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    • 1. 发明授权
    • Process to make olefins and aromatics from organics
    • 从有机物中制备烯烃和芳烃的方法
    • US09573859B2
    • 2017-02-21
    • US14560451
    • 2014-12-04
    • TOTAL RESEARCH & TECHNOLOGY FELUY
    • Nikolai NesterenkoWalter VermeirenGiacomo GrassoSander Van DonkWolfgang Garcia
    • C07C1/20B01J21/16B01J27/14B01J29/89B01J29/90B01J29/80B01J21/08B01J29/18B01J29/40B01J29/65B01J38/12C07C1/26C07C1/32C07C2/86C07C4/06
    • C07C1/20B01J21/08B01J21/16B01J27/14B01J29/18B01J29/40B01J29/65B01J29/90B01J38/12B01J2229/16B01J2229/18B01J2229/36B01J2229/37C07C1/26C07C1/322C07C2/864C07C4/06C07C2529/40Y02P20/584Y02P30/42C07C15/02C07C11/02
    • The present invention relates to a process to make light olefins and aromatics, in a combined XTO-OC process, from an oxygen-containing, halogenide-containing or sulphur-containing organic feedstock comprising: a0) providing a first portion and a second portion of said oxygen-containing, halogenide-containing or sulphur-containing organic feedstock, a) providing a catalyst comprising zeolitic molecular sieves containing at least 10 membered ring pore openings or larger in their microporous structure, b) providing an XTO reaction zone, an OC reaction zone and a catalyst regeneration zone, said catalyst circulating in the three zones, such that at least a portion of the regenerated catalyst is passed to the OC reaction zone, at least a portion of the catalyst in the OC reaction zone is passed to the XTO reaction zone and at least a portion of the catalyst in the XTO reaction zone is passed to the regeneration zone; c) contacting the first portion of said oxygen-containing, halogenide-containing or sulphur-containing organic feedstock in the XTO reactor with the catalyst at conditions effective to convert at least a portion of the feedstock to form a XTO reactor effluent comprising light olefins and a heavy hydrocarbon fraction; d) separating said light olefins from said heavy hydrocarbon fraction; e) contacting said heavy hydrocarbon fraction and the second portion of said oxygen-containing, halogenide-containing or sulphur-containing organic feedstock in the OC reactor with the catalyst at conditions effective to convert at least a portion of said heavy hydrocarbon fraction and oxygen-containing, halogenide-containing or sulphur-containing organic feedstock to light olefins and aromatics.
    • 本发明涉及一种在组合的XTO-OC方法中由含氧,含卤素或含硫有机原料制备轻质烯烃和芳族化合物的方法,包括:a0)提供第一部分和第二部分 所述含氧,含卤素或含硫有机原料,a)提供包含在其微孔结构中含有至少10元环孔孔或更大的沸石分子筛的催化剂,b)提供XTO反应区,OC反应 区域和催化剂再生区,所述催化剂在三个区域中循环,使得至少一部分再生催化剂通过OC反应区,OC反应区中的至少一部分催化剂通过XTO 反应区和XTO反应区中的至少一部分催化剂通入再生区; c)在有效地转化至少一部分原料以形成包含轻质烯烃的XTO反应器流出物的条件下,将XTO反应器中的含氧卤化物或含硫有机原料的第一部分与催化剂接触, 重质烃馏分; d)从所述重质烃馏分中分离出所述轻质烯烃; e)在OC反应器中将所述重质烃部分和第二部分所述含氧卤化物或含硫有机原料与所述催化剂接触,所述条件有效地将至少一部分所述重质烃部分和氧 - 含有卤化物或含硫有机原料至轻质烯烃和芳族化合物。
    • 2. 发明授权
    • Process to make olefins from organics
    • 从有机物制造烯烃的方法
    • US09556082B2
    • 2017-01-31
    • US14560015
    • 2014-12-04
    • TOTAL RESEARCH & TECHNOLOGY FELUY
    • Nikolai NesterenkoWalter VermeirenGiacomo GrassoSander Van DonkWolfgang Garcia
    • C07C1/20B01J21/16B01J27/14B01J29/89B01J29/90B01J29/80B01J21/08B01J29/18B01J29/40B01J29/65B01J38/12C07C1/26C07C1/32C07C4/06
