Chemical Industry and Engineering Progress ›› 2024, Vol. 43 ›› Issue (7): 3729-3746.DOI: 10.16085/j.issn.1000-6613.2023-2277
• Column: Thermochemical Reaction Engineering Technology • Previous Articles Next Articles
CHEN Liang1(
), LUO Dongmei1, WANG Zhenghao1, ZHONG Shan1, TANG Siyang1, LIANG Bin1,2(
)
Received:2023-12-27
Revised:2024-03-25
Online:2024-08-14
Published:2024-07-25
Contact:
LIANG Bin
陈良1(
), 罗冬梅1, 王正豪1, 钟山1, 唐思扬1, 梁斌1,2(
)
通讯作者:
梁斌
作者简介:陈良(1996—),男,博士研究生,研究方向为化学链制氢。E-mail:1573496497@qq.com。
基金资助:CLC Number:
CHEN Liang, LUO Dongmei, WANG Zhenghao, ZHONG Shan, TANG Siyang, LIANG Bin. Research progress of industrial by-product gas-fueled chemical looping hydrogen generation technology[J]. Chemical Industry and Engineering Progress, 2024, 43(7): 3729-3746.
陈良, 罗冬梅, 王正豪, 钟山, 唐思扬, 梁斌. 工业副产气化学链回收氢气技术研究进展[J]. 化工进展, 2024, 43(7): 3729-3746.
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| 类型 | H2/% | CO/% | CH4/% | N2/% | CO2/% | 其他 /% | 年产量 /108·m-3 |
|---|---|---|---|---|---|---|---|
| 焦炉煤气 | 54~59 | 5~8 | 23~27 | 3~6 | 2~4 | 2~3 | 1114 [ |
| 高炉煤气 | 1~2 | 28~33 | 0.2~0.5 | 55~60 | 6~12 | — | 18000 [ |
| 甲醇驰放气 | 60~75 | 5~7 | 5~11 | 0.5~2 | 2~13 | — | 239 [ |
| 氯碱尾气 | 92 | — | — | — | — | 8 | 5.27 [ |
| 醋酸尾气 | 5~15 | 60~85 | 1~3 | 4~7 | 6~15 | — | 7.20 [ |
| 类型 | H2/% | CO/% | CH4/% | N2/% | CO2/% | 其他 /% | 年产量 /108·m-3 |
|---|---|---|---|---|---|---|---|
| 焦炉煤气 | 54~59 | 5~8 | 23~27 | 3~6 | 2~4 | 2~3 | 1114 [ |
| 高炉煤气 | 1~2 | 28~33 | 0.2~0.5 | 55~60 | 6~12 | — | 18000 [ |
| 甲醇驰放气 | 60~75 | 5~7 | 5~11 | 0.5~2 | 2~13 | — | 239 [ |
| 氯碱尾气 | 92 | — | — | — | — | 8 | 5.27 [ |
| 醋酸尾气 | 5~15 | 60~85 | 1~3 | 4~7 | 6~15 | — | 7.20 [ |
| 因素 | 化学链制氢 (载氧体:Fe2O3/MgAl2O4) | 化学链制氢 (载氧体:Fe2O3/ZrO2) | 甲烷蒸汽重整 |
|---|---|---|---|
| 总投资/×106USD | 369.6 | 369.6 | 678.1 |
| 总运行成本/×106USD | 246.5 | 289 | 207.7 |
| 年产氢量/Mt | 0.24 | 0.24 | 0.24 |
| 利率/% | 10 | 10 | 10 |
| 寿命/年 | 25 | 25 | 25 |
| 年生产成本/×106USD | 287.2 | 329.7 | 332.7 |
| H2生产成本/USD·kg-1 | 1.41 | 1.62 | 1.64 |
| 因素 | 化学链制氢 (载氧体:Fe2O3/MgAl2O4) | 化学链制氢 (载氧体:Fe2O3/ZrO2) | 甲烷蒸汽重整 |
|---|---|---|---|
| 总投资/×106USD | 369.6 | 369.6 | 678.1 |
| 总运行成本/×106USD | 246.5 | 289 | 207.7 |
| 年产氢量/Mt | 0.24 | 0.24 | 0.24 |
| 利率/% | 10 | 10 | 10 |
| 寿命/年 | 25 | 25 | 25 |
| 年生产成本/×106USD | 287.2 | 329.7 | 332.7 |
| H2生产成本/USD·kg-1 | 1.41 | 1.62 | 1.64 |
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