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Космические корабли и станции, автоматические КА и методы их проектирования, бортовые комплексы управления, системы и средства жизнеобеспечения, особенности технологии производства ракетно-космических систем

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Мониторинг СМИ и социальных сетей. Сканирование интернета, новостных сайтов, специализированных контентных площадок на базе мессенджеров. Гибкие настройки фильтров и первоначальных источников.

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Применить Всего найдено 7448. Отображено 198.
20-04-2002 дата публикации

СПОСОБ ПОЛУЧЕНИЯ УКСУСНОЙ КИСЛОТЫ И/ИЛИ МЕТИЛАЦЕТАТА ПОСРЕДСТВОМ ИЗОМЕРИЗАЦИИ И КАРБОНИЛИРОВАНИЯ

Номер: RU2181355C2
Принадлежит: АСЕТЕКС ШИМИ (FR)

FIELD: organic synthesis. SUBSTANCE: acetic acid and/or methyl acetate are prepared from methanol/methyl formate mixture using isomerization and carbonylation reactions. Carbonylation reactions proceeds simultaneously with isomerization at 150-250 C in presence of carbon monoxide, water, solvent and a catalytic system containing halogenated promoter and iridium compound. Partial pressure of carbon monoxide is maintained between 0,1•10 5 Pa and 25•10 5 Pa, amount of water being below 5% of the total weight of reaction mixture. Solvent is an aliphatic acid containing 2 to 10 carbon atoms. Process involves formation of methyl and formyl radicals at their respective molar ratio greater than unity. Number of reactants providing formyl radicals is no more than 20% of the reaction mixture. EFFECT: increased productivity of process. 21 cl, 2 ex сс ПЧ сэ (19) РОССИЙСКОЕ АГЕНТСТВО ПО ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ ВИ "” 2181 355. (51) МПК? 13) С2 С 07С 51/10, 53/08, 69/14, 67/293 12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ РОССИЙСКОЙ ФЕДЕРАЦИИ (21), (22) Заявка: 98119400/04, 21.03.1997 (24) Дата начала действия патента: 27.03.1997 (30) Приоритет: 27.03.1996 ЕК 9603781 10.07.1996 ЕК 9608590 (43) Дата публикации заявки: 20.11.2000 (46) Дата публикации: 20.04.2002 (56) Ссылки: ЦЗ 3772380 АЛ, 13.11.1973. ЕР 0045637 А\Л, 10.02.1981. 5Ц 43774 А, 30.07.1974. ($ 4613693 АЛ, 23.09.1986. (85) Дата перевода заявки РСТ на национальную фазу: 27.10.1998 (86) Заявка РСТ: ЕК 97/00551 (27.03.1997) (87) Публикация РСТ: М/О 97/35828 (02.10.1997) (98) Адрес для переписки: 129010, Москва, ул. Б. Спасская, 25, стр.3, ООО "Юридическая фирма Городисский и Партнеры", Е_.В.Томской (71) Заявитель: АСЕТЕКС ШИМИ (ЕК) (72) Изобретатель: ПАТУА Карль (ЕК), ПЕРРОН Робер (ЕК), ТЪЕБО Даниель (ЕК) (73) Патентообладатель: АСЕТЕКС ШИМИ (ЕКВ) (74) Патентный поверенный: Томская Елена Владимировна (54) СПОСОБ ПОЛУЧЕНИЯ УКСУСНОЙ КИСЛОТЫ И/МЛИ МЕТИЛАЦЕТАТА ПОСРЕДСТВОМ ИЗОМЕРИЗАЦИИ И КАРБЬОНИЛИРОВАНИЯ (57) Изобретение относится к ...

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27-04-2016 дата публикации

КАТАЛИТИЧЕСКАЯ СИСТЕМА НА ОСНОВЕ АЗОТИРОВАННОГО СМЕШАННОГО ОКСИДА И СПОСОБ ПОЛУЧЕНИЯ ЭТИЛЕН-НЕНАСЫЩЕННЫХ КАРБОНОВЫХ КИСЛОТ ИЛИ СЛОЖНЫХ ЭФИРОВ

Номер: RU2582996C2

Изобретение относится к способу получения α, β этилен-ненасыщенных карбоновых кислот или сложных эфиров, содержащему этапы, где вызывают контакт формальдегида или его подходящего источника с карбоновой кислотой или сложным эфиром формулы R-CH-COOR, где Rобозначает водород или алкильную группу, a Rобозначает водород, алкильную или арильную группу, в присутствии катализатора и возможно в присутствии спирта, где данный катализатор содержит азотированный оксид металла, имеющий, по меньшей мере, два типа катионов металлов Ми М, где Мвыбирают из металлов или металлоидов группы 3, 4, 13 (также называемой IIIA) или 14 (также называемой IVA) Периодической таблицы, и Мвыбирают из металлов металлоидов или фосфора группы 5 или 15 (также называемой VA) Периодической таблицы. Изобретение также относится к каталитической системе для реакции формальдегида или его подходящего источника с карбоновой кислотой или сложным эфиром формулы R-CH-COOR, где Rобозначает водород или алкильную группу, a Rобозначает ...

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20-02-2001 дата публикации

4-АРИЛ-1-ФЕНИЛАЛКИЛ-1,2,3,6-ТЕТРАГИДРОПИРИДИНЫ, СПОСОБЫ ИХ ПОЛУЧЕНИЯ, ФАРМАЦЕВТИЧЕСКАЯ КОМПОЗИЦИЯ НА ИХ ОСНОВЕ И ПРОМЕЖУТОЧНЫЕ ВЕЩЕСТВА

Номер: RU2163237C2
Принадлежит: САНОФИ (FR)

Изобретение относится к новым 4-арил-1-фенилалкил-1,2,3,6-тетрагидропиридинам ф-лы (I), где Y-CH или -N-; R1-H, галоген, CF3; R2-H, галоген, (C3 - C4)алкил или (C1 - C4)алкокси; R3 и R4 - H или (C1 - C3)алкил; X представляет собой: a) (C3 - C6 )алкил, (C3 - C6)алкокси или (C1 - C4)алкоксикарбонил(C3 - C6)алкокси, b) (C3 - C7)циклоалкил или c) заместитель, выбираемый из группы, включающей фенил, феноксибензил, их солям, сольватам или четвертичным аммониевым солям. Соединения ф-лы (I) обладают нейротропной и нейрозащитной активностью и могут быть использованы в медицине для лечения заболеваний центральной нервной системы. изобретение относится также к промежуточным соединения ф-лы (II'), где R'1-галоген или CF3, и ф-лы (i), где R1 - R4 и Y имеют указанные значения для соединений ф-лы (I), и W обозначает метиленовую или карбонильную группу. 6 с. и 5 з.п. ф-лы, 1 табл.

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27-09-2004 дата публикации

НОВЫЕ ПРОИЗВОДНЫЕ ПРОСТОГО ПРОПАРГИЛОВОГО ЭФИРА

Номер: RU2237058C2

Изобретение относится к соединениям общей формулы I включая их оптические изомеры и смеси таких изомеров, где r1 обозначает водород, С1-С6алкил, С3-С6циклоалкил или арил, необязательно замещенный 1-3 атомами галогена, R2 и R3 каждый независимо друг от друга обозначают водород или С1-С6алкил, R4 обозначает С1-С6алкил или С3-С6алкинил, R5, R6, R7 и r8 каждый обозначает водород и , r10 обозначает арил, необязательно замещенный 1-3 заместителями, выбранными из группы, включающей галоген, С1-С6алкил, С1-С6алкокси, С1-С6галоалкил, С1-С4галоалкокси, С1-С4алкокси, С1-С4алкил, С1-С6алкилтио, С3-С6алкинилокси, нитро и С1-С6алкоксикарбонил или необязательно замещенный гетероарил, представляющий собой ароматическую кольцевую систему, содержащую в качестве гетероатома по крайней мере один атом кислорода или серы, r11 обозначает водород, С1-С6алкил или С3-С6алкинил, R12 обозначает водород или С1-С6алкил, Z обозначает водород -CO-R16 или -CO-COOR16 и R16 обозначает С1-С6алкил, -СН2-СО- С1-С6алкил или ...

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20-11-2007 дата публикации

СИНТЕЗ КИСЛОРОДЗАМЕЩЕННЫХ БЕНЗОЦИКЛОГЕПТЕНОВ В КАЧЕСТВЕ ЦЕННЫХ ПРОМЕЖУТОЧНЫХ ПРОДУКТОВ ДЛЯ ПОЛУЧЕНИЯ ТКАНЕСЕЛЕКТИВНЫХ ЭСТРОГЕНОВ

Номер: RU2310643C2

Изобретение относится к новым промежуточным продуктам и усовершенствованному способу получения соединения С: Предлагаемый в изобретении способ получения основан на использовании недорогих исходных материалов, позволяет получать промежуточные продукты с высоким выходом и высокой степенью чистоты без необходимости проводить операции по хроматографической очистке и может быть реализован в условиях крупномасштабного промышленного производства. Изобретение относится к усовершенствованным способам получения соединения формулы I: соединения формулы II: соединения формулы III: соединения формулы VIII: соединения формулы IX: а также к реагенту, состоящему из трибромида бора и 2,6-диметилпиридина, для щадящего и селективного отщепления метильной группы в ароматических простых метиловых эфирах. 11 н. и 1 з.п. ф-лы.

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20-01-2000 дата публикации

СПОСОБ ДИСПРОПОРЦИОНИРОВАНИЯ СМЕСЕЙ ЖИРНЫХ И СМОЛЯНЫХ КИСЛОТ

Номер: RU2144527C1

Предложен способ диспропорционирования смесей жирных и смоляных кислот путем нагревания при температуре 230-260° С в течение 1-5 ч в присутствии 0,5-2% 2,2' - тиобис(4-метил-6-трет-бутилфенол) и йода, взятых в соотношении 1: 1 - 20:1, при этом получают продукт с массовой долей абиетиновой кислоты <1% и жирных кислот с несопряженными двойными связями <2%. Предлагаемый способ диспропорционирования прост в исполнении с использованием доступных катализаторов.

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10-01-2002 дата публикации

ОБРАБОТКА ФОРМАЛЬДЕГИДСОДЕРЖАЩИХ СМЕСЕЙ

Номер: RU2000103219A
Принадлежит:

... 1. Способ удаления разновидностей формальдегида из жидкой органической смеси, содержащей по меньшей мере карбоновую кислоту или сложный эфир карбоновой кислоты и разновидности формальдегида и образующей двухфазную смесь с водой, который содержит стадию подвергания жидкой органической смеси по меньшей мере одной экстракции в системе жидкость-жидкость, где воду используют в качестве экстрагента с получением потока органической фазы и потока водной фазы так, что поток органической фазы содержит значительно уменьшенную концентрацию разновидностей формальдегида по сравнению с жидкой органической смесью. 2. Способ по п. 1, где указанный поток органической фазы содержит менее, чем 2,5% по массе формальдегида. 3. Способ по п. 2, где концентрация формальдегида в указанном потоке органической фазы составляет менее, чем 10% от концентрации формальдегида в указанной жидкой органической смеси. 4. Способ по п. 3, где указанный поток органической фазы содержит менее, чем 0,5% по массе формальдегида. 5 ...

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10-04-2005 дата публикации

СИНТЕЗ 4-ФЕНИЛМАСЛЯНОЙ КИСЛОТЫ

Номер: RU2003136765A
Принадлежит:

... 1. Способ получения соединения формулы I Формула I где R независимо выбран из водорода, галогена, C1-C4 алкила, алкенила, алкинила, C3-C6 циклоалкила, C1-C4 алкокси, алкенокси, алкинокси; и X представляет собой водород, катион щелочного металла, аммоний или замещенный аммоний; который включает; взаимодействие соединения формулы II; Формула II где R определен выше, с соединением формулы III Формула III, и b) взаимодействие полученного соединения с водным раствором основания. 2. Способ по п.1, где соединение формулы IV представляет собой гидроксид натрия. 3. Способ по п.1, где все R представляют собой водород. 4. Способ по п.1, где взаимодействие соединения формулы I с соединением формулы II проводят в присутствии катализатора. 5. Способ по п.4, где катализатор представляет собой кислоту Льюиса. 6. Способ по п.5, где катализатор представляет собой хлорид алюминия, хлорид цинка, хлорид железа, хлорид олова, трибромид бора, трифторид бора или серную кислоту. 7. Способ по п.6, где катализатор ...

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27-09-2003 дата публикации

Способ получения α-разветвленных монокарбоновых насыщенных кислот

Номер: RU2002100750A
Принадлежит:

Способ получения α-разветвленных монокарбоновых насыщенных кислот путем теломеризации жирных кислот С3, С4 с этиленом при повышенной температуре и давлении в присутствии радикального инициатора, отличающийся тем, что в качестве инициатора используют аддукт ацетона с перекисью водорода, а процесс ведут при температуре 40-100°С, давлении 10-50 атм в течение 1-6 ч и при мольном соотношении жирных кислот, ацетона, перекиси водорода равном 1,0:0,25:0,07-1,0:0,012:0,002.

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07-02-1970 дата публикации

Способ получения арилметилмалоновых кислот

Номер: SU263494A1
Принадлежит:

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15-08-1986 дата публикации

Катализатор для получения уксусной кислоты

Номер: SU1251795A3

1. A process for the production of acetic acid by catalytic rearrangement of methyl formate at elevated temperature and elevated pressure in the presence of a metal catalyst, a halogen promoter and carbon monoxide, characterised in that the reaction is carried out in the liquid phase at a temperature of 140 to 300 degrees C and a CO partial pressure of 2 to 250 bar at the reaction temperature by means of a metal catalyst system comprising rhodium, a rhodium salt or a rhodium complex and at least one metal compound of Group VI B in the presence of a halogen promoter but in the absence of ligands of Group V A, the rhodium compound being supplied in an amount of 0.05 to 5 mg atom of rhodium per mole of methyl formate supplied and at an atomic ratio of rhodium : Group VI B metal of 1 : 100 to 10 : 1 and an atomic ratio of rhodium : halogen of 1 : 1000 to 1 : 1.

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06-04-1967 дата публикации

Formtrennmittel fuer das Herausloesen von Kautschukgegenstaenden aus Formen

Номер: DE0001238201B
Автор: ARON ERWIN

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07-07-2005 дата публикации

SPEZIFISCH MARKIERTE PROTEINE, AMINOSÄURE UND BIOCHEMISCHE VORLÄUFER

Номер: DE0060020547D1
Принадлежит: ABBOTT LAB, ABBOTT LABORATORIES, ABBOTT PARK

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20-07-1974 дата публикации

Номер: DD0000107258A5
Автор:
Принадлежит:

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25-02-1982 дата публикации

VERFAHREN ZUR HERSTELLUNG ALIPHATISCHER CARBONSAEUREN

Номер: DE0003124743A1
Принадлежит:

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16-07-1970 дата публикации

Verfahren zur Herstellung von Acrylmethylmalonsaeuren

Номер: DE0001568936A1
Принадлежит:

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21-03-1974 дата публикации

Номер: DE0002009928B2

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23-05-1990 дата публикации

Номер: DE0003108203C2
Принадлежит: FMC CORP., PHILADELPHIA, PA., US

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27-10-1994 дата публикации

Process for the preparation of 13-(Z)-retinoic acid

Номер: DE0004313089A1
Принадлежит:

... 13-(Z)-retinoic acid is prepared by a) reaction of 5-hydroxy-4-methyl-2-(5H)-furanone with a [3-methyl-5-(2,6,6-trimethyl-1-cyclohexene-1-yl)-2,4-pentadienyl] triarylphosphonium salt and b) subsequent partial isomerisation of the mixture of 13-(Z)- and 11,13-di-(Z)-retinoic acid obtained, characterised in that in reaction step a) the reaction is carried out in the presence of lithium hydroxide as alkali metal hydroxide and in dimethylformamide as solvent at temperatures from +10 to -9 DEG C and/or in reaction step b) the isomerisation is carried out by irradiation with light in the wavelength range between 200 and 600 nm of the isomer mixture obtained as in a) in an organic solvent in the presence of a photon sensitiser.

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24-10-1968 дата публикации

Verfahren zur Herstellung von Fumarsaeure

Номер: DE0001443110A1
Принадлежит:

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08-06-1972 дата публикации

Номер: DE0001468201C2
Автор:
Принадлежит:

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03-05-1967 дата публикации

AN IMPROVED PROCESS FOR THE PREPARATION OF SATURATED ALIPHATIC ALPHA-SUSTITUTED DI-ACIDS

Номер: GB0001067311A
Автор:
Принадлежит:

... 1,067,311. Saturated alpha-substituted aliphatic diacids. BOUGIES DE LA COUR. Aug. 4, 1964 [Aug. 7, 1963], No. 30999/64. Heading C2C. Saturated alpha-substituted aliphatic diacids are prepared by the carboxylation of a mixture of oleic acid and formic (at least 80% pure) with a mixture of sulphuric acid and either phosphoric, glacial acetic, or mono-, di-, or trichloroacetic acids. The oleic and formic acid mixture is preferably emulsified, and the carboxylizing mixture is preferably sulphuric and 12-40% phosphoric or 5 to 20% of acetic or the chloroacetic acids. The alpha-substituted diacids are salted out, e.g. with acetic acid and further separated by distillation if necessary.

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23-04-1986 дата публикации

POLYMERISATION OF FATTY ACIDS

Номер: GB0008606951D0
Автор:
Принадлежит:

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22-11-1972 дата публикации

Номер: GB0001297362A
Автор:
Принадлежит:

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11-09-1974 дата публикации

ORGANIC SYNTHESIS AND PRODUCTS THEREOF

Номер: GB0001366706A
Автор:
Принадлежит:

... 1366706 Synthesis of organic compounds using polymers as intermediate supports YEDA RESEARCH & DEVELOPMENT CO Ltd 28 July 1971 [30 July 1970] 35343/71 Heading C2C [Also in Division C3] The invention comprises a process for synthesizing organic compounds wherein an organic moiety is chemically linked to a crosslinked polymeric carrier, converted into a reactive species (the concentration of said species being such as to prevent interreaction), said species is reacted with another organic compound to form the desired product, and said product is split from the supporting polymer. Specific embodiments refer to the use of a styrene/divinyl benzene copolymer which has been chloromethylated. In one case the chloromethylated polymer is reacted with a carboxylic acid preferably containing an alpha -CH 2 - group. This group is then rendered reactive by treatment with trityl lithium to produce a negative charge, and the reactive species is then acylated or alkylated with an acyl or alkyl halide.

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09-10-1985 дата публикации

13,14,19,19,20,20-Hexadehydro derivatives of carboprostacyclins and process for their preparation

Номер: GB0002156343A
Принадлежит:

Compounds of formula (I> wherein R = H or C1-C6 alkyl m = 1-5 one of R1 and R2 is H or C1-C6 alkyl and the other is OH one of R3 and R4 is H and the other is H or C1-C4 alkyl R5 = C1-C6 alkyl and their salts are useful in therapy.6 ...

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15-02-1989 дата публикации

Preparation of pure fumaric acid

Номер: GB0002207915A
Принадлежит:

A process for the preparation of pure fumaric acid from a solution of maleic acid comprises purifying the solution by contacting with activated charcoal and isomerizing the maleic acid in the presence of this urea and Hcl and either NaHSO3 or Na2SO3.

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15-11-1989 дата публикации

Leukotriene disease antagonists

Номер: GB0002218416A
Принадлежит:

New alkenoic acid derivatives can be prepared by reaction of corresponding aldehydic esters with phosphorous compounds in inert solvents and in the presence of bases followed by hydrolysis of the intermediate esters. The new alkenoic acid derivatives can be used as active compounds in medicaments.

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13-10-1971 дата публикации

PROCESS FOR CONTINUOUS PRODUCTION OF MONO-ALKYLATED AROMATIC COMPOUNDS

Номер: GB0001249525A
Автор:
Принадлежит:

... 1,249,525. Process for continuous production of mono-alkylated aromatic compounds. ARMOUR INDUSTRIAL CHEMICAL CO. 6 May, 1969 [6 May, 1968], No. 22936/69. Heading C2C. A continuous process for the mono-alkylation of aromatic compounds comprises (a) introducing into a continuous reaction zone (I) a substantially anhydrous substituted unsaturated aliphatic hydrocarbon reactant having from 8 to 54 carbon atoms, (II) a substantially anhydrous aromatic reactant which is a mono-, di-, or tri-carbocyclic compound or a substituted derivative thereof in which the substituents are 1 or 2 methyl, methoxy, phenoxy, or hydroxy groups in which the aromatic reactant is introduced at a molar rate of at least 2 moles per mole of the aliphatic reactant, and (III) substantially anhydrous hydrogen fluoride, in which the hydrogen fluoride is introduced at a molar rate of at least 3 moles per mole of aliphatic reactant: (b) mixing the reactants and hydrogen fluoride for a residence time of from 2 to 60 minutes ...

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21-12-1983 дата публикации

COMPOUNDS

Номер: GB0008330568D0
Автор:
Принадлежит:

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19-12-1984 дата публикации

IRON-CATALYZED COUPLING REACTION

Номер: GB0002098610B
Автор:
Принадлежит: UPJOHN CO, UPJOHN THE CO

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20-02-1985 дата публикации

4-substituted-2-indanols

Номер: GB0002143820A
Принадлежит:

Alcohols of the formula in which R<1> is phenyl, optionally substituted with halogen or C1-4 alkyl are novel. They can be used in preparing insecticides of the pyrethroid type.

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03-07-1985 дата публикации

Polysubstituted derivatives of naphthalene a process for preparing them and their use in the pharmaceutical and cosmetic fields

Номер: GB0002150563A
Принадлежит:

New 2,6-disubstituted derivatives of naphthalene have the formula (I) wherein n is 1 or 2, R1 to R4 are hydrogen or CH3, R5 is (ii)CN, (iv) 2-oxazolinyl, wherein m is 0 or 1, R6 is hydrogen, alkyl, OR9 wherein R9 is H, alkyl or wherein R10 is alkyl or aryl, or R6 is when m=1, r' and r'' representing H, alkyl, mono- or poly-hydroxyalkyl, aryl or a heterocycle when taken together, R7 is H or alkyl, R8 is H, alkyl and the acetal of said compounds, and the salts of the compounds of formula I. These compounds are usefully employed in the pharmaceutical and cosmetic fields.

