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公开(公告)号:US08419828B2
公开(公告)日:2013-04-16
申请号:US12811793
申请日:2009-01-07
申请人: Zaida Diaz , Henricus Abraham Geers , Ewout Martijn Van Jarwaarde , Arian Nijmeijer , Eric Johannes Puik
发明人: Zaida Diaz , Henricus Abraham Geers , Ewout Martijn Van Jarwaarde , Arian Nijmeijer , Eric Johannes Puik
IPC分类号: B01D53/22
CPC分类号: B01D53/225 , B01D53/228 , B01D2256/24 , B01D2257/304 , B01D2257/306 , B01D2257/308 , B01D2257/504 , B01D2317/022 , C10L3/10 , C10L3/102 , C10L3/12 , Y02C10/10
摘要: The invention concerns a process for the removal of gaseous acidic contaminants, especially carbon dioxide and/or hydrogen sulphide, in two or more stages from a gaseous hydrocarbonaceous feedstream (1) comprising hydrocarbons and said acidic contaminants, using one or more membranes in each separation stages. The gaseous hydrocarbonaceous feedstream is especially a natural gas stream. The process is especially suitable for feedstreams comprising very high amounts of acidic contaminants, especially carbon dioxide, e.g. more than 25 vol. %, or even more than 45 vol. %. In a first stage (2) a pure or almost pure stream of acidic contaminants is separated from the feedstream, the acidic contaminants (4) stream suitably containing less than 5 vol % of hydrocarbons. The remaining stream (3) comprises the hydrocarbons and still a certain amount of gaseous acidic contaminants. In a second stage (5) a pure or almost pure stream of hydrocarbons (8) is separated from the remaining stream, where after the then remaining stream (6) is combined with the feed for the first stage (1), the hydrocarbon stream suitably containing less than 5 vol % of acidic contaminants.
摘要翻译: 本发明涉及一种从包含烃和所述酸性污染物的气态烃类进料流(1)在两个或多个阶段中除去气态酸性污染物,特别是二氧化碳和/或硫化氢的方法,其中在每个分离中使用一个或多个膜 阶段 气态烃类进料流特别是天然气流。 该方法特别适合于包含非常高量的酸性污染物,特别是二氧化碳的进料流,例如二氧化碳。 超过25卷 %,甚至超过45体积。 %。 在第一阶段(2),纯净或几乎纯净的酸性污染物流与进料流分离,酸性污染物(4)流适当地含有少于5体积%的烃。 剩余的流(3)包含烃和仍然一定量的气态酸性污染物。 在第二阶段(5)中,将纯的或几乎纯的烃类物流(8)与剩余物流分离,其中当然后的剩余物流(6)与第一级(1)的进料相结合时,烃流 适当地含有少于5体积%的酸性污染物。
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公开(公告)号:US07931731B2
公开(公告)日:2011-04-26
申请号:US12544800
申请日:2009-08-20
申请人: Gijsbert Jan Van Heeringen , Ewout Martijn Van Jarwaarde , Hendrik Jan Van Der Ploeg , Cornelis Jacobus Smit
发明人: Gijsbert Jan Van Heeringen , Ewout Martijn Van Jarwaarde , Hendrik Jan Van Der Ploeg , Cornelis Jacobus Smit
CPC分类号: C21B13/0073 , B01D53/229 , B01D53/75 , B01D53/77 , B01D2255/20707 , B01D2256/16 , B01D2257/304 , B01D2257/308 , B01D2257/408 , B01D2257/502 , B01D2257/504 , C01B3/36 , C01B2203/025 , C01B2203/04 , C01B2203/0405 , C01B2203/0415 , C01B2203/047 , C01B2203/0475 , C01B2203/0485 , C01B2203/049 , C01B2203/0877 , C01B2203/0883 , C01B2203/0894 , C01B2203/1211 , C01B2203/1252 , C01B2203/147 , C01B2203/86 , C10J2300/0916 , C10J2300/0936 , C10J2300/0943 , C10J2300/0959 , C10J2300/0969 , C10J2300/0973 , C10J2300/1678 , C10K1/08 , C21B2100/282 , C21B2100/42 , C21B2100/64 , Y02C10/10 , Y02P10/122 , Y02P10/128 , Y02P10/136 , Y02P20/152 , Y02P30/30
摘要: A process to prepare elemental iron by contacting an iron ore feed with a reducing gas at a pressure of between 1 and 10 bar to obtain iron and an off-gas includes preparing the reducing gas by performing the following steps: (a) partially oxidizing a mixture comprising a solid or liquid carbonaceous fuel and oxygen at a pressure of between 10 and 80 bar, thereby obtaining a gas comprising H2 and CO; (b) removing CO2 and H2S from the gas obtained in step (a) to obtain an intermediate gas comprising H2 and CO; (c) supplying the intermediate gas obtained in step (b) to a H2-selective membrane to obtain a H2-rich permeate gas and a CO-rich retentate; and (d) heating H2-rich permeate to obtain a heated H2-rich permeate as the reducing gas.
