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    • 74. 发明申请
    • PLANT AND PROCESS FOR PRODUCING NITRIC ACID
    • 生产硝酸的装置和方法
    • WO2018052304A1
    • 2018-03-22
    • PCT/NL2017/050619
    • 2017-09-19
    • STAMICARBON B.V.
    • POSTMA, Leonardus HubertusMUÑOZ LÓPEZ, Maria PazVOORWINDEN, Martinus
    • C01B21/26C01B21/40B01D53/86
    • 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.
    • 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。
    • 76. 发明申请
    • UREA PRODUCTION WITH BI-PRESSURIZED SYNTHESIS
    • 双加压合成尿素生产
    • WO2017171546A1
    • 2017-10-05
    • PCT/NL2017/050196
    • 2017-03-30
    • STAMICARBON B.V.
    • COLOMA GONZÁLEZ, JuanDIELTJENS, Luc Louis MariaMENNEN, Johannes Henricus
    • C07C273/04B01J19/24
    • 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.
    • 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。
    • 78. 发明申请
    • PROCESS FOR THE PRODUCTION OF METHANOL
    • 甲醇生产工艺
    • WO2017065613A1
    • 2017-04-20
    • PCT/NL2016/050711
    • 2016-10-17
    • STAMICARBON B.V. ACTING UNDER THE NAME OF MT INNOVATION CENTER
    • IAQUANIELLO, GaetanoSALLADINI, Annarita
    • C01B3/38C07C29/151C07C31/04
    • C07C29/1518C01B3/382C01B2203/0244C01B2203/043C01B2203/0475C01B2203/061C01B2203/1058C01B2203/1064C01B2203/107C01B2203/148Y02P30/30C07C31/04
    • 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).
    • 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)。