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公开(公告)号:US20160332152A1
公开(公告)日:2016-11-17
申请号:US14907714
申请日:2014-07-16
Applicant: BASF SE , DOW GLOBAL TECHNOLOGIES LLC
Inventor: Andrei-Nicolae PARVULESCU , Ulrich MUELLER , Joaquim Henrique TELES , Bianca SEELIG , Philip KAMPE , Markus WEBER , Peter RESCH , Christian BARTOSCH , Dominic RIEDEL , Daniel URBANCZYK , Alexander SCHROEDER , Ulrike WEGERLE
IPC: B01J29/90 , B01J37/02 , B01J37/00 , C07D301/12 , B01J37/30 , B01J38/48 , B01J38/06 , B01J38/02 , B01J29/70 , B01J37/08
CPC classification number: B01J29/90 , B01J29/7088 , B01J29/89 , B01J35/00 , B01J37/0009 , B01J37/0045 , B01J37/0201 , B01J37/0203 , B01J37/06 , B01J37/08 , B01J37/10 , B01J37/30 , B01J38/02 , B01J38/06 , B01J38/48 , B01J2229/183 , B01J2229/186 , B01J2229/42 , C07D301/12 , C07D303/04 , Y02P20/584
Abstract: The present invention relates to a process for the regeneration of a catalyst comprising a titanium-containing zeolite, said catalyst having been used in a process for the preparation of an olefin oxide and having phosphate deposited thereon, said process for the regeneration comprising the steps: (a) separating the reaction mixture from the catalyst, (b) washing the catalyst obtained from (a) with liquid aqueous system; (c) optionally drying the catalyst obtained from (b) in a gas stream comprising an inert gas at a temperature of less than 300° C.; (d) calcining the catalyst obtained from (c) in a gas stream comprising oxygen at a temperature of at least 300° C.
Abstract translation: 本发明涉及一种用于再生包含含钛沸石的催化剂的方法,所述催化剂已用于制备烯烃氧化物并沉积有磷酸盐的方法中,所述再生方法包括以下步骤: (a)将反应混合物与催化剂分离,(b)用液体水系洗涤由(a)获得的催化剂; (c)任选地在低于300℃的温度下将包含惰性气体的气流中的(b)得到的催化剂干燥; (d)在至少300℃的温度下,将由(c)得到的催化剂在包含氧的气流中煅烧
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公开(公告)号:US20160176834A1
公开(公告)日:2016-06-23
申请号:US14907998
申请日:2014-07-16
Applicant: BASF SE , DOW GLOBAL TECHNOLOGIES LLC
Inventor: Joaquim Henrique TELES , Bianca SEELIG , Dominic RIEDEL , Philip KAMPE , Daniel URBANCZYK , Markus WEBER , Ulrich MUELLER , Andrei-Nicolae PARVULESCU , Kai GUMLICH , Peter BASSLER , Christian BARTOSCH , Richard JACUBINAS , Meinolf WEIDENBACH , Werner WITZL
IPC: C07D301/12 , B01J27/188 , B01J27/18 , B01J29/70
CPC classification number: C07D301/12 , B01J27/18 , B01J27/188 , B01J29/7038 , B01J29/7088 , B01J35/002 , B01J35/1019 , B01J2229/186 , Y02P20/52
Abstract: A continuous process for the preparation of propylene oxide, comprising (i) providing a liquid feed stream comprising propene, hydrogen peroxide, acetonitrile, water, optionally propane, and at least one dissolved potassium salt of a phosphorus oxyacid wherein the molar ratio of potassium relative to phosphorus in the at least one potassium salt of a phosphorus oxyacid is in the range of from 0.6 to 1.4; (ii) passing the liquid feed stream provided in (i) into an epoxidation reactor comprising a catalyst comprising a titanium zeolite of structure type MVVW comprising zinc, and subjecting the liquid feed stream to epoxidation reaction conditions in the epoxidation reactor, obtaining a reaction mixture comprising propylene oxide, acetonitrile, water, the at least one dissolved potassium salt of a phosphorus oxyacid, optionally propene, and optionally propane; (iii) removing an effluent stream from the epoxidation reactor, the effluent stream comprising propylene oxide, acetonitrile, water, at least a portion of the at least one dissolved potassium salt of a phosphorus oxyacid, optionally propene, and optionally propane.
