〇 ’大塚電子公司製)或雷射折射及散射式粒度分佈測定 裝置(SALD-3000J,島津製作所製)測定。 接下來,將包含此等複合體之懸浮液各l00/zl,如表 斤丁刀別斗加於I有預先調製之L-白胺酸水溶液(5 mg/ml) 400 &quot; 1之容器(筒徑0 18 mm)(實施例3及4)中以及 裝有溶解乳糖之水溶液(5mg/ml)彻…之容器(筒徑㈣ _)(實施例5)中(對於各實施例,使用1〇個容器),調製 付冷康乾力呆用試料。又關 、了寸又,關於比較例,用葡聚糖40之水溶 液(5 mg/ml)400 “ 1 抑秩與 # 。&gt; τ ^ A I代替貝軛例3之L-白胺酸水溶液,並 同樣地調製冷凍乾燥用試料(10個)(比較例2)。 之後,對於用棚狀冷凍乾燥機(LY0VAc gT_4, LEYBOLD公司製)進行冷;東乾燥所得到之非粉末狀冷滚乾 燥組成物(冷康乾燥塊),計算出衰變指數。接下來,將含 有得到之非粉末狀冷;東乾燥組成物(冷凍乾燥塊)之容器安 裝在被設計成空氣噴射流路3之孔徑為012随,排出流 路4之孔徑為01.8 _之噴射型乾燥粉末吸入裝置(且有 :供給空氣量…之風箱體10,參照實施形態例;及 弟1圖)中。 其結果’對於實詞3, 4及5之冷;東乾燥組成物,確 遇精由將空氣量約2〇ml從吸入裝置導入容器内(賦與由空 氣速度約35m/sec及空翁、、六曰从^ 叹工虱*置約40ml/sec之空氣所產生 衝擊),可將容器内之非於古 非心末狀之冷凍乾燥塊微粒化,並 間從容器經由微粒排屮、、六竹 + 徘出机路4噴射排出。與實施例1同樣 315314 91 200418520 地’使用安裝空氣呼吸器(美國Amherst Process Instrument 公司製)(測定條件,呼吸速率:60L/min ;呼吸體積:1L ; 加速· 19)之粒度分布計(氣膠分析儀(aerosizer):美國 Amherest Process Instrument公司製))將其回收,測定經微 粒化之粒子之粒度分佈,並從其算出空氣力學平均粒徑(# m 土 S D ) 〇 另一方面,比較例2之冷凍乾燥組成物,藉由空氣速 籲度約35m/sec及空氣流量約4〇ml/sec之空氣所產生之衝 擊,完全未分散,因此無法測定空氣力學之平均粒徑。 將以非溶解狀態存在於各懸浮液中之粒子之幾何學平 均粒徑,各冷凍乾燥組成物(實施例3至5及比較例〇之衰 變指數,及從該裝置喷射之粒子之空氣力學平均粒徑(〆⑴ 土 SD)示於表3中。(Amherest i &gt; manufactured by Kasei Kogyo Co., Ltd.) The particle size distribution of the micronized particles was measured and recovered, and the aerodynamic mean particle size (U m ± SD) was calculated therefrom. On the other hand, the freeze-dried composition of Comparative Example 1 was produced by air at a speed of about 35 rn / sec, and the air flow was about 40ml / sec. It is dispersed, so the aerodynamic average particle diameter cannot be measured. The geometric mean particle diameter of the particles existing in each suspension in a state other than the cleavage state, each cold; the decay index of φ pz L tv dried composition (Example 2, Comparative Example 1), and from this device The aerodynamic mean particle size (# m 土 SD) of the particles injected by Jin &amp; Xia F is shown in Table 2. 89 315314 200418520 &lt; Table 2 &gt; Composition 1 Average particle size (μπι) Average particle size (pm: tSD, Example 2) 1.19 LipofectAMINE2 000 + Olig〇_RNA + Leucine ^ ^ 1) 1.19 LipofectAMINE2 000 + Olig〇-RNA + _glucan 40 __MMAD), ° · 165 "^ η ± 1.4-96- ^ 〇 · 002 The method is shown in Table 2 and shows a non-powder freeze-drying method with a decay index of 0165. The block (Example 2) 'is the same as in Example 1. Even though the sample before the freeze-drying is in a non-dissolved state (in which it is suspended), the air capture rate is about 35 m / sec and the air flow rate is about 40 mi /. The impact caused by the air of sec is bad, and it is formed into a particulate dry powder preparation suitable for pulmonary administration with an aerodynamic average particle size of 5 micrometers or less. In contrast, the display decay index is 0.00. 〇2 non-powdered cold beam dry lump (Comparative Example υ, due to the above impact, completely undispersed and micronized, not suitable for η weeks to be made into a dry powder preparation for pulmonary administration. Examples 3 to 5 Comparative Example 2 Supe, an active dendrimer (positive polymer) for gene introduction rfect (manufactured by Qiagen) 36〇g and oHgRNA (manufactured by Otsuka Pharmaceutical Co., Ltd.) 5 // g (Example 3, Comparative Example 2) or PEGFP-C2 (manufactured by Clontech) which is a plastid DNA 24 / zg (Examples 4 and 5), mixed and suspended in the presence of OPTI-MEM 12G (^ 1) to form a composite. The geometric average particle size of the 315314 90 200418520 composite was determined by dynamic light scattering photometry as ls__〇 ' (Made by Otsuka Electronics Co., Ltd.) or a laser refraction and scattering particle size distribution measuring device (SALD-3000J, manufactured by Shimadzu Corporation). Next, each of the suspensions containing these complexes is 100 / zl, such as the surface of a knife. The bucket was added to a container (tube diameter 0 18 mm) (Examples 3 and 4) with a previously prepared aqueous L-leucine solution (5 mg / ml) 400 &quot; 1 and an aqueous solution (5 mg of dissolved lactose) / ml) in a container (tube diameter _ _) (Example 5) (for each example, 10 containers were used) to prepare a sample for cold and dry work. , Aqueous solution of dextran 40 (5 mg / ml) 400 "1 抑 rank and #" &gt; τ ^ AI instead of the L-leucine aqueous solution of yoke example 3. 10 samples were prepared in the same manner (Comparative Example 2). Thereafter, the samples were cooled with a shed-type freeze dryer (LY0VAc gT_4, manufactured by LEYBOLD); the non-powdered cold-rolled dry obtained by Toray Dry Composition (Lengkang dry block), calculate the decay index. Next, install the container containing the obtained non-powdered cold; east-dried composition (freeze-dried block) in a jet designed to have an air jet flow path 3 with a hole diameter of 012, and an ejection flow path 4 with a hole diameter of 01.8 mm. Type dry powder inhalation device (and: the air box 10 that supplies the amount of air, etc., refer to the embodiment example; and Figure 1). As a result, 'for the words 3, 4 and 5 are cold; the dry composition is dry, and the amount of air is about 20ml from the inhalation device into the container (the air speed is about 35m / sec and the air wing ,, Sixth, from the impact of ^ sighing lice * placed at about 40ml / sec air), the non-palatine and non-heart-shaped freeze-dried blocks in the container can be atomized, and the particles are discharged from the container through the particles. Bamboo + hover out of the machine path 4 jet ejection. The same as Example 1, 315314 91 200418520, a particle size distribution meter (aerosol) using an air respirator (manufactured by Amherst Process Instrument, USA) (measurement conditions, respiration rate: 60L / min; respiration volume: 1L; acceleration · 19) (Aerosizer: manufactured by Amherest Process Instrument Company, USA)) It was collected, the particle size distribution of the micronized particles was measured, and the aerodynamic average particle size (# m 土 SD) was calculated from it. On the other hand, a comparative example The freeze-dried composition of 2 is completely undispersed by the impact of air having an air velocity of about 35 m / sec and an air flow rate of about 40 ml / sec, so the average particle size of aerodynamics cannot be measured. The geometric mean particle diameter of the particles present in each suspension in an undissolved state, the decay index of each freeze-dried composition (Examples 3 to 5 and Comparative Example 0, and the aerodynamic mean of the particles sprayed from the device The particle size (〆⑴ soil SD) is shown in Table 3.

