Process for reforming hydrocarbons and process for starting up a gas-to-liquid process

Patent metadata

Field	Value
Publication number	US-9428696-B2
Application number	US-201314409425-A
Country	US
Kind code	B2
Filing date	May 21, 2013
Priority date	Jun 19, 2012
Publication date	Aug 30, 2016
Grant date	Aug 30, 2016

Abstract

The invention relates to a process for the production of synthesis gas by the use of autothermal reforming or catalytic partial oxidation in which, after removal of water, effluent gas from the ATR or CPO is recycled to the feed of the ATR or CPO.

First claim

The invention claimed is:

1. A process for the production of synthesis gas from a hydrocarbon feedstock comprising:
adding steam to the hydrocarbon feedstock to form a mixture of hydrocarbons and steam,
passing said mixture through an autothermal reforming stage (ATR) or catalytic partial oxidation (CPO) stage and withdrawing a stream of hot effluent synthesis gas from the ATR or CPO,
removing water from said hot effluent synthesis gas to form a dehydrated synthesis gas, and
directly recycling at least a portion of said dehydrated synthesis gas into the hydrocarbon feedstock or into said mixture of hydrocarbons and steam, and without passing said dehydrated synthesis gas through a carbon-dioxide removal in the recycle, in which the molar ratio of dehydrated synthesis gas to mixture of hydrocarbons and steam is 0.1 to 2.5.

2. The process according to claim 1 in which the steam to carbon molar ratio at which the ATR or CPO is operated is 0.2 to 3.0.

3. The process according to claim 1 in which the dehydrated synthesis gas is introduced to the hydrocarbon feedstock or mixture of hydrocarbons and steam by a recycle-compressor.

4. The process according to claim 1 in which the dehydrated synthesis gas is introduced to the hydrocarbon feedstock or mixture of hydrocarbons and steam by an ejector.

5. The process according to claim 1 in which prior to removing water from said hot effluent synthesis gas, the synthesis gas is cooled by passing the synthesis gas through a cooling train of waste heat boilers and/or steam superheaters.

6. The process according to claim 1 in which the hot effluent synthesis gas is used as heat exchanging medium in a heat exchange reformer operated in series or in parallel with the ATR or CPO.

7. The process according to claim 1 in which said hydrocarbon feedstock is a gas that has passed through at least one pre-reforming stage.

8. The method according to claim 1 in which said hydrocarbon feedstock or said mixture of hydrocarbons and steam are preheated before being combined with said dehydrated synthesis gas.

9. A method for starting up a gas-to-liquid (GTL) process comprising:
adding steam to a hydrocarbon feedstock to form a mixture of hydrocarbons and steam,
passing said mixture through an autothermal reforming stage (ATR) or catalytic partial oxidation (CPO) stage and withdrawing a stream of hot effluent synthesis gas from the ATR or CPO,
removing water from said hot effluent synthesis gas to form a dehydrated synthesis gas,
directly recycling at least a portion of said dehydrated synthesis gas into the hydrocarbon feedstock or into said mixture of hydrocarbons and steam without passing said dehydrated synthesis gas through a carbon-dioxide removal in the recycle, and in which the molar ratio of dehydrated synthesis gas to mixture of hydrocarbons and steam is 0.1 to 2.5, and
subsequently passing at least part of the dehydrated synthesis gas as feed to downstream GTL process and shifting from recycling dehydrated synthesis gas to recycling off-gas.

10. The method according to claim 9 wherein the H 2 /CO molar ratio of the dehydrated synthesis gas is below 2.3.

11. The method according to claim 9 in which said hydrocarbon feedstock is a gas that has passed through at least one pre-reforming stage.

12. The method according to claim 9 in which said hydrocarbon feedstock or said mixture of hydrocarbons and steam are preheated in a fired-heater, before being combined with said dehydrated synthesis gas.

13. The method according to claim 9 in which the dehydrated synthesis gas is introduced to the hydrocarbon feedstock or mixture of hydrocarbons and steam by a recycle-compressor.

14. The method according to claim 13 in which the recycle-compressor is an existing recycle-compressor used for recycling off-gas from downstream gas-to-liquid (GTL) process.

15. The method according to claim 13 in which the off-gas after passing through the recycle-compressor is subjected to a conversion stage for removal of olefin by hydrogenation.

Assignees

• Haldor Topsoe As
• Haldor Topsoe As

Inventors

• Dahl Per Juul

Classifications

• C10G2/30 Primary

  from carbon monoxide with hydrogen · CPC title

• C01B2203/148

  involving a recycle stream to the feed of the process for making hydrogen or synthesis gas · CPC title

• C01B2203/1241

  Natural gas or methane · CPC title

• C01B3/382 Primary

  Processes with two or more reaction steps, of which at least one is catalytic, e.g. steam reforming and partial oxidation · CPC title

• Y02P20/129

  Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines · CPC title