JPS62100288A - Production apparatus for microorganism-containing capsule - Google Patents

Production apparatus for microorganism-containing capsule

Info

Publication number
JPS62100288A
JPS62100288A JP24017085A JP24017085A JPS62100288A JP S62100288 A JPS62100288 A JP S62100288A JP 24017085 A JP24017085 A JP 24017085A JP 24017085 A JP24017085 A JP 24017085A JP S62100288 A JPS62100288 A JP S62100288A
Authority
JP
Japan
Prior art keywords
rotary container
microorganism
nozzle
rotating container
coating agent
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP24017085A
Other languages
Japanese (ja)
Inventor
Hironori Nakamura
裕紀 中村
Naomichi Mori
直道 森
Ichiro Nakajima
一郎 中島
Jiichi Nishimoto
西本 滋一
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hitachi Plant Technologies Ltd
Original Assignee
Hitachi Plant Technologies Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hitachi Plant Technologies Ltd filed Critical Hitachi Plant Technologies Ltd
Priority to JP24017085A priority Critical patent/JPS62100288A/en
Publication of JPS62100288A publication Critical patent/JPS62100288A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J13/00Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
    • B01J13/02Making microcapsules or microballoons
    • B01J13/04Making microcapsules or microballoons by physical processes, e.g. drying, spraying

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Immobilizing And Processing Of Enzymes And Microorganisms (AREA)
  • Manufacturing Of Micro-Capsules (AREA)

Abstract

PURPOSE:To obtain microorganism-containing capsules having uniform particle diameters, by extruding microorganism suspension from the inner wall of a nozzle, releasing a film-forming agent solution along the outer wall of the nozzle, forming liquid drops which cover the microorganism suspension with the film-forming agent solution and introducing them into a gelatinizing solution bath. CONSTITUTION:An inverted cone type rotary container 1 is set on the top of a hollow vertical shaft 2 and a great number of nozzles 7 are set at equal intervals at the outermost peripheral part of the rotary container 1. A pipe 12 to feed a film-forming agent solution is laid at the central part above the rotary container 1, a solution bath to feed the film-forming agent solution is set at a lower top part of the rotary container 1 and the film-forming agent solution is introduced from the lower top part to the nozzle 7 with rotation of the rotary container 1. A microorganism suspension is fed from a hollow part of the hollow vertical shaft 2 to an inner part of the rotary container 1.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は微生物懸濁液を高分子被膜剤の内部に閉じ込め
た微生物内包カプセルを製造する装置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to an apparatus for manufacturing a microorganism-containing capsule in which a microorganism suspension is confined inside a polymer coating agent.

〔従来の技術〕[Conventional technology]

粒径が1〜5m程度の比較的大型の微生物包括カプセル
を製造する装置として、同心二重管の内管から微生物懸
濁液を、外管から被膜剤液全同時に放出して液滴化し、
ゲル化剤液中に落下させるものが考えられる。この装置
により、中心部分の′微生物湿濁液の外側を被膜剤液が
覆った液滴が得られ、さらに被膜剤1夜がゲル化剤液中
でダル化し、微生物包括カプセルが連続して得られる。
As a device for manufacturing relatively large microorganism-containing capsules with a particle size of about 1 to 5 m, the microorganism suspension is simultaneously discharged from the inner tube of a concentric double tube and the coating agent liquid is released from the outer tube to form droplets.
One possibility is to drop it into the gelling agent solution. With this device, droplets are obtained in which the outside of the microbial suspension in the central part is covered with the coating agent solution, and the coating agent is further thickened in the gelling agent solution, and microbial-enclosing capsules are continuously obtained. It will be done.

しかし、多量のカプセルを得るためには多数の同心二重
管を備えなげればならず、装置が複雑化する問題がある
However, in order to obtain a large number of capsules, a large number of concentric double tubes must be provided, which poses a problem of complicating the apparatus.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

本発明の目的は簡単な装置で多量の微生物内包カプセル
が得られる装置全提供することにある。
An object of the present invention is to provide an entire device that can obtain a large amount of microorganism-containing capsules with a simple device.

