公开(公告)号：US20150343409A1

公开(公告)日：2015-12-03

申请号：US14655680

申请日：2013-12-27

Applicant: STAMICARBON B.V.

Inventor： Fredericus Henricus Maria BUITINK ,  Luc Louis Maria DIELTJENS

IPC: B01J19/00 ,  B01D3/00

CPC classification number: B01J19/00 ,  B01D3/009 ,  B01J2219/00024 ,  B01J2219/00027 ,  B01J2219/0004 ,  B01J2219/185 ,  C07C273/04 ,  Y10T29/49718

Abstract: Disclosed is a method of increasing the capacity of an existing urea plant. With reference to the regular components of a urea plant, including a synthesis section comprising a high pressure carbamate condenser and a reactor, and a recovery section, the method comprises installing an additional reactor between the recovery section and the high pressure carbamate condenser. The additional reactor is preferably installed in connection with an ejector, so as to allow ground placement of the additional reactor.

Abstract translation: 公开了提高现有尿素装置的能力的方法。 关于尿素装置的常规部件，包括包含高压氨基甲酸酯冷凝器和反应器的合成部分和回收部分，该方法包括在回收部分和高压氨基甲酸铵冷凝器之间安装另外的反应器。 附加的反应器优选地与喷射器结合安装，以允许附加反应器的地面放置。

公开(公告)号：US20150276308A1

公开(公告)日：2015-10-01

申请号：US14432726

申请日：2013-10-01

Applicant: Laura Annamaria PELLEGRINI ,  STAMICARBON B.V. ACTING UNDER THE NAME OF MT INNOVATION CENTER

Inventor： Laura Annamaria Pellegrini

IPC: F25J3/02

CPC classification number: F25J3/0266 ,  C10L3/102 ,  C10L3/103 ,  C10L3/104 ,  F25J3/0209 ,  F25J3/0233 ,  F25J2200/04 ,  F25J2200/08 ,  F25J2200/40 ,  F25J2200/74 ,  F25J2200/78 ,  F25J2210/66 ,  F25J2220/66 ,  F25J2235/60 ,  Y02C10/12

Abstract: The invention relates to a process for the removal of CO2 from acid gas by cryogenic distillation performed in two steps. The feed mixture is first distilled at high pressure (at least 45 bar) in a first distillation column. The top product or a part thereof is then, after heating, subjected to a second distillation step at a lower pressure (lower than 45 bar). The top product of the second distillation step is methane of high purity (more than 99 mol.%). The bottom product of the second distillation step is recycled back to the first distillation column. The method according to the invention allows complete separation of methane also at higher level of acidic components, is economical and does not result in solid CO2 build-up, which is a common problem in cryogenic distillation.

Abstract translation: 本发明涉及通过两步进行的低温蒸馏从酸性气体中除去CO 2的方法。 首先在第一蒸馏塔中高压（至少45巴）蒸馏进料混合物。 然后，顶部产品或其一部分在加热后进行较低压力（低于45巴）的第二蒸馏步骤。 第二蒸馏步骤的顶部产物是高纯度（大于99mol％）的甲烷。 第二蒸馏步骤的底部产物被循环回到第一蒸馏塔。 根据本发明的方法允许在较高水平的酸性组分中完全分离甲烷，是经济的并且不会导致固体CO 2堆积，这是在低温蒸馏中的常见问题。

公开(公告)号：US09108164B2

公开(公告)日：2015-08-18

申请号：US14223897

申请日：2014-03-24

Applicant: STAMICARBON B.V.

Inventor： Jozef Hubert Meessen ,  Axel Erben ,  John Krijgsman ,  Winfried Liebig

IPC: B01D61/46 ,  B01D61/42 ,  B01D53/58 ,  B01D53/73 ,  B01D61/44 ,  C07C273/14 ,  C02F1/469 ,  C02F101/16 ,  C02F103/18

CPC classification number: B01D61/422 ,  B01D53/58 ,  B01D53/73 ,  B01D61/44 ,  B01D61/445 ,  C02F1/4693 ,  C02F2101/16 ,  C02F2103/18 ,  C07C273/14 ,  Y02A50/2346

Abstract: The invention is directed to a process for the removal of ammonia from an ammonia-containing gas stream by treating the ammonia in the ammonia-containing gas stream with an acid, during which treatment an aqueous stream comprising an ammonium salt, wherein the aqueous stream comprising the ammonium salt is treated with electrodialysis, whereby the acid is recovered and an aqueos stream comprising an ammonium hydroxide salt is formed.

