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公开(公告)号：US09637426B2
公开(公告)日：2017-05-02
申请号：US14524278
申请日：2014-10-27
Applicant: UOP LLC
Inventor： Robert Edison Tsai , Xin X. Zhu , Tokhanh Ngo , William Yanez , Lisa Lane
CPC classification number: C07C7/005 , B01D53/002 , B01D2256/16 , B01D2256/24 , B01D2257/7022 , C01B3/52 , C01B2203/0233 , C01B2203/048 , C01B2203/0495 , C01B2203/0872 , C01B2203/1235 , C01B2203/1247
Abstract: Embodiments of apparatuses and methods for reforming of hydrocarbons including recovery of products are provided. In one example, a method comprises separating a reforming-zone effluent to form a net gas phase stream and a liquid phase hydrocarbon stream. The net gas phase stream is compressed, partially condensed and cooled to form a partially condensed, compressed net gas phase stream. The partially condensed, compressed net gas phase stream is separated to form an intermediate gas phase stream. The intermediate gas phase stream and the liquid phase hydrocarbon stream are combined to form a two-phase combined stream. The two-phase combined stream is cooled and separated to form an H2-rich stream and a cooled second intermediate liquid phase hydrocarbon stream that is enriched with C3/C4 hydrocarbons and further comprises C5+ hydrocarbons.
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公开(公告)号：US09816753B2
公开(公告)日：2017-11-14
申请号：US15587243
申请日：2017-05-04
Applicant: UOP LLC
Inventor： Robert Edison Tsai , Xin X. Zhu , Tokhanh Ngo , William Yanez , Bryan K. Glover
CPC classification number: F25J3/0242 , C01B3/34 , C01B3/52 , C01B2203/0227 , C01B2203/0415 , C01B2203/048 , C01B2203/1247 , C07C7/005 , F25J3/0247 , F25J3/0252 , F25J2200/08 , F25J2205/02 , F25J2215/10 , F25J2215/62 , F25J2230/08 , F25J2230/60 , F25J2245/02 , F25J2270/90
Abstract: Embodiments of apparatuses and methods for reforming of hydrocarbons including recovery of products are provided. In one example, a method comprises separating a reforming-zone effluent to form a net gas phase stream and a liquid phase hydrocarbon stream. The net gas phase stream is compressed, partially condensed and cooled to form a partially condensed, compressed net gas phase stream. The partially condensed, compressed net gas phase stream is separated to form an intermediate gas phase stream. The intermediate gas phase stream is cooled to form a cooled intermediate gas phase stream. The liquid phase hydrocarbon stream is cooled to form a cooled liquid phase hydrocarbon stream. The cooled intermediate gas phase stream is contacted with the cooled liquid phase hydrocarbon stream to form an H2-rich stream and a cooled second intermediate liquid phase hydrocarbon stream that is enriched with C3/C4 hydrocarbons.
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公开(公告)号：US09663423B2
公开(公告)日：2017-05-30
申请号：US14524309
申请日：2014-10-27
Applicant: UOP LLC
Inventor： Bryan K. Glover , Robert Edison Tsai , Xin X. Zhu , William Yanez
CPC classification number: C07C7/005 , B01D53/002 , B01D53/047 , B01D53/1487 , B01D53/1493 , B01D53/261 , B01D2252/20 , B01D2252/205 , B01D2253/102 , B01D2253/104 , B01D2253/106 , B01D2253/108 , B01D2256/16 , B01D2256/24 , B01D2257/702 , B01D2257/7022 , B01D2257/7027 , B01D2259/4146 , C01B3/34 , C01B3/56 , C01B2203/0227 , C01B2203/043 , C01B2203/048
Abstract: Embodiments of apparatuses and methods for reforming of hydrocarbons including recovery of products are provided. In one example, a method comprises separating a reforming-zone effluent to form a net gas phase stream and a liquid phase hydrocarbon stream. The net gas phase stream is compressed, partially condensed and cooled, and separated to form an intermediate gas phase stream. The intermediate gas phase stream is cooled to form a cooled intermediate gas phase stream. The liquid phase hydrocarbon stream is cooled to form a cooled liquid phase hydrocarbon stream. The cooled intermediate gas phase stream is contacted with the cooled liquid phase hydrocarbon stream to form an H2-rich stream and a cooled second intermediate liquid phase hydrocarbon stream that is enriched with C3/C4 hydrocarbons. The H2-rich stream is contacted with an adsorbent to form an H2-ultra rich stream.
