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1.发明申请
公开(公告)号：WO2015128043A1
公开(公告)日：2015-09-03
申请号：PCT/EP2014/079224
申请日：2014-12-23
Applicant: SAUDI BASIC INDUSTRIES CORPORATION , SABIC GLOBAL TECHNOLOGIES B.V. , OPRINS, Arno Johannes Maria , HOUSMANS, Thomas Hubertus Maria , RAJAGOPALAN, Vijayanand , NARAYANASWAMY, Ravichander
Inventor： OPRINS, Arno Johannes Maria , HOUSMANS, Thomas Hubertus Maria , RAJAGOPALAN, Vijayanand , NARAYANASWAMY, Ravichander
CPC classification number: C10G67/049 , C10G9/36 , C10G47/00 , C10G49/00 , C10G69/06 , C10G2300/205 , C10G2300/206 , C10G2300/301 , C10G2300/302 , C10G2300/44
Abstract: The present invention relates to a process for the preparation of a feedstock for a hydroprocessing unit, wherein said feedstock is based on crude oil containing asphaltenes, said process comprising the steps of: mixing said crude oil with a solvent, wherein said solvent is at least one member chosen from the group of steam cracker cracked distillate (CD), steam cracker carbon black oil (CBO), low asphaltenes containing crude oil residue having a boiling point above 300 deg C and aromatic rich hydrocarbons streams, wherein a mixing ratio solvent: crude oil is such that no aggregation of asphaltenes in said combined mixture of solvent and crude oil takes place under mixing conditions; feeding said combined mixture of solvent and crude oil to one or more hydroprocessing units.
Abstract translation: 本发明涉及一种用于制备用于加氢处理装置的原料的方法，其中所述原料基于含有沥青质的原油，所述方法包括以下步骤：将所述原油与溶剂混合，其中所述溶剂至少为 选自蒸汽裂解裂化馏分（CD），蒸汽裂化器炭黑油（CBO），含有沸点高于300℃的原油残余物的低沥青质和富含芳烃的烃流的一个成员，其中混合比溶剂： 原油使得在混合条件下在所述溶剂和原油的混合物中不发生沥青质的聚集; 将所述溶剂和原油的混合物加入到一个或多个加氢处理单元中。
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2.发明申请
公开(公告)号：WO2015000840A1
公开(公告)日：2015-01-08
申请号：PCT/EP2014/063848
申请日：2014-06-30
Applicant: SAUDI BASIC INDUSTRIES CORPORATION , SABIC GLOBAL TECHNOLOGIES , WARD, Andrew Mark , HOUSMANS, Thomas Hubertus Maria , OPRINS, Arno Johannes Maria
CPC classification number: C10G69/06 , C10G67/0445 , C10G69/00 , C10G2300/1044 , C10G2300/1051 , C10G2300/1055 , C10G2300/1059 , C10G2300/1085 , C10G2400/20 , C10G2400/30 , Y02P30/40
Abstract: The present invention relates to a process for cracking a hydrocarbon feedstock in a steam cracker unit, comprising the following steps of: feeding a liquid hydrocarbon feedstock to a hydrocracking unit, separating the stream thus hydrocracked in said hydrocracking unit into a high content aromatics stream and a gaseous stream comprising C2-C4 paraffins, hydrogen and methane, separating C2-C4 paraffins from said gaseous stream, feeding said C2-C4 paraffins thus separated to the furnace section of a steam cracker unit.
Abstract translation: 本发明涉及一种用于在蒸汽裂解装置中裂解烃原料的方法，包括以下步骤：将液体烃原料进料到加氢裂化装置，将在所述加氢裂化装置中如此加氢裂化的物流分离成高含量芳族化合物物流， 包含C2-C4链烷烃，氢和甲烷的气流，从所述气流中分离出C 2 -C 4链烷烃，将所分离的所述C2-C4链烷烃进料到蒸汽裂化装置的炉部分。
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Patent Agency Ranking3.发明申请METHOD FOR CONVERTING A HIGH-BOILING HYDROCARBON FEEDSTOCK INTO LIGHTER BOILING HYDROCARBON PRODUCTS 审中-公开将高沸点碳氢化合物转化为更高沸点的碳氢化合物产品的方法
公开(公告)号：WO2015000845A1
公开(公告)日：2015-01-08
申请号：PCT/EP2014/063853
申请日：2014-06-30
Applicant: SAUDI BASIC INDUSTRIES CORPORATION , SABIC GLOBAL TECHNOLOGIES B.V. , WARD, Andrew, Mark , NARAYANASWAMY, Ravichander , RAJAGOPALAN, Vijayanand , POWALE, Lakshmikant Suryakant , HOUSMANS, Thomas, Hubertus, Maria , OPRINS, Arno, Johannes, Maria , TURNER, William, Jay
Inventor： WARD, Andrew, Mark , NARAYANASWAMY, Ravichander , RAJAGOPALAN, Vijayanand , POWALE, Lakshmikant Suryakant , HOUSMANS, Thomas, Hubertus, Maria , OPRINS, Arno, Johannes, Maria , TURNER, William, Jay
CPC classification number: C10G69/00 , C10G65/00 , C10G65/10 , C10G65/12 , C10G69/06 , C10G2300/1011 , C10G2400/20 , C10G2400/30
Abstract: The present invention relates to a process for converting a high- boiling hydrocarbon feedstock into lighter boiling hydrocarbon products, said lighter boiling hydrocarbon products being suitable as a feedstock for petrochemicals processes, said converting process comprising the following steps of: feeding a hydrocarbon feedstock having a boiling point of > 350 deg Celsius to a cascade of hydrocracking unit(s), feeding the bottom stream of a hydrocracking unit as a feedstock for a subsequent hydrocracking unit, wherein the process conditions in each hydrocracking unit(s) are different from each other, in which the hydrocracking conditions from the first to the subsequent hydrocracking unit(s) increase from least severe to most severe, and processing the lighter boiling hydrocarbon products from each hydrocracking unit(s) as a feedstock for one or more petrochemicals processes.
