TWM623516U - Membrane emulsification apparatus - Google Patents

Membrane emulsification apparatus Download PDF

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TWM623516U
TWM623516U TW110208219U TW110208219U TWM623516U TW M623516 U TWM623516 U TW M623516U TW 110208219 U TW110208219 U TW 110208219U TW 110208219 U TW110208219 U TW 110208219U TW M623516 U TWM623516 U TW M623516U
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Taiwan
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tank
thin film
continuous phase
emulsification
fluid
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TW110208219U
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Chinese (zh)
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王潮鴻
彭宣融
俞睿陽
董志宏
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財團法人食品工業發展研究所
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Priority to TW110208219U priority Critical patent/TWM623516U/en
Priority to CN202122058228.4U priority patent/CN215822804U/en
Publication of TWM623516U publication Critical patent/TWM623516U/en

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Abstract

The membrane emulsification apparatus as provided includes a continuous phase tank, a disperse phase tank, a membrane emulsification tank, at least one detection device, a water bath apparatus, a continuous phase transfer pump, and a disperse phase transfer equipment. The continuous phase tank accommodates continuous phase fluid. The disperse phase tank accommodates disperse phase fluid. The membrane emulsification tank receives the continuous phase fluid and the dispersed phase fluid from the continuous phase tank and the disperse phase tank, respectively. At least one porous membrane tube is arranged in the membrane emulsification tank, and thereby the continuous phase fluid and the dispersed phase fluid are mixed to form an emulsion. The at least one detection device is coupled to or between the continuous phase tank, the dispersed phase tank and the thin film emulsification tank to detect the real-time status of one or more of the continuous-phase fluid, the dispersed phase fluid and the emulsion. In response to the real-time status, the continuous phase transfer pump, the disperse phase transfer equipment, and the water bath apparatus control the flow rates of the continuous phase and the disperse phase respectively, and provides a water bath fluid to circulate between the continuous phase tank, the dispersed phase tank and the thin film emulsification tank to control their respective temperatures.

Description

薄膜乳化設備 Thin film emulsification equipment

本創作是關於一種乳化設備,特別是關於一種薄膜乳化設備。 This creation is about an emulsifying device, especially a thin-film emulsifying device.

乳化技術(Emulsion)為將兩種不互融的液體(或氣體與液體)中的一種以0.2~50μm的細微粒顆粒型式散於另一種液體(或氣體)中,於食品、化妝品、醫藥及工業上皆被廣泛的應用。其中具有低能耗及低剪切力特性之薄膜乳化法近年來受重視,其目的為以天然或合成的高分子材料把液體、固體甚至氣體包裹,藉由壁材的包覆提供心材與外界環境間的物理屏障,進而賦予心材原本沒有的特性,且所獲得的乳化液滴其包含粒徑小、分布窄、穩定性高、質地均勻細緻及輸送特性佳等優勢,同時因過程不產熱,所以也不會破懷熱敏感物質,用於揮發性香料時可有效延長產品貨架期。 Emulsion technology (Emulsion) is to disperse one of two immiscible liquids (or gas and liquid) in another liquid (or gas) in the form of 0.2~50μm fine particles, which is used in food, cosmetics, medicine and It is widely used in industry. Among them, the thin film emulsification method with the characteristics of low energy consumption and low shear force has received attention in recent years. Its purpose is to wrap liquid, solid or even gas with natural or synthetic polymer materials, and provide the core material and the external environment by coating the wall material. The physical barrier between them, and then endows the heartwood with the characteristics that the heartwood does not have originally, and the obtained emulsified droplets have the advantages of small particle size, narrow distribution, high stability, uniform and fine texture, and good conveying characteristics. At the same time, because the process does not generate heat, Therefore, it will not break the heat-sensitive substances, and can effectively extend the shelf life of products when used in volatile fragrances.

薄膜乳化的原理機制為乳化液之分散相流體在溫和的製程條件下,經由孔隙大小一致的多孔膜管而進入另一邊的連續相流體中,而連續相流體則需藉由外力持續產生擾動才可將分散相流體從多孔膜管上不斷刷下,目的在於使分散相流體以細小顆粒形式分布於連續相流體中,達到均勻乳化之效果。 The principle mechanism of thin film emulsification is that the dispersed phase fluid of the emulsion enters the continuous phase fluid on the other side through a porous membrane tube with the same pore size under mild process conditions, and the continuous phase fluid needs to be continuously disturbed by external force. The dispersed phase fluid can be continuously brushed down from the porous membrane tube, the purpose is to make the dispersed phase fluid distribute in the continuous phase fluid in the form of fine particles to achieve the effect of uniform emulsification.

目前已知的薄膜乳化設備中具有許多不同形式之機構外型設計,雖技術上具備諸多優勢,但現有操作設備的設計仍存在許多問題,例如缺乏保溫機制、連續相及分散相於製程中之壓力比例的有效控制、多功能性及自動化 模式之設計等,因此存在有人員操作失誤造成損失及產品品質不佳的隱患。若能針對上述問題點進行改良設計,將可大幅降低人員操作失誤造成的損失,並能使產品品質均一化。 The currently known thin-film emulsification equipment has many different forms of mechanical design. Although there are many technical advantages, there are still many problems in the design of the existing operating equipment, such as the lack of heat preservation mechanism, continuous phase and dispersed phase in the process. Efficient control of pressure ratio, versatility and automation The design of the mode, etc., so there are hidden dangers of loss of personnel operation errors and poor product quality. If we can improve the design for the above problems, it will greatly reduce the loss caused by operator error and make the product quality uniform.

有鑑於此,本創作之一構想即在於提供一種薄膜乳化設備,其具有保溫機制,能適用各種熔點的原料,並可藉此控制乳化反應的效能。 In view of this, one idea of the present creation is to provide a thin film emulsification equipment, which has a heat preservation mechanism, can be applied to raw materials with various melting points, and can control the efficiency of the emulsification reaction.

本創作之另一構想在於提供一種薄膜乳化設備,其具有檢測元件能即時檢測薄膜乳化設備中連續相流體、分散相流體以及乳化液的即時狀態,並可自動補償以達製程自動化之效,提高乳化液產製效率和品質。 Another idea of the present creation is to provide a thin film emulsification equipment, which has a detection element that can instantly detect the real-time state of the continuous phase fluid, dispersed phase fluid and emulsion in the thin film emulsification equipment, and can automatically compensate to achieve the effect of process automation and improve Emulsion production efficiency and quality.

本創作之又一構想在於提供一種薄膜乳化設備,能於尚未洩料之狀態下切換模式直接進行多重乳化反應,可簡化現有製程程序。 Another idea of the present invention is to provide a thin film emulsification device, which can switch modes to directly perform multiple emulsification reactions in a state where the material has not yet been released, thereby simplifying the existing process procedures.

本創作之再一構想在於提供一種薄膜乳化設備,其建構有自動化模式,可適當切換薄膜乳化設備的操作模式;結合連續相流體、分散相流體以及乳化液等即時狀態的即時監控和自動補償,可降低人為操作誤差,提高乳化製程的一致性。 Another idea of the present creation is to provide a thin film emulsification equipment, which is constructed with an automatic mode, which can appropriately switch the operation mode of the thin film emulsification equipment; It can reduce human operation error and improve the consistency of emulsification process.

