Recompressed transcritical cycle with vaporization in cryogenic or low-temperature applications, and/or with coolant fluid

Patent metadata

Field	Value
Publication number	US-12066154-B2
Application number	US-202017598773-A
Country	US
Kind code	B2
Filing date	Mar 18, 2020
Priority date	Mar 29, 2019
Publication date	Aug 20, 2024
Grant date	Aug 20, 2024

Abstract

A process for regasifying a fluid and generating electrical energy includes subjecting an operating fluid to 1) pumping, the pumping step including a low pressure pumping step 1a) and a high pressure pumping step 1b), 2) heating in a recuperator to obtain a heated flow, the heating step including a low temperature heat recovery step 2a) and a high temperature heat recovery step 2b), 3) further heating through a high temperature source to obtain a further heated flow, 4) expanding in a turbine, with generation of electrical energy to obtain an expanded flow, 5) cooling by heat exchange to obtain a cooled flow, and 6) condensing the flow of the operating fluid and regasifying the fluid. After low pressure pumping, a portion of the flow of the operating fluid is subjected to recompression to obtain a flow combined with the flow of the operating fluid obtained from step 2a).

First claim

What is claimed is:

1. A process for regasifying a fluid and generating electrical energy, said process comprising subjecting a flow of an operating fluid to the following steps:
1) pumping, said pumping step comprising a low pressure pumping step 1a) using a low-pressure pump and a high pressure pumping step 1b) using a high-pressure pump,
2) heating in a recuperator, thus obtaining a heated flow, said heating step comprising a low temperature heat recovery step 2a), thus obtaining a first heated flow, and a high temperature heat recovery step 2b), thus obtaining a second heated flow,
3) further heating through a high temperature source, thus obtaining a further heated flow,
4) expanding in a turbine, with generation of electrical energy, thus obtaining an expanded flow,
5) cooling in a heat recuperator by heat exchange, in a step 5a) with the second heated flow of step 2b), and in a step 5b) with the first heated flow of step 2a), thus obtaining a cooled flow, and
6) condensing said cooled flow of said operating fluid to regasify said operating fluid,
wherein after the low pressure pumping step 1a), a portion of the flow of said operating fluid output from the low-pressure pump is subjected to a recompression step, thus obtaining a flow which is combined with the first heated flow of the operating fluid obtained from step 2a).

2. The process of claim 1 , wherein the portion of the flow of said operating fluid output from the low-pressure pump is subjected to a vaporization step prior to said recompression step.

3. The process of claim 2 , wherein said vaporization step is carried out by a low temperature heat source.

4. The process of claim 1 , wherein step 3) is carried out by a high temperature heat source.

5. The process of claim 1 , wherein an expansion step is carried out after step 5) and prior to step 6).

6. The process of claim 1 , wherein step 6) is carried out by heat exchange with said operating fluid.

7. The process of claim 1 , wherein step 6) is carried out by heat exchange by an intermediate fluid which acquires heat in step 6) and releases heat to said operating fluid.

8. The process of claim 1 , wherein a step of superheating said operating fluid is carried out after step 6).

9. The process of claim 8 , wherein said superheating step is carried out by a low temperature heat source.

10. A liquefied natural gas (LNG) regasification line comprising a regasification section for performing a process for regasifying a fluid and generating electrical energy, said process comprising subjecting a flow of an operating fluid to the following steps:
1) pumping, said pumping step comprising a low pressure pumping step 1a) using a low-pressure pump and a high pressure pumping step 1b) using a high-pressure pump,
2) heating in a recuperator, said heating step comprising a low temperature heat recovery step 2a), thus obtaining a first heated flow, and a high temperature heat recovery step 2b), thus obtaining a second heated flow,
3) further heating through a high temperature source, thus obtaining a further) heated flow,
4) expanding in a turbine, with generation of electrical energy, thus obtaining an expanded flow,
5) cooling in a heat recuperator by heat exchange, in a step 5a) with the second heated flow of step 2b), and in a step 5b) with the first heated flow of step 2a), thus obtaining a cooled flow, and
6) condensing said cooled flow of said operating fluid to regasify said operating fluid,
wherein after the low pressure pumping step 1a), a portion of the flow of said operating fluid output from the low-pressure pump is subjected to a recompression step, thus obtaining a flow which is combined with the first heated flow of the operating fluid obtained from step 2a),

wherein at least step 6) of said process is carried out inside said regasification section.

11. A liquefied natural gas (LNG) regasification plant comprising one or more regasification lines according to claim 10 .

Assignees

• Saipem Spa

Inventors

• Sbarsi Massimiliano
• Aurilio Lucio
• Fantolini Anton Marco
• De Rinaldis Salvatore

Classifications

• F17C2265/05

  Regasification · CPC title

• F17C2260/046

  Enhancing energy recovery · CPC title

• F17C2227/0362

  in a turbine · CPC title

• F17C2227/0327

  with recovery of heat · CPC title

• F17C2227/0323

  in a closed loop · CPC title