    • C07C1/20B01J21/08B01J21/16B01J27/14B01J29/18B01J29/40B01J29/65B01J29/90B01J38/12B01J2229/16B01J2229/18B01J2229/36B01J2229/37C07C1/26C07C1/322C07C4/06C07C2529/40Y02P20/584Y02P30/42C07C11/02
    • The present invention relates to a process to make light olefins, in a combined XTO-OC process, from an oxygen-containing, halogenide-containing or sulphur-containing organic feedstock comprising: a0) providing a first portion and a second portion of said oxygen-containing, halogenide-containing or sulphur-containing organic feedstock, a) providing a catalyst comprising zeolitic molecular sieves containing at least 10 membered ring pore openings or larger in their microporous structure, b) providing an XTO reaction zone, an OC reaction zone and a catalyst regeneration zone, said catalyst circulating in the three zones, such that at least a portion of the regenerated catalyst is passed to the OC reaction zone, optionally at least a portion of the catalyst in the OC reaction zone is passed to the XTO reaction zone and at least a portion of the catalyst in the XTO reaction zone is passed to the regeneration zone; c) contacting the first portion of said oxygen-containing, halogenide-containing or sulphur-containing organic feedstock in the XTO reactor with the catalyst at conditions effective to convert at least a portion of the feedstock to form a XTO reactor effluent comprising light olefins and a heavy hydrocarbon fraction; d) separating said light olefins from said heavy hydrocarbon fraction; e) contacting said heavy hydrocarbon fraction and the second portion of said oxygen-containing, halogenide-containing or sulphur-containing organic feedstock in the OC reactor with the catalyst at conditions effective to convert at least a portion of said heavy hydrocarbon fraction and oxygen-containing, halogenide-containing or sulphur-containing organic feedstock to light olefins.
    • 本发明涉及一种在组合的XTO-OC方法中由含氧,含卤素或含硫有机原料制备轻质烯烃的方法,包括:a)提供所述氧气的第一部分和第二部分 a)提供包含在其微孔结构中含有至少10元环孔或更大孔沸石分子筛的催化剂,b)提供XTO反应区,OC反应区和 催化剂再生区,所述催化剂在三个区域中循环,使得至少一部分再生催化剂通入OC反应区,任选地将OC反应区中的至少一部分催化剂通入XTO反应 区域,并且XTO反应区中的至少一部分催化剂被传送到再生区; c)在有效地转化至少一部分原料以形成包含轻质烯烃的XTO反应器流出物的条件下,将XTO反应器中的含氧卤化物或含硫有机原料的第一部分与催化剂接触, 重质烃馏分; d)从所述重质烃馏分中分离出所述轻质烯烃; e)在OC反应器中将所述重质烃部分和第二部分所述含氧卤化物或含硫有机原料与所述催化剂接触,所述条件有效地将至少一部分所述重质烃部分和氧 - 含卤素或含硫有机原料转化成轻质烯烃。
    • 3. 发明申请
    • Process to Make Olefins from Oxygenates
    • 从氧化烯制备烯烃的方法
    • US20150099912A1
    • 2015-04-09
    • US14565539
    • 2014-12-10
    • TOTAL RESEARCH & TECHNOLOGY FELUY
    • Nikolai NesterenkoWalter VermeirenGiacomo GrassoSander Van DonkWolfgang Garcia
    • C07C1/22C07C4/06
    • C07C1/22B01J21/08B01J21/16B01J27/14B01J29/18B01J29/40B01J29/65B01J29/90B01J37/10B01J38/12B01J2229/16B01J2229/186B01J2229/36C07C1/20C07C1/26C07C1/322C07C4/06C07C2529/40C10G3/44C10G3/49C10G3/62C10G9/00C10G55/04C10G2400/20Y02P20/584Y02P30/20Y02P30/42C07C11/02
    • The present invention relates to a process to make light olefins, in a combined XTO-OC process, from an oxygen-containing, halogenide-containing or sulphur-containing organic feedstock comprising: a) providing a catalyst comprising zeolitic molecular sieves containing 10 member and larger channels in their microporous structure, b) providing an XTO reaction zone, an OC reaction zone and a catalyst regeneration zone, said catalyst circulating in the three zones, such that at least a portion of the regenerated catalyst