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公开(公告)号：WO2022177438A1
公开(公告)日：2022-08-25
申请号：PCT/NL2022/050095
申请日：2022-02-22
Applicant: STAMICARBON B.V.
Inventor： GEURTS, Wilhelmus Hubertus
IPC: B01J10/00 , B01J19/00 , C01C1/18 , C07C273/04
Abstract: Some embodiments of the disclosure pertain to a plant and a process for producing a urea-containing product. The plant comprises a medium pressure dissociation unit and a high pressure CO2 stripper each receiving a part of the urea synthesis solution. Stripped urea solution is further treated in a medium pressure treatment unit.
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公开(公告)号：WO2020235999A1
公开(公告)日：2020-11-26
申请号：PCT/NL2020/050326
申请日：2020-05-22
Applicant: STAMICARBON B.V.
Inventor： PUCI, Giusy Elisa , DIRKX, Wilfried Marc Renaat
IPC: B01D47/05 , B01D47/06 , B01D47/10 , B01D47/12 , C07C273/16
Abstract: Disclosed is a urea finishing method including an off-gas treatment, the method comprising urea finishing and supplying the off-gas to a quenching zone and to a scrub column comprising a sump and a venturi stage, wherein the sump has a split sump configuration with two compartments.
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73.发明申请
公开(公告)号：WO2019240586A1
公开(公告)日：2019-12-19
申请号：PCT/NL2019/050370
申请日：2019-06-17
Inventor： CINOTTI, Pierlorenzo , COLOZZI, Michele , CORTESE, Simona , MICCIO, Marino , PALO, Emma , BARBATO, Lucia , PALMA, Vincenzo , BARBA, Daniela
IPC: B01J37/08 , B01J37/20 , B01J21/04 , B01J23/755 , B01J23/83 , B01J37/00 , B01J37/02 , B01D53/86 , C01B17/04
Abstract: Disclosed is a catalyst suitable for the catalytic oxidative cracking of a H 2 S- containing gas stream. The catalyst comprises at least one or more active metals selected from the group consisting of iron, cobalt, and nickel, supported by a carrier comprising ceria and alumina. The active metal is preferably in the form of its sulphide. Also disclosed is a method for the production of hydrogen from a H 2 S-containing gas stream, comprising subjecting the gas stream to catalytic oxidative cracking so as to form H 2 and S 2 , using a catalyst in accordance with any one of the composition claims.
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公开(公告)号：WO2019093891A1
公开(公告)日：2019-05-16
申请号：PCT/NL2018/050747
申请日：2018-11-09
Applicant: STAMICARBON B.V.
IPC: C07C273/04 , B01D5/00 , B01J3/00
Abstract: Processes and plants for the production of purified urea solution are described. In a described urea production process, urea is produced in a synthesis section without a high pressure stripper and the urea solution is subjected to purification after the recovery section, to give purified urea solution and off-gas. The purification comprises e.g. steam stripping.
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公开(公告)号：WO2018052304A1
公开(公告)日：2018-03-22
申请号：PCT/NL2017/050619
申请日：2017-09-19
Applicant: STAMICARBON B.V.
Abstract: Disclosed is a dual pressure plant for the production of nitric acid on the basis of the oxidation of ammonia. The plant comprises a reactor configured to produce a burner gas stream; a gas cooling section configured to form a cooled burner gas; a condensation section configured to form an aqueous nitric acid condensate and an uncondensed nitrogen oxides gas stream; an absorption section configured to produce raw nitric acid and a tail gas; and a tail gas treatment system configured to form a purified tail gas. In a tail gas heating section a further heat exchanger configured to receive heat from the burner gas stream, said further heat exchanger being positioned relatively close to the reactor.
Abstract translation: 公开了一种用于基于氨的氧化来生产硝酸的双压力设备。 该设备包括构造成产生燃烧器气流的反应器; 气体冷却部分，其被配置成形成冷却的燃烧器气体; 配置成形成含水硝酸冷凝物和未冷凝的氮氧化物气流的冷凝部分; 吸收部，其构造成产生生硝酸和尾气; 以及构造成形成净化尾气的尾气处理系统。 在尾气加热段中设置另一热交换器，该另一热交换器构造成接收来自燃烧器气流的热量，所述另一热交换器相对靠近反应器设置。
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Patent Agency Ranking
公开(公告)号：WO2017196167A1
公开(公告)日：2017-11-16
申请号：PCT/NL2017/050287
申请日：2017-05-09
Applicant: STAMICARBON B.V.