根據本創作之上述構想,提供一種薄膜乳化設備,其包括:一連續相槽體以容納一連續相流體;一分散相槽體以容納一分散相流體;一薄膜乳化槽分別自該連續相槽體與該分散相槽體接收該連續相流體和該分散相流體,該薄膜乳化槽內設置有至少一多孔膜管,分散相流體會從多孔膜管外側通入內側,並與該連續相流體於所述多孔膜管內側混合以形成一乳化液;至少一檢測裝置,係分別耦接於該連續相槽體、該分散相槽體和該薄膜乳化槽或其間,以 檢測該連續相流體、該分散相流體與該乳化液中其一或多者之一即時狀態;一連續相輸送源,其與該連續相槽體和薄膜乳化槽體連通,該連續相輸送源係回應該即時狀態適時調節連續相溶液或已混合分散相溶液之乳化液之流速;一分散相輸送源,該分散相輸送源係回應該即時狀態適時調節分散相之流速,與連續相輸送源互相搭配,以維持連續相溶液及分散相溶液之比例平衡;以及一水浴設備,其與該連續相槽體、該分散相槽體和該薄膜乳化槽流體連通,該水浴設備係回應該即時狀態而提供一水浴流體流通於該連續相槽體、該分散相槽體和該薄膜乳化槽間,以控制該連續相槽體、該分散相槽體和該薄膜乳化槽的各自溫度。 According to the above concept of the present invention, a thin film emulsification equipment is provided, which includes: a continuous phase tank body to accommodate a continuous phase fluid; a dispersed phase tank body to accommodate a dispersed phase fluid; a thin film emulsification tank from the continuous phase tank, respectively The body and the dispersed phase tank body receive the continuous phase fluid and the dispersed phase fluid. At least one porous membrane tube is arranged in the thin film emulsification tank. The fluid is mixed inside the porous membrane tube to form an emulsion; at least one detection device is respectively coupled to the continuous phase tank, the dispersed phase tank and the thin film emulsification tank or between them, so as to Detect the instantaneous state of one or more of the continuous phase fluid, the dispersed phase fluid and the emulsion; a continuous phase delivery source, which is communicated with the continuous phase tank body and the thin film emulsification tank body, the continuous phase delivery source It is to adjust the flow rate of the continuous phase solution or the emulsion that has been mixed with the dispersed phase solution in response to the real-time state; a disperse phase conveying source, the disperse phase conveying source is in response to the real-time state. Timely adjust the flow rate of the disperse phase, and the continuous phase conveying source Matching each other to maintain the ratio of the continuous phase solution and the dispersed phase solution in balance; and a water bath device, which is in fluid communication with the continuous phase tank body, the dispersed phase tank body and the thin film emulsification tank, and the water bath device responds to the real-time state A water bath fluid is provided to circulate among the continuous phase tank, the dispersed phase tank and the thin film emulsification tank to control the respective temperatures of the continuous phase tank, the dispersed phase tank and the thin film emulsification tank.

根據上述構想,其中該連續相槽體、該分散相槽體與該薄膜乳化槽係各自具有由一內管和一外管所形成之一夾套式結構,其中該內管與該外管之間形成一引流通道,該水浴流體係於該連續相槽體、該分散相槽體與該薄膜乳化槽的各自引流通道中流通,亦可於各管路上外加引流通道,並進行連接。 According to the above concept, wherein the continuous phase tank, the dispersed phase tank and the thin film emulsification tank each have a jacketed structure formed by an inner tube and an outer tube, wherein the inner tube and the outer tube are A drainage channel is formed between them, and the water bath system circulates in the respective drainage channels of the continuous phase tank body, the dispersed phase tank body and the thin film emulsification tank, and additional drainage channels can be added to each pipeline and connected.

根據上述構想,其中所述至少一檢測裝置包括至少一溫度檢測裝置,係設置於該連續相槽體、該分散相槽體、該薄膜乳化槽和該水浴設備中其一或多者上。 According to the above concept, the at least one detection device includes at least one temperature detection device, which is disposed on one or more of the continuous phase tank, the dispersed phase tank, the thin film emulsification tank and the water bath equipment.

根據上述構想,其中所述至少一檢測裝置包括一分光光度計或一工業相機,其設置於該薄膜乳化槽之下游處以檢測該乳化液的一即時濁度,藉此監控該乳化液之一即時乳化狀態。 According to the above concept, wherein the at least one detection device includes a spectrophotometer or an industrial camera, which is disposed downstream of the film emulsification tank to detect an instant turbidity of the emulsion, thereby monitoring an instant turbidity of the emulsion emulsified state.

根據上述構想,所提供之薄膜乳化設備更包括一連續相輸送源以將該連續相流體自該連續相槽體泵送至該薄膜乳化槽,其中所述至少一檢測裝置包括設置於該連續相槽體與該連續相輸送源之間的一第一流量檢測裝置、以 及設置在該分散相槽體與該薄膜乳化槽之間的一第二流量檢測裝置,以分別檢測該連續相流體與該分散相流體之一即時流量與流速。 According to the above concept, the provided thin-film emulsification equipment further includes a continuous-phase delivery source to pump the continuous-phase fluid from the continuous-phase tank to the thin-film emulsification tank, wherein the at least one detection device comprises a a first flow detection device between the tank body and the continuous phase conveying source, to and a second flow detection device arranged between the dispersed phase tank body and the thin film emulsification tank to detect an instant flow rate and flow rate of the continuous phase fluid and the dispersed phase fluid respectively.

根據上述構想,其中所述至少一檢測裝置包括設置在該薄膜乳化槽之一第一壓力檢測裝置、以及設置在該薄膜乳化槽下游的一第二壓力檢測裝置,以分別檢測該分散相流體和該連續相流體之一即時流體壓力。 According to the above concept, wherein the at least one detection device includes a first pressure detection device disposed in the thin film emulsification tank, and a second pressure detection device disposed downstream of the thin film emulsification tank to detect the dispersed phase fluid and The instantaneous fluid pressure of one of the continuous phase fluids.

根據上述構想,所提供之薄膜乳化設備更包括一二次乳化回路,該二次乳化回路連接於該薄膜乳化槽以接收該乳化液並將該乳化液回送至該薄膜乳化槽中進行再次乳化。 According to the above concept, the provided thin film emulsification equipment further includes a secondary emulsification circuit, the secondary emulsification circuit is connected to the thin film emulsification tank to receive the emulsion and return the emulsion to the thin film emulsification tank for re-emulsification.

根據上述構想,所提供之薄膜乳化設備更包括一自動控制裝置,係與所述至少一檢測元件、連續相輸送源、分散相輸送源及水浴設備電性耦接,預設為手動模式時,可以建立操作參數資料庫;而預設為自動模式時,設備將回應於該即時狀態的接收而切換該薄膜乳化設備中的連續相輸送源、分散相輸送源或水浴設備至少一設定參數,進行該連續相流體和該分散相流體的各自即時狀態或溫度的相應調整。 According to the above concept, the provided thin-film emulsification equipment further includes an automatic control device, which is electrically coupled to the at least one detection element, the continuous phase conveying source, the dispersed phase conveying source and the water bath equipment. When the preset is in the manual mode, A database of operating parameters can be established; and when the preset is automatic mode, the device will switch at least one setting parameter of the continuous phase delivery source, the dispersed phase delivery source or the water bath equipment in the thin film emulsification device in response to the receipt of the real-time state, and perform the operation. Corresponding adjustment of the respective instantaneous states or temperatures of the continuous phase fluid and the dispersed phase fluid.

根據上述構想,其中該自動控制裝置包括:一處理器,其回應於該即時狀態的接收而令該薄膜乳化設備於組件之操作參數上自動切換,並控制該連續相流體和該分散相流體的各自即時狀態的相應調整;一使用者介面裝置,可依據需求進行手動及自動模式之設定,其對操作者顯示該連續相流體、該分散相流體與該乳化液的該即時狀態,並且供操作者進行對該薄膜乳化設備的操作控制;以及一儲存裝置,其儲存所接收之該連續相流體、該分散相流體與該乳化液的該即時狀態,並儲存有該薄膜乳化設備之該操作模式的相關程式指令。 According to the above concept, wherein the automatic control device includes: a processor, which, in response to the receipt of the real-time state, causes the thin-film emulsification device to automatically switch on the operating parameters of the components, and controls the flow of the continuous phase fluid and the dispersed phase fluid. Corresponding adjustment of the respective real-time states; a user interface device that can set manual and automatic modes according to requirements, which displays the real-time states of the continuous phase fluid, the dispersed phase fluid and the emulsion to the operator, and is available for operation The operator controls the operation of the thin film emulsification device; and a storage device that stores the received state of the continuous phase fluid, the dispersed phase fluid and the emulsion, and stores the operation mode of the thin film emulsification device related program instructions.

