TW200904397A - Method and apparatus for washing and collection of particles - Google Patents

Method and apparatus for washing and collection of particles Download PDF

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Publication number
TW200904397A
TW200904397A TW96126015A TW96126015A TW200904397A TW 200904397 A TW200904397 A TW 200904397A TW 96126015 A TW96126015 A TW 96126015A TW 96126015 A TW96126015 A TW 96126015A TW 200904397 A TW200904397 A TW 200904397A
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Taiwan
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cleaning
particles
particle
container
cleaning liquid
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TW96126015A
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Chinese (zh)
Inventor
Yu-Fang Hu
Shou-Min Huang
Yao-Kun Huang
Pei-Fang Lei
Shih-Hwa Tsai
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Tty Biopharm Co Ltd
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Priority to TW96126015A priority Critical patent/TW200904397A/en
Publication of TW200904397A publication Critical patent/TW200904397A/en

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Abstract

The present invention discloses a process for washing and collection particles from a emulsion solution including the steps of contacting a container with the primal particles solution; a other container for collection the washed out solution; a connecting tube connects with those contains; a push equipment to control the flow rate to throughout the apparatus. In accordance with the Stoke's law to deduce a noble formula that control the flow rate of washing solution and the length of tube to obtain a appropriate particle distribution. The improvement comprises preventing the agglomerate or breakage from the washing and collection process.

Description

200904397 九、發明說明: 【發明所屬之技術領域】 本發明係-種粒子清洗收集裳置,尤其是一種能夠以 控制流體流速以及路徑長度來達到清洗之目的,並收集不 同尺寸之粒子的裴置。 【先前技術】 一般的包覆藥物的膠囊在完成藥物包覆後,通常會經 過清洗的步驟,以去除膠囊表面殘留的藥物或雜質。 於1 980年代,日本武田製藥首先開發使用生物可分 解高分子乳酸一羥基乙酸_2_羥基丁酸共聚物 (p〇ly(laCtic/g|yco丨ic acid),PLGA)來包覆促黃體生成激素 Leuprohde acetate(H. Okada, Y. Ogawa, Τ. Yashiki, ^Prolonged release microcapsule and its production" US Patent 4,652,441, 1987 ; M. Yamamoto, S. Takeda, Y.200904397 IX. Description of the Invention: [Technical Field] The present invention relates to a particle cleaning and collecting device, in particular, a device capable of controlling the fluid flow rate and the path length for cleaning purposes, and collecting particles of different sizes . [Prior Art] A general drug-coated capsule usually undergoes a washing step after the drug is coated to remove the drug or impurities remaining on the surface of the capsule. In the 1980s, Takeda Pharmaceutical Co., Ltd. first developed the use of biodegradable polymer lactic acid monoglycolic acid 2-hydroxybutyric acid copolymer (p〇ly (laCtic/g|yco丨ic acid), PLGA) to coat the luteinizing body. Leuprohde acetate (H. Okada, Y. Ogawa, Τ. Yashiki, ^Prolonged release microcapsule and its production" US Patent 4,652,441, 1987; M. Yamamoto, S. Takeda, Y.

Ogawa, “Method for producing microcapsu丨e” Jpn Paieni >App/_ 22978/1985,February 7,1985),在產品製程中使 用水相/油相/水相(W/O/VV)的雙重乳化法製成包覆藥物之緩 釋型膠囊’在固化膠囊製程中乃是將藥物與PLGA —次乳 化溶液(W/0)注入聚乙烯醇(pva,Polyvinyl a丨cohol)水溶 液中進行第一次乳化’並以藉由水相乾燥法(jn-wate「 drying method)來進行膠囊固化,此時膠囊表面仍有殘留 藥物和PVA附著’而習用的處理方式’如一般使用的膠囊 清洗機是使用離心方式和重新注入清水來清洗殘留藥物和 PVA的附著(中華民國專利公告第182619號,發明人為山 200904397 田稔、石黑聖子、小川泰亮的「延長釋放之製劑及其聚合 物」;中華民國專利公告第1 90424號,發明人為剛田弘 晃、井上彌生、小川泰亮的「延長釋放之膠囊」;Y. Ogawa,Ogawa, “Method for producing microcapsu丨e” Jpn Paieni >App/_ 22978/1985, February 7, 1985), double emulsion of aqueous/oil phase/water phase (W/O/VV) in product process The method is to prepare a sustained-release capsule coated with a drug. In the process of curing the capsule, the drug and the PLGA-secondary emulsification solution (W/0) are injected into the aqueous solution of polyvinyl alcohol (pva, polyvinyl acohol) for the first time. Emulsification 'and capsule solidification by the water-phase drying method (jn-wate "drying method", at this time, there is still residual drug and PVA adhesion on the surface of the capsule] and the conventional treatment method is used as a general-purpose capsule cleaning machine. Centrifugal method and re-injection of clean water to clean the adhesion of residual drug and PVA (Republic of China Patent Notice No. 182619, inventor is Shan 200904397 Tian Hao, Shi Heshengzi, Xiaochuan Tailiang's "Prolonged Release Preparation and Polymer"; Republic of China Patent Publication No. 1 90424, the inventors are "Kyoto Haru, Inoue Yayoi, Ogawa Tailiang's "Extended Release Capsule"; Y. Ogawa,

