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1. 发明授权

US09903584B2 Systems for converting fuel 有权
公开(公告)号：US09903584B2
公开(公告)日：2018-02-27
申请号：US14116636
申请日：2012-05-11
申请人： Liang-Shih Fan , Hyung R. Kim , Fanxing Li , Liang Zeng , Dawei Wang , Fei Wang
发明人： Liang-Shih Fan , Hyung R. Kim , Fanxing Li , Liang Zeng , Dawei Wang , Fei Wang
IPC分类号： F23C10/01 , F23C10/00 , C01B3/22 , C10J3/72 , F23C10/04 , F23C10/20 , F23C10/32 , B01J8/18 , B01J8/38 , B01J8/00 , B01J8/32 , C10J3/06 , B01J8/12
CPC分类号： F23C10/005 , B01J8/002 , B01J8/12 , B01J8/125 , B01J8/1827 , B01J8/32 , B01J8/388 , B01J2208/00061 , B01J2208/00513 , B01J2208/00557 , B01J2208/0061 , B01J2208/00654 , B01J2208/00778 , B01J2208/0084 , B01J2208/00902 , B01J2208/00938 , C01B3/22 , C10J3/06 , C10J3/721 , C10J3/723 , C10J3/725 , C10J2300/1807 , F23C10/04 , F23C10/20 , F23C10/32
摘要： A system for converting fuel may include a first moving bed reactor, a second reactor, and a non-mechanical valve. The first moving bed reactor may include at least one tapered section and multiple injection gas ports. The multiple injection gas ports may be configured to deliver a fuel to the first moving bed reactor. The first moving bed reactor may be configured to reduce an oxygen carrying material with a fuel by defining a countercurrent flowpath for the fuel relative to the oxygen carrying material. The second reactor may communicate with the first moving bed reactor and may be operable to receive an oxygen source. The second reactor may be configured to regenerate the reduced oxygen carrying material by oxidation.

2. 发明授权

US09504975B2 System and process for injecting catalyst and/or additives into a fluidized catalytic cracking unit 有权
公开(公告)号：US09504975B2
公开(公告)日：2016-11-29
申请号：US13193052
申请日：2011-07-28
申请人： George Yaluris , Lenny Lee Albin , Alfred Ferdinand Jordan
发明人： George Yaluris , Lenny Lee Albin , Alfred Ferdinand Jordan
IPC分类号： B01J8/24 , B65G53/28 , B01J8/00 , B01J8/32 , B01J8/06 , B01J8/18 , C10G11/18
CPC分类号： B01J8/0015 , B01J8/0025 , B01J8/003 , B01J8/0035 , B01J8/004 , B01J8/006 , B01J8/06 , B01J8/18 , B01J8/24 , B01J8/32 , B01J2208/00548 , B01J2208/00752 , B01J2208/00761 , B01J2208/00769 , B65G53/28 , C10G11/18 , C10G2300/80
摘要： A preferred embodiment of a system for loading catalyst and/or additives into a fluidized catalytic cracking unit includes a bin for storing at least one of the catalyst and/or additives, and a loading unit in fluid communication with the storage bin and the fluidized catalytic cracking unit on a selective basis. The loading unit is capable of being evacuated so that a resulting vacuum within the loading unit draws the catalyst and/or additive from the bin. The loading unit is also capable of being pressurized so that the catalyst and/or additive is transferred from the loading unit to the fluidized catalytic cracking unit.

