Chemical Industry and Engineering Progress ›› 2022, Vol. 41 ›› Issue (12): 6285-6294.DOI: 10.16085/j.issn.1000-6613.2022-0321
• Energy processes and technology • Previous Articles Next Articles
LI Haoyang1,2(), ZHANG Wei1,3, LI Xiaosen1(), XU Chungang1()
Received:
2022-03-03
Revised:
2022-04-14
Online:
2022-12-29
Published:
2022-12-20
Contact:
LI Xiaosen, XU Chungang
李昊阳1,2(), 张炜1,3, 李小森1(), 徐纯刚1()
通讯作者:
李小森,徐纯刚
作者简介:
李昊阳(1997—),男,硕士研究生,研究方向为天然气水合物开采及综合技术研发。E-mail:lihy1@ms.giec.ac.cn。
基金资助:
CLC Number:
LI Haoyang, ZHANG Wei, LI Xiaosen, XU Chungang. Research process of hydrate-based hydrogen storage[J]. Chemical Industry and Engineering Progress, 2022, 41(12): 6285-6294.
李昊阳, 张炜, 李小森, 徐纯刚. 水合物储氢的研究进展[J]. 化工进展, 2022, 41(12): 6285-6294.
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URL: https://hgjz.cip.com.cn/EN/10.16085/j.issn.1000-6613.2022-0321
晶型 | 孔穴 | 表述 | 孔穴数 | 孔穴直径/Å | 配位数 | 理想表达式 |
---|---|---|---|---|---|---|
sI | 小 | 512 | 2 | 3.95 | 20 | 6X·2Y·46H2O |
大 | 51262 | 6 | 4.33 | 24 | ||
sII | 小 | 512 | 16 | 3.91 | 20 | 8X·16Y·136·H2O |
大 | 51264 | 8 | 4.73 | 28 | ||
sH | 小 | 512 | 3 | 3.91 | 20 | 1X·3Y·2Z·34H2O |
中 | 435663 | 2 | 4.06 | 20 | ||
大 | 51268 | 1 | 5.71 | 36 |
晶型 | 孔穴 | 表述 | 孔穴数 | 孔穴直径/Å | 配位数 | 理想表达式 |
---|---|---|---|---|---|---|
sI | 小 | 512 | 2 | 3.95 | 20 | 6X·2Y·46H2O |
大 | 51262 | 6 | 4.33 | 24 | ||
sII | 小 | 512 | 16 | 3.91 | 20 | 8X·16Y·136·H2O |
大 | 51264 | 8 | 4.73 | 28 | ||
sH | 小 | 512 | 3 | 3.91 | 20 | 1X·3Y·2Z·34H2O |
中 | 435663 | 2 | 4.06 | 20 | ||
大 | 51268 | 1 | 5.71 | 36 |
方法 | 存储条件 | 理论储氢密度 (质量分数) | 安全性 | 文献 |
---|---|---|---|---|
高压气态储氢 | 298K,35~70MPa | 5.7%(70MPa) | 危险 | [ |
低温液化储氢 | 23K,0.3~0.5MPa | 7.6% | 危险 | [ |
固体材料储氢 | 413K,0.001MPa | 4.0%(MgH2) | 安全 | [ |
氢气水合物 | 280K,300MPa | 3.77%~4.97%(H2/H2O) | 安全 | [ |
方法 | 存储条件 | 理论储氢密度 (质量分数) | 安全性 | 文献 |
---|---|---|---|---|
高压气态储氢 | 298K,35~70MPa | 5.7%(70MPa) | 危险 | [ |
低温液化储氢 | 23K,0.3~0.5MPa | 7.6% | 危险 | [ |
固体材料储氢 | 413K,0.001MPa | 4.0%(MgH2) | 安全 | [ |
氢气水合物 | 280K,300MPa | 3.77%~4.97%(H2/H2O) | 安全 | [ |
文献 | 体系 | 促进剂浓度 (摩尔分数) | 温度 /K | 压力 /MPa |
---|---|---|---|---|
Smirnov等[ | H2/H2O | 260 | 200 | |
258 | 100 | |||
178 | 50 | |||
Hashimoto等[ | H2/THF | 5.56% | 277.5 | 0.33 |
277.6 | 0.55 | |||
277.8 | 1.03 | |||
278.0 | 1.55 | |||
278.2 | 2.13 | |||
279.2 | 4.87 | |||
280.1 | 8.30 | |||
280.8 | 11.3 | |||
281.4 | 13.3 | |||
H2/TBAB | 3.6% | 285.4 | 0.18 | |
285.5 | 0.70 | |||
285.8 | 1.19 | |||
286.1 | 3.27 | |||
