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1. 发明授权

US06548720B2 Process for the manufacture of 1,1,1,3,3-pentafluoropropene, 2-chloro-pentafluoropropene and compositions comprising saturated derivatives thereof 失效
标题翻译：用于制备1,1,1,3,3-五氟丙烯，2-氯 - 五氟丙烯的方法和包含其饱和衍生物的组合物
公开(公告)号：US06548720B2
公开(公告)日：2003-04-15
申请号：US10061002
申请日：2002-01-30
申请人： William H. Manogue , V. N. Mallikarjuna Rao , Allen Capron Sievert , Steven H. Swearingen
发明人： William H. Manogue , V. N. Mallikarjuna Rao , Allen Capron Sievert , Steven H. Swearingen
IPC分类号： C07C1700
CPC分类号： C07C19/08 , B01J23/868 , B01J27/12 , B01J27/132 , B01J37/0009 , B01J37/06 , C07C17/00 , C07C17/087 , C07C17/21 , C07C17/23 , C07C17/354 , C07C17/38 , C07C43/12 , Y02P20/582 , C07C21/18
摘要： A process is disclosed for producing the pentfluropropenes of the formula CF3CX═CF2, where X is H or Cl. The process involves hydrodehalogenating CF3CCl2CF3 with hydrogen at an elevated temperature in the vapor phase over a catalyst comprising an elemental metal, metal oxide, metal halide and/or metal oxyhalide (the metal being copper, nickel, chromium and the halogen of said halides and said oxyhalides being fluorine and/or chlorine. Processes for producing the hydrofluorocarbons CF3CH2CHF2, CF3CHFCF3 and CF3CH2CF3 are also disclosed which involve (a) hydrodehalogenating CF3CCl2CF3 with the hydrogen as indicated above to produce a product comprising CF3CCl═CF2, CF3CH═CF2, HCl and HF; and (b) either reacting the CF3CCl═CF2 and/or CF3CH═CF2 produced in (a) in the vapor phase with hydrogen to produce CF3CH2CHF2, reacting CF3CCl═CF2 produced in (a) with HF to produce CF3CHFCF3, or reacting the CF3CH═CF2produced in (a) with HF to produce CF3CH2CF3. Azeotrope compositions of CF3CHFCH3 with HF, and a process for recovering HF from a product mixture comprising HF and CF3CHFCF3 are also disclosed. Also disclosed are compositions and a process for producing compositions comprising (c1) CF3CHFCF3, CF3CH2CF3 or CHF2CH2CF3 and (c2) at least one saturated halogenated hydrocarbon and/or ether having the formula: CnH2n+2−a−bClaFbOc wherein n is an integer from 1 to 4, a is an integer from 0 to 2n+1, b is an integer from 1 to 2n+2−a, and c is 0 or 1, provided that when c is 1 then n is an integer from 2 to 4, and provided that component (c2) does not include the selected component (c1) compound, wherein the molar ratio of component (c2) to component (c1) is between about 1:99 and a molar ratio of HF to component (c1) in an azeotrope or azeotrope-like composition of component (c1) with HF. The process involves (A) combining (i) the azeotropic composition with (ii) the fluorination precursor to component (c2); and (B) reacting a sufficient amount of the HF from the azeotrope or azeotrope-like composition(i) with precursor component (ii) to provide a composition containing components (c1) and (c2) in the desired ratio. The compositions include at least two (c1) compounds, at least one of which is an ether.
摘要翻译：公开了制备式CF 3 C X = CF 2的五氟丙烯的方法，其中X是H或Cl。该方法包括在气相中在升高的温度下在含有元素金属，金属氧化物，金属卤化物和/或金属卤氧化物（金属为铜，镍，铬和所述卤化物的卤素和所述卤化物的催化剂）的催化剂中用氢气脱氢CF 3 CCl 2 CF 3 还公开了用于制备氢氟烃CF 3 CH 2 CHF 2，CF 3 CHFCF 3和CF 3 CH 2 CF 3的方法，其涉及（a）如上所述用氢气将CF 3 CCl 2 CF 3加氢脱卤以产生包含CF 3 CCl = CF 2，CF 3 CH = CF 2，HCl和HF的产物将（a）中产生的CF 3 CCl = CF 2和/或CF 3 CH = CF 2与氢气反应以产生CF 3 CH 2 CHF 2，使（a）中制备的CF 3 CCl = CF 2与HF反应产生CF 3 CHFCF 3，或使 CF3CH = CF2，在HF中产生CF 3 CH 2 CF 3，CF 3 CHFCH 3与HF的共沸组合物，以及从含有HF和CF 3 CHFCF 3的产物混合物中回收HF的方法也被公开。还公开了组合物和制备组合物的方法，其包含（c1）CF 3 CHFCF 3，CF 3 CH 2 CF 3或CHF 2 CH 2 CF 3和（c2）至少一种具有下式的饱和卤代烃和/或醚：CnH2n + 2-a-bClaFbOc其中n是如图1〜图4所示，a为0〜2n + 1的整数，b为1〜2n + 2-a的整数，c为0或1，条件是当c为1时，n为2〜4的整数，并且条件是组分（c2）不包括选择

