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1. 发明授权

US07563357B2 Process for cracking synthetic crude oil-containing feedstock 有权
标题翻译：裂解含合成原油的原料的工艺
公开(公告)号：US07563357B2
公开(公告)日：2009-07-21
申请号：US11698514
申请日：2007-01-26
申请人： Paul F Keusenkothen , James N McCoy , James Earl Graham , Chad David Reimann
发明人： Paul F Keusenkothen , James N McCoy , James Earl Graham , Chad David Reimann
IPC分类号： C10G9/14
CPC分类号： C10G69/06 , Y10S585/921
摘要： A process for steam cracking liquid hydrocarbon feedstocks containing synthetic crude oil comprises i) hydroprocessing a wide boiling range aliquot containing a) normally liquid hydrocarbon portion substantially free of resids and b) thermally cracked hydrocarbon liquid, boiling in a range from about 600° to about 1050° F., to provide a synthetic crude oil substantially free of resids; ii) adding to the synthetic crude oil a normally liquid hydrocarbon component boiling in a range from about 100° to about 1050° F.; and iii) cracking the mixture resulting from ii) in a cracker furnace comprising a radiant coil outlet to provide a cracked effluent, wherein the cracking is carried out under conditions sufficient to effect a radiant coil outlet temperature which is greater than the optimum radiant coil outlet temperature for cracking the synthetic crude oil separately. A method for upgrading synthetic crude for use in cracking is also provided, as well as a feedstock for cracking.
摘要翻译：含有合成原油的蒸汽裂解液体烃原料的方法包括：i）加氢处理宽沸点等分试样，其含有基本上不含残渣的通常液体烃部分，和b）热裂解烃液体，沸点在约600°至约 1050°F，以提供基本上不含残渣的合成原油; ii）向合成原油中加入在约100°至约1050°F范围内沸腾的通常液体烃组分; 和iii）在包含辐射线圈出口的裂化炉中裂解由ii）产生的混合物以提供裂化流出物，其中裂化在足以实现大于最佳辐射线圈出口的辐射盘管出口温度的条件下进行分别裂解合成原油的温度。还提供了用于提高用于裂化的合成粗品的方法以及用于裂化的原料。

2. 发明授权

US09057027B2 Process for cracking synthetic crude oil-containing feedstock 有权
公开(公告)号：US09057027B2
公开(公告)日：2015-06-16
申请号：US12478998
申请日：2009-06-05
申请人： Paul F Keusenkothen , James N McCoy , James Earl Graham , Chad David Reimann
发明人： Paul F Keusenkothen , James N McCoy , James Earl Graham , Chad David Reimann
IPC分类号： C10L1/04 , C10G69/06
CPC分类号： C10G69/06 , Y10S585/921
摘要： A process for steam cracking liquid hydrocarbon feedstocks containing synthetic crude oil comprises i) hydroprocessing a wide boiling range aliquot containing a) normally liquid hydrocarbon portion substantially free of resids and b) thermally cracked hydrocarbon liquid, boiling in a range from about 600° to about 1050° F., to provide a synthetic crude oil substantially free of resids; ii) adding to the synthetic crude oil a normally liquid hydrocarbon component boiling in a range from about 100° to about 1050° F.; and iii) cracking the mixture resulting from ii) in a cracker furnace comprising a radiant coil outlet to provide a cracked effluent, wherein the cracking is carried out under conditions sufficient to effect a radiant coil outlet temperature which is greater than the optimum radiant coil outlet temperature for cracking the synthetic crude oil separately. A method for upgrading synthetic crude for use in cracking is also provided, as well as a feedstock for cracking.