Abstract translation: 一种用于制备环氧丙烷的连续方法,包括(i)提供包含丙烯,过氧化氢,乙腈,水,任选的丙烷和至少一种溶解的含磷酸钾的液体进料流,其中钾相对的摩尔比 在磷氧基酸的至少一种钾盐中的磷在0.6至1.4的范围内; (ii)将(i)中提供的液体进料流送入包含催化剂的环氧化反应器中,所述催化剂包含含锌的结构型MVVW的钛沸石,并使液体进料流在环氧化反应器中进行环氧化反应条件,得到反应混合物 包括环氧丙烷,乙腈,水,所述至少一种溶解的含磷酸的钾盐,任选的丙烯,以及任选的丙烷; (iii)从环氧化反应器中除去流出物流,所述流出物流包含环氧丙烷,乙腈,水,所述至少一种溶解的含磷酸的钾盐,任选的丙烯和任选的丙烷的至少一部分。
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公开(公告)号:US20160115140A1
公开(公告)日:2016-04-28
申请号:US14787956
申请日:2014-04-28
Applicant: BASF SE , DOW GLOBAL TECHNOLOGIES LLC
Inventor: Joaquim H. TELES , Dominic RIEDEL , Bianca SEELIG , Philip KAMPE , Daniel URBANCZYK , Markus WEBER , Alexander SCHROEDER , Andrei-Nicolae PARVULESCU , Ulrich MUELLER , Meinolf WEIDENBACH , Werner WITZL , Holger BAER
IPC: C07D301/12 , B01D3/14 , C07D301/32
CPC classification number: C07D301/12 , B01D3/143 , C07D301/32
Abstract: A continuous process for the preparation of propylene oxide, comprising (a) reacting propene, optionally admixed with propane, with hydrogen peroxide in a reaction apparatus in the presence of acetonitrile as solvent, obtaining a stream S0 containing propylene oxide, acetonitrile, water, at least one further component B, optionally propene and optionally propane, wherein the normal boiling point of the at least one component B is higher than the normal boiling point of acetonitrile and wherein the decadic logarithm of the octanol-water partition coefficient (log Kow) of the at least one component B is greater than zero; (b) separating propylene oxide from S0, obtaining a stream S1 containing acetonitrile, water and the at least one further component B; (c) dividing S1 into two streams S2 and S3; (d) subjecting S3 to a vapor-liquid fractionation in a fractionation unit, obtaining a vapor fraction stream S4 being depleted of the at least one component B; (e) recycling at least a portion of S4, optionally after work-up, to (a).
Abstract translation: 一种用于制备环氧丙烷的连续方法,包括(a)在乙腈作为溶剂的存在下,在反应装置中将丙烯任选与丙烷混合,与过氧化氢反应,得到含有环氧丙烷,乙腈,水的流S0 至少一种另外的组分B,任选的丙烯和任选的丙烷,其中至少一种组分B的标准沸点高于乙腈的标准沸点,其中辛醇 - 水分配系数(log Kow)的十进制对数 所述至少一个组分B大于零; (b)从S0分离环氧丙烷,得到含有乙腈,水和至少一种其它组分B的料流S1; (c)将S1划分成两个流S2和S3; (d)使S3在分馏装置中进行汽 - 液分馏,得到耗尽至少一种B成分的蒸汽馏分流S4; (e)将至少一部分S4,任选地在后处理之后再循环至(a)。
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公开(公告)号:US20230030960A1
公开(公告)日:2023-02-02
申请号:US17785966
申请日:2020-12-18
Applicant: BASF SE
Inventor: Andrei-Nicolae PARVULESCU , Ulrich MUELLER , Jaroslaw Michael MORMUL , Joaquim Henrique TELES , Dominic RIEDEL , Markus WEBER
IPC: B01J29/70 , B01J29/89 , B01J37/02 , C07D301/12 , B01J35/10
Abstract: The present invention relates to a molding comprising a zeolitic material having framework type MWW, wherein the framework structure comprises Ti, Si, and O, wherein the zeolitic material further comprises Zn and an alkaline earth metal M, the molding further comprising a binder, wherein the molding exhibits a specific Lewis acidity. Further, the present invention relates to the method of preparation of said molding and the use thereof.
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公开(公告)号:US20220219154A1
公开(公告)日:2022-07-14
申请号:US17606875
申请日:2020-04-27
Applicant: BASF SE
Inventor: Andrei-Nicolae PARVULESCU , Hans-Juergen LUETZEL , Dominic RIEDEL , Ulrich MUELLER , Joaquim Henrique TELES , Markus WEBER
Abstract: A chemical molding comprising a zeolitic material which exhibits a type I nitrogen adsorption/desorption isotherm determined as described in Reference Example 1, and which has framework type MFI and a framework structure comprising Si, O, and Ti, the molding further comprising a binder for said zeolitic material, the binder comprising Si and O, wherein the molding exhibits a total pore volume of at least 0.4 mL/g and a crushing strength of at least 6 N.
