Method of controlling the supply and allocation of hydrogen gas in a hydrogen system of a refinery integrated with olefins and aromatics plants
원문보기
IPC분류정보
국가/구분
United States(US) Patent
등록
국제특허분류(IPC7판)
C10G-069/00
C10G-009/00
C10G-035/04
C10G-045/58
C10G-069/04
C10G-069/06
C10G-047/00
C10G-049/26
C10G-069/10
C10G-011/02
C10G-045/02
C10G-045/44
출원번호
US-0120853
(2014-12-23)
등록번호
US-10160925
(2018-12-25)
우선권정보
EP-14156632 (2014-02-25)
국제출원번호
PCT/EP2014/079223
(2014-12-23)
국제공개번호
WO2015/128042
(2015-09-03)
발명자
/ 주소
Oprins, Arno Johannes Maria
Ward, Andrew Mark
Schaerlaeckens, Egidius Jacoba Maria
Velasco Pelaez, Raúl
Narayanaswamy, Ravichander
Rajagopalan, Vijayanand
Van Willigenburg, Joris
출원인 / 주소
SAUDI BASIC INDUSTRIES CORPORATION
대리인 / 주소
Norton Rose Fulbright US LLP
인용정보
피인용 횟수 :
0인용 특허 :
19
초록▼
A method of controlling the supply and allocation of hydrogen gas in a hydrogen system of a refinery integrated with olefins and aromatics plants to convert crude oil into petrochemicals. The method includes one or more supply sources that provide hydrogen at individual rates, purities, pressures an
A method of controlling the supply and allocation of hydrogen gas in a hydrogen system of a refinery integrated with olefins and aromatics plants to convert crude oil into petrochemicals. The method includes one or more supply sources that provide hydrogen at individual rates, purities, pressures and costs, multiple consumption sites that consume hydrogen at individual rates, purities and pressures and an interconnecting hydrogen distribution network. The method further includes the integration of hydrogen consuming process units with hydrogen producing process units in which hydrogen recovered from the effluents from the hydrogen consuming process units and hydrogen recovered from the hydrogen producing process units are re-used in the hydrogen consuming process units.
대표청구항▼
1. A method of controlling supply and allocation of hydrogen gas in a hydrogen system of a refinery integrated with olefins and aromatics plants to convert crude oil into petrochemicals, the system comprising one or more supply sources that provide hydrogen at individual rates, purities, pressures a
1. A method of controlling supply and allocation of hydrogen gas in a hydrogen system of a refinery integrated with olefins and aromatics plants to convert crude oil into petrochemicals, the system comprising one or more supply sources that provide hydrogen at individual rates, purities, pressures and costs, multiple consumption sites that consume hydrogen at individual rates, purities and pressures and an interconnecting hydrogen distribution network, said method comprising the integration of hydrogen consuming process units with hydrogen producing process units, wherein both hydrogen recovered from the effluents from the hydrogen consuming process units and hydrogen recovered from the hydrogen producing process units are re-used in the hydrogen consuming process units, wherein the method comprises the steps of: feeding a crude oil fraction together with hydrogen to one or more hydrogen consuming units;separating the effluent(s) from said one or more hydrogen consuming units into one or more streams comprising methane, ethane, propane, butane, pitch and BTX;feeding said one or more streams comprising ethane, propane and butane to one or more hydrogen producing units to produce hydrogen;integrating said stream comprising hydrogen originating from said hydrogen producing units into said hydrogen stream(s) to be fed to said one or more hydrogen consuming units, wherein at least 25 wt. % of said crude oil fraction is converted into a low boiling hydrocarbon fraction comprising ethane, propane and butanes, wherein said hydrogen producing process units comprise a steam cracking unit and one or more units chosen from the group of propane dehydrogenation unit (PDH), butane dehydrogenation unit (BDH) and combined PDH and BDH unit. 2. The method according to claim 1, wherein at least 50 wt % of said feed is converted into a low boiling hydrocarbon fraction comprising ethane, propane and butanes. 