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1. 发明授权

EP2716910B1 DISC-TYPE SOLAR STIRLING ENGINE POWER GENERATION DEVICE CAPABLE OF OPERATING CONTINUOUSLY DAY AND NIGHT 有权
公开(公告)号：EP2716910B1
公开(公告)日：2020-02-05
申请号：EP12789424.4
申请日：2012-05-23
申请人： Wuhan Kaidi Engineering Technology Research Institute Co., Ltd.
发明人： CHEN, Yilong , YANG, Qingping , ZHANG, Yanfeng
IPC分类号： F03G6/00 , F02G1/043 , F03G6/02 , F03G6/06

2. 发明授权

EP2865731B1 METHOD FOR FISCHER-TROPSCH SYNTHESIS AND FOR UTILIZING EXHAUST 有权
标题翻译：用于费氏合成和利用排放的方法
公开(公告)号：EP2865731B1
公开(公告)日：2017-10-04
申请号：EP13810561.4
申请日：2013-04-25
申请人： Wuhan Kaidi Engineering Technology Research Institute Co., Ltd.
发明人： CHEN, Yilong , SONG, Kan , KUAI, Pingyu , ZHANG, Yanfeng , JIN, Jiaqi
IPC分类号： C10G2/00 , B01D53/047 , C07C9/04 , C07C7/12 , C01B3/50 , C10K3/00 , C10K1/32 , C01B3/56 , C01B3/34
CPC分类号： C10G2/40 , B01D53/047 , B01D2257/108 , B01D2257/7025 , C01B3/34 , C01B3/56 , C01B2203/0283 , C01B2203/043 , C01B2203/062 , C01B2203/148 , C10G2/332 , C10G2300/4081 , C10K1/32 , C10K3/00 , Y02C20/20 , Y02P20/156

3. 发明授权

EP2799522B1 MICROWAVE PLASMA BIOMASS ENTRAINED FLOW GASIFIER AND PROCESS 有权
标题翻译：微波等离子体生物质气流床气化炉及工艺
公开(公告)号：EP2799522B1
公开(公告)日：2017-09-20
申请号：EP12863948.1
申请日：2012-10-26
申请人： Wuhan Kaidi Engineering Technology Research Institute Co., Ltd.
发明人： CHEN, Yilong , ZHANG, Yanfeng , XIA, Minggui , ZHANG, Liang
IPC分类号： C10J3/46 , C10J3/48 , C10J3/18 , C10J3/50 , C10J3/72
CPC分类号： C10J3/72 , C10J3/18 , C10J3/466 , C10J3/485 , C10J3/506 , C10J3/723 , C10J2200/152 , C10J2300/0906 , C10J2300/0916 , C10J2300/0959 , C10J2300/0976 , C10J2300/1238 , Y02P20/145
摘要： A microwave plasma biomass entrained flow gasifier comprising a gasifier body (8), a fuel inlet arranged at the lower part of the gasifier body (8), a synthetic gas outlet at the top part of the gasifier body (8), and a slag discharge outlet (10) at the bottom part of the gasifier body (8). Arranged outside the gasifier body (8) is a fuel preprocessing system, comprising a fuel crushing apparatus (1), a sieving apparatus (2) arranged downstream to the fuel crushing apparatus (1), a particle diameter-qualified fuel chamber (3) and a particle diameter-unqualified fuel chamber (4) arranged in parallel and downstream to the sieving apparatus (2), and a gasifier-front chamber arranged downstream to the particle diameter-qualified fuel chamber (3), where the gasifier-front chamber (5) is connected at the bottom part thereof to the gasifier body (8) via a burner. Arranged at the synthesis gas outlet (9) at the top part of the gasifier is a synthesis gas monitoring unit (12). Also provided is a process utilizing the gasifier for biomass entrained flow gasification. The process comprises: 1) a biomass fuel is preprocessed; 2) a microwave plasma working gas is introduced into a plasma generator, excited into plasma then injected into the gasifier; 3) biomass fuel powdery particles are injected into the gasifier via the burner, while at the same time, an oxidizer is fed into the system via an oxygen/steam inlet, injected into the gasifier simultaneously with the biomass fuel, the biomass fuel is subjected to a thermochemical reaction within the gasifier; 4) the temperature and content of the synthesis gas are monitored for implementing adjustments in oxygen flow rate, steam flow rate, and microwave power; the temperature at the synthesis gas outlet is between 900°C and 1200°C; finally, the synthesis gas is drawn out from the synthesis gas outlet at the top part, while at the same time a liquid slag is discharged via the slug discharge outlet.
摘要翻译：本发明公开了一种微波等离子体生物质夹带流气化炉，包括气化炉体（8），设置在气化炉体（8）下部的燃料入口，气化炉体（8）顶部的合成气出口，炉渣排气口10位于气化器本体8的底部。燃料预处理系统包括燃料破碎装置（1），布置在燃料破碎装置（1）下游的筛分装置（2），颗粒直径合格的燃料室（3）（2）平行且下游布置的粒径不合格燃料室（4）以及布置在粒径合格燃料室（3）下游的气化器前室，其中气化器前室（5）的底部通过燃烧器连接到气化器本体（8）。合成气监测单元（12）设置在气化器顶部的合成气出口（9）处。还提供了利用气化器进行生物质夹带气流的方法。该过程包括：1）对生物质燃料进行预处理; 2）将微波等离子体工作气体引入等离子体发生器，激发成等离子体，然后注入气化器; 3）通过燃烧器将生物质燃料粉末颗粒注入气化器中，同时经由氧气/蒸汽入口将氧化剂供给到系统中，与生物质燃料同时注入到气化器中，生物质燃料经受到气化器内的热化学反应; 4）监测合成气的温度和含量，以实施氧气流量，蒸汽流量和微波功率的调整; 合成气出口处的温度在900℃和1200℃之间; 最后，合成气从顶部的合成气出口排出，同时液渣通过排渣口排出。

