| 灰融聚流化床粉煤气化制氢技术方案设计 |
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| 引用本文： | 毕可军,卞素君. 灰融聚流化床粉煤气化制氢技术方案设计[J]. 化工设计通讯, 2012, 0(1): 88-90 |
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| 作者姓名： | 毕可军 卞素君 |
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| 作者单位： | [1]陕西华祥能源科技集团有限公司,陕西西安710075 [2]平煤神马集团飞行化工公司,河南平顶山467001 |
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| 摘 要： | 介绍灰融聚流化床粉煤气化技术特点、工艺流程、制氢能力以及后续配套工艺;提出采用多种干法除尘方案,使煤气含尘小于10mg/m3,再利用煤气中的水蒸气进行CO变换,从而简化制氢工艺。
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| 关 键 词： | 灰融聚流化床粉煤气化 制氢 后续工序 |
Scheme Design for Hydrogen Production from CAGGTM |
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| BI Ke-jun,BIAN Su-jun. Scheme Design for Hydrogen Production from CAGGTM[J]. Chemical Engineering Design Communications, 2012, 0(1): 88-90 |
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| Authors: | BI Ke-jun BIAN Su-jun |
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| Affiliation: | 1. Shaanxi Huaxiang Energy Technology Group Co., Ltd., Xi＇an Shaannxi 710075, China; 2. Feixing Chemical Company of China Pingmei Shenma Group, Pingdingshan Henan 467001, China) |
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| Abstract: | Introduce CAGGTM technical characteristics, process flow, hydrogen production capacity and subsequent matching process. Propose a variety of drying methods to remove dust, so the gas dust content is less than 10 mg/m3. CO shift can be made by water vapor, in the gas to simplify the hydrogen production process. |
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| Keywords: | CAGG^TM hydrogen production subsequent procedures |
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