子分类：
| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 101 | 风力和上升气流涡轮机 | CN200780020628.6 | 2007-04-20 | CN101460739A | 2009-06-17 | 巴里·罗斯·艾尔兰 |
| 本发明涉及发电领域，更具体而言，涉及使用风力涡轮机来发电。在烟囱的上部上安装垂直轴的风力涡轮机。在烟囱的外部上设置转子叶片，并且借助于短的驱动轴将旋转的转子叶片生成的机械能传递给发电机。使用所述驱动轴来驱动发电机中的转子，以在定子中感应电压。在替选的配置中，风力涡轮机和发电机是一体化的。转子叶片直接耦接于旋转的、感应电流的永磁体组或转子以便绕着静止的、产生电流的定子旋转。在任一配置中，转子叶片均利用与烟囱或主风关联的上升气流而旋转。 | ||||||
| 102 | 尤其用于橡胶制品的连续气体式烘焙炉 | CN200680005765.8 | 2006-01-09 | CN101128298A | 2008-02-20 | D·波梅勒 |
| 连续的气体式烘焙炉，其包括加热装置，所述加热装置对一烘焙区(29)进行加热，而待处理制品被移动穿过该烘焙区，所述气体式烘焙炉由至少一个模组(1、2、3、4)形成，所述模组包括：一气体燃烧器(5、6、7、8)的热交换器(13、14、15、16)、以及将被加热的空气朝烘焙区(29)推动及引导的装置(32、33、35、36、41、42)，其中，所述热交换器的气体燃烧回路与穿过所述烘焙区的热空气回路分离，热空气引导部件包括：把热空气输送到所述烘焙区(29)两侧的通道(38、39)；与经所述烘焙区中部排出空气的一空气排放通道(40)。本发明的特征在于它还包括：用于保证对气态排放物进行高温分解的装置，所述装置处理在炉子的给定区段中流动的一部分气体；以及至少一个催化床(76、76′)，其布置在所述热空气回路上。 | ||||||
| 103 | 在废钢基础上二次钢生产所用的方法和设备 | CN200580041578.0 | 2005-12-02 | CN101103126A | 2008-01-09 | M·迈恩 |
| 在废钢基础上的二次钢生产，其中，废钢(10)经过一个装料装置(1)被投入到一个废钢预热器(2)中，在此被预热，然后被送入到一个熔化设备(3)中，在此仅用一次能源加以熔化，离开熔化设备(3)的过程气体(19)不再用于直接预热废钢(10)，而是依本发明间接地通过加热一种气态预热介质例如空气(18)或惰性气体加以利用，从而实现：在能源上、流动技术上和空间布置上，使预热和熔化分开、后燃烧和预热分开。 | ||||||
| 104 | 清洁蓄热式燃烧器介质床的设备和方法 | CN200580037886.6 | 2005-10-25 | CN101057103A | 2007-10-17 | C·西马德; S·梅纳德; W·D·史蒂文斯; E·J·威尔逊; P·班克斯; L·贝莱; B·D·伯里奇; T·I·费尔普斯 |
| 燃烧炉的蓄热式燃烧设备和从该设备中移除污染物的方法。所述设备包括：在点燃过程中当提供燃料和燃烧气体时可周期性地引导加热气体和废气进入燃烧炉的燃烧器，包括耐火颗粒的介质床，和用于在所述点燃过程中将燃烧气体输送至所述燃烧器以及用于在所述点燃终止时从所述燃烧炉中抽出废气的管道。所述管道使所述燃烧气体和所述废气连续地穿过所述介质床。提供了周期性地输送除污气体的快速气流进入所述介质床的装置。所述快速气流具有足够的力以驱除来自废气并聚集在所述介质床中的污染物。 | ||||||
| 105 | 用于热量回收的方法和设备 | CN200580030868.5 | 2005-07-15 | CN101031673A | 2007-09-05 | 埃林·奈斯; 托尔比约恩·斯伦高; 奥托·K·索纽; 比约恩·P·莫克斯内斯 |
| 本发明涉及一种用于从自工业过程中，例如用于生产铝的电解过程，除去的废气中回收热量的方法和装置。热量通过抽出/吸取系统回收，其中废气包括灰尘和/或颗粒。当废气与热量回收部件接触时，热量被回收。热量回收部件的流动条件和结构使得在表面上的灰尘和/或颗粒的沉积物保持在稳定的受限制的水平。在优选的实施例中，热量回收部件具有圆形的或者延长的椭圆形截面并且可以装配有翅片或者肋。 | ||||||
| 106 | 燃气热量控制方法和装置 | CN200610004144.X | 2006-02-20 | CN1854609A | 2006-11-01 | 田边浩史; 山下秀和 |
| 本发明提供一种可在高炉煤气中混合2种增热用煤气(第1增热用煤气、第2增热用煤气)以进行热量控制等的燃气热量控制方法和装置。根据高炉煤气的混合流量(FFB)、转炉煤气的混合流量(FmL)、预先设定的高炉煤气热量(CALBF)和预先设定的转炉煤气热量(CALmL)，算出并预测第1混合煤气的热量，根据该预测的热量、设定热量(CAL)和预先设定的焦炉煤气热量(CALmC)，算出焦炉煤气的混合流量相对燃气轮机消耗燃气流量的流量比，根据该流量比和与燃气轮机消耗燃气流量相对应的燃气轮机燃气要求信号(CSO)，算出焦炉煤气的混合流量要求值，根据该混合流量要求值，控制燃气生成系统中设置的焦炉煤气流量控制阀的开度以控制焦炉煤气的混合流量。 | ||||||
| 107 | Regeneration rotary kiln | US14902273 | 2014-10-02 | US10094559B2 | 2018-10-09 | Norio Muto; Motoharu Suzuki; Toshiki Nakamura; Satoshi Kitaoka; Masashi Wada; Kazuhiko Kawai; Kazumi Hayashi |
| Provided is a regeneration rotary kiln capable of reducing the proportion of combustible gas in waste gas and capable of reducing cost for generating superheated steam.A regeneration rotary kiln (1) is characterized by including: a superheated steam generation unit (2) that generates superheated steam; a tube (3) capable of rotating about its axis and having a heating section (A) where, while the superheated steam is being supplied thereto, carbon fiber reinforced plastic (10) containing a matrix resin and carbon fibers is heated to generate combustible gas (10G) from the matrix resin to extract the carbon fibers (10S) from the carbon fiber reinforced plastic (10); a first combustion chamber (43a) that is placed outside the tube (3) and that burns the gas (10G) introduced from the heating section (A) to heat the heating section (A); and a second combustion chamber (43b) that burns the gas (10G) introduced from the first combustion chamber (43a) to supply heat for generating the superheated steam. | ||||||
| 108 | CONTINUOUS ANNEALING EQUIPMENT | US15756685 | 2016-08-19 | US20180245222A1 | 2018-08-30 | Takanori NAGAI |