is passed to the OC reaction zone, at least a portion of the catalyst in the OC reaction zone is passed to the XTO reaction zone and at least a portion of the catalyst in the XTO reaction zone is passed to the regeneration zone; c) contacting said oxygen-containing, halogenide-containing or sulphur-containing organic feedstock in the XTO reactor with the catalyst at conditions effective to convert at least a portion of the feedstock to form a XTO reactor effluent comprising light olefins and a heavy hydrocarbon fraction; d) separating said light olefins from said heavy hydrocarbon fraction; e) contacting said heavy hydrocarbon fraction in the OC reactor with the catalyst at conditions effective to convert at least a portion of said heavy hydrocarbon fraction to light olefins.
    • 本发明涉及一种在组合的XTO-OC方法中由含氧的含卤素或含硫有机原料制备轻质烯烃的方法,包括:a)提供包含含有10个成员的沸石分子筛和 在其微孔结构中较大的通道,b)提供XTO反应区,OC反应区和催化剂再生区,所述催化剂在三个区中循环,使得至少一部分再生催化剂通过OC反应区 ,将OC反应区中的至少一部分催化剂通入XTO反应区,并将XTO反应区中的至少一部分催化剂通入再生区; c)在有效地转化至少一部分原料以形成包含轻质烯烃和重质烃部分的XTO反应器流出物的条件下,将XTO反应器中的含氧卤化物或含硫有机原料与催化剂接触 ; d)从所述重质烃馏分中分离出所述轻质烯烃; e)使OC反应器中的所述重质烃馏分与催化剂在有效将至少一部分所述重质烃馏分转化为轻质烯烃的条件下接触。
    • 4. 发明申请
    • Process to Make Olefins from Organics
    • 从有机物制造烯烃的工艺
    • US20150158784A1
    • 2015-06-11
    • US14560015
    • 2014-12-04
    • TOTAL RESEARCH & TECHNOLOGY FELUY
    • Nikolai NesterenkoWalter VermeirenGiacomo GrassoSander Van DonkWolfgang Garcia
    • C07C1/20C07C4/06
    • C07C1/20B01J21/08B01J21/16B01J27/14B01J29/18B01J29/40B01J29/65B01J29/90B01J38/12B01J2229/16B01J2229/18B01J2229/36B01J2229/37C07C1/26C07C1/322C07C4/06C07C2529/40Y02P20/584Y02P30/42C07C11/02
    • The present invention relates to a process to make light olefins, in a combined XTO-OC process, from an oxygen-containing, halogenide-containing or sulphur-containing organic feedstock comprising: a0) providing a first portion and a second portion of said oxygen-containing, halogenide-containing or sulphur-containing organic feedstock, a) providing a catalyst comprising zeolitic molecular sieves containing at least 10 membered ring pore openings or larger in their microporous structure, b) providing an XTO reaction zone, an OC reaction zone and a catalyst regeneration zone, said catalyst circulating in the three zones, such that at least a portion of the regenerated catalyst is passed to the OC reaction zone, optionally at least a portion of the catalyst in the OC reaction zone is passed to the XTO reaction zone and at least a portion of the catalyst in the XTO reaction zone is passed to the regeneration zone; c) contacting the first portion of said oxygen-containing, halogenide-containing or sulphur-containing organic feedstock in the XTO reactor with the catalyst at conditions effective to convert at least a portion of the feedstock to form a XTO reactor effluent comprising light olefins and a heavy hydrocarbon fraction; d) separating said light olefins from said heavy hydrocarbon fraction; e) contacting said heavy hydrocarbon fraction and the second portion of said oxygen-containing, halogenide-containing or sulphur-containing organic feedstock in the OC reactor with the catalyst at conditions effective to convert at least a portion of said heavy hydrocarbon fraction and oxygen-containing, halogenide-containing or sulphur-containing organic feedstock to light olefins.