3. 发明申请

US20160061442A1 METHOD AND DEVICE FOR CHEMICAL LOOP COMBUSTION OF LIQUID HYDROCARBON FEEDSTOCKS 审中-公开
标题翻译：液化石油气化学循环燃烧方法与装置
公开(公告)号：US20160061442A1
公开(公告)日：2016-03-03
申请号：US14783480
申请日：2014-03-11
申请人： IFP ENERGIES NOUVELLES , TOTAL RAFFINAGE CHIMIE
发明人： Mahdi Yazdanpanah , Tiago Sozinho , Thierry Gauthier , Florent Guillou
IPC分类号： F23C10/01 , F23C10/22 , F23C10/00
CPC分类号： F23C10/01 , B01J8/0055 , B01J8/007 , B01J8/28 , B01J8/32 , B01J8/388 , B01J2208/00513 , B01J2208/00902 , F23C6/04 , F23C10/005 , F23C10/10 , F23C10/22 , F23C2206/101 , F23C2900/10003 , F23C2900/99008 , Y02E20/346
摘要： The invention relates to a method for chemical looping (CLC) oxidation-reduction combustion of liquid hydrocarbon feedstocks carried out in a fluidized bed, wherein liquid hydrocarbon feedstock (2) is partly vaporized on contact with a hot solid (1) in form of particles so as to form a partly vaporized liquid feedstock and to form coke on said solid (1), prior to contacting partly vaporized liquid feedstock (19) with a redox active mass in form of particles (12) so as to achieve combustion of partly vaporized liquid feed (19). Hot solid particles (1) used to carry the coke can notably form a second fluidized-bed particle circulation loop, the first one being the circulation loop of the oxygen-carrying redox active mass (12) circulating between the oxidation and combustion reactors, thus allowing coke-carrying particles (1) to be recycled to the process.
摘要翻译：本发明涉及在流化床中进行的液体烃原料的化学循环（CLC）氧化 - 还原燃烧的方法，其中液体烃原料（2）在与颗粒形式的热固体（1）接触时部分蒸发以在部分蒸发的液体原料（19）与颗粒（12）形式的氧化还原活性物质接触之前，在所述固体（1）上形成部分蒸发的液体原料并形成焦炭，以实现部分蒸发的液体进料（19）。用于承载焦炭的热固体颗粒（1）可以显着地形成第二流化床颗粒循环回路，第一个是在氧化和燃烧反应器之间循环的携氧氧化还原活性物质（12）的循环回路，因此允许将焦炭携带的颗粒（1）再循环到该方法中。

4. 发明申请

US20140363343A1 Apparatuses and Methods for Controlling Heat for Rapid Thermal Processing of Carbonaceous Material 审中-公开
标题翻译：用于控制碳质材料快速热处理的热量的装置和方法
公开(公告)号：US20140363343A1
公开(公告)日：2014-12-11
申请号：US14346517
申请日：2012-09-14
申请人： Sathit Kulprathipanja , Paolo Palmas
发明人： Sathit Kulprathipanja , Paolo Palmas
IPC分类号： C10B53/02
CPC分类号： C10B53/02 , B01J8/0055 , B01J8/1836 , B01J8/26 , B01J8/32 , B01J2208/00176 , B01J2208/00194 , B01J2208/00292 , B01J2208/00513 , C10B49/22 , C10C5/00 , F23C10/04 , F23C2206/103 , F23G2201/304 , F23G2203/502 , F23G2209/26 , F28D7/1615 , F28F1/14 , Y02E50/14
摘要： Embodiments of apparatuses and methods for controlling heat for rapid thermal processing of carbonaceous material are provided herein. The apparatus comprises a reheater for containing a fluidized bubbling bed comprising an oxygen-containing gas, inorganic heat carrier particles, and char and for burning the char into ash to form heated inorganic particles. An inorganic particle cooler is in fluid communication with the reheater to receive a first portion of the heated inorganic particles. The inorganic particle cooler is configured to receive a cooling medium for indirect heat exchange with the first portion of the heated inorganic particles to form first partially-cooled heated inorganic particles that are fluidly communicated to the reheater and combined with a second portion of the heated inorganic particles to form second partially-cooled heated inorganic particles. A reactor is in fluid communication with the reheater to receive the second partially-cooled heated inorganic particles.
摘要翻译：本文提供了用于控制用于碳质材料的快速热处理的热量的装置和方法的实施例。该装置包括一个再热器，用于容纳包含含氧气体，无机热载体颗粒和炭的流化鼓泡床，并用于将炭烧成灰分以形成加热的无机颗粒。无机颗粒冷却器与再热器流体连通以接收第一部分加热的无机颗粒。无机颗粒冷却器构造成接收用于与加热的无机颗粒的第一部分进行间接热交换的冷却介质，以形成第一部分冷却的加热的无机颗粒，其流体连通到再热器并与第二部分加热的无机颗粒颗粒形成第二部分冷却的加热无机颗粒。反应器与再热器流体连通以接收第二部分冷却的加热的无机颗粒。

5. 发明申请

US20120114546A1 Hybrid TCS-siemens process equipped with 'turbo charger' FBR; method of saving electricity and equipment cost from TCS-siemens process polysilicon plants of capacity over 10,000 MT/YR 审中-公开
标题翻译：混合TCS-西门子工艺配备“涡轮增压器”FBR; TCS西门子工艺多晶硅厂的生产能力超过10000吨/年的节电方法和设备成本
公开(公告)号：US20120114546A1
公开(公告)日：2012-05-10
申请号：US13200989
申请日：2011-10-06
申请人： Yong Chee , Tetsunori Kunimune
发明人： Yong Chee , Tetsunori Kunimune
IPC分类号： C01B33/027 , B01J8/26
CPC分类号： B01J8/0055 , B01J8/1836 , B01J8/1872 , B01J8/32 , B01J8/44 , B01J2208/00168 , B01J2208/00725 , C01B33/1071 , C01B33/10731 , C01B33/10736 , C01B33/10742 , C01B33/10773
摘要： A ‘hybrid’ TCS (Trichlorosilane)-Siemens process is provided to save electricity and initial investment cost from TCS synthesizing process and silicon tetrachloride to TCS converting process in a TCS-Siemens polysilicon plant, whose size is over 10,000 MT/YR of polysilicon. The ‘hybrid’ TCS-Siemens process of the current application is equipped with one direct chlorination FBR (Fluidized Bed Reactor) and one hydro-chlorination FBR. Three different TCS-Siemens processes are compared based on mass balance calculation. The hybrid TCS-Siemens process saves at least 78,000,000Kwhr/year of electricity from TCS generation only from a 10,000 MT/YR polysilicon plant when compared with a ‘Closed Loop TCS-Siemens Process’, which is equipped with only high-pressure, high-temperature operating hydro-chlorination FBRs.
摘要翻译：提供了一种“混合”TCS（三氯硅烷）-Siemens工艺，用于将TCS合成工艺和四氯化硅的电力和初始投资成本节省到TCS西门子多晶硅工厂的TCS转换过程中，其大小超过10,000 MT / YR的多晶硅。目前应用的“混合”TCS-西门子工艺配备了一个直接氯化FBR（流化床反应器）和一个加氢氯化FBR。基于质量平衡计算，对三种不同的TCS-西门子工艺进行比较。与“闭环TCS-西门子工艺”相比，混合型TCS-西门子工艺节省了来自TCS产能的至少7800万千瓦时/年的电力，而该“闭环TCS-西门子工艺”仅配备高压高温度运行加氢氯化FBRs。

6. 发明授权

US08118243B2 Fluidized bed systems and methods including micro-jet flow 有权
标题翻译：流化床系统和方法包括微喷流
公开(公告)号：US08118243B2
公开(公告)日：2012-02-21
申请号：US11937736
申请日：2007-11-09
申请人： Robert Pfeffer , Jose A. Quevedo , Juergen Flesch
发明人： Robert Pfeffer , Jose A. Quevedo , Juergen Flesch
IPC分类号： B02C19/00
CPC分类号： B01J8/32 , B01F3/18 , B01F13/02 , B01F13/0272 , B01J8/1818 , B01J8/1872 , B82Y15/00 , B82Y30/00
摘要： Methods and systems for enhancing fluidization of nanoparticle and/or nanoagglomerates are provided. A fluidization chamber is provided with a fluidizing medium directed in a first fluidizing direction, e.g., upward into and through a bed containing a volume of nanoparticles and/or nanopowders. A second source of air/gas flow is provided with respect to the fluidization chamber, the secondary air/gas flow generally being oppositely directed relative to the fluidizing medium. Turbulence created by the secondary gas flow is advantageously effective to aerate the agglomerates and the shear generated by the jet is advantageously effective to break apart nanoagglomerates and/or reduce the tendency for nanoagglomerates to form or reform. A downwardly directed source of secondary gas flow located near the main gas distributor leads to full fluidization of the entire amount of powder in the column. The oppositely directed fluid flow facilitates powder circulation within the fluidization chamber, thereby enhancing fluidization results.
摘要翻译：提供了用于增强纳米颗粒和/或纳米团聚体的流化的方法和系统。流化室设置有以第一流化方向（例如向上）流入并穿过含有一定体积纳米颗粒和/或纳米粉末的床的流化介质。相对于流化室提供第二气/气流源，二次空气/气流通常相对于流化介质相反地定向。由二次气流产生的湍流有利于使附聚物充气，并且由射流产生的剪切有利于有效地分离纳米颗粒和/或降低纳米颗粒形成或改性的倾向。位于主气体分配器附近的向下定向的二次气流源导致柱中全部粉末的充分流化。相反导向的流体流动促进流化室内的粉末循环，从而增强流化结果。

7. 发明申请

US20110280769A1 SYSTEM AND PROCESS FOR INJECTING CATALYST AND/OR ADDITIVES INTO A FLUIDIZED CATALYTIC CRACKING UNIT 有权
标题翻译：将催化剂和/或添加剂注入流化催化裂化装置的系统和方法
公开(公告)号：US20110280769A1
公开(公告)日：2011-11-17
申请号：US13193052
申请日：2011-07-28
申请人： George Yaluris , Lenny Lee Albin , Alfred Ferdinand Jordan
发明人： George Yaluris , Lenny Lee Albin , Alfred Ferdinand Jordan
IPC分类号： F27B15/08
CPC分类号： B01J8/0015 , B01J8/0025 , B01J8/003 , B01J8/0035 , B01J8/004 , B01J8/006 , B01J8/06 , B01J8/18 , B01J8/24 , B01J8/32 , B01J2208/00548 , B01J2208/00752 , B01J2208/00761 , B01J2208/00769 , B65G53/28 , C10G11/18 , C10G2300/80
摘要： A preferred embodiment of a system for loading catalyst and/or additives into a fluidized catalytic cracking unit includes a bin for storing at least one of the catalyst and/or additives, and a loading unit in fluid communication with the storage bin and the fluidized catalytic cracking unit on a selective basis. The loading unit is capable of being evacuated so that a resulting vacuum within the loading unit draws the catalyst and/or additive from the bin. The loading unit is also capable of being pressurized so that the catalyst and/or additive is transferred from the loading unit to the fluidized catalytic cracking unit.
摘要翻译：用于将催化剂和/或添加剂加载到流化催化裂化装置中的系统的优选实施方案包括用于储存催化剂和/或添加剂中的至少一种的容器以及与储存箱和流化催化剂流体连通的装载单元选择性地开裂单元。装载单元能够被排空，使得装载单元内的所得真空从箱中抽出催化剂和/或添加剂。加载单元还能够被加压，使得催化剂和/或添加剂从装载单元转移到流化催化裂化装置。

8. 发明申请

US20080179433A1 Fluidized Bed Systems And Methods Including Micro-Jet Flow 有权
标题翻译：流化床系统和包括微喷流的方法
公开(公告)号：US20080179433A1
公开(公告)日：2008-07-31
申请号：US11937736
申请日：2007-11-09
申请人： Robert Pfeffer , Jose A. Quevedo , Juergen Flesch
发明人： Robert Pfeffer , Jose A. Quevedo , Juergen Flesch
IPC分类号： B02C19/06
CPC分类号： B01J8/32 , B01F3/18 , B01F13/02 , B01F13/0272 , B01J8/1818 , B01J8/1872 , B82Y15/00 , B82Y30/00
摘要： Methods and systems for enhancing fluidization of nanoparticle and/or nanoagglomerates are provided. A fluidization chamber is provided with a fluidizing medium (e.g., a fluidizing gas) directed in a first fluidizing direction, e.g., upward into and through a bed containing a volume of nanoparticles and/or nanopowders. A second source of air/gas flow is provided with respect to the fluidization chamber, the secondary air/gas flow generally being oppositely (or substantially oppositely) directed relative to the fluidizing medium. Turbulence created by the secondary gas flow, e.g., a jet from a micro-jet nozzle, is advantageously effective to aerate the agglomerates and the shear generated by the jet is advantageously effective to break apart nanoagglomerates and/or reduce the tendency for nanoagglomerates to form or reform. A downwardly directed source of secondary gas flow located near the main gas distributor leads to full fluidization of the entire amount of powder in the column. In addition, the oppositely directed fluid flow facilitates powder circulation within the fluidization chamber, thereby enhancing fluidization results. Use of oppositely directed fluid flow is believed to transition a bed that is exhibiting agglomerate bubbling fluidization (ABF) behavior into a bed that exhibits agglomerate particulate fluidization (APF) behavior
摘要翻译：提供了用于增强纳米颗粒和/或纳米团聚体的流化的方法和系统。流化室设置有以第一流化方向（例如向上）引导入并穿过含有一定体积的纳米颗粒和/或纳米粉末的床的流化介质（例如，流化气体）。相对于流化室设置第二气/气流源，二次空气/气体流通常相对于流化介质相反（或大致相反地）流动。由次级气流产生的湍流，例如来自微喷嘴的射流，有利于使附聚物充气，并且由射流产生的剪切有利于有效地分离纳米团聚体和/或降低纳米颗粒形成的趋势或改革。位于主气体分配器附近的向下定向的二次气流源导致柱中全部粉末的充分流化。此外，相反导向的流体流动促进流化室内的粉末循环，从而增强流化结果。认为使用相反导向的流体流动将使附聚发泡流化（ABF）行为的床转变为显示附聚颗粒流化（APF）行为的床

9. 发明授权

US07166742B2 Fluid bed process for the acetoxylation of ethylene in the production of vinyl acetate 失效
标题翻译：在乙酸乙烯酯生产中乙烯乙酰氧基化的流化床方法
公开(公告)号：US07166742B2
公开(公告)日：2007-01-23
申请号：US10721669
申请日：2003-11-25
申请人： Larry M. Cirjak , Michael F. Lemanski , David R. Wagner , Nancy C. Benkalowycz , Patricia R. Blum , Marc A. Pepera , Christos Paparizos
发明人： Larry M. Cirjak , Michael F. Lemanski , David R. Wagner , Nancy C. Benkalowycz , Patricia R. Blum , Marc A. Pepera , Christos Paparizos
IPC分类号： C07C67/05
CPC分类号： C07C67/055 , B01J8/24 , B01J8/32 , B01J8/388 , B01J19/002 , C07C69/01 , C07C69/15
摘要： A fluid bed process for the manufacture of vinyl acetate from ethylene, acetic acid and oxygen comprising feeding ethylene and acetic acid into a fluid bed reactor through a first inlet, introducing the oxygen into the reactor through a second inlet, co-joining the oxygen, ethylene and acetic acid in the reactor in contact with a fluid bed catalyst to produce vinyl acetate. The particle size diameter of the particulate catalyst material has a range of 60% of the particles being below 200 microns (0.1 mm) with no more than 40% of the particles being below 40 microns (0.04 mm).
摘要翻译：一种用于从乙烯，乙酸和氧气制造乙酸乙烯酯的流化床方法，包括通过第一入口将乙烯和乙酸进料到流化床反应器中，通过第二入口将氧气引入反应器，共同连接氧气，乙烯和乙酸在反应器中与流化床催化剂接触以产生乙酸乙烯酯。颗粒催化剂材料的粒度直径范围为60％以下的颗粒低于200微米（0.1mm），不超过40％的颗粒低于40微米（0.04mm）。

10. 发明授权

US5866006A Coated single particles and their use in fluid bed chromatography 失效
标题翻译：使用涂层颗粒的流化床色谱法
公开(公告)号：US5866006A
公开(公告)日：1999-02-02
申请号：US4316
申请日：1998-01-08
申请人： Allan Otto Fog Lihme , Claus Schafer Nielsen , Thorkild Christian B.o slashed.g Hansen
发明人： Allan Otto Fog Lihme , Claus Schafer Nielsen , Thorkild Christian B.o slashed.g Hansen
IPC分类号： B01D39/14 , B01D15/02 , B01D15/18 , B01J2/08 , B01J2/16 , B01J8/00 , B01J8/08 , B01J8/18 , B01J8/20 , B01J8/22 , B01J8/24 , B01J8/32 , B01J13/00 , B01J13/02 , B01J20/22 , B01J20/28 , B01J20/281 , B01J20/283 , B01J20/284 , B01J20/285 , B01J20/32 , B01J47/10 , C02F1/28 , C02F1/72 , C02F3/10 , C02F3/12 , C02F3/34 , C07B63/00 , C08K3/00 , C08K3/22 , C08K5/00 , C08L101/00 , C12M1/40 , G01N30/58 , G01N30/88 , B01D15/08
CPC分类号： B01J20/28019 , B01D15/1807 , B01J13/02 , B01J2/16 , B01J20/28004 , B01J20/28011 , B01J20/28014 , B01J20/28021 , B01J20/28026 , B01J20/2803 , B01J20/3219 , B01J20/3251 , B01J20/3253 , B01J20/3255 , B01J20/3274 , B01J47/10 , B01J8/008 , B01J8/085 , B01J8/1845 , B01J8/1872 , B01J8/1881 , B01J8/20 , B01J8/22 , B01J8/32 , C02F1/286 , C02F1/722 , C02F3/085 , C02F3/10 , C02F3/108 , C02F3/342 , B01D2215/021 , Y02W10/15 , Y10S435/815 , Y10S530/811 , Y10S530/812 , Y10S530/813
摘要： A fluidized bed chromatographic process for purification and binding of molecules in a liquid by binding the molecules to an active substance covalently bound to chromatographic adsorbent particles in which process a fluidized bed of the adsorbent particles is formed and said liquid is passed through the fluidized bed, wherein the chromatographic adsorbent particles are formed of a porous composite material having pores allowing access to the interior of the composite material by the molecules, and the porous composite material includes: (i) density controlling particles which are either (a) hollow low density particles which are impermeable to the liquid and have a density providing floatation of the adsorbent particles in the liquid or, (b) high density particles having a density providing sedimentation of the adsorbent particles in the liquid; (ii) a matrix formed by consolidating at least one conglomerating agent selected from the group consisting of natural and synthetic organic monomers and polymers; and (iii) an active substance for binding molecules in the liquid; the density controlling particles being embedded in the matrix, and the active substance being covalently bound to the matrix; wherein;the adsorbent particles have a relative density with respect to the liquid which is less than 0.95 or greater than 1.1 and a particle size within the range of 50-750 .mu.m, and each of the relative density and particle size range of the adsorbent particles is selected to provide desired floatation/sedimentation properties of the adsorbent particles in the liquid in the fluidized bed process with substantially no turbulence.
摘要翻译：一种用于通过将分子结合到与色谱吸附剂颗粒共价结合的活性物质来纯化和结合液体中的分子的流化床层析方法，其中形成吸附剂颗粒的流化床并使液体通过流化床，其中色谱吸附剂颗粒包括多孔复合材料，其具有允许通过分子进入复合材料内部的孔，其中每个吸收颗粒的多孔复合材料由以下组成：（i）单一密度控制颗粒，其为（a ）一种中空低密度颗粒，其不透液体并且具有提供吸附剂颗粒在液体中浮选的密度，或（b）具有提供吸附剂颗粒在液体中沉降的密度的高密度颗粒; （ii）通过固结至少一种选自天然和合成有机单体和聚合物的聚集剂形成的基体; 和（iii）用于结合液体中的分子的活性物质; 所述密度控制粒子嵌入所述基质中，所述活性物质与所述基质共价结合; 其中吸附剂颗粒相对于液体的相对密度小于0.95或大于1.1，粒径在1-1000um范围内，并且选择吸附剂颗粒的每个相对密度和粒度范围以在流化床工艺中的液体中提供吸附剂颗粒的期望的浮选/沉降特性，在流化床中基本上没有湍流。

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