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1. 发明授权

US08685232B2 Fluid catalytic cracking (FCC) process for manufacturing propylene and ethylene in increased yield 有权
标题翻译：用于制备丙烯和乙烯的流化催化裂化（FCC）方法，其产率增加
公开(公告)号：US08685232B2
公开(公告)日：2014-04-01
申请号：US13133759
申请日：2009-12-08
申请人： Sukumar Mandal , Asit Kumar Das , Ashwani Yadav , Manoj Yadav , Akhilesh Bhatnagar , Rajeshwar Dongara , Veera Venkata Satya Bhaskara Sita Rama Murthy Katravulapalli
发明人： Sukumar Mandal , Asit Kumar Das , Ashwani Yadav , Manoj Yadav , Akhilesh Bhatnagar , Rajeshwar Dongara , Veera Venkata Satya Bhaskara Sita Rama Murthy Katravulapalli
IPC分类号： C10G11/18 , C10G11/00 , C07C4/06 , C07C4/02
CPC分类号： C10G11/18 , C10G11/05 , C10G2400/20
摘要： Manufacture of propylene and ethylene in a FCC unit. Each FCC riser comprises an acceleration zone, a lift stream feed nozzle, a main hydrocarbon stock feed nozzle, and an olefinic naphtha feed nozzle. Mixed FCC catalyst comprising at least 2 percent by weight pentasil zeolite and at least 10 percent by weight Y-zeolite is injected at the bottom of each FCC riser. Olefinic naptha is injected through the olefinic feed nozzle, main hydrocarbon stock is injected through the main hydrocarbon stock feed nozzle and lift stream is injected through the lift stream feed nozzle. Lift stream comprises olefinic C4 hydrocarbon stream and optionally steam and/or a fuel gas. Olefinic C4 hydrocarbon steam is cracked in the acceleration zone at 600 to 800° C., 0.8 to 5 kg/cm2 (gauge) pressure, WHSV 0.2 to 100 hr up 1 and vapour residence time 0.2 to 5 seconds.
摘要翻译：在FCC装置中制造丙烯和乙烯。每个FCC提升管包括加速区，提升流进料喷嘴，主烃原料喷嘴和烯烃石脑油进料喷嘴。包含至少2重量百分比的pentasil沸石和至少10重量％Y-沸石的混合FCC催化剂注入每个FCC提升管的底部。通过烯烃进料喷嘴注入含油棕榈蜡，主要烃类原料通过主要烃类原料进料喷嘴注入，提升料流通过提升料流进料喷嘴注入。提升料流包括烯烃C 4烃料流和任选的蒸汽和/或燃料气体。烯烃C4烃蒸汽在600至800℃，0.8至5kg / cm2（表压）压力，WHSV 0.2至100小时升高1和蒸汽停留时间0.2至5秒的加速区域中开裂。

2. 发明申请

US20130313159A1 PROCESS FOR IMPROVING AROMATICITY OF HEAVY AROMATIC HYDROCARBONS 审中-公开
标题翻译：改善重质芳烃的芳香性的方法
公开(公告)号：US20130313159A1
公开(公告)日：2013-11-28
申请号：US13983968
申请日：2012-02-10
申请人： Mahesh Marve , Suyog Salgarkar , Manthan Malvankar , Amit Parekh , Vinod Rayan , Ashwani Yadav , Harender Bisht , Manoj Yadav , Sukumar Mandal , Asit Das
发明人： Mahesh Marve , Suyog Salgarkar , Manthan Malvankar , Amit Parekh , Vinod Rayan , Ashwani Yadav , Harender Bisht , Manoj Yadav , Sukumar Mandal , Asit Das
IPC分类号： C10G21/16 , C10G21/14
CPC分类号： C10G21/16 , C10G21/14 , C10G73/10 , C10G73/12 , C10G2300/1096 , C10G2300/44 , C10G2400/30
摘要： A process for producing paraffin extracted clarified slurry oil (raffinate) with improved aromaticity from the feed stock such as clarified slurry oil (CSO) is provided. The obtained paraffin extracted clarified slurry oil with improved aromaticity is suitable for a variety of industrial applications. For example, it can be used as a valuable feedstock for producing carbon black.
摘要翻译：提供了一种从原料如澄清浆料油（CSO）生产具有改进的芳香性的石蜡提取澄清浆料油（萃余液）的方法。所得石蜡提取澄清浆料油具有改善的芳香度，适用于各种工业应用。例如，它可以用作生产炭黑的有价值的原料。

