IP Library › Granted Patent US 7,299,653
Granted Patent B2
US 7,299,653 · App. 10/537,261 · Granted Nov 27, 2007

Refrigerator system using non-azeotropic refrigerant, and non-azeotropic refrigerant for very low temperature used for the system

Assignee: Nihon Freezer Co., Ltd.
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 7,299,653
App. No.
10/537,261
Granted
Nov 27, 2007
Kind
B2
Abstract

A single-stage refrigerating system includes a compressor, a condenser, an evaporator, and a heat exchanger for exchanging heat between a refrigerant in a path from the evaporator to the compressor and a refrigerant in another path from the condenser to the evaporator, and a non-azeotropic refrigerant mixture used in the system. The refrigerant mixture is a combination of a refrigerant having a normal boiling point of approximately room temperature and a low-boiling-point refrigerant having a normal boiling point below −60° C. A dew point of the refrigerant mixture at a pressure in the condensing process after the compression is above room temperature. The boiling point is higher than the dew point at a pressure in the lower-pressure region in a path from the evaporator to the compressor. The combination may include butane or isobutane as the high-boiling-point refrigerant component having a normal boiling point of approximately room temperature and having a low evaporating pressure and ethane or ethylene as the low-boiling-point refrigerant component suitable for achieving ultra-low temperature.

Claims (31)

1. A refrigerating system using a non-azeotropic refrigerant mixture, wherein

the non-azeotropic refrigerant mixture comprises a refrigerant having a normal boiling point of approximately room temperature and a low-boiling-point refrigerant having a normal boiling point of −60° C. or less;

the refrigerating system is a single-stage refrigerating system comprising a compressor, a condenser, an evaporator, and a heat exchanger for exchanging heat between a refrigerant in a path from the evaporator to the compressor and a refrigerant in another path from the condenser to the evaporator;

a dew point of the refrigerant mixture at a pressure in the condensing process after the compression is above room temperature; and

the refrigerating system is operated in the range in which the boiling point is higher than the dew point at a pressure in the lower-pressure region in the path from the evaporator to the compressor.

2. A non-azeotropic refrigerant mixture used in a single-stage refrigerating system comprising a compressor, a condenser, an evaporator, and a heat exchanger for exchanging heat between a refrigerant in a process from the evaporator to the compressor and a refrigerant in a path from the condenser to the evaporator, wherein

the non-azeotropic refrigerant mixture comprises a refrigerant having a normal boiling point of approximately room temperature and a low-boiling-point refrigerant having a normal boiling point of −60° C. or less;

a dew point of the refrigerant mixture at a pressure in the condensing process after the compression is above room temperature; and

the boiling point is higher than the dew point at a pressure in the lower-pressure region in the path from the evaporator to the compressor.

3. The non-azeotropic refrigerant mixture for ultra-low temperature according to claim 2 , wherein

the high-boiling-point refrigerant gas having a normal boiling point of approximately room temperature is at least one selected from the group consisting of butane, isobutane, butanes, R134a, and ethylacetylene; and

the low-boiling-point refrigerant gas having a normal boiling point of −60° C. or less is at least one selected from the group consisting of ethane, ethylene, and R-14.

4. The non-azeotropic refrigerant mixture for ultra-low temperature according to claim 3 , wherein

the high-boiling-point refrigerant gas having a normal boiling point of approximately room temperature is butane or isobutane;

the low-boiling-point refrigerant gas having a normal boiling point of −60° C. or less is ethane or ethylene; and

the characteristics are improved by adding R-14 (perfluoromethane) to the gas mixture.

5. The non-azeotropic refrigerant mixture for ultra-low temperature according to claim 4 , wherein

the high-boiling-point gas is butane and the low-boiling-point gas is ethane;

the mixing ratio of the butane-ethane gas mixture is in the range from 90/10 to 60/40; and

the content of R-14 (perfluoromethane) in the gas mixture is between above 0% and 9%.

6. The non-azeotropic refrigerant mixture for ultra-low temperature according to claim 4 , wherein

the high-boiling-point gas is butane and the low-boiling-point gas is ethylene;

the mixing ratio of the butane-ethylene gas mixture is in the range from 90/10 to 70/30; and

the content of R-14 (perfluoromethane) in the gas mixture is between above 0% and 7.5%.

7. The non-azeotropic refrigerant mixture for ultra-low temperature according to claim 4 , wherein

the high-boiling-point gas is isobutane and the low-boiling-point gas is ethane;

the mixing ratio of the isobutane-ethane gas mixture is in the range from 90/10 to 70/30; and

the content of R-14 (perfluoromethane) in the gas mixture is between above 0% and 15%.

8. The non-azeotropic refrigerant mixture for ultra-low temperature according to claim 4 , wherein p 1 the high-boiling-point gas is isobutane and the low-boiling-point gas is ethylene;

the mixing ratio of the isobutane-ethylene gas mixture is in the range from 90/10 to 80/20; and

the content of R-14 (perfluoromethane) in the gas mixture is between above 0% and 10%.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 24, 2007
From: KURITA, SUSUMU; KURITA, NOBUYOSHI
To: NIHON FREEZER CO., LTD.
Reel/Frame 019604/0477 →
Continuity (1)
Related Publication 20060065013A1 · Mar 30, 2006