JPH0643660Y2 - Frozen grain production equipment - Google Patents

Frozen grain production equipment

Info

Publication number
JPH0643660Y2
JPH0643660Y2 JP1987184616U JP18461687U JPH0643660Y2 JP H0643660 Y2 JPH0643660 Y2 JP H0643660Y2 JP 1987184616 U JP1987184616 U JP 1987184616U JP 18461687 U JP18461687 U JP 18461687U JP H0643660 Y2 JPH0643660 Y2 JP H0643660Y2
Authority
JP
Japan
Prior art keywords
frozen
container
particles
refrigerant gas
refrigerant
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.)
Expired - Lifetime
Application number
JP1987184616U
Other languages
Japanese (ja)
Other versions
JPH0188365U (en
Inventor
多計城 秦
洋介 岡田
Original Assignee
大陽酸素株式会社
株式会社不二精機製造所
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 大陽酸素株式会社, 株式会社不二精機製造所 filed Critical 大陽酸素株式会社
Priority to JP1987184616U priority Critical patent/JPH0643660Y2/en
Publication of JPH0188365U publication Critical patent/JPH0188365U/ja
Application granted granted Critical
Publication of JPH0643660Y2 publication Critical patent/JPH0643660Y2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Description

【考案の詳細な説明】 〔産業上の利用分野〕 本考案は、ウイルス等の危険物質や有害物質を含む被凍
結原料から微細な凍結粒を製造するための装置に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention relates to an apparatus for producing fine frozen particles from a material to be frozen containing dangerous substances such as viruses and harmful substances.

〔従来の技術〕[Conventional technology]

従来の凍結粒製造装置として、例えば特公昭58-17392号
に開示されたものが知られている。
As a conventional frozen grain manufacturing apparatus, for example, one disclosed in Japanese Patent Publication No. 58-17392 is known.

この装置は、密閉断熱容器の上部に被凍結原料の噴霧ノ
ズルを配設すると共に排気ダクトを連通接続し、噴霧ノ
ズルの下方近傍部位に環状の冷媒噴出管を容器内壁面に
沿わせて配設し、容器底部にスクレーパを配設すると共
に凍結粒取出口を設けてなる。而して、かかる装置によ
れば、噴出管から容器内方に向けて液体窒素等の冷媒を
噴出すると共に噴霧ノズルから水等の液状原料を下向き
に噴霧すると、原料の噴霧微粒子は、それが自然落下す
る間に噴出冷媒及びその蒸発ガスと十字流接触、向流接
触又は並流接触して熱交換され、凍結する。この凍結粒
は容器底部に堆積し、スクレーパにより凍結粒取出口か
ら容器外に回収される。一方、冷媒ガスは排気ダクトか
ら容器外に排出される。
In this device, a spray nozzle for the raw material to be frozen is placed on top of a closed heat-insulating container, an exhaust duct is connected in communication, and an annular refrigerant jetting pipe is placed near the lower part of the spray nozzle along the inner wall surface of the container. Then, a scraper is arranged at the bottom of the container and a frozen grain take-out port is provided. Thus, according to such an apparatus, when a refrigerant such as liquid nitrogen is ejected from the ejection pipe toward the inside of the container and a liquid raw material such as water is sprayed downward from the spray nozzle, the atomized fine particles of the raw material are While spontaneously falling, the jet refrigerant and its evaporative gas are cross-flowed, counter-currently contacted, or co-currently contacted with each other to exchange heat and freeze. The frozen particles accumulate on the bottom of the container and are collected outside the container by a scraper from the frozen particle outlet. On the other hand, the refrigerant gas is discharged out of the container through the exhaust duct.

〔考案が解決しようとする問題点〕[Problems to be solved by the invention]

ところが、このような従来装置では、上記した如く凍結
粒の回収と冷媒ガスの排気とを別経路で行うようにして
いるため、次のような問題があった。
However, such a conventional device has the following problems because the frozen particles are collected and the refrigerant gas is discharged through different paths as described above.

