JPH08157810A - Control of composition change during transfer of mixed liquid of non-azeotropic cooling medium - Google Patents
Control of composition change during transfer of mixed liquid of non-azeotropic cooling mediumInfo
- Publication number
- JPH08157810A JPH08157810A JP6307719A JP30771994A JPH08157810A JP H08157810 A JPH08157810 A JP H08157810A JP 6307719 A JP6307719 A JP 6307719A JP 30771994 A JP30771994 A JP 30771994A JP H08157810 A JPH08157810 A JP H08157810A
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- medium
- cooling
- azeotropic
- filling
- 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.)
- Granted
Links
Landscapes
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は非共沸冷媒混合液を移充
填する際の組成変化を一定範囲内に調整する方法に関す
るものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for adjusting the compositional change when a non-azeotropic refrigerant mixed liquid is refilled within a certain range.
【0002】[0002]
【従来の技術】近年、クロロフルオロカーボンの影響に
よるオゾン層破壊の環境問題のために、1995年末ま
でのクロロフルオロカーボン全廃が決定している。ま
た、オゾン層破壊に対する影響の少ないハイドロクロロ
フルオロカーボンについても、いずれ全廃する方向にあ
る。そこで、これらクロロフルオロカーボンまたはハイ
ドロクロロフルオロカーボンの代替冷媒としては、単一
成分の冷媒や共沸系冷媒での代替が困難であるため、非
共沸混合冷媒の採用が有力となっている。2. Description of the Related Art In recent years, due to the environmental problem of ozone layer depletion due to the influence of chlorofluorocarbons, it has been decided to abolish chlorofluorocarbons by the end of 1995. In addition, hydrochlorofluorocarbons, which have little influence on the destruction of the ozone layer, will eventually be completely abolished. Therefore, as a substitute refrigerant for these chlorofluorocarbons or hydrochlorofluorocarbons, it is difficult to substitute a single-component refrigerant or an azeotropic refrigerant, so that the adoption of a non-azeotropic mixed refrigerant has become effective.
【0003】今日までに使用されてきた、単一成分もし
くは共沸系冷媒については、組成の変動はないため、移
充填の際、気相充填もしくは液相充填ともに特に組成変
化を調整する技術は必要なかった。With respect to the single-component or azeotropic refrigerants that have been used up to now, there is no change in the composition. Therefore, there is a technique for adjusting the composition change especially in the gas phase filling or the liquid phase filling at the time of transfer filling. I didn't need it.
【0004】[0004]
【発明が解決しようとする課題】非共沸混合冷媒の充填
の場合も単一成分と同様の充填方法が考えられるが、そ
の際沸点が低い成分が選択的に気相側に蒸発するため、
気相充填方法では正確な液組成の充填が不可能である。
一方、液相充填法でも、移充填に伴いボンベなどの冷媒
容器内の気相の体積が増加することで低沸点成分が選択
的に気相側に気化するため、結果として液組成が変化し
てしまうという問題がある。このため、空調機中の冷媒
容器への冷媒充填に際して、一台一台の冷媒組成が変化
し、全ての空調機に同一の冷凍能力を発揮させることが
困難となる。また、この組成変化のためボンベ内の冷媒
を全て使いきることができず不経済である。A similar filling method to a single component can be considered when filling a non-azeotropic mixed refrigerant, but at that time, a component having a low boiling point selectively evaporates to the gas phase side.
An accurate liquid composition cannot be filled by the vapor phase filling method.
On the other hand, even in the liquid-phase filling method, the volume of the gas phase in a refrigerant container such as a cylinder increases with transfer and the low boiling point components are selectively vaporized to the gas phase side, resulting in a change in the liquid composition. There is a problem that it will end up. Therefore, when the refrigerant is filled in the refrigerant container in the air conditioner, the composition of the refrigerant changes one by one, which makes it difficult for all the air conditioners to exhibit the same refrigerating capacity. Further, due to this change in composition, it is uneconomical because all the refrigerant in the cylinder cannot be used up.
【0005】[0005]
【課題を解決するための手段】本発明は、上記問題に鑑
み、非共沸冷媒混合液を移充填する際の組成変化を調整
する方法を提供することを目的とする。SUMMARY OF THE INVENTION In view of the above problems, it is an object of the present invention to provide a method for adjusting the composition change when a non-azeotropic refrigerant mixed liquid is refilled.