M. Yamamoto, H. Okada, Υ. Yashiki, Τ. Shimamoto, "A new technique to efficiently entrap leuprolide acetate into microcapsules of polylactic acid or copoly(lactic/glycolic) acid", Chem. Pharm. Bull. 1988, 36, 1 095-1 1 03) 〇M. Yamamoto, H. Okada, Υ. Yashiki, Τ. Shimamoto, "A new technique to efficiently entrap leuprolide acetate into microcapsules of polylactic acid or copoly(lactic/glycolic) acid", Chem. Pharm. Bull. 1988, 36 , 1 095-1 1 03) 〇

然而’運用習用之方法來清洗膠囊,實際上是容易造 成膠囊的聚集與形變,尤其若是將習用之方法用於清洗如 PLGA高分子膠囊,則會因為此類膠囊的硬度不高,而更 容易產生形變,因而硬度不高的膠囊就不適合利用離心方 式來清洗與收集;而且一般利用離心收集的方式僅能達成 清洗殘留藥物和如PVA等的雜質附著,並無法對膠囊粒子 大小進行篩選。However, 'using the conventional method to clean the capsules is actually easy to cause the aggregation and deformation of the capsules. Especially if the conventional method is used for cleaning such as PLGA polymer capsules, it is easier because the hardness of such capsules is not high. Capsules which are deformed and thus have a low hardness are not suitable for cleaning and collection by centrifugation; and generally, the method of centrifugal collection can only achieve the adhesion of cleaning residual drugs and impurities such as PVA, and the capsule particle size cannot be screened.