すなわち、被凍結原料が噴霧ノズルから噴霧された段階
若しくは噴霧粒子が噴出冷媒と衝突した段階で、5〜10
μ程度に超微粒子化された原料粒子が発生する。かかる
原料粒子は、超微粒であるが故に、凍結後も自然落下す
ることなく容器内に浮遊して、冷媒ガスと共に排気ダク
トから排出される虞れがある。したがって、取出口から
の凍結粒の回収率が低下する。しかも、かかる超微凍結
粒が排気ダクト内壁に付着・堆積するといった弊害もあ
る。特に、被凍結原料がウィルス等の危険・有害物質を
含む場合には、上記した如く排気ダクトから排出される
超微凍結粒をそのまま放置しておくことができず、何ら
かのハザード対策を講じておく必要があるが、容易では
なく、万全を期することが困難である。
That is, when the material to be frozen is sprayed from the spray nozzle or the spray particles collide with the ejected refrigerant,
Raw material particles that have been made into ultrafine particles of about μ are generated. Since the raw material particles are ultrafine particles, they may float in the container without free fall even after freezing, and may be discharged from the exhaust duct together with the refrigerant gas. Therefore, the recovery rate of frozen particles from the outlet decreases. Moreover, there is also a harmful effect that such ultra-fine frozen particles adhere to and accumulate on the inner wall of the exhaust duct. In particular, if the material to be frozen contains dangerous or harmful substances such as viruses, the ultra-fine frozen particles discharged from the exhaust duct cannot be left as they are, and some kind of hazard countermeasures should be taken. It is necessary, but it is not easy and it is difficult to make every effort.

本考案は、従来装置における上記した問題をすべて解決
し、凍結粒の回収率を向上させうる凍結粒製造装置を提
供することを目的とするものである。
An object of the present invention is to provide a frozen grain manufacturing apparatus capable of solving all the above-mentioned problems in the conventional apparatus and improving the recovery rate of frozen grains.

〔問題点を解決するための手段〕[Means for solving problems]

本考案の凍結粒製造装置は、上記の目的を達成すべく、
特に、密閉断熱容器の上部に液体窒素等の冷媒を噴出す
る噴出ノズルと危険物質や有害物質を含む被凍結原料を
噴霧する噴霧ノズルとを配設すると共に、その底部に排
気口兼用の凍結粒取出口を設け、この凍結粒取出口に、
凍結粒取出口から排出される凍結粒及び冷媒ガスのすべ
てを回収する回収容器を接続し、この回収容器に、凍結
粒の通過を阻止するフィルタを介して冷媒ガスの排気経
路を接続したものである。
The frozen grain manufacturing apparatus of the present invention achieves the above-mentioned object,
In particular, a spray nozzle for spraying a refrigerant such as liquid nitrogen and a spray nozzle for spraying a frozen material containing a dangerous substance or a harmful substance are arranged on the upper part of the closed heat-insulating container, and a frozen particle also serving as an exhaust port is provided on the bottom part thereof. An outlet is provided, and at this frozen grain outlet,
A collection container that collects all frozen particles and refrigerant gas discharged from the frozen particle outlet is connected, and an exhaust path for the refrigerant gas is connected to this collection container through a filter that blocks the passage of frozen particles. is there.

〔作用〕[Action]

噴出ノズルから冷媒が噴出されると、その蒸発ガスによ
り容器内は冷気相雰囲気に保持される。また、冷媒ガス
は容器における唯一の開口部である凍結粒取出口から排
気され、容器内において取出口に向かうガス流を形成す
る。
When the refrigerant is ejected from the ejection nozzle, the vaporized gas keeps the interior of the container in a cold gas phase atmosphere. Further, the refrigerant gas is exhausted from the frozen grain outlet which is the only opening in the container, and forms a gas flow toward the outlet in the container.

そして、被凍結原料が噴霧ノズルから噴霧されると、そ
の噴霧微粒子は落下しつつ冷媒ガスと熱交換して凍結さ
れる。このとき、噴霧微粒子と冷媒ガスとは並流接触す
ることから、その接触時間が長くなり、噴霧微粒子の凍
結がより効果的に行われ、良質な微凍結粒が得られる。
Then, when the raw material to be frozen is sprayed from the spray nozzle, the sprayed fine particles fall and exchange heat with the refrigerant gas to be frozen. At this time, since the sprayed fine particles and the refrigerant gas are in parallel contact with each other, the contact time becomes longer, the sprayed fine particles are frozen more effectively, and fine frozen particles of good quality are obtained.

このようにして得られた微凍結粒は、冷媒ガスと共に取
出口から容器外に排出される。このとき、超微凍結粒も
前記ガス流に乗って冷媒ガスと共に取出口から取出され
ることになる。
The micro-frozen particles thus obtained are discharged together with the refrigerant gas from the outlet through the container. At this time, the ultra-fine frozen particles also ride on the gas flow and are taken out from the take-out port together with the refrigerant gas.

