Chemical Industry and Engineering Progress ›› 2024, Vol. 43 ›› Issue (7): 3534-3550.DOI: 10.16085/j.issn.1000-6613.2024-0441
• Column: Thermochemical Reaction Engineering Technology • Previous Articles
LIU Wenjin(), ZHANG Yuming(), LI Jiazhou, ZHANG Wei, CHEN Zhewen
Received:
2024-03-18
Revised:
2024-04-23
Online:
2024-08-14
Published:
2024-07-10
Contact:
ZHANG Yuming
通讯作者:
张玉明
作者简介:
刘文津(1995—),男,博士研究生,研究方向为燃料热转化。E-mail:lwj15910652331@163.com。
基金资助:
CLC Number:
LIU Wenjin, ZHANG Yuming, LI Jiazhou, ZHANG Wei, CHEN Zhewen. State of the art and prospect of typical petroleum thermal processing technology[J]. Chemical Industry and Engineering Progress, 2024, 43(7): 3534-3550.
刘文津, 张玉明, 李家州, 张炜, 陈哲文. 典型石油热加工技术发展现状及展望[J]. 化工进展, 2024, 43(7): 3534-3550.
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技术名称 | 研发单位 | 反应器 | 热载体 | 裂化器 温度/℃ | 压力 /MPa | 裂化停留时间/s | 裂化器气氛 |
---|---|---|---|---|---|---|---|
延迟焦化[ | 美国标准石油公司率先研发 | 管式炉+焦炭塔 | 无 | 500 | 0.1~0.35 | ≤60 | H2O |
流化焦化[ | Exxon Mobile率先研发 | 流化床裂化器+燃烧器 | 热焦粉 | 480~550 | 0.07~0.09 | 1~2 | H2O |
灵活焦化[ | Exxon Mobile率先研发 | 流化床裂化器+加热器+气化器 | 热焦粉 | 480~550 | 0.07~0.09 | 1~2 | H2O、H2、CO |
ART[ | 恩格尔哈德&凯洛格公司 | 流化床裂化器+燃烧器 | 惰性颗粒 | 450~530 | 0.1~0.3 | <2 | H2O、NH3 |
KKI[ | 日本神户制钢&兴亚石油&出光兴产 | 流化床裂化器+加热器+气化器+还原器 | 铁矿石粉 | 500~560 | 0.5~1 | 0.3~0.8 | H2O |
OSI[ | 中国石油大学(北京) | 流化床裂化-气化耦合反应器 | 混合热载体 | 450~700 | 0.1 | 1~20 | H2O、H2、CO |
技术名称 | 研发单位 | 反应器 | 热载体 | 裂化器 温度/℃ | 压力 /MPa | 裂化停留时间/s | 裂化器气氛 |
---|---|---|---|---|---|---|---|
延迟焦化[ | 美国标准石油公司率先研发 | 管式炉+焦炭塔 | 无 | 500 | 0.1~0.35 | ≤60 | H2O |
流化焦化[ | Exxon Mobile率先研发 | 流化床裂化器+燃烧器 | 热焦粉 | 480~550 | 0.07~0.09 | 1~2 | H2O |
灵活焦化[ | Exxon Mobile率先研发 | 流化床裂化器+加热器+气化器 | 热焦粉 | 480~550 | 0.07~0.09 | 1~2 | H2O、H2、CO |
ART[ | 恩格尔哈德&凯洛格公司 | 流化床裂化器+燃烧器 | 惰性颗粒 | 450~530 | 0.1~0.3 | <2 | H2O、NH3 |
KKI[ | 日本神户制钢&兴亚石油&出光兴产 | 流化床裂化器+加热器+气化器+还原器 | 铁矿石粉 | 500~560 | 0.5~1 | 0.3~0.8 | H2O |
OSI[ | 中国石油大学(北京) | 流化床裂化-气化耦合反应器 | 混合热载体 | 450~700 | 0.1 | 1~20 | H2O、H2、CO |
研发单位 | 技术特点 | 应用现状 |
---|---|---|
中国石油大学(北京)[ | 电磁感应加热供能 | 2022年工业示范 |
Lummus公司[ | 蒸汽裂解炉主要压缩机的蒸汽涡轮部分更换为电动驱动,可实现CO2零排放 | 2022年首次工业化应用 |
BASF公司、沙特基础工业公司和Linde公司[ | 直接加热,电流直接应用于反应器内的管道; 间接加热,利用放置在管道周围加热电气元件的辐射加热 | 2023年启动建设工业化装置 |
中石化上海工程公司和华东理工大学[ | 新型高收率、低排放SH-III型裂解炉 | 2023年完成技术包开发 |
Coolbrook公司和Linde公司[ | 通过旋转叶片流的空气动力,转化为可再生能源电力给蒸汽裂解炉供能 | 2024年建成首批工业装置 |
Shell公司和Dow公司[ | 基于理论电气化模型改造现有燃气蒸汽裂解炉 | 2025年开始建造中试装置 |
研发单位 | 技术特点 | 应用现状 |
---|---|---|
中国石油大学(北京)[ | 电磁感应加热供能 | 2022年工业示范 |
Lummus公司[ | 蒸汽裂解炉主要压缩机的蒸汽涡轮部分更换为电动驱动,可实现CO2零排放 | 2022年首次工业化应用 |
BASF公司、沙特基础工业公司和Linde公司[ | 直接加热,电流直接应用于反应器内的管道; 间接加热,利用放置在管道周围加热电气元件的辐射加热 | 2023年启动建设工业化装置 |
