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公开(公告)号：US20240382922A1
公开(公告)日：2024-11-21
申请号：US18286598
申请日：2022-04-05
Applicant: BASF SE
Inventor： Frank HUETTEN , Florian WOLFF
Abstract: The invention relates to a method of closed-loop control of the temperature in a chemical engineering apparatus (101, 201, 301, 401), in which, in a primary circuit (102, 202, 302, 402), a liquid is conveyed out of the apparatus (101, 201, 301, 401), fed at least partly to a heat transferer (103, 203, 303, 403) and recycled at least partly back to the apparatus (101, 201, 301, 401), where the heat transferer (103, 203, 303, 403) is cooled or heated by a heat transfer medium in a secondary circuit (104, 204, 304, 404), comprising the steps of: providing a target value for the temperature of the liquid in the apparatus (101, 201, 301, 401), detecting an actual value for the temperature of the liquid in the apparatus (101, 201, 301, 401) and calculating the temperature difference between the actual value and the target value of the liquid in the apparatus (101, 201, 301, 401). According to the invention, a heat flow taken from or added to the liquid in the primary circuit (102, 202, 302, 402) by the heat transferer (103, 203, 303, 403) is ascertained, a control signal is calculated on the basis of a defined closed-loop control algorithm, where the closed-loop control algorithm is configured such that the control signal is dependent on the heat flow and the temperature difference between the actual value and the target value of the liquid in the apparatus (101, 201, 301, 401), and the flow rate of the stream of liquid through the heat transferer (103, 203, 303, 403) in the primary circuit (102, 202, 302, 402) and/or a flow rate of the heat transfer medium through the heat transferer in the secondary circuit (104, 204, 304, 404) is/are manipulated on the basis of the control signal.
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Patent Agency Ranking
公开(公告)号：US20170267621A1
公开(公告)日：2017-09-21
申请号：US15615852
申请日：2017-06-07
Applicant: BASF SE
Inventor： Ulrich HAMMON , Thomas WALTER , Markus OTTENBACHER , Frank HUETTEN
IPC: C07C51/487 , B01D3/00 , B01D3/14 , B01J19/24 , C07C51/42 , C07C57/04 , C07C51/48 , C07C51/44 , B01D3/34
CPC classification number: C07C51/487 , B01D3/009 , B01D3/143 , B01D3/346 , B01J19/24 , B01J2219/24 , C07C51/42 , C07C51/44 , C07C51/48 , C07C57/04
Abstract: A plant (1) for recovering acrylic acid, which includes: a absorption column (201); a dissociation column (205); a first line (101) connected to the dissociation column (205); a second line (102) connecting the absorption column (201) and the dissociation column (205); a third line (103) feeding a substream of the mother acid obtained in the crystallization into the dissociation column (205); a fourth line (104) connecting the crystallization apparatus and the absorption column (201); and a fifth line (105) connecting the dissociation column (205) and the absorption column (201).
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公开(公告)号：US20230174447A1
公开(公告)日：2023-06-08
申请号：US17916063
申请日：2021-03-24
Applicant: BASF SE
Inventor： Rainer PAPP , Frank HUETTEN , Dirk JUNGMANN , Edward RICHMOND
CPC classification number: C07C45/505 , B01J19/0006 , B01J23/75 , B01J2219/00164
Abstract: Process for hydroformylation of olefins having 6 to 20 carbon atoms in the presence of a cobalt catalyst in the presence of an aqueous phase with thorough mixing in a reactor wherein a hydroformylation products-containing first stream is withdrawn at the top of the reactor and an aqueous phase-containing second stream is withdrawn from the bottom of the reactor via at least one line leading out of the bottom of the reactor, which process comprises controlling one or more mass flow parameters of the second stream in accordance with the density of the second stream.
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4.发明申请公开(公告)号：US20150344621A1
公开(公告)日：2015-12-03
申请号：US14822921
申请日：2015-08-11
Applicant: BASF SE
Inventor： Frank HUETTEN , Otto MACHHAMMER , Thomas DANIEL , Markus OTTENBACHER , Daniel PFEIFFER , Stefanie HERZOG , Manfred HEILIG , Klaus Joachim MUELLER-ENGEL
IPC: C08G63/81
CPC classification number: C08G63/81 , C07C51/252 , C07C51/42 , C07C51/47 , C07C57/04 , Y02P20/582
Abstract: An aqueous solution comprising acrylic acid and the conjugate base thereof in a total amount of at least 10% by weight, based on the weight of the aqueous solution, and propionic acid and the conjugate base thereof, formic acid and the conjugate base thereof, acetic acid and the conjugate base thereof, benzoic acid and the conjugate base thereof, maleic anhydride, maleic acid and the conjugate bases thereof, phthalic anhydride, phthalic acid and the conjugate bases thereof, acrolein, benzaldehyde, 2-furaldehyde, and at least 20 mol % of at least one alkali metal cation; process for preparing this solution; and the use of this solution for preparation of polymer by free-radical polymerization.
