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Применить Всего найдено 26559. Отображено 100.
20-08-2008 дата публикации

СИСТЕМА ПРИГОТОВЛЕНИЯ ГУМИНОВЫХ И ФУЛЬВОКИСЛОТ

Номер: RU0000075656U1
Автор: Жеребцов Сергей Игоревич, Мандров Герман Александрович, Потапов Вадим Петрович, Счастливцев Евгений Леонидович
Принадлежит: Институт угля и углехимии Сибирского отделения Российской академии наук (ИУУ СО РАН)

Система приготовления гуминовых и фульвокислот, отличающаяся тем, что, с целью повышения выхода целевых продуктов, применяется малоотходная замкнутая технология, в которой в качестве химического реактора используется виброцентробежная мельница ЦЭМ-7, снабженная центробежным насосом, установленным на подающей линии мельницы для многократного прокачивания угольной суспензии через мельницу, а конечные целевые продукты выделяются в форме гидрогелей гуминовых кислот и технической пасты фульвокислот, позволяющих отделять остаточный бурый уголь и регенерированную соляную кислоту с целью возврата их в технологический цикл на повторную переработку. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) 75 656 (13) U1 (51) МПК C07C 63/00 C07C 17/00 (2006.01) (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ, ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ (21), (22) Заявка: 2008113149/22 , 04.04.2008 (24) Дата начала отсчета срока действия патента: 04.04.2008 (45) Опубликовано: 20.08.2008 (73) Патентообладатель(и): Институт угля и углехимии Сибирского отделения Российской академии наук (ИУУ СО РАН) (RU) U 1 7 5 6 5 6 R U Ñòðàíèöà: 1 U 1 Формула полезной модели Система приготовления гуминовых и фульвокислот, отличающаяся тем, что, с целью повышения выхода целевых продуктов, применяется малоотходная замкнутая технология, в которой в качестве химического реактора используется виброцентробежная мельница ЦЭМ-7, снабженная центробежным насосом, установленным на подающей линии мельницы для многократного прокачивания угольной суспензии через мельницу, а конечные целевые продукты выделяются в форме гидрогелей гуминовых кислот и технической пасты фульвокислот, позволяющих отделять остаточный бурый уголь и регенерированную соляную кислоту с целью возврата их в технологический цикл на повторную переработку. 7 5 6 5 6 (54) СИСТЕМА ПРИГОТОВЛЕНИЯ ГУМИНОВЫХ И ФУЛЬВОКИСЛОТ R U Адрес для переписки: 650099, г.Кемерово, пр-кт Советский, 61, а/я 19, Г.А. Мандрову (72) Автор(ы): Потапов ...

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Номер записи: 1
15-07-2021 дата публикации

Устройство для получения мелкодисперсного порошка

Номер: RU0000205452U1
Автор: Владимир Павлович Умнов, Дмитрий Олегович Чухланцев
Принадлежит: Общество С Ограниченной Ответственностью "Новые Дисперсные Материалы"

Полезная модель относится к порошковой металлургии, в частности к оборудованию для плазменного получения металлических порошков. Устройство содержит катодный электрод 1 возбуждения дуги, анодный электрод 2, блок управления 8, электрически соединенные с упомянутым блоком управления 8 устройство 4 для подачи расходуемого материала 3 в зону плазменного распыления 5 и электрическую схему для возбуждения и питания электрической дуги. Устройство содержит измеритель 11 разности электрических потенциалов между расходуемым материалом 3 и катодным электродом 1 возбуждения дуги, выход которого соединен с упомянутым блоком управления, выполненным с возможностью управлять скоростью подачи расходуемого материала в зону плазменного распыления. Устройство обеспечивает повышение качества получаемого порошка. 3 ил. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 205 452 U1 (51) МПК B22F 9/14 (2006.01) B22F 1/00 (2006.01) B01J 19/08 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ (52) СПК B22F 9/14 (2020.08); B22F 1/00 (2020.08); B01J 19/08 (2020.08); B01J 19/088 (2020.08) (21)(22) Заявка: 2020118945, 09.06.2020 (24) Дата начала отсчета срока действия патента: (73) Патентообладатель(и): ОБЩЕСТВО С ОГРАНИЧЕННОЙ ОТВЕТСТВЕННОСТЬЮ "НОВЫЕ ДИСПЕРСНЫЕ МАТЕРИАЛЫ" (RU) Дата регистрации: 15.07.2021 (45) Опубликовано: 15.07.2021 Бюл. № 20 2 0 5 4 5 2 R U (54) Устройство для получения мелкодисперсного порошка (57) Реферат: Полезная модель относится к порошковой Устройство содержит измеритель 11 разности металлургии, в частности к оборудованию для электрических потенциалов между расходуемым плазменного получения металлических порошков. материалом 3 и катодным электродом 1 Устройство содержит катодный электрод 1 возбуждения дуги, выход которого соединен с возбуждения дуги, анодный электрод 2, блок упомянутым блоком управления, выполненным управления 8, электрически соединенные с с возможностью управлять скоростью подачи упомянутым блоком управления 8 ...

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Номер записи: 2
26-01-2012 дата публикации

Integrated process for the manufacture of fluorinated olefins

Номер: US20120022302A1
Автор: Haluk Kopkalli, Hsueh Sung Tung, Selma Bektesevic
Принадлежит: Honeywell International Inc

The instant invention relates, at least in part, to a method increasing the cost efficiency for dehydrohalogenation production of a fluorinated olefin by recovering and recycling spent dehydrohalogenation agent. In one aspect, the present invention relates to dehydrohalogenating a fluorinated alkane (e.g. pentafluoropropane and/or hexafluoropropane) in the presence of a dehydrohalogenating agent to produce a fluorinated olefin (e.g. tetrafluoropropenes and/or pentafluoropropenes). Removal of spent dehydrohalogenating agent from the reactor allows for facile separation of organic and dehydrohalogenating agent, the latter of which is recycled.

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Номер записи: 3
01-03-2012 дата публикации

Process of making a chlorinated hydrocarbon

Номер: US20120053374A1
Автор: Akihiro Saito, Dai Tsunoda, Jun Kawakami, Kikuo Yamamoto, Masayuki Moriwaki, Shunsuke Hosaka, Tadahiro Fukuju, Yasutaka Komatsu
Принадлежит: Tokuyama Corp

A process of making a chlorinated hydrocarbon through a thermal dehydrochlorination step in which an unsaturated compound represented by the following general formula (2) is obtained by thermally decomposing a saturated compound represented by the following general formula (1). CCl 3 —CCl 2-m H m —CCl 3-n H n   (1) CCl 2 ═CCl 2-m H m-1 —CCl 3-n H n   (2) (in the above formulas, m is 1 or 2, and n is an integer of 0 to 3.)

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Номер записи: 4
08-03-2012 дата публикации

Methods to produce 3,3,3-trifluoropropene

Номер: US20120059201A1
Автор: Daniel C. Merkel, Hsueh Sung Tung, Konstantin A. Pokrovski
Принадлежит: Honeywell International Inc

Disclosed is a process for the preparation of 3,3,3-trifluoropropene comprising the steps of; (1) fluorination of 240fa to form 245fa; (2) conversion of 245fa to a cis/trans mixture of 1234ze; (3) hydrogenation of the cis/trans mixture of 1234ze to form 254fb; and (4) dehydrofluorination of 254fb to produce 3,3,3-trifluoropropene. Alternatively or additionally, a second process for the preparation of the desired compound comprises the following steps; (1) fluorination of HCC-240fa to form HCFC-244fa; (2) conversion of 244fa to a cis/trans mixture of HFO-1234ze; (3) hydrogenation of the cis/trans mixture of 1234ze to form HFC-254fb; and (4) dehydrofluorination of 254fb to produce 3,3,3-trifluoropropene.

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Номер записи: 5
08-03-2012 дата публикации

Manufacturing process for iodinated aromatic compounds

Номер: US20120059203A1
Автор: Han Seok Kim, Il Hoon Cha, Jong In Lee, Yoon Seo Lee
Принадлежит: SK Chemicals Co Ltd

Disclosed is a method for preparing an iodinated aromatic compound. More specifically, disclosed is a method of preparing an iodinated aromatic compound by iodinating an aromatic compound in the presence of oxygen over a zeolite catalyst, in which the aromatic compound and a monoiodo analog of the aromatic compound, or a monoiodo aromatic compound, as raw materials, are allowed to react with iodine. In comparison with a method in which only the aromatic compound is used as a raw material without adding the monoiodo compound, the disclosed method can increase the productivity of diiodo compounds and the selectivity to a p-diiodo compound and, at the same time, suppress side reactions, thus lengthening the life span of the catalyst.

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Номер записи: 6
15-03-2012 дата публикации

Process for producing 2,3,3,3-tetrafluoropropene

Номер: US20120065437A1
Автор: Daniel C. Merkel, Haiyou Wang, Hsueh S. Tung, Konstantin A. Pokrovski
Принадлежит: Honeywell International Inc

The instant invention relates to a process and method for manufacturing 2,3,3,3-tetrafluoropropene by dehydrohalogenating a reactant stream of 2-chloro-1,1,1,2-tetrafluoropropane that is substantially free from impurities, particularly halogenated propanes, propenes, and propynes.

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Номер записи: 7
22-03-2012 дата публикации

Process For Preparing 3,3,3-Trifluoropropene

Номер: US20120071699A1
Автор: Andrew Paul Sharratt, Claire Mcguinness
Принадлежит: MEXICHEM AMANCO HOLDING SA DE CV

The invention provides a process for preparing 3,3,3-trifluoropropene (1243zf), the process comprising contacting a compound of formula CX 3 CH 2 CH 2 X or CX 3 CH═CH 2 , with hydrogen fluoride (HF) in the presence of a zinc/chromia catalyst, wherein each X independently is F, Cl, Br or I, provided that in the compound of formula CX 3 CH═CH 2 , at least one X is not F.

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Номер записи: 8
03-05-2012 дата публикации

Disubstituted-aminodifluorosulfinium salts, process for preparing same and method of use as deoxofluorination reagents

Номер: US20120108801A1
Автор: Alexandre L'heureux, Michel A. Couturier
Принадлежит: OMEGACHEM INC

The invention relates to disubstituted-aminodifluorosulfinium salts represented by the formula (I). Processes for preparing same and methods of use as deoxofluorinating reagent is also provided.

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Номер записи: 9
31-05-2012 дата публикации

Hydrogenation Process for Fluorocarbons

Номер: US20120134892A1
Автор: Gus Cerri, Haluk Kopkalli, Hsueh Sung Harry Tung, Orlando George Rodrigues, Stephen A. Cottrell, Yuon Chiu
Принадлежит: Honeywell International Inc

Disclosed is a process and apparatus for the catalytic hydrogenation of fluoro-olefins to fluorocarbons where the reaction is carried out in a multi-tube shell and tube reactor. Reactions involving hydrogenation of fluoro-olefins are typically exothermic. In commercial processes where a fluoro-olefin C n H 2n-x F x to C n H 2n-x2 F x is hydrogenated (e.g., hexafluoropropylene to 236ea, 1225ye to 245eb, and the like), inadequate management or control of heat removal may induce excess hydrogenation, decomposition and hot spots resulting in reduced yields and potential safety issues. In the hydrogenation of fluoro-olefins, it is therefore necessary to control the reaction temperature as precisely as practical to overcome challenges associated with heat management and safety.

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Номер записи: 10
28-06-2012 дата публикации

Compositions comprising 1,1,1,2,3-pentafluoropropane or 2,3,3,3- tetrafluoropropene

Номер: US20120165578A1
Автор: Barry Asher Mahler, Jeffrey P. Knapp, Mario Joseph Nappa
Принадлежит: EI Du Pont de Nemours and Co

Disclosed are compositions comprising HFC-245 eb and at least one additional compound selected from the group consisting of HFO-1234 ze , HFC-245 fa , HFC-236 cb , HFC-236 ea , HFC-236 fa , HFC-227 ea , HFC-227 ca , HFO-1225 yc , HFO-1225 zc , HFO-1225 ye , methane, ethane, propane, HFC-23, HFC-143 a , HFC-134, HFC-134 a , FC-1216, HFO-1234 yf , HFC-254 eb , HFO-1243 zf , and HFC-254 fb . Compositions comprising HFC-245 eb are useful in processes to make HFO-1234 yf . Also disclosed are compositions comprising HFO-1234 yf and at least one additional compound selected from the group consisting of HFO-1234 ze , HFC-254 eb , HFC-254 fb , HFO-1243 zf , HFCHFC-245 eb , HFC-245 fa , HFC-245 cb , HFC-236 cb , HFC-236 ea , HFC-236 fa , HFC-227 ea , HFC-227 ca , HFO-1225 yc , HFO-1225 zc , HFO-1225 ye , methane, ethane, propane, HFC-23, HFC-134, HFC-134 a , HFO-1132 a and FC-1216. Compositions comprising HFO-1234 yf are useful as heat transfer compositions for use in refrigeration, air-conditioning and heat pump systems.

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Номер записи: 11
26-07-2012 дата публикации

Process for separating hydrogen fluoride from organic feedstocks

Номер: US20120190901A1
Автор: Daniel C. Merkel, Hsueh Sung Tung, Konstantin A. Pokrovski
Принадлежит: Honeywell International Inc

Provided is a process for purifying an organic feedstock comprising (a) distilling a raw organic feedstock comprising hydrogen fluoride, 2-chloro-1,1,1,2-tetrafluoropropane, and 2-chloro-3,3,3-trifluoropropene to produce a first distillate stream comprising an azeotrope-like composition of 2-chloro-1,1,1,2-tetrafluoropropane, 2-chloro-3,3,3-trifluoropropene, and hydrogen fluoride, and a first bottoms stream rich in hydrogen fluoride; (b) cooling said first distillate stream to produce an intermediate composition comprising an organic layer rich in 2-chloro-1,1,1,2-tetrafluoropropane and 2-chloro-3,3,3-trifluoropropene, and an acid layer rich in hydrogen fluoride; and, optionally but preferably, (c) distilling said organic layer to produce a second distillate stream comprising an azeotrope-like composition of 2-chloro-1,1,1,2-tetrafluoropropane, 2-chloro-3,3,3-trifluoropropene, and hydrogen fluoride, and a second bottoms stream comprising a purified organic feedstock substantially free of hydrogen fluoride.

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Номер записи: 12
16-08-2012 дата публикации

Fluorinated aromatic materials and their use in optoelectronics

Номер: US20120208989A1
Автор: Haoran Sun
Принадлежит: University of South Dakota

Fluorinated aromatic materials, their synthesis and their use in optoelectronics. In some cases, the fluorinated aromatic materials are perfluoroalkylated aromatic materials that may include perfluoropolyether substituents.

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Номер записи: 13
25-10-2012 дата публикации

Purification of trans-1,3,3,3-tetrafluoropropene

Номер: US20120266750A1
Автор: Raymond Hilton Thomas, Stephen A. Cottrell
Принадлежит: Honeywell International Inc

Disclosed is a process for removing impurities from a product stream comprising trans HFO-1234ze and an HFO-1234 impurity that uses one or more adsorbents that are selective for the HFO-1234 impurity, such that the HFO-1234 impurity is removed from the product stream. One such impurity is HFO-1234zc, which is removed from its mixture with trans HFO-1234ze by action of an adsorbent having pores in the range of from about 5 angstroms to about 10 angstroms.

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Номер записи: 14
25-10-2012 дата публикации

Process for producing trans-1233zd

Номер: US20120271069A1
Автор: Haiyou Wang, Hsueh Sung Tung
Принадлежит: Honeywell International Inc

Trans-1233zd, the trans-isomer of 1-chloro-3,3,3-trifluoropropene (HCFO-1233zd) can be used as blowing agents, solvents, cleaning agents, as well as monomers of macromolecule compounds, and can be prepared through the dehydrochlorination of 1,1,1-trifluoro-3,3-dichloropropane (HCFC-243fa) with the help of a catalyst. The present invention is directed to an integrated process is proposed to produce trans-1233zd from 243fa, which is consisted of the following four major unit operations: (1) Catalytic dehydrochlorination of 243fa into trans/cis-1233zd, (2) HCl recovery, (3) Catalytic isomerization of cis-1233zd into trans-1233zzd, and (4) Isolation of trans-1233zd.

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Номер записи: 15
29-11-2012 дата публикации

Process for producing 2-chloro-3,3,3-trifluoropropene

Номер: US20120302803A1
Автор: Kenichi Katsukawa, Masatoshi Nose, Tsuneo Yamashita
Принадлежит: Daikin Industries Ltd

The present invention provides a process for producing 2-chloro-3,3,3-trifluoropropene represented by the chemical formula: CF 3 CCl═CH 2 , comprising mixing a fluorine-containing alkane, in a liquid state, represented by the formula: CF 3 CH—ClCH 2 X, wherein X is halogen, with an aqueous solution containing at least one metal hydroxide selected from the group consisting of alkali metal hydroxides and alkali earth metal hydroxides in the presence of a catalyst to perform a dehydrohalogenation reaction of the fluorine-containing alkane. According to the present invention, 2-chloro-3,3,3-trifluoropropene (HCFO-1233xf) can be obtained at a very high yield at a relatively low reaction temperature.

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Номер записи: 16
20-12-2012 дата публикации

Purification of cis-1,1,1,4,4,4-hexafluoro-2-butene via extractive distillation

Номер: US20120323054A1
Автор: Jeffrey P. Knapp
Принадлежит: EI Du Pont de Nemours and Co

A process for separating cis-1,1,1,4,4,4-hexafluoro-2-butene from a first mixture comprising cis-1,1,1,4,4,4-hexafluoro-2-butene and at least one chlorofluoroolefin is disclosed. The process involves the steps of contacting said first mixture with at least one extractive agent, to form a second mixture, distilling said second mixture; and recovering cis-1,1,1,4,4,4-hexafluoro-2-butene substantially free of chlorofluoroolefin.

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Номер записи: 17
27-12-2012 дата публикации

Method for producing substituted fluorine-containing olefin

Номер: US20120330072A1
Автор: Masato Ohashi, Sensuke Ogoshi, Takabumi Nagai, Takashi Shibanuma
Принадлежит: Daikin Industries Ltd, Osaka University NUC

This invention relates to a method of reacting fluoroolefin with an organic magnesium compound in the presence of a catalyst comprising nickel or palladium so as to efficiently produce fluoroolefin, such as TFE, in which a fluorine (F) atom or atoms bonded to the sp 2 hybridized carbon atom are substituted with an organic group.

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Номер записи: 18
03-01-2013 дата публикации

Method for producing fluorine-containing alkane

Номер: US20130006022A1
Автор: Kakeru Hanabusa, Kazuhiro Takahashi, Takehiro Chaki, Yuko Shiotani
Принадлежит: Daikin Industries Ltd

The present invention provides a method for producing a fluorine-containing alkane, which comprises reacting at least one fluorine-containing compound selected from the group consisting of chlorine-containing fluoroalkanes and fluorine-containing alkenes with hydrogen gas in the presence of catalysts, wherein two or more catalysts having different catalytic activities are used, and the fluorine-containing compound and hydrogen gas, which are starting materials, are sequentially brought into contact with the catalysts in the order of the catalyst having a lower catalytic activity followed by the catalyst having a higher catalytic activity. According to the present invention, in the method for producing a fluorine-containing alkane by using chlorine-containing fluoroalkane or fluorine-containing alkene as a starting material, and subjection it to a reduction reaction or a hydrogen addition reaction, the objective fluorine-containing alkane can be produced with high productivity.

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Номер записи: 19
07-03-2013 дата публикации

Dehydrofluorination of pentafluoroalkanes to form tetrafluoroolefins

Номер: US20130060069A1
Автор: Benjamin Bin Chen, Maher Y. Elsheikh, Olga C.N. Keeley, Philippe Bonnet
Принадлежит: Arkema Inc

A method for producing a tetrafluoroolefin, such as 2,3,3,3-tetrafluoropropene (HFO-123434), comprises dehydrofluorinating a pentafluoroalkane in a gas phase in the presence of a catalyst comprising chromium oxyfluoride. In a preferred embodiment, 2,3,3,3-tetrafluoropropene (HFO-1234yf) is produced by forming a catalyst comprising chromium oxyfluoride by calcining CrF3?xH2O, where x is 1-10, in the presence of a flowing gas comprising nitrogen to form a calcined chromium oxyfluoride, and dehydrofluorinating 1,1,1,2,2-pentafluoropropane (HFC-245cb) in a gas phase in the presence of the catalyst to form the 2,3,3,3-tetrafluoropropene (HFO-1234yf).

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Номер записи: 20
28-03-2013 дата публикации

PROCESS

Номер: US20130079562A1
Автор: McCarthy John Charles, Sharratt Andrew Paul
Принадлежит:

A process for isomerising a (hydrohalo)fluoroalkene, the process comprising contacting the (hydrohalo)fluoroalkene with a catalyst a catalyst which is a chromia-containing catalyst supported on AlFor fluorinated alumina. 1. A process for isomerising a (hydrohalo)fluoroalkene , the process comprising contacting the (hydrohalo)fluoroalkene with a catalyst which is a chromia-containing catalyst supported on AlFor fluorinated alumina.2. A process for isomerising a (hydrohalo)fluoroalkene , the process comprising contacting a E-(hydrohalo)fluoroalkene with a catalyst which is a chromia-containing catalyst supported on AlFor fluorinated alumina to convert the E-(hydrohalo)fluoroalkene to a Z-(hydrohalo)fluoroalkene a Z-(hydrohalo)fluoroalkene.3. A process according to claim 1 , wherein the isomerisation results in the changing of the ratio of the E and Z isomers.4. A process according to claim 3 , wherein the ratio of the Z isomer to the E isomer increases.5. A process according to claim 1 , wherein the isomerisation is carried out as an in situ step in the synthesis of the (hydrohalo)fluoroalkene.6. A process according to claim 5 , wherein the isomerisation results in a changing of the ratio of the E to Z isomer compared to what it would have been if the catalyst had not been utilized.7. A process according to claim 1 , wherein the ratio of E to Z isomers changes from that which is the kinetic equilibrium from the reaction preparing the (hydrohalo)fluoroalkene.8. A process according to claim 1 , wherein the chromia-containing catalyst contains an additional metal selected from zinc claim 1 , magnesium claim 1 , nickel claim 1 , cobalt claim 1 , silver claim 1 , copper claim 1 , aluminium claim 1 , tin claim 1 , zirconium claim 1 , and mixtures thereof claim 1 , and preferably comprises zinc.9. A process according to claim 1 , wherein the metal in the chromia-containing catalyst is present at a level of at least 0.01% by weight of the catalyst claim 1 , or wherein the ...

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Номер записи: 21
28-03-2013 дата публикации

PROCESS FOR CONVERTING GASEOUS ALKANES TO LIQUID HYDROCARBONS

Номер: US20130079564A1
Автор: Waycuilis John J.
Принадлежит: MARATHON GTF TECHNOLOGY, LTD.

