Methods and apparatuses for removal of hydrogen sulfide and carbon dioxide from biogas

Patent metadata

Field	Value
Publication number	US-9339760-B2
Application number	US-201313834494-A
Country	US
Kind code	B2
Filing date	Mar 15, 2013
Priority date	Jun 11, 2010
Publication date	May 17, 2016
Grant date	May 17, 2016

Abstract

Methods, systems and apparatuses herein provide a unique and novel process to remove H 2 S from biogas. Methods, systems and apparatuses herein provide a unique and novel process to remove H 2 S from biogas with ease of operation and reduced operating and capital costs. Methods, systems and apparatuses herein provide a unique and novel process to remove H 2 S over CO 2 from biogas.

First claim

We claim:

1. A method for removing contaminants in a biogas comprising:
(a) heating and aerating anaerobic digester effluent in an aeration reactor to produce a first effluent with an alkaline pH;
(b) contacting the first effluent from step (a) with an input biogas in a reactor to produce a treated biogas and a second effluent that has a lower pH as compared to the pH of the first effluent;
(c) recovering the treated biogas from step (b), wherein the treated biogas has less H 2 S as compared to the input biogas;
(d) aerating the second effluent of step (b) to produce a third effluent, wherein the third effluent has an alkaline pH; and
(e) contacting the third effluent of step (d) with the recovered biogas of step (c) to remove CO 2 in the biogas.

2. The method of claim 1 , wherein heating the anaerobic digester effluent comprises using a heat exchanger with the exhaust from a biogas engine as the heated air stream.

3. The method of claim 1 , wherein heating the anaerobic digester effluent comprises heating the effluent to a temperature from about 140° F. to about 170° F.

4. The method of claim 1 , wherein aerating the anaerobic digester effluent is accomplished using micro-aerators that aerate the effluent at a rate from 5 gallons/cfm to 25 gallons/cfm.

5. The method of claim 1 , wherein contacting the alkaline effluent with an input biogas comprises using an alkaline effluent with a pH from about 9.0 to about 12.0.

6. The method of claim 1 , wherein contacting an input biogas with the alkaline effluent comprises using a bubble column reactor.

7. The method of claim 6 , wherein the bubble column reactor has an inlet orifice sparger.

8. The method of claim 6 , wherein the bubble column has a churn-turbulent flow regime.

9. The method of claim 1 , wherein contacting the alkaline effluent with an input biogas comprises a gas:liquid ratio selected from the group consisting of: 20:1, 21:1, 22:1, 23:1, 24:1, 25:1, 26:1, 27:1, 28:1, 29:1, and 30:1.

10. The method of claim 1 , wherein contacting the alkaline effluent with an input biogas comprises a gas:liquid ratio of 21-25:1.

11. A method for removing contaminants in a biogas comprising:
(a) aerating an anaerobic digester effluent that has previously been mixed with a biogas; and
(b) remixing the aerated anaerobic digester effluent of step (a) with the same biogas that had previously been mixed with an anaerobic digester effluent to remove contaminants from the biogas.

Assignees

• Kennedy Nicholas
• Zhao Quan-Bao
• Jiang Anping
• Frear Craig
• Dvorak Stephen W
• Dvo Inc
• Univ Washington State

Inventors

• Kennedy Nicholas
• Zhao Quan-Bao
• Jiang Anping
• Frear Craig
• Dvorak Stephen W

Classifications

• C05F17/15

  the material being gas · CPC title

• C05F17/50

  Treatments combining two or more different biological or biochemical treatments, e.g. anaerobic and aerobic treatment or vermicomposting and aerobic treatment · CPC title

• C02F3/30

  Aerobic and anaerobic processes · CPC title

• C10L2290/542

  Adsorption of impurities during preparation or upgrading of a fuel · CPC title

• C05F17/40 Primary

  Treatment of liquids or slurries · CPC title