Abstract translation: 包含丙烯酸及其共轭碱的水溶液的总量为至少10重量％，基于水溶液的重量，丙酸及其共轭碱，甲酸及其共轭碱，乙酸 酸及其共轭碱，苯甲酸及其共轭碱，马来酸酐，马来酸及其共轭碱，邻苯二甲酸酐，邻苯二甲酸及其共轭碱，丙烯醛，苯甲醛，2-糠醛，和至少20摩尔 ％的至少一种碱金属阳离子; 制备该溶液的方法; 以及使用该溶液通过自由基聚合制备聚合物。
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公开(公告)号：US20160090347A1
公开(公告)日：2016-03-31
申请号：US14857967
申请日：2015-09-18
Applicant: BASF SE
Inventor： Ulrich HAMMON , Thomas WALTER , Markus OTTENBACHER , Frank HUETTEN
CPC classification number: C07C51/487 , B01D3/009 , B01D3/143 , B01D3/346 , B01J19/24 , B01J2219/24 , C07C51/42 , C07C51/44 , C07C51/48 , C07C57/04
Abstract: The present invention relates to the process for recovering acrylic acid, comprising the steps a) division of a heated mother acid stream in direction of an absorption column (201) and a dissociation column (205), b) feeding of a heated mother acid substream as runback to the dissociation column (205), c) feeding-in of at least one stripping gas stream to the dissociation column (205), d) feeding-in of a secondary component stream comprising oligomeric acrylic acid from the condensation column (201) to the dissociation column (205), e) dissociation of part of oligomeric acrylic acid in the dissociation column (205) to give monomeric acrylic acid, f) removal of secondary components comprised in the secondary component stream in the dissociation column (205), g) discharge of monomeric acrylic acid as gas mixture with introduced circulating stripping gas stream from the dissociation column (205) and h) feeding-in of the gas mixture to the condensation column (201).
Abstract translation: 本发明涉及回收丙烯酸的方法，包括步骤a）在吸收塔（201）和解离塔（205）的方向上分离加热的母体酸流，b）加热加热的母体酸性流 作为分离塔（205）的回流，c）将至少一个汽提气流进料到解离塔（205），d）从冷凝塔（201）中加入包含低聚丙烯酸的二次组分料流 ）解离塔（205），e）解离塔（205）中部分低聚丙烯酸的解离以得到单体丙烯酸，f）除去在解离塔（205）中的次要组分流中包含的次要组分， g）从引入的离解塔（205）的引入的循环汽提气流中排出作为气体混合物的单体丙烯酸，以及h）将气体混合物进入冷凝塔（201）。
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公开(公告)号：US20130289305A1
公开(公告)日：2013-10-31
申请号：US13933732
申请日：2013-07-02
Applicant: BASF SE
Inventor： Stefanie HERZOG , Stefan ALTWASSER , Markus OTTENBACHER , Frank HUETTEN , Annebart Engbert WENTINK , Alexander SCHAEFER
IPC: C07C57/04
CPC classification number: C07C57/04 , C07B2200/05 , C07C51/235 , C07C51/353 , C07C53/08
Abstract: A process for preparing acrylic acid from ethanol and formaldehyde, in which, in a reaction zone A, the ethanol is partially oxidized to acetic acid in a heterogeneously catalyzed gas phase reaction, the product gas mixture A obtained and a formaldehyde source are used to obtain a reaction gas input mixture B which comprises acetic acid and formaldehyde and has the acetic acid in excess over the formaldehyde, and the formaldehyde present in reaction gas input mixture B is aldol-condensed with acetic acid present in reaction gas input mixture B to acrylic acid under heterogeneous catalysis in a reaction zone B, and unconverted acetic acid still present along-side the acrylic acid target product in the product gas mixture B obtained is removed therefrom, and the acetic acid removed is recycled into the production of reaction gas input mixture B.
Abstract translation: 一种从乙醇和甲醛制备丙烯酸的方法，其中在反应区A中乙醇在非均相催化气相反应中部分氧化成乙酸，得到的产物气体混合物A和甲醛源用于获得 反应气体输入混合物B，其包含乙酸和甲醛，并且乙酸超过甲醛，反应气体输入混合物B中存在的甲醛与反应气体输入混合物B中存在的乙酸醛醛缩合成丙烯酸 在反应区B中的非均相催化下，从得到的产物气体混合物B中沿着丙烯酸目标产物仍然存在未转化的乙酸，除去乙酸，再循环到反应气体输入混合物B 。
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