United States Environmental Protection Agency Air and Energy Engineering Research Laboratory Research Triangle Park, NC 27711 Research and Development EPA/600/SR-93/170 December 1993 &EPA Project Summary Biomass Gasification Pilot Plant Study A.M. Furman, S.G. Kimura, R.E. Ayala, and J. F. Joyce A gasification pilot program carried out at General Electric's (GE's) Re- search and Development Center, using two biomass feedstocks: bagasse pel- lets and wood chips. The object of the testing was to determine the properties of biomass product gas and its suit- ability as a fuel for gas-turbine-based power generation cycles. The feed- stocks were gasified at a feed rate of about 1 ton/hr*, using GE's pressur- ized, fixed-bed gasifier and a single stage of cyclone paniculate removal, operating at 538°C. The biomass prod- uct gas was analyzed for chemical com- position, paniculate loading, fuel-bound nitrogen (FBN) levels, and sulfur and alkali metal content. Both feedstocks gasified easily. The composition and heating value of the biomass product gas were compatible with gas turbine combustion require- ments. However, the paniculate removal performance of the pilot facility single- stage cyclone did not meet turbine specifications. In addition, alkali metal compounds in the paniculate matter (at 538°C) carried over from the gasifier exceeded turbine limits. Improved par- ticulate removal technology, designed specifically for biomass feedstock char- acteristics, could meet turbine require- ments for both paniculate and alkali loading. FBN compounds were also measured since they can be convened to nitrogen oxides (NOx) during com- *Readers more familiar with metric units may use the following factors to convert to that system: 1 ton = 907 kg, and 1 atm = 98 kPa. bustion in a gas turbine. Since this conversion is highly dependent on gas turbine combustor design, no firm con- clusions regarding NOx production can be reached without actual combustion testing. This Project Summary was developed by the U.S. EPA's Air and Energy Engi- neering Research Laboratory, Research Triangle Park, NC, to announce key find- ings of the research project that is fully documented in a separate report of the same title (see Project Report ordering information at back). Introduction The gasification performance of two bio- mass feedstocks—wood chips and ba- gasse—was evaluated in the pilot Inte- grated Gasification Combined Cycle (IGCC) facility located at GE's Research and Development Center in Schenectady, NY. The overall objective of this program was to evaluate biomass as a feedstock for a biomass gasification/gas turbine sys- tem, which is a potentially cost-effective and highly efficient approach for using for- est and agricultural wastes for power gen- eration. Specific objectives were to mea- sure gas composition and to determine whether the product gas would meet gas turbine requirements. The pilot IGCC facility consists of a pressurized, fixed-bed gasifier with a nomi- nal operating pressure of 20 atm and a hot gas cleanup system, consisting of a high-temperature cyclone, a solid-sorbent desulfurization system, and a polishing cyclone. The gasifier has a nominal ca- pacity for coal gasification of 1 ton/hr. Since desulfurization is not an issue for Printed on Recycled Paper ------- the biomass feedstocks evaluated, only the gasifier and high-temperature cyclone were used. The product gas was flared. Because the pilot gasifier and its asso- ciated fuel feeding system were designed for operation on coal, the issue of feeding of biomass, with its lower density and different flow properties, was addressed before gasification testing. Bagasse, which was supplied as small cylindrical pellets, was found to feed easily with some modi- fications to the fuel feeding equipment. However, it was necessary to evaluate several wood chip samples before one was found that could be fed at the re- quired feed rate. A total of 42.5 tons of bagasse was gasified during a 32-hr test, and 83.8 tons of wood chips were gasified in an 81-hr test. These quantities of fuel represented the total fuel available to the program. Wood chips were provided by the Ver- mont Department of Public Service. The bagasse pellets were obtained from the Winrock International Institute for Agricul- tural Development. Both biomass fuels gasified readily. Their reactivity was higher than that for coal. Gasification capacities of both fuels were limited by feed rate or system ca- pacity, and not by gasification kinetics. Product gas compositions for both biom- ass feedstocks indicated that they would have combustion characteristics compat- ible with gas turbine combustor require- ments. However, particulate removal per- formance of the single cyclone was inad- equate to meet fuel contaminant specifi- cations. In particular, alkali metals, which are present in the fine particulate material carried over from the gasifier and which cause hot corrosion on gas turbine hot gas path components, were present at levels well in excess of turbine specifica- tion limits. The low density of particulates and their poor flow properties, which made removal from the cyclone difficult, caused the cyclone to perform poorly. This result was not unexpected since the cyclone had been designed for removing contaminants from coal gas. In order to achieve con- taminant levels consistent with gas tur- bine requirements, it will be necessary to improve particulate removal. This improve- ment is well within the state-of-the-art of particulate cleanup technology. A second class of contaminant mea- sured was fuel-bound nitrogen (FBN) com- pounds. Typical of these are ammonia, cyanides, and nitrogen-containing organic compounds. A large fraction of FBN will be converted to nitrogen oxides (NOx) dur- ing combustion in conventional gaxs tur- bine combustors. Thus, when stringent NOx emissions requirements (< 10 ppm) are in effect, it may be necessary to consider alternative approaches to reducing the level of this pollutant. One potential ap- proach is to utilize advanced combustion techniques such as "rich-quench-lean" to reduce the conversion of FBN. This tech- nology is still in an early stage of develop- ment and will require significant effort to bring it to a suitable stage of commercial readiness. A second approach is to cool the fuel gas and "scrub" the gas with wa- ter to remove the FBN compounds. This approach lowers the overall plant effi- ciency, reduces the heating value of the fuel, and creates an environmental dis- posal problem associated with the dis- posal of the "scrub" water. Other ap- proaches include the use of commercially available selective catalytic reduction (SCR) technology to reduce the NO level in the exhaust gas. Note that FBNJ pro- duction is a strong function of both the feedstock and gasifier, with higher tem- perature gasifiers such as fluidized and entrained gasifiers producing less FBN than fixed-bed gasifiers. A system trade- off study would help determine the best system level approach to NOx reduction by identifying the capital equipment cost differences and the associated plant effi- ciency impact on the overall system de- sign. The tests at the GE-CRD pilot plant have demonstrated the successful gasifi- cation of biomass and the general suit- ability of biomass fuel gas for use in a gas turbine. Areas of possible future develop- ment include improved particulate removal, improved low NOx combustion, and pre- and post-gas cleanup. These accomplishments represent a key step in the overall development of a Biomass-IGCC power generation system -&U.S. GOVERNMENT PRINTING OFFICE: I«W4 - 550-067/80140 ------- ------- A. Furman, S. Kimura, R. Ayala, and J. Joyce are with GE Research and Develop- ment Center, Schenectady, NY 12301. Carol R. Purvis is the EPA Project Officer (see below). The complete report, entitled "Biomass Gasification Pilot Plant Study," (Order No. PB94-114766/AS; Cost: $27.00; subject to change) will be available only from: National Technical Information Service 5285 Port Royal Road Springfield, VA 22161 Telephone: 703-487-4650 The EPA Project Officer can be contacted at: Air and Energy Engineering Research Laboratory U.S. Environmental Protection Agency Research Triangle Park, NC 27711 United States Environmental Protection Agency Center for Environmental Research Information Cincinnati, OH 45268 Official Business Penalty for Private Use $300 BULK RATE POSTAGE & FEES PAID EPA PERMIT No. G-35 EPA/600/SR-93/170 ------- |