L I叼内容J 本發明人有鑒於目前利用離心收集膠囊的方式,會造 成膠囊形變或聚集的現象,而且無法依照膠囊的粒子二小 ^丁師選’因此經過不斷的研究以及實驗之後,終於發明 出此粒子清洗收集裝置。 本發明之目的係在於提供一供釣α批ΐ丨+ 路徑長度來達到清洗之目Γ 制流體流速以及 置。 目的,並收集不同尺寸之粒子的裝 為達上述目的 本發明之粒子清洗收集 裝置,其係包 200904397 括: 一盛裝容器,其内部盛裝有清洗液以及混合於該清洗 液中欲清洗的粒子; 一收集容器; 一連接管,其一端係設置在盛裝容器中,且深入清洗 液内’而另端係設置在收集容器巾,而該連接管的中段位 置設有可將清洗液由盛裝容器推往該收集容器中的一推動 裝置’以控制清洗液在連接管内的流速,#中該連接管的 長度以及清洗液於連接管内的流速係根據欲收集之粒子尺 寸,並配合史托克定律(stokes,Law)演澤之運算式計 得。 主…係猎由連接管的推動裝置,可將盛裝容器内的 清洗液,ϋ同欲清洗的粒子—起吸人連接管内,由於史托 克定律(⑽kes’ Law)能夠㈣粒子沉降的速度,而再經過 本發明所演繹出的公式決^連接f的長度,以及清洗液通 ^連接官的料,故可讓通料接管的粒子達到清洗的目 的’而且不會讓粒子變形或聚集,此夕卜,尚可讓不同尺寸 的粒子分開,較小的粒子可進入收隼 ^ BI 队木令窃中,而較大的粒 千則留在連接管内,依此原則進行 日φ 〗延仃夕-欠的流速的改變,並 更換收集容器,即可收集到不同尺寸的粒子。 【實施方式】 明參看第一及二圖所示,本發 置,其係包括: 月之粒子清洗收集裝 -盛裝容器㈠〇),其係可為—τΜ部具有開口(ι 200904397 1 )的容器,其内部盛裝有清洗液(1 2)以及混合於該 清洗液(1 2 )中顆粒大小不一的欲清洗粒子(1 3 ), 該清洗液(1 2 )可為清水、酒精等,可視欲清洗粒子(1 3)的性質以及欲去除之雜質而決定,該欲清洗粒子(1 3 )係高分子粒子,而該高分子粒子可為一種微膠囊型的 醫藥組合物’其係可為聚胜肽之聚乳酸或聚醇甘酸酸或其共 聚合物之微膠囊組合物,其中聚胜肽為五氧—脯胺酸_組胺酸_ 色胺酸-絲胺酸-路胺酸-右旋-亮胺酸-亮胺酸-精胺酸-脑胺酸_ 乙胺基(5-oxo-Pro-His-Trp-Ser-Tyr-D-Leu-Leu-A「g-Pro _ NH-C2H5,藥品名為柳培林(Leup「0|jde Acetate))。 一收集谷器(30),其亦為頂部具有開口(31) 的谷器,其係用以收集欲收集之粒子(1 3,); 。一連接管(20),其一端(21)係設置在盛裝容 器(10)中,且伸入清洗液(12)内,而另端(22) 係設置在收集容器(3 〇 )巾’而該連接管(2 〇 )的中 段位置設有可將清洗液(1 2 )自盛裝容器(i Q )推往 該收集容器(3 0 )中的-推動裝置(2 3 ),以控制清 '先液(1 2)在連接官(2〇)内的流速,該推動裝置(2 3 )可為螺動幫浦、離心式幫浦、往復式幫浦等於所屬領 域具有通常知識者所知可用於推動液體的推動裝置皆包含 於本發明之料’以該連接管(2〇)的長度以及清洗 液於連接管(2 ◦)内的流速係根據欲收集之粒子(丄3 該運算式如下:z= ί162) (18// \ Kg{p-p0)d\ 200904397 „其:L為連接管所需要的長度;Q為清洗液進入連接 :ΐίί:: 接管之直徑;"為清洗液的黏度々為 又0為α洗液的密度;d為欲收集之粒子之半徑。 、旋承置木(4〇),其係包括一底板以及凸設於 該底板的上表面的卡固片(4 ",該卡固片(4ι)係 以螺旋狀環設於底板的上表面,以形成—螺旋狀的容置空 間(4 2 ),供該連接管(2 〇 )中段位置放置其中。 使用本發明之粒子清洗收集裝置時,先將清洗液(i 2 )以及欲清洗粒?(")放入盛裝容器(i 〇 )中, 再使用-連接管(2 〇 ),其係具有以史托克定律(⑽心 Law)演繹之新穎運算式所計算出來的長度,將該連接管(2 〇) 一端放入盛裝容器(1〇)且浸入清洗液(丄2 )中,LI叼Content J The present inventors have in view of the current phenomenon of collecting capsules by centrifugation, which may cause deformation or aggregation of the capsules, and cannot be selected according to the particles of the capsules. Therefore, after continuous research and experiments, the inventors finally invented. The particle cleaning collection device is taken out. SUMMARY OF THE INVENTION It is an object of the present invention to provide a target flow rate for cleaning and a path length for cleaning. The purpose of the present invention is to collect particles of different sizes and to prepare the particle cleaning and collecting device of the present invention for the above purpose. The kit 200904397 comprises: a container containing a cleaning liquid and particles mixed in the cleaning liquid to be cleaned; a collecting container; a connecting tube, one end of which is disposed in the holding container and deep into the cleaning liquid and the other end is disposed in the collecting container, and the middle portion of the connecting tube is provided to push the cleaning liquid from the container to the container a pushing device in the collecting container to control the flow rate of the cleaning liquid in the connecting pipe, the length of the connecting pipe and the flow rate of the cleaning liquid in the connecting pipe are according to the particle size to be collected, and cooperate with the Stokes law (stokes , Law) The calculation of the performance of Ze. The main... is the pushing device of the connecting pipe, which can wash the cleaning liquid in the container and the particles to be cleaned into the connecting pipe, because the Stoke law ((10)kes' Law) can (4) the speed of particle sedimentation, And the formula deduced by the invention determines the length of the connection f, and the cleaning liquid is connected to the official material, so that the particles of the material can be cleaned for the purpose of cleaning and the particles are not deformed or aggregated. In addition, it is still possible to separate particles of different sizes, smaller particles can enter the smashing of the BI team, and the larger granules remain in the connecting pipe. According to this principle, the φ 〗 〖 - A change in the flow rate of the underflow and the replacement of the collection container allows the collection of particles of different sizes. [Embodiment] Referring to the first and second figures, the present invention includes: a monthly particle cleaning and collecting device-containing container (1), which may have an opening of -τΜ with an opening (ι 200904397 1 ) a container containing a cleaning liquid (1 2) and a cleaning particle (1 3 ) mixed with the particle size of the cleaning liquid (1 2 ), the cleaning liquid (1 2 ) may be water, alcohol, or the like. Depending on the nature of the particles (13) to be cleaned and the impurities to be removed, the particles (13) are to be washed, and the polymer particles may be a microcapsule-type pharmaceutical composition. a microcapsule composition of polylactic acid or polyglycolic acid or a copolymer thereof of a polypeptide, wherein the polypeptide is pentoxide-proline-histamine _ tryptophan-serine-glucuric acid - dextro-leucine-leucine-arginine-encephalin_ethylamine (5-oxo-Pro-His-Trp-Ser-Tyr-D-Leu-Leu-A"g-Pro _ NH-C2H5, the drug name is Leup "0|jde Acetate". A collection trough (30), which is also a trough with an opening (31) at the top, which is used to collect the particles to be collected. 1 3,); A connecting pipe (20), one end (21) of which is disposed in the containing container (10) and protrudes into the cleaning liquid (12), and the other end (22) is disposed in the collecting container (3) 〇) towel' and the middle section of the connecting pipe (2 〇) is provided with a pushing device (2 3 ) for pushing the cleaning liquid (1 2 ) from the container (i Q ) into the collecting container (30) In order to control the flow rate of the clear liquid (1 2) in the joint official (2〇), the pushing device (2 3 ) can be a screw pump, a centrifugal pump, a reciprocating pump equal to the field The propelling device known to the skilled person to be used for pushing the liquid is included in the material of the present invention. The length of the connecting tube (2〇) and the flow rate of the cleaning liquid in the connecting tube (2◦) are based on the particles to be collected (丄3 The expression is as follows: z= ί162) (18// \ Kg{p-p0)d\ 200904397 „It: L is the length required for the connecting pipe; Q is the cleaning fluid entering the connection: ΐίί:: the diameter of the connecting pipe; "The viscosity of the cleaning solution is 0 and the density of the alpha lotion; d is the radius of the particles to be collected. a screw-on wood (4 inch), which comprises a bottom plate and a fastening piece (4 " protruding from the upper surface of the bottom plate, the fastening piece (4ι) is arranged on the bottom plate by a spiral ring a surface to form a spiral-shaped accommodating space (4 2 ) for the middle portion of the connecting tube (2 〇) to be placed therein. When using the particle cleaning collecting device of the present invention, the cleaning liquid (i 2 ) and the cleaning liquid are first cleaned. The granules (") are placed in a container (i 〇), and the - connection tube (2 〇) is used, which has a length calculated by the novel equations deduced by Stork's law ((10) Heart Law). Place one end of the connecting tube (2 〇) into the container (1〇) and immerse it in the cleaning solution (丄2).

