Progress 06/01/09 to 01/31/10
Outputs OUTPUTS: TDA is developing a highly effective sorbent that can remove sulfur compounds from simulated biogas streams with very high capacity. Our sorbent bed is used as a polisher that is located downstream of a bulk desulfurization system to remove any residual hydrogen sulfide (H2S) and all other organic sulfur species (e.g., mercaptans, sulfide, disulfides). This will be a key technology that enables the use of biogas in distributed fuel cell CHP systems. In Phase I, we synthesized and tested a large number of sorbent formulations to identify the ones with high sulfur capacity and removal efficiency. TDA's sorbent achieved over 35% wt. capacity for H2S and over 4% wt. capacity for mercaptans and other organic sulfur compounds. The large pores of the support also allowed us to effectively remove the large disulfide species (e.g., dimethyl disulfide) that are difficult to remove using conventional microporous sorbents. The new adsorbent could reduce the sulfur concentration of the gas to less than 4 ppbv to ensure maximum protection to the fuel cell. We also demonstrated that we could regenerate the sorbent for multiple adsorption/regeneration cycles, which may be a potential advantage in larger installations (over 20 MW). PARTICIPANTS: Nothing significant to report during this reporting period. TARGET AUDIENCES: Because its properties are similar to those of natural gas, biogas produced by the anaerobic digesters (referred to as anaerobic digester gas or ADG) is often used to meet the heating demands of the farm, dairy or food processing facilities. In a potential CHP application, the biogas generated from manure is combusted in a boiler/steam turbine combination to generate both electricity and useful heat. The electricity demand varies greatly depending on the size of the facility and the nature of the process. PROJECT MODIFICATIONS: Nothing significant to report during this reporting period.
Impacts In a preliminary engineering and cost analysis, we showed the economic viability of the new sorbent used as an expendable sulfur polishing bed for a fuel cell CHP system. For a typical 2,000 cow dairy, we estimated the added cost of desulfurization to be less than 0.36 cents/kWh. The overall impact of the gas clean-up system on the cost of electricity (COE) is small contributing less than 3.4% to the COE (based on a cost of the electricity in California for industrial use of 10.56 cents/kWh in 2009).
Publications
- No publications reported this period
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