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21-05-1964 дата публикации

Production of fumaric acid

Номер: GB0000958695A
Автор:
Принадлежит:

White fumaric acid is obtained from coloured aqueous maleic acid solution by contacting the solution at 55 DEG to 85 DEG C. with a bromine-providing material wherein the oxidation state of the bromine is less than plus 5, and an oxidizing agent, the initial concentration of the maleic acid solution being 10% to 70% by weight, the amount of bromine-providing material being present in an amount equivalent in bromine content to at least 0.001% of ammonium bromide based on the weight of the maleic acid, the oxidizing agent having a standard oxidation reduction potential of at least 1.23 volts and being present in an amount oxidatively equivalent to from 0.003% to 10% of ammonium persulphate based on the weight of the maleic acid. In examples fumaric acid is obtained from maleic acid using ammonium bromide, ammonium persulphate and hydrogen peroxide. Other bromine-providing materials mentioned are cadmium ammonium bromide, sodium bromide, hydrogen bromide, manganese bromide, elemental bromine ...

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18-11-1964 дата публикации

Metallometallic salts of aromatic mono carboxylic acids and process for their preparation

Номер: GB0000975772A
Автор:
Принадлежит:

Metallic salts of a -metallo aromatic monocarboxylic acids of formula where R1 and R2 are hydrogen or an alkyl, alkenyl or aryl substituent, M and M1 are alkali metals or alkaline earth metals, a is from 1 to 5 and y is the valency of M are made by reacting an amide or hydride of an alkali metal or an alkaline earth metal or the free alkali metal or alkaline earth metal with an alkyl substituted benzoic acid or an alkali or alkaline earth metal salt of said acid, said acid containing at least one a -hydrogen atom on an alkyl group. The invention also includes as new compounds sodium a -sodio-p-toluate and sodium a -sodio-o-toluate. The alkyl-substituted benzoic acids may be prepared by oxidizing the corresponding alkyl-substituted aromatic hydrocarbon. The reaction may be carried out at a temperature between 70 DEG and 225 degrees, preferably by grinding in a ball-mill in an inert atmosphere such as nitrogen or under an inert liquid blanket. When a metal amide is used ...

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16-09-1964 дата публикации

Process for the production of trans-dec-2-en-9-one-1-acid

Номер: GB0000969817A
Автор:
Принадлежит:

Trans-dec-2-en-9-one-1-acid is prepared by condensing a hept-2-en-7-al-1-acid alkyl ester with a propargyl halide in the presence of magnesium, zinc or aluminium to give a 7-hydroxy-dec-2-en-9-yne -1-acid alkyl ester to which water is added and split off in the presence of catalytic amounts of basic mercury sulphate and a solubilizing agent, to give a deca-2,7-dien-9-one-1-acid alkyl ester which is selectively reduced by hydrogenation in the presence of a palladium catalyst poisoned with quinoline to give a dec-2-en-9-one-1-acid alkyl ester which is optionally isomerized, and saponified.

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24-11-1982 дата публикации

Production of fumaric acid from wash waters of exhaust gases resulting from hydrocarbon oxidation

Номер: GB2098612A
Принадлежит:

Fumaric acid is produced from the wash waters of exhaust gases resulting from hydrocarbon oxidation, which contain maleic acid. The process comprises a thermal pre- treatment of the impure maleic acid solution, with optional concurrent concentration, with transformation of part of the impurities to facilitate their elimination from the final product, subsequent hot filtration, isomerization of the maleic acid to fumaric acid, crystallization according to a pre-set time/temperature chart, removal of the mother liquors by filtration, subsequent dissolution in water or in a fumaric acid solution, decolorization, recrystallization and drying.

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01-06-1967 дата публикации

Fumaric acid production

Номер: GB0001070758A
Автор:
Принадлежит:

Fumaric acid crystals are obtained by the isomerization of an aqueous maleic acid solution in the presence of at least 2 p.p.m. by weight, based on maleic acid solution, of dodecyl alcohol and a known catalyst for the isomerization. The acid crystals are of increased size and strength. An example describes the isomerization in the presence of dodecyl alcohol using an ammonium bromide/ammonium persulphate catalyst.

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17-07-1985 дата публикации

Preparation of -alkylated acetic acid derivatives

Номер: GB0002151225A
Принадлежит:

This invention provides a process for preparing a alpha -alkylated acetic acid derivative represented by the formula (II) wherein Z is -COOR or -CN in which R is straight-chain or branched-chain alkyl, cycloalkyl, substituted or unsubstituted phenyl, or substituted or unsubstituted aralkyl, R' is substituted or unsubstituted straight-chain or branched-chain alkyl or alkenyl, and Y is an optionally substituted heterocyclic group or optionally substituted aromatic group, the process comprising subjecting an acetic acid derivative represented by the formula Y-CH2-Z (I) wherein Y and Z are as defined above to electrolytic reduction in the presence of an alkylating agent.

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13-07-1933 дата публикации

A process for the production of substituted carboxylic acids or carbonyl compounds

Номер: GB0000395193A
Автор:
Принадлежит:

Substituted carboxylic acids or carbonyl compounds are manufactured by condensing aliphatic mono-olefines or technical mixtures containing aliphatic with or without aromatic mono-olefines, with substances having a double bond between two carbon atoms conjugated with one or more carboxyl or carbonyl groups, e.g. maleic acid or anhydride, crotonic acid, crotonaldehyde, acrolein or quinone, and recovering the substituted carboxylic acids or carbonyl compounds from the reaction mass. As mono-olefines may be employed amylene, butylene or products containing mono-olefines, e.g. cracking benzine. The temperature of the reaction is usually above 160 DEG C. The products may be used as such or may be converted with other substances into synthetic resins, pharmaceutical preparations, plasticizing means, lacquers or insulating materials. In examples: (1) amylene (produced from fermentation amyl alcohol) is heated in an autoclave to 180 DEG C. with maleic anhydride and the product treated with lye and ...

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13-01-1971 дата публикации

IMPROVEMENTS IN AND RELATING TO THE PRODUCTION OF CARBONYL COMPOUNDS

Номер: GB0001219332A
Автор: MEE ALEC, ALEC MEE
Принадлежит:

Подробнее
10-01-1936 дата публикации

Process for the manufacture of condensation products

Номер: GB0000441016A
Автор:
Принадлежит:

Aliphatic dicarboxylic acids or acid anhydrides substituted by residues of saturated aliphatic or alicyclic hydrocarbons or aryl or arylene derivatives thereof are prepared by interacting saturated aliphatic or alicyclic hydrocarbons, ethers or ketones or aryl or arylene derivatives thereof which contain at least one hydrogen atom attached to at least one aliphatic carbon atom and all the aliphatic atoms of which are connected by single bonds with a -b -unsaturated aliphatic dicarboxylic acid anhydrides or compounds which are converted into these anhydrides under the reaction conditions. The reaction may be accelerated by a copper catalyst and by the use of heat and pressure. Suitable starting materials include paraffinic hydrocarbons such as heptane or paraffin oil, completely or partially saturated cyclic hydrocarbons such as cyclohexane, decahydronaphthalene and tetrahydronaphthalene, aromatic hydrocarbons with saturated side chains such as toluene, ethylbenzene and propylbenzene, ethers ...

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21-07-1982 дата публикации

PROSTACYCLIN DERIVATIVES THEIR USE AND PREPARATION

Номер: GB0002012265B
Автор:
Принадлежит: SANKYO CO, SANKYO CO LTD

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04-04-1962 дата публикации

Metal salts of 2-carboxy-3-metallo-propenes

Номер: GB0000893268A
Автор:
Принадлежит:

... 893,268. Metal salts of 2-carboxy-3-metallopropenes. ETHYL CORPORATION. Nov. 30, 1959 [Dec. 2, 1958], No. 40568/59. Class 2 (3). The invention comprises a metal salt of 2- carboxy-3-metallo-propene. They may be of formula (when both the metal of the salt and the metallo-substituent are monovalent) where each R represents hydrogen or hydrocarbon groups which can be the same or different, R1 is an alkylene group and M and Ml are metals which may be the same or different. It is preferred that M and M1 are alkali or alkaline earth metals. They may be prepared by reacting a metal salt of a 2-carboxy-propene with a metallating agent such as a metal amide, hdyride or in some cases the metal itself and compounds of formula RxM. Lower alkyl derivatives of metal amides may also be used. Compounds specified include sodium, potassium, lithium, calcium and magnesium amides, potassium, aluminium, magnesium, cacsium, beryllium, rubidium, copper, titanium and zirconium hydrides ...

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17-12-1980 дата публикации

2-ARYL-PROPIONIC ACID PRECURSORS

Номер: GB0001581619A
Автор:
Принадлежит:

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26-09-1979 дата публикации

MIXTURES OF POLY BRANCHED MONOCARBOXYLIC ACIDS AND PREPARATION THEREOF

Номер: GB0001553702A
Автор:
Принадлежит:

The mixtures of the acids of the formula (I) or (Ia) - the symbols are defined in Claim 1 - contain the individual acids, classified according to the numerical value of n or m and n', in the following amounts: 1) n = 1 : 10 to 40% n = 2 : 15 to 35% n = 3 : 30 to 10% n = 4 : 25 to 10% and n = 5 : 20 to 5% and 2) m = 1 and n' = 1 : 10 to 15% m = 1 and n' = 2 : 20 to 30% m = 1 and n' = 3 : 15 to 20% m = 2 and n' = 2 : 25 to 30% and m = 2 and n' = 3 : 15% The acid mixtures are used in the form of their heavy metal salts as siccatives; they have the advantage that the theoretical metal content is achieved. They can also be used for separating metal cations from solutions. These mixtures are obtained by free radical teleomerisation of acids (R2)2CHCOOH or R1CH2COOH (R1 = C1-C4-alkyl, R2 = CH3 or n-butyl) with gamma -olefins CH3CH=CH2 or C2H5CH=CH2 in a molar ratio of carboxylic acid : olefin of from 1 : 0.3 to 1 : 1.5 at from 150 to 180 DEG C in the presence of from 1 to 5% of peroxide initiator ...

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29-11-1978 дата публикации

TWO-STEP METHOD FOR THE PREPARATION OF SUBSTITUTED DICARBOXYLIC ACIDS

Номер: GB0001533819A
Автор:
Принадлежит:

... 1533819 Polymer-substituted acids and derivatives thereof LUBRIZOL CORP 3 June 1977 [11 June 1976] 23733/77 Heading C3P A two-step process for producing polymersubstituted acids and derivatives thereof, especially polyisobutenyl succinic anhydride, comprises (1) reacting an alkylating hydrocarbon polymer with 30-90% of the total amount of acidic reagent selected from maleic acid, fumaric acid, itaconic acid or an anhydride or ester thereof in the presence of 0-0À4 mole of Cl 2 per mole of acidic reagent, and subsequently (2) introducing the remainder of the acidic reagent and continuing the reaction in the presence of added Cl 2 in amount up to 4 moles per mole of added acidic reagent.

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31-10-2008 дата публикации

Method for producing 4-oxoquinoline compound

Номер: AP0200804621A0
Принадлежит:

Подробнее
31-10-2008 дата публикации

Method for producing 4-oxoquinoline compound

Номер: AP0200804621D0
Принадлежит:

Подробнее
15-02-1969 дата публикации

Obtaining made up (alpha-alcoylidène acyl) - phénile.

Номер: OA0000001269A
Автор:
Принадлежит:

Подробнее
31-03-2002 дата публикации

Process for the preparation of isotretinoin

Номер: AP0200202414D0
Автор:
Принадлежит:

Подробнее
10-09-1993 дата публикации

Carboxymethlcyclopropane derivatives.

Номер: AP0000000284A
Принадлежит:

Novel 2-(2-chloro-2-fluorocyclopropyl)-acetic acid derivatives of formula i wherein x is oxygen or -nr-, y is hydrogen, or is c1-c20alkyl, c-c7cycloalkyl, c3-c20alkenyl, c3-c20alkynyl, benzyl or aryl, each of which is unsubstituted or substituted, and r is hydrogen or c1-c6alkyl, can be used as pesticides. Especially insects and arachnids can be controlled.

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01-05-1992 дата публикации

Novel aryloxy alcohol benzenes, processes for their preparation as well as the pharmaceutical compositions containing them.

Номер: AP0000000188A
Принадлежит:

This invention has a subject matter novel aryloxy alkylbenzenes, their processes for production and the pharmaceutical compositions containing them.

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31-12-2000 дата публикации

Process for the solid phase synthesis of of aldehyde, ketone, oxine, amine, hydroxamic acid and B-unsaturated carboxylic acid and aldehyde compounds.

Номер: AP2000001994A0
Принадлежит:

This invention is directed to a process for the solid phase synthesis of aldehyde, ketone, oxime, amine, hydroxamic acid and a,b-unsaturated carboxylic acid and aldehyde compounds and to polymeric hydroxylamine resin compounds useful therefor.

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31-07-1991 дата публикации

CARBOXYMETHYLCYCLOPROPANE DERIVATIVES

Номер: AP0009100308A0
Автор:
Принадлежит:

Подробнее
31-01-1991 дата публикации

NOVEL ARYLOXY ALCOYL BENZENES,PROCESS FOR THEIR PREPARATION AS THE PHARMACEUTICAL COMPOSITION CONTAINING THEM

Номер: AP0009000223A0
Автор:
Принадлежит:

Подробнее
31-03-2002 дата публикации

Process for the preparation of isotretinoin

Номер: AP2002002414A0
Принадлежит:

The present invention relates to a process for the preparation of 13-cis isomer of vitamin a acid, commonly known as isotretinoin, in a single step.

Подробнее
31-05-2014 дата публикации

Method for producing 4-oxoquinoline compound

Номер: AP0000002914A
Принадлежит:

Подробнее
31-10-2008 дата публикации

Method for producing 4-oxoquinoline compound

Номер: AP2008004621A0
Принадлежит:

Подробнее
18-04-2006 дата публикации

Process for the preparation of isotretinoin.

Номер: OA0000012002A
Принадлежит:

Подробнее
31-03-2002 дата публикации

Process for the preparation of isotretinoin

Номер: AP0200202414A0
Автор:
Принадлежит:

Подробнее
31-01-1991 дата публикации

NOVEL ARYLOXY ALCOYL BENZENES,PROCESS FOR THEIR PREPARATION AS THE PHARMACEUTICAL COMPOSITION CONTAINING THEM

Номер: AP0009000223D0
Автор:
Принадлежит:

Подробнее
31-07-1991 дата публикации

CARBOXYMETHYLCYCLOPROPANE DERIVATIVES

Номер: AP0009100308D0
Автор:
Принадлежит:

Подробнее
25-02-1983 дата публикации

PROCEDURE FOR THE PRODUCTION OF D-ARYLOXYPROPIONS [UREN, THEIR SALTS AND ESTERS

Номер: AT0000370079B
Автор: GRAS GEORGES
Принадлежит:

Подробнее
15-04-1977 дата публикации

VERFAHREN ZUR HERSTELLUNG VON NEUEN POLYENVERBINDUNGEN

Номер: ATA260174A
Автор:
Принадлежит:

Подробнее
15-06-1977 дата публикации

VERFAHREN ZUR HERSTELLUNG VON ALFA-ARYLPROPIONSAUREN

Номер: ATA425974A
Автор:
Принадлежит:

Подробнее
15-08-1990 дата публикации

VERFAHREN ZUR HERSTELLUNG VON NEUEN POLYPRENYLVERBINDUNGEN

Номер: ATA228183A
Автор:
Принадлежит:

Подробнее
15-02-1975 дата публикации

KUNSTSTOFFZUSAMMENSETZUNG

Номер: ATA609873A
Автор:
Принадлежит:

Подробнее
15-01-2012 дата публикации

PROCEDURE FOR THE SYNTHESIS OF INSATIATED ONES OMEGA FATTY ACIDS

Номер: AT0000538208T
Принадлежит:

Подробнее
15-02-1975 дата публикации

PLASTIC COMPOSITION

Номер: AT0000609873A
Автор:
Принадлежит:

Подробнее
15-05-1980 дата публикации

HERBICIDE AND PLANT GROWTH-ADJUSTING MEANS

Номер: AT0000342178A
Автор:
Принадлежит:

Подробнее
15-03-1984 дата публикации

SUBSTITUTED ARYL CONNECTIONS AND THEIR MANUFACTURING PROCESSES.

Номер: AT0000006586T
Автор: SIRCAR, ILA
Принадлежит:

Подробнее
21-03-2013 дата публикации

Covalently Functionalized Carbon Nanostructures and Methods for Their Separation

Номер: US20130072669A1
Принадлежит: University of Maryland, College Park

The present invention is directed to carbon nanostructures, e.g., carbon nanotubes, methods of covalently functionalizing carbon nanostructures, and methods of separating and isolating covalently functionalized carbon. In some embodiments, carbon nanotubes are reacted with alkylating agents to provide water soluble covalently functionalized carbon nanotubes. In other embodiments, carbon nanotubes are reacted with a thermally-responsive agent and exposed to light in order to separate carbon nanotubes of a specific chirality from a mixture of carbon nanotubes. 1. A method comprising:a) introducing one or more defects onto a carbon nanostructure; andb) reacting said carbon nanostructure comprising said one or more defects with an alkylating agent,wherein covalent functionalization propagates from said one or more defects to produce a covalently functionalized carbon nanostructure.2. The method of claim 2 , wherein said carbon nanostructure is a carbon nanotube.3. The method of claim 1 , wherein covalent functionalization propagates from said one or more defects to create alternating sections of functionalized and intact regions of said covalently functionalized carbon nanostructure.4. The method of claim 1 , wherein said one or more defects are introduced by treating said carbon nanostructure with HOand HCl.5. The method of claim 1 , wherein said reacting comprises combining said carbon nanostructure comprising said one or more defects claim 1 , said alkylating agent claim 1 , liquid ammonia claim 1 , and an alkali metal.6. The method of claim 5 , wherein said alkylating agent is a compound having Formula I:{'br': None, 'sub': 2', 'm, 'sup': '1', 'X—(CH)—R\u2003\u2003I'} X is halo;', 'm is an integer from 1-30;', {'sup': 1', '2, 'sub': '2', 'Ris H or COR; and'}, {'sup': '2', 'Ris hydrogen or a monovalent cation.'}], 'wherein7. The method of claim 2 , wherein said one or more defects are introduced onto one carbon nanotube type or chirality that is part of a mixture of ...

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04-04-2013 дата публикации

Processes for producing acrylic acids and acrylates

Номер: US20130085295A1
Принадлежит: Celanese International Corp

In one embodiment, the invention is to a process for producing an acrylate product. The process comprises the step of reacting an alcohol and oxygen in a reactor to produce a high temperature alkylenating agent stream comprising an alkylenating agent. The process further comprises the step of contacting an alkanoic acid with at least a portion of the high temperature alkylenating agent stream under conditions effective to form a crude product stream comprising acrylate product and alkylenating agent. The process further comprises the step of separating at least a portion of the crude product stream to form at least one alkylenating agent stream and at least one purified acrylate product stream comprising acrylate product.

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18-04-2013 дата публикации

POLYLACTIC ACID DECOMPOSITION METHOD

Номер: US20130095545A1
Автор: Tsubota Jun
Принадлежит: OSAKA GAS CO., LTD.

A primary object of the present invention is to provide a polylactic acid decomposition method that efficiently decomposes polylactic acid so that the polylactic acid can readily undergo degradation by a biological treatment such as methane fermentation. Specifically, the present invention provides a polylactic acid decomposition method involving a step of impregnating a polylactic acid-containing organic material with a treatment solution containing an organic acid salt and/or inorganic acid salt of an amine compound. 2. The method according to claim 1 , wherein the organic acid salt and/or inorganic acid salt of an amine compound represented by Formula (I) has buffering capacity.3. The method according to claim 1 , wherein the organic acid salt and/or inorganic acid salt of an amine compound represented by Formula (I) is at least one salt selected from the group consisting of ammonium carbonate claim 1 , ammonium hydrogen carbonate claim 1 , diammonium hydrogenphosphate claim 1 , triammonium phosphate claim 1 , ammonium borate claim 1 , and triammonium citrate.4. The method according to claim 1 , wherein the treatment is performed at a molecular ammonia concentration of 500 mg/L or more.5. The method according to claim 1 , wherein the treatment is performed at a temperature of greater than 40° C.6. The method according to claim 1 , wherein the treatment is performed at a pH of 8 to 9.7. The method according to claim 1 , wherein the polylactic acid-containing organic material is a mixture of polylactic acid and garbage.9. The method according to claim 8 , comprising heating the polylactic acid-containing organic material to a temperature of greater than 40° C. in the presence of molecular ammonia.10. The method according to claim 9 , wherein the molecular ammonia has a concentration of 500 mg/L or more.11. The method according to claim 9 , wherein the heating is performed at a pH of 8 to 9. The present invention relates to a polylactic acid decomposition method ...

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10-10-2013 дата публикации

Processes for Producing Acrylic Acids and Acrylates with Diluted Reaction Mixture and By-Product Recycle

Номер: US20130267736A1
Принадлежит: Celanese International Corp

In one embodiment, the invention is to a process for producing an acrylate product. The process comprises the step of providing a diluted crude acrylate stream comprising the acrylate product and an alkylenating agent. The process further comprises the step of separating at least a portion of the diluted crude acrylate stream to form an alkylenating agent stream and an intermediate product stream. The alkylenating agent stream comprises at least 1 wt. % alkylenating agent and the intermediate product stream comprises acrylate product.

