Chemical Industry and Engineering Progress ›› 2025, Vol. 44 ›› Issue (S1): 74-83.DOI: 10.16085/j.issn.1000-6613.2025-0305
• Chemical processes and equipment • Previous Articles Next Articles
GUO Xuhao(
), YE Yiming, QI Xin, HU Shilin, ZHANG Pingzhu(
)
Received:2025-02-28
Revised:2025-05-06
Online:2025-11-24
Published:2025-10-25
Contact:
ZHANG Pingzhu
通讯作者:
张平柱
作者简介:郭栩豪(1998—),男,硕士研究生,研究方向为同位素分离。E-mail:15991088025@163.com。
CLC Number:
GUO Xuhao, YE Yiming, QI Xin, HU Shilin, ZHANG Pingzhu. Simulation of enrichment of 10B by cryogenic distillation of boron trifluoride[J]. Chemical Industry and Engineering Progress, 2025, 44(S1): 74-83.
郭栩豪, 叶一鸣, 齐鑫, 胡石林, 张平柱. 三氟化硼低温精馏法富集10B工艺的模拟[J]. 化工进展, 2025, 44(S1): 74-83.
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URL: https://hgjz.cip.com.cn/EN/10.16085/j.issn.1000-6613.2025-0305
| 参数 | 10BF3 | 11BF3 |
|---|---|---|
| C1 | 168.504 | 168.613 |
| C2 | -12179.500 | -12667.000 |
| C3 | 47.325 | 51.412 |
| C4 | -0.131 | -0.128 |
| C5 | -15.831 | -15.636 |
| C6 | 3.543×10-7 | 1.580×10-7 |
| C7 | 3.058 | 3.187 |
| C8 | 144.790 | 144.790 |
| C9 | 260.900 | 260.900 |
| 参数 | 10BF3 | 11BF3 |
|---|---|---|
| C1 | 168.504 | 168.613 |
| C2 | -12179.500 | -12667.000 |
| C3 | 47.325 | 51.412 |
| C4 | -0.131 | -0.128 |
| C5 | -15.831 | -15.636 |
| C6 | 3.543×10-7 | 1.580×10-7 |
| C7 | 3.058 | 3.187 |
| C8 | 144.790 | 144.790 |
| C9 | 260.900 | 260.900 |
| 参数 | 10BF3 | 11BF3 |
|---|---|---|
| 分子量 | 67 | 68 |
| 正常沸点/K | 172.84 | 172.71 |
| 临界温度/K | 260.90 | 260.68 |
| 临界压力/kPa | 4991.97 | 4977.64 |
| 偏心因子 | 0.4349 | 0.4302 |
| 参数 | 10BF3 | 11BF3 |
|---|---|---|
| 分子量 | 67 | 68 |
| 正常沸点/K | 172.84 | 172.71 |
| 临界温度/K | 260.90 | 260.68 |
| 临界压力/kPa | 4991.97 | 4977.64 |
| 偏心因子 | 0.4349 | 0.4302 |
| 精馏塔编号 | 塔顶丰度 | 塔底丰度 | 分离因子S | 全塔平均相对挥发度 | 最小理论塔板数N |
|---|---|---|---|---|---|
| CD1 | 14.2 | 30.1 | 2.602 | 1.00716 | 134 |
| CD2 | 13.4 | 31.9 | 3.027 | 1.00778 | 142 |
| 精馏塔编号 | 塔顶丰度 | 塔底丰度 | 分离因子S | 全塔平均相对挥发度 | 最小理论塔板数N |
|---|---|---|---|---|---|
| CD1 | 14.2 | 30.1 | 2.602 | 1.00716 | 134 |
| CD2 | 13.4 | 31.9 | 3.027 | 1.00778 | 142 |
| 参数 | CD1 | CD2 |
|---|---|---|
| 10BF3进料组成(摩尔分数)/% | 19.8 | 31.8 |
| 填料高度/m | 180 | 180 |
| 理论塔板数/块 | 180 | 180 |
| 进料流量/kg·h-1 | 1.065 | 0.36 |
| 塔底流量/kg·h-1 | 0.36 | 0.012 |
| 进料压力/kPa | 225 | 180 |
| 操作压力/kPa | 180 | 150 |
| 塔釜加热功率/kW | 7 | 7 |
| 塔顶冷凝形式 | 全冷凝 | |
| 参数 | CD1 | CD2 |
|---|---|---|
| 10BF3进料组成(摩尔分数)/% | 19.8 | 31.8 |
| 填料高度/m | 180 | 180 |
| 理论塔板数/块 | 180 | 180 |
| 进料流量/kg·h-1 | 1.065 | 0.36 |
| 塔底流量/kg·h-1 | 0.36 | 0.012 |
| 进料压力/kPa | 225 | 180 |
| 操作压力/kPa | 180 | 150 |
| 塔釜加热功率/kW | 7 | 7 |
| 塔顶冷凝形式 | 全冷凝 | |
| 结果及对比 | 一级塔 | 二级塔 | ||
|---|---|---|---|---|
| 塔顶10BF3丰度 | 塔底10BF3丰度 | 塔顶10BF3丰度 | 塔底10BF3丰度 | |
| 实验结果/% | 12.60 | 34.00 | 32.90 | 69.00 |
| IDEAL模拟结果/% | 13.63 | 31.85 | 30.78 | 62.80 |
| IDEAL相对误差/% | 8.17 | 6.32 | 6.44 | 8.99 |
| PR模拟结果/% | 12.36 | 34.31 | 33.04 | 71.10 |
| PR相对误差/% | 1.90 | 0.91 | 0.43 | 3.04 |
| 结果及对比 | 一级塔 | 二级塔 | ||
|---|---|---|---|---|
| 塔顶10BF3丰度 | 塔底10BF3丰度 | 塔顶10BF3丰度 | 塔底10BF3丰度 | |
| 实验结果/% | 12.60 | 34.00 | 32.90 | 69.00 |
| IDEAL模拟结果/% | 13.63 | 31.85 | 30.78 | 62.80 |
| IDEAL相对误差/% | 8.17 | 6.32 | 6.44 | 8.99 |
| PR模拟结果/% | 12.36 | 34.31 | 33.04 | 71.10 |
| PR相对误差/% | 1.90 | 0.91 | 0.43 | 3.04 |
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