315314 92 200418520 &lt;表3&gt; 冷凍乾燥組成物幾t學之平_ n - 均粒控(μπι) 均粒徑(pmitSD, MMAD)_ 實施例 3 ) Superfect 11.12 + 〇ligo- RNA+ 白 胺酸 4)Superfect+pEGF 3.74 P-C2+白胺酸 0.225 0.189 1.578 土 1.403 1.646 土 1.420 5)Superfect + pEGF 3.74 P-C2 +乳糖 0.080 2.848 士 1.837 比較例 0.003 完全不分散無 法測定 2)Superfect + OHg〇 11.12 -RNA+葡聚糖40 如表3所示’顯示衰至0.225(G 變指數為0.080以上)之非斗入古此人 )之非心末狀冷凍乾燥塊,與實施例 同樣地,縱使在冷凍乾燥前 矜…、 / 引之°式枓為非溶解狀態(在其中/ % &gt;予狀恶)且很易凝集成幾 .女子之千均粒徑為11微米之; 子,亦可糟由空氣速度約3 ^ ^ ^ 、、 ee及空氣流量約40ml/Sl 之工乳所產生之衝擊而崩 為5 «丰τ , 形成為空氣力學之平均粒二 為议^下之適於經肺μ 相對於此,顯示衰變指數為&quot;㈡狀“…劑。 (比較叫藉由上述衝擊…之J粉末狀冷康乾^ 調製成為經肺投與用 ::77政及微粒化,不適; 足乾燥粉末製劑。 結果,縱使在冷凍乾 卞月j之忒枓為非溶解狀態(在其 315314 93 為懸净狀態),藉由在本 以提供能,月中所規疋之特定空氣衝擊,可 敌t…周I適於經肺投與 組成物,亦即,在太心- 冷凍乾燥 中亦適用,sφ ?又努用乾知粉末吸入系統 了有效地經肺投與。又,藉由使 基因ρ53(適用於肺癌)及囊 W Ρ制蜊 rrFTp^ ⑴)及展胞性纖維症膜貫通型調節蛋白 基因(適用於囊胞性纖維症)等代替本實施例所 二(_FP_e2)’可將能得心療效果之基因或 反義刀子导糟由經肺投與導入體内。又,〇iig〇_RNA為 RNAi(RNA干擾物)之一,係 ' 务 你』適用RNAi技術之雙股 RNA藉由導入對應於標的基因之短雙股rnA,可以特異 f生抑制祆的基因之傳信RNA之機能,亦可適用於肺癌等之 治療。 所以,本發明之經肺投與用乾燥粉末吸入系統被認為 於基因治療中可有效地利用。 •實施例6 將為基因導入用活性型樹狀分子之Superfect (Qiagen 公司製)360 v g及〇lig0-RNA(大塚製藥公司製)5 # g,於 OPTI-MEM I 1200 // l(GibcoBRL公司製)存在下混合懸 浮’以形成複合體。該複合體之幾何學平均粒徑用雷射折 射及散射式粒度分佈測定裝置(SALD-3000J,島津製作所 製)測定。接下來,將包含此等複合體之懸浮液各i 00 #!, 分別添加於裝有預先調製之L-纈胺酸水溶液(2.5 mg/ml) 400 &quot; 1之容器(筒徑0 18 mm)(l〇個)中,調製得冷凍乾燥 94 315314 200418520 用试料。之後,用棚狀冷凍乾燥機(LY〇VAC gT_4, LEYBOLD公司製)進行冷;東乾燥,對於所得収非粉末狀 冷凍乾燥組成物(冷凍乾燥塊),計算出衰變指數。 。接下來,⑩含有得到之非粉末狀冷康乾燥組成物(冷束 乾煉塊)之容器安裝在被設計成空氣喷射流路3之孔徑為 0 1.2 mm ’排出*路4之孔徑為必J ·8 mm之噴射型乾燥粉 末吸入裝置(具有可供給空氣量約2〇ml之風箱體ι〇,參照 實施形態例1及第1圖)。 結果,對於實施例6之冷束乾燥組成物,確認藉由將 空氣量約20ml從吸入装置導入容器内(賦與由空氣速度約 3 5m/sec及空氣流量約4〇ml/sec之空氣所產生之衝擊广可 將容器内之非粉末狀之冷;東乾燥塊微粒化,並瞬間從容哭 經由微粒排出流路4噴射排出。與實施例i同樣地,使用 女叙空氣呼吸器(美國Amhem Ργ〇_8 &amp;价細如公司 製κ測定條件,呼吸速率:飢/min;呼吸體m速: 19)之粒度分布計(氣膠分析儀(aer〇sizer):美目—咖 ss Instrument公司製))將其回收,測定經微粒化之粒 孝度刀佈,並攸其异出空氣力學平均粒徑 SD) 〇 一 將以非溶解狀態存在於各懸浮液中之粒子之幾何學平 均粒仫’及各冷凍乾燥組成物之衰變指數,及從該裝置噴 射之粒子之空氣力學平均粒徑(Wm± SD)示於表4中。、 315314 95 200418520 &lt;表4&gt; μ ~_-_ 變指數空氣力學之平 __ ^m) 均粒徑(μπι士SD, ^TsTTpeTfect + OlTg 1 3T9 ~~~~~— MADJ_ 〇-Ι^Α +纈胺酸 0.275 1.589±1.553 如表 4 所示,-;- # ρ 又‘數為0.275之非粉末狀冷凍 乾燥組成物(冷凍乾燥塊),每 一灵苑例1同樣地,縱使在冷 凍乾燥前之試料為非溶觫&amp; At / i b %狀恶(在其中為懸浮狀態)且很易 旋集成幾何學之平均粒徑為 ~ Μ从未之粒子,亦可藉由空氣 速度約35m/sec及空氣流量約 里4 40ml/sec之空氣所產生之衝 擊而衰變,形成為空氣力學夕巫仏丄 一 予之平均粒徑為5微米以下之適 於經肺投與之微粒狀乾燥粉末製劑。 以上之實施例2至6之紝罢ls — _ &lt;、、、。果顯不,與貫施例1同樣地, 縱使在冷凍乾燥前之試料為非 、丁十馬非/谷解狀態(在其中為懸浮狀 態),藉由在本發明中所規定之特定空氣衝擊,可以提供能 調製成適於經肺投與之微粒化乾燥粉末之冷床乾燥組成 物,亦即顯示縱使添加成分斟、、六 &gt; ^ 力乂刀對/谷媒而言係不溶性或難溶 性,在本發明之經肺投盥用齡如。 一用也^木粉末吸入系統中亦適用, 且可有效地經肺投與。 實施例7至8 分別調製騰島素(重組人類胰島素結晶,比利時 Biobras公司製’比活性:26.4u/mg)(在實施例7中為〇.2 mg’在實施例8中$ ! mg)溶於鹽酸水溶液所得之水溶液 以及表5所示各種載體溶於精製水所得之溶液,若將彼等 315314 96 200418520 心 添加比率混合’可以得到各個懸浮狀態之懸 ’于次。该懸洋液所包含之粒子之幾何學平均粒徑用 射及散射式粒度分佈測定裝置(SALD-3000J,島津f作 製)測定。 衣作所 接下來,將該懸浮液充填於容器(筒徑018 mm)中,田 ^狀冷’東乾燥機(LY〇VAC GT_4,leyb〇ld公司製)進&quot; 冷凍乾燥。對於得到之非粉末狀冷凍乾燥組成物(冷凍: 塊)計算出衰變指數。接下來,將充填非粉末狀冷康乾2 成物之容器(筒徑0 18 mm)安裳在被設計成空氣導入^路 =自之ΓΓ為01 ·&quot;mm且吸引流路16之孔徑為〇 ·&quot;咖 自己吸入型乾燥粉末吸入裝置(參照實施形態例3及第3 =)。使用其並藉由二段式塵埃測定器(英國c〇pla公司 製)(對於冷凍乾燥塊賦與空氣速度約95m/sec及空氣^旦 =29 5 mi/sec之空氣所產生之衝擊),計算出有效粒子二^ (%)。將以非溶解狀態存在於各懸浮液中之粒子之幾何學平 句粒;L,各冷凍乾煉組成物之衰變指數及有效粒子比率 示於表5中。 °) 315314 97 200418520 平均ί,朋展有效粒子 ^极經指數比例(%) /令/東乾燥組成物 ^_Ιμνη) /)騰島素 0.2mg+ 白胺酉ϊ 〇Τ52^ 0·1η^+ 精胺酸 0.042 mg °*292 95.3 (PH6.5) 57.9 8)騰島素1 mg+苯基丙胺酸 〇.63 〇-6mg +精胺酸 〇.iimg(pH6.4) °*238 如表5所示,顯示衰變---- 凍乾燥組成物(冷凍乾燥塊),縱使Α 之非知末狀々 非溶解狀態之有效成份(騰島素),二:燥前之試料包含 =中易於微粒化’而可調製成適於經肺投與之乾燥粉 t施例9 $ 1 1 分別調製胰島素(重組人類胰島 曰 J尔、、、口曰曰,比利時315314 92 200418520 &lt; Table 3 &gt; Freeze-dried composition ji Xuepingping_ n-average particle size control (μπι) average particle size (pmitSD, MMAD) _ Example 3) Superfect 11.12 + 〇ligo- RNA + leucine 4 ) Superfect + pEGF 3.74 P-C2 + Leucine 0.225 0.189 1.578 P 1.403 1.646 P 1.420 5) Superfect + pEGF 3.74 P-C2 + Lactose 0.080 2.848 ± 1.837 Comparative Example 0.003 Does not measure completely without dispersion 2) Superfect + OHg〇11.12- As shown in Table 3, RNA + dextran 40 is a non-heart-shaped freeze-dried block that shows a non-dominated ancient person who declines to 0.225 (G change index is greater than 0.080) as in the example. Forehead ..., / Introduced ° formula is in a non-dissolved state (in which /% &gt; pre-shaped evil) and easily condensed into a few. Women's thousand-average particle size is 11 microns; son, can also be damaged by air The speed of about 3 ^ ^ ^, ee, and the impact of the working milk with an air flow of about 40ml / Sl collapsed into 5 «Feng τ, the average particle size formed as aerodynamics is the best suitable for lung μ relative Here, it is shown that the decay index is "㈡". (Compared to J by the above impact ... Lenticular Lengkang ^ is formulated to be administered via the lungs: 77 and micronized, uncomfortable; dry powder formulation. As a result, even after freeze-drying the j month is in an undissolved state (in its 315314 93 is Suspended state), by providing specific energy in the month, the specific air impact specified in the month can be t ... Week I is suitable for pulmonary administration of the composition, that is, also suitable for Taixin-freeze-drying Sφ? It also uses the dry powder inhalation system to effectively administer through the lungs. Moreover, by making the gene ρ53 (applicable to lung cancer) and cysts (made from rrFTp ^ ⑴), and cell spreading fibrosis membrane through-type regulation A protein gene (suitable for cystic fibrosis) instead of the second (_FP_e2) of this embodiment can be used to introduce a gene or an antisense knife that can achieve cardiac effect from the lung into the body. Also, 〇iig〇_ RNA is one of RNAi (RNA interfering substances). It is a 'double-stroke' RNA suitable for RNAi technology. By introducing a short double-stranded rnA corresponding to the target gene, it can specifically inhibit the function of the signaling RNA of the gene. Can also be applied to the treatment of lung cancer, etc. Therefore, the pulmonary administration of the present invention The dry powder inhalation system is considered to be effective for gene therapy. • Example 6 Superfect (manufactured by Qiagen) 360 vg and lig0-RNA (manufactured by Otsuka Pharmaceutical Co., Ltd.), which are active dendrimers for gene introduction 5 # g, mixed and suspended in the presence of OPTI-MEM I 1200 // l (manufactured by GibcoBRL) to form a complex. The geometric average particle diameter of the composite was measured using a laser refracting and scattering type particle size distribution measuring device (SALD-3000J, manufactured by Shimadzu Corporation). Next, each of the suspensions containing these complexes i 00 #! Were separately added to a container (prepared with an aqueous L-valine acid solution (2.5 mg / ml) 400 &quot; 1 (bar diameter 0 18 mm) ) (10 pieces), prepared as freeze-dried samples for use in 94 315314 200418520. After that, it was cooled with a shed-type freeze dryer (LY0VAC gT_4, manufactured by LEYBOLD); dried in the east, and a decay index was calculated for the obtained non-powder freeze-dried composition (freeze-dried block). . Next, the container containing the obtained non-powdered cold-kang dry composition (cold bundle dry smelting block) is installed in the air jet flow path 3 with a hole diameter of 0 1.2 mm 'the diameter of the discharge * path 4 is required J · 8 mm spray-type dry powder inhalation device (with an air box capable of supplying air of about 20 ml, refer to Embodiment Example 1 and Figure 1). As a result, it was confirmed that the cold beam drying composition of Example 6 was introduced into the container from the suction device with an air volume of about 20 ml (applied to an air chamber with an air speed of about 35 m / sec and an air flow rate of about 40 ml / sec. The generated impact can widen the non-powder-like coldness in the container; the East dry block becomes micronized, and is instantly ejected and ejected through the particle exhaust flow path 4. As in Example i, a female air respirator (Amhem, USA) is used. Ργ〇_8 & The price is as fine as the company's κ measurement conditions, respiration rate: hunger / min; respiration rate m: 19) particle size distribution meter (aerosizer): Meme—coffee ss Instrument Manufactured by the company)) Recovered, measured the micronized knives of the filial piety, and measured the aerodynamic mean particle diameter SD) 〇 The geometric average of the particles that will exist in each suspension in an undissolved state Granules' and the decay index of each freeze-dried composition, and the aerodynamic mean particle size (Wm ± SD) of the particles sprayed from the device are shown in Table 4. , 315314 95 200418520 &lt; Table 4 &gt; μ ~ _-_ Variable exponential aerodynamic level __ ^ m) Average particle size (μπι SD, ^ TsTTpeTfect + OlTg 1 3T9 ~~~~~ — MADJ_ 〇-Ι ^ Α + Valinic acid 0.275 1.589 ± 1.553 As shown in Table 4,-;-# ρ and a non-powder freeze-dried composition (freeze-dried block) having a number of 0.275, the same as in Example 1 of each spiritual garden. The samples before freeze-drying are non-soluble &amp; At / ib% (e.g. in a suspended state), and the average particle diameter of the integrated geometry is ~ M never, can also be determined by air velocity 35m / sec and air flow of about 4 40ml / sec. The impact of air decays, forming aerodynamics. The average particle size is 5 micrometers or less, which is suitable for pulmonary administration. Powder formulation. The above examples 2 to 6 ls — _ &lt; ,,,, etc., but the results are not the same as in Example 1, even if the sample before the freeze-drying is Fei, Dingma Mafei / Valley The solution state (in which it is suspended) can be modulated by the specific air impact specified in the present invention. The composition was dried on a cold bed of micronized dry powder administered by the lung, that is, it showed that even if the added ingredients were added, the squeegee was insoluble or hardly soluble to / cereal media. The age of the lung is as follows. It can also be used in the wood powder inhalation system, and can be effectively administered through the lungs. Examples 7 to 8 respectively modulate Tengdaosu (recombinant human insulin crystals, manufactured by Biobras, Belgium). Activity: 26.4u / mg) (0.2 mg 'in Example 7; mg in Example 8), an aqueous solution obtained by dissolving in an aqueous hydrochloric acid solution, and a solution obtained by dissolving various carriers shown in Table 5 in purified water, If they are mixed with 315314 96 200418520, the ratio of each suspension state can be obtained. The geometric mean particle size of the particles contained in the suspension is measured by a radiation and scattering particle size distribution device (SALD-3000J , Manufactured by Shimadzu Corporation). The next step is to fill the suspension in a container (cylinder diameter 018 mm), and place it in a field-shaped cold 'East dryer (LYOVAC GT_4, manufactured by leybold). Freeze-dried. For non-powder obtained Freeze-dried the composition (freeze: block) to calculate the decay index. Next, a container filled with non-powdered cold Kanggan 2 products (tube diameter 0 18 mm) Ansang is designed to introduce air ^ road = since ΓΓ is 01 · mm, and the pore diameter of the suction flow path 16 is 0. The self-inhalation type dry powder inhalation device (refer to Embodiment Examples 3 and 3). Using it and using a two-stage dust tester (manufactured by Copla, UK) (applying an air velocity of about 95 m / sec and air impact of air denier = 29 5 mi / sec to the freeze-dried block), Calculate the effective particle size ^ (%). The geometric properties of the particles present in each suspension in an undissolved state are shown in Table 5. L, the decay index and the effective particle ratio of each freeze-dried composition are shown in Table 5. °) 315314 97 200418520 average, effective active particles ^ polar warp index ratio (%) / order / East dry composition ^ _Ιμνη) /) Tengdaosu 0.2mg + white amine 〇Τ52 ^ 0 · 1η ^ + fine Amino acid 0.042 mg ° * 292 95.3 (PH6.5) 57.9 8) Tensin 1 mg + phenylalanine 0.63 0-6 mg + arginine 0.1mg (pH6.4) ° * 238 as shown in Table 5 Display, display decay ---- freeze-dried composition (freeze-dried block), even though the active ingredient (Tengdaosu) in the non-dissolved state of A is insoluble, two: the sample before drying contains = easy to micronize 'And can be made into a dry powder suitable for pulmonary administration Example 9 $ 1 1 Modulate insulin separately (recombinant human islets called Jer, ,, and mouth, Belgium

