The LM2500, which is designed for liquid, gaseous, or dual
fuel operation, already has a substantial capability for
low-Btu gas operation. In general, however, the LM2500 will
require only limited modifications for operation on a
biomass fuel. During an atmospheric component test
conducted, M&I evaluated key features of the LM2500
combustor at atmospheric conditions for reduced complexity.
Features included in this test were combustor light-off and
blow-out, low speed efficiency, temperature profile and
flammability limits.
The second analysis -- a sector test -- used a five-cup
portion of a standard annular combustor. M&I's sector high
pressure test facility has the capability to achieve 40 bar
of pressure at 250 pps mass flow and 1400oF temperature.
The key objectives of the sector test were to obtain
flammability, efficiency and emissions information on
biomass fuels as simulated in an installed, operating
environment. A fuel system control specification also was
defined so the gas turbine can operate on the low Btu
biomass fuel. Biomass fuel has approximately one-seventh
the heating value of natural gas and may be supplied at
temperatures as high as 450C (842F).
Both tests were successfully completed, and demonstrated
that the LM2500 combustor and fuel nozzle designs are
acceptable and within the expected operational envelope as
compared to common fuel parameters such as on natural gas
or distillates.
BIG-GT Project
The BIG-GT project was initially divided into three phases: preliminary investigation, equipment development, and implementation. Phase I was completed in September 1992 and Phase II will be finished in June 1997. Phase III will be initiated in mid-1997. Once these have concluded, a fourth phase will provide for debugging and pre-commercial operation, and the fifth phase for actual commercial operation of a BIG-GT facility. Phase II activity includes the modification and component testing of the LM2500 combustor and fuel nozzles affected by the fuel change. These changes will be accomplished within the time and budgetary constraints of the project's Phase II. Two independent project teams were established for Phase II of the project to work in parallel to develop distinct technology packages for possible implementation in Phase III. Each team was led by a gasifier system manufacturer, which was responsible for the performance of the gasifier/gas clean-up train, integration of the gas turbine and steam bottoming cycle, the overall system control, and the provision of process guarantees. GE worked with both project teams. The final package was decided in late 1995, and TPS Termiska Processor was selected for the gasification technology. This integrated low-pressure BIG-GT design will have a net combined-cycle output around 30 megawatts for a fully-fired LM2500. Successful implementation of the BIG-GT demonstration facility would open the door for worldwide commercial application of sustainable biomass power generation. The increased usage of biomass could provide a basis for rural development and employment in developing countries and for utilization of excess crop lands in the industrial world.