2. 发明授权

US6018083A Process for the production of fluorocarbons 失效
公开(公告)号：US6018083A
公开(公告)日：2000-01-25
申请号：US283450
申请日：1999-04-01
申请人： William H. Manogue , Mario Joseph Nappa , Allen Capron Sievert , V. N. Mallikarjuna Rao
发明人： William H. Manogue , Mario Joseph Nappa , Allen Capron Sievert , V. N. Mallikarjuna Rao
IPC分类号： C07C17/00 , C07C17/04 , C07C17/21 , C07C17/23 , C07C19/08 , C07C21/18 , C07C17/25 , C07C17/08
CPC分类号： C07C21/18 , C07C17/00 , C07C17/04 , C07C17/21 , C07C17/23 , C07C19/08
摘要： A process is disclosed for the separation of a mixture of HF and CF.sub.3 CClFCF.sub.3. The process involves placing the mixture in a separation zone at a temperature of from about -30.degree. C. to about 100.degree. C. and at a pressure sufficient to maintain the mixture in the liquid phase, whereby an organic-enriched phase comprising less than 50 mole percent HF is formed as the bottom layer and an HF-enriched phase comprising more than 90 mole percent HF is formed as the top layer. The organic-enriched phase can be withdrawn from the bottom of the separation zone and subjected to distillation in a distillation column to recover essentially pure CF.sub.3 CClFCF.sub.3. The distillate comprising HF and CF.sub.3 CClFCF.sub.3 can be removed from the top of the distillation column while essentially pure CF.sub.3 CClFCF.sub.3 can be recovered from the bottom of the distillation column. The HF-enriched phase can be withdrawn from the top of the separation zone and subjected to distillation in a distillation column. The distillate comprising HF and CF.sub.3 CClFCF.sub.3 can be removed from the top of the distillation column while essentially pure HF can be recovered from the bottom of the distillation column. If desired, the two distillates can be recycled to the separation zone.Also disclosed are compositions of hydrogen fluoride in combination with an effective amount of CF.sub.3 CClFCF.sub.3 to form an azeotrope or azeotrope-like composition with hydrogen fluoride. Included are compositions containing from about 38.4 to 47.9 mole percent CF.sub.3 CClFCF.sub.3.Also disclosed are processes for producing 1,1,1,2,3,3,3-heptafluoropropane. One process uses a mixture comprising HF and CF.sub.3 CClFCF.sub.3 and is characterized by preparing essentially pure CF.sub.3 CClFCF.sub.3 as indicated above, and reacting the CF.sub.3 CClFCF.sub.3 with hydrogen. Another process uses an azeotropic composition as described above, and reacts the CF.sub.3 CClFCF.sub.3 with hydrogen in the presence of HF.Also disclosed is a process for producing hexafluoropropene. This process is characterized by preparing essentially pure CF.sub.3 CClFCF.sub.3 as indicated above, and dehalogenating the CF.sub.3 CClFCF.sub.3.