【0006】すなわち、本発明は、第1の冷媒容器に充
填されたジフルオロメタン(R32)、1,1,1,
2,2−ペンタフルオロエタン(R125)および1,
1,1,2−テトラフルオロエタン(R134a)から
なる非共沸冷媒混合液を2以上の第2の冷媒容器へ分け
て移充填するに際して、1回目の移充填に先立って第1
の冷媒容器に充填された前記混合液中のR32およびR
125の混合液組成をR32=23. 4〜24. 0wt
%およびR125=25. 2〜26. 0wt%とするこ
とにより、移充された第2の冷媒容器中の混合液組成を
R32/R125/R134a=23±1/25±2/
52±2wt%の範囲となるように調整することを特徴
とする非共沸冷媒混合液移充填時の組成変化調整方法で
ある。That is, according to the present invention, difluoromethane (R32), 1, 1, 1, filled in the first refrigerant container is used.
2,2-pentafluoroethane (R125) and 1,
When separately transferring the non-azeotropic refrigerant mixture liquid consisting of 1,1,2-tetrafluoroethane (R134a) to two or more second refrigerant containers, the first transfer is performed prior to the first transfer.
R32 and R in the mixed liquid filled in the refrigerant container of
The mixed liquid composition of 125 is R32 = 23.4 to 24.0 wt.
% And R125 = 25.2 to 26.0 wt%, the mixed liquid composition in the transferred second refrigerant container is R32 / R125 / R134a = 23 ± 1/25 ± 2 /
It is a composition change adjusting method at the time of refilling a non-azeotropic refrigerant mixed liquid, which is characterized in that it is adjusted to a range of 52 ± 2 wt%.
【0007】R32/R125/R134a=23/2
5/52wt%からなる非共沸混合冷媒はクロロジフル
オロメタンの代替冷媒として注目されている。空調機な
どの特性を維持するために、この非共沸冷媒混合液は空
調機中の冷媒容器においてR32/R125/R134
a=23±1/25±2/52±2wt%となるように
維持管理する必要がある。R32 / R125 / R134a = 23/2
A non-azeotropic mixed refrigerant composed of 5/52 wt% is drawing attention as an alternative refrigerant for chlorodifluoromethane. In order to maintain the characteristics of the air conditioner and the like, this non-azeotropic refrigerant mixed liquid is used as R32 / R125 / R134 in the refrigerant container in the air conditioner.
It is necessary to maintain and manage so that a = 23 ± 1/25 ± 2/52 ± 2 wt%.
【0008】上記非共沸冷媒混合液は、ボンベなどの第
1の冷媒容器から2以上の第2の冷媒容器、例えばサー
ビス缶などへ移充填したり、ボンベやサービス缶などの
第1の冷媒容器から2以上の第2の冷媒容器、例えば空
調機中の冷媒容器へ移充填することがある。この場合、
ボンベやサービス缶中の非共沸冷媒混合液は一回の操作
で使い切るのではなく、移充填を複数回行うことにより
使い切ることが通常である。The above non-azeotropic refrigerant mixture liquid is transferred from a first refrigerant container such as a cylinder to two or more second refrigerant containers, for example, a service can or the like, or the first refrigerant such as a cylinder or a service can. The container may be refilled with two or more second refrigerant containers, for example, a refrigerant container in an air conditioner. in this case,
The non-azeotropic refrigerant mixed liquid in the cylinder or the service can is usually used up by transferring and filling a plurality of times instead of using it up in a single operation.
【0009】一回の操作でないと、非共沸冷媒混合液の
組成が変動するという前述の問題が生じる。1回目の移
充填に先立って、ボンベやサービス缶などの冷媒容器に
充填された前記非共沸冷媒混合液中のR32およびR1
25の混合液組成をR32=23. 4〜24. 0wt%
およびR125=25. 2〜26. 0wt%とすること
により複数回の移充填に伴う組成変動を調整できる。If the operation is not performed once, the above-mentioned problem that the composition of the non-azeotropic refrigerant mixed liquid varies occurs. Prior to the first transfer and filling, R32 and R1 in the non-azeotropic refrigerant mixed liquid filled in a refrigerant container such as a cylinder or a service can.
The mixed liquid composition of 25 is R32 = 23.4 to 24.0 wt%
And by setting R125 = 25.2 to 26.0 wt%, it is possible to adjust the composition variation due to the multiple transfer filling.
【0010】本発明の方法は、冷媒メーカーにおいてひ
とつのボンベから2以上の他のボンベやサービス缶へ移
充填する場合、空調機メーカーにおいてひとつのボンベ
から2以上の空調機への冷媒充填時、または修理、漏洩
時にひとつのサービス缶から2以上の空調機への冷媒充
填時などにおいて好適に利用できる。According to the method of the present invention, when a refrigerant manufacturer transfers and fills one cylinder to two or more other cylinders or service cans, when an air conditioner manufacturer fills the refrigerant from one cylinder to two or more air conditioners, Alternatively, it can be preferably used when repairing or leaking, when filling a refrigerant from one service can into two or more air conditioners.
【0011】[0011]
【実施例】以下例1〜2は実施例、例3は比較例であ
る。EXAMPLES Examples 1 and 2 below are examples, and Example 3 is a comparative example.