Embodiments disclose a process for converting gaseous alkanes to higher molecular weight hydrocarbons, olefins or mixtures thereof wherein a gaseous feed containing alkanes may be reacted with a dry bromine vapor to form alkyl bromides and hydrobromic acid vapor. The mixture of alkyl bromides and hydrobromic acid then may be reacted over a synthetic crystalline alumino-silicate catalyst, such as a ZSM-5 or an X or Y type zeolite, at a temperature of from about 250° C. to about 500° C. so as to form hydrobromic acid vapor and higher molecular weight hydrocarbons, olefins or mixtures thereof. Various methods are disclosed to remove the hydrobromic acid vapor from the higher molecular weight hydrocarbons, olefins or mixtures thereof and to generate bromine from the hydrobromic acid for use in the process. 1. A process comprising:separating hydrobromic acid from a gaseous stream comprising hydrobromic acid and hydrocarbons;converting said hydrobromic acid to at least bromine; andcontacting said bromine with gaseous alkanes to form bromination products comprising alkyl bromides.2. The process of wherein said step of separating said hydrobromic acid from said hydrocarbons comprises:contacting said gaseous stream with water.3. The process of wherein said step of contacting said gaseous stream with said water comprises:neutralizing said hydrobromic acid to form an aqueous solution comprising said water and a metal bromide salt, the metal of said metal bromide salt being selected from Cu, Zn, Fe, Co, Ni, Mn, Ca or Mg bromide.4. The process of wherein said step of converting comprises:oxidizing said aqueous solution containing said metal bromide salt to form at least said bromine and a reaction product selected from the group consisting of a metal hydroxide, a metal oxy-bromide species and combinations thereof; andseparating said bromine from said reaction product5. The process of wherein said water that contacts said gaseous stream comprises said reaction product.6. The ...

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Номер записи: 22
04-04-2013 дата публикации

Synthesis of Alkyl Cyclopentadiene Compounds

Номер: US20130085289A1
Автор: Cao Xianyi, Harlan C. Jeff, Rix Francis C.
Принадлежит: UNIVATION TECHNOLOGIES, LLC

A method of synthesizing an alkyl cyclopentadiene compound is disclosed. The method includes contacting at least one cyclopentadienyl anion source and at least one alkyl group source to form at least one alkyl cyclopentadiene compound. The method further includes extracting the alkyl cyclopentadiene compound with a hydrocarbon solvent. The alkyl cyclopentadiene compound may be converted to a metallocene catalyst compound. 1. A method of synthesizing at least one alkyl cyclopentadiene compound comprising:contacting at least one cyclopentadienyl anion source and at least one alkyl group source to form at least one alkyl cyclopentadiene compound; andextracting the alkyl cyclopentadiene compound with a hydrocarbon solvent.2. The method of wherein the cyclopentadienyl anion source comprises at least one reagent selected from group consisting of a cyclopentadienyl Grignard reagent claim 1 , sodium cyclopentadienyl claim 1 , lithium cyclopentadienyl claim 1 , potassium cyclopentadienyl claim 1 , and any combination thereof.3. The method of or wherein the cyclopentadienyl anion source comprises a cyclopentadienyl Grignard reagent.4. The method of any preceding claim wherein the alkyl group source comprises at least one reagent selected from the group consisting of an alkyl halide and an alkyl sulfonate.5. The method of any preceding claim wherein a mole ratio of the alkyl group source to the cyclopentadienyl anion source is less than 1:1.6. The method of any preceding claim wherein a mole ratio of the alkyl group source to the cyclopentadienyl anion source is in the range of from 0.5:1 to 1:1.7. The method of any preceding claim wherein the alkyl cyclopentadiene compound comprises a Cto Calkyl group.8. The method of any preceding claim wherein the alkyl cyclopentadiene compound comprises an alkyl group substituted with one or more heteroatoms or one or more heteroatom-containing groups.9. The method of any preceding claim wherein the alkyl cyclopentadiene compound comprises ...

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Номер записи: 23
18-04-2013 дата публикации

LEAVING SUBSTITUENT-CONTAINING COMPOUND, ORGANIC SEMICONDUCTOR MATERIAL FORMED THEREFROM, ORGANIC ELECTRONIC DEVICE, ORGANIC THIN-FILM TRANSISTOR AND DISPLAY DEVICE USING THE ORGANIC SEMICONDUCTOR MATERIAL, METHOD FOR PRODUCING FILM-LIKE PRODUCT, PI-ELECTRON CONJUGATED COMPOUND AND METHOD FOR PRODUCING THE PI ELECTRON CONJUGATED COMPOUND

Номер: US20130095605A1
Автор: Goto Daisuke, Kato Takuji, Matsumoto Shinji, Mohri Masataka, Sagisaka Toshiya, Shinoda Masato, TANO Takanori, YAMAMOTO Satoshi, Yutani Keiichiro
Принадлежит: RICOH COMPANY, LTD.

A leaving substituent-containing compound represented by General Formula (I), wherein the leaving substituent-containing compound can be converted to a compound represented by General Formula (Ia) and a compound represented by General Formula (II), by applying energy to the leaving substituent-containing compound, in General Formulas (I), (Ia) and (II), X and Y each represent a hydrogen atom or a leaving substituent, where one of X and Y is the leaving substituent and the other is the hydrogen atom; Qto Qeach represent a hydrogen atom, a halogen atom or a monovalent organic group; Qand Qeach represent a hydrogen atom or a monovalent organic group other than the leaving substituent; and among the monovalent organic groups represented by Qto Q, adjacent monovalent organic groups may be linked together to form a ring. 2: The leaving substituent-comprising compound according to claim 1 , wherein the leaving substituent represented by X or Y is a substituted or unsubstituted ether group or acyloxy group comprising a carbon atom.3: The leaving substituent-comprising compound according to claim 1 , wherein in the General Formula (I) claim 1 , at least one pair selected from (Q claim 1 , Q) claim 1 , (Q claim 1 , Q) claim 1 , (Q claim 1 , Q) claim 1 , (Q claim 1 , Q) and (Q claim 1 , Q) forms a ring structure which optionally has a substituent claim 1 , and one pair optionally forms a ring structure with adjacent pair or pairs.4: The leaving substituent-comprising compound according to claim 1 , wherein in the General Formula (I) claim 1 , at least one pair selected from (Q claim 1 , Q) claim 1 , (Q claim 1 , Q) and (Q claim 1 , Q) forms a ring structure which optionally has a substituent.5: The leaving substituent-comprising compound according to claim 3 , wherein the ring structure is an aryl group or a heteroaryl group.614-. (canceled)16: The method according to claim 15 , wherein the leaving substituent represented by X or Y is a substituted or unsubstituted ether group ...

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Номер записи: 24
25-04-2013 дата публикации

PROCESSES FOR THE PRODUCTION OF FLUOROPROPANES AND HALOPROPENES AND AZEOTROPIC COMPOSITIONS OF 2-CHLORO-3,3,3-TRIFLUORO-1-PROPENE WITH HF AND OF 1,1,1,2,2-PENTAFLUOROPROPANE WITH HF

Номер: US20130102814A1
Автор: RAO VELLIYUR NOTT MALLIKARJUNA, SIEVERT ALLEN CAPRON
Принадлежит: E I DU PONT DE NEMOURS AND COMPANY

A process is disclosed for making CFCHCHF, CFCH═CHF and/or CFCH═CHCl. The process involves reacting at least one starting material selected from the group consisting of halopropanes of the formula CXCHClCHX, halopropenes of the formula CXCCl═CHand halopropenes of the formula CX═CClCHX, wherein each X is independently F or Cl, with HF in a reaction zone to produce a product mixture comprising HF, HCl, CFCHCHF, CFCH═CHF and CFCH═CHCl; and recovering the CFCHCHF, CFCH═CHF and/or CFCH═CHCl from the product mixture. Also disclosed is a process for making CFCFCHand/or CFCF═CH. The process involves reacting at least one starting material selected from the group consisting of halopropanes of the formula CXCHClCHX, halopropenes of the formula CXCCl═CHand halopropenes of the formula CX═CClCHX, wherein each X is independently F or Cl, with HF in a reaction zone to produce a product mixture comprising HF, HCl, CFCFCHand CFCF═CH; and recovering the CFCFCHand/or CFCF═CHfrom the product mixture. In each of the processes the molar ratio of HF to total amount of starting material fed to the reaction zone is at least stoichiometric. Also disclosed is an azeotropic composition comprising CFCCl═CH, and HF. Also disclosed is an azeotropic composition comprising CFCFCH, and HF. 1. A process for making at least one product compound selected from the group consisting of CFCHCHF , CFCH═CHF and CFCH═CHCl , comprising:{'sub': 3', '2', '3', '2', '2', '2', '3', '2', '2', '3', '3, 'reacting at least one starting material selected from the group consisting of halopropanes of the formula CXCHClCHX, halopropenes of the formula CXCCl═CH, and halopropenes of the formula CX═CClCHX, wherein each X is independently selected from the group consisting of F and Cl, with HF in a reaction zone, optionally in the presence of a fluorination catalyst, to produce a product mixture comprising HF, HCl, CFCHCHF, CFCH═CHF and CFCH═CHCl, wherein the molar ratio of HF to total amount of starting material fed to the ...

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Номер записи: 25
25-04-2013 дата публикации

Process

Номер: US20130102815A1
Автор: Andrew P. Sharratt, Claire Mcguiness, John W. Smith
Принадлежит: MEXICHEM AMANCO HOLDING SA DE CV

The invention provides a process for the preparation of 2,3,3,3-tetrafluoropropene (1234yf) comprising (a) contacting 1,1,1-trifluoro-2,3-difluoropropane (243db) with hydrogen fluoride (HF) in the presence of a zinc/chromia catalyst to produce a compound having the formula CF 3 CHFCH 2 X, wherein X is Cl or F, and (b) dehydrohalogenating the

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Номер записи: 26
25-04-2013 дата публикации

PROCESSES AND SYSTEMS FOR THE STAGED SYNTHESIS OF ALKYL BROMIDES

Номер: US20130102820A1
Автор: Turner William J., Waycuilis John J.
Принадлежит: MARATHON GTF TECHNOLOGY, LTD.

Processes and systems for synthesizing hydrocarbon products, such as high molecular weight hydrocarbons, olefins or mixtures thereof, from alkyl bromides wherein one or more streams of alkyl bromides may be reacted in sequential or concurrent stages at different temperatures. The catalyst used in the synthesis stages may be the same or different and at least in one instance is chosen to form hydrocarbon products having a significant C paraffin content. The stages may be conducted in one or more reactors and the catalyst may be deployed in fixed beds or fluidized beds. 1. A process comprising:providing alkyl bromides;reacting at least a first portion of the alkyl bromides in the presence of a first catalyst and at a first temperature sufficient to form a first hydrocarbon product containing at least hydrocarbons having at least 5 carbon atoms and having a substantial C6+ paraffin content; andreacting at least a second portion of the alkyl bromides in the presence of a second catalyst and at a second temperature sufficient to form a second hydrocarbon product containing at least hydrocarbons having at least 5 carbon atoms and having a substantial substituted aromatic content.2. The process of wherein the steps of reacting at least the first portion of the alkyl bromides and reacting at least the second portion of the alkyl bromides occurs concurrently.3. The process of wherein said first temperature is from about 150° C. to about 300° C.4. The process of wherein said first temperature is from about 225° C. to about 275° C.5. The process of wherein said second temperature is from about 300° C. to about 450° C.6. The process of wherein said second temperature is from about 350° C. to about 425° C.7. The process of wherein the step of reacting at least the first portion of the alkyl bromides and the step of reacting at least the second portion of the alkyl bromides are each performed at a pressure in the range of about 1 to about 100 bar.8. The process of further ...

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Номер записи: 27
02-05-2013 дата публикации

PURIFICATION METHOD OF 2,3,3,3-TETRAFLUOROPROPENE

Номер: US20130105296A1
Автор: Chaki Takehiro, Takahashi Kazuhiro
Принадлежит: DAIKIN INDUSTRIES, LTD.

This invention provides a method for purifying HFO-1234yf by removing HF from a mixture of HFO-1234yf and HF under simple and economically advantageous conditions. According to the present invention, this is a purification method for 2,3,3,3-tetrafluoropropene, (1) the purification method comprising the step of subjecting a mixture comprising 2,3,3,3-tetrafluoropropene and hydrogen fluoride to extractive distillation in a distillation column A using an extractant, thereby obtaining a fraction I that contains 2,3,3,3-tetrafluoropropene and has a lower ratio of hydrogen fluoride to 2,3,3,3-tetrafluoropropene than that of the mixture, while obtaining a fraction II that contains hydrogen fluoride and has a lower ratio of 2,3,3,3-tetrafluoropropene to hydrogen fluoride than that of the mixture; (2) the extractant comprising at least one member selected from the group consisting of: (i) alcohols represented by ROH, wherein R is a Calkyl group, (ii) ethers represented by ROR′, wherein R and R′ are the same or different, and each is a Calkyl group, (iii) fluorinated alcohols represented by RfOH, wherein Rf is a Cfluoroalkyl group, (iv) ketones represented by RCOR′, wherein R and R′ are the same or different, and each is a Calkyl group, (v) esters represented by RCOOR′, wherein R and R′ are the same or different, and each is a Calkyl group, (vi) polyols represented by R(OH)n, wherein R is a Calkyl group, and n is an integer of 2 to 3, and (vii) ethylene glycols represented by RO(CHCHO)R, wherein Rand Rare the same or different, and each is hydrogen or a Calkyl group, and n is an integer of 1 to 3. 1. A method for purifying 2 ,3 ,3 ,3-tetrafluoropropene ,(1) the purification method comprising the step of subjecting a mixture comprising 2,3,3,3-tetrafluoropropene and hydrogen fluoride to extractive distillation in a distillation column A using an extractant, thereby obtaining a fraction I that contains 2,3,3,3-tetrafluoropropene and has a lower ratio of hydrogen fluoride to 2, ...

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Номер записи: 28
09-05-2013 дата публикации

CATION-EXCHANGED ZEOLITE CATALYST AND PROCESS FOR PRODUCING MONO-IODO BENZENE THROUGH TRANSIODINATION BY USING IT

Номер: US20130116484A1
Автор: Cha Il-Hoon, Choi Won-Choon, Kim Han-Seok, Lim Jae-Bong, Min Da-Young, Park Yong-Ki, Yi Yong-Jin
Принадлежит: SK Chemicals Co., Ltd.

The present invention relates to a cation-exchanged zeolite catalyst for an transiodination and a process for producing mono-iodo benzene by using it. Particularly, the cation-exchanged zeolite catalyst has a molar ratio of Si/Al from 5 to 100 and is ion-exchanged with an alkali metal or an alkaline earth metal in range of 2% to 50% of ion exchange capacity. 1. A process for producing mono-iodo benzene from reactants containing multi-iodo benzene and benzene , comprising the step of performing a transiodination by using a cation-exchanged zeolite catalyst ,wherein the multi-iodo benzene is one or more selected from the group consisting of di-iodo benzene and tri-iodo benzene, andthe catalyst has a molar ratio of Si/Al from 5 to 100 and is ion-exchanged with an alkali metal or an alkaline earth metal in the range of 2% to 50% of ion exchange capacity.2. The process for producing mono-iodo benzene according to claim 1 , wherein the molar ratio of Si/Al is 5 to 15.3. The process for producing mono-iodo benzene according to claim 1 , wherein 20% to 50% of the ion exchange capacity is ion-exchanged with sodium (Na).4. The process for producing mono-iodo benzene according to claim 1 , wherein 10% to 50% of the ion exchange capacity is ion-exchanged with potassium (K).5. The process for producing mono-iodo benzene according to claim 1 , wherein the zeolite catalyst is any one selected from the group consisting of Y claim 1 , BEA claim 1 , and ZSM-5 zeolites.6. The process for producing mono-iodo benzene according to claim 1 , wherein the multi-iodo benzene includes one or more selected from the group consisting of m-di-iodo benzene claim 1 , o-di-iodo benzene claim 1 , and tri-iodo benzene.7. The process for producing mono-iodo benzene according to claim 1 , wherein a molar ratio of benzene/multi-iodo benzene in the reactants is 2:1 to 25:1.8. The process for producing mono-iodo benzene according to claim 1 , wherein the transiodination is carried out at the temperature of ...

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Номер записи: 29
16-05-2013 дата публикации

CAPTURE OF FLUORINATED VINYL MONOMERS USING IONIC LIQUIDS

Номер: US20130123448A1
Автор: NOELKE CHARLES JOSEPH, Shiflett Mark Brandon
Принадлежит: E I DU PONT DE NEMOURS AND COMPANY

A method for capturing certain fluorinated vinyl monomers from a gaseous mixture using ionic liquids is described. The gaseous mixture is contacted with at least one ionic liquid, whereby at least a portion of the fluorinated vinyl monomer is absorbed by the ionic liquid. The method is useful for reducing emissions of fluorinated vinyl monomers and for increasing the product yields in the manufacture of polymers from these monomers. 1. A method for capturing a fluorinated vinyl monomer from a gaseous mixture comprising the steps of:{'sub': 2', '3', '2', '2', '2', '2', '3', '3', '5', '3', '2', '4', '3', '3', '3', '3', '4', '2', '3', '5, 'a) providing a gaseous mixture comprising at least one fluorinated vinyl monomer selected from the group consisting of CHF, CHF, CHF, CHF, CHF, CHF, CHF, and CHF; and'}b) contacting the gaseous mixture with at least one ionic liquid, whereby at least a portion of the fluorinated vinyl monomer is absorbed by the ionic liquid;wherein said ionic liquid comprises an anion and a cation,3. The method according to wherein the anion is selected from one or more members of the group consisting of: [CHCO] claim 1 , [HSO] claim 1 , [CHOSO] claim 1 , [CHOSO] claim 1 , [AlCl] claim 1 , [CO] claim 1 , [HCO] claim 1 , [NO] claim 1 , [NO] claim 1 , [SO] claim 1 , [PO] claim 1 , [HPO] claim 1 , [HPO] claim 1 , [PO] claim 1 , [HPO] claim 1 , [HPO] claim 1 , [HSO] claim 1 , [CuCl] claim 1 , Cl claim 1 , Br claim 1 , I claim 1 , SCN claim 1 , and a fluorinated anion.4. The method according to wherein the fluorinated anion is selected from one or more members of the group consisting of 1 claim 3 ,1 claim 3 ,2 claim 3 ,2-tetrafluoroethanesulfonate; 2-chloro-1 claim 3 ,1 claim 3 ,2-trifluoroethanesulfonate; 1 claim 3 ,1 claim 3 ,2 claim 3 ,3 claim 3 ,3 claim 3 ,3-hexafluoropropanesulfonate; 1 claim 3 ,1 claim 3 ,2-trifluoro-2-(trifluoromethoxy)ethanesulfonate; 1 claim 3 ,1 claim 3 ,2-trifluoro-2-(pentafluoroethoxy)ethanesulfonate; 2-(1 claim 3 ,2 claim 3 , ...

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Номер записи: 30
23-05-2013 дата публикации

PROCESS FOR THE PREPARATION OF CHYMASE MODULATORS

Номер: US20130131401A1
Автор: Anzalone Luigi, Dorziotis Llias Konstantinos, Feibush Penina, Li Xun, Villani Frank J.
Принадлежит: Janssen Pharmaceutica, NV

The present invention is a process for the preparation of chymase modulators, useful in the treatment of inflammatory and serine protease mediated disorders. 2. A process as in claim 1 , wherein the compound of formula (II) is present in an excess of its corresponding trans isomer; wherein the brominating agent is 1-bromo-pyrrolidine-2 claim 1 ,5-dione; wherein the brominating agent is present in an amount of about 1.1 molar equivalents; wherein the catalyst is manganese acetate hydrate; wherein the catalyst is present in an amount of about 0.5 molar equivalents; wherein the organic solvent is acetonitrile; and wherein the compound of formula (II) is reacted with brominating agent at a temperature in the range of from about 25° C. to about 70° C. This application is a divisional of U.S. application Ser. No. 13/570,545, filed on Aug. 9, 2012, which is a divisional of nonprovisional U.S. application Ser. No. 12/608,585, filed on Oct. 29, 2009, now U.S. Pat. No. 8,263,785, issued on Sep. 11, 2012, which claims the benefit of U.S. Provisional Application No. 61/197,815, filed on Oct. 29, 2008, which are all incorporated by reference herein in their entirety.The present invention is a process for the preparation of chymase modulators, useful in the treatment of inflammatory and serine protease mediated disorders.The present invention is directed to a process for the preparation of compounds of formula (I)whereinis independently selected from the group consisting of aryl, heteroaryl, and benzo fused heterocyclyl; optionally substituted with Rand R;Ris one to three substituents independently selected from the group consisting of Calkyl, methoxy, Calkoxy, NH, NH(Calkyl), —N(C)dialkyl, aryl, heteroaryl, halogen, hydroxy, and nitro;wherein the Calkyl and Calkoxy substituents of Rare optionally substituted with a substituent independently selected from the group consisting of —NRR, aryl heteroaryl, one to three halogens and hydroxy; wherein Rand Rare substituents independently ...

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Номер записи: 31
23-05-2013 дата публикации

METHOD FOR PRODUCING FLUORINATED ORGANIC COMPOUNDS

Номер: US20130131403A1
Автор: DUBEY RAJESH K., MUKHOPADHYAY SUDIP, NAIR HARIDASAN K., SHIA GEORGE A., SINGH Rajiv R.
Принадлежит: HONEYWELL INTERNATIONAL INC.

Disclosed is a method for producing fluorinated organic compounds, including hydrofluoropropenes, which preferably comprises converting at least one compound of formula (I): 118.-. (canceled)19. A method of preparing fluorinated organic compounds comprising:{'sub': 2', '2', '3', '2, 'reacting CF═CFCl with CHFCl under conditions effective to produce a product composition comprising CFCClFCHCl.'}20. The method of wherein the reacting step is conducted in a gas phase.21. The method of wherein the reacting step is in the presence of a Ni-mesh catalyst.22. The method of wherein the product composition further comprises FClCCFCHCl.23. A method of preparing fluorinated organic compounds comprising: reacting CF═CFCl with CHFCl under conditions effective to produce CFClCFCHCl.24. The method of wherein the reacting step is conducted in a gas phase.25. The method of wherein the reacting step is in the presence of an AlClcatalyst.26. The method of wherein the product composition further comprises CFCClFCHCl. This application is claiming the priority benefit of U.S. Provisional Application Ser. No. 60/733,378 and is Continuation-in-Part of U.S. patent application Ser. No. 11/118,503, (pending) filed on Apr. 29, 2005, which in turn claims the priority benefit of U.S. Provisional Patent Application Nos. 60/567,427 and 60/567,425 filed Apr. 16, 2004.This application is also a Continuation-in-Part of U.S. patent application Ser. No. 11/118,504, (pending) filed on Apr. 29, 2005, which in turn claims the priority benefit of U.S. Provisional Patent Application Nos. 60/567,426 and 60/567,429 filed Apr. 16, 2004.This application is also a Continuation-in-Part of U.S. patent application Ser. No. 11/118,530, (pending) filed on Apr. 29, 2005, which in turn claims the priority benefit of U.S. Provisional Patent Application No. 60/567,428.The disclosures of each of the above-mentioned applications are incorporated herein by reference. Also incorporated herein by reference are the following U. ...