    • 本发明涉及一种在组合的XTO-OC方法中由含氧,含卤素或含硫有机原料制备轻质烯烃的方法,包括:a)提供所述氧气的第一部分和第二部分 a)提供包含在其微孔结构中含有至少10元环孔或更大孔沸石分子筛的催化剂,b)提供XTO反应区,OC反应区和 催化剂再生区,所述催化剂在三个区域中循环,使得至少一部分再生催化剂通入OC反应区,任选地将OC反应区中的至少一部分催化剂通入XTO反应 区域,并且XTO反应区中的至少一部分催化剂被传送到再生区; c)在有效地转化至少一部分原料以形成包含轻质烯烃的XTO反应器流出物的条件下,将XTO反应器中的含氧卤化物或含硫有机原料的第一部分与催化剂接触, 重质烃馏分; d)从所述重质烃馏分中分离出所述轻质烯烃; e)在OC反应器中将所述重质烃部分和第二部分所述含氧卤化物或含硫有机原料与所述催化剂接触,所述条件有效地将至少一部分所述重质烃部分和氧 - 含卤素或含硫有机原料转化成轻质烯烃。
    • 5. 发明申请
    • Process to Make Olefins from Oxygenates
    • 从氧化烯制备烯烃的方法
    • US20150152020A1
    • 2015-06-04
    • US14560144
    • 2014-12-04
    • Total Research & Technology Feluy
    • Nikolai NesterenkoWalter VermeirenGiacomo GrassoSander Van DonkWolfgang Garcia
    • C07C1/20C07C4/06
    • C07C1/20B01J21/08B01J21/16B01J27/14B01J29/18B01J29/40B01J29/65B01J29/90B01J38/02B01J38/12B01J2229/16B01J2229/18B01J2229/36B01J2229/37C07C1/26C07C1/322C07C4/06C07C2529/40Y02P20/584Y02P30/42C07C11/02
    • The present invention relates to a process to make light olefins, in a combined XTO-OC process, from an oxygen-containing, halogenide-containing or sulphur-containing organic feedstock comprising:a0) providing a first portion and a second portion of said oxygen-containing, halogenide-containing or sulphur-containing organic feedstock,a) providing a catalyst comprising zeolitic molecular sieves containing at least 10 membered ring pore openings or larger in their microporous structure,b) providing an XTO reaction zone, an OC reaction zone and a catalyst regeneration zone, said catalyst circulating in the three zones, such that at least a portion of the regenerated catalyst is passed to the OC reaction zone, at least a portion of the catalyst in the OC reaction zone is passed to the XTO reaction zone and at least a portion of the catalyst in the XTO reaction zone is passed to the regeneration zone;c) contacting the first portion of said oxygen-containing, halogenide-containing or sulphur-containing organic feedstock in the XTO reactor with the catalyst at conditions effective to convert at least a portion of the feedstock to form a XTO reactor effluent comprising light olefins and a heavy hydrocarbon fraction;d) separating said light olefins from said heavy hydrocarbon fraction;e) contacting said heavy hydrocarbon fraction and the second portion of said oxygen-containing, halogenide-containing or sulphur-containing organic feedstock in the OC reactor with the catalyst at conditions effective to convert at least a portion of said heavy hydrocarbon fraction and oxygen-containing, halogenide-containing or sulphur-containing organic feedstock to light olefins.