3. 发明授权

US06376727B1 Processes for the manufacture of 1,1,1,3,3-pentafluoropropene, 2-chloro-pentafluoropropene and compositions comprising saturated derivatives thereof 失效
标题翻译：用于制造1,1,1,3,3-五氟丙烯，2-氯 - 五氟丙烯的方法和包含其饱和衍生物的组合物
公开(公告)号：US06376727B1
公开(公告)日：2002-04-23
申请号：US09367900
申请日：1999-08-19
申请人： V. N. Mallikarjuna Rao , Allen Capron Sievert
发明人： V. N. Mallikarjuna Rao , Allen Capron Sievert
IPC分类号： C07C1700
CPC分类号： C07C19/08 , B01J23/868 , B01J27/12 , B01J27/132 , B01J37/0009 , B01J37/06 , C07C17/00 , C07C17/087 , C07C17/21 , C07C17/23 , C07C17/354 , C07C17/38 , C07C43/12 , Y02P20/582 , C07C21/18
摘要： Disclosed are azeotropic compositions comprising CF3CHFCF3 and HF. Also disclosed are compositions and a process for producing compositions comprising (c1) CF3CHFCF3, CF3CH2CF3, or CHF2CH2CF3, and (c2) at least one saturated halogenated hydrocarbon and or ether having the formula: CnH2n+2−a−bClaFbOc wherein n is an integer from 1-4, a is an integer from 0-2n+1, b is an integer from 1-2n+2a, and c is 0 or 1, provided that when c is 1 then n is an integer from 2-4, and provided that component (c2) does not include the selected component (c1) compound, wherein the molar ratio of component (c2) to component (c1) is between about 1:99 and a molar ratio of HF to component (c1) in an azeotrope or azeotrope-like composition of component (c1) with HF. The process involves (A) combining (1) the azeotropic composition with (ii) the fluorination precursor to component (c2); and (B) reacting a sufficient amount of the HF from the azeotrope or azeotrope-like composition (1) with the precursor component (ii) to provide a composition containing components (c1) and (c2) in the desired ratio. The compositions include at least two (c1) compounds, at least one of which is an ether.
摘要翻译：公开了包含CF 3 CHFCF 3和HF的共沸组合物。还公开了组合物和制备包含（c1）CF 3 CHFCF 3，CF 3 CH 2 CF 3或CHF 2 CH 2 CF 3的组合物和（c2）至少一种具有下式的饱和卤代烃和或醚的组合物和方法：C n H 2n + 2-a-b Cl a F b O c其中n是整数从1-4开始，a是0-2n + 1的整数，b是1-2n + 2a的整数，c是0或1，条件是当c为1时，n为2-4的整数，（c2）与成分（c1）的摩尔比为约1:99，HF与成分（c1）的摩尔比在下述式（c2）中，式（c2）组分（c1）与HF的共沸物或类共沸组合物。该方法包括（A）将（1）共沸组合物与（ii）氟化前体与组分（c2）组合; 和（B）使足够量的来自共沸物或类共沸组合物（1）的HF与前体组分（ii）反应，以提供含有所需比例的组分（c1）和（c2）的组合物。组合物包括至少两种（c1）化合物，其中至少一种是醚。