另端則連接有一收集容器(3⑹,之後將該連接管(2 〇 )與一推動裝置(2 3 )連接,並且以史托克定律(St0kes, Law)演繹之新穎運算式所計算出欲收集之粒子(丄3,) 尺寸需要達到的流速,接著開啟該推動裝置(2 3 ),使 含有欲清洗粒+ ( 1 3 )的清洗液(χ 2 )流動至連接管 (2 0 )中,則欲得到之尺寸的粒子會隨著清洗液(丄2 ) 進入收集容器(3 0)内。最後可更換收集容器(3 〇), 並調整推動裝置(2 3 )的流速,以收集在不同尺寸之粒 子0 上述配合史托克定律(Stokes’ Law)演繹之運算式係經 由以下推導而得: 「史托克定律(Stokes’ Law)」的公式(1)如下: 200904397 Ο) g(p-p〇)d2 18// 黏度(poise,P ) 粒子直徑(cm) 重力常數(980 cm/s) L :終速(cm/sec) μ : P :固體密度(cm3/g) d : 流體密度(cm3/g) g: 請參看第三及四圖所示,D表示連接管(2〇)之直 表示連接管(20)之半徑u示水流在連接 管(2 0 ) X軸最尚速度,Ux表示水流在連接管(2 〇) χ 軸之平均速度;Uy表示水流在連接管(2 〇 ) y軸之平均 速度。已知欲收集之粒子之半徑(d)、密度(p)、溶液密度 (ρσ)、溶液黏度(//),如此就可以求得連接管(2 〇 )的 長度: 在連接管(20)中粒子(l3a)在χ轴之速度分 量可以表示成(2)式:At the other end, a collecting container (3 (6) is connected, and then the connecting tube (2 〇) is connected with a pushing device (23), and is calculated by the novel arithmetic formula deduced by Stokes Law. The particle (丄3,) size needs to reach the flow rate, and then the pushing device (2 3 ) is turned on, so that the cleaning liquid (χ 2 ) containing the cleaning particles + ( 13 ) flows into the connecting tube (20). The particles of the desired size will enter the collection container (30) with the cleaning solution (丄2). Finally, the collection container (3 〇) can be replaced, and the flow rate of the pushing device (23) can be adjusted to collect differently. Particles of size 0 The above-mentioned formulas in conjunction with Stokes' Law are derived from the following derivation: "The formula (1) of "Stokes' Law" is as follows: 200904397 Ο) g(pp 〇)d2 18// Viscosity (Pise) Particle diameter (cm) Gravity constant (980 cm/s) L : Final speed (cm/sec) μ : P : Solid density (cm3/g) d : Fluid density ( Cm3/g) g: Please refer to the third and fourth figures, D indicates that the connecting pipe (2〇) directly indicates the connecting pipe (20) U shown in the flow path connecting pipe (20) is still the most X-axis velocity, Ux denotes the average flow velocity in the connection pipe axis χ (2 billion); mean flow velocity Uy denotes the connection pipe (2 billion) y-axis of. Knowing the radius (d), density (p), solution density (ρσ), and solution viscosity (//) of the particles to be collected, the length of the connecting pipe (2 〇) can be obtained: in the connecting pipe (20) The velocity component of the middle particle (l3a) on the x-axis can be expressed as (2):

