Dynamic analysis of process reactors
The approach and methodology of conducting a dynamic analysis is presented in this poster session in order to describe how this type of analysis can be used to evaluate the operation and control of process reactors. Dynamic analysis of the PyGas{trademark} gasification process is used to illustrate the utility of this approach. PyGas{trademark} is the gasifier being developed for the Gasification Product Improvement Facility (GPIF) by Jacobs-Siffine Engineering and Riley Stoker. In the first step of the analysis, process models are used to calculate the steady-state conditions and associated sensitivities for the process. For the PyGas{trademark} gasifier, the process models are non-linear mechanistic models of the jetting fluidized-bed pyrolyzer and the fixed-bed gasifier. These process sensitivities are key input, in the form of gain parameters or transfer functions, to the dynamic engineering models.
- Research Organization:
- USDOE Morgantown Energy Technology Center (METC), WV (United States)
- OSTI ID:
- 426207
- Report Number(s):
- DOE/METC-95/1018-Vol.1; CONF-9506162-Vol.1; ON: DE95009732; TRN: 97:000255-0005
- Resource Relation:
- Conference: Advanced coal-fired power systems `95 review meeting, Morgantown, WV (United States), 27-29 Jun 1995; Other Information: PBD: Jun 1995; Related Information: Is Part Of Proceedings of the advanced coal-fired power systems `95 review meeting. Volume I; McDaniel, H.M.; Mollot, D.J.; Venkataraman, V.K.; PB: 463 p.
- Country of Publication:
- United States
- Language:
- English
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