4. 发明授权

US06224781B1 Compositions comprising hydrofluorocarbons and their manufacture 有权
标题翻译：包含氢氟碳化合物及其制备的组合物
公开(公告)号：US06224781B1
公开(公告)日：2001-05-01
申请号：US09137343
申请日：1998-08-20
申请人： Barry A. Mahler , V. N. Mallikarjuna Rao , Allen Capron Sievert , Munirpallam A. Subramanian , Edwin James Warwas
发明人： Barry A. Mahler , V. N. Mallikarjuna Rao , Allen Capron Sievert , Munirpallam A. Subramanian , Edwin James Warwas
IPC分类号： A62D100
CPC分类号： A62D1/0057 , A62D1/00
摘要： A process is disclosed for producing compositions including (a) a compound selected from the group consisting of CHF2CF3, CHF2CHF2, CH2FCF3, CH3CF3, CH3CHF2, CH2FCF2CHF2 and CHF2CF2CF2CHF2 and (b) at least one saturated halogenated hydrocarbon and/or ether having the formula: CnH2n+2−a−bClaFbOc wherein n is an integer from 1 to 4, a is an integer from 0 to 2n+1, b is an integer from 1 to 2n+2−a, and c is 0 or 1, provided that when c is 1 then n is an integer from 2 to 4, and provided that component (b) does not include the selected component (a) compound, wherein the molar ratio of component (b) to component (a) is between about 1:99 and a molar ratio of HF to component (a) in an azeotrope or azeotrope-like composition of component (a) with HF. This process involves (A) combining (i) the azeotrope or azeotrope-like composition with (ii) at least one fluorination precursor compound wherein the precursor component (ii) is the fluorination precursor to component (b); and (B) reacting a sufficient amount of the HF from the azeotrope or azeotrope-like composition (i) with precursor component (ii) to provide a composition containing components (a) and (b) in said ratio.
摘要翻译：公开了用于制备组合物的方法，其包括（a）选自CHF 2 CF 3，CHF 2 CHF 2，CH 2 FFC 3，CH 3 CF 3，CH 3 CHF 2，CH 2 F 2 CHF 2和CHF 2 CF 2 CF 2 CHF 2的化合物和（b）至少一种具有下式的饱和卤代烃和/或醚：其中n为1〜4的整数，a为0〜2n + 1的整数，b为1〜2n + 2-a的整数，c为0或1，条件是当c为1时，n为组分（b）与组分（a）的摩尔比为约1:99，摩尔比为2〜4的整数，并且组分（b）不包括所选择的组分（a）化合物，其中组分 HF与组分（a）在组分（a）的共沸物或类共沸组合物中与HF混合。该方法包括：（i）将共沸物或类共沸组合物与（ii）至少一种氟化前体化合物组合（其中前体组分（ii）为组分（b）的氟化前体）; 和（B）使来自共沸物或类共沸组合物（i）的足够量的HF与前体组分（ii）反应，以提供含有所述比例的组分（a）和（b）的组合物。

5. 发明授权

US06143938A Process for perhalocycloalkane purification 失效
标题翻译：全卤烷烃纯化方法
公开(公告)号：US06143938A
公开(公告)日：2000-11-07
申请号：US429271
申请日：1999-10-29
申请人： Allen Capron Sievert , V. N. Mallikarjuna Rao
发明人： Allen Capron Sievert , V. N. Mallikarjuna Rao
IPC分类号： C07C17/04 , C07C17/20 , C07C17/395 , C07C19/08 , C07C17/38
CPC分类号： C07C19/08 , C07C17/04 , C07C17/206 , C07C17/395
摘要： A process is disclosed for recovering at least one perhalocycloalkane selected from the group consisting of octafluorocyclobutane, hexafluoro-bis(trifluoromethyl)cyclobutane (1,2 and 1,3; cis and trans), 1,2-dichloro-1,2,3,3,4,4-hexafluorocyclobutane (cis and trans), 1,1,2,2-tetrachloro-3,3,4,4-tetrafluorocyclobutane, 1-chloro-1,2,2,3,3,4-hexafluoro-4-(trifluoromethyl)-cyclobutane, heptafluoro(trifluoromethyl)cyclobutane and chloroheptafluoro-cyclobutane from a mixture comprising (a) the perhalocycloalkane, (b) olefinic impurity and optionally (c) saturated fluorine-containing impurity selected from the group consisting of hydrochlorofluorocarbons, hydrofluorocarbons and mixtures thereof. The process involves (1) contacting the mixture with chlorine under conditions suitable for chlorinating the olefinic impurity, thereby converting the olefinic impurity to a saturated impurity containing at least one chlorine substituent and reducing the hydrogen content of the saturated fluorine-containing impurity (if present), and (2) separating said at least one perhalocycloalkane from the products produced during the chlorination of (1).Also disclosed is a process for producing n-decafluorobutane. The process involves contacting a mixture comprising octafluorocyclobutane (i.e., C-318) and 1,1,1,2,3,4,4,4-octafluorobutene-2 (FC-1318my) with chlorine under conditions suitable for converting the FC-1318my to 2,3-dichloro-1,1,1,2,3,4,4,4-octa-fluorobutane (i.e., CFC-318mbb); separating the C-318 from the CFC-318mbb; and reacting the CFC-318mbb with HF.
摘要翻译：公开了一种用于回收至少一种选自八氟环丁烷，六氟 - 双（三氟甲基）环丁烷（1,2和1,3;顺式和反式）的全卤烷烃的方法，1,2-二氯-1,2,3 ，3,4,4-六氟环丁烷（顺式和反式），1,1,2,2-四氯-3,3,4,4-四氟环丁烷，1-氯-1,2,2,3,3,4-四氟环丁烷六氟代-4-（三氟甲基） - 环丁烷，七氟（三氟甲基）环丁烷和氯三氟环丁烷，其包含（a）全卤代环烷烃，（b）烯属杂质和任选的（c）饱和含氟杂质，氢氯氟烃，氢氟碳化合物及其混合物。该方法包括（1）在适于氯化烯烃杂质的条件下使混合物与氯接触，从而将烯烃杂质转化为含有至少一个氯取代基的饱和杂质并降低饱和含氟杂质的氢含量（如果存在）和（2）从（1）的氯化期间产生的产物中分离出所述至少一种全卤烷烃。还公开了制备正九氟丁烷的方法。该方法包括使包含八氟环丁烷（即C-318）和1,1,1,2,3,4,4,4-八氟丁烯-2（FC-1318my）的混合物与氯在适于转化FC- 1318my至2,3-二氯-1,1,1,2,3,4,4,4-八氟丁烷（即CFC-318mbb）; 将C-318与CFC-318mbb分离; 并使CFC-318mbb与HF反应。

