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    SYSTEM AND METHOD FOR HYDROGENATING AROMATIC COMPOUND
    42.
    发明申请
    SYSTEM AND METHOD FOR HYDROGENATING AROMATIC COMPOUND 审中-公开
    用于氢化芳族化合物的方法和系统

    公开(公告)号：US20170057890A1

    公开(公告)日：2017-03-02

    申请号：US15119805

    申请日：2015-02-20

    Applicant: CHIYODA CORPORATION

    Inventor： Hironori Kawai ,  Masato Shiraga ,  Kenichi Imagawa ,  Tatsuo Ishiyama

    IPC: C07C5/10 ,  C07C1/04 ,  C01B3/38

    CPC classification number: C07C5/10 ,  B01J8/0285 ,  B01J8/067 ,  B01J2208/00168 ,  B01J2208/00274 ,  C01B3/38 ,  C01B2203/0233 ,  C01B2203/0244 ,  C01B2203/025 ,  C01B2203/0288 ,  C01B2203/0445 ,  C01B2203/1058 ,  C01B2203/1241 ,  C01B2203/148 ,  C07C1/0485 ,  C07C2521/04 ,  C07C2521/08 ,  C07C2521/12 ,  C07C2523/42 ,  C07C2523/44 ,  C07C2523/755 ,  C07C2601/14 ,  C07C2601/16 ,  C07C2602/10 ,  C07C2603/24 ,  C10G45/44 ,  C07C13/18

    Abstract: In a system for hydrogenation of an aromatic compound, an excessive temperature rise in the hydrogenation reaction unit is prevented, and the amount of the dilution gas to be circulated is minimized. The hydrogenation system (1) comprises a hydrogenation reaction unit (2) for producing a hydrogenated aromatic compound by adding hydrogen to an aromatic compound via a hydrogenation reaction, a separation unit (3) for separating the hydrogenated aromatic compound from a product of the hydrogenation reaction unit, and a transportation unit (4) for circulating at least a part of a residual component remaining in the separation unit after separating the hydrogenated aromatic compound therefrom to the hydrogenation reaction unit. The hydrogen supplied to the hydrogenation reaction unit consists of diluted hydrogen (L2) diluted by a dilution compound having a higher molar specific heat than nitrogen, and the dilution compound includes a component circulated to the hydrogenation reaction unit as the residual component.

    Abstract translation: 在芳香族化合物的氢化体系中，防止了氢化反应单元的过度升温，使循环用稀释气体的量最小化。 氢化体系（1）包括氢化反应单元（2），用于通过氢化反应向芳族化合物中加入氢气生成氢化芳族化合物;分离单元（3），用于将氢化芳族化合物与氢化产物分离 反应单元和输送单元（4），用于在将氢化芳族化合物从氢化反应单元中分离出之后使残留在分离单元中的剩余成分的至少一部分循环。 提供给氢化反应单元的氢由稀释化合物稀释的稀氢（L2）组成，其稀释化合物的摩尔比热比氮更高，稀释化合物包括作为残留组分循环到氢化反应单元的组分。

    METHOD TO OBTAIN METHYLENE MALONATE VIA BIS(HYDROXYMETHYL) MALONATE PATHWAY
    43.
    发明申请
    METHOD TO OBTAIN METHYLENE MALONATE VIA BIS(HYDROXYMETHYL) MALONATE PATHWAY 审中-公开
    通过双（羟甲基）马来酸酐路线获得亚甲基马来酸盐的方法

    公开(公告)号：US20170050167A1

    公开(公告)日：2017-02-23

    申请号：US15345976

    申请日：2016-11-08

    Applicant: SIRRUS, INC.

    Inventor： Bernard Miles Malofsky ,  Adam Gregg Malofsky ,  Jeffrey M. Sullivan ,  Philip B. Kisanga ,  John Joseph Anderson ,  Michael Charles Milner Cockrem ,  Philip Jay Carlberg

    IPC: B01J19/24 ,  B01J29/40 ,  B01J8/06

    CPC classification number: B01J19/245 ,  B01J8/067 ,  B01J29/40 ,  B01J2208/00168 ,  B01J2208/065 ,  B01J2219/00033 ,  B01J2219/0004 ,  B01J2219/00087 ,  B01J2219/00177 ,  B01J2219/24 ,  C07C67/31 ,  C07C67/327 ,  C07C67/333 ,  C07C67/56 ,  C07C69/593 ,  C08F222/14 ,  C09D4/00 ,  C09J4/00

    Abstract: Method to obtain methylene malonate and related monomers following a bis(hydroxymethyl) malonate pathway. A bis(hydroxymethyl) malonate intermediary is subsequently reacted (i.e., subjected to thermolysis) to provide a methylene malonate monomer species. A source of formaldehyde (e.g., formalin) is provided in the presence of a basic catalyst (e.g., calcium hydroxide), to which a malonate (e.g., diethyl malonate) is added under suitable reaction conditions to obtain the desired intermediary (e.g., dialkyl bis(hydroxymethyl) malonate). The intermediary is reacted (i.e., subjected to thermolysis) under suitable conditions in the presence of a suitable catalyst (e.g., a zeolite) to obtain a methylene malonate monomer. In an exemplary embodiment, the thermolysis reaction includes the addition of the bis(hydroxymethyl) malonate intermediary onto a heated catalyst. The reaction product is collected and purified. The disclosed methods may be performed in a continuous operation. Discrete steps may be performed by using modular units within a plant.