【0012】「例1」R32/R125/R134a=
23. 4/26. 0/50.6(wt%)の組成の冷媒
を10リットルの元ボンベに9リットル充填し、この元
ボンベから液相充填法により1リットルの子ボンベに
0.9リットルずつ移充填を行った。"Example 1" R32 / R125 / R134a =
9 liters of a 10 liter original cylinder was filled with a refrigerant having a composition of 23.4 / 26.0 / 50.6 (wt%), and 0.9 liters was added from this original cylinder to a 1 liter child cylinder by the liquid phase filling method. Transfer and filling were performed one by one.
【0013】移充填をした子ボンベの液組成を分析した
ところいずれもR32、R125およびR134aの組
成が23±1、25±2、52±2wt%の範囲内であ
った。Analysis of the liquid composition of the child cylinders transferred and filled revealed that the compositions of R32, R125 and R134a were all within the ranges of 23 ± 1, 25 ± 2 and 52 ± 2 wt%.
【0014】「例2」R32/R125/R134a=
24. 0/25. 2/50.8(wt%)の組成の冷媒
を10リットルの元ボンベに9リットル充填し、この元
ボンベから液相充填法により1リットルの子ボンベに
0.9リットルずつ移充填を行った。"Example 2" R32 / R125 / R134a =
9 liters of a 10 liter original cylinder was filled with a refrigerant having a composition of 24.0 / 25.2 / 50.8 (wt%), and 0.9 liter was added from this original cylinder to a 1 liter child cylinder by a liquid phase filling method. Transfer and filling were performed one by one.
【0015】移充填をした子ボンベの液組成を分析した
ところいずれもR32、R125およびR134aの組
成が23±1、25±2、52±2wt%の範囲内であ
った。When the liquid composition of the transfer-filled cylinder was analyzed, the compositions of R32, R125 and R134a were in the range of 23 ± 1, 25 ± 2 and 52 ± 2 wt% in all cases.
【0016】「例3」R32/R125/R134a=
23/25/52(wt%)の組成の冷媒を10リット
ルの元ボンベに9リットル充填し、この元ボンベから液
相充填法により1リットルの子ボンベに0.9リットル
ずつ移充填を行った。"Example 3" R32 / R125 / R134a =
A 10-liter original cylinder was filled with 9 liters of a refrigerant having a composition of 23/25/52 (wt%), and 0.9 liters were transferred from this original cylinder to a 1-liter sub-cylinder by a liquid phase filling method. .
【0017】移充填をした子ボンベの液組成を分析した
ところ、9番目および最後に充填した子ボンベ中のR3
2、R125およびR134aの組成が23±1、25
±2、52±2wt%の範囲内ではなかった。Analysis of the liquid composition of the transfer-filled subsidiary cylinder revealed that R3 in the 9th and last packed subsidiary cylinders was analyzed.
2, the composition of R125 and R134a is 23 ± 1,25
It was not within the range of ± 2 and 52 ± 2 wt%.
【0018】[0018]
【発明の効果】本発明によれば、非共沸混合冷媒を移充
填する際、組成変化を調整できる。この方法は、冷媒メ
ーカーでのボンベ充填、空調機メーカーでの空調機への
冷媒充填、修理、漏洩時にサービス缶から空調機への充
填などの分野で利用できる。According to the present invention, the composition change can be adjusted when the non-azeotropic mixed refrigerant is refilled. This method can be used in fields such as cylinder filling by a refrigerant manufacturer, refrigerant filling in an air conditioner by an air conditioner manufacturer, repair, and filling from a service can into an air conditioner at the time of leakage.
Claims (3)
タン(R32)、1,1,1,2,2−ペンタフルオロ
エタン(R125)および1,1,1,2−テトラフル
オロエタン(R134a)からなる非共沸冷媒混合液を
2以上の第2の冷媒容器へ分けて移充填するに際して、
1回目の移充填に先立って第1の冷媒容器に充填された
前記混合液中のR32およびR125の混合液組成をR
32=23. 4〜24. 0wt%およびR125=2
5. 2〜26. 0wt%とすることにより、移充された
第2の冷媒容器中の混合液組成をR32/R125/R
134a=23±1/25±2/52±2wt%の範囲
となるように調整することを特徴とする非共沸冷媒混合
液移充填時の組成変化調整方法。1. Difluoromethane (R32), 1,1,1,2,2-pentafluoroethane (R125) and 1,1,1,2-tetrafluoroethane (R134a) filled in a first refrigerant container. ), The non-azeotropic refrigerant mixture liquid is divided into two or more second refrigerant containers and transferred,
Prior to the first transfer and filling, the composition of the mixed solution of R32 and R125 in the mixed solution filled in the first refrigerant container was changed to R
32 = 23.4 to 24.0 wt% and R125 = 2
By setting it to be 5.2 to 26.0 wt%, the mixed liquid composition in the transferred second refrigerant container becomes R32 / R125 / R.