4. 发明授权

EP2799523B1 EXTERNALLY HEATED MICROWAVE PLASMA GASIFIER AND SYNTHESIS GAS PRODUCTION METHOD 有权
公开(公告)号：EP2799523B1
公开(公告)日：2018-12-12
申请号：EP12862129.9
申请日：2012-10-26
申请人： Wuhan Kaidi Engineering Technology Research Institute Co., Ltd.
发明人： CHEN, Yilong , ZHANG, Yanfeng , XIA, Minggui , ZHANG, Liang
IPC分类号： C10J3/84 , C10J3/18 , C01B3/26
CPC分类号： C10B21/10 , C01B3/26 , C01B2203/0277 , C01B2203/0861 , C10J3/18 , C10J3/84 , C10J2300/0916 , C10J2300/0946 , C10J2300/0969 , C10J2300/0976 , C10J2300/0993 , C10J2300/1238 , C10J2300/1246 , C10J2300/1631 , C10J2300/1637 , C10J2300/1807 , Y02P20/134 , Y02P20/145
摘要： The present invention relates to an externally heated microwave plasma gasifier and a synthesis gas production method, comprising mainly a vertically arranged cylindrical gasifier main body, a feeder apparatus in communication with the main body and arranged at the middle-section of the gasifier main body, an upper-layer steam nozzle arranged at a clearance area, a lower-level carbon dioxide/steam nozzle arranged at a bed-layer area, a synthesis gas outlet at the top part of the gasifier main body, a monitoring unit arranged on the outlet, and a microwave plasma generator arranged in the clearance area and on the upper end of the upper-layer steam nozzle; also provided is an external heating apparatus utilizing an external heat source for heating the gasifier main body, where the external heating apparatus is arranged integrally with the gasifier main body or arranged separately from the gasifier main body. Because the external heat source is used to supply heat, the amount of biomass chemical energy converted into thermal energy is reduced, so much so that no additional oxidizer is added for oxidation reaction, this allows for high effective ingredient content in the synthesis gas, for highly efficient and economic subsequent utilization process, and for comprehensive utilization in combination with various forms of energy.