そして、凍結粒取出口から排出された凍結粒及び冷媒ガ
スは、この取出口に接続した回収容器にすべて回収さ
れ、更に、冷媒ガスは、回収容器からフィルタを通って
排気経路に排出される。このとき、凍結粒は、フィルタ
を通過し得ず、冷媒ガスと共に排気経路に排出されるこ
とはない。すなわち、回収容器に回収された冷媒ガス
は、フィルタにより凍結粒と完全に分離されて、排気経
路から排出され、危険・有害物質を含む凍結粒が冷媒ガ
スと共に回収容器外に漏れるような虞れは皆無となる。
The frozen particles and the refrigerant gas discharged from the frozen particle outlet are all collected in the recovery container connected to this outlet, and the refrigerant gas is discharged from the recovery container to the exhaust path through the filter. At this time, the frozen particles cannot pass through the filter and are not discharged to the exhaust path together with the refrigerant gas. That is, the refrigerant gas collected in the collection container is completely separated from the frozen particles by the filter and is discharged from the exhaust path, and the frozen particles containing dangerous and harmful substances may leak out of the collection container together with the refrigerant gas. Disappears.

このように、断熱容器内で製造された凍結粒はすべて取
出口から回収容器に回収されることから、凍結粒の回収
率が大幅に向上する。さらに、凍結粒は冷媒ガスと共に
回収容器に回収されるから、断熱容器から回収容器への
回収経路において凍結粒が融解接着したり詰ったりする
ようなことがなく、所定の凍結硬度を維持した状態で回
収容器に回収されることになる。
As described above, since all the frozen particles manufactured in the heat insulating container are collected in the collection container from the outlet, the recovery rate of the frozen particles is significantly improved. Further, since the frozen particles are collected together with the refrigerant gas in the collection container, the frozen particles are not melted and adhered or clogged in the collection path from the heat insulating container to the collection container, and the predetermined freeze hardness is maintained. Will be collected in a collection container.

しかも、凍結粒及び冷媒ガスのすべてが、断熱容器の一
箇所(凍結粒取出口)から取り出され且つ一箇所(回収
容器)に回収されることから、ハザード対策を一箇所に
講じておく(回収容器と排気経路との接続箇所にのみフ
ィルタを配設しておく)だけでよい。その結果、複数箇
所にハザード対策を講じておく必要がある場合に比し
て、ハザード対策が極めて容易となることは勿論、ハザ
ード対策に万全を期することができ、危険物質や有害物
質を含む凍結粒の製造を極めて安全に行うことができ
る。
Moreover, since all frozen particles and refrigerant gas are taken out from one location (frozen particle outlet) of the heat insulating container and collected in one location (collection container), take hazard countermeasures in one location (collection). It is sufficient to dispose the filter only at the connection between the container and the exhaust path). As a result, compared to the case where it is necessary to take hazard countermeasures at multiple places, it is extremely easy to take hazard countermeasures, and it is also possible to take all possible measures to prevent hazards, including hazardous substances and harmful substances. Frozen granules can be manufactured extremely safely.

〔実施例〕〔Example〕

以下、本考案の構成を第1図に示す実施例に基づいて具
体的に説明する。この実施例は、被凍結原料として菌体
含有の懸濁液を、冷媒として液体窒素を夫々使用した例
に係る。
Hereinafter, the structure of the present invention will be specifically described with reference to the embodiment shown in FIG. This example relates to an example in which a suspension containing cells is used as a raw material to be frozen and liquid nitrogen is used as a refrigerant.

第1図に示す凍結粒製造装置1において、3は密閉断熱
容器、4は断熱容器3の上部に配設された冷媒7の噴出
ノズル、5は断熱容器3の上部に配設された被凍結原料
9の噴霧ノズル、12は断熱容器4の被凍結粒取出口6に
接続された回収容器、2は取出口6から回収容器12に至
る回収経路に配設された凍結粒破砕装置、14は回収容器
12に凍結粒9b,9′bの通過を阻止するフィルタ14aを介
して接続された冷媒ガスの排気経路である。
In the frozen grain production apparatus 1 shown in FIG. 1, 3 is a closed heat-insulating container, 4 is a nozzle 7 for ejecting the refrigerant arranged on the upper part of the heat-insulating container 3, and 5 is a frozen object arranged on the upper part of the heat-insulating container 3. A spray nozzle for the raw material 9, 12 is a collection container connected to the frozen grain extraction port 6 of the heat insulating container 4, 2 is a frozen particle crushing device arranged in the collection path from the extraction port 6 to the collection container 12, and 14 is Collection container
An exhaust path for the refrigerant gas is connected to 12 through a filter 14a that blocks passage of frozen particles 9b and 9'b.

