會議論文
| 學年 | 102 |
|---|---|
| 學期 | 1 |
| 發表日期 | 2013-10-31 |
| 作品名稱 | Operability analysis of adiabatic water gas shift reactor systems for hydrogen generation for fuel cells |
| 作品名稱（其他語言） | |
| 著者 | Hung, Hao-Chia; Chen, Yih-Hang |
| 作品所屬單位 | 淡江大學化學工程與材料工程學系 |
| 出版者 | |
| 會議名稱 | FILTRATION AND SEPARATION SYMPOSIUM 2013 |
| 會議地點 | 東京, 日本 |
| 摘要 | In this work, steady-state mathematical models were developed to describe water gas shift (WaS) reactors. Gas cleaning un it includes was reactor and preferential reactor which converted carbon monoxide into hydrogen for fuel cell systems in order to prevent ppm level of carbon monoxide poisoning PI catalyst in the anode side of PEMFCs. was reactor systems consisted of was reactors and intercoo lers. Based on the was reactors model, optim izat ion problems were formulated to minimize the reactor volume wh ile mai ntaining the hydrogen flow rate (3 kW PEMFC used) and CO concentration constraint 0.953 mol%. The WGS reactor structures, single and multiple, were in vestigated. The optimizat ion procedure was carried out by using SQP method and the optimal variables studied include: reactor inlet temperatures and water feed f1owate. The results show that two WGS reactors in series with an intercooler can reduce the volume of a single reactor by 30.75%. Then, design heuristic was built to provide a quick determinat ion of WGS reactor system f1owsheet. From sensitivity analysis, control structures are explored here. The result shows a single WGS reactor system has larger operability range than two WGS reactors in series. |
| 關鍵字 | |
| 語言 | en |
| 收錄於 | |
| 會議性質 | 國際 |
| 校內研討會地點 | |
| 研討會時間 | 20131031~20131101 |
| 通訊作者 | Yih-Hang Chen |
| 國別 | JPN |
| 公開徵稿 | Y |
| 出版型式 | 紙本 |
| 出處 | FILTRATION AND SEPARATION SYMPOSIUM 2013, pp.201-206. |
| 相關連結 |
機構典藏連結 ( http://tkuir.lib.tku.edu.tw:8080/dspace/handle/987654321/96777 ) |