M289194 八、新型說明： 【新型所屬之技術領域】 ^ 1T-Z11! ^#] #^ ^ ^ ^ ^ ^ ^ ^ 混人：二另：：热囷之乾燥槽中進行菌種與粉粒劑载體 此口相接，另错由該槽體直 乾焊之㈣或熱之風量予以控制 獲致該粉粒劑之接菌與乾燥濃縮之作举 機構，整體據以提高接菌粉粒 卞菜 口 π TJLd之保存與囷體密度及降低 成本之叙粒劑接菌乾燥濃縮裝置者。 【先前技術】 按’於大量或高密度乾燥g種時’係將含菌之撥酵液 體於直立式之乾燥槽頂端以噴霧之方式投人㈣中，使含 菌之酸酵液體自槽體頂㈣下至底部之收集桶中，於該落 :滯留於槽體之期間，同時利用冷或熱之風量予以控制乾 燥，使含菌之醱酵液體於槽體飄浮狀態下逐漸乾燥，形成 一固狀之粉粒劑落下，俾以獲致該高純度含菌之粉粒劑。 请苓閱第四圖所示，係為一般常用乾燥菌種之作業方 式’該乾燥槽6 0係於槽體近底部適當處設有一入風口 6 1 ’俾以將冷或熱之風量送進槽體中，又於乾燥槽6 〇頂 部設有一排氣口 6 2，槽體上方一侧設有一具喷霧方式之 入料口 6 3，俾將該含菌之醱酵液體以喷霧投入槽體中， 再利用冷或熱之風量予以控制乾燥，藉以獲致該固狀之菌 種粉粒劑者。 M289194 【内容】（所欲解決之技術問題） :本創作者發現’於 業，有如下所述之缺點： 囷禋钇森之結構中作 1、由於該乾燥粉粒劑菌 醱酵液體於乾燥槽中滞 v成’係依據該含菌之 高度與體積呈相對之擴大，：㈣，因此該槽體之筒身 造成使用空間上之困於月未 每揮乾燥之功能，然卻 π上之困擾及處理設傷成本之增加。 Z、在乾烯過程中，係刺 業，血法遠治f #^或熱之風量進行乾燥作 度過高易有其耐熱程度，若溫 且合使鬥插ί 溫度過低則不易達成乾燥， =曰=種相互間因過潮而沾黏成不適使用 顆 狀作業程序之負擔，且影響該菌種之存活率者員粒 拌機後ί菌種於使用時，需額外添加粉劑於混 種= 卑形成一具載體之乾燥粉粒劑，以供菌 以養魅存環境，惟如此之繁翁業 及能源相對消耗。 勿使成本 綜上所述之各項缺點，致使整體粉 縮之功效不佳，實有待改良之必要性。^接囷與乾燦濃 (解決問題之技術手段） 本創作有鑑於此，乃憑恃著長期對於乾燥濃縮裝置之 縮=融會貫通之構思，而創作出一種粉粒劑接菌乾燥濃 '、'衣置之改良，主要係具有一無菌橫式密閉中空筒身之 燥槽’該乾燥财設具有㈣裝置，乾_筒身設有複』 M289194 :吸口、接種口，且於筒身上端設有一入料口盘一抽 過真空泵浦作彭，又於= 該氣液分離槽係透 筒身底端外緣圍設有一：當m:出料口 ’於乾燥槽 與市水接設，可導人蒸氣加熱或與市水冷卻雙重功 载體:二 備之粉料载體由入料口投入，並將粉料 噴，同時將該供接種之液態菌種由接種口 再空份混合，形成-粉粒劑之載體， 乾燥濃縮之絲，使口：；=風裝置之減壓乾燥作業，俾達 效试ri 達到保存及提高菌體密度之目的，且有 〆夕θ體筒身體積、增加位、^ ^ 據以達實用性與創新效益者。ι避免^原之浪費’ (對知先前技術之功效） 如下之若干功:月件知’本創作相較先前技術’確可達到 1、 乾燥保存：本創作粉粒 過該真空抽氣與加M 辰縮衣置’係透 效增加粉粒劑之乾二=置予以減壓乾燥作業，可有 2、 降低志太/、，縮功 並大幅縮短乾燥時間者。 且具有可同時粉粒作乾燥濃縮裝置之係採橫式筒身， 可減少槽體筒：之二囷：減壓乾燥濃縮之設計’其不僅 單位產能，俾達降::本:::使用空間可以變大、增加 M289194 从甚3、作業統—：本創作粉粒劑之接菌料奸声、曲 作業，係可於同一盔菌之綮 菜”乾‘痕縮 業與降低成本之功i。 以完成作業’俾達簡化作 Ί高粉料載體之培養密度··本創作 :氣口與滤網設置，可產生螺旋切線旋 免抽二心 戟體培養讀與时率提高之雙重功效。 5、可瞬間高溫加熱或低溫冷卻··由於 置之夾套設計’係可利用蒸氣將槽體瞬間予以高心：裳 ::水循環冷卻’並導入無菌乾燥低溫冷風，亦；口瞬二 低溫冷卻之功效。 達瞬間 【實施方式】 濃縮：：Γ!一〜三圖所示，係為本創作粉粒劑接菌乾燥 、、、衣置之改良及作動配置示意圖，其係包括： ” 乾爍槽1 0，係為一橫式中空密閉之筒身者； -入料π 1 1，係設於乾燥槽i 0筒身 开 入料之管口者； 例形成一 =管：，係於乾燥槽i 0之筒身上方設有數呼 數具噴霧裝置之接種口13; 1 上延：㈣管14 ’係由乾燥槽10之筒身適當位置處向 口之伸一官口，且該抽氣管i 4之管口處偏心設有—抽= 口 1 5及一漏斗狀濾網i 6，並利用該抽氣口丄5鱼—， ’夜分離槽5 0相接通’並透過真空泵浦2 〇作動 $礼 分離槽5 Q係可將水氣、空氣與微粒物分離者；於真^液 M289194 f 2 0作動抽氣時可產生螺㈣線旋❹ 末顆粒上升附著於偏6處， =抽氣，且粉 剝落網上之附著粒使其落回至槽體内，俾可Ζ粒撞擊並 4阻塞； 避免抽氣管1 一攪拌裝置3 0，係於乾燥槽i 〇内樞 翼3 2之擾拌軸3 1，且於槽體外部設-馬達具有授拌 轴3 1插接，俾可達驅動授掉之功效者； 3與授拌 一乾燥裝置4 0 ,係於乾燥槽丄〇筒 有-適當半徑之夹套41，該筒 套二：緣：設 數進氣口42，俾供冷風之導入，該4間貝設有複 數蒸氣入口 43,且該蒸氣入口…二：:有複 另於夹套4 1底侧設有複數蒸氣出口 4 4，且該 作為水入口者，將該蒸氣入口（水出 ㈣出口（水入口）4 4、真空泵浦2 〇及 係利用熱交換原理，將教++ / 市水接設，其 ，、乂換㈣將熱療氣打入水中 入降溫，因此乾燥槽i 〇可達瞵 』用冷水¥ 降至低溫，使且有導入Λ 溫’亦可瞬間 -出/、Λ 市水冷卻之雙重功效者； 出枓口 1 7，係於乾燥槽丄〇之 垂設-排料出cr，且於管口處有 蜱：貝、下 成-具自動出料口設計者； ㈣蝶闊18’以形 置之件之組成’本創作粉粒劑接菌乾燥濃縮裝 :作方式敘述如下’將預先準備之粉料载體由入料口 =，其亦係可投入二種以上之粉料載體，經 33讀攪拌轴31轉動，以將粉料载體均勻料混合， M289194 且兼有破碎大顆團塊之效果，再利用吉 抽真空，且透過遽網16之抽氣口 ^空果浦2〇將筒内 侦乳口 1 5偏心 旋切線旋風，避免抽氣阻塞且有对担& 累 盅监^ t、* + ^, 有效&向粉料載體回收率， =將热U入夾套4 1内’使進行加熱滅菌，以減 其I，混拌與1 菌作業可同時進行，而在初操作階： 守，忒供接種之液悲菌種可由接種口 i 、又 -混入粉料載體上，其亦可間歇性摔作_務、句勻噴灑 及速度，使液態菌種與粉料載體充分混合:二大小 ’： = 粒劑載體可提供菌種滋養與生存環境: 再抽真工加熱，以便除去水分，即為減廢操 ==由抽真空並導入低溫度之乾燥無菌冷風:使 :身内^度控制至預設溫度以下’以便於除水， 冷風乾燥濃縮作業，其中，哕诘厭 … 該減壓刼作與減壓冷風乾燥濃 ίΠΓ屮’亦可採單—或同時使用，最後再將 Ϊ : 7自動排料浅出；使可在無菌狀態 體種到载體上，經乾燥濃縮達到保存及提高菌 度目的’ Μ效減少槽體筒身體積、增加單位產能盥 C免月^源之浪費，據以達實用性與創新效益者。 所述，本創作之「粉粒劑接菌乾燥濃縮裝置之改 妒二，才曰可於無菌狀態下完成接菌與乾燥濃縮作業之 以衣置’使預先準備之粉料載體由乾燥槽人料口投入， ί攪拌裝置Μ混拌，再將液態_由接種Π混入粉料載 ΐ上*7時進行乾燥與接®作業，而後經減壓乾燥濃縮作 ^ η產生粉粒劑之載體，整體據以達粉粒劑乾燥濃 M289194 =保$與提高菌體密度之目的，且有效減少槽艫筒身體 、曰加單位產能與避免能源浪費，俾使整體確具產業實 用性與Ϊ本效益，且其構成結構又未曾見於書刊或公開使 :誠付合新型專利中請要件，懇請鈞局明鑑，平日准 予專利，至為感禱。 :陳明者，以上所述乃是本創作之具體實施立即所 之技術原理’若依本創作之構想所作之改 =能作用仍未超出說明書及圖示所涵蓋之時所= 在本創作之範圍内，合予陳明。 守均應 【圖式簡單說明】 =一圖為本創作乾刼濃縮裝置之剖面示意圖。 圖為本創作乾㈣料置之侧視®。 =二圖為本創作乾燥濃縮裝置之作動配置示意圖。 圖為習用乾燥濃縮裝置之剖面示意圖。 【主要元件符號說明】 (本創作） 10· •乾燥槽 12· •呼吸口 14· •抽氣管 16· •濾網 18· •出料蝶閥 3 0· •攪拌裝置 11··入料口 1 3 · ·接種口 1 5 · ·抽氣口 1 7 · ·出料口 2 0 ··真空泵浦 31··攪拌軸 M289194 3 2 · ·攪拌翼 4 Ο ··乾燥裝置 4 4 2 · ·進氣口 4 4 4 ··蒸氣出口（水入口） Ε (習用） 6 0 · ·乾燥槽 6 6 2 · ·排氣口 6 3 · ·馬達 1 · ·夾套 3 ··蒸氣入口（水出口） 0 ··氣液分離槽 1··入風口 3··入料口M289194 VIII, new description: [New technology field] ^ 1T-Z11! ^#] #^ ^ ^ ^ ^ ^ ^ ^ Mixed people: two other:: hot and dry in the trough and powder The carrier is connected to the mouth, and the wrong body is controlled by the direct dry welding of the tank body (4) or the amount of hot air is controlled to obtain the mechanism for inoculating and drying the powder granules, and the whole is used to improve the pickled powder leeks. The storage of the π TJLd and the concentration of the corpus callosum and the cost reduction of the granulating agent for drying and concentrating the device. [Prior Art] According to 'Drying a large or high-density g-type', the bacteria-containing fermentation liquid is sprayed into the top of the vertical drying tank and sprayed into the liquid (4) to make the bacteria-containing acid fermentation liquid from the tank. The top (four) down to the bottom of the collection barrel, in the fall: during the period of retention in the tank, while using the cold or hot air volume to control the drying, so that the bacteria-containing fermentation liquid is gradually dried in the floating state of the tank, forming a The solid powder granules are dropped, and the granules are obtained by the high purity bacteria. Please refer to the fourth figure, which is the working mode of commonly used dry bacteria. 'The drying tank 60 is equipped with an air inlet 6 1 ' at the appropriate place near the bottom of the tank to feed cold or hot air. In the tank body, an exhaust port 6 2 is arranged on the top of the drying tank 6 ,, and a spray inlet 6 3 is arranged on the upper side of the tank body, and the bacteria-containing fermentation liquid is sprayed into the spray. In the tank body, the amount of cold or hot air is used to control the drying, so as to obtain the solid powder granules. M289194 [Contents] (Technical problems to be solved): The creator found that 'the industry has the following disadvantages: 1. In the structure of Lucerne, the dry powder granules are dried in the yeast. The stagnation of the groove in the groove is relatively enlarged according to the height and volume of the bacterium, and (4), so that the barrel of the tank body is used in the space to be trapped in the function of drying every month, but on the π Trouble and deal with the increase in the cost of injury. Z. In the process of dry olefins, the industry is stabbing, the blood method is far from the f#^ or the hot air volume is too high to have a high degree of heat resistance. If the temperature is too high, the temperature is too low and it is difficult to achieve drying. , =曰=A kind of burden between the species due to over-wet and sticking to the unsuitable use of the granular