| Continuous annealing equipment (1) including a cleaning device (11, 12) for performing a cleaning treatment on a steel strip (S) and an annealing device (12) for performing an annealing treatment on the steel strip (S) comprises an exhaust gas passage (31, 41) through which an exhaust gas discharged from the annealing device (12) flows, a solution circulation passage (32, 51) through which a cleaning solution used in the cleaning device (11, 12) circulates, and a heat exchanger (53) which forms a part of the solution circulation passage (32, 51) and contacts with the exhaust gas. | ||||||
| 109 | Continuous heating furnace | US14867370 | 2015-09-28 | US09982943B2 | 2018-05-29 | Kimiyoshi Satoh |
| A continuous heating furnace includes a furnace main body, a conveyance unit configured to convey a baking object W in the furnace main body, a plurality of heating sections heated by combustion, each having a first radiation surface configured to be heated by combustion and transfers heat to the baking object conveyed by the conveyance unit and arranged in the conveyance direction of the baking object in the furnace main body, and a cooling preheater having a second radiation surface configured to receive radiant heat from the baking object when being opposite to the baking object conveyed by the conveyance unit and a gas flow path configured to preheat a gas used for combustion in the heating section by the heat from the second radiation surface. | ||||||
| 110 | Carbon baking heat recovery ring furnace | US13794448 | 2013-03-11 | US09970710B2 | 2018-05-15 | Mike McGee; Tom Haines; Kenneth Meyer; Steve Hillock |
| Contemplated devices and methods reduce heat loss and energy demand of a carbon baking ring furnace by employing a preferably internal bypass conduit that feeds a portion of a heated cooling air stream from the cooling zone directly to the flue ducts of the firing and/or pre-heat zones. | ||||||
| 111 | DEVICE FOR HEATING IRON AND STEEL PRODUCTS, AND METHOD FOR HEATING IRON AND STEEL PRODUCTS | US15557586 | 2016-03-25 | US20180044758A1 | 2018-02-15 | Yasuyuki YAMAMOTO; Kimio IINO; Shinichi KOGA |
| A device for heating an iron and steel product (steel product), the device including: a preheating chamber for preheating the steel product; a heating chamber for heating the steel product to a desired temperature which is connected to the preheating chamber; a plurality of burners arranged so as to sandwich the steel product from above and below in the heating chamber; and a means for causing an exhaust gas containing combustion gas in the burners to flow into the preheating chamber, wherein the burners form flames with a fuel and an oxidizing agent having an oxygen concentration of 80 vol % or more and have a function of blowing away fats and oils adhered onto the surface of the steel product by the flames, and the preheating chamber has a structure for preheating the steel product by an exhaust gas which has been made to flow thereinto by the means. | ||||||
| 112 | Method and equipment for heat recovery | US14088942 | 2013-11-25 | US09732981B2 | 2017-08-15 | Erling Naess; Otto Kristian Sonju; Torbjorn Slungaard; Bjorn Petter Moxnes |
| The present invention relates to a method and equipment for recovering heat from exhaust gas removed from an industrial process, such as an electrolysis process for the production of aluminum. Heat is recovered by means of an extraction/suction system, where the exhaust gas contains dust and/or particles. The heat is recovered as the exhaust gas being brought into contact with heat-recovery elements. Flow conditions and the design of the heat recovery elements are such that the deposits of the dust and/or particles on the surfaces stated are kept at a stable, limited level. In preferred embodiments, the heat-recovery elements have a circular or an extended, elliptical cross-section and may be equipped with fins or ribs. | ||||||