Biobras公司製,比活性:26.4 U/mg)l ma〜从技 溶於鹽酸水溶液 所得之溶液以及苯基丙胺酸〇·5 mg溶於精製水所得之溶 液,將彼等混合,若藉由氫氧化鈉調整各種pH值,可以 得到各種懸浮狀態之懸浮液。該該懸浮液所包含之粒子之 幾何學平均粒徑用雷射折射及散射式粒度分佈測定裝2 (SALD- 3000J,島津製作所製)測定。 、 接下來,將該懸浮液充填於容器(筒徑0丨8 mm)中,用 棚狀冷;東乾燥機(LYOVAC 〇 丁,LEYB0LD公司製)進行 315314 98 200418520 幸乞*品。大' 塊)出、^到之非粉末狀冷來乾燥組成物(冷凌乾燥 出衣文指數。接下來,將充填非粉末狀冷凍乾燥也 成物之衮哭(兮斤 ^ °°问從必18 mm)安裝在被設計成空氣喷射流路 I孔經Α ,Λ Ί 〇 :.mm且流出流路之孔徑為0 1.8 mm之喷射 ,粉末吸入装置(具有可供給空氣量約20ml之風 制使用其並藉由二段式塵埃測定器(英國€〇ρΐπ公 二對於冷;東乾燥塊賦與空氣速度約35油“ &amp;空氣流量 — Sec之空氣所產生之衝擊”計算出有效粒子比率 ^ /I非溶解狀態存在於各料液中之粒子之幾何學平 H各冷;東乾燥組成物之衰變指數及有效粒子比率 示於表6中。 (/〇) &lt;表6&gt; 酸 〇.5mg (ρΗ6·0) 0.39 0.36 75.1 72.0 1〇)胰島素1 mg +苯基丙 0.55 胺酸 〇.5mg (ρΗ6·4) · 11)騰島素1 mg +苯基丙 0.61 jL!^g.5mg (ρΗ6·6) __ 如表示,顯示衰 乾燥組成物(冷床乾燥塊),縱使冷;東乾燥前之:料::’東 溶解肤態之有效成份(胰島素),但藉由上述空氣衝二3非 :器中易於微粒化,可調製成適於經肺投與之:::末= 例 12 至 13 315314 99 200418520 分別調製胰島素(重組人類胰島素結晶,比利時 Bl〇bras公司製,比活性·· 26.4 U/mg)0.1 mg溶於鹽酸水溶 液所得之水,谷液以及表7所示各種載體溶於精製水所得之 溶液,將彼等混合並用氫氧化鈉調整pH值,可以得到各 们b浮狀恶之%浮液。該懸浮液所包含之粒子之幾何學平 均粒径用雷射折射及散射式粒度分佈測定裝置(SALD、 3〇〇〇J ’島津製作所製)測定。 接下來’將該懸浮液充填於容器(筒徑0丨8 mm)中,用 棚狀~凍乾燥機(LY〇VAC GT_4,leyb〇ld公司製)進行 東乾秌對於得到之非粉末狀冷凍乾燥組成物(冷凍乾燥 塊)5十异出衰變指數。接下來,將充填非粉末狀冷;東乾燥組 成物之容器(筒徑0 18 mm)安裝在被設計成空氣導入流路 17之孔徑為4 1.99 mm且吸引流路16之孔徑為0 。己吸入型乾燥粉末吸入裝置(參照實施形態例3及第3 3)。使用其並藉由二段式塵埃測定器(英國公 1 )(對於冷凍乾燥塊賦與空氣速度約95m/sec = 約2 Q S 1 / 札成量 m SeC之空氣所產生之衝擊),計算出有效粒子比 。將以非洛解狀態存在於各懸浮液中之粒子之幾何與巫 :叔技,各冷康乾燥組成物之衰變減及有效粒子比^ 不於表7中〇 个I /〇) 315314 100 200418520 〈表7 &gt; 指數 —比 -—-—_ 冷凍乾燥組成物 效粒子 复(〇/〇) ^68^7 ' 58.9 〜—一 _ 粉末狀冷 試料包含 氣衝擊, 之乾燥粉 0.115 0.051 1 2)胰島素〇. 1 mg+白胺酸 基結S 胺酸 〇 · 5 m g (ρ Η 6 · 4) 1 3)胰島素0· lmg+白胺醯 0.67 酸 1.5mg (pH6.5) · 如 i 7 所示,顯示^ 凍乾燥組成物(冷凍乾燥塊),縱使冷凍乾燥前1 非溶解狀態之有效成份(胰島素),作:二 ^ 丁 ] 错由上述空 在容器中易於微粒化,而可調萝忐南 衣成通於經肺投盘 末製劑。 〃 實施例1 4 分別調製胰島素(重組人類胰 a 勹I、、,口曰曰,比利時 公司製’比活性:26,4u/mg)〇lmg溶於鹽酸水溶 液所得之水溶液以及绳胺酸〇·5 mg溶於精製水所得之容 :夜’將彼等混合並用氮氧化納調整pH值至65,可以得到 懸浮狀態之歸液。該懸浮液所包含之粒子之幾何學平均 粒徑用t射折射及散射式粒纟分佈測定裳置(Μα 3_】,島津製作所製)測定。接下來,將該懸浮液充填於 容器(筒徑0 18 mm)中,用棚狀冷凍乾燥機(ly〇vac❿ 4 ’ LEYBOLD公司製)進行冷凌乾燥。對於得到之非粉末 狀冷凍乾燥組成物(冷凍乾燥塊)計算出衰變指數。 接下來,將充填非粉末狀冷凍乾燥組成物之容器(筒徑 0 18 mm)安裝在被設計成空氣導入流路17之孔徑為0 315314 101 200418520 l_99mm且吸引流路16之孔徑為019911^之自己吸入型 乾燥粉末吸入裝置(參照實施形態例3及第3圖)中。 用其對於容器中之非粉纟狀冷凌乾燥組成物(冷;東乾 燥塊)賦與空氣速度約i m/sec及空氣流量約17爪…“之 工就所產生之衝擊,將生成之粒子從裝置直接喷射於安裝 人工肺型空氣呼吸器(美國Amhem Process 公 司製)(測定條件,呼吸速率:丨L/min;呼吸體積:〇il) 籲之氣勝分析儀(aerosizer)(美國Amherest ProcessBiobras company, specific activity: 26.4 U / mg) l ma ~ a solution obtained by dissolving in technical hydrochloric acid solution and a solution obtained by dissolving 0.5 mg of phenylalanine in purified water, and mixing them, if by hydrogen Sodium oxide adjusts various pH values to obtain suspensions in various suspension states. The geometric average particle diameter of the particles contained in this suspension was measured using a laser refraction and scattering particle size distribution measuring device 2 (SALD-3000J, manufactured by Shimadzu Corporation). Next, the suspension was filled in a container (tube diameter 0 丨 8 mm), and shed-shaped cold; East dryer (LYOVAC 〇 丁, manufactured by LEYBOLD company) 315314 98 200418520 Xingqi * product. Large 'pieces), non-powdered cold-to-dry composition (cold ling drying, clothing index). Next, fill the non-powdered freeze-dried composition with wailing (^^ ° 从 从18 mm) Installed in a jet designed as an air jet channel I through A, Λ 〇 〇: .mm, and the diameter of the outflow channel is 0 1.8 mm, a powder inhalation device (with a wind capacity of about 20ml) The system uses it and calculates the effective particles by using a two-stage dust tester (UK € 0ρΐπ male two for cold; East dry block gives an air speed of about 35 oil &amp; air flow-the impact of air from Sec). The ratio ^ / I of the particles in the non-dissolved state is present in the geometrical flatness of each particle; the decay index and the effective particle ratio of the dried composition are shown in Table 6. (/ 〇) &lt; Table 6 &gt; Acid 0.5 mg (ρΗ6 · 0) 0.39 0.36 75.1 72.0 1〇) insulin 1 mg + phenylpropane 0.55 amino acid 0.5 mg (ρΗ 6.4) · 11) Tengdaosu 1 mg + phenylpropane 0.61 jL! ^ G .5mg (ρΗ6 · 6) __ As indicated, it shows the dry composition (cold-bed drying block), even if it is cold; The skin's active ingredient (insulin), but with the above-mentioned air flushing, it is easy to be micronized in the device, and can be adjusted to be suitable for pulmonary administration. ::: terminal = Examples 12 to 13 315314 99 200418520 separately modulate insulin (Recombinant human insulin crystals, manufactured by Blobas, Belgium, specific activity · 26.4 U / mg) 0.1 mg of water obtained by dissolving in hydrochloric acid aqueous solution, cereal solution and various carriers shown in Table 7 dissolved in purified water. They are mixed and the pH value is adjusted with sodium hydroxide to obtain the% floating liquid of each of the b-shaped floating evils. The geometric average particle diameter of the particles contained in the suspension is measured by a laser refraction and scattering type particle size distribution measuring device (SALD 3, 00J 'Made by Shimadzu Corporation.' Next, 'The suspension was filled in a container (tube diameter 0 丨 8 mm), using a shed-freeze dryer (LY〇VAC GT_4, leybold company). Production) Tokai dryness was performed on the obtained non-powdered freeze-dried composition (freeze-dried block) with a 50-fold abnormal decay index. Next, the non-powdered cold-to-dried composition container (tube diameter 0 18 mm) was filled. ) Installed in the air guide The pore diameter of the flow path 17 is 4 1.99 mm and the pore diameter of the suction flow path 16 is 0. A suction type dry powder inhalation device (refer to Embodiment Examples 3 and 3) is used. A two-stage dust detector is used ( British public 1) (For the freeze-dried block, the impact caused by air with an air velocity of about 95m / sec = about 2 QS 1 / sizing amount m SeC), the effective particle ratio was calculated. The geometry and magic of the particles existing in each suspension in a non-protonated state: the reduction of the decay and the effective particle ratio of each Lengkang dry composition ^ not shown in Table 7 0 I / 〇) 315314 100 200418520 <Table 7 &gt; Index-ratio ------_ freeze-dried composition effect particles complex (〇 / 〇) ^ 68 ^ 7 '58.9 ~ — 一 _ powdery cold sample contains gas impact, dry powder 0.115 0.051 1 2 ) Insulin 0.1 mg + Leucinyl Amino Acid 0.5 mg (ρ Η 6 · 4) 1 3) Insulin 0.1 mg + Leucamine 0.67 Acid 1.5 mg (pH 6.5) · As shown in i 7 It shows that ^ freeze-dried composition (freeze-dried block), even if it is 1 effective ingredient (insulin) in a non-dissolved state before freeze-drying, as: two ^ D] because the above-mentioned empty in the container is easy to micronize, and adjustable loquat Nanyi Chengtong is a preparation prepared by transpulmonary injection. 1 Example 14 Insulin (recombinant human pancreas a 勹 I, ,, 口, said by the Belgian company, "specific activity: 26,4u / mg), respectively, 0.01 mg of an aqueous solution obtained by dissolving in an aqueous hydrochloric acid solution, and lanine acid. The content of 5 mg dissolved in purified water: night 'mix them and adjust the pH value to 65 with sodium nitroxide, you can get the suspension liquid. The geometric average particle diameter of the particles contained in the suspension was measured by t-ray refraction and scattering particle size distribution measurement (Mα 3_), manufactured by Shimadzu Corporation. Next, this suspension was filled in a container (tube diameter 0 18 mm), and subjected to chilling and drying using a shed-type freeze dryer (lyavac 4 'LEYBOLD). For the obtained non-powder freeze-dried composition (freeze-dried cake), a decay index was calculated. Next, install a non-powdered freeze-dried composition container (tube diameter 0 18 mm) in the hole diameter 0 315314 101 200418520 l_99mm designed for the air introduction channel 17 and 019911 ^ Self-inhalation type dry powder inhalation device (refer to Embodiment 3 and Fig. 3). Use it to give non-powder-like chilled cold-dried dry composition (cold; east dry block) with an air speed of about im / sec and an air flow of about 17 claws ... "The impact of the work will generate the particles Directly sprayed from the device to an artificial lung-type air respirator (made by Amhem Process, USA) (measurement conditions, breathing rate: 丨 L / min; breathing volume: 0il) aerosizer (Amherest Process, USA)