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10-10-2013 дата публикации

Processes for Producing Acrylic Acids and Acrylates with Controlled Oxygen Concentration Across Reactor

Номер: US20130267737A1
Принадлежит: Celanese International Corporation

In one embodiment, the invention is to a process for producing an acrylate product. The process comprises the step of producing a crude product stream by reacting reactants comprising an alkanoic acid, an alkylenating agent and oxygen in the presence of a catalyst, wherein the oxygen concentration across the reactor is from 0.5 to 10 wt %. The oxygen may be fed to the reactor through a plurality of feeds. The invention is also directed to methods of monitoring the oxygen concentration for the reaction and adjusting the oxygen concentration and/or placement of oxygen feed(s). The process further comprises the step of separating at least a portion of the crude product stream to form an alkylenating agent stream and an intermediate product stream. 1. A process for producing an acrylate product , the process comprising the steps of:(a) contacting in a reactor reactants comprising an alkanoic acid, an alkylenating agent and a plurality of oxygen feed streams over a catalyst under conditions effective to form a crude product stream comprising acrylate product and alkylenating agent; and(b) separating at least a portion of the crude product stream to form at least one alkylenating agent stream and at least one purified acrylate product stream comprising acrylate product;wherein oxygen concentration across the reactor ranges from 0.5 wt % to 10 wt %.2. The process of claim 1 , wherein the plurality of oxygen feeds is configured across a length of the reactor.3. The process of claim 1 , wherein the plurality of oxygen feeds comprises at least three oxygen feeds.4. The process of claim 1 , wherein the plurality of oxygen feeds is fed to the reactor separately from the alkanoic acid and alkylenating agent feed.5. The process of claim 1 , wherein the reactor has an inlet oxygen concentration and an outlet oxygen concentration and the outlet concentration is substantially similar to or greater than the inlet concentration.6. The process of claim 5 , wherein variance between the ...

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01-01-2015 дата публикации

Continuous process of oxidative cleavage of vegetable oils

Номер: US20150005521A1
Принадлежит: Novamont SpA

A continuous process for the oxidative cleavage of vegetable oils containing triglycerides of unsaturated carboxylic acids, to obtain saturated carboxylic acids, comprising feeding to a first continuous reactor a vegetable oil, an oxidizing compound and catalyst capable of catalyzing the oxidation reaction of the olefinic double bond to obtain an intermediate compound containing vicinal diols: feeding to a second continuous reactor said intermediate compound, a compound containing oxygen and a catalyst capable of catalyzing the oxidation reaction of the vicinal diols to carboxylic groups, to obtain saturated monocarboxylic acids (i) and triglycerides containing saturated carboxylic acids with more than one acid function (ii); separating the saturated monocarboxylic acids (i) from the triglycerides (ii); hydrolyzing in a third reactor the triglycerides (ii) to obtain glycerol and saturated carboxylic acids with more than one acid function; and purifying said saturated carboxylic acids by fractioned crystallization by means of wash column (melt crystallization).

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12-01-2017 дата публикации

METHODS FOR THE SYNTHESIS OF OLEFINS AND DERIVATIVES

Номер: US20170008828A1
Принадлежит:

The invention provides a method of producing acrylic acid. The method includes contacting fumaric acid with a sufficient amount of ethylene in the presence of a cross-metathesis transformation catalyst to produce about two moles of acrylic acid per mole of fumaric acid. Also provided is an acrylate ester. The method includes contacting fumarate diester with a sufficient amount of ethylene in the presence of a cross-metathesis transformation catalyst to produce about two moles of acrylate ester per mole of fumarate diester. An integrated process for process for producing acrylic acid or acrylate ester is provided which couples bioproduction of fumaric acid with metathesis transformation. An acrylic acid and an acrylate ester production also is provided. 172-. (canceled)73. A process for producing an acrylate ester comprising: (1) fumABC, zwf purU, and', '(2) fumABC, zwf glyA, 'a) culturing in a sufficient amount of nutrients and media a non-naturally occurring microbial organism comprising a set of metabolic modification obligatorily coupling fumaric acid product to grow of said microbial organism, said set of metabolic modifications comprising disruption of at least one of the gene sets comprisingor an ortholog thereof, to produce stable growth-coupled production of fumaric acid;b) performing diesterification of said fumaric acid to produce fumarate diester, andc) contacting said fumarate diester with a sufficient amount of ethylene in the presence of a cross-metasthesis catalyst to produce about two moles of an acylate ester per mole of fumarate diester.74. The process of claim 73 , wherein said genes encoding said metabolic modifications (a) fumABC claim 73 , zwf claim 73 , purU further comprises disruption of at least one gene selected from ackA-pta claim 73 , gdhA claim 73 , pntAB or ackA-pta claim 73 , yibO claim 73 , ythE.75. The process of claim 73 , wherein said disruption comprises a deletion of at least one gene within said gene set.76. The process of ...

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17-01-2019 дата публикации

PROCESS FOR PREPARING ALKYL SALICYLIC ACID AND PRODUCTS THEREOF

Номер: US20190016660A1
Принадлежит:

This invention relates to a process for preparing an alkylsalicylic acid. The process comprises reacting salicylic acid with an olefin having at least four carbon atoms at a temperature ranging from about 50° C. to about 200° C. in the presence of an arylsulfonic acid-containing catalyst (such as para-toluene sulfonic acid), to produce an alkylsalicylic acid. The resulting alkylsalicylic acid has various applications such as a food preservative, an oil field chemical for oil recovery, and a component in a color toner agent for electrophotography. 1. A process for preparing an alkylsalicylic acid , comprising:reacting salicylic acid with an olefin having at least four carbon atoms at a temperature ranging from about 50° C. to about 200° C. in the presence of an arylsulfonic acid-containing catalyst, to produce an alkylsalicylic acid with a residual olefin of less than about 2 wt %, wherein the molar ratio of the olefin to salicylic acid is about 1:1 to about 1.3:1.2. The process of claim 1 , wherein the catalyst is para-toluene sulfonic acid claim 1 , xylene sulfonic acid claim 1 , naphthalene sulfonic acid claim 1 , phenol sulfonic acid claim 1 , or combinations thereof.3. The process of claim 2 , wherein the catalyst is para-toluene sulfonic acid claim 2 , and wherein the catalyst is at least 95% pure claim 2 , contains 0-5% water claim 2 , and contains 0-5% sulfuric acid.4. The process of claim 1 , wherein the olefin is added to the reaction in two or more portions over a course of about 30 minutes to about 20 hours under the reaction temperature.5. The process of claim 4 , wherein the olefin is added to the reaction in two or more portions over the course of about 2 to about 6 hours claim 4 , under reaction temperature.6. The process of claim 1 , wherein the olefin is an α-olefin containing 4 to 24 carbon atoms claim 1 , or a mixture thereof.7. The process of claim 1 , wherein the molar ratio of the arylsulfonic acid to salicylic acid is about 0.5:1 to about 1.5: ...

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22-01-2015 дата публикации

PROCESS FOR PREPARING MODIFIED V-TI-P CATALYSTS FOR SYNTHESIS OF 2,3-UNSATURATED CARBOXYLIC ACIDS

Номер: US20150025272A1
Принадлежит: EASTMAN CHEMICAL COMPANY

The invention relates to a catalyst composition comprising a mixed oxide of vanadium, titanium, and phosphorus modified with alkali metal. The titanium component is derived from a water-soluble, redox-active organo-titanium compound. The catalyst composition is highly effective at facilitating the vapor-phase condensation of formaldehyde with acetic acid to generate acrylic acid, particularly using an industrially relevant aqueous liquid feed. 1. A catalyst composition comprising a mixed oxide of vanadium (V) , titanium (Ti) , phosphorus (P) , and alkali metal (M) , wherein the titanium component is the residue of an organo-titanium compound , wherein the organo-titanium compound is titanium(IV) bis(ammonium lactate)dihydroxide.2. The catalyst composition according to claim 1 , which has the general formula VTiPMO claim 1 , wherein a is a number from 0.3 to 6.0 claim 1 , b is a number from 2.0 to 13.0 claim 1 , c is a number from 0.01 to 1.25 claim 1 , and d is the number of atoms required to satisfy the valences of V claim 1 , Ti claim 1 , P claim 1 , and M.3. The catalyst composition according to claim 2 , wherein a ranges from 1.0 to 4.0 claim 2 , b ranges from 4.0 to 10.0 claim 2 , and c ranges from 0.25 to 0.75.4. The catalyst composition according to claim 1 , wherein the alkali metal is selected from at least one of lithium claim 1 , sodium claim 1 , potassium claim 1 , rubidium claim 1 , and cesium.5. The catalyst composition according to claim 1 , wherein the alkali metal comprises potassium.6. The catalyst composition according to claim 1 , which further comprises a pre-shaped support.7. The catalyst composition according to claim 6 , wherein the pre-shaped support comprises silica claim 6 , alumina claim 6 , titanium oxide claim 6 , titanium pyrophosphate claim 6 , zirconium oxide claim 6 , or zirconium pyrophosphate.8. The catalyst composition according to claim 6 , wherein the pre-shaped support has a particle size ranging from 0.1 mm to 20 mm.9. A ...

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09-02-2017 дата публикации

PROCESS FOR RUTHENIUM-CATALYZED TRANSVINYLATION OF CARBOXYLIC ACIDS

Номер: US20170036988A1
Принадлежит:

The invention relates to a process for transvinylation of a carboxylic acid feedstock with a vinyl ester feedstock to obtain a vinyl ester product and the corresponding acid of the vinyl ester feedstock in the presence of one or more ruthenium catalysts, wherein a) the vinyl ester feedstock, the carboxylic acid feedstock and a ruthenium catalyst are fed to the reactor, and b) the transvinylation reaction is carried out, characterized in that a carbonyl-free Ru(III) carboxylate is used as the ruthenium catalyst and in that no carbon monoxide is supplied, c) the reaction is carried out at a temperature of 110 to 170° C., d) upon completion of the transvinylation reaction, the vinyl ester feedstock and the corresponding acid are separated from the reaction mixture by distillation, e) the vinyl ester product is separated by distillation from the bottom product of the distillation, and f) the remaining reaction mixture is recycled into the reactor. 1. A process for transvinylation of a reactant carboxylic acid with a reactant vinyl ester to afford a product vinyl ester and the corresponding acid of the reactant vinyl ester in the presence of one or more ruthenium catalysts , whereina) the reactant vinyl ester, the reactant carboxylic acid and a ruthenium catalyst are supplied to the reactor, andb) the transvinylation reaction is performed,whereinthe ruthenium catalyst employed is a carbonyl-free Ru(III) carboxylate and no carbon monoxide is supplied,c) the reaction is performed at a temperature of 110° C. to 170° C.,d) after completion of the transvinylation reaction the reactant vinyl ester and the corresponding acid are distillatively removed from the reaction mixture, ande) the product vinyl ester is distillatively removed from the bottoms product of the distillation, andf) the remaining reaction mixture is recycled into the reactor.2. The process as claimed in claim 1 , wherein the residence time in the reaction zone is 0.25 to 5 hours.3. The process as claimed in ...

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01-05-2014 дата публикации

Processes for Regenerating Catalyst for Producing Acrylic Acids and Acrylates

Номер: US20140121410A1
Принадлежит: Celanese International Corporation

In one embodiment, the invention is to a process for producing an acrylate product. The process comprises the step of reacting an alkanoic acid and an alkylenating agent over a catalyst to produce a crude acrylate product stream, and to product a used catalyst. The used catalyst may then be contacted with a regenerating stream to form a regenerated catalyst. Alkanoic acid and alkylenating agent may then be reacted over the regenerated catalyst to product additional crude acrylate product stream. 1. A process for producing an acrylate product , the process comprising the steps of: i) a crude acrylate product stream comprising acrylate product and residual alkylenating agent and', 'ii) used catalyst;, '(a) contacting an alkanoic acid and an alkylenating agent in a reactor over an initial catalyst under conditions effective to form(b) contacting the used catalyst with a regenerating stream to form a regenerated catalyst;(c) separating at least a portion of the crude acrylate product stream to form an alkylenating agent stream comprising at least 1 wt % alkylenating agent and an intermediate product stream comprising acrylate product.2. The process of claim 1 , wherein the regenerating stream comprises oxygen or hydrogen3. The process of claim 2 , wherein the regenerating stream comprises at least 1 wt % oxygen.4. The process of claim 1 , wherein the initial catalyst has a deactivation point and wherein step (b) is performed at the deactivation point.5. The process of claim 4 , wherein the deactivation point is a point wherein the conversion of alkanoic acid is less than 30% claim 4 , the selectivity of alkanoic acid to acrylate product is less than 85% claim 4 , and the space time yield is less than 300 g/L/hr.6. The process of claim 1 , further comprising the step of:(d) contacting an alkanoic acid and an alkylenating agent over the regenerated catalyst under conditions effective to form additional acrylate product.7. The process of claim 6 , wherein steps (a) claim 6 ...

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15-02-2018 дата публикации

CONTINUOUS PROCESS OF OXIDATIVE CLEAVAGE OF VEGETABLE OILS

Номер: US20180044277A1
Принадлежит:

A continuous process for the oxidative cleavage of vegetable oils containing triglycerides of unsaturated carboxylic acids, to obtain saturated carboxylic acids, comprising feeding to a first continuous reactor a vegetable oil, an oxidizing compound and catalyst capable of catalyzing the oxidation reaction of the olefinic double bond to obtain an intermediate compound containing vicinal diols: feeding to a second continuous reactor said intermediate compound, a compound containing oxygen and a catalyst capable of catalyzing the oxidation reaction of the vicinal diols to carboxylic groups, to obtain saturated monocarboxylic acids (i) and triglycerides containing saturated carboxylic acids with more than one acid function (ii); separating the saturated monocarboxylic acids (i) from the triglycerides (ii); hydrolyzing in a third reactor the triglycerides (ii) to obtain glycerol and saturated carboxylic acids with more than one acid function; and purifying said saturated carboxylic acids by fractioned crystallization by means of wash column (melt crystallization). 1. A continuous process for the oxidative cleavage of vegetable oils containing triglycerides of unsaturated carboxylic acids , for obtaining saturated carboxylic acids , which comprises the steps of:a) feeding to a first continuous reactor at least a vegetable oil and an oxidizing compound in the presence of a catalyst capable of catalyzing the oxidation reaction of the olefinic double bond to obtain an intermediate compound containing vicinal diols;b) feeding to a second continuous reactor said intermediate compound, oxygen or a compound containing oxygen, and a catalyst capable of catalyzing the oxidation reaction of said diols to carboxylic groups, to obtain saturated monocarboxylic acids (i) and triglycerides containing saturated monocarboxylic acids with more than one acid function (ii);c) transferring the product of step b) to an apparatus suitable to separate the saturated monocarboxylic acids (i) from ...

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14-02-2019 дата публикации

PROCESS FOR THE SYNTHESIS OF (2E, 4E, 6Z, 8E)-8-(3,4-DIHYDRONAPHTHALEN-1(2H)-YLIDENE)-3,7-DIMETHYLOCTA-2, 4, 6-TRIENOIC ACID

Номер: US20190047933A1
Принадлежит:

This invention relates to a novel method for the synthesis of (2E,4E,6Z,8E)-8-(3,4-dihydronaphthalen-1(2H)-ylidene)-3,7-dimethylocta-2,4,6-trienoic acid. In particular, the invention relates to several improvements in several individual steps of the multi-step synthesis scheme 1. A method for the synthesis of MRZ-20321 comprising one or more of the steps of:(a) synthesizing E-2/Z-2 by performing a bromination of 1 in a solvent selected from benzotrifluoride and 1,3-bis(trifluoromethyl)benzene, particularly benzotrifluoride;(b) lithiating 1;(c) adding tetralone to lithiated 1;(d) synthesizing Z-7 starting from Z-5, wherein said method comprises the step of synthesizing the methyl ester Z-6;(e) reducing Z-6 to obtain Z-7;(f) oxidizing Z-7 with stabilized 2-iodoxybenzoic acid (SIBX);(g) reacting Z-8 with E-3/Z-3 in the presence of a lithium dialkylamide, particularly lithium diisopropylamide or lithium diethylamide, particularly lithium diisopropylamide; and/or(h) recrystallizing MRZ-20321 from isopropanol or from n-heptane or from mixtures of n-heptane and 2-methyl tetrahydrofuran.2. The method of claim 1 , wherein step (a) is performed in benzotrifluoride as solvent.3. The method of or claim 1 , wherein said bromination in step (a) is performed with N-bromosuccinimide.4. The method of claim 3 , wherein said bromination is performed by using a radical initiator selected from azobisisobutyronitrile claim 3 , and dibenzoyl peroxide claim 3 , particularly azobisisobutyronitrile.5. The method of any one of to claim 3 , wherein said lithiating in step (b) is performed by using a lithiating reagent selected from a lithium dialkylamide claim 3 , particularly lithium diisopropylamide or lithium diethylamide; a lithium claim 3 , sodium or potassium salt of bis(trimethylsilyl)amide (HMDS) claim 3 , particularly lithium bis(trimethylsilyl)amide; and lithium tetramethylpiperidine.6. The method of any one of to claim 3 , wherein said step (d) comprises reacting Z-5 with a ...

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12-03-2015 дата публикации

CONTINUOUS PROCESS FOR THE PRODUCTION OF DERIVATIVES OF SATURATED CARBOXYLIC ACIDS

Номер: US20150073162A1
Принадлежит:

Provided is a continuous process for the oxidative cleavage of derivatives of unsaturated carboxylic acids for the production of saturated carboxylic acids and their derivatives which comprises the steps of: 1. A. continuous process for the oxidative cleavage of derivatives of unsaturated carboxylic acids for the production of saturated carboxylic acids , which comprises the steps of:a) feeding to a first continuous reactor at least a derivative of an unsaturated carboxylic acid, an oxidizing compound and a catalyst capable of catalyzing the oxidation reaction of the olefinic double bond to obtain an intermediate compound containing vicinal diols;b) feeding to a second continuous reactor said intermediate compound, a compound containing oxygen and an aqueous phase comprising a catalyst capable of catalyzing the oxidation reaction of the vicinal diols to carboxylic groups, to obtain saturated monocarboxylic acids (i) and derivatives of saturated carboxylic acids with more than one acid function (ii), the output of this second continuous reactor comprising an aqueous phase and an organic phase;b′) separating the aqueous phase from the organic phase of the product obtained as output from step b);c) transferring the organic phase of the product of step b) to an apparatus suitable to separate the saturated monocarboxylic acids (i) from the derivatives of carboxylic acids having more than one acid function (ii)2. The continuous process according to claim 1 , wherein the said step b′) is performed by continuous centrifuging.3. The continuous process according to claim 1 , wherein the said step b′) is performed by means of a disc separator.4. The continuous process according to claim 1 , wherein in step b′) an organic solvent is added to improve the separation of the two phases.5. The continuous process according to of claim 1 , wherein the catalysts of steps a) and b) contained in the aqueous phase of step b′) are recovered and recycled as catalysts of step b).6. The ...

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29-05-2014 дата публикации

Process for Liquid Phase Hydrogenation of Phthalates

Номер: US20140148613A1
Автор: Reine Travis A.

Disclosed is a process for the liquid phase hydrogenation of phthalates to cyclohexanoates. By using a reactor with a multiplicity of tubes, with a cooling fluid supplied to the outside of the tubes, shortcomings of traditional recycle mode fixed bed reactors can be overcome. Feed dilution can be avoided, resulting in much higher reaction rates. 1. A process for the liquid phase hydrogenation of phthalates to cyclohexanoates , the process comprising:(a) feeding a liquid feed comprising phthalates and a gas feed comprising hydrogen to a multiplicity of tubes containing a catalyst;(b) converting at least part of the phthalates to cyclohexanoates in the tubes; and(c) supplying a cooling fluid to the outside of the tubes so as to maintain the temperature in the tubes in a desired range.2. A process according to claim 1 , wherein the temperature is maintained in a range from 90° C. to 170° C.3. A process according to claim 1 , wherein the cooling fluid is subcooled.4. A process according to claim 1 , wherein the cooling fluid is water.5. A process according to claim 1 , wherein the liquid and gas feeds are fed co-currently to the cooling fluid.6. A process according to claim 1 , wherein the liquid and gas feeds are fed counter-currently to the cooling fluid.7. A process according to claim 1 , wherein the tubes are surrounded by a shell and the cooling fluid passes through the shell.8. A process according to claim 1 , wherein the liquid feed comprises 90 to 100% phthalate.9. A process according to claim 1 , wherein the temperature in the tubes is maintained in a range from 105° C. to 120° C.10. A process according to claim 1 , wherein the liquid feed makes a single pass through the tubes.11. A process according to claim 1 , wherein the liquid feed is not mixed with a diluent stream.12. A process according to claim 1 , wherein the volumetric ratio between the gas feed flowrate and the liquid feed flowrate is selected such that flow in the multiplicity of tubes is in the ...

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05-06-2014 дата публикации

Method for the Synthesis of Diacids or Diesters from Natural Fatty Acids and/or Esters

Номер: US20140155647A1
Автор: Jean-Luc Dubois
Принадлежит: Arkema France SA

Disclosed herein a process for the synthesis of diacids or diesters of general formula ROOC—(CH 2 )x-COOR, in which n represents an integer between 5 and 14 and R is either H or an alkyl radical of 1 to 4 carbon atoms, starting from long-chain natural monounsaturated fatty acids or esters comprising at least 10 adjacent carbon atoms per molecule, of formula CH 3 —(CH 2 )n-CHR 1 —CH 2 —CH═CH—(CH 2 )p-COOR, in which R represents H or an alkyl radical comprising from 1 to 4 carbon atoms, R 1 is either H or OH, and n and p, which are identical or different, are indices between 2 and 11.

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05-05-2022 дата публикации

COMPOSITIONS AND METHODS OF PREPARATION THEREOF

Номер: US20220135510A1
Принадлежит:

Described herein are methods of preparing compounds derived from triglycerides or condensation polymers such as polyesters and/or polyamides. The methods may include subjecting triglyceride or condensation polymer containing matter to mechanical processing in the presence of a nucleophile.

