JPS6356917B2 - - Google Patents

Description

DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a refrigeration composition used in an absorption refrigerator.

In general, absorption refrigerators are formed with a closed cycle consisting of a generator containing a refrigeration composition, a condenser, an evaporator, and an absorber.When the liquid refrigerant is evaporated in the evaporator, heat is taken from the outside, and the evaporation The heat is used for freezing. The refrigerant vapor evaporated in the evaporator is absorbed in the absorber by the refrigeration composition containing a high concentration of absorbent sent from the generator, and is returned to the generator as a refrigeration composition containing a low concentration of absorbent. . The refrigeration composition containing a low concentration of absorbent is heated in a generator with an external heat source to release refrigerant vapor, which is condensed in a condenser and sent back to the evaporator.

Conventionally, refrigeration compositions used in absorption refrigerators consisting of such cycles include refrigeration compositions using water (H ₂ O) as a refrigerant and lithium bromide (LiBr) as an absorbent, and refrigeration compositions using ammonia (NH ₃ ) as an absorbent. Refrigeration compositions using a refrigerant and water (H ₂ O) as an absorbent have been put into practical use.

However, since H ₂ O-LiBr-based refrigeration compositions use water as a refrigerant, the evaporation temperature cannot be set below 0°C, and therefore they cannot be used for purposes other than air conditioning. Air-cooling of the condenser is difficult due to limited solubility in water, the vapor pressure is too low so a significant negative pressure must be maintained in the equipment, and corrosion control is required due to the corrosive nature of the solution. There are drawbacks such as restrictions on the addition of agents and materials for equipment.

In addition, NH ₃ - H ₂ O-based refrigeration compositions have a fairly high vapor pressure, so the equipment must be designed to withstand high pressure, and ammonia gas is explosive and toxic, which can be dangerous. Currently, it is hardly used for type refrigerators. Therefore, a system has been proposed in which alcohols such as methanol and ethanol are used as refrigerants to obtain temperatures below 0°C, and halides such as lithium bromide (LiBr) and zinc bromide (ZnBr ₂ ) are used as absorbents. being researched. However, in this system, the solubility of halide in alcohol is low, and halide crystals tend to precipitate in low concentration ranges, resulting in a narrow operating concentration range.The viscosity of the solution is high, which increases the power required for liquid circulation. Disadvantages have been pointed out, such as the liquid film of the concentrated absorbent solution in the absorber becoming thicker and the alcohol absorption rate decreasing.

In view of the above-mentioned problems with refrigeration compositions, studies have recently been conducted on systems that use various fluorocarbon compounds as refrigerants and various organic solvents that dissolve these fluorocarbon compounds as absorbents. , some of which are disclosed in Japanese Patent Application Laid-open Nos. 54-55849 and 1983.
- Proposed in Publication No. 79175, etc. but,
There are many possible combinations of systems in which a fluorocarbon compound is used as a refrigerant and an organic solvent is used as an absorbent, and the current situation is that sufficient research has not yet been conducted on individual combinations. 22) etc. as a refrigerant,
Refrigeration compositions using tetraethylene glycol dimethyl ether as an absorbent have attracted attention, but their vapor pressure is as high as that of the NH ₃ --H ₂ O system.

In view of the problems of the refrigeration compositions used in conventional absorption refrigerators, the present invention provides a refrigeration composition that is particularly safe to handle, does not have a very high vapor pressure, and is less corrosive to equipment. As a result of intensive research, it was discovered that a refrigeration composition using dichlorotrifluoroethane as a refrigerant and diethylene glycol dimethyl ether as an absorbent is well suited to the above purpose and is an excellent refrigeration composition. This led to the present invention. That is, the present invention is a refrigeration composition for an absorption refrigerator that uses dichlorotrifluoroethane as a refrigerant and diethylene glycol dimethyl ether as an absorbent.

Dichlorotrifluoroethane used as a refrigerant in the present invention has three isomers with different structural formulas, namely CHCl ₂ - CF ₃ (R123), CHClF - CClF ₂
(R123a) and CHF ₂ -CCl ₂ F (R123b), but since their physical properties are almost similar, either isomer can be used. Therefore, in the following explanation, the case where R123a is used as dichlorotrifluoroethane will be exemplified and explained.

FIG. 1 shows a temperature-vapor pressure diagram using the absorbent concentration as a parameter for the refrigeration composition of the present invention using R123a as a refrigerant and diethylene glycol dimethyl ether as an absorbent.

In general, a refrigeration cycle that uses fluorocarbons as a refrigerant involves the generation of fluorocarbon gas from a dilute absorbent solution (a solution with a high concentration of fluorocarbons), the condensation of the generated fluorocarbon gas, the evaporation (vaporization) of liquefied fluorocarbons, and the evaporation (vaporization) of a concentrated absorbent solution (a solution with a low concentration of fluorocarbons). This is achieved by repeating processes such as absorption of fluorocarbon gas into a solution), but the concentration of the absorbent dilute solution and concentrated solution depends on the operating conditions of the refrigerator,
i.e. the heating temperature of the dilute absorbent solution (temperature inside the generator);
It is arbitrarily set according to the evaporation temperature of liquefied fluorocarbon (temperature inside the evaporator) and the absorption temperature of fluorocarbon gas (temperature inside the absorber). In a refrigeration cycle using such CFCs as a refrigerant, as in the present invention, CFCs are used as refrigerants.
When R123a is used and diethylene glycol dimethyl ether is used as an absorbent, the liquefied R123a
When the evaporation temperature is about 0°C and the absorption temperature is about 42 to 54°C, the concentration of the dilute absorbent solution is about 52% by weight (hereinafter, % means % by weight unless otherwise specified), and the concentration of the concentrated solution is about 52% by weight. It is appropriate to set it to approximately 62%.