3. 发明申请

US20090236264A1 Process for Cracking Synthetic Crude Oil-Containing Feedstock 有权
标题翻译：含合成原油的原料裂解工艺
公开(公告)号：US20090236264A1
公开(公告)日：2009-09-24
申请号：US12478998
申请日：2009-06-05
申请人： Paul F. Keusenkothen , James N. McCoy , James Earl Graham , Chad David Reimann
发明人： Paul F. Keusenkothen , James N. McCoy , James Earl Graham , Chad David Reimann
IPC分类号： C10L1/04
CPC分类号： C10G69/06 , Y10S585/921
摘要： A process for steam cracking liquid hydrocarbon feedstocks containing synthetic crude oil comprises i) hydroprocessing a wide boiling range aliquot containing a) normally liquid hydrocarbon portion substantially free of resids and b) thermally cracked hydrocarbon liquid, boiling in a range from about 600° to about 1050° F., to provide a synthetic crude oil substantially free of resids; ii) adding to the synthetic crude oil a normally liquid hydrocarbon component boiling in a range from about 100° to about 1050° F.; and iii) cracking the mixture resulting from ii) in a cracker furnace comprising a radiant coil outlet to provide a cracked effluent, wherein the cracking is carried out under conditions sufficient to effect a radiant coil outlet temperature which is greater than the optimum radiant coil outlet temperature for cracking the synthetic crude oil separately. A method for upgrading synthetic crude for use in cracking is also provided, as well as a feedstock for cracking.
摘要翻译：含有合成原油的蒸汽裂解液体烃原料的方法包括：i）加氢处理宽沸点等分试样，其含有基本上不含残渣的通常液体烃部分，和b）热裂化烃液体，沸点在约600°至约 1050°F，以提供基本上不含残渣的合成原油; ii）向合成原油中加入在约100°至约1050°F范围内沸腾的通常液体烃组分; 和iii）在包含辐射线圈出口的裂化炉中裂解由ii）产生的混合物以提供裂化流出物，其中裂化在足以实现大于最佳辐射线圈出口的辐射盘管出口温度的条件下进行分别裂解合成原油的温度。还提供了用于提高用于裂化的合成粗品的方法以及用于裂化的原料。

4. 发明申请

US20080179218A1 Process for cracking synthetic crude oil-containing feedstock 有权
标题翻译：裂解含合成原油的原料的工艺
公开(公告)号：US20080179218A1
公开(公告)日：2008-07-31
申请号：US11698514
申请日：2007-01-26
申请人： Paul F. Keusenkothen , James N. Mccoy , James Earl Graham , Chad David Reimann
发明人： Paul F. Keusenkothen , James N. Mccoy , James Earl Graham , Chad David Reimann
IPC分类号： C10G9/14
CPC分类号： C10G69/06 , Y10S585/921
摘要： A process for steam cracking liquid hydrocarbon feedstocks containing synthetic crude oil comprises i) hydroprocessing a wide boiling range aliquot containing a) normally liquid hydrocarbon portion substantially free of resids and b) thermally cracked hydrocarbon liquid, boiling in a range from about 600° to about 1050° F., to provide a synthetic crude oil substantially free of resids; ii) adding to the synthetic crude oil a normally liquid hydrocarbon component boiling in a range from about 100° to about 1050° F.; and iii) cracking the mixture resulting from ii) in a cracker furnace comprising a radiant coil outlet to provide a cracked effluent, wherein the cracking is carried out under conditions sufficient to effect a radiant coil outlet temperature which is greater than the optimum radiant coil outlet temperature for cracking the synthetic crude oil separately. A method for upgrading synthetic crude for use in cracking is also provided, as well as a feedstock for cracking.
摘要翻译：含有合成原油的蒸汽裂解液体烃原料的方法包括：i）加氢处理宽沸点等分试样，其含有基本上不含残渣的通常液体烃部分，和b）热裂解烃液体，沸点在约600°至约 1050°F，以提供基本上不含残渣的合成原油; ii）向合成原油中加入在约100°至约1050°F范围内沸腾的通常液体烃组分; 和iii）在包含辐射线圈出口的裂化炉中裂解由ii）产生的混合物以提供裂化流出物，其中裂化在足以实现大于最佳辐射线圈出口的辐射盘管出口温度的条件下进行分别裂解合成原油的温度。还提供了用于提高用于裂化的合成粗品的方法以及用于裂化的原料。

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