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05-04-2018 дата публикации

PROCESS FOR THE PRODUCTION OF ETHYLENICALLY UNSATURATED CARBOXYLIC ACIDS OR ESTERS

Номер: US20180093937A1
Принадлежит:

The present invention relates to a process for the production of an ethylenically unsaturated carboxylic acid or ester, preferably α,β ethylenically unsaturated carboxylic acids or esters, by the liquid phase reaction of formaldehyde or a suitable source thereof with a non-cyclic carboxylic acid ester in the presence of a basic metal salt. 1. A process for production of an ethylenically unsaturated carboxylic acid or ester , unsaturated carboxylic by a liquid phase reaction of formaldehyde or a suitable source thereof with a non-cyclic carboxylic acid ester in the presence of a basic metal salt.2. The process according to claim 1 , wherein the basic metal salt is a group I or a group II metal salt.3. The process according to claim 1 , wherein the basic metal salt is selected from group I or group II metal oxides claim 1 , hydroxides claim 1 , carbonates claim 1 , hydrogen carbonates claim 1 , methyl carbonates claim 1 , alkoxides claim 1 , fluorides and phosphates.4. The process according to claim 1 , wherein the basic metal salt is selected from potassium oxide claim 1 , caesium oxide claim 1 , sodium oxide claim 1 , rubidium oxide claim 1 , barium oxide claim 1 , potassium hydroxide claim 1 , caesium hydroxide claim 1 , sodium hydroxide claim 1 , rubidium hydroxide claim 1 , barium hydroxide claim 1 , potassium phosphate claim 1 , caesium phosphate claim 1 , sodium phosphate claim 1 , rubidium phosphate claim 1 , barium phosphate claim 1 , sodium methoxide claim 1 , potassium methoxide claim 1 , rubidium methoxide claim 1 , sodium t-butoxide claim 1 , potassium t-butoxide claim 1 , rubidium t-butoxide claim 1 , caesium t-butoxide claim 1 , sodium fluoride claim 1 , potassium fluoride claim 1 , rubidium fluoride claim 1 , caesium fluoride claim 1 , potassium carbonate claim 1 , caesium carbonate claim 1 , sodium carbonate claim 1 , rubidium carbonate claim 1 , barium carbonate claim 1 , potassium hydrogen carbonate claim 1 , sodium hydrogen carbonate claim 1 , ...

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06-04-2017 дата публикации

High-Purity Dibasic Acid Compositions and Methods of Making the Same

Номер: US20170096383A1
Принадлежит: Elevance Renewable Sciences Inc

High-purity dibasic acid compositions are generally disclosed. In some embodiments, the dibasic acid compositions are solutions or suspensions. In some other embodiments, the compositions are solid-state compositions. In some such embodiments, the solid-state compositions include a dibasic acid as a crystalline solid and further include a low quantity of certain impurities, such as monobasic acids, various esters, and the like. Methods and systems for making such high-purity dibasic acid compositions are also disclosed.

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14-04-2016 дата публикации

CYCLOPROPANATION OF SUBSTITUTED PHENYLACETONITRILES OR PHENYL ACETATES

Номер: US20160102049A1
Принадлежит:

The present invention relates to a process for the cyclopropanation with ethylene carbonate or ethylene sulfate of a compound of formula (II): wherein G is —CN or —COOR in which R is a C-Cstraight or branched alkyl X and Y are independently selected from the group consisting of hydrogen, fluorine, chlorine, bromine, iodine, RO— and RS— wherein Ris C1-C4 straight or branched alkyl chain. 2. The process according to wherein X is linked to the position 4 and Y to the position 3 of the phenyl ring.3. The process according to wherein G is —CN or —COOEt.4. The process according to wherein X is as defined above and Y is hydrogen or fluorine.5. The process according to wherein X is bromine claim 1 , CHO— or CHS— and Y is hydrogen or fluorine.6. The process according to wherein the base is selected from the group consisting of sodium claim 1 , potassium or lithium tertbutylate claim 1 , potassium carbonate claim 1 , sodium hydride claim 1 , lithium bis(trimethylsilyl)amide (LiHMDS); Lithium diisopropylamide (LDA).7. The process according to wherein Y is CO.8. The process according to wherein the reaction is carried out at a temperature ranging from 130° C. to 180° C.9. The process according to wherein the molar ratio between the compound of formula (II) and the compound of formula (III) is from 1:20 to 1:30.10. The process according to wherein the reaction is carried out in the presence of a compound able to complex alkaline metal cations.11. The process according to wherein the compound able to complex alkaline metal cations is selected from the group consisting of polyethylene glycols (PEG) claim 10 , phosphonium salts claim 10 , crown ethers.12. The process according to wherein the compound able to complex alkaline metal cations is selected from the group consisting of PEG-200 and PEG-6000.13. The process according to wherein the compound of formula (II) and the compound able to complex alkaline metal cations are present in a molar ratio ranging from 1:0.02 to 1:2.14. The ...

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16-04-2015 дата публикации

Bio-Based Acrylic Acid And Its Derivatives

Номер: US20150105584A1
Принадлежит:

Lactic acid, lactic acid derivatives, or mixtures thereof are dehydrated using a catalyst and process to produce bio-acrylic acid, acrylic acid derivatives, or mixtures thereof. A method to produce the catalyst is also provided. 2. A method of preparing a catalyst comprising the following steps:{'sub': 2', '4', '3', '2', '3', '4', '3', '2', '2', '4', '3', '4, 'a. combining KHPO, Ba(NO), and HPOto form a mixture, wherein the molar ratio of Ba(NO), KHPO, and HPOis about 3:1:4;'}b. calcining said mixture at about 450° C. to about 650° C. to produce a dried solid; andc. grinding said dried solid to produce said catalyst.3. A method of preparing a catalyst comprising the following steps:{'sub': 2', '4', '3', '2,', '3', '4', '3', '2', '2', '4', '3', '4, 'a. combining KHPO, Ba(NO)and HPOto form a mixture, wherein the molar ratio of Ba(NO), KHPO, and HPOis about 3:1:4;'}b. calcining said solid mixture at about 450° C. to about 650° C. to produce a dried solid;c. grinding said dried solid to produce a ground solid; andd. contacting said ground solid with a gaseous mixture comprising water and lactic acid at a temperature of about 375° C. and a total pressure of about 10 barg to about 25 barg to produce said catalyst, and wherein the partial pressure of water in said gaseous mixture is about 3.5 bar to about 13 bar.4. A method of making acrylic acid claim 1 , acrylic acid derivatives claim 1 , or mixtures thereof comprising contacting a stream comprising lactic acid claim 1 , lactic acid derivatives claim 1 , or mixtures thereof with the catalyst of claim 1 , wherein said stream further comprises:a. diluent; andb. inert gas selected from the group consisting of air, nitrogen helium, argon, carbon dioxide, carbon monoxide, steam, and mixtures thereof.5. The method of claim 4 , wherein said diluent is water.6. The method of claim 5 , wherein the water partial pressure in said stream is about 10 psi (0.7 bar) or more.7. The method of claim 5 , wherein the water partial pressure ...

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21-04-2016 дата публикации

SYNTHESIS OF INTERMEDIATES FOR PRODUCING PROSTACYCLIN DERIVATIVES

Номер: US20160107973A1
Принадлежит: United Therapeutics Corporation

The present disclosure provides regioselective methods for synthesizing intermediates useful in making prostacyclin derivatives, such as treprostinil. 2. The method of claim 1 , wherein said solution is heated at a temperature ranging from 175° C. to 195° C.3. The method of claim 1 , wherein X is hydrogen or an alkoxy group.4. The method of claim 3 , wherein the organic solvent comprises at least one of triglyme claim 3 , N-methylpyrrolidinone claim 3 , tetradecane claim 3 , tetrahydronaphthalene claim 3 , Dowtherm claim 3 , p-chlorophenol claim 3 , 1 claim 3 ,2-dichlorobenzene claim 3 , and diphenyl ether.7. The method of claim 6 , further comprising forming from the compound of formula 5 treprostinil using a process comprising Pauson-Khand cyclization.8. The method of claim 6 , wherein Ris benzyl or substituted benzyl.9. The method of claim 6 , wherein Ris CHCOOR claim 6 , wherein Ris Calkyl.10. The method of claim 1 , wherein X is OR claim 1 , where Ris Calkyl; unsubstituted or substituted aryl; or unsubstituted or substituted benzyl.11. The method of claim 10 , wherein Ris methyl.12. The method of claim 10 , wherein Ris ethyl.15. The method of claim 14 , further comprising forming from the compound of formula 5 treprostinil using a process comprising Pauson-Khand cyclization.16. The method of claim 14 , wherein Ris benzyl or substituted benzyl.17. The method of claim 14 , wherein Ris CHCOOR.19. The method of claim 18 , further comprising forming from the compound of formula 11 treprostinil using a process comprising Pauson-Khand cyclization.20. The method of claim 18 , wherein Ris Calkyl.21. The method of claim 18 , wherein Ris a phenolic protecting group.22. The method of claim 21 , wherein Ris benzyl. The present application claims priority to U.S. provisional application No. 62/066,009 filed Oct. 20, 2014, which is incorporated herein by reference in its entirety.The present application generally relates to chemical synthetic methods and in particular, to ...

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30-04-2015 дата публикации

METHOD FOR PRODUCING 2-ISOPROPYLIDENE-5-METHYL-4-HEXENYL BUTYRATE

Номер: US20150119597A1
Принадлежит:

Provided is a simple and efficient method for producing 2-isopropylidene-5-methyl-4-hexenyl butyrate. More specifically, provided is a method for producing 2-isopropylidene-5-methyl-4-hexenyl butyrate, the method including the steps of: isomerizing 2-isopropenyl-5-methyl-4-hexenoic acid ester (1) into 2-isopropylidene-5-methyl-4-hexenoic acid ester (2), reducing thus formed 2-isopropylidene-5-methyl-4-hexenoic acid ester (2) into 2-isopropylidene-5-methyl-4-hexenol (3), and butyrylating thus formed 2-isopropylidene-5-methyl-4-hexenol (3) into 2-isopropylidene-5-methyl-4-hexenyl butyrate (4), 3. The method for producing 2-isopropylidene-5-methyl-4-hexenyl butyrate according to claim 1 , wherein the step of isomerizing is carried out in the presence of a base.4. The method for producing 2-isopropylidene-5-methyl-4-hexenyl butyrate according to claim 1 , wherein R is selected from the group consisting of methyl claim 1 , ethyl claim 1 , n-propyl claim 1 , n-butyl claim 1 , cyclopentylmethyl claim 1 , cyclohexylmethyl claim 1 , isopropyl claim 1 , isobutyl claim 1 , sec-butyl claim 1 , t-butyl claim 1 , t-amyl claim 1 , diethylmethylcarbinyl claim 1 , triethylcarbinyl claim 1 , cyclopentyldimethylcarbinyl claim 1 , 1-methyl-1-cyclopentyl claim 1 , 1-methyl-1-cyclohexyl claim 1 , 1-ethyl-1-cyclopentyl claim 1 , 1-ethyl-1-cyclohexyl claim 1 , 1-isopropyl-1-cyclopentyl claim 1 , 1-isopropyl-1-cyclohexyl claim 1 , 1-t-butyl-1-cyclopentyl claim 1 , 1-t-butyl-1-cyclohexyl claim 1 , bicyclo[2.2.1]heptyl claim 1 , 2-methyl-2-bicyclo[2.2.1]heptyl claim 1 , 2-ethyl-2-bicyclo[2.2.1]heptyl claim 1 , isobornyl claim 1 , and 2-bicyclo[2.2.1]heptyldimethylcarbinyl.5. The method for producing 2-isopropylidene-5-methyl-4-hexenyl butyrate according to claim 3 , wherein the base comprises one or more of sodium methoxide claim 3 , sodium ethoxide claim 3 , sodium t-butoxide claim 3 , sodium t-amyloxide claim 3 , lithium methoxide claim 3 , lithium ethoxide claim 3 , lithium t-butoxide ...

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09-06-2022 дата публикации

METHOD FOR PROCESSING BENZENE POLYCARBOXYLIC ACID ESTERS AND USE OF SAME TO PRODUCE CYCLOHEXANE POLYCARBOXYLIC ACID ESTERS

Номер: US20220177405A1
Принадлежит:

The present invention relates to a process for purifying benzenepolycarboxylic esters and for preparing cyclohexanepolycarboxylic esters by hydrogenating the purified benzenepolycarboxylic esters. The invention further relates to benzenepolycarboxylic esters and cyclohexanepolycarboxylic esters having a small proportion of by-products, especially of dialkyl ethers, and especially to diisononyl cyclohexane-1,2-dicarboxylate having a small proportion of diisononyl ether. The invention also relates to the use of the cyclohexanepolycarboxylic esters as plasticizers, especially in products intended for human contact, such as children's toys, food packaging and medical articles. 115.-. (canceled)17. The process according to claim 16 , wherein the crude ester used for workup comprises{'sub': 4', '12, '91% to 99.8% by weight of at least one ester of a benzenepolycarboxylic acid with at least one C-Cmonoalkanol,'}{'sub': 4', '12, '0.05% to 1% by weight of at least one di-(C-C-alkyl) ether,'}{'sub': 4', '12, '0.1% to 5% by weight of at least one C-Cmonoalkanol, and'}0.05% to 3% by weight of water.18. The process according to claim 16 , wherein thermal purification is accomplished using at least one column havinga side feed for the crude ester,a rectifying section above the feed point for the crude ester,a reflux feed for at least a portion of the condensed vapor above the rectifying section,a feed for the steam-containing gas stream in the region of the bottom of the column.19. The process according to claim 18 , wherein the rectifying section above the feed point for the crude ester has 0 to 10 theoretical plates.20. The process according to claim 16 , wherein a third portion of the organic phase is recycled into the esterification of the benzenepolycarboxylic acid with the at least one C-Cmonoalkanol.21. The process according to claim 16 , wherein the discharge of a portion of the organic phase is batchwise or continuous.22. The process according to claim 16 , wherein the ...

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27-05-2021 дата публикации

Isomerization method of cyclohexane dicarboxylic acid

Номер: US20210155572A1
Принадлежит: Hanwha Solutions Corp

Provided is an isomerization method of cyclohexane dicarboxylic acid using zirconia or titania as an isomerization catalyst.

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11-05-2017 дата публикации

OXIDIC COMPOSITION

Номер: US20170128916A1
Принадлежит: BASF SE

An oxidic composition comprising vanadium, tungsten, phosphorus, oxygen and optionally tin, where the molar ratio of phosphorus to the sum total of vanadium, tungsten and any tin in the oxidic composition is in the range from 1.4:1 to 2.4:1. 1. An oxidic composition , comprising; vanadium , tungsten , phosphorus , oxygen and optionally tin , wherein the molar ratio of phosphorus to the sum total of vanadium , tungsten and any tin in the oxidic composition is in the range from 1.4:1 to 2.4:1.2. The oxidic composition according to claim 1 , wherein the molar ratio of phosphorus to the sum total of vanadium claim 1 , tungsten and any tin is in the range from 1.8:1 to 2.3:1.3. The oxidic composition according to claim 1 , wherein the molar ratio of vanadium to tungsten in the oxidic composition is in the range from 10:1 to 1:100.4. The oxidic composition according to claim 1 , wherein the oxidic composition comprises not more than 1000 molar ppm claim 1 , of molybdenum.5. The oxidic composition according to claim 1 , wherein the oxidic composition comprises not more than 1000 molar ppm claim 1 , of bismuth.6. The oxidic composition according to claim 1 , wherein the oxidic composition comprises not more than 1000 molar ppm claim 1 , of titanium.7. The oxidic composition according to claim 1 , wherein the oxidic composition comprises tin.8. The oxidic composition according to claim 7 , wherein the molar ratio of vanadium to tin in the oxidic composition is in the range from 100:1 to 1:100.9. The oxidic composition according to claim 1 , further comprising a support material.10. The oxidic composition according to claim 1 , wherein the oxidic composition is a catalyst.11. The oxidic composition according to claim 1 , wherein the oxidic composition is an unsupported catalyst.12. The oxidic composition according to claim 9 , wherein the oxidic composition is a supported catalyst.13. A process for producing an oxidic composition claim 9 , comprising:providing a support ...

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11-05-2017 дата публикации

ISOMERIZATION OF MUCONIC ACID

Номер: US20170129839A1
Принадлежит:

Various embodiments disclosed relate to isomerization of muconic acid. In various embodiments, the present invention provides a method of forming trans,trans-muconic acid. The method includes heating a starting material composition to form a product composition including trans,trans-muconic acid. The starting material composition includes cis,cis-muconic acid, cis,trans-muconic acid, or a combination thereof. The starting material composition also includes an electrophilic compound, an organic solvent, or a combination thereof. 1. A method of forming trans ,trans-muconic acid , the method comprising: cis,cis-muconic acid, cis,trans-muconic acid, or a combination thereof, and', 'an electrophilic compound, an organic solvent, or a combination thereof., 'heating a starting material composition to form a product composition comprising trans,trans-muconic acid, wherein the starting material composition comprises'}2. The method of claim 1 , wherein the organic solvent is a polar aprotic solvent.3. The method of claim 1 , wherein the organic solvent comprises dimethylsulfoxide (DMSO) claim 1 , acetonitrile (CHCN) claim 1 , tetrahydrofuran (THF) claim 1 , ethyl acetate (EtOAc) claim 1 , dimethylformamide (DMF) claim 1 , γ-valerolactone (GVL) claim 1 , methanol claim 1 , ethanol claim 1 , 2-propanol claim 1 , hexanol claim 1 , toluene claim 1 , or a combination thereof.4. The method of claim 1 , wherein the organic solvent is dimethylsulfoxide (DMSO).5. The method of claim 1 , wherein the starting material composition further comprises water claim 1 , DO claim 1 , or a combination thereof.6. The method of claim 5 , wherein the starting material composition is substantially free of solvents other than DMSO and the water and DO.7. The method of claim 1 , wherein about 0.000001 wt % to about 20 wt % of the starting material composition is water claim 1 , DO claim 1 , or a combination thereof.8. The method of claim 1 , wherein the concentration of the cis claim 1 ,cis-muconic ...

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11-05-2017 дата публикации

PROCESS FOR PREPARING ACRYLIC ACID FROM FORMALDEHYDE AND ACETIC ACID

Номер: US20170129841A1
Принадлежит: BASF SE

The invention relates to a process for preparing acrylic acid from formaldehyde and acetic acid, comprising 1. A process for preparing acrylic acid from formaldehyde and acetic acid , comprising(i) providing a gaseous stream S1 comprising formaldehyde, acetic acid and acrylic acid, where the molar ratio of acrylic acid to the sum total of formaldehyde and acetic acid in stream S1 is in the range from 0.005:1 to 0.3:1;(ii) contacting stream S1 with an aldol condensation catalyst in a reaction zone to obtain a gaseous stream S2 comprising acrylic acid.2. The process according to claim 1 , wherein the molar ratio of acrylic acid to the sum total of formaldehyde and acetic acid in stream S1 in (i) is in the range from 0.02:1 to 0.1:1.3. The process according to claim 1 , wherein the molar ratio of acetic acid:formaldehyde in stream S1 in (i) is in the range from 0.25:1 to 4.4:1.4. The process according to claim 1 , wherein at least 65% by volume of stream S1 in (i) consists of formaldehyde claim 1 , acetic acid claim 1 , acrylic acid claim 1 , water and inert gas.6. The process according to claim 5 , wherein stream S2b is at least partly recycled into the reaction zone in (ii).7. The process according to claim 5 , wherein the acrylic acid content of stream S2b is in the range from 0.01% to 0.5% by volume claim 5 , based on the total volume of stream S2b.8. The process according to claim 5 , further comprising(iv) working up stream S2a to obtain a product stream SP comprising acrylic acid and a recycling stream SR comprising acrylic acid, where the recycling stream SR comprises not more than 10% of the acrylic acid present in stream S2.9. The process according to claim 8 , wherein at least a portion of the recycling stream SR is recycled into the reaction zone in (ii).10. The process according to claim 1 , wherein stream S1 comprises a stream comprising formaldehyde and acetic acid claim 1 , of the recycling stream SR and optionally of stream S2b.11. The process ...

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23-04-2020 дата публикации

METHOD OF MAKING A CROSS METATHESIS PRODUCT

Номер: US20200123197A1
Принадлежит:

Method of making a cross metathesis product, the method comprising at least step (X) or step (Y): (X) reacting in a cross metathesis reaction a first compound comprising a terminal olefinic group with a second compound comprising a terminal olefinic group, wherein the first and the second compound may be identical or may be different from one another; or (Y) reacting in a ring-closing metathesis reaction two terminal olefinic groups which are comprised in a third compound; wherein the reacting in step (X) or step (Y) is performed in the presence of a ruthenium carbene complex comprising a [Ru═C]-moiety and an internal olefin. 1. Method of making a cross metathesis product , the method comprising at least step (X) or step (Y):(X) reacting in a cross metathesis reaction a first compound comprising a terminal olefinic group with a second compound comprising a terminal olefinic group, wherein the first and the second compound may be identical or may be different from one another; or(Y) reacting in a ring-closing metathesis reaction two terminal olefinic groups which are comprised in a third compound;wherein the reacting in step (X) or step (Y) is performed in the presence of a ruthenium carbene complex comprising a [Ru═C]-moiety and an internal olefin which may be a Z-olefin or an E-olefin.2. Method of claim 1 , wherein more than 1 equivalent of said internal olefin is employed per equivalent of said first or second compound claim 1 , respectively said third compound.3. Method of or claim 1 , further comprising step (Z) after step (X) or step (Y):(Z) removing said internal olefin and/or a metathesis product which is formed from said internal olefin in step (X) or step (Y).4. Method of any one of the preceding claims claim 1 , wherein said internal olefin is a Colefin.5. Method of any one of the preceding claims claim 1 , wherein said internal olefin is Z-2-butene or E-2-butene.6. Method of any one of the preceding claims claim 1 , wherein the first claim 1 , the second ...