Instrument公司製)中,並測定微粒之粒度分佈。然後從該 結果算出該微粒之空氣力學平均粒徑(//± SD)。將各冷;東 乾燥組成物之衰變指數及從裝置喷射之粒子之空氣力學平 均粒徑示於表8中。 &lt;表8&gt; 衰變空氣力學之平均 指數粒徑(pm±SD, MMAD) ’ 〇·221 1.875 土 1.384 均粒徑(μηι)Instrument Co., Ltd.), and measured the particle size distribution of the fine particles. From this result, the aerodynamic average particle size (/ ± SD) of the particles was calculated. Table 8 shows the decay index and the aerodynamic mean particle diameter of the particles sprayed from the device for each of the cold and dry compositions. &lt; Table 8 &gt; The average exponential particle size of decay aerodynamics (pm ± SD, MMAD) ′ 〇 · 221 1.875 soil 1.384 average particle size (μηι)

14)騰島素 〇img+ 0.57 結員胺酸0.5 m g 如表8所示,顯示衰變指數至少〇·221之非粉末狀冷 /東乾燥組成物(冷/東乾燦塊)’縱使冷;東乾燥前之試料包含 非溶解狀態之有效成份(胰島素),但藉由上述空氣衝擊, 在谷為中易於微粒化,且可調製成適於經肺投與之乾燥粉 末製劑。 ^ 315314 102 200418520 參考例1至5 將胰島素(重組人類胰島素結晶,比利時Biobras公司 製,比活性:26.4 U/mg)(l mg,2 mg)或胰島素與表9 、 ^ μ yj\ 各種載體分別溶於包含鹽酸之注射蒸德水中並調製成〇 2 ml ’將其充填於容器(筒徑0 18 mm)中,用棚狀冷;東乾操 機(LYOVAC GT-4,LEYBOLD公司製)進行冷;;東乾燥。對 於得到之非粉末狀冷凍乾燥組成物(冷凍乾燥塊)計算出奢 變指數。接下來,將充填非粉末狀冷凍乾燥組成物之容哭 (筒徑0 1 8 mm)安裝在被設計成空氣導入流路1 7之孔徑為 必1.99 mm且吸引流路16之孔徑為0 1.99 mm之自己吸入 型乾燥粉末吸入裝置(參照實施形態例3及第3圖)。使用 其並藉由二段式塵埃測定器(英國Copley公司製)(對於泠 /東乾$呆塊賦與空氣速度約95m/sec及空氣流量約295 ml/sec之空氣所產生之衝擊),計算出有效粒子比率⑼)。 將各冷凍乾燥塊之衰變指數及有效粒子比率(%)示於 中。 ,、 &lt;表9&gt; ——_ 指數 &amp; ;東乾燥組成物14) Tengdaosu 〇img + 0.57 Amino acid 0.5 mg As shown in Table 8, a non-powdered cold / east dry composition (cold / donggan cane) showing a decay index of at least 0.21 'cold even though east; The sample before drying contains the active ingredient (insulin) in a non-dissolved state, but by the above-mentioned air impact, it is easy to be micronized in Guwei, and can be adjusted into a dry powder preparation suitable for pulmonary administration. ^ 315314 102 200418520 Reference Examples 1 to 5 Insulin (recombinant human insulin crystal, manufactured by Biobras, Belgium, specific activity: 26.4 U / mg) (l mg, 2 mg) or insulin with Table 9, ^ μ yj \ various carriers respectively Soluble in hydrochloric acid-injected distilled German water and prepared into 0.2 ml 'Fill it in a container (tube diameter 0 18 mm) and cool it in a shed shape; use a dry dryer (LYOVAC GT-4, manufactured by LEYBOLD) Cold; East dry. The luxury index was calculated for the obtained non-powder freeze-dried composition (freeze-dried cake). Next, install the non-powder-free freeze-dried composition Rongjing (tube diameter 0 18 mm) in the air inlet flow path 17 designed to have a pore diameter of 1.99 mm and the suction flow path 16 to have a pore diameter of 0 1.99 mm self-inhalation type dry powder inhalation device (refer to Embodiment 3 and Fig. 3). Using it and using a two-stage dust tester (manufactured by Copley Company, UK) (improving the impact of air with a velocity of about 95 m / sec and an air flow of about 295 ml / sec on the Ling / Donggan $ block), Calculate the effective particle ratio i). The decay index and effective particle ratio (%) of each freeze-dried block are shown in. , &Lt; Table 9 &gt; ——_ Index &amp;

$ 騰島素 lmg 0.159 ^ 2)胰島素lmg+白胺酸i.4mg 0.145 1 3)胰島素lmg +纈胺酸i.〇mg 〇.110 1 4)胰島素 2mg 0.177 島素 2mg+白胺酸 i.4mg 0.137 如表9所示,顯示衰變指數至少〇·丨丨〇之非粉末狀冷 凍乾燥組成物(冷凍乾燥塊),在容器中易被上述空氣衝擊 315314 103 200418520 微粒化,且可調製成適於經肺投與之乾燥粉末製劑。 參考例6 j 1 〇 分別將胰島素(重組人類胰島素結晶,比利時Biobras 公司製,比活性:26.4 11/1^)1!^及表7所示各種載體(1.5 mg)溶於包含鹽酸之注射蒸餾水中,並調製成〇 5mi。將其 充填於谷器(筒徑0 18 mm)中’用棚狀冷凍乾燥機 參(LYOVAC GT_4’ LEYB0LD么\司製)進行冷;東乾燥。對於 得到之非粉末狀冷凍乾燥組成物(冷凍乾燥塊),計算出衰 變指數。接下來,將充填得到之非粉末狀冷殊乾燥組成物 之容器(筒徑0 18 mm)安裝在被設計成空氣喷射流路3之 孔徑為0 1.2 mm且流出流路4之孔徑為0丨·8 mm之喷射 型乾燥粉末吸入裝置(具有可供給空氣量約2〇 ml之風箱 體:參照實施形態例1及第1圖)。使用其對於容器中之非 粉末狀冷凍乾燥組成物(冷凍乾燥塊)賦與空氣速度約 _ 35m/Sec及空氣流量約40ml/sec之空氣衝擊’將生成之粒 子從裝置直接喷射於安裝人工肺型空氣呼吸器(美國 Amherst Process Instrument公司製;測定條件呼吸速率: 60 L/min ;呼吸體積:1L)之粒度分佈計(氣膠分析儀 (aerosizer):美國 Amherest Process Instrument 公司製;r w$ Tensin 1mg 0.159 ^ 2) Insulin 1mg + Leucine i.4mg 0.145 1 3) Insulin 1mg + Valinic acid i.〇mg 〇.110 1 4) Insulin 2mg 0.177 Insulin 2mg + Leucine i.4mg 0.137 As shown in Table 9, non-powder freeze-dried compositions (freeze-dried blocks) showing a decay index of at least 0 · 丨 丨 〇 are easily impacted by the air in the container 315314 103 200418520, and can be adjusted to be suitable for Dry powder formulations for pulmonary administration. Reference Example 6 j 1 〇 Insulin (recombinant human insulin crystal, manufactured by Biobras, Belgium, specific activity: 26.4 11/1 ^) 1! ^ And various carriers (1.5 mg) shown in Table 7 were dissolved in distilled distilled water containing hydrochloric acid Medium and modulated to 〇5mi. Fill it in a trough (tube diameter 0 18 mm) ’and use a shed-type freeze dryer ginseng (LYOVAC GT_4’ LEYB0LD Modified / made by the company) to cool; dry in the east. For the obtained non-powder freeze-dried composition (freeze-dried cake), the decay index was calculated. Next, install the filled non-powdered cold dry composition container (tube diameter 0 18 mm) in the air jet flow path 3 with a hole diameter of 0 1.2 mm and the outflow channel 4 with a hole diameter of 0 丨· 8 mm spray-type dry powder inhalation device (with a wind box capable of supplying air of about 20 ml: refer to Embodiment Example 1 and Figure 1). Use the non-powder freeze-dried composition (freeze-dried block) in the container to give an air impact of about _ 35m / Sec and an air flow of about 40ml / sec. 'The generated particles are directly sprayed from the device to the installation of artificial lungs Type air respirator (manufactured by American Amherst Process Instrument Company; measurement condition: breathing rate: 60 L / min; breathing volume: 1L) particle size distribution meter (aerosizer): American Amherest Process Instrument company; rw