    • 本发明涉及一种在组合的XTO-OC方法中由含氧,含卤素或含硫有机原料制备轻质烯烃的方法,包括:a)提供所述氧气的第一部分和第二部分 a)提供包含在其微孔结构中含有至少10元环孔或更大孔沸石分子筛的催化剂,b)提供XTO反应区,OC反应区和 催化剂再生区,所述催化剂在三个区域中循环,使得至少一部分再生催化剂通过OC反应区,OC反应区中的至少一部分催化剂通入XTO反应区 并且将XTO反应区中的至少一部分催化剂送入再生区; c)在有效地转化至少一部分原料以形成包含轻质烯烃的XTO反应器流出物的条件下,将XTO反应器中的含氧卤化物或含硫有机原料的第一部分与催化剂接触, 重质烃馏分; d)从所述重质烃馏分中分离出所述轻质烯烃; e)在OC反应器中将所述重质烃部分和第二部分所述含氧卤化物或含硫有机原料与所述催化剂接触,所述条件有效地将至少一部分所述重质烃部分和氧 - 含卤素或含硫有机原料转化成轻质烯烃。
    • 7. 发明授权
    • Process to make olefins from oxygenates
    • 从含氧化合物制备烯烃的方法
    • US09561990B2
    • 2017-02-07
    • US14560144
    • 2014-12-04
    • TOTAL RESEARCH & TECHNOLOGY FELUY
    • Nikolai NesterenkoWalter VermeirenGiacomo GrassoSander Van DonkWolfgang Garcia
    • C07C1/20B01J21/16B01J27/14B01J29/89B01J29/90B01J29/80B01J21/08B01J29/18B01J29/40B01J29/65B01J38/02B01J38/12C07C1/26C07C1/32C07C4/06
    • C07C1/20B01J21/08B01J21/16B01J27/14B01J29/18B01J29/40B01J29/65B01J29/90B01J38/02B01J38/12B01J2229/16B01J2229/18B01J2229/36B01J2229/37C07C1/26C07C1/322C07C4/06C07C2529/40Y02P20/584Y02P30/42C07C11/02
    • The present invention relates to a process to make light olefins, in a combined XTO-OC process, from an oxygen-containing, halogenide-containing or sulphur-containing organic feedstock comprising: a0) providing a first portion and a second portion of said oxygen-containing, halogenide-containing or sulphur-containing organic feedstock, a) providing a catalyst comprising zeolitic molecular sieves containing at least 10 membered ring pore openings or larger in their microporous structure, b) providing an XTO reaction zone, an OC reaction zone and a catalyst regeneration zone, said catalyst circulating in the three zones, such that at least a portion of the regenerated catalyst is passed to the OC reaction zone, at least a portion of the catalyst in the OC reaction zone is passed to the XTO reaction zone and at least a portion of the catalyst in the XTO reaction zone is passed to the regeneration zone; c) contacting the first portion of said oxygen-containing, halogenide-containing or sulphur-containing organic feedstock in the XTO reactor with the catalyst at conditions effective to convert at least a portion of the feedstock to form a XTO reactor effluent comprising light olefins and a heavy hydrocarbon fraction; d) separating said light olefins from said heavy hydrocarbon fraction; e) contacting said heavy hydrocarbon fraction and the second portion of said oxygen-containing, halogenide-containing or sulphur-containing organic feedstock in the OC reactor with the catalyst at conditions effective to convert at least a portion of said heavy hydrocarbon fraction and oxygen-containing, halogenide-containing or sulphur-containing organic feedstock to light olefins.