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08-09-2022 дата публикации

RECYCLE CONTENT (C4)ALKANOIC ACID

Номер: US20220281796A1
Принадлежит: EASTMAN CHEMICAL COMPANY

A process for preparing a recycle content (C)alkanoic acid (i.e., butyric acid and/or isobutyric acid) derived from a recycle propylene composition, a recycle (C)alkanal are provided. 147-. (canceled)48. A method of making recycle (C)alkanoic acid (r-(C)alkanoic acid) , said method comprising carboxylating a recycle propylene composition (r-propylene) to thereby produce a carboxylation effluent comprising (C)alkanoic acid , wherein said r-propylene is derived directly or indirectly from cracking recycle pyoil composition (r-pyoil).49. A method of making recycle (C)alkanoic acid (r-(C)alkanoic acid) , said method comprising oxidizing a recycle (C)alkanal (r-(C)alkanal) to thereby produce an oxidation effluent comprising (C)alkanoic acid , wherein said r-(C)alkanal is produced from a recycled propylene composition (r-propylene) and said r-propylene is derived directly or indirectly from cracking recycle pyoil composition (r-pyoil).50. A method of obtaining a recycle content in (C)alkanoic acid comprising:method 1:a. obtaining a propylene composition designated as having recycle content, and{'sub': '4', 'claim-text': 'wherein, whether or not the designation so indicates, at least a portion of said propylene composition is derived directly or indirectly from cracking a recycle pyoil composition (r-pyoil); or', 'b. feeding said propylene to a reactor under conditions effective to make (C)alkanoic acid, and'}method 2:{'sub': '4', 'a. obtaining an (C)alkanal designated as having recycle content, and'}{'sub': 4', '4, 'claim-text': {'sub': '4', 'wherein, whether or not the designation so indicates, at least a portion of said (C)alkanal is produced from a recycle propylene composition that is derived directly or indirectly from cracking a recycle pyoil composition (r-pyoil).'}, 'b. feeding said (C)alkanal to a reactor under conditions effective to make (C)alkanoic acid, and'}51. The method of claim 48 , wherein the r-propylene is directly or indirectly derived from cracking r ...

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02-06-2016 дата публикации

PROCESS FOR PREPARING ACRYLIC ACID

Номер: US20160152541A1
Принадлежит: BASF SE

The present invention relates to a process for preparing acrylic acid from acetic acid and formaldehyde, which comprises (a) provision of a stream S comprising acetic acid and formaldehyde, where the molar ratio of acetic acid to formaldehyde in the stream S is in the range from 0.5:1 to 2:1; (b) contacting of the stream S with an aldol condensation catalyst comprising vanadium, phosphorus and oxygen to give a stream S comprising acrylic acid, where, in (b), the space velocity WHSV is in the range from 0.35 to 7.0 kg/kg/h. 1. A process for preparing acrylic acid from acetic acid and formaldehyde , the process comprising:{'b': 1', '1, '(a) providing a stream S comprising acetic acid and formaldehyde, where a molar ratio of acetic acid to formaldehyde in the stream S is in a range of from 0.5:1 to 2:1;'}{'b': 1', '2, '(b) contacting the stream S with an aldol condensation catalyst comprising vanadium, phosphorus and oxygen to give a stream S comprising acrylic acid,'}where, in (b), a space velocity WHSV, defined as ([formaldehyde]+[acetic acid])/[aldol condensation catalyst]/time, is in a range of from 0.35 to 7.0 kg/kg/h, wherein [formaldehyde], [acetic acid], and [aldol condensation catalyst] represent mass of formaldehyde, acetic acid, and the aldol condensation catalyst, respectively.2. The process according to claim 1 , wherein a content of vanadium in the aldol condensation catalyst as per (b) is in a range of from 2 to 20% by weight claim 1 , a content of phosphorus is in a range of from 2 to 20% by weight claim 1 , and a content of oxygen is in a range of from 20 to 60% by weight claim 1 , in each case based on a total weight of the aldol condensation catalyst.3. The process according to claim 1 , wherein the aldol condensation catalyst as per (b) additionally comprises a support material.4. The process according to claim 1 , wherein the aldol condensation catalyst as per (b) additionally comprises at least one further element M selected from the group ...

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15-06-2017 дата публикации

Process for ruthenium-catalysed transvinylation of carboxylic acids

Номер: US20170166511A1
Принадлежит: Wacker Chemie AG

A process for selective transvinylation of a reactant carboxylic acid with a reactant vinyl ester to give a product vinyl ester and the corresponding acid of the reactant vinyl ester in the presence of one or more ruthenium catalysts, wherein a) the reactant vinyl ester, the reactant carboxylic acid and the ruthenium catalyst are supplied to a reactor, wherein b) the molar ratio of reactant vinyl ester to reactant carboxylic acid is 1:3 to 3:1, and c) the transvinylation reaction is conducted, d) on completion of the transvinylation reaction, the reactant vinyl ester and the corresponding acid are separated from the reaction mixture by distillation, e) the product vinyl ester is separated by distillation from the bottom product of the distillation, and f) the remaining reaction mixture is recycled into the reactor.

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15-06-2017 дата публикации

METHOD FOR CHEMICAL CONVERSION OF UNSATURATED FATTY ACID BY CARBON CHAIN EXTENSION REACTION

Номер: US20170166512A1
Принадлежит: Bizen Chemical Co., Ltd.

The present invention relates to a method for the chemical conversion of an unsaturated fatty acid, particularly a carbon chain extension reaction. According to the present invention, a method for extending the length of a carbon chain in an unsaturated fatty acid by two carbon atoms is provided, said method comprising a step of heating a malonic acid ester derivative of an unsaturated fatty acid to reflux in a lower fatty acid solution in the presence of an antioxidative agent. It is preferred that the unsaturated fatty acid is an unsaturated fatty acid having 16 to 24 carbon atoms. It is preferred that the unsaturated fatty acid is selected from the group consisting of linoleic acid, linolenic acid, arachidonic acid, stearidonic acid, icosatetraenoic acid, icosapentaenoic acid, tetracosahexaenoic acid and docosahexaenoic acid. According to the method of the present invention, a carbon chain extension reaction can be completed within a shorter time. 1. A method of extending a carbon chain of an unsaturated fatty acid by two carbons , comprising reacting a malonic ester derivative obtained from the unsaturated fatty acid with a lower fatty acid in the presence of an antioxidant.2. (canceled)3. (canceled)4. (canceled)5. (canceled)6. (canceled)7. (canceled)8. (canceled)9. A method of extending a carbon chain of an unsaturated fatty acid by two carbons , comprising reacting a malonic ester derivative obtained from the unsaturated fatty acid with a lower fatty acid.10. The method of or , wherein the unsaturated fatty acid is an unsaturated fatty acid with 16-24 carbons.11. The method of or , wherein the unsaturated fatty acid is selected from the group selected from linoleic acid , linolenic acid , arachidonic acid , stearidonic acid , icosatetraenoic acid , icosapentaenoic acid , tetracosahexaenoic acid , and docosahexaenoic acid.12. The method of or , wherein the malonic ester derivative is a derivative selected from the group consisting of a diethyl malonate ...

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23-06-2016 дата публикации

PROCESS FOR PREPARING ACRYLIC ACID FROM FORMALDEHYDE AND ACETIC ACID

Номер: US20160176797A1
Принадлежит: BASF SE

The present invention relates to a process for preparing acrylic acid from formaldehyde and acetic acid, comprising reacting formaldehyde and acetic acid via an aldol condensation in a reaction unit comprising n reaction zones arranged in series, each comprising an aldol condensation catalyst, where n is at least 2, and wherein at least one stream leaving a reaction zone, before being fed into the reaction zone immediately downstream, is mixed with a stream comprising formaldehyde and optionally comprising acetic acid. The present invention further relates to an apparatus for preparing acrylic acid from formaldehyde and acetic acid and to the use of this apparatus. 1. A process for preparing acrylic acid from formaldehyde and acetic acid , comprising{'b': '0', '(a) providing a stream S() comprising formaldehyde and acetic acid;'}{'b': 0', '0, 'claim-text': (i) feeding a stream S(x−1) into the reaction zone R(x);', '(ii) contacting the stream S(x−1) with the aldol condensation catalyst present in the reaction zone R(x) to obtain a stream S(x) comprising acrylic acid;', '(iii) removing the stream S(x) from the reaction zone R(x);, '(b) reacting formaldehyde present in S() with acetic acid present in S() by means of an aldol condensation in a reaction unit comprising n reaction zones R(x) arranged in series, each comprising an aldol condensation catalyst, where n is at least 2, to obtain a stream S(n) comprising acrylic acid from the last reaction zone R(n) of the reaction unit comprising the n reaction zones arranged in series, wherein the process comprises, for each reaction zone R(x) of the reaction unit comprising the n reaction zones arranged in serieswhere, when x is less than n, the stream S(x) additionally comprises acetic acid and, downstream of at least one of the reaction zones R(x), the stream leaving this reaction zone R(x) as stream S(x), before being fed into the reaction zone R(x+1) immediately downstream, is mixed with a stream Z(x) comprising ...

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29-06-2017 дата публикации

METHOD FOR PRODUCING RENEWABLE MIDDLE-DISTILLATE COMPOSITION, USE OF THE COMPOSITION AND FUEL CONTAINING THE SAME

Номер: US20170183593A1
Принадлежит: Neste Oyj

The present invention provides a fuel comprising a renewable middle distillate composition obtainable by hydrodeoxygenation of a feedstock comprising levulinic acid dimers/oligomers and fractionated distillation. The renewable middle distillate composition contains less than 10.0 wt.-% aromatics. 1. A fuel comprising:a renewable middle distillate composition, wherein the renewable middle distillate composition is obtained from a feedstock having dimers and/or oligomers of levulinic acid and/or of levulinic acid derivatives (levulinic acid dimers/oligomers), subjected to hydrodeoxygenation followed by fractionated distillation, wherein the renewable middle distillate composition contains less than 10.0 wt.-% aromatics, as determined in accordance with ASTM D2425.2. The fuel according to claim 1 , wherein the renewable middle distillate composition contains at most 9.5 wt.% of aromatics claim 1 , as determined in accordance with ASTM D2425.3. The fuel according to claim 1 , wherein the freezing point of the renewable middle distillate composition is −70° C. or lower.4. The fuel according to claim 1 , wherein the renewable middle distillate composition contains at least 50 wt. % of cycloparaffins claim 1 , as determined in accordance with ASTM D2425.5. The fuel according to claim 1 , wherein the renewable middle distillate composition contains at most 80 wt.% of cycloparaffins claim 1 , as determined in accordance with ASTM D2425.6. The fuel according to claim 1 , wherein the fuel further contains fossil fuel claim 1 , HEFA (hydroprocessed ester and fatty acids) fuel and/or HVO (hydrotreated vegetable oil) fuel.7. The fuel according to claim 1 , wherein the BOCLE lubricity of the renewable middle distillate composition is 0.75 mm or less as determined in accordance with ASTM D5001-10 (2014).8. A method for production of a renewable middle distillate composition claim 1 , the method comprising:subjecting a feedstock containing dimers and/or oligomers of levulinic acid ...

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18-09-2014 дата публикации

PROCESS FOR ISOMERIZATION AND DECARBOXYLATION OF UNSATURATED ORGANIC COMPOUNDS WITH A METAL CATALYST OR CATALYST PRECURSOR

Номер: US20140275592A1

Disclosed is the use of a metal catalyst or catalyst precursor that catalyzes the isomerization of an unsaturated fatty acid, unsaturated fatty acid derivative, or an unsaturated triglyceride. Also disclosed is the use of a metal catalyst or catalyst precursor that catalyzes the decarboxylation of an unsaturated organic compound. Also disclosed is the use of a catalyst or catalyst precursor for the dual function isomerization and decarboxylation of an unsaturated fatty acid to an unsaturated organic compound. 1. A process for the production of an isomerized unsaturated organic compound , the process comprising contacting an unsaturated fatty acid , unsaturated fatty acid derivative , or an unsaturated triglyceride in the presence of a catalyst or catalyst precursor containing a ruthenium or osmium compound at a temperature at which isomerization occurs and recovering the isomerized unsaturated organic compound product , wherein the isomerization does not require the step of adding a carboxylic acid anhydride and the catalyst or catalyst precursor does not contain a phosphine ligand.2. The process of comprising the additional step of contacting an additional acid to said unsaturated fatty acid claim 1 , unsaturated fatty acid derivative claim 1 , alkene claim 1 , or an unsaturated triglyceride in the presence of a catalyst or catalyst precursor.3. The process of wherein the additional acid is a monocarboxylic acid.4. The process of wherein the monocarboxylic acid is benzoic acid claim 3 , cinnamic acid claim 3 , propanoic acid claim 3 , undecanoic acid claim 3 , acetic acid claim 3 , stearic acid claim 3 , or oleic acid.5. The process of wherein the catalyst or catalyst precursor contains ruthenium and osmium compounds.6. The process of wherein the ruthenium catalyst or catalyst precursor compound is selected from the group consisting of ruthenium carbonyl or ruthenium chloride.7. The process of wherein the osmium catalyst or catalyst precursor compound is osmium ...

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27-06-2019 дата публикации

Synthesis of Azelaic Acid

Номер: US20190194115A1
Принадлежит: PCI Synthesis, Inc.

This invention concerns a method of synthesizing Azelaic Acid. Particular reference is made to providing a new synthetic process for preparing azelaic acid in large scale with high purity (e.g., >99.7% with any individual impurity not more than 0.1%), which can be used as an active pharmaceutical ingredient. 1. A process for manufacturing azelaic acid comprising the step of:(a) decarboxylating heptane-1,1,7,7-tetracarboxylic acid with an organic base;thereby forming azelaic acid.2. (canceled)3. The process of claim 1 , wherein the organic base is triethylamine claim 1 , trimethylamine claim 1 , methylamine claim 1 , di-isopropyl ethylamine claim 1 , diethylamine claim 1 , propylamine claim 1 , butylamine claim 1 , tripropylamine claim 1 , ethylmethylamine claim 1 , ethylamine claim 1 , diethylmethylamine claim 1 , phenylamine claim 1 , alanine claim 1 , aniline claim 1 , ammonia claim 1 , dimethylaminopyridine or pyridine.4. The process of claim 1 , wherein the organic base is triethylamine.5. The process of claim 1 , wherein the organic base is at a molar/molar ratio of bases with respect to carboxylic acids from about 0.6 to about 2.6. The process of claim 1 , wherein the decarboxylation is performed using a solvent having a boiling temperature of at most about 200° C.7. The process of claim 1 , wherein the solvent is toluene claim 1 , tetrahydrofuran claim 1 , methyl tert-butyl ether claim 1 , dimethylsulfoxide claim 1 , acetonitrile claim 1 , 1 claim 1 ,2-dimethoxyethane claim 1 , dioxane claim 1 , benzene claim 1 , xylenes claim 1 , methyl t-butyl ether claim 1 , methylene chloride claim 1 , chloroform claim 1 , methyl ethyl ketone claim 1 , methyl isobutyl ketone claim 1 , acetone claim 1 , acetonitrile claim 1 , benzene claim 1 , N claim 1 ,N-dimethylformamide claim 1 , N claim 1 ,N-dimethylacetamide claim 1 , N-methylpyrrolidinone claim 1 , hexane claim 1 , heptane claim 1 , or xylene.8. The process of claim 1 , wherein the decarboxylation is performed at a ...

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04-08-2016 дата публикации

METHOD FOR CATALYTIC CONVERSION OF KETOACIDS VIA KETOACID DIMER INTERMEDIATE AND HYDROTREATMENT TO HYDROCARBONS

Номер: US20160221912A1
Принадлежит: Neste Oyj

The present invention relates to catalytic conversion of ketoacids, including methods for increasing the molecular weight of ketoacids. The method can include providing in a reactor a raw material having at least one ketoacid. The raw material is then subjected to one or more C-C-coupling reaction(s) in the presence of an ion exchange resin catalyst to produce at least one ketocid dimer. The method can include providing in a reactor a feedstock having the at least one ketoacid dimer and subjecting the feedstock to one or more C-C-coupling reaction(s) at a temperature of at least 200° C. 1. A method for increasing the molecular weight of a ketoacid , the method comprising:providing in a reactor a raw material comprising having at least one ketoacid;subjecting the raw material to first C-C-coupling reaction(s) in a presence of an ion exchange resin catalyst so as to produce at least one ketoacid dimer;providing in a reactor a feedstock having the at least one ketoacid dimer; andsubjecting the feedstock to second C-C-coupling reaction(s) at a temperature of at least 200° C.2. The method according to claim 1 , wherein the at least one ketoacid dimer is a dimer of a γ-ketoacid; and/orwherein the content of the at least one ketoacid dimer in the feedstock is at least 30 wt-%.3. The method according to claim 1 , wherein the first and second C-C-coupling reaction(s) are conducted in first and second reactors claim 1 , respectively.4. The method according to claim 1 , wherein the content of water in the feedstock is less than 15.0 wt %.5. The method according to claim 1 , wherein the at least one ketoacid in the raw material is γ-ketoacid claim 1 , preferably levulinic acid; and/orwherein an average pore diameter of the ion exchange resin catalyst in the range of 150-300 Å; and/orwherein the first C-C-coupling reaction(s) are conducted at a temperature in the range of 100-190° C.6. The method according to claim 1 , wherein the raw material is subjected to the first C-C- ...

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16-10-2014 дата публикации

Cyclic Alkyl Amino Carbene (CAAC) Ruthenium Complexes as Improved Catalysts for Ethenolysis Reactions

Номер: US20140309433A1
Принадлежит:

Described herein are compounds and methods of catalyzing ethenolysis reactions, optionally on an industrial scale. In certain embodiments, the catalysts bear cyclic alkyl amino carbene (CAAC) ligands with an ortho substituent, such as a methyl substituent, on an N-aryl ring. When used to catalyze ethenolysis reactions, certain such compounds produce a turnover number greater than 50,000. 2. The compound of claim 1 , wherein X is chloro.3. The compound of claim 1 , wherein Ris methyl.4. The compound of claim 1 , wherein Ris ethyl or methyl.5. The compound of claim 1 , wherein the compound is a compound of Formula I or a compound of Formula II; and Ris ethyl or methyl.6. The compound of claim 1 , wherein the compound is a compound of Formula I or a compound of Formula II; and Ris phenyl.7. The compound of claim 1 , wherein the compound is a compound of Formula I or a compound of Formula II; and Rand R claim 1 , taken together with the carbon atom to which they are attached claim 1 , form a cyclohexyl ring.8. The compound of claim 1 , wherein Ris methyl claim 1 , ethyl claim 1 , iso-propyl claim 1 , or tert-butyl.9. The compound of claim 1 , wherein the compound is a compound of Formula I; and Ris H or methyl.10. The compound of claim 1 , wherein Ris iso-propyl.11. The compound of claim 1 , wherein the compound is a compound of Formula III; and Ris phenyl.12. The compound of claim 1 , wherein the compound is a compound of Formula IV; and Ris n-propyl.14. A method of producing an olefin product comprising:providing an olefinic substrate;providing an alpha olefin;{'claim-ref': {'@idref': 'CLM-00001', 'claim 1'}, 'contacting the olefinic substrate with the alpha olefin in the presence of a compound of under reaction conditions effective to allow a metathesis reaction to occur, thereby producing the olefin product.'}15. The method of claim 14 , wherein the olefin product is a terminal olefin product.16. The method of claim 14 , wherein the olefinic substrate comprises at ...

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07-09-2017 дата публикации

Methods for Preparing Phenolic Branched Chain Alkyl Fatty Acids or Esters Thereof and Methods for Killing Microorganisms

Номер: US20170253552A1

Disclosed are methods for preparing phenolic branched chain fatty acids or alkyl esters thereof, involving subjecting in a pressurized container (a) at least one phenolic compound, (b) unsaturated fatty acids having 6 to 25 carbon atoms, alkyl esters thereof, or mixtures thereof, and (c) H-ferrierite zeolite catalyst in the presence of distilled water or alcohol and a nitrogen atmosphere at a temperature of about 100° C. to about 400° C. and a pressure of about 10 to about 1000 psi, and isolating saturated phenolic branched chain fatty acids or alkyl esters thereof or mixtures thereof. Also disclosed are methods for killing microorganisms on or in an object, involving contacting said object with an effective microorganisms killing amount of a composition comprising phenolic branched chain fatty acids or alkyl esters thereof, and optionally a carrier; the phenolic branched chain fatty acids or alkyl esters thereof may be produced by the methods described herein.

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11-11-2021 дата публикации

METHOD OF MAKING CYCLOBUTANE-1, 2-DIACIDS DEGRADABLE BUILDING BLOCKS FOR MATERIALS

Номер: US20210347718A1
Автор: Chu Qianli, Wang Zhihan
Принадлежит: University of North Dakota

A method of making cyclobutane-1,2-diacid building blocks includes using trans-cinnamic acid in its beta form (head to head packing) and photodimerizing the trans-cinnamic acid to create cis-cyclobutane-1,2-dicarboxylic acid (CBDA). 1. A method of making a cis-cyclobutane-1 ,2-dicarboxylic acid monomer comprises:a. melting trans-cinnamic acid;b. dissolving trans-cinnamic acid from step a in an organic solvent to form a trans-cinnamic acid solution;c. mixing the trans-cinnamic acid solution from step b into a poor solvent to create a slurry; andd. irradiating the slurry from step c with a UV irritation source to photo-dimerize β-trans-cinnamic acid and form cis-cyclobutane-1,2-dicarboxylic acid.2. The method of claim 1 , wherein melting is done between 134 and 240 degrees Celsius in step a.3. The method of claim 1 , wherein the organic solvent is selected from the group consisting of dimethylformamide claim 1 , dimethyl sulfoxide claim 1 , diethylformamide claim 1 , N-methyl-2-pyrrolidone tetrahydrofuran claim 1 , acetonitrile claim 1 , and alcohols in step b.4. The method of claim 1 , wherein dissolving trans-cinnamic acid in the organic solvent comprises heating the trans-cinnamic acid in the organic solvent.5. The method of claim 1 , wherein dissolving trans-cinnamic acid in the organic solvent comprises sonicating the trans-cinnamic acid in the organic solvent.6. The method of claim 1 , further comprising filtering the trans-cinnamic acid solution between steps b and c to avoid formation of α-trans-cinnamic acid.7. The method of claim 1 , wherein the poor solvent is selected from the group consisting of ice water claim 1 , brine claim 1 , hexane claim 1 , cyclohexane claim 1 , pentane claim 1 , heptane claim 1 , and petroleum ether.8. The method of claim 1 , wherein the poor solvent has a temperature lower than 15 degrees Celsius.9. The method of claim 1 , wherein mixing the trans-cinnamic acid solution into the poor solvent in step c comprises adding the ...