Abstract translation: 本发明涉及一种将高沸点烃原料转化成较轻沸点烃产物的方法，所述较轻沸点烃产物适合作为石化工艺的原料，所述转化方法包括以下步骤：将具有 沸点> 350摄氏度加氢裂化装置的级联，将加氢裂化装置的底部料流作为后续加氢裂化装置的原料进料，其中每个加氢裂化装置的工艺条件彼此不同 ，其中来自第一至后续加氢裂化装置的加氢裂化条件从最不严重到最严重的加氢裂化条件增加，并且将来自每个加氢裂化装置的较轻沸点的烃产物作为一种或多种石化工艺的原料加工。
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4.发明申请
公开(公告)号：WO2015000844A1
公开(公告)日：2015-01-08
申请号：PCT/EP2014/063852
申请日：2014-06-30
Applicant: SAUDI BASIC INDUSTRIES CORPORATION , SABIC GLOBAL TECHNOLOGIES B.V. , WARD, Andrew Mark , OPRINS, Arno Johannes Maria , HOUSMANS, Thomas Hubertus Maria , NARAYANASWAMY, Ravichander , RAJAGOPALAN, Vijayanand , POWALE, Lakshmikant Suryakant
Inventor： WARD, Andrew Mark , OPRINS, Arno Johannes Maria , HOUSMANS, Thomas Hubertus Maria , NARAYANASWAMY, Ravichander , RAJAGOPALAN, Vijayanand , POWALE, Lakshmikant Suryakant
CPC classification number: C10G69/06 , C10G9/36 , C10G51/00 , C10G2400/20 , C10G2400/30 , Y02P30/40
Abstract: The present invention relates to process for cracking a hydrocarbon feedstock in a steam cracker unit, comprising the following steps of: feeding a hydrocarbon feedstock to a first hydrocracking unit, feeding the hydrocarbon feedstock thus cracked to a separation unit for obtaining a stream high in paraffins and naphtenes, a stream high in heavy aromatics and a stream high in mono-aromatics feeding the stream high in paraffins and naphtenes to a second hydrocracking unit, wherein the process conditions in the first hydrocracking unit differ from the process conditions in the second hydrocracking unit, separating the stream thus hydrocracked in the second hydrocracking unit in a high content aromatics stream and gaseous stream comprising C2-C4 paraffins, hydrogen and methane, feeding the gaseous stream to a steam cracker unit.
Abstract translation: 本发明涉及在蒸汽裂化装置中裂解烃原料的方法，包括以下步骤：将烃原料进料到第一加氢裂化装置，将由此裂化的烃原料送入分离装置，以获得高的链烷烃流 和萘酚，高重量芳族化合物的流和高单链芳烃的物流将高级链烷烃和萘的物流送入第二加氢裂化装置，其中第一加氢裂化装置中的工艺条件与第二加氢裂化装置中的工艺条件不同 ，在高含量芳族化合物流中将在第二加氢裂化装置中如此加氢裂化的物流和包含C 2 -C 4链烷烃，氢气和甲烷的气流分离，将气流送入蒸汽裂化装置。
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公开(公告)号：WO2015000841A1
公开(公告)日：2015-01-08
申请号：PCT/EP2014/063849
申请日：2014-06-30
Applicant: SAUDI BASIC INDUSTRIES CORPORATION , SABIC GLOBAL TECHNOLOGIES B.V. , HOUSMANS, Thomas, Hubertus, Maria , OPRINS, Arno, Johannes, Maria
CPC classification number: C10G69/02 , C10G65/00 , C10G65/10 , C10G65/18 , C10G67/0445 , C10G69/06 , C10G69/14 , C10G2300/1044 , C10G2300/1051 , C10G2300/1055 , C10G2300/1059 , C10G2300/107 , C10G2300/1077 , C10G2400/20 , C10G2400/30
Abstract: The present invention relates to a process for upgrading refinery heavy residues to petrochemicals, comprising the following steps of: (a) separating a hydrocarbon feedstock in a distillation unit into a to overhead stream and a bottom stream (b) feeding said bottom stream to a hydrocracking reaction area (c) separating reaction products, which are generated from said reaction area of step (b) into a stream rich in mono-aromatics and in a stream rich in poly-aromatics (d) feeding said stream rich in mono-aromatics to a gasoline hydrocracker (GHC) unit, (e) feeding said stream rich in poly-aromatics to a ring opening reaction area.
