公开(公告)号：US09732033B2

公开(公告)日：2017-08-15

申请号：US15246334

申请日：2016-08-24

Applicant: Stamicarbon B.V.

Inventor： Johannes Henricus Mennen ,  Jozef Hubert Meessen

IPC: C07C273/04 ,  B01D5/00 ,  B01D47/00 ,  B23P15/26 ,  B01J10/00

CPC classification number: C07C273/04 ,  B01D5/006 ,  B01D5/009 ,  B01D47/00 ,  B01J10/00 ,  B23P15/26 ,  Y10T29/49352

Abstract: Disclosed is a plant for the production of urea. The plant comprises conventional sections for synthesis and recovery, for evaporation and condensation, for urea finishing, and for dust scrubbing. According to the invention, an additional evaporation and condensation loop is introduced from and to the dust scrubbing section. This loop results in a more favorable energy consumption of the plant.

公开(公告)号：US20150133690A1

公开(公告)日：2015-05-14

申请号：US14398433

申请日：2013-05-02

Applicant: STAMICARBON B.V.

Inventor： Johannes Henricus Mennen ,  Jozef Hubert Meessen

IPC: C07C273/04 ,  B01D47/00 ,  B23P15/26 ,  B01D5/00

CPC classification number: C07C273/04 ,  B01D5/006 ,  B01D5/009 ,  B01D47/00 ,  B01J10/00 ,  B23P15/26 ,  Y10T29/49352

Abstract: Disclosed is a plant for the production of urea. The plant comprises conventional sections for synthesis and recovery, for evaporation and condensation, for urea finishing, and for dust scrubbing. According to the invention, an additional evaporation and condensation loop is introduced from and to the dust scrubbing section. This loop results in a more favorable energy consumption of the plant.

Abstract translation: 公开了一种用于生产尿素的设备。 该设备包括用于合成和回收的常规部分，用于蒸发和冷凝，用于尿素整理和用于灰尘洗涤。 根据本发明，从灰尘洗涤部分引入附加的蒸发和冷凝环路。 该循环导致植物更有利的能量消耗。

公开(公告)号：US20150119603A1

公开(公告)日：2015-04-30

申请号：US14398425

申请日：2013-05-02

Applicant: STAMICARBON B.V.

Inventor： Johan Albert Arno Van Den Tillaart ,  Jozef Hubert Meessen

IPC: C07C273/04 ,  B01J19/00

CPC classification number: C07C273/04 ,  B01J10/00 ,  B01J19/0013 ,  B01J2219/00051 ,  Y02P20/142

Abstract: Method for the production of urea from ammonia and carbon dioxide in a urea plant containing a high-pressure synthesis section with a horizontal pool condenser, wherein the method comprises exchanging heat from a high pressure process medium received in a shell section of the pool condenser to a medium pressure urea containing solution received in a first heat exchanging section provided in the pool condenser to at least decompose ammonium carbamate into NH3 and CO2, wherein the method further comprises exchanging heat from the high pressure process medium to a low pressure steam condensate received in a second heat exchanging section provided in the pool condenser to produce low pressure steam. The invention also relates to an apparatus for the production of urea from ammonia and carbon dioxide.

Abstract translation: 在含有具有水平冷凝器的高压合成部分的尿素装置中由氨和二氧化碳生产尿素的方法，其中所述方法包括将从所述池冷凝器的壳部分中接收的高压处理介质的热交换到 容纳在所述池冷凝器中的第一热交换部分中的中压含尿素溶液以至少将氨基甲酸铵分解成NH 3和CO 2，其中所述方法还包括将热量从所述高压处理介质交换到低压蒸汽冷凝物 设置在池冷凝器中以产生低压蒸汽的第二热交换部分。 本发明还涉及一种用于从氨和二氧化碳生产尿素的设备。

公开(公告)号：US09505712B2

公开(公告)日：2016-11-29

申请号：US14398425

申请日：2013-05-02

Applicant: STAMICARBON B.V.