Niven: Pharmaceutical Techn〇1〇gy,72_78 (i993))中並測 定微粒之粒度分佈。然後從該結果算出該微粒之空氣力學 平均粒徑(// m± SD)。 將充填非粉末狀冷凍乾燥組成物之容器(筒徑0工8 315314 104 200418520 mm)安裝在被設計成空氣導入流路n之孔徑為必1 且吸引流路之孔徑為4 1.99 mm之自己吸入型乾燥粉末口 入裝置(參照實施形態例3及第3圖)。使用其並藉由二段 式塵埃測定器(英目Copley么'司製)(對於冷凍乾;塊:: 空氣速度約95m/Sec及空氣流量約295 ml/sec之空氣所產 生之衝擊),計算出有效粒子比率(%)。 將各冷凍乾燥塊之衰變指數,以及從裝置噴射之粒子 之空氣力學平均粒徑m± SD)及有效粒子比率示於 表10中。 ' &lt;表 10&gt; 冷凍乾燥組成物 衰變 指數 空氣力學之平均 粒徑(pm±SD, MMAD) 有效粒罕^ 比例(%) 參6 )胰島素+異白胺酸 0.124 1·759±1·425 71.1 ~~ 參7 )胰島素+白胺酸 0.250 1.954 士 1.454 74.1 參8)胰島素+纈胺酸 0.124 2.007士 1.438 72.1 參9)胰島素+苯基丙胺酸 0.204 1.872士 1.477 62.0 參10)胰島素+D-甘露醇 0.160 2.239±1.435 61.2 如表1 0所示,顯示衰變指數至少0 ·丨24之非粉末狀冷 束乾燥组成物(冷凍乾燥塊),藉由空氣速度約35rn/sec及 空氣流量約40ml/sec生成之空氣衝擊或者空氣速度約 95m/sec及空氣流量約295 nli/sec生成之空氣衝擊,在容 器中易被微粒化〜而且藉由空氣速度約95m/sec及空氣流 量約295 ml/sec生成之空氣衝擊而微粒化之粒子之平均粒 控為5微米以下,可調製成適於經肺投與之乾燥粉末製 劑。 產^上之利用可能1 105 315314 200418520 若藉由本發明之經肺投與用乾燥粉末吸入系統,可將 冷康乾燥組成物經微粒化成送達肺所需要之大小,同時可 將該微粒吸入投與至肺。㈣,若依照本發明之經肺投與 用乾燥粉末吸入系統,使用(投與)調製成非粉末狀態之冷 成物時’於將其微粒化之同_,可吸入投與。藉 ::二為了製劑之微粒化而進行特別之操作。因此,若依 經肺投與用乾燥粉末吸入系統(製劑系統),將 製造㈣中損失(藥物之不活性化及充填操作造 性化二丄::失(以微粒狀保存造成之藥物不活 投=之在Λ造過混入夾雜物之虞,而可以安 王之一疋置。其在以蛋白質及胜肽等— /性物質為有效成分之製劑上特別有用: '又门貝μ 之有二經肺投與用乾燥粉末吸入系統中得到 *放粒子比率至少為1〇%以上 經肺投與用乾燥粉末吸入㈣’古*依知、本發明之 20%以上,25%以卜&quot; 效粒子比率可提高至 國專利公報第6153224 ::二Χ及:5%:上。而若依照美 多數中,附著於肺下/ 載’在先前乾粉吸入裝置之 效成分之1〇%。'又,:,有效成分(粒子)不超過被吸入有 -般吸入用粉末製劑到:::=5 : 6 7 3:公報中記載, 中排出之藥物之約i 〇Q/ ^里到達率),為從該製劑 粉末吸入系統,從可:、;戶“ ’亡發明之經肺投與用乾燥 有效粒子比率之觀點古成比先丽之吸入用粉末製劑高之 婪分 、^之’可謂極有用的投盥系祐 …發明之冷;東乾燥組成物及喷射型乾燥粉末吸 315314 106 200418520 入裝置’僅藉由空翕厭 ?—叩 &gt;、土 u手&amp;將空氣從空氣喷射流路噴射 至谷态内並將空新種亍I^ 、#m 讀錢與冷滚錢組絲,就可將該冷 =組成物微粒化。基於此,利用簡單構造之置 於具有平易之構造,可以低以“ 〆及入衣置由 ^ 乂低成本生產,結果可以大量擴張。 又’若依照喷射型之乾燥於古 r ^ M ^ ^ 钇认叔末吸入裝置,藉由調整風 =空氣壓送手段之麼縮速度,可以二 末製劑)之吸引量以符合使用者之 贺:“j(私 匯集成一根,針部扎入容哭 b 错由將針部 $土 谷益之口栓之作業將變得容易。 者’若依照自己吸入型之乾燥粉末吸入裝 使用者之吸氣壓產生空氣衝擊, 猎由 (n ^ /h ^ π -χ 將~凌乾燥組成物霧 :㈣化),且可於使用者吸氣之同時, 物經微粒化並投與至肺’藉此可以 := 量之藥物投與。又,由於I ++ 于…知失且女定 化 而務化(微粒化)以外之 作’操作容易。又,與喷射型同樣, 卜之特別知 根,扎入容器之口栓背部之作孝… 、’ 匯集成- 丹| &lt;忭菜將變得容易。 依照本發明之乾燥粉末吸入裝置, 空氣導入流路之針部扎入容器之口栓,葬吸引流路及 壓,可將上述容器内之空氣從吸引口吸入::'t者之吸氣 部之空氣導入流路流入容器内以々 工軋經由針 、工乳衝擊職座卜、十、、人 乾垛組成物,並可從容器中吸引 /、上述々凍 成物。 MM之冷;東乾燥組 又’尤其是在實施形態例4中記载之 吸入裝置之情況,可以發揮下述效果。 &quot;明乾燥粉末 315314 107 200418520 在對於冷康乾燥組成物賦與有㈣$ 器吸引出經微粒化之粉末狀冷康乾燥組成物之情况亚= 徑必須增大。“之戴面積增大’因此針部之直 伴持不:::口徑大之針部扎入口栓,必須將容器確實 保持以不偏維針部之軸線之方式靠近針尖,並用“ 針尖壓入口栓。 $大力將 之保末吸人裝置藉由具備保持容器 …作體之保持部運轉部,可以將容器用保持部::;構 亚/口者引導部在針部之轴線上移動並靠近針尖, 作操作體’可用比較小的力使針部扎入容器之〇拾。曰由知 像這樣,若依照本發明之乾燥粉末吸入裝置 且確實地將針部扎入容器之口拴。 j谷易 X,若構成為「上述外殼形成筒狀,在該外殼之前邱 •:成上述吸引口部,在上述外殼内形成上述容: 將上述針部以針尖朝向上述收納室之方式配設在上;; 成内’將與上述針部之空氣導人流路連通並供導入 =導入σ设置在上述外殼之壁部’藉由上述保持部運轉部 ,上述保持部在上述收納室中,以上料殼之轴方向前進 及後退」,可以形成鉛筆形之乾燥粉末吸入裝置,其容易 用且攜帶方便。 《、又’關於上述外殼’若藉由在上述保持部後退之位置 ①成有上述容器之出人口之外殼本體,以及用絞鏈連結於 3153J4 108 200418520 =殼本體之上述出入口之蓋子所形成之保持部運轉 持部:備在蓋上上述蓋子使上述出入口關閉之時使上述保 述保:f:且在拉起上述蓋子使上述出入口打開之時使上 ^ ”寺部後退之上述機構部,且上述蓋 邱夕4。仏A ^现卞兼做為上述機構 作體,將可使保持部運轉部之機構部簡略化,在製 有::又’由於在容器之口栓被針尖扎入之同 0 1盍住谷态之出入口,所以變得易於使 [圖式簡單說明] 第i圖為顯示實施形態例i記載之 入裝魏型υ之剖面圖。又,圖中箭頭表二= 流動(在下文之第2圖及第3圖中亦同)。 二乳之 第2圖為顯示實施形態例2記載 入裝置(自己吸入型1}之剖面圖。 乾心心末吸 第3圖為顯示實施形態例3記載之 入裝置(自己吸入型2)之剖面圖。 乾知‘末吸 第4圖為顯示實施形態例4記載之 入裝置(自己吸入型3)之透視圖。 ‘以吸 第5圖為上述乾燥粉末吸入裝置(自己吸 面圖。 土 之剖 弟6圖之(a)為上述乾燥粉末吸入裝置(自己吸 之4刀d面圖’(b)為該乾燥粉末吸入裝置之 3) 圖。 ,。丨艾侧面 第7至圖為說明上述乾燥粉末吸入裝置 型3)之動作之剖面圖。 (目己吸入 J ί 5314 109Niven: Pharmaceutical Technolgy, 72-78 (i993)) and measured the particle size distribution of the microparticles. From this result, the aerodynamic average particle size (/ m ± SD) of the particles was calculated. A container filled with a non-powder freeze-dried composition (tube diameter: 0 315 314 104 200418520 mm) is installed in a self-inhalation designed so that the air introduction flow path n has a diameter of 1 and the suction flow path has a diameter of 4 1.99 mm Type dry powder feeding device (refer to Embodiment 3 and Figure 3). Use it with a two-stage dust tester (made by Copeley Co., Ltd.) (for freeze-drying; block: the impact of air with an air speed of about 95 m / Sec and an air flow of about 295 ml / sec), The effective particle ratio (%) was calculated. Table 10 shows the decay index of each freeze-dried block, the aerodynamic mean particle diameter (m ± SD) of the particles sprayed from the device, and the effective particle ratio. '&lt; Table 10 &gt; Decay index of freeze-dried composition Aerodynamic mean particle size (pm ± SD, MMAD) Effective particle size ratio (%) See 6) Insulin + isoleucine 0.124 1 · 759 ± 1 · 425 71.1 ~~ cf. 7) insulin + leucine 0.250 1.954 ± 1.544 74.1 cf. 8) insulin + valine 0.124 2.007 +1.438 72.1 cf. 9) insulin + phenylalanine 0.204 1.872 +1.477 62.0 cf. 10) insulin + D- Mannitol 0.160 2.239 ± 1.435 61.2 As shown in Table 10, a non-powdered cold beam dried composition (freeze-dried block) showing a decay index of at least 0 · 丨 24, with an air velocity of about 35rn / sec and an air flow rate of about 40ml The air impact generated by / sec or the air velocity is about 95m / sec and the air flow rate is about 295 nli / sec. The air impact generated by the container is easy to be atomized ~ and the air velocity is about 95m / sec and the air flow rate is about 295 ml / The average particle size of the particles impacted by the air generated by sec is 5 micrometers or less, and it can be adjusted into a dry powder formulation suitable for pulmonary administration. The use of the product is possible 1 105 315314 200418520 If the dry powder inhalation system for transpulmonary administration of the present invention is used, the cold-kang dry composition can be micronized to the size required for delivery to the lungs, and the microparticles can be inhaled and administered at the same time. To the lungs. That is, if the dry powder inhalation system for pulmonary administration according to the present invention is used (administrated) and prepared into a non-powdered cryogenic product, it can be administered by inhalation when it is micronized. By using :: 二, special operations are performed for the micronization of the preparation. Therefore, if the dry powder inhalation system (preparation system) for pulmonary administration is used, the manufacturing process will be lost (the inactivation of the drug and the filling operation will be artificial). It can be mixed with inclusions in Λ, but can be placed in one of the kings. It is particularly useful in preparations that use proteins and peptides and / or sexual substances as active ingredients: 'Youmenbei μ has two The dry powder inhalation system for pulmonary administration has a * discharge particle ratio of at least 10% or more. The inhalation of the dry powder for pulmonary administration is inhaled. According to the knowledge, more than 20% of the present invention, 25% is effective. The particle ratio can be increased to National Patent Gazette No. 6153224 :: two X and: 5%: up. And according to the US majority, attached to the lungs / loaded '10% of the effective ingredients of the previous dry powder inhalation device. ' :, The active ingredient (particles) does not exceed the inhaled powder formulation for general inhalation to :: == 5: 6 7 3: as described in the bulletin, the drug reaches approximately i 〇Q / ^ arrival rate), In order to inhale the system from the powder of the preparation, the following can be: View of effective particle ratio Gucheng has higher greed than inhale powder for inhalation, and it can be said to be extremely useful .... Cold for invention; East dry composition and spray type dry powder suction 315314 106 200418520 into The device 'only through the air exhaustion?-叩 &gt;, soil hand & spray air from the air jet flow path into the valley state and empty new species 亍 I ^, #m read money and cold roll money, The cold composition can be made into particles. Based on this, a simple structure can be used to produce a low-cost structure, which can be produced at a low cost by "〆" and "入 衣衣 由", resulting in a large expansion. The spray type is dried in the ancient r ^ M ^ ^ yttrium identification tertiary inhalation device. By adjusting the speed of the air = air pressure feeding method, the amount of suction can be adjusted to meet the user's congratulations: "j ( The private parts are gathered into one, and the needle is inserted into Rong cry b. The operation of attaching the needle $ 土 谷 益 的 口 口 will be easy. If you inhale the dry powder inhalation type according to your own inhalation type, the air pressure will generate air impact. , Hunting consists of (n ^ / h ^ π -χ drying ~ Ling (Mist: haze), and at the same time as the user inhales, the matter is micronized and administered to the lungs', so that: = the amount of drug administration. Also, because I ++ is known to ... It is easy to operate if it is not made into a chemical product (micronized). Also, as with the spray type, Bu Zhikun knows the roots, and puts it into the mouth of the container, and plugs the filial piety on the back. According to the dry powder inhalation device of the present invention, the needle of the air introduction channel is inserted into the mouth plug of the container, and the suction channel and pressure are buried, and the air in the container can be sucked in through the suction port: 't The air introduction flow path of the suction part of the person flows into the container to smash the composition through the needle, the working milk, and the worker's dry stack, and can attract and / or freeze the above-mentioned frozen products from the container. The coldness of the MM; the east drying group, and particularly the case of the inhalation device described in the fourth embodiment, the following effects can be exhibited. &quot; Ming dry powder 315314 107 200418520 In the case where the cold-kang dry composition is provided with a device to attract the powdered cold-kang dry composition, the diameter must be increased. "The wearing area has increased, so the straight part of the needle does not hold ::: The needle with a large diameter is inserted into the plug, and the container must be kept close to the needle tip in a way that does not deflect the axis of the needle, and press the needle with the needle tip . $ Strongly absorbing the suction device By having a holding part operation part which holds the container ... as the body, the holding part for the container can be moved along the axis of the needle and close to the needle tip. As the operating body, a relatively small force can be used to pierce the needle into the container. In this way, if the dry powder inhalation device according to the present invention is used, the needle is surely inserted into the mouth of the container. Gu Yi X, if the structure is "the casing is formed in a cylindrical shape, Qiu is formed before the casing: the suction opening is formed, and the volume is formed in the casing: the needle portion is arranged with the needle tip facing the storage room" Above; Chengnei 'will communicate with the air-guiding flow path of the needle portion and introduce it = introduction σ is provided on the wall portion of the housing' by the holding portion operating portion, the holding portion is in the storage room, above The forward and backward movement of the material shell in the axial direction "can form a pencil-shaped dry powder inhalation device, which is easy to use and convenient to carry. <<, and 'about the above-mentioned case' is formed by forming the case main body with the above-mentioned container exit position at the position where the holding portion is retracted, and a hinge connected to the hinge of 3153J4 108 200418520 = the above-mentioned entrance and exit of the case body. Holding section: The holding section is provided with the above-mentioned mechanism when the cover is closed to close the entrance and exit: f: and the mechanism section that retracts the temple section when the cover is opened to open the entrance and exit, And the above cover Qiu Xi 4. 仏 A ^ Now 卞 also serves as the above-mentioned mechanism, which can simplify the mechanism section of the operation section of the holding section, and has the following: 'Because the pin at the mouth of the container was pierced by the needle tip It is the same as the entrance and exit of the valley state, so it is easy to make the drawing [simple description] Figure i is a cross-sectional view showing the installation Wei type υ described in Example i. Also, the second arrow table in the figure = flow (The same applies to the second and third figures below.) The second figure of the second milk is a cross-sectional view showing the insertion device (self-inhalation type 1) described in the second embodiment of the embodiment. The entrance device described in Embodiment 3 (from A cross-sectional view of a self-inhalation type 2). Dry know 'The last suction figure 4 is a perspective view showing the insertion device (self-inhalation type 3) described in Embodiment Example 4.' The suction figure 5 is the dry powder inhalation device ( Self-suction surface diagram. (A) of Figure 6 of the soil section is the above-mentioned dry powder inhalation device (4 side view of self-suction d) (b) is the 3) diagram of the dry powder inhalation device. Figures 7 to 7 are cross-sectional views illustrating the operation of the dry powder inhalation device type 3). (Head inhalation J ί 5314 109