Abstract translation: 本发明涉及一种将炼厂重质残渣升级至石化产品的方法，包括以下步骤：（a）将蒸馏单元中的烃原料分离成塔顶物流和塔底物流（b），将塔底物料送入 （c）将从步骤（b）的所述反应区域产生的反应产物分离成富含单芳族化合物的流和富含多芳族化合物的流（d）将富含单芳族化合物的所述物流 到汽油加氢裂化器（GHC）单元，（e）将富含多芳族化合物的所述物流加入开环反应区。
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6.发明申请
公开(公告)号：WO2015000846A1
公开(公告)日：2015-01-08
申请号：PCT/EP2014/063854
申请日：2014-06-30
Applicant: SAUDI BASIC INDUSTRIES CORPORATION , SABIC GLOBAL TECHNOLOGIES B.V. , WARD, Andrew, Mark , HOUSMANS, Thomas, Hubertus, Maria , OPRINS, Arno, Johannes, Maria
CPC classification number: C10G69/06 , C10G55/04 , C10G67/00 , C10G67/0445 , C10G69/00 , C10G69/14 , C10G2400/20 , C10G2400/30
Abstract: The present invention relates to method of producing aromatics and light olefins from a hydrocarbon feedstock comprising the steps of: (a) subjecting the hydrocarbon feedstock to a solvent extraction process in a solvent extraction unit; (b) separating from the solvent extracted hydrocarbon feedstock obtained in step (a) a raffinate fraction comprising paraffins and a fraction comprising aromatics and naphtenes; (c) converting said fraction comprising aromatics and naphtenes in a hydrocracking unit and separating into a high content aromatics fraction and a stream high in light paraffins;; (d) converting said raffinate fraction in a steam cracking unit into light olefins.
Abstract translation: 本发明涉及从烃原料制备芳族化合物和轻质烯烃的方法，包括以下步骤：（a）使烃原料在溶剂萃取单元中进行溶剂萃取过程; （b）从步骤（a）中获得的溶剂萃取的烃原料中分离出一种含有链烷烃和包含芳烃和萘的馏分的萃余馏分; （c）在加氢裂化装置中将包含芳族化合物和萘的所述馏分转化成高含量芳族化合物部分和轻质石蜡中的高流量; （d）将蒸汽裂解装置中的所述残液馏分转化为轻质烯烃。
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7.发明申请PROCESS FOR THE PRODUCTION OF LIGHT OLEFINS AND AROMATICS FROM A HYDROCARBON FEEDSTOCK 审中-公开从石油生产中生产轻油和芳烃的方法
公开(公告)号：WO2015000842A1
公开(公告)日：2015-01-08
申请号：PCT/EP2014/063850
申请日：2014-06-30
Applicant: SAUDI BASIC INDUSTRIES CORPORATION , SABIC GLOBAL TECHNOLOGIES B.V. , WARD, Andrew Mark , OPRINS, Arno Johannes Maria , HOUSMANS, Thomas Hubertus Maria
CPC classification number: C10G69/06 , C10G69/00 , C10G69/04 , C10G2300/1044 , C10G2300/1051 , C10G2300/1055 , C10G2300/1059 , C10G2300/107 , C10G2300/1077 , C10G2300/1085 , C10G2400/20 , C10G2400/30 , Y02P30/40
Abstract: The present invention relates to a process for the production of light olefins and aromatics from a hydrocarbon feedstock, comprising the following steps of: (a) feeding a hydrocarbon feedstock into a FCC unit (b) separating reaction products, which are generated from the FCC reaction, into a bottom stream, and middle stream and a top stream; (c) feeding the middle stream from (b) to a gasoline hydrocracker (GHC) unit, (d) separating reaction products of said GHC of step (c) into an overhead gas stream comprising hydrogen, methane and C2-C4 paraffins, and a bottom stream comprising aromatic hydrocarbon compounds, (e) feeding the overhead stream from the gasoline hydrocracker (GHC) unit into a steam cracker unit.
Abstract translation: 本发明涉及从烃原料生产轻质烯烃和芳族化合物的方法，包括以下步骤：（a）将烃原料进料到FCC装置中（b）分离由FCC生成的反应产物 反应，进入底部流，中流和顶流; （c）将中间物流从（b）加入到汽油加氢裂化器（GHC）单元中，（d）将步骤（c）的所述GHC的反应产物分离成包含氢，甲烷和C 2 -C 4链烷烃的塔顶气流，以及 包含芳族烃化合物的底部物流，（e）将来自汽油加氢裂化器（GHC）装置的塔顶馏出物进料到蒸汽裂化装置中。
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