| 113 | Treatment device and treatment method for chlorine bypass dust | US13806297 | 2011-06-08 | US09695086B2 | 2017-07-04 | Junichi Terasaki; Kenzaburou Kondou |
| In accordance with the present invention, there is provided a treat chlorine bypass dust while preventing increases in chemical cost and concentrations of heavy metals in clinker, and ensuring stability in quality of cement. In a chlorine bypass facility 1 extracting a part G of combustion gas, while cooling it, from a kiln exhaust gas passage, which runs from an inlet end of a cement kiln to a bottom cyclone, and recovering a high chlorine concentration chlorine bypass dust D5 from the extracted gas G1, a slurry S containing chlorine bypass dust and SO2 gas or/and CO2 gas are contacted with each other to obtain solid content. The slurry containing chlorine bypass dust and an exhaust gas from the chlorine bypass facility or/and the exhaust gas from the cement kiln can be contacted with each other, and the solid content can be fed to a cement finishing process, which allows cement with low CaO and Ca(OH)2 contents and with stable property such as setting time to be produced. | ||||||
| 114 | Device for the closed-loop control of process gases in a plant for producing directly reduced metal ores | US14128103 | 2012-06-01 | US09400139B2 | 2016-07-26 | Robert Millner; Jan-Friedemann Plaul; Norbert Rein; Gerald Rosenfellner |
| A device for closed-loop control of process gases (11) in a plant (8) for producing directly reduced metal ores includes at least one reduction unit (10), an appliance upstream of the reduction unit (10) for separating gas mixtures (18), a gas purification appliance (13) connected downstream of the reduction unit (10) for rate control of process gases (11). Process gases (11) are obtained by recycling from the production process itself and from a plant for pig iron generation (1) via a supply conduit (16). An open-loop pressure control appliance (15) upstream of a junction of the supply conduit (16) into a return conduit (14) for the process gases (11) such that a pressure level for the appliance for separating gas mixtures (18) is kept constant and the process gases (9,11) are controlled in a closed-loop manner in a plant for producing directly reduced metal ores (8). | ||||||
| 115 | Clinker kiln with slider for tertiary air duct | US13568731 | 2012-08-07 | US09121639B2 | 2015-09-01 | Jörg Hammerich; Robert Mathai |
| A slider unit for a tertiary air duct between a clinker cooler and a calciner of a clinker kiln line. The slider unit has at least one shutoff device, which is insertable into a tertiary air duct to seal it without further reducing the cross section of the tertiary air duct, and provides reliable sealing of the tertiary air duct and control of the tertiary air flow, if the slider unit has at least one control device which is insertable into a section of the tertiary air duct to reduce its cross section. | ||||||
| 116 | DEVICE FOR THE CLOSED-LOOP CONTROL OF PROCESS GASES IN A PLANT FOR PRODUCING DIRECTLY REDUCED METAL ORES | US14128103 | 2012-06-01 | US20140138884A1 | 2014-05-22 | Robert Millner; Jan-Friedemann Plaul; Norbert Rein; Gerald Rosenfellner |
| A device for closed-loop control of process gases (11) in a plant (8) for producing directly reduced metal ores includes at least one reduction unit (10), an appliance upstream of the reduction unit (10) for separating gas mixtures (18), a gas purification appliance (13) connected downstream of the reduction unit (10) for rate control of process gases (11). Process gases (11) are obtained by recycling from the production process itself and from a plant for pig iron generation (1) via a supply conduit (16). An open-loop pressure control appliance (15) upstream of a junction of the supply conduit (16) into a return conduit (14) for the process gases (11) such that a pressure level for the appliance for separating gas mixtures (18) is kept constant and the process gases (9,11) are controlled in a closed-loop manner in a plant for producing directly reduced metal ores (8). | ||||||
