Reducing methane slack when starting and stopping biogas fermenters
A novel method reduces methane slack when operating a biogas fermenter. When starting up a freshly charged fermenter, the methane portion of the produced biogas is initially so low and the portions of carbon dioxide and nitrogen are so high that the biogas cannot be directly used in a combined heat and power plant. Conventionally, the biogas generated during the startup phase has a small portion of methane that is discharged directly into the atmosphere or is flared off if the methane fraction is larger. The initially produced methane is consequently not used and becomes methane slack. To reduce methane slack, the biogas with the low methane fraction is fed to a gas treatment unit in which non-methane components of the gas mixture are partially separated, and the remaining gas mixture with a higher methane content is returned to the biogas fermenter until the methane fraction is sufficiently high.
1. A method comprising:
generating biogas in a freshly charged biogas fermenter, wherein the biogas has a concentration of methane;
supplying the biogas to a gas treatment unit;
increasing the concentration of methane of the biogas by partially removing non-methane components from the biogas;
measuring the concentration of methane in the biogas;
recirculating the biogas into the biogas fermenter so long as the concentration of methane remains lower than a predetermined upper limit; and
purging the biogas fermenter with carbon dioxide-containing off-gas until a concentration of carbon dioxide in the biogas fermenter has reached an upper carbon dioxide limit.
2. A method comprising:
generating biogas in a freshly charged biogas fermenter, wherein the biogas has a concentration of methane;
supplying the biogas to a gas treatment unit;
increasing the concentration of methane of the biogas by partially removing non-methane components from the biogas;
measuring the concentration of methane in the biogas;
recirculating the biogas into the biogas fermenter so long as the concentration of methane remains lower than a predetermined upper limit; and
purging the biogas fermenter with carbon dioxide-containing off-gas until the concentration of methane of the biogas has reached a predetermined lower limit.
3. A method comprising:
generating biogas in a biogas fermenter, wherein the biogas has a concentration of methane;
purging the biogas fermenter with carbon dioxide-containing off-gas;
supplying the biogas and the carbon dioxide-containing off-gas mixture from the biogas fermenter to a gas treatment unit;
increasing the concentration of methane of the biogas by partially removing non-methane components from the biogas and from the carbon dioxide-containing off-gas; and
stopping the purging of the biogas fermenter with carbon dioxide-containing off-gas and stopping the supplying of the biogas and the carbon dioxide-containing off-gas to the gas treatment unit when a concentration of carbon dioxide in the biogas fermenter exceeds an upper carbon dioxide limit.
4. The method of claim 3 , wherein the carbon dioxide-containing off-gas used for purging the biogas fermenter is generated in a biogas utilization unit.
5. The method of claim 3 , further comprising:
supplying the biogas to an off-gas chimney after the concentration of methane falls below a predetermined lower limit.
6. The method of claim 3 , further comprising:
purging the biogas fermenter with fresh air until the concentration of carbon dioxide in the biogas fermenter has dropped below a lower carbon dioxide limit.
7. The method of claim 3 , wherein the non-methane components are partially removed from the biogas using pressurized water washing.
8. The method of claim 1 , further comprising:
supplying the biogas to a biogas utilization unit when the concentration of methane exceeds the predetermined upper limit.
9. The method of claim 1 , further comprising:
connecting a biogas outlet of the biogas fermenter to an off-gas chimney after the concentration of methane falls below a predetermined lower limit.
10. The method of claim 1 , wherein the predetermined upper limit of the concentration of methane falls within the range of 30% to 50% of the biogas by volume.
11. The method of claim 1 , further comprising:
generating biogas in a second biogas fermenter at the same time as the generating the biogas in the freshly charged biogas fermenter.
12. The method of claim 2 , further comprising:
supplying the biogas to a biogas utilization unit when the concentration of methane exceeds the predetermined upper limit.
13. The method of claim 2 , further comprising:
connecting a biogas outlet of the biogas fermenter to an off-gas chimney after the concentration of methane falls below a predetermined lower limit.
14. The method of claim 2 , wherein the predetermined upper limit of the concentration of methane falls within the range of 30% to 50% of the biogas by volume.
15. The method of claim 2 , further comprising:
generating biogas in a second biogas fermenter at the same time as the generating the biogas in the freshly charged biogas fermenter.
16. The method of claim 3 , further comprising:
supplying the biogas to a biogas utilization unit when the concentration of methane exceeds the predetermined upper limit.
17. The method of claim 3 , further comprising:
connecting a biogas outlet of the biogas fermenter to an off-gas chimney after the concentration of methane falls below a predetermined lower limit.
18. The method of claim 3 , wherein the concentration of methane of the biogas is increased until the concentration of methane reaches a predetermined upper limit.
19. The method of claim 18 , wherein the predetermined upper limit of the concentration of methane falls within 30% to 50% of the biogas by volume.
20. The method of claim 3 , further comprising:
generating biogas in a second biogas fermenter at the same time as the generating the biogas in the biogas fermenter.