Abstract translation: 本发明涉及一种通过用酸处理含氨气体物流中的氨来从含氨气流中除去氨的方法，在此期间处理包含铵盐的水流，其中含水流包含 用电渗析处理铵盐，由此回收酸，形成包含氢氧化铵盐的气流。

公开(公告)号：US20150128595A1

公开(公告)日：2015-05-14

申请号：US14400268

申请日：2013-05-10

Applicant: STAMICARBON B.V. acting under the name of MT INNOVATION CENTER ,  ENEA - CASACCIA RESEARCH CENTRE ,  YEDA RESEARCH AND DEVELOPMENT CO. LTD.

Inventor： Gaetano Iaquaniello ,  Daniela Capoferri ,  Fabrizio Fabrizi ,  Michael Epstein

IPC: F01K13/00 ,  F01K7/16 ,  F03G6/00 ,  F01K3/08

CPC classification number: F01K13/00 ,  F01K3/004 ,  F01K3/08 ,  F01K3/24 ,  F01K7/16 ,  F01K7/22 ,  F03G6/005 ,  F22B1/006 ,  F22B1/028 ,  Y02E10/46 ,  Y02E20/16

Abstract: Method for modifying a solar thermal power plant operating on conventional oil based technology into a hybrid solar thermal power plant, wherein the method comprises: providing an oil based solar thermal power plant comprising a solar collection system with at least one radiation absorber tube containing a heat transfer oil to be heated by means of the solar collection system, providing an molten salts solar thermal power plant, wherein the molten salts solar thermal power plant comprises a solar collection system to heat a molten salts mixture coupling of the respective plants such that the hybrid solar thermal power plant is configured to heat medium temperature steam that is generated by the oil based solar power plant by means of the molten salts mixture thereby producing high temperature steam and subsequently supplying it to a steam turbine to generate electricity.

Abstract translation: 一种用于将以常规油基技术运行的太阳能热电厂修改为混合太阳能热电厂的方法，其中所述方法包括：提供一种油基太阳能热电厂，其包括具有至少一个包含热量的辐射吸收管的太阳能收集系统 通过太阳能收集系统转移待加热的油，提供一种熔盐太阳能热电厂，其中该熔盐太阳能发电厂包括一个太阳能收集系统，用于加热各种植物耦合的熔盐混合物，使混合物 太阳能发电厂被配置为通过熔盐混合物加热由油基太阳能发电厂产生的介质温度的蒸汽，从而产生高温蒸汽，随后将其供应给蒸汽涡轮发电。

公开(公告)号：US20150086440A1

公开(公告)日：2015-03-26

申请号：US14398439

申请日：2013-05-02

Applicant: STAMICARBON B.V.

Inventor： Alexander Aleida Antonius Scheerder

IPC: F28F9/18 ,  F28F19/06 ,  B21D53/08

CPC classification number: F28F9/18 ,  B01J3/04 ,  B01J19/0013 ,  B01J19/006 ,  B01J19/02 ,  B01J19/24 ,  B01J2219/00081 ,  B01J2219/00256 ,  B01J2219/00768 ,  B01J2219/024 ,  B01J2219/0286 ,  B01J2219/182 ,  B01J2219/192 ,  B21D53/08 ,  B23K31/027 ,  B23K2101/14 ,  B23K2103/04 ,  B23K2103/05 ,  B23K2103/18 ,  F28D7/06 ,  F28D2021/0022 ,  F28F9/185 ,  F28F19/06 ,  F28F21/083 ,  Y02P20/142 ,  Y10T29/49373 ,  Y10T29/49968