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Номер записи: 32
06-06-2013 дата публикации

METHOD OF PRODUCING IODIZING AGENT, AND METHOD OF PRODUCING AROMATIC IODINE COMPOUND

Номер: US20130144071A1
Автор: Hagiwara Yuji, KATAOKA Kazuhide, MIDORIKAWA Koji, SUGA Seiji, YOSHIDA Junichi
Принадлежит:

A method of the present invention, for producing an iodizing agent, includes the step of electrolyzing iodine molecules in a solution by using an acid as a supporting electrolyte. This realizes (i) a method of producing an iodine cation suitable for use as an iodizing agent that does not require a sophisticated separation operation after iodizing reaction is completed, and (ii) an electrolyte used in the method. Further, a method of the present invention, for producing an aromatic iodine compound, includes the step of causing an iodizing agent, and an aromatic compound whose nucleus has one or more substituent groups and two or more hydrogen atoms, to react with each other under the presence of a certain ether compound. This realizes such a method of producing an aromatic iodine compound that position selectivity in iodizing reaction of an aromatic compound is improved. 17-. (canceled)9. The method of producing an aromatic iodine compound claim 8 , according to claim 8 , wherein:{'sub': '3-12', 'the cyclic ether compound contains a Cring.'}10. The method of producing an aromatic iodine compound claim 8 , according to claim 8 , wherein:the iodizing agent is an iodine cation.11. The method of producing an aromatic iodine compound claim 8 , according to claim 8 , further comprising the steps of:separating a solid reaction product from a reaction solution obtained in the step (a); andrecrystallizing the reaction product thus separated from the reaction solution.12. The method of producing an aromatic iodine compound claim 8 , according to claim 8 , further comprising the step of isolating a reaction product by carrying out distillation process with respect to a reaction solution obtained in the step (a).13. (canceled) This application is a divisional of U.S. patent application Ser. No. 12/530,274 filed on Sep. 8, 2009, which is a 371 of PCT/JP2008/054184 filed on Mar. 7, 2008 and claims priority to Japanese Application No. 2007-061067 filed on Mar. 9, 2007 and Japanese ...

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Номер записи: 33
13-06-2013 дата публикации

Process for cis-1-chloro-3,3,3-trifluoropropene

Номер: US20130150632A1
Автор: Andrew Joseph Poss, Michael Van Der Puy, Rajiv Ratna Singh, Yian Zhai
Принадлежит: Honeywell International Inc

Disclosed is a process for the preparation of cis-1-chloro-3,3,3-trifluoropropene (cis-1233zd) comprising the steps of (a) providing CF 3 CHClCHCl 2 (233da), and (b) treating the 233da with a dechlorinating agent to produce a mixture of compounds including cis-1-chloro-3,3,3-trifluoropropene, preferably wherein the amount of the cis-isomer generated in the reaction is not less than 30%.

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Номер записи: 34
13-06-2013 дата публикации

PROCESS FOR MAKING CIS-1-CHLORO-3,3,3-TRIFLUOROPROPENE

Номер: US20130150633A1
Автор: Poss Andrew Joseph, Singh Rajiv Ratna, Zhai Yian
Принадлежит: HONEYWELL INTERNATIONAL INC.

Disclosed is a process for making cis-1-chloro-3,3,3-trifluoropropene comprising reacting 3,3,3-trifluoropropyne with HCl in a reaction vessel at a yield of at least about 80%. 1. A process for making cis-1-chloro-3 ,3 ,3-trifluoropropene comprising reacting 3 ,3 ,3-trifluoropropyne with HCl in a reaction vessel at a yield of at least about 80%.2. The process of claim 1 , wherein a solvent is used in the reaction vessel.3. The process of claim 2 , wherein the solvent comprises an ionic solvent.4. The process of claim 3 , wherein the ionic solvent comprises one or more solvents with ammonium ions.5. The process of claim 4 , wherein the ionic solvent is selected from the group consisting of salts of 1-alkyl-3-methylimidazolium claim 4 , 1-alkylpyridinium claim 4 , and N-methyl-N-alkylpyrrolidinium claim 4 , and mixtures thereof.6. The process of claim 4 , wherein the ionic solvent comprises 1-butyl-3-methylimidazolium chloride claim 4 ,7. The process of claim 1 , wherein a catalyst is used in the reaction vessel.8. The process of claim 7 , wherein the catalyst is on a support.9. The process of claim 8 , wherein the catalyst support comprises activated carbon.10. The process of claim 7 , wherein the catalysts comprises one or more mineral acids.11. The process of claim 10 , wherein the mineral acid comprises HSO.12. The process of claim 7 , wherein the catalyst comprises a Lewis acid or a mixture of Lewis acids.13. The process of claim 12 , wherein the Lewis acids comprises metal salts or mixtures thereof.14. The process of claim 13 , wherein the metal salts are selected from the group consisting of copper and antimony and mixtures thereof.15. The process of claim 13 , wherein the Lewis acids are selected from the group consisting of CuCl claim 13 , CuCl claim 13 , SbCl claim 13 , ZnCl claim 13 , MgCl claim 13 , AlCl claim 13 , FeCl claim 13 , and the like (MCl).16. The process of claim 13 , wherein the Lewis acid comprises CuCl.17. The process of claim 16 , wherein ...

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Номер записи: 35
13-06-2013 дата публикации

PROCESS FOR 1,1,2-TRICHLORO-3,3,3-TRIFLUOROPROPANE

Номер: US20130150634A1
Автор: Poss Andrew Joseph, Singh Rajiv Ratna, Zhai Yian
Принадлежит: HONEYWELL INTERNATIONAL INC.

Disclosed is a process for making the compound 1,1,2-trichloro-3,3,3-trifluoro-propane (233da) by the catalytic fluorination of 1,1,1,2,3,3-hexachloropropane. 233da is a starting material used in the production cis-1-chloro-3,3,3-trifluoropropene (cis-1233zd). 1. A process for making the compound 1 ,1 ,2-trichloro-3 ,3 ,3-trifluoropropane (233da) from 1 ,1 ,1 ,2 ,3 ,3-hexachloropropane comprising the steps:(a) fluorinating a metal catalyst; and(b) fluorinating 1,1,1,2,3,3-hexachloropropane in the presence of the fluorinated metal catalyst, to produce a reaction mixture containing 1,1,2-trichloro-3,3,3-trifluoropropane.2. The process of claim 1 , wherein the metal catalyst is selected from the group consisting of SbCl claim 1 , TiCl claim 1 , SnCl claim 1 , TaCl claim 1 , and NbCl.3. The process of claim 2 , wherein the catalyst comprises SbCl.4. The process of claim 3 , wherein the fluorination of the catalyst is conducted at a temperature of about 90° C. for about two hours.5. The process of claim 4 , wherein the fluorination of the hexachloropropane is conducted at a temperature of about 100° C. for about 15 hours.6. The process of claim 3 , wherein the fluorination of the catalyst is conducted at a temperature of about 70° C. for about two hours.7. The process of claim 6 , wherein the fluorination of the hexachloropropane is conducted at a temperature of about 100° C. for about 20 hours.8. The process of claim 2 , wherein the catalyst comprises TaCl.9. The process of claim 8 , wherein the fluorination of the catalyst is conducted at a temperature of about 90° C. for about two hours.10. The process of claim 9 , wherein the fluorination of the hexachloropropane is conducted at a temperature of about 90° C. for about six hours.11. A process for making the compound 1 claim 9 ,1 claim 9 ,2-trichloro-3 claim 9 ,3 claim 9 ,3-trifluoropropane (233da) from trans-1-chloro-3 claim 9 ,3 claim 9 ,3-trifluoropropene (trans-1233zd) comprising reacting chlorine gas with trans- ...

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Номер записи: 36
20-06-2013 дата публикации

METHOD FOR PRODUCING A FLUOROCOMPOUND

Номер: US20130158304A1
Автор: Mizukado Junji, Quan Heng-dao, Sekiya Akira, Tamura Masanori
Принадлежит:

An object is to provide a method for producing 1,1,1,4,4,4-hexafluoro-2-butene with high efficiency, which is suitable for a flow reaction, and cis-1,1,1,4,4,4-hexafluoro-2-butene can be efficiently obtained when isomerization of hexafluoro-1,3-butadiene is conducted using a catalyst and the resultant mixture is successively subjected to catalytic hydrogenation to produce cis-1,1,1,4,4,4-hexafluoro-2-butene, wherein the whole process is performed by a flow catalytic reaction. 1. A method for producing cis-1 ,1 ,1 ,4 ,4 ,4-hexafluoro-2-butene from hexafluoro-1 ,3-butadiene , wherein cis-1 ,1 ,1 ,4 ,4 ,4-hexafluoro-2-butene is produced through hexafluoro-2-butyne by a flow catalytic reaction.2. The method according to claim 1 , which has the first step of conducting isomerization of hexafluoro-1 claim 1 ,3-butadiene by a catalytic reaction to obtain hexafluoro-2-butyne.3. The method according to claim 2 , wherein the catalyst used in the first step is halogenated alumina.4. The method according to claim 3 , wherein the catalyst is obtained by reacting chlorofluorocarbon (CFCs) claim 3 , hydrochlorofluorocarbon (HCFCs) claim 3 , or hydrofluorocarbon (HFCs) with alumina at 20 to 600° C.5. The method according to claim 1 , wherein the reaction temperature in the first step is 20 to 400° C.6. The method according to claim 1 , which has the second step of obtaining cis-1 claim 1 ,1 claim 1 ,1 claim 1 ,4 claim 1 ,4 claim 1 ,4-hexafluoro-2-butene from hexafluoro-2-butyne by a catalytic hydrogenation reaction.7. The method according to claim 6 , wherein the catalyst used in the second step comprises at least one metal selected from palladium claim 6 , copper claim 6 , silver claim 6 , and bismuth and a carrier having the metal supported thereon.8. The method according to claim 7 , wherein the carrier is aluminum fluoride claim 7 , alumina claim 7 , or activated carbon.9. The method according to claim 6 , wherein the catalyst comprises a mixture of palladium and bismuth and ...

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Номер записи: 37
20-06-2013 дата публикации

METHOD FOR REMOVING MOISTURE FROM FLUORINE-CONTAINING COMPOUNDS

Номер: US20130158305A1
Автор: Takahashi Kazuhiro
Принадлежит: Daikin Industries Ltd.

The present invention provides a method for removing moisture from fluorine-containing compounds, the method comprising bringing a fluorine-containing compound contaminated with moisture into contact with an aqueous solution containing a metal salt. The method of the present invention can continuously and efficiently remove moisture from various fluorine-containing compounds, such as hydrofluoroolefins. In addition, the method produces less waste, etc., and is an industrially advantageous moisture removal method. 1. A method for removing moisture from fluorine-containing compounds , the method comprising bringing a fluorine-containing compound contaminated with moisture into contact with an aqueous solution containing a metal salt.2. The method according to claim 1 , wherein the fluorine-containing compound is at least one compound selected from the group consisting of hydrofluoroolefins claim 1 , hydrochlorocarbons claim 1 , hydrochlorofluorocarbons claim 1 , and hydrofluorocarbons.3. The method according to claim 2 , wherein the fluorine-containing compound is a hydrofluoroolefin.4. The method according to claim 3 , wherein the fluorine-containing compound is 2 claim 3 ,3 claim 3 ,3 claim 3 ,3-tetrafluoropropene.5. The method according to claim 1 , wherein the metal salt is at least one member selected from the group consisting of lithium chloride claim 1 , calcium chloride claim 1 , magnesium chloride claim 1 , and lithium bromide.6. The method according to claim 5 , wherein the metal salt is lithium chloride.7. The method according to claim 1 , wherein the aqueous solution containing a metal salt has a concentration of 20 to 50 wt. %.8. The method according to claim 1 , comprising the steps of reducing the moisture content of the metal salt-containing aqueous solution used in the method according to claim 1 , and then reusing the aqueous solution to remove the moisture from the fluorine-containing compound.9. A method for removing moisture from fluorine- ...

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Номер записи: 38
27-06-2013 дата публикации

METHOD FOR PRODUCING A CHLORINATED HYDROCARBON HAVING 3 CARBON ATOMS

Номер: US20130165705A1
Автор: Hosaka Shunsuke, Komatsu Yasutaka, Moriwaki Masayuki, OKADA Naoya, YAMAMOTO Kikuo
Принадлежит: TOKUYAMA CORPORATION

A method of producing a chlorinated hydrocarbon having 3 carbon atoms, comprising a conversion step for converting a chloropropane represented by the following formula (1) into a chloropropane represented by the following formula (2) by reacting it with chlorine in the presence of anhydrous aluminum chloride. 1. A method of producing a chlorinated hydrocarbon having 3 carbon atoms , comprising a conversion step for converting a chloropropane represented by the following formula (1) into a chloropropane represented by the following formula (2) by reacting it with chlorine in the presence of anhydrous aluminum chloride ,{'br': None, 'sub': 3', '(2-m)', 'm', '(3-n)', 'n, 'CCl—CClH—CClh\u2003\u2003(1),'}{'b': '1', 'claim-text': {'br': None, 'sub': 3', '(3-m)', '(m-1)', '(3-n)', 'n, 'CCl—CClH—CClH\u2003\u2003(2),'}, 'In the above formula (), m is 1 or 2, and n is an integer of 0 to 3,'}In the above formula (2), m and n are the same integers as in the formula (1), respectively.2. The method of producing a chlorinated hydrocarbon having 3 carbon atoms according to claim 1 , wherein the conversion step is carried out by putting at least the chloropropane represented by the above formula (1) and anhydrous aluminum chloride into a reactor and then supplying chlorine into the reactor.3. The method of producing a chlorinated hydrocarbon having 3 carbon atoms according to claim 2 , wherein the supply of chlorine into the reactor is started after anhydrous aluminum chloride is dissolved.4. The method of producing a chlorinated hydrocarbon having 3 carbon atoms according to claim 1 , wherein the conversion step is carried out by putting a solution containing at least anhydrous aluminum chloride and the chloropropane represented by the above formula (1) into a reactor and then supplying chlorine into the reactor.5. The method of producing a chlorinated hydrocarbon having 3 carbon atoms according to claim 4 , wherein the solution containing at least anhydrous aluminum chloride and ...

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Номер записи: 39
11-07-2013 дата публикации

PROCESS FOR PRODUCING DIOXOLANE

Номер: US20130178638A1
Автор: Mastroianni Sergio
Принадлежит: Rhodia Operations

A process is described for producing dioxolane from crude glycerol obtained from raw materials such as the crude glycerol obtained during production of biodiesel or glycerol obtained during conversion of fats or oils. Further, the described method can dissolve the glycerol in an organic solvent and form an insoluble phase including salts included in the crude glycerol, and then react the glycerol obtained with an aldehyde or a ketone. 1. A process for producing dioxolane , the process comprising the following steps:(a) bringing together crude glycerol and at least one organic solvent comprising from 1 carbon atom to 10 carbon atoms and comprising at least one of a ketone, an aldehyde, an alcohol, an acetal and/or a ketal function, so as to form a liquid phase comprising the-glycerol dissolved in the solvent(s) and to also form an insoluble phase;(b) separating the insoluble phase and the liquid phase;(c) optionally separating the solvent and the glycerol from the liquid phase;(d) adding to the liquid phase or to the glycerol (if step (c) is carried out) a catalyst, and optionally a ketone or an aldehyde, so as to form a dioxolane by catalyzed reaction between the glycerol and the ketone or the aldehyde; and(e) recovering the dioxolane.2. The process as defined by claim 1 , wherein the crude glycerol originates from a renewable raw material.3. The process as defined by claim 1 , wherein the crude glycerol is obtained during production of biodiesel or obtained during conversion of a fat or an oil.4. The process as defined by claim 1 , wherein the ketone is selected from the group consisting of an acetone claim 1 , a cyclohexanone claim 1 , a methylcylohexanone claim 1 , a cyclopentanone claim 1 , a methylcyclopentanone and a methyl isobutyl ketone.5. The method as defined by claim 1 , wherein the aldehyde is selected from the group consisting of a formaldehyde claim 1 , an acetaldehyde and a furfuraldehyde.6. The method as defined by claim 1 , wherein the alcohol is ...

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Номер записи: 40
11-07-2013 дата публикации

Vaporization of Liquid Halogen by Contact with a Preheated Gas

Номер: US20130178675A1
Автор: Gondolfe Joseph M., Kurukchi Sabah A., LIU Yijun, Moodley Anand, Waycuilis John J.
Принадлежит: MARATHON GTF TECHNOLOGY, LTD.

A method is provided for vaporizing a liquid elemental halogen. A heating gas is preheated in the absence of halogen to a preheat temperature which results in a preheated heating gas. The preheated heating gas is directly contacted with a feed of a liquid elemental halogen and heats the feed to a vaporizing temperature sufficient to vaporize at least a portion of the feed to a quantity of an elemental halogen vapor. A gas mixture results which includes the heating gas and the quantity of the elemental halogen vapor. 1. A process for vaporizing a liquid elemental halogen comprising:a) preheating a heating gas in the absence of halogen to a preheat temperature, thereby resulting in a preheated heating gas;b) directly contacting a feed of a liquid elemental halogen with said preheated heating gas; andc) heating said feed of said liquid elemental halogen with said preheated heating gas to a vaporizing temperature sufficient to vaporize at least a portion of said feed of said liquid elemental halogen to a quantity of an elemental halogen vapor, thereby forming a gas mixture including said heating gas and said quantity of said elemental halogen vapor.2. The process of claim 1 , wherein said heating gas is preheated in the absence of water.3. The process of claim 1 , wherein said elemental halogen is bromine.4. The process of claim 1 , wherein said heating gas comprises a hydrocarbon.5. The process of claim 1 , wherein said heating gas has a majority mole fraction of methane.6. The process of claim 1 , wherein said heating gas does not substantially react with said elemental halogen when heating said liquid elemental halogen with said preheated heating gas.7. The process of claim 1 , wherein said elemental halogen vapor is saturated in said heating of said gas mixture.8. The process of claim 1 , wherein said preheat temperature is less than the halogenation initiation temperature of said elemental halogen and said heating gas.9. The process of claim 1 , wherein said ...

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Номер записи: 41
25-07-2013 дата публикации

Method for preparing optically active 1-bromo-1-[3,5-bis(trifluoromethyl)phenyl]ethane

Номер: US20130190540A1
Автор: Kennosuke Matsuda, Kimiyuki Shibuya, Koichi Yamazaki, Tadaaki Ohgiya, Taichi Kusakabe
Принадлежит: Kowa Co Ltd

A method for preparing optically active 1-bromo-1-[3,5-bis(trifluoromethyl)-phenyl]ethane having a high optical purity, which comprises the step of brominating optically active 1-[3,5-bis(trifluoromethyl)phenyl]ethanol by using, as a brominating agent, (a) a combination of a phosphorus halide and hydrogen bromide, (b) a combination of 1,2-dibromo-1,1,2,2-tetrachloroethane and an organic phosphorous compound represented by the general formula (I): P(R 1 )(R 2 )(R 3 ) (in the formula, R 1 , R 2 , and R 3 independently represent a C 6-10 aryl group, a C 6-10 aryloxy group, a C 1-10 alkyl group, a C 1-10 alkoxyl group, a C 3-6 cycloalkyl group, or a C 3-6 cycloalkoxy group), or (c) a combination of N-bromosuccinimide and a dialkyl sulfide.

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Номер записи: 42
25-07-2013 дата публикации

CATALYST SYSTEM, COMPRISING CATALYST PELLETS AND DILUENT BEADS WITH PREDEFINED DIMENSIONS AND PHYSICOCHEMICAL PROPERTIES

Номер: US20130190541A1
Автор: Du Preez Lorette, Lee Stephen Kevin, Marsella Andrea, Vidotto Sandro
Принадлежит: INEOUS EUROPE AG

A catalyst system for use in oxychlorination, the catalyst system comprising catalyst pellets comprising a catalyst carried on a substrate the pellets having length x, breadth y and depth z, intrinsic density P and bulk density p and diluent beads having length x±25%, breadth y±25% and depth z±25%, intrinsic density≧P+25% and a bulk density p ±25%. 132-. (canceled)33. A catalyst system for use in oxychlorination , said catalyst system comprising catalyst pellets comprising a catalyst carried on a first substrate , said catalyst pellets having a length x , breadth y and depth z and bulk density ρ and diluent beads comprising a second substrate different from that of the first substrate said beads having a length x±25% , breadth y±25% depth z±25% and bulk density p±25% and said diluent beads having a thermal conductivity at least 5 times greater than the thermal conductivity of said catalyst pellets.34. A catalyst system as claimed in wherein x is in the range 3 to 7 mm.35. A catalyst system as claimed in wherein y is in the range 4 to 7 mm.36. A catalyst system as claimed in wherein z is in the range 4 to 7 mm.37. A catalyst system as claimed in wherein said catalyst pellets comprise alumina.38. A catalyst system as claimed in wherein said diluent beads comprise graphite.39. A catalyst system as claimed in wherein the thermal conductivity of said diluent beads is less than 50 times greater than the thermal conductivity of said pellets.40. A catalyst system as claimed in wherein said pellets are trigonal prisms or right circular cylinders.41. A catalyst system as claimed in wherein said beads are right circular cylinders having a right circular bore having a diameter in the range 2.0 to 4.0 mm.42. A catalyst system as claimed in wherein the lateral compressive strength of the beads is 2 to 4 times that of the pellets.43. A method of preparing 1 claim 33 ,2-dichloroethane comprising passing ethylene claim 33 , hydrogen chloride and a molecular oxygen containing gas ...

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Номер записи: 43
01-08-2013 дата публикации

SYNTHESIS OF FLUORINATED OLEFINS FROM FLUORINATED ALCOHOLS

Номер: US20130197280A1
Автор: Cherstkov Victor Filippovich, Nappa Mario Joseph, Stepanov Andrei Aleksandrovich
Принадлежит: EI DU PONT DE NEMOURS AND COMPANY

Disclosed is a process for producing a hydrofluoroalkene, RCF═CHcomprising contacting a hydrofluoroalkanol of structure RCFCHOH, with a lewis acid to produce a mixture, diluting said mixture with a solvent to produce a solvent mixture, contacting the solvent mixture with a reactive metal, heating the solvent mixture and reactive metal for a sufficient amount of time to produce a hydrofluoroalkene, and condensing and collecting the volatile products comprising the hydrofluoroalkene, wherein Ris F, or a fluorine-substituted alkyl group. 1. A process for producing a hydrofluoroalkene , RCF═CHcomprising:{'sub': f', '2', '2', 'f, 'contacting a hydrofluoroalkanol of structure RCFCHOH, with a lewis acid to produce a mixture, diluting said mixture with a solvent to produce a solvent mixture, contacting the solvent mixture with a reactive metal, heating the solvent mixture and reactive metal for a sufficient amount of time to produce a hydrofluoroalkene, and condensing and collecting the volatile products comprising the hydrofluoroalkene, wherein Ris F, or a fluorine-substituted alkyl group.'}2. The process of claim 1 , wherein said fluorine-substituted alkyl group Ris CF claim 1 , CF claim 1 , n-CF claim 1 , i-CF claim 1 , n-CF claim 1 , or CHFCFCF—.3. The process of claim 1 , wherein the mole ratio of said lewis acid to hydrofluoroalkanol is from about 1:1 to about 2:1.4. The process of claim 1 , wherein said Lewis acid is selected from the group consisting of titanium (IV) halides claim 1 , zirconium (IV) halides claim 1 , hafnium (IV) halides claim 1 , vanadium (III) halides claim 1 , vanadium (IV) halides claim 1 , niobium (V) halides claim 1 , tantalum (V) halides claim 1 , boron (III) halides and aluminum (III) halides.5. The process of claim 1 , wherein said Lewis acid is selected from the group consisting of titanium tetrachloride claim 1 , zirconium tetrachloride claim 1 , hafnium tetrachloride claim 1 , vanadium trichloride claim 1 , vanadium tetrachloride claim 1 ...