operation procedure, and the survival rate affecting the strain is granules. When the bacteria are used, additional powder is added to the mixture. Kind = humble to form a carrier of dry powder granules, in order to provide bacteria for the environment, but the relative consumption of energy and energy. Do not make the cost In summary of the shortcomings described above, the overall effect of the powder shrinking is not good, and it is necessary to improve. ^接囷和干灿浓 (Technical means to solve the problem) In view of this, this creation is based on the concept of long-term drying and concentrating equipment, and creates a kind of powder granules to be dried and concentrated. The improvement is mainly made up of a dry trough with a sterile horizontal closed hollow cylinder. The dry concession has a (four) device, and the dry body has a complex M289194: a suction port, an inoculating port, and an inlet at the end of the barrel. The material tray is pumped through the vacuum pump for Peng, and the = gas-liquid separation tank is connected to the outer edge of the bottom of the cylinder body: when the m: discharge port is connected to the city water in the drying tank, it can lead people Steam heating or dual-worker with municipal water cooling: the powder carrier of the second preparation is input from the inlet, and the powder is sprayed, and the liquid bacteria to be inoculated are mixed from the inoculum and then formed into - The carrier of the powder granules, the dried concentrated silk, the mouth:; = the dehumidification drying operation of the wind device, the 俾达效试验 ri achieves the purpose of preserving and increasing the density of the bacteria, and has the volume of the body of the θ θ body, increasing Bit, ^ ^ based on practical and innovative benefits. ι Avoid the waste of the original '(The effect of knowing the prior art) The following several work: Moonlight knows 'this creation is better than the previous technology' 1. Dry preservation: The creation of the powder through the vacuum pumping and adding M 辰 缩 衣 ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' The utility model has a horizontally-rolling cylinder which can simultaneously use the powder as a drying and concentrating device, and can reduce the tank body: the second one: the design of the vacuum drying and concentrating, which not only has the unit capacity, but also reaches the lower limit::::: The space can be enlarged, the M289194 is increased from the 3, the operation system is: the granules of the present granules are smothered and smashed, and the stalks of the same Helmet can be dried and reduced in cost. i. In order to complete the operation, the 培养 简化 简化 简化 Ί Ί Ί Ί Ί Ί 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本5, can be instantaneous high-temperature heating or low-temperature cooling · · Because of the jacket design ' can use steam to instantly raise the tank body: skirt:: water circulation cooling 'and introduce sterile dry low-temperature cold wind, also; mouth instantaneous two low-temperature cooling The effect of the instant. [Embodiment] Concentration:: Γ! One to three figures, is a schematic diagram of the drying and sterilizing