100:薄膜乳化設備 100: Film emulsification equipment

110:連續相槽體 110: Continuous phase tank

120:分散相槽體 120: Dispersed phase tank

130:薄膜乳化槽 130: Film emulsification tank

140:水浴設備 140: Water bath equipment

150:自動控制裝置 150: Automatic control device

200:薄膜乳化設備 200: Film emulsification equipment

210:連續相槽體 210: Continuous phase tank

212:連續相引流通道 212: Continuous phase drainage channel

213:出料口 213: discharge port

214:連續相輸送源 214: Continuous Phase Delivery Source

216:二次乳化回路 216: Secondary emulsification circuit

220:分散相槽體 220: Dispersed phase tank

220a、220b:通道 220a, 220b: channel

221:入料分支通道 221: Feeding branch channel

222:分散相引流通道 222: Dispersed phase drainage channel

224:分散相輸送源(氣壓源) 224: Dispersed phase delivery source (air pressure source)

226:抽氣裝置 226: Air extraction device

228:分散相輸送源(蠕動泵) 228: Disperse phase delivery source (peristaltic pump)

230:薄膜乳化槽 230: Film emulsification tank

231:多孔膜管 231: Porous membrane tube

232:乳化槽引流通道 232: Drainage channel of emulsification tank

240:水浴設備 240: Water bath equipment

250:連接引流通道 250: Connect the drainage channel

260:乳化狀態檢測裝置 260: Emulsification state detection device

90:控制面板 90: Control Panel

F:流量檢測裝置(流量計) F: flow detection device (flow meter)

P:壓力檢測裝置(壓力計) P: Pressure detection device (pressure gauge)

T:溫度檢測裝置(溫度計) T: temperature detection device (thermometer)

V1、V2、V3、V4、V5、V6:開關閥 V 1 , V 2 , V 3 , V 4 , V 5 , V 6 : On-off valve

為能更進一步瞭解本創作之特徵與技術內容,請參閱下述有關本創作實施例之詳細說明及如附圖式。惟所揭詳細說明及如附圖式係僅提供參考與說明之用,並非用以對本創作加以限制;其中:第一圖係一方塊圖,說明本創作之薄膜乳化設備的一示意配置及流程;第二圖說明根據本創作實施例之薄膜乳化設備的具體配置圖;及第三圖係一示意圖,說明根據本創作實施例之薄膜乳化設備的使用者介面裝置。 For a further understanding of the features and technical content of the present creation, please refer to the following detailed descriptions about the embodiments of the present creation and the accompanying drawings. However, the detailed descriptions and the accompanying drawings are only for reference and description, and are not intended to limit the creation. Among them: the first figure is a block diagram illustrating a schematic configuration and flow of the film emulsification equipment of the creation. ; Figure 2 illustrates a specific configuration diagram of the film emulsification apparatus according to the embodiment of the present invention; and Figure 3 is a schematic diagram illustrating the user interface device of the film emulsification apparatus according to the embodiment of the present invention.

下文係參照圖式、並且以示例實施例說明本創作之概念,在圖式或說明中,相似或相同的部分係使用相同的元件符號;再者,圖式係為利於理解而繪製,圖式中各層之厚度與形狀並非元件之實際尺寸或成比例關係。需特別注意的是,圖式中未繪示、或說明書中未描述之元件,可為熟習本創作所屬領域技藝之人士所知之形式。 The following describes the concept of the present invention with reference to the drawings and exemplary embodiments. In the drawings or descriptions, similar or identical parts use the same reference numerals; The thickness and shape of each layer are not the actual size or proportional relationship of the element. It should be noted that the elements not shown in the drawings or described in the specification may be in the form known to those skilled in the art to which the present invention belongs.

請參閱第一圖,其係一方塊圖,說明本創作之薄膜乳化設備的一示意配置及流程。如第一圖所示,本創作之薄膜乳化設備100主要包括彼此流體連通的連續相槽體110、分散相槽體120、薄膜乳化槽130和水浴設備140;以及包括與薄膜乳化設備100電性及訊號耦接的一自動控制裝置150。 Please refer to the first figure, which is a block diagram illustrating a schematic configuration and flow of the thin film emulsification equipment of the present invention. As shown in the first figure, the thin film emulsification device 100 of the present invention mainly includes a continuous phase tank body 110, a dispersed phase tank body 120, a thin film emulsification tank 130 and a water bath device 140 that are in fluid communication with each other; and an automatic control device 150 coupled to the signal.

在本創作之薄膜乳化設備100中,連續相槽體110用於容納一連續相流體,分散相槽體120用於容納一分散相流體,薄膜乳化槽130分別自連續相槽體110與分散相槽體120接收連續相流體和分散相流體(分別如箭頭A1和A2所 示);如熟習本創作技術人士所理解,薄膜乳化槽130內係設置有至少一多孔膜管,分散相流體即通過薄膜乳化槽130的所述多孔膜管並於其內與連續相流體混合而形成一乳化液自薄膜乳化槽130排出(如箭頭A3所示)。 In the thin film emulsification apparatus 100 of the present invention, the continuous phase tank 110 is used to accommodate a continuous phase fluid, the dispersed phase tank 120 is used to accommodate a dispersed phase fluid, and the thin film emulsification tank 130 is separated from the continuous phase tank 110 and the dispersed phase, respectively. Tank 120 receives continuous phase fluid and dispersed phase fluid (as indicated by arrows A1 and A2, respectively). As understood by those skilled in the art, the thin film emulsification tank 130 is provided with at least one porous membrane tube, and the dispersed phase fluid passes through the porous membrane tube of the thin film emulsification tank 130 and communicates with the continuous phase fluid therein. After mixing, an emulsion is formed and discharged from the film emulsification tank 130 (as indicated by arrow A3).

在本創作之薄膜乳化設備100中,自薄膜乳化槽130排出之乳化液在經濁度檢測後係輸入至連續相槽體110,並視實際應用所需、依管路及閥門的配置與安排而繼續泵送至薄膜乳化槽130進行再次反應(如箭頭A2所示)、或自出料口排出(如箭頭A4所示)。 In the thin film emulsification device 100 of the present invention, the emulsion discharged from the thin film emulsification tank 130 is input to the continuous phase tank body 110 after turbidity detection, and the configuration and arrangement of pipelines and valves are required according to the actual application. And continue to be pumped to the film emulsification tank 130 for re-reaction (as shown by arrow A2), or discharged from the discharge port (as shown by arrow A4).

更甚者,在本創作之薄膜乳化設備100中,藉由管路及閥門的配置及設計,可依應用所需調整所形成之乳化液的流向。根據本創作,薄膜乳化設備100另設有一二次乳化回路(如箭頭B所示),藉由流量閥的調節令自薄膜乳化槽130排出之部分乳化液得通過二次乳化回路再次進入薄膜乳化槽130中進行再次乳化。 What's more, in the thin film emulsification apparatus 100 of the present invention, the flow direction of the formed emulsion can be adjusted according to the needs of the application through the configuration and design of the pipelines and valves. According to the present invention, the thin-film emulsification device 100 is further provided with a secondary emulsification circuit (as indicated by arrow B), through the adjustment of the flow valve, part of the emulsified liquid discharged from the thin-film emulsification tank 130 can pass through the secondary emulsification circuit and enter the thin film again Re-emulsification is performed in the emulsification tank 130 .

在本創作中,係利用水浴設備140對彼此流體串聯相通的分散相槽體120、薄膜乳化槽130和連續相槽體110進行溫度控制,若管路加設夾層式設計,則亦能一起進行溫度控制;換言之,如第一圖所示,水浴設備140提供之水浴流體可依序通過分散相槽體120、薄膜乳化槽130和連續相槽體110(如箭頭C所示),以對其進行加熱、冷卻或持溫等操作。如圖所示,水浴流體最後回到水浴設備140供循環使用。 In this creation, the water bath equipment 140 is used to control the temperature of the dispersed phase tank 120 , the thin film emulsification tank 130 and the continuous phase tank 110 , which are fluidly connected in series with each other. Temperature control; in other words, as shown in the first figure, the water bath fluid provided by the water bath device 140 can sequentially pass through the dispersed phase tank 120, the thin film emulsification tank 130 and the continuous phase tank 110 (as shown by arrow C) to Perform operations such as heating, cooling or keeping warm. As shown, the water bath fluid is eventually returned to the water bath apparatus 140 for recycling.

在本創作中,與薄膜乳化設備100電性及訊號耦接的自動控制裝置150回應於連續相流體、分散相流體和乳化液的即時狀態的接收進行連續相流體和分散相流體的各自即時狀態的相應調整(例如、但不限於:溫度、壓力、流量、流速等),將於下文詳細說明。 In the present invention, the automatic control device 150 electrically and signally coupled to the thin film emulsification apparatus 100 performs respective real-time states of the continuous-phase fluid and the dispersed-phase fluid in response to receiving the real-time states of the continuous-phase fluid, the dispersed-phase fluid, and the emulsion. Corresponding adjustments (eg, but not limited to: temperature, pressure, flow, flow rate, etc.) will be described in detail below.

