METHOD AND APPARATUS FOR CONTINUOUSLY PRODUCING 1,1,1,2,3-PENTAFLUOROPROPANE WITH HIGH YIELD
申请人:FOOSUNG CO., LTD.
公开号:US20140135538A1
公开(公告)日:2014-05-15
A method and apparatus for method of continuously producing 1,1,1,2,3-pentafluoropropane with high yield is provided. The method includes (a) bringing a CoF
3
-containing cobalt fluoride in a reactor into contact with 3,3,3-trifluoropropene to produce a CoF
2
-containing cobalt fluoride and 1,1,1,2,3-pentafluoropropane, (b) transferring the CoF
2
-containing cobalt fluoride in the reactor to a regenerator and bringing the transferred CoF
2
-containing cobalt fluoride into contact with fluorine gas to regenerate a CoF
3
-containing cobalt fluoride, and (c) transferring the CoF
3
-containing cobalt fluoride in the regenerator to the reactor and employing the transferred CoF
3
-containing cobalt fluoride in Operation (a). Accordingly, the 1,1,1,2,3-pentafluoropropane can be continuously produced with high yield from the 3,3,3-trifluoropropene using a cobalt fluoride (CoF
2
/CoF
3
) as a fluid catalyst, thereby improving the reaction stability and readily adjusting the optimum conversion rate and selectivity.
提供一种用高产率连续生产
1,1,1,2,3-五氟丙烷的方法和装置。该方法包括(a)将含
CoF3的
氟化
钴在反应器中与
3,3,3-三氟丙烯接触,产生含
CoF2的
氟化
钴和
1,1,1,2,3-五氟丙烷,(b)将反应器中的含 的
氟化
钴转移到再生器,并使转移后的含 的
氟化
钴与
氟气接触以再生含 的
氟化
钴,(c)将再生器中的含 的
氟化
钴转移到反应器,并在操作(a)中使用转移后的含 的
氟化
钴。因此,可以利用
氟化
钴( / )作为流动催化剂,从
3,3,3-三氟丙烯高产率连续生产
1,1,1,2,3-五氟丙烷,从而提高反应稳定性,便于调整最佳转化率和选择性。
[EN] PROCESS FOR THE PREPARATION OF 1,1,1,3,3,3-HEXAFLUOROPROPANE AND AT LEAST ONE OF 1,1,1,2,3,3-HEXAFLUOROPROPANE AND 1,1,1,2,3,3,3-HEPTAFLUOROPROPANE<br/>[FR] PROCEDE POUR PREPARER DU 1,1,1,3,3,3-HEXAFLUOROPROPANE, DU 1,1,1,2,3,3-HEXAFLUOROPROPANE ET/OU DU 1,1,1,2,3,3,3-HEPTAFLUOROPROPANE
申请人:DU PONT
公开号:WO2005037742A1
公开(公告)日:2005-04-28
A process is disclosed for the manufacture of 1,1,1,3,3,3-hexafluoropropane (HFC-236fa) and at least one 1,1,1,2,3,3-hexafluoropropane (HFC-236ea) and 1,1,1,2,3,3,3-heptafluoropropane (HFC-227ea). The process involves (a) reacting HF, Cl2, and at least one halopropene of the formula CX3CCl=CX2 (where each X is independently F or Cl) to produce a product including both CF3CCl2CF3 and CF3CClFCClF2; (b) reacting CF3CCl2CF3 and CF3CClFCClF2 produced in (a) with hydrogen to produce a product comprising CF3CH2CF3 and at least one compound selected from the group consisting of CHF2CHFCF3, and CF3CHFCF3; and (c) recovering from the product produced in (b), CF3CH2CF3 and at least one compound selected from the group consisting of CHF2CHFCF3 and CF3CHFCF3. In (a), the CF3CCl2CF3 and CF3CClFCClF2 are produced in the presence of a chlorofluorination catalyst including a ZnCr2O4/crystalline α-chromium oxide composition, a ZnCr2O4/crystalline α-chromium oxide composition which has been treated with a fluorinating agent, a zinc halide/α-chromium oxide composition and/or a zinc halide/α-chromium oxide composition which has been treated with a fluorinating agent.
揭示了一种用于制造
1,1,1,3,3,3-六氟丙烷(HFC-236fa)和至少一种
1,1,1,2,3,3-六氟丙烷(HFC-236ea)以及1,1,1,2,3,3,3-
七氟丙烷(HFC-227ea)的工艺。该工艺涉及(a)反应HF、Cl2和至少一种具有分子式CX3CCl=CX2的卤代
丙烯,其中每个X独立地为F或Cl,以产生包括CF3CCl2CF3和CF3CClFCClF2在内的产物;(b)将(a)中产生的CF3CCl2CF3和CF3CClFCClF2与氢反应,以产生包括CF3CH2CF3和从CHF2CHFCF3和CF3CHFCF3组成的至少一种化合物的产物;(c)从(b)中产生的产物中回收CF3CH2CF3和从CHF2CHFCF3和CF3CHFCF3组成的至少一种化合物。在(a)中,CF3CCl2CF3和CF3CClFCClF2在存在包括ZnCr2O4/结晶α-
氧化铬组合物、经过
氟化剂处理的ZnCr2O4/结晶α-
氧化铬组合物、
锌卤化合物/α-
氧化铬组合物和/或经过
氟化剂处理的
锌卤化合物/α-
氧化铬组合物的
氯氟化催化剂的情况下产生。
[EN] PROCESSES FOR SEPARATION OF 1,3,3,3-TETRAFLUOROPROPENE FROM HYDROGEN FLUORIDE BY AZEOTROPIC DISTILLATION<br/>[FR] PROCÉDÉS DE SÉPARATION DE 1,3,3,3-TÉTRAFLUOROPROPÈNE DE FLUORURE D'HYDROGÈNE PAR DISTILLATION AZÉOTROPIQUE
申请人:DU PONT
公开号:WO2009105521A1
公开(公告)日:2009-08-27
Disclosed herein is a process for the separation of HFC-1234ze and HF by azeotropic distillation. Additionally disclosed is a process for the separation of HFC1234ze, HFC-245eb and/or 245fa, and HF by azeotropic distillation.
本文披露了一种通过共沸蒸馏分离HFC-1234ze和HF的方法。此外,还披露了一种通过共沸蒸馏分离HFC1234ze、HFC-245eb和/或245fa和HF的方法。