    Abstract translation: 获得二（羟甲基）丙二酸酯途径后亚甲基丙二酸酯和相关单体的方法。 随后将双（羟甲基）丙二酸酯中间体反应（即进行热解）以提供亚甲基丙二酸酯单体种类。 在碱性催化剂（如氢氧化钙）的存在下提供甲醛源（如福尔马林），在合适的反应条件下加入丙二酸酯（如丙二酸二乙酯），得到所需的中间体（如二烷基 双（羟甲基）丙二酸酯）。 在合适的条件下，在合适的催化剂（例如沸石）的存在下，使中间体反应（即进行热解），得到亚甲基丙二酸酯单体。 在一个示例性实施方案中，热解反应包括在加热的催化剂上加入双（羟甲基）丙二酸酯中间体。 收集并纯化反应产物。 所公开的方法可以在连续操作中执行。 离散步骤可以通过使用工厂内的模块化单元来执行。

    METHOD AND SYNTHESIS REACTOR FOR PRODUCING CARBON NANOTUBES
    45.
    发明申请
    METHOD AND SYNTHESIS REACTOR FOR PRODUCING CARBON NANOTUBES 审中-公开
    用于生产碳纳米管的方法和合成反应器

    公开(公告)号：US20160152476A1

    公开(公告)日：2016-06-02

    申请号：US15012806

    申请日：2016-02-01

    Applicant: SHANDONG DAZHAN NANOMATERIALS CO., LTD.

    Inventor： Yan LI

    IPC: C01B31/02 ,  B01J8/18 ,  B01J8/24

    CPC classification number: C01B32/162 ,  B01J8/0025 ,  B01J8/003 ,  B01J8/007 ,  B01J8/1863 ,  B01J8/228 ,  B01J23/745 ,  B01J2208/00168 ,  B01J2208/00752 ,  C01B32/16

    Abstract: A synthesis reactor for producing carbon nanotubes. The reactor includes a main reactor, a feeder, a settler, an air inlet device, and a product outlet. The main reactor communicates with the settler in the form of a communicating vessel. The feeder communicates with the settler via a catalyst inlet. The air inlet device is disposed under the settler. The wall of the main reactor is provided with a heat exchanger. The product outlet is disposed at the lower part of the main reactor. A method for producing a carbon nanotube, includes: 1) drying red mud for 1 to 4 hour(s) at the temperature of between 101° C. and 109° C.; 2) smashing and sieving the red mud through a 200-mesh sieve to yield a catalyst; and 3) adding the catalyst to a synthesis reactor.

    Abstract translation: 一种用于生产碳纳米管的合成反应器。 反应器包括主反应器，进料器，沉降器，进气装置和产品出口。 主反应器以连通容器的形式与沉降器连通。 进料器通过催化剂入口与沉降器连通。 进气装置设置在沉降器下方。 主反应器的壁设有热交换器。 产品出口设置在主反应器的下部。 碳纳米管的制造方法包括：1）在101℃〜109℃的温度下干燥红泥1〜4小时。 2）通过200目筛粉碎和筛分红泥，得到催化剂; 和3）将催化剂加入到合成反应器中。

    REACTOR AND PROCESS FOR PARAFFIN DEHYDROGENATION TO OLEFINS
    47.
    发明申请
    REACTOR AND PROCESS FOR PARAFFIN DEHYDROGENATION TO OLEFINS 审中-公开
    对于烯烃脱氢的反应器和方法

    公开(公告)号：US20160068454A1

    公开(公告)日：2016-03-10

    申请号：US14783005

    申请日：2014-04-04

    Applicant: SAUDI BASIC INDUSTRIES CORPORATION

    Inventor： Zeeshan Nawaz ,  Faisal Baksh

    IPC: C07C5/333 ,  B01J8/24 ,  B01J8/18 ,  B01J8/26

    CPC classification number: C07C5/3337 ,  B01J8/0055 ,  B01J8/1836 ,  B01J8/24 ,  B01J8/26 ,  B01J23/92 ,  B01J23/96 ,  B01J38/02 ,  B01J38/30 ,  B01J2208/00168 ,  B01J2208/00203 ,  C07C5/3335 ,  C07C5/48 ,  C07C2521/04 ,  C07C2523/26 ,  C07C2523/42 ,  C10G11/05 ,  C10G11/182 ,  C10G2300/1081 ,  C10G2400/20 ,  Y02P20/584 ,  C07C11/02

    Abstract: Disclosed herein is a method and apparatus for dehydrogenation of a paraffin comprising: providing a dehydrogenation reactor comprising an integrated fluidized bed reactor and a regenerator reactor, wherein the integrated fluidized bed reactor has a first longitudinal axis and comprises an inner surface defining an interior space, wherein the regenerator reactor has a second longitudinal axis and is positioned at least partially within the interior space; activating a deactivated catalyst present in the regenerator reactor by performing a exothermic catalyst regeneration reaction to produce an activated catalyst and heat; transferring the heat to the integrated fluidized bed reactor; and dehydrogenating a paraffm present in the integrated fluidized bed reactor by performing an endothermic reaction with a catalyst, the paraffm, and at least a portion of the transferred heat to forma dehydrogenation product.