密閉断熱容器3は底部を下窄まり截頭円錐状とした横断
面形状円形のもので、底部中央に排気口兼用の凍結粒取
出口6を設けてある。容器3の形状は任意であるが、そ
の大きさは製造しようとする凍結粒径に応じて決定して
おく。この実施例では、凍結粒径を100μとして、容器
3を高さ550mm,内径200mmのものに構成してある。ま
た、取出口6の径は約10mmとした。その結果、容器3の
内圧は、凍結粒製造時、約0.2kg/cm2Gまで上昇すること
となった。
The closed heat-insulating container 3 has a circular cross-sectional shape with a frustoconical shape in which the bottom is narrowed down, and a frozen grain outlet 6 also serving as an exhaust port is provided at the center of the bottom. The shape of the container 3 is arbitrary, but its size is determined according to the frozen particle size to be manufactured. In this embodiment, the frozen particle size is 100 μ, and the container 3 is configured to have a height of 550 mm and an inner diameter of 200 mm. The diameter of the outlet 6 was set to about 10 mm. As a result, the internal pressure of the container 3 was increased to about 0.2 kg / cm 2 G during the production of frozen particles.

噴出ノズル4は容器3の上壁部に固設されたもので、冷
媒7を下方向に噴出する。冷媒7の噴出圧力は容器内圧
力に応じて設定するが、この実施例では1.0〜1.5kg/cm2
Gとした。冷媒7は噴出後ガス化されて容器3内を冷気
相雰囲気に保持し、冷媒ガス7aは取出口6から排出さ
れ、下方向のガス流を形成する。噴出ノズル4からの冷
媒噴出量は温度センサ8により制御して、容器3内の温
度を−110℃以下に保持する。なお、噴出ノズル4は、
第2図に示す如く、容器3の内壁面に添設され且つ下面
部に多数の噴出口4a…を備えた環状管でもって構成して
おいてもよい。
The jet nozzle 4 is fixed to the upper wall of the container 3 and jets the refrigerant 7 downward. The ejection pressure of the refrigerant 7 is set according to the pressure inside the container, but in this embodiment, it is 1.0 to 1.5 kg / cm 2.
G The refrigerant 7 is gasified after being jetted and holds the inside of the container 3 in a cold gas phase atmosphere, and the refrigerant gas 7a is discharged from the outlet 6 to form a downward gas flow. The amount of the refrigerant jetted from the jet nozzle 4 is controlled by the temperature sensor 8 to keep the temperature inside the container 3 at -110 ° C or lower. The ejection nozzle 4 is
As shown in FIG. 2, it may be configured by an annular pipe attached to the inner wall surface of the container 3 and provided with a large number of ejection ports 4a on its lower surface.

噴霧ノズル5は容器3の上壁部中央に固設されたもの
で、被凍結原料9を下方向に噴霧する。噴霧圧力は容器
内圧の影響を受けないように設定しておくが、この実施
例では8kg/cm2Gとした。原料の噴霧微粒子9aは冷媒ガ
ス7aと熱交換して凍結されるが、両者7a,9aは並流接触
することから、その接触時間が長くなり、噴霧微粒子9a
の凍結がより効果的に行われ、良質な微凍結粒9bが得ら
れる。かくして得られた微凍結粒9bは冷媒ガス7aと共に
取出口6から排出される。このとき、冒頭で述べた如く
して発生する超微凍結粒9b′もガス流7aに乗って取出口
6から排出される。したがって、容器3内で得られた凍
結粒9b…,9b′…はすべて一箇所6に回収され、その回
収率が向上する。
The spray nozzle 5 is fixed to the center of the upper wall of the container 3, and sprays the raw material 9 to be frozen downward. The spraying pressure is set so as not to be affected by the pressure inside the container, but in this example, it was set to 8 kg / cm 2 G. The atomized fine particles 9a of the raw material are frozen by exchanging heat with the refrigerant gas 7a, but since both 7a and 9a are in parallel flow contact, the contact time becomes longer, and the atomized fine particles 9a
Is more effectively frozen, and fine frozen particles 9b of high quality are obtained. The fine frozen particles 9b thus obtained are discharged from the outlet 6 together with the refrigerant gas 7a. At this time, the ultra-fine frozen particles 9b 'generated as described at the beginning are also discharged from the outlet 6 along with the gas flow 7a. Therefore, all the frozen particles 9b ..., 9b '... Obtained in the container 3 are collected in one place 6, and the recovery rate thereof is improved.