〔問題点を解決するための手段および作用〕回転容器の
遠心力を利用し、周辺部に設けたノズルから液滴を発生
させる装置は簡単で多量の液滴が得られることに着目し
、微生物懸濁液をノズルの内側から放出させ、被膜剤液
をノズルの外壁に沿って放出させ、微生物懸濁液を内包
しなから構成される装置を考えた。
[Means and actions for solving the problem] We focused on the fact that a device that uses the centrifugal force of a rotating container to generate droplets from a nozzle installed at its periphery is simple and can produce a large amount of droplets. We devised a device in which the suspension is discharged from the inside of the nozzle, the coating agent liquid is discharged along the outer wall of the nozzle, and the microbial suspension is not encapsulated.

すなわち、本発明装置は、鉛直軸の回りに回転する逆円
錐型の回転容器の下側頂部から回転容器の内部に供給し
た微生物懸濁液を、回転容器の周辺部に等間隔に設けた
ノズルの内側から放出させ、・同時に、回転容器の下側
頂部から側面外壁に、及び上面に供給した被膜剤液をノ
ズルの外壁に沿って放出させることによって、微生物懸
濁液を被膜剤液で包んだ液滴を形成させ、回転容器の周
囲に飛散する液滴をゲル化剤液中に落下させてゲル化す
るように構成したことを特徴とする。
That is, the device of the present invention supplies a microorganism suspension into the inside of the rotating container from the lower top of the rotating container in the form of an inverted cone that rotates around a vertical axis, through nozzles provided at equal intervals around the periphery of the rotating container. At the same time, the coating agent solution supplied from the lower top of the rotating container to the side outer wall and the upper surface is released along the outer wall of the nozzle, thereby enveloping the microorganism suspension in the coating agent solution. The present invention is characterized in that the liquid droplets are formed, and the liquid droplets scattered around the rotating container fall into the gelling agent liquid and are gelled.

〔実 施 例〕〔Example〕

第1図に本発明装置の一実施例を示す。 FIG. 1 shows an embodiment of the apparatus of the present invention.

逆円錐型の回転容器lは、下側の頂部に連結した中空の
回転軸2とモータ3及びベル)4によって平動される。
The inverted cone-shaped rotating container 1 is moved horizontally by a hollow rotating shaft 2 connected to the lower top, a motor 3, and a bell) 4.

微生物懸濁液5は、ポンプ6によって回転@2の中空部
を経て、回転容器lの内部に供給され、回転容器10周
辺部に等間隔に設けられたノズル7の各々から均一に放
出される。
The microbial suspension 5 is supplied into the rotating container l by a pump 6 through the hollow part of the rotation@2, and is uniformly discharged from each nozzle 7 provided at equal intervals around the rotating container 10. .

被膜剤液8はポンプ9によって被膜剤液槽]、 0に送
られ、液中に浸漬した回転容器1の頂部近傍位置に液面
が保持される。被膜剤液は回転容器lの回転による遠心
力と液自体の表面張力の作用によって、回転容器1の側
面外壁を膜状に均一に広がって周辺部に至る。また、被
膜剤f夜8はポンプ11によって回転容器1の中心部の
上方から供給管12を通って供給され、回転容器lの上
面を膜状に均一に広がって周辺部に至る。これらの被膜
剤液はさらにノズル7の外壁に沿って各々から均一に放
出される。このとき、被膜剤液が重合触媒を必要とする
重合性の薬剤である場合は、重合触媒液13がポンプ1
4、ポンプ15によって被膜剤液槽10及び供給管ll
内の被膜剤液に供給される。
The coating agent liquid 8 is sent by a pump 9 to a coating agent liquid tank], 0, and the liquid level is maintained at a position near the top of the rotating container 1 immersed in the liquid. Due to the centrifugal force caused by the rotation of the rotating container 1 and the surface tension of the liquid itself, the coating agent liquid spreads uniformly over the outer side wall of the rotating container 1 in the form of a film and reaches the periphery. Further, the coating agent f 8 is supplied by the pump 11 from above the center of the rotary container 1 through the supply pipe 12, and spreads uniformly over the upper surface of the rotary container 1 in the form of a film to reach the periphery. These coating agent liquids are further discharged uniformly from each along the outer wall of the nozzle 7. At this time, if the coating agent liquid is a polymerizable agent that requires a polymerization catalyst, the polymerization catalyst liquid 13 is
4. The coating agent liquid tank 10 and the supply pipe ll are connected by the pump 15.
It is supplied to the coating agent liquid inside.