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4.发明申请METHODS AND APPARATUSES FOR REFORMING OF HYDROCARBONS INCLUDING RECOVERY OF PRODUCTS USING AN ABSORPTION ZONE AND A PRESSURE SWING ADSORPTION ZONE 有权用于改造碳氢化合物的方法和装置，包括使用吸收区和压力旋转吸收区恢复产物公开(公告)号：US20160115100A1
公开(公告)日：2016-04-28
申请号：US14524309
申请日：2014-10-27
Applicant: UOP LLC
Inventor： Bryan K. Glover , Robert Edison Tsai , Xin X. Zhu , William Yanez
IPC: C07C7/00 , B01D53/047 , B01D53/14 , C01B3/56
CPC classification number: C07C7/005 , B01D53/002 , B01D53/047 , B01D53/1487 , B01D53/1493 , B01D53/261 , B01D2252/20 , B01D2252/205 , B01D2253/102 , B01D2253/104 , B01D2253/106 , B01D2253/108 , B01D2256/16 , B01D2256/24 , B01D2257/702 , B01D2257/7022 , B01D2257/7027 , B01D2259/4146 , C01B3/34 , C01B3/56 , C01B2203/0227 , C01B2203/043 , C01B2203/048
Abstract: Embodiments of apparatuses and methods for reforming of hydrocarbons including recovery of products are provided. In one example, a method comprises separating a reforming-zone effluent to form a net gas phase stream and a liquid phase hydrocarbon stream. The net gas phase stream is compressed, partially condensed and cooled, and separated to form an intermediate gas phase stream. The intermediate gas phase stream is cooled to form a cooled intermediate gas phase stream. The liquid phase hydrocarbon stream is cooled to form a cooled liquid phase hydrocarbon stream. The cooled intermediate gas phase stream is contacted with the cooled liquid phase hydrocarbon stream to form an H2-rich stream and a cooled second intermediate liquid phase hydrocarbon stream that is enriched with C3/C4 hydrocarbons. The H2-rich stream is contacted with an adsorbent to form an H2-ultra rich stream.
Abstract translation: 提供了包括产物回收的烃类重整装置和方法的实施例。 在一个实例中，一种方法包括分离重整区流出物以形成净气相物流和液相烃流。 净气相流被压缩，部分冷凝和冷却，并分离以形成中间气相物流。 中间气相物流被冷却以形成冷却的中间气相物流。 将液相烃流冷却以形成冷却的液相烃流。 冷却的中间气相物流与冷却的液相烃物流接触以形成富H2的物流和富含C3 / C4烃的冷却的第二中间液相烃物流。 富H2流与吸附剂接触以形成富H2流。
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5.发明申请公开(公告)号：US20170234613A1
公开(公告)日：2017-08-17
申请号：US15587243
申请日：2017-05-04
Applicant: UOP LLC
Inventor： Robert Edison Tsai , Xin X. Zhu , Tokhanh Ngo , William Yanez , Bryan K. Glover
CPC classification number: F25J3/0242 , C01B3/34 , C01B3/52 , C01B2203/0227 , C01B2203/0415 , C01B2203/048 , C01B2203/1247 , C07C7/005 , F25J3/0247 , F25J3/0252 , F25J2200/08 , F25J2205/02 , F25J2215/10 , F25J2215/62 , F25J2230/08 , F25J2230/60 , F25J2245/02 , F25J2270/90
Abstract: Embodiments of apparatuses and methods for reforming of hydrocarbons including recovery of products are provided. In one example, a method comprises separating a reforming-zone effluent to form a net gas phase stream and a liquid phase hydrocarbon stream. The net gas phase stream is compressed, partially condensed and cooled to form a partially condensed, compressed net gas phase stream. The partially condensed, compressed net gas phase stream is separated to form an intermediate gas phase stream. The intermediate gas phase stream is cooled to form a cooled intermediate gas phase stream. The liquid phase hydrocarbon stream is cooled to form a cooled liquid phase hydrocarbon stream. The cooled intermediate gas phase stream is contacted with the cooled liquid phase hydrocarbon stream to form an H2-rich stream and a cooled second intermediate liquid phase hydrocarbon stream that is enriched with C3/C4 hydrocarbons.
