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
    • 2. 发明申请
    • PROCESS FOR PRODUCING EPOXIDES
    • 生产环氧化物的方法
    • WO2010014898A3
    • 2010-03-25
    • PCT/US2009052399
    • 2009-07-31
    • DOW GLOBAL TECHNOLOGIES INCFAN WILLIAM WKNEUPPER CHRISTIAN DNOORMANN SASCHA NPATRASCU RENATE P
    • FAN WILLIAM WKNEUPPER CHRISTIAN DNOORMANN SASCHA NPATRASCU RENATE P
    • C07D301/26
    • C07D301/26B01D3/009Y02P20/127
    • A process for producing epoxides, the process including: (a) feeding at least one aqueous alkali and at least one halohydrin to a reactive distillation column, wherein the reactive distillation column includes a feed zone, a top zone disposed above the feed zone, and a bottom zone disposed below the feed zone; (b) concurrently in the reactive distillation column: (i) reacting at least a portion of the halohydrin with the alkali to form an epoxide; and (ii) stripping water and the epoxide from a basic aqueous residue; (c) recovering the water and the epoxide from the reactive distillation column as an overheads fraction; (d) condensing and phase separating the overheads fraction to form an organic overheads fraction including the epoxide and an aqueous overheads fraction including water; and (e) maintaining a liquid holdup per plate in the feed zone at a residence time of 10 seconds or less.
    • 一种制备环氧化物的方法,该方法包括:(a)将至少一种碱金属和至少一种卤代醇进料到反应性蒸馏塔中,其中反应蒸馏塔包括进料区,设置在进料区上方的顶部区,以及 位于进料区下方的底部区域; (b)在反应蒸馏塔中同时进行:(i)使至少一部分卤代醇与碱反应形成环氧化物; 和(ii)从碱性含水残余物中除去水和环氧化物; (c)从反应蒸馏塔中回收水和环氧化物作为塔顶馏分; (d)冷凝和相分离塔顶馏分以形成包括环氧化物和包含水的含水塔顶馏分的有机塔顶馏分; 和(e)在10秒或更短的停留时间内在进料区中保持每个板的液体滞留量。
    • 4. 发明申请
    • PROCESS FOR PRODUCING EPOXIDES
    • 生产环氧化物的方法
    • WO2010014898A9
    • 2011-03-03
    • PCT/US2009052399
    • 2009-07-31
    • DOW GLOBAL TECHNOLOGIES INCFAN WILLIAM WKNEUPPER CHRISTIAN DNOORMANN SASCHA NPATRASCU RENATE P
    • FAN WILLIAM WKNEUPPER CHRISTIAN DNOORMANN SASCHA NPATRASCU RENATE P
    • C07D301/26
    • C07D301/26B01D3/009Y02P20/127
    • A process for producing epoxides, the process including: (a) feeding at least one aqueous alkali and at least one halohydrin to a reactive distillation column, wherein the reactive distillation column includes a feed zone, a top zone disposed above the feed zone, and a bottom zone disposed below the feed zone; (b) concurrently in the reactive distillation column: (i) reacting at least a portion of the halohydrin with the alkali to form an epoxide; and (ii) stripping water and the epoxide from a basic aqueous residue; (c) recovering the water and the epoxide from the reactive distillation column as an overheads fraction; (d) condensing and phase separating the overheads fraction to form an organic overheads fraction including the epoxide and an aqueous overheads fraction including water; and (e) maintaining a liquid holdup per plate in the feed zone at a residence time of 10 seconds or less.
    • 一种制备环氧化物的方法,该方法包括:(a)将至少一种碱金属和至少一种卤代醇进料到反应性蒸馏塔中,其中反应蒸馏塔包括进料区,设置在进料区上方的顶部区,以及 位于进料区下方的底部区域; (b)在反应蒸馏塔中同时进行:(i)使至少一部分卤代醇与碱反应形成环氧化物; 和(ii)从碱性含水残余物中除去水和环氧化物; (c)从反应蒸馏塔中回收水和环氧化物作为塔顶馏分; (d)冷凝和相分离塔顶馏分以形成包括环氧化物和包含水的含水塔顶馏分的有机塔顶馏分; 和(e)在10秒或更短的停留时间内在进料区中保持每个板的液体滞留量。
    • 6. 发明申请
    • PROCESS FOR PRODUCING EPOXIDES
    • 生产环氧化物的方法
    • WO2010014898A2
    • 2010-02-04
    • PCT/US2009/052399
    • 2009-07-31
    • DOW GLOBAL TECHNOLOGIES, INC.FAN, William, W.KNEUPPER, Christian, D.NOORMANN, Sascha, N.PATRASCU, Renate, P.