ノズル7の先端で、被膜剤液が微生物懸濁液を内包しな
がら液滴16になる。液滴1bは、ゲル化剤液槽17内
のゲル化剤液18中に落下して外側の被膜剤液がゲル化
し、微生物内包カプセル19になる。
At the tip of the nozzle 7, the coating agent liquid becomes a droplet 16 while containing the microorganism suspension. The droplet 1b falls into the gelling agent liquid 18 in the gelling agent liquid tank 17, and the outer coating agent liquid gels, forming a microorganism-containing capsule 19.

ノズル7は第2図に示すように、同一水平面内で、先端
方向を遠心方向に対して一定角度を保って取り付けるこ
とにより、回転容器lの回転によるノズル外壁を流れる
被膜剤液の片寄りを少なくすることができ、微生物が被
膜剤に完全罠内包されたカプセルを得ることができる。
As shown in Fig. 2, the nozzle 7 is installed in the same horizontal plane with the tip direction kept at a constant angle with respect to the centrifugal direction, thereby preventing the coating agent liquid flowing on the outer wall of the nozzle from shifting due to the rotation of the rotating container l. It is possible to obtain capsules in which microorganisms are completely encapsulated in the coating agent.

被膜剤としては、天然高分子物質、アクリル系樹脂、ア
クリルイミド系樹脂、アクリルアミド系樹脂、エポキシ
系樹脂、スチレン系樹脂、ビニール系樹脂、メラミン系
樹脂、ポリウレタン系樹脂、ポリエチレングリコールア
クリレート系樹脂、ポリエチレングリコールメタクリレ
ート系樹脂などを用いることができる。
Coating agents include natural polymer substances, acrylic resins, acrylimide resins, acrylamide resins, epoxy resins, styrene resins, vinyl resins, melamine resins, polyurethane resins, polyethylene glycol acrylate resins, and polyethylene. Glycol methacrylate resin or the like can be used.

実験1 第1図に示した装置で、内径1.5n++n、外径2.
、長さ61のノズル20本を逆円錐型の容器の周辺部に
等間隔に備えた回転容器を用いた。ノズルはすべて水平
面内にあり、ノズル外壁を流れる被膜剤液の片寄りをな
(すため、先端方向を遠心方向に対して40°になるよ
うに取り付けた。ノズル先端の回転半径は35+mであ
る。回転容器の頂角は110°とし、回転速度500 
rpmで回転させた。
Experiment 1 The apparatus shown in Fig. 1 was used with an inner diameter of 1.5n++n and an outer diameter of 2.5n.
A rotating container was used in which 20 nozzles each having a length of 61 mm were provided at equal intervals around the periphery of the inverted conical container. All nozzles are in a horizontal plane, and in order to prevent the coating liquid flowing on the outer wall of the nozzle from being biased, the nozzles were installed so that the tip direction was 40° with respect to the centrifugal direction.The rotation radius of the nozzle tip was 35+ m. .The apex angle of the rotating container is 110°, and the rotation speed is 500.
Rotated at rpm.