Inventor： HIGGINS, Brian Sayre , TATE III, John Marshall , YATES, Robert Arthur , POMERLEAU, Marcel Julien , HEON, Jon Michael , DIRKX, Wilfried Marc Renaat , COLOMA GONZÁLEZ, Juan
IPC: B01D47/06 , B01D47/10 , B01D53/58 , C07C273/16 , C05C9/00
Abstract: Disclosed are methods and systems for removing submicron particles from a gas stream, in particular from urea prilling off-gas, wherein a Venturi ejector is used. A method comprises contacting a gas stream containing submicron particles in a Venturi ejector with an injected high velocity scrubbing liquid to provide a pumping action, wherein the scrubbing liquid has an initial velocity of at least 2 m/s and wherein the ratio of scrubbing liquid and gas flow is between 0.0005 and 0.0015 (m³/h) / (m³/h). The disclosure also pertains to a prilling tower having a gas stream treatment system comprising a Venturi ejector at the top of the prilling tower, and to a method of modifying an existing prilling tower.
Abstract translation: 公开了用于从气流，特别是尿素造粒废气中去除亚微米颗粒的方法和系统，其中使用文丘里喷射器。 一种方法包括使文丘里喷射器中含有亚微米颗粒的气流与注入的高速洗涤液接触以提供泵送作用，其中洗涤液的初始速度为至少2m / s，并且其中洗涤液和 气体流量在0.0005和0.0015（m3 / h）/（m3 / h）之间。 本发明还涉及具有气流处理系统的造粒塔以及改造现有造粒塔的方法，所述气流处理系统包括位于造粒塔顶部的文丘里喷射器。
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公开(公告)号：WO2017171546A1
公开(公告)日：2017-10-05
申请号：PCT/NL2017/050196
申请日：2017-03-30
Applicant: STAMICARBON B.V.
IPC: C07C273/04 , B01J19/24
Abstract: Disclosed is a urea plant wherein, in deviation from conventional plants, a high-pressure synthesis section is operated with two different pressures. The synthesis section comprises a reactor, which is operated under a first high pressure. The synthesis section also comprises a stripper and a condenser, both operated at substantially the same second high pressure. In accordance with the invention, the first pressure is substantially higher than the second pressure. The disclosed plant particularly comprises a compression unit capable of converting a pressure difference into work, or more specifically, mechanical energy for compression. This compression unit is positioned between a liquid outlet of the condenser and a liquid inlet of the reactor, and in fluid communication therewith. In order to make use of a pressure drop (expansion as a result of a liquid being depressurized), said compression unit is configured to obtain compression energy from one or more events in the urea production process ( i.e. , at one or more points in the urea production plant), at which a loss of energy occurs, such as decompression of a high energy stream. Typically, the compression unit is thereby configured to utilize mechanical energy recovered from a decompression unit positioned downstream of the stripper and upstream of the recovery section.
Abstract translation: 公开了一种尿素装置，其中与常规装置不同，高压合成段在两种不同的压力下操作。 合成部分包括在第一高压下操作的反应器。 合成部分还包括汽提器和冷凝器，二者均在基本上相同的第二高压下操作。 根据本发明，第一压力显着高于第二压力。 所公开的设备特别包括能够将压力差转换成功的压缩单元，或者更具体地说，包括用于压缩的机械能。 该压缩单元位于冷凝器的液体出口和反应器的液体入口之间并与其流体连通。 为了利用压降（由于液体被减压而引起的膨胀），所述压缩单元被配置为从尿素生产过程中的一个或多个事件获得压缩能量（即， 在尿素生产厂中的一个或多个点），在该点发生能量损失，例如高能量流的减压。 典型地，压缩单元因此被配置成利用从位于汽提器下游和回收段上游的减压单元回收的机械能。
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公开(公告)号：WO2017111585A1
公开(公告)日：2017-06-29
申请号：PCT/NL2016/050902
申请日：2016-12-21
Applicant: STAMICARBON B.V.
Inventor： PUCI, Giusy Elisa , DOBREE, Joey
CPC classification number: C05C1/00 , B01D53/1418 , B01D53/58 , B01D53/78 , B01D2257/406 , C05C9/005
Abstract: The invention relates to a process for the production of urea ammonium nitrate, a system and a method of modifying a plant. The process comprises treating ammonia-containing off-gas resulting from the production of ammonium nitrate (AN off-gas) with acidic scrubbing liquid in a finishing treatment section having a gas inlet in fluid communication with a gas outlet of a finishing section of a urea production unit, wherein the finishing section is adapted to solidify urea liquid, and wherein said finishing treatment section is adapted to subject ammonia-containing off-gas of the finishing section to treatment with an acidic scrubbing liquid.