第 I置(自 第 裝置(自 第 裝置(自 11圖係為本發明之其他實施形態之乾燥粉末吸入 己吸入型4)之透視圖。 12圖係為本發明之其他實施形態之乾燥粉末吸入 已吸入型5)之透視圖。 1 3圖係為本發明之其他實施形態之乾燥粉末吸入 己吸入型5)之透視圖。 1 2 4 容器 1 a 口栓 Θ /東乾燥組成物 3 空氣喷射流路 排出流路 5 針部 6 吸入口 7 吸氣構件 8 筒狀安全罩 9 空氣壓送手段 10 風箱體 11 吸進閥 12 吸進口 13 吐出閥 14 吐出口 15 接續口 16a 吸引流路16之前端 π 17a 空氣導入流路1 7之 前端口 18 吸入口 19 吸氣構件 20 收容室 21 外殼 21A 鉸鏈 22 保持部 23 引導部 24 保持部運轉部 26 外殼本體 27 蓋子 28 窗子 29 導入口 30 逆止閥 31 110 吸引口 315314 32a 咬嘴之蓋子 34 周壁部 36 控制桿 39 連結體 41 鉸鏈 42a 隔壁部3 3之導入溝 43 間隙 端 47 壁 49 操作體 咬嘴 隔壁告P 取出體 機構部 鉸鏈 第2導入路 周壁部34之導入溝 第2導入路42之一端 第2導入路42之另一 通氣孔 操作體 111 315314The perspective view of the first device (from the device (from Figure 11 is a dry powder inhalation type 4 of another embodiment of the present invention inhalation type 4). Figure 12 is a dry powder inhalation of another embodiment of the present invention Perspective view of inhaled type 5). Figure 1 3 is a perspective view of a dry powder inhalation type 5) of another embodiment of the present invention. 1 2 4 Container 1 a spigot Θ / East dry composition 3 Air jet flow path discharge flow path 5 Needle section 6 Suction port 7 Suction member 8 Cylindrical safety cover 9 Air pressure feeding means 10 Air box 11 Suction valve 12 Intake inlet 13 Outlet valve 14 Outlet port 15 Continuation port 16a Suction flow path 16 front end π 17a Air introduction flow path 1 7 Front port 18 Suction port 19 Suction member 20 Storage chamber 21 Housing 21A Hinge 22 Holder 23 Guide 24 Holding part running part 26 housing body 27 cover 28 window 29 introduction port 30 check valve 31 110 suction port 315314 32a mouthpiece cover 34 peripheral wall portion 36 lever 39 connecting body 41 hinge 42a introduction groove 43 of the partition portion 3 3 gap end 47 Wall 49 Operating body biting mouth Next door Take-out body mechanism part hinge 2nd introduction path Peripheral groove of the second introduction path 34 of the introduction wall 42 One end of the second introduction path 42 Another ventilation hole operating body 111 315314

Claims (1)