微生物懸濁液として、20000■/lの活性汚泥に成
型助剤としてのアルギン酸ナトリウムを0.6%で混合
したものを用いた。また、被膜剤液として、可塑剤とし
てのメチルエチルケトンを25%で添加したポリウレタ
ンプレポリマーヲ用いた。
As a microorganism suspension, a mixture of 20,000 μ/l of activated sludge and 0.6% of sodium alginate as a forming aid was used. Further, a polyurethane prepolymer to which 25% of methyl ethyl ketone as a plasticizer was added was used as a coating agent liquid.

活性汚泥−アルギン酸ナトリウム混合液を回転軸の中空
部から回転容器の内部に150m1/minで供給し、
ポリウレタンプレポリマーを頂部及び上面中心部から1
5 ml / minずつの流量で連続的に供給した。
Activated sludge-sodium alginate mixed solution is supplied from the hollow part of the rotating shaft into the rotating container at a rate of 150 ml/min,
1 from the top and center of the top surface of the polyurethane prepolymer
It was supplied continuously at a flow rate of 5 ml/min.

周囲に飛散する液滴をゲル化剤液中ころ、液滴中のアル
ギン酸ナトリウムが水に不溶のアルギン酸カルシウムに
なりさらにポリウレタンプレポリマーの重合が完了して
ゲル化し、平均粒径2.3 mの球形の活性汚泥内包カ
プセルが連続して得られた。
When the droplets scattered around are transferred to a roller in the gelling agent solution, the sodium alginate in the droplets becomes calcium alginate which is insoluble in water, and the polymerization of the polyurethane prepolymer is completed and gelatinized, resulting in an average particle size of 2.3 m. Spherical activated sludge-containing capsules were continuously obtained.

実験2 実験1と同じ装置を用いた。回転容器の回転速度は50
0 rpmとした。
Experiment 2 The same apparatus as Experiment 1 was used. The rotation speed of the rotating container is 50
It was set to 0 rpm.

微生物懸濁液として40000η/lに濃縮した活性汚
泥を用いた。また、被膜剤液として架橋剤としてのNN
’−メチレンビスアクリルアミドを2%で混合したポリ
エチレングリコールジメタクリソート30%溶液に、さ
らに成形助剤としてアルギン酸ナトリウムを0.8%で
混合したものを用いた。
Activated sludge concentrated to 40,000 η/l was used as a microbial suspension. In addition, NN as a crosslinking agent is used as a coating agent liquid.
A 30% solution of polyethylene glycol dimethacrysote mixed with 2% of '-methylenebisacrylamide was used, which was further mixed with 0.8% of sodium alginate as a molding aid.

活性汚泥を回転軸の中空部から回転容器の内部に80 
ml / minで供給し、ポリエチレングリコールジ
メタクリレート−アルギン酸ナトリウム混合液を頂部及
び上面中心部から36 rnll minずつの流量で
連続的に供給した。なお、同時に重合触媒液として重合
促進剤のNNN’N’−テトラメチルエチレンジアミン
10%溶液を4 rrtl / minずつの流量で頂
部及び上面中心部に供給した。周囲に飛散する液滴をゲ
ル化剤液としての2%塩化カルシウムと1%ベルオキン
ニ硫硫酸カリウム台溶液中に落下させたところ、液滴中
のアルギン酸ナトリウムが水に不溶のアルギン酸カルシ
ウムになり、さらにポリエチレングリコールジメタクリ
レートの重合が完了してゲル化し、平均粒径2.5簡の
球形の活性汚泥内包カプセルが連続して得られた。
Activated sludge is poured into the rotating container from the hollow part of the rotating shaft for 80 minutes.
ml/min, and the polyethylene glycol dimethacrylate-sodium alginate mixture was continuously fed from the top and the center of the top surface at a flow rate of 36 rnll min. At the same time, a 10% solution of NNN'N'-tetramethylethylenediamine, which is a polymerization promoter, was supplied as a polymerization catalyst liquid to the top and the center of the upper surface at a flow rate of 4 rrtl/min. When the droplets scattered around were dropped into a gelling agent solution of 2% calcium chloride and 1% potassium sulfate solution, the sodium alginate in the droplets turned into calcium alginate, which is insoluble in water, and further The polymerization of polyethylene glycol dimethacrylate was completed and gelatinized, and spherical activated sludge-containing capsules with an average particle size of 2.5 capsules were continuously obtained.