請參閱第二圖,其說明了根據本創作實施例之薄膜乳化設備200的具體配置。如第二圖所示,本創作之薄膜乳化設備200包含連續相槽體210、分散相槽體220、薄膜乳化槽230、水浴設備240、以及複數個檢測裝置(下文說明)。連續相槽體210用以容納連續相流體,分散相槽體220用以容納分散相流體,薄膜乳化槽230用於接收連續相槽體210內之連續相流體與分散相槽體220內之分散相流體,薄膜乳化槽230內設置有多孔膜管231,連續相流體與分散相流體於多孔膜管231內混合以形成一乳化液。 Please refer to the second figure, which illustrates the specific configuration of the thin film emulsification apparatus 200 according to the embodiment of the present invention. As shown in the second figure, the thin film emulsification equipment 200 of the present invention includes a continuous phase tank 210, a dispersed phase tank 220, a thin film emulsification tank 230, a water bath equipment 240, and a plurality of detection devices (described below). The continuous phase tank 210 is used to accommodate the continuous phase fluid, the dispersed phase tank 220 is used to accommodate the dispersed phase fluid, and the thin film emulsification tank 230 is used to receive the continuous phase fluid in the continuous phase tank 210 and dispersion in the dispersed phase tank 220 For the phase fluid, a porous membrane tube 231 is arranged in the thin film emulsification tank 230. The continuous phase fluid and the dispersed phase fluid are mixed in the porous membrane tube 231 to form an emulsion.

在本創作之薄膜乳化設備200中,連續相槽體210、分散相槽體220和薄膜乳化槽230或其間係視應用所需而耦接有至少一個檢測裝置,例如、但不限於溫度檢測裝置(T)、壓力檢測裝置(P)和乳化狀態檢測裝置260(如分光光度計或工業相機),以分別檢測連續相流體、分散相流體與乳化液中其一或多者之一即時狀態(例如、但不限於:溫度、壓力和濁度)。水浴設備240與連續相槽體210、分散相槽體220和薄膜乳化槽230流體連通,水浴設備240提供一水浴流體流通於連續相槽體210、分散相槽體220和薄膜乳化槽230間(如第一圖中箭頭C所示方向),以控制連續相槽體210、分散相槽體220和薄膜乳化槽230的各自溫度,並能回應前述即時狀態而自動進行溫度調節。 In the thin film emulsification apparatus 200 of the present invention, the continuous phase tank 210, the dispersed phase tank 220, the thin film emulsification tank 230 or at least one detection device, such as, but not limited to, a temperature detection device, are coupled according to application requirements. (T), a pressure detection device (P) and an emulsion state detection device 260 (such as a spectrophotometer or an industrial camera) to detect the instantaneous state of one or more of the continuous phase fluid, dispersed phase fluid and emulsion, respectively ( For example, but not limited to: temperature, pressure and turbidity). The water bath equipment 240 is in fluid communication with the continuous phase tank body 210, the dispersed phase tank body 220 and the thin film emulsification tank 230, and the water bath equipment 240 provides a water bath fluid to circulate between the continuous phase tank body 210, the dispersed phase tank body 220 and the thin film emulsification tank 230 ( As shown by the arrow C in the first figure), to control the respective temperatures of the continuous phase tank 210, the dispersed phase tank 220 and the thin film emulsification tank 230, and can automatically adjust the temperature in response to the aforementioned real-time state.

根據本創作實施例,薄膜乳化設備200還包含連續相輸送源214,連續相輸送源214抽取連續相槽體210內之連續相流體,並將連續相流體送入薄膜乳化槽230中供進行前述乳化反應。在本創作實施例中,連續相輸送源214可為、但不限於沉水泵或平流泵,使連續相流體可以在輸送管路中循環輸送至薄膜乳化槽230(如第一圖中箭頭A2所示方向)。 According to the present inventive embodiment, the thin-film emulsification apparatus 200 further includes a continuous-phase transport source 214. The continuous-phase transport source 214 extracts the continuous-phase fluid in the continuous-phase tank body 210, and sends the continuous-phase fluid into the thin-film emulsification tank 230 for the above-mentioned process. emulsification reaction. In this creative embodiment, the continuous-phase delivery source 214 can be, but not limited to, a submersible pump or an advection pump, so that the continuous-phase fluid can be circulated in the delivery pipeline to the thin-film emulsification tank 230 (as indicated by arrow A2 in the first figure). direction).

根據本創作實施例,薄膜乳化設備200還包含分散相輸送源,其抽取分散相槽體220內之分散相流體,並分散相流體送入薄膜乳化槽230中供進行前述乳化反應(如第一圖中箭頭A1所示方向)。在本創作實施例中,分散相輸送源可包括、但不限於蠕動泵228、氣壓源224、或二者之組合;當可理解,本創作所屬領域之技術人士可以依照不同的分散相流體性狀及需求選擇分散相輸送源的類型和具體配置。 According to the present inventive embodiment, the thin-film emulsification apparatus 200 further includes a disperse-phase transport source, which extracts the disperse-phase fluid in the disperse-phase tank 220, and sends the disperse-phase fluid into the thin-film emulsification tank 230 for the aforementioned emulsification reaction (eg, the first The direction indicated by the arrow A1 in the figure). In the embodiment of the present invention, the disperse phase delivery source may include, but is not limited to, the peristaltic pump 228, the air pressure source 224, or a combination of the two; it should be understood that those skilled in the art of the present invention may follow different disperse phase fluid properties and needs to select the type and specific configuration of the disperse phase delivery source.

在本實施例中,在分散相槽體220的上蓋處設有壓力檢測裝置P與卸壓閥以及二個通道220a、220b,其中壓力檢測裝置P可為、但不限於一氣壓錶。其中通道220a連接氣壓源224、抽氣裝置226及蠕動泵228,並於連通處有V5可進行切換;另一通道220b則延伸至接近分散相槽體220底部,當開啟抽氣裝置226,可作為分散相流體輸入通道,而開啟氣壓源224或蠕動泵228,則作為分散相流體輸出通道。 In this embodiment, a pressure detection device P, a pressure relief valve and two channels 220a and 220b are provided on the upper cover of the dispersed phase tank body 220 , wherein the pressure detection device P can be, but is not limited to, a barometer. The channel 220a is connected to the air pressure source 224, the air suction device 226 and the peristaltic pump 228, and there is a V 5 at the connection for switching; the other channel 220b extends close to the bottom of the dispersed phase tank 220. When the air suction device 226 is turned on, It can be used as a disperse phase fluid input channel, and when the air pressure source 224 or peristaltic pump 228 is turned on, it can be used as a disperse phase fluid output channel.

在本實施例中,薄膜乳化槽230中的多孔膜管231兩端係以橡膠墊圈及迫緊塊固定,迫緊塊有開口可連通管路,分別作為薄膜乳化槽230之入口和出口。分散相流體進入薄膜乳化槽230後,在溫和的製程條件下經由孔隙大小一致的多孔膜管231外側擠入多孔膜管231內側,而多孔膜管231內側即為連續相流體循環通道,連續相流體則需藉由外力持續產生擾動將剛擠入多孔膜管231內側之分散相流體液滴從多孔膜管231上不斷刷下,使分散相流體以細小顆粒形式分布於連續相流體中達到均勻乳化之效果。 In this embodiment, both ends of the porous membrane tube 231 in the thin film emulsification tank 230 are fixed with rubber gaskets and pressing blocks. After the dispersed phase fluid enters the film emulsification tank 230, it is squeezed into the inside of the porous membrane tube 231 through the outside of the porous membrane tube 231 with the same pore size under mild process conditions, and the inside of the porous membrane tube 231 is the continuous phase fluid circulation channel. The fluid needs to be continuously disturbed by external force to continuously brush the dispersed phase fluid droplets that have just been squeezed into the inner side of the porous membrane tube 231 from the porous membrane tube 231, so that the dispersed phase fluid is distributed in the form of fine particles in the continuous phase fluid to achieve uniformity. Emulsifying effect.

