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公开(公告)号:US2431585A
公开(公告)日:1947-11-25
申请号:US60572345
申请日:1945-07-18
Applicant: ICI LTD
Inventor: EDGAR ROUT ALFRED
IPC: B01J27/18 , C07C201/08 , C07C205/06
CPC classification number: C07C201/08 , B01J27/1802 , C07C205/06
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公开(公告)号:US2238195A
公开(公告)日:1941-04-15
申请号:US22051438
申请日:1938-07-21
Applicant: ATLANTIC REFINING CO
Inventor: THOMPSON KENNETH M
IPC: C07B43/02 , C07C201/08
CPC classification number: C07B43/02
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公开(公告)号:US20210260560A1
公开(公告)日:2021-08-26
申请号:US17260414
申请日:2018-11-15
Applicant: NORAM INTERNATIONAL LIMITED
Inventor: Stefan F. Meili
IPC: B01J19/24 , B01J19/00 , B01J10/00 , C07C201/08
Abstract: A nitration reactor (10) incorporating sections of downward flow for use in preparing nitrated organic compounds. It comprises a first vertically-oriented reactor section (12), a second vertically-oriented reactor section (14), a connecting section (16) between the two reactor sections, one or more inlets (20, 22) for introducing nitration reactants into the reactor, an outlet (24) for the removal of nitration reaction products, a vertically-downward flowpath (26) for the nitration reactants in one of the reactor sections or the connecting section, and operating conditions that produce a flow regime in the vertically-downward flowpath that is a dispersed flow regime or a bubbly flow regime. The invention overcomes the limitations of prior art nitration reactors of the type in which fluids flow largely in a vertically upward direction, with respect to hydrostatic demands and plant layout considerations.
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公开(公告)号:US11001552B2
公开(公告)日:2021-05-11
申请号:US16620001
申请日:2018-07-16
Applicant: LONZA LTD
Inventor: Michael Bersier , Anna Kulesza , Paul Hanselmann , Christof Aellig , Sarah Filliger
IPC: C07C201/08 , C07C205/58
Abstract: The invention discloses a method for preparation of 5-fluoro-2-methyl-3-nitrobenzoic acid and its methyl ester by conversion of 5-fluoro-2-methylbenzoic acid with fuming nitric acid and oleum and subsequent conversion with methanol.
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公开(公告)号:US10662145B2
公开(公告)日:2020-05-26
申请号:US16288031
申请日:2019-02-27
Applicant: FUDAN UNIVERSITY
Inventor: Fener Chen , Lingdong Wang , Ge Meng , Zedu Huang , Dang Cheng , Haihui Peng , Guanfeng Liang
IPC: C07C227/18 , C07C201/08 , C07C227/16 , C07C227/06
Abstract: The invention relates to the chemical synthesis of pharmaceutical API, and specifically to a method of synthesizing diclofenac sodium, which is a kind of nonsteroidal anti-inflammatory drug for relieving pain. The method includes: nitrating phenylacetate to prepare o-nitrophenylacetate (2); hydrogenating o-nitrophenylacetate (2) to prepare o-aminophenylacetate (3); amidating an amino group of o-aminophenylacetate (3) to obtain 2-(2-benzoylaminophenyl) acetate (4); 2-(2-benzoylaminophenyl) acetate (4) reacting with thionyl chloride to prepare a chloroimine intermediate, and then condensing the intermediate of chloroimine with 2,6-dichlorophenol using an inorganic base to prepare (E)-methyl-2-(2-((2,6-dichlorophenoxy)(phenyl)methyleneamino) phenyl ester (5); subjecting (E)-methyl-2-(2-((2,6-dichlorophenoxy)(phenyl)methyleneamino) phenyl ester (5) to Chapman rearrangement to afford methyl 2-(2-(N-(2,6-dichlorophenyl)benzoylamino)phenyl) ester (6); and hydrolyzing methyl 2-(2-(N-(2,6-dichlorophenyl)benzoylamino)phenyl) ester (6) to provide the target compound as of diclofenac sodium API. The overall yield is up to 67% based on methyl phenylacetate.
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公开(公告)号:US10513487B2
公开(公告)日:2019-12-24
申请号:US15320807
申请日:2015-06-22
Applicant: Covestro Deutschland AG
Inventor: Thomas Knauf , Peter Drinda , Stefan Wershofen , Klaus-Gerd Gruner , Volker Hartjes
IPC: C07C201/08 , C07C205/06 , B01J19/24 , C07C201/16
Abstract: This invention relates to methods for producing chemical products, wherein the one or more feed materials are reacted to form a chemical product or a chemical composition. The invention further relates to plants for performing such methods, said plants being designed in such a way that, during an interruption of the methods, no input of at least one feed material into the reaction occurs and the plant parts not affected by a revision measure, maintenance measure, repair measure, or cleaning measure are operated in so-called re-circulation mode. It is thereby achieved, among other things, that only the affected plant part needs to be shut down for the time of the measure, which can be advantageous with regard to the productivity and economy of the method and the quality of the produced products. Finally, the invention relates to methods for operating plants in the event that individual plant parts are taken out of service.
