Method of using an indirect heat exchanger and facility for processing liquefied natural gas comprising such heat exchanger

Patent metadata

Field	Value
Publication number	US-11988460-B2
Application number	US-201816617120-A
Country	US
Kind code	B2
Filing date	May 28, 2018
Priority date	May 30, 2017
Publication date	May 21, 2024
Grant date	May 21, 2024

Abstract

The invention relates to a method of using an indirect heat exchanger comprising a plurality of heat exchange modules arranged in a rectangular grid. Each heat exchange module comprises a plurality of first and second fluid flow channels extending in a first and second direction. The indirect heat exchanger comprises first and second manifolds fluidly connecting the first and second fluid flow channels of one heat exchange module with the first and second fluid flow channels of adjacent heat exchange modules thereby forming one or more first fluid paths. The invention also relates to a facility for processing liquefied natural gas including at least one indirect heat exchanger as described above.

First claim

What is claimed is:

1. A method of using an indirect heat exchanger comprising:
a first inlet for receiving a first fluid flow;
a first outlet for discharging the first fluid flow,
a second inlet for receiving a second fluid flow,
a second outlet for discharging the second fluid flow,
a first heat exchange module positioned adjacent to a second heat exchange module in a first direction;
a third heat exchange module positioned adjacent to the first heat exchange module or the second heat exchange module in a second direction;
a fourth heat exchange module positioned adjacent to the first heat exchange module or the second heat exchange module or the third heat exchange module in a third direction; wherein the first direction, the second direction, and the third direction are perpendicular with respect to each other; the heat exchange modules each comprising a first module face and a second module face being opposite to each other in the first direction, the heat exchange modules each comprising a third module face and a fourth module face being opposite to each other in the second direction, and the heat exchange modules each comprising a plurality of first fluid flow channels extending between the first module face and the second module face for accommodating the first fluid flow and a plurality of second fluid flow channels extending between the third module face and the fourth module face for accommodating the second fluid flow,
first manifolds fluidly connecting the plurality of first fluid flow channels of one of the heat exchange modules with the plurality of first fluid flow channels of an adjacent heat exchange module thereby forming one or more first fluid paths connecting the first inlet with the first outlet and running through two or more heat exchange modules, and
second manifolds fluidly connecting the plurality of second fluid flow channels of one of the heat exchange modules with the plurality of second fluid flow channels of an adjacent heat exchange module thereby forming one or more second fluid paths connecting the second inlet with the second outlet and running through two or more heat exchange modules;
wherein the first fluid flow channels having a first channel length, L 1 in the first direction, the first channel length L 1 being smaller or equal to the thermal entrance length L TL1 of the first fluid in the first fluid flow channels for predetermined design operating parameters of the indirect heat exchanger,
the second fluid flow channels having a second channel length L 2 in the second direction, the second channel length L 2 being smaller or equal to thermal entrance length L TL2 of the second fluid in the second fluid flow channels for predetermined design operating parameters of the indirect heat exchanger,
the method comprising the steps of:
bringing the first fluid flow in one of the first fluid flow channels and recollecting the first fluid flow in one of the first manifolds several times when traveling through the indirect heat exchanger;
bringing the second fluid flow in one of the second fluid flow channels and recollecting the second fluid flow in one of the second manifolds several times when traveling through the indirect heat exchanger, and
the first manifolds collecting the first fluid from one heat exchange module of the plurality of heat exchange modules, conveying at least part of the first fluid to an adjacent heat exchange module, and feeding the first fluid to the first fluid flow channels of the second heat exchange module,
wherein at least one of the first manifolds and the second manifolds fluidly connecting at least two of the heat exchange modules adjacent one another in the third direction.

2. The method of claim 1 , wherein the first channel length L 1 is longer or shorter than the second channel length L 2 .

3. The method of claim 1 , wherein the first heat exchange module and the second heat exchange module being adjacent in the first direction, wherein the first and adjacent heat exchange modules are positioned at an intermediate distance with respect to each other, thereby creating the first manifolds and wherein heat exchange modules adjacent in the second direction are positioned at an intermediate distance (dy) with respect to each other, thereby creating the second manifolds.

4. The method of claim 1 , wherein within the heat exchange modules the plurality of first fluid flow channels and the plurality of second fluid flow channels are stacked in the third direction.

5. The method of claim 1 , wherein the first manifolds fluidly connect the first and second heat exchange modules adjacent in the first direction, and the second manifolds fluidly connect the first and second heat exchange modules adjacent in the first direction.

6. The method of claim 1 , wherein the first manifolds fluidly connecting the heat exchange modules adjacent in the first direction and the first manifolds fluidly connecting two of the heat exchange modules adjacent in the second or third direction.

7. The method of claim 1 , wherein the second manifolds fluidly connecting two of the heat exchange modules adjacent in the second direction and the second manifolds fluidly connecting two of the heat exchange modules adjacent in the first or third direction.

8. The method of claim 1 , wherein the first inlet comprises a first distribution header, the first outlet comprises a first collection header, the second inlet comprises a second distribution header and the second outlet comprises a second collection header.

9. The method of claim 1 , wherein a first set of the first fluid paths and a first set of the second fluid paths being associated with a first set of the heat exchange modules and a second set of the first fluid paths and a second set of the second fluid paths being associated with a second set of the heat exchange modules.

10. The method of claim 1 , comprising the step of using the indirect heat exchanger for the processing of liquefied natural gas or liquefying natural gas.

11. The method of claim 1 , wherein the first fluid flow channels and/or the second fluid flow channels having a diameter of less than 1 mm.

12. The method of claim 1 , wherein the second manifolds collecting the second fluid from a heat exchange module, conveying at least part of the second fluid to an adjacent heal exchange module and feeding the second fluid to the second fluid flow channels of the adjacent heat exchange module.

13. The method of claim 1 , wherein the indirect heat exchanger comprising at least 8 heat exchanger modules.

14. The method of claim 10 , wherein
the first fluid being a refrigerant,
the second fluid being a process stream, and
flow rates of the refrigerant and the process stream being in the order of 0.5 to 20 m/s.

15. The method of claim 1 , further comprising the step of controlling a flow rate of the first fluid flow, inlet temperature of the first fluid flow, inlet pressure of the first fluid flow, flow rate of the second fluid flow, inlet temperature of the second fluid flow, inlet pressure of the second fluid flow, such that the first fluid flow and the second fluid flow are laminar in the first fluid flow channels and the second fluid flow channels.

16. The method of claim 15 , wherein the first fluid flow in the first fluid flow channels and the second fluid flow in the second fluid flow channels having a Reynolds number up to 900.

17. The method of claim 1 , wherein each module comprises a length and a width, each in a range from 10 cm and up to 50 cm, and a height in a range from 20 cm and up to 100 cm.

Assignees

• Shell Oil Co
• Shell Usa Inc

Inventors

• Botman Maarten Joannes
• Brinkert Jacob
• De Vries Marcel
• Niekerk Roy
• Scholten Rudolfus Johannes

Classifications

• F28D9/0093 Primary

  Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids · CPC title

• F25J1/0022

  Hydrocarbons, e.g. natural gas · CPC title

• F25J1/0235

  Heat exchange integration · CPC title

• F25J1/0272

  Multiple identical heat exchangers in parallel · CPC title

• F28D9/0043

  the plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another · CPC title