초록 ▼

In a method for adsorptively drying purified biogas and regenerating laden absorbents, foreign matter is not allowed to enter the purified biogas, the content of methane in the gas remains virtually unchanged and the effort involved in regenerating the laden adsorbent is reduced. Drying and regenera

In a method for adsorptively drying purified biogas and regenerating laden absorbents, foreign matter is not allowed to enter the purified biogas, the content of methane in the gas remains virtually unchanged and the effort involved in regenerating the laden adsorbent is reduced. Drying and regeneration are effected in a closed biogas cycle, wherein separate layers based on silica gel and molecular sieves are used as the adsorbent. The biogas to be dried first flows through the silica gel layer. The adsorbent is regenerated with exclusively heated, dried biomethane having a temperature of up to 150° C. which, after contact with adsorbent, is recirculated to the outflow of purified biogas. After regeneration, the bed is cooled by biomethane, which is subsequently recirculated to the outflow of purified biogas. Methane-containing water accumulating during drying and regeneration is recirculated to the biogas generation and/or purification.

대표청구항 ▼

1. A gas drying process, comprising: providing a purified biogas having a methane content of at least 90% by volume;providing an adsorber with adsorbents in the form of separate layers based on silica gel and molecular sieves;adsorptively drying the purified biogas with the adsorbents and regenerati

1. A gas drying process, comprising: providing a purified biogas having a methane content of at least 90% by volume;providing an adsorber with adsorbents in the form of separate layers based on silica gel and molecular sieves;adsorptively drying the purified biogas with the adsorbents and regenerating laden adsorbents in a closed biogas circuit; andconducting the biogas to be dried first through a layer of silica gel, and wherein regenerating further comprises regenerating the adsorbent using exclusively heated dried biomethane having a temperature of up to 150° C. and, after contact with the adsorbent, recycling the biomethane back into a starting stream of the purified biogas; andon completion of regeneration, contacting cooled dried biomethane with the adsorbent and recycling back into the starting stream of the purified biogas, and conducting methane-containing water obtained during the drying and regeneration back to a biogas production and/or purification. 2. The process according to claim 1, which comprises removing a portion of water by cooling the purified biogas prior to supplying the purified biogas to the adsorber. 3. The process according to claim 1, wherein the layer of silica gel is formed from at least two layers including a lower macroporous layer and an upper mesoporous layer, with a volume ratio between the lower layer to the upper layer lying between 1:1 and 1:4. 4. The process according to claim 1, which comprises passing the biomethane for the regeneration through a bed of the adsorbent at a temperature of 110 to 150° C., with a continuous measurement of the temperature of the exiting biomethane, and a shutdown of a supply of biomethane after a rise in the exit temperature to 40 to 50° C. 5. The process according to claim 1, which comprises pumping the biogas to be dried through the adsorber at ambient pressure or with a slightly elevated pressure of up to 1 bar. 6. The process according to claim 1, wherein a volume ratio of a first layer being the silica gel layer to a second layer being the molecular sieves is 20:1 to 3:1. 7. The process according to claim 1, which comprises carrying out the adsorption during an adsorption time between 12 and 14 hours and thereby reducing a water content in the dried biomethane to below 20 mg/m3 (STP). 8. The process according to claim 1, which comprises cooling the regenerated adsorbents, prior to reuse, down to 10 to 30° C. with cooled biomethane. 9. The process according to claim 8, which comprises cooling the regenerated adsorbents with cooled biomethane having a temperature of between 5 and 15° C. 10. The process according to claim 1, which comprises indirectly heating at least a lower region of the adsorber during the regeneration. 11. The process according to claim 1, which comprises regenerating the laden adsorber under reduced pressure.