JPS6321293Y2 - - Google Patents
Info
- Publication number
- JPS6321293Y2 JPS6321293Y2 JP11925483U JP11925483U JPS6321293Y2 JP S6321293 Y2 JPS6321293 Y2 JP S6321293Y2 JP 11925483 U JP11925483 U JP 11925483U JP 11925483 U JP11925483 U JP 11925483U JP S6321293 Y2 JPS6321293 Y2 JP S6321293Y2
- Authority
- JP
- Japan
- Prior art keywords
- distillation
- pot
- pipe
- liquid level
- liquid
- 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
Links
- 238000004821 distillation Methods 0.000 claims description 74
- 239000007788 liquid Substances 0.000 claims description 39
- 238000010438 heat treatment Methods 0.000 claims description 22
- 239000006260 foam Substances 0.000 claims description 12
- 238000001704 evaporation Methods 0.000 claims description 8
- 230000008020 evaporation Effects 0.000 claims description 8
- 238000011084 recovery Methods 0.000 claims description 8
- 238000009423 ventilation Methods 0.000 claims description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000005108 dry cleaning Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000010721 machine oil Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Description
【考案の詳細な説明】
本考案は、石油系ドライクリーニング液（JIS
K2201−５）や機械油等の被蒸留液を蒸留する蒸
留装置の改良に関する。[Detailed explanation of the invention] This invention is based on petroleum-based dry cleaning liquid (JIS
K2201-5), machine oil, and other liquids to be distilled.
従来の蒸留装置では、一定時間当たりの蒸留量
を多くするためには蒸留釜を大きくする必要があ
り、このため、全体としては大型装置となり、一
般のクリーニング店に於いては、多蒸留量の蒸留
装置を設けようとしても、設置場所に困つていた
のが現状だつた。 In conventional distillation equipment, in order to increase the amount of distillation per certain period of time, it is necessary to increase the size of the distillation pot, which results in a large-sized device as a whole. Even if they tried to install a distillation device, they were having trouble finding a place to install it.
本考案は、このような事情に鑑み開発されたも
ので、蒸留釜を大きくすることなく多量の蒸留量
が得られ、一般のクリーニング店の実情に合致し
た多蒸留量で且つ小型な蒸留装置を提供すること
を目的とする。 The present invention was developed in view of these circumstances, and it is possible to obtain a large amount of distillation without increasing the size of the distillation pot, and to create a small-sized distillation device with a large amount of distillation that meets the actual situation of general cleaning shops. The purpose is to provide.
本考案に係る蒸留装置につき説明するに、その
構成は、蒸留蒸気回収管１０を備えた蒸留釜５
に、加熱用蒸気入口管８及び加熱用蒸気出口管９
を有する加熱釜７を設け、該蒸留釜５の横に液位
調整器２を併設し、蒸留釜５及び液位調整器２の
被蒸留液面より下の部分を蒸留釜流入管４により
連通し、また、蒸留釜５及び液位調整器２の被蒸
留液面より上の部分を圧力バランス管６により連
通して成る蒸留装置に於いて、前記圧力バランス
管６を、通気を保ちながら蒸留釜５内で発生した
蒸発泡を液位調整器２内に循環させ得る断面積、
即ち蒸留能力１／時間に対して大旨100mm2以上
の断面積を有する泡循環管６′にしたことを特徴
とする。 To explain the distillation apparatus according to the present invention, its configuration includes a distillation pot 5 equipped with a distillation vapor recovery pipe 10.
, a heating steam inlet pipe 8 and a heating steam outlet pipe 9
A heating pot 7 is provided, and a liquid level regulator 2 is installed next to the distillation pot 5, and the portions of the distillation pot 5 and the liquid level regulator 2 below the level of the liquid to be distilled are communicated through a distillation pot inflow pipe 4. In addition, in a distillation apparatus in which the distillation pot 5 and the portion of the liquid level regulator 2 above the level of the liquid to be distilled are communicated through a pressure balance tube 6, the pressure balance tube 6 is used to carry out distillation while maintaining ventilation. A cross-sectional area that can circulate the evaporation bubbles generated in the pot 5 into the liquid level regulator 2,
That is, it is characterized in that the bubble circulation pipe 6' has a cross-sectional area of approximately 100 mm 2 or more for a distillation capacity of 1/hour.