5. 发明授权

EP2799521B1 MICROWAVE PLASMA BIOMASS GASIFYING FIXED BED GASIFIER AND PROCESS 有权
公开(公告)号：EP2799521B1
公开(公告)日：2018-12-12
申请号：EP12863868.1
申请日：2012-10-26
申请人： Wuhan Kaidi Engineering Technology Research Institute Co., Ltd.
发明人： CHEN, Yilong , ZHANG, Yanfeng , XIA, Minggui , ZHANG, Liang
IPC分类号： C10J3/18 , C10J3/20 , C10J3/06 , C10J3/26 , C10J3/72
CPC分类号： C10J3/72 , C10J3/06 , C10J3/18 , C10J3/723 , C10J2300/0916 , C10J2300/0959 , C10J2300/0976 , C10J2300/1238 , C10J2300/1246 , Y02P20/129 , Y02P20/145
摘要： A microwave plasma biomass gasifying fixed bed gasifier comprising a vertically arranged gasifier body (2). The upper part of the gasifier body (2) is a gasifier clearance area (8). The lowest part of the gasifier body (2) is a fixed bed layer. Provided on the gasifier body are a raw material and fuel inlet, a product gas outlet, an oxygen/steam inlet (4 and 5). Provided at the bottom part of the gasifier body is a slug discharging outlet (7). Arranged at the product gas outlet is a synthesis gas monitoring unit (6). Arranged on the gasifier body is at least one section of microwave plasma generator (3). Also provided is a biomass gasification process utilizing the gasifier. The process comprises: 1) a biomass is fed into the gasifier via a feeder apparatus, and gasified on the microwave plasma fixed bed layer; a biomass fixed carbon content is subjected to a combustion reaction in an oxidation area on the bed layer, a high temperature flue gas is generated, the flue gas is transmitted upwards to a feeder area to heat a fuel fed into the gasifier, while at the same time, is subjected to a chemical reaction with high temperature steam injected from the lower layer oxygen/steam nozzle and an activity-rich microwave plasma-activated oxidizer of a first-section microwave plasma generator, where the temperature of a reaction area is controlled between 700°C and 1600°C; 2) a synthesis gas generated from the reaction is transmitted upwards to the clearance area, and is further cracked via a second-section microwave plasma generator; 3) a residual coke substance is transmitted downwards to the fixed bed layer to gradually release heat to maintain bed temperature, a burned biomass slag is discharged outside the gasifier via the slag discharging outlet; and 4) online monitoring is implemented via the synthesis gas monitoring unit arranged at the product gas outlet at the top part of the gasifier.

6. 发明授权

EP2801723B1 SOLAR ENERGY AND EXTERNAL SOURCE STEAM COMPLEMENTARY POWER GENERATION APPARATUS 有权
标题翻译：太阳能和外部源蒸汽互补发电装置
公开(公告)号：EP2801723B1
公开(公告)日：2017-09-20
申请号：EP12858668.2
申请日：2012-10-18
申请人： Wuhan Kaidi Engineering Technology Research Institute Co., Ltd.
发明人： CHEN, Yilong , YANG, Qingping , ZHANG, Yanfeng
IPC分类号： F03G6/06 , F01K11/02
CPC分类号： F03G6/00 , F01D17/00 , F01D17/02 , F01D17/04 , F01D17/06 , F01D17/08 , F01D17/085 , F01D19/00 , F01D19/02 , F01D21/00 , F01K11/02 , F03G6/003 , F03G6/005 , F03G6/06 , F03G6/065 , F03G6/067 , F22B1/006 , F24S20/20 , Y02E10/41 , Y02E10/44 , Y02E10/46 , Y02E20/16 , Y02P80/154
摘要： A solar energy and external source steam complementary power generation apparatus comprising a solar steam generation device, an external source steam regulator (15), a turboset (2) and a generator (1). A steam output end of the solar steam generation device is connected to a high-pressure steam inlet (3) of the turboset (2) through a first regulating valve (15); a steam output end of the external source steam regulator (15) is connected to the high-pressure steam inlet (3) of the turboset (2) through a second regulating valve (20) and a second switching valve (19). A low-pressure steam outlet (4) of the turboset (2) is connected to a circulating water input end of the solar steam generation device through a condenser (5), a deaerator (6), a water feed pump (7) and a first switching valve (16) in turn. An output end of the water feed pump (7) is connected to an external source steam water return bypass (11) through a fourth switching valve (23).
摘要翻译：一种太阳能和外部蒸汽源补充发电装置，包括太阳能蒸汽发生装置，外部蒸汽源调节器（15），涡轮机（2）和发电机（1）。太阳能蒸汽发生装置的蒸汽输出端通过第一调节阀（15）与涡轮机组（2）的高压蒸汽入口（3）连接。外源蒸汽调节器（15）的蒸汽输出端通过第二调节阀（20）和第二转换阀（19）连接到涡轮机组（2）的高压蒸汽入口（3）。涡轮机组2的低压蒸汽出口4通过冷凝器5，除气器6，给水泵7和冷凝器5连接到太阳能蒸汽发生装置的循环水入口端，第一转换阀（16）。供水泵（7）的输出端通过第四开关阀（23）连接到外部蒸汽回水旁路（11）。

