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JPS5911526B2 - Dry ice manufacturing method - Google Patents
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JPS5911526B2 - Dry ice manufacturing method - Google Patents

Dry ice manufacturing method

Info

Publication number
JPS5911526B2
JPS5911526B2 JP56133319A JP13331981A JPS5911526B2 JP S5911526 B2 JPS5911526 B2 JP S5911526B2 JP 56133319 A JP56133319 A JP 56133319A JP 13331981 A JP13331981 A JP 13331981A JP S5911526 B2 JPS5911526 B2 JP S5911526B2
Authority
JP
Japan
Prior art keywords
dry ice
carbon dioxide
container
liquefied carbon
ice
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
Application number
JP56133319A
Other languages
Japanese (ja)
Other versions
JPS5836912A (en
Inventor
英明 山田
政治 渋谷
薫 越部
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.)
EKIKA CARBON DIOXIDE CO
Original Assignee
EKIKA CARBON DIOXIDE CO
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 EKIKA CARBON DIOXIDE CO filed Critical EKIKA CARBON DIOXIDE CO
Priority to JP56133319A priority Critical patent/JPS5911526B2/en
Publication of JPS5836912A publication Critical patent/JPS5836912A/en
Publication of JPS5911526B2 publication Critical patent/JPS5911526B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は、市販の低水分量の液化炭酸ガス(以下LCO
2と称す)からドライアイスを製造するにあたり、該L
CO2を加湿する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention utilizes commercially available low water content liquefied carbon dioxide (hereinafter referred to as LCO).
2) in producing dry ice from L.
This invention relates to a method for humidifying CO2.

近年、小型のドライアイス製造機により0.2〜10k
g程度の小さなドライアイスを消費地で製造することが
普及しばしめでいるが、原料であるLaO2は溶接、清
涼飲料等にも多量に使用されているものであり、その露
点温度は一40°C以下と水分量が非常に低い。
In recent years, small dry ice making machines have been used to produce 0.2~10k
It is becoming increasingly common to produce dry ice as small as 1.5 oz. in the region where it is consumed, but the raw material, LaO2, is used in large quantities for welding, soft drinks, etc., and its dew point temperature is -40°C. Water content is very low.

液化炭酸ガスからドライアイスを製造する場合、適度な
水分(露点温度で一15°Cから一30°C1第一表参
照)を含有していないと、ドライアイス成形後、時間の
経過とともにその内部がざら目状で脆くなってくるので
、このようなドライアイスは劣化したドライアイスとし
てきられれているが、このことは一般に知られている事
実である。
When producing dry ice from liquefied carbon dioxide, if it does not contain an appropriate amount of moisture (dew point temperature: -15°C to -130°C, see Table 1), the inside of the dry ice will deteriorate over time after it is formed. Since the dry ice becomes rough and brittle, this type of dry ice is considered to be degraded dry ice, and this is a generally known fact.

一方、工場で大型のドライアイスを大量に生産するドラ
イアイスメーカーは、その原料の液化炭酸ガス中に含ま
れる水分量を適度に調整してドライアイスを製造するこ
とによりその劣化を防止している。
On the other hand, dry ice manufacturers that produce large quantities of large dry ice at their factories prevent deterioration by adjusting the amount of moisture contained in the raw material, liquefied carbon dioxide, to an appropriate level. .

したがって、消費地で低温容器または貯槽に貯えられた
LaO2よりドライアイスを製造する場合、適当量の水
分を加えることが考えられるが、LaO2の圧力が20
kg/cI!前後と高く、またその液温か一20°C程
度と低いため、実際には加湿することはなかなか困難で
あった。
Therefore, when producing dry ice from LaO2 stored in a low-temperature container or storage tank at a consumption site, it is conceivable to add an appropriate amount of moisture, but if the pressure of LaO2 is 20
kg/cI! Since the temperature of the liquid is high, and the temperature of the liquid is as low as -20°C, it is actually quite difficult to humidify it.

しかし、前述したように堅い緻密な劣化し難いドライア
イスを製造するためには、氷の蒸気圧を利用して低温の
LaO2の液温(−20°C前後)附近の露点温度にL
aO2を加湿すれば、その目的が達成されることに発明
者は着目し、LaO2を簡単にしかも連続的に加湿して
ドライアイスを製造する方法を見出したのである。
However, as mentioned above, in order to produce dry ice that is hard, dense, and resistant to deterioration, it is necessary to use the vapor pressure of ice to maintain the dew point temperature of the low-temperature LaO2 liquid (around -20°C).
The inventor noticed that the objective could be achieved by humidifying aO2, and discovered a method for manufacturing dry ice by simply and continuously humidifying LaO2.