如圖所示,在本創作之薄膜乳化設備200中,連續相槽體210、分散相槽體220、薄膜乳化槽230及連續相流體和分散相流體所流經之管路皆具有夾套式結構之設計;換言之,連續相槽體210、分散相槽體220、薄膜乳化槽230及連續相流體和分散相流體所流經之管路係各自具有由一內管和一外管,其中 內管與外管之間形成一引流通道。具體而言,連續相槽體210的內管與外管之間係形成連續相引流通道212,分散相槽體220的內管與外管之間係形成分散相引流通道222,薄膜乳化槽230的內管與外管之間係形成乳化槽引流通道232,連續相流體和分散相流體所流經之管路的內管與外管之間係形成引流通道(圖未示出),連續相引流通道212、分散相引流通道222、乳化槽引流通道232之間係由一連接引流管250所連接;在本創作實施例中,水浴設備240所提供之水浴流體係依序經由連接引流管250而流通於分散相槽體220的分散相引流通道222、薄膜乳化槽230的乳化槽引流通道232、連續相槽體210的連續相引流通道212,連續相流體和分散相流體所流經之管路的內管與外管之間係形成引流通道,並且回到水浴設備240中循環使用(即如第一圖中箭頭C所示)。根據本創作,利用水浴流體在乳化製程中對連續相流體、分散相流體及乳化液進行冷卻、加熱與保溫等作業,可使得薄膜乳化設備200內的連續相流體、分散相流體及乳化液之溫度分佈更為均勻。又藉由控制連續相槽體210的連續相引流通道212、分散相槽體220的分散相引流通道222、薄膜乳化槽230的乳化槽引流通道232、連續相流體和分散相流體所流經之管路的引流通道、以及連接引流管250的流體路徑,可避免作為熱源或冷源之水浴流體以逐漸堆積之方式充滿於夾套內部,造成冷點及熱點的產生而影響乳化反應效果。另外,透過以水浴設備進行持溫的機制,可以避免具有高熔點的連續相流體與分散相流體在乳化製程中因製程溫度降低而發生固化導致堵塞。 As shown in the figure, in the thin film emulsification equipment 200 of the present invention, the continuous phase tank body 210, the dispersed phase tank body 220, the thin film emulsification tank 230, and the pipelines through which the continuous phase fluid and the dispersed phase fluid flow are all jacketed The design of the structure; in other words, the continuous phase tank body 210, the dispersed phase tank body 220, the thin film emulsification tank 230 and the pipeline system through which the continuous phase fluid and the dispersed phase fluid flow each have an inner tube and an outer tube, wherein A drainage channel is formed between the inner tube and the outer tube. Specifically, the continuous phase drainage channel 212 is formed between the inner tube and the outer tube of the continuous phase tank body 210 , the dispersed phase drainage channel 222 is formed between the inner tube and the outer tube of the dispersed phase tank body 220 , and the film emulsification tank 230 The emulsification tank drainage channel 232 is formed between the inner tube and the outer tube, and a drainage channel (not shown) is formed between the inner tube and the outer tube of the pipeline through which the continuous phase fluid and the dispersed phase fluid flow. The drainage channel 212 , the dispersed phase drainage channel 222 , and the emulsification tank drainage channel 232 are connected by a connection drainage pipe 250 ; in the present creative embodiment, the water bath flow system provided by the water bath device 240 is connected through the connection drainage pipe 250 in sequence. The disperse phase drainage channel 222 of the dispersed phase tank body 220, the emulsification tank drainage channel 232 of the thin film emulsification tank 230, the continuous phase drainage channel 212 of the continuous phase tank body 210, and the pipes through which the continuous phase fluid and the dispersed phase fluid flow. A drainage channel is formed between the inner tube and the outer tube of the circuit, and is returned to the water bath device 240 for recycling (ie, as shown by arrow C in the first figure). According to the present invention, the continuous phase fluid, the dispersed phase fluid and the emulsion are cooled, heated and kept warm in the emulsification process by using the water bath fluid, so that the continuous phase fluid, the dispersed phase fluid and the emulsion in the thin film emulsification device 200 can be separated from each other. The temperature distribution is more uniform. By controlling the continuous phase drainage channel 212 of the continuous phase tank body 210, the dispersed phase drainage channel 222 of the dispersed phase tank body 220, the emulsification tank drainage channel 232 of the thin film emulsification tank 230, the continuous phase fluid and the dispersed phase fluid flow through. The drainage channel of the pipeline and the fluid path connecting the drainage tube 250 can prevent the water bath fluid serving as a heat source or a cold source from filling the inside of the jacket gradually, resulting in the generation of cold spots and hot spots and affecting the effect of the emulsification reaction. In addition, through the mechanism of maintaining the temperature with water bath equipment, the continuous phase fluid and the dispersed phase fluid with high melting point can be prevented from being solidified and blocked due to the decrease of the process temperature during the emulsification process.

利用本創作之薄膜乳化設備200中的各式管路連接及開關閥之設置,可控制分散相流體、連續相流體和乳化液等之流向,以進行乳化、再次乳化、出料等作業的操控。具體說明如下:在乳化製程進行時,連續相輸送源214(例如、但不限於沉水泵)抽取連續相槽體210中之連續相流體,並將連續相流體打入薄膜乳化槽230以進 行乳化製程。詳言之,當設置在連續相槽體210與薄膜乳化槽230之間的開關閥V1和可控制流量的開關閥V2呈開啟狀態,且二次乳化回路中可控制流量的開關閥V3關閉時,連續相槽體210內的連續相流體被泵送而流經管路進入薄膜乳化槽230(如第一圖中箭頭A2所示)。連續相槽體210和連續相輸送源214之間的管路上設有流量檢測裝置(例如流量計或流速計)F,以即時檢測並調整泵送之連續相流體的流量和流速。同時,透過分散相輸送源224或228的運作,分散相槽體220係通過氣壓輸送(當分散相輸送源224為一氣壓源時)、或是由蠕動泵推送(當分散相輸送源228為一蠕動泵時)、或是二者結合並且配合抽氣裝置226與開關閥V5之操作輸送模式,將其內部之分散相流體經由注入通道輸送至薄膜乳化槽230及其中的多孔膜管231管間空隙中,進以與連續相流體進行混合和乳化(如第一圖中箭頭A1所示)。此外,在分散相槽體220與薄膜乳化槽230之間還可設有入料分支通道221、可二段控制流量之開關閥V6及流量檢測裝置(例如流量計)(F)等,令分散相流體慢慢擠入多孔膜管231中被連續相流體沖刷包覆以形成乳化液。 Using the various pipeline connections and the setting of on-off valves in the thin film emulsification equipment 200 of the present invention, the flow direction of the dispersed phase fluid, the continuous phase fluid and the emulsion can be controlled, so as to control operations such as emulsification, re-emulsification, and discharge. . The specific description is as follows: during the emulsification process, the continuous phase transport source 214 (such as, but not limited to, a submersible pump) extracts the continuous phase fluid in the continuous phase tank body 210, and drives the continuous phase fluid into the thin film emulsification tank 230 for emulsification Process. Specifically, when the on-off valve V 1 and the on-off valve V 2 that can control the flow rate between the continuous phase tank body 210 and the thin-film emulsification tank 230 are in an open state, and the on-off valve V that can control the flow rate in the secondary emulsification circuit 3 When closed, the continuous phase fluid in the continuous phase tank body 210 is pumped and flows through the pipeline into the thin film emulsification tank 230 (as indicated by the arrow A2 in the first figure). The pipeline between the continuous phase tank 210 and the continuous phase delivery source 214 is provided with a flow detection device (eg, a flow meter or a flow meter) F to detect and adjust the flow rate and flow rate of the pumped continuous phase fluid in real time. At the same time, through the operation of the disperse phase conveying source 224 or 228, the disperse phase tank body 220 is conveyed by air pressure (when the disperse phase conveying source 224 is an air pressure source), or is pushed by a peristaltic pump (when the disperse phase conveying source 228 is an air pressure source) When a peristaltic pump is used), or a combination of the two and cooperates with the operation and delivery mode of the suction device 226 and the switch valve V5 , the dispersed phase fluid in the inside is transported to the thin film emulsification tank 230 and the porous membrane tube 231 therein through the injection channel. In the space between the tubes, it is further mixed and emulsified with the continuous phase fluid (as indicated by the arrow A1 in the first figure). In addition, between the disperse phase tank 220 and the thin film emulsification tank 230, there can also be provided a feed branch channel 221, an on -off valve V6 that can control the flow in two stages, and a flow detection device (such as a flow meter) (F), etc., so that The dispersed phase fluid is slowly squeezed into the porous membrane tube 231 and is washed and coated by the continuous phase fluid to form an emulsion.