Abstract translation: 本发明涉及生产尿素硝酸铵的方法，系统和修饰植物的方法。 该方法包括在具有与尿素精制部分的气体出口流体连通的气体入口的精整处理部分中用酸性洗涤液处理由生产硝酸铵（AN废气）而产生的含氨废气 生产单元，其中精整部分适于固化尿素液体，并且其中所述精整处理部分适于使精整部分的含氨废气接受酸性洗涤液的处理。
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公开(公告)号：WO2017065613A1
公开(公告)日：2017-04-20
申请号：PCT/NL2016/050711
申请日：2016-10-17
Inventor： IAQUANIELLO, Gaetano , SALLADINI, Annarita
IPC: C01B3/38 , C07C29/151 , C07C31/04
CPC classification number: C07C29/1518 , C01B3/382 , C01B2203/0244 , C01B2203/043 , C01B2203/0475 , C01B2203/061 , C01B2203/1058 , C01B2203/1064 , C01B2203/107 , C01B2203/148 , Y02P30/30 , C07C31/04
Abstract: Disclosed is a process for the production of methanol from a hydrocarbon feed. Particularly, the process is suitable for a hydrocarbon feed that has not been subjected to the removal of carbon dioxide. The process of the invention comprises the steps of (a) providing a hydrocarbon feed; (b) subjecting the hydrocarbon feed to Catalytic Partial Oxidation (CPO) so as to obtain a synthesis gas mixture; and (c) subjecting the synthesis gas mixture to methanol-forming conditions together with an additional feed of hydrogen (H 2 ), so as to obtain methanol; wherein the hydrocarbon feed is a CO 2 - containing hydrocarbon feed and wherein the Catalytic Partial Oxidation is conducted in the presence of a molar excess of H 2 O, and wherein the additional hydrogen feed is obtained by recovering blowdown gas obtained from the reactor in which the methanol formation takes place and subjecting the recovered gas to pressure swing absorption so as to extract hydrogen therefrom, and wherein gas remaining after hydrogen extraction is recycled as a feed to the Catalytic Partial Oxidation. The process of the invention is particularly suitable for the production of methanol in off-shore circumstances, such as by Floating Production Storage and Offloading (FPSO).
Abstract translation: 公开了一种从烃进料生产甲醇的方法。 特别地，该方法适用于未经过去除二氧化碳的烃类进料。 本发明的方法包括以下步骤：（a）提供烃进料; （b）使烃进料经受催化部分氧化（CPO）以获得合成气混合物; 和（c）使合成气体混合物与另外的氢气进料（H 2）一起进入甲醇形成条件以获得甲醇; 其中所述烃进料是含CO 2的烃进料，并且其中所述催化部分氧化在摩尔过量的H 2 O存在下进行，并且其中所述另外的 通过回收从其中发生甲醇形成的反应器获得的排出气体，并且使回收的气体进行变压吸附以从其中提取氢气，并且其中在氢气提取之后剩余的气体作为催化剂的进料被再循环而获得氢气进料 部分氧化。 本发明的方法特别适用于在海上环境中生产甲醇，例如浮式生产储存和卸载（FPSO）。
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80.发明申请
公开(公告)号：WO2016140574A1
公开(公告)日：2016-09-09
申请号：PCT/NL2016/050150
申请日：2016-03-04
Inventor： CROPPI, Chiara , MARTORELLI, Francesco Simone , PALO, Emma , IAQUANIELLO, Gaetano , SALLADINI, Annarita
CPC classification number: C07C5/333 , B01D53/226 , B01D53/228 , B01D53/229 , B01D69/02 , B01D71/022 , B01D2053/221 , B01D2256/24 , B01D2256/245 , B01D2257/108 , B01D2325/04 , B01J19/245 , B01J19/2475 , B01J2219/24 , C07C5/3335 , C07C5/3337 , C07C7/144 , C07C2521/04 , C07C2523/26 , C07C2523/42 , C07C11/06 , C07C11/04 , C07C11/08 , C07C15/46
Abstract: Disclosed is a method and plant for the catalytic dehydrogenation of alkanes, such as propane. The plant is a plant of hybrid architecture wherein one or more membrane-assisted reactor configurations according to open architecture are combined with one or more membrane-containing reactors of closed architecture. Hydrogen remaining in the reaction mixture after separation in the membrane separation unit of a first open architecture configuration, is fed to a first membrane-reactor of the closed architecture type. Also disclosed are methods of modifying plants so as to create the hybrid architecture plant.
Abstract translation: 公开了用于烷烃如丙烷的催化脱氢的方法和设备。 该植物是混合结构的植物，其中根据开放结构的一个或多个膜辅助反应器构造与一个或多个封闭结构的含膜反应器组合。 在第一开放结构构造的膜分离单元中分离后残留在反应混合物中的氢气被供给到封闭结构类型的第一膜反应器。 还公开了修改植物以创建混合建筑工厂的方法。
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