U maxU max

y — R R 2〇, 、2 (2) (3) 而連接官(2 0)中粒子(1 3a)在y軸之速度分 量可以使用Stokes’ Law加以表示: u = - _^y. (4) 18// dt K } -jw·! (5) 11 200904397 y = -Μ + c (6) 假設粒子(1 3 a)在t=0推入> β ^ 〇進入連接管(20)的位 置疋在隶鬲位置2R,以此做為邊®你屯 马逯界條件,可以得到式(7)。 y = _uyt+2R (?) dy = -uydt (8) 在連接官(20)中粒子最終掉落在管壁的距離l與 粒子(1 3a)在X軸之速度分量^的關係可以使用式⑻ 加以表示:y — RR 2〇, , 2 (2) (3) The velocity component of the particle (1 3a) in the joint officer (2 0) on the y-axis can be expressed using Stokes' Law: u = - _^y. (4 18// dt K } -jw·! (5) 11 200904397 y = -Μ + c (6) Suppose the particle (1 3 a) is pushed in t=0 > β ^ 〇 into the connecting tube (20) Position 疋 at the 鬲 position 2R, as a side 屯 屯 屯 屯 条件 条件 条件 , 。 。 。 。 。 。 。 。 。 。 。 。 。 。 y = _uyt+2R (?) dy = -uydt (8) The relationship between the distance l at which the particles eventually fall on the tube wall and the velocity component of the particle (1 3a) on the X axis in the joint officer (20) can be used. (8) To indicate:

XX

XX

XX

X -2- ι-( y-R, ~R~} dt (9) ί(2ϋ^ν 當y 3m.X -2- ι-( y-R, ~R~} dt (9) ί(2ϋ^ν when y 3m.