7. 发明公开

EP2876080A1 PROCESS FOR COMPREHENSIVELY UTILIZING LOW CARBON EMISSION FISCHER-TROPSCH SYNTHESIS TAIL GAS 审中-公开
标题翻译：费托的综合使用方法SYNTHESEENDGAS低碳排放
公开(公告)号：EP2876080A1
公开(公告)日：2015-05-27
申请号：EP13819821.3
申请日：2013-07-11
申请人： Wuhan Kaidi Engineering Technology Research Institute Co., Ltd.
发明人： CHEN, Yilong , KUAI, Pingyu , GONG, Yan , ZHAN, Xiaodong , ZHANG, Yanfeng , JIN, Jiaqi
IPC分类号： C01B3/38
CPC分类号： C01B3/16 , C01B3/34 , C01B2203/0233 , C01B2203/0283 , C01B2203/04 , C01B2203/0445 , C01B2203/047 , C01B2203/0475 , C01B2203/062 , C01B2203/0805 , C01B2203/0827 , C01B2203/1241 , C01B2203/142 , C01B2203/84 , C07C1/0485 , C07C4/06 , C07C2523/755 , C10G2/00 , C10G2/30 , C10G2/332 , C10K1/005 , C10K3/04 , C10K3/06 , Y02P20/121
摘要： Disclosed is a process for comprehensively utilizing low carbon emission Fischer-Tropsch synthesis tail gas. In the process, a non-cycling tail gas generated after a Fischer-Tropsch synthesis reaction is steam reformed and converted into a hydrogen-rich synthesis gas, and then highly purified hydrogen is separated and extracted from the hydrogen-rich synthesis gas for use. The process comprises the following steps: 1) conducting a steam conversion reaction to obtain converted gas; 2) conducting a Fischer-Tropsch synthesis reaction to obtain a hydrocarbon fuel; 3) after a pre-reforming reaction, converting a hydrocarbon compound containing two or more carbon atoms into methane; 4) conducting a reforming reaction to convert the methane and steam into hydrogen and carbon monoxide; 5) separating the hydrogen and carbon monoxide from the gas; and 6) providing heat for a reforming reactor. The present invention effectively utilizes the Fischer-Tropsch synthesis tail gas, especially a tail gas containing a large amount of inert constituents, and converts the tail gas into the hydrogen for use. Furthermore, the present invention effectively utilizes the residual combustible constituents in the reformed gas after the hydrogen is separated, thus improving energy utilization efficiency.
摘要翻译：公开了一种用于综合利用低碳排放费托合成尾气的方法。在这个过程中，费 - 托合成反应后生成的非循环尾气是蒸汽重整和转换成富氢的合成气体，然后高度纯化的氢被用于分离并从富含氢气的合成气萃取。该方法包括以下步骤：1）在进行蒸汽转化反应以得到转化气体; 2）进行费 - 托合成反应得到的烃燃料; 3）之后的预重整反应，将含两个或多个碳原子为甲烷的烃化合物; 4）在进行重整反应的甲烷和蒸汽转化成氢和一氧化碳; 5）分离从气体中的氢气和一氧化碳; 和6），用于重整反应器提供热量。本发明有效地利用了费 - 托合成尾气，爱尤其是含有大量的惰性成分的尾气和尾气转换成氢以供使用。进一步，本发明有效地利用了重整气体中的残余的可燃成分的氢被分离之后，由此提高能量利用效率。