    • 本发明涉及一种在组合的XTO-OC方法中由含氧,含卤素或含硫有机原料制备轻质烯烃的方法,包括:a)提供所述氧气的第一部分和第二部分 a)提供包含在其微孔结构中含有至少10元环孔或更大孔沸石分子筛的催化剂,b)提供XTO反应区,OC反应区和 催化剂再生区,所述催化剂在三个区域中循环,使得至少一部分再生催化剂通过OC反应区,OC反应区中的至少一部分催化剂通入XTO反应区 并且将XTO反应区中的至少一部分催化剂送入再生区; c)在有效地转化至少一部分原料以形成包含轻质烯烃的XTO反应器流出物的条件下,将XTO反应器中的含氧卤化物或含硫有机原料的第一部分与催化剂接触, 重质烃馏分; d)从所述重质烃馏分中分离出所述轻质烯烃; e)在OC反应器中将所述重质烃部分和第二部分所述含氧卤化物或含硫有机原料与所述催化剂接触,所述条件有效地将至少一部分所述重质烃部分和氧 - 含卤素或含硫有机原料转化成轻质烯烃。
    • 8. 发明申请
    • PROCESS TO MAKE OLEFINS AND AROMATICS FROM ORGANICS
    • 从有机物制备油脂和芳香油的工艺
    • US20150152021A1
    • 2015-06-04
    • US14560451
    • 2014-12-04
    • TOTAL RESEARCH & TECHNOLOGY FELUY
    • Nikolai NesterenkoWalter VermeirenGiacomo GrassoSander Van DonkWolfgang Garcia
    • C07C1/20C07C4/06C07C2/86
    • C07C1/20B01J21/08B01J21/16B01J27/14B01J29/18B01J29/40B01J29/65B01J29/90B01J38/12B01J2229/16B01J2229/18B01J2229/36B01J2229/37C07C1/26C07C1/322C07C2/864C07C4/06C07C2529/40Y02P20/584Y02P30/42C07C15/02C07C11/02
    • The present invention relates to a process to make light olefins and aromatics, in a combined XTO-OC process, from an oxygen-containing, halogenide-containing or sulphur-containing organic feedstock comprising: a0) providing a first portion and a second portion of said oxygen-containing, halogenide-containing or sulphur-containing organic feedstock, a) providing a catalyst comprising zeolitic molecular sieves containing at least 10 membered ring pore openings or larger in their microporous structure, b) providing an XTO reaction zone, an OC reaction zone and a catalyst regeneration zone, said catalyst circulating in the three zones, such that at least a portion of the regenerated catalyst is passed to the 00 reaction zone, at least a portion of the catalyst in the 00 reaction zone is passed to the XTO reaction zone and at least a portion of the catalyst in the XTO reaction zone is passed to the regeneration zone; c) contacting the first portion of said oxygen-containing, halogenide-containing or sulphur-containing organic feedstock in the XTO reactor with the catalyst at conditions effective to convert at least a portion of the feedstock to form a XTO reactor effluent comprising light olefins and a heavy hydrocarbon fraction; d) separating said light olefins from said heavy hydrocarbon fraction; e) contacting said heavy hydrocarbon fraction and the second portion of said oxygen-containing, halogenide-containing or sulphur-containing organic feedstock in the OC reactor with the catalyst at conditions effective to convert at least a portion of said heavy hydrocarbon fraction and oxygen-containing, halogenide-containing or sulphur-containing organic feedstock to light olefins and aromatics.
    • 本发明涉及一种在组合的XTO-OC方法中由含氧,含卤素或含硫有机原料制备轻质烯烃和芳族化合物的方法,包括:a0)提供第一部分和第二部分 所述含氧,含卤素或含硫有机原料,a)提供包含在其微孔结构中含有至少10元环孔孔或更大的沸石分子筛的催化剂,b)提供XTO反应区,OC反应 区域和催化剂再生区,所述催化剂在三个区域中循环,使得至少一部分再生催化剂通过00反应区,将00反应区中的至少一部分催化剂传递至XTO 反应区和XTO反应区中的至少一部分催化剂通入再生区; c)在有效地转化至少一部分原料以形成包含轻质烯烃的XTO反应器流出物的条件下,将XTO反应器中的含氧卤化物或含硫有机原料的第一部分与催化剂接触, 重质烃馏分; d)从所述重质烃馏分中分离出所述轻质烯烃; e)在OC反应器中将所述重质烃部分和第二部分所述含氧卤化物或含硫有机原料与所述催化剂接触,所述条件有效地将至少一部分所述重质烃部分和氧 - 含有卤化物或含硫有机原料至轻质烯烃和芳族化合物。