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1. 发明申请

US20100147672A1 TUBULAR CRACKING FURNACE 有权
标题翻译：管状破碎炉
公开(公告)号：US20100147672A1
公开(公告)日：2010-06-17
申请号：US12593216
申请日：2008-03-28
申请人： Guoqing Wang , Lijun Zhang , Zhiguo Du , Shuo Chen , Zhaobin Zhang , Cong Zhou , Xianfeng Zhou
发明人： Guoqing Wang , Lijun Zhang , Zhiguo Du , Shuo Chen , Zhaobin Zhang , Cong Zhou , Xianfeng Zhou
IPC分类号： F28F13/12 , C10G9/20 , B23P11/00
CPC分类号： F28F13/12 , C10G2400/20 , F28D2021/0059 , F28F1/40 , F28F19/00 , Y10T29/4935
摘要： This invention relates to a tubular cracking furnace, especially an ethylene cracking furnace, which comprises a convection section and a or dual radiant section(s), at least one heat transfer intensifying member arranged in at least one pass each radiant tube in said radiant section, said at least one heat transfer intensifying member comprises a first heat transfer intensifying member, which is arranged at a location between 10D and 25D upstream of the extreme point of said at least one pass radiant tube metal temperature, wherein D is the inner diameter of the radiant tube having heat transfer intensifying members. The present invention could achieve the best enhanced heat transfer result with given number of heat transfer intensifying member, by optimizing the locations of heat transfer intensifying members in the radiant tube.
摘要翻译：本发明涉及一种管状裂解炉，特别是一种乙烯裂解炉，其包括一个对流段和一个或两个辐射区，至少一个传热增强构件，其布置在至少一个通路中，每个辐射管中的每个辐射管所述至少一个传热增强构件包括第一传热增强构件，其布置在所述至少一个通过辐射管金属温度的极限点上游的10D和25D之间的位置，其中D是辐射管具有传热增强构件。通过优化辐射管中的传热增强构件的位置，本发明可以通过给定数量的传热增强构件实现最佳的增强的传热结果。

2. 发明授权

US08585890B2 Tubular cracking furnace 有权
标题翻译：管式裂解炉
公开(公告)号：US08585890B2
公开(公告)日：2013-11-19
申请号：US12593216
申请日：2008-03-28
申请人： Guoqing Wang , Lijun Zhang , Zhiguo Du , Shuo Chen , Zhaobin Zhang , Cong Zhou , Xianfeng Zhou
发明人： Guoqing Wang , Lijun Zhang , Zhiguo Du , Shuo Chen , Zhaobin Zhang , Cong Zhou , Xianfeng Zhou
IPC分类号： C10G9/14 , B01J8/00
CPC分类号： F28F13/12 , C10G2400/20 , F28D2021/0059 , F28F1/40 , F28F19/00 , Y10T29/4935
摘要： This invention relates to a tubular cracking furnace, especially an ethylene cracking furnace, which comprises a convection section and a or dual radiant section(s), at least one heat transfer intensifying member arranged in at least one pass each radiant tube in said radiant section, said at least one heat transfer intensifying member comprises a first heat transfer intensifying member, which is arranged at a location between 10D and 25D upstream of the extreme point of said at least one pass radiant tube metal temperature, wherein D is the inner diameter of the radiant tube having heat transfer intensifying members. The present invention could achieve the best enhanced heat transfer result with given number of heat transfer intensifying member, by optimizing the locations of heat transfer intensifying members in the radiant tube.
摘要翻译：本发明涉及一种管状裂解炉，特别是一种乙烯裂解炉，其包括一个对流段和一个或两个辐射区，至少一个传热增强构件，其布置在至少一个通路中，每个辐射管中的每个辐射管所述至少一个传热增强构件包括第一传热增强构件，其布置在所述至少一个通过辐射管金属温度的极限点上游的10D和25D之间的位置，其中D是辐射管具有传热增强构件。通过优化辐射管中的传热增强构件的位置，本发明可以通过给定数量的传热增强构件实现最佳的增强的传热结果。