上述乳化液自薄膜乳化槽230經管路輸出至連續相槽體210(如第一圖中箭頭A3所示)。在本創作實施例中,薄膜乳化槽230至連續相槽體210之間的管路上係設置有檢測元件以檢測乳化液的即時狀態。舉例而言,在管路上設置一乳化狀態檢測裝置260(如分光光度計或工業相機)檢測乳化液的濁度,進以確認乳化液的乳化程度;或設置有壓力檢測裝置(壓力計)P,檢測流經管路的乳化液壓力等。 The above-mentioned emulsion is output from the thin film emulsification tank 230 to the continuous phase tank body 210 through pipelines (as indicated by arrow A3 in the first figure). In this creative embodiment, a detection element is arranged on the pipeline between the thin film emulsification tank 230 and the continuous phase tank body 210 to detect the real-time state of the emulsion. For example, an emulsification state detection device 260 (such as a spectrophotometer or an industrial camera) is installed on the pipeline to detect the turbidity of the emulsion to confirm the degree of emulsification of the emulsion; or a pressure detection device (pressure gauge) P is installed , detect the pressure of the emulsion flowing through the pipeline, etc.

根據本創作實施例,連續相槽體210底部與出料口213相連,並利用開關閥V4的切換控制乳化液的出料(如第一圖中箭頭A4所示)。 According to this creative embodiment, the bottom of the continuous phase tank 210 is connected to the discharge port 213, and the discharge of the emulsion is controlled by switching the on-off valve V4 (as indicated by the arrow A4 in the first figure).

在本實施例中,除溫度檢測裝置T外,薄膜乳化槽230的外層亦設有壓力檢測裝置(壓力計)P與洩氣閥以檢測及調整薄膜乳化槽230內的即時壓力,俾利控制乳化製程的各式影響因素,其中壓力檢測裝置P可為、但不限於油壓錶。 In this embodiment, in addition to the temperature detection device T, the outer layer of the film emulsification tank 230 is also provided with a pressure detection device (pressure gauge) P and a vent valve to detect and adjust the real-time pressure in the film emulsification tank 230, so as to control the emulsification. Various influencing factors of the manufacturing process, wherein the pressure detection device P may be, but not limited to, an oil pressure gauge.

根據本創作之構想,薄膜乳化設備200係進一步設計有二次乳化回路216以供乳化液進行多重乳化。當乳化液(即連續相流體挾帶分散相流體之顆粒)從薄膜乳化槽230流出後,通過可控制流量的開關閥V2、V3的調節,部分乳化液可經由二次乳化回路216回送至連續相槽體210,另一部分乳化液則行經原本通道沖刷包覆擠入多孔膜之乳化液,再次進行乳化,並持續進行後續循環至乳化液達到設定的乳化狀態,乳化製程結束。具體而言,當一次乳化製程結束時,可視乳化液的即時狀態選擇關閉輸送源及將乳化液送至出料口213進行出料,或是調整可控制流量的開關閥V2以限制原本通道之流量,並開啟可控制流量的開關閥V3並調整為適當通過流量,以開啟二次乳化回路216,以對乳化液進行多重乳化。 According to the concept of the present invention, the thin-film emulsification device 200 is further designed with a secondary emulsification circuit 216 for multiple emulsification of the emulsified liquid. When the emulsion (that is, the particles of the dispersed phase fluid entrained by the continuous phase fluid) flow out from the thin film emulsification tank 230 , part of the emulsion can be returned through the secondary emulsification circuit 216 through the adjustment of the on-off valves V 2 and V 3 that can control the flow. After reaching the continuous phase tank 210 , another part of the emulsion flows through the original channel to wash and coat the emulsion that is extruded into the porous membrane, and emulsify again, and the subsequent circulation is continued until the emulsion reaches the set emulsifying state, and the emulsifying process ends. Specifically, when the first emulsification process is over, depending on the real-time status of the emulsified liquid, the delivery source can be closed and the emulsified liquid can be sent to the discharge port 213 for discharging, or the flow-controllable on - off valve V2 can be adjusted to limit the original channel. The flow rate can be controlled, and the on-off valve V3 that can control the flow rate is opened and adjusted to an appropriate flow rate, so as to open the secondary emulsification circuit 216 to perform multiple emulsification of the emulsion.

如前述說明,根據本創作之薄膜乳化設備在適當處係設有檢測裝置,以即時檢測設備內各流體和乳化液的各自即時狀態。根據本創作實施例,膜乳化設備200之檢測裝置包括乳化狀態檢測裝置260設置於薄膜乳化槽230之流體出口,以即時監測乳化液之乳化程度(即即時液體濁度)。在另一實施例中(圖未示出),可設置乳化狀態檢測裝置以分別即時監測連續相槽體210內之連續相流體與薄膜乳化槽230內之乳化液的乳化程度。根據本創作,乳化狀態檢測裝置為分光光度計、也可以是工業相機。 As described above, the thin film emulsification equipment according to the present invention is provided with a detection device at an appropriate place, so as to detect the real-time status of each fluid and emulsion in the equipment in real time. According to the present inventive embodiment, the detection device of the membrane emulsification apparatus 200 includes an emulsification state detection device 260 disposed at the fluid outlet of the membrane emulsification tank 230 to monitor the emulsification degree (ie, instant liquid turbidity) of the emulsion in real time. In another embodiment (not shown), an emulsification state detection device can be provided to monitor the emulsification degree of the continuous phase fluid in the continuous phase tank 210 and the emulsion in the thin film emulsification tank 230 respectively. According to the present invention, the emulsification state detection device is a spectrophotometer or an industrial camera.

根據本創作,薄膜乳化設備200之檢測裝置包括流量檢測裝置F。如上述說明,在薄膜乳化設備200的連續相槽體210與連續相輸送源214之間設有第一流量檢測裝置F,且在分散相槽體220與薄膜乳化槽230之間設有第二流量檢 測裝置F,第一和第二流量檢測裝置分別檢測連續相流體與分散相流體之一即時流量與流速。根據本創作實施例,流量檢測裝置F可為流量計或流速計。 According to the present invention, the detection device of the thin film emulsification apparatus 200 includes a flow detection device F. As described above, a first flow detection device F is provided between the continuous phase tank 210 and the continuous phase conveying source 214 of the thin film emulsification apparatus 200 , and a second flow detection device F is provided between the dispersed phase tank 220 and the thin film emulsification tank 230 flow detection A measuring device F, the first and second flow measuring devices respectively detect the instantaneous flow and flow rate of one of the continuous phase fluid and the dispersed phase fluid. According to the present inventive embodiment, the flow detection device F may be a flow meter or a flow meter.

此外,薄膜乳化設備200之檢測裝置包括壓力檢測裝置P。如上述說明,在薄膜乳化槽230處設置有第一壓力檢測裝置P,且在薄膜乳化槽230下游設置有第二壓力檢測裝置P,以分別即時檢測分散相流體和連續相流體之一即時流體壓力。在另一實施例中(圖未示出),壓力檢測裝置分別即時監測連續相槽體210內之連續相流體、分散相槽體220內之分散相流體與薄膜乳化槽230內的乳化液的壓力。根據本創作實施例,壓力檢測裝置P可以為氣壓錶或油壓錶,並且配合卸壓閥或是藉由連續相輸送源及分散相輸送源的調控做即時的壓力調整。 In addition, the detection device of the thin film emulsification apparatus 200 includes a pressure detection device P. As shown in FIG. As described above, a first pressure detection device P is provided at the thin film emulsification tank 230, and a second pressure detection device P is provided downstream of the thin film emulsification tank 230, so as to detect instantaneously one of the dispersed phase fluid and the continuous phase fluid, respectively. pressure. In another embodiment (not shown in the figure), the pressure detection device monitors the continuous phase fluid in the continuous phase tank 210, the dispersed phase fluid in the dispersed phase tank 220, and the emulsion in the thin film emulsification tank 230 in real time, respectively. pressure. According to the present inventive embodiment, the pressure detection device P can be a barometer or an oil pressure gauge, and cooperates with a pressure relief valve or performs real-time pressure adjustment through the regulation of the continuous phase delivery source and the dispersed phase delivery source.

薄膜乳化設備200之檢測裝置包括溫度檢測裝置T,溫度檢測裝置T可設置在各槽體處以分別即時監測連續相槽體210內之連續相流體、分散相槽體220內之分散相流體與薄膜乳化槽230內之乳化液的溫度。 The detection device of the thin film emulsification apparatus 200 includes a temperature detection device T, which can be installed at each tank to monitor the continuous phase fluid in the continuous phase tank 210, the dispersed phase fluid and the thin film in the dispersed phase tank 220 in real time respectively. The temperature of the emulsion in the emulsification tank 230.

