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Dynamic model for an oxygen-staged slagging entrained flow gasifier
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Yang, Zhiwei, Wang, Zhe, Wu, Yuxi, Wang, Jihong, Lu, Junfu, Li, Zheng and Ni, Weidou. (2011) Dynamic model for an oxygen-staged slagging entrained flow gasifier. Energy & Fuels, Vol.25 (No.8). pp. 3646-3656. ISSN 0887-0624
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Official URL: http://dx.doi.org/10.1021/ef200742s
Abstract
A dynamic gasifier model including slag flow behavior simulation was established to simulate a new type of oxygen-staged gasifier recently developed in China. A reactor network model (RNM) is used to simulate the internal gas-solid reaction zone of the gasifier, in which the reactor is divided into several zones based on the understanding of the flow characteristics in the gasifier, with each zone represented by either a plug-flow reactor or a well-stirred reactor. This space division concept can provide a more reasonable temperature distribution prediction than one-dimensional models, without costing too much computational expense. In addition, a widely accepted slag layer model is used to simulate the time-varying slag accumulation and flow on the wall and the heat transfer process through the wall. Using the developed model, two kinds of oxygen-staged gasifiers were simulated: the refractory wall gasifier and the membrane wall gasifier. The RNM predictions were compared with industrial data and computational fluid dynamics (CFD) model results, and good agreement has been observed. The temperature distribution simulation results also showed that staged oxygen feeding can reduce the temperature near the main burner significantly, therefore extending the lifetime of the burner compared with that of without staged oxygen feed. Dynamic simulation results suggest that the dynamic response of the refractory wall gasifier is much slower than that of the membrane wall gasifier. In the membrane wall gasifier, the dynamic response of the syngas temperature and composition is rather fast compared to that of the wall temperature. However, for the refractory wall gasifier, the dynamic response of syngas temperature is as slow as that of the wall temperature indicating that different control strategies should be taken into account for better slag flow and syngas temperature control for these two kinds of gasifier.
| Item Type: | Journal Article |
|---|---|
| Subjects: | T Technology > TK Electrical engineering. Electronics Nuclear engineering T Technology > TP Chemical technology |
| Divisions: | Faculty of Science > Engineering |
| Library of Congress Subject Headings (LCSH): | Coal gasification -- Mathematical models, Coal gasification plants -- Mathematical models |
| Journal or Publication Title: | Energy & Fuels |
| Publisher: | American Chemical Society |
| ISSN: | 0887-0624 |
| Date: | August 2011 |
| Volume: | Vol.25 |
| Number: | No.8 |
| Number of Pages: | 11 |
| Page Range: | pp. 3646-3656 |
| Identification Number: | 10.1021/ef200742s |
| Status: | Peer Reviewed |
| Publication Status: | Published |
| Access rights to Published version: | Restricted or Subscription Access |
| Funder: | National Basic Research Program of China (973 Program), Guo jia zi ran ke xue ji jin wei yuan hui (China) [National Natural Science Foundation of China] (NSFC) |
| Grant number: | 2010-CB227006 (973P), 51010143 (NSFC) |
| URI: | http://wrap.warwick.ac.uk/id/eprint/38590 |
Data sourced from Thomson Reuters' Web of Knowledge
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