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04-10-2018 дата публикации

Methods for Preparing Phenolic Branched Chain Alkyl Fatty Acids or Esters Thereof and Methods for Killing Microorganisms

Номер: US20180282254A1
Принадлежит:

Disclosed are methods for preparing phenolic branched chain fatty acids or alkyl esters thereof, involving subjecting in a pressurized container (a) at least one phenolic compound, (b) unsaturated fatty acids having 6 to 25 carbon atoms, alkyl esters thereof, or mixtures thereof, and (c) H-ferrierite zeolite catalyst in the presence of distilled water or alcohol and a nitrogen atmosphere at a temperature of about 100° C. to about 400° C. and a pressure of about 10 to about 1000 psi, and isolating saturated phenolic branched chain fatty acids or alkyl esters thereof or mixtures thereof. Also disclosed are methods for killing microorganisms on or in an object, involving contacting said object with an effective microorganisms killing amount of a composition comprising phenolic branched chain fatty acids or alkyl esters thereof, and optionally a carrier; the phenolic branched chain fatty acids or alkyl esters thereof may be produced by the methods described herein. 1. (canceled)2. (canceled)3. (canceled)4. (canceled)5. (canceled)6. (canceled)7. (canceled)8. (canceled)9. (canceled)10. (canceled)11. (canceled)12. (canceled)13. (canceled)14. (canceled)15. (canceled)16. A method for killing microorganisms on or in an object , said method comprising contacting said object with an effective microorganisms killing amount of a composition comprising phenolic branched chain fatty acids or alkyl esters thereof , and optionally a carrier.17. The method according to claim 16 , wherein said phenolic branched chain fatty acids or alkyl esters thereof is produced by a method comprising subjecting in a pressurized container (a) at least one phenolic compound claim 16 , (b) unsaturated fatty acids having 6 to 25 carbon atoms claim 16 , alkyl esters thereof claim 16 , or mixtures thereof claim 16 , and (c) H-ferrierite zeolite catalyst in the presence of distilled water or alcohol and a nitrogen atmosphere at a temperature of about 100° C. to about 400° C. and a pressure of about 10 to ...

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13-10-2016 дата публикации

NITRIDED MIXED OXIDE CATALYST SYSTEM AND A PROCESS FOR THE PRODUCTION OF ETHYLENICALLY UNSATURATED CARBOXYLIC ACIDS OR ESTERS

Номер: US20160297739A1
Принадлежит:

The invention relates to a method of producing an ethylenically unsaturated carboxylic acid or ester, preferably an α, β ethylenically unsaturated carboxylic acid or ester. The method includes contacting formaldehyde or a suitable source thereof with a carboxylic acid or ester in the presence of a catalyst and optionally in the presence of an alcohol. The catalyst comprises a nitrided metal oxide having at least two types of metal cations, Mand M, wherein Mis selected from the metals of group 2, 3, 4, 13 (called also IIIA) or 14 (called also IVA) of the periodic table and M2 is selected from the metals of groups 5 or 15 (called also VA) of the periodic table. The invention extends to a catalyst system. 1. A method of producing an ethylenically unsaturated carboxylic acid or ester comprising the steps of contacting formaldehyde or a suitable source thereof with a carboxylic acid or ester in the presence of a catalyst and optionally in the presence of an alcohol , wherein the catalyst comprises a nitrided metal oxide having at least two types of metal cations , Mand M , wherein Mis selected from the metals of group 3 , 4 , 13 (called also IIIA) or 14 (called also IVA) of the periodic table and Mis selected from the metals of groups 5 or 15 (called also VA) of the periodic table.2. A method according to claim 1 , wherein the nitrided metal oxide consists of two to four metal cations claim 1 , and oxygen and nitrogen anions.3. A method according to claim 1 , wherein the Mtype of metal is selected from one or more metals in the list consisting of:—B claim 1 , Al claim 1 , Ga claim 1 , In claim 1 , Tl claim 1 , Sc claim 1 , Y claim 1 , La claim 1 , Ac claim 1 , Si claim 1 , Ge claim 1 , Sn claim 1 , Pb claim 1 , Ti claim 1 , Zr claim 1 , Hf and Rf.4. A method according to claim 1 , wherein the Mtype of metal is selected from one or more metals in the list consisting of:—P(5+) claim 1 , Nb(5+) claim 1 , As(5+) Sb(5+) and Ta(5+).5. A method according to claim 1 , wherein ...

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26-11-2015 дата публикации

Method for synthesising biobased unsaturated acids

Номер: US20150336871A1
Принадлежит: Oleon Sas, OMEGA CAT SYSTEM

The invention relates to a method for preparing a compound of formula (I), wherein n is an integer from 1 to 21, said method comprises reacting a light olefin fraction, in the presence of a metathesis catalyst, with a compound having from 10 to 24 carbon atoms, of the following formula (II): wherein, n is an integer from 1 to 21, R corresponds to a hydrogen atom or an alkyl or alkenyl chain from 1 to 20 carbon atoms optionally substituted by at least one hydroxyl group, said compound of formula (II) being used alone or in a mixture of compounds of formula (II).

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26-11-2015 дата публикации

Methods Of Making Fused Ring Compounds

Номер: US20150336922A1
Автор: He Meng, Kumar Anil
Принадлежит:

The present invention relates to methods of making fused ring compounds, such as indeno-fused naphthols, and fused ring indenopyran compounds, such as indeno-fused naphthopyrans, that each employ an unsaturated compound represented by the following Formula II. 111-. (canceled)14. The method of claim 13 , wherein claim 13 ,{'sup': 1', '2, 'sub': 1', '6', '3', '7', '1', '5', '10, 'Rfor each m, and Rfor each n, are in each case independently selected from C-Calkyl, C-Ccycloalkyl, C-Chaloalkyl, fluoro, chloro, and —O—R′,'}{'sup': 3', '4, 'sub': 1', '8', '1', '8', '3', '7, 'Rand Rare each independently selected from hydrogen, C-Calkyl, C-Chaloalkyl, and C-Ccycloalkyl, and'}{'sub': 1', '6, 'B and B′ are each independently selected from aryl substituted with C-Calkoxy, and aryl substituted with morpholino.'}1720-. (canceled) This application claims the benefit of U.S. Provisional Patent Application No. 61/459,613, filed on Dec. 16, 2010 which is incorporated herein by reference in its entirety.The present invention relates to methods of making fused ring compounds and fused ring indenopyran compounds that each involve the use of certain unsaturated compounds.Indeno-fused ring compounds, such as A and B ring fused inden-6-ol compounds, have many uses, such as intermediates in the synthesis of photochromic compounds and materials, such as indeno-fused ring pyran compounds, including A and B ring fused indenopyran compounds. Photochromic materials, such as indeno-fused naphthopyrans, in response to certain wavelengths of electromagnetic radiation (or “actinic radiation”), typically undergo a transformation from one form or state to another form, with each form having a characteristic or distinguishable absorption spectrum associated therewith. Typically, upon exposure to actinic radiation, many photochromic materials are transformed from a closed-form, which corresponds to an unactivated (or bleached, e.g., substantially colorless) state of the photochromic material, to an ...

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03-12-2015 дата публикации

PROCESS FOR PREPARING ACRYLIC ACID USING AN ALUMINUM-FREE ZEOLITIC MATERIAL

Номер: US20150343431A1
Принадлежит: BASF SE

The present invention relates to a process for preparing acrylic acid comprising (i) providing a stream comprising a formaldehyde source and acetic acid and (ii) contacting this stream with an aldol condensation catalyst comprising a zeolitic material, wherein the framework structure of the zeolitic material in (ii) includes Si and O, and has a molar Al:Si ratio of 0:1 to 0.001:1, and wherein the framework structure of the zeolitic material in (ii), in addition to Si and any Al, comprises one or more elements selected from the group consisting of tetravalent elements Y other than Si and trivalent elements X other than Al. 1. A process for preparing acrylic acid , the process comprisingcontacting a stream S4 comprising a formaldehyde source and acetic acid with an aldol condensation catalyst comprising a zeolitic material to obtain a stream S6 comprising acrylic acid;whereina framework structure of the zeolitic material comprises Si, O, and optionally Al, andone or more elements selected from the group consisting of a tetravalent element Y other than Si and a trivalent element X other than Al; andthe framework structure of the zeolitic material has a molar Al:Si ratio of from 0:1 to 0.001:1.2. The process according to claim 1 , wherein the framework structure of the zeolitic material comprises YOwhere Y is optionally selected from the group consisting of Sn claim 1 , Ti claim 1 , Zr claim 1 , Ge claim 1 , V and any combination thereof.3. The process according to claim 1 , wherein the framework structure of the zeolitic material comprises XOwhere X is optionally selected from the group consisting of B claim 1 , In claim 1 , Ga claim 1 , Fe claim 1 , Ta and any combination thereof.4. The process according to claim 1 , wherein the zeolitic material comprises one or more non-framework elements Z selected from the group consisting of Ti claim 1 , Zr claim 1 , V claim 1 , Nb claim 1 , Ta claim 1 , Cr claim 1 , Mo claim 1 , W claim 1 , Mn claim 1 , Fe claim 1 , Co claim 1 , ...

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10-12-2015 дата публикации

PRODUCTION OF METHACRYLIC ACID

Номер: US20150353462A1
Автор: LANGE Jean-Paul
Принадлежит:

The invention relates to a process for producing methacrylic acid, comprising: converting a C3-oxygenate into propanoic acid, wherein said C3-oxygenate is a compound selected from the group consisting of 1-propanol, monopropylene glycol, monohydroxyacetone, 2-hydroxypropanal, glycerol and dihydroxyacetone; and reacting the propanoic acid with formaldehyde or a precursor of formaldehyde into methacrylic acid. Said C3-oxygenate preferably contains 2 oxygen atoms, and most preferably it is monopropylene glycol. 1. Process for producing methacrylic acid , comprising:converting a C3-oxygenate into propanoic acid, wherein said C3-oxygenate is a compound selected from the group consisting of 1-propanol, monopropylene glycol, monohydroxyacetone, 2-hydroxypropanal, glycerol and dihydroxyacetone; andreacting the propanoic acid with formaldehyde or a precursor of formaldehyde into methacrylic acid.2. Process according to claim 1 , wherein the C3-oxygenate is selected from the group consisting of 1-propanol claim 1 , monohydroxyacetone claim 1 , 2-hydroxypropanal claim 1 , glycerol and dihydroxyacetone.3. Process according to claim 1 , wherein the C3-oxygenate contains 2 oxygen atoms.4. Process according to claim 3 , wherein the C3-oxygenate containing 2 oxygen atoms is monopropylene glycol claim 3 , monohydroxyacetone or 2-hydroxypropanal claim 3 , preferably monopropylene glycol.5. Process according to any one of to claim 3 , wherein the C3-oxygenate originates from converting a renewable feedstock into the C3-oxygenate.6. Process according to claim 5 , wherein the renewable feedstock is a sugar source claim 5 , preferably sucrose claim 5 , glucose claim 5 , xylose or fructose (or from glycerol from triglycerides?).7. Process according to any one of to claim 5 , wherein the C3-oxygenate is a C3-diol claim 5 , preferably monopropylene glycol claim 5 , comprising:converting the C3-diol into propanal;converting the propanal into propanoic acid; andreacting the propanoic acid ...

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10-12-2015 дата публикации

PROCESS FOR THE PREPARATION OF 4-METHYLPENT-3-EN-1-OL DERIVATIVES

Номер: US20150353463A1
Принадлежит: FIRMENICH SA

The present invention concerns a process for the preparation with high selectivity of a compound of formula (I) by isomerization at room temperature of compound of formula (II) in the presence of a complex of formula [Ru(dienyl)H]X. 3. A process according to claim 1 , characterized in that said X represents a CHOH group.4. A process according to claim 1 , characterized in that said A represents NO claim 1 , HSO claim 1 , BF claim 1 , PF claim 1 , SbF claim 1 , AsF claim 1 , F or RSO wherein Ris a fluoride atom or a Calkyl or Caromatic group optionally substituted by one to three Calkyl groups or Cfluoroalkylgroup.5. A process according to claim 1 , characterized in that said A represents NO claim 1 , BF claim 1 , PF claim 1 , SbF claim 1 , AsF claim 1 , F or RSO wherein Ris a fluoride atom or a Calkyl or Cfluoroalkylgroup.6. A process according to claim 1 , characterized in that said dienyl is cyclooctadienyl claim 1 , or norbornadienyl claim 1 , or 2 claim 1 ,4-dimethyl-pentadienyl claim 1 , or 2 claim 1 ,7-dimethyl-octadienyl or cycloheptadienyl or 2 claim 1 ,3 claim 1 ,4-trimethypenta-1 claim 1 ,3-dienyl. The present invention relates to the field of organic synthesis and more specifically it concerns a process for the preparation of 4-methylpent-3-en-1-ol derivatives as defined in formula (I) via an isomerization presenting a good selectivity.Many 4-methylpent-3-en-1-ol derivatives as defined in formula (I) are useful products as such or useful intermediates of the preparation of other important raw materials. The compounds of formula (I), which are poly-isoprenoid derivatives, are of particular interest for the perfumery industry, and in particular 4,8-dimethylnona-3,7-dien-1-ol or 4,8,12-trimethyltrideca-3,7,11-trien-1-ol. The latter compound is described as an important intermediate for the preparation of industrially relevant compounds such as Cetalox® (dodecahydro-3a,6,6,9a-tetramethyl-naphtho[2,1-b]furan; origin: Firmenich SA, Geneva, Switzerland).The ...

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30-11-2017 дата публикации

METHOD OF MANUFACTURING BHCD AND DERIVATIVES THEREOF

Номер: US20170342016A1
Принадлежит:

The present disclosure provides a method of manufacturing bis(2-hydroxyethyl) cyclohexane-1,4-dicarboxylate (BHCD) and derivatives thereof. The method includes the following steps. A first reactant including bis-hydroxyethyl terephthalate (BHET) is provided. 2-(2-hydroxyethoxy)ethyl 2-hydroxyethyl terephthalate (BHEET) is added to the first reactant including BHET to form a second reactant. The second reactant is hydrogenated. 1. A method of manufacturing bis(2-hydroxyethyl) cyclohexane-1 ,4-dicarboxylate (BHCD) and derivatives thereof , the method comprising:providing a first reactant comprising bis-hydroxyethyl terephthalate (BHET);adding 2-(2-hydroxyethoxy)ethyl 2-hydroxyethyl terephthalate (BHEET) to the first reactant comprising BHET to form a second reactant; andhydrogenating the second reactant.2. The method of claim 1 , wherein the BHET in the first reactant is existed as monomer claim 1 , dimer claim 1 , oligomer or a combination thereof.3. The method of claim 2 , wherein the BHET dimer is 0-100 parts by weight based on 100 parts by weight of the BHET monomer in the first reactant.4. The method of claim 2 , wherein the BHET dimer is 0-80 parts by weight based on 100 parts by weight of the BHET monomer in the first reactant.5. The method of claim 2 , wherein the BHET dimer is 0-60 parts by weight based on 100 parts by weight of the BHET monomer in the first reactant.7. The method of claim 1 , wherein hydrogenating the second reactant is under a solvent-free condition.8. The method of claim 1 , wherein hydrogenating the second reactant is at a temperature in a range of 80° C.−115° C.9. The method of claim 1 , wherein hydrogenating the second reactant is at a temperature in a range of 85° C.−110° C.10. The method of claim 1 , wherein the BHEET is 0.5-100 parts by weight based on 100 parts by weight of the BHET monomer in the second reactant.11. The method of claim 1 , wherein the BHEET is 7-60 parts by weight based on 100 parts by weight of the BHET monomer in ...

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22-10-2020 дата публикации

CYCLOADDITION REACTIONS USING QUANTUM DOTS

Номер: US20200331836A1
Принадлежит:

Disclosed herein are methods in which colloidal quantum dots (QDs) can serve as visible-light chromophores, photocatalysts, and reusable scaffolds for homo- and hetero-intermolecular [2+2] photocycloadditions. The methods may lead to >90% tunable regioselectivity and up to 98% diastereoselectivity for previously minor syn-cyclobutane products, including the syn-head-to-tail cyclobutane. 9. The method of claim 1 , wherein the compound of formula (I) and the compound of formula (II) are the same.10. The method of claim 1 , wherein the compound of formula (I) and the compound of formula (II) are different.11. The method of claim 1 , wherein the quantum dots are CdSe quantum dots.12. The method of claim 1 , further comprising separating the quantum dots from the substituted cyclobutane compound after step (d).13. The method of claim 1 , wherein the quantum dots have an average radius of 1.0 to 1.4 nm.14. The method of claim 1 , wherein the quantum dots further comprise a capping molecule on the surface of the quantum dots.15. The method of claim 14 , wherein the capping molecule is oleic acid.16. The method of claim 1 , wherein the solvent is tetrahydrofuran.17. The method of claim 1 , comprising irradiating the mixture for 24-72 hours.18. The method of claim 1 , comprising irradiating the mixture using a 16.5 W white-light LED with a 455 nm longpass filter.19. The method of claim 1 , comprising irradiating the mixture using a blue LED with emission centered at 467 nm.20. The method of claim 1 , wherein the quantum dots are present in the mixture in an amount of 0.4 mol % to 1.2 mol %. This application claims priority to U.S. Provisional Patent Application No. 62/835,778, filed on Apr. 18, 2019, the entire contents of which are fully incorporated herein by reference.This invention was made with government support under Grant 9550-17-1-0271 awarded by the Air Force Office of Scientific Research. The government has certain rights in the invention.Provided herein are ...

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21-11-2019 дата публикации

UPGRADING LIGNOCELLULOSIC OR CARBOHYDRATE MATERIAL

Номер: US20190352248A1
Принадлежит: Neste Oyj

The present disclosure relates to a method for upgrading lignocellulosic material carbohydrates and/or carbohydrate derivatives by dimerisation and/or oligomerisation using specific catalysts and to the use of the upgraded products. 115-. (canceled)16. A method for upgrading carbohydrates , carbohydrate derivatives or lignocellulosic material , the method comprising:providing a feedstock containing carbohydrates, carbohydrate derivatives or lignocellulosic material, wherein the lignocellulosic material, carbohydrates or carbohydrate material includes angelica lactone; anddimerising and/or oligomerising the carbohydrates, carbohydrate derivatives or lignocellulosic material in a presence of a heterogeneous catalyst to produce a dimer and/or oligomer;wherein oligomerising constitutes formation of trimers or higher;wherein the lignocellulosic material is levulinic acid, an ester of levulinic acid and/or a dehydration product of levulinic acid; andwherein the heterogeneous catalyst is an inorganic catalyst containing an alkali metal compound and/or an alkaline earth metal compound and at least one further metal compound.17. The method according to claim 16 , wherein the heterogeneous catalyst is a supported catalyst.18. The method according to claim 17 , wherein the heterogeneous catalyst is a catalyst comprising:the alkali metal compound and/or the alkaline earth metal compound on a support formed by the further metal compound.19. The method according to claim 18 , wherein the support is formed by an oxide of the further metal.20. The method according to claim 17 , wherein the heterogeneous catalyst is a catalyst comprising:an oxide of the alkali metal and/or an oxide of the alkaline earth metal on a support formed by an oxide of the further metal.21. The method according to claim 16 , wherein the heterogeneous catalyst is a catalyst comprising:the alkali metal compound and/or the alkaline earth metal compound as a mixed compound.22. The method according to claim 21 , ...

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04-06-2015 дата публикации

Verfahren zur ruthenium-katalysierten umvinylierung von carbonsäuren

Номер: WO2015078747A1
Принадлежит: Wacker Chemie AG

Gegenstand der Erfindung ist ein Verfahren zur selektiven Umvinylierung einer Eduktcarbonsäure mit einem Eduktvinylester zu einem Produktvinylester und der korrespondierenden Säure des Eduktvinylesters in Gegenwart von einem oder mehreren Rutheniumkatalysatoren, wobei a) der Eduktvinylester, die Eduktcarbonsäure und der Rutheniumkatalysator einem Reaktor zugeführt werden, dadurch gekennzeichnet, dass b) das molare Verhältnis von Eduktvinylester zu Eduktcarbonsäure 1:3 bis 3:1 beträgt, und c) die Umvinylierungsreaktion durchgeführt wird, d) nach Abschluß der Umvinylierungsreaktion der Eduktvinylester und die korrespondierende Säure aus dem Reaktionsgemisch destillativ abgetrennt werden, e) aus dem Sumpfprodukt der Destillation der Produktvinylester destillativ abgetrennt wird, und f) das verbleibende Reaktionsgemisch in den Reaktor zurückgeführt wird.

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24-11-2022 дата публикации

ISOMERIZATION METHOD OF CYCLOHEXANE DICARBOXYLIC ACID

Номер: US20220371981A1
Принадлежит:

The present disclosure relates to an isomerization method of a cyclohexane dicarboxylic acid (CHDA) and, more specifically, to a method for preparing a trans-cyclohexane dicarboxylic acid (t-CHDA) from a cis-cyclohexane dicarboxylic acid (c-CHDA) by means of catalytic isomerization. 1. An isomerization method of a cyclohexane dicarboxylic acid , comprising: heat-treating a mixed solution prepared by mixing a cyclohexane dicarboxylic acid containing a cis isomer , water , and an isomerization catalyst to isomerize the cis isomer to a trans isomer ,{'sup': '2', 'wherein the isomerization catalyst contains zirconia and has a BET specific surface of 50 m/g or more.'}2. The isomerization method according to claim 1 , wherein:{'sub': cat', '3, 'the isomerization catalyst has a total amount of acid sites of 400 umol/gor more as measured by an ammonia-temperature programmed desorption (NH-TPD) method.'}3. The isomerization method according to claim 1 , wherein:{'sub': '3', 'the isomerization catalyst is composed of acid sites such that, based on the total amount of acid sites (100 mol %) measured by the ammonia-temperature programmed desorption (NH-TPD), the amount of weak acid sites with an acid site desorption temperature of 50 to 150° C. is 5 to 75 mol %, the amount of middle acid sites with an acid site desorption temperature of 150 to 450° C. is 15 to 95 mol %, and the amount of strong acid sites with an acid site desorption temperature of 450° C. or more corresponds to the rest.'}4. The isomerization method according to claim 1 , wherein:the zirconia in the isomerization catalyst is a monoclinic zirconia, a tetragonal zirconia, or a mixture thereof.5. The isomerization method according to claim 1 , wherein:the isomerization catalyst further comprises a heterogeneous transition metal oxide.6. The isomerization method according to claim 5 , wherein:the isomerization catalyst is a titania-zirconia composite, a lanthania-zirconia composite, an yttria-zirconia composite, ...

