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    • 1. 发明授权
    • Coker feed method and apparatus
    • 科克饲料方法和装置
    • US07736470B2
    • 2010-06-15
    • US11716634
    • 2007-03-12
    • Te-Hung ChenChristopher P. EppigTimothy M. HealyScott F. MassenzioRobert W. MosleyRutton D. Patel
    • Te-Hung ChenChristopher P. EppigTimothy M. HealyScott F. MassenzioRobert W. MosleyRutton D. Patel
    • C10B57/04
    • C10B1/04C10B31/12C10B55/00
    • Described herein are methods and mechanisms for laterally dispensing fluid to a coke drum in a predictable and maintainable manner that alleviates thermal stress. In one embodiment, the methods and mechanisms utilize a split piping system to dispense fluid through two or more inlets into a spool that is connected to a coke drum and a coke drum bottom deheader valve. A combination of block valves and clean out ports provides a more effective means to clean the lines and allows fluid to be laterally dispensed in a controllable and predictable manner. The fluid is preferably introduced to the spool in opposing directions toward a central vertical axis of the spool at equal but opposing angles ranging from minus thirty (−30) to thirty (30) degrees relative to a horizontal line laterally bisecting the spool. Alternatively, however, fluid can be introduced to the spool tangentially.
    • 这里描述了以可预测和可维护的方式将流体横向分配到焦炭鼓的方法和机构,其缓解热应力。 在一个实施例中,方法和机构利用分裂管道系统将流体通过两个或更多个入口分配到连接到焦炭鼓和焦炭鼓底部去头阀的线轴中。 阻塞阀和清洁口的组合提供了更有效的方法来清洁管线并允许流体以可控和可预测的方式横向分配。 优选地,流体相对于横向等分线轴的水平线以相反的方向相对于卷轴的中心垂直轴线以相反但相对的角度从零三十(-30)至三十(30)度的角度引导到卷轴。 但是,替代地,流体可以切向地引入到阀芯。
    • 2. 发明申请
    • Coker feed method and apparatus
    • 科克饲料方法和装置
    • US20080179165A1
    • 2008-07-31
    • US11716634
    • 2007-03-12
    • Te-Hung ChenChristopher P. EppigTimothy M. HealyScott F. MassenzioRobert W. MosleyRutton D. Patel
    • Te-Hung ChenChristopher P. EppigTimothy M. HealyScott F. MassenzioRobert W. MosleyRutton D. Patel
    • B01D1/00
    • C10B1/04C10B31/12C10B55/00
    • Described herein are methods and mechanisms for laterally dispensing fluid to a coke drum in a predictable and maintainable manner that alleviates thermal stress. In one embodiment, the methods and mechanisms utilize a split piping system to dispense fluid through two or more inlets into a spool that is connected to a coke drum and a coke drum bottom deheader valve. A combination of block valves and clean out ports provides a more effective means to clean the lines and allows fluid to be laterally dispensed in a controllable and predictable manner. The fluid is preferably introduced to the spool in opposing directions toward a central vertical axis of the spool at equal but opposing angles ranging from minus thirty (−30) to thirty (30) degrees relative to a horizontal line laterally bisecting the spool. Alternatively, however, fluid can be introduced to the spool tangentially.
    • 这里描述了以可预测和可维护的方式将流体横向分配到焦炭鼓的方法和机构,其缓解热应力。 在一个实施例中,方法和机构利用分裂管道系统将流体通过两个或更多个入口分配到连接到焦炭鼓和焦炭鼓底部去头阀的线轴中。 阻塞阀和清洁口的组合提供了更有效的方法来清洁管线并允许流体以可控和可预测的方式横向分配。 优选地,流体相对于横向等分线轴的水平线以相反的方向相对于卷轴的中心垂直轴线以相反但相对的角度从零三十(-30)至三十(30)度的角度引导到卷轴。 但是,替代地,流体可以切向地引入到阀芯。
    • 6. 发明授权
    • Process for upgrading hydrocarbonaceous materials
    • 烃类材料升级工艺
    • US5318697A
    • 1994-06-07
    • US947378
    • 1992-09-18
    • Stephen C. PaspekJeffrey B. HauserChristopher P. EppigHarry A. Adams
    • Stephen C. PaspekJeffrey B. HauserChristopher P. EppigHarry A. Adams
    • C10G9/00C10G9/26C10G9/42
    • C10G9/00
    • This invention relates to a process for upgrading a hydrocarbonaceous material to a product having a lower boiling point than the initial boiling point of said hydrocarbonaceous material and/or a higher boiling point than the final boiling point of said hydrocarbonaceous material, the process comprising heating a feed composition comprising said hydrocarbonaceous material in an enclosed space in the absence of externally supplied water or hydrogen at a temperature in the range of about 750.degree. F. to about 1300.degree. F. and a pressure sufficient to maintain the specific gravity of the contents of said enclosed space in the range of about 0.05 to about 1.5 for an effective period of time to yield said product, said feed composition being characterized by the absence of aromatic compounds with boiling points at atmospheric pressure below about 350.degree. F.
