JP2545879B2 - Coolant - Google Patents
CoolantInfo
- Publication number
- JP2545879B2 JP2545879B2 JP62238440A JP23844087A JP2545879B2 JP 2545879 B2 JP2545879 B2 JP 2545879B2 JP 62238440 A JP62238440 A JP 62238440A JP 23844087 A JP23844087 A JP 23844087A JP 2545879 B2 JP2545879 B2 JP 2545879B2
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- performance
- coefficient
- cfc
- freon
- 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 - Fee Related
Links
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Detergent Compositions (AREA)
Description
【発明の詳細な説明】 産業上の利用分野 本発明は、冷凍機の動作流体、いわゆる冷媒に関す
る。TECHNICAL FIELD The present invention relates to a working fluid of a refrigerator, a so-called refrigerant.
従来技術とその問題点 従来、冷媒としては、クロロフルオロ炭化水素、フル
オロ炭化水素、これらの共沸組成物並びにその近辺の組
成の組成物が知られている。これらは、フロン又はフロ
ン系冷媒と称され、現在ジクロロジフルオロメタン(以
下フロン−12という)、クロロジフルオロメタン(以下
フロン−22という)等が主に使用されている。しかしな
がら、近年、大気中に放出された場合に、ある種のフロ
ンが成層圏のオゾン層を破壊し、その結果、人類を含む
地球上の生態系に重大な悪影響を及ぼすことが指摘され
ている。このような指摘は、未だ科学的に実証されてい
るとは言い難いが、趨勢としては、オゾン層破壊の可能
性の高いフロンについては、国際的な取り決めにより、
使用及び生産を統制する方向にある。統制の対象となる
フロンの一種にフロン−12がある。冷凍・空調設備の普
及に伴い、需要が毎年増大しているフロンの使用及び生
産の統制は、居住環境をはじめとして、現在の社会機構
に与える影響が大きい。従って、冷凍性能、特に成績係
数に優れた冷媒の開発が緊急の課題となっている。オゾ
ン層を破壊するおそれがないフロンとして、ジフルオロ
メタン(フロン−32)が考えられるが、これは、成績係
数が低いのが欠点である。2. Description of the Related Art Conventional technology and its problems Conventionally, as refrigerants, chlorofluorohydrocarbons, fluorohydrocarbons, azeotropic compositions thereof, and compositions having compositions in the vicinity thereof are known. These are called CFCs or CFC-based refrigerants, and currently dichlorodifluoromethane (hereinafter CFC-12), chlorodifluoromethane (CFC-22), etc. are mainly used. However, in recent years, it has been pointed out that, when released into the atmosphere, certain types of CFCs destroy the ozone layer in the stratosphere, and as a result, have a serious adverse effect on the earth's ecosystem including humankind. It is hard to say that such a point has been scientifically proven, but the trend is that regarding fluorocarbons, which have a high possibility of ozone depletion, by international agreement,
It is in the direction of controlling the use and production. One of the CFCs that is subject to control is CFC-12. With the spread of refrigeration and air-conditioning equipment, the control of the use and production of CFCs, whose demand is increasing every year, has a great impact on the current social mechanism including the living environment. Therefore, the development of a refrigerant having excellent refrigeration performance, particularly a coefficient of performance, has become an urgent issue. Difluoromethane (CFC-32) is considered as a CFC that does not have a risk of depleting the ozone layer, but its disadvantage is its low coefficient of performance.
ここに、成績係数とは、冷凍能力/圧縮仕事の比で示
されるのである。冷凍能力は、被冷却体が奪われる単位
時間当たりの熱量であり、圧縮仕事は、単位時間当たり
の冷凍機運転のための動力の仕事量であるから、成績係
数は、冷媒の効率に相当するものである。Here, the coefficient of performance is indicated by the ratio of refrigerating capacity / compression work. The coefficient of performance corresponds to the efficiency of the refrigerant because the refrigerating capacity is the amount of heat per unit time taken by the object to be cooled and the compression work is the amount of work of power for operating the refrigerator per unit time. It is a thing.
問題点を解決するための手段 本発明者は、成績係数に優れ、且つ大気中に放出され
た場合にもオゾン層に及ぼす影響が小さい新たな冷媒を
得るべく、種々研究を重ねてきた。Means for Solving Problems The present inventor has conducted various studies in order to obtain a new refrigerant that has an excellent coefficient of performance and has a small effect on the ozone layer even when it is discharged into the atmosphere.
その結果、ジフルオロメタン(フロン−32)にテトラ
フルオロエタンを特定割合で配合する場合には、高い成
績係数を発揮する冷媒が得られることを見出した。As a result, it was found that a refrigerant showing a high coefficient of performance can be obtained when difluoromethane (CFC-32) is mixed with tetrafluoroethane at a specific ratio.