6. 发明授权

US6107267A Compositions comprising CF.sub.3 CF.sub.2 CHF.sub.2 and their manufacture 失效
标题翻译：包含CF 3 CF 2 CHF 2的组合物及其制备
公开(公告)号：US6107267A
公开(公告)日：2000-08-22
申请号：US137342
申请日：1998-08-20
申请人： V. N. Mallikarjuna Rao , Allen Capron Sievert , Munirpallam A. Subramanian
发明人： V. N. Mallikarjuna Rao , Allen Capron Sievert , Munirpallam A. Subramanian
IPC分类号： B01D3/36 , C11D7/30 , C11D7/50
CPC分类号： C11D7/5036 , B01D3/36 , C11D7/30
摘要： A process is disclosed for recovering HF from a product mixture including HF and CF.sub.3 CF.sub.2 CHF.sub.2. The process involves (1) distilling the product mixture to remove all products which have a lower boiling point than the lowest boiling azeotrope containing HF and CF.sub.3 CF.sub.2 CHF.sub.2 ; and (2) distilling the azeotrope to recover HF as an azeotropic composition containing HF and CF.sub.3 CF.sub.2 CHF.sub.2. Also disclosed are compositions of hydrogen fluoride in combination with an effective amount of CF.sub.3 CF.sub.2 CHF.sub.2 to form an azeotrope or azeotrope-like composition with hydrogen fluoride, (e.g., compositions containing from about 57.1 to 67.2 mole percent CF.sub.3 CF.sub.2 CHF.sub.2).A process for producing certain compositions comprising(a) CF.sub.3 CF.sub.2 CHF.sub.2 and (b) at least one saturated halogenated hydrocarbon and/or ether having the formula:C.sub.n H.sub.2n+2-a-b Cl.sub.a F.sub.b O.sub.cwherein n is an integer from 1 to 4, a is an integer from 0 to 2n+1, b is an integer from 1 to 2n+2-a, and c is 0 or 1, provided that when c is 1 then n is an integer from 2 to 4 (and provided that component (b) does not include CF.sub.3 CF.sub.2 CF.sub.2) is also disclosed. This process involves (A) combining (i) an azeotropic composition of CF.sub.3 CF.sub.2 CHF.sub.2 and HF with (ii) at least one fluorination precursor compound wherein the precursor component (ii) is the fluorination precursor to component (b); and (B) reacting a sufficient amount of the HF from the azeotropic composition (i) with precursor component (ii), to provide a composition containing components (a) and (b) in the desired ratio. In addition, certain compositions are disclosed which include (a) CF.sub.3 CF.sub.2 CHF.sub.2 and (b) at least two saturated halogenated hydrocarbons and/or ethers having the formula:C.sub.n H.sub.2n+2-a-b Cl.sub.a F.sub.b O.sub.cwherein the molar ratio of said at least one compound to HFC-227ca is between about 1:99 and about 43:57 and c is 1 for at least one of the component (b) compounds.
摘要翻译：公开了从包含HF和CF 3 CF 2 CHF 2的产物混合物中回收HF的方法。该方法包括（1）蒸馏产物混合物以除去所有具有比含有HF和CF 3 CF 2 CHF 2的最低沸点共沸物沸点低的产物; 和（2）蒸馏共沸物以回收HF作为含有HF和CF 3 CF 2 CHF 2的共沸组合物。还公开了氟化氢与有效量的CF 3 CF 2 CHF 2组合以与氟化氢形成共沸物或类共沸组合物的组合物（例如，含有约57.1至67.2摩尔％CF 3 CF 2 CHF 2的组合物）。一种制备某些组合物的方法，其包含（a）CF 3 CF 2 CHF 2和（b）至少一种具有下式的饱和卤代烃和/或醚：n为1至4的整数，a为从 0〜2n + 1，b为1〜2n + 2-a的整数，c为0或1，条件是当c为1时，n为2〜4的整数（（b）成分也不包括CF 3 CF 2 CF 2）。该方法包括：（i）将CF 3 CF 2 CHF 2和HF的共沸组合物与（ii）至少一种氟化前体化合物组合（其中前体组分（ii）是组分（b）的氟化前体）; 和（B）使足够量的来自共沸组合物（i）的HF与前体组分（ii）反应，从而以所需的比例提供含有组分（a）和（b）的组合物。此外，公开了某些组合物，其包括（a）CF 3 CF 2 CHF 2和（b）至少两种具有下式的饱和卤代烃和/或醚：CnH2n + 2-a-bClaFbOc，其中所述至少一种化合物与HFC- 对于至少一种组分（b）化合物，227ca为约1:99至约43:57，c为1。

