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公开(公告)号:US11441838B2
公开(公告)日:2022-09-13
申请号:US16278017
申请日:2019-02-15
Applicant: UOP LLC
Inventor: Thuy T. Vu , Robert E. Tsai , Xin X. Zhu , Amit Goyal , William Yanez , Sudipta K. Ghosh
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 liquid phase hydrocarbon stream. The H2-rich stream may be contacted with an adsorbent to form an H2-ultra rich stream and a gas stream. C3/C4 hydrocarbons are absorbed from the gas stream with the liquid phase hydrocarbon stream. The gas stream may be contacted with an H2/hydrocarbon separation membrane to separate the PSA tail gas stream and form an H2-rich permeate stream and an H2 depleted non-permeate residue stream.
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公开(公告)号:US20200263922A1
公开(公告)日:2020-08-20
申请号:US16278017
申请日:2019-02-15
Applicant: UOP LLC
Inventor: Thuy T. Vu , Robert E. Tsai , Xin X. Zhu , Amit Goyal , William Yanez , Sudipta K. Ghosh
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 liquid phase hydrocarbon stream. The H2-rich stream may be contacted with an adsorbent to form an H2-ultra rich stream and a gas stream. C3/C4 hydrocarbons are absorbed from the gas stream with the liquid phase hydrocarbon stream. The gas stream may be contacted with an H2/hydrocarbon separation membrane to separate the PSA tail gas stream and form an H2-rich permeate stream and an H2 depleted non-permeate residue stream.
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公开(公告)号:US20140260419A1
公开(公告)日:2014-09-18
申请号:US13836119
申请日:2013-03-15
Applicant: UOP LLC
Inventor: Paul C. Steacy , Lawrence W. Miller , Thuy T. Vu
IPC: F25J3/02
CPC classification number: C07C5/327 , B01D3/4216 , C07C7/04 , C07C9/08 , C07C11/06
Abstract: A portion of the overhead vapor from a distillation column is used to heat a process stream. The temperature and flow rate of the stream out of a heat exchanger are controlled so that the vapor is condensed.
Abstract translation: 来自蒸馏塔的一部分塔顶蒸气用于加热工艺流。 控制热交换器流出的温度和流速,使蒸气冷凝。
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