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公开(公告)号:US20210002241A1
公开(公告)日:2021-01-07
申请号:US16500313
申请日:2018-04-13
Applicant: BASF SE
Inventor: Nicolai Tonio WOERZ , Ulrich MUELLERE , Andrei-Nicolae PARVULESCU , Dominic RIEDEL , Marvin KRAMP , Daniel URBANCZYK , Ulrike WEGERLE , Christian MUELLER , Bernd METZEN , Markus WEBER , Joaquim Henrique TELES
IPC: C07D301/32 , C07D301/19
Abstract: The invention relates to a process for preparing propylene oxide, comprising (i) providing a stream comprising propene, propane, hydrogen peroxide or a source of hydrogen peroxide, water, and an organic solvent; (ii) passing the liquid feed stream provided in (i) into an epoxidation zone comprising an epoxidation catalyst comprising a titanium zeolite, and subjecting the liquid feed stream to epoxidation reaction conditions in the epoxidation zone, obtaining a reaction mixture comprising propene, propane, propylene oxide, water, and the organic solvent; (iii) removing an effluent stream from the epoxidation zone, the effluent stream comprising propene, propane, propylene oxide, water, and the organic solvent; (iv) separating propene and propane from the effluent stream by distillation, comprising subjecting the effluent stream to distillation conditions in a distillation unit, obtaining a gaseous stream (S1) which is enriched in propene and propane compared to the effluent stream subjected to distillation conditions, and a liquid bottoms stream (S2) which is enriched in propylene oxide, water and organic solvent compared to the effluent stream subjected to distillation conditions; (v) separating propane from the stream (S1) in a separation zone, comprising subjecting the stream (S1) to washing conditions in a scrubber, wherein a solvent mixture comprising organic solvent and water is added as entraining agent, obtaining a bottoms stream (S3), which comprises organic solvent, water and at least 70 weight-% of the propene comprised in (S1); and a gaseous top stream (S4), which comprises at least 5 weight-% of the propane comprised in stream (S1).
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公开(公告)号:US20190169149A1
公开(公告)日:2019-06-06
申请号:US16318221
申请日:2017-07-19
Applicant: BASF SE , Dow Global Technologies LLC
Inventor: Joaquim Henrique TELES , Marvin KRAMP , Christian MUELLER , Nicolai Tonio WOERZ , Bernd METZEN , Tobias KELLER , Dominic RIEDEL , Heiner SCHELLING , Markus WEBER , Daniel URBANCZYK , Andrei-Nicolae PARVULESCU , Ulrike WEGERLE , Ulrich MUELLER , Meinolf WEIDENBACH , Werner J. WITZL , Karsten LUECKE
IPC: C07D301/32 , C07D301/12 , B01D3/00 , B01D3/40 , B01D3/14 , B01D5/00
CPC classification number: C07D301/32 , B01D1/28 , B01D3/00 , B01D3/009 , B01D3/143 , B01D3/40 , B01D5/006 , B01J29/085 , B01J29/7038 , B01J29/86 , B01J29/89 , B01J35/002 , B01J35/023 , B01J37/0045 , B01J2229/186 , B01J2229/42 , C07D301/12 , C07D303/04 , Y02P20/127 , Y02P20/52
Abstract: The present invention is related to a process for preparing propylene oxide, comprising (i) providing a stream comprising propene, hydrogen peroxide or a source of hydrogen peroxide, water, and an organic solvent; (ii) passing the liquid feed stream provided in (i) into an epoxidation zone comprising an epoxidation catalyst comprising a titanium zeolite, and subjecting the liquid feed stream to epoxidation reaction conditions in the epoxidation zone, obtaining a reaction mixture comprising propene, propylene oxide, water, and the organic solvent; (iii) removing an effluent stream from the epoxidation zone, the effluent stream comprising propylene oxide, water, organic solvent, and propene; (iv) separating propene from the effluent stream by distillation, comprising (iv.1) subjecting the effluent stream to distillation conditions in a distillation unit, obtaining a gaseous top stream S0 enriched in propene compared to the effluent stream subjected to distillation conditions, and a liquid bottoms stream S01 enriched in propylene oxide, water and organic solvent compared to the effluent stream subjected to distillation conditions; (iv.2) returning a condensed portion of the stream S0 to an upper part of the distillation unit.
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