Incidentally, when the operating conditions are set to other than the above, the dilute solution concentration and concentrated solution concentration conditions of the absorbent can be changed accordingly. Furthermore, the refrigeration composition of the present invention uses a refrigeration cycle similar to the above, and a heat pump cycle (not shown) configured in a system in which an evaporator absorbs heat from outside air and a condenser or absorber releases heat. ) can also be applied as is.

Next, an example of the operation of an absorption refrigeration cycle using the refrigeration composition of the present invention will be explained based on the flow sheet of FIG. 2 and the operating cycle diagram of FIG. 3. The operating cycle diagram in Figure 3 is R123a in Figure 1.
- From the temperature-vapor pressure diagram of diethylene glycol dimethyl ether-based refrigeration composition, pure R123a and diethylene glycol dimethyl ether concentration is 52
This is an excerpt of the % and 62% line diagrams.

First, a 52% dilute solution of diethylene glycol dimethyl ether in which R123a was dissolved as a refrigerant (third
When the 52% dilute solution (point A in the figure) is heated to about 102°C using the external heat source 3 in the generator 1 at a temperature of about 88°C and a pressure of 1100 mmHg (absolute pressure; the same applies hereafter), the 52% dilute solution becomes a 62% concentrated solution ( During this time, R123a gas corresponding to a pressure of 1100 mmHg is generated. Next, this R123a gas is introduced into condenser 2 and cooled through cooling pipe 4 to approximately 40°C (the extension line from B to A is
It condenses and liquefies at the temperature at the point where it intersects the R123a line. Next, the pressure of the liquid R123a is reduced by the pressure reducing valve 5 and introduced into the evaporator 3. When the temperature inside the absorber 4 is set at approximately 42 to 54°C, the pressure inside the evaporator 3 is reduced to approximately 230 mmHg, which corresponds to the vapor pressure, and liquid R123a is sprayed from the nozzle 6 and evaporates at approximately 0°C. The heat of evaporation is then taken away from the brine flowing through the tube 7 to cool it and use it for freezing.

Next, the evaporated R123a gas is introduced into the absorber 4,
It is cooled from the generator 1 through the heat exchanger 8 to the nozzle 9.
It is absorbed into a 62% concentrated solution of diethylene glycol dimethyl ether (point C in Figure 3) at about 54°C which is sprayed from the solution. 10 is a cooling pipe for adjusting the temperature inside the absorber 4 within a predetermined range.

The concentrated solution that has absorbed the R123a gas is diluted to become a 52% dilute solution of diethylene glycol dimethyl ether (point D in Figure 3), and the concentrated solution and heat exchanger are sent from the generator 1 to the absorber 4 via the heat exchanger 8. After being replaced and heated, it is introduced into the generator 1 by the pump 11 (point A in Figure 3), and the same cycle is repeated thereafter.

In the above example, the case where the evaporation temperature of liquid R123a in the evaporator 3 was 0°C was explained, but the above operating conditions may be selected and implemented as appropriate depending on the degree or speed of freezing or cooling required. be able to.

As explained above, according to the refrigeration composition of the present invention which uses dichlorotrifluoroethane as a refrigerant and diethylene glycol dimethyl ether as an absorbent, as is clear from the above-mentioned operation cycle, the vapor pressure during operation is the highest. Approximately in the container
The vapor pressure is 1100 mmHg, which is considerably lower than the vapor pressure when using methane-based fluorocarbons, and the pressure-resistant structure of the refrigerator can be significantly relaxed.

In addition, small pieces of steel, stainless steel, and copper were separately immersed in 5 ml each of a 95% concentrated solution of R123a in diethylene glycol dimethyl ether and heated under reflux at 180°C for 10 days, but in all cases, almost no coloration was observed in the solution. Furthermore, the refrigeration composition of the present invention was found to have excellent corrosion resistance and thermal stability, and has extremely desirable characteristics as a refrigeration composition for absorption refrigerators. It has been demonstrated that

[Brief explanation of the drawing]

Figure 1 shows dichlorotrifluoroethane
Temperature-vapor pressure diagram using various concentrations of the absorbent as parameters for the refrigeration composition of the present invention using R123a as a refrigerant and diethylene glycol dimethyl ether as an absorbent, FIG. 2 is a flow sheet of an absorption refrigeration cycle, FIG. 3 is an operating cycle diagram using the refrigeration composition of the present invention. 1... Generator, 2... Condenser, 3... Evaporator,
4... Absorber, 5... Pressure reducing valve, 8... Heat exchanger,
11...Pump.

Claims (1)

[Claims] 1. A refrigeration composition for an absorption refrigerator, characterized in that dichlorotrifluoroethane is used as a refrigerant and diethylene glycol dimethyl ether is used as an absorbent.