286.3 | 6.05 | |||
286.6 | 7.93 | |||
287.2 | 13.4 | |||
Du等[ | H2/叔丁胺 | 5.56% | 268.4 | 9.54 |
269.2 | 12.53 | |||
269.9 | 15.09 | |||
271.5 | 20.85 | |||
273.2 | 26.12 | |||
274.0 | 29.95 | |||
8.86% | 270.4 | 11.75 | ||
271.3 | 15.01 | |||
271.8 | 17.14 | |||
272.6 | 19.83 | |||
273.1 | 21.63 | |||
274.0 | 27.72 | |||
Wang等[ | H2/C3H8 | 33%(体积分数) | 279.05 | 1.60 |
278.25 | 1.40 | |||
277.84 | 1.20 | |||
276.83 | 1.00 | |||
275.90 | 0.80 | |||
274.71 | 0.60 | |||
273.72 | 0.40 |
文献 | 体系 | 促进剂浓度 (摩尔分数) | 温度 /K | 压力 /MPa |
---|---|---|---|---|
Smirnov等[ | H2/H2O | 260 | 200 | |
258 | 100 | |||
178 | 50 | |||
Hashimoto等[ | H2/THF | 5.56% | 277.5 | 0.33 |
277.6 | 0.55 | |||
277.8 | 1.03 | |||
278.0 | 1.55 | |||
278.2 | 2.13 | |||
279.2 | 4.87 | |||
280.1 | 8.30 | |||
280.8 | 11.3 | |||
281.4 | 13.3 | |||
H2/TBAB | 3.6% | 285.4 | 0.18 | |
285.5 | 0.70 | |||
285.8 | 1.19 | |||
286.1 | 3.27 | |||
286.3 | 6.05 | |||
286.6 | 7.93 | |||
287.2 | 13.4 | |||
Du等[ | H2/叔丁胺 | 5.56% | 268.4 | 9.54 |
269.2 | 12.53 | |||
269.9 | 15.09 | |||
271.5 | 20.85 | |||
273.2 | 26.12 | |||
274.0 | 29.95 | |||
8.86% | 270.4 | 11.75 | ||
271.3 | 15.01 | |||
271.8 | 17.14 | |||
272.6 | 19.83 | |||
273.1 | 21.63 | |||
274.0 | 27.72 | |||
Wang等[ | H2/C3H8 | 33%(体积分数) | 279.05 | 1.60 |
278.25 | 1.40 | |||
277.84 | 1.20 | |||
276.83 | 1.00 | |||
275.90 | 0.80 | |||
274.71 | 0.60 | |||
273.72 | 0.40 |
晶型 结构 | 体系 | 生成温压条件 | 储氢密度(质量分数) |
---|---|---|---|
sI | H2/CO2 | 200MPa,270K | 0.37% |
sII | 纯水 | 200~300MPa,240~249K | 5.3% |
sII | H2/THF | 6.5MPa,270K | 1% |
sH | H2/MTBE | 100MPa,270K | 1.4% |
sc | H2/TBAB | 16MPa,281.15K | 0.046% |
晶型 结构 | 体系 | 生成温压条件 | 储氢密度(质量分数) |
---|---|---|---|
sI | H2/CO2 | 200MPa,270K | 0.37% |
sII | 纯水 | 200~300MPa,240~249K | 5.3% |
sII | H2/THF | 6.5MPa,270K | 1% |
sH | H2/MTBE | 100MPa,270K | 1.4% |
sc | H2/TBAB | 16MPa,281.15K | 0.046% |
文献 | 强化方法 | 研究课题 |
---|---|---|
谢应明等[ | 机械搅拌 | 搅拌式强化以TBAB为促进剂储氢 |
吕秋楠等[ | 鼓泡 | 研究鼓泡器中水合物的生成动力学 |
郝文峰[ | 喷雾 | 利用半连续喷淋式反应釜生成水合物 |
Zhong等[ | 表面活性剂 | 利用十二烷基硫酸钠(SDS)促进生成水合物 |
吴宛青等[ | 表面活性剂 | 研究不同表面活性剂促进水合物生成的动力学 |
Samad等[ | 纳米粒子 | 研究银纳米颗粒对水合物生成的促进效果 |
胡腾等[ | 多孔介质 | 研究石英砂对水合物生成的影响 |
文献 | 强化方法 | 研究课题 |
---|---|---|
谢应明等[ | 机械搅拌 | 搅拌式强化以TBAB为促进剂储氢 |
吕秋楠等[ | 鼓泡 | 研究鼓泡器中水合物的生成动力学 |
郝文峰[ | 喷雾 | 利用半连续喷淋式反应釜生成水合物 |
Zhong等[ | 表面活性剂 | 利用十二烷基硫酸钠(SDS)促进生成水合物 |
吴宛青等[ | 表面活性剂 | 研究不同表面活性剂促进水合物生成的动力学 |
Samad等[ | 纳米粒子 | 研究银纳米颗粒对水合物生成的促进效果 |
胡腾等[ | 多孔介质 | 研究石英砂对水合物生成的影响 |
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