Heat exchangers for low temperature carbon dioxide separation from natural gas

Patent metadata

Field	Value
Publication number	US-10281209-B2
Application number	US-201715846898-A
Country	US
Kind code	B2
Filing date	Dec 19, 2017
Priority date	Jun 30, 2015
Publication date	May 7, 2019
Grant date	May 7, 2019

Abstract

A reboiler in fluid communication with a fractionator column in an offshore low temperature process removing carbon dioxide from natural gas has a vessel volume. A carbon steel tubing bundle is disposed within the vessel volume. Each tube in the bundle has an outer surface with a porous granular metal layer deposited thereon. The granular metal layer comprises a pore size distribution which promotes bubble nucleation during vaporization of a nearly pure liquid carbon dioxide stream.

First claim

The invention claimed is:

1. A reboiler in fluid communication with a fractionator column in an offshore low temperature system removing carbon dioxide from natural gas, the bottom reboiler comprising:
a rigid vessel having an outer shell defining a vessel volume, the rigid vessel having an inlet in fluid communication with a fractionator for receiving a liquid stream therefrom and an outlet for returning a vapor to the fractionator; and
a carbon steel tubing bundle disposed within the vessel volume each tube in the carbon steel tubing bundle having an outer surface and an inner surface, the outer surface having a granular metal layer deposited thereon, and the inner surface being generally smooth relative thereto, wherein the granular metal layer comprises a pore size distribution adapted to promote and increase bubble nucleation during vaporization of a nearly pure liquid carbon dioxide stream on the outer surfaces of the tubes and wherein the outer surface having the granular metal layer deposited thereon increases an overall heat transfer coefficient of each tube in the carbon steel tubing bundle by at least 1.3 times that of a bare outer surface of a tube in an otherwise identical carbon steel tubing bundle.

2. The reboiler of claim 1 wherein the granular metal layer is metallurgically bonded to each tube in the carbon steel tubing bundle.

3. The reboiler of claim 1 wherein the shell is produced from a carbon steel.

4. The reboiler of claim 1 wherein a weight of the reboiler is less than 27,000 kg.

5. The reboiler of claim 1 wherein a weight of the reboiler is less than 22,000 kg.

6. The reboiler of claim 1 wherein the inner surface has a plurality of fins extending radially inwardly relative thereto.

7. The reboiler of claim 1 wherein the reboiler is a bottom reboiler which receives a liquid bottoms stream from a fractionator column.

8. The reboiler of claim 1 wherein the carbon steel tubing bundle is horizontally disposed within the vessel volume.

9. The reboiler of claim 1 wherein the nearly pure liquid carbon dioxide stream within the reboiler has a purity of greater than 90 mol %.

10. The reboiler of claim 1 wherein the nearly pure liquid carbon dioxide stream within the reboiler has a purity greater than 95 mol %.

11. The reboiler of claim 1 wherein the nearly pure liquid carbon dioxide stream within the reboiler has a purity of about 97 mol %.

12. The reboiler of claim 1 wherein a temperature of a bottoms stream entering the reboiler is between 10.4° C. and 10.8° C.

13. The reboiler of claim 1 wherein a bottoms stream inlet operating pressure is about 46.5 bar-g.

14. The reboiler of claim 1 wherein a tube-side stream temperature within the carbon steel tubing bundle is between 20.9° C. and 32.5° C.

15. The reboiler of claim 1 wherein a tube-side stream temperature within the carbon steel tubing bundle is between 15.5° C. and 25.0° C.

16. The reboiler of claim 1 wherein an outside tube diameter in the carbon steel tubing bundle is less than 5.0 cm.

17. The reboiler of claim 1 wherein an outside tube diameter in the carbon steel tubing bundle is less than or equal to 2.5 cm.

18. A reboiler in fluid communication with a fractionator column in an offshore low temperature system removing carbon dioxide from natural gas, the reboiler comprising:
a rigid vessel having a carbon steel outer shell defining a vessel volume, the rigid vessel having an inlet in fluid communication with the fractionator for receiving a liquid stream therefrom and an outlet for returning a vapor to the fractionator;
a carbon steel tubing bundle horizontally disposed within the vessel volume, each tube in the carbon steel bundle having an outer surface and an inner surface, the outer surface having a granular metal layer deposited thereon, and the inner surface having a plurality of fins extending radially inwardly relative thereto, wherein the granular metal layer comprises a pore size distribution adapted to promote and increase a bubble nucleation during vaporization of liquid carbon dioxide on the outer surfaces of the tubes; and
a liquid carbon dioxide stream within the rigid vessel having a purity greater than 90 mol %, wherein the outer surface having the granular metal layer deposited thereon increases an overall heat transfer coefficient (U-value) of each tube in the carbon steel tubing bundle at least 1.3 times that of a bare outer surface of a tube in an otherwise identical carbon steel tubing bundle.

Assignees

• Uop Llc

Inventors

• Zhou Lubo
• Godry Thomas J
• Xu Zhanping

Classifications

• B01D53/002

  by condensation · CPC title

• Y02P70/34

  Cross-Sectional Technologies · mapped topic

• F25J2290/44

  Particular materials used, e.g. copper, steel or alloys thereof or surface treatments used, e.g. enhanced surface · CPC title

• F28F2009/226

  Transversal partitions · CPC title

• B01D53/00

  Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols, (recovery of volatile solvents by condensation B01D5/00; sublimation B01D7/00; cold traps, cold baffles B01D8/00; working-up undefined gaseous mixtures obtained by cracking hydrocarbon oils C10G70/00; cleaning coal gas C10K; working-up of natural gas, or synthetic natural gas, C10L3/10; separation of difficult-to-condense gases or air by liquefaction F25J; for investigating materials G01N30/00) · CPC title