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Номер записи: 44
01-08-2013 дата публикации

PROCESS FOR MANUFACTURING PERFLUOROOLEFINS BY PYROLYSIS OF PERFLUOROCARBONS IN THE PRESENCE OF HYDROGEN

Номер: US20130197281A1
Автор: Hintzer Klaus, Jürgens Michael, Kämpf Günther J., Lochhaas Kai Helmut, Luther Klaus, Shyshkov Oleg, Streiter André, Troe Jürgen, Zipplies Tilman C.
Принадлежит: 3M INNOVATIVE PROPERTIES COMPANY

A process is described of pyrolyzing at least one perfluorinated hydrocarbon, or a material containing at least one perfluorinated hydrocarbon, in the presence of hydrogen, to yield a reaction mixture containing difluorocarbene. 1. A process comprising pyrolyzing at least one perfluorinated hydrocarbon , or a material containing at least one perfluorinated hydrocarbon , in a pyrolysis zone at a temperature between about 580 K and about 2000 K in the presence of hydrogen to yield a reaction mixture containing difluorocarbene , wherein the hydrogen is present in the pyrolysis zone in a molar ratio from about 0.1 to 8 mol hydrogen per mol of perfluorinated hydrocarbon.2. The process of wherein the pyrolysis is carried at in the pyrolysis zone at a temperature of from about from 600 K to 1100 K.3. The process of further comprising quenching said reaction mixture after it exits the pyrolysis zone to yield a product mixture containing tetrafluoroethene and/or hexafluoropropene and claim 1 , optionally claim 1 , separating tetrafluoroethene and/or hexafluoropropene from said product mixture.4. The process according wherein the perfluorinated hydrocarbon is a gas claim 1 , a liquid claim 1 , or a mixture thereof.5. The process according to wherein the perfluorinated hydrocarbon comprises a straight chain or branched perfluroalkane represented by the formula CF claim 1 , wherein n is an integer of from 2 to 25.6. The process according to claim 1 , wherein the perfluorinated hydrocarbon has a boiling point of not more than 250° C.7. The process according to wherein the pyrolysis is carried out in the absence of added carbon.8. The process according to further comprising quenching the reaction mixture comprising difluorocarbene to yield a product mixture containing tetrafluoroethene and/or hexafluoropropene and feeding back into the pyrolysis zone at least a part of the product mixture after removing tetrafluorethene and/or hexafluoropropene therefrom.9. The process according ...

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Номер записи: 45
01-08-2013 дата публикации

METHOD FOR PRODUCING 2-CHLORO-3,3,3,-TRIFLUOROPROPENE (HCFC-1233xf)

Номер: US20130197282A1
Автор: Daniel C. Markel, Hsueh S. Tung
Принадлежит: Honeywell International Inc

The present invention relates to an improved method for manufacturing 2-chloro-3,3,3,-trifluoropropene (HCFC-1233xf) by reacting 1,1,2,3-tetrachloropropene, 1,1,1,2,3-pentachloropropane, and/or 2,3,3,3-tetrachloropropene with hydrogen fluoride, in a vapor phase reaction vessel in the presence of a vapor phase fluorination catalyst and stabilizer. HCFC-1233xf is an intermediate in the production of 2,3,3,3-tetrafluoropropene (HFO-1234yf) which is a refrigerant with low global warming potential.

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Номер записи: 46
08-08-2013 дата публикации

CATALYST FOR PREPARING VINYL CHLORIDE, METHODS OF PREPARATION AND APPLICATION THEREOF

Номер: US20130204052A1
Автор: Jiang Biao, Zhong Jinguang
Принадлежит:

The present invention discloses a catalyst used in preparing vinyl chloride, its method of preparation, and its applications. Said catalyst used in making vinyl chloride comprises activated carbon as a support, a barium compound and a phosphorus compound supported thereon. The barium compound accounts for 0.2% to 20% of the total mass of the catalyst and the phosphorus compound accounts for 0% to 10% of the total mass of the catalyst based on the mass percentage. A water-soluble barium compound, a water-soluble phosphorus compound, an aqueous polymer monomer, and water are mixed to form a solution or emulsion A. The activated carbon is added into the solution or emulsion A. The activated carbon is removed from water after impregnation, spin-dried, and then the monomers are polymerized. The activated carbon, after polymerization step, is heated to remove water and to decompose and carbonize the polymer. The catalyst after carbonization was activated to obtain a catalyst used in making vinyl chloride. 1. A catalyst for the preparation of vinyl chloride , characterized in that:said catalyst comprises activated carbon as a carrier, a barium compound and a phosphorus compound supported on the carrier, wherein said barium compound has a mass percentage of 0.2% to 20% and said phosphorous compound has a mass percentage of 0% to 10% based on the total mass of the catalyst.2. The catalyst of claim 1 , wherein said barium compound is barium chloride and said phosphorus compound is phosphoric acid.3. A method for preparing a catalyst of used in preparing vinyl chloride claim 1 , characterized in that said method comprising the steps of:(1) mixing a water-soluble barium compound, a water-soluble phosphorus compound, an aqueous polymer monomer, and water to obtain a solution A or an emulsion A;(2) impregnating the activated carbon in the solution A or the emulsion A;(3) polymerizing the aqueous polymeric monomer on the activated carbon after spin-drying;(4) heating the activated ...

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Номер записи: 47
15-08-2013 дата публикации

SELECTIVE DEHYDROHALOGENATION OF TERTIARY HALOGENATED HYDROCARBONS AND REMOVAL OF TERTIARY HALOGENATED HYDROCARBON IMPURITIES FROM A HALOGENATED HYDROCARBON PRODUCT

Номер: US20130206578A1
Автор: Au-Yeung Patrick H., Bronkema Jason L., Frank Timothy C., Hickman Daniel A., Holden Bruce S., Johnston Robin K., McCabe Terrence, Patel Mukund R., Trippeer Michael L.
Принадлежит: DOW AGROSCIENCES LLC

A process for converting a tertiary halogenated hydrocarbons in a tertiary halogenated hydrocarbon-containing stream to a corresponding unhalogenated or less-halogenated unsaturated hydrocarbon product with the release of hydrogen halide involves contacting the tertiary halogenated hydrocarbon with a sorbent-type dehydrohalogenation catalyst in a reaction zone and optionally passing a stripping gas through the reaction zone to remove vapor phase reaction products from the reaction zone. A process for removing a tertiary chlorinated hydrocarbon impurity from 1,3-dichloro-1-propene involves contacting a mixture containing the 1,3-dichloro--propene and the tertiary chlorinated hydrocarbon impurity with a dehydrochlorination catalyst effective to catalyze a conversion of the tertiary chlorinated hydrocarbon impurity to a corresponding unchlorinated or less-chlorinated unsaturated hydrocarbon and hydrogen chloride and distilling the 1,3-dichloro-1-propene to produce a purified cis-1,3-dichloro- 1-propene fraction and a purified trans-1,3-dichloro-1-propene fraction. 131-. (canceled)32. A method for removing a tertiary halogenated hydrocarbon impurity from a target hydrocarbon compound , comprising:providing a first mixture comprising a target hydrocarbon compound and a tertiary halogenated hydrocarbon impurity;contacting the first mixture containing the tertiary halogenated hydrocarbon impurity with a dehydrohalogenation catalyst effective to catalyze a conversion of the tertiary halogenated hydrocarbon impurity to a corresponding unhalogenated or less-halogenated unsaturated hydrocarbon and hydrogen halide, thereby providing a modified mixture; anddistilling the modified mixture to separate and recover a purified target hydrocarbon compound.33. The method in accordance with wherein the tertiary halogenated hydrocarbon has a boiling point within 5° C. of the boiling point of the target hydrocarbon compound.34. The method in accordance with wherein the target hydrocarbon ...

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Номер записи: 48
15-08-2013 дата публикации

SELECTIVE DEHYDROHALOGENATION OF TERTIARY HALOGENATED HYDROCARBONS AND REMOVAL OF TERTIARY HALOGENATED HYDROCARBON IMPURITIES FROM A HALOGENATED HYDROCARBON PRODUCT

Номер: US20130206579A1
Автор: Au-Yeung Patrick H., Bronkema Jason L., Frank Timothy C., Hickman Daniel A., Holden Bruce S., Johnston Robin K., McCabe Terrence, Patel Mukund R., Trippeer Michael L.
Принадлежит: DOW AGROSCIENCES LLC

A process for converting a tertiary halogenated hydrocarbons in a tertiary halogenated hydrocarbon-containing stream to a corresponding unhalogenated or less-halogenated unsaturated hydrocarbon product with the release of hydrogen halide involves contacting the tertiary halogenated hydrocarbon with a sorbent-type dehydrohalogenation catalyst in a reaction zone and optionally passing a stripping gas through the reaction zone to remove vapor phase reaction products from the reaction zone. A process for removing a tertiary chlorinated hydrocarbon impurity from 1,3-dichloro-1-propene involves contacting a mixture containing the 1,3-dichloro-1-propene and the tertiary chlorinated hydrocarbon impurity with a dehydrochlorination catalyst effective to catalyze a conversion of the tertiary chlorinated hydrocarbon impurity to a corresponding unchlorinated or less-chlorinated unsaturated hydrocarbon and hydrogen chloride and distilling the 1,3-dichloro-1-propene to produce a purified cis-1,3-dichloro-1-propene fraction and a purified trans-1,3-dichloro-1-propene fraction. 1. A method for removing a tertiary chlorinated hydrocarbon impurity from 1 ,3-dichloro-1-propene , comprising:providing a first mixture comprising 1,3-dichloro-1-propene and a tertiary chlorinated hydrocarbon impurity;contacting the first mixture containing the tertiary chlorinated hydrocarbon impurity with a dehydrochlorination catalyst effective to catalyze a conversion of the tertiary chlorinated hydrocarbon impurity to a corresponding unchlorinated or less-chlorinated unsaturated hydrocarbon and hydrogen chloride; anddistilling the 1,3-dichloro-1-propene to separate and recover a purified cis-1,3-dichloro-1-propene fraction and a purified trans-1,3-dichloro-1-propene fraction;wherein the tertiary chlorinated hydrocarbon impurity comprises an impurity selected from the group consisting of 2-chloro-2-methylpentane, 2-chloro-2,3-dimethylbutane, 4-chloro-4-methyl-1-pentene and mixtures thereof.2. The method ...

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Номер записи: 49
15-08-2013 дата публикации

BLOWING AGENTS, FOAM PREMIXES AND FOAMS CONTAINING HALOGENATED OLEFIN BLOWING AGENT AND ADSORBENT

Номер: US20130210946A1
Автор: Bogdan Mary C., LING Yiu Keung, Williams David J.
Принадлежит: HONEYWELL INTERNATIONAL INC.

The invention provides polyurethane and polyisocyanurate foams and methods for the preparation thereof. More particularly, the invention relates to closed-celled, polyurethane and polyisocyanurate foams and methods for their preparation. Preferably, the foams are produced with a polyol premix composition which comprises a combination of a hydrohaloolefin blowing agent, a polyol, a catalyst and an adsorbent material. 1. A polyol premix composition comprising at least one blowing agent , a polyol , at least one surfactant , a catalyst , and an adsorbing agent , wherein the blowing agent comprises a hydrohaloolefin , and optionally a hydrocarbon , fluorocarbon , chlorocarbon , fluorochlorocarbon , halogenated hydrocarbon , COor other gas generating material , or combinations thereof.2. The polyol premix composition of wherein the adsorbing agent is a halogen ion scavenger selected from the group consisting of a silica gel claim 1 , fumed silica claim 1 , activated charcoal claim 1 , calcium sulfate claim 1 , calcium chloride claim 1 , montmorillonite clay claim 1 , a molecular sieve claim 1 , and combinations thereof.3. The polyol premix composition of wherein the halogen ion scavenger comprises a molecular sieve having a pore diameter between about 3 Å to about 8 Å.4. The polyol premix composition of claim 1 , wherein the absorbing materials is provided in an amount between about 0.1 wt. % and about 20 wt. %.5. The polyol premix composition of wherein the catalyst comprises an amine catalyst having the formula RRN-[A-NR]Rwherein each of R claim 1 , R claim 1 , R claim 1 , and Ris independently H claim 1 , a Cto Calkyl group claim 1 , a Cto Calkenyl group claim 1 , a Cto Calcohol group claim 1 , or a Cto Cether group claim 1 , or Rand Rtogether form a Cto Ccyclic alkyl group claim 1 , a Cto Ccyclic alkenyl group claim 1 , a Cto Cheterocyclic alkyl group claim 1 , or a Cto Cheterocyclic alkenyl group; A is a Cto Calkyl group claim 1 , a Cto Calkenyl group claim 1 , or ...

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Номер записи: 50
15-08-2013 дата публикации

PROCESS FOR THE PRODUCTION OF HCFC-1233zd

Номер: US20130211154A1
Автор: Cottrell Stephen A., Merkel Daniel C., Pokrovski Konstantin A., Tung Hsueh Sung, WANG HAIYOU
Принадлежит: HONEYWELL INTERNATIONAL INC.

A process for the manufacture of 1-chloro-3,3,3-trifluoropropene (HCFC-1233zd) at commercial scale from the reaction of HCC-240 and HF is disclosed. In one embodiment, HCC-240fa and HF are fed to a reactor operating at high pressure. Several different reactor designs useful in this process include; a stirred-tank reactor (batch and/or continuous flow); a plug flow reactor; a static mixer used as a reactor; at least one of the above reactors operating at high pressure; optionally combined with a distillation column running at a lower pressure; and combinations of the above; and/or with a distillation column. The resulting product stream consisting of 1233zd, HCl, HF, and other byproducts is partially condensed to recover HF by phase separation. The recovered HF phase is recycled to the reactor. The HCl is scrubbed from the vapor stream and recovered as an aqueous solution. The remaining organic components including the desired HCFC-1233zd are scrubbed, dried and distilled to meet commercial product specifications. 1. A process for the production of 1-chloro-3 ,3 ,3-trifluoropropene (HCFC-1233zd) comprising the steps of:(a) reacting HCC-240 and HF in a high pressure liquid phase reactor to generate an effluent reaction stream comprising HCFC-1233zd, intermediates and byproducts of HCFC-1233zd, HCl and unreacted HCC-240 and HF; and(b) at least partially condensing the effluent stream from reaction step (a) to form a condensate comprising HCFC-1233zd.2. The process of claim 1 , further comprising the following steps:(c) separating the condensate from step (b) using phase separation, to form an HF-rich layer and an organic rich layer; and(d) recycling the HF-rich layer from step (c) to the reactor in step (a).3. The process of claim 2 , further comprising the following steps:(e) feeding the organic rich layer from step (c) to an aqueous HCl recovery system to remove and recover the HCl as a solution in water;(f) distilling the HCl-free organic components from step (e) ...

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Номер записи: 51
15-08-2013 дата публикации

Process for making tetrafluoropropene

Номер: US20130211155A1
Автор: Andrew Joseph Poss, David Nalewajek, Haridasan K. Nair, Rajiv Ratna Singh
Принадлежит: Honeywell International Inc

The present invention describes a process for making CF 3 CH═CHF (HFO-1234ze). The process involves the addition of carbon tetrachloride (CCl 4 ) to 1,2-dichloroethylene to form CCl 3 CHClCHCl 2 . The compound CCl 3 CHClCHCl 2 thus can then either be treated with HF to produce CF 3 CHClCHClF as the main product, or it can be converted to CCl 2 ═CHCHCl 2 (1230za) by dechlorination. CCl 2 ═CHCHCl 2 can be treated with HF such that the main product obtained is CF 3 CHClCHClF. CF 3 CH═CHCl may be produced as a by-product, but upon treatment with HF, it affords the compound CF 3 CHClCHClF. The desired compound, CF 3 CH═CHF (HFO-1234ze), is obtained as a trans/cis mixture by dehydrochlorination of CF 3 CH 2 CHClF or by dechlorination of CF 3 CHClCHClF.

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Номер записи: 52
15-08-2013 дата публикации

PROCESS FOR 1,3,3,3-TETRAFLUOROPROPENE

Номер: US20130211156A1
Автор: NAIR HARIDASAN K., Nalewajek David, Poss Andrew Joseph, Singh Rajiv Ratna
Принадлежит: HONEYWELL INTERNATIONAL INC.

The present invention provides a simple three step process for the production of 1,3,3,3-tetrafluoropropene (HFO-1234ze). In the first step, carbon tetrachloride is added to vinyl fluoride to afford the compound CClCHCHClF (HCFC-241fb). HCFC-241fb is then fluorinated with anhydrous HF to afford CFCHCHClF (HCFC-244fa) in the second step. Dehydrochlorination of HCFC-244fa, in the third step, affords the desired product, CFCH═CHF (HFO-1234ze). Following similar chemistry, vinyl chloride may be used in place of vinyl fluoride. 1. A process for the production of 1 ,3 ,3 ,3-tetrafluoropropene (HFO-1234ze) comprising the steps of:{'sub': 3', '2, '(a) reacting carbon tetrachloride with vinyl fluoride to afford the compound CClCHCHClF (HCFC-241fb);'}{'sub': 3', '2, '(b) fluorinating HCFC-241fb with HF to afford the compound CFCHCHClF (HCFC-244fa); and'}{'sub': '3', '(c) dehydrochlorinating HCFC-244fa to produce the compound CFCH═CHF (HFO-1234ze).'}2. A process for the production of 1 ,3 ,3 ,3-tetrafluoropropene (HFO-1234ze) comprising the steps of:{'sub': 3', '2', '2, '(a) reacting carbon tetrachloride with vinyl chloride to afford the compound CClCHCHCl;'}{'sub': 3', '2', '2, '(b) fluorinating the compound CClCHCHClto generate the compound CF3CH2CHClF (HCFC-244fa); and'}{'sub': '3', '(c) dehydrochlorinating HCFC-244fa to produce the compound CFCH═CHF (HFO-1234ze).'}3. The process of claim 1 , wherein the reaction of carbon tetrachloride with the vinyl halide compound is conducted in the presence of triethylphosphate and an iron material selected from the group consisting of supported or unsupported iron powder claim 1 , iron nanopowder and iron nanoparticles claim 1 , at an elevated temperature.4. The process of claim 3 , wherein the elevated temperature is from about 120° C. to 130° C.5. The process of claim 1 , wherein the step (b) fluorination reaction is conducted with an excess equivalent of hydrogen fluoride in the presence of a fluorination catalyst.6. The process of ...

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Номер записи: 53
22-08-2013 дата публикации

Method of calibrating and correcting color-bleed factors for color separation in dna analysis

Номер: US20130214177A1
Автор: CHING MING LAI
Принадлежит: Analogic Corp

A method includes calibrating color bleed factors of optical detector channels of a sample processing apparatus through processing a color bleed calibration substance which includes a plurality of different size fragments replicated from different groups of DNA loci, wherein fragments in a same group are labeled with a same fluorescent dye, and fragments in different groups are labeled with different fluorescent dyes having different emission spectra, wherein the different size fragments are processed during different acquisition times.

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Номер записи: 54
22-08-2013 дата публикации

Process for Preparing R-1234yf by Base Mediated Dehydrohalogenation

Номер: US20130217927A1
Автор: Low Robert Elliott, McCarthy John Charles, Sharratt Andrew Paul
Принадлежит: MEXICHEM AMANCO HOLDING S.A. DE C.V.

The invention relates to a process for preparing 2,3,3,3-tetrafluoropropene (CFCF═CH), performed using the steps of dehydrohalogenating 1,1,1,2,2-pentafluoropropane (CHCFCF, HFC-245ca) 1,1,1,2-tetrafluoro-2-chloropropane, 1,1,1,2,3-pentafluoropropane (CHFCHFCF, HFC-245eb) and/or 1,1,1,2-tetrafluoro-3-chloropropane in the presence of a base, and converting a trifluorodichloropropane or a difluorotrichloropropane or a fluorotetrachloropropane to CHCFCF, 1,1,1,2-tetrafluoro-2-chloropropane, CHFCHFCF, and/or 1,1,1,2-tetrafluoro-3-chloropropane. 1. A process for preparing 2 ,3 ,3 ,3-tetrafluoropropene (CFCF═CH) , comprising the steps of:{'sub': 3', '2', '3', '2', '3, 'dehydrohalogenating 1,1,1,2,2-pentafluoropropane (CHCFCF, HFC-245ca) 1,1,1,2-tetrafluoro-2-chloropropane, 1,1,1,2,3-pentafluoropropane (CHFCHFCF, HFC-245eb) and/or 1,1,1,2-tetrafluoro-3-chloropropane in the presence of a base; and'}{'sub': 3', '2', '3', '2', '3, 'converting a trifluorodichloropropane or a difluorotrichloropropane or a fluorotetrachloropropane to CHCFCF, 1,1,1,2-tetrafluoro-2-chloropropane, CHFCHFCF, and/or 1,1,1,2-tetrafluoro-3-chloropropane.'}2. A process according to carried out at a temperature of from −50 to 300° C. and a pressure of from 0 to 30 bara.3. A process according to wherein the base is selected from a metal hydroxide claim 1 , a metal amide and mixtures thereof.4. A process according to wherein the base is an alkali metal hydroxide.5. A process according to wherein the alkali metal hydroxide is selected from sodium hydroxide and potassium hydroxide.6. A process according to wherein the base is an alkaline earth metal hydroxide.7. A process according to wherein the alkaline earth metal hydroxide is calcium hydroxide.8. A process according to wherein the process is carried out in a solvent.9. A process according to wherein the solvent is selected from water claim 8 , alcohols claim 8 , diols claim 8 , polyols claim 8 , polar aprotic solvents and mixtures thereof.10. A process ...

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Номер записи: 55
22-08-2013 дата публикации

PROCESS FOR PRODUCING 2,3,3,3-TETRAFLUOROPROPENE

Номер: US20130217928A1
Автор: KOMATSU Yuzo, Takahashi Kazuhiro, UEDA Akinori
Принадлежит: DAIKIN INDUSTRIES, LTD.

