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    • 16. 发明申请
    • PROCESS FOR PREPARING BENZENE FROM METHANE
    • 从甲烷制备苄苯的方法
    • US20120165585A1
    • 2012-06-28
    • US13393837
    • 2010-08-23
    • Christian SchneiderMartin KarchesJoana Coelho TsouSebastian AhrensDieter Stuetzer
    • Christian SchneiderMartin KarchesJoana Coelho TsouSebastian AhrensDieter Stuetzer
    • C07C2/76
    • C07C2/76Y02P20/584C07C15/02
    • The present invention relates to a process for nonoxidatively dehydroaromatizing a reactant stream comprising C1-C4-aliphatics, comprising the steps of I. feeding reactant stream E into a reaction zone 1, converting reactant stream E under nonoxidative conditions in the presence of a particulate catalyst to a product stream P comprising aromatic hydrocarbons and discharging product stream P from reaction zone 1, II. transferring the catalyst with reduced activity as a result of deposited coke into a reaction zone 2, III. at least partly regenerating the catalyst with supply of a hydrogen-comprising gas stream H in a reaction zone 2, at least some of the coke deposited being converted to methane to form a methane-comprising gas stream M which is fed at least partly to reaction zone 1, IV. discharging the catalyst from reaction zone 2 and V. recycling at least a portion of the discharged catalyst into reaction zone 1, reaction zone 1 and reaction zone 2 being arranged spatially adjacent to one another in the same reactor.
    • 本发明涉及一种使含有C 1 -C 4脂族化合物的反应物流非氧化脱氢芳化的方法,其包括以下步骤:将反应物流E加入到反应区1中,在非氧化条件下在颗粒催化剂存在下转化反应物流E 涉及包含芳烃并从反应区1排出产物流P的产物流P。 由于沉积的焦炭导致反应区2,III的转移,催化剂活性降低。 在反应区2中供应含氢气流H至少部分地再生催化剂,沉积的焦炭中的至少一些转化成甲烷以形成含甲烷的气流M,其至少部分地进料至反应 区1,IV。 将催化剂从反应区2排出,并将至少一部分排出的催化剂再循环到反应区1中,反应区1和反应区2在相同的反应器中彼此空间上相邻布置。
    • 17. 发明授权
    • Process for preparing benzene from methane
    • 从甲烷制备苯的方法
    • US08796496B2
    • 2014-08-05
    • US13393837
    • 2010-08-23
    • Christian SchneiderMartin KarchesJoana Coelho TsouSebastian AhrensDieter Stuetzer
    • Christian SchneiderMartin KarchesJoana Coelho TsouSebastian AhrensDieter Stuetzer
    • C07C2/76C07C15/02
    • C07C2/76Y02P20/584C07C15/02
    • The present invention relates to a process for nonoxidatively dehydroaromatizing a reactant stream comprising C1-C4-aliphatics, comprising the steps of I. feeding reactant stream E into a reaction zone 1, converting reactant stream E under nonoxidative conditions in the presence of a particulate catalyst to a product stream P comprising aromatic hydrocarbons and discharging product stream P from reaction zone 1, II. transferring the catalyst with reduced activity as a result of deposited coke into a reaction zone 2, III. at least partly regenerating the catalyst with supply of a hydrogen-comprising gas stream H in a reaction zone 2, at least some of the coke deposited being converted to methane to form a methane-comprising gas stream M which is fed at least partly to reaction zone 1, IV. discharging the catalyst from reaction zone 2 and V. recycling at least a portion of the discharged catalyst into reaction zone 1, reaction zone 1 and reaction zone 2 being arranged spatially adjacent to one another in the same reactor.
    • 本发明涉及一种使含有C 1 -C 4脂族化合物的反应物流非氧化脱氢芳化的方法,其包括以下步骤:将反应物流E加入到反应区1中,在非氧化条件下在颗粒催化剂存在下转化反应物流E 涉及包含芳族烃并从反应区域1排出产物流P的产物流P。 由于沉积的焦炭进入反应区域2,III而导致活性降低的催化剂。 在反应区2中供应含氢气流H至少部分地再生催化剂,沉积的焦炭中的至少一些转化成甲烷以形成含甲烷的气流M,其至少部分地进料至反应 区1,IV。 从反应区2排出催化剂,并将至少一部分排出的催化剂再循环到反应区1中,反应区1和反应区2在相同的反应器中彼此空间上相邻布置。
    • 19. 发明申请
    • METHOD FOR PRODUCING TOLUYLENEDIAMINE BY HYDROGENATING DINITROTOLUENE
    • 通过加氢精氨酸生产戊烯二胺的方法
    • US20110275858A1
    • 2011-11-10
    • US13142718
    • 2009-12-21
    • Joana Coelho TsouSteffen OehlenschlaegerEkkehard SchwabWolfgang MackenrothHartwig VossStefan MaixnerSamuel NetoSven BoehmekeFrederik van Laar
    • Joana Coelho TsouSteffen OehlenschlaegerEkkehard SchwabWolfgang MackenrothHartwig VossStefan MaixnerSamuel NetoSven BoehmekeFrederik van Laar
    • C07C209/36
    • C07C209/36C07C211/50
    • A process for preparing tolylenediamine by hydrogenating dinitrotoluene with hydrogen in the presence of a suspended catalyst in a vertically upright reactor (1), at the upper end of which is arranged a motive jet nozzle (2) through which the reaction mixture drawn off from the reactor bottom, via an external loop, is sprayed into the upper region of the reactor (1) and then flows into a central inserted tube (4) which is arranged in the longitudinal direction of the reactor, flows through the latter from the top downward and flows upward again outside the inserted tube (4) in an internal loop motion, with a heat exchanger (6) in the interior of the reactor (1), through which cooling water flows, and absorbs some of the heat of reaction as it does so, with a feed for the dinitrotoluene at the upper end of the reactor (1) and a feed for the hydrogen at the lower end of the reactor (1), and wherein, in addition to the heat exchanger (6) arranged in the interior of the reactor (1), a further heat exchanger (W) is used in the external loop, in which water absorbs the rest of the heat of reaction by indirect heat exchange with the reaction mixture, which comprises utilizing the heat of reaction to raise steam with a pressure of at least 4 bar gauge by performing the hydrogenation of dinitrotoluene to tolylenediamine at a temperature of ≧180° C.
    • 一种通过在悬浮催化剂存在下用氢气将二硝基甲苯氢化在垂直直立反应器(1)中制备甲苯二胺的方法,其上端设置有动力喷嘴(2),反应混合物从其中排出 反应器底部通过外部环路喷射到反应器(1)的上部区域中,然后流入沿着反应器的纵向布置的中心插入管(4),其从顶部向下流动 并且在反应器(1)的内部具有热交换器(6),内部循环运动再次向外流过插入的管(4),冷却水通过该换热器(6)流过,并吸收一些反应热 用反应器(1)上端的二硝基甲苯进料和反应器(1)下端的氢气进料,并且其中除了设置在反应器(1)的下端的热交换器 反应器(1)的内部,一个furt 她的热交换器(W)用于外部回路中,其中水通过与反应混合物的间接热交换吸收剩余的反应热,其中包括利用反应热量以至少4的压力升高蒸汽 通过在≥180℃的温度下进行二硝基甲苯氢化成甲苯二胺来测定。