CIESC Journal ›› 2021, Vol. 72 ›› Issue (9): 4607-4615.DOI: 10.11949/0438-1157.20210188
• Fluid dynamics and transport phenomena • Previous Articles Next Articles
Yang LIU(
),Iqra AYUB,Fusheng YANG,Zhen WU,Zaoxiao ZHANG(
)
Received:2021-01-31
Revised:2021-06-07
Online:2021-09-05
Published:2021-09-05
Contact:
Zaoxiao ZHANG
通讯作者:
张早校
作者简介:刘洋(1994—),男,博士研究生,基金资助:CLC Number:
Yang LIU, Iqra AYUB, Fusheng YANG, Zhen WU, Zaoxiao ZHANG. Hydrogen thermal coupling transfer mechanism based on metal hydride high temperature heat storage technology[J]. CIESC Journal, 2021, 72(9): 4607-4615.
刘洋, AYUB Iqra, 杨福胜, 吴震, 张早校. 基于金属氢化物高温蓄热的氢热耦合传递机理[J]. 化工学报, 2021, 72(9): 4607-4615.
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Fig.11 Variation curves of average bed reaction fraction and heat transfer fluid output temperature with time under different wall heat transfer coefficients
| 壁面传热系数/ (W/(m2·K)) | 峰值点对应 时间/s | 峰值点对应 温度/℃ | 反应锋面形成 时间/s | 反应锋面形成 温度/℃ | 初始下降 斜率/(℃/s) | 有效输出 温度/℃ |
|---|---|---|---|---|---|---|
| 1000 | 34.60 | 331.27 | 91.66 | 327.65 | 0.063 | 313.23 |
| 1500 | 34.60 | 333.87 | 84.71 | 329.84 | 0.080 | 313.67 |
| 2000 | 32.06 | 335.32 | 80.23 | 331.19 | 0.086 | 313.96 |
| 2500 | 32.06 | 336.26 | 76.31 | 332.59 | 0.088 | 314.03 |
| 3000 | 32.06 | 336.91 | 71.35 | 333.11 | 0.097 | 314.14 |
Table 1 Peak point, reaction front parameters and output temperature under different wall heat transfer coefficients
| 壁面传热系数/ (W/(m2·K)) | 峰值点对应 时间/s | 峰值点对应 温度/℃ | 反应锋面形成 时间/s | 反应锋面形成 温度/℃ | 初始下降 斜率/(℃/s) | 有效输出 温度/℃ |
|---|---|---|---|---|---|---|
| 1000 | 34.60 | 331.27 | 91.66 | 327.65 | 0.063 | 313.23 |
| 1500 | 34.60 | 333.87 | 84.71 | 329.84 | 0.080 | 313.67 |
| 2000 | 32.06 | 335.32 | 80.23 | 331.19 | 0.086 | 313.96 |
| 2500 | 32.06 | 336.26 | 76.31 | 332.59 | 0.088 | 314.03 |
| 3000 | 32.06 | 336.91 | 71.35 | 333.11 | 0.097 | 314.14 |
Fig.12 Variation curves of average bed reaction fraction and heat transfer fluid output temperature with time under different bed thermal conductivity
| 床层热导率/ (W/(m·K)) | 峰值点对应 时间/s | 峰值点对应 温度/℃ | 有效输出 温度/℃ | 平台末端 时间/s | 反应完成 时间/s | 300℃对应 时间/s | 余热散热 时间/s | 散热段斜率/ (℃/s) |
|---|---|---|---|---|---|---|---|---|
| 1.0 | 32.06 | 336.91 | 314.14 | 8113.33 | 8901.81 | 11204.18 | 2302.37 | 0.0061 |
| 1.5 | 32.06 | 338.56 | 317.92 | 6156.81 | 7073.56 | 9174.89 | 2101.33 | 0.0085 |
| 2.0 | 34.60 | 339.56 | 322.50 | 5311.92 | 6175.61 | 8040.73 | 1865.12 | 0.0121 |
| 2.5 | 33.64 | 340.24 | 325.43 | 4912.98 | 5672.79 | 7306.30 | 1633.51 | 0.0156 |
| 3.0 | 34.78 | 340.73 | 327.11 | 4201.35 | 5324.55 | 6869.36 | 1544.81 | 0.0175 |
Table 2 Peak point and reactor output parameters under different bed thermal conductivity
| 床层热导率/ (W/(m·K)) | 峰值点对应 时间/s | 峰值点对应 温度/℃ | 有效输出 温度/℃ | 平台末端 时间/s | 反应完成 时间/s | 300℃对应 时间/s | 余热散热 时间/s | 散热段斜率/ (℃/s) |
|---|---|---|---|---|---|---|---|---|
| 1.0 | 32.06 | 336.91 | 314.14 | 8113.33 | 8901.81 | 11204.18 | 2302.37 | 0.0061 |
| 1.5 | 32.06 | 338.56 | 317.92 | 6156.81 | 7073.56 | 9174.89 | 2101.33 | 0.0085 |
| 2.0 | 34.60 | 339.56 | 322.50 | 5311.92 | 6175.61 | 8040.73 | 1865.12 | 0.0121 |
| 2.5 | 33.64 | 340.24 | 325.43 | 4912.98 | 5672.79 | 7306.30 | 1633.51 | 0.0156 |
| 3.0 | 34.78 | 340.73 | 327.11 | 4201.35 | 5324.55 | 6869.36 | 1544.81 | 0.0175 |
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