This invention provides a process for producing 2,3,3,3-tetrafluoropropene, the process comprising: (1) a first reaction step of reacting hydrogen fluoride with at least one chlorine-containing compound selected from the group consisting of a chloropropane represented by Formula (1): CClXCHClCHCl, wherein each X is the same or different and is CI or F, a chloropropene represented by Formula (2): CClYCCl═CH, wherein each Y is the same or different and is CI or F, and a chloropropene represented by Formula (3): CZ═CClCHCl, wherein each Z is the same or different and is CI or F in a gas phase in the absence of a catalyst while heating; and (2) a second reaction step of reacting hydrogen fluoride with a reaction product obtained in the first reaction step in a gas phase in the presence of a fluorination catalyst while heating. According to the process of this invention, 2,3,3,3-tetrafluoropropene (HFO-1234yf) can be obtained with high selectivity, and catalyst deterioration can be suppressed. 1. A process for producing 2 ,3 ,3 ,3-tetrafluoropropene , the process comprising:{'sub': 2', '2', '2', '2', '2', '2, '(1) a first reaction step of reacting hydrogen fluoride with at least one chlorine-containing compound selected from the group consisting of a chloropropane represented by Formula (1): CClXCHClCHCl, wherein each X is the same or different and is Cl or F, a chloropropene represented by Formula (2): CClYCCl═CH, wherein each Y is the same or different and is Cl or F, and a chloropropene represented by Formula (3): CZ═CClCHCl, wherein each Z is the same or different and is Cl or F in a gas phase in the absence of a catalyst while heating; and'}(2) a second reaction step of reacting a reaction product obtained in the first reaction step with hydrogen fluoride in a gas phase in the presence of a fluorination catalyst while heating.2. The process according to claim 1 , wherein the reaction temperature in the first reaction step is 250 to 600° C. claim 1 , and the reaction ...

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Номер записи: 56
22-08-2013 дата публикации

Azeotrope-Like Composition of Hexafluoropropane, Hexafluoropropene and Hydrogen Fluoride

Номер: US20130217929A1
Автор: HULSE RYAN, Merkel Daniel C., Pham Hang T., Pokrovski Konstantin A., SINGH Rajiv R., TUNG HSUEH S.
Принадлежит: HONEYWELL INTERNATIONAL INC.

The present invention relates to an azeotropic or azeotrope-like mixture consisting essentially of 1,1,1,2,3,3-hexafluoropropane, hexafluoropropene and hydrogen fluoride. 112-. (canceled)13. A method for removing 1 ,1 ,1 ,2 ,3 ,3-hexafluoropropane from a mixture containing 1 ,1 ,1 ,2 ,3 ,3-hexafluoropropane and at least one impurity , comprising adding hydrogen fluoride and , optionally , hexafluoropropene to the mixture in an effective amount to form an azeotropic or azeotrope-like composition of 1 ,1 ,1 ,2 ,3 ,3-hexafluoropropane , hexafluoropropene , and hydrogen fluoride , and separating the azeotropic composition from the impurity.14. The method of wherein the impurity does not form an azeotropic mixture with 1 claim 13 ,1 claim 13 ,1 claim 13 ,2 claim 13 ,3 claim 13 ,3-hexafluoropropane claim 13 , hexafluoropropene claim 13 , hydrogen fluoride or a mixture thereof.15. The method of wherein the impurity does form an azeotropic mixture with 1 claim 13 ,1 claim 13 ,1 claim 13 ,2 claim 13 ,3 claim 13 ,3-hexafluoropropane claim 13 , hexafluoropropene claim 13 , hydrogen fluoride or a mixture thereof.16. The method of wherein the impurity comprises a halocarbon.17. The method of wherein the impurity is miscible with 1 claim 13 ,1 claim 13 ,1 claim 13 ,2 claim 13 ,3 claim 13 ,3-hexafluoropropane.18. The method of wherein the impurity is selected from the group consisting of 1 claim 13 ,1 claim 13 ,1 claim 13 ,2 claim 13 ,3-pentafluoropropane claim 13 , 1 claim 13 ,1 claim 13 ,1 claim 13 ,3 claim 13 ,3-pentafluoropropane claim 13 , 1 claim 13 ,1 claim 13 ,1 claim 13 ,2-tetrafluoropropane claim 13 , 1 claim 13 ,1 claim 13 ,1 claim 13 ,3-tetrafluoropropane claim 13 , (E)1 claim 13 ,2 claim 13 ,3 claim 13 ,3 claim 13 ,3-pentafluoropropene claim 13 , (Z)1 claim 13 ,2 claim 13 ,3 claim 13 ,3 claim 13 ,3-pentafluoropropene claim 13 , 3 claim 13 ,3 claim 13 ,3-trifluoropropene claim 13 , 1 claim 13 ,1 claim 13 ,1-trifluoropropane claim 13 , 3 claim 13 ,3 claim 13 ,3- ...

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Номер записи: 57
29-08-2013 дата публикации

Fluoroalkylation Methods And Reagents

Номер: US20130225815A1
Автор: Hiroyuki Morimoto, John F. Hartwig, Patrick Fier
Принадлежит: University of Illinois

A method of forming a fluorinated molecular entity includes reacting in a reaction mixture an aromatic halide, copper, a fluoroalkyl group, and a ligand. The aromatic halide includes an aromatic group and a halogen substituent bonded to the aromatic group. The ligand includes at least one group-V donor selected from phosphorus and an amine. The overall molar ratio of copper to aromatic halide in the reaction mixture is from 0.2 to 3. The method further includes forming a fluoroalkylarene including the aromatic group and the fluoroalkyl group bonded to the aromatic group. A composition, which may be used in the method, consists essentially of copper, the fluoroalkyl group, and the ligand, where the molar ratio of copper to the fluoroalkyl group is approximately 1.

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Номер записи: 58
29-08-2013 дата публикации

PROCESS FOR DEHYDROHALOGENATION OF HALOGENATED ALKANES

Номер: US20130225881A1
Автор: CHIU YUON, COOK George R., Cottrell Stephen A., KOPKALLI HALUK, Merkel Daniel C., SCHEIDLE Peter
Принадлежит: HONEYWELL INTERNATIONAL INC.

A process for the manufacture of halogenated olefins in semi-batch mode by dehydrohalogenation of halogenated alkanes in the presence of an aqueous base such as KOH which simultaneously neutralizes the resulting hydrogen halide. During the process, aqueous base is continuously added to the haloalkane which results in better yields, lower by-product formation and safer/more controllable operation. 118-. (canceled)19. A process for preparing a hydrofluoroolefin comprising:a. introducing an alkali-metal hydroxide feed stream into a reactor charged with at least one halogenated propane comprising at least one of 1-chloro-1,1,3,3,3-pentafluoropropane (HFCF-235fa) or 1,1,1,2,3,3-hexafluoropropane (HFCF-236ea)b. reacting, in a liquid phase, said halogenated propane with said an aqueous base in said reactor to produce a halogenated propene comprising 1,1,3,3,3-pentafluoropropene (HFO-1225zc); andc. removing at least a portion of said halogenated propene from said reactor as a vapor product stream,wherein steps (a), (b), and (c) are at least partially performed simultaneously.20. The process of wherein said halogenated propane is HFCF-235fa.21. The process of wherein said halogenated propane is HFCF-236fa.22. The process of further comprising refluxing at least a portion of any unreacted halogenated propane in said vapor product stream back to said reactor.23. The process of further comprises refluxing water in said vapor product stream back to said reactor.24. The process of wherein said reacting occurs at a temperature of about 40 to about 75° C.25. The process of claim 24 , wherein said reacting occurs at a temperature of about 50 to about 60° C.26. The process of claim 19 , wherein said aqueous base is an alkali metal hydroxide.27. The process of claim 26 , wherein said alkali metal hydroxide is potassium hydroxide.28. The process of claim 27 , wherein potassium hydroxide is present in a concentration of about 10 to about 50 wt. %.29. A method for preparing 1 claim 27 ,1 ...

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Номер записи: 59
29-08-2013 дата публикации

HYDROGENATION CATALYST

Номер: US20130225882A1
Автор: Merkel Daniel C., TUNG HSEUH S., WANG HAIYOU
Принадлежит: HONEYWELL INTERNATIONAL INC.

An alpha-alumina support for a hydrogenation catalyst useful in hydrogenating fluoroolefins is provided. 1. A composition comprising:a. about 90 to about 99.9 of alumina, wherein said alumina is at least about 90 wt. % alpha-alumina; andb. about 0.1 to about 10 weight percent of at least one zero-valent metal, wherein said zero-valent metal is selected from the group consisting of Pd, Ru, Pt, Rh, Ir, Fe, Co, Ni, Cu, Ag, Re, Os, and Au.2. An article of manufacture comprising a supported hydrogenation catalyst , wherein said supported hydrogenation catalyst comprises:a. a support comprising alpha-alumina and having at least one surface, andb. at least one zero-valent metal disposed on at least a portion of said surface, wherein said zero-valent metal is present in an amount from about 0.1 to about 10 weight percent based upon the total weight of the support and reduced zero-valent metal.3. The article of wherein said zero-valent metal is selected from the group consisting of Pd claim 2 , Ru claim 2 , Pt claim 2 , Rh claim 2 , Ir claim 2 , Fe claim 2 , Co claim 2 , Ni claim 2 , Cu claim 2 , Ag claim 2 , Re claim 2 , Os claim 2 , and Au.4. The article of wherein said support comprises at least about 50 wt. % alpha-alumina.5. The article of wherein said support comprises at least about 75 wt. % alpha-alumina.6. The article of wherein said support consists essentially of said alpha-alumina.7. The article of wherein said zero-valent metal is selected from the group consisting of Pd claim 6 , Ru claim 6 , Pt claim 6 , Rh claim 6 , Ir claim 6 , Fe claim 6 , Co claim 6 , Ni claim 6 , Cu claim 6 , Ag claim 6 , Re claim 6 , Os claim 6 , and Au8. The article of wherein said metal is Pd.9. The article of wherein said metal comprises about 0.1 to about 5 weight percent of the combined weight of said catalyst and said support.10. The article of wherein said metal comprises about 0.1 to about 1 weight percent of the combined weight of said catalyst and said support.11. A method for ...

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Номер записи: 60
05-09-2013 дата публикации

PROCESS FOR SEPARATION OF TETRAFLUOROETHYLENE FROM CARBON DIOXIDE USING IONIC LIQUIDS

Номер: US20130231448A1
Автор: Shiflett Mark Brandon, Yokozeki Akimichi
Принадлежит: E I DU PONT DE NEMOURS AND COMPANY

A process for separating tetrafluoroethylene from a mixture comprising tetrafluoroethylene and carbon dioxide by contacting the mixture with at least one ionic liquid. 1. A process for separating tetrafluoroethylene from a mixture comprising tetrafluoroethylene and carbon dioxide , comprising contacting the mixture with at least one ionic liquid in which carbon dioxide is soluble to a greater extent than tetrafluoroethylene , and separating the tetrafluoroethylene from the mixture.3. The process of wherein at least one of R claim 1 , R claim 1 , R claim 1 , R claim 1 , R claim 1 , R claim 1 , R claim 1 , R claim 1 , R claim 1 , and Rcomprises F.4. The process of wherein an ionic liquid comprises an anion selected from the group consisting of [CHCO] claim 1 , [HSO] claim 1 , [CHOSO] claim 1 , [CHSOSO] claim 1 , [AlCl] claim 1 , [CO] claim 1 , [HCO] claim 1 , [NO] claim 1 , [NO] claim 1 , [SO] claim 1 , [PO] claim 1 , [HPO] claim 1 , [HPO] claim 1 , [HSO] claim 1 , [CuCl] claim 1 , Cl claim 1 , Br claim 1 , I claim 1 , SCN claim 1 , and any fluorinated anion.5. The process of wherein an ionic liquid comprises an anion selected from the group consisting of [CHCO] claim 2 , [HSO] claim 2 , [CHOSO] claim 2 , [CHOSO] claim 2 , [AlCl] claim 2 , [CO] claim 2 , [HCO] claim 2 , [NO] claim 2 , [NO] claim 2 , [SO] claim 2 , [PO] claim 2 , [HPO] claim 2 , [HPO] claim 2 , [HSO] claim 2 , [CuCl] claim 2 , Cl claim 2 , Br claim 2 , I claim 2 , SCN claim 2 , and any fluorinated anion.6. The process of wherein an ionic liquid comprises an anion selected from the group consisting of [CHCO] claim 3 , [HSO] claim 3 , [CHOSO] claim 3 , [CHSOSO] claim 3 , [AlCl] claim 3 , [CO] claim 3 , [HCO] claim 3 , [NO] claim 3 , [NO] claim 3 , [SO] claim 3 , [PO] claim 3 , [HPO] claim 3 , [HPO] claim 3 , [HSO] claim 3 , [CuCl] claim 3 , Cl claim 3 , Br claim 3 , I claim 3 , SCN claim 3 , and any fluorinated anion.7. The process of wherein an ionic liquid comprises an anion selected from the group ...

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Номер записи: 61
12-09-2013 дата публикации

METHOD OF FORMING THIN FILM

Номер: US20130237677A1
Автор: Araki Takayuki, Kodani Tetsuhiro
Принадлежит: DAIKIN INDUSTRIES, LTD.

A vinylidene fluoride homopolymer represented by the formula (4): 124.-. (canceled)25. A vinylidene fluoride homopolymer represented by the formula (4):{'br': None, 'sub': '3', 'sup': '1', 'CF-(A)—I\u2003\u2003(4)'}{'sup': '1', 'wherein Arepresents a structural unit of vinylidene fluoride homopolymer which comprises crystal form I alone or as main component and has a number average degree of polymerization of 5 to 12.'}26. (canceled)27. (canceled)28. The vinylidene fluoride homopolymer of claim 25 , wherein the vinylidene fluoride homopolymer comprises crystal form I alone or as main component and when attention is given to proportions of the respective vinylidene fluoride homopolymers having crystal form I claim 25 , II or III which are calculated by IR analysis claim 25 , the proportion of vinylidene fluoride homopolymers having crystal form I satisfies both of (Equation 1):{'br': None, 'i': I', 'I', 'II, '100≧-form/(-form+-form)≧50% by weight\u2003\u2003(Equation 1)'}{'br': None, 'and (Equation 2){'br': None, 'i': I', 'I', 'III, '100≧-form/(-form+-form)≧50% by weight\u2003\u2003(Equation 2).'}29. (canceled)30. The vinylidene fluoride homopolymer of claim 28 , wherein the proportion of vinylidene fluoride homopolymers having crystal form I satisfies both of (Equation 3):{'br': None, 'i': I', 'I', 'II, '100≧-form/(-form+-form)≧70% by weight\u2003\u2003(Equation 3)'}{'br': None, 'and (Equation 4){'br': None, 'i': I', 'I', 'III, '100≧-form/(-form+-form)≧70% by weight\u2003\u2003(Equation 4).'}31. (canceled) This application is a Divisional of U.S. application Ser. No. 12/641,183 filed Dec. 17, 2009, which is a Divisional of U.S. application Ser. No. 11/231,992 filed Sep. 22, 2005, which is a continuation-in-part of PCT international application No. PCT/JP2004/004028 filed on Mar. 24, 2004 and which claims benefit of Japanese Patent Application No. JP 2003-86179 filed Mar. 26, 2003 and Japanese Patent Application No. JP 2003-422989 filed Dec. 19, 2003. The above-noted ...

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Номер записи: 62
19-09-2013 дата публикации

PROCESS FOR THE MANUFACTURE OF 2-CHLORO-1,1,1,2-TETRAFLUOROPROPANE BY LIQUID PHASE FLUORINATION OF 2-CHLORO-3,3,3-TRIFLUOROPROPANE

Номер: US20130245341A1
Автор: Bonnet Phillppe, Pigamo Anne, Wendlinger Laurent
Принадлежит:

Process of catalytic fluorination in liquid phase of product 2-chloro-3, 3, 3-trifluoropropene into product 2-chloro-1, 1, 1, 2-tetrafluoropropane, with an ionic liquid based catalyst. Process for manufacturing 2, 3, 3, 3-tetrafluoropropene. 1. Process comprising catalytic fluorination in the liquid phase of 2 chloro-3 ,3 ,3-trifluoropropene into 2-chloro-1 ,1 ,1 ,2-tetrafluoropropane , with HF and an ionic liquid as a catalyst.2. Process according to claim 1 , wherein the catalyst is obtained by reaction of at least one halogenated or oxyhalogenated Lewis acid based on aluminum claim 1 , titanium claim 1 , niobium claim 1 , tantalum claim 1 , tin claim 1 , antimony claim 1 , nickel claim 1 , zinc or iron with a salt of general formula Y+A− claim 1 , in which A− denotes a halide anion or hexafluoroantimonate anion and Y+ denotes a quaternary ammonium cation claim 1 , quaternary phosphonium cation or ternary sulfonium cation.3. Process according to claim 1 , wherein the catalyst is the fluorinated complex catalyst methyl-methyl-imidazolium SbF.4. Process according to claim 1 , carried out in a catalyst-rich phase.5. Process according to in which chlorine is added during the reaction.6. Process according to claim 1 , wherein a gas is injected.7. Process according to the claim 6 , in which the flow of gas claim 6 , compared. to the flow of the 2-chloro-3 claim 6 ,3 claim 6 ,3-trifluoropropene lie between 0.5:1 and 5:1.8. Process according to claim 1 , in which the 2-chloro-1 claim 1 ,1 claim 1 ,1 claim 1 ,2-tetrafluoropropane is withdrawn in the gaseous state.9. Process according to claim 1 , in which the temperature of the reaction ranges between 30° C. and 200° C.10. Process according to claim 1 , in which the pressure of the reaction is higher than 2 bar.11. Process according to claim 1 , in which the molar ratio of HF: 2-chloro-3 claim 1 ,3 claim 1 ,3-trifluoropropene lies between 0.5:1 and 50:1.12. Process according to claim 1 , comprising:(i) contacting 2-chloro- ...

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Номер записи: 63
26-09-2013 дата публикации

CATALYTIC ISOMERIZATION OF 2,3,3,3-TETRAFLUOROPROPENE

Номер: US20130253234A1
Автор: Nappa Mario Joseph
Принадлежит: E I DU PONT DE NEMOURS AND COMPANY

An isomerization process is disclosed. The process involves contacting 2,3,3,3-tetrafluoropropene with a suitable catalyst in a reaction zone to produce a product mixture comprising 1,3,3,3-tetrafluoropropene. 1. A process comprising: contacting 2 ,3 ,3 ,3-tetrafluoropropene with a suitable catalyst in a reaction zone to produce a product mixture comprising 1 ,3 ,3 ,3-tetrafluoropropene.2. The process of wherein said suitable catalyst comprises chromium oxyfluoride.3. The process of wherein said chromium oxyfluoride is prepared by treating chromium oxide with a fluorinating agent.4. The process of wherein said fluorinating agent is selected from the group consisting of HF claim 3 , CClF and hydrofluorocarbons.5. The process of wherein said suitable catalyst comprises a transition metal modified chromium oxide or a transition metal modified chromium oxyfluoride.6. The process of wherein said transition metal is selected from the group consisting of magnesium claim 5 , Group VIIB metals claim 5 , Group IIIB metals claim 5 , and zinc.7. The process of wherein said transition metal is supported on chromium oxide or chromium oxyfluoride.8. The process of wherein said suitable catalyst is selected from the group consisting of alumina claim 1 , fluorided alumina claim 1 , aluminum fluoride and mixtures thereof.9. The process of wherein said suitable catalyst is selected from the group consisting of transition metal modified alumina claim 8 , transition metal modified fluorided alumina claim 8 , transition metal modified aluminum fluoride and mixtures thereof.10. The process of wherein said transition metal is selected from the group consisting of magnesium claim 9 , Group VIIB metals claim 9 , Group IIIB metals claim 9 , and zinc.11. The process of wherein said transition metal is supported on alumina claim 10 , fluorided alumina or aluminum fluoride.12. The process of wherein the isomerization yield of 1 claim 1 ,3 claim 1 ,3 claim 1 ,3-tetrafluoropropene is at least 70 ...

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Номер записи: 64
26-09-2013 дата публикации

METHOD FOR PRODUCING FLUORINATED ORGANIC COMPOUNDS

Номер: US20130253235A1
Автор: Johnson Robert C., Merkel Daniel C., TUNG HSUEH S.
Принадлежит: HONEYWELL INTERNATIONAL INC.

Disclosed are processes for the production of fluorinated olefins, preferably adapted to commercialization of CFCF═CH(1234yf). In certain preferred embodiments the processes comprise first exposing a compound of Formula (IA) 120.-. (canceled)21. A process for making a tetrafluoropropene , comprising: dehydrohalogenating 2-chloro-1 ,1 ,1 ,2-tetrafluoropropane (HCFC-244bb) in the presence of a caustic agent.22. The process of wherein the tetrafluoropropene is 2 claim 21 ,3 claim 21 ,3 claim 21 ,3-tetrafluoropropene.23. The process of wherein the caustic agent is at least one agent selected from the group consisting of KOH claim 21 , NaOH claim 21 , Ca(OH) claim 21 , and CaO.24. The process of wherein the caustic agent is KOH.25. The process of wherein the caustic agent is provided in a solution having a caustic agent strength of between about 2 wt % and about 100 wt. %.26. The process of wherein the caustic agent is provided in a solution having a caustic agent strength of between about 5 wt % and about 90 wt. %.26. The process of wherein the caustic agent is provided in a solution having a caustic agent strength of between about 10 wt % and about 80 wt. %.27. The process of wherein a mole ratio of the caustic agent:HCFC-244bb is from about 1:1 to about 2:1.28. The process of wherein a mole ratio of caustic agent:HCFC-244bb is from about 1.1:1 to about 1.5:1.27. The process of wherein a mole ratio of caustic agent:HCFC-244bb is from about 1.2:1 to about 1.4:1.28. The process of wherein the dehydrohalogenating step is conducted at a temperature from about 20° C. to about 100° C.29. The process of wherein the dehydrohalogenating step is conducted at a temperature from about 30° C. to about 90° C.30. The process of wherein the dehydrohalogenating step is conducted at a temperature from about 40° C. to about 80° C.31. The process of wherein a reaction pressure of the process ranges from atmospheric pressure claim 21 , super-atmospheric pressure and sub-atmospheric ...

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Номер записи: 65
03-10-2013 дата публикации

Integrated process to coproduce trans-1-chloro-3,3,3-trifluoropropene, trans-1,3,3,3-tetrafluoropropene, and 1,1,1,3,3-pentafluoropropane

Номер: US20130261353A1
Автор: Daniel C. Merkel, Haiyou Wang, Hsueh Sung Tung, Konstantin A. Pokrovski
Принадлежит: Honeywell International Inc

Disclosed is an integrated manufacturing process to co-produce (E) 1-chloro-3,3,3-trifluoropropene, (E) 1,3,3,3-tetrafluoropropene, and 1,1,1,3,3-pentafluoro-propane starting from a single starting feed material or a mixture of unsaturated hydrochloro-carbon feed materials comprising 1,1,1,3-tetrachloropropene and/or 1,1,3,3-tetrachloro-propene. The process includes a combined liquid or vapor phase reaction/purification operation which directly produces (E) 1-chloro-3,3,3-trifluoro-propene (1233zd (E)) from these feed materials, which may also include 240fa. In the second liquid phase fluorination reactor 1233zd (E) is contacted with HF in the presence of catalyst to produce 1,1,1,3,3-pentafluoropropane (245fa) with high conversion and selectivity. A third reactor is used for dehydrofluorination of 245fa to produce (E) 1,3,3,3-tetrafluoro-propene (1234ze (E)) by contacting in the liquid phase with a caustic solution or in the vapor phase using a dehydrofluorination catalyst. This operation may be followed by one or more purification processes to recover the 1234ze (E) product.