3. 发明授权

US09024100B2 Process for producing olefins 有权
标题翻译：烯烃生产方法
公开(公告)号：US09024100B2
公开(公告)日：2015-05-05
申请号：US12669269
申请日：2008-07-18
申请人： Guoqing Wang , Zhaobin Zhang , Shuo Chen , Lijun Zhang
发明人： Guoqing Wang , Zhaobin Zhang , Shuo Chen , Lijun Zhang
IPC分类号： C07C5/327 , C07C4/02 , C10G51/02 , C10G35/09 , C10G11/05 , C10G11/18
CPC分类号： C10G35/09 , C10G11/05 , C10G11/18
摘要： The present invention discloses a process for producing olefins from petroleum saturated hydrocarbons. The process of the present invention comprises: contacting a preheated petroleum saturated hydrocarbons feedstock with a dehydrogenation catalyst in a dehydrogenation reaction zone of a reaction system to obtain a petroleum hydrocarbon stream containing unsaturated hydrocarbon compounds, in which the dehydrogenation reaction has a conversion rate of at least 20%; and contacting the obtained petroleum hydrocarbon stream containing the unsaturated hydrocarbon compounds with olefins cracking catalyst in an olefin cracking zone of the reaction system to obtain a product stream containing olefins with a reduced number of carbon atoms.
摘要翻译：本发明公开了一种从石油饱和烃生产烯烃的方法。本发明的方法包括：使预热的石油饱和烃原料与脱氢催化剂在反应体系的脱氢反应区中接触，得到含有不饱和烃化合物的石油烃流，其中脱氢反应的转化率为至少20％; 并将所得到的含有不饱和烃化合物的石油烃物流与烯烃裂化催化剂在反应体系的烯烃裂化区中接触，得到含有碳原子数减少的烯烃的产物流。

4. 发明申请

US20100274063A1 PROCESS FOR PRODUCING OLEFINS 有权
标题翻译：生产油脂的方法
公开(公告)号：US20100274063A1
公开(公告)日：2010-10-28
申请号：US12669269
申请日：2008-07-18
申请人： Guoqing Wang , Zhaobin Zhang , Shuo Chen , Lijun Zhang
发明人： Guoqing Wang , Zhaobin Zhang , Shuo Chen , Lijun Zhang
IPC分类号： C07C4/06
CPC分类号： C10G35/09 , C10G11/05 , C10G11/18
摘要： The present invention discloses a process for producing olefins from petroleum saturated hydrocarbons. The process of the present invention comprises: contacting a preheated petroleum saturated hydrocarbons feedstock with a dehydrogenation catalyst in a dehydrogenation reaction zone of a reaction system to obtain a petroleum hydrocarbon stream containing unsaturated hydrocarbon compounds, in which the dehydrogenation reaction has a conversion rate of at least 20%; and contacting the obtained petroleum hydrocarbon stream containing the unsaturated hydrocarbon compounds with olefins cracking catalyst in an olefin cracking zone of the reaction system to obtain a product stream containing olefins with a reduced number of carbon atoms.
摘要翻译：本发明公开了一种从石油饱和烃生产烯烃的方法。本发明的方法包括：使预热的石油饱和烃原料与脱氢催化剂在反应体系的脱氢反应区中接触，得到含有不饱和烃化合物的石油烃流，其中脱氢反应的转化率为至少20％; 并将所得到的含有不饱和烃化合物的石油烃物流与烯烃裂化催化剂在反应体系的烯烃裂化区中接触，得到含有碳原子数减少的烯烃的产物流。

