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公开(公告)号:US20160355399A1
公开(公告)日:2016-12-08
申请号:US15110422
申请日:2014-12-16
CPC分类号: C01B3/16 , B01J8/003 , B01J8/0415 , B01J8/0469 , B01J8/0492 , B01J2208/00672 , B01J2208/00752 , B01J2208/025 , B01J2219/00024 , C01B3/40 , C01B3/586 , C01B2203/0233 , C01B2203/0288 , C01B2203/0445 , C01B2203/047 , C01B2203/1011 , C01B2203/142 , C10K3/04
摘要: A method for loading an axial-radial flow vessel containing a bed of a particulate catalyst having a radial-flow portion and an axial-flow portion supported on and in fluid communication with the radial flow portion, includes: (i) placing a first catalyst material in the radial-flow portion and (ii) placing a second catalyst material in the axial-flow portion, wherein the second catalyst material has a smaller particle size than the first catalyst material. A vessel loaded with first and second catalyst materials is also described.
摘要翻译: 一种用于装载包含颗粒催化剂床的轴向 - 径向流动容器的方法,该颗粒催化剂床具有支撑在径向流动部分上并与其径向流动部分流体连通的径向流动部分和轴向流动部分,包括:(i)将第一催化剂 径向流动部分中的材料和(ii)将第二催化剂材料放置在轴向流动部分中,其中第二催化剂材料具有比第一催化剂材料更小的粒度。 还描述了装载有第一和第二催化剂材料的容器。
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公开(公告)号:US20190031604A1
公开(公告)日:2019-01-31
申请号:US16062748
申请日:2016-11-28
发明人: Ola ERLANDSSON , Andreas Erik Johan MAGNUSSON , Kate MCFARLANE , John David PACH , Daniel Thomas SHELDON , Darren WARD
IPC分类号: C07C273/14 , C07C273/10 , C01C1/04 , C01B3/50 , C07C45/29 , C07C29/151 , C07C1/20
CPC分类号: C07C273/14 , C01B3/50 , C01B2203/0283 , C01B2203/061 , C01B2203/062 , C01B2203/068 , C01C1/0405 , C01C1/0488 , C07C1/20 , C07C29/1516 , C07C29/1518 , C07C45/29 , C07C45/38 , C07C273/04 , C07C273/10 , Y02P20/125
摘要: A process for the production of formaldehyde-stabilised urea is described comprising the steps of: (a) generating a synthesis gas comprising hydrogen, nitrogen, carbon monoxide, carbon dioxide and steam in a synthesis gas generation unit, (b) subjecting the synthesis gas to one or more stages of water-gas shift in one or more water-gas shift reactors to form a shifted gas; (c) recovering carbon dioxide from the shifted gas in a carbon dioxide removal unit to form a carbon dioxide-depleted synthesis gas; (d) synthesising methanol from the carbon dioxide-depleted synthesis gas in a methanol synthesis unit and recovering the methanol and a methanol synthesis off-gas comprising nitrogen, hydrogen and residual carbon monoxide; (e) subjecting at least a portion of the recovered methanol to oxidation with air in a formaldehyde production unit; (f) subjecting the methanol synthesis off-gas to methanation in a methanation reactor containing a methanation catalyst to form an ammonia synthesis gas; (g) synthesising ammonia from the ammonia synthesis gas in an ammonia production unit and recovering the ammonia; (h) reacting a portion of the ammonia and at least a portion of the recovered carbon dioxide stream in a urea production unit to form a urea stream; and (i) stabilising the urea by mixing the urea stream and a stabiliser prepared using formaldehyde recovered from the formaldehyde production unit, wherein a portion of the synthesis gas generated by the synthesis gas generation unit by-passes either the one or more water-gas shift reactors; the carbon dioxide removal unit; or the one or more water-gas shift reactors and the carbon dioxide removal unit.
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公开(公告)号:US20200109108A1
公开(公告)日:2020-04-09
申请号:US16500441
申请日:2018-03-22
发明人: Sam BARKER , Thomas DAVISON , John David PACH
IPC分类号: C07C273/02 , C07C29/151 , C01C1/04 , C07C45/38 , C01B3/34
摘要: A process for the production of formaldehyde-stabilised urea is described comprising the steps of: (a) generating a synthesis gas; (b) subjecting the synthesis gas to one or more stages of water-gas shift in one or more water-gas shift reactors to form a shifted gas; (c) cooling the shifted gas to below the dew point and recovering condensate to form a dried shifted gas; (d) recovering carbon dioxide from the dried shifted gas in a carbon dioxide removal unit to form a carbon dioxide-depleted synthesis gas; (e) synthesising methanol from the carbon dioxide-depleted synthesis gas in a methanol synthesis unit and recovering the methanol and a methanol synthesis off-gas; (f) subjecting at least a portion of the recovered methanol to oxidation with air to form formaldehyde in a stabiliser production unit; (g) subjecting the methanol synthesis off-gas to methanation in a methanation reactor containing a methanation catalyst to form an ammonia synthesis gas; (h) synthesising ammonia from the ammonia synthesis gas in an ammonia production unit and recovering the ammonia; (i) reacting a portion of the ammonia and at least a portion of the recovered carbon dioxide stream in a urea production unit to form a urea stream; and (j) stabilising the urea by mixing the urea stream and a stabiliser prepared using the formaldehyde produced in the stabiliser production unit, wherein the carbon dioxide removal unit operates by means of absorption using a liquid absorbent and comprises an absorbent regeneration unit, wherein the process includes recovering a carbon dioxide-containing gas stream from the absorbent regeneration unit, compressing at least a portion of the recovered carbon dioxide-containing gas stream to form a compressed carbon dioxide-containing gas stream and passing the compressed carbon dioxide-containing gas stream to the methanol synthesis unit.