| 117 | METHOD AND EQUIPMENT FOR HEAT RECOVERY | US14088942 | 2013-11-25 | US20140069625A1 | 2014-03-13 | Erling NAESS; Otto Kristian SONJU; Torbjorn SLUNGAARD; Bjorn Petter MOXNES |
| The present invention relates to a method and equipment for recovering heat from exhaust gas removed from an industrial process, such as an electrolysis process for the production of aluminium. Heat is recovered by means of an extraction/suction system, where the exhaust gas contains dust and/or particles. The heat is recovered as the exhaust gas being brought into contact with heat-recovery elements. Flow conditions and the design of the heat recovery elements are such that the deposits of the dust and/or particles on the surfaces stated are kept at a stable, limited level. In preferred embodiments, the heat-recovery elements have a circular or an extended, elliptical cross-section and may be equipped with fins or ribs. | ||||||
| 118 | METALLURGICAL PLANT WITH EFFICIENT WASTE-HEAT UTILIZATION | US14005658 | 2012-03-08 | US20140000535A1 | 2014-01-02 | Robert Millner; Gerald Rosenfellner |
| A metallurgical plant has a plant positioned upstream of a steel-generating plant and has a gas-generating plant which generates an export gas. Carbon dioxide and/or water contained in the export gas is removed from the export gas in a separation device. A resulting product gas is heated, before being supplied to the upstream plant, in a firing unit through the combustion of a heating gas. Excess thermal energy produced during the combustion of the heating gas which is not used for heating the product gas is thermally utilized. The utilization may take place within the firing unit through steam generation and/or downstream of the firing unit to preheat the heating gas and/or an oxidation gas used for the combustion of the heating gas and/or through the pre-heating and/or drying of raw materials to be supplied to the upstream plant and/or to the gas-generating plant. | ||||||
| 119 | CARBON BAKING HEAT RECOVERY RING FURNACE | US13794448 | 2013-03-11 | US20130337391A1 | 2013-12-19 | Mike McGee; Tom Haines; Kenneth Meyer; Steve Hilock |
| Contemplated devices and methods reduce heat loss and energy demand of a carbon baking ring furnace by employing a preferably internal bypass conduit that feeds a portion of a heated cooling air stream from the cooling zone directly to the flue ducts of the firing and/or pre-heat zones. | ||||||
| 120 | Use of photovoltaics for waste heat recovery | US12031303 | 2008-02-14 | US08420928B2 | 2013-04-16 | Adam D. Polcyn |
| A device for recovering waste heat in the form of radiated light, e.g. red visible light and/or infrared light includes a housing having a viewing window, and a photovoltaic cell mounted in the housing in a relationship to the viewing window, wherein rays of radiated light pass through the viewing window and impinge on surface of the photovoltaic cell. The housing and/or the cell are cooled so that the device can be used with a furnace for an industrial process, e.g. mounting the device with a view of the interior of the heating chamber of a glass making furnace. In this manner, the rays of the radiated light generated during the melting of glass batch materials in the heating chamber pass through the viewing window and impinge on the surface of the photovoltaic cells to generate electric current which is passed onto an electric load. | ||||||
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