7. 发明授权

US06683226B2 Process for the production of hexafluoropropylene from CClF2CClFCF3 and azeotropes of CClF2CClFCF3 with HF 失效
标题翻译：从CClF2CClFCF3生产六氟丙烯的方法和与HF的CClF2CClFCF3的共沸物
公开(公告)号：US06683226B2
公开(公告)日：2004-01-27
申请号：US10367317
申请日：2003-02-14
申请人： Allen Capron Sievert , V. N. Mallikarjuna Rao
发明人： Allen Capron Sievert , V. N. Mallikarjuna Rao
IPC分类号： C07C1723
CPC分类号： C07C21/18 , C07C17/00 , C07C17/206 , C07C17/23 , C07C19/10 , Y02P20/582
摘要： A process for the manufacture of CF3CF═CF2 is disclosed. The process involves contacting 2,3-dichloro-1,1,1,2,3,3-hexafluoropropane with at least 0.1 mole of hydrogen in a reaction vessel of titanium, nickel or iron or their alloys, which is either empty or packed with particles or formed shapes of titanium, nickel or iron or their alloys, at a temperature within the range of from about 350° C. to about 600° C. and for a time sufficient to produce hexafluoropropene. Also disclosed are compositions which comprise hydrogen fluoride in combination with an effective amount of CClF2CClFCF3 to form an azeotrope or azeotrope-like composition with hydrogen fluoride. The compositions contain from about 8.7 to 33.6 mole percent CClF2CClFCF3.
摘要翻译：公开了制备CF 3 CF = CF 2的方法。该方法包括在钛，镍或铁或其合金的反应容器中将2,3-二氯-1,1,1,2,3,3-六氟丙烷与至少0.1摩尔的氢气接触，其为空或包装具有钛，镍或铁或其合金的颗粒或形成形状，在约350℃至约600℃的温度下，并持续足以产生六氟丙烯的时间。还公开了包含氟化氢与有效量的CClF 2 CClFCF 3组合以与氟化氢形成共沸物或类共沸组合物的组合物。组合物含有约8.7至33.6摩尔％CClF 2 CClFCF 3。