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06-11-2000 дата публикации

Metho dof obtaining cyclopropyl acetylene

Номер: PL338455A1
Автор: [UNK]
Принадлежит: Du Pont Pharm Co

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02-05-2001 дата публикации

Synthesis of cyclopropylacetylene from propiolic acid (2-propynoic acid)

Номер: GB2355724A
Автор: Karel M J Brands
Принадлежит: Merck and Co Inc

A process for the preparation of cyclopropaneacetylene (<B>5</B>), a key intermediate in the synthesis of the HIV transcriptase inhibitor DMP-266, by a two step-process comprising: (i) the alkylation of propiolic acid (<B>1</B>) with a 1,3-disubstituted propane (<B>2</B>) under basic conditions followed by cycloalkylation of the 6-substituted 2-hexynoic acid product (<B>3</B>) to give a 3-cyclopropaneacetylene carboxylic acid (<B>4</B>); and (ii) decarboxylation of (<B>4</B>) in the presence of a copper catalyst to yield cyclopropaneacetylene (<B>5</B>) <EMI ID=1.1 HE=69 WI=156 LX=224 LY=1033 TI=CF>

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25-10-2017 дата публикации

A catalyst and a process for the production of ethylenicallly unsaturated carboxylic acids or esters

Номер: GB201714756D0
Автор: [UNK]
Принадлежит: Lucite International UK Ltd

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17-02-2011 дата публикации

Process for continuous catalytic hydrogenation

Номер: DE502005010794D1
Принадлежит: Evonik Oxeno GmbH

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03-07-1990 дата публикации

Method of preparing (R)-succinic acid derivatives

Номер: US4939288A
Автор: John J. Talley
Принадлежит: Monsanto Co

Method for preparing a biologically active 2-substituted succinic acid derivative involving asymmetrically catalytically hydrogenating the corresponding 2(E)-alkylidene succinate derivative in the presence of a rhodium complexed (R,R)-bisphosphine compound.

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12-06-1979 дата публикации

Epoxy resin compositions (case B) containing cumene-maleic anhydride residue

Номер: US4158090A
Принадлежит: Gulf Research and Development Co

A new composition capable of being cured to a solid resin highly resistant to boiling acetone which comprises: (a) a 1,2-epoxy resin containing on the average more than one 1,2-epoxy group per molecule; (b) a residue remaining from the process wherein cumene (C) is reacted with maleic anhydride (MA) in the presence of (that is, in contact with) zinc chloride to obtain a reaction product containing dimethylbenzyl succinic anhydride (DMBSA), 5-phenyl-5-methylhexane-1,2,3,4-tetracarboxylic acid dianhydride (PMTD) and addition products of C and MA containing more than two anhydride groups per molecule (AP) and wherein a sufficient amount of said DMBSA is removed from said reaction product to give a residue containing a maximum of 25 weight percent DMBSA; and (c) an accelerator.

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22-07-2002 дата публикации

Method for producing branched fatty acid and branched fatty acid ester

Номер: JP3303947B2
Принадлежит: Kao Corp

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13-07-2006 дата публикации

Process for the continuous catalytic hydrogenation of hydrogenatable compounds on solid, fixed-bed catalysts with a hydrogen-containing gas

Номер: DE102004063673A1
Принадлежит: Oxeno Olefinchemie GmbH

Die Erfindung betrifft die Herstellung von alicyclischen Carbonsäuren oder deren Derivaten durch Selektivhydrierung der entsprechenden aromatischen Carbonsäure(-derivate) in mindestens zwei hintereinandergeschalteten Reaktoren, wobei mindestens ein Reaktor in Schlaufenfahrweise betrieben wird. Die Katalysatorvolumina werden in dem Verfahren so eingestellt, dass benötigte Katalysatorvolumen bezogen auf den Umsatz möglichst gering ist. The invention relates to the preparation of alicyclic carboxylic acids or their derivatives by selective hydrogenation of the corresponding aromatic carboxylic acid (s) in at least two reactors connected in series, wherein at least one reactor is operated in loop mode. The catalyst volumes are adjusted in the process so that the required catalyst volume based on the conversion is minimized.

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16-06-1984 дата публикации

酸の製造方法

Номер: JPS59104342A
Принадлежит: BP Chemicals Ltd

(57)【要約】本公報は電子出願前の出願データであるた め要約のデータは記録されません。

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21-05-2019 дата публикации

一种环己烷-1,2-二甲酸二元酯的制备方法

Номер: CN106554278B

本发明涉及加氢制备环己烷‑1,2‑二甲酸二元酯领域,公开了一种环己烷‑1,2‑二甲酸二元酯的制备方法,该方法包括:(1)将含有邻苯二甲酸二元酯的加氢原料和H 2 在第一催化剂的存在下在主加氢反应器内进行第一接触,得到第一气‑液混合流体;(2)将所述第一气‑液混合流体进行气液分离;(3)将氢气通过平均孔径为纳米尺寸的孔注入到经步骤(2)分离出的主加氢反应液中,得到第二气‑液混合流体;(4)将所述第二气‑液混合流体在第二催化剂的存在下在后加氢反应器内进行第二接触,得到第三气‑液混合流体;(5)将所述第三气‑液混合流体进行气液分离;该方法具有原料转化率和产品选择性高以及顺式结构产品含量高的优点。

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10-12-2001 дата публикации

Method of preparing acetic acid and/or methyl acetate by isomerization or methyl formate

Номер: RU2176635C2
Принадлежит: Асетекс Шими

FIELD: chemical industry. SUBSTANCE: described is preparation of acetic acid and derivatives thereof by isomerization of methyl formate in the presence of water, aliphatic C 1 -C 10 carboxylic acid as solvent, and catalyst system. Catalyst system comprises one iodide promoter and one iridium-based compound. Process is carried out in the presence of carbon monoxide partial pressure of which is maintained from 0,1•10 5 Pa to 25•10 5 Pa at 150-250 C. Amount of methyl formate in reaction mixture is maintained at less than 20 wt.%. EFFECT: greater process efficiency. 14 cl, 1 ex 599 с ПЧ с» (19) (13) ВИ `” 2 176 635 ^С2 61) МК’ © 07 С 51/353, 53/08, 69/14, 67/293 РОССИЙСКОЕ АГЕНТСТВО ПО ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ РОССИЙСКОЙ ФЕДЕРАЦИИ (21), (22) Заявка: 98119441/04, 27.03.1997 (71) Заявитель: АСЕТЕКС ШИМИ (ЕКВ) (24) Дата начала действия патента: 27.03.1997 (72) Изобретатель: ПАТУА Карль (ЕК), (30) Приоритет: 27.03.1996 ЕК 96 03 781 ПЕРРОН Робер (ЕК), ТЬЕБО Даниель (ЕК) (43) Дата публикации заявки: 10.10.2000 (73) Патентообладатель: АСЕТЕКС ШИМИ (ЕК) (46) Дата публикации: 10.12.2001 (74) Патентный поверенный: (56) Ссылки: Ц$ 4 918 226 АЛ, 17.04.1990. ЗЧ 437 Томская Елена Владимировна 145 А, 30.07.1914. ЕР О 045 637 АТ, 10.02.1982. ЕК 2 630 437 АЛ, 25.04.1988. (85) Дата перевода заявки РСТ на национальную фазу: 27.10.1998 (86) Заявка РСТ: ЕК 97/00553 (27.03.1997) (87) Публикация РСТ: М/О 97/35829 (02.10.1997) (98) Адрес для переписки: 129010, Москва, ул. Большая Спасская 25, стр.3, ООО "Юридическая фирма Городисский и Партнеры", Томской Е.В. (54) СПОСОБ ПОЛУЧЕНИЯ УКСУСНОЙ КИСЛОТЫ И/ИЛИ МЕТИЛАЦЕТАТА ПОСРЕДСТВОМ ИЗОМЕРИЗАЦИИ МЕТИЛФОРМИАТА (57) Изобретение относится к технологии получения уксусной кислоты и ее производных путем изомеризации метилформиата в присутствии воды, алифатической карбоновой кислоты С.-Сло в качестве растворителя и каталитической системы. Каталитическая система содержит один йодидный промотор и одно соединение на ...

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21-03-2019 дата публикации

A catalyst and a process for the production of ethylenically unsaturated carboxylic acids or esters

Номер: WO2019053438A1
Принадлежит: LUCITE INTERNATIONAL UK LIMITED

A catalyst has a modified silica support and comprises a modifier metal, zirconium and/or hafnium, and a catalytic metal on the modified support. The catalyst has at least a proportion, typically, at least 25%, of modifier metal present in moieties having a total of up to 2 modifier metal atoms. The moieties may be derived from a monomeric and/or dimeric cation source. A method of production:- provides a silica support with isolated silanol groups with optional treatment to provide isolated silanol groups (-SiOH) at a level of <2.5 groups per nm2; contacting the optionally treated silica support with a monomeric zirconium or hafnium modifier metal compound to effect adsorption onto the support; optionally calcining the modified support for a time and temperature sufficient to convert the monomeric zirconium or hafnium compound adsorbed on the surface to an oxide or hydroxide of zirconium or hafnium in preparation for catalyst impregnation. A method of producing an ethylenically unsaturated carboxylic acid or ester, typically, an a, β ethylenically unsaturated carboxylic acid or ester, comprising the steps of contacting formaldehyde or a suitable source thereof with a carboxylic acid or ester in the presence of catalyst and optionally in the presence of an alcohol, wherein said catalyst is used.

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18-05-2020 дата публикации

에틸렌성 불포화 카복실산 또는 에스테르의 제조를 위한 촉매 및 방법

Номер: KR20200053567A

촉매는 개질된 실리카 지지체를 가지며, 개질제 금속 지르코늄 및/또는 하프늄 및 개질된 지지체 상의 촉매 금속을 포함한다. 촉매는, 개질제 금속의 적어도 일부분, 전형적으로 적어도 25%가 총 최대 2개의 개질제 금속 원자를 갖는 모이어티로 존재하는 개질제 금속을 갖는다. 상기 모이어티는 단량체 및/또는 이량체 양이온 공급원으로부터 유도될 수 있다. 제조 방법은 하기 단계를 포함한다: 선택적인 처리와 함께, 단리된 실라놀 기를 갖는 실리카 지지체를 제공하여, nm 2 당 <2.5개 기의 수준의 단리된 실라놀 기 (-SiOH)를 제공하는 단계; 선택적으로 처리된 실리카 지지체를 단량체 지르코늄 또는 하프늄 개질제 금속 화합물과 접촉시켜 상기 지지체 상에 흡착시키는 단계; 선택적으로, 촉매 함침을 위한 준비 시, 표면 상에 흡착된 단량체 지르코늄 또는 하프늄 화합물을 지르코늄 또는 하프늄의 산화물 또는 수산화물로 전환시키기에 충분한 시간 및 온도 동안, 개질된 지지체를 하소시키는 단계. 에틸렌성 불포화 카복실산 또는 에스테르, 전형적으로 α, β 에틸렌성 불포화 카복실산 또는 에스테르의 제조 방법은 촉매의 존재 하에 그리고 선택적으로 알콜의 존재 하에 포름알데히드 또는 이의 적합한 공급원을 카복실산 또는 에스테르와 접촉시키는 단계를 포함하며, 여기서 상기 촉매가 사용된다.

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09-01-2018 дата публикации

一种赖诺普利中间体的制备方法

Номер: CN105777546B
Принадлежит: Suzhou Lead Biotechnology Co Ltd

本发明提供一种赖诺普利中间体的制备方法,所述赖诺普利中间体为(R)‑2‑羟基‑4‑苯基丁酸乙酯,本发明的制备方法以廉价易得的苯甲醛和丙酮酸为原料,通过缩合,生物酶催化不对称还原,双键氢化以及酯化四步高效的反应,最终以83%的总收率得到光学纯的目标产物(R)‑HPBE。

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27-03-2002 дата публикации

通过异构化和羰基化反应制备乙酸和/或乙酸甲酯的方法

Номер: CN1081619C
Принадлежит: ACETIQUES CHIMIE

本发明公开了一种通过异构化反应和羰基化反应制备乙酸和/或乙酸甲酯的方法。尤其是,该制备乙酸和/或乙酸甲酯的方法包括提供甲酰基的试剂和提供甲基的试剂的反应,在一氧化碳、水、溶剂和包括至少一种含卤助催化剂和至少一种铱化合物的催化体系存在下进行的,按照本方法,一氧化碳的分压维持为0.1×10 5 ~25×10 5 Pa,提供甲酰基的试剂的量维持在不高于反应混和物重量的20%(重量)范围内,并且提供甲基和甲酰基的试剂的加入量使得甲基和甲酰基的摩尔比大于1。本方法尤其适用于由甲醇和甲酸甲酯的混和物制备乙酸和/或乙酸甲酯。

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09-03-2016 дата публикации

一种芳基烷基羧酸(甲酯)的合成方法及系统

Номер: CN104370729B
Автор: 刘春德

本发明公开一种芳基烷基羧酸(甲酯)的合成方法及系统,所述的方法是将烯基羧酸(甲酯)与芳香烃为原料,输入反应器,在温度80~300℃、压力0~10MPa、烯基羧酸(甲酯)与芳香烃的摩尔比为1:1~10、空速为0.05~30h -1 的条件下,在树脂或固体酸催化剂催化下进行傅—克烷基化反应,环流反应3~30小时,脱芳香烃,得到所述的芳基烷基羧酸(甲酯)。本方法由于采用了树脂或固体酸催化环流反应工艺,避免了废物排放。

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24-04-1984 дата публикации

Process for synthesizing a multicomponent acidic catalyst composition containing zirconium by an organic solution method

Номер: US4444904A
Автор: Ji-Yong Ryu
Принадлежит: Exxon Research and Engineering Co

A process for preparing a catalyst composition wherein a Metal Hydrocarboxide I, such as aluminum sec-butoxide, a Metal Hydrocarboxide II, such as zirconium butoxide, an acidic phosphorus-oxygen composition, such as phosphoric acid, and water, are reacted in the presence of a liquid organic medium, such as acetone, to form a catalyst precursor composition, which is then calcined to form the catalyst, is disclosed. The catalyst is useful for condensing carboxylic acids or their ester with aldehydes or acetals to synthesize α,β-ethylenically unsaturated acids or esters, such as methylmethacrylate.

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22-03-2019 дата публикации

一种12位苯并环丁烯脱氢枞酸(β-甲基丙烯酰氧基乙基)酯、其制备方法及其应用

Номер: CN109503382A

本发明公开了一种12位苯并环丁烯脱氢枞酸(β‑甲基丙烯酰氧基乙基)酯、其制备方法及其应用,12位苯并环丁烯脱氢枞酸(β‑甲基丙烯酰氧基乙基)酯的分子结构式为: 12位苯并环丁烯脱氢枞酸(β‑甲基丙烯酰氧基乙基)酯的制备方法为,以脱氢枞酸为原料,依次经过溴化、Suzuki偶联、酰氯化和醇解反应,即得。本发明12位苯并环丁烯脱氢枞酸(β‑甲基丙烯酰氧基乙基)酯,可以进行自由基聚合和开环后聚合,通过多种反应途径合成功能性单体制备高分子材料,利用本申请可自由基聚合的松香苯并环丁烯单体所制备的树脂的热稳定性、耐水性和介电性能均有提升;加强了对松香的再加工利用,提高了松香的使用价值,减少了石化资源的使用。

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30-09-2015 дата публикации

一种富马酸生产工艺

Номер: CN104045550B
Автор: 张培红

本发明公开了一种富马酸生产工艺,将的顺式丁烯二酸水溶液进行搅拌、脱色处理,而后进行过滤,除去活性碳和杂质,再按顺序加入尿素、磷酸氢二铵催化剂、反应;而后离心、出料、干燥、包装。本发明使生产出的富马酸色度好,催化效率高,同时产生的废水中残留的无机盐无需降解即可排放。

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18-02-2020 дата публикации

Method of producing acrylic acid from lactic acid or lactide using molten salt catalysts

Номер: RU2714490C1

FIELD: technological processes. SUBSTANCE: invention relates to an improved method of producing acrylic acid with high selectivity and output, involving the following steps: a) contacting a stream of incoming materials containing lactic acid, lactide or mixtures thereof with a first molten salt catalyst in a first reactor at a first reaction temperature during a first reaction time to obtain a first stream containing 2-bromopropionic acid (2-BrPA); b) contacting said 2-BrPA with a second molten salt catalyst in a second reactor at a second reaction temperature for a second reaction time to obtain a second stream containing 3-bromopropionic acid (3-BrPA) and said acrylic acid; and c) contacting said 3-BrPA with an amine in a third reactor at a third reaction temperature for a third reaction time to obtain a third stream containing said acrylic acid; wherein said first molten salt catalyst comprises an anion (Br - ) bromide; and wherein said second molten salt catalyst comprises Br - , wherein said acrylic acid of said second stream is combined with said acrylic acid of said third stream into production stream of said acrylic acid; wherein said acrylic acid in said production stream has a common yield of acrylic acid and total acrylic acid selectivity. EFFECT: disclosed is an improved method of producing acrylic acid. 15 cl, 2 dwg, 6 tbl, 56 ex РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 714 490 C1 (51) МПК C07C 51/353 (2006.01) C07C 51/363 (2006.01) C07C 51/377 (2006.01) C07C 53/19 (2006.01) C07C 57/04 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК C07C 51/353 (2020.01); C07C 51/363 (2020.01); C07C 51/377 (2020.01); Y02P 20/582 (2020.01) (21)(22) Заявка: 2019124936, 07.03.2018 (24) Дата начала отсчета срока действия патента: Дата регистрации: 18.02.2020 07.03.2017 US 62/467,964; 11.01.2018 US 62/616,010 (73) Патентообладатель(и): ДЗЕ ПРОКТЕР ЭНД ГЭМБЛ КОМПАНИ (US) (45) Опубликовано: 18.02.2020 Бюл. № 5 (56) ...

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23-03-2018 дата публикации

A kind of preparation method of cyclenes yl carboxylic acid

Номер: CN107827733A
Принадлежит: PUYANG SHENGHUADE CHEMICAL CO Ltd

本发明公开了一种环烯基羧酸的制备方法,所述的分子式Ⅰ所示的环烯基羧酸的制备方法包括:在压力容器中,以水相为溶剂,氮气加压表压1.0~5.0MPa的惰性环境,120~300℃的条件下,由分子式Ⅱ所示的不饱脂肪酸和1,3丁二烯进行聚合反应1~3小时,然后将合成液移入精馏釜在负压的条件下进行精馏,得到分子式Ⅰ所示的环烯基羧酸,总体上,本发明具有反应速度快,反应周期短,在水相中进行反应,便于对环烯基羧酸进行提纯,操作简单方便,能够进行连续生产,有效提高产品质量,具有极高的使用价值的优点。

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05-07-2006 дата публикации

连续催化氢化方法

Номер: CN1796352A
Принадлежит: OKSENNO OLEFIN CHEMICAL GmbH

本发明涉及通过在至少三个串联反应器中选择性氢化相应芳族羧酸(衍生物)来制备脂环族羧酸或它们的衍生物的方法,其中至少一个反应器以环路操作方式运行。在该方法中的催化剂体积以使得基于转化率的所需催化剂体积尽可能低的方式设定。

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19-06-2015 дата публикации

PROCESS FOR THE SYNTHESIS OF BIOSOURCES UNSATURATED ACIDS

Номер: FR2992642B1
Принадлежит: Novance SA, OMEGA CAT SYSTEM

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17-05-2017 дата публикации

Polylactic acid decomposition method

Номер: EP2589621B1
Автор: Jun Tsubota
Принадлежит: Osaka Gas Co Ltd

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22-11-1995 дата публикации

Process for the preparation of branched chain fatty acids and alkyl esters thereof

Номер: EP0683150A1
Принадлежит: Kao Corp

A process for preparing branched chain fatty acids or alkyl esters thereof comprising at least a step wherein unsaturated fatty acids having 10 to 25 carbon atoms, alkyl esters thereof or mixtures thereof are subjected to skeletal isomerization reaction in the presence of water or a lower alcohol at a temperature of 150 to 350°C using a zeolite as a catalyst, the zeolite having a linear pore structure of pore size that is small enough to retard dimerization and large enough to allow diffusion of the branched chain fatty acids or alkyl esters thereof.

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07-02-1984 дата публикации

Process for synthesizing a multicomponent acidic catalyst composition by an organic solution method

Номер: US4430252A
Автор: Ji-Yong Ryu
Принадлежит: Exxon Research and Engineering Co

A process for preparing a catalyst composition wherein a Metal Hydrocarboxide I, such as aluminum secbutoxide, a Metal Hydrocarboxide II, such as silicon ethoxide, an acidic phosphorus-oxygen composition, such as phosphoric acid, and water, are reacted in the presence of a liquid organic medium, such as acetone, to form a catalyst precursor composition, which is then calcined to form the catalyst, is disclosed. The catalyst is useful for condensing carboxylic acids or their ester with aldehydes or acetals to synthesize α, β-ethylenically unsaturated acids or esters, such as methylmethacrylate.

