MARC

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086 0 |a E 1.99:doe/mc/25177--5034 
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088 |a doe/mc/25177--5034 
245 0 0 |a Commercial second-generation PFBC plant transient model  |h [electronic resource] :  |b Task 15. 
260 |a Washington, D.C. :  |b United States. Dept. of Energy ;  |a Oak Ridge, Tenn. :  |b distributed by the Office of Scientific and Technical Information, U.S. Dept. of Energy,  |c 1995. 
300 |a 300 p. :  |b digital, PDF file. 
336 |a text  |b txt  |2 rdacontent. 
337 |a computer  |b c  |2 rdamedia. 
338 |a online resource  |b cr  |2 rdacarrier. 
500 |a Published through the Information Bridge: DOE Scientific and Technical Information. 
500 |a 04/01/1995. 
500 |a "doe/mc/25177--5034" 
500 |a "DE96000570" 
500 |a White, J.S.; Getty, R.T.; Torpey, M.R. 
520 3 |a The advanced pressurized fluidized bed combustor (APFBC) power plant combines an efficient gas-fired combined cycle, a low-emission PFB combustor, and a coal pyrolysis unit (carbonizer) that converts coal, Americàs most plentiful fuel, into the gas turbine fuel. From an operation standpoint, the APFBC plant is similar to an integrated gasification combined cycle (IGCC) plant, except that the PFBC and fluid bed heat exchanger (FBHE) allow a considerable fraction of coal energy to be shunted around the gas turbine and sent directly to the steam turbine. By contrast, the fuel energy in IGCC plants and most other combined cycles is primarily delivered to the gas turbine and then to the steam turbine. Another characteristic of the APFBC plant is the interaction among three large thermal inertias--carbonizer, PFBC, and FBHE--that presents unique operational challenges for modeling and operation of this type of plant. This report describes the operating characteristics and dynamic responses of the APFBC plant and discusses the advantages and shortcomings of several alternative control strategies for the plant. In particular, interactions between PFBC, FBHE, and steam bottoming cycle are analyzed and the effect of their interactions on plant operation is discussed. The technical approach used in the study is described in Section 2. The dynamic model is introduced in Section 3 and described is detail in the appendices. Steady-state calibration and transient simulations are presented in Sections 4 and 5. The development of the operating philosophy is discussed in Section 6. Potential design changes to the dynamic model and trial control schemes are listed in Sections 7 and 8. Conclusions derived from the study are presented in Section 9. 
536 |b AC21-89MC25177. 
650 7 |a Design.  |2 local. 
650 7 |a Fluidized-bed Combustion.  |2 local. 
650 7 |a Coal.  |2 local. 
650 7 |a Numerical Data.  |2 local. 
650 7 |a Mathematical Models.  |2 local. 
650 7 |a Engineering Drawings.  |2 local. 
650 7 |a Fluidized Bed Heat Exchangers.  |2 local. 
650 7 |a Chars.  |2 local. 
650 7 |a Fluidized-bed Combustors.  |2 local. 
650 7 |a Pressurization.  |2 local. 
650 7 |a Gas Turbines.  |2 local. 
650 7 |a Operation.  |2 local. 
650 7 |a Pyrolysis.  |2 local. 
650 7 |a Response Functions.  |2 local. 
650 7 |a Combined-cycle Power Plants.  |2 local. 
650 7 |a Coal, Lignite, And Peat.  |2 edbsc. 
650 7 |a Fossil-fueled Power Plants.  |2 edbsc. 
710 2 |a Gilbert/Commonwealth (Firm).  |4 res. 
710 1 |a United States.  |b Department of Energy.  |4 spn. 
710 2 |a National Energy Technology Laboratory (U.S.).  |4 res. 
710 1 |a United States.  |b Department of Energy.  |b Office of Scientific and Technical Information.  |4 dst. 
856 4 0 |u http://www.osti.gov/servlets/purl/161472/  |z Online Access 
907 |a .b73163260  |b 03-07-23  |c 02-11-13 
998 |a web  |b 02-11-13  |c f  |d m   |e p  |f eng  |g dcu  |h 0  |i 2 
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952 f f |p Can circulate  |a University of Colorado Boulder  |b Online  |c Online  |d Online  |e E 1.99:doe/mc/25177--5034  |h Superintendent of Documents classification  |i web  |n 1