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公开(公告)号:US20190047852A1
公开(公告)日:2019-02-14
申请号:US16078846
申请日:2017-02-06
摘要: A method is described for revamping an ammonia production facility said ammonia production facility having a front end comprising one or more reformers fed with a hydrocarbon feedstock at a hydrocarbon feed stock feed rate and a high-temperature shift reactor fed with a reformed gas obtained from said one or more reformers and containing a fixed bed of iron-containing water-gas shift catalyst, said front end operating at a first steam- to-carbon ratio and a first pressure drop, said method comprising the steps of (i) replacing the iron-containing water-gas shift catalyst with a low-steam water-gas shift catalyst to form a modified front end, (ii) operating the modified front end at a second steam-to-carbon ratio and a second pressure drop, wherein the second steam-to-carbon ratio is at least 0.2 less than the first steam-to-carbon ratio and the second pressure drop is less than the first pressure drop, and (iii) increasing the hydrocarbon feed stock feed rate to said one or more reformers.
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公开(公告)号:US20180072659A1
公开(公告)日:2018-03-15
申请号:US15552072
申请日:2015-12-18
IPC分类号: C07C273/14 , C01B3/02 , C01C1/04 , C01B3/38 , C01B3/48 , C01B3/52 , C01B3/56 , C07C29/151 , C07C45/29 , C07C45/38 , C07C273/10 , C10J3/82
CPC分类号: C07C273/14 , C01B3/025 , C01B3/382 , C01B3/48 , C01B3/52 , C01B3/56 , C01B2203/0233 , C01B2203/0244 , C01B2203/025 , C01B2203/0283 , C01B2203/0415 , C01B2203/042 , C01B2203/043 , C01B2203/0475 , C01B2203/061 , C01B2203/062 , C01B2203/068 , C01B2203/1241 , C01B2203/1252 , C01B2203/141 , C01B2203/142 , C01B2203/145 , C01B2203/148 , C01C1/0488 , C07C29/1518 , C07C45/29 , C07C45/38 , C07C273/04 , C07C273/10 , C10J3/82 , C10J2300/0916 , C10J2300/093 , C10J2300/0956 , C10J2300/0959 , C10J2300/0976 , C10J2300/1838 , C10J2300/1853 , Y02E50/18 , Y02P20/52 , C07C31/04 , C07C47/04
摘要: A process is described for the production of formaldehyde, comprising (a) subjecting methanol to oxidation with air in a formaldehyde production unit thereby producing a formaldehyde-containing stream; (b) separating said formaldehyde-containing stream into a formaldehyde product stream and a formaldehyde vent gas stream; wherein the vent gas stream, optionally after treatment in a vent gas treatment unit, is passed to one or more stages of: (i) synthesis gas generation, (ii) carbon dioxide removal, (iii) methanol synthesis or (iv) urea synthesis.
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公开(公告)号:US20190263753A1
公开(公告)日:2019-08-29
申请号:US16344610
申请日:2017-10-03
发明人: Thomas DAVISON , John David PACH
IPC分类号: C07C273/02 , C07C273/04 , C07C273/16 , C07C31/04 , C07C29/151 , C01C1/04 , C01B3/02
摘要: An integrated process for the production of a formaldehyde-stabilised urea is described comprising the steps of: (a) generating a synthesis gas comprising hydrogen, nitrogen, carbon monoxide, carbon dioxide and steam in a synthesis gas generation unit; (b) dividing the synthesis gas into a first synthesis gas stream and a smaller second synthesis gas stream; (c) subjecting the first synthesis gas stream to one or more stages of water-gas shift in one or more water-gas shift reactors to form a shifted gas; (d) cooling the shifted gas to below the dew point and recovering condensate to form a dried shifted gas; (e) recovering carbon dioxide from the dried shifted gas in a carbon dioxide removal unit to form a carbon dioxide-depleted synthesis gas; (f) subjecting the carbon dioxide-depleted synthesis gas to a stage of methanation in one or more methanation reactors to form an ammonia synthesis gas; (g) synthesising ammonia from the ammonia synthesis gas in an ammonia production unit and recovering the ammonia; (h) reacting a portion of the ammonia and at least a portion of the recovered carbon dioxide stream in a urea production unit to form a urea stream; and (i) stabilising the urea by mixing the urea stream and a stabiliser prepared using formaldehyde to form a stabilised urea, wherein the formaldehyde is generated by steps comprising; (1) passing the second portion of synthesis gas through a scrubber to remove contaminants therefrom and form a scrubbed synthesis gas; (2) synthesising methanol from the scrubbed synthesis gas in a methanol synthesis unit, and recovering the methanol and a methanol synthesis off-gas; (3) combining the methanol synthesis off-gas with the shifted gas and (4) subjecting at least a portion of the recovered methanol to oxidation with air in a formaldehyde stabiliser production unit to produce formaldehyde.