3. 发明申请

US20120172649A1 PROCESS FOR RECOVERY OF PROPYLENE AND LPG FROM FCC FUEL GAS USING STRIPPED MAIN COLUMN OVERHEAD DISTILLATE AS ABSORBER OIL 有权
标题翻译：从FCC燃料气中回收丙烯和液化石油气的方法使用分散的主塔作为吸油剂
公开(公告)号：US20120172649A1
公开(公告)日：2012-07-05
申请号：US13380928
申请日：2010-06-09
申请人： Manoj Yadav , Sukumar Mandal , Asit Kumar Das , Yogesh Gupta , Minaz Makhania , Gobind Tulsi , Shailendra Arora , Shubhangi Jaguste
发明人： Manoj Yadav , Sukumar Mandal , Asit Kumar Das , Yogesh Gupta , Minaz Makhania , Gobind Tulsi , Shailendra Arora , Shubhangi Jaguste
IPC分类号： C07C7/11
CPC分类号： C10G53/08 , C10G5/04 , C10G5/06 , C10G7/02 , C10G11/18 , C10G31/06 , C10G55/06 , C10G70/06 , C10G2300/301 , C10G2400/20 , C10G2400/26 , C10G2400/28
摘要： A process is disclosed for enhanced recovery of propylene and LPG from the fuel gas produced in Fluid catalytic cracking unit by contacting a heavier hydrocarbon feed with FCC catalyst. In the conventional process, the product mixture from FCC main column overhead comprising naphtha, LPG and fuel gas, are first condensed and gravity separated to produce unstabilized naphtha, which is subsequently used in the absorber to absorb propylene and LPG from fuel gas. However, the recovery of propylene beyond 97 wt % is difficult in this process since unstabilized naphtha already contains propylene of 5 mol % or above. In the present invention, C4 and lighter components from unstabilized naphtha are first stripped off in a separate column to obtain a liquid fraction almost free from propylene (
摘要翻译：公开了一种通过使较重的烃进料与FCC催化剂接触，从流化催化裂化装置产生的燃料气体中提高丙烯和LPG的回收率的方法。在常规方法中，首先将来自包含石脑油，液化石油气和燃料气体的FCC主塔架塔的产物混合物冷凝并重力分离以产生不稳定的石脑油，其随后用于吸收器以从燃料气体中吸收丙烯和LPG。然而，在该方法中丙烯的回收率超过97wt％是困难的，因为未稳定的石脑油已经含有5mol％或更高的丙烯。在本发明中，C4和来自不稳定石脑油的较轻组分首先在分开的塔中汽提，得到几乎不含丙烯（<0.1mol％）和其它LPG组分的液体组分。在吸收器中使用这种汽提的液体馏分，在冷却至20℃至30℃之后，从燃料气体中吸收较高量的丙烯和LPG，导致丙烯的回收率提高。

