Methods, systems, and apparatuses for utilizing a fischer-tropsch purge stream
Systems, apparatuses and methods of utilizing a Fischer-Tropsch (“FT”) tail gas purge stream for recycling are disclosed. One or more methods include removing an FT tail gas purge stream from an FT tail gas produced by an FT reactor, treating the FT tail gas purge stream with steam in a water gas shift (“WGS”) reactor, having a WGS catalyst, to produce a shifted FT purge stream including carbon dioxide and hydrogen, and removing at least a portion of the carbon dioxide from the shifted FT purge stream, producing a carbon dioxide stream and a treated purge stream. Other embodiments are also disclosed.
1. A method of producing Fischer-Tropsch (“FT”) hydrocarbons via FT synthesis in an FT reactor having an FT synthesis catalyst, the method comprising:
a. producing a syngas comprising hydrogen and carbon monoxide in a syngas preparation unit, comprising a stream methane reformer, using a carbonaceous feed;
b. producing a liquid FT hydrocarbon stream, an FT tail gas stream and an FT water stream using the syngas gas as a feed in the FT reactor under FT operating conditions;
c. removing an FT tail gas purge stream from the FT tail gas stream, leaving a remainder FT tail gas stream;
d. treating the FT tail gas purge stream with steam in a water gas shift (“WGS”) reactor, having a WGS catalyst, to produce carbon dioxide and hydrogen, which form a shifted FT purge stream; and
e. treating the shifted FT purge stream in a carbon dioxide removal unit, which removes carbon dioxide from the shifted FT purge stream, producing a carbon dioxide stream and a treated purge stream; and
f. further comprising recycling the carbon dioxide stream as an input to the steam methane reformer.
2. The method of claim 1 , wherein the WGS reactor comprises a low temperature water gas shift reactor.
3. The method of claim 1 , wherein the WGS reactor comprises a medium temperature water gas shift reactor.
4. The method of claim 1 , wherein the WGS reactor comprises a high temperature water gas shift reactor.
5. The method of claim 1 , wherein two or more WGS reactors are used in series to treat the FT tail gas purge stream.
6. The method of claim 1 , further comprising recycling the remainder FT tail gas stream as an input to the syngas preparation unit.
7. The method of claim 1 , further comprising using the treated purge stream as fuel for the syngas preparation unit.
8. The method of claim 1 , further comprising using the treated purge stream to sweeten natural gas.
9. The method of claim 1 , further comprising using the treated purge stream to hydrotreat FT wax.
10. The method of claim 1 , wherein the carbon dioxide removal unit is an amine unit.
11. The method of claim 1 , wherein the carbon dioxide removal unit is carbon dioxide removal membrane.
12. A method of enhancing a Fischer-Tropsch (“FT”) purge stream, comprising:
a. removing an FT tail gas purge stream from an FT tail gas produced by an FT reactor, leaving a remainder FT tail gas;
b. treating the FT tail gas purge stream with steam in a water gas shift (“WGS”) reactor, having a WGS catalyst, to produce a shifted FT purge stream comprising carbon dioxide and hydrogen;
c. removing at least a portion of the carbon dioxide from the shifted FT purge stream, thereby producing a carbon dioxide stream and a treated purge stream; and
d. further comprising using the carbon dioxide stream as an input to a steam methane reformer acting as a syngas preparation unit.
13. The method of claim 12 , wherein the water gas shift reactor comprises a low temperature water gas shift reactor.
14. The method of claim 12 , wherein the water gas shift reactor comprises a medium temperature water gas shift reactor.
15. The method of claim 12 , wherein the water gas shift reactor comprises a high temperature water gas shift reactor.
16. The method of claim 12 , wherein two or more WGS reactors are used in series to treat the FT tail gas purge stream.
17. The method of claim 12 , further comprising recycling the remainder FT tail gas as an input to a front end of the steam methane reformer.
18. The method of claim 12 , further comprising using the treated purge stream as a fuel for the syngas preparation unit.
19. The method of claim 12 , wherein the step of removing at least a portion of the carbon dioxide from the shifted FT purge stream is performed using a carbon dioxide removal membrane.
20. The method of claim 12 , wherein the step of removing at least a portion of the carbon dioxide from the shifted FT purge stream is performed using an amine unit.
21. The method of claim 1 , further comprising removing a second portion of the FT tail gas from the FT tail gas and adding the second portion of the FT tail gas to the shifted purge stream to form a combined stream, prior to treatment of the combined stream in the carbon dioxide removal unit.
22. The method of claim 12 , further comprising removing a second portion of the FT tail gas from the FT tail gas and adding the second portion of the FT tail gas to the shifted purge stream to form a combined stream, prior to treatment of the combined stream in the carbon dioxide removal unit.