8. 发明授权

US6093859A Process for the manufacture of 1,1,1,3,3-pentafluoropropane 失效
标题翻译：制备1,1,1,3,3-五氟丙烷的方法
公开(公告)号：US6093859A
公开(公告)日：2000-07-25
申请号：US323736
申请日：1999-06-01
申请人： Mario Joseph Nappa , V. N. Mallikarjuna Rao , Allen Capron Sievert
发明人： Mario Joseph Nappa , V. N. Mallikarjuna Rao , Allen Capron Sievert
IPC分类号： B01J27/06 , B01J21/10 , B01J23/06 , B01J23/26 , B01J27/10 , B01J27/12 , B01J27/125 , B01J27/132 , B01J27/138 , C07B61/00 , C07C17/25 , C07C17/354 , C07C17/383 , C07C19/08
CPC分类号： C07C19/08 , B01J27/10 , B01J27/12 , C07C17/25 , C07C17/354 , C07C17/383 , B01J21/10 , B01J23/06 , B01J23/26 , B01J27/125 , B01J27/132 , B01J27/138
摘要： A process is disclosed for producing the hydrofluorocarbon CF.sub.3 CH.dbd.CF.sub.2. The process involves dehydrofluorinating CF.sub.3 CH.sub.2 CF.sub.3 at an elevated temperature in the vapor phase over a catalyst of (1) aluminum fluoride, (2) fluorided alumina, (3) metal supported on a trivalent aluminum compound containing fluoride anion, (4) lanthanum fluoride, (5) fluorided lanthanum oxide, (6) metal supported on a trivalent lanthanum compound containing fluoride anion, (7) trivalent chromium compounds and/or (8) catalysts of (a) at least one compound selected from the oxides, fluorides and oxyfluorides of magnesium, zinc and mixtures of magnesium and zinc, and optionally (b) at least one compound selected from the oxides, fluorides and oxyfluorides of aluminum, provided that the atomic ratio of aluminum to the total of magnesium and zinc in said catalyst is about 1:4, or less, to produce a product containing CF.sub.3 CH.dbd.CF.sub.2 and HF. The CF.sub.3 CH.dbd.CF.sub.2 may then be reacted in the vapor phase with hydrogen over a hydrogenation catalyst in the presence of HF to produce CF.sub.3 CH.sub.2 CHF.sub.2.
摘要翻译：公开了一种生产氢氟烃CF 3 CH = CF 2的方法。该方法包括在（1）氟化铝，（2）氟化氧化铝，（3）负载在含氟化物阴离子的三价铝化合物上的金属，（4）氟化镧（（ⅰ））的催化剂上，在气相中升高的温度下，将CF 3 CH 2 CF 3脱氟化氢 5）氟化镧氧化物，（6）负载在含氟化物阴离子的三价镧化合物上的金属，（7）三价铬化合物和/或（a）至少一种选自氧化物，氟化物和氟氧化物的化合物的催化剂镁，锌和镁和锌的混合物，以及任选地（b）至少一种选自铝的氧化物，氟化物和氟氧化物的化合物，条件是铝与所述催化剂中镁和锌的原子比为约1 ：4或更少，以产生含有CF 3 CH = CF 2和HF的产物。然后在HF存在下，CF 3 CH = CF 2可以在气相中与氢气在氢化催化剂上反应生成CF 3 CH 2 CHF 2。

