| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 1 | 一种环保生物颗粒炉 | CN201610490735.6 | 2016-06-29 | CN106016271A | 2016-10-12 | 朱广友; 饶冰 |
| 本发明公开了一种环保生物颗粒炉，包括方形炉体，炉体外部设有保温层，炉体上方设有进料口和出气口，所述进料口上方设有绞龙，进料口上设有过滤网，过滤网周围设有一圈圆弧凸起，炉体侧面中部设有燃烧器，所述燃烧器下方设有气嘴，所述气嘴面对的炉体内壁为半圆形，炉体下方设有积灰室，积灰室下方设有出料口，炉体与积灰室通过铁丝网隔开，本发明结构精巧，使用方便，能够控制进料大小，炉体内燃烧效率高，运行稳定，使用时间长。 | ||||||
| 2 | 一种防止回火的垃圾干燥焚烧炉 | CN201611018510.7 | 2016-11-18 | CN106402888A | 2017-02-15 | 刘金山 |
| 本发明涉及一种防止回火的垃圾干燥焚烧炉，包括炉体，所述炉体包括外炉壳和内炉壳，所述外炉壳和内炉壳之间为真空保温层，所述内炉壳内设置内炉腔、垃圾干燥腔和中转箱，所述垃圾干燥腔设置在内炉腔外侧，垃圾干燥腔上端连接进料槽，所述内炉腔和垃圾干燥腔之间设置倾斜导料板，所述倾斜导料板下端连接中转箱，所述中转箱上下两端设置进料阀和出料阀，所述内炉腔下端还连接助燃料加料通道，所述助燃料加料通道上设置进料门，内炉腔上端设置烟气通道，所述防止回火的垃圾干燥焚烧炉，可通过垃圾燃烧产生的热量烘干垃圾，节约能源，节约空间，且设置中转箱，防止垃圾干燥箱内的垃圾被引燃。 | ||||||
| 3 | 一种车间废气处理装置 | CN201610927625.1 | 2016-10-31 | CN106352357A | 2017-01-25 | 刘风云 |
| 本发明公开了一种车间废气处理装置，从车间内抽出的废气通过离心风机进入第一热交换室的换热装置进行预热，预热后进入燃烧室，通过高温燃烧将废气中的有机物分解为二氧化碳和水，形成洁净的烟气，此时的烟气温度较高，无法直接排出，设置烟气再次进入第一热交换室为换热装置本身加热，使得烟气温度大大降低，为了提高热源利用率还设置了第二热交换室，通过为水循环管路继续加热进行降温，使得烟气达到排放的温度，可以满足用户的实际需求，便于在产业上推广和应用。 | ||||||
| 4 | 飞灰处理系统 | CN201510801554.6 | 2015-11-18 | CN105465791A | 2016-04-06 | 丁奇勇; 吕溥; 刘向坤; 郝迎志; 姜鸿安; 王福核; 戴立虹 |
| 本发明提供了一种飞灰处理系统，用于处理焚烧产生的飞灰，包括第一燃烧装置，以及，与所述第一燃烧装置连通的第二燃烧装置；所述第一燃烧装置用于利用400—700℃的温度将飞灰预热；所述第二燃烧装置用于利用1100—1600℃的温度对预热后的飞灰进行加热熔化；并且，所述第二燃烧装置还包括液态排渣口，熔融状态的飞灰经所述液态排渣口排出。本发明飞灰处理系统具有很好通用性且能耗低。 | ||||||
| 5 | 一种集散式废气处理系统及处理方法 | CN201710154121.5 | 2017-03-15 | CN106907721A | 2017-06-30 | 何群伟; 李良城 |
| 本发明公开了一种集散式废气处理系统及处理方法，包括处理中心、存储仓库以及多个废气收集点，在处理中心设有废气处理装置和监控终端，在每个废气收集点都设有废气收集器，在处理中心、废气收集器、存储仓库内均设有无线通信模块，处理中心和存储仓库以及废气收集器之间均通过无线通讯模块进行通讯，工厂通过密封的风管将产生的废气送到废气收集器，当废气收集器中的废气浓度饱和后通过无线通信模块向处理中心发出信号；处理中心收到废气收集器的信号后通向存储仓库发出信号；存储仓库派出集装箱货车去用空的废气收集器替换已经饱和的废气收集器，并将饱和的废气收集器送到处理中心进行处理，本发明解决小工厂买不起，用不起废气处理装置的问题。 | ||||||
| 6 | 一种剩余石化油泥渣与城市污泥混合燃烧资源化利用的方法 | CN201710181636.4 | 2017-03-23 | CN106885251A | 2017-06-23 | 李进平; 胡洁琼; 甘金华; 伍亮; 徐琼 |
| 本发明公开了一种剩余石化油泥渣与城市污泥混合燃烧资源化利用的方法，步骤是：（1）剩余石化油泥渣与城市污泥的预处理：将剩余石化油泥渣和城市污泥分别在一定条件下烘至恒重，经过研磨后得到不同样品；（2）混合样品的制备：将剩余石化油泥渣样品与城市污泥样品按照质量百分比进行混合，剩余石化油泥渣样品占混合样品总质量的10%~90%；（3）混合样品燃烧特性分析：将混合样品，剩余石化油泥渣样品和城市污泥样品分别在氧浓度的气氛下，用不同的升温速率，将其加热得到的TG和DTG曲线图。方法易行，操作简便，不仅能提高剩余石化油泥渣的使用率，而且还能提高城市污泥的燃烧效率，具有良好的环境效益、社会效益和经济效益。 | ||||||
| 7 | 一种电池生产用废弃橡胶纸环保型焚烧处理设备 | CN201611015665.5 | 2016-11-18 | CN106524192A | 2017-03-22 | 吴保康 |
| 本发明属于电池生产技术领域，尤其涉及一种电池生产用废弃橡胶纸环保型焚烧处理设备。本发明要解决的技术问题是提供一种焚烧均匀、环保性高、处理效果佳的电池生产用废弃橡胶纸环保型焚烧处理设备。为了解决上述技术问题，本发明提供了这样一种电池生产用废弃橡胶纸环保型焚烧处理设备，包括有底板、左架、右架、支杆、水箱、软管、单向阀、出气口、缸体、活塞、推杆、盘形凸轮、第一滑块、第二滑块等；底板顶部左端焊接有左架，左架右侧上部通过挂钩连接的方式对称连接有弹簧。本发明达到了焚烧均匀、环保性高、处理效果佳的效果，并且，本设备结构合理，制作成本低和易于维修，又因为有加强筋的作用。 | ||||||
| 8 | 一种垃圾破碎装置 | CN201610427940.8 | 2016-06-16 | CN105903751A | 2016-08-31 | 李珊珊 |