4. 发明授权

US08618344B2 Process for recovery of propylene and LPG from FCC fuel gas using stripped main column overhead distillate as absorber oil 有权
标题翻译：使用汽提主塔顶馏出物作为吸收剂油从FCC燃料气中回收丙烯和LPG的方法
公开(公告)号：US08618344B2
公开(公告)日：2013-12-31
申请号：US13380928
申请日：2010-06-09
申请人： Manoj Yadav , Sukumar Mandal , Asit Kumar Das , Yogesh Gupta , Minaz Makhania , Gobind Tulsi , Shailendra Arora , Shubhangi Jaguste
发明人： Manoj Yadav , Sukumar Mandal , Asit Kumar Das , Yogesh Gupta , Minaz Makhania , Gobind Tulsi , Shailendra Arora , Shubhangi Jaguste
IPC分类号： C07C7/04
CPC分类号： C10G53/08 , C10G5/04 , C10G5/06 , C10G7/02 , C10G11/18 , C10G31/06 , C10G55/06 , C10G70/06 , C10G2300/301 , C10G2400/20 , C10G2400/26 , C10G2400/28
摘要： A process is disclosed for enhanced recovery of propylene and LPG from the fuel gas produced in Fluid catalytic cracking unit by contacting a heavier hydrocarbon feed with FCC catalyst. In the conventional process, the product mixture from FCC main column overhead comprising naphtha, LPG and fuel gas, are first condensed and gravity separated to produce unstabilized naphtha, which is subsequently used in the absorber to absorb propylene and LPG from fuel gas. However, the recovery of propylene beyond 97 wt % is difficult in this process since unstabilized naphtha already contains propylene of 5 mol % or above. In the present invention, C4 and lighter components from unstabilized naphtha are first stripped off in a separate column to obtain a liquid fraction almost free from propylene (
摘要翻译：公开了一种通过使较重的烃进料与FCC催化剂接触，从流化催化裂化装置产生的燃料气体中提高丙烯和LPG的回收率的方法。在常规方法中，首先将来自包含石脑油，液化石油气和燃料气体的FCC主塔架塔的产物混合物冷凝并重力分离以产生不稳定的石脑油，其随后用于吸收器以从燃料气体中吸收丙烯和LPG。然而，在该方法中丙烯的回收率超过97wt％是困难的，因为未稳定的石脑油已经含有5mol％或更高的丙烯。在本发明中，C4和来自不稳定石脑油的较轻组分首先在分开的塔中汽提，得到几乎不含丙烯（<0.1mol％）和其它LPG组分的液体组分。在吸收器中使用这种汽提的液体馏分，在冷却至20℃至30℃之后，从燃料气体中吸收较高量的丙烯和LPG，导致丙烯的回收率提高。

5. 发明授权

US08451035B2 Synthesizable DLL on system-on-chip 有权
标题翻译：片上系统上的合成DLL
公开(公告)号：US08451035B2
公开(公告)日：2013-05-28
申请号：US12969220
申请日：2010-12-15
申请人： Prateek Sikka , Rajesh Chopra , Manoj Yadav
发明人： Prateek Sikka , Rajesh Chopra , Manoj Yadav
IPC分类号： H03L7/06
CPC分类号： H03K5/135 , G06F17/5045
摘要： The present disclosure provides an emulator mapping process on a system-on-a-chip (SoC) for debugging. The implementation reduces manual intervention and makes the emulation mapping process very generic and technology independent and hence it reduces overall project cycle time. In the present disclosure, the SoCs containing analog delay locked loops are made suitable for emulation by configuring analog delay locked loop module in parallel with a synthesizable delay logic module. Further, selection logic is provided to select any one of the module at a time.
摘要翻译：本公开提供了用于调试的片上系统（SoC）上的仿真器映射过程。该实现减少了手动干预，并使仿真映射过程非常通用和独立于技术，从而减少了整个项目周期的时间。在本公开中，通过与可合成的延迟逻辑模块并联配置模拟延迟锁定环模块，包含模拟延迟锁定环路的SoC适于仿真。此外，提供选择逻辑以一次选择模块中的任何一个。