, 3R 2R,而 -R, 3R 2R, and -R

-) + C dy (1 0) (11) (12) 時 (13) x 當y-) + C dy (1 0) (11) (12) When (13) x When y

4R uv R 3R2 3 而x = L時4R uv R 3R2 3 and x = L

RR

R 3i^ D/2 ; iZ, (14) _Q_ tcD2 18" L·' (ΙΕμ ) )nD j [s(p~p0)d\ (Q:=入連接管之Γ公尺公升™ (15) 式(15)即是本發明所採用之運算式。 12 200904397 在連接s (20)中粒子(1 3a)最終掉落在管壁 的距離L即為連接官(2 〇 )所需要的長度,利用公式(Η) 可以將粒川3a)密度、流體密度、流體黏度,藉由 控制抓體進入連接官(2 〇 )的通量和連接管(2 〇 )管 長,就可收集固定大小的粒子(丄3a)。R 3i^ D/2 ; iZ, (14) _Q_ tcD2 18" L·' (ΙΕμ ) )nD j [s(p~p0)d\ (Q:=Metric liters into the connecting tube TM (15) Equation (15) is the arithmetic expression used in the present invention. 12 200904397 The distance L at which the particles (1 3a) eventually fall on the tube wall in the connection s (20) is the length required for the connection officer (2 〇), Using the formula (Η), you can collect the fixed-size particles by controlling the density of the grabbing body, the fluid density, and the fluid viscosity by controlling the flux entering the joint (2 〇) and the length of the connecting tube (2 〇). (丄3a).

月/看第五圖所不,當管徑D = 〇 635 cm、流體通量 0.33 mL/s、液體黏度 μ=1 〇2 Μ =1 〇2χΐ〇2 p 松度~=1.〇〇細3、粒子(l3a)密度p=1〇2g/c=3體 重力常數g = 980 cm/s以及欲收集之粒子的直徑 d=3〇Xl〇-4cm,代入式(9),可得需要連接管(2 0 )長度 約為4.6 m。 —依此類推,欲留住粒徑20微米(μιη)的粒子需要連接 β ( 2 0 )長度為18.4公尺以上;而粒徑1〇|im的粒子需 要連接管(2 0 )長度為41.4公尺以上。 實施例 下述實施例係使用本發明之裝置的流程,其係僅用於 不範本發明的使用方法,讓於所屬領域具有通常知識者能 夠更清楚了解本發明的實施方式,而並非意欲限制本發明 的範圍,因此,只要在不脫離本發明之原則下所做的改變, 如粒子形狀、種類等,皆屬於本發明之範嗜。 經由水相/油相/水相(W/0/W)製程所得之2公升含有 0.25%聚乙烯醇(PVA,Polyvinyl alcohol)懸浮水溶液,其 懸浮物為尚分子乳酸一經基乙酸-2-經基丁酸共聚物 13 200904397 (p〇ly(laCtiC/glyC〇lic acid),PLGA)包覆促黃體生成激素 Leuprolide acetate之微膠囊,其密度為)〇2 g/cm3,而 此流體之密度大約等於1 〇 g/cm3,欲收集粒子之粒徑在 10μΓΠ以上,連接管之内管徑為〇 625公分,連接管長度 至少為41.4公尺。 首先,將懸浮液體以蠕動幫浦以每分鐘彳〇毫升的速 度將2公升清水打入連接管中,經過大約33小時使所有 含PLGA的清水進入連接管中,再將通入連接管之液體流 () 速調快至每分鐘200毫升,此時可以將粒徑小於1〇微米 之PLGA微粒經由連接管一端進入收集容器中。 請參看第六圖所示,再重新使用蠕動幫浦,將盛裝容 器中含有PLGA微粒的水溶液以每分鐘1〇毫升的速度輸 入連接管中,清洗並收集大於1〇μηΊ以上之微粒,重複上Month / see the fifth picture, when the diameter D = 〇 635 cm, fluid flux 0.33 mL / s, liquid viscosity μ = 1 〇 2 Μ =1 〇 2 χΐ〇 2 p looseness ~ = 1. 3, particle (l3a) density p = 1 〇 2g / c = 3 body weight constant g = 980 cm / s and the diameter of the particles to be collected d = 3 〇 Xl 〇 -4cm, substituted into the formula (9), can be obtained The connecting tube (20) has a length of approximately 4.6 m. - and so on, to retain particles with a particle size of 20 microns (μιη) need to connect β (20) to a length of 18.4 meters or more; and particles with a particle size of 1〇|im need a connecting tube (20) with a length of 41.4 More than a meter. The following examples are intended to be illustrative of the embodiments of the present invention, and are not intended to limit the scope of the present invention. The scope of the invention, therefore, is intended to be within the scope of the invention as long as the changes are made without departing from the principles of the invention, such as particle shape, type, and the like. 2 liters of the aqueous solution obtained by the aqueous phase/oil phase/aqueous phase (W/0/W) process contains 0.25% polyvinyl alcohol (PVA, Polyvinyl alcohol) suspension aqueous solution, and the suspension is a molecular lactic acid-based acetic acid-2-peracetate Butyric acid copolymer 13 200904397 (p〇ly(laCtiC/glyC〇lic acid), PLGA) coated microcapsules of luteinizing hormone Leuprolide acetate, the density of which is 〇2 g/cm3, and the density of this fluid is about Equal to 1 〇g/cm3, the particle size of the particles to be collected is 10 μΓΠ or more, the inner diameter of the connecting tube is 〇625 cm, and the length of the connecting tube is at least 41.4 m. First, the suspended liquid is pumped into the connecting pipe at a speed of 彳〇ml per minute with a peristaltic pump. After about 33 hours, all the water containing PLGA is put into the connecting pipe, and then the liquid flowing into the connecting pipe is introduced. The flow () speed is as fast as 200 ml per minute. At this time, PLGA particles having a particle size of less than 1 μm can be introduced into the collection container through one end of the connecting tube. Please refer to the sixth figure, and then re-use the peristaltic pump to input the aqueous solution containing PLGA particles into the connecting tube at a speed of 1 liter per minute. Clean and collect more than 1〇μηΊ particles, repeat

