公开(公告)号：US20030007900A1

公开(公告)日：2003-01-09

申请号：US09407042

申请日：1999-09-27

Inventor： TAKU SHIMIZU ,  KAZUAKI KIMURA ,  KIYOSHI OKAZOE ,  ATSUSHI TATANI ,  NAOHIKO UKAWA ,  MASAO HINO ,  SUSUMU OKINO ,  TAKASHI HARUKI ,  TORU TAKASHINA ,  EIJI OCHI

IPC: B01D050/00 ,  B01D053/00 ,  B01J008/08 ,  F01N003/01

CPC classification number: C10M173/02 ,  B01D53/46 ,  B01D53/501 ,  C10M2215/042 ,  C10M2229/045 ,  C10M2229/046 ,  C10N2220/13 ,  C10N2240/58 ,  F23J15/003 ,  F23J15/022 ,  F23J2215/20 ,  F23J2219/50

Abstract: Five combustion exhaust gas treatment systems capable of removing dust and selenium (Se) in combustion exhaust gas and making harmless are proposed: (1) combustion exhaust gas is cooled to 350null C. or less, dust is separated, Se is transformed into insoluble compound, and Se is separated; (2) combustion exhaust gas is cooled to 350null C. or less, dust is separated, Se elution preventive agent is added, and dust is formed into scale; (3) dust in combustion exhaust gas is collected by dust collector, dust is formed into slurry by making use of part of circulation liquid in desulfurization apparatus, and tetravalent Se in dust slurry is transformed into insoluble compound, which is separated into solid and liquid; (4) dust is separated from combustion exhaust gas by dust collector, and it is heated to gasify Se, and is led into desulfurization apparatus, etc., and formed into slurry, and Se is made into insoluble compound; and (5) a treating agent for making tetravalent Se insoluble is added to part of circulation liquid in desulfurization apparatus, and it is sprayed into combustion exhaust gas to make Se insoluble.

Abstract translation: 提出了能够除去燃烧废气中的灰尘和硒（Se），无害化的五种燃烧废气处理系统：（1）燃烧废气冷却至350℃以下，灰尘分离，Se转化为不溶性 化合物，Se分离; （2）将燃烧废气冷却至350℃以下，分离灰尘，加入Se洗脱预防剂，形成灰尘; （3）燃烧废气中的灰尘由集尘器收集，利用脱硫装置中循环液的一部分形成粉尘，并将粉尘浆中的四价硒转化为不溶性化合物，分离成固体和液体 ; （4）灰尘通过集尘器与燃烧废气分离，并被加热气化Se，并被引入脱硫装置等，形成浆料，Se成不溶性化合物; （5）在脱硫装置的一部分循环液中加入四价Se不溶性的处理剂，喷入燃烧废气中使Se不溶。

公开(公告)号：US20020192124A1

公开(公告)日：2002-12-19

申请号：US10198358

申请日：2002-07-19

Applicant: MITSUBISHI MATERIALS CORPORATION

Inventor： Hiromichi Koizumi

IPC: C01G043/01 ,  B01J008/08

CPC classification number: C01G43/01 ,  C01B7/191 ,  C01B7/195 ,  C01B7/197 ,  C01F11/22 ,  C01P2004/61 ,  C01P2006/10

Abstract: A depleted UF6 processing plant including a first fluidized bed reactor configured to react depleted UF6 with steam to produce UO2F2 and hydrogen fluoride, a second fluidized bed reactor connected to the first fluidized bed reactor and configured to react the UO2F2 with steam to produce U3O8, hydrogen fluoride and oxygen, a gas cooler configured to cool the hydrogen fluoride generated in the first and second fluidized bed reactors down to 150 to 300null C., and a fluorine fixing reactor containing granular calcium carbonate and connected to the gas cooler to receive the hydrogen fluoride cooled down to 150 to 300null C. from the gas cooler. The fluorine fixing reactor is configured to form granular calcium fluoride from the granular calcium carbonate and the hydrogen fluoride passing through the fluorine fixing reactor.

Abstract translation: 一种耗尽的UF 6加工设备，其包括第一流化床反应器，其被配置为使耗尽的UF6与蒸汽反应以产生UO2F2和氟化氢;第二流化床反应器，连接到第一流化床反应器并且被配置为使UO2F2与蒸汽反应以产生U3O8，氢 氟化物和氧气，构造成将在第一和第二流化床反应器中产生的氟化氢冷却至150至300℃的气体冷却器和含有颗粒状碳酸钙并连接到气体冷却器以接收氢气的氟定影反应器 氟化物从气体冷却器冷却至150至300℃。 氟定影反应器由粒状碳酸钙和通过氟定影反应器的氟化氢形成颗粒状氟化钙。

公开(公告)号：US20020054836A1

公开(公告)日：2002-05-09

申请号：US09987932

申请日：2001-11-16

Inventor： Chalmer G. Kirkbride ,  James A. Doyle ,  Fred Hildebrandt

IPC: B01J008/18 ,  B01J008/08

CPC classification number: C10G1/06 ,  C10B1/04 ,  C10G1/02 ,  C10G1/08

Abstract: The invention relates to a continuous process for producing synthetic crude oil from oil bearing material, e.g., oil shale or tar sand, through continuous process for producing synthetic crude oil from bituminous tar sand or shale. The process includes treating the tar sand or shale to produce a fluidizable feed, feeding the fluidizable feed to a fluidized bed reactor, and fluidizing and reacting the fluidizable feed in the fluidized bed reactor with substantially only hydrogen.

Abstract translation: 本发明涉及通过从沥青焦油砂或页岩生产合成原油的连续方法从含油材料例如油页岩或焦油砂生产合成原油的连续方法。 该方法包括处理焦油砂或页岩以产生可流化的进料，将可流化的进料送入流化床反应器，并使流化床反应器中的可流化的进料基本上仅含氢气流化和反应。

公开(公告)号：US20020016374A1

公开(公告)日：2002-02-07

申请号：US09877227

申请日：2001-06-11

Inventor： Stanely John Becker ,  Timothy Crispin Bristow ,  Robert William Clarke ,  Michele Fiorentino ,  David Newton ,  Ian Allan Beattie Reid ,  Bruce Leo Williams

IPC: B01J008/08 ,  C07C027/06

CPC classification number: C07C253/26 ,  B01J8/1818 ,  B01J8/22 ,  B01J2208/00115 ,  B01J2208/00884 ,  B01J2219/00263 ,  C07C51/215 ,  C07C51/252 ,  C07C253/24 ,  Y02P20/582 ,  C07C57/145 ,  C07C53/08 ,  C07C255/08

Abstract: A process and apparatus for contacting (a) at least one gaseous reactant and (b) at least one liquid selected from the group consisting of reactants, coolants and mixtures thereof in the presence of a fluidized bed of catalyst, in which the liquid is introduced into the reactor through at least one inlet located within the fluidization zone and the gaseous reactant is introduced into the reactor through at least one inlet located within the fluidization zone adjacent the support means.

Abstract translation: 一种用于使（a）至少一种气体反应物和（b）在催化剂流化床存在下从反应物，冷却剂及其混合物中选择的至少一种液体接触的方法和装置，其中引入液体 通过位于流化区内的至少一个入口进入反应器，并且通过位于邻近支撑装置的流化区内的至少一个入口将气态反应物引入反应器。

公开(公告)号：US20010024631A1

公开(公告)日：2001-09-27

申请号：US09843586

申请日：2001-04-26

Applicant: Metabolix, Inc.

Inventor： Daniel Horowitz ,  Tillman U. Gerngross

IPC: B01J008/08 ,  F25B029/00

CPC classification number: C08J3/03 ,  C08G63/06 ,  C08G63/88 ,  C08J2367/04

Abstract: Methods and apparati have been developed for producing a suspension of predominately amorphous polymer particles, wherein the method includes thermally treating a suspension that includes crystalline or semi-crystalline polymer particles. The thermal treatment includes (a) heating a suspension of polymer particles of an appropriate size to a temperature effective to cause the polymer to become amorphous, and then (b) cooling the suspension of amorphous polymer particles below the melting point of the polymer at a rate effective to prevent substantial coalescence of the polymer particles. The method and apparati are effective for use with a variety of polymers having suitable crystallization parameters, although polyhydroxyalkanoate (PHA) polymers are preferred, particularly in an aqueous suspension medium. For PHA polymers, the polymer particles subjected to treatment preferably are of a size of less than 5 nullm, or more preferably less than 1.5 nullm in diameter.