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Номер записи: 66
10-10-2013 дата публикации

METHOD FOR MANUFACTURING SILICON-BASED NANOCOMPOSITE CATHODE ACTIVE MATERIAL FOR LITHIUM SECONDARY BATTERY AND LITHIUM SECONDARY BATTERY USING SAME

Номер: US20130264190A1
Автор: Cho Chu-hyun, Doh Chil-hoon, Ha Yoon-cheol
Принадлежит:

A method for manufacturing a silicon-based nanocomposite anode active material for the lithium secondary battery and the lithium secondary battery using same, comprising the following steps: a first step of mounting a silicon-based wire between two electrodes, which are placed in a methanol-based solvent atmosphere, and manufacturing a dispersion solution in which silicon-based nanoparticles are dispersed by means of high-voltage pulse discharging; and a second step of manufacturing a silicon-based nanocomposite body by compositing the silicon-based nanoparticles in the solution and a different type of material. By using the silicon-based nanocomposite anode in the lithium secondary battery according to the method, the advantages provided are of improving electronic conductivity and lithium-ion conductivity by means of the different type of material having a high-capacity characteristic, which encases the silicon-based nanoparticles, and of providing the lithium-ion secondary battery having enhanced battery capacity and charge/discharge cycle properties. 1. A method of preparing a silicon-based nanocomposite anode active material for a lithium secondary battery , comprising the steps of:(a) mounting a silicon-based wire between two electrodes provided in a methanol-based solvent atmosphere and then conducting high-voltage discharge to prepare a dispersion solution in which silicon nanoparticles are dispersed; and(b) combining the silicon nanoparticles with a different kind of material to prepare silicon-based nanocomposites.2. The method of claim 1 , wherein the silicon-based wire is made in the form of a wire claim 1 , bar or ribbon by molding any one selected from among a silicon wafer claim 1 , a silicon powder claim 1 , a silicon alloy claim 1 , and a mixed powder of silicon and a metal.3. The method of claim 1 , wherein claim 1 , in step (a) claim 1 , the methanol-based solvent is pure methanol claim 1 , a mixed solvent containing 50% or more of methanol or a ...

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Номер записи: 67
10-10-2013 дата публикации

PROCESS FOR THE PREPARATION OF 2,3,3,3 TETRAFLUOROPROPENE

Номер: US20130267740A1
Автор: Bonnet Philippe, Doucet Nicolas, Pigamo Anne, Wendlinger Laurent
Принадлежит: Arkema France

The present invention provides a process for preparing 2,3,3,3-tetrafluoropropene, comprising the following steps: (a) catalytic reaction of 1,1,1,2,3-pentachloropropane and/or 1,1,2,2,3-pentachloropropane with HF into product 2-chloro-3,3,3-trifluoropropene; (b) catalytic reaction of the thus-obtained 2-chloro-3,3,3-trifluoropropene into 2,3,3,3-tetrafluoropropene. 1. Process for preparing 2 ,3 ,3 ,3-tetrafluoropropene , comprising the steps:(a) catalytic reaction of 1,1,1,2,3-pentachloropropane and/or 1,1,2,2,3-pentachloropropane with HF into 2-chloro-3,3,3-trifluoropropene;(b) catalytic reaction of said 2-chloro-3,3,3-trifluoropropene into 2,3,3,3-tetrafluoropropene.2. The process of claim 1 , wherein step (b) comprises:(i) contacting 2-chloro-3,3,3-trifluoro-1-propene with hydrogen fluoride in the gas phase in the presence of a fluorination catalyst under conditions sufficient to produce a reaction mixture;(ii) separating the reaction mixture into a first stream comprising HCl, 2,2,2,3-tetrafluoropropene and a second stream comprising HF, unreacted 2-chloro-3,3,3-trifluoro-1-propene 1,1,1,2,2-pentafluoropropane; and(iii) recycling at least a part of the second stream back to step (i).3. The process according to claim 2 , wherein the first stream is separated into HCl and 2 claim 2 ,2 claim 2 ,2 claim 2 ,3-tetrafluoropropene.4. The process of claim 1 , wherein step (b) comprises:(i) contacting 2-chloro-3,3,3-trifluoro-1-propene with hydrogen fluoride in the gas phase in the presence of a fluorination catalyst under conditions sufficient to produce a reaction mixture comprising HCl and fluorinated products;(ii) separating the reaction mixture into HCl and a stream containing the fluorinated products;(iii) separating said stream containing the fluorinated products into a first stream comprising 2,2,2,3-tetrafluoropropene and a second stream comprising HF, unreacted 2-chloro-3,3,3-trifluoro-1-propene and 1,1,1,2,2-pentafluoropropane; and(iv) recycling at least a ...

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Номер записи: 68
10-10-2013 дата публикации

PROCESS FOR THE MANUFACTURE OF 2-CHLORO-3,3,3-TRIFLUOROPROPENE BY GAS PHASE FLUORINATION OF PENTACHLOROPROPANE

Номер: US20130267741A1
Автор: Bonnet Philippe, Doucet Nicolas, Pigamo Anne, Wendlinger Laurent
Принадлежит: Arkema France

The present invention provides a process of catalytic fluorination in gas phase of product 1,1,1,2,3- pentachloropropane or/and 1,1,2,2,3-pentachloropropane into product 2-chloro-3,3,3-trifluoropropene in presence of a catalyst and oxygen. 1. Process comprising the catalytic fluorination in the gas phase of 1 ,1 ,1 ,2 ,3-pentachloropropane and/or 1 ,1 ,2 ,2 ,3-pentachloropropane into 2-chloro-3 ,3 ,3-trifluoropropene in the presence of Hf , a catalyst and oxygen.2. Process according to claim 1 , wherein the ratio of oxygen with respect to 1 claim 1 ,1 claim 1 ,1 claim 1 ,2 claim 1 ,3-pentachloropropane and/or 1 claim 1 ,1 claim 1 ,1 claim 1 ,2 claim 1 ,2 claim 1 ,3-pentachloropropane is 0.05 to 15 mole.3. Process according to wherein said catalyst comprises Ni—Cr claim 1 , preferably supported.4. Process according to claim 1 , wherein said catalyst is supported on a support selected from fluorinated alumina claim 1 , fluorinated chromia claim 1 , fluorinated activated carbon or graphite carbon.5. Process according to claim 1 , wherein said catalyst further comprises a co-catalyst selected from Ni claim 1 , Co claim 1 , Zn claim 1 , Mn or mixtures thereof and wherein said co-catalyst is present in an amount from about 1-10 wt % of said catalyst.6. Process according to claim 1 , wherein said catalyst is activated with a fluorine-containing compound.7. Process according to claim 1 , in which said 1 claim 1 ,1 claim 1 ,1 claim 1 ,2 claim 1 ,3-pentachloropropane contains up to 40 mol % of 1 claim 1 ,1 claim 1 ,2 claim 1 ,2 claim 1 ,3-pentachloropropane.8. Process according to claim 1 , carried out at a pressure from 1 to 20 bars.9. Process according to claim 1 , carried out at a temperature of from 200 to 450° C.10. Process according to claim 1 , carried out with a contact time from 6 to 100 sec.11. Process according to claim 1 , carried out at a molar ratio of 1 claim 1 ,1 claim 1 ,1 claim 1 ,2 claim 1 ,3-pentachloropropane and/or 1 claim 1 ,1 claim 1 ,2 claim 1 ,2 ...

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Номер записи: 69
17-10-2013 дата публикации

INDUCTION FOR THERMOCHEMICAL PROCESSES, AND ASSOCIATED SYSTEMS AND METHODS

Номер: US20130272930A1
Автор: McAlister Roy Edward
Принадлежит:

Induction for thermochemical processes, and associated systems and methods. A method in accordance with a particular embodiment includes placing first and second substrates in a reactor, with each substrate having a surface facing toward the other. Method can further include directing a precursor gas into the reactor and activating an induction coil proximate to the facing surfaces of the substrates to dissociate the precursor gas. A constituent of the precursor gas is deposited on both the first and second surfaces, and heat radiated from each surface and/or a constituent deposited on the surface is received at the other surface and/or the constituent deposited on the other surface. 120-. (canceled)21. A reactor system for forming a material , comprising:a reactor vessel having a reaction zone;an induction coil positioned around the reaction zone;a reactant supply coupled in fluid communication with the reaction zone;a first substrate support positioned at the reaction zone to support a first substrate having a first surface;a second substrate support positioned at the reaction zone to support a second substrate having a second surface facing toward the first surface of the first substrate;a first insulator positioned at least proximate to the first substrate support, with at least one of the first substrate support and the first insulator positioned to insulate otherwise exposed surfaces of the first substrate, other than the first surface; anda second insulator positioned at least proximate to the second substrate support, with at least one of the second substrate support and the second insulator positioned to insulate otherwise exposed surfaces of the second substrate, other than the second surface.22. The system of claim 21 , further comprising:a first seal positioned to allow the first support to be withdrawn from the reaction zone while the induction coil is active and the reactant supply is delivering reactant to the reaction zone; anda second seal ...

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Номер записи: 70
17-10-2013 дата публикации

Process for Preparing R-1234yf By Base Mediated Dehydrohalogenation

Номер: US20130274528A1
Автор: Low Robert Elliott, McCarthy John Charles, Sharratt Andrew Paul
Принадлежит: MEXICHEM AMANCO HOLDING S.A. DE C.V.

The invention relates to a process for preparing 2,3,3,3-tetrafluoropropene (CFCF═CH), performed using the steps of dehydrohalogenating 1,1,1,2,2-pentafluoropropane (CHCFCF, HFC-245ca) 1,1,1,2-tetrafluoro-2-chloropropane, 1,1,1,2,3-pentafluoropropane (CHFCHFCF, HFC-245eb) and/or 1,1,1,2-tetrafluoro-3-chloropropane in the presence of a base, and converting a trifluorodichloropropane or a difluorotrichloropropane or a fluorotetrachloropropane to CHCFCF, 1,1,1,2-tetrafluoro-2-chloropropane, CHFCHFCF, and/or 1,1,1,2-tetrafluoro-3-chloropropane. 1. A process for preparing 2 ,3 ,3 ,3-tetrafluoropropene (CFCF═CH) , which process comprises{'sub': 3', '3', '3', '2, 'dehydrohalogenating a compound of formula CFCFYCHor CFCFHCYH, wherein Y is F, Cl, Br, or I, in the presence of a base selected from an alkali metal hydroxide and an alkaline earth metal hydroxide, wherein the process is carried out in the absence of a phase transfer catalyst.'}2. A process according to carried out at a temperature of from −50 to 300° C. and a pressure of from 0 to 30 bara.3. A process according to wherein the alkali metal hydroxide is selected from sodium hydroxide and potassium hydroxide.4. A process according to wherein the alkaline earth metal hydroxide is calcium hydroxide.5. A process according to wherein the process is carried out in a solvent.6. A process according to wherein the solvent is selected from water claim 5 , alcohols claim 5 , diols claim 5 , polyols claim 5 , polar aprotic solvents and mixtures thereof.7. A process according to wherein the solvent is water claim 6 , and wherein the process optionally is carried out in the presence of a co-solvent or diluent.8. A process according to wherein the solvent is carried out in a polar aprotic solvent selected from diglyme claim 6 , dimethylformamide (DMF) claim 6 , dioxane claim 6 , acetonitrile claim 6 , hexamethylphosphoramide (HMPA) and N-methylpyrrolidone (NMP).9. A process according to wherein CFCF═CHis prepared by{'sub': 3', '2 ...

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Номер записи: 71
24-10-2013 дата публикации

TITANIUM OXIDE PHOTOCATALYST HAVING COPPER COMPOUNDS SUPPORTED THEREON, AND METHOD FOR PRODUCING SAME

Номер: US20130281283A1
Автор: Hashimoto Kazuhito, Hosogi Yasuhiro, Kuroda Yasushi, Li Ding, Miyauchi Masahiro, Qiu Xiaoqing, SHIMODAIRA Yoshiki, Sunada Kayano
Принадлежит:

A copper compound-carried titanium oxide photocatalyst which is excellent in a photocatalytic activity and a viral inactivation property and a production process for the same can be provided by a copper compound-carried titanium oxide photocatalyst comprising titanium oxide in which a content of rutile type titanium oxide is 50% by mole or more and a monovalent copper compound and a divalent copper compound which are carried on a surface of the titanium oxide described above and a production process for a copper compound-carried titanium oxide photocatalyst, comprising a step of carrying a monovalent copper compound and a divalent copper compound on a surface of titanium oxide in which a content of rutile type titanium oxide is 50% by mole or more. 1. A copper compound-carried titanium oxide photocatalyst comprising titanium oxide in which a content of rutile type titanium oxide is 50% by mole or more and a monovalent copper compound and a divalent copper compound which are carried on a surface of the titanium oxide described above.2. The copper compound-carried titanium oxide photocatalyst according to claim 1 , wherein an abundance ratio of monovalent copper to a sum of monovalent copper and divalent copper is 20 to 70% by mole.3. The copper compound-carried titanium oxide photocatalyst according to claim 1 , wherein the monovalent copper compound contains copper (I) oxide.4. The copper compound-carried titanium oxide photocatalyst according to claim 1 , wherein the divalent copper compound contains copper (II) hydroxide.5. The copper compound-carried titanium oxide photocatalyst according to claim 1 , wherein the titanium oxide described above is obtained by a vapor phase method.6. A production process for a copper compound-carried titanium oxide photocatalyst claim 1 , comprising a step of carrying a monovalent copper compound and a divalent copper compound on a surface of titanium oxide in which a content of rutile type titanium oxide is 50% by mole or more.7. ...

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Номер записи: 72
24-10-2013 дата публикации

Nanocrystalline Copper Oxide and Method for the Production thereof

Номер: US20130281287A1
Автор: Grossmann Frank, HAGEMEYER Alfred, Wegner Oliver, Woelk Hans-Joerg
Принадлежит:

A nanocrystalline supported or unsupported copper oxide with a residual carbon content of <10% and a BET surface area >95 m/g. Further, a method for the production of a supported, or unsupported nanocrystalline copper oxide is disclosed, as well as the use thereof in catalysis, in particular in the steam reforming of methanol or in the hydrogenation of esters. 17-. (canceled)8. Method for the production of nanocrystalline copper oxide with a BET surface area >95 m/g comprising the steps ofa) the introduction of a copper starting compound into a reaction chamber by means of a :carrier fluid, and wherein the copper starting compound is introduced into the reaction chamber in the form of a solution, slurry, suspension or in solid aggregate state,b) a thermal treatment of the copper starting compound in a treatment zone of the reaction chamber by means of a pulsating flow at a temperature of from 200 to 500° C.,c) the formation of nanocrystalline copper oxide material,d) the discharge of the nanocrystalline copper oxide material obtained in steps b) and c) from the reactor wherein the nanocrystalline copper oxide has a primary particle size of from 4 nm to 20 nm for primary crystallites and a secondary particle size of from 20 nm to 100 nm for secondary crystallites.9. Method according to claim 8 , wherein the copper starting compound is used as suspension with an average particle sire of <10 μm.10. Method according to claim 8 , wherein the particle size is obtained by grinding the copper starting compound before the production of the suspension.11. Method according to claim 8 , wherein the copper starting compound is used as solution.12. Method according to claim 8 , wherein claim 8 , as copper starting compound claim 8 , a compound selected from the group consisting of a copper salt of an organic acid claim 8 , a hydroxide claim 8 , a nitrate claim 8 , a carbonate claim 8 , a hydroxocarbonate or mixtures thereof is used.13. Method according to claim 12 , wherein claim ...

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Номер записи: 73
24-10-2013 дата публикации

PROCESS FOR THE PREPARATION OF DICHLOROFULVENE

Номер: US20130281744A1
Автор: Faber Dominik, Hodges George Robert, ROBINSON ALAN JAMES, Shaw Andrew Charles
Принадлежит: SYNGENTA CROP PROTECTION LLC

The invention relates to a process for the preparation of formula (I) which process comprises pyrolysing a compound of formula (II) wherein X is chloro or bromo, and to compounds which may be used as intermediates for the manufacture of the compound of formula I and to the preparation of said intermediates. 2. A process according to claim 1 , wherein the compound of formula II is pyrolysed in a reactor at temperatures of 200 to 1000° C.3. A process according to claim 2 , wherein the compound of formula II is conveyed to the reactor in gaseous form.4. A process according to claim 3 , wherein the compound of formula II is conveyed to the reactor under continuous carrier gas flow.5. A process according to claim 4 , wherein the carrier gas is selected from nitrogen claim 4 , gaseous hydrogen chloride and gaseous xylene.6. A process according to claim 2 , wherein the product is transferred after the pyrolysis reaction from the outlet of the reactor into a trap containing an inert solvent.7. A process according to claim 2 , wherein the reactor and the vessel containing the compound of formula II is kept under reduced pressure.8. A process according to claim 1 , wherein X is chloro.11. A process for the preparation of the compound of formula I which process comprises pyrolysing a compound of formula IIIe according to .12. A process for the preparation of the compound of formula I which process comprises pyrolysing a compound of formula IIIf according to . The present invention relates to a process for the preparation of dichlorofulvene from a substituted cyclopentadiene and to compounds which may be used as intermediates for the manufacture of dichlorofulvene and to the preparation of said intermediates.Dichlorofulvene is an important intermediate for the preparation of fungicidally active carboxamides as described, for example, in WO 2007/048556.According to WO 2010/049228, dichlorofulvene can be prepared by reacting a compound of formula IIwherein X is chloro or bromo, ...

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Номер записи: 74
07-11-2013 дата публикации

COMPOSITIONS CONTAINING A COMBINATION OF Z AND E STEREOISOMERS OF HYDROFLUOROOLEFINS

Номер: US20130296617A1
Автор: Bonnet Philippe, Elsheikh Maher Y.
Принадлежит: Arkema Inc.

Disclosed are the combinations containing Z and E stereoisomers of hydrofluoroolefins where the more toxic isomer is less than about 30% weight of the combination (vs the sum of Z+E), to minimize the toxicity impact in the applications they will. be used for such as cooling and heat fluids, foams blowing agents or solvents. Also disclosed are means to obtain combinations containing Z and E stereoisomers of hydrofluoroolefins. 1. A method of preparing a combination of Z and E isomers of a hydrofluoroolefin comprising from a trace up to about 30% by weight of the E isomer from a combination having more than about 30% by weight of the E isomer comprising distillation of a combination of Z and E isomers of a hydrofluoroolefin having more than about 30% by weight of the E isomer.2. A method of preparing a combination of Z and E isomers of a hydrofluoroolefin comprising from a trace up to about 30% by weight of the E isomer from a combination having more than about 30% by weight of the E isomer comprising reactive distillation of a combination of Z and E isomers of a hydrofluoroolefin having more than about 30% by weight of the E isomer followed by distillation.3. A method of preparing a combination of Z and E isomers of a hydrofluoroolefin comprising from a trace up to about 30% by weight of the E isomer from a combination having more than about 30% by weight of the E isomer comprising isomerization in the presence of a catalyst of a combination of Z and E isomers of a hydrofluoroolefin having more than about 30% by weight of the E isomer.4. The methods of wherein said catalyst is selected from fluorinated alumina or activated carbon.5. The methods of wherein said isomerization takes place in the presence of a Lewis acid.6. A method of preparing a combination of Z and E isomers of a hydrofluoroolefin comprising from a trace up to about 30% by weight of the E isomer from a combination having more than about 30% by weight of the E isomer comprising extractive distillation ...

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Номер записи: 75
07-11-2013 дата публикации

PROCESS FOR THE SEPARATION OF CONTAMINANT OR MIXTURE OF CONTAMINANTS FROM A CH4- COMPRISING GASEOUS FEED STREAM

Номер: US20130296627A1
Автор: Tuinier Martin Jan, Van Sint Annaland Martin
Принадлежит:

The invention provides a process for the separation of a contaminant or mixture of contaminants from a CH-comprising gaseous feed stream, comprising the subsequent steps of: a) passing a CH-comprising gaseous feed stream comprising the contaminant or the mixture of contaminants into and through a cold porous body having a temperature below the sublimation temperature of the contaminant or the mixture of contaminants and contacting the CH-comprising gaseous feed stream at elevated pressure with the surface of the cold porous body to obtain a porous body comprising solid contaminant or mixture of contaminants and a contaminant-depleted product gas; and b) reducing the pressure to obtain fluid contaminant or mixture of contaminants and a cold porous body. c) removing the fluid contaminant or mixture of contaminants, wherein the contaminant is selected from CO, hydrogen sulphide, mercaptans, siloxanes and carbonyl sulphide, or a mixture thereof. 1. A process for the separation of a contaminant or mixture of contaminants from a CH-comprising gaseous feed stream , comprising the subsequent steps of:{'sub': 4', '4, 'a) passing a CH-comprising gaseous feed stream comprising the contaminant or the mixture of contaminants into and through a cold porous body having a temperature below the sublimation temperature of the contaminant or the mixture of contaminants and contacting the CH-comprising gaseous feed stream at elevated pressure with the surface of the cold porous body to obtain a porous body comprising solid contaminant or mixture of contaminants and a contaminant-depleted product gas; and'}b) reducing the pressure to obtain fluid contaminant or mixture of contaminants and a cold porous body.c) removing the fluid contaminant or mixture of contaminants,{'sub': '2', 'wherein the contaminant is selected from CO, hydrogen sulphide, mercaptans, siloxanes and carbonyl sulphide, or a mixture thereof.'}2. A process according to for the separation of COfrom a CH-comprising ...

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Номер записи: 76
14-11-2013 дата публикации

PROCESS FOR THE MANUFACTURE OF FLUORINATED OLEFINS

Номер: US20130303808A1
Автор: Tung Hsueh Sung, WANG HAIYOU
Принадлежит:

Provided are methods for producing fluorinated organic compounds, which preferably comprises converting at least one compound of formula (I) CHXCHZCFto at least one compound of formula (II) CHX═CZCFwhere X and Z are independently H or F, with the proviso that X and Z are not the same. The converting step comprises catalytically reacting at least one compound of formula (I), preferably via dehydrogenation or oxidative dehydrogenation. In another aspect, the inventive method of preparing fluorinated organic compounds comprises converting a reaction stream comprising at least one pentafluoropropene to a product stream comprising at least one pentafluoropropane and at least one compound of formula (I), separating out the compound of formula (I) from the product stream, and converting the compound of formula (I) separated from the product stream to at least one compound of formula (II), wherein the conversion the compound of formula (I) to 3,3,3-trifluoropropyne is substantially limited. 115.-. (canceled)17. The method of claim 16 , wherein said conditions are effective to substantially limit the concentration of 3 claim 16 ,3 claim 16 ,3-trifluoropropyne formed in said final product stream to less than about 100 parts per million.18. The method of claim 16 , wherein said conditions are effective to substantially limit the concentration of 3 claim 16 ,3 claim 16 ,3-trifluoropropyne formed in said final product stream to less than about 50 parts per million.19. The method of claim 16 , wherein said conditions are effective to substantially limit the concentration of 3 claim 16 ,3 claim 16 ,3-trifluoropropyne formed in said final product stream to less than about 20 parts per million.20. The method according to claim 16 , wherein said processing step comprises: {'br': None, 'sub': 2', '3, 'CHXCHZCF\u2003\u2003(I)'}, '(a) reacting said at least one pentafluoropropene to obtain a first product stream comprising at least one pentafluoropropane and at least one compound of ...