9. 发明授权

US5945573A Process for the manufacture of 1,1,1,3,3-pentafluoropropane 失效
标题翻译：制备1,1,1,3,3-五氟丙烷的方法
公开(公告)号：US5945573A
公开(公告)日：1999-08-31
申请号：US5400
申请日：1998-01-09
申请人： Mario Joseph Nappa , V. N. Mallikarjuna Rao , Allen Capron Sievert
发明人： Mario Joseph Nappa , V. N. Mallikarjuna Rao , Allen Capron Sievert
IPC分类号： B01J27/06 , B01J21/10 , B01J23/06 , B01J23/26 , B01J27/10 , B01J27/12 , B01J27/125 , B01J27/132 , B01J27/138 , C07B61/00 , C07C17/25 , C07C17/354 , C07C17/383 , C07C19/08 , C07C17/34
CPC分类号： C07C19/08 , B01J27/10 , B01J27/12 , C07C17/25 , C07C17/354 , C07C17/383 , B01J21/10 , B01J23/06 , B01J23/26 , B01J27/125 , B01J27/132 , B01J27/138
摘要： A process is disclosed for producing the hydrofluorocarbon CF.sub.3 CH.sub.2 CHF.sub.2. The process involves dehydrofluorinating CF.sub.3 CH.sub.2 CF.sub.3 at an elevated temperature in the vapor phase over a catalyst of (1) aluminum fluoride, (2) fluorided alumina, (3) metal supported on a trivalent aluminum compound containing fluoride anion, (4) lanthanum fluoride, (5) fluorided lanthanum oxide, (6) metal supported on a trivalent lanthanum compound containing fluoride anion, (7) trivalent chromium compounds and/or (8) catalysts of (a) at least one compound selected from the oxides, fluorides and oxyfluorides of magnesium, zinc and mixtures of magnesium and zinc, and optionally (b) at least one compound selected from the oxides, fluorides and oxyfluorides of aluminum, provided that the atomic ratio of aluminum to the total of magnesium and zinc in said catalyst is about 1:4, or less, to produce a product containing CF.sub.3 CH.dbd.CF.sub.2 and HF; and reacting the CF.sub.3 CH.dbd.CF.sub.2 in the vapor phase with hydrogen over a hydrogenation catalyst in the presence of HF to produce CF.sub.3 CH.sub.2 CHF.sub.2.
摘要翻译：公开了用于生产氢氟烃CF 3 CH 2 CHF 2的方法。该方法包括在（1）氟化铝，（2）氟化氧化铝，（3）负载在含氟化物阴离子的三价铝化合物上的金属，（4）氟化镧（（ⅰ））的催化剂上，在气相中升高的温度下将CF 3 CH 2 CF 3脱氟化氢 5）氟化镧氧化物，（6）负载在含氟化物阴离子的三价镧化合物上的金属，（7）三价铬化合物和/或（a）至少一种选自氧化物，氟化物和氟氧化物的化合物的催化剂镁，锌和镁和锌的混合物，以及任选地（b）至少一种选自铝的氧化物，氟化物和氟氧化物的化合物，条件是铝与所述催化剂中镁和锌的原子比为约1 ：4或更少，以产生含有CF 3 CH = CF 2和HF的产物; 并在氢气存在下使氢气中的CF 3 CH = CF 2与氢气反应，生成CF 3 CH 2 CHF 2。

10. 发明授权

US06281395B1 1,1,1,2,3,3,3-heptafluoropropane manufacturing process 有权
标题翻译： 1,1,1,2,3,3,3-七氟丙烷制造方法
公开(公告)号：US06281395B1
公开(公告)日：2001-08-28
申请号：US09283451
申请日：1999-04-01
申请人： Mario Joseph Nappa , V. N. Mallikarjuna Rao , Allen Capron Sievert
发明人： Mario Joseph Nappa , V. N. Mallikarjuna Rao , Allen Capron Sievert
IPC分类号： C07C1708
CPC分类号： C07C17/087 , B01J23/26 , C07C17/21 , C07C19/08 , C07C21/18
摘要： A process is disclosed for the manufacture of CF3CHFCF3 containing less than 0.01 ppm (CF3)2C═CF2. The process involves (a) contacting hexafluoropropene in the vapor phase at a temperature of less than about 260° C. with hydrogen fluoride in the presence of a selected fluorination catalyst or produce a product containing less than 10 parts (CF3)2C═CF2 per million parts of CF3CHFCF3; and (b) treating the product of (a) as necessary to remove excess (CF3)2C═CF2. Suitable catalysts include: (i) an activated carbon treated to contain from about 0.1 to about 10 weight % added alkali or alkaline earth metals, (ii) three dimensional matrix porous carbonaceous materials, (iii) supported metal catalysts comprising trivalent chromium, and (iv) unsupported chrome oxide prepared by the pyrolysis of (NH4)2Cr2O7.
摘要翻译：公开了用于制造含有小于0.01ppm（CF 3）2 C = CF 2的CF 3 CHFCF 3的方法。该方法包括（a）在选择的氟化催化剂存在下，在小于约260℃的温度下，使氟化氢在气相中接触六氟丙烯，或者产生含有小于10份（CF 3）2 C = CF 2的产物百万份CF3CHFCF3; 和（b）根据需要处理（a）的产物以除去过量（CF 3）2 C = CF 2。合适的催化剂包括：（i）经处理以包含约0.1至约10重量％的加入的碱金属或碱土金属的活性炭，（ii）三维基体多孔碳质材料，（iii）包含三价铬的载体金属催化剂和（ iv）通过（NH 4）2 Cl 2 O 7的热解制备的无载体的氧化铬。

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