根據本創作之薄膜乳化設備200還包括與其電性連接的一自動控制裝置150,其由處理器、使用者介面裝置和儲存裝置所構成,可回應於前述針對連續相流體、分散相流體和乳化液所檢測得到的溫度、壓力、濁度等即時狀態,依流體種類而相應地切換薄膜乳化設備200之操作模式與各式操作參數,或根據檢測裝置檢測到的乳化程度、流量、流速、壓力和溫度等數據以自動控制元件(圖未示出)進行補償。自動控制裝置係與所述至少一檢測元件、連續相輸送源214、分散相輸送源224或228及水浴設備240電性耦接,預設為手動模式時,可以建立操作參數資料庫;而預設為自動模式時,設備將回應於即時狀態的接收而切換薄膜乳化設備200中的連續相輸送源214、分散相輸送源224或228 或水浴設備240至少一設定參數,進行連續相流體和分散相流體的各自即時狀態或溫度的相應調整。 The thin-film emulsification apparatus 200 according to the present invention further includes an automatic control device 150 electrically connected to it, which is composed of a processor, a user interface device and a storage device, which can respond to the foregoing for continuous phase fluid, dispersed phase fluid and emulsification According to the real-time status of temperature, pressure, turbidity, etc. detected by the liquid, the operation mode and various operating parameters of the thin film emulsification device 200 are correspondingly switched according to the type of fluid, or according to the degree of emulsification, flow rate, flow rate, and pressure detected by the detection device. Data such as temperature and temperature are compensated by automatic control elements (not shown in the figure). The automatic control device is electrically coupled to the at least one detection element, the continuous phase delivery source 214, the dispersed phase delivery source 224 or 228, and the water bath device 240. When the manual mode is preset, an operating parameter database can be established; When set to automatic mode, the apparatus will switch the continuous phase delivery source 214, the dispersed phase delivery source 224 or 228 in the thin film emulsification apparatus 200 in response to receiving the immediate status Or at least one setting parameter of the water bath device 240 is used to adjust the respective instantaneous states or temperatures of the continuous phase fluid and the dispersed phase fluid.

詳言之,根據本創作,薄膜乳化設備200的操作模式可分為自動模式及手動模式。在手動模式中,使用者須先如自行設定連續相流體及分散相流體之種類和黏度等資訊,以利於後續的建檔,並且參數設定上可以設定個別設定連續相流體與分散相流體的流速和流量及製程溫度等,亦可直接設定連續相流體及分散相流體之壓力比,藉由壓力檢測裝置P所得數據自動進行輸送源之參數補償,可因應不同黏度之連續相流體及分散相流體及製程中連續相流體壓力有所變動之情況,降低人為調校的誤差。此模式於每次製程皆會記錄錶頭及檢測裝置全程所記錄的數據和製程中參數的調校時機,並經過分析建立模型。若有參數修正需求,可直接開啟此模型進行修改再另存成一新模型或取代原有模型,並於自動模式中可直接套用。 In detail, according to the present invention, the operation modes of the thin film emulsification apparatus 200 can be divided into an automatic mode and a manual mode. In the manual mode, the user must first set the information such as the type and viscosity of the continuous phase fluid and the dispersed phase fluid to facilitate the subsequent file creation, and the parameter setting can set the flow rate of the continuous phase fluid and the dispersed phase fluid individually. According to the flow rate and process temperature, the pressure ratio of the continuous phase fluid and the disperse phase fluid can also be directly set, and the parameters of the conveying source can be automatically compensated by the data obtained by the pressure detection device P, which can respond to the continuous phase fluid and disperse phase fluid of different viscosities. And the continuous phase fluid pressure in the process fluctuates to reduce the error of manual adjustment. In this mode, the data recorded by the meter head and the testing device and the adjustment timing of parameters in the process are recorded in each process, and a model is established through analysis. If there is a need for parameter correction, you can directly open the model to modify it and save it as a new model or replace the original model, which can be directly applied in the automatic mode.

第三圖係一示意圖,說明根據本創作實施例之薄膜乳化設備200的使用者介面裝置(即控制面板)90,可依據需求進行手動及自動模式之設定。根據本創作實施例,控制面板90對操作者顯示薄膜乳化設備200中各式檢測裝置所檢測到的乳化程度、流量、流速、壓力和溫度等數據,並可供操作者進行手動調整連續相狀態、分散相狀態和乳化液狀態如乳化程度、流量、流速、壓力和溫度。應當理解,圖示控制面板90的顯示內容僅為示意,但顯示內容不限於此。 FIG. 3 is a schematic diagram illustrating the user interface device (ie, the control panel) 90 of the thin film emulsification apparatus 200 according to the present inventive embodiment, which can be set in manual and automatic modes according to requirements. According to this creative embodiment, the control panel 90 displays to the operator data such as the degree of emulsification, flow rate, flow rate, pressure and temperature detected by various detection devices in the thin film emulsification apparatus 200, and allows the operator to manually adjust the continuous phase state , dispersed phase state and emulsion state such as degree of emulsification, flow rate, flow rate, pressure and temperature. It should be understood that the display content of the control panel 90 is only for illustration, but the display content is not limited thereto.

綜上所述,本創作之薄膜乳化設備具有持溫及溫控機制,能適用各種熔點的原料,並可藉此控制乳化反應的效能;又利用檢測元件能檢測薄膜乳化設備中連續相流體、分散相流體以及乳化液的即時狀態,並可自動補償以 達製程自動化之效。透過二次乳化回路的設計,本創作之薄膜乳化設備能於尚未洩料之狀態下直接進行多重乳化反應,提高乳化液產製效率和品質;又因建構有自動化模式,可適當切換薄膜乳化設備的操作模式;結合連續相流體、分散相流體以及乳化液等即時狀態的即時監控和自動補償,可降低人為操作誤差,提高乳化製程的一致性。 To sum up, the thin film emulsification equipment of this creation has a temperature holding and temperature control mechanism, which can be applied to raw materials with various melting points, and can control the efficiency of the emulsification reaction; Real-time status of dispersed phase fluids and emulsions, with automatic compensation to Achieve the effect of process automation. Through the design of the secondary emulsification circuit, the film emulsification equipment of this creation can directly perform multiple emulsification reactions before the material is discharged, so as to improve the production efficiency and quality of the emulsion; and because of the automatic mode, the film emulsification equipment can be appropriately switched. Combined with the real-time monitoring and automatic compensation of the real-time status of continuous phase fluid, dispersed phase fluid and emulsion, it can reduce human operation errors and improve the consistency of the emulsification process.

需注意的是,本創作所提之前述實施例係僅用於例示說明本創作,而非用於限制本創作之範圍。熟習本創作所屬領域技藝之人對本創作所進行之諸般修飾和變化皆不脫離本創作之精神與範疇。不同實施例中相同或相似的構件、或不同實施例中以相同元件符號表示的構件係具有相同的物理或化學特性。此外,在適當的情況下,本創作之上述實施例係可互相組合或替換,而非僅限於上文所描述的特定實施例。在一實施例中所描述的特定構件與其他構件的連接關係亦可應用於其他實施例中,其皆落於本創作如附申請專利範圍之範疇。 It should be noted that the foregoing embodiments mentioned in the present creation are only used to illustrate the present creation, rather than to limit the scope of the present creation. All modifications and changes made to this creation by people who are familiar with the art in the field to which this creation belongs are not departing from the spirit and scope of this creation. The same or similar components in different embodiments, or components denoted by the same reference numerals in different embodiments, have the same physical or chemical properties. In addition, the above-described embodiments of the present invention may be combined or replaced with each other under appropriate circumstances, and are not limited to the specific embodiments described above. The connection relationship between a specific component and other components described in one embodiment can also be applied to other embodiments, which all fall within the scope of the present invention and the scope of the appended claims.