すなわち、本発明は、ジフルオロメタン65〜1重量%
と1,1,1,2−テトラフルオロエタン35〜99重量%とから
なる冷媒に係る。That is, the present invention is difluoromethane 65-1 wt%
And 1,1,1,2-tetrafluoroethane of 35 to 99% by weight.
本発明冷媒組成物は、ジフルオロメタン65〜1重量%
と1,1,1,2−テトラフルオロエタン(フロン−134a)35
〜99重量%とからなるものであり、ジフルオロメタンと
テトラフルオロエタンを上記した範囲の割合で配合する
ことによって、高い成績係数を発揮する冷媒が得られ
る。The refrigerant composition of the present invention comprises 65 to 1% by weight of difluoromethane.
And 1,1,1,2-tetrafluoroethane (CFC-134a) 35
The blending ratio of difluoromethane and tetrafluoroethane in the above range provides a refrigerant exhibiting a high coefficient of performance.
発明の作用及び効果 本発明組成物は、非共沸組成物である。一般に、単一
化合物及び共沸組成物では、蒸発器における蒸発温度
は、蒸発が定圧下に行われるために、一定であるが、非
共沸組成物では、蒸発器入口で低温となり、蒸発器出口
で高温となる。一方、被冷却流体は、蒸発器での冷媒の
流れと向流方向に熱交換するように流されるので、冷媒
の蒸発温度が一定であっても、流れに沿って温度勾配を
有する。すなわち、蒸発器内では、冷媒と被冷却流体と
の温度差は、被冷却流体が進むにしたがって、小さくな
る。本発明による非共沸組成物冷媒を使用する場合に
は、蒸発器内での被冷却流体の温度勾配に近付けること
が可能となり、冷凍の効率、即ち成績係数を高めること
ができる。Effects and Effects of the Invention The composition of the present invention is a non-azeotropic composition. In general, for single compounds and azeotropic compositions, the evaporation temperature in the evaporator is constant because evaporation takes place under constant pressure, but for non-azeotropic compositions, the temperature is low at the evaporator inlet and It becomes hot at the exit. On the other hand, the fluid to be cooled is flowed so as to exchange heat with the flow of the refrigerant in the evaporator in a countercurrent direction, so that even if the evaporation temperature of the refrigerant is constant, there is a temperature gradient along the flow. That is, in the evaporator, the temperature difference between the refrigerant and the fluid to be cooled becomes smaller as the fluid to be cooled advances. When the non-azeotropic composition refrigerant according to the present invention is used, the temperature gradient of the fluid to be cooled in the evaporator can be approximated, and the refrigeration efficiency, that is, the coefficient of performance can be increased.
実 施 例 以下に実施例及び比較例を示し、本発明の特徴とする
ところをより一層明らかにする。Examples Examples and comparative examples will be shown below to further clarify the features of the present invention.
実施例1〜5及び比較例1 フロン−32とフロン−134aとを第1表に示す種々の割
合(重量比)で混合し、冷媒とした。Examples 1 to 5 and Comparative Example 1 Freon-32 and Freon-134a were mixed at various ratios (weight ratios) shown in Table 1 to prepare refrigerants.
第1表 フロン−32 フロン−134a 比較例1 100 0 実施例1 60 40 実施例2 40 60 実施例3 20 80 実施例4 5 95 実施例5 1 99 1馬力の冷凍機において、凝縮器における冷媒の凝縮
開始温度を50℃、蒸発器入口における冷媒の温度を0
℃、蒸発器過熱度を5℃とし、第1表に示す組成の冷媒
を使用して、運転を行なった。第2表に各冷媒の(I)
最高蒸発温度[℃]、(II)冷媒能力[kcal/m3]、(I
II)成績係数及び(IV)圧縮機吐出温度[℃]を示す。Table 1 Freon-32 Freon-134a Comparative Example 1 100 0 Example 1 60 40 Example 2 40 60 Example 3 20 80 Example 4 5 95 Example 5 1 99 1 Refrigerant in a condenser in a 1-hp refrigerator The condensation start temperature of 50 ℃, the temperature of the refrigerant at the evaporator inlet is 0
C., the degree of superheat of the evaporator was 5.degree. C., and the operation was performed using the refrigerant having the composition shown in Table 1. Table 2 shows (I) of each refrigerant
Maximum evaporation temperature [℃], (II) Refrigerant capacity [kcal / m 3 ], (I
II) Performance coefficient and (IV) Compressor discharge temperature [° C] are shown.
尚、第2表には、フロン−32のみを使用する場合(比
較例1)の結果を併せて示す。In addition, Table 2 also shows the results when only Freon-32 was used (Comparative Example 1).