5. 发明授权

US07135105B2 Pyrolysis furnace with new type heat supply and method of high temperature cracking using the same 有权
公开(公告)号：US07135105B2
公开(公告)日：2006-11-14
申请号：US10246473
申请日：2002-09-19
申请人： Qingquan Zeng , Guoqing Wang , Shixing Xu , Zhaobin Zhang
发明人： Qingquan Zeng , Guoqing Wang , Shixing Xu , Zhaobin Zhang
IPC分类号： C07C4/04 , F28D7/00
CPC分类号： C10G9/20
摘要： The present invention provides a pyrolysis furnace with new type heat supply and a method of high temperature cracking using the same. The present invention employs top burners and bottom burners combined heat supply; the inlet of crossover section is connected from middle-upper portion of side wall of radiant section wall; and the present invention has the feature of uniform heat supply, high effectiveness, flexible and simple operation and control, and small investment, it is suitable for cracking reaction of hydrocarbons feedstock.

6. 发明授权

US08916030B2 Ethylene cracking furnace 有权
标题翻译：乙烯裂解炉
公开(公告)号：US08916030B2
公开(公告)日：2014-12-23
申请号：US13124590
申请日：2009-10-15
申请人： Xiou He , Guoqing Wang , Changli Li , Lijun Zhang , Jinke Li , Chen Shao , Guang Li , Yuping Guo
发明人： Xiou He , Guoqing Wang , Changli Li , Lijun Zhang , Jinke Li , Chen Shao , Guang Li , Yuping Guo
IPC分类号： C10G9/14 , B01J8/00 , C07C4/02
CPC分类号： C07C4/02 , C10G2400/20
摘要： An ethylene cracking furnace comprising a high pressure steam drum (1), a convection section (2), a radiant section (3), multiple groups of radiant coils (4) arranged vertically in the firebox of radiant section, burners (5) and transfer line exchangers (6), each radiant coil comprising a first-pass tube (7), a second-pass tube (8) and a connection member (9); feedstocks being introduced into an inlet end of the first-pass tube and outflow from an outlet end of the second-pass tube, said first-pass tube (7) and said second-pass tube (8) are non-split coils, and the centerlines of the respective radiant tubes (7, 8) are within a common plane; said connection member (9) is a tridimensional structural member comprising an inlet bending tube (10), a return bending tube (11) and an outlet bending tube (12); said inlet bending tubes (10) and said outlet bending tubes (12) are arranged at two sides of the plane containing the centerlines of said first-pass tubes (7) and said second-pass tubes (8), respectively; the projections of the respective connection members (9) in a side view are the same curve line that is symmetrical, continuous and closed; the inner diameters of said radiant coils (7, 8) is varied at least once along the length of the tubes.
摘要翻译：一种乙烯裂解炉，包括高压蒸汽桶（1），对流部分（2），辐射部分（3），在辐射部分的火箱中垂直布置的多组辐射线圈（4），燃烧器（5）和传输线交换器（6），每个辐射线圈包括第一通道管（7），第二通管（8）和连接构件（9）; 原料被引入第一管的入口端并从第二通管的出口端流出，所述第一通管（7）和所述第二通管（8）是非分裂线圈，并且各辐射管（7,8）的中心线在公共平面内; 所述连接构件（9）是包括入口弯曲管（10），返回弯管（11）和出口弯管（12）的立体结构构件; 所述入口弯管（10）和出口弯管（12）分别布置在包含所述第一通管（7）和所述第二通管（8）的中心线的平面的两侧; 各连接构件（9）的侧视图的突起是对称的，连续的和闭合的相同的曲线; 所述辐射线圈（7,8）的内径沿着管的长度改变至少一次。