摘要翻译: 通过使铁矿石原料与1〜10巴压力的还原气体接触来制备元素铁,得到铁和废气的方法包括通过以下步骤制备还原气体:(a)将 混合物包含固体或液体含碳燃料和压力为10至80巴的氧气,从而获得包含H 2和CO的气体; (b)从步骤(a)获得的气体中除去CO 2和H 2 S,得到包含H 2和CO的中间气体; (c)将步骤(b)中获得的中间气体供应到H 2选择性膜,以获得富H2的渗透气体和富CO的滞留物; 和(d)加热富H2的渗透物,以获得加热的富H 2的渗透物作为还原气体。
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公开(公告)号:US20110041687A1
公开(公告)日:2011-02-24
申请号:US12811793
申请日:2009-01-07
申请人: Zaida Diaz , Henricus Abraham Geers , Ewout Martijn Van Jarwaarde , Arian Nijmeijer , Eric Johannes Puik
发明人: Zaida Diaz , Henricus Abraham Geers , Ewout Martijn Van Jarwaarde , Arian Nijmeijer , Eric Johannes Puik
CPC分类号: B01D53/225 , B01D53/228 , B01D2256/24 , B01D2257/304 , B01D2257/306 , B01D2257/308 , B01D2257/504 , B01D2317/022 , C10L3/10 , C10L3/102 , C10L3/12 , Y02C10/10
摘要: The invention concerns a process for the removal of gaseous acidic contaminants, especially carbon dioxide and/or hydrogen sulphide, in two or more stages from a gaseous hydrocarbonaceous feedstream (1) comprising hydrocarbons and said acidic contaminants, using one or more membranes in each separation stages. The gaseous hydrocarbonaceous feedstream is especially a natural gas stream. The process is especially suitable for feedstreams comprising very high amounts of acidic contaminants, especially carbon dioxide, e.g. more than 25 vol. %, or even more than 45 vol. %. In a first stage (2) a pure or almost pure stream of acidic contaminants is separated from the feedstream, the acidic contaminants (4) stream suitably containing less than 5 vol % of hydrocarbons. The remaining stream (3) comprises the hydrocarbons and still a certain amount of gaseous acidic contaminants. In a second stage (5) a pure or almost pure stream of hydrocarbons (8) is separated from the remaining stream, where after the then remaining stream (6) is combined with the feed for the first stage (1), the hydrocarbon stream suitably containing less than 5 vol % of acidic contaminants.
摘要翻译: 本发明涉及一种从包含烃和所述酸性污染物的气态烃类进料流(1)在两个或多个阶段中除去气态酸性污染物,特别是二氧化碳和/或硫化氢的方法,其中在每个分离中使用一个或多个膜 阶段 气态烃类进料流特别是天然气流。 该方法特别适合于包含非常高量的酸性污染物,特别是二氧化碳的进料流,例如二氧化碳。 超过25卷 %,甚至超过45体积。 %。 在第一阶段(2),纯净或几乎纯净的酸性污染物流与进料流分离,酸性污染物(4)流适当地含有少于5体积%的烃。 剩余的流(3)包含烃和仍然一定量的气态酸性污染物。 在第二阶段(5)中,将纯的或几乎纯的烃类物流(8)与剩余物流分离,其中当然后的剩余物流(6)与第一级(1)的进料相结合时,烃流 适当地含有少于5体积%的酸性污染物。
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公开(公告)号:US20110009684A1
公开(公告)日:2011-01-13
申请号:US12811791
申请日:2009-01-07
申请人: Zaida Diaz , Henricus Abraham Geers , Ewout Martijn Van Jarwaarde , Arian Nijmeijer , Eric Johannes Puik
发明人: Zaida Diaz , Henricus Abraham Geers , Ewout Martijn Van Jarwaarde , Arian Nijmeijer , Eric Johannes Puik
IPC分类号: C07C7/144
CPC分类号: B01D53/225 , B01D2256/24 , B01D2257/304 , B01D2257/306 , B01D2257/308 , B01D2257/504 , B01D2317/022 , B01D2317/025 , C10L3/10 , C10L3/102 , C10L3/12 , Y02C10/10
摘要: The invention concerns a process for the removal of gaseous acidic contaminants, especially carbon dioxide and/or hydrogen sulphide, in two or more stages from a gaseous hydrocarbonaceous feedstream (1) comprising hydrocarbons and said acidic contaminants, using one or more membranes in each separation stages. The gaseous hydrocarbonaceous feedstream is especially a natural gas stream. The process is especially suitable for feedstreams comprising high amounts of acidic contaminants, e.g. between 10 and 95 vol. % of carbon dioxide and/or hydrogen sulphide, especially between 15 and 70 vol. %. In a first stage (2) a clean or almost clean hydrocarbon stream (3) is separated from the feedstream, the hydrocarbon stream suitably containing less than 5 vol % of acidic contaminants. The remaining stream (4) comprises the acidic contaminants and a certain amount of hydrocarbons. In a second stage (6) a pure or almost pure stream of acidic contaminants (8) is separated from the remaining stream (7), where after the then remaining stream is combined with the feed for the first stage (1), the acidic contaminants stream suitably containing less than 5 vol % of hydrocarbons.
摘要翻译: 本发明涉及一种从包含烃和所述酸性污染物的气态烃类进料流(1)在两个或多个阶段中除去气态酸性污染物,特别是二氧化碳和/或硫化氢的方法,其中在每个分离中使用一个或多个膜 阶段 气态烃类进料流特别是天然气流。 该方法特别适用于包含大量酸性污染物的进料流,例如 10至95体积 二氧化碳和/或硫化氢的百分比,特别是15至70体积%。 %。 在第一阶段(2),清洁或几乎清洁的烃流(3)与进料流分离,烃流合适地含有小于5体积%的酸性污染物。 剩余的流(4)包含酸性污染物和一定量的烃。 在第二阶段(6)中,将纯的或几乎纯净的酸性污染物流(8)与剩余的流(7)分离,其中在剩余的流与第一阶段(1)的进料结合后,酸性 适当地含有少于5体积%的烃的污染物流。
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公开(公告)号:US20100050812A1
公开(公告)日:2010-03-04
申请号:US12544800
申请日:2009-08-20
申请人: Gijsbert Jan Van Heeringen , Ewout Martijn Van Jarwaarde , Hendrik Jan Van Der Ploeg , Cornelis Jacobus Smit
发明人: Gijsbert Jan Van Heeringen , Ewout Martijn Van Jarwaarde , Hendrik Jan Van Der Ploeg , Cornelis Jacobus Smit
CPC分类号: C21B13/0073 , B01D53/229 , B01D53/75 , B01D53/77 , B01D2255/20707 , B01D2256/16 , B01D2257/304 , B01D2257/308 , B01D2257/408 , B01D2257/502 , B01D2257/504 , C01B3/36 , C01B2203/025 , C01B2203/04 , C01B2203/0405 , C01B2203/0415 , C01B2203/047 , C01B2203/0475 , C01B2203/0485 , C01B2203/049 , C01B2203/0877 , C01B2203/0883 , C01B2203/0894 , C01B2203/1211 , C01B2203/1252 , C01B2203/147 , C01B2203/86 , C10J2300/0916 , C10J2300/0936 , C10J2300/0943 , C10J2300/0959 , C10J2300/0969 , C10J2300/0973 , C10J2300/1678 , C10K1/08 , C21B2100/282 , C21B2100/42 , C21B2100/64 , Y02C10/10 , Y02P10/122 , Y02P10/128 , Y02P10/136 , Y02P20/152 , Y02P30/30
摘要: A process to prepare elemental iron by contacting an iron ore feed with a reducing gas at a pressure of between 1 and 10 bar to obtain iron and an off-gas includes preparing the reducing gas by performing the following steps: (a) partially oxidizing a mixture comprising a solid or liquid carbonaceous fuel and oxygen at a pressure of between 10 and 80 bar, thereby obtaining a gas comprising H2 and CO; (b) removing CO2 and H2S from the gas obtained in step (a) to obtain an intermediate gas comprising H2 and CO; (c) supplying the intermediate gas obtained in step (b) to a H2-selective membrane to obtain a H2-rich permeate gas and a CO-rich retentate; and (d) heating H2-rich permeate to obtain a heated H2-rich permeate as the reducing gas.
摘要翻译: 通过使铁矿石原料与1〜10巴压力的还原气体接触来制备元素铁,得到铁和废气的方法包括通过以下步骤制备还原气体:(a)将 混合物包含固体或液体含碳燃料和压力为10至80巴的氧气,从而获得包含H 2和CO的气体; (b)从步骤(a)获得的气体中除去CO 2和H 2 S,得到包含H 2和CO的中间气体; (c)将步骤(b)中获得的中间气体供应到H 2选择性膜,以获得富H2的渗透气体和富CO的滞留物; 和(d)加热富H2的渗透物,以获得加热的富H 2的渗透物作为还原气体。
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