以下、本考案を第２図に示す一実施例に基づい
て説明すに、図中２は液位調整器であり、液位調
整器流入管１、ボールタツプ３等から成るが、被
蒸留液面を一定にし、且つ泡循環管６′を連結で
き、蒸発泡をある程度蓄えることができるもので
あればこれに限定されない。 Hereinafter, the present invention will be explained based on an embodiment shown in FIG. It is not limited to this, as long as it can maintain a constant value, connect the foam circulation pipe 6', and store evaporated foam to a certain extent.
５は蒸留釜であり、上部に蒸留蒸気回収管１０
を設けてある。 5 is a distillation pot, and a distillation steam recovery pipe 10 is installed at the top.
is provided.
７は加熱釜であり、加熱用蒸気入口管８及び加
熱用蒸気出口管９を備え、蒸留釜５の下部に設け
てある。 Reference numeral 7 denotes a heating pot, which is provided at the lower part of the distillation pot 5 and includes a heating steam inlet pipe 8 and a heating steam outlet pipe 9.
４は蒸留釜流入管であり、蒸留釜５及び液位調
整器２の被蒸留液面より下の部分を連通し、液位
調整器２内に流入した被蒸留液を蒸留釜５に通す
役割を持つ。 Reference numeral 4 denotes a distillation pot inflow pipe, which communicates the distillation pot 5 and a portion of the liquid level regulator 2 below the level of the liquid to be distilled, and serves to pass the liquid to be distilled that has flowed into the liquid level regulator 2 to the distillation pot 5. have.
６′は泡循環管であり、蒸留釜５及び液位調整
器２の被蒸留液面より上の部分を連通し、蒸留釜
５内で発生し、泡循環管６′と蒸留釜５の連結部
にまで達した蒸発泡の全量を通気を保ちながら液
位調整器２に循環させるのに必要にして十分な断
面積、即ち蒸留能力１／時間に対して大旨100
mm2以上の断面積を持つ。 Reference numeral 6' denotes a bubble circulation pipe, which communicates the distillation pot 5 and the portion of the liquid level regulator 2 above the surface of the liquid to be distilled, and connects the bubble circulation pipe 6' and the distillation pot 5, which are generated in the distillation pot 5. The cross-sectional area is necessary and sufficient to circulate the entire amount of evaporated bubbles that have reached 1/2 to the liquid level regulator 2 while maintaining ventilation, that is, approximately 100% for the distillation capacity 1/hour.
With a cross-sectional area of mm 2 or more.
次に第１図及び第２図に基づいて、従来の蒸留
装置及び本考案に係る蒸留装置の作用について説
明する。 Next, the operation of the conventional distillation apparatus and the distillation apparatus according to the present invention will be explained based on FIGS. 1 and 2.
先ず、従来の蒸留装置について説明するに、液
位調整器２内に入つた被蒸留液は、蒸留釜流入管
４を通り蒸留釜５内に入る。このとき、液位調整
器２と蒸留釜５を連通する圧力バランス管６の働
きにより、液位調整器２と蒸留釜５の内部の圧力
が同一となるため、液位調整器２と蒸留釜５の被
蒸留液面は同一に保たれ、ある一定の液面に達し
たら、液位調整器２内に装着されたボールタツプ
３の働きにより、液位調整器流入管１を通つて液
位調整器２に入る被蒸留液は流入停止の状態とな
る。 First, a conventional distillation apparatus will be described. The liquid to be distilled that has entered the liquid level regulator 2 passes through the distillation pot inlet pipe 4 and enters the distillation pot 5. At this time, the internal pressures of the liquid level regulator 2 and the distillation pot 5 become the same due to the function of the pressure balance pipe 6 that communicates the liquid level regulator 2 and the distillation pot 5. The liquid level to be distilled (5) is kept the same, and when it reaches a certain level, the liquid level is adjusted by the action of the ball tap 3 installed in the liquid level regulator 2 through the liquid level regulator inlet pipe 1. The liquid to be distilled entering the vessel 2 is in a state where the inflow is stopped.