〔発明の効果〕〔Effect of the invention〕

本発明によれば、微生物内包カプセルを効率よく製造す
ることができる。
According to the present invention, microorganism-containing capsules can be efficiently manufactured.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明の実施例を示す装置系統図、第2図は本
発明に係る回転容器におけるノズルの取付状況を示す平
面図である。 l・・・回転容器、    2・・・回転軸5・・・微
生物懸濁液、  7・・・ノズル8・・・被膜剤液、 
   10・・・被膜剤液槽12・・・供給管、   
 16・・・液 滴17・・・ゲル化剤液槽、  18
・・・ゲル化剤液。 第1図 第2図
FIG. 1 is a system diagram of an apparatus showing an embodiment of the present invention, and FIG. 2 is a plan view showing how nozzles are installed in a rotating container according to the present invention. l... Rotating container, 2... Rotating shaft 5... Microbial suspension, 7... Nozzle 8... Coating agent liquid,
10... Coating agent liquid tank 12... Supply pipe,
16...Liquid drop 17...Gelling agent liquid tank, 18
...gelling agent liquid. Figure 1 Figure 2

Claims (1)

【特許請求の範囲】[Claims] 中空の鉛直軸の回りに回転する逆円錐型の回転容器と、
前記鉛直軸の中空部を経て回転容器の下側頂部から回転
容器の内部に微生物懸濁液を供給する手段と、回転容器
の周辺部に等間隔に設けられ、回転容器の回転に伴い前
記微生物懸濁液を外部に放出する複数のノズルと、回転
容器の中心上方から回転容器の上面に向けて被膜剤液を
供給する供給管と、回転容器の下側頂部位置近傍に被膜
剤液の液面を保持する被膜剤液槽と、回転容器の回転に
よつて前記ノズルから飛散する液滴をゲル化剤液中に受
入れるゲル化剤液槽を具備したことを特徴とする微生物
内包カプセルの製造装置。
an inverted cone-shaped rotating container that rotates around a hollow vertical axis;
means for supplying a microbial suspension into the rotary container from the lower top of the rotary container via the hollow part of the vertical shaft; A plurality of nozzles that discharge the suspension to the outside, a supply pipe that supplies the coating agent solution from above the center of the rotating container toward the top surface of the rotating container, and a coating agent liquid that is placed near the top of the lower side of the rotating container. Production of a microorganism-containing capsule characterized by comprising a coating agent liquid tank that holds a surface and a gelling agent liquid tank that receives droplets scattered from the nozzle by rotation of a rotating container into the gelling agent liquid. Device.
JP24017085A 1985-10-28 1985-10-28 Production apparatus for microorganism-containing capsule Pending JPS62100288A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24017085A JPS62100288A (en) 1985-10-28 1985-10-28 Production apparatus for microorganism-containing capsule

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24017085A JPS62100288A (en) 1985-10-28 1985-10-28 Production apparatus for microorganism-containing capsule

Publications (1)

Publication Number Publication Date
JPS62100288A true JPS62100288A (en) 1987-05-09

Family

ID=17055522

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24017085A Pending JPS62100288A (en) 1985-10-28 1985-10-28 Production apparatus for microorganism-containing capsule

Country Status (1)

Country Link
JP (1) JPS62100288A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02290233A (en) * 1989-04-28 1990-11-30 Mitsubishi Kakoki Kaisha Ltd Manufacturing device for granular gel

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02290233A (en) * 1989-04-28 1990-11-30 Mitsubishi Kakoki Kaisha Ltd Manufacturing device for granular gel

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