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| United States Patent | 4983312 |
| Link to this page | http://www.wikipatents.com/4983312.html |
| Inventor(s) | Tamura; Koji (Kawanishi, JP);
Kashiwagi; Hiroshi (Settsu, JP);
Noguchi; Masahiro (Osaka, JP) |
| Abstract | The present invention provides a refrigerant comprising tetrafluoroethane
and either chlorodifluoromethane or chlorodifluoroethane. |
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| Publication Date |
January 8, 1991 |
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| Priority Data |
Sep 21, 1987[JP]62-238439 |
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Title Information  |
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Market Review  |
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Description  |
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TECHNICAL FIELD
This invention relates to a working fluid for a refrigerator, which is
called a refrigerant.
PRIOR ART AND PROBLEMS THEREOF
Refrigerants heretofore known include chlorofluoroalkanes, fluoroalkanes,
azeotropic compositions thereof and other materials having a similar
composition. These are generally called flons or flon refrigerants. Among
them, chiefly used at present are dichlorodifluoromethane (hereinafter
referred to as "Flon-12"), chlorodifluoromethane (hereinafter called
"Flon-22") and the like. In recent years, however, it has been pointed out
that certain kinds of flons released into the atmosphere would destroy the
stratospheric ozone layer, thereby inflicting a serious adverse influence
on the ecosystem including humans on the earth. Although said proposition
may have yet to be scientifically and completely established, there is a
tendency toward the control, under an international agreement, of use and
production of flons which are likely to destroy the ozone layer. The flons
to be controlled include Flon-12. With the spread of refrigerators and
air-conditioning systems, the control over the use and production of
flons, which are in greater demand year after year, greatly affects our
residential environment and the current social framework as a whole. In
consequence, there is an urgent demand for development of novel
refrigerants having a high refrigerating performance, particularly a high
coefficient of performance, which can substitute for Flon-12.
Tetrafluoroethane may be offered as flons free of ozone layer-destroying
risks but has the defect of being low in coefficient of performance.
The term "coefficient of performance" used herein means the ratio of
refrigerating capacity to compressing work. The refrigerating capacity is
the quantity of heat removed per a unit time from the substances being
cooled, and the compressing work is the work volume achieved per a unit
time by power for operating the refrigerator. Accordingly the coefficient
of performance corresponds to the refrigeration efficiency of the
refrigerant.
MEANS FOR SOLUTION OF THE PROBLEMS
We conducted extensive research to develop novel refrigerants which have a
high coefficient of performance and which, when released into the
atmosphere, would exert little influence on the ozone layer. Our research
revealed that a refrigerant comprising tetrafluoroethane and
chlorodifluoromethane or chlorodifluoroethane can exhibit a higher
coefficient of performance than tetrafluoroethane.
The present invention, therefore, provides a refrigerant comprising
tetrafluoroethane and either chlorodifluoromethane or chlorodifluorethane.
BRIEF DESCRIPTION OF THE DRAWINGS
FIGS. 1 and 2 show graphs illustrating the refrigerating performance of the
refrigerants according to the present invention.
CONSTRUCTION OF THE INVENTION
Preferred refrigerant compositions of the invention are those comprising 95
to 5% by weight of tetrafluoroethane and 5 to 95% by weight of either
chlorodifluoromethane o chlorodifluoroethane. Refrigerants containing
chlorodifluoromethane or chlorodifluoroethane in the foregoing ratio have
an improved coefficient of performance compared with tetrafluoroethane
singly used. A preferable mixing ratio is as follows. Of refrigerants
composed of tetrafluoroethane and chlorodifluoromethane, preferred are
those comprising 90 to 5% by weight of the former and 10 to 95% by weight
of the latter, and particularly preferred are those comprising 80 to 20%
by weight of the former and 20 to 80% by weight of the latter. Of
refrigerants composed of tetrafluoroethane and chlorodifluoroethane,
preferred are those comprising 80 to 5% by weight of the former and 20 to
95% by weight of the latter. In particular, refrigerants composed of 80 to
20% by weight of tetrafluoroethane and 20 to 80% by weight of
chlorodifluoromethane and those composed of 80 to 5% by weight of
tetrafluoroethane and 20 to 95% by weight of chlorodifluoroethane can
display a higher coefficient of performance than Flon-12.
Examples of tetrafluoroethane for use in the invention are
1,1,1,2-tetrafluoroethane (Flon-134a) and 1,1,2,2-tetrafluoroethane
(Flon-134). Examples of chlorodifluoroethane for use herein are
1-chloro-1,1-difluoroethane (Flon-142b), 1-chloro-1,2-difluoroethane
(Flon-142a) and 2-chloro-1,1-difluoroethane (Flon-142). Among the
compositions of the invention, Flon-134a and Flon-134 can achieve a
similar degree of effect and thus can be replaced by each other or mixed
with each other in use. This can be done in respect of Flon-142a,
Flon-142b and Flon-142.