述步驟三次之後,可以收集到粒徑大於1〇微米之pLGA 微粒。 經實驗結果驗證了(1 5)式的理論推論,將本系統之連 I 接管長度設計為大於41.4公尺,以每分鐘1〇毫升的速度 輸入連接官中,可以收集到粒徑大於,〇微米之pLGA微 粒。 本發明之裝置可用於收集生物可分解之微膠囊製程 中尤其可以收集如PLGA等高分子硬度較低之微粒子, 可以避免在清洗、收集製程中產生聚集或形變。 【圖式簡單說明】 第一圖係本發明之立體圖。 14 200904397 第二圖係本發明之平面示意圖。 —第三圖係本發明所運用之史托克定律 徑示意圖。 的流速分布與管 第四圖係本發明所運 下距離與速度分量的示意 第五圖係本發明所運 大小與落下距離的關係 用之史托克定律於管 圖。 用之史托克定律於管 圖。 内之粒子落 内粒子之粒 第After three steps, pLGA particles having a particle size greater than 1 μm can be collected. The experimental results verify the theoretical inference of (1 5), and the length of the I-connector of the system is designed to be greater than 41.4 meters. The input is connected at a speed of 1 〇 per minute, and the particle size can be collected. Micron pLGA particles. The device of the invention can be used for collecting biodegradable microcapsules, in particular, it can collect fine particles with low hardness such as PLGA, and can avoid aggregation or deformation during cleaning and collection processes. BRIEF DESCRIPTION OF THE DRAWINGS The first drawing is a perspective view of the present invention. 14 200904397 The second figure is a schematic plan view of the invention. - The third figure is a schematic diagram of the Stoker's law path used in the present invention. Flow Rate Distribution and Tubes The fourth diagram is a schematic representation of the distance and velocity components of the present invention. The fifth diagram is the relationship between the size and the drop distance of the present invention. Use the Stoker's law in the chart. The particles inside are falling inside the particles

六圖係本發明實施例中所收集 之粒子的粒徑分佈 【主要元件符號說明】 (1 1 )開口 (1 0)盛裝容器 3 )欲清洗粒子 (1 3 a)粒子 1 ) 一端 3 )推動裝置 1 )開口 1 )卡固片 (1 2 )清洗液 (i (1 3 ’)欲收集之粒子 (2 0 )連接管 (2 (2 2 )另端 (2 (3 〇 )收集容器 (3The six figures are the particle size distribution of the particles collected in the examples of the present invention. [Main component symbol description] (1 1 ) Opening (10) container 3) Particles to be cleaned (1 3 a) Particles 1) One end 3) Push Device 1) Opening 1) Fixing piece (1 2 ) Cleaning solution (i (1 3 ') Particles to be collected (2 0 ) Connecting tube (2 (2 2 ) Other end (2 (3 〇) collecting container (3

(40)迴旋承置架 (4 (4 2 )容置空間 15(40) Rotary bearing frame (4 (4 2 ) accommodating space 15

Claims (1)