    • FAN, William, W.KNEUPPER, Christian, D.NOORMANN, Sascha, N.PATRASCU, Renate, P.
    • C07D301/26
    • C07D301/26B01D3/009Y02P20/127
    • A process for producing epoxides, the process including: (a) feeding at least one aqueous alkali and at least one halohydrin to a reactive distillation column, wherein the reactive distillation column includes a feed zone, a top zone disposed above the feed zone, and a bottom zone disposed below the feed zone; (b) concurrently in the reactive distillation column: (i) reacting at least a portion of the halohydrin with the alkali to form an epoxide; and (ii) stripping water and the epoxide from a basic aqueous residue; (c) recovering the water and the epoxide from the reactive distillation column as an overheads fraction; (d) condensing and phase separating the overheads fraction to form an organic overheads fraction including the epoxide and an aqueous overheads fraction including water; and (e) maintaining a liquid holdup per plate in the feed zone at a residence time of 10 seconds or less.
    • 一种生产环氧化物的方法,所述方法包括:(a)将至少一种碱水溶液和至少一种卤代醇供入反应性蒸馏塔中,其中所述反应性蒸馏塔包含进料区,顶部 设置在进料区上方的底部区和设置在进料区下方的底部区; (b)同时在反应蒸馏塔中:(ⅰ)使至少一部分卤代醇与碱反应形成环氧化物; 和(ii)从碱性含水残余物中汽提水和环氧化物; (c)从反应蒸馏塔回收水和环氧化物作为塔顶馏分; (d)冷凝和相分离塔顶馏分以形成包括环氧化物和含水塔顶馏分的有机塔顶馏分; 和(e)在停留时间为10秒或更少时在进料区保持每个板的液体滞留量。
    • 9. 发明申请
    • PROCESS AND APPARATUS FOR PRODUCING AND PURIFYING EPICHLOROHYDRINS
    • 生产和净化二氢氯仿的方法和装置
    • WO2009108419A1
    • 2009-09-03
    • PCT/US2009/031630
    • 2009-01-22
    • DOW GLOBAL TECHNOLOGIES INC.KNEUPPER, Christian, D.BASILE, Perry, S.FAN, William, W.NOORMANN, Sascha
    • KNEUPPER, Christian, D.BASILE, Perry, S.FAN, William, W.NOORMANN, Sascha
    • C07D301/12
    • C07D301/12C07D301/32
    • A process and apparatus are disclosed for the purification of epichlorohydrin. The process includes distilling and/or fractionating a feed stream containing epichlorohydrin, dichlorohydrin(s), and one or more other substances, subjecting at least a portion of the liquid phase effluent to a dichlorohydrin dehydrochlorination process for converting residual dichlorohydrin(s) in the liquid phase effluent to epichlorohydrin, and recovering purified epichlorohydrin from the vapor phase effluent in which the distillation/fractionation pressure and/or temperature of step (1) is adjusted to retain at least 5 weight-percent epichlorohydrin in the liquid phase effluent. The apparatus for making purified epichlorohydrin includes a dehydrochlorination apparatus, a first liquid-vapor contacting apparatus, and a second liquid-vapor contacting apparatus connected to the dehydrochlorination apparatus for recycling a distillate to the dehydrochlorination apparatus. Advantages include more efficient recovery of epichlorohydrins and reduced capital investment in recovery equipment.
    • 公开了用于纯化表氯醇的方法和装置。 该方法包括蒸馏和/或分馏含有表氯醇,二氯丙醇和一种或多种其它物质的进料流,将至少一部分液相流出物进行二氯丙醇脱氯化氢处理,以将残留的二氯丙醇 液相流出物至表氯醇,并从气相流出物回收纯化的表氯醇,其中调节步骤(1)的蒸馏/分馏分压和/或温度以在液相流出物中保留至少5重量%的表氯醇。 用于制备纯化的表氯醇的装置包括脱氯化氢装置,第一液 - 蒸气接触装置和连接到脱氯化氢装置的第二液 - 蒸气接触装置,用于将馏出物再循环到脱氯化氢装置。 优点包括更有效地回收表氯醇,减少回收设备的资金投入。