3. A method of controlling supply and allocation of hydrogen gas in a hydrogen system of a refinery integrated with olefins and aromatics plants to convert crude oil into petrochemicals, the system comprising one or more supply sources that provide hydrogen at individual rates, purities, pressures and costs, multiple consumption sites that consume hydrogen at individual rates, purities and pressures and an interconnecting hydrogen distribution network, said method comprising the integration of hydrogen consuming process units with hydrogen producing process units, wherein both hydrogen recovered from the effluents from the hydrogen consuming process units and hydrogen recovered from the hydrogen producing process units are re-used in the hydrogen consuming process units, wherein the method comprises the steps of: feeding a crude oil fraction together with hydrogen to one or more hydrogen consuming units;separating the effluent(s) from said one or more hydrogen consuming units into one or more streams comprising methane, ethane, propane, butane, pitch and BTX;feeding said one or more streams comprising ethane, propane and butane to one or more hydrogen producing units for producing one or more streams comprising hydrogen;integrating said stream comprising hydrogen originating from said hydrogen producing units into said hydrogen stream(s) to be fed to said one or more hydrogen consuming units, wherein at least 25 wt % of said crude oil fraction is converted into a low boiling hydrocarbon fraction comprising ethane, propane and butanes, wherein said hydrogen producing process units comprise a steam cracking unit and one or more units chosen from the group of propane dehydrogenation unit (PDH), butane dehydrogenation unit (BDH) and combined PDH, a BDH unit, a feed hydrocracking unit, gas oil hydrocracking unit, aromatic ring opening unit, resid hydrocracking unit, gasoline hydrocracker unit, a hydrodesulphurization unit, hydro-dearomatization unit and hydro-dealkylation unit. 4. A method of controlling supply and allocation of hydrogen gas in a hydrogen system of a refinery integrated with olefins and aromatics plants to convert crude oil into petrochemicals, the system comprising one or more supply sources that provide hydrogen at individual rates, purities, pressures and costs, multiple consumption sites that consume hydrogen at individual rates, purities and pressures and an interconnecting hydrogen distribution network, said method comprising the integration of hydrogen consuming process units with hydrogen producing process units, wherein both hydrogen recovered from the effluents from the hydrogen consuming process units and hydrogen recovered from the hydrogen producing process units are re-used in the hydrogen consuming process units, wherein the method comprises the steps of: feeding a crude oil fraction together with hydrogen to one or more hydrogen consuming units;separating the effluent(s) from said one or more hydrogen consuming units into one or more streams comprising methane, ethane, propane, butane, pitch and BTX;feeding said one or more streams comprising ethane, propane and butane to one or more hydrogen producing units for producing one or more streams comprising hydrogen;integrating said stream comprising hydrogen originating from said hydrogen producing units into said hydrogen stream(s) to be fed to said one or more hydrogen consuming units, wherein at least 25 wt. % of said crude oil fraction is converted into a low boiling hydrocarbon fraction comprising ethane, propane and butanes, wherein said hydrogen producing process units comprise a steam cracking unit and one or more units chosen from the group of propane dehydrogenation unit (PDH), butane dehydrogenation unit (BDH) and combined PDH, a BDH unit, a catalytic naphtha reformer unit and liquefied petroleum gas (LPO) unit. 5. The method according to claim 1, further comprising setting cut points of one or more separation units, setting operation conditions of hydrogen consuming process units and setting operation conditions of hydrogen producing process units in a process control system, wherein the values of said cut points and operation conditions are such that said supply and allocation of hydrogen gas in a hydrogen system of a refinery is controlled. 