加熱用蒸気入口管８を通して加熱釜７に入つた
加熱用蒸気は、加熱釜７を加熱して、加熱用蒸気
出口管９より外部に放出され、加熱釜７の熱伝導
により加熱された被蒸留液は、蒸留釜５内で一部
は蒸発蒸気となり、また一部は蒸発泡となり、蒸
発蒸気は蒸留蒸気回収管１０を通して回収され
る。圧力バランス管６の役割は蒸留釜５内の圧力
と液位調整器２内の圧力を同一にするためのもの
であり、その役割上断面積は小さく、ガス管の口
径で１インチ前後、即ち断面積600mm2前後のもの
が使用されている。 The heating steam that enters the heating pot 7 through the heating steam inlet pipe 8 heats the heating pot 7 and is discharged to the outside from the heating steam outlet pipe 9, and the heated distillate is heated by the heat conduction of the heating pot 7. A part of the liquid becomes evaporated vapor in the distillation pot 5, and another part becomes evaporated foam, and the evaporated vapor is recovered through the distillation vapor recovery pipe 10. The role of the pressure balance pipe 6 is to equalize the pressure in the distillation pot 5 and the pressure in the liquid level regulator 2, and due to its role, the cross-sectional area is small, about 1 inch in diameter of the gas pipe, i.e. Those with a cross-sectional area of around 600mm2 are used.
また蒸留釜５の容積を大きくしないで多量の蒸
留量を得ること、すなわち蒸留釜５内に於ける蒸
発蒸気の量を多くするには、加熱釜７の温度を上
げれば良い訳であるが、温度を上げれば蒸留釜５
内に発生する蒸発泡の量も多くなり、遂には蒸留
蒸気回収管１０に達してしまう。このような状態
になると蒸発蒸気と共に蒸発泡も蒸留蒸気回収管
１０を通して回収され、回収液は汚れたものとな
り、本来の蒸留の意味を失う。したがつて、従来
の蒸留装置では加熱釜７の温度をある限度以上に
上げることは出来なかつた。 In addition, in order to obtain a large amount of distillation without increasing the volume of the distillation pot 5, that is, to increase the amount of evaporated steam in the distillation pot 5, it is sufficient to raise the temperature of the heating pot 7. If you raise the temperature, the distillation pot 5
The amount of evaporation bubbles generated within the distillation vapor recovery pipe 10 also increases, and eventually reaches the distillation vapor recovery pipe 10. In such a state, evaporated bubbles as well as evaporated vapor are collected through the distillation vapor recovery pipe 10, and the recovered liquid becomes dirty, losing the original meaning of distillation. Therefore, in the conventional distillation apparatus, it was not possible to raise the temperature of the heating pot 7 above a certain limit.
次に本考案に係る蒸留装置について説明する
に、基本的な構成は従来のものと同じであり、相
違点は、第１図の圧力バランス管６を泡循環管
６′としたことである。 Next, the distillation apparatus according to the present invention will be explained.The basic structure is the same as the conventional one, and the difference is that the pressure balance pipe 6 in FIG. 1 is replaced with a bubble circulation pipe 6'.
蒸留蒸気の量を多くするためには、蒸留釜５の
容積を増してやる方法があるが、これは「より小
型装置に」という時代の要求に逆行する。 In order to increase the amount of distilled steam, there is a method of increasing the volume of the distillation pot 5, but this goes against the demands of the times for ``smaller equipment.''
よつて、本考案に係る泡循環管６′を設けるこ
とに依り、加温により蒸留釜５内に発生する蒸発
泡が増大し、泡循環管６′及び蒸留釜５の連結部
に達すれば、蒸発泡は泡循環管６′を通して液位
調整器２に循環される。 Therefore, by providing the bubble circulation pipe 6' according to the present invention, the evaporation bubbles generated in the distillation pot 5 due to heating increase, and if they reach the connection part between the bubble circulation pipe 6' and the distillation pot 5, The evaporated foam is circulated to the level regulator 2 through the foam circulation pipe 6'.