RESULTS AND EFFECTS OF THE INVENTION
The refrigerants of the invention ar smaller in the ratio of specific heat
and lower in the temperature of gas discharged from the compressor than
Flon-22 and are consequently suitable for use as a cooling medium for a
refrigeration cycle using a relatively high temperature as in an
air-conditioning equipment of the heat pump type.
The composition of the invention is a nonazeotropic composition. Generally
a single compound or an azeotrope is vaporized at a constant temperature
in an evaporator because of its evaporation done under constant pressure,
whereas a non-azeotropic composition has a low temperature at the inlet of
the evaporator and a high temperature at the outlet thereof. On the other
hand, a fluid to be cooled is caused to flow in countercurrent to the
refrigerant in the evaporator to undergo heat exchange and thus has a
temperature gradient along the flow direction even if the refrigerant is
vaporized at a constant temperature. In other words, a temperature
difference between the refrigerant and the fluid to be cooled diminishes
in the evaporator as the fluid flows forwardly. In use, the refrigerant of
the non-azeotropic composition according to the invention can be rendered
close in temperature to the temperature gradient of the fluid to be cooled
in the evaporator, so that the refrigeration efficiency, namely the
coefficient of performance, can be enhanced.
EXAMPLES
The features of the present invention will be clarified below with
reference to the following Examples and Comparison Example.
EXAMPLES 1 TO 6 AND COMPARISON EXAMPLE 1
Refrigerants were prepared by mixing together Flon-134a and Flon-22 in the
various proportions shown below in Table 1 (weight ratio).
TABLE 1
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Flon-134a
Flon-22
______________________________________
Comp. Example 1 100 0
Example 1 95 5
Example 2 80 20
Example 3 60 40
Example 4 40 60
Example 5 20 80
Example 6 5 95
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A refrigerator was operated with an output of 1 hp. using the refrigerants
of the composition shown in Table 1. Each refrigerant started condensation
at 50.degree. C. in a condenser and had a temperature of 0.degree. C. in
the inlet of the evaporator with superheat of 5.degree. C. Table 2 below
shows (I) the maximum evaporating temperature (.degree. C.), (II)
refrigerating capacity (kcal/m.sup.3), (III) coefficient of performance
and (IV) discharge temperature (.degree. C.) at the compressor.
Table 2 also shows the results achieved by using Flon-134a alone
(Comparison Example 1).
TABLE 2
______________________________________
Maximum Refriger-
evaporating ating Coefficient
Discharge
temperature capacity of perform-
temperature
(.degree.C.) (kcal/m.sup.3)
ance (.degree.C.)
(I) (II) (III) (IV)
______________________________________
Comp. Ex-
0.0 440 4.16 61.6
ample 1
Example 1
0.3 456 4.19 62.3
Example 2
0.9 503 4.27 64.5
Example 3
1.4 563 4.33 67.3
Example 4
1.3 620 4.32 70.5
Example 5
0.9 676 4.28 73.6
Example 6
0.3 716 4.21 76.2
______________________________________
FIG. 1 indicates a graph illustrating the relationship between the
proportions of Flon-134a and Flon-22 and the coefficient of performance
(curve A).
The results shown in Table 2 and FIG. 1 reveal that the refrigerants of the
present invention have outstanding properties.
EXAMPLES 7 TO 12
The properties of refrigerants were investigated in the same manner as in
Examples 1 to 6 with the exception of using the refrigerants prepared by
mixing together Flon-134a and Flon-142b in the various proportions (weight
ratio) shown below in Table 3.
TABLE 3
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Flon-134a
Flon-142b
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Example 7 95 5
Example 8 80 20
Example 9 60 40
Example 10 40 60
Example 11 20 80
Example 12 5 95
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Table 4 shows (I) the maximum evaporating temperature (.degree. C.), (II)
refrigerating capacity (kcal/m.sup.3), (III) coefficient of performance
and (IV) discharge temperature (.degree. C.) at the compressor in respect
of the refrigerants.
FIG. 2 indicates a graph illustrating the relationship between the
proportions of Flon-134a and Flon-142b and the coefficient of performance
(curve B).
TABLE 4
______________________________________
Maximum Refriger-
evaporating ating Coefficient
Discharge
temperature capacity of perform-
temperature
(.degree.C.) (kcal/m.sup.3)
ance (.degree.C.)
(I) (II) (III) (IV)
______________________________________
Example 7
0.5 431 4.24 61.4
Example 8
1.6 402 4.46 60.7
Example 9
2.2 363 4.63 60.0
Example 10
2.1 323 4.68 59.3
Example 11
1.4 281 4.61 58.9
Example 12
0.4 251 4.48 58.7
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Description  |
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