Abstract: The present application relates to a method of manufacturing a tube sheet (7) and heat exchanger assembly for a pool reactor or pool condenser for use in the production of urea from ammonia and carbon dioxide, wherein the method comprises manufacturing of the tube sheet (7) from a carbon steel material grade and providing said tube sheet (7) with corrosion protective layers (8, 9) of an austenitic- ferritic duplex stainless steel grade, wherein the heat exchanger comprises at least one U-shaped tube (13) of an austenitic-ferritic duplex stainless steel grade, the method further comprises inserting at least two sleeves (11) of an austenitic-ferritic duplex stainless steel grade through the tube sheet (7) such that both ends of the sleeve (11) extend in a direction away from the tube sheet (7), the method further comprises connecting the sleeves (11), at least the opposing ends thereof, to at least the protective layers (8,9) of the tube sheet (7) and finally, connecting both ends of the at least one U-shaped tube (13) to the respective sleeves (11).

Abstract translation: 本申请涉及制造管板（7）和用于从氨和二氧化碳生产尿素的池式反应器或池式冷凝器的热交换器组件的方法，其中该方法包括制造管板（7 ），并且为所述管板（7）提供具有奥氏体 - 铁素体双相不锈钢等级的腐蚀保护层（8,9），其中所述热交换器包括至少一个U形管（13），所述U形管 奥氏体 - 铁素体双相不锈钢级，该方法还包括通过管板（7）插入至少两个奥氏体 - 铁素体双相不锈钢级的套筒（11），使得套筒（11）的两端在 远离管板（7）的方向，该方法还包括至少将套管（11）的相对端部连接到管板（7）的至少保护层（8,9）上，最后连接 的两端 至少一个U形管（13）到相应的套筒（11）。

公开(公告)号：US20150037246A1

公开(公告)日：2015-02-05

申请号：US14384138

申请日：2013-03-11

Applicant: STAMICARBON B.V. ACTING UNDER THE NAME OF MT INNOVATION CENTER

Inventor： Barbara Morico ,  Annarita Salladini ,  Gaetano Iaquaniello

IPC: C01B3/38 ,  C01B3/50 ,  B01J7/00

CPC classification number: C01B3/382 ,  B01J7/00 ,  B01J8/009 ,  B01J8/067 ,  B01J19/02 ,  B01J2208/00212 ,  B01J2219/0004 ,  B01J2219/0286 ,  C01B3/384 ,  C01B3/48 ,  C01B3/501 ,  C01B2203/0233 ,  C01B2203/0283 ,  C01B2203/0405 ,  C01B2203/0833 ,  C01B2203/143 ,  C01B2203/146 ,  C01B2203/82 ,  Y02P20/134

Abstract: Disclosed is a process for the production of hydrogen in a reactor system comprising a steam reforming reaction zone comprising a reforming catalyst and a membrane separation zone comprising a hydrogen-selective membrane. The process involves a reaction system of so-called open architecture, wherein the reforming zone and the membrane separation zone operate independently of each other. The invention provides the heat for the reforming reaction through heat exchange from liquid molten salts, preferably heated by solar energy.

Abstract translation: 公开了一种在反应器系统中生产氢气的方法，其包括包含重整催化剂和包含氢选择性膜的膜分离区的蒸汽重整反应区。 该方法涉及所谓的开放结构的反应体系，其中重整区和膜分离区彼此独立地操作。 本发明通过液体熔融盐的热交换提供热重整反应，优选由太阳能加热。

公开(公告)号：US20150026943A1

公开(公告)日：2015-01-29

申请号：US14127962

申请日：2012-10-12

Applicant: Stamicarbon B.V.

Inventor： Johannes Henricus Mennen

IPC: C07C273/16 ,  B29C43/00

CPC classification number: C07C273/16 ,  B01J2/22 ,  B01J2/30 ,  B29C43/006 ,  B29K2075/02 ,  C05C9/005 ,  C05C9/02 ,  C07C273/14 ,  Y10T29/49716

Abstract: Disclosed is a method for urea finishing. A urea solution is subjected to crystallization and, other than in conventional processes, the urea crystals are shaped by exerting mechanical force onto them. Thus, the conventional prilling or granulation finishing steps can be avoided, and so are the corresponding emissions of ammonia and/or dust. The crystallization comprises a flash crystallization. The invention also pertains to the urea particles obtainable by the process, to a urea plant, and to a method of modifying an existing urea plant.