以下図1および実施例により詳細に説明する。This will be explained in detail below with reference to FIG. 1 and examples.

LaO2が低温で充填されている低温容器または貯槽1
とドライアイス製造機2を結ぶ配管の途中に耐圧性の加
湿容器3を設ける。
Cryogenic container or storage tank 1 filled with LaO2 at low temperature
A pressure-resistant humidifying container 3 is provided in the middle of the piping connecting the dry ice manufacturing machine 2 and the dry ice manufacturing machine 2.

該容器内のL CO7の入・出口部に適宜の網等を配置
して充填物の氷または多孔質物質がLaO2の通過によ
り移動するこ志を防止する。
Appropriate nets or the like are placed at the inlet and outlet of LCO7 in the container to prevent the ice or porous material in the filling from moving due to the passage of LaO2.

また必要ならば、該容器の上下に注水弁4および排水弁
5等を設置しても良い。
Further, if necessary, a water injection valve 4, a drain valve 5, etc. may be installed above and below the container.

さらにこのような加湿容器を1個以上設ければ、その交
互の使用により長時間ドライアイスが製造できる利点が
ある。
Furthermore, if one or more such humidifying containers are provided, there is an advantage that dry ice can be produced for a long time by alternately using them.

この加湿容器の中に氷の砕片を充填し、低温容器または
貯槽1の弁を開いて低温のLCO2をゆっくり通すと、
氷はLCO2により冷却され、LCO2はその液温(−
20°C前後)に対する水分飽和点近くの露点温度にま
で加湿されるから、この加湿LCO2でドライアイスを
製造することにより所要の品質のドライアイスが得られ
る。
Fill this humidifying container with crushed ice, open the valve of the cryogenic container or storage tank 1, and slowly let low-temperature LCO2 pass through.
Ice is cooled by LCO2, and LCO2 is cooled by its liquid temperature (-
Since the dry ice is humidified to a dew point temperature close to the moisture saturation point (approximately 20° C.), dry ice of the required quality can be obtained by producing dry ice with this humidified LCO2.

また、前記加湿容器3中に水分保持性の大きな天然、合
成もしくは金属製等の多孔質物質を収納し、これに水を
含ませ、次いで前記同様に低温のLCO2を通すことに
より水は急速にLCO2と同温度の氷となり前記同様に
使用できるので、加湿されたL Co□をドライアイス
製造機に供給できる。
In addition, a porous material such as natural, synthetic, or metal having a high water retention property is housed in the humidifying container 3, water is impregnated with the material, and the water is rapidly removed by passing low-temperature LCO2 in the same manner as above. Since it becomes ice at the same temperature as LCO2 and can be used in the same manner as described above, humidified LCo□ can be supplied to a dry ice manufacturing machine.

実施例 1 図1のフローシートに示すとおり、内径80朋長さ32
0關の円筒形の耐圧性の加湿容器2の中に氷の砕片を入
れておき、LCO2低温容器から低温のLCO2(圧力
19に9/c111、液温−21℃、露点温度−60°
C5すなわち水分含量0.0004重量%)を毎分1.
6 kgの流量で通し、ドライアイス製造機1(液化炭
酸株式会社製ドライアイスMD−058型)でドライア
イスを製造した。
Example 1 As shown in the flow sheet of Figure 1, the inner diameter is 80 mm and the length is 32 mm.
A piece of crushed ice is placed in a cylindrical pressure-resistant humidifying container 2 of 0°C, and low-temperature LCO2 (pressure 19 to 9/c111, liquid temperature -21°C, dew point temperature -60°
C5 (moisture content 0.0004% by weight) per minute.
Dry ice was manufactured using dry ice manufacturing machine 1 (Dry Ice MD-058 model manufactured by Liquefied Carbonate Co., Ltd.) by passing through the mixture at a flow rate of 6 kg.

このとき液化炭酸ガスはドライアイス製造機の入口で露
点温度−26°C1すなわち0.0231重量%に加湿
されており、この液化炭酸ガスで製造したドライアイス
は、製造直後表面にツヤがあり、その密度は1.5に9
/lであった。
At this time, the liquefied carbon dioxide gas is humidified at the entrance of the dry ice manufacturing machine to a dew point temperature of -26°C1, or 0.0231% by weight, and the dry ice manufactured with this liquefied carbon dioxide gas has a glossy surface immediately after manufacturing. Its density is 1.5 to 9
/l.

