CN103463826B - 精馏分离方法 - Google Patents
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- CN103463826B CN103463826B CN201310364127.7A CN201310364127A CN103463826B CN 103463826 B CN103463826 B CN 103463826B CN 201310364127 A CN201310364127 A CN 201310364127A CN 103463826 B CN103463826 B CN 103463826B
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CN107266320B (zh) * | 2017-06-26 | 2020-01-24 | 安徽省化工设计院 | 一种硝基氯苯精馏分离中综合能耗回收的工艺方法 |
CN109320417A (zh) * | 2018-11-29 | 2019-02-12 | 武汉有机实业有限公司 | 利用间壁塔精制苯甲酸苄酯的装置及方法 |
CN114805080A (zh) * | 2022-06-10 | 2022-07-29 | 福建技术师范学院 | 一种连续分离3-氯-4-氟硝基苯的方法 |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
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CN1177513A (zh) * | 1996-04-30 | 1998-04-01 | 巴斯福股份公司 | 用于多组分混合物连续分馏的分壁式蒸馏塔 |
CN1469765A (zh) * | 2000-09-20 | 2004-01-21 | �����ɷ� | 蒸馏分离c5+切取馏分的方法和装置 |
CN101289396A (zh) * | 2008-05-30 | 2008-10-22 | 浙江富盛控股集团有限公司 | 一种邻、间、对硝基氯苯混合组分的分离利用方法 |
CN101759569A (zh) * | 2010-01-12 | 2010-06-30 | 南京师范大学 | 多股侧线出料精馏和连续结晶集成法提取高纯度对硝基氯化苯和邻硝基氯化苯的方法 |
CN201832434U (zh) * | 2010-10-15 | 2011-05-18 | 中国石油化工股份有限公司 | 一种新型分壁精馏塔 |
CN102583393A (zh) * | 2012-02-27 | 2012-07-18 | 天津大学 | 一种三氯氢硅提纯的双热泵精馏装置及操作方法 |
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Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
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CN1177513A (zh) * | 1996-04-30 | 1998-04-01 | 巴斯福股份公司 | 用于多组分混合物连续分馏的分壁式蒸馏塔 |
CN1469765A (zh) * | 2000-09-20 | 2004-01-21 | �����ɷ� | 蒸馏分离c5+切取馏分的方法和装置 |
CN101289396A (zh) * | 2008-05-30 | 2008-10-22 | 浙江富盛控股集团有限公司 | 一种邻、间、对硝基氯苯混合组分的分离利用方法 |
CN101759569A (zh) * | 2010-01-12 | 2010-06-30 | 南京师范大学 | 多股侧线出料精馏和连续结晶集成法提取高纯度对硝基氯化苯和邻硝基氯化苯的方法 |
CN201832434U (zh) * | 2010-10-15 | 2011-05-18 | 中国石油化工股份有限公司 | 一种新型分壁精馏塔 |
CN102583393A (zh) * | 2012-02-27 | 2012-07-18 | 天津大学 | 一种三氯氢硅提纯的双热泵精馏装置及操作方法 |
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Denomination of invention: Distillation separation method Effective date of registration: 20230117 Granted publication date: 20150513 Pledgee: Industrial and Commercial Bank of China Limited Yangzhou Hanjiang Sub-branch Pledgor: Yangzhou Tongyang Chemical Equipment Co.,Ltd. Registration number: Y2023320000030 |
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