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Номер записи: 77
21-11-2013 дата публикации

METHODS FOR PRODUCING 1-CHLORO-3,3,3-TRIFLUOROPROPENE FROM 2-CHLORO-3,3,3-TRIFLUOROPROPENE

Номер: US20130310614A1
Автор: Tung Hsueh Sung, WANG HAIYOU
Принадлежит: HONEYWELL INTERNATIONAL INC.

The present invention provides processes for the production of HCFO-1233zd, 1-chloro-3,3,3-trifluoropropene, from the starting material, 2-chloro-3,3,3-trifluoropropene (HCFO-1233xf). In a first process, HCFO-1233zd is produced by the isomerization of HCFO-1233xf. In a second process, HCFO-1233zd is produced in a two-step procedure which includes (i) dehydrochlorination of HCFO-1233xf into trifluoropropyne; and (ii) hydrochlorination of the trifluoropropyne into HCFO-1233zd.

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Номер записи: 78
28-11-2013 дата публикации

COPOLYMERIZABLE SURFACTANTS

Номер: US20130317190A1
Автор: Busch Stefan, Held Uwe, Klagge Ronald, Mausberg Thomas, Scherer Markus, Schliwka Thomas
Принадлежит: Cognis IP Management GmbH

The invention relates to the use of compounds of the formula (I), R—CH(O—(AO)X)—CH—O—(AO)—CH—CH═CH, where: R denotes an alkyl radical which has 8 to 18 carbon atoms and can be saturated or unsaturated, straight-chain or branched; X denotes a sulfate or phosphate group or hydrogen; (AO) denotes an alkylene oxide unit, selected from the group consisting of ethylene oxide, propylene oxide or butylene oxide; n denotes a number in the range of 0 to 50; and m denotes zero or a number in the range of 1 to 30; as copolymerizable emulsifiers in the emulsion polymerization of olefinically unsaturated monomers. 3. The method of claim 2 , wherein X is a sulfate or phosphate group.4. The method of claim 3 , wherein the sulfate or phosphate group is in partly or wholly neutralized form.5. The method of claim 2 , wherein the degree of alkoxylation n is from 1 to 30.6. The method of claim 5 , wherein the degree of alkoxylation n is from 3 to 10 and (AO) is an ethylene oxide unit.7. A process for preparing a polymer by emulsion polymerization of an olefinically unsaturated monomer claim 1 , which process comprises utilizing said compound (I) according to as a copolymerizable emulsifier.8. The compound of claim 1 , wherein X is a sulfate or phosphate group.9. The compound of claim 8 , wherein the sulfate or phosphate group is in partly or wholly neutralized form.10. The compound of claim 1 , wherein the degree of alkoxylation n is from 1 to 30.11. The compound of claim 10 , wherein the degree of alkoxylation n is from 3 to 10 and (AO) is an ethylene oxide unit.12. The method of claim 2 , wherein the compound of formula (I) is copolymerized in the polymer.13. The method of claim 2 , further comprising initiating the reaction with potassium peroxodisulfate or a redox initiator.14. The method of claim 2 , wherein the compound of formula (I) is in salt form. The present invention lies within the polymer sector and relates to allyl ethers with a specific structure and also to their use as ...

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Номер записи: 79
28-11-2013 дата публикации

METHOD FOR PURIFYING 2,3,3,3-TETRAFLUOROPROPENE

Номер: US20130317262A1
Автор: KURASHIMA Kazuyoshi, Watanabe Kunio, Yamamoto Hiroshi
Принадлежит: Asahi Glass Company, Limited

To provide a method for purifying R-1234yf, whereby it is possible to efficiently remove even impurities such as R-1243zf, etc. which are difficult to separate by distillation purification, from a mixture containing R-1234yf as the main component and various impurities, such as a gas formed by reacting R-1214ya with hydrogen. The method for purifying R-1234yf comprises a step of bringing a mixture which contains R-1234yf as the main component and also contains hydrohaloalkene impurities other than R-1234yf and hydrohaloalkane impurities, into contact with a solvent that has an extraction/removal index (r), as represented by the formula r=[4×(δD−17.2)+(δP−8.3)+(δH−2.6)], of at most 6.5, so as to remove at least a part of the hydrohaloalkene impurities and hydrohaloalkane impurities. 2. The method for purifying 2 claim 1 ,3 claim 1 ,3 claim 1 ,3-tetrafluoropropene according to claim 1 , wherein the hydrohaloalkene impurities include a hydrohalopropene.3. The method for purifying 2 claim 1 ,3 claim 1 ,3 claim 1 ,3-tetrafluoropropene according to claim 1 , wherein the hydrohaloalkane impurities include at least one of a hydrohalopropane and a hydrohaloethane.4. The method for purifying 2 claim 1 ,3 claim 1 ,3 claim 1 ,3-tetrafluoropropene according to claim 1 , wherein at least a part of at least one member selected from the group consisting of 3 claim 1 ,3 claim 1 ,3-trifluoropropene claim 1 , 3 claim 1 ,3-difluoropropene and 1 claim 1 ,2 claim 1 ,3 claim 1 ,3 claim 1 ,3-pentafluoropropene claim 1 , as the hydrohaloalkene impurities claim 1 , is removed from the mixture.5. The method for purifying 2 claim 1 ,3 claim 1 ,3 claim 1 ,3-tetrafluoropropene according to claim 1 , wherein at least a part of 3 claim 1 ,3 claim 1 ,3-trifluoropropene claim 1 , as the hydrohaloalkene impurities claim 1 , is removed from the mixture.6. The method for purifying 2 claim 1 ,3 claim 1 ,3 claim 1 ,3-tetrafluoropropene according to claim 1 , wherein at least a part of at least one member ...

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Номер записи: 80
05-12-2013 дата публикации

POWER SUPPLY ARRANGEMENT WITH AN INVERTER FOR PRODUCING N-PHASE AC CURRENT

Номер: US20130323137A1
Автор: Averberg Andreas
Принадлежит: AEG Power Solutions B.V.

A power supply arrangement (MF) with an inverter () for generating N-phase AC current and at least one N-phase AC current transformer () having primary windings () and secondary windings (), wherein the primary windings () are connected in a polygon and a sum vector of the voltages present at the N secondary windings () becomes zero when the transformer is idling, wherein each vertex of the polygon formed by the primary windings () is connected via a corresponding capacitor (C C C) with a corresponding phase conductor terminal of the inverter (). 1. A power supply arrangement (MF)comprising{'b': 12', '2', '211', '212', '213', '221', '222', '223', '211', '212', '213', '221', '222', '223', '2, 'claim-text': [{'b': 211', '212', '213', '11', '12', '13, 'each vertex of the polygon formed by the primary windings (, , ) is connected via a corresponding capacitor (C, C, C) with a corresponding phase conductor terminal of the inverter,'}, {'b': 221', '222', '223', '221', '222', '223, 'the voltage across at least N−1 secondary windings (, , ) is discretely or continuously adjustable, and/or capacitors are provided in series with the secondary windings (, , ), wherein at least N−1 of the capacitors have an adjustable capacitance.'}], 'an inverter () for generating N-phase AC current and at least one N-phase AC current transformer () having primary windings (, , ) and secondary windings (, , ), wherein the primary windings (, , ) are connected in a polygon and a vector sum of the voltages present at the N secondary windings (, , ) becomes zero when the transformer () is idling, wherein'}2221222223. The power supply arrangement (MF) according to claim 1 , wherein the outputs of the power supply arrangement (MF) are arranged parallel to the secondary windings ( claim 1 , claim 1 , ).3221222223212223. The power supply arrangement (MF) according to claim 2 , wherein the outputs of the power supply arrangement (MF) are arranged parallel to series-connected circuits claim 2 , with ...

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Номер записи: 81
05-12-2013 дата публикации

Process for preparing styrene derivatives

Номер: US20130324745A1
Автор: Axel VON WANGELIN JACOBI, Bernd Wilhelm Lehnemann, Matthias Gotta, Samet GUELAK
Принадлежит: Saltigo GmbH

A process is provided which allows the synthesis of a large number of styrene derivatives with formation of C—C bonds, with use being possible of economically advantageous substrates, readily available carbon nucleophiles, and both inexpensive and environmentally unproblematic catalyst systems, permitting reaction under mild conditions and a high compatibility with functional groups on the reactants involved.

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Номер записи: 82
12-12-2013 дата публикации

CYCLOPROPYL PIDA BORONATE

Номер: US20130331585A1
Автор: Burke Michael D., Duncton Matthew
Принадлежит:

Provided are protected cyclopropylboronic acids that include a substituted cyclopropyl group and a boronic ester group having a protecting group. The protecting group is a pinene-derived iminodiacetic acid (PIDA) group or PIDA-based group. 2. The protected organoboronic acid of claim 1 , wherein Ris homochiral.3. The protected organoboronic acid of claim 1 , wherein Ris substituted cycloalkyl.4. The protected organoboronic acid of claim 1 , wherein Ris isopinocampheyl.5. The protected organoboronic acid of claim 1 , wherein one of R claim 1 , R claim 1 , R claim 1 , and Ris substituted alkyl and the others are hydrogen.6. The protected organoboronic acid of claim 1 , wherein one of R claim 1 , R claim 1 , R claim 1 , and Ris trifluoromethyl and the others are hydrogen.8. The protected organoboronic acid of claim 7 , wherein Ris substituted cycloalkyl.9. The protected organoboronic acid of claim 7 , wherein Ris isopinocampheyl.10. The protected organoboronic acid of claim 7 , wherein one of Rand Ris substituted alkyl.11. The protected organoboronic acid of claim 7 , wherein one of Rand Ris trifluoromethyl.13. The protected organoboronic acid of claim 12 , wherein Ris substituted cycloalkyl.14. The protected organoboronic acid of claim 12 , wherein Ris isopinocampheyl.15. The protected organoboronic acid of claim 12 , wherein Ris substituted alkyl.16. The protected organoboronic acid of claim 12 , wherein Ris trifluoromethyl.17. The protected organoboronic acid of claim 12 , wherein the protected organoboronic acid has a trans stereochemistry with respect to the cyclopropyl ring.19. The protected organoboronic acid of claim 18 , wherein the protected organoboronic acid has a trans stereochemistry with respect to the cyclopropyl ring.21. The method of claim 20 , wherein Ris substituted cycloalkyl.22. The method of claim 20 , wherein Ris isopinocampheyl.23. The method of claim 20 , wherein one of R claim 20 , R claim 20 , R claim 20 , and Ris substituted alkyl and the ...

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Номер записи: 83
19-12-2013 дата публикации

PROCESS FOR SEPARATING HYDROGEN FLUORIDE FROM ORGANIC FEEDSTOCKS

Номер: US20130338408A1
Автор: Merkel Daniel C., Pokrovski Konstantin A., TUNG HSUEH S.
Принадлежит: HONEYWELL INTERNATIONAL INC.

Provided is a process for purifying an organic feedstock comprising (a) distilling a raw organic feedstock comprising hydrogen fluoride, 2-chloro-1,1,1,2-tetrafluoropropane, and 2-chloro-3,3,3-trifluoropropene to produce a first distillate stream comprising an azeotrope-like composition of 2-chloro-1,1,1,2-tetrafluoropropane, 2-chloro-3,3,3-trifluoropropene, and hydrogen fluoride, and a first bottoms stream rich in hydrogen fluoride; (b) cooling said first distillate stream to produce an intermediate composition comprising an organic layer rich in 2-chloro-1,1,1,2-tetrafluoropropane and 2-chloro-3,3,3-trifluoropropene, and an acid layer rich in hydrogen fluoride; and, optionally but preferably, (c) distilling said organic layer to produce a second distillate stream comprising an azeotrope-like composition of 2-chloro-1,1,1,2-tetrafluoropropane, 2-chloro-3,3,3-trifluoropropene, and hydrogen fluoride, and a second bottoms stream comprising a purified organic feedstock substantially free of hydrogen fluoride. 117-. (canceled)18. A process for producing 2 ,3 ,3 ,3-tetrafluoropropene comprising:a. reacting 2-chloro-3,3,3-trifluoropropene with hydrogen fluoride to produce a crude product stream comprising 2-chloro-1,1,1,2-tetrafluoropropane, hydrogen fluoride, and 2-chloro-3,3,3-trifluoropropene;b. distilling said crude product stream to produce a first distillate stream comprising an azeotrope-like composition of 2-chloro-1,1,1,2-tetrafluoropropane, 2-chloro-3,3,3-trifluoropropene, and hydrogen fluoride, and a first bottoms stream rich in hydrogen fluoride;c. cooling said distillate stream to produce a first intermediate composition comprising an organic layer rich in 2-chloro-1,1,1,2-tetrafluoropropane and 2-chloro-3,3,3-trifluoropropene, and an acid layer rich in hydrogen fluoride;d. distilling said organic layer to produce a second distillate stream comprising an azeotrope-like composition of 2-chloro-1,1,1,2-tetrafluoropropane, 2-chloro-3,3,3-trifluoropropene, and ...

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Номер записи: 84
02-01-2014 дата публикации

Method for Production of 1-Chloro-3,3,3-Trifluoropropene

Номер: US20140005446A1
Автор: IMURA Hideaki, Takada Naoto
Принадлежит: CENTRAL GLASS COMPANY, LIMITED

A production method of 1-chloro-3,3,3-trifluoropropene according to the present invention includes bringing a composition containing a compound of the general formula (1): CF—CH—CHClX (where X is a fluorine atom or a chlorine atom) into contact with a solid catalyst in the presence of hydrogen chloride. In this production method, the composition containing ozone depleting HCFC such as 3-chloro-1,1,1,3-tetraluoforpropane or 3,3-dichloro-1,1,1-trifluoropropane can be efficiently converted to the 1-chloro-3,3,3-trifluoropropene, which has less influence on the global environment and is useful as a solvent, a cleaning agent, a coolant, a working fluid, a propellant, a raw material for fluorinated resins etc. 2. The production method according to claim 1 , wherein the compound of the general formula (1) is CF—CH—CHClF.3. The production method according to claim 1 , wherein the solid catalyst contains a metal fluoride or metal chloride having a bond of the formula: M-X (where M is at least one metal atom selected from the group consisting of those of atomic number 13 and atomic numbers 22 to 78; and X is a fluorine atom or a chlorine atom).4. The production method according to claim 1 , wherein the solid catalyst contains at least one metal oxide selected from the group consisting of alumina claim 1 , titania claim 1 , zirconia and niobia.5. The production method according to claim 1 , wherein the solid catalyst has been treated in advance by contact with hydrogen fluoride.6. The production method according to 1 claim 1 , wherein the 1 claim 1 ,3 claim 1 ,3 claim 1 ,3-trifluoropropene is produced from 1 claim 1 ,1 claim 1 ,1 claim 1 ,3 claim 1 ,3-pentachloropropane by the following steps:forming a first composition containing the compound of the general formula (1) and hydrogen chloride by contact reaction of the 1,1,1,3,3-pentachloropropane and hydrogen chloride;recovering the hydrogen chloride from the first composition; andbringing a second composition containing the ...

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Номер записи: 85
02-01-2014 дата публикации

Method for Production of 1-Chloro-3,3,3-Trifluoropropene

Номер: US20140005447A1
Автор: IMURA Hideaki, OKAMOTO Masamune, Takada Naoto
Принадлежит: CENTRAL GLASS COMPANY, LIMITED

A production method of 1-chloro-3,3,3-trifluoropropene according to the present invention includes bringing a raw material composition containing 1,3,3,3-tetrafluoropropene and an acid composition containing hydrogen chloride into contact with each other in gas phase in the presence of a catalyst. This production method allows not only use of hydrogen chloride containing hydrogen fluoride, which has been generated during a preceding step (production of 1,1,1,3,3-pentafluoropropane as a raw material or analogues thereof), but also use of any of trans and cis isomers of the 1,1,1,3,3-pentafluoropropane for production of the 1-chloro-3,3,3-trifluoropropene. It is thus possible to efficiently produce the 1-chloro-3,3,3-trifluoropropene, which is known as an environment-adaptive chlorofluorocarbon. As the catalyst, preferred is an alumina catalyst treated by contact with hydrogen fluoride. 1. A production method of 1-chloro-3 ,3 ,3-trifluoropropene , comprising bringing a raw material composition containing 1 ,3 ,3 ,3-tetrafluoropropene and an acid composition containing hydrogen chloride into contact with each other in gas phase in the presence of a catalyst.2. The production method according to claim 1 , wherein the raw material composition further contains 1 claim 1 ,1 claim 1 ,1 claim 1 ,3 claim 1 ,3-pentafluoropropane.3. The production method according to claim 1 , wherein the 1 claim 1 ,3 claim 1 ,3 claim 1 ,3-tetrafluoropropene is obtained by fluorination of 1 claim 1 ,1 claim 1 ,1 claim 1 ,3 claim 1 ,3-pentachloropropane.4. The production method according to claim 1 , wherein the catalyst is a catalyst having a bond of the formula: M-X where M is at least one kind of metal atom selected from the group consisting of aluminium (Al) claim 1 , titanium (Ti) claim 1 , iron (Fe) claim 1 , cobalt (Co) claim 1 , antimony (Sb) claim 1 , tin (Sn) claim 1 , tungsten (W) claim 1 , niobium (Nb) claim 1 , chromium (Cr) claim 1 , and zirconium (Zr); and X is at least one kind ...

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Номер записи: 86
09-01-2014 дата публикации

Catalytic or photocatalytic preparation method of parylene af4

Номер: US20140011986A1
Автор: Chien-Yi Sun, Chun-Hsu Lin, Chun-Shih LI, Yo-Chun CHOU, Yung-Yu Yin
Принадлежит: YUAN-SHIN MATERIALS TECHNOLOGY CORP

The present invention disclosed a preparation method of parylene AF4, which provides a reactant and a reducing agent with the use of catalyst or exposure to UV light with photo-initiator, to shorten the reaction time as a result of minimized the byproduct(s) formation, and obtain high purity (>99.0%) of parylene AF4 product under high concentrated reaction mixture.

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Номер записи: 87
09-01-2014 дата публикации

PROCESS TO MANUFACTURE 2-CHLORO-1,1,1,2-TETRAFLUOROPROPANE (HCFC-244bb)

Номер: US20140012047A1
Автор: Cottrell Stephen A., Johnson Robert C., Merkel Daniel C.
Принадлежит: HONEYWELL INTERNATIONAL INC.

The invention provides an improved process to manufacture 2-chloro-1,1,1,2-tetrafluoropropane (HCFC-244bb) by reacting 2-chloro-3,3,3,-trifluoropropene (HCFO-1233xf) with hydrogen fluoride, in a liquid phase reaction in the presence of hydrogen chloride and a liquid phase fluorination catalyst. The hydrogen chloride is added into the reaction from an external source at a pressure of about 100 psig or more. The HCFC-244bb is an intermediate in the production of 2,3,3,3-tetrafluoropropene-1 (HFO-1234yf). 1. A process for the production of 2-chloro-1 ,1 ,1 ,2-tetrafluoropropane which comprises reacting 2-chloro-3 ,3 ,3 ,-trifluoropropene with hydrogen fluoride , in a liquid phase reaction in the presence of hydrogen chloride and a liquid phase fluorination catalyst , wherein the hydrogen chloride is added into the reaction from an external source at a pressure of about 100 psig or more.2. The process of wherein the reacting is conducted in a liquid phase reaction vessel.3. The process of wherein the reacting is conducted continuously.4. The process of wherein the mole ratio of hydrogen fluoride to 2-chloro-3 claim 1 ,3 claim 1 ,3-trifluoropropene fed to the reaction ranges from at least 1:1 to about 50:1.5. The process of wherein the mole ratio of hydrogen chloride to 2-choro-3 claim 1 ,3 claim 1 ,3-trifluoropropene fed to the reaction ranges from at least 0.1:1 to about 10:1.6. The process of wherein the liquid phase fluorination catalyst comprises SbCl claim 1 , SbCl claim 1 , SbF claim 1 , SnCl claim 1 , TaCl claim 1 , TiCl claim 1 , NbCl claim 1 , MoCl claim 1 , FeCl claim 1 , CrF claim 1 , Cr2O3 claim 1 , a fluorinated species of SbCl claim 1 , a fluorinated species of SbCl claim 1 , a fluorinated species of SnCl claim 1 , a fluorinated species of TaCl claim 1 , a fluorinated species of TiCl claim 1 , a fluorinated species of NbCl claim 1 , a fluorinated species of MoCl claim 1 , a fluorinated species of FeCl claim 1 , a fluorinated species of CrO claim 1 , or ...

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Номер записи: 88
09-01-2014 дата публикации

PROCESSES FOR SELECTIVE DEHYDROHALOGENATION OF HALOGENATED ALKANES

Номер: US20140012049A1
Автор: MUKHOPADHYAY SUDIP, Tung Hsueh Sung, WANG HAIYOU
Принадлежит: HONEYWELL INTERNATIONAL INC.

Disclosed are processes for producing halogenated olefins, and preferably tetrafluorinated propene(s), from one or more alkanes having both fluorine substituents and non-fluorine substituents, preferably with a high degree of conversion and selectivity. Preferably the process comprises the use of a catalyzed reaction in which the catalyst is selected from the group consisting of activated carbons, halogentated mono- and di-valent metal oxides, mono- and di-valent Lewis acid metal halides, zero-valent metals, and combinations of these. 1. A process for the production fluorinated olefin having from three to six carbon atoms , the process comprising exposing a fluorinated and chlorinated alkane having from two to six carbon atoms and a degree of non-fluorine halogen substitution of N and a degree of fluorine substitution of M to conditions effective to convert at least about 20% by weight of said alkane to one or more olefins having a degree of non-fluorine halogen substitution of a N−1 and a degree of fluorine substitution of M.2. The process of wherein said fluorinated olefins has the same number of carbon atoms as said alkane.3. (canceled)4. (canceled)5. (canceled)6. (canceled)9. (canceled)10. (canceled)11. The process of wherein said exposing step comprises conditions effective to convert at least about 70% by weight of said compounds of Formula (I) to one or more compounds of Formula (II).12. The process of wherein said exposing step comprises conditions effective to convert at least about 80% by weight of said compounds of Formula (I) to one or more compounds of Formula (II).13. The process of wherein said exposing step comprises conditions effective to convert at least about 90% by weight of said compounds of Formula (I) to one or more compounds of Formula (II).14. (canceled)15. The process of wherein said fluorinated olefin having a degree of substitution of N+1 comprises hexafluorpropene.16. The process of wherein said fluorinated olefin having a degree of ...

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Номер записи: 89
09-01-2014 дата публикации

Process for the Preparation of 2,3,3,3,-Tetrafluoropropene (R-1234yf)

Номер: US20140012050A1
Автор: McGuiness Claire, Sharratt Andrew P., Smith John W.
Принадлежит: MEXICHEM AMANCO HOLDING S.A. DE C.V.