第2表 (I) (II) (III) (IV) 比較例1 0.0 1210 3.85 101.0 実施例1 3.1 1030 4.34 84.5 実施例2 5.3 917 4.73 76.4 実施例3 5.8 743 4.96 68.6 実施例4 2.6 532 4.53 63.3 実施例5 0.6 459 4.24 62.0 また、第1図には、フロン−32とフロン−134aとの組
成比と成績係数との関係を表わすグラフを示す。Table 2 (I) (II) (III) (IV) Comparative Example 1 0.0 1210 3.85 101.0 Example 1 3.1 1030 4.34 84.5 Example 2 5.3 917 4.73 76.4 Example 3 5.8 743 4.96 68.6 Example 4 2.6 532 4.53 63.3 Example 5 0.6 459 4.24 62.0 FIG. 1 is a graph showing the relationship between the composition ratio of freon-32 and freon-134a and the coefficient of performance.
第2表及び第1図に示す結果から、本発明冷媒の優れ
た特性が明らかである。From the results shown in Table 2 and FIG. 1, the excellent properties of the refrigerant of the present invention are clear.
第1図は、本発明冷媒の性能を示すグラフである。 FIG. 1 is a graph showing the performance of the refrigerant of the present invention.
Claims (1)
−テトラフルオロエタン35〜99重量%とからなる冷媒。1. Difluoromethane 65 to 1% by weight and 1,1,1,2
A refrigerant consisting of 35 to 99% by weight of tetrafluoroethane.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62238440A JP2545879B2 (en) | 1987-09-21 | 1987-09-21 | Coolant |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62238440A JP2545879B2 (en) | 1987-09-21 | 1987-09-21 | Coolant |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6479288A JPS6479288A (en) | 1989-03-24 |
JP2545879B2 true JP2545879B2 (en) | 1996-10-23 |
Family
ID=17030254
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62238440A Expired - Fee Related JP2545879B2 (en) | 1987-09-21 | 1987-09-21 | Coolant |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2545879B2 (en) |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5403504A (en) * | 1990-12-17 | 1995-04-04 | E. I. Du Pont De Nemours And Company | Process for heating and cooling using substantially constant boiling compositions of fluorinated hydrocarbons |
AU1642192A (en) * | 1991-03-18 | 1992-10-21 | Allied-Signal Inc. | Non-azeotropic refrigerant compositions comprising difluoromethane; 1,1,1-trifluoroethane; or propane |
US5234613A (en) * | 1991-09-30 | 1993-08-10 | E.I. Du Pont De Nemours And Company | Substantially constant boiling compositions of difluoromethane and propane |
US5232618A (en) * | 1991-09-30 | 1993-08-03 | E. I. Du Pont De Nemours And Company | Substantially constant boiling compositions of difluoromethane and trifluoroethane or perfluoroethane |
US5290466A (en) * | 1991-10-31 | 1994-03-01 | E. I. Du Pont De Nemours And Company | Compositions of difluoromethane and tetrafluoroethane |
US5294359A (en) * | 1992-02-03 | 1994-03-15 | Alliedsignal Inc. | Refrigerant compositions |
JP2613526B2 (en) * | 1992-07-04 | 1997-05-28 | 花王株式会社 | Composition for working fluid of refrigerator |
EP0687286B1 (en) * | 1993-03-02 | 1996-10-16 | E.I. Du Pont De Nemours And Company | Compositions including a hexafluoropropane |
JP2012236884A (en) * | 2011-05-10 | 2012-12-06 | Fujitsu General Ltd | Mixed refrigerant and air conditioner using the same |
JP2022070188A (en) * | 2020-10-26 | 2022-05-12 | グリーンアース株式会社 | Global warming alleviation method by air conditioner using coolant r410a |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3607755A (en) * | 1968-11-25 | 1971-09-21 | Allied Chem | Novel halocarbon compositions |
JPS5340693A (en) * | 1976-08-13 | 1978-04-13 | Montedison Spa | Spraying agent composites for aerosol |
JPS59117579A (en) * | 1982-12-24 | 1984-07-06 | Matsushita Electric Ind Co Ltd | Refrigerant composition |
-
1987
- 1987-09-21 JP JP62238440A patent/JP2545879B2/en not_active Expired - Fee Related
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3607755A (en) * | 1968-11-25 | 1971-09-21 | Allied Chem | Novel halocarbon compositions |
JPS5340693A (en) * | 1976-08-13 | 1978-04-13 | Montedison Spa | Spraying agent composites for aerosol |
JPS59117579A (en) * | 1982-12-24 | 1984-07-06 | Matsushita Electric Ind Co Ltd | Refrigerant composition |
Also Published As
Publication number | Publication date |
---|---|
JPS6479288A (en) | 1989-03-24 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
LAPS | Cancellation because of no payment of annual fees |