さらに48時間経過後もざら目状の部分ができなかった
Furthermore, no rough areas were formed even after 48 hours had passed.

すなわちドライアイスの劣化は認められなかった。In other words, no deterioration of the dry ice was observed.

実施例 2 実施例1の加湿容器に焼結金属の大小の固まりを密に入
れ、水をかけて前記焼結金属塊に水分を含ませ、余分な
水分は低部のバルブより排出した。
Example 2 Large and small chunks of sintered metal were placed tightly in the humidifying container of Example 1, water was poured over the container to moisten the sintered metal chunks, and excess moisture was discharged through a valve at the bottom.

次にLCO2容器から最初きわめてゆっくりとLCO2
を加湿容器内に通して水分を氷となしたのち、実施例1
と同じ操作条件でドライアイスを製造したがドライアイ
スの品質は実施例1と同じであった。
Next, the LCO2 is collected very slowly at first from the LCO2 container.
Example 1
Dry ice was produced under the same operating conditions as in Example 1, but the quality of the dry ice was the same as in Example 1.

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

第1図はこの発明の実施例1および実施例2に共通する
フローシートである。 1は液化炭酸ガスの低温容器または貯槽、2はドライア
イス製造機、3は耐圧性の加湿容器、4は注水弁、5は
排水弁。
FIG. 1 is a flow sheet common to Example 1 and Example 2 of the present invention. 1 is a low temperature container or storage tank for liquefied carbon dioxide gas, 2 is a dry ice making machine, 3 is a pressure-resistant humidifying container, 4 is a water injection valve, and 5 is a drain valve.

Claims (1)

【特許請求の範囲】 1 ドライアイスを製造する際に液化炭酸ガス低温容器
またはその貯槽とドライアイス製造機の間に1基以上の
水分の加湿容器を設置し、この中に氷の砕片を詰めて低
水分量の低温液化炭酸ガスを通すことにより、液化炭酸
ガスを加湿することを特徴とするドライアイスの製造法
。 2 ドライアイスを製造する際に液化炭酸ガス低温容器
またはその貯槽とドライアイス製造機の間に1基以上の
水分の加湿容器を設置し、この中に多孔質物質を充填し
、これに水を吸収させてから低水分量の低温液化炭酸ガ
スを通して氷を生成させ、この中に前記液化炭酸ガスを
通過させることにより該液化炭酸ガスを加湿することを
特徴とするドライアイスの製造法。
[Scope of Claims] 1. When manufacturing dry ice, one or more humidifying containers are installed between a liquefied carbon dioxide gas low temperature container or its storage tank and a dry ice manufacturing machine, and crushed ice pieces are packed in this container. A method for producing dry ice characterized by humidifying liquefied carbon dioxide gas by passing low-temperature liquefied carbon dioxide gas with a low moisture content through the ice. 2. When manufacturing dry ice, one or more humidifying containers are installed between the liquefied carbon dioxide gas low-temperature container or its storage tank and the dry ice manufacturing machine, and a porous material is filled in the container, and water is poured into the container. 1. A method for producing dry ice, which comprises absorbing and then passing low-temperature liquefied carbon dioxide gas with a low water content to generate ice, and humidifying the liquefied carbon dioxide gas by passing the liquefied carbon dioxide gas through the ice.
JP56133319A 1981-08-27 1981-08-27 Dry ice manufacturing method Expired JPS5911526B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56133319A JPS5911526B2 (en) 1981-08-27 1981-08-27 Dry ice manufacturing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56133319A JPS5911526B2 (en) 1981-08-27 1981-08-27 Dry ice manufacturing method

Publications (2)

Publication Number Publication Date
JPS5836912A JPS5836912A (en) 1983-03-04
JPS5911526B2 true JPS5911526B2 (en) 1984-03-16

Family

ID=15101908

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56133319A Expired JPS5911526B2 (en) 1981-08-27 1981-08-27 Dry ice manufacturing method

Country Status (1)

Country Link
JP (1) JPS5911526B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58163423A (en) * 1982-03-24 1983-09-28 Nippon Sanso Kk Method for dissolving liquid carbon dioxide in water
JPS63141816A (en) * 1986-12-03 1988-06-14 Hitachi Ltd Air-conditioner for automobile
JP2797403B2 (en) * 1989-04-20 1998-09-17 三菱化学株式会社 Dry ice manufacturing method

Also Published As

Publication number Publication date
JPS5836912A (en) 1983-03-04

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