泡循環管６′を通して液位調整器２に循環され
た蒸発泡は冷えて再び被蒸留液となり、蒸留釜流
入管４を通り再び蒸留釜５内に流入する。 The evaporated foam circulated to the liquid level regulator 2 through the foam circulation pipe 6' cools and becomes a liquid to be distilled again, and flows into the still 5 again through the still inlet pipe 4.
また、泡循環管６′は第１図に於ける圧力バラ
ンス管６の役割も兼用しているが、従来の圧力バ
ランス管６は、蒸発泡を循環させるには余りにも
断面積が小さく、また、蒸発泡を循環させるとい
う技術的思想も織り込まれていなかつたことは言
うに及ばない。 Further, the bubble circulation pipe 6' also serves as the pressure balance pipe 6 in FIG. 1, but the conventional pressure balance pipe 6 has a too small cross-sectional area to circulate evaporation foam, Needless to say, the technical concept of circulating evaporation bubbles was not incorporated.
以上のような構成、作用を有することに依り、
本考案は次のような特有の効果を有する。 By having the above structure and function,
The present invention has the following unique effects.
多量の蒸発泡が発生しても、蒸発泡が泡循環管
６′により液位調整器２に循環するので、従来の
ように多蒸留量を得るために蒸留釜を大きくする
必要が無く、且つ加熱釜７を従来より高温度にす
ることができる。すなわち、本考案に係る泡循環
管６′を設けることにより、多蒸留量で且つ小型
な蒸留装置を提供することができる。 Even if a large amount of evaporation foam is generated, the evaporation foam is circulated to the liquid level regulator 2 through the foam circulation pipe 6', so there is no need to enlarge the distillation pot to obtain a large distillation amount as in the conventional method. The heating pot 7 can be heated to a higher temperature than before. That is, by providing the bubble circulation pipe 6' according to the present invention, it is possible to provide a small-sized distillation apparatus with a large distillation amount.
したがつて、従来、一般のクリーニング店に於
いては多蒸留量の蒸留装置を設けようとしても設
置場所に困つていたが、本考案に係る蒸留装置な
らば、このような問題も解消され、極めて実用的
な蒸留装置に係る考案である。 Therefore, in the past, ordinary dry cleaners had trouble finding a place to install a distillation device with a high distillation rate, but with the distillation device of the present invention, such problems can be solved. , is an invention related to an extremely practical distillation apparatus.
図面は本考案の一実施例を示すものであり、第
１図は従来の蒸留装置を示す構成略図、第２図は
本考案蒸留装置を示す構成略図である。
１……液位調整器流入管、２……液位調整器、
３……ボールタツプ、４……蒸留釜流入管、５…
…蒸留釜、６……圧力バランス管、６′……泡循
環管、７……加熱釜、８……加熱用蒸気入口管、
９……加熱用蒸気出口管、１０……蒸留蒸気回収
管、Ａ……被蒸留液。
The drawings show an embodiment of the present invention, and FIG. 1 is a schematic diagram showing the structure of a conventional distillation apparatus, and FIG. 2 is a schematic diagram showing the structure of the distillation apparatus of the present invention. 1...Liquid level regulator inflow pipe, 2...Liquid level regulator,
3...Ball tap, 4...Distillation pot inflow pipe, 5...
... Distillation kettle, 6 ... Pressure balance pipe, 6' ... Bubble circulation pipe, 7 ... Heating kettle, 8 ... Steam inlet pipe for heating,
9... Steam outlet pipe for heating, 10... Distillation steam recovery pipe, A... Liquid to be distilled.