| 本发明公开一种垃圾破碎装置，具体涉及垃圾处理装置技术领域。包括进料口、压碎装置、高温处理装置、回收装置，所述进料口的右端设置有压碎装置，压碎装置的右端设置有高温处理装置，高温处理装置的右端设置有回收装置，压碎装置包括压碎机本体、压力机、冲头，压力机设置在压碎机本体顶部，冲头设置在压力机上。所述进料口设置在压碎装置左上端。所述冲头包括圆形底座、圆柱形冲刀。本发明具有结构简单、针对目前对垃圾进行碾压处理的方式优化，实现可对各种分类的垃圾统一处理等优点。 | ||||||
| 9 | 用于将分解热供给到废轮胎的碳处理系统 | CN200980155181.2 | 2009-11-23 | CN102292597A | 2011-12-21 | 全永珉 |
| 本发明涉及一种用于将分解热供给到废轮胎的碳处理系统。本发明的该碳处理系统包括：碳储存箱，该碳储存箱接收从用于热分解废轮胎的热分解炉中分离的碳；燃烧器，该燃烧器接收热分解废轮胎的过程中产生的蒸汽中包含的油或者气体，并燃烧接收到的油或气体；以及燃烧炉，该燃烧炉布置在所述燃烧器的一侧，以使用该燃烧器作为点火源来燃烧由所述碳储存箱供给的碳，并将燃烧过程产生的热供应至热分解炉。本发明如此构造的系统完全燃烧从废轮胎分离的碳，以防止污染，并且重新利用燃烧过程产生的热，以最大化其操作经济性，因此具有极大的工业实用性。 | ||||||
| 10 | SYSTEM FOR USING HEAT TO PROCESS AN AGRICULTURAL PRODUCT, A FLUIDIZED BED COMBUSTOR SYSTEM, AND METHODS OF EMPLOYING THE SAME | US12114347 | 2008-05-02 | US20080271335A1 | 2008-11-06 | Glenn D. Kimball |
| Systems and related methods of using heat to process an agricultural product are provided. The system comprises a circulating fluidized bed combustor, a first conduit system, and an indirect heating dryer. The circulating fluidized bed combustor comprises a combustion chamber configured to combust a fuel to generate a mixture comprising hot gases and particulate matter, and a separation chamber configured to separate at least a portion of the particulate matter from the mixture to form a flow of cleaned hot gas. The first conduit system is configured to conduct the cleaned hot gas to a heat exchanger. The indirect heating dryer is in heat conductive contact with the heat exchanger and configured to use the heat from the cleaned hot gas to indirectly dry the agricultural product without contacting the agricultural product with the cleaned hot gas. The system and methods provide hot gas for efficient and low cost energy formed from alternative and lower cost fuels, including biomass sources, and allows for flexibility and efficiency in numerous manufacturing processes. | ||||||
| 11 | DEVICE USING Ni-BASED HEAT RESISTANT ALLOY FOR INCINERATION OR GASIFICATION | JP2003367112 | 2003-10-28 | JP2007154213A | 2007-06-21 | MATSUOKA KEI; NOGUCHI MANABU; SAKAMOTO HIDEYUKI |
| <P>PROBLEM TO BE SOLVED: To provide a device for incinerating or gasifying a waste material or solid fuel such as coal, which has enhanced durability and function in comparison with a conventional device by forming a portion that is particularly required to have high-temperature corrosion resistance with the use of an alloy having the high-temperature corrosion resistance. <P>SOLUTION: The device for incinerating or gasifying the waste material or the solid fuel such as coal employs a Ni-based heat resistant alloy in a member or equipment composing the device. The heat resistant alloy comprises, by mass%, 23 to 40% Cr, 5 to 15% W, 0.3 to 4% Si, 1.5 to 2.5% Al, 0.1 to 5% of at least one element selected from among Ti, Zr, Hf, V, Nb and Ta, 0.1 to 0.5% C, 2.0% or less Mn, 5% or less Fe, and the balance Ni with unavoidable impurities. The Ni-based heat resistant alloy includes Nb for converting carbides into a Nb compound, or an additive element for inhibiting a deficient phase from being produced. <P>COPYRIGHT: (C)2007,JPO&INPIT | ||||||