6. The method according to claim 1, further comprising purging excess hydrogen and/or supplying additional hydrogen from hydrogen producing units. 7. The method according to claim 1, further comprising feeding said effluent(s) from said hydrogen consuming process units to separating unit(s) and separating the effluents from said separating unit(s) into a lights fraction, a C2 fraction, a C3 fraction and a C4 fraction. 8. The method according to claim 7, further comprising feeding said C2 fraction to said steam cracking unit, said C3 fraction to said propane dehydrogenation unit and said C4 fraction to said butane dehydrogenation unit, respectively. 9. The method according to claim 7, further comprising feeding said C3 fraction and/or said C4 fraction to a said LPG aromatization unit. 10. The method according to claim 1, further comprising feeding a crude oil fraction to a catalytic naphtha reformer unit for producing hydrogen, wherein the hydrogen thus produced is sent to a hydrogen consuming unit. 11. The method according to claim 7, further comprising feeding said C2 fraction to said steam cracking unit. 12. The method according to claim 7, further comprising feeding said C3 fraction to said propane dehydrogenation unit. 13. The method according to claim 7, further comprising feeding said C4 fraction to said butane dehydrogenation unit. 14. The method according to claim 7, further comprising feeding said C3 fraction and said C4 fraction to a LPG aromatization unit. 15. The method according to claim 7, further comprising feeding said C3 fraction to a LPG aromatization unit. 16. The method according to claim 7, further comprising feeding said C4 fraction to a LPG aromatization unit. 17. The method according to claim 1, further comprising feeding a crude oil fraction to a catalytic naphtha reformer unit for producing hydrogen. 18. The method according to claim 1, further comprising supplying additional hydrogen to said hydrogen producing units.
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이 특허에 인용된 특허 (19)
Oballa, Michael C.; Simanzhenkov, Vasily; Weitkamp, Jens; Gläser, Roger; Traa, Yvonne; Demir, Fehime, Aromatic saturation and ring opening process.
Imai Tamotsu (Mt. Prospect IL) Abrevaya Hayim (Chicago IL) Bricker Jeffery C. (Buffalo Grove IL) Jan Deng-Yang (Mt. Prospect IL), Dehydrogenation catalyst composition and hydrocarbon dehydrogenation process.
Olbrich Michael E. (Lake Jackson TX) McKay Dwight L. (Bartlesville OK) Montgomery ; deceased Dean P. (late of Washington County OK) Montgomery by B. Jean ; administratrix (Bartlesville OK), Dehydrogenation process.
Fournier, Antoine; Nocca, Jean Luc, Process and apparatus for integration of a high-pressure hydroconversion process and a medium-pressure middle distillate hydrotreatment process, whereby the two processes are independent.
Duddy, John E.; Wisdom, Lawrence I.; Gragnani, Andrea, Process and installation for conversion of heavy petroleum fractions in a boiling bed with integrated production of middle distillates with a very low sulfur content.
Bulford Stanley N. (Shepperton GB2) Davies Evan E. (Woking GB2), Process for aromatizing C3-C8hydrocarbon feedstocks using a gallium containing catalyst sup.
Davies Evan E. (Woking GB2) Kolombos Alexander J. (Thames Ditton GB2), Process for converting C3-C12hydrocarbons to aromatics over gallia-activated zeolite.
Bigeard Pierre-Henri,FRX ; Morel Frederic,FRX ; Gueret Christophe,FRX ; Briot Patrick,FRX ; Marion Pierre,FRX, Process for converting heavy crude oil fractions, comprising an ebullating bed conversion step and a hydrocracking step.
Weiss, Wilfried; Barbier, Jeremie, Process for converting petroleum feedstocks comprising an ebullating-bed hydrocracking stage, a maturation stage and a stage of separating the sediments for the production of fuel oils with a low sediment content.
Franck Jean-Pierre (Bougival FRX) Freund Edouard (Rueil Malmaison FRX) Marcilly Christian (Houilles FRX) Miquel Jean (Paris FRX), Process for manufacturing olefinic hydrocarbons with respectively two and three carbon atoms per molecule.
Colyar, James J.; Duddy, John, Process for multistage residue hydroconversion integrated with straight-run and conversion gasoils hydroconversion steps.
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