会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 25. 发明授权
    • Fouling tolerant fixed bed reactor with virtual second bed
    • 具有虚拟第二床的防污固定床反应器
    • US06689329B2
    • 2004-02-10
    • US09974561
    • 2001-10-10
    • Ramesh GuptaSalvatore Joseph Rossetti
    • Ramesh GuptaSalvatore Joseph Rossetti
    • B01J804
    • B01J8/008B01J8/025B01J8/0278B01J2208/00707C10G49/002
    • The invention is directed to a bypass device for extending the operating life of fixed bed reactors. The device may be placed within a fixed catalyst bed to partition the bed into a first top bed and a second virtual bed. The bypass device allows any fluid feedstock to bypass the first top bed of the fixed catalyst bed as it fouls and enter the second virtual bed under conditions that promote depositing any foulants contained in the bypass flow on the top surface of the second virtual bed rather than in the interstices of the second virtual bed. The invention also relates to an improved fixed bed reactor comprising the inventive bypass device and a method for extending the operating life of a fixed bed reactor that employs the inventive bypass device.
    • 本发明涉及一种用于延长固定床反应器的使用寿命的旁路装置。 该装置可以放置在固定的催化剂床内以将床分隔成第一顶床和第二虚拟床。 旁路装置允许任何流体原料绕其固定的催化剂床的第一顶层,因为它在有助于沉积在第二虚拟床的顶表面上的旁路流中的任何污染物的条件下进入第二虚拟床,而不是 在第二个虚拟床的空隙中。 本发明还涉及一种改进的固定床反应器,其包括本发明的旁路装置和用于延长采用本发明旁路装置的固定床反应器的使用寿命的方法。
    • 28. 发明授权
    • Combination cocurrent and countercurrent staged hydroprocessing with a
vapor stage
    • 组合并流和逆流分级加氢处理与蒸气阶段
    • US6153086A
    • 2000-11-28
    • US73414
    • 1998-05-06
    • Ramesh GuptaHenry JungEdward S. EllisJames J. SchorfheideLarry L. Iaccino
    • Ramesh GuptaHenry JungEdward S. EllisJames J. SchorfheideLarry L. Iaccino
    • C10G65/12C10G45/00C10G47/00C10G65/00C10G65/02C10G69/04C10G69/06
    • C10G65/12C10G65/00C10G69/04C10G69/06C10G2300/202C10G2300/207
    • A hydroprocessing process includes a cocurrent flow liquid reaction stage, a countercurrent flow liquid reaction stage and a vapor reaction stage in which feed components are catalytically hydroprocessed by reacting with hydrogen. Both liquid stages both produce a liquid and a vapor effluent, with the cocurrent stage liquid effluent the feed for the countercurrent stage and the countercurrent stage liquid effluent the hydroprocessed product liquid. Both liquid stage vapor effluents are combined and catalytically reacted with hydrogen in a vapor reaction stage, to form a hydroprocessed vapor. This vapor is cooled to condense and recover a portion of the hydroprocessed hydrocarbonaceous vapor components as additional product liquid. The uncondensed vapor is rich in hydrogen and is cleaned up if necessary, to remove contaminants, and then recycled back into the cocurrent stage as hydrogen-containing treat gas. Fresh hydrogen is introduced into the countercurrent stage and the countercurrent stage effluent contains sufficient, and preferably all of the hydrogen for the vapor stage reaction.
    • 加氢处理方法包括并流流动液体反应阶段,逆流流动反应阶段和蒸气反应阶段,其中进料组分通过与氢反应进行催化加氢处理。 两个液相都产生液体和蒸汽流出物,并流阶段液体流出物是逆流阶段的进料和逆流阶段液体流出加氢产物液体。 两个液相蒸气流出物在蒸气反应阶段中与氢组合并催化反应,形成加氢处理的蒸汽。 将该蒸气冷却以冷凝并回收一部分加氢处理的含烃蒸汽组分作为另外的产物液体。 未冷凝的蒸汽富含氢气,如果需要,将其清除,以除去污染物,然后再循环回到并流阶段作为含氢处理气体。 将新鲜氢气引入逆流阶段,逆流阶段流出物含有足够的,优选全部用于蒸气阶段反应的氢气。
    • 29. 发明授权
    • Integrated staged catalytic cracking and staged hydroprocessing process
    • 综合分级催化裂化和分段加氢处理
    • US6123830A
    • 2000-09-26
    • US222863
    • 1998-12-30
    • Ramesh GuptaEdward S. Ellis
    • Ramesh GuptaEdward S. Ellis
    • C10G69/04C10G69/02
    • C10G69/04
    • Disclosed is a catalytic cracking process that includes more than one catalytic cracking reaction step. The process integrates catalytic cracking steps with hydroprocessing in order to maximize olefins production, distillate quality and octane level of the overall cracked product. Preferably, one hydroprocessing step is included between the cat cracking reaction steps, and a portion of the hydroprocessed products, i.e., a naphtha and mid distillate fraction, is combined with cracked product for further separation and hydroprocessing. It is also preferred that the first catalytic cracking reaction step be a short contact time reaction step.
    • 公开了包括多于一个催化裂化反应步骤的催化裂化方法。 该方法将催化裂化步骤与加氢处理相结合,以使烯烃的产生最大化,馏出物质量和整个裂解产物的辛烷值达到最大。 优选地,在催化裂化反应步骤和一部分加氢处理产物(即石脑油和中间馏分馏分)之间包括一个加氢处理步骤,与裂化产物结合进一步分离和加氢处理。 还优选的是,第一催化裂化反应步骤是短接触时间反应步骤。