200904397 十、申請專利範圍: 子清洗收集裝置,其係包括: ’其内部盛裝清洗液以及混合於該清洗液 1 · 一種粒 一盛裝容器 中欲清洗的粒子 一收集容器; 一連接官’其一端係設置在盛裝容器中,且深入清洗 液内’而另端係設置在收集容器中,而該連接管的中段位 置設有可將清洗液由盛裝容器推往該收集容器中的一推動 裝置’以控制清洗液在連接管内的流速,其中該連接管的 長度以及清洗液於連接管内的流速係根據欲收集之粒子尺 寸,並配合史托克定律(St0kes,Law)演繹之運算式計算而 得。 2 ·如申清專利範圍第1項所述之粒子清洗收集裝 置,其中該欲清洗粒子係高分子粒子。 3 ·如申請專利範圍第2項所述之粒子清洗收集裝 置,其中邊而分子粒子係·一種微膠囊型的醫藥組合物。 i 4 ·如申請專利範圍第3項所述之粒子清洗收集裝 置,其中該微膠囊型的醫藥組合物係一種選自於以下之群 組的微膠囊組合物:聚胜肽之聚乳酸、聚醇甘酸酸及其共聚 合物。 5 ·如申請專利範圍第4項所述之粒子清洗收集裝置, 其中該聚胜肽為五氧-脯胺酸-組胺酸—色胺酸-絲胺酸-酪胺酸 -右旋-亮胺酸-亮胺酸·精胺酸-脯胺酸-乙胺基。 6 .如申請專利範圍第1至5項中任一項所述之粒子 16 200904397 清洗收集裝置’其中該清洗液為清水 7.如申請專利範圍第1至5項中任_項 清洗收集裝置’其中該推動裝置為蠕動幫浦。以之粒子 8 ·如t請㈣範圍第丄至5項中任 清洗收集裝置,其中該推動裝置為離 4之粒子 [如申請專利範圍第…項中任幫二所这 清洗收集裝置,其中該推動裝置為往復式幫浦。迷之粒子 1 〇 .如申請專利範圍第i至5項中 子清洗收集裝置,*尚包含—迴旋承置架,㈣粒 板以及凸設於該底板的上表面的卡固 ,、匕括一底 旋狀環設於底板的上表面,;:::片係以螺 置其中的螺旋狀容置空間。 罝放 •、圖式: 如次頁 17200904397 X. Patent application scope: Sub-cleaning collection device, which includes: 'The inside is filled with cleaning liquid and mixed with the cleaning liquid 1 · A particle-containing container is used to clean the particles - a collection container; It is disposed in the container and deep into the cleaning liquid, and the other end is disposed in the collecting container, and the middle portion of the connecting tube is provided with a pushing device for pushing the cleaning liquid from the container to the collecting container. To control the flow rate of the cleaning liquid in the connecting pipe, wherein the length of the connecting pipe and the flow rate of the cleaning liquid in the connecting pipe are calculated according to the particle size to be collected, and calculated according to the calculation formula of Stokes' Law (St0kes, Law) . The particle cleaning and collecting device according to claim 1, wherein the particles to be washed are polymer particles. The particle cleaning and collecting device according to claim 2, wherein the molecular particle system is a microcapsule type pharmaceutical composition. The particle cleaning collection device according to claim 3, wherein the microcapsule-type pharmaceutical composition is a microcapsule composition selected from the group consisting of polylactic acid and poly-polypeptide. Alcoholic acid and its copolymer. 5. The particle cleaning collection device of claim 4, wherein the polypeptide is pentoxide-proline-glycine-tryptophan-serine-tyrosine-dextro-bright Amino acid-leucine acid arginine-proline-ethylamine. 6. The particle 16 according to any one of claims 1 to 5, 200904397, a cleaning and collecting device, wherein the cleaning liquid is fresh water. 7. The cleaning collecting device of any one of items 1 to 5 of the patent application scope. The pushing device is a peristaltic pump.颗粒8····························································· The pushing device is a reciprocating pump. Particles of the fascination 1 如. For the neutron cleaning collection device of the scope of the patent range ith to 5, * still includes - the rotating bearing frame, (4) the slab and the fastening of the upper surface of the bottom plate, including one The bottom spiral ring is disposed on the upper surface of the bottom plate;;:: the film system is screwed into the spiral receiving space therein. •放、,图: 如次页 17
TW96126015A 2007-07-17 2007-07-17 Method and apparatus for washing and collection of particles TW200904397A (en)

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