IP Library Granted Patent US 7,109,248
Granted Patent B2
US 7,109,248 · App. 11/078,636 · Granted Sep 19, 2006

Converting natural gas to longer-chain hydrocarbons

View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 7,109,248
App. No.
11/078,636
Granted
Sep 19, 2006
Kind
B2
Abstract

Natural gas is processed to generate longer-chain hydrocarbons, the process comprising subjecting the gas to steam reforming to generate a mixture of carbon monoxide and hydrogen, and then subjecting this mixture to Fischer-Tropsch synthesis. The Fischer-Tropsch synthesis is performed at an elevated temperature above 230° C. and with a gas hourly space velocity greater than 10 000 hr −1 so as to achieve a selectivity to the production of C5+ hydrocarbons that is less than 65%. The resulting liquid product can be used as a vehicle fuel, while the tail gases may be used to generate electricity.

Claims (6)

1. A process for processing natural gas to generate longer-chain hydrocarbons, the process comprising subjecting the gas to steam reforming to generate a mixture of carbon monoxide and hydrogen, and then subjecting this mixture to Fischer-Tropsch synthesis in a reactor comprising a plurality of metal sheets in a stack, defining flow channels for the reaction and flow channels for a coolant, the channels being in good thermal contact with each other, wherein the Fischer-Tropsch synthesis is performed at an elevated temperature above 230° C. and with a gas hourly space velocity greater than 10,000 hr −1 so as to achieve a selectivity to the production of C5+hydrocarbons that is less than 65%, and a conversion of carbon monoxide that is no greater than 75%.

2. A process as claimed in claim 1 wherein the Fischer-Tropsch synthesis is performed at a pressure in the range 17–21 atmospheres.

3. A process as claimed in claim 1 wherein the output from the Fischer-Tropsch synthesis is separated by condensation into a liquid phase and a tail gas, and at least part of this tail gas is used to generate electricity.

4. A process as claimed in claim 3 wherein the electricity provides power to compress the gas mixture to a suitable pressure for the Fischer-Tropsch synthesis.

5. A process as claimed in claim 4 wherein electric power is also used to produce pure water suitable for use in the steam/methane reforming step.

6. A process for processing natural gas to generate longer-chain hydrocarbons, the process comprising subjecting the gas to steam reforming to generate a mixture of carbon monoxide and hydrogen, and then subjecting this mixture to Fischer-Tropsch synthesis in a reactor comprising a plurality of metal sheets in a stack, defining flow channels for the reaction and flow channels for a coolant, the channels being in good thermal contact with each other, wherein the Fischer-Tropsch synthesis is performed at an elevated temperature above 230° C. and with a gas hourly space velocity greater than 10,000 hr −1 so as to achieve a chain growth probability factor (α) not more than 0.7, and a conversion of carbon monoxide that is no greater than 75%.

Assignments (2)
NUNC PRO TUNC ASSIGNMENT Recorded Oct 21, 2006
From: GTL MICROSYSTEMS AG
To: COMPACTGTL PLC
Reel/Frame 018407/0951 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 21, 2005
From: BOWE, MICHAEL JOSEPH
To: GTL MICROSYSTEMS AG
Reel/Frame 016129/0376 →