拾、申請專利範圍: 能H肺&amp;與用之冷束乾燥組成物,係將包含非溶解狀 4加成刀之組成液經冷凍乾燥而調製成,且具有下 述⑴至(iii)之特性: (1)具有非粉末之塊狀形態; (U)衰變指數為0 05以上;以及 ㈣藉由承受具有至少lm/sec之空氣速度及至少 17ml/sec之空氣流量之空氣衝擊,可成為平均粒徑在⑺ 微米以下或有效粒子比率在1〇%以上之微粒。 •如申請專利範圍f i項之冷“燥組成物,其中,包含 做為有效成分之高分子藥物。 :種經肺投與用乾燥粉末製劑之製造方法,係包含在收 $下述^乾燥組成物之容器中’使用可將下述空氣衝 =賦與該容器内之冷柬乾燥組成物之裝置,導入具備該 、氣衝輋此力之空氣,藉此使得上述冷凍乾燥組成物形 成:、句粒仏在1 〇微米以下或有效粒子比率在10%以上 之微粒;其中該冷凍乾燥組成物藉由將包含非溶解狀態 之添加成分之組成液經冷凍乾燥而調製成,且具有下述 (i)至(iii)之特性: (1)具有非粉末之塊狀形態, (ii)衰變指數為〇.〇5以上,以及 (111)藉由承51具有至少lm/sec之空氣速度及至少 1 7ml/See之空氣流量之空氣衝擊,可成為平均粒徑在1 〇 微米以下或有效粒子比率在1〇%以上之微粒。 315314 112 200418520 4·如申請專利範圍第3項之 造方法,其中,姑、人、土 ,、用乾&amp;粉末製劑之製 高分子藥物。’7乾‘組成物包含做為有效成份之 士申π專利範圍第3項之經 造方法,其中”用乾^粉末製劑之製 吸入裝置做為裳ί ⑷卿記載之乾燥粉末 (Α)經肺投與用 ::乾秌組成物微粒化: 收容於宠哭+ 係將以非粉末狀態 吸入所得Μ 東㈣組成物㈣^使被驗者 1侍喊粒用之裝置,其具備·· 嘴射流路之針部,具有排出流路之針部, 送手段,:之空氣喷射流路中輸送空氣用之空氣壓 又ΜA與上述針部之排出流路連通之吸入 ’ 且構成為: 述針部扎入供密封上述容器之口 射流路及排出泣攸命L、丄、 工乱育 允 抓〃上述容器内部連通,並用上述 二i ^手段使空氣經由上述空氣喷射流路噴射於 上述容器内,藉由該喷射空氣之衝擊使上述冷乾 燥組成物微粒化,且得到之微粒經由上述排出流路 從吸入口排出;或者 ⑻、I…又與用乾燥粉末吸人裝置,係、將以非粉末狀態 收容於容^中之冷滚乾燥組成物微粒化並使被驗者 吸入得到之微粒用之裝置,其具備·· ”有吸引*路之針部,具有空氣導入流路之針部以 315314 ]13 200418520 及與上述吸引流路連通之吸入口; 且構成為: 在上述針部扎入供密封上述容器之口栓之狀態,藉 由使用者之吸氣壓從上述吸入口吸入上述容器内之 空氣,同時使空氣經由上述空氣導人流路流入已成 為負壓之容器内,藉由流入之空氣衝擊將上述冷凍 乾爍組成物微粒化,且得到之微粒經由上述吸引流 路從吸入口排出。 6·種經肺投與用乾燥粉末吸入系統,係將下述(丨)及(2) 組合使用: (1)收容具有冷凍乾燥組成物之容器,該冷凍乾燥組成 物係將包含非溶解狀態之添加成分之組成液經冷凌 乾燥而調製成,且具有下述⑴至(iii)之特性·· (1) 具有非粉末之塊狀形態, (Π)衰變指數為〇·〇5以上,以及 (1U)藉由承受具有至少lm/sec之空氣速度及至少 1 7ml/sec之空氣流量之空氣衝擊,可成為平均粒徑在μ 微米以下或有效粒子比率在丨〇%以上之微粒; (2) 具備可將上述空氣衝擊賦與於上述容器内之冷凍乾 、ί、、、且成物之手^又以及排出經微粒化之粉末狀冷康乾 燥組成物之手段之裝置。 7·如申請專利範圍第6項之經肺投與用乾燥粉末吸入系 統,其中,在吸入時將上述容器與上述裝置組合使用。 8·如申請專利範圍第6項之經肺投與用乾燥粉末吸入系 315314 114 200418520 二二該冷’東乾燥組成物係包含做為有效成份之高 9.:;申6項之經肺投與用乾燥粉末吸入系 、、’、 使用下述(A)或(B)做為裝置: ⑷=與用乾燥粉末吸入裝置,其係將以非粉末狀 悲收谷於容器中之冷;東乾燥組成物經微粒化並使使 用者吸入所得微粒用之裝 1 具有空氣喷射流路之針部,具;排:流路之針部, 在上^針^之空氣噴射流路中輸送空氣用之空氣壓 以及與上述針部之排出流路連通之吸入 口 ; 且構成為: 使上述針部#L入供密封上述容器之口栓以將空氣喷 2流路及排出流路與上述容器内部連通,並用上述 空氣^送手段使空氣經由上述空氣喷射流路噴射於 ^述容器内,藉由該喷射空氣之衝擊使上述冷凍乾 秌組成物經微粒化,且得到之微粒經由上述排出流 路從吸入口排出;或者 爪 ^肺投與用乾燥粉末吸人裝i,其係將以非粉末狀 心收办方;谷裔中之冷凍乾燥組成物經微粒化並使被 馬双者吸入得到之微粒用之裝置,其具備·· 一有吸引流路之針部,具有空氣導入流路之針部以 及)、上述吸彳丨流路連通之吸入口; 且構成為: 115 315314 200418520 在上述針部扎入供宓射μ 、 1、*封上述容器之口栓之狀態,藉 由被.k者之吸氣壓從上述吸入口吸入上述容器内之 工孔’同日寸使空氣經由上述空氣導入流路流入已成 為負壓之容器内,Μ ώ、、六λ ± 丄 猎由流入之空氣衝擊將上述冷凍 乾燥組成物經微粒化, 了1匕且侍到之微粒經由上述吸引 流路從吸入口排出。Scope of patent application: Can be used for lung and cold beam drying composition, which is prepared by freeze-drying a composition solution containing a non-dissolved 4-addition knife, and has the following ⑴ to (iii) Features: (1) Non-powder morphology; (U) Decay index above 0 05; and ㈣ By withstanding air impact with an air velocity of at least lm / sec and an air flow of at least 17 ml / sec, it can become Particles with an average particle size of less than ⑺ microns or an effective particle ratio of 10% or more. • The "dry" composition as described in the scope of patent application for fi, which contains high-molecular drug as an active ingredient .: A manufacturing method for dry powder preparation for pulmonary administration, which is included in the following: ^ dry composition In the container of the material, 'the device that can flush the following air with the cold-dried composition in the container is used to introduce the air with the force to blow the air, so that the freeze-dried composition is formed :, Fine particles with a particle size of less than 10 microns or an effective particle ratio of more than 10%; wherein the freeze-dried composition is prepared by freeze-drying a composition liquid containing an additive component in a non-dissolved state, and has the following ( i) to (iii) characteristics: (1) has a non-powdered morphology, (ii) has a decay index of 0.05 or more, and (111) has an air velocity of at least lm / sec and at least by bearing 51 The air impact of 17ml / See air flow can become fine particles with an average particle size of less than 10 microns or an effective particle ratio of more than 10%. 315314 112 200418520 4 · The manufacturing method of item 3 in the scope of patent application, where , Aunt Polymer drugs for human, soil, and dry &amp; powder preparations. The '7 dry' composition contains the active method of Shishen's patent scope item 3 as the active ingredient. The inhalation device is used as a dry powder (Α) recorded by the ί⑷ for administration by the lungs :: The dry composition is micronized: Contained in a pet cry + The Μ㈣Μ composition obtained by inhalation in a non-powder state ^^ The device for the subject 1 to serve granules is provided with a needle part of the mouth jet flow path, a needle part for the discharge flow path, and a sending means: the air pressure for conveying air in the air jet flow path is The inhalation of the above-mentioned needle's discharge flow path is communicated and is constituted as follows: the needle is inserted into the mouth jet flow path for sealing the container, and the discharge valve L, 丄, and work disturbance allow the internal communication of the container, and use the above The second method means that the air is sprayed into the container through the air jet flow path, the cold-dried composition is atomized by the impact of the jet air, and the obtained particles are discharged from the suction port through the exhaust flow path; or , I ... and a device for sucking people with dry powder, and is a device for micronizing the cold-roll drying composition contained in a non-powdered state in a container and making the particles inhaled by the subject. The device includes ... " There is a needle part for the suction path, and a needle part with an air introduction flow path is 315314] 13 200418520 and a suction port communicating with the suction flow path; and it is structured as follows: the needle part is inserted into the mouth plug for sealing the container In the state, the air in the container is sucked from the suction port by the suction pressure of the user, and the air is caused to flow into the container that has become a negative pressure through the air introduction channel, and the freeze-dried composition is caused by the impact of the inflowing air. The particles are made into particles, and the obtained particles are discharged from the suction port through the suction flow path. 6. A dry powder inhalation system for pulmonary administration, which is a combination of the following (丨) and (2): (1) a container containing a freeze-dried composition, the freeze-dried composition will include an undissolved state The composition liquid of the added ingredients is prepared by cold-drying, and has the following characteristics (i) to (iii): (1) It has a non-powdered morphology, and (Π) has a decay index of 0.05 or more, And (1U) can withstand an air impact with an air velocity of at least lm / sec and an air flow of at least 17 ml / sec, and can become particles having an average particle size of less than μm or an effective particle ratio of more than 0%; ( 2) Equipped with a means that can apply the above-mentioned air impact to the freeze-dried, dried, and finished products in the container, as well as a method for discharging the powdered cold-kill dry composition. 7. The dry powder inhalation system for pulmonary administration according to item 6 of the patent application, wherein the above-mentioned container and the above-mentioned device are used in combination during inhalation. 8. If the dry powder inhalation system for pulmonary administration according to item 6 of the patent application is 315314 114 200418520 22, the cold 'East dry composition system contains as high as 9. With the dry powder inhalation system, use the following (A) or (B) as the device: ⑷ = With the dry powder inhalation device, which is to cool the grain in the container in a non-powder state; Packing for drying the composition to make the user inhale the obtained particles 1 Needle part with air jet flow path, with row: Needle part of flow path, for conveying air in the air jet flow path of upper needle ^ The air pressure and the suction port communicating with the discharge flow path of the needle part; and the structure is: the needle part #L is inserted into the mouth plug for sealing the container to spray the air flow path and the discharge flow path to the inside of the container; The air is sprayed into the container through the air jet flow path by the air sending means, and the freeze-dried composition is atomized by the impact of the jet air, and the obtained particles pass through the exhaust flow path. Discharged from the suction port; or A dry powder suction device for lung administration, which is intended for non-powder-shaped recipients; the freeze-dried composition of the cereal is micronized and the device is used to inhale the particles obtained by the horse and the person. It has a needle part with a suction flow path, a needle part with an air introduction flow path, and a suction port communicating with the suction channel and the flow path; and is configured as: 115 315314 200418520 Injecting μ, 1, and * the state of the mouth plug of the container, by the suction pressure of the .k person sucked into the hole in the container from the suction port on the same day, the air has flowed in through the air introduction flow path. In the container with negative pressure, the above-mentioned freeze-dried composition is micronized by the impact of the inflowing air, and the particles that have been treated are discharged from the suction port through the suction flow path. 1〇.-種經肺投與方法,包含使用冷;東乾燥組成物,該冷滚 乾燥組成物係將包含非溶角早狀態之添加成分之組成液 經冷凍乾燥而調製成,其具有下述特性·· (i) 具有非粉末之塊狀形態, (ii) 衰變指數為0.05以上,以及 (iii) 藉由承受具有至少lm/sec之空氣速度及至少 17ml/sec之空氣流量之空氣衝擊,可成為平均粒徑在⑺ 微米以下或有效粒子比率在丨〇%以上之微粒,·10. A method for pulmonary administration, including the use of cold and dry composition, the cold-roll drying composition is prepared by freeze-drying a composition liquid containing an additive component in an insoluble state in an early state, which has the following Description of characteristics: (i) having a non-powder morphology, (ii) a decay index of 0.05 or more, and (iii) by being subjected to air impact with an air velocity of at least lm / sec and an air flow of at least 17 ml / sec Can become fine particles with an average particle size of less than 微米 microns or an effective particle ratio of more than 0%, 使用時,藉由將上述空氣衝擊賦與該冷凍乾燥組成物, 形成平均粒徑在10微米以下或有效粒子比率在ι〇%以 上之微粒,然後藉由令使用者吸入該經微粒化之粉末而 施行投與。 11 ·如申請專利範圍第1〇項之經肺投與方法,其中,該冷 凍乾燥組成物被收容於容器内,以及該經微粒化之粉末 係用具備可將上述空氣衝擊賦與該容器内之冷康乾燥 組成物之手段以及可從容器中排出經微粒化之粉末狀 冷;東乾燥組成物之手段之裝置調製而成。 12·如申請專利範圍第1〇項之經肺投與方法,其中,該A 315314 116 凍乾燥組成物係包… 如申請專利範圍第丨“、、有效成份之鬲分子藥物。 在下述⑷或⑻中記㈣投m其中,使用 置: 乾無粉末吸入裝置做為裝 (A)經肺投與用乾燥粉末 態收容於容器中人 衣,/、係將以非粉末狀 用者吸入所:微粒组:物經微粒化並使使 在上述針部針部’具有排出流路之針部, 送手段,以及流路中輸送空氣用之空氣壓 口;且構成為Ϊ “部之排出流路連通之吸入 IS針部礼入供密封上述容器之口栓以將空氣喷 :及排出流路與上述容器内部連通 空氣壓送丰以社+ 一 ⑺上逆 μ又二軋經由上述空氣喷射流路噴射於 燥組I::藉由該噴射空氣之衝擊使上述冷凌乾 ‘礆粒化’且得到之微粒經由上述排出流 路攸吸入口排出;或者 ⑻^肺,與用乾燥粉末吸人裝置,其係將以非粉末狀 〜收谷方、谷為中之冷凍乾燥組成物經微粒化並使被 驗者吸入得到之微粒用之裝置,其具備:… 具有吸引流路之針部,具有空氣導入流路之針部以 及與上述吸Μ流路連通之吸入口; 且構成為: 在上述針部扎入供密封上述容器之口栓之狀態,藉 315314 117 200418520 由被驗者之吸氣壓從上述吸入口吸入上述容器内之 空氣,同時使空氣經由上述空氣導入流路流入已成 為負I之谷為内,藉由流入之空氣衝擊將上述冷凍 乾燦組成物經微粒化,且得到之微粒經由上述吸引 流路從吸入口排出。 14.一種冷凍乾燥組成物在吸入式經肺投與之使用,其中, • 該冷凍乾燥組成物係將包含非溶解狀態之添加成分之 組成液經冷凍乾燥而調製成,且具有下述特性: (I) 具有非粉末之塊狀形態, (II) 衰變指數為0.05以上,以及 (III) 藉由承受具有至少lm/sec之空氣速度及至少 1 7ml/sec之空氣流量之空氣衝擊,可成為平均粒徑在⑺ 微米以下或有效粒子比率在以上之微粒;並且 將該冷凍乾燥組成物粉末化使成為具有上述平均粒徑 g 或有效粒子比率之微粒來使用。 15·如申請專利範圍第14項之冷床乾燥組成物在經肺投與 之使用,其中,該冷凍乾燥組成物被收容於容器内,以 及該經微粒化之粉末係用具備可將上述空氣衝擊賦與 該容器内之冷凍乾燥組成物之手段以及可從容器中排 出經微粒化之粉末狀冷凍乾燥組成物之手段之裝置調 製而成。 ~ 16·如申請專利範圍第14項之冷凍乾燥組成物在經肺投與 之使用,其中,該冷凍乾燥組成物係包含做為有效成份 之南分子藥物。 315314 118 17’:=::=^造:、入式_^ 性: /、中,该冷凍乾燥組成物具有下述特 ==溶解狀態之添加成分之組成液經嫌燥 (ii)具有非粉末之塊狀形態, (di)衰變指數為0.05以上,以及 (iv)藉由承, 17 八有至V im/sec之空氣速度及至少 微米氣流量之空氣衝擊,可成為平均粒徑在10 於使用/將粒子比率在1〇%以上之微粒;並且 述平均組成物經微粒化使成為具有上 A上述有效粒子比率。 1 8 ·如申睛專利 投與用乾焊= 乾燥組成物在製造經肺 係包含做2 制,其中,該冷純㈣成物 u為有效成份之高分子藥物。 19‘^專=圍第17項之冷;東乾燥組成物在製造經肺 被收容:二:製劑之使用’其中’該冷凍乾燥組成物 上述4彳|.^’以及該經録化之粉末_具備可將 :讀擊賦與該容⑼之冷;東乾燥組成物之手段 容器中排出經微.粒化之粉末狀冷㈣ 物之手段之裳置調製而成。 2°’:ΐ=;解狀態之添加成分之組成液之使用,其用 衣“、调製經肺投與用乾燥粉末製劑用之冷;東乾燁 組成物,該冷凌乾燥組成物具有下述特性. 3I53J4 119 200418520 ⑴具有非粉末之塊狀形態, (Η)衰變指數為0·05以上,以及 (-)藉由承受具有至少lm/sec之空氣速度及至少 10::二空:右流量之空氣之衝擊,可成為平均粒徑在 “下或有效粒子比率在10%以上之微粒; 亚且於使用時經微粒化為上述平均粒徑或上述有效粒 子比率。 4 π从m .如申請專利範圍第2G項之包含非溶解狀態之添加成分 之組成液之!用,其中’該冷滚乾燥組成物係包含做為 有效成份之南分子藥物。 22.如申請專利範圍第2G項之包含非溶解狀態之添加成分 之組成液之使用,其中,該冷凍乾燥組成物係收容於容 器内,以及該經微粒化之粉末係用具備可將上述空氣衝 擊賦與該容器内之冷;東乾燥組成物之手段以及可從容 器中排出經微粒化之粉末狀冷;東乾燥組成物之手段之 装置調製而成。 315314 120In use, by applying the above-mentioned air impact to the freeze-dried composition, particles having an average particle diameter of less than 10 microns or an effective particle ratio of more than 10% are formed, and then the user is inhaled into the micronized powder. And implementation of investment. 11 · The method for pulmonary administration according to item 10 of the patent application scope, wherein the freeze-dried composition is contained in a container, and the micronized powder is provided with a device capable of imparting the above-mentioned air impact to the container. It is prepared by the means of drying the composition by cold and the device that can discharge the micronized powdery cold from the container; the device by the means of drying the composition. 12. If the method for pulmonary administration of item 10 in the scope of patent application, wherein the A 315314 116 freeze-dried composition is packaged ... As in the scope of application for patent scope, the active ingredient is a molecular drug. ⑻ 中 记 ㈣m. Among them, the use device is: Dry powder-free inhalation device as a container (A) Dry powder for pulmonary administration is stored in a container in a container, and / or is to be inhaled by a non-powdered user: Particle group: The object is atomized and the needle portion of the above-mentioned needle portion has a discharge channel, a delivery means, and an air pressure port for conveying air in the channel; and is configured as a "portion of the discharge channel" The connected inhalation IS needle part is used to seal the mouth of the container to spray air: and the discharge flow path communicates with the inside of the container. Spraying on dry group I :: The above-mentioned cold lingers are dried and 'granulated' by the impact of the sprayed air, and the obtained particles are discharged through the above-mentioned exhaust flow path suction port; or lungs, and a device for inhaling with dry powder , It will be non-powdered ~ Device for harvesting grains and grains in the freeze-dried composition by micronizing and inhaling the particulates obtained by the subject, comprising: a needle portion having a suction flow path, a needle portion having an air introduction flow path, and The suction port which is in communication with the suction channel; and is configured as follows: in the state where the mouth of the needle is inserted into the mouth plug for sealing the container, the subject is sucked into the container from the suction port by the suction pressure of 315314 117 200418520 At the same time, the air is flowed into the valley that has become negative I through the air introduction flow path, and the freeze-dried bright composition is micronized by the impact of the inflowing air, and the obtained particles are sucked in from the suction flow path. Mouth drains. 14. A freeze-dried composition is used for inhaled pulmonary administration, wherein: The freeze-dried composition is prepared by freeze-drying a composition liquid containing an additive component in a non-dissolved state, and has the following characteristics: (I) has a non-powdered morphology, (II) has a decay index of 0.05 or more, and (III) can withstand air impact with an air velocity of at least lm / sec and an air flow of at least 17 ml / sec, which can become Microparticles having an average particle diameter of ⑺ microns or less or an effective particle ratio or more; and powdering the freeze-dried composition into particles having the above-mentioned average particle diameter g or effective particle ratio for use. 15. If the cold-bed drying composition of item 14 of the patent application is used for pulmonary administration, wherein the freeze-dried composition is contained in a container, and the micronized powder is provided with the above-mentioned air The means for impact imparting the freeze-dried composition in the container and the means for discharging the micronized powdery freeze-dried composition from the container are prepared. ~ 16. If the freeze-dried composition according to item 14 of the patent application is used for pulmonary administration, the freeze-dried composition contains a South molecular drug as an active ingredient. 315314 118 17 ': = :: = ^ made :, formula_ ^ properties: /, medium, the freeze-dried composition has the following characteristics == dissolved components of the composition of the added component after being dry (ii) has a non- The lumpy morphology of the powder, (di) decay index is above 0.05, and (iv) by the air impact of air velocity of at least 17 to V im / sec and air impact of at least micron air flow, the average particle size can be 10 In the use / fine particles having a particle ratio of 10% or more; and the average composition is micronized to have the above effective particle ratio of A. 1 8 · If you apply for a patent, dry welding for administration = dry composition in the manufacture of transpulmonary system contains 2 systems, of which the cold pure product U is the polymer drug with active ingredients. 19 '^ Special = cold around item 17; East dry composition is contained in the lungs during manufacture: 2: Use of the preparation' wherein 'the freeze-dried composition above 4 彳 |. ^' And the recorded powder _It is equipped with a device that can be used to: read the blow to impart the coldness of the capacity; to discharge the micro-granulated powdery cold-cooled material in the container of the method of drying the composition. 2 ° ': ΐ =; the use of a composition solution of the added ingredients in a solution state, the use of clothing ", the preparation of dry powder preparation for pulmonary administration for cold; The following characteristics. 3I53J4 119 200418520 ⑴ has a non-powdered morphology, (Η) the decay index is greater than 0.05, and (-) by withstanding an air velocity of at least lm / sec and at least 10 :: two air: The impact of the air at the right flow rate can become fine particles with an average particle size of "under" or an effective particle ratio of 10% or more; and when used, it is micronized into the above average particle size or the effective particle ratio. 4 π from m. As in the patent application scope of item 2G, the composition liquid containing the added components in a non-dissolved state! "Wherein, the cold-roll-dried composition contains a South molecular drug as an active ingredient. 22. Use of a composition liquid containing non-dissolved added ingredients in the scope of application for item 2G, wherein the freeze-dried composition is contained in a container, and the micronized powder is provided with the above-mentioned air. The impact imparts the coldness in the container; the means for drying the composition and the powdery cold that can be discharged from the container; the device for the means for drying the composition. 315314 120
TW092135122A 2002-12-13 2003-12-12 Dry powder inhale system for pulmonary administration TWI327073B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002363158 2002-12-13

