Chemical Industry and Engineering Progress ›› 2025, Vol. 44 ›› Issue (8): 4754-4771.DOI: 10.16085/j.issn.1000-6613.2025-0550
• Process systems modeling and simulation • Previous Articles
CHEN Sheng1(
), LIU Zhongwei2, LYU Rongrong1, MIAO Chao3, ZHOU Siya4, JIANG Jingjing3, CHEN Rui4, HUANG Ganghua3, HE Meng1, ZHU Liyun5(
)
Received:2025-04-14
Revised:2025-05-06
Online:2025-09-08
Published:2025-08-25
Contact:
CHEN Sheng, ZHU Liyun
陈昇1(
), 刘忠伟2, 吕蓉蓉1, 苗超3, 周斯雅4, 江晶晶3, 陈锐4, 黄刚华3, 何萌1, 朱丽云5(
)
通讯作者:
陈昇,朱丽云
作者简介:陈昇(1987—),男,博士,正高级工程师,研究方向为多相流、承压设备风险防控、泄漏检监测、腐蚀防护。E-mail:chensheng_csei@163.com。
基金资助:CLC Number:
CHEN Sheng, LIU Zhongwei, LYU Rongrong, MIAO Chao, ZHOU Siya, JIANG Jingjing, CHEN Rui, HUANG Ganghua, HE Meng, ZHU Liyun. Simulation of multi-field interactive damage caused by acid gas condensation erosion in high-sulfur natural gas desulfurization purification units[J]. Chemical Industry and Engineering Progress, 2025, 44(8): 4754-4771.
陈昇, 刘忠伟, 吕蓉蓉, 苗超, 周斯雅, 江晶晶, 陈锐, 黄刚华, 何萌, 朱丽云. 高含硫天然气脱硫净化装置酸气凝露冲蚀多场交互损伤模拟[J]. 化工进展, 2025, 44(8): 4754-4771.
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URL: https://hgjz.cip.com.cn/EN/10.16085/j.issn.1000-6613.2025-0550
| 类型 | 参数 | 数值 |
|---|---|---|
| 气相 | ||
| 氮气 | 体积分数εnitrogen | 0.658 |
| 二氧化碳 | 体积分数εcarbon-dioxide | 0.256 |
| 水蒸气 | 体积分数εwater-vapor | 0.063 |
| 硫化氢 | 体积分数εhydrogen-sulfide | 0.023 |
| 液相 | ||
| 水 | — | — |
| 二氧化碳(溶解) | — | — |
| 硫化氢(溶解) | — | — |
| 离散相 | ||
| 液滴 | 质量流率/kg·s-1 | 0.0586 |
| 类型 | 参数 | 数值 |
|---|---|---|
| 气相 | ||
| 氮气 | 体积分数εnitrogen | 0.658 |
| 二氧化碳 | 体积分数εcarbon-dioxide | 0.256 |
| 水蒸气 | 体积分数εwater-vapor | 0.063 |
| 硫化氢 | 体积分数εhydrogen-sulfide | 0.023 |
| 液相 | ||
| 水 | — | — |
| 二氧化碳(溶解) | — | — |
| 硫化氢(溶解) | — | — |
| 离散相 | ||
| 液滴 | 质量流率/kg·s-1 | 0.0586 |
| 类型 | 参数 | 数值 |
|---|---|---|
| 速度入口 | 入口压力/Pa | 106000 |
| 温度/K | 313.15 | |
| 湍流强度/% | 7.306 | |
| 水力直径/m | 0.6 | |
| 速度/m·s-1 | 23.34 | |
| 压力出口 | 出口压力/Pa | 97000 |
| 湍流强度/% | 7.306 | |
| 水力直径/m | 0.6 | |
| 壁面材料 | 离散边界条件类型 | 逸出 |
| 密度/kg·m-3 | 7850 | |
| 壁面边界条件 | 温度/K | 293.15 |
| 壁厚/m | 0.01 | |
| 离散相剪切条件 | 反射系数, φ=0.5 | |
| 壁面粗糙度 | 标准 |
| 类型 | 参数 | 数值 |
|---|---|---|
| 速度入口 | 入口压力/Pa | 106000 |
| 温度/K | 313.15 | |
| 湍流强度/% | 7.306 | |
| 水力直径/m | 0.6 | |
| 速度/m·s-1 | 23.34 | |
| 压力出口 | 出口压力/Pa | 97000 |
| 湍流强度/% | 7.306 | |
| 水力直径/m | 0.6 | |
| 壁面材料 | 离散边界条件类型 | 逸出 |
| 密度/kg·m-3 | 7850 | |
| 壁面边界条件 | 温度/K | 293.15 |
| 壁厚/m | 0.01 | |
| 离散相剪切条件 | 反射系数, φ=0.5 | |
| 壁面粗糙度 | 标准 |
| 项目 | 公式 |
|---|---|
| 气相黏度拟合公式 | |
| 气相热导率 | |
| 气相比热容 | |
| 液相中CO2(l)溶解度 | |
| 液相中H2S(l)溶解度 |
| 项目 | 公式 |
|---|---|
| 气相黏度拟合公式 | |
| 气相热导率 | |
| 气相比热容 | |
| 液相中CO2(l)溶解度 | |
| 液相中H2S(l)溶解度 |
| 位置 | 壁厚/mm | 减薄速率/mm·a-1 |
|---|---|---|
| a1 | 5.25 | 0.38 |
| a2 | 6.01 | 0.32 |
| a3 | 5.00 | 0.40 |
| a4 | 6.00 | 0.32 |
| a5 | 6.13 | 0.31 |
| a6 | 8.96 | 0.08 |
| a7 | 8.99 | 0.08 |
| a8 | 5.08 | 0.41 |
| a9 | 4.45 | 0.44 |
| a10 | 3.63 | 0.51 |
| a11 | 3.91 | 0.49 |
| a12 | 4.13 | 0.47 |
| 位置 | 壁厚/mm | 减薄速率/mm·a-1 |
|---|---|---|
| a1 | 5.25 | 0.38 |
| a2 | 6.01 | 0.32 |
| a3 | 5.00 | 0.40 |
| a4 | 6.00 | 0.32 |
| a5 | 6.13 | 0.31 |
| a6 | 8.96 | 0.08 |
| a7 | 8.99 | 0.08 |
| a8 | 5.08 | 0.41 |
| a9 | 4.45 | 0.44 |
| a10 | 3.63 | 0.51 |
| a11 | 3.91 | 0.49 |
| a12 | 4.13 | 0.47 |
| 液滴相质量分数 | 气相冷凝速率/kg·s-1 | 硫化氢体积分数 | 二氧化碳体积分数 | 液滴大小/µm |
|---|---|---|---|---|
| 0.05 | 0.36 | 0.01 | 0.200 | 30 |
| 0.1 | 0.10 | 0.02 | 0.225 | 50 |
| 0.15 | 0.12 | 0.03 | 0.256 | 100 |
| 0.2 | 0.14 | 0.04 | 0.300 | 150 |
| 0.18 | 30~150 |
| 液滴相质量分数 | 气相冷凝速率/kg·s-1 | 硫化氢体积分数 | 二氧化碳体积分数 | 液滴大小/µm |
|---|---|---|---|---|
| 0.05 | 0.36 | 0.01 | 0.200 | 30 |
| 0.1 | 0.10 | 0.02 | 0.225 | 50 |
| 0.15 | 0.12 | 0.03 | 0.256 | 100 |
| 0.2 | 0.14 | 0.04 | 0.300 | 150 |
| 0.18 | 30~150 |
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