7. 发明授权

US07226884B2 Composite for catalytic distillation and its preparation 有权
标题翻译：复合催化蒸馏及其制备
公开(公告)号：US07226884B2
公开(公告)日：2007-06-05
申请号：US10361084
申请日：2003-02-06
申请人： Yuanyi Yang , Dongfeng Li , Wei Dai , Shuo Chen , Guoqing Wang , Lihua Liao , Jianmin Cheng , Yanlai Guo , Hui Peng
发明人： Yuanyi Yang , Dongfeng Li , Wei Dai , Shuo Chen , Guoqing Wang , Lihua Liao , Jianmin Cheng , Yanlai Guo , Hui Peng
IPC分类号： B01J29/04
CPC分类号： B01J37/0246 , B01J23/44 , B01J29/7007 , B01J37/0215 , B01J37/0225 , B01J37/0242 , B01J37/0244 , C07C5/05 , Y02P20/127 , Y02P20/52 , C07C11/06
摘要： The present invention relates to a composite for catalytic distillation, comprising a substrate material, and a modifying material and an active material, wherein said substrate material is made of porous materials, said modified material comprises at least one metal oxide, and said active material comprises an active component for a catalytic reaction. The catalytic distillation composite according to the present invention serves as both distillation packings and catalysts, and can allow catalysts to make the best of its effenciency, provide sufficient contact areas between gas and liquid phases, which facilitates mass transfer between gas and liquid phases, boosts effects in both reaction and separation and is liable for filling, removing and utilizing in industries.
摘要翻译：本发明涉及一种用于催化蒸馏的复合材料，其包括基材，以及改性材料和活性材料，其中所述基材由多孔材料制成，所述改性材料包括至少一种金属氧化物，所述活性材料包括用于催化反应的活性组分。根据本发明的催化蒸馏复合材料既用作蒸馏填料也用作催化剂，并且可以使催化剂充分发挥其效率，在气相和液相之间提供足够的接触面积，这有助于气相和液相之间的质量传递，在反应和分离过程中都会产生影响，并且可以在工业中进行填充，除去和利用。

8. 发明申请

US20070203375A1 COMPOSITE FOR CATALYTIC DISTILLATION AND ITS PREPARATION 有权
标题翻译：复合材料用于催化蒸馏及其制备
公开(公告)号：US20070203375A1
公开(公告)日：2007-08-30
申请号：US11741395
申请日：2007-04-27
申请人： Yuanyi YANG , Dongfeng Li , Wei Dai , Shuo Chen , Guoqing Wang , Lihua Liao , Jianmin Cheng , Yanlai Guo , Hui Peng
发明人： Yuanyi YANG , Dongfeng Li , Wei Dai , Shuo Chen , Guoqing Wang , Lihua Liao , Jianmin Cheng , Yanlai Guo , Hui Peng
IPC分类号： C07C5/00 , C07C2/64
CPC分类号： B01J37/0246 , B01J23/44 , B01J29/7007 , B01J37/0215 , B01J37/0225 , B01J37/0242 , B01J37/0244 , C07C5/05 , Y02P20/127 , Y02P20/52 , C07C11/06
摘要： The present invention relates to a composite for catalytic distillation, comprising a substrate material, and a modifying material and an active material, wherein said substrate material is made of porous materials, said modified material comprises at least one metal oxide, and said active material comprises an active component for a catalytic reaction. The catalytic distillation composite according to the present invention serves as both distillation packings and catalysts, and can allow catalysts to make the best of its efficiency, provide sufficient contact areas between gas and liquid phases, which facilitates mass transfer between gas and liquid phases, boosts effects in both reaction and separation and is liable for filling, removing and utilizing in industries.
摘要翻译：本发明涉及一种用于催化蒸馏的复合材料，其包括基材，以及改性材料和活性材料，其中所述基材由多孔材料制成，所述改性材料包括至少一种金属氧化物，所述活性材料包括用于催化反应的活性组分。根据本发明的催化蒸馏复合材料既用作蒸馏填料也用作催化剂，并且可以使催化剂充分发挥其效率，在气相和液相之间提供足够的接触面积，这有利于气相和液相之间的质量传递，在反应和分离过程中都会产生影响，并且可以在工业中进行填充，除去和利用。