Abstract translation: 公开了一种尿素整理方法。 尿素溶液进行结晶，除了常规方法之外，尿素晶体通过对其施加机械力而成形。 因此，可以避免常规的造粒或造粒整理步骤，氨和/或粉尘的相应排放也是如此。 结晶包括闪晶结晶。 本发明还涉及通过该方法获得的尿素颗粒，尿素装置以及改进现有尿素装置的方法。

公开(公告)号：US20140364647A1

公开(公告)日：2014-12-11

申请号：US14366950

申请日：2012-12-18

Applicant: STAMICARBON B.V. ACTING UNDER THE NAME OF MT INNOVATION CENTER

Inventor： Gaetano Iaquaniello ,  Barbara Cucchiella ,  Elena Antonetti

IPC: C07C273/10 ,  C01B3/26 ,  C01C1/04

CPC classification number: C07C273/10 ,  C01B3/025 ,  C01B3/26 ,  C01B3/382 ,  C01B3/384 ,  C01B3/386 ,  C01B3/48 ,  C01B2203/0233 ,  C01B2203/0244 ,  C01B2203/0261 ,  C01B2203/0283 ,  C01B2203/04 ,  C01B2203/043 ,  C01B2203/0445 ,  C01B2203/0475 ,  C01B2203/068 ,  C01B2203/1241 ,  C01B2203/141 ,  C01B2203/146 ,  C01C1/04

Abstract: Disclosed is a process for the production of ammonia comprising a step wherein synthesis gas is formed in two different ways, viz. by catalytic partial oxidation (31) and by steam reforming, and wherein the combined streams of synthesis gas are subjected to a water gas shift reaction (50). Also disclosed is a process of producing urea, wherein ammonia is formed (90) in a process involving said combined streams and wherein carbon dioxide (110) formed in the same process is reacted with said ammonia so as to form urea.

Abstract translation: 公开了一种生产氨的方法，包括以两种不同方式形成合成气的步骤，即， 通过催化部分氧化（31）和通过蒸汽重整，并且其中合成气流经受水煤气变换反应（50）。 还公开了一种生产尿素的方法，其中在涉及所述组合料流的方法中形成氨（90），并且其中在相同方法中形成的二氧化碳（110）与氨反应以形成尿素。

公开(公告)号：US20250162983A1

公开(公告)日：2025-05-22

申请号：US18877886

申请日：2024-09-06

Applicant: Stamicarbon B.V.

Inventor： Rahul PATIL ,  Lambertus Wilhelmus GEVERS ,  Chuanbo GAO

IPC: C07C273/16 ,  C05C1/00 ,  C05G5/20

Abstract: The disclosure pertains to a urea production process wherein vapor from an evaporation unit for concentrating urea solution is condensed and the resulting process condensate, which contains urea originating from urea entrained in the vapor, is combined with a second urea solution to obtain a dilute urea solution that is suitable e.g. for DEF.

公开(公告)号：US20250108349A1

公开(公告)日：2025-04-03

申请号：US18850232

申请日：2023-08-29

Applicant: STAMICARBON B.V.

Inventor： Barbara CUCCHIELLA ,  Juan GONZALEZ COLOMA

IPC: B01J2/16 ,  B01J19/26

Abstract: The disclosure pertains to a fluidized bed granulation process, for instance for urea melt. An embodiment of the process comprises providing a fluidized bed of the particles in a granulation compartment of the fluidized bed granulator; forming a film of the granulation liquid in the form of a hollow conical frustum projecting into the granulation compartment by supplying the granulation liquid through a first channel of a granulation nozzle; supplying secondary gas stream through a secondary gas channel of the granulation nozzle into the granulation compartment, wherein the secondary gas channel is provided as an annulus around the first channel, wherein the exit of the secondary gas channel is directly exposed to the fluidized bed in the granulation compartment, wherein particles from the fluidized bed are entrained in said secondary gas stream.