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公开(公告)号:US10040745B2
公开(公告)日:2018-08-07
申请号:US15515271
申请日:2015-10-07
Applicant: SYNGENTA PARTICIPATIONS AG
Inventor: Denis Gribkov
IPC: C07C45/46 , C07C45/63 , C07C201/00 , C07C205/00 , C07C201/08 , C07C201/12 , C07C205/45
Abstract: A process for the preparation of a compound of formula (I) wherein R1 is hydrogen, fluoro or chloro; which process comprises: a) reacting a compound of formula (II) wherein R1 is hydrogen, fluoro or chloro; with a nitration agent to the compound of formula (III) wherein R1 is hydrogen, fluoro or chloro; b) reacting the compound of formula (III) with trichloroisocyanuric acid in the presence of sulfuric acid or fuming sulfuric acid to the compound of formula (IV) wherein R1 is hydrogen, fluoro or chloro; and c) reacting the compound of formula (III) with chlorine gas at a temperature from 180° C. to 250° C. to the compound of formula (I).
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公开(公告)号:US10023524B2
公开(公告)日:2018-07-17
申请号:US15320804
申请日:2015-06-22
Applicant: Covestro Deutschland AG
Inventor: Thomas Knauf , Peter Drinda
IPC: C07C201/08 , C07C201/16 , B01J19/24
Abstract: The present invention relates to a process for the continuous production of nitrobenzene by the nitration of benzene with nitric acid and sulphuric acid under adiabatic conditions, not the entire production plant being shut down during a production stop, but the production plant being entirely or at least partly operated in recirculation mode. The invention further relates to a plant for producing nitrobenzene and to a method for operating a plant for producing nitrobenzene.
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公开(公告)号:US20180127435A1
公开(公告)日:2018-05-10
申请号:US15860058
申请日:2018-01-02
Applicant: ANGUS Chemical Company
Inventor: Daniel M. Trauth , George D. Green , Raymond J. Swedo , Richard L. James , Ian A. Tomlinson
IPC: C07D498/10 , A01N43/76 , C07C215/28 , C07C205/04 , C07C205/05 , C07C205/15 , C07C205/16 , C07C215/20 , A01N43/90 , C07C201/08 , C07C201/12 , C07C205/02 , C07C205/06 , C07C205/18 , C07C215/08 , C07C215/42 , C07C239/10 , C07D263/04 , C07D263/52 , C08G18/32 , C07D498/04
CPC classification number: C07D498/10 , A01N43/76 , A01N43/90 , C07C201/08 , C07C201/12 , C07C205/02 , C07C205/04 , C07C205/05 , C07C205/06 , C07C205/15 , C07C205/16 , C07C205/18 , C07C215/08 , C07C215/20 , C07C215/28 , C07C215/42 , C07C239/10 , C07C2601/08 , C07C2601/14 , C07C2601/18 , C07C2602/10 , C07D263/04 , C07D263/52 , C07D498/04 , C08G18/3271 , Y02P20/582
Abstract: Provided is a process for the formation of nitrated compounds by the nitration of hydrocarbon compounds with dilute nitric acid. Also provided are processes for preparing industrially useful downstream derivatives of the nitrated compounds, as well as novel nitrated compounds and derivatives, and methods of using the derivatives in various applications.
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公开(公告)号:US09771290B2
公开(公告)日:2017-09-26
申请号:US14784443
申请日:2014-04-15
Applicant: BAYER MATERIALSCIENCE AG
Inventor: Thomas Knauf , Antoni Mairata , Erik Sluyts , Jan Van Tricht
IPC: C02F9/00 , C02F1/02 , C02F1/20 , C02F1/66 , C07C201/16 , C07C201/08 , C02F101/32 , C02F101/38 , C02F103/18 , C02F101/16 , C02F103/36
CPC classification number: C02F9/00 , C02F1/025 , C02F1/20 , C02F1/66 , C02F2101/16 , C02F2101/322 , C02F2101/38 , C02F2103/18 , C02F2103/36 , C02F2301/066 , C07C201/08 , C07C201/16 , C07C205/06
Abstract: The present invention provides a process for working up alkaline waste water which is formed during washing of crude nitrobenzene obtained by nitration of benzene, wherein (i) the alkaline waste water is heated to a temperature of from 150° C. to 500° C. under an increased pressure with respect to atmospheric pressure with exclusion of oxygen; (ii) a base is added to the waste water obtained in (i); and (iii) the waste water obtained in (ii) is purified further by stripping with a stripping gas and the stripping gas stream loaded with impurities is then cooled to a temperature of from 10° C. to 60° C.
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