凍結粒破砕装置2は2段構造の噴射ガン10,11を具備し
てなる。第1噴射ガン10は取出口6に接続され、第2噴
射ガン11は回収容器12に接続されており、各噴射ガン1
0,11内には衝突盤10a,11aが配設されている。各噴射ガ
ン10,11にドライブガス13として加圧窒素ガス(3〜10k
g/cm2G)を供給すると、凍結粒9b…,9b′…は取出口6
から第1噴射ガン10内に吸引供給され、衝突盤10aに衝
突して破砕され、更に第2噴射ガン11内に加速供給され
て衝突盤11aに衝突して破砕され、その破砕粒9c…は回
収容器12に回収される。一方、冷媒ガス7aは凍結粒ない
し破砕粒と共に噴射ガン10,11を経過して回収容器12に
排出され、ドライブガスと共に回収容器12から排気され
る。このように、凍結粒ないし破砕粒と冷媒ガスとの分
離が一箇所で行うことができ、回収容器12からの排気経
路14にフィルタ14aを介装しておくことによってハザー
ド対策も極めて容易になしうる。しかも、凍結粒製造装
置1から凍結粒破砕装置2に至る凍結粒の回収経路ない
し処理経路においては、凍結粒の溶解が冷媒ガスによっ
て防止され、凍結粒が付着したり詰ったりする等の弊害
が全く生じない。
The frozen particle crushing device 2 is equipped with injection guns 10 and 11 having a two-stage structure. The first injection gun 10 is connected to the outlet 6, the second injection gun 11 is connected to the recovery container 12, and each injection gun 1
Collision plates 10a and 11a are arranged in the 0 and 11. Pressurized nitrogen gas (3-10k) as drive gas 13 for each injection gun 10,11
g / cm 2 G), the frozen particles 9b ..., 9b '...
Is sucked and supplied into the first injection gun 10 and collides with the collision plate 10a to be crushed, and further acceleratedly supplied into the second injection gun 11 and collides with the collision plate 11a and is crushed, and the crushed particles 9c ... It is collected in the collection container 12. On the other hand, the refrigerant gas 7a passes through the injection guns 10 and 11 together with the frozen particles or the crushed particles and is discharged into the recovery container 12, and is exhausted from the recovery container 12 together with the drive gas. In this way, the frozen particles or crushed particles and the refrigerant gas can be separated from each other at one place, and by installing the filter 14a in the exhaust path 14 from the collection container 12, it is possible to easily take a hazard countermeasure. sell. In addition, in the frozen particle recovery path or the processing path from the frozen particle manufacturing apparatus 1 to the frozen particle crushing apparatus 2, the frozen particles are prevented from being melted by the refrigerant gas, and the frozen particles may be stuck or clogged. It does not occur at all.

なお、被凍結原料及び冷媒は、上記実施例で使用したも
のに限定されないことは勿論であり、また凍結粒製造装
置からの凍結粒の回収手段ないし処理手段並びに冷媒ガ
スの排気手段も、本考案の基本原理を逸脱しない範囲に
おいて上記実施例に限定されない。
It should be noted that the material to be frozen and the refrigerant are not limited to those used in the above embodiment, and the means for collecting or treating the frozen particles from the apparatus for producing frozen particles and the means for exhausting the refrigerant gas are also the present invention. The present invention is not limited to the above-described embodiment as long as it does not deviate from the basic principle.

〔考案の効果〕[Effect of device]

以上の説明から容易に理解されるように、本考案の凍結
粒製造装置は、密閉断熱容器内で得られる凍結粒を冷媒
ガスと共に一個所から取出すようにしたものであるか
ら、冒頭で述べた如き問題をすべて解決して、凍結粒の
回収率を向上させうるものである。しかも、凍結粒及び
冷媒ガスのすべてを、断熱容器の一箇所(凍結粒取出
口)から取り出し、一箇所(回収容器)に回収するよう
に構成したから、ハザード対策を凍結粒,冷媒ガスの回
収経路,排出経路上の一箇所に講じておく(回収容器と
排気経路との接続箇所にのみフィルタを配設しておく)
だけでよい。したがって、凍結粒や冷媒ガスの排出経路
ないし回収経路が多岐に亘るため、複数箇所にハザード
対策を講じておく必要があるものと異なって、ハザード
対策が極めて容易となることは勿論、ハザード対策に万
全を期することができ、危険物質や有害物質を含む凍結
粒の製造を極めて安全に行うことができる。
As will be easily understood from the above description, the frozen grain manufacturing apparatus of the present invention is designed to take out the frozen grains obtained in the closed heat-insulating container together with the refrigerant gas from one place, and therefore, the above description was given at the beginning. It is possible to solve all such problems and improve the recovery rate of frozen particles. In addition, all frozen particles and refrigerant gas are taken out from one location (frozen particle outlet) of the heat insulation container and collected in one location (recovery container). Take it at one place on the route and discharge route (provide the filter only at the connection point between the collection container and the exhaust route)
Just enough. Therefore, since there are various discharge routes and recovery routes for frozen particles and refrigerant gas, it is very easy to take measures against hazards, unlike those requiring measures to be taken at multiple places. It is possible to make every effort, and it is possible to manufacture frozen particles containing dangerous substances and harmful substances extremely safely.

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

第1図は本考案に係る凍結粒製造装置の一実施例を示す
概略の縦断側面図、第2図はその変形例を示す概略の縦
断側面図である。 1……凍結粒製造装置、3……密閉断熱容器、4……噴
出ノズル、5……噴霧ノズル、6……凍結粒取出口、7
……冷媒、9……被凍結原料、9b,9b′……凍結粒、12
……回収容器、14……排気経路、14a……フィルタ。
FIG. 1 is a schematic vertical sectional side view showing an embodiment of a frozen grain manufacturing apparatus according to the present invention, and FIG. 2 is a schematic vertical sectional side view showing a modified example thereof. 1 ... Frozen particle manufacturing device, 3 ... closed heat insulation container, 4 ... ejection nozzle, 5 ... spray nozzle, 6 ... frozen particle outlet, 7
…… Refrigerant, 9 …… Frozen raw material, 9b, 9b ′ …… Frozen grain, 12
…… Collection container, 14 …… Exhaust path, 14a …… Filter.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】密閉断熱容器の上部に液体窒素等の冷媒を
噴出する噴出ノズルと危険物質や有害物質を含む被凍結
原料を噴霧する噴霧ノズルとを配設すると共に、その底
部に排気口兼用の凍結粒取出口を設け、この凍結粒取出
口に、凍結粒取出口から排出される凍結粒及び冷媒ガス
のすべてを回収する回収容器を接続し、この回収容器
に、凍結粒の通過を阻止するフィルタを介して冷媒ガス
の排気経路を接続してあることを特徴とする凍結粒製造
装置。
1. A hermetically sealed container is provided with a jet nozzle for jetting a refrigerant such as liquid nitrogen and a spray nozzle for spraying a material to be frozen containing a dangerous substance or a harmful substance on the upper part of the hermetically sealed container, and also serves as an exhaust port at the bottom thereof. Is equipped with a frozen grain outlet, and a collection container for collecting all of the frozen grains and refrigerant gas discharged from the frozen grain outlet is connected to this frozen grain outlet, and the frozen grain is prevented from passing through this collection container. An apparatus for producing frozen particles, characterized in that an exhaust path for the refrigerant gas is connected via a filter.
JP1987184616U 1987-12-03 1987-12-03 Frozen grain production equipment Expired - Lifetime JPH0643660Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1987184616U JPH0643660Y2 (en) 1987-12-03 1987-12-03 Frozen grain production equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1987184616U JPH0643660Y2 (en) 1987-12-03 1987-12-03 Frozen grain production equipment

Publications (2)

Publication Number Publication Date
JPH0188365U JPH0188365U (en) 1989-06-12
JPH0643660Y2 true JPH0643660Y2 (en) 1994-11-14

Family

ID=31475964

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1987184616U Expired - Lifetime JPH0643660Y2 (en) 1987-12-03 1987-12-03 Frozen grain production equipment

Country Status (1)

Country Link
JP (1) JPH0643660Y2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007511728A (en) * 2003-11-13 2007-05-10 ザ・ビーオーシー・グループ・ピーエルシー Liquid cooling

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2618104B2 (en) * 1991-03-25 1997-06-11 三菱電機株式会社 Apparatus and method for producing ultrafine frozen particles

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007511728A (en) * 2003-11-13 2007-05-10 ザ・ビーオーシー・グループ・ピーエルシー Liquid cooling

Also Published As

Publication number Publication date
JPH0188365U (en) 1989-06-12

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