9. 发明授权

US07642388B2 Composite for catalytic distillation and its preparation 有权
标题翻译：复合催化蒸馏及其制备
公开(公告)号：US07642388B2
公开(公告)日：2010-01-05
申请号：US11741395
申请日：2007-04-27
申请人： Yuanyi Yang , Dongfeng Li , Wei Dai , Shuo Chen , Guoqing Wang , Lihua Liao , Jianmin Cheng , Yanlai Guo , Hui Peng
发明人： Yuanyi Yang , Dongfeng Li , Wei Dai , Shuo Chen , Guoqing Wang , Lihua Liao , Jianmin Cheng , Yanlai Guo , Hui Peng
IPC分类号： C07C5/00 , B01D3/34 , B01J23/00 , B01J29/70 , C10G47/10
CPC分类号： B01J37/0246 , B01J23/44 , B01J29/7007 , B01J37/0215 , B01J37/0225 , B01J37/0242 , B01J37/0244 , C07C5/05 , Y02P20/127 , Y02P20/52 , C07C11/06
摘要： The present invention relates to a composite for catalytic distillation, comprising a substrate material, and a modifying material and an active material, wherein said substrate material is made of porous materials, said modified material comprises at least one metal oxide, and said active material comprises an active component for a catalytic reaction. The catalytic distillation composite according to the present invention serves as both distillation packings and catalysts, and can allow catalysts to make the best of its efficiency, provide sufficient contact areas between gas and liquid phases, which facilitates mass transfer between gas and liquid phases, boosts effects in both reaction and separation and is liable for filling, removing and utilizing in industries.
摘要翻译：本发明涉及一种用于催化蒸馏的复合材料，其包括基材，以及改性材料和活性材料，其中所述基材由多孔材料制成，所述改性材料包括至少一种金属氧化物，所述活性材料包括用于催化反应的活性组分。根据本发明的催化蒸馏复合材料既用作蒸馏填料也用作催化剂，并且可以使催化剂充分发挥其效率，在气相和液相之间提供足够的接触面积，这有利于气相和液相之间的质量传递，在反应和分离过程中都会产生影响，并且可以在工业中进行填充，除去和利用。

10. 发明授权

US09677133B2 Biological chip hybridization system 有权
公开(公告)号：US09677133B2
公开(公告)日：2017-06-13
申请号：US14006540
申请日：2012-02-10
申请人： Jiaming Ye , Pinhong Wang , Guoqing Wang , Liqing Duan , Kaijun Zhao , Jinxiu Zhang , Xiumei Song , Dong Wang , Huafang Gao , Wanli Xing
发明人： Jiaming Ye , Pinhong Wang , Guoqing Wang , Liqing Duan , Kaijun Zhao , Jinxiu Zhang , Xiumei Song , Dong Wang , Huafang Gao , Wanli Xing
IPC分类号： C12Q1/68 , G01N33/50 , G01N33/543 , B01L3/00 , B01L7/00 , G01N35/00
CPC分类号： C12Q1/6876 , B01L3/5027 , B01L7/52 , B01L2300/0636 , B01L2300/0816 , B01L2300/0887 , B01L2300/1822 , B01L2300/1827 , B01L2300/1844 , B01L2400/0622 , G01N33/543 , G01N2035/00158
摘要： A hybridization system is provided, which comprises a biological chip having a substrate (1) with a probe dot matrix (3) and a cover plate (2) with at least two through-holes (4), where a hybrid chamber (5) is formed between the substrate (1) and the cover plate (2), at least two fluid channels (6) are interconnected respectively with the hybrid chamber (5) by the two through-holes (4), and a fluid control device is interconnected with the fluid channels (6). The biological chip hybridization system integrates hybridizing, cleaning and drying functions, uses power provided by the fluid control device as the drive force for promoting the liquid flow for automatically reciprocation flow in the fluid channels (6) and the chamber (5) to achieve a dynamic hybridization, thus improving the hybrid efficiency and uniformity, and achieving automatic control.

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