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1. 发明授权

US5123939A Cyclone for separating a mixture of gas and solid particles by centrifuging, with heat recovery 失效
标题翻译：用于通过离心分离气体和固体颗粒的混合物的循环，具有热回收
公开(公告)号：US5123939A
公开(公告)日：1992-06-23
申请号：US786840
申请日：1991-11-01
申请人： Jean-Xavier Morin , Jean Aubry , Jean-Paul Tessier
发明人： Jean-Xavier Morin , Jean Aubry , Jean-Paul Tessier
IPC分类号： B04C3/02 , B01D45/12 , B01J8/00 , B04C3/06 , B04C5/02 , B04C5/20 , B04C9/00
CPC分类号： F28D13/00 , B01D45/12 , B01J8/0055 , B04C3/06 , B04C5/02 , B04C5/20 , B04C9/00
摘要： A cyclone for separating a mixture of gas and solid particles by centrifuging into a fraction that is enriched in particles and a gaseous fraction that is depleted in particles, the cyclone comprising a cylindrical vessel into which a duct for injecting the mixture of gas and solid particles opens out tangentially, an axial duct for removing the gaseous fraction, means for removing the fraction that is enriched in particles, which means are situated in the bottom portion of the cylindrical vessel, gas injection means serving to fluidize the solid particle enriched fraction as a dense bed, and heat exchanger means for exchanging heat between the dense fluidized bed that is formed and a fluid to be vaporized and/or reheated, together with means for adjusting the level of the dense bed.
摘要翻译：将气体和固体颗粒的混合物离心分离成富集颗粒的部分和耗尽颗粒的气体馏分的旋风分离器，旋风分离器包括一个圆柱形容器，用于注入气体和固体颗粒混合物的管道切向地打开用于除去气体馏分的轴向管道，用于去除富集颗粒的馏分的装置，该装置位于圆柱形容器的底部中，气体注入装置用于使富含固体颗粒的馏分流化为致密床和用于在所形成的致密流化床与待蒸发和/或再加热的流体之间进行热交换的热交换器装置，以及用于调节致密床层的装置的装置。

2. 发明授权

US5508007A Circulating fluidized bed reactor including external heat exchangers fed by internal recirculation 失效
标题翻译：循环流化床反应器，包括通过内部再循环进料的外部热交换器
公开(公告)号：US5508007A
公开(公告)日：1996-04-16
申请号：US344633
申请日：1994-11-17
申请人： Jean Vidal , Jean-Xavier Morin , Jean-Paul Tessier
发明人： Jean Vidal , Jean-Xavier Morin , Jean-Paul Tessier
IPC分类号： B01J8/24 , B01J8/28 , F22B1/02 , F22B29/00 , F22B31/00 , F23C10/00 , F23C10/04 , F23C10/10 , F23C10/12 , F23C99/00 , B01J8/18 , F27B15/08 , F27B15/14
CPC分类号： F22B31/0084 , F23C10/10 , F23C10/12 , F23C2206/103
摘要： A circulating fluidized bed reactor includes a lower zone having a fluidization grid, primary and secondary air injection inlets, and fuel feed inlets, an upper zone, internal bubbling beds at the top of the lower zone collecting solid matter from recirculation internal to the reactor and delivering a fraction thereof to external bubbling bed heat exchangers close coupled with the walls of the reactor level with the internal beds. The external heat exchangers reject the solid matter into the lower zone after exchanging heat with an external fluid. The reactor is simple in structure and benefits from the advantages of bubbling external beds while maintaining conventional design in the lower zone.
摘要翻译：循环流化床反应器包括具有流化栅格的下区域，一次和二次空气注入入口和燃料进料入口，上部区域，位于下部区域顶部的内部鼓泡床，从固体物质的内部再循环回收反应器，将其一部分输送到与内部床紧邻地与反应器水平壁相连的外部鼓泡床热交换器。外部热交换器在与外部流体交换热量后将固体物质排入下部区域。反应器结构简单，并且受益于鼓泡外部床的优点，同时保持下部区域的常规设计。

3. 发明授权

US5707591A Circulating fluidized bed reactor having extensions to its heat exchange area 失效
标题翻译：循环流化床反应器具有其热交换区域的延伸
公开(公告)号：US5707591A
公开(公告)日：1998-01-13
申请号：US723386
申请日：1996-09-30
申请人： Jean-Claude Semedard , Pierre Gauville , Pascale Amadieu , Jean Aubry , Jean-Xavier Morin
发明人： Jean-Claude Semedard , Pierre Gauville , Pascale Amadieu , Jean Aubry , Jean-Xavier Morin
IPC分类号： F23C10/06 , F22B31/00 , F23C10/02 , F23M5/08 , F27B15/14
CPC分类号： F22B31/0084 , F22B31/003
摘要： A circulating fluidized bed reactor comprising a top zone surrounded by walls provided with heat exchange tubes, the heat exchange tubes being interconnected by fins, and a bottom zone provided with a fluidization grid, a primary air injection device beneath the grid, a secondary air injection device above the grid, and a fuel injection device, the walls surrounding the bottom zone being provided with heat exchange tubes. The walls of the zones are provided with vertical heat exchange panels referred to as "extensions" that extend perpendicularly to the walls of the zones, that are made up of tubes inside the reactor, that are of horizontal width lying in the range 150 mm to 500 mm, and that are spaced apart from one another via a distance lying in the range 1.5 times to 4 times their width, the width being defined as the distance between the inside faces of the fins of the walls and the most distant generator lines of the most distant tubes of the extensions.
摘要翻译：一种循环流化床反应器，包括由设置有热交换管的壁包围的顶部区域，所述热交换管由翅片互连，以及设置有流化栅格的底部区域，网格下方的一次空气注入装置，二次空气注入在燃料喷射装置上方，围绕底部区域的壁设有热交换管。这些区域的壁设置有垂直的热交换板，称为“延伸部”，其垂直于区域的壁延伸，该区域由反应器内部的管构成，水平宽度在150mm至 500mm，并且通过距离为其宽度的1.5倍至4倍的距离彼此间隔开，宽度被限定为壁的翅片的内表面和最远的发电机线之间的距离最远的管子的扩展。

4. 发明授权

US08318101B2 Oil-derived hydrocarbon converter having an integrated combustion installation comprising carbon dioxide capture 失效
标题翻译：具有集成燃烧装置的含油烃转化器包括二氧化碳捕获
公开(公告)号：US08318101B2
公开(公告)日：2012-11-27
申请号：US12086659
申请日：2006-12-22
申请人： Jean-Xavier Morin , Corinne Beal , Silvestre Suraniti
发明人： Jean-Xavier Morin , Corinne Beal , Silvestre Suraniti
IPC分类号： B01J8/18 , F27B15/00
CPC分类号： F23C10/005 , B01J29/90 , C10G11/182 , C10G2300/708 , C10G2300/807 , F23C10/01 , F23C2900/99008 , Y02E20/346 , Y02P30/446
摘要： The invention relates to an oil-derived hydrocarbon converter comprising a catalytic cracking vessel (1) in the presence of catalyst particles in fluidized phase and a regenerator, for regenerating said catalyst particles by burning off the coke deposited on them, said catalyst circulating between said cracking vessel and said regenerator, said regenerator being a reactor (2) integrated into a combustion installation for steam generation comprising carbon dioxide capture. According to the invention, said regenerator is a reduction reactor (2) for an oxygen support, which is fed with solid fuel, comprising said particles provided with coke, and is equipped with a cyclone (C2) for separating the solids and with exchangers (E2), this reduction reactor for said oxygen support being associated with an oxidation reactor (3) for said oxygen support and equipped with a cyclone (C3) for separating the solids and with exchanges (E3), said oxygen support circulating between these two reactors, and in that said oxygen support consists of metal oxide particles having a mean diameter different from that of said catalyst particles.
摘要翻译：本发明涉及一种油衍生烃转化器，其包括在流化相中的催化剂颗粒存在下的催化裂解容器（1）和再生器，用于通过烧掉沉积在其上的焦炭来再生所述催化剂颗粒，所述催化剂在所述裂解容器和所述再生器，所述再生器是集成在用于产生蒸汽的燃烧装置中的反应器（2），包括二氧化碳捕获。根据本发明，所述再生器是用于氧气载体的还原反应器（2），其供给固体燃料，所述固体燃料包含所述提供有焦炭的颗粒，并且配备有用于分离固体和交换器的旋风分离器（C2） E2），用于所述氧气载体的还原反应器与用于所述氧气载体的氧化反应器（3）相关联，并配备有用于分离固体和交换（E3）的旋风分离器（C3），所述氧载体在这两个反应器之间循环并且所述氧载体由平均直径不同于所述催化剂颗粒的金属氧化物颗粒组成。

5. 发明授权

US07987993B2 Solid separator especially for a combustion facility 有权
标题翻译：固体分离器特别用于燃烧设备
公开(公告)号：US07987993B2
公开(公告)日：2011-08-02
申请号：US12087636
申请日：2007-01-23
申请人： Jean-Xavier Morin , Corinne Beal , Silvestre Suraniti
发明人： Jean-Xavier Morin , Corinne Beal , Silvestre Suraniti
IPC分类号： B07B13/00 , B07C5/12
CPC分类号： B01D45/06 , B01D45/08
摘要： A separator of solids for separating first and second solids, the diameter and density of the first solids being larger than the diameter and density of the second solids. A first substantially vertical internal baffle (2) forms a passage in the low portion of the separator and forms two compartments (1A, 1B) on the passage of the fluidized solids. The fluidization of each compartment is independently controlled by two fluidization gas inlets (3A, 3B) in order to obtain the desired velocity field for separating the first and second solids in the first compartment (1A) and discharging the second solids through a vent (8), as well as for transferring the first solids into the second compartment (1B). The first baffle (2) is provided on at least one of its substantially vertical faces with fluidization gas ejectors (E2) and the first compartment (1A) is equipped with an internal obstacle arrangement deflecting the path of the solids and at least partially provided with fluidization gas ejectors (E4A) directed towards said first baffle (2).
摘要翻译：用于分离第一和第二固体的固体分离器，第一固体的直径和密度大于第二固体的直径和密度。第一基本垂直的内部挡板（2）在分离器的低部分形成通道，并在流化固体的通道上形成两个隔室（1A，1B）。每个隔室的流化独立地由两个流化气体入口（3A，3B）控制，以便获得用于分离第一隔室（1A）中的第一和第二固体的期望的速度场，并且通过排气口排出第二固体（8 ），以及用于将第一固体转移到第二隔室（1B）中。第一挡板（2）在其基本上垂直的表面中的至少一个上设置有流化气体喷射器（E2），并且第一隔室（1A）配备有将固体的路径偏转并且至少部分地设置有朝向所述第一挡板（2）的流化气体喷射器（E4A）。

6. 发明授权

US07658167B2 Fluidized-bed device with oxygen-enriched oxidizer 有权
标题翻译：具有富氧氧化剂的流化床装置
公开(公告)号：US07658167B2
公开(公告)日：2010-02-09
申请号：US11579097
申请日：2005-05-26
申请人： Jean-Xavier Morin , Silvestre Suraniti
发明人： Jean-Xavier Morin , Silvestre Suraniti
IPC分类号： F23C10/20
CPC分类号： F23C10/20 , B01J8/0055 , B01J8/1818 , B01J8/1863 , B01J8/26 , B01J8/44 , F23C10/10 , F23L7/005 , F23L7/007 , Y02E20/344
摘要： The invention relates to a fluidized-bed device (F1, F2) provided with a hearth (1, 23) equipped with gas mixture feeds called primary feeds, said gas mixture being enriched with oxygen, and said hearth (1, 23) being provided with a network of two types of primary feed nozzle, a first type of nozzle (B1, B′1) injecting a first gas mixture at a first level close to the hearth (1, 23) and a second type of nozzle (B2, B′2) injecting a second oxygen-enriched gas mixture at a second level above the first level.According to the invention, said second type of nozzle (B2, B′2) consists of a device for mixing oxygen with a second gas component and connected by its lower end to an oxygen feed (11A, 11A′) and to a feed of second gas component, and of a device for injecting this mixture into the combustion chamber.
摘要翻译：本发明涉及一种流化床装置（F1，F2），其设有装有称为初级进料的气体混合物进料的炉床（1,23），所述气体混合物富含氧气，所述炉床（1）和具有两种类型的主进料喷嘴的网络，第一类型的喷嘴（B1，B'1）将第一气体混合物注入靠近炉床（1,23）的第一级和第二类型的喷嘴（B2， B'2）在第一级以上的第二级注入第二富氧气体混合物。根据本发明，所述第二类型的喷嘴（B2，B'2）由用于将氧气与第二气体组分混合并通过其下端连接到氧气进料（11A，11A'）的装置组成，第二气体成分和用于将该混合物注入燃烧室的装置。

7. 发明申请

US20090133611A1 Circulating Fluidized Bed Device Provided With An Oxygen-Fired Furnace 有权
标题翻译：带有氧气炉的循环流化床装置
公开(公告)号：US20090133611A1
公开(公告)日：2009-05-28
申请号：US11921585
申请日：2006-06-14
申请人： Jean-Xavier Morin , Corinne Beal , Silvestre Suraniti
发明人： Jean-Xavier Morin , Corinne Beal , Silvestre Suraniti
IPC分类号： F23K1/00
CPC分类号： F23C10/10 , F23L7/007 , Y02E20/322 , Y02E20/344
摘要： The invention relates to a circulating fluidized bed device provided with an oxygen-fired furnace (1) , a separator (2) for separating gas and solid particles, a return circuit for returning solids to the furnace (3), and an outlet duct (4) leaving the separator and conveying gases to a heat-recovery boiler, the device being characterized in that it includes injector means for injecting combustible) gas into the outlet from the separator 2), said combustible gas being propelled by recycled carbon dioxide into the residual vortex created at the outlet from the separator, so as to ensure intimate mixing takes place in the downstream duct (4) with the combustion flue gases, thereby reducing the oxygen content of said flue gases by residual combustion.
摘要翻译：本发明涉及一种循环流化床装置，该装置设有氧气炉（1），用于分离气体和固体颗粒的分离器（2），将固体返回到炉（3）的回流回路和出口管 4）离开分离器并将气体输送到热回收锅炉，该装置的特征在于其包括用于将可燃气体喷射到来自分离器2的出口的喷射器装置），所述可燃气体由再循环的二氧化碳推进到在分离器的出口处产生的残余涡流，以便确保在下游管道（4）中与燃烧烟道气发生紧密混合，从而通过残余燃烧来减少所述烟道气的氧含量。

8. 发明授权

US06737031B2 Method of simultaneously reducing CO2 and SO2 emissions in a combustion installation 有权
标题翻译：同时减少燃烧装置中二氧化碳和二氧化硫排放的方法
公开(公告)号：US06737031B2
公开(公告)日：2004-05-18
申请号：US09951389
申请日：2001-09-14
申请人： Corinne Beal , Jean-Xavier Morin , Michel Vandycke
发明人： Corinne Beal , Jean-Xavier Morin , Michel Vandycke
IPC分类号： C01B1716
CPC分类号： B01D53/501 , B01D53/62 , B01D2251/404 , B01D2257/504 , F23C2206/10 , F23J7/00 , F23J15/003 , F23J15/006 , F23J2215/20 , F23J2215/50 , F23J2900/01007 , Y02A50/2342 , Y02C10/04 , Y02E20/324 , Y02E20/326
摘要： The method of simultaneously reducing carbon dioxide (CO2) emissions and sulfur dioxide (SO2) emissions produced by the combustion of carbon-containing matter in a hearth consists in injecting into the hearth a calcium-based agent, a fraction of which absorbs SO2 after decarbonization, and then, after the flue gases have been subjected to intermediate cooling, in causing them to transit via a first reactor and in putting them in contact therein with the other fraction of the absorbant that has not reacted with SO2 so as to capture CO2 from the flue gases by carbonization, then, in a separator, in extracting the solids contained in the flue gases output from the first reactor so as to subject them to heat treatment in a second reactor in order to extract CO2 therefrom by decarbonization and in order to recycle the resulting regenerated CO2 absorbant to the first reactor.
摘要翻译：同时减少二氧化碳（CO2）排放和炉内含碳物质燃烧产生的二氧化硫（SO2）排放的方法是在炉内注入钙基剂，其中一部分在脱碳后吸收SO2 然后，在烟道气已经进行中间冷却之后，使得它们经由第一反应器运输并使其与未与SO 2反应的吸收剂的其它部分接触以从其中吸收CO 2 烟道气通过碳化，然后在分离器中提取从第一反应器输出的烟道气中所含的固体，以使其在第二反应器中进行热处理，以便通过脱碳从其中提取二氧化碳，并且为了将得到的再生的CO 2吸收剂再循环到第一反应器。

9. 发明授权

US5662051A Method of treating solid residue resulting from combustion of a sulfur-containing fuel, and heat treatment apparatus for implementing the method 失效
标题翻译：处理含硫燃料燃烧产生的固体残渣的方法以及用于实施该方法的热处理装置
公开(公告)号：US5662051A
公开(公告)日：1997-09-02
申请号：US416974
申请日：1995-04-05
申请人： Jean-Xavier Morin
发明人： Jean-Xavier Morin
IPC分类号： F23C10/00 , B01D53/50 , C10L10/00 , F23J3/00
CPC分类号： B01D53/508 , C10L10/00
摘要： A method of treating solid residue resulting from combustion of a sulfur-containing fuel in the hearth of a boiler having a circulating fluidized bed, in which method limestone is inserted into the hearth so as to make it possible to absorb the resulting sulfur dioxide in the form of calcium sulfate CaSO.sub.4, the method further including the following steps:1) prior to being inserted into the hearth, the fuel is ground down to less than 100 microns;2) prior to being inserted into the hearth, the limestone is ground down to a grain-size centered in the range 100 microns to 150 microns, with a maximum of 1 mm;3) at the base of the hearth, the combustion residue is collected, which residue includes lime and calcium sulfate resulting from taking up the sulfur dioxide SO.sub.2 evolved by the combustion, and the residue is subjected to heat treatment in a reactor, in which both solid matter based on lime CaO, and also a gaseous mixture containing, in particular, sulfur dioxide SO.sub.2 are obtained;4) the sulfur dioxide is routed to a sulfuric acid manufacturing unit; and5) the solid matter is quenched with water, and is then ground, these two operations reactivating the specific surface area of the solid matter, and a portion of this solid matter is re-injected into the hearth of the boiler in the form of a suspension in water, the remaining fraction of the matter being routed to a cement plant.
摘要翻译：一种在具有循环流化床的锅炉的炉床中处理含硫燃料的燃烧产生的固体残渣的方法，其中将石灰石插入炉床中，以便能够吸收所产生的二氧化硫形式的硫酸钙CaSO 4，该方法还包括以下步骤：1）在插入炉床之前，将燃料研磨至小于100微米; 2）在插入炉床之前，将石灰石粉碎成中心在100微米至150微米范围内的粒度，最大为1毫米; 3）在炉膛的底部，收集燃烧残留物，残留物包含由燃烧产生的二氧化硫SO2吸收的石灰和硫酸钙，残留物在反应器中进行热处理，基于石灰CaO的固体物质，以及特别是含有二氧化硫SO 2的气态混合物; 4）将二氧化硫送至硫酸制造单位; 5）固体物质用水淬火，然后研磨，这两个操作重新激活固体物质的比表面积，并将该固体物质的一部分重新注入锅炉的炉床，形式为在水中的悬浮液，剩余部分的物质被送到水泥厂。

10. 发明授权

US5570578A Heat recovery method and device suitable for combined cycles 失效
标题翻译：热回收方法和装置适用于联合循环
公开(公告)号：US5570578A
公开(公告)日：1996-11-05
申请号：US159541
申请日：1993-12-01
申请人： Jean-Fran.cedilla.ois Saujet , Pascale Amadieu , Georges Hubert , Francine Hrisafovic , Jean-Xavier Morin
发明人： Jean-Fran.cedilla.ois Saujet , Pascale Amadieu , Georges Hubert , Francine Hrisafovic , Jean-Xavier Morin
IPC分类号： F01K7/22 , F01K7/32 , F01K23/10 , F02C6/18 , F22B1/18 , F22B33/14 , F01K7/00 , F22B1/00
CPC分类号： F01K23/106 , F01K7/32 , Y02E20/16
摘要： A heat recovery method is disclosed suitable for combined gas turbine/steam turbine cycles including at the exhaust of a gas turbine a waste heat boiler in which water is first treated in a degassing unit connected to a first evaporator and comprising a certain number of heat exchangers. The boiler uses an ultrasupercritical steam cycle with four pressure levels with subcritical fluid intermediate evaporator stages.
摘要翻译：公开了一种热回收方法，其适用于组合的燃气轮机/蒸汽轮机循环，包括在燃气轮机的排气处，废热锅炉，其中首先在连接到第一蒸发器的脱气单元中处理水，并且包括一定数量的热交换器。锅炉采用超临界蒸汽循环，四级压力水平与亚临界流体中间蒸发器级。

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