    • 本发明涉及一种将含烃材料升级成沸点低于所述含烃材料的起始沸点的产物和/或比所述含烃材料的最终沸点高的沸点的方法,该方法包括加热 在不存在外部供应的水或氢的情况下,在约750°F至约1300°F的温度范围内将包含所述含烃材料的进料组合物包含在封闭空间中,并且具有足以保持内含物的比重的压力 所述封闭空间在约0.05至约1.5的范围内有效的时间以产生所述产物,所述进料组合物的特征在于不存在沸点在大气压下低于约350°F的芳族化合物。
    • 7. 发明授权
    • Process for making light hydrocarbonaceous liquids in a delayed coker
    • 在延迟焦化炉中制造轻质含烃液体的方法
    • US5316655A
    • 1994-05-31
    • US792016
    • 1991-11-13
    • Stephen C. PaspekChristopher P. EppigJeffrey B. HauserCarl Polisena
    • Stephen C. PaspekChristopher P. EppigJeffrey B. HauserCarl Polisena
    • C10B57/04C10G9/00C10G50/00C10G51/02C10G9/26
    • C10G9/00C10G50/00C10G51/023C10G9/005
    • A process for making a light hydrocarbonaceous liquid in a delayed coker comprising:(A) providing a hydrocarbonaceous feed to the coke drum and heating the feed to a temperature of about 800.degree. F. to about 1200.degree. F. to provide an intermediate product; and(B) introducing said intermediate product into the coke drum, operating the coke drum to convert the intermediate product to a final comprising light liquid and coke, and separating the light liquid from the coke;step (A) being conducted in combination with either step (A) (i) or step (A) (ii);Step (A) (i) comprising maintaining the feed during step (A) in an enclosed space and subjecting the feed to a pressure that is at least about 500 psig and is sufficient to maintain the specific gravity of the contents of the enclosed space at least about 0.05 to convert said feed to said intermediate product, the intermediate product containing fractions having a lower boiling point than the initial boiling point of the feed and/or a higher boiling point than the final boiling point of the feed, then reducing the pressure on the intermediate product below about 500 psig prior to step (B);step (A) (ii) comprising contacting the intermediate product from step (A) prior to and/or during step (B) with at least one preheated stripping gas and dissolving at least part of the intermediate product in the stripping gas.
    • 一种在延迟焦化器中制造轻质含烃液体的方法,包括:(A)向焦炭鼓提供烃质进料并将进料加热至约800°F至约1200°F的温度以提供中间产物; 和(B)将所述中间产物引入焦炭鼓中,操作焦炭鼓以将中间产物转化成包含轻质液体和焦炭的最终产物,并将轻质液体与焦炭分离; 步骤(A)与步骤(A)(i)或步骤(A)(ii)组合进行; 步骤(A)(i)(i)包括在步骤(A)期间将进料保持在封闭空间中,并使进料经受至少约500psig的压力并足以将封闭空间的内容物的比重维持在 至少约0.05以将所述进料转化成所述中间产物,所述中间产物含有比所述进料的初始沸点低的沸点和/或比所述进料的最终沸点高的沸点,然后降低所述压力 在步骤(B)之前约500psig下的中间产物; 步骤(A)(ii)包括在步骤(B)之前和/或步骤(B)期间使来自步骤(A)的中间产物与至少一个预热的汽提气体接触并将至少部分中间产物溶解在汽提气体中。