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16-11-2018 дата публикации

A kind of synthetic method of royal jelly acid

Номер: CN108821964A
Автор: 张卫东

本发明公开了一种王浆酸的合成方法。本发明以来源广泛的1,8‑辛二醇为起始原料,依次通过加成反应、氧化反应、Knoevenagel反应‑水解,采用的步骤较少,所得到的副产物少,提高了产率,降低了生产成本。

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10-01-2014 дата публикации

METHOD FOR PRODUCING HIGHLY FORTED CARBONIC ACIDS AND THEIR SALTS

Номер: RU2012121456A

1. Способ приготовления высокофторированных карбоксильных кислот и их солей, а также их веществ-предшественников, включающий воздействие на высокофторированный этиленовый водород, имеющий общую формулу (I):производным муравьиной кислоты в соответствии с общей формулой (II):в присутствии радикального инициатора для образования вещества -предшественника карбоновой кислоты в виде О - эфиров, S - эфиров либо амидного аддукта общей формулы (III):и, факультативно, в том случае, если будет получена кислота, гидролиз аддукта формулы (III) для того, чтобы образовать карбоновую кислоту или ее соли с общей формулой (IV):где в формулах (II) и (III) R представляет собой остаток OМ, SM, OR′, SR′ или NR′R′′, где R′ и R′′ являются независимыми друг от друга линейными или разветвленными либо циклическими алифатическими или ароматическими остатками, которые содержат по крайней мере один атом углерода и которые не имеют альфа-Н-атом и где в формулах (I), (III) и (IV) Rпредставляет собой Н либо перфорированные или частично фторированные, линейные, разветвленные, алифатические или ароматические атомы углерода, содержащие остатки и n составляет 1 или О, гл представляет собой число от 0 до 6, а Мпредставляет собой катион, включающий Н.2. Способ по п.1, где Rпредставляет собой фторированный или перфорированный, линейный или разветвленный алкильный остаток, который может содержать один или несколько катенарных атомов кислорода.3. Способ по п.1, отличающийся тем, что Rпредставляет собой одно из следующих:R′-O-(CF)′-,R-(CF)′-,R-(О-CF)′-,R′-(O-CF-CF)′-,R′-(О-CFCF(CF))′-,R′-(O-CF(CF)-CF)′-,где Rпредставляет собой фторированный или перфорированный, линейный или разветвленный алкильный остаток РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (51) МПК C07C 51/353 (13) 2012 121 456 A (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ЗАЯВКА НА ИЗОБРЕТЕНИЕ (21)(22) Заявка: 2012121456/04, 18.11.2010 (71) Заявитель(и): 3М Инновейтив Пропертиз Компани (US) Приоритет(ы): (30) Конвенционный приоритет: ...

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26-05-1987 дата публикации

Preparation process fo a branched alkanoic acid

Номер: KR870001042B1

2-Ethyl-2-methyl-butanoic acid (I) is prepd. by reacting 2- ethylbutene-1-ol (II) with formic acid in the presnce of sulphuric acid and then quenching the reaction mixture with water. The reaction temp. is pref. in the range 0-25 deg. C, esp. 10-20deg. C although temps. as high as 50deg. C may be used. (I) is a chmical intermediate and has particular use in the prepn. of 5-(2,6-disubstd. benzamido)- 3-(1-ethyl-1-methylpropyl) isoxazoles, which are herbicides.

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03-11-2017 дата публикации

A kind of preparation method of 1,2 cyclohexane cyclohexanedimethanodibasic dibasic ester

Номер: CN107311860A
Автор: 吕耀武, 李超
Принадлежит: Jiangsu Feixiang Chemicals Co Ltd

本发明公开一种1,2‑环己烷二甲酸二元酯的制备方法,包括以下步骤:以邻苯二甲酸二元酯为原料,使用固定床反应器进行催化加氢反应,所述固定床反应器中加载以Pd、Ru、Ni、Cu中的一种或多种为活性组分、以氧化铝和氧化硅为载体的催化剂;加氢反应完成后,将反应液从精馏柱的上段通入精馏柱中,在精馏柱下段通入水,进行精馏;在精馏过程中,控制精馏柱温度为100~200℃,水和反应液的体积比为0.5~3.0:1,液体总空速0.1~2.5h ‑1 ,使用上述方法,可以显著降低能耗和用水量,将1,2‑环己烷二甲酸二元酯纯度提高到99.5%以上。

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25-07-2018 дата публикации

Catalyst for producing bio-based acrylic acid and its derivatives and the method for making thereof

Номер: RU2662229C2

FIELD: chemistry. SUBSTANCE: present invention relates to a catalyst for the production of acrylic acid based on a biological feed comprising phosphate anions and at least one monovalent cation and at least one multivalent cation. Process for the preparation of a catalyst is also provided. Lactic acid, lactic acid derivatives or mixtures thereof are dehydrated by a catalyst in a process for the production of acrylic acid, acrylic acid derivatives or mixtures thereof based on biological raw materials. In particular, the invention relates to a catalyst for the conversion of lactic acid, lactic acid derivatives or mixtures thereof to acrylic acid, acrylic acid derivatives or mixtures thereof comprising (a) phosphate anions described by formulas (Ic) and (IIc), (b) to at least two different cations, wherein the catalyst is neutrally charged, and β and γ greater than or equal to 0 and less than or equal to 1, wherein n is at least 2, wherein the molar ratio of said phosphate anions in said catalyst is from about 0.1 to about 10, said at least two different cation include at least one monovalent cation and at least one multivalent cation, and wherein said multivalent cation is selected from the group consisting of metal cations Be, Mg, Ca, Sr, Ba and their mixtures. [H (2-2γ) PO (4-γ) ] (1+(n-1)γ)- (1+(n-1)γ) (IIc), and [H (1-β) P (1+β) O (4+3β) ] 2(1+β)- (Ic). EFFECT: catalyst allows to obtain products with high yield, selectivity and efficiency. 14 cl, 7 ex РОССИЙСКАЯ ФЕДЕРАЦИЯ ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) (19) RU (11) (13) 2 662 229 C2 (51) МПК B01J 37/04 (2006.01) B01J 27/18 (2006.01) B01J 37/08 (2006.01) B01J 37/10 (2006.01) C07C 57/04 (2006.01) C07C 51/377 (2006.01) C07C 57/055 (2006.01) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК B01J 37/04 (2006.01); B01J 27/18 (2006.01); B01J 37/08 (2006.01); B01J 37/10 (2006.01); C07C 57/04 (2006.01); C07C 51/377 (2006.01) (21)(22) Заявка: 2016110109, 16.10.2014 16.10.2014 Дата регистрации: 25.07.2018 16 ...

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20-03-2015 дата публикации

Method of obtaining highly fluorinated carboxylic acids and their salts

Номер: RU2544855C2

FIELD: chemistry. SUBSTANCE: invention relates to a method of obtaining highly fluorinated carboxylic acids and their salts, as well as substances-precursors, which includes an impact on a highly fluorinated olefin, which has the general formula (I): R f -(O) n -(CF 2 ) m -CF=CF 2 of a formic acid derivative in accordance with the general formula (II): HCOR in the presence of a radical initiator to form a substance-precursor of carboxylic acid in the form of O-ethers, S-ethers or an amide adduct of the general formula (III): R f -(O) n -(CF 2 ) m -CFH-CF 2 -COO and, optionally, in case of an acid obtaining, hydrolysis of an adduct of formula (III) to form carboxylic acid or its salts with the general formula (IV): R f -(O) n -(CF 2 ) m -CFH-CF 2 -COO - M + , where in formulas (II) and (III) R represents a residue O - M + , S - M + , OR' or SR' or NR'R", where R' and R" are independent on each other linear or branched or cyclic aliphatic residues, which contain at least one carbon atom and which do not have an alpha-H-atom, where the alpha-H-atom represents a hydrogen atom, bond with a carbon atom, bound with O, S or N in groups OR', SR' or NR'R", and where in formulas (I), (III), (IV) R f represents H, either a perfluorinated or fluorinated linear or branched alkyl residue which can contain one or several catenary oxygen atoms, and n constitutes 1 or 0, m represents a number from 0 to 6, and M + represents a cation. EFFECT: method makes it possible to obtain target compounds with the high output. 8 cl, 7 ex РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (51) МПК C07C 51/353 C07C 231/12 C07C 233/05 C07C 233/06 C07C 51/367 C07C 53/21 ФЕДЕРАЛЬНАЯ СЛУЖБА C07C 67/347 ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ C07C 69/63 C07C 69/708 C07C 235/06 (12) ОПИСАНИЕ (21)(22) Заявка: (13) 2 544 855 (2006.01) (2006.01) (2006.01) (2006.01) (2006.01) (2006.01) (2006.01) (2006.01) (2006.01) (2006.01) C07C C07C C2 59/135 (2006.01) 67/38 (2006.01) ИЗОБРЕТЕНИЯ К ПАТЕНТУ ...

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18-04-2007 дата публикации

Process for producing trans-1,4-cyclohexanedicarboxylic acid

Номер: CN1310868C
Принадлежит: Mitsubishi Kasei Corp

(1)一种用于生产反式-1,4-环己二羧酸(t-CHDA)的方法,该法包括加热粗CHDA至180℃或更高,并保持粗CHDA在180℃或更高和低于t-CHDA熔点范围的温度下,以沉淀在熔融的顺式-1,4-环己二羧酸(c-CHDA)中的异构化所形成的t-CHDA;(2)一种t-CHDA的生产方法,其中粉末或颗粒的粗CHDA在不低于c-CHDA熔点到低于t-CHDA熔点的温度下进行热处理,以使顺式异构体异构化成反式异构体,同时保持粉状颗粒的状态;(3)一种t-CHDA的生产方法,其中保持粗CHDA在不低于c-CHDA熔点和低于t-CHDA熔点的温度下,同时使粗CHDA保持流动,以制备粉状颗粒的t-CHDA;和(4)一种净化粗CHDA的方法,其中使通过氢化TPA等的步骤制得的粗CHDA在惰性气体下加热,通过蒸发除去杂质。上述方法可使用于通过使用简单和容易的方法以有良好效率生产高纯度的t-CHDA的c-CHDA异构化。

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28-10-2021 дата публикации

Patent RU2020113238A3

Номер: RU2020113238A3
Автор: [UNK]
Принадлежит: [UNK]

ВИ“? 2020113238” АЗ Дата публикации: 28.10.2021 Форма № 18 ИЗ,ПМ-2011 Федеральная служба по интеллектуальной собственности Федеральное государственное бюджетное учреждение 5 «Федеральный институт промышленной собственности» (ФИПС) ОТЧЕТ О ПОИСКЕ 1. . ИДЕНТИФИКАЦИЯ ЗАЯВКИ Регистрационный номер Дата подачи 2020113238/04(022363) 13.09.2018 РСТ/СВ2018/052606 13.09.2018 Приоритет установлен по дате: [ ] подачи заявки [ ] поступления дополнительных материалов от к ранее поданной заявке № [ ] приоритета по первоначальной заявке № из которой данная заявка выделена [ ] подачи первоначальной заявки № из которой данная заявка выделена [ ] подачи ранее поданной заявки № [Х] подачи первой(ых) заявки(ок) в государстве-участнике Парижской конвенции (31) Номер первой(ых) заявки(ок) (32) Дата подачи первой(ых) заявки(ок) (33) Код страны 1. 1714756.2 13.09.2017 СВ Название изобретения (полезной модели): [Х] - как заявлено; [ ] - уточненное (см. Примечания) КАТАЛИЗАТОР И СПОСОБ ПОЛУЧЕНИЯ ЭТИЛЕННЕНАСЫЩЕННЫХ КАРБОНОВЫХ КИСЛОТ ИЛИ СЛОЖНЫХ ЭФИРОВ Заявитель: МИЦУБИСИ КЕМИКАЛ ЮКей ЛИМИТЕД, СВ 2. ЕДИНСТВО ИЗОБРЕТЕНИЯ [Х] соблюдено [ ] не соблюдено. Пояснения: см. Примечания 3. ФОРМУЛА ИЗОБРЕТЕНИЯ: [Х] приняты во внимание все пункты (см. Примечания) [ ] приняты во внимание следующие пункты: [ ] принята во внимание измененная формула изобретения (см. Примечания) 4. КЛАССИФИКАЦИЯ ОБЪЕКТА ИЗОБРЕТЕНИЯ (ПОЛЕЗНОЙ МОДЕЛИ) (Указываются индексы МПК и индикатор текущей версии) ВО1. 21/08 (2006.01) ВО1.] 32/00 (2006.01) С07С 51/353 (2006.01) ВО1. 21/06 (2006.01) ВОТ. 35/02 (2006.01) С07С 67/313 (2006.01) ВО1. 23/02 (2006.01) ВОТ. 37/02 (2006.01) ВОТ. 31/02 (2006.01) В01. 37/08 (2006.01) 5. ОБЛАСТЬ ПОИСКА 5.1 Проверенный минимум документации РСТ (указывается индексами МПК) 5.2 Другая проверенная документация в той мере, в какой она включена в поисковые подборки: 5.3 Электронные базы данных, использованные при поиске (название базы, и если, возможно, поисковые термины): Езрасепе, Соозе, Сооз]е Ржеп$, ...

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21-10-2005 дата публикации

Method for preparing acetic acid and/or methyl acetate by methyl formate isomerisation

Номер: KR100509404B1
Принадлежит: 아쓰떽스 쉬미

메틸 포르메이트 이성질화 반응에 의한 아세트산 및/또는 메틸 아세테이트의 제조 방법을 개시한다. 이 방법은 메틸 포르메이트, 물, 용매, 및 하나 이상의 할로겐화 촉진제 및 하나 이상의 이리듐 화합물을 포함하는 촉매계의 존재하에 수행된다. 이 방법에 따라, 반응중 0.1 x 10 5 Pa 내지 25 x 10 5 Pa 의 일산화탄소 부분압을 유지하며, 메틸 포르메이트의 양을 반응 매질의 중량을 기준으로 20 중량 % 미만으로 유지한다.

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06-07-2016 дата публикации

Method for preparing (R)-2-hydroxy-4-phenylbutanoate

Номер: CN105732373A
Принадлежит: Suzhou Lead Biotechnology Co Ltd

本发明提供一种制备(R)?2?羟基?4?苯基丁酸乙酯的方法,以廉价易得的苯甲醛和丙酮酸为原料,通过缩合,酯化,生物酶催化不对称还原和双键氢化四步高效的反应,最终以82%的总收率得到光学纯的目标产物(R)?HPBE。

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26-06-2020 дата публикации

Catalyst for producing ethylenically unsaturated carboxylic acid or carboxylic acid ester and production method

Номер: CN111344059A
Принадлежит: Lucite International UK Ltd

一种催化剂具有改性的二氧化硅载体并且包括改性金属锆和/或铪和改性的载体上的催化金属。催化剂的改性金属的至少一部分,典型地至少25%以共有至多2个改性金属原子的基团形式存在。基团可以源自单体和/或二聚体阳离子源。一种生产方法:提供具有孤立硅醇基的二氧化硅载体,可选地处理载体以提供含量<2.5基团/nm 2 的孤立硅醇基(‑SiOH);使可选地处理的二氧化硅载体与单体锆或铪改性金属化合物接触,以实现到载体上的吸附;可选地在准备用于催化剂浸渍时,用足以将吸附在表面上的单体锆或铪化合物转化为锆或铪的氧化物或氢氧化物的时间和温度来煅烧改性的载体。一种生产烯属不饱和羧酸或酯,典型地α,β‑烯属不饱和羧酸或酯的方法,包括步骤:在催化剂的存在下,并且可选地在醇的存在下,使甲醛或适宜的甲醛来源与羧酸或酯接触,其中,使用所述催化剂。

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28-05-2021 дата публикации

Organic microporous polymer supported metal catalyst and preparation method thereof

Номер: CN109529941B
Принадлежит: Huaihua University

本发明涉及一种有机微孔聚合物负载金属催化剂及其制备方法,该催化剂具有如通式(I)的结构: 其中,Ar为5至6个环原子的芳族或杂芳族环; 为取代或未取代的5至6个环原子的芳族环或杂芳族环;X 1 为卤素阴离子、醋酸根、硝酸根或硫酸根;n为整数,R 1 为H、甲基或取代或未取代的芳基,且n=0时,R 1 不为H;R 2 为H或烷基;M为过渡金属。上述有机微孔聚合物负载金属催化剂具有如通式(I)的结构,其中的M与P和有机框架构成六元环状配合体,因此其中的M与P和有机框架具有更强的配合能力,使得有机微孔聚合物负载金属催化剂的稳定性更高。

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29-06-2009 дата публикации

Synthesis of 4-phenylbutyric acid

Номер: KR100905139B1
Принадлежит: 스탠니슬로우 알 벌진스키

화학식(Ⅰ)의 화합물을 제조하는 방법: Process for preparing the compound of formula (I): 화학식Ⅰ은 방향족화합물을 부티로락톤과 반응시키고 나서, 염기로 중화시켜 얻는다. 상기 반응은 촉매의 존재하에서 일어날 수 있다. 바람직한 촉매로는 루이스산이 있다. 바람직한 화학식Ⅰ의 생성물은 4-페닐부티르산으로, 이는 벤젠과 부티로락톤을 염화알루미늄의 존재하에 반응시킨 다음, 염기로 중화하는 것으로 얻는다. Formula I is obtained by reacting an aromatic compound with butyrolactone and neutralizing it with a base. The reaction can take place in the presence of a catalyst. Preferred catalysts are Lewis acids. A preferred product of formula I is 4-phenylbutyric acid, which is obtained by reacting benzene and butyrolactone in the presence of aluminum chloride and then neutralizing with a base. 4-페닐부티르산, 루이스산 4-phenylbutyric acid, Lewis acid

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03-12-2009 дата публикации

Unsaturated dicarboxylic acids from unsaturated cyclic hydrocarbons and acrylic acid by metathesis, their use as monomers for polyamides, polyesters, polyurethanes and further conversion to diols and diamines

Номер: DE102008002090A1
Принадлежит: EVONIK DEGUSSA GmbH

Es wird ein Verfahren zur Herstellung alpha, beta-ungesättigter Dicarbonsäuren und den entsprechenden gesättigten Dicarbonsäuren beschrieben, bei dem das entsprechende Cycloalken und Acrylsäure mit einem Ruthenium-Katalysator über eine Metathese-Reaktion bei hohen Substratkonzentrationen bis hin zur Reaktion in Substanz umgesetzt werden, wobei die dabei entstehende Dicarbonsäure ausfällt. The invention relates to a process for preparing alpha, beta-unsaturated dicarboxylic acids and the corresponding saturated dicarboxylic acids, in which the corresponding cycloalkene and acrylic acid are reacted with a ruthenium catalyst via a metathesis reaction at high substrate concentrations up to the reaction in substance, the resulting dicarboxylic acid precipitates.

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13-10-2020 дата публикации

Method for synthesizing acrylic acid

Номер: CN111763143A

本发明涉及一种丙烯酸的合成方法,具体涉及乙酸和甲醛水溶液经过催化转化制备丙烯酸的工艺方法。包括在含有羟醛缩合催化剂存在下乙酸与甲醛的接触反应得到丙烯酸的反应过程以及分离过程;所说的反应过程的产物经所说的分离过程至少得到乙酸、丙烯酸、水。其中,所说的分离过程得到乙酸循环用于反应过程。该方法丙烯酸的收率可达95%以上。

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15-02-1982 дата публикации

Method for preparing hydrochloride of n-alkyl derivatives of 1-phenyl-2-amino-1,3-propanediol

Номер: SU906366A3

The invention relates to novel 1-phenyl-2-amino-1,3-propanediol-N-alkyl derivatives having the general formula I <IMAGE> (I) wherein R1 is hydrogen, alkyl having from 1 to 8 carbon atoms or phenoxymethyl, and R2 is hydrogen, alkyl having from 1 to 8 carbon atoms or 2,2-diphenylethyl, with the proviso that if R1 is phenoxymethyl then R2 may stand only for methyl, and if R2 is 2,2-diphenylethyl then R1 may stand only for hydrogen, and its isomers and pharmaceutically acceptable salts. Furthermore, the invention relates to a process for preparing these compounds. The novel 1-phenyl-2-amino-1,3-propanediol-N-alkyl derivatives having the general formula I possess significant anti-anginose activity and show several other biological activities.

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27-07-2011 дата публикации

ORGANIC COMPOUNDS

Номер: RU2010101236A

1. Способ получения соединения формулы (I) ! ! где ! R1 означает OR3 или NR4R5; ! R2 означает C1-С7алкил или С3-С8циклоалкил; ! R3 означает водород, C1-С7алкил, фенил- или нафтилС1-С4алкил, арил, гетероциклил или С3-С8циклоалкил, каждый из которых незамещен или замещен; или означает SiRR'R'', где R, R' и R'' независимо друг от друга означают C1-С7алкил, арил или фенилС1-С4алкил; ! R4 и R5 независимо друг от друга означают водород, C1-C7алкил, фенил- или нафтилС1-С4алкил, арил, гетероциклил или С3-С8циклоалкил, каждый из которых незамещен или замещен; ! или R4 и R5 могут вместе образовывать 3-7-членное азотсодержащее насыщенное углеводородное кольцо, которое может содержать один или более гетероатомов, выбранных из N или О, и которое может быть незамещенным или замещенным; ! или его соль; ! где указанный процесс включает одну или более следующих стадий: ! с) введение соединения формулы (II) или его соли ! ! где R1 и R2 означают то, что определено для соединения формулы (I), в реакцию кросс-метатезиса с получением соединения формулы (III) или его соли ! ! где R1 и R2 означают то, что определено для соединения формулы (I); ! d) введение указанного соединения формулы (III) или его соли в реакцию гидрирования с получением соединения формулы (I) или его соли. ! 2. Способ получения соединения формулы (III) ! ! где ! R1 означает OR3 или NR4R5; ! R2 означает C1-С7алкил или С3-С8циклоалкил; ! R3 означает водород, C1-С7алкил, фенил- или нафтилС1-С4алкил, арил, гетероциклил или С3-С8циклоалкил, каждый из которых незамещен или замещен; или означает SiRR'R'', где R, R' и R'' независимо друг от друга означают C1-С7алкил, арил или фенилС1-С4алкил; ! R4 и R5 независимо друг от друга означают водород, C1-С7алкил, фенил- или нафтил� РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) 2010 101 236 (13) A (51) МПК C07C 51/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ, ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ЗАЯВКА НА ИЗОБРЕТЕНИЕ (21)(22) Заявка: ...

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