8. 发明公开

EP2716910A1 DISC-TYPE SOLAR STIRLING ENGINE POWER GENERATION DEVICE CAPABLE OF OPERATING CONTINUOUSLY DAY AND NIGHT 审中-公开
标题翻译： TAG IN NACHT BETREIBBARE STRMERZEUGUNGSVORRICHTUNG MIT EINEM STIRLINGMOTOR MITSCHEIBENFÖRMIGENSOLARZELLEN
公开(公告)号：EP2716910A1
公开(公告)日：2014-04-09
申请号：EP12789424.4
申请日：2012-05-23
申请人： Wuhan Kaidi Engineering Technology Research Institute Co., Ltd.
发明人： CHEN, Yilong , YANG, Qingping , ZHANG, Yanfeng
IPC分类号： F03G6/00 , F02G1/043
CPC分类号： F03G6/068 , F02G1/043 , F02G2254/10 , F02G2254/30 , F03G6/02 , Y02E10/46
摘要： A disc-type solar Stirling engine power generation device capable of operating continuously day and night comprises a solar disc-type Stirling engine power generation unit (1). A burner (2) and a burner position adjustment mechanism (3) capable of adjusting a burning opening of the burner to aim at a heat receiver of the disc-type solar Stirling engine unit or leave the heat receiver are disposed on each disc-type solar Stirling engine unit. The position adjustment mechanism is installed on a support (1a) of the disc-type solar Stirling engine. The burner (2) is installed on the position adjustment mechanism. A fuel supply system (4) of the burner is connected to the burner through a main switching valve (4c), a branch switching valve (5), a regulation valve (6), and a flexible fuel pipe (7). The Stirling power generation device is capable of stably generating power during nights and cloudy days.
摘要翻译：能够日夜不间断运转的盘式太阳能斯特林发动机发电装置由太阳能盘型斯特林发动机发电机组（1）构成。能够调节燃烧器的燃烧口的燃烧器（2）和燃烧器位置调节机构（3）设置在盘型太阳能斯特林发动机单元的热接收器上或离开热接收器太阳能斯特林发动机单元。位置调整机构安装在盘式太阳能斯特林发动机的支架（1a）上。燃烧器（2）安装在位置调节机构上。燃烧器的燃料供给系统（4）通过主切换阀（4c），分支切换阀（5），调节阀（6）和柔性燃料管（7）连接到燃烧器。斯特林发电装置能够在夜间和阴天内稳定地发电。

