# US 7,610,766 B2 · High-speed defrost refrigeration system

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- Number: US 7,610,766 B2
- Document ID: US7610766B2
- Status: Granted
- Kind: B2
- Application number: 11/056,117
- Filed: 2005-02-14
- Published: 2005-06-30
- Granted: 2009-11-03
- Earliest claimed: 2002-07-08
- Inventors: Serge Dubé
- Web page: https://patentgrep.com/patent/US7610766B2

## CPC

- F25B 5/02: arranged in parallel
- F25B 41/00: Fluid-circulation arrangements
- F25B 47/022: {hot gas defrosting}
- F25B 43/006: {Accumulators}
- F25B 2341/0015: using two or more ejectors
- F25B 2400/075: with parallel compressors
- F25B 2400/16: Receivers
- F25B: REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS

## Abstract

A defrost refrigeration system of the type having a main refrigeration circuit operating a refrigeration cycle. The defrost refrigeration system comprises a first line extending from the first compressor to the evaporator stage and is adapted to receive a portion of discharged low-pressure refrigerant from the first compressor. Valves are provided for stopping a suction of cooling refrigerant in an evaporator of the evaporator stage and for directing a flow of defrost refrigerant to release heat to defrost the evaporator. A second line is provided for directing the refrigerant having released heat to the expansion stage of the refrigeration cycle. A pressure reducing device is optionally positioned downstream of the condensing stage for adjusting a pressure of the refrigerant in the high-pressure liquid state mixing with the defrost refrigerant having released heat.

## Claims

### Claim 1

A defrost refrigeration system of the type having a main refrigeration circuit operating a refrigeration cycle, wherein a refrigerant goes through at least a compressing stage having at least a first and a second compressor, wherein said refrigerant is compressed to a high-pressure gas state to then reach a condensing stage, wherein said refrigerant in said high-pressure gas state is condensed at least partially to a high-pressure liquid state to then reach an expansion stage, wherein said refrigerant in said high-pressure liquid state is expanded to a first low-pressure liquid state to then reach an evaporator stage, wherein said refrigerant in said first low-pressure liquid state is evaporated, at least partially to a first low-pressure gas state by absorbing heat, to then return to said compressing stage, said defrost refrigeration system comprising a first line extending from said first compressor to the evaporator stage and adapted to receive all of the discharged refrigerant from said first compressor, a valve for stopping a suction by the compressing stage of said refrigerant in said first low-pressure liquid state in at least one evaporator of the evaporator stage and directing a flow of said discharged refrigerant to release heat to defrost the at least one evaporator and thereby changing phase at least partially to a second low-pressure liquid state, a second line for directing all of said refrigerant having released heat to the expansion stage of the refrigeration cycle, and a pressure reducing device downstream of the condensing stage for adjusting a pressure of the refrigerant in the high-pressure liquid state mixing with said refrigerant having released heat.

### Claim 2 (depends on 1)

The defrost refrigeration system according to claim 1, further comprising a pressure reducing device in the first line so as to reduce a pressure of the discharged low-pressure refrigerant prior to defrosting the at least one evaporator.

### Claim 3 (depends on 1)

The defrost refrigeration system according to claim 1, wherein all of the refrigerant in the high-pressure gas state discharged by the second compressor is directed to the condensing stage.

### Claim 4 (depends on 1)

The defrost refrigeration system in accordance with claim 1, further comprising a sub-cooling system liquefying a mixture of the cooling refrigerant and the defrost refrigerant.

### Claim 5 (depends on 1)

The defrost refrigeration system in accordance with claim 1, further comprising a sub-cooling system liquefying the cooling refrigerant prior to being mixed with the defrost refrigerant.

### Claim 6

A method for defrosting evaporators in a refrigeration system of the type having a cooling refrigerant circulating sequentially between a compression stage, a condensing stage, an expansion stage and an evaporation stage to then return to the compression stage, comprising:
i) stopping a suction of the cooling refrigerant in a first evaporator of the evaporation stage;
ii) directing defrost refrigerant from the compression stage to the first evaporator so as to defrost the first evaporator;
iii) directing the defrost refrigerant from the first evaporator upstream of the expansion stage; and
iv) mixing the cooling refrigerant exiting from the condensing stage with the defrost refrigerant by controlling a cooling refrigerant pressure downstream of the condensing stage; and
v) exposing the mixture of cooling refrigerant and defrost refrigerant to a heat exchanger to remove excess gas from the mixture;
vi) directing all of the mixture to the expansion stage;
whereby a second evaporator of the evaporation stage is cooled with the mixture of cooling refrigerant from the condensing stage with the defrost refrigerant.

### Claim 7 (depends on 6)

The method according to claim 6, wherein the defrost refrigerant in step ii) is compressed to a reduced pressure by a dedicated compressor.

### Claim 8 (depends on 6)

The method according to claim 6, wherein step ii) comprises converting a portion of the cooling refrigerant into the defrost refrigerant by reducing a pressure of the portion of the cooling refrigerant exiting the compression stage.

### Claim 9 (depends on 6)

The method according to claim 6, further comprising a step of liquefying the cooling refrigerant prior to step iv).

### Claim 10

A method for installing a defrost system in a refrigeration system of the type having a cooling refrigerant circulating sequentially during a refrigeration cycle between a compression stage, a condensing stage, an expansion stage and an evaporation stage to then return to the compression stage, comprising:
providing a valve to stop a suction of cooling refrigerant in at least a first evaporator of the evaporation stage;
positioning a first line feeding the first evaporator with defrost refrigerant from the compression stage in a defrost cycle;
positioning a second line between the first evaporator and a main line between the condensing stage and the expansion stage to direct the defrost refrigerant from the first evaporator to the main line to feed at least a second evaporator in the refrigeration cycle;
providing a pressure reducing device in the main line to reduce the pressure of the cooling refrigerant for a subsequent mixing with the defrost refrigerant from the second line in the refrigeration cycle; and
providing a sub-cooling system f or liquefying all of the mixture of cooling refrigerant and defrost refrigerant.

### Claim 11 (depends on 10)

The method according to claim 10, further comprising a step of providing a pressure reducing configuration so as to convert the cooling refrigerant fed to the first evaporator into a defrost refrigerant of a given reduced pressure.

### Claim 12 (depends on 11)

The method according to claim 11, wherein the pressure reducing configuration has a pressure regulator in the first line.

### Claim 13 (depends on 11)

The method according to claim 11, wherein the pressure reducing configuration has a compressor directly connected to the first line such that an output of the compressor is below an output of other compressors of the compression stage.

### Claim 14 (depends on 10)

The method according to claim 10, further comprising a step of providing a sub-cooling system for liquefying the cooling refrigerant prior to mixing the cooling refrigerant with the defrost refrigerant in the main line.