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公开(公告)号:US20180072658A1
公开(公告)日:2018-03-15
申请号:US15552063
申请日:2015-12-18
IPC分类号: C07C273/14 , C01B3/02 , C01B3/48 , C01B3/52 , C01B3/56 , C01C1/04 , C07C273/10 , C07C45/38 , C07C45/29 , C10J3/82 , C07C29/151
CPC分类号: C07C273/14 , C01B3/025 , C01B3/382 , C01B3/48 , C01B3/52 , C01B3/54 , C01B3/56 , C01B3/586 , C01B2203/0233 , C01B2203/0244 , C01B2203/0283 , C01B2203/0415 , C01B2203/042 , C01B2203/0445 , C01B2203/047 , C01B2203/0475 , C01B2203/06 , C01B2203/061 , C01B2203/062 , C01B2203/068 , C01B2203/1241 , C01B2203/1252 , C01B2203/142 , C01C1/0488 , C07C29/1518 , C07C45/29 , C07C45/38 , C07C273/04 , C07C273/10 , C10J3/82 , C10J2300/0916 , C10J2300/093 , C10J2300/0956 , C10J2300/0976 , C10J2300/1838 , C10J2300/1853 , Y02P20/125 , Y02P20/52 , C07C31/04 , C07C47/04
摘要: A process for the production of formaldehyde-stabilised urea is described comprising the steps of: (a) generating a synthesis gas comprising hydrogen, nitrogen, carbon monoxide, carbon dioxide and steam in a synthesis gas generation unit; (b) recovering carbon dioxide from the synthesis gas to form a carbon dioxide-depleted synthesis gas; (c) synthesising methanol from the carbon dioxide-depleted synthesis gas in a methanol synthesis unit and recovering the methanol and a methanol synthesis off-gas comprising nitrogen, hydrogen and residual carbon monoxide; (d) subjecting at least a portion of the recovered methanol to oxidation with air in a formaldehyde production unit; (e) subjecting the methanol synthesis off-gas to methanation in a methanation reactor containing a methanation catalyst to form an ammonia synthesis gas; (f) synthesising ammonia from the ammonia synthesis gas in an ammonia production unit and recovering the ammonia; (g) reacting a portion of the ammonia and at least a portion of the recovered carbon dioxide stream in a urea production unit to form a urea stream; and (h) stabilising the urea by mixing the urea stream and a stabiliser prepared using formaldehyde recovered from the formaldehyde production unit, wherein a source of air is compressed and divided into first and second portions, the first portion is provided to the formaldehyde production unit for the oxidation of methanol and the second portion is further compressed and provided to the synthesis gas generation unit.
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公开(公告)号:US20180002185A1
公开(公告)日:2018-01-04
申请号:US15541406
申请日:2016-01-11
发明人: John David PACH , Daniel SHELDON , David WAILS
CPC分类号: C01C1/0488 , B01J23/56 , B01J23/8906 , B01J23/8953 , C01B3/025 , C01B2203/0233 , C01B2203/0244 , C01B2203/025 , C01B2203/0283 , C01B2203/044 , C01B2203/047 , C01B2203/0475 , C01B2203/048 , C01B2203/068 , C01B2203/1058 , C01B2203/1076 , C01C1/0411 , Y02C10/06 , Y02C10/08 , Y02P20/52
摘要: A process for production of ammonia includes: providing a reaction stream including carbon monoxide and hydrogen; passing the reaction stream and steam over a water gas shift catalyst in a catalytic shift reactor, forming a shifted gas mixture depleted in carbon monoxide and enriched in hydrogen; passing the shifted gas mixture with an oxygen-containing gas over a selective oxidation catalyst at ≧175° C., forming a selectively oxidized gas stream with a portion of the carbon monoxide converted to carbon dioxide; removing some of the carbon dioxide from the selectively oxidized gas stream in a carbon dioxide removal unit; passing the carbon dioxide depleted stream over a methanation catalyst in a methanator to form a methanated gas stream, optionally adjusting its hydrogen:nitrogen molar ratio to form an ammonia synthesis gas; and passing the ammonia synthesis gas over an ammonia synthesis catalyst in an ammonia converter to form ammonia.
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