134a = 23 ± 1/25 ± 2/52 ± 2 wt%, a composition change adjusting method at the time of refilling a non-azeotropic refrigerant mixed liquid, characterized in that it is adjusted to fall within a range of 23 ± 1/25 ± 2/52 ± 2 wt%.
である請求項1の方法。2. The method of claim 1, wherein the first refrigerant container is a cylinder or a service can.
る請求項1の方法。3. The method of claim 1, wherein the second refrigerant container is a refrigerant container in an air conditioner.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP30771994A JP3575090B2 (en) | 1994-12-12 | 1994-12-12 | Adjusting composition change during non-azeotropic refrigerant mixture transfer and filling |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP30771994A JP3575090B2 (en) | 1994-12-12 | 1994-12-12 | Adjusting composition change during non-azeotropic refrigerant mixture transfer and filling |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH08157810A true JPH08157810A (en) | 1996-06-18 |
JP3575090B2 JP3575090B2 (en) | 2004-10-06 |
Family
ID=17972429
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP30771994A Expired - Fee Related JP3575090B2 (en) | 1994-12-12 | 1994-12-12 | Adjusting composition change during non-azeotropic refrigerant mixture transfer and filling |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3575090B2 (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1998023703A1 (en) * | 1996-11-28 | 1998-06-04 | Daikin Industries, Ltd. | Method of charging mixed cooling medium |
WO1998030651A1 (en) * | 1997-01-13 | 1998-07-16 | Daikin Industries, Ltd. | Method for filling mixed refrigerant |
WO2004099336A1 (en) * | 2003-05-07 | 2004-11-18 | Zhe Jiang Lantian Environmental Protection Hi-Tech Co. Ltd. | Environmental refrigerant instead of hcfc-22 |
JPWO2014038604A1 (en) * | 2012-09-04 | 2016-08-12 | ダイキン工業株式会社 | Method for charging mixed refrigerant containing 2,3,3,3-tetrafluoropropene |
JP6315071B1 (en) * | 2016-11-28 | 2018-04-25 | ダイキン工業株式会社 | Method for transferring and filling refrigerant composition |
CN108700341A (en) * | 2017-02-03 | 2018-10-23 | 大金工业株式会社 | The method that is used using the mixture of fluorinated hydrocarbons as refrigerant and use the mixture as the refrigerating plant of refrigerant |
-
1994
- 1994-12-12 JP JP30771994A patent/JP3575090B2/en not_active Expired - Fee Related
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1998023703A1 (en) * | 1996-11-28 | 1998-06-04 | Daikin Industries, Ltd. | Method of charging mixed cooling medium |
US6058717A (en) * | 1996-11-28 | 2000-05-09 | Daikin Industries, Ltd. | Method for charging refrigerant blend |
AU722935B2 (en) * | 1996-11-28 | 2000-08-17 | Daikin Industries, Ltd. | Method for charging refrigerant blend |
KR100473961B1 (en) * | 1996-11-28 | 2005-05-16 | 다이킨 고교 가부시키가이샤 | Method of charging mixed cooling medium |
WO1998030651A1 (en) * | 1997-01-13 | 1998-07-16 | Daikin Industries, Ltd. | Method for filling mixed refrigerant |
WO2004099336A1 (en) * | 2003-05-07 | 2004-11-18 | Zhe Jiang Lantian Environmental Protection Hi-Tech Co. Ltd. | Environmental refrigerant instead of hcfc-22 |
US7459101B2 (en) | 2003-05-07 | 2008-12-02 | Zhejiang Lantian Environmental Protection Hi-Tech Co. Ltd. | Environmentally friendly alternative refrigerant for HCFC-22 |
JPWO2014038604A1 (en) * | 2012-09-04 | 2016-08-12 | ダイキン工業株式会社 | Method for charging mixed refrigerant containing 2,3,3,3-tetrafluoropropene |
US9528735B2 (en) | 2012-09-04 | 2016-12-27 | Daikin Industries, Ltd. | Method for filling mixed refrigerant containing 2,3,3,3-tetrafluoropropene |
JP6315071B1 (en) * | 2016-11-28 | 2018-04-25 | ダイキン工業株式会社 | Method for transferring and filling refrigerant composition |
WO2018097310A1 (en) * | 2016-11-28 | 2018-05-31 | ダイキン工業株式会社 | Method for transfer-filling refrigerant composition |
CN108700341A (en) * | 2017-02-03 | 2018-10-23 | 大金工业株式会社 | The method that is used using the mixture of fluorinated hydrocarbons as refrigerant and use the mixture as the refrigerating plant of refrigerant |
Also Published As
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