Apparatus and process for treating natural gas

Patent metadata

Field	Value
Publication number	US-10010858-B2
Application number	US-201615012965-A
Country	US
Kind code	B2
Filing date	Feb 2, 2016
Priority date	Jan 5, 2010
Publication date	Jul 3, 2018
Grant date	Jul 3, 2018

Abstract

A process is described for treating a natural gas stream containing methane and one or more higher hydrocarbons including the steps of mixing at least a portion of the natural gas stream with steam; passing the mixture adiabatically over a supported precious metal reforming catalyst to generate a reformed gas mixture comprising methane, steam, carbon dioxide, carbon monoxide and hydrogen; cooling the reformed gas mixture to below the dew point to condense water and removing the condensate to provide a de-watered reformed gas mixture, and passing the de-watered reformed gas mixture through an acid gas recovery unit to remove carbon dioxide and at least a portion of the hydrogen and carbon monoxide, thereby generating a methane stream. The methane stream may be used to adjust the composition of a natural gas stream, including a vaporized LNG stream, to meet pipeline specifications.

First claim

What is claimed:

1. An apparatus for treating a natural gas stream containing methane and one or more higher hydrocarbon comprising:
(i) means for adding steam and hydrogen to a natural gas stream,
(ii) a reformer vessel operatively connected to the means for adding steam and hydrogen, said reformer vessel containing a catalyst consisting of a supported precious metal reforming catalyst, configured such that the natural gas stream, steam, and hydrogen are passed over the catalyst to generate a reformed gas mixture comprising methane, steam, carbon dioxide, carbon monoxide and hydrogen,
(iii) heat exchange means operatively connected to the reformer vessel to cool the reformed gas mixture to below the dew point and separation equipment operatively connected to the heat exchange means to recover process condensate and provide a de-watered reformed gas mixture,
(iv) an acid gas recovery unit operatively connected to the separation equipment to remove carbon dioxide and at least a portion of the hydrogen and carbon monoxide, thereby generating a methane stream, and
(v) a drying unit comprising a bed of a solid desiccant or a liquid desiccant compound for drying the methane stream.

2. The apparatus according to claim 1 further comprising a natural gas liquefaction unit operatively connected to the acid gas recovery unit to liquefy at least a portion of the methane stream.

3. The apparatus according to claim 1 forming part of an offshore natural gas processing facility that is a fixed off-shore facility or a floating off-shore facility.

4. The apparatus according to claim 1 comprising means to supply at least one of natural gas, a synthetic natural gas mixture comprising methane, or one or more higher hydrocarbon to the means for adding steam and hydrogen, wherein the natural gas comprises at least one of associated gas, shale gas, tight sand gas, or coal bed methane.

5. The apparatus according to claim 1 comprising a purification unit containing a purification material suitable for removing mercury, said unit installed upstream of the means for adding steam and hydrogen.

6. The apparatus according to claim 1 further comprising a desulphuriser vessel containing one or more purification material suitable for removing a sulphur compound, said unit installed upstream of the means for adding steam and hydrogen.

7. The apparatus according to claim 6 comprising a fired heater through which is passed the natural gas stream and optionally a portion of the steam fed to the reformer vessel, said heater installed upstream of said desulphuriser vessel.

8. The apparatus according to claim 1 wherein the means for adding steam and hydrogen comprises a saturator.

9. The apparatus according to claim 1 wherein the steam reformer is an adiabatic steam reformer vessel containing a supported precious metal catalyst comprising 0.1-10% by weight of one or more of Pt, Pd, Ir, Rh, or Ru.

10. The apparatus according to claim 1 further comprising one or more heat exchanger, configured to exchange heat between the reformed gas mixture and water to generate at least a portion of the steam fed to the reformer vessel.

11. The apparatus according to claim 1 wherein the separation equipment is operatively connected to the means for adding steam and hydrogen to the natural gas stream so that at least a portion of the recovered condensate is used to generate at least a portion of the steam added to the natural gas stream.

12. The apparatus according to claim 1 wherein the acid gas recovery unit comprises at least one of a membrane, a physical wash solvent system, or an amine wash system.

13. The apparatus according to claim 1 further comprising a mixing unit configured to combine natural gas with the de-watered reformed gas mixture or methane stream to provide a methane-enriched natural gas.

14. The apparatus according to claim 1 , wherein the heat exchange means is a heat exchanger.

Assignees

• Johnson Matthey Plc

Inventors

• Catchpole Stephen John

Classifications

• C01B3/38

  using catalysts · CPC title

• B01J2219/00103

  in a heat exchanger separate from the reactor · CPC title

• C10L3/08 Primary

  Production of synthetic natural gas · CPC title

• C10L2290/06

  Heat exchange, direct or indirect · CPC title

• F25J1/0022

  Hydrocarbons, e.g. natural gas · CPC title