9. 发明公开

EP2659961A1 METHOD AND DEVICE FOR PREPARING HIGH TEMPERATURE WATER VAPOUR RICH IN ACTIVE PARTICLES USING PLASMA 审中-公开
标题翻译：方法和设备活性颗粒的高温蒸汽高比例的生产使用等离子
公开(公告)号：EP2659961A1
公开(公告)日：2013-11-06
申请号：EP11853087.2
申请日：2011-08-11
申请人： Wuhan Kaidi Engineering Technology Research Institute Co. Ltd
发明人： CHEN, Yilong , ZHANG, Yanfeng , CAO, Minxia , LI, Hong
IPC分类号： B01J19/08 , B01F5/04 , C10J3/00
CPC分类号： B01J12/002 , B01J19/088 , B01J2219/0869 , B01J2219/0883 , B01J2219/0894 , C10J3/00 , C10J2300/0916 , C10J2300/0946 , C10J2300/0976 , C10J2300/1238
摘要： Disclosed is a method and device for preparing a high temperature water vapor enriched in active particles using plasma, the device comprising a plasma generator (1) and a high temperature vapor generator (2), wherein the middle of one end of the high temperature vapor generator (2) is provided with a high temperature plasma inlet (4) in communication with an outlet (1b) of the plasma generator (1); the plasma generator (1) has an inlet (1a) for non-oxidizing gases; the high temperature plasma inlet (4) is surrounded by an annular vapor inlet (3d), which annular vapor inlet (3d) has rotary guide blades (7) mounted therein. The casing of the high temperature vapor generator (2) has a shape of stepped increasing stages divided into 1-4 stage(s), and an annular narrow orifice (3a, 3b, 3c) for vapor entrance is provided between two adjacent casing parts at each stage, with the annular narrow orifice (3a, 3b, 3c) connected to a vapor pressure feeding device (3). The method comprises the steps of: spraying the prepared vapor and the high temperature plasma working materials ionized by the plasma generator (1) into the high temperature vapor generator (2) through their respective inlets, intensively mixing the high temperature vapor and the high temperature plasma, and heating and activating the vapor so as to form the vapor with active particle.
摘要翻译：公开的是用于制备使用等离子体在活性粒子富集的高温水蒸汽的方法及装置，该装置包括等离子体发生器（1）和一高温蒸汽发生器（2），worin高温蒸气的一端的中间发电机（2）连通的出口设置有高温等离子体入口（4）与（1）的等离子体发生器（图1b）; 等离子发生器（1）具有入口（1a）中的非氧化性气体; 高温等离子体入口（4）是由环形设计蒸气入口（3D）该环形设计蒸气入口（3D）具有旋转导向叶片（7）安装在其中的建筑物包围。高温蒸汽发生器（2）的壳体具有分为1-4级（S）阶梯增加段的形状，并且环形设计窄孔（3A，3B，3C），用于蒸气入口两个相邻的壳体部分之间提供在每个阶段，与环形设计窄孔（3A，3B，3C）连接到一个蒸气压送装置（3）。该方法包括以下步骤：喷雾制备的蒸气，并通过其respectivement入口由等离子体发生器（1）电离成高温蒸汽发生器（2）高温等离子体工作材料，充分混合的高温蒸汽和高温等离子体，并加热和活化的蒸气，从而形成与活性颗粒的蒸气。

10. 发明公开

EP3251745A1 MONODISPERSE TRANSITION METAL NANO-CATALYST FOR FISCHER-TROPSCH SYNTHESIS AND PREPARATION METHOD THEREFOR AND APPLICATION THEREOF 审中-公开
标题翻译：用于费 - 托合成的单分散过渡金属纳米催化剂及其制备方法及其应用
公开(公告)号：EP3251745A1
公开(公告)日：2017-12-06
申请号：EP16742731.9
申请日：2016-01-26
申请人： Wuhan Kaidi Engineering Technology Research Institute Co., Ltd.
发明人： CHEN, Yilong , ZHENG, Shenke , CHEN, Jiangang , SONG, Dechen , ZHAN, Xiaodong , ZHANG, Yanfeng
IPC分类号： B01J23/745 , B01J23/75 , B01J23/889 , C10G2/00
CPC分类号： C10G2/332 , B01J23/745 , B01J23/75 , B01J23/889 , B01J31/02 , B01J35/0013 , B01J35/12 , B01J37/0072 , B01J37/04 , B01J2231/62 , B01J2531/005 , C10G2/00
摘要： A monodisperse transition metal nano-catalyst for Fischer-Tropsch synthesis and a preparation method therefor and an application thereof. The catalyst comprises transition metal. The transition metal is stably dispersed in an organic solvent in the form of monodisperse metal nanoparticles. The particle size of the transition metal is 1-100 nm. The specific surface area of the catalyst is 5-300 m 2 /g. The dispersity of the metal nanoparticles of the catalyst is high, and the catalyst can be directly applied to a Fischer-Tropsch synthesis reaction without filtering, cleaning, high-temperature roasting, and activated reduction.
摘要翻译：用于费 - 托合成的单分散过渡金属纳米催化剂及其制备方法及其应用。该催化剂包含过渡金属。过渡金属以单分散金属纳米颗粒的形式稳定地分散在有机溶剂中。过渡金属的粒径为1〜100nm。催化剂的比表面积为5-300m 2 / g。催化剂的金属纳米粒子的分散性高，可以不经过滤，清洗，高温焙烧，活化还原而直接应用于费 - 托合成反应。

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