Publications (2)

Publication Number Publication Date
TW200418520A true TW200418520A (en) 2004-10-01
TWI327073B TWI327073B (en) 2010-07-11

Family

ID=40490921

Family Applications (1)

Application Number Title Priority Date Filing Date
TW092135122A TWI327073B (en) 2002-12-13 2003-12-12 Dry powder inhale system for pulmonary administration

Country Status (7)

Country Link
JP (1) JP4822709B2 (en)
AR (1) AR042454A1 (en)
CU (1) CU20050115A7 (en)
EA (1) EA009775B1 (en)
MY (1) MY154957A (en)
TW (1) TWI327073B (en)
ZA (1) ZA200505312B (en)

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05963A (en) * 1990-04-13 1993-01-08 Toray Ind Inc Polypeptide composition
JP3492154B2 (en) * 1997-06-26 2004-02-03 サンデン株式会社 Beverage vending machine
JP3547612B2 (en) * 1998-03-20 2004-07-28 株式会社日立ユニシアオートモティブ Inhalation type dispenser
GB2353222B (en) * 1999-06-23 2001-09-19 Cambridge Consultants Inhalers
HU229310B1 (en) * 1999-10-29 2013-10-28 Nektar Therapeutics Dry powder compositions having improved dispersivity
JP4931282B2 (en) * 2000-10-02 2012-05-16 日本ケミカルリサーチ株式会社 Bioactive peptide-containing powder
JP3943845B2 (en) * 2001-02-15 2007-07-11 芳枝 米谷 Liposome vector

Also Published As

Publication number Publication date
EA009775B1 (en) 2008-04-28
MY154957A (en) 2015-08-28
CU20050115A7 (en) 2009-02-20
JPWO2004054555A1 (en) 2006-04-13
TWI327073B (en) 2010-07-11
EA200500967A1 (en) 2006-02-24
AR042454A1 (en) 2005-06-22
ZA200505312B (en) 2006-10-25
JP4822709B2 (en) 2011-11-24

Similar Documents

Publication Publication Date Title
TW570819B (en) Dry powder inhalation system for transpulmonary administration
CN103841960B (en) For the method and formulation for sucking
CA2981038C (en) Dry powder vancomycin compositions and associated methods
JP2009136688A (en) Flow resistance modulated aerosolized active agent delivery
RO121834B1 (en) Device for the delivery of an active agent
JP2007530465A (en) Highly breathable insulin microparticles
AU2012254999A1 (en) Dry powder vancomycin compositions and associated methods
CN109996536A (en) Antimycotic dried powder
CN110799176A (en) Methods of treating pulmonary diseases
US10561608B2 (en) Dry powder Vancomycin compositions and associated methods
CN106456707A (en) Dry-powder peptide medicament
Wanning et al. Impact of excipient choice on the aerodynamic performance of inhalable spray-freeze-dried powders
US20060057106A1 (en) Freeze-dried interferon-y composition for transpulmonary administration and inhalation system therefor
JP4258647B2 (en) Dry powder inhalation system for pulmonary administration
TW200418520A (en) Dry powder inhale system for pulmonary administration
CN109771397B (en) Equipment integration and method for improving pulmonary inhalation medication through lactose micropowder predeposition
de Boer et al. Pulmonary drug delivery: delivery to and through the lung
CN106727448B (en) Octreotide acetate dry powder inhalation preparation and preparation method thereof
Hoppentocht et al. Design and development of a disposable high dose dry powder inhaler for aminoglycosides
WO2013175781A1 (en) Pharmaceutical composition for inhalation

Legal Events

Date Code Title Description
MM4A Annulment or lapse of patent due to non-payment of fees