Claims (1)
用蒸気入口管８及び加熱用蒸気出口管９を有する
加熱釜７を設け、該蒸留釜５の横に液位調整器２
を併設し、蒸留釜５及び液位調整器２の被蒸留液
面より下の部分を蒸留釜流入管４により連通し、
また、蒸留釜５及び液位調整器２の被蒸留液面よ
り上の部分を圧力バランス管６により連通して成
る蒸留装置に於いて、前記圧力バランス管６を、
通気を保ちながら蒸留釜５内で発生した蒸発泡を
液位調整器２内に循環させ得る断面積、即ち蒸留
能力１／時間に対して大旨100mm2以上の断面積
を有する泡循環管６′にしたことを特徴とする蒸
留装置。 A heating pot 7 having a heating steam inlet pipe 8 and a heating steam outlet pipe 9 is installed in a distillation pot 5 equipped with a distillation steam recovery pipe 10, and a liquid level regulator 2 is installed next to the distillation pot 5.
The distillation pot 5 and the portion of the liquid level regulator 2 below the level of the liquid to be distilled are connected through the distillation pot inflow pipe 4.
In addition, in a distillation apparatus in which the distillation pot 5 and the portion of the liquid level regulator 2 above the level of the liquid to be distilled are connected through a pressure balance tube 6, the pressure balance tube 6 is
A foam circulation pipe 6 having a cross-sectional area capable of circulating the evaporation bubbles generated in the distillation pot 5 into the liquid level regulator 2 while maintaining ventilation, that is, a cross-sectional area of approximately 100 mm 2 or more per distillation capacity 1/hour. A distillation device characterized by:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11925483U JPS6028001U (en) | 1983-07-29 | 1983-07-29 | distillation equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11925483U JPS6028001U (en) | 1983-07-29 | 1983-07-29 | distillation equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6028001U JPS6028001U (en) | 1985-02-25 |
| JPS6321293Y2 true JPS6321293Y2 (en) | 1988-06-13 |
Family
ID=30273772
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11925483U Granted JPS6028001U (en) | 1983-07-29 | 1983-07-29 | distillation equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6028001U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107531483A (en) * | 2015-05-14 | 2018-01-02 | 中外炉工业株式会社 | Steam circulation regenerative system |
-
1983
- 1983-07-29 JP JP11925483U patent/JPS6028001U/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107531483A (en) * | 2015-05-14 | 2018-01-02 | 中外炉工业株式会社 | Steam circulation regenerative system |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6028001U (en) | 1985-02-25 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US3558436A (en) | Distilation apparatus for desalinisation of saline water to recover fresh water as condensate | |
| US4230536A (en) | Method for the distillation purification of organic heat transfer fluids | |
| US8394241B2 (en) | Distillation-type drinking fountain and energy-saving heating unit thereof | |
| US3370636A (en) | Apparatus for reconcentrating liquid desiccant | |
| SE8402229L (en) | VERTICAL ROD TYPE FILM MOVIES | |
| US4309243A (en) | Vertical tube distillers | |
| JPS6321293Y2 (en) | ||
| US3451897A (en) | Apparatus for reconcentrating glycol and the like | |
| US4911233A (en) | Interface fluid heat transfer system | |
| US4139418A (en) | Method and apparatus for the distillation purification of organic heat transfer fluids | |
| US3443623A (en) | Apparatus for reconcentrating liquid desiccant | |
| US4919257A (en) | Condensate skimming reflux column | |
| US833271A (en) | Distilling apparatus. | |
| JPS622672B2 (en) | ||
| US2721455A (en) | Absorption refrigeration | |
| US2051760A (en) | Refrigeration | |
| JP4143210B2 (en) | Reboiler | |
| JPS6314293Y2 (en) | ||
| US4201631A (en) | Method for controlling the flow through a distillation apparatus and a device for carrying out the method | |
| JPH067780Y2 (en) | Liquid mixture separator | |
| US1924894A (en) | Fluid apparatus | |
| USRE23442E (en) | Absorption refrigeration | |
| US20030178294A1 (en) | Device for distilling a medium | |
| JPS55160287A (en) | Heat pipe | |
| JPH029340Y2 (en) |