| 12 | SYSTEM FOR USING HEAT TO PROCESS AN AGRICULTURAL PRODUCT, A FLUIDIZED BED COMBUSTOR SYSTEM, AND METHODS OF EMPLOYING THE SAME | US13950391 | 2013-07-25 | US20130305557A1 | 2013-11-21 | Glenn D. Kimball |
| Systems and related methods of using heat to process an agriculture/product are provided. The system comprises a circulating fluidized bed combustor, a first conduit system, and an indirect heating dryer. The circulating fluidized bed combustor comprises a combustion chamber configured to combust a fuel to generate a mixture comprising hot gases and particulate matter, and a separation chamber configured to separate at least a portion of the particulate matter from the mixture to form a flow of cleaned hot gas. The first conduit system is configured to conduct the cleaned hot gas to a heat exchanger. The indirect heating dryer is in heat conductive contact with the heat exchanger and configured to use the heat from the cleaned hot gas to indirectly dry the agricultural product without contacting the agricultural product with the cleaned hot gas. The system and methods provide hot gas for efficient and low cost energy formed from alternative and lower cost fuels, including biomass sources, and allows for flexibility and efficiency in numerous manufacturing processes. | ||||||
| 13 | System and Process for the Combustion of Solid Fuels | US13069014 | 2011-03-22 | US20120240831A1 | 2012-09-27 | Guilherme Martins Ferreira; Luis Filipe Von Rainer Fabiani; Luiz Felipe De Pinho; Rodrigo De Sousa Borges |
| A system that provides for the efficient combustion of solid fuels is disclosed. The system includes a combustion chamber, a solid fuel dosing system for determining an amount of solid fuel to supply to the combustion chamber, a solid fuel conveying air blower for conveying solid fuel from the solid fuel dosing system to the combustion chamber, and an air combustion fan for supplying air to the combustion chamber via air conveying piping. The system may optionally further include a measurement and auxiliary fuel control system for determining an amount of auxiliary fuel to supply to the combustion chamber. Combustion of the auxiliary fuel raises a temperature of the combustion chamber to a level suitable for combustion of the solid fuel. The combustion chamber may be mounted on a displacement trolley. | ||||||
| 14 | CARBON TREATMENT SYSTEM FOR SUPPLYING DECOMPOSITION HEAT TO WASTE TIRES | US13145985 | