JPH0350472A - Frozen particle manufacturing device - Google Patents
Frozen particle manufacturing deviceInfo
- Publication number
- JPH0350472A JPH0350472A JP18323389A JP18323389A JPH0350472A JP H0350472 A JPH0350472 A JP H0350472A JP 18323389 A JP18323389 A JP 18323389A JP 18323389 A JP18323389 A JP 18323389A JP H0350472 A JPH0350472 A JP H0350472A
- Authority
- JP
- Japan
- Prior art keywords
- container
- gas
- frozen
- partition plate
- particles
- 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
Links
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
この発明は、ブラスト、クリーニング等の表面処理用の
砥粒、研磨材等として好適に用いる氷粒等の凍結粒を製
造するための装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an apparatus for producing frozen grains such as ice grains suitable for use as abrasive grains, abrasives, etc. for surface treatments such as blasting and cleaning. It is something.
第4図は例えば特開昭63−91470号公報に開示さ
れた従来の凍結粒製造装置を示す縦断面構成図である。FIG. 4 is a vertical cross-sectional configuration diagram showing a conventional frozen grain manufacturing apparatus disclosed in, for example, Japanese Patent Application Laid-Open No. 63-91470.
図において、(1〉は凍結粒製造のための断熱性容器、
(la)は冷気排出口(2)は凍結粒回収手段、(3)
は噴霧手段、(4)は冷媒蒸発ガス発生手段、〈5)は
網状体、(6)は凍結粒取出管、(6a)はバルブ、(
7a)は冷気相領域、(7b)は冷媒蒸発ガス発生領域
、(8)は噴霧器、(8a)はノズル、(9)は原料供
給管、Qlは噴霧ガス導入管、αυは冷媒供給管、0は
冷媒、(l2a)は冷媒蒸発ガス、0はパブリング管、
(14a)は被凍結原料の噴霧粒子、(14b)は凍結
粒である。In the figure, (1> is an insulated container for producing frozen grains,
(la) is a cold air outlet (2) is a means for collecting frozen grains, (3)
(4) is a refrigerant evaporative gas generating means, (5) is a mesh body, (6) is a frozen particle extraction pipe, (6a) is a valve, (
7a) is a cold gas phase region, (7b) is a refrigerant evaporative gas generation region, (8) is a sprayer, (8a) is a nozzle, (9) is a raw material supply pipe, Ql is a spray gas introduction pipe, αυ is a refrigerant supply pipe, 0 is refrigerant, (l2a) is refrigerant evaporation gas, 0 is pubbling pipe,
(14a) is the sprayed particle of the raw material to be frozen, and (14b) is the frozen particle.
次に動作について説明する。容器(1)は周壁の上端部
に冷気排出口(la)を有する断熱容器に構成され、凍
結粒回収手段(2)は下窄まり角錐状体(5)とその最
下端部たる中心部に垂設した凍結粒取出管(6)とを備
えている。網状体(5)は容器(1〉の内周壁に取り付
けられ、容器(1)内を上位の冷気相領域(7a)と下
位の冷媒蒸発ガス発生領域(7b)とに区画している。Next, the operation will be explained. The container (1) is constructed as an insulated container having a cold air outlet (la) at the upper end of the peripheral wall, and the frozen particle collection means (2) is connected to a pyramid-shaped body (5) converging at the bottom and a center portion at its lowermost end. It is equipped with a vertically installed frozen particle extraction pipe (6). The mesh body (5) is attached to the inner circumferential wall of the container (1>) and divides the inside of the container (1) into an upper cold gas phase region (7a) and a lower refrigerant evaporative gas generation region (7b).
網状体(5)は耐低温性を有し、且つ冷媒蒸発ガスのみ
を経過させる程度のメシュ度の金網である。噴霧手段(
3〉は容器(1)の上壁中央部位に噴霧器(8)を設け
ると共に、この噴霧器(8)に被凍結原料、例えば水を
供給する原料供給管(9〉及び適宜に加圧且つ冷却した
窒素ガス等の噴霧ガスを導入する噴霧ガス導入管OOを
接続してなり、被凍結原料たる水を噴霧ガスの圧力によ
って噴霧器(8)の先端のノズル(8a)から下方に霧
状に噴出するものである。The mesh body (5) is a wire mesh that is resistant to low temperatures and has a mesh degree that allows only evaporated refrigerant gas to pass through. Spraying means (
3> is provided with a sprayer (8) at the center of the upper wall of the container (1), and a raw material supply pipe (9>) that supplies the raw material to be frozen, such as water, to the sprayer (8), and a material supply pipe (9>) that is pressurized and cooled as appropriate. A spray gas introduction pipe OO is connected to introduce a spray gas such as nitrogen gas, and water, which is the raw material to be frozen, is sprayed downward in the form of a mist from the nozzle (8a) at the tip of the sprayer (8) by the pressure of the spray gas. It is something.
冷媒蒸発ガス発生手段(4)は冷媒蒸発ガス発生領域(
7b)に冷媒供給管Ql)から所定量の冷媒、例えば液
体窒素0を供給収容し、この冷媒(自)中にパブリング
管0から窒素ガス、アルゴンガス又は乾燥空気等のパブ
リング用ガスを注入することによって、冷媒蒸発ガス(
12a)を発生させるようにする。The refrigerant evaporative gas generation means (4) has a refrigerant evaporative gas generation area (
7b) is supplied with a predetermined amount of refrigerant, for example, liquid nitrogen 0, from the refrigerant supply pipe Ql), and a pubbling gas such as nitrogen gas, argon gas, or dry air is injected into this refrigerant (self) from the pubbling pipe 0. By this, refrigerant evaporation gas (
12a).
このように構成した凍結粒製造装置にあっては、冷媒蒸
発ガス(12a)は冷媒蒸発ガス発生領域(7b)から
網状体(5)を通過して冷気相領域(7a)に至り、該
領域(7a)を冷気排出口(la)方向に上昇する。In the frozen particle manufacturing apparatus configured in this way, the refrigerant evaporative gas (12a) passes through the reticulated body (5) from the refrigerant evaporative gas generation region (7b) to reach the cold gas phase region (7a), and (7a) is raised toward the cold air outlet (la).
すなわち、冷媒蒸発ガス(12a)は被凍結原料の噴霧
粒子つまり霧状の水滴(14a)と逐次熱交換すること
によって密度差を生じながら冷気排出口(1a)方向に
徐々に上昇する。一方、水滴(14a)は冷気相領域(
7a)を自然落下し、この間において、上昇してくる冷
媒蒸発ガス(12a)と向流接触して徐々に熱交換が進
んで凍結し、その凍結粒たる氷粒( 14b )は網状
体(5)上に落下し、回収される。That is, the refrigerant evaporated gas (12a) gradually rises toward the cold air outlet (1a) while generating a density difference by successively exchanging heat with spray particles of the material to be frozen, that is, atomized water droplets (14a). On the other hand, the water droplet (14a) is in the cold gas phase region (
During this time, the ice particles (14b) fall into countercurrent contact with the rising evaporated refrigerant gas (12a), gradually proceeding with heat exchange, and freeze. ) and is collected.
従来の凍結粒製造装置は以上のように構或されているの
で、凍結粒の製造は冷媒蒸発ガスと噴霧粒子との向流接
触による熱交換による凍結によって行なっている。その
ため、低温の凍結粒を得るためや、十分な熱交換を行な
い冷媒蒸発ガスの熱交換効率を高めるためには、向流接
触する時間あるいは距離を長く設定する必要があり、そ
のために断熱性容器αυを縦方向に長くすることになり
、製造装置そのものが大きくなるなどの問題点があった
。Since the conventional frozen grain production apparatus is constructed as described above, frozen grains are produced by freezing through heat exchange through countercurrent contact between the evaporated refrigerant gas and the sprayed particles. Therefore, in order to obtain low-temperature frozen particles or to perform sufficient heat exchange and increase the heat exchange efficiency of refrigerant evaporation gas, it is necessary to set the time or distance of countercurrent contact to be long. This resulted in problems such as increasing the length of αυ in the vertical direction, making the manufacturing equipment itself larger.
この発明は上記のような問題点を解消するためになされ
たもので、冷媒蒸発ガスの冷却熱交換効率を高めるとと
もに、容器(1)の高さを低くすることができ、小型化
がはかれる凍結粒製造装置を得ることを目的とする。This invention was made in order to solve the above-mentioned problems, and it is possible to improve the efficiency of cooling heat exchange of refrigerant evaporation gas, reduce the height of the container (1), and reduce the size of the freezing device. The purpose is to obtain a grain manufacturing device.
この発明に係る凍結粒製造装置は容器内に、下降する被
凍結原料の噴霧粒子と上昇する冷媒蒸発ガスをスパイラ
ル状あるいはジグザグ状に流動させ向流接触させる仕切
り板を設けたものである。The frozen granule manufacturing apparatus according to the present invention is provided with a partition plate in a container to cause the descending spray particles of the raw material to be frozen and the ascending evaporative refrigerant gas to flow in a spiral or zigzag manner and come into countercurrent contact.
この発明における凍結粒製造装置は容器内に装着された
スパイラル状あるいはジグザグ状の仕切り板により、冷
媒蒸発ガスと噴霧粒子との向流接触する時間を十分にと
ることにより、冷媒蒸発ガスによる冷却熱交換効率を高
め、かつ、十分低温の凍結粒を製造する。The frozen particle production apparatus of this invention uses a spiral or zigzag partition installed in the container to allow sufficient time for countercurrent contact between the evaporated refrigerant gas and the spray particles, thereby generating heat generated by the evaporated refrigerant gas. To improve exchange efficiency and produce frozen grains at a sufficiently low temperature.
以下、この発明の一実施例を図について説明する。第1
図において、(自)は容器(1)の内周部に取り付けら
れたスパイラル状の仕切り板である。仕切り板0はステ
ンレス鋼等の薄板で構成され、スパイラル状に所定の巻
数をもつ。また仕切り板αQに噴霧粒子の付着が問題に
なるような場合には仕切り板(ト)の表面にぬれ性の悪
い高分子材料(例えばテフロン樹脂等)をコーテング(
図示せず)する。An embodiment of the present invention will be described below with reference to the drawings. 1st
In the figure, (self) is a spiral partition plate attached to the inner circumference of the container (1). The partition plate 0 is made of a thin plate made of stainless steel or the like, and has a predetermined number of spiral turns. In addition, if adhesion of spray particles to the partition plate αQ becomes a problem, coat the surface of the partition plate (G) with a polymeric material with poor wettability (for example, Teflon resin, etc.).
(not shown).
このように構成した凍結粒製造装置にあっては、冷媒蒸
発ガス(12a)は冷媒蒸発ガス発生領域(7b)から
網状体(5〉を通過し、通過した冷媒蒸発ガス(12a
)は、スパイラル状の仕切り板(自)があるため、この
仕切り板a!9に沿って旋回しながら冷気排出口(la
)方向に徐々に上昇する。一方、被凍結原料たる水の噴
霧粒子(l4a)は噴霧器(8)の先端のノズル(8a
)から下方に霧状に噴出する。この噴霧粒子(14a)
もスパイラル状の仕切り板Q篩に沿って旋回しながら自
然落下してゆく。In the frozen particle production apparatus configured in this way, the refrigerant evaporative gas (12a) passes through the reticulated body (5>) from the refrigerant evaporative gas generation region (7b), and the refrigerant evaporative gas (12a) that has passed through the refrigerant evaporative gas (12a) passes through the reticulated body (5>).
) has a spiral partition plate (self), so this partition plate a! While rotating along 9, open the cold air outlet (la
) gradually rises in the direction of On the other hand, the spray particles (l4a) of water, which is the raw material to be frozen, are sprayed through the nozzle (8a) at the tip of the sprayer (8).
) is ejected downward in the form of mist. This spray particle (14a)
The particles also fall naturally while rotating along the spiral partition plate Q sieve.
このような動作によって、落下する噴霧粒子、即ち水滴
(14a)と上昇してくる冷媒蒸発ガス(12a)はス
パイラル状の仕切り板(ト)の空間に沿って流動し、互
に向流接触して徐々に熱交換が進んで、水滴(14a)
は凍結する。その凍結粒だろ水粒(14a)は最終的に
網状体(5)上に落下し、回収される。上昇する冷媒蒸
発ガス(12a)と落下する水滴(14a)はスパイラ
ル状の仕切り板(ト)に沿って移動するため、従来例の
直接上昇・落下する動作と異なり、互に向流接触する時
間さらには距離が長くなるため、十分な熱交換が行なわ
れ、冷媒蒸発ガスによる冷却熱交換効率が高まり、従来
例より低温の凍結粒が得られるとともに、容器(1)の
小型化が図れるといった効果が得られる。Due to this operation, the falling spray particles, that is, water droplets (14a) and the rising refrigerant evaporation gas (12a) flow along the space of the spiral partition plate (G), and come into countercurrent contact with each other. As the heat exchange gradually progresses, water droplets (14a)
freezes. The frozen water particles (14a) eventually fall onto the net-like body (5) and are collected. Since the rising evaporated refrigerant gas (12a) and the falling water droplets (14a) move along the spiral partition plate (G), unlike the direct rising and falling motion of the conventional example, the time for countercurrent contact with each other is reduced. Furthermore, since the distance is longer, sufficient heat exchange takes place, increasing the cooling heat exchange efficiency by the refrigerant evaporation gas, producing frozen particles at a lower temperature than in the conventional case, and making it possible to downsize the container (1). is obtained.
なお、上記実施例では噴霧器(8)のノズル(8a)は
下方に向けた場合について示したが、第2図に示すよに
ノズル(8a)をスパイラル状の仕切り板0!9に沿っ
て上昇してくる冷媒蒸発ガス(l2a)に対向するよう
に角度をもたせれば、水滴(14a)の落下方向が仕切
り板(ハ)に沿う方向となり、互いの向流接触の度合い
が向上する。In the above embodiment, the nozzle (8a) of the sprayer (8) is directed downward, but as shown in FIG. If the water droplets (14a) are angled so as to face the incoming refrigerant evaporated gas (l2a), the falling direction of the water droplets (14a) will be along the partition plate (c), and the degree of countercurrent contact with each other will be improved.
また、上記実施例ではスパイラル状仕切り板(ト)は固
定した場合について示したが、仕切り板(自)をモータ
(図示せず)によって回転駆動しても、さらに冷却熱交
換効率の向上が図れる。In addition, although the above embodiment shows the case where the spiral partition plate (T) is fixed, the cooling heat exchange efficiency can be further improved even if the partition plate (T) is rotationally driven by a motor (not shown). .
また、上記各実施例において仕切り板0はスパイラル状
に設けたが、第3図に示すように、容器(1〉の内壁に
交互に仕切り板顛を設け、冷媒蒸発ガス(12a)及び
噴霧粒子(14a)がジグザグ状に流動するようにして
もよく、上記各実施例と同様、向流接触の時間及び距離
を長くすることができる。Furthermore, although the partition plates 0 were provided in a spiral shape in each of the above embodiments, as shown in FIG. (14a) may be made to flow in a zigzag pattern, and as in each of the above embodiments, the time and distance of countercurrent contact can be lengthened.
以上のように、この発明によれば容器内に、下降する被
凍結原料の噴霧粒子、と上昇する冷媒蒸発ガスをスパイ
ラル状、あるいはジグザグ状に流動させ向流接触させる
仕切り板を設けたので、噴霧粒子と冷媒蒸発ガスとの向
流接触の時間と距離が長くなり、冷却熱交換効率が高く
なると共に、容器の小型化が図れる効果がある。As described above, according to the present invention, a partition plate is provided in the container to cause the descending spray particles of the raw material to be frozen and the ascending refrigerant evaporated gas to flow in a spiral or zigzag pattern and come into countercurrent contact. The time and distance of countercurrent contact between the spray particles and the evaporated refrigerant gas are increased, the cooling heat exchange efficiency is increased, and the container can be made smaller.
第l図はこの発明の一実施例による凍結粒製造装置の内
部を示す斜視構成図、第2図はこの発明の他の実施例に
よる凍結粒製造装置の内部を示す斜視構成図、第3図は
この発明の他の実施例による凍結粒製造装置を示す断面
構成図、及び第4図は従来の凍結粒製造装置を示す断面
構成図である。
(l)・・・断熱性容器、(3〉・・・噴霧手段、(8
)・・・噴霧器、(9)・・・原料供給管、Ql)・・
・冷媒供給管、0・・・冷媒、(12a)・・・蒸発ガ
ス、(l4a)・・・噴霧粒子、(14b)・・・凍結
粒、
(至)・・・仕切り板
なお、
図中、
同一符号は同一又は相当部分を示
す。
代
理
人
大
岩
増
雄
第1図
1:断熱性容器
3:噴霧手段
8:噴霧器
9:原料供給管
11:冷媒供給管
12:冷媒
12a:蒸発ガス
14a:噴霧粒子
14b:凍結粒
15:仕切り板
第2図
第3図FIG. 1 is a perspective configuration diagram showing the inside of a frozen grain production apparatus according to an embodiment of the present invention, FIG. 2 is a perspective construction diagram showing the inside of a frozen grain production apparatus according to another embodiment of the invention, and FIG. 3 FIG. 4 is a cross-sectional configuration diagram showing a frozen grain manufacturing apparatus according to another embodiment of the present invention, and FIG. 4 is a cross-sectional configuration diagram showing a conventional frozen grain manufacturing apparatus. (l)...Insulating container, (3>...Spraying means, (8
)...Sprayer, (9)...Raw material supply pipe, Ql)...
- Refrigerant supply pipe, 0... Refrigerant, (12a)... Evaporated gas, (l4a)... Spray particles, (14b)... Frozen particles, (To)... Partition plate. , Same symbols indicate the same or equivalent parts. Agent Masuo Oiwa Figure 1: Insulating container 3: Spraying means 8: Sprayer 9: Raw material supply pipe 11: Refrigerant supply pipe 12: Refrigerant 12a: Evaporated gas 14a: Spray particles 14b: Frozen particles 15: Partition plate 2 Figure 3
Claims (1)
を供給する第1供給手段、被凍結原料の噴霧粒子を容器
上部より上記容器内に供給する第2供給手段及び上記容
器内に設けられ、下降する上記噴霧粒子と上昇する上記
蒸発ガスをスパイラル状又はジグザグ状に流動させ向流
接触させる仕切り板を備えた凍結粒製造装置。an insulating container, a first supply means for supplying evaporated gas of a refrigerant into the container from the lower part of the container, a second supply means for supplying atomized particles of the raw material to be frozen into the container from the upper part of the container, and a second supply means provided in the container. . A frozen particle production apparatus comprising a partition plate that causes the descending spray particles and the ascending evaporative gas to flow in a spiral or zigzag pattern and come into countercurrent contact with each other.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18323389A JPH0350472A (en) | 1989-07-14 | 1989-07-14 | Frozen particle manufacturing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18323389A JPH0350472A (en) | 1989-07-14 | 1989-07-14 | Frozen particle manufacturing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0350472A true JPH0350472A (en) | 1991-03-05 |
Family
ID=16132109
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP18323389A Pending JPH0350472A (en) | 1989-07-14 | 1989-07-14 | Frozen particle manufacturing device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0350472A (en) |
-
1989
- 1989-07-14 JP JP18323389A patent/JPH0350472A/en active Pending
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