The invention provides a process for the preparation of 2,3,3,3-tetrafluoropropene (1234yf) comprising (a) contacting 1,1,1-trifluoro-2,3-difluoropropane (243db) with hydrogen fluoride (HF) in the presence of a zinc/chromia catalyst to produce a compound having the formula CFCHFCHX, wherein X is Cl or F, and (b) dehydrohalogenating the compound of formula CFCHFCHX to produce 1234yf. 1. A process for preparing 1234yf , the process comprising:{'sub': '4', '(i) telomerising ethylene and carbon tetrachloride (CCl) to produce 1,1,1,3-tetrachloropropane;'}(ii) converting 1,1,1,3-tetrachloropropane (250fb) to 3,3,3-trifluoropropene (1243zf);{'sub': 3', '2, '(iii) contacting 1243zf with a compound of formula AB to produce a compound of formula CFCHACHB, wherein A and B represent, independently, H, F, Cl, Br or I, provided that A and B are not both H or F;'}{'sub': 3', '2', '3', '2, '(iv) contacting the compound of formula CFCHACHB with hydrogen fluoride (HF) in the presence of a zinc/chromia catalyst to produce a compound having the formula CFCHFCHX, wherein X is Cl or F; and'}{'sub': 3', '2, '(v) dehydrohalogenating the compound of formula CFCHFCHX to produce 1234yf.'}2. A process according to wherein step (i) comprises contacting ethylene with CClin the liquid and/or vapour phase in the presence of a catalyst in an amount of from about 0.01 to about 50 mol %.3. A process according to wherein step (i) the catalyst comprises iron claim 2 , copper and/or peroxide.4. A process according to wherein step (i) the molar ratio of CCl:ethylene is from about 1:1 to about 50:1.5. A process according to wherein step (i) is conducted at a temperature of from about 20 to about 300° C. and a pressure of from 0 to about 40 bara.6. A process according to wherein the 250fb is purified before conversion to 1243zf.7. A process according to wherein step (ii) comprises fluorination of 250fb to produce a compound of formula CFCHCHCl (253fb) claim 1 , followed by dehydrohalogenation of the 253fb ...

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Номер записи: 90
09-01-2014 дата публикации

AZEOTROPE-LIKE COMPOSITION OF 2-CHLORO-3,3,3-TRIFLUOROPROPENE (HCFC-1233XF) AND HYDROGEN FLUORIDE (HF)

Номер: US20140012052A1
Автор: Merkel Daniel C., Pham Hang T., Pokrovski Konstantin A., SINGH Rajiv R., TUNG HSUEH S.
Принадлежит: HONEYWELL INTERNATIONAL INC.

Provided are azeotropic and azeotrope-like compositions of 2-chloro-3,3,3-trifluoropropene (HCFO-1233xf) and hydrogen fluoride (HF). Such azeotropic and azeotrope-like compositions are useful as intermediates in the production of 2,3,3,3-tetrafluoropropene (HFO-1234yf). 112-. (canceled)13. A method of forming an azeotropic or azeotrope-like composition which comprises forming a blend consisting essentially of from about 6.2 mole percent to about 90.7 mole percent hydrogen fluoride and from about 9.3 mole percent to about 93.8 mole percent 2-chloro-3 ,3 ,3-trifluoropropene to thereby form an azeotropic or azeotrope-like composition having a boiling point of from about 0° C. to about 61° C. at a pressure of from about 15 psia to about 107 psia.14. The method of wherein the composition consists of hydrogen fluoride and 2-chloro-3 claim 13 ,3 claim 13 ,3-trifluoropropene.15. The method of wherein the hydrogen fluoride in present in an amount of from about 15 to about 50 weight percent.16. The method of wherein the 2-chloro-3 claim 13 ,3 claim 13 ,3-trifluoropropene is present in the amount from about 50 to about 85 weight percent.17. The method of wherein the composition has a boiling point of about 0° C. at a pressure of about 15 psia; or a boiling point of from about 25° C. at a pressure of about 38 psia; or a boiling point of about 61° C. at a pressure of about 107 psia.18. The method of further comprising the step of separating 2-chloro-3 claim 13 ,3 claim 13 ,3-trifluoropropene from an azeotropic or azeotrope-like composition of 2-chloro-3 claim 13 ,3 claim 13 ,3-trifluoropropene and hydrogen fluoride using pressure swing distillation.19. The method of further comprising the step of feeding the azeotropic or azeotrope-like composition of 2-chloro-3 claim 13 ,3 claim 13 ,3-trifluoropropene and hydrogen fluoride to a fluorination reactor as a source of hydrogen fluoride.20. A method for removing 2-chloro-3 claim 13 ,3 claim 13 ,3-trifluoropropene from a mixture ...

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Номер записи: 91
16-01-2014 дата публикации

PROCESS FOR THE REDUCTION OF RfCCX IMPURITIES IN FLUOROOLEFINS

Номер: US20140018582A1
Автор: Mario Joseph Nappa, Xuehui Sun
Принадлежит: EI Du Pont de Nemours and Co

The present disclosure relates to processes for reducing the concentration of R f C≡CX impurities in fluoroolefins. The process involves: contacting a mixture comprising at least one fluoroolefin and at least one R f C≡CX impurity with at least one amine to reduce the concentration of the at least one R f C≡CX impurity in the mixture; wherein R f is a perfluorinated alkyl group, and X is H, F, Cl, Br or I. The present disclosure also relates to processes for making at least one hydrotetrafluoropropene product selected from the group consisting of CF 3 CF═CH 2 , CF 3 CH═CHF, and mixtures thereof and reducing the concentration of CF 3 C═CH impurity generated during the process. The present disclosure also relates to processes for making at least one hydrochlorotrifluoropropene product selected from the group consisting of CF 3 CCl═CH 2 , CF 3 CH═CHCl, and mixtures thereof and reducing the concentration of CF 3 C≡CH impurity generated during the process.

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Номер записи: 92
23-01-2014 дата публикации

HYDRO(CHLORO)FLUOROOLEFINS AND METHOD FOR PREPARATION THEREOF

Номер: US20140024864A1
Автор: Dubois Jean-Luc
Принадлежит: Arkema France

A subject of the invention is a compound of formula (I) XCFRin which: in which X represents a branched or linear unsaturated hydrocarbon radical having up to 5 carbon atoms, unsubstituted or substituted, R represents Cl, F, Br, I or H, Z is equal to 1, 2 or 3, and the bio-carbon content of which is at least 1%. 122-. (canceled)23. A process for preparation of a compound of formula (I) ,{'br': None, 'sub': z', '3-z, 'XCFR\u2003\u2003(I),'} X is a substituted or unsubstituted, linear or branched, unsaturated hydrocarbon radical having up to 5 carbon atoms,', 'each R is independently Cl, F, Br, I or H, and', 'z is equal to 1, 2, or 3;, 'wherein providing a carbon-containing chain derived from alcohol produced from a biomass, and', 'converting said chain to said compound of formula (I)., 'said process comprising the steps of24. The process according to claim 23 , wherein said alcohol is methanol claim 23 , ethanol claim 23 , n-propanol claim 23 , or n-butanol.25. The process according to claim 23 , wherein said alcohol is produced by fermentation of said biomass.26. The process according to claim 23 , wherein said alcohol is produced by:i) producing methane from said biomass,ii) steam reforming said methane to a synthesis gas, or producing a synthesis gas by direct gasification of said biomass, andiii) producing said alcohol from said synthesis gas.27. The process according to claim 23 , wherein said alcohol is produced by:i) producing methane from said biomass, andii) directly oxidizing said methane to methanol.28. The process according to claim 23 , wherein said step of providing said carbon-containing chain comprises the step of converting said alcohol to an olefin.29. The process according to claim 28 , wherein said step of converting said alcohol to an olefin comprises converting methanol to DME and dehydrating the DME to said olefin.30. The process according to claim 23 , wherein said step of providing said carbon-containing chain comprises the step of converting ...

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Номер записи: 93
30-01-2014 дата публикации

Process for Preparing C3-6(Hydro)Fluoroalkenes by Dehydrohalogenating C3-6 Halo(Hydro)Fluoroalkanes in the Presence of a Zinc/Chromia Catalyst

Номер: US20140031596A1
Автор: Seddon Leslie Richard, Sharratt Andrew Paul
Принадлежит: MEXICHEM AMANCO HOLDING S.A. DE C.V.

The invention relates to a process for preparing a C3-6 (hydro)fluoroalkene comprising dehydrohalogenating a C3-6 hydro(halo)fluoroalkane in the presence of a zinc/chromia catalyst, wherein the C3-6 (hydro)fluoroalkene produced is isomerised in the presence of the zinc/chromia catalyst. 1. A process for preparing a C(hydro)fluoroalkene comprising dehydrohalogenating a Chydro(halo)fluoroalkane in the presence of a zinc/chromia catalyst , wherein the C(hydro)fluoroalkene produced is isomerised in the presence of the zinc/chromia catalyst.2. A process according to wherein the C(hydro)fluoroalkene exists in E and Z isomers claim 1 , and the ratio of E and Z isomers is changed in the presence of the zinc/chromia catalyst.3. A process according to wherein the presence of the zinc/chromia catalyst changes the ratio of E and Z isomers from that which is the kinematic determined mixture of isomers from the preparation of the C(hydro)fluoroalkene.4. A process according to wherein a desired isomer of the C(hydro)fluoroalkene is recovered in a subsequent step.5. A process according to carried out at a temperature of from −70 to 400° C. and a pressure of from 0 to 30 bara.6. A process according to for preparing a (hydro)fluoropropene comprising dehydrohalogenating a hydro(halo)fluoropropane.7. A process according to wherein the (hydro)fluoropropene produced is selected from tetrafluoropropenes and pentafluoropropenes.8. A process according for preparing 1 claim 7 ,2 claim 7 ,3 claim 7 ,3 claim 7 ,3-pentafluoropropene (CFCF═CHF).9. A process according to for preparing 1 claim 7 ,3 claim 7 ,3 claim 7 ,3-tetrafluoropropene (CFCH═CHF).10. A process according to for preparing 2 claim 7 ,3 claim 7 ,3 claim 7 ,3-tetrafluoropropene (CFCF═CH) and 1 claim 7 ,2 claim 7 ,3 claim 7 ,3 claim 7 ,3-pentafluoropropene (CFCF═CHF).11. A process according to for preparing 2 claim 7 ,3 claim 7 ,3 claim 7 ,3-tetrafluoropropene (CFCF═CH) and 1 claim 7 ,3 claim 7 ,3 claim 7 ,3-tetrafluoropropene (CFCH═ ...

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Номер записи: 94
30-01-2014 дата публикации

PROCESS FOR THE MANUFACTURE OF 2,3,3,3-TETRAFLUOROPROPENE BY GAS PHASE FLUORINATION OF PENTACHLOROPROPANE

Номер: US20140031597A1
Автор: Deur-Bert Dominique, Doucet Nicolas, Pigamo Anne, Wendlinger Laurent
Принадлежит:

The present invention provides a process of catalytic fluorination in gas phase of product 1,1,1,2,3-pentachloropropane or/and 1,1,2,2,3-pentachloropropane into product 2,3,3,3-tetrafluoropropene in presence of a catalyst. 122-. (canceled)23. A process of producing 2 ,3 ,3 ,3-tetrafluoropropene comprising contacting 1 ,1 ,1 ,2 ,3-pentachloropropane and/or 1 ,1 ,2 ,2 ,3-pentachloropropane with hydrogen fluoride in gas phase in the presence of a fluorination catalyst to produce 2 ,3 ,3 ,3-tetrafluoropropene.24. Process according to claim 23 , carried out in a single stage.25. Process according to claim 23 , wherein the product 2 claim 23 ,3 claim 23 ,3 claim 23 ,3-tetrafluoropropene is present at a concentration of at least 1%.26. Process of claim 23 , wherein said catalyst is a chromium catalyst.27. Process of claim 26 , wherein said catalyst further comprises a co-catalyst selected from the group consisting of Ni claim 26 , Co claim 26 , Zn claim 26 , Mn claim 26 , Mg and mixtures thereof claim 26 , and wherein said co-catalyst is present in an amount from about 1-10 wt % of said fluorination catalyst.28. Process of claim 23 , carried out in the presence of a catalyst comprising Ni—Cr.29. Process of claim 23 , wherein said catalyst is supported on a support comprising fluorinated alumina claim 23 , fluorinated chromia claim 23 , fluorinated activated carbon or graphite carbon.30. Process of claim 23 , wherein the fluorination catalyst is activated with a fluorine-containing compound.31. Process of claim 23 , in which the 1 claim 23 ,1 claim 23 ,1 claim 23 ,2 claim 23 ,3-pentachloropropane contains up to 40 mol % of isomer 1 claim 23 ,1 claim 23 ,2 claim 23 ,2 claim 23 ,3-pentachloropropane.32. Process of claim 23 , which is carried out at a pressure from 3 to 20 bars.33. Process of claim 23 , carried out at a temperature of from 200 to 450° C.34. Process of claim 23 , carried out with a contact time from 6 to 100 sec.35. Process of claim 23 , carried out with a ...

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Номер записи: 95
06-02-2014 дата публикации

CATALYTIC GAS PHASE FLUORINATION

Номер: US20140039228A1
Автор: Doucet Nicolas, Pigamo Anne, Wendlinger Laurent
Принадлежит:

The present invention relates to a fluorination process, comprising: 120-. (canceled)21. A fluorination process , comprising:an activation stage comprising contacting a fluorination catalyst with an oxidizing agent-containing gas flow for at least one hour; andat least one reaction stage comprising reacting a chlorinated compound with hydrogen fluoride in gas phase in the presence of the fluorination catalyst, so as to produce a fluorinated compound.22. The process of claim 21 , further comprising a plurality of reaction stages alternating with a plurality of regeneration stages claim 21 , wherein the plurality of reaction stages comprise reacting the chlorinated compound with hydrogen fluoride in gas phase in the presence of the fluorination catalyst claim 21 , and the plurality of regeneration stages comprise contacting the fluorination catalyst with an oxidizing agent-containing gas flow.23. The process of claim 22 , wherein the oxidizing agent-containing gas flow of the activation stage and/or the regeneration stages is an oxygen-containing gas flow.24. The process of claim 22 , wherein the activation stage and/or the regeneration stages comprise contacting the fluorination catalyst with the oxidizing agent-containing gas flow for at least 2 hours.25. The process of claim 22 , wherein the oxidizing agent-containing gas flow of the activation stage and/or the regeneration stages contains hydrogen fluoride in addition to the oxidizing agent claim 22 , and wherein the proportion of oxidizing agent in the oxidizing agent-containing gas flow of the activation stage and/or the regeneration stages is preferably from 2 to 98 mol % relative to the total amount oxidizing agent and hydrogen fluoride.26. The process of claim 22 , wherein the oxidizing agent-containing gas flow of the activation stage and/or the regeneration stages does not contain hydrogen fluoride.27. The process of claim 26 , wherein the oxidizing agent-containing gas flow of the activation stage and/or ...

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Номер записи: 96
20-02-2014 дата публикации

METHOD AND ARRANGEMENT FOR GENERATING OXYGEN

Номер: US20140048409A1
Автор: Hilbig Rainer, Keur Wilhelmus Cornelis, Klee Mareike, Koerber Achim Gerhard Rolf
Принадлежит: KONINKLIJKE PHILIPS N.V.

The present invention relates to a method of generating oxygen. The method addresses the objects of reducing the servicing work and improving the purity of the generated oxygen. According to the invention, the method comprises the steps of: providing an oxygen comprising gas at a primary side of a dense voltage drivable membrane (); applying a voltage between a conductive element at the primary side of the membrane () and a conductive element at a secondary side of the membrane (), the conductive elements being electrically connected to the membrane (), wherein a plasma () is generated at at least one of the primary side and the secondary side of the membrane (), the plasma () being used as conductive element. 1. Method of generating oxygen , said method comprising the steps of:{'b': '12', 'providing an oxygen comprising gas at a primary side of a dense voltage drivable membrane ();'}{'b': 12', '12', '12, 'claim-text': {'b': 18', '20', '12', '18', '20', '12', '12, 'a plasma (, ) is generated at at least one of the primary side and the secondary side of the membrane (), the plasma (, ) being used as the conductive element at the primary side of the membrane () and/or as the conductive element at the secondary side of the membrane ().'}, 'applying a voltage between a conductive element at the primary side of the membrane () and a conductive element at a secondary side of the membrane (), the conductive elements being electrically connected to the membrane (), wherein'}2182012. Method according to claim 1 , wherein the plasma ( claim 1 , ) is generated both at the primary side and the secondary side of the membrane ().31820. Method according to claim 1 , wherein the plasma ( claim 1 , ) is generated to provide a charge carrier density in the range of ≦1×10.412. Method according to claim 1 , wherein the membrane () is heated to a temperature in the range of ≧500° C. to ≦700° C.51820. Method according to claim 1 , wherein the plasma ( claim 1 , ) is generated by applying ...

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Номер записи: 97
20-02-2014 дата публикации

DEVICE FOR TREATING GASES USING SURFACE PLASMA

Номер: US20140050631A1
Автор: BEDEL Laurent, JOUVE Michel
Принадлежит: Commissariat A L'Energie Atomique Et Aux Energies Alternatives

A device for treating gases using surface plasma, including: 2. The device for treating gases by means of a surface plasma of claim 1 , wherein the first and the second electrodes are arranged so that an inter-electrode distance is in the range between 2 and 15 mm claim 1 , advantageously between 4 and 8 mm.3. The device for treating gases by means of a surface plasma of claim 1 , wherein the first and second electrodes each have a width in the range between 1 mm and 10 cm claim 1 , advantageously between 3 and 5 mm.4. The device for treating gases by means of a surface plasma of claim 1 , wherein the catalytic support is selected from the group comprising a wafer of dense material and a metal or ceramic foam.5. The device for treating gases by means of a surface plasma of claim 1 , wherein the catalytic support appears in the form of a metal or ceramic honeycomb.6. The device for treating gases by means of a surface plasma of claim 1 , wherein the catalytic support has a thickness in the range between 1 mm and 10 cm.7. The device for treating gases by means of a surface plasma of claim 1 , wherein the catalytic support comprises a catalyst selected from the group comprising metal oxides claim 1 , nitrides claim 1 , metals claim 1 , and mixtures thereof.8. The device for treating gases by means of a surface plasma of claim 7 , wherein the metal claim 7 , the metal oxide claim 7 , or the nitride are based on a metal selected from the group comprising Pt claim 7 , Ag claim 7 , Ru claim 7 , Rh claim 7 , Cu claim 7 , Fe claim 7 , Cr claim 7 , Pd claim 7 , Zn claim 7 , Mn claim 7 , Co claim 7 , Ni. V claim 7 , Mo claim 7 , Au claim 7 , Ir claim 7 , Ce.9. The device for treating gases by means of a surface plasma of claim 1 , wherein it comprises at least two dielectric substrates claim 1 , the at least one catalytic support being positioned between two main surfaces comprising the first electrodes claim 1 , or between two main surfaces comprising the second electrodes.10 ...

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Номер записи: 98
20-02-2014 дата публикации

Method for Purifying Trans-1,3,3,3-Tetrafluoropropene

Номер: US20140051896A1
Автор: IMURA Hideaki, OKAMOTO Masamune, Takada Naoto
Принадлежит:

Disclosed is a method for purifying a trans-1,3,3,3-tetrafluoropropene, in which a composition containing trans-1,3,3,3-tetrafluoropropene and at least one impurity selected from the group consisting of CHClF, CFCHCHClF, CFCHCHF, CHFCH═CF, CFCH═CHCl, CFCH═CH, CFC≡CH, and cis-1,3,3,3-tetrafluoropropene is brought into contact with a solid adsorbent to reduce an impurity content thereof. By this method, it is possible to remove the impurity in trans-1,3,3,3-tetrafluoropropene by a simple operation. 1. A method for purifying a trans-1 ,3 ,3 ,3-tetrafluoropropene , comprising the step of bringing a composition containing trans-1 ,3 ,3 ,3-tetrafluoropropene and at least one impurity selected from the group consisting of CHClF , CFCHCHClF , CFCHCHF , CHFCH═CF , CFCH═CHCl , CFCH═CH , CFC≡CH , and cis-1 ,3 ,3 ,3-tetrafluoropropene into contact with a solid adsorbent to reduce an impurity content thereof.2. The purification method according to claim 1 , wherein one of the impurities is cis-1 claim 1 ,3 claim 1 ,3 claim 1 ,3-tetrafluoropropene or CFCHCHF.3. The purification method according to claim 1 , wherein the solid adsorbent is zeolite A or zeolite X.4. A method for producing trans-1 claim 1 ,3 claim 1 ,3 claim 1 ,3-tetrafluoropropene claim 1 , comprising the step of purifying a trans-1 claim 1 ,3 claim 1 ,3 claim 1 ,3-tetrafluoropropene by bringing a composition containing trans-1 claim 1 ,3 claim 1 ,3 claim 1 ,3-tetrafluoropropene and at least one impurity selected from the group consisting of CHClF claim 1 , CFCHCHClF claim 1 , CFCHCHF claim 1 , CHFCH═CF claim 1 , CFCH═CHCl claim 1 , CFCH═CH claim 1 , CFC≡CH claim 1 , and cis-1 claim 1 ,3 claim 1 ,3 claim 1 ,3-tetrafluoropropene into contact with a solid adsorbent to reduce an impurity content thereof.5. A solid-liquid claim 1 , heterogeneous mixture claim 1 , comprising:{'sub': 2', '3', '2', '3', '2', '3', '2', '2', '2', '2', '3', '3', '2', '3, 'a composition containing trans-1,3,3,3-tetrafluoropropene and at least ...

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Номер записи: 99
27-02-2014 дата публикации

METHOD FOR TREATING LIQUIDS WITH WAVE ENERGY FROM AN ELECTRICAL ARC

Номер: US20140054241A1
Автор: Foret Todd
Принадлежит: FORET PLASMA LABS, LLC

A method for treating a liquid includes providing an apparatus: (a) a pump volute or hydrocyclone head having an inlet, and a throat having an outlet and a central axis, (b) a tank connected to the outlet of the throat, wherein the tank has a maximum inner diameter that is larger than an inner diameter of the outlet of the throat, and (d) a wave energy source comprising a first electrode within the pump volute or hydrocyclone head that is aligned with the central axis, and a second electrode within the tank that is spaced apart and axially aligned with first electrode along the central axis. The liquid is supplied to the inlet of the pump volute or hydrocyclone head. The first electrode, second electrode or both electrodes are moved along the central axis. The liquid is irradiated with one or more wave energies produced by the wave energy source. 1. A method for treating a liquid comprising the steps of:providing an apparatus comprising: (a) a pump volute or hydrocyclone head having an inlet, and a throat having an outlet and a central axis, (b) a tank connected to the outlet of the throat, wherein the tank has a maximum inner diameter that is larger than an inner diameter of the outlet of the throat, and (c) a wave energy source comprising a first electrode within the pump volute or hydrocyclone head that is aligned with the central axis, and a second electrode within the tank that is spaced apart and axially aligned with first electrode along the central axis;supplying the liquid to the inlet of the pump volute or hydrocyclone head;moving the first electrode, the second electrode or both the first and second electrodes along the central axis; andirradiating the liquid with one or more wave energies produced by the wave energy source.2. The method as recited in claim 1 , further comprising the step of exposing the liquid to a catalyst.3. The method as recited in claim 1 , further comprising the step of filtering the irradiated liquid.4. The method as recited in ...

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Номер записи: 100