Method for the purification of gases containing volatile organic compounds

Patent metadata

Field	Value
Publication number	US-9975088-B2
Application number	US-201515113830-A
Country	US
Kind code	B2
Filing date	Jan 23, 2015
Priority date	Feb 3, 2014
Publication date	May 22, 2018
Grant date	May 22, 2018

Abstract

The present invention relates to a method for purifying a gas comprising: a) feeding the gas ( 1 ) to an absorber ( 5 ) and bringing into contact said gas ( 1 ) with a stream ( 3 ) (or alternatively ( 3 ′)) to obtain a liquid ( 4 ) and a purified gas stream ( 2 ); b) feeding the liquid ( 4 ) to a conditioning tank ( 9 ) and adding a mineral nutrient medium ( 6 ) and a suitable amount of base ( 7 ) to the liquid ( 4 ) to obtain a liquid effluent ( 8 ); c) feeding the liquid effluent ( 8 ) to an anaerobic bioreactor ( 14 ) to obtain a biomethane stream ( 11 ) and a liquid stream ( 12 ); d) feeding the liquid stream ( 12 ) to a degasser ( 20 ) to obtain a gas stream ( 18 ) and a stream ( 3 ′); and e) recirculating the stream ( 3 ′) by feeding it to the absorber ( 5 ).

First claim

The invention claimed is:

1. A method for purifying a gas containing volatile organic compounds which comprises:
a) feeding the gas ( 1 ) to an absorber ( 5 ) and bringing into contact said gas ( 1 ) with an aqueous stream ( 3 ) the pH of which is comprised between 8.0 and 9.5 to obtain a liquid ( 4 ) comprising volatile organic compounds, and a purified gas stream ( 2 );
b) feeding the liquid ( 4 ) comprising volatile organic compounds obtained in step a) to a conditioning tank ( 9 ) and adding a mineral nutrient medium ( 6 ) and a suitable amount of base ( 7 ) to the liquid ( 4 ) to obtain a liquid effluent ( 8 ) the pH of which is comprised between 7.5 and 10 and the total alkalinity of which is comprised between 750 and 5,000 mg CaCO 3 /L;
c) feeding the liquid effluent ( 8 ) obtained in step b) to an anaerobic bioreactor ( 14 ) to obtain a biomethane stream ( 11 ) wherein the percentage of carbon dioxide is equal to or less than 15% by volume with respect to the volume of the stream ( 11 ) expressed as a dry base, and an output liquid stream ( 12 ) exiting the bioreactor the pH of which is comprised between 7.0 and 8.5;
d) feeding the output liquid stream ( 12 ) exiting the bioreactor obtained in step c) to a degasser ( 20 ) to obtain a gas stream ( 18 ) comprising methane, and an aqueous stream ( 3 ′); and
e) recirculating the aqueous stream ( 3 ′) by feeding it to the absorber ( 5 );
wherein:
total alkalinity of each of the streams of steps a), c), d) and e) and of each of said absorber ( 5 ), conditioning tank ( 9 ), anaerobic bioreactor ( 14 ) and degasser ( 20 ) is equal to total alkalinity of the liquid effluent ( 8 ) of step b) ±20% of the total value.

2. The method according to claim 1 , further comprising purge ( 21 ) and the addition of an aqueous stream ( 19 ) after step d), wherein the daily purge volume is comprised between 1 and 10% by volume with respect to total liquid volume of the system.

3. The method according to claim 1 , which further comprises feeding the aqueous stream ( 3 ′) obtained in step d) to a buffer tank ( 22 ) to obtain the stream ( 3 ) and recirculating said stream ( 3 ) by feeding it to the absorber ( 5 ).

4. The method according to claim 1 , wherein the method further comprises carrying out additional steps f), g) and h) before step a), wherein said steps comprise:
f) feeding the gas ( 1 ) to an alkaline scrubber ( 27 ) and bringing into contact said gas ( 1 ) with an aqueous stream ( 28 ) at a pH comprised between 11 and 13to obtain a liquid stream ( 23 ) and the gas stream ( 1 ′);
g) feeding the liquid stream ( 23 ) obtained in step f) to a hydrolysis tank ( 25 ) and adding a suitable amount of base ( 24 ) to the stream ( 23 ) to obtain a liquid effluent ( 26 ) and the aqueous stream ( 28 ); and
h) feeding the liquid effluent ( 26 ) obtained in step g) to the conditioning tank ( 9 ) and recirculating the aqueous stream ( 28 ) by feeding it to the alkaline scrubber ( 27 ).