    Abstract translation: 本文公开了一种用于脱氢石蜡的方法和装置，包括：提供包含集成流化床反应器和再生器反应器的脱氢反应器，其中所述一体化流化床反应器具有第一纵向轴线并且包括限定内部空间的内表面， 其中所述再生器反应器具有第二纵向轴线并且至少部分地定位在所述内部空间内; 通过进行放热催化剂再生反应来活化再生器反应器中存在的失活的催化剂以产生活化的催化剂和加热; 将热量传递到集成流化床反应器; 并通过与催化剂，石蜡和至少一部分转移的热量进行吸热反应，使整合的流化床反应器中存在的石蜡脱氢形成脱氢产物。

    Reactor, toner production method, and toner
    49.
    发明授权
    Reactor, toner production method, and toner 有权
    反应器，调色剂生产方法和调色剂

    公开(公告)号：US08728700B2

    公开(公告)日：2014-05-20

    申请号：US13597853

    申请日：2012-08-29

    Applicant: Junichi Watanabe ,  Kenichi Uehara

    Inventor： Junichi Watanabe ,  Kenichi Uehara

    IPC: B01J19/00 ,  G03G9/087

    CPC classification number: B01J8/087 ,  B01J8/20 ,  B01J19/2415 ,  B01J2208/00168 ,  B01J2208/0084 ,  B01J2219/00772 ,  B01J2219/00774 ,  B01J2219/00777 ,  B01J2219/185 ,  B01J2219/1943 ,  G03G9/0806

    Abstract: A reactor, which heats a slurry raw material including a solid component, including a reaction tube, wherein the slurry raw material is continuously fed from an end of the reaction tube relative to the central axial direction of the reaction tube so as to be flown toward another end of the reaction tube to be heated; and plural perforated plates arranged in the reaction tube so as to separate the inside of the reaction tube into plural compartments. The reactor satisfies the relations (½)·D′≦D

    Abstract translation: 一种反应器，其对包括反应管的固体成分的浆料原料进行加热，其中，从反应管的端部向反应管的中心轴方向连续供给浆料原料，使其向 待加热的反应管的另一端; 和多个穿孔板，布置在反应管中，以将反应管的内部分离成多个隔室。 反应器满足关系（½）·D'＆nlE; D

    METHOD FOR GENERATING ELECTRICITY AND FOR PRODUCING GASOLINE FROM METHANOL AND SYSTEM THEREFOR
    50.
    发明申请
    METHOD FOR GENERATING ELECTRICITY AND FOR PRODUCING GASOLINE FROM METHANOL AND SYSTEM THEREFOR 有权
    从甲醇生产汽油和生产汽油的方法及其系统

    公开(公告)号：US20130014430A1

    公开(公告)日：2013-01-17

    申请号：US13547272

    申请日：2012-07-12

    Applicant: Masaki IIJIMA

    Inventor： Masaki IIJIMA

    IPC: B01J8/00 ,  F01K13/00 ,  F01D15/10 ,  C10L1/04

    CPC classification number: C10G3/42 ,  B01J8/02 ,  B01J8/0285 ,  B01J2208/00168 ,  C10G3/49 ,  C10G2300/805 ,  C10G2400/02 ,  C10L1/06 ,  C10L2270/023 ,  C10L2290/06 ,  F01K13/00 ,  Y02P30/20

    Abstract: A method for generating electric power and for producing gasoline from methanol, includes the steps of: synthesizing gasoline by reacting methanol under a catalyst; recovering heat generated from the gasoline synthetic reaction of methanol by cooling the reaction with coolant to vaporize the coolant; and generating electric power by using the coolant vapor produced in the heat recovery. The power generation step may include generating electric power with a plurality of steam turbines in series, e.g., a high-pressure turbine, a medium-pressure turbine, and a low-pressure turbine.

    Abstract translation: 一种从甲醇产生电力和生产汽油的方法，包括以下步骤：通过在催化剂下使甲醇反应合成汽油; 通过冷却与冷却剂的反应来蒸发冷却剂来回收由汽油合成甲醇反应产生的热量; 并通过使用在热回收中产生的冷却剂蒸汽发电。 发电步骤可以包括利用多个串联的蒸汽轮机（例如高压涡轮机，中压涡轮机和低压涡轮机）来产生电力。

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