of the granules, and the improvement and actuation configuration of the garment. The system includes: Slot 10 is a horizontal hollow seal The body of the barrel; - the feed material π 1 1, is set in the drying tank i 0 tube body to open the mouth of the material; the case forms a = tube:, is placed in the drying tank i 0 above the barrel with a number of calls The inoculating port 13 of the spray device; 1 is extended: (4) the tube 14' is extended from the appropriate position of the barrel of the drying tank 10 to the mouth of the mouth, and the mouth of the suction pipe i 4 is eccentrically provided - pumping = mouth 1 5 and a funnel-shaped filter i 6, and using the suction port 丄5 fish-, 'night separation tank 50-phase connected' and through the vacuum pump 2 〇 action $ 礼 separation tank 5 Q system can be water vapor, Separation of air and particulate matter; when the real liquid M289194 f 2 0 is used for pumping, the snail (four) line can be produced. At the end, the particles rise and adhere to the 6th position, = pumping, and the powder peels off the attached particles on the net. Returning to the tank body, the crucible can collide and block 4; avoid the suction pipe 1 a stirring device 30, which is attached to the mixing shaft 3 of the inner wing 3 of the drying tank i, and is disposed outside the tank - The motor has a mixing shaft 31 inserted, and the 俾 can drive the function of the lifting; 3 and the mixing and drying device 40, which is attached to the drying tank, has a jacket 41 of appropriate radius, the sleeve Two: edge: set the number of air inlets 42, the introduction of cold air, the four shells are provided with a plurality of steam inlets 43, and the steam inlets ... two:: there is a plurality of steam on the bottom side of the jacket 4 1 Exit 4 4, and as the water inlet, the steam inlet (water outlet (four) outlet (water inlet) 4 4, vacuum pumping 2 〇 and the system using heat exchange, will teach ++ / city water connection,乂 ( ( 四 四 ( 四 将 将 将 将 将 将 将 将 将 将 将 将 四 四 四 四 四 四 四 四 四 四 四 四 四 四 四 四 四 四 四 四 四 四 四 四 四 四 四 四 四 四 四 四 四 四 四Efficient; Outlet 1 7, tied in the drying trough - discharge out cr, and there are 蜱 at the nozzle: Bei, Xiacheng - with automatic discharge design; (four) Butterfly wide 18' The composition of the shaped piece 'This creative powder granules are dried and concentrated. The method is as follows: 'Prepare the powder carrier prepared in advance from the inlet port=, which can also be used to put more than two kinds of powder carrier After 33 readings, the stirring shaft 31 rotates to uniformly mix the powder carrier, M289194 and the effect of breaking the large mass, and then use the Kyrgyzstan Vacuuming, and through the suction port of the 遽 net16 ^ 空果浦 2 〇 侦 侦 侦 侦 侦 侦 侦 侦 侦 侦 , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , Effective & recovery to powder carrier, = heat U into the jacket 4 1 'to heat sterilization, to reduce its I, mixing and 1 bacteria can be carried out simultaneously, and in the initial operation stage: 守, 忒The liquid septic species for inoculation can be mixed into the powder carrier by the inoculating port i, and it can also be intermittently smashed into the _ service, the sentence spray and the speed, so that the liquid bacteria and the powder carrier are thoroughly mixed: two sizes' : = Granule carrier can provide nourishment and living environment for bacteria: Re-steaming to remove water, that is, reducing waste operation == by vacuuming and introducing low temperature dry sterile cold wind: so that: Below the preset temperature, in order to remove water, cold air drying and concentration work, among them, swearing... The decompression 刼 与 与 减压 减压 减压 减压 减压 亦可 亦可 亦可 亦可 亦可 亦可 亦可 亦可 亦可 亦可 亦可 亦可 亦可 亦可 亦可 亦可 亦可 亦可 亦可 亦可 亦可 亦可 亦可 亦可 亦可Automatic discharge is shallow; it can be planted in the aseptic state onto the carrier, dried and concentrated to save Bacteria purpose of improving 'Μ effective in reducing the volume of barrel tank, increasing the waste capacity wash unit C ^ source of Free months, according to those of practicality and benefits of innovation. According to the creation of the "Powder Granule Inoculating Drying and Concentrating Device", it is possible to complete the inoculation and drying and concentration operation under the aseptic condition to make the pre-prepared powder carrier from the drying tank. The feed port is put into, the stirring device is mixed, and the liquid_mixed mash is mixed into the powder loading **7 to dry and connect to the work, and then dried under reduced pressure to obtain the carrier of the granules. The whole is based on the dryness of the powder granules M289194 = the purpose of maintaining the density of the bacteria, and effectively reducing the body of the tank, adding unit capacity and avoiding energy waste, so that the overall industry practicality and cost-effectiveness And its structure has not been seen in books or publicly made: the requirements of the new patents in Chengfu, please ask the bureau to understand, and grant patents on weekdays, to the pray. Chen Ming, the above is the specifics of this creation. Implementing the technical principle of the immediate work 'If the change made according to the concept of this creation = the role still does not exceed the time covered by the specification and the illustration = within the scope of this creation, the combination of Chen Ming. Brief description] = one picture is Schematic diagram of the creation of the cognac concentrating device. Figure is the side view of the creation of the dry (4) material. The second picture is the schematic diagram of the active configuration of the dry concentrating device. The picture shows the cross section of the conventional drying concentrating device. Description] (This creation) 10· • Drying tank 12· • Breathing port 14 • • Exhaust pipe 16 • • Filter net 18 • • Discharge butterfly valve 3 0 • Stirring device 11··Inlet port 1 3 · Inoculating port 1 5 · · Suction port 1 7 · · Discharge port 2 0 ·· Vacuum pump 31··Agitator shaft M289194 3 2 · · Stirring wing 4 Ο ··Drying device 4 4 2 · ·Inlet port 4 4 4 ·· Vapor outlet (water inlet) Ε (conventional) 6 0 · · Drying tank 6 6 2 · · Exhaust port 6 3 · · Motor 1 · · Jacket 3 ··Vapor inlet (water outlet) 0 ··Gas-liquid separation tank 1··Air inlet 3··Inlet
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