200:薄膜乳化設備 200: Film emulsification equipment

210:連續相槽體 210: Continuous phase tank

212:連續相引流通道 212: Continuous phase drainage channel

213:出料口 213: discharge port

214:連續相輸送源 214: Continuous Phase Delivery Source

216:二次乳化回路 216: Secondary emulsification circuit

220:分散相槽體 220: Dispersed phase tank

220a、220b:通道 220a, 220b: channel

221:入料分支通道 221: Feeding branch channel

222:分散相引流通道 222: Dispersed phase drainage channel

224:分散相輸送源(氣壓源) 224: Dispersed phase delivery source (air pressure source)

226:抽氣裝置 226: Air extraction device

228:分散相輸送源(蠕動泵) 228: Disperse phase delivery source (peristaltic pump)

230:薄膜乳化槽 230: Film emulsification tank

231:多孔膜管 231: Porous membrane tube

232:乳化槽引流通道 232: Drainage channel of emulsification tank

240:水浴設備 240: Water bath equipment

250:連接引流通道 250: Connect the drainage channel

260:乳化狀態檢測裝置 260: Emulsification state detection device

F:流量檢測裝置 F: flow detection device

P:壓力檢測裝置 P: Pressure detection device

T:溫度檢測裝置 T: temperature detection device

V1、V2、V3、V4、V5、V6:開關閥 V 1 , V 2 , V 3 , V 4 , V 5 , V 6 : On-off valve

Claims (9)

一種薄膜乳化設備,包括:一連續相槽體,用以容納一連續相流體;一分散相槽體,用以容納一分散相流體;一薄膜乳化槽,其分別自該連續相槽體與該分散相槽體接收該連續相流體和該分散相流體,該薄膜乳化槽內設置有至少一多孔膜管,該連續相流體與該分散相流體於所述多孔膜管內混合以形成一乳化液;至少一檢測裝置,係分別耦接於該連續相槽體、該分散相槽體和該薄膜乳化槽或其間,以檢測該連續相流體、該分散相流體與該乳化液中其一或多者之一即時狀態;以及一水浴設備,其與該連續相槽體、該分散相槽體和該薄膜乳化槽流體連通,該水浴設備提供一水浴流體流通於該連續相槽體、該分散相槽體和該薄膜乳化槽間,以控制該連續相槽體、該分散相槽體和該薄膜乳化槽的各自溫度,並能回應該即時狀態而自動進行溫度調節。 A thin film emulsification device, comprising: a continuous phase tank body for accommodating a continuous phase fluid; a dispersed phase tank body for accommodating a dispersed phase fluid; a thin film emulsification tank, which are respectively separated from the continuous phase tank body and the The dispersed phase tank body receives the continuous phase fluid and the dispersed phase fluid, at least one porous membrane tube is arranged in the thin film emulsification tank, and the continuous phase fluid and the dispersed phase fluid are mixed in the porous membrane tube to form an emulsion liquid; at least one detection device, respectively coupled to the continuous phase tank, the dispersed phase tank and the thin film emulsification tank or among them, to detect one of the continuous phase fluid, the dispersed phase fluid and the emulsion One of more than one instant state; And a water bath equipment, which is in fluid communication with the continuous phase tank, the dispersed phase tank and the thin film emulsification tank, the water bath equipment provides a water bath fluid flow in the continuous phase tank, the dispersion Between the phase tank and the thin film emulsification tank, the respective temperatures of the continuous phase tank, the dispersed phase tank and the thin film emulsification tank can be controlled, and the temperature can be adjusted automatically in response to the immediate state. 如請求項1所述的薄膜乳化設備,其中該連續相槽體、該分散相槽體、該薄膜乳化槽與連續相流體和分散相流體所流經之管路係各自具有由一內管和一外管所形成之一夾套式結構,其中該內管與該外管之間形成一引流通道,該水浴流體係於該連續相槽體、該分散相槽體、該薄膜乳化槽與連續相流體和分散相流體所流經之管路的各自引流通道中流通。 The thin film emulsification device according to claim 1, wherein the continuous phase tank body, the dispersed phase tank body, the thin film emulsification tank and the pipeline system through which the continuous phase fluid and the dispersed phase fluid flow each have an inner pipe and A jacket-type structure formed by an outer tube, wherein a drainage channel is formed between the inner tube and the outer tube, and the water bath flow system is in the continuous phase tank, the dispersed phase tank, the film emulsification tank and the continuous The phase fluid and the dispersed phase fluid flow through the respective drainage channels of the pipeline. 如請求項1所述的薄膜乳化設備,其中所述至少一檢測裝置包括至少一溫度檢測裝置,係設置於該連續相槽體、該分散相槽體、該薄膜乳化槽和該水浴設備中其一或多者上。 The thin film emulsification equipment according to claim 1, wherein the at least one detection device comprises at least one temperature detection device, which is arranged in the continuous phase tank body, the dispersed phase tank body, the thin film emulsification tank and the water bath equipment. one or more. 如請求項1所述的薄膜乳化設備,其中所述至少一檢測裝置包括一分光光度計或一工業相機,其設置於該薄膜乳化槽之下游處以檢測該乳化液的一即時濁度,藉此監控該乳化液之一即時乳化狀態。 The film emulsification apparatus of claim 1, wherein the at least one detection device comprises a spectrophotometer or an industrial camera, which is disposed downstream of the film emulsification tank to detect an instant turbidity of the emulsion, thereby Monitor the instant emulsification status of one of the emulsions. 如請求項1所述的薄膜乳化設備,更包括一連續相輸送源以將該連續相流體自該連續相槽體泵送至該薄膜乳化槽,其中所述至少一檢測裝置包括設置於該連續相槽體與該連續相輸送源之間的一第一流量檢測裝置、以及設置在該分散相槽體與該薄膜乳化槽之間的一第二流量檢測裝置,以分別檢測該連續相流體與該分散相流體之一即時流量與流速。 The thin-film emulsification apparatus of claim 1, further comprising a continuous-phase transport source to pump the continuous-phase fluid from the continuous-phase tank to the thin-film emulsification tank, wherein the at least one detection device comprises a A first flow detection device between the phase tank body and the continuous phase conveying source, and a second flow detection device arranged between the dispersed phase tank body and the film emulsification tank to detect the continuous phase fluid and the film respectively. The instantaneous flow and flow rate of one of the dispersed phase fluids. 如請求項1所述的薄膜乳化設備,其中所述至少一檢測裝置包括設置在該薄膜乳化槽之一第一壓力檢測裝置、以及設置在該薄膜乳化槽下游的一第二壓力檢測裝置,以分別檢測該分散相流體和該連續相流體之一即時流體壓力。 The film emulsification apparatus according to claim 1, wherein the at least one detection device comprises a first pressure detection device arranged in the film emulsification tank, and a second pressure detection device arranged downstream of the film emulsification tank, so as to The instantaneous fluid pressure of one of the dispersed phase fluid and the continuous phase fluid is detected, respectively. 如請求項1所述的薄膜乳化設備,更包括一二次乳化回路,該二次乳化回路連接於該薄膜乳化槽以接收該乳化液並將該乳化液回送至該薄膜乳化槽中進行再次乳化。 The thin film emulsification equipment according to claim 1, further comprising a secondary emulsification circuit, the secondary emulsification circuit is connected to the thin film emulsification tank to receive the emulsion and return the emulsion to the thin film emulsification tank for re-emulsification . 如請求項1所述的薄膜乳化設備,更包括一自動控制裝置,係與所述至少一檢測元件電性耦接,於自動模式時以回應於該即時狀態的接收自動進行一連續相輸送源和一分散相輸送源的相應調整。 The thin-film emulsification apparatus according to claim 1, further comprising an automatic control device electrically coupled to the at least one detection element, in the automatic mode, in response to the receiving of the real-time state, automatically performing a continuous-phase conveying source and a corresponding adjustment of the disperse phase delivery source. 如請求項8所述的薄膜乳化設備,其中該自動控制裝置包括:一處理器,於操作前可先設定該薄膜乳化設備之模式為一手動模式或一自動模式,並於自動模式下可令該連續相輸送源和該分散相輸送源依據該連續相 流體、該分散相流體與該乳化液中至少其一或多者的所述即時狀態自動進行相應調整;一使用者介面裝置,其對操作者顯示該連續相流體、該分散相流體與該乳化液的該即時狀態,並且供操作者進行對該薄膜乳化設備的操作控制;以及一儲存裝置,其儲存所接收之該連續相流體、該分散相流體與該乳化液的該即時狀態,並儲存有不同模式下該薄膜乳化設備之該操作模式的相關程式指令。 The thin film emulsification device as claimed in claim 8, wherein the automatic control device comprises: a processor, which can set the mode of the thin film emulsification device to be a manual mode or an automatic mode before operation, and can make the The continuous phase delivery source and the dispersed phase delivery source depend on the continuous phase The real-time state of at least one or more of the fluid, the dispersed phase fluid and the emulsion is automatically adjusted accordingly; a user interface device that displays the continuous phase fluid, the dispersed phase fluid and the emulsion to the operator The immediate state of the liquid, and for the operator to control the operation of the thin film emulsification device; and a storage device, which stores the received continuous phase fluid, the dispersed phase fluid and the immediate state of the emulsion, and stores There are program instructions related to this mode of operation of the thin film emulsification device in different modes.
TW110208219U 2021-07-13 2021-07-13 Membrane emulsification apparatus TWM623516U (en)

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