Inventor： Johan Albert Arno Van Den Tillaart ,  Jozef Hubert Meessen

IPC: C07C273/04 ,  B01J10/00 ,  B01J19/00

CPC classification number: C07C273/04 ,  B01J10/00 ,  B01J19/0013 ,  B01J2219/00051 ,  Y02P20/142

Abstract: Method for the production of urea from ammonia and carbon dioxide in a urea plant containing a high-pressure synthesis section with a horizontal pool condenser, wherein the method comprises exchanging heat from a high pressure process medium received in a shell section of the pool condenser to a medium pressure urea containing solution received in a first heat exchanging section provided in the pool condenser to at least decompose ammonium carbamate into NH3 and CO2, wherein the method further comprises exchanging heat from the high pressure process medium to a low pressure steam condensate received in a second heat exchanging section provided in the pool condenser to produce low pressure steam. The invention also relates to an apparatus for the production of urea from ammonia and carbon dioxide.

Abstract translation: 在含有具有水平冷凝器的高压合成部分的尿素装置中由氨和二氧化碳生产尿素的方法，其中所述方法包括将从所述池冷凝器的壳部分中接收的高压处理介质的热交换到 容纳在所述池冷凝器中的第一热交换部分中的中压含尿素溶液以至少将氨基甲酸铵分解成NH 3和CO 2，其中所述方法还包括将热量从所述高压处理介质交换到低压蒸汽冷凝物 设置在池冷凝器中以产生低压蒸汽的第二热交换部分。 本发明还涉及一种用于从氨和二氧化碳生产尿素的设备。

公开(公告)号：US09556077B2

公开(公告)日：2017-01-31

申请号：US14098496

申请日：2013-12-05

Applicant: Stamicarbon B.V.

Inventor： Jozef Hubert Meessen ,  Pantelis Orfanidis

IPC: B01D47/00 ,  C05C9/00 ,  C01C1/12 ,  C05C3/00 ,  C07C273/16

CPC classification number: C05C3/00 ,  B01D53/54 ,  B01D53/58 ,  B01D53/80 ,  B01D2251/506 ,  B01D2257/406 ,  B01D2257/70 ,  C01C1/12 ,  C01C1/22 ,  C05C3/005 ,  C05C9/00 ,  C07C273/16

Abstract: The invention relates to a method for recovery of urea dust and ammonia from a gas stream by contacting said gas stream with an aqueous sulphuric acid solution, thus forming an acid solution of ammonium sulphate and urea, characterized in that the acid solution is concentrated to a melt comprising less than 5 wt % of water, which melt is subsequently transferred into solid particles comprising urea and ammonium sulphate.

Abstract translation: 本发明涉及通过使所述气流与硫酸水溶液接触从气流中回收尿素灰尘和氨的方法，从而形成硫酸铵和尿素的酸溶液，其特征在于将酸溶液浓缩至 熔体包含少于5重量％的水，该熔体随后转移到包含尿素和硫酸铵的固体颗粒中。

公开(公告)号：US09458098B2

公开(公告)日：2016-10-04

申请号：US14398433

申请日：2013-05-02

Applicant: STAMICARBON B.V.

Inventor： Johannes Henricus Mennen ,  Jozef Hubert Meessen

IPC: B01D47/00 ,  C07C273/04 ,  B01D5/00 ,  B23P15/26

CPC classification number: C07C273/04 ,  B01D5/006 ,  B01D5/009 ,  B01D47/00 ,  B01J10/00 ,  B23P15/26 ,  Y10T29/49352

Abstract: Disclosed is a plant for the production of urea. The plant comprises conventional sections for synthesis and recovery, for evaporation and condensation, for urea finishing, and for dust scrubbing. According to the invention, an additional evaporation and condensation loop is introduced from and to the dust scrubbing section. This loop results in a more favorable energy consumption of the plant.

Abstract translation: 公开了一种用于生产尿素的设备。 该设备包括用于合成和回收的常规部分，用于蒸发和冷凝，用于尿素整理和用于灰尘洗涤。 根据本发明，从灰尘洗涤部分引入附加的蒸发和冷凝环路。 该循环导致植物更有利的能量消耗。

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。