6. 发明申请

US20110240523A1 FLUID CATALYTIC CRACKING (FCC) PROCESS FOR MANUFACTURING PROPYLENE AND ETHYLENE IN INCREASED YIELD 有权
标题翻译：流化床催化裂化（FCC）在增加乙烯和乙烯中制备丙烯和乙烯的方法
公开(公告)号：US20110240523A1
公开(公告)日：2011-10-06
申请号：US13133759
申请日：2009-12-08
申请人： Sukumar Mandal , Asit Kumar Das , Ashwani Yadav , Manoj Yadav , Akhilesh Bhatnagar , Rajeshwar Dongara , Veera Venkata satya Bhaskara sita Rama Murthy Katravulapalli
发明人： Sukumar Mandal , Asit Kumar Das , Ashwani Yadav , Manoj Yadav , Akhilesh Bhatnagar , Rajeshwar Dongara , Veera Venkata satya Bhaskara sita Rama Murthy Katravulapalli
IPC分类号： C10G11/04
CPC分类号： C10G11/18 , C10G11/05 , C10G2400/20
摘要： A fluid catalytic cracking (FCC) process for manufacturing propylene and ethylene in increased yield. The process comprises cracking an olefinic naphtha stream and main hydrocarbon stock in combination with an olefinic C4 hydrocarbon stream in different zones of one or more risers of an FCC unit. Each FCC riser comprises an acceleration zone at the lower portion thereof, a lift stream feed nozzle at the bottom of the acceleration zone, a main hydrocarbon stock feed nozzle above the acceleration zone and an olefinic naphtha feed nozzle at a location along the acceleration zone between the lift stream feed nozzle and main hydrocarbon stock feed nozzle. The cracking is carried out on a mixed FCC catalyst comprising at least 2 percent by weight pentasil zeolite and at least 10 percent by weight Y-zeolite. The catalyst is injected at the bottom of each FCC riser, the olefinic naptha is injected through the olefinic feed nozzle, the main hydrocarbon stock is injected through the main hydrocarbon stock feed nozzle and the lift stream is injected through the lift stream feed nozzle at the bottom of the acceleration zone. The lift stream comprises the olefinic C4 hydrocarbon stream with or without steam and/or a fuel gas. The olefinic C4 hydrocarbon steam is cracked in the acceleration zone at 600 to 8000° C. and pressure of 0.8 to 5 kg/cm up 2 (gauge) and weight hourly space velocity (WHSV) of 0.2 to 100 hr up 1 and vapour residence time of 0.2 to 5 seconds.
摘要翻译：用于以增加的产率制造丙烯和乙烯的流化催化裂化（FCC）方法。该方法包括在FCC单元的一个或多个立管的不同区域中与烯属烃石脑油流和主要烃类物料一起裂化。每个FCC提升管包括其下部的加速区，加速区底部的升力流进料喷嘴，加速区上方的主烃储料供给喷嘴和沿加速区的位置处的烯烃石脑油进料喷嘴，升降机进料喷嘴和主油料进料喷嘴。裂化在包含至少2重量百分比的pentasil沸石和至少10重量％Y-沸石的混合FCC催化剂上进行。在每个FCC提升管的底部注入催化剂，通过烯烃进料喷嘴注入烯烃萘，主要烃类原料通过主要烃类原料进料喷嘴注入，提升流通过提升料流进料喷嘴注入底部的加速区。提升流包括具有或不具有蒸汽和/或燃料气体的烯烃C4烃流。烯烃C4烃蒸汽在600-8000℃的加速区裂化，压力为0.8-5kg / cm 2（表压），重时空速（WHSV）为0.2〜100小时-1，蒸汽停留时间为0.2〜5秒。

7. 发明申请

US20110140748A1 SYNTHESIZABLE DLL ON SYSTEM-ON-CHIP 有权
标题翻译：系统在片上的合成DLL
公开(公告)号：US20110140748A1
公开(公告)日：2011-06-16
申请号：US12969220
申请日：2010-12-15
申请人： Prateek Sikka , Rajesh Chopra , Manoj Yadav
发明人： Prateek Sikka , Rajesh Chopra , Manoj Yadav
IPC分类号： H03L7/06
CPC分类号： H03K5/135 , G06F17/5045
摘要： The present disclosure provides an emulator mapping process on a system-on-a-chip (SoC) for debugging. The implementation reduces manual intervention and makes the emulation mapping process very generic and technology independent and hence it reduces overall project cycle time. In the present disclosure, the SoCs containing analog delay locked loops are made suitable for emulation by configuring analog delay locked loop module in parallel with a synthesizable delay logic module. Further, selection logic is provided to select any one of the module at a time.
摘要翻译：本公开提供了用于调试的片上系统（SoC）上的仿真器映射过程。该实现减少了手动干预，并使仿真映射过程非常通用和独立于技术，从而减少了整个项目周期的时间。在本公开中，通过与可合成的延迟逻辑模块并联配置模拟延迟锁定环模块，包含模拟延迟锁定环路的SoC适于仿真。此外，提供选择逻辑以一次选择模块中的任何一个。

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