Split refrigerant compressor for the liquefaction of natural gas

Patent metadata

Field	Value
Publication number	US-11268753-B2
Application number	US-201716320497-A
Country	US
Kind code	B2
Filing date	Jul 26, 2017
Priority date	Aug 1, 2016
Publication date	Mar 8, 2022
Grant date	Mar 8, 2022

Abstract

A compressor system is disclosed, including a first compressor unit having: at least a first gas inlet at a first gas pressure level; a second gas inlet at a second gas pressure level; and a gas discharge; a second compressor unit having: at least a third gas inlet at a third gas pressure level; a fourth gas inlet at a fourth gas pressure level; and a gas delivery. The gas discharge of the first compressor unit is fluidly coupled to one of the third gas inlet and fourth gas inlet of the second compressor unit.

First claim

What is claimed is:

1. A compressor system for compressing a first refrigerant comprising:
a first compressor unit comprising: a first gas inlet that is configured to receive the first refrigerant at a first gas pressure level; a second gas inlet that is configured to receive the first refrigerant at a second gas pressure level and is located downstream of the first gas inlet; and a gas discharge located downstream of the second gas inlet; and
a second compressor unit comprising: a third gas inlet that is configured to receive the first refrigerant at a third gas pressure level; a fourth gas inlet that is configured to receive the first refrigerant at a fourth gas pressure level and is located downstream of the third gas inlet;
wherein the gas discharge of the first compressor unit is fluidly coupled to the fourth gas inlet of the second compressor unit;
wherein the fourth gas pressure level is higher than the first gas pressure level and higher than the second gas pressure level, and the second gas pressure level is higher than the first gas pressure level; and
wherein (i) if the second gas pressure level is lower than the third pressure level, then the flow rate through a compression stage from the third gas inlet to fourth gas inlet is reduced, and (ii) if the second gas pressure level is higher than the third pressure level, then the flow rate through a compression stage from the second gas inlet to fourth gas inlet is reduced.

2. The compressor system of claim 1 , wherein the second compressor unit has only the third gas inlet and the fourth gas inlet as gas inlets.

3. The compressor system of claim 1 , wherein the first compressor unit has a first compressor stage with a single impeller and a second compressor stage with a single impeller, and
wherein the second compressor unit has a third compressor stage with a single impeller and a fourth compressor stage with two impellers.

4. The compressor system of claim 1 , wherein the first compressor unit is housed in a first casing, and the second compressor unit is housed in a second casing.

5. The compressor system of claim 1 , wherein the first straight compressor unit and the second compressor unit are housed in a common casing.

6. The compressor system of claim 5 , wherein a first impeller group consisting of impellers included in the first compressor unit and a second impeller group consisting of impellers included in the second compressor unit are positioned in line and in a back-to-back arrangement.

7. The compressor system of claim 1 , wherein the first compressor unit and the second compressor unit are arranged and control led to rotate at substantially the same rotational speed.

8. The compressor system of claim 1 , wherein the first compressor unit and the second compressor unit are arranged and controlled to rotate at different rotational speeds.

9. The compressor system of claim 8 , further comprising a gearbox arranged between the first compressor unit and the second compressor unit.

10. The compressor system of claim 8 , wherein the first compressor unit is driven by a first driver and the second compressor unit is driven by a second driver.

11. A refrigerant system for liquefaction of natural gas, comprising:
a natural gas line; and
at least a first refrigerant circuit comprising
the compressor system of claim 1 ;
a high-temperature heat exchange arrangement for discharging heat from a first refrigerant delivered by the compressor system; and
a low-temperature heat exchange arrangement, wherein the first refrigerant is in heat exchange relationship with at least one of a second refrigerant and natural gas flowing in the natural gas line to remove heat therefrom,

wherein the low-temperature temperature heat exchange arrangement comprises heat exchangers, each heat exchanger fluidly coupled with each gas inlet in the compressor system.

12. A method for compressing a first refrigerant by using a first compressor unit comprising: a first gas inlet; a second gas inlet located downstream of the first gas inlet; and a gas discharge located downstream of the second gas inlet and a second compressor unit comprising: a third gas inlet; a fourth gas inlet located downstream of the third gas inlet, the method comprising:
introducing a single gas flow of the first refrigerant at a first gas pressure level into the first gas inlet;
introducing a single gas flow of the first refrigerant at a second gas pressure level into the second gas inlet;
introducing a gas flow of the first refrigerant at a third gas pressure level into the third gas inlet;
introducing a gas flow of the first refrigerant at a fourth gas pressure level into the fourth gas inlet; and
introducing a gas flow of the first refrigerant from the first compressor unit into the fourth gas inlet of the second compressor unit,
wherein the fourth gas pressure level is higher than the first gas pressure level and higher than the second gas pressure level, and the second gas pressure level is higher than the first gas pressure; and
wherein (i) if the second gas pressure level is lower than the third pressure level, then the flow rate through a compression stage from the third gas inlet to fourth gas inlet is reduced, and (ii) if the second gas pressure level is higher than the third pressure level, then the flow rate through a compression stage from the second gas inlet to fourth gas inlet is reduced.

13. A natural gas liquefaction method comprising:
removing heat from a refrigerant flow of a first refrigerant compressed by the compressor system of claim 1 ;
dividing the refrigerant flow into a first partial stream, a second partial stream, a third partial stream and a fourth partial stream;
expanding each partial stream at a respective pressure level;
removing heat from at least one of a second refrigerant and natural gas flowing in a natural gas line by means of the partial streams;
introducing the first partial stream and the second partial stream into the first gas inlet and the second gas inlet of the first compressor unit of the compressor system respectively;
introducing the third partial stream and the fourth partial stream into the third gas inlet and the fourth gas inlet of a second compressor unit of the compressor system respectively; and
introducing the first refrigerant compressed by the first compressor unit into the fourth gas inlet of the second compressor unit.

14. The compressor system of claim 1 , wherein a single gas flow of the first refrigerant at the first gas pressure level and a single gas flow of the first refrigerant at the second gas pressure level are provided to the first compressor unit.

Assignees

• Nuovo Pignone Tecnologie Srl
• Nuovo Pignone Tech Srl

Inventors

• Grimaldi Angelo
• Pelagotti Antonio

Classifications

• F25J1/0214

  as a dual level refrigeration cascade with at least one MCR cycle · CPC title

• F25J2230/20

  Integrated compressor and process expander; Gear box arrangement; Multiple compressors on a common shaft · CPC title

• F25J1/0055

  originating from an incorporated cascade · CPC title

• F04D17/122 Primary

  the individual rotor discs being, one for each stage, on a common shaft and axially spaced, e.g. conventional centrifugal multi- stage compressors · CPC title

• F25J1/0022 Primary

  Hydrocarbons, e.g. natural gas · CPC title