中石化上海工程公司和华东理工大学[ | 新型高收率、低排放SH-III型裂解炉 | 2023年完成技术包开发 |
Coolbrook公司和Linde公司[ | 通过旋转叶片流的空气动力,转化为可再生能源电力给蒸汽裂解炉供能 | 2024年建成首批工业装置 |
Shell公司和Dow公司[ | 基于理论电气化模型改造现有燃气蒸汽裂解炉 | 2025年开始建造中试装置 |
技术名称 | 乙烯 | 丙烯 | 尾气(主要是甲烷) | 丁二烯 | C4抽余油 | 粗汽油 | 焦炭 | 酸性气 | 丙烯/乙烯 | 总烯烃 |
---|---|---|---|---|---|---|---|---|---|---|
蒸汽裂解 | 36.25 | 16.56 | 16.98 | 5.11 | 4.58 | 18.49 | 1.77 | 0.17 | 0.46 | 52.81 |
ACO催化热裂解 | 31.93 | 29.44 | 15.14 | 0 | 0 | 21.62 | 1.75 | 0.12 | 0.92 | 61.37 |
技术名称 | 乙烯 | 丙烯 | 尾气(主要是甲烷) | 丁二烯 | C4抽余油 | 粗汽油 | 焦炭 | 酸性气 | 丙烯/乙烯 | 总烯烃 |
---|---|---|---|---|---|---|---|---|---|---|
蒸汽裂解 | 36.25 | 16.56 | 16.98 | 5.11 | 4.58 | 18.49 | 1.77 | 0.17 | 0.46 | 52.81 |
ACO催化热裂解 | 31.93 | 29.44 | 15.14 | 0 | 0 | 21.62 | 1.75 | 0.12 | 0.92 | 61.37 |
技术 名称 | 原料性质 | 操作参数 | 产物分布 | ||||||||||||||||
---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
原料 类型 | 密度(20℃) /g·cm-3 | 康氏 残炭值 | C质量分数 /% | H质量分数 /% | S质量分数 /% | N质量分数 /% | 催化剂类型 | 反应 温度 /℃ | 停留 时间/s | 干气(主要是甲烷) | 乙烯 | 丙烯 | 碳四 烯烃 | 汽油 | 柴油+ 煤油 | 焦炭 | 总低碳烯烃 | 丙烯 /乙烯 | |
HCC[ | 常压 渣油 | 0.888 | 4.1 | 86.39 | 13.25 | 0.117 | 0.177 | LCM-5 | 670 | 1.5 | 17.33 | 26.1 | 14.99 | 9.13 | — | — | 8.99 | 50.22 | 0.57 |
CPP[ | 常压 渣油 | 0.8953 | 4.3 | 86.52 | 13.03 | 0.15 | 0.28 | CEP-1(SY) | 640 | <1 | 16.74 | 20.37 | 18.23 | 7.52 | 14.82 | 7.93 | 10.66 | 46.12 | 0.9 |
DCP[ | 重质 油A | 0.91 | 4.13 | 86.48 | 12.98 | 0.33 | 0.19 | LTD纳米分子筛 | 650 | 0.8 | 1.62 | 3.43 | 20.55 | 19.98 | 26.19 | 10.21 | 8.6 | 43.96 | 5 |
MDCP[ | 重质 油A | 0.91 | 4.13 | 86.48 | 12.98 | 0.33 | 0.19 | 纳米分子筛 | 一级620/二级670 | 一级0.3/二级0.5 | 7.91 | 16.06 | 24.57 | 10.91 | 14.27 | 9.23 | 9.54 | 51.54 | 1.53 |
技术 名称 | 原料性质 | 操作参数 | 产物分布 | ||||||||||||||||
---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
原料 类型 | 密度(20℃) /g·cm-3 | 康氏 残炭值 | C质量分数 /% | H质量分数 /% | S质量分数 /% | N质量分数 /% | 催化剂类型 | 反应 温度 /℃ | 停留 时间/s | 干气(主要是甲烷) | 乙烯 | 丙烯 | 碳四 烯烃 | 汽油 | 柴油+ 煤油 | 焦炭 | 总低碳烯烃 | 丙烯 /乙烯 | |
HCC[ | 常压 渣油 | 0.888 | 4.1 | 86.39 | 13.25 | 0.117 | 0.177 | LCM-5 | 670 | 1.5 | 17.33 | 26.1 | 14.99 | 9.13 | — | — | 8.99 | 50.22 | 0.57 |
CPP[ | 常压 渣油 | 0.8953 | 4.3 | 86.52 | 13.03 | 0.15 | 0.28 | CEP-1(SY) | 640 | <1 | 16.74 | 20.37 | 18.23 | 7.52 | 14.82 | 7.93 | 10.66 | 46.12 | 0.9 |
DCP[ | 重质 油A | 0.91 | 4.13 | 86.48 | 12.98 | 0.33 | 0.19 | LTD纳米分子筛 | 650 | 0.8 | 1.62 | 3.43 | 20.55 | 19.98 | 26.19 | 10.21 | 8.6 | 43.96 | 5 |
MDCP[ | 重质 油A | 0.91 | 4.13 | 86.48 | 12.98 | 0.33 | 0.19 | 纳米分子筛 | 一级620/二级670 | 一级0.3/二级0.5 | 7.91 | 16.06 | 24.57 | 10.91 | 14.27 | 9.23 | 9.54 | 51.54 | 1.53 |
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