# US 12,222,143 B2 · Vapor compression system and method for vapor oil recovery

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- Number: US 12,222,143 B2
- Document ID: US12222143B2
- Status: Granted
- Kind: B2
- Application number: 17/301,263
- Filed: 2021-03-30
- Published: 2021-10-14
- Granted: 2025-02-11
- Earliest claimed: 2020-04-08
- Assignees: Carrier Corporation
- Applicants: Carrier Corporation
- Inventors: Anthony S. Molavi; Scott T. McDonough; William T. Slay
- Web page: https://patentgrep.com/patent/US12222143B2

## CPC

- F25B 31/004: {oil recirculating arrangements}
- F25B 43/02: for separating lubricants from the refrigerant
- F25B 13/00: Compression machines, plants or systems, with reversible cycle (defrosting cycles F25B47/02)
- F25B 41/40: Fluid line arrangements
- F25B 49/02: for compression type machines, plants or systems
- F25B 2400/0411: for expansion valves or capillary tubes
- F25B 2400/13: Economisers
- F25B 2400/23: Separators
- F25B 2600/2501: Bypass valves
- F25B: REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS

## Abstract

A vapor compression system including: a compressor having a compressor suction port and a compressor discharge port configured to circulate a working fluid through a flow circuit; a first heat exchanger operably coupled to the compressor discharge port; a second heat exchanger operably coupled to the compressor suction port; a heat recovery heat exchanger operably coupled to the first and second heat exchangers wherein the heat recovery heat exchanger is configured to: receive the working fluid in a first phase from the first heat exchanger; receive the working fluid in a second phase from the second heat exchanger; exchange heat between the working fluid in the first phase and the second phase; and a bypass valve positioned between the heat recovery heat exchanger discharge and the second heat exchanger and defining a first flow path and a second flow path.

## Claims

### Claim 1

A vapor compression system, comprising:
a compressor having a suction port and a discharge port configured to circulate a working fluid through a flow circuit;
a first heat exchanger operably coupled to the compressor discharge port;
a second heat exchanger operably coupled to the compressor suction port;
a heat recovery heat exchanger operably coupled to the second heat exchanger and the first heat exchanger, wherein the heat recovery heat exchanger has a first portion for receiving a first phase and a second portion for receiving a second phase, and the heat recovery heat exchanger is configured to:
receive the working fluid in the first phase from the first heat exchanger,
receive the working fluid in the second phase from the second heat exchanger, and
exchange heat between the working fluid in the first phase and the second phase;
an orifice and a bypass valve positioned between the heat recovery heat exchanger discharge and the second heat exchanger and defining a first flow path and a second flow path, wherein the heat recovery heat exchanger is located between the first heat exchanger and the second heat exchanger in the flow circuit; and
a controller in communication with the bypass valve and the compressor, the controller being configured to:
determine when the compressor is operating below a predetermined operating load capacity;
open the bypass valve allowing the working fluid in the first phase to flow from the first portion of the heat recovery heat exchanger through the first flow path via the orifice and the second flow path via the bypass valve, to the second heat exchanger, when a compressor load is equal to or less than the predetermined operating load capacity; and
close the bypass valve allowing the working fluid in the first phase to flow from the first portion of the heat recovery heat exchanger through the first flow path via the orifice to the second heat exchanger, when the compressor load is greater than the predetermined operating load capacity.

### Claim 2 (depends on 1)

The vapor compression system of claim 1, wherein the working fluid in the first phase comprises a mixture of vapor refrigerant and oil, and the working fluid in the second phase comprises a mixture of liquid refrigerant and oil.

### Claim 3 (depends on 1)

The vapor compression system of claim 1, wherein the predetermined operating load capacity comprises 25% of the maximum operating load capacity.

### Claim 4 (depends on 1)

The vapor compression system of claim 1, wherein the controller comprises:
a memory configured to store the predetermined operating load capacity; and
a processor operably coupled to the memory, wherein the controller is configured to:
receive a signal indicative of the compressor load; and
compare the operating compressor load to at least one signal indicative of the predetermined operating load capacity.

### Claim 5 (depends on 4)

The vapor compression system of claim 4, wherein the predetermined operating load capacity is equal to or greater than 25% of the compressor maximum operating load capacity.

### Claim 6 (depends on 1)

A method of operating the vapor compression system as described in claim 1, the method comprising:
operating a compressor to direct a working fluid in a first phase through a first heat exchanger and a heat recovery heat exchanger;
operating the heat recovery heat exchanger to direct the working fluid in the first phase through at least one of an orifice and a bypass valve;
determining whether a compressor operating load is equal to or less than a predetermined operating load capacity;
operating a controller to direct the working fluid in the first phase to a second heat exchanger by a first flow path when the compressor operating load is greater than a predetermined operating load capacity; and
operating the controller to direct the working fluid in the first phase to the second heat exchanger by the first flow path and a second flow path when the compressor operating load is less than or equal to the predetermined operating load capacity.

### Claim 7 (depends on 6)

The method of claim 6, wherein the predetermined operating load capacity comprises 25% of the maximum operating load capacity of the compressor.

### Claim 8 (depends on 6)

The method of claim 6, wherein the compressor comprises a screw compressor configured to operate at variable loads.

### Claim 9 (depends on 6)

The method of claim 6, wherein working fluid comprises a refrigerant/oil mixture having a first phase and a second phase, wherein,
the first phase comprises a mixture of vapor refrigerant and oil, and
the second phase comprises a mixture of liquid refrigerant and oil.

### Claim 10 (depends on 6)

The method of claim 6, wherein the predetermined operating load capacity is equal to or greater than 25% of the compressor maximum operating load capacity.