5. The method according to claim 1 , wherein the method further comprises carrying out steps f′), g′), and h′) after step a), wherein said steps comprise:
f′) feeding the purified gas stream ( 2 ) obtained in step a) to an alkaline scrubber ( 27 ) and bringing into contact said purified gas stream ( 2 ) with an aqueous stream ( 32 ) at a pH comprised between 11 and 13 to obtain a liquid stream ( 29 ) and the purified gas stream ( 2 ′);
g′) feeding the liquid stream ( 29 ) obtained in step f′) to a hydrolysis tank ( 25 ) and adding a suitable amount of base ( 31 ) to the stream ( 29 ) to obtain a liquid effluent ( 30 ) and the aqueous stream ( 32 ); and
h′) feeding the liquid effluent ( 30 ) obtained in step g′) to the conditioning tank ( 9 ) and recirculating the aqueous stream ( 32 ) by feeding it to the alkaline scrubber ( 27 ).

6. The method according to claim 1 , wherein the method further comprises an additional step i) after step a), wherein said step comprises feeding the purified gas stream ( 2 ) obtained in step a) to a fixed-bed aerobic bioreactor ( 33 ) to obtain the purified gas stream ( 2 ″).

7. The method according to claim 4 , wherein base ( 7 ) of step b) and base ( 24 ) of step g) and base ( 31 ) of step g′) are independently selected from the group consisting of alkaline or alkaline earth metal carbonates, alkaline or alkaline earth metal hydroxides, and alkaline or alkaline earth metal hydrogen carbonates.

8. The method according to claim 1 , wherein step c) is carried out at a temperature comprised between 14° C. and 34° C.

9. The method according to claim 1 , wherein the method further comprises an additional step j) after step c), wherein said step comprises feeding the biomethane stream ( 11 ) obtained in step c) to a dehumidifier ( 16 ) to obtain a dry biomethane stream ( 15 ).

10. The method according to claim 1 , wherein the pH of the liquid effluent ( 8 ) is comprised between 7.5 and 8.5.

11. The method according to claim 1 , wherein the pH of the output liquid stream ( 12 ) exiting the bioreactor is comprised between 7.0 and 7.8.

12. The method according to claim 11 , wherein total alkalinity of the liquid effluent ( 8 ) of step b) is comprised between 1,000 and 3,000 mg CaCO 3 /L.

13. The method according to claim 1 , wherein the method further comprises an additional step after step c), wherein said step comprises:
k) recirculating from 1 to 95% of the output liquid stream ( 12 ) to the liquid effluent ( 8 ) before the bioreactor ( 14 ); or alternatively,
l) recirculating from 1 to 95% of the output liquid stream ( 12 ) to the conditioning tank ( 9 ).

14. The method according to claim 1 , wherein the degasser ( 20 ) is an air stripper and step d) comprises bringing into contact said liquid stream ( 12 ) with an air stream ( 17 ).

15. The method according to claim 5 , wherein the base ( 7 ) of step b) and base ( 31 ) of step g′) are independently selected from the group consisting of alkaline or alkaline earth metal carbonates, alkaline or alkaline earth metal hydroxides, and alkaline or alkaline earth metal hydrogen carbonates.

Assignees

• Univ Valencia
• Dsf Bv

Inventors

• Waalkens Albert
• Gabaldón Garcia Maria Carmen
• Peñarrocha Oltra Josep Manuel
• Álvarez Hornos Francisco Javier

Classifications

• B01D2251/304

  of sodium · CPC title

• Y02C20/20

  of methane · CPC title

• C02F9/00

  Multistage treatment of water, waste water or sewage · CPC title

• B01D2256/245

  Methane · CPC title

• C02F3/28

  Anaerobic digestion processes · CPC title