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Patent Agency Ranking
6.发明授权公开(公告)号：US09399607B2
公开(公告)日：2016-07-26
申请号：US14524301
申请日：2014-10-27
Applicant: UOP LLC
Inventor： Robert Edison Tsai , Xin X. Zhu , Bryan K. Glover , Eleftherios Adamopoulos , William Yanez
CPC classification number: C07C7/005 , B01D53/002 , B01D53/047 , B01D53/229 , B01D53/261 , B01D2053/221 , B01D2253/102 , B01D2253/104 , B01D2253/106 , B01D2253/108 , B01D2256/16 , B01D2256/24 , B01D2257/102 , B01D2257/108 , B01D2257/502 , B01D2257/7022 , B01D2257/7027 , B01D2257/80 , B01D2259/4146 , C01B3/34 , C01B3/501 , C01B3/56 , C01B2203/0405 , C01B2203/042 , C01B2203/043 , C01B2203/048 , C01B2203/1247 , C07C7/12 , C07C7/144 , C10L3/12 , C10L2290/542 , C10L2290/548
Abstract: Embodiments of apparatuses and methods for reforming of hydrocarbons including recovery of products are provided. In one example, a method comprises separating a reforming-zone effluent into a net gas phase stream and a liquid phase hydrocarbon stream. The net gas phase stream is separated for forming an H2-rich stream and a first intermediate liquid phase hydrocarbon stream. The H2-rich stream is contacted with an adsorbent to form an H2-ultra rich stream and a PSA tail gas stream. The PSA tail gas stream is contacted with an H2/hydrocarbon separation membrane to separate the PSA tail gas stream and form an H2-ultra rich permeate stream and a PSA tail gas hydrocarbon-containing non-permeate residue stream.
Abstract translation: 提供了包括产物回收的烃类重整装置和方法的实施例。 在一个实例中，一种方法包括将重整区流出物分离成净气相流和液相烃流。 净气相流被分离以形成富H 2流和第一中间液相烃流。 富H2流与吸附剂接触以形成富H2流和PSA尾气流。 PSA尾气流与H2 /烃分离膜接触以分离PSA尾气流并形成富H2的富含渗透物流和含PSA尾气烃的非渗透物残留物流。
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7.发明申请公开(公告)号：US20160115024A1
公开(公告)日：2016-04-28
申请号：US14524291
申请日：2014-10-27
Applicant: UOP LLC
Inventor： Robert Edison Tsai , Xin X. Zhu , Tokhanh Ngo , William Yanez , Bryan K. Glover
IPC: C01B3/56 , B01D53/14 , B01D53/047 , C07C7/12 , C10L3/12
CPC classification number: C01B3/56 , B01D53/04 , B01D53/047 , B01D53/1437 , B01D53/1487 , B01D53/1493 , B01D53/261 , B01D2256/16 , B01D2257/108 , B01D2257/702 , B01D2257/7022 , C01B2203/0227 , C01B2203/043 , C01B2203/048 , C01B2203/1247 , C01B2203/141 , C01B2203/143 , C01B2203/148 , C07C7/12
Abstract: Embodiments of apparatuses and methods for reforming of hydrocarbons including recovery of products are provided. In one example, a method comprises separating a reforming-zone effluent into a net gas phase stream and a liquid phase hydrocarbon stream. The net gas phase stream is separated for forming an H2-rich stream and a first intermediate liquid phase hydrocarbon stream. The H2-rich stream is contacted with an adsorbent to form an H2-ultra rich stream and a PSA tail gas stream. The PSA tail gas stream and at least a portion of the liquid phase hydrocarbon stream are cooled and contacted with each other to form a H2, C2− hydrocarbons-containing gas stream and a cooled second intermediate liquid phase hydrocarbon stream.
Abstract translation: 提供了包括产物回收的烃类重整装置和方法的实施例。 在一个实例中，一种方法包括将重整区流出物分离成净气相流和液相烃流。 净气相流被分离以形成富H 2流和第一中间液相烃流。 富H2流与吸附剂接触以形成富H2流和PSA尾气流。 PSA尾气流和至少一部分液相烃流被冷却并彼此接触以形成含H2，C2-烃的气流和冷却的第二中间液相烃流。
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公开(公告)号：US09670114B2
公开(公告)日：2017-06-06
申请号：US14524285
申请日：2014-10-27
Applicant: UOP LLC
Inventor： Robert Edison Tsai , Xin X Zhu , Tokhanh Ngo , William Yanez , Bryan K. Glover
CPC classification number: F25J3/0242 , C01B3/34 , C01B3/52 , C01B2203/0227 , C01B2203/0415 , C01B2203/048 , C01B2203/1247 , C07C7/005 , F25J3/0247 , F25J3/0252 , F25J2200/08 , F25J2205/02 , F25J2215/10 , F25J2215/62 , F25J2230/08 , F25J2230/60 , F25J2245/02 , F25J2270/90
Abstract: Embodiments of apparatuses and methods for reforming of hydrocarbons including recovery of products are provided. In one example, a method comprises separating a reforming-zone effluent to form a net gas phase stream and a liquid phase hydrocarbon stream. The net gas phase stream is compressed, partially condensed and cooled to form a partially condensed, compressed net gas phase stream. The partially condensed, compressed net gas phase stream is separated to form an intermediate gas phase stream. The intermediate gas phase stream is cooled to form a cooled intermediate gas phase stream. The liquid phase hydrocarbon stream is cooled to form a cooled liquid phase hydrocarbon stream. The cooled intermediate gas phase stream is contacted with the cooled liquid phase hydrocarbon stream to form an H2-rich stream and a cooled second intermediate liquid phase hydrocarbon stream that is enriched with C3/C4 hydrocarbons.
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9.发明授权公开(公告)号：US09327973B1
公开(公告)日：2016-05-03
申请号：US14524291
申请日：2014-10-27
Applicant: UOP LLC
Inventor： Robert Edison Tsai , Xin X. Zhu , Tokhanh Ngo , William Yanez , Bryan K. Glover
IPC: B01D53/047 , C01B3/56 , C07C7/12 , C10L3/12 , B01D53/14
CPC classification number: C01B3/56 , B01D53/04 , B01D53/047 , B01D53/1437 , B01D53/1487 , B01D53/1493 , B01D53/261 , B01D2256/16 , B01D2257/108 , B01D2257/702 , B01D2257/7022 , C01B2203/0227 , C01B2203/043 , C01B2203/048 , C01B2203/1247 , C01B2203/141 , C01B2203/143 , C01B2203/148 , C07C7/12
Abstract: Embodiments of apparatuses and methods for reforming of hydrocarbons including recovery of products are provided. In one example, a method comprises separating a reforming-zone effluent into a net gas phase stream and a liquid phase hydrocarbon stream. The net gas phase stream is separated for forming an H2-rich stream and a first intermediate liquid phase hydrocarbon stream. The H2-rich stream is contacted with an adsorbent to form an H2-ultra rich stream and a PSA tail gas stream. The PSA tail gas stream and at least a portion of the liquid phase hydrocarbon stream are cooled and contacted with each other to form a H2, C2− hydrocarbons-containing gas stream and a cooled second intermediate liquid phase hydrocarbon stream.
Abstract translation: 提供了包括产物回收的烃类重整装置和方法的实施例。 在一个实例中，一种方法包括将重整区流出物分离成净气相流和液相烃流。 净气相流被分离以形成富H 2流和第一中间液相烃流。 富H2流与吸附剂接触以形成富H2流和PSA尾气流。 PSA尾气流和至少一部分液相烃流被冷却并彼此接触以形成含H2，C2-烃的气流和冷却的第二中间液相烃流。
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10.发明申请公开(公告)号：US20160115099A1
公开(公告)日：2016-04-28
申请号：US14524301
申请日：2014-10-27
Applicant: UOP LLC
Inventor： Robert Edison Tsai , Xin X. Zhu , Bryan K. Glover , Eleftherios Adamopoulos , William Yanez
CPC classification number: C07C7/005 , B01D53/002 , B01D53/047 , B01D53/229 , B01D53/261 , B01D2053/221 , B01D2253/102 , B01D2253/104 , B01D2253/106 , B01D2253/108 , B01D2256/16 , B01D2256/24 , B01D2257/102 , B01D2257/108 , B01D2257/502 , B01D2257/7022 , B01D2257/7027 , B01D2257/80 , B01D2259/4146 , C01B3/34 , C01B3/501 , C01B3/56 , C01B2203/0405 , C01B2203/042 , C01B2203/043 , C01B2203/048 , C01B2203/1247 , C07C7/12 , C07C7/144 , C10L3/12 , C10L2290/542 , C10L2290/548
Abstract: Embodiments of apparatuses and methods for reforming of hydrocarbons including recovery of products are provided. In one example, a method comprises separating a reforming-zone effluent into a net gas phase stream and a liquid phase hydrocarbon stream. The net gas phase stream is separated for forming an H2-rich stream and a first intermediate liquid phase hydrocarbon stream. The H2-rich stream is contacted with an adsorbent to form an H2-ultra rich stream and a PSA tail gas stream. The PSA tail gas stream is contacted with an H2/hydrocarbon separation membrane to separate the PSA tail gas stream and form an H2-ultra rich permeate stream and a PSA tail gas hydrocarbon-containing non-permeate residue stream.
Abstract translation: 提供了包括产物回收的烃类重整装置和方法的实施例。 在一个实例中，一种方法包括将重整区流出物分离成净气相流和液相烃流。 净气相流被分离以形成富H 2流和第一中间液相烃流。 富H2流与吸附剂接触以形成富H2流和PSA尾气流。 PSA尾气流与H2 /烃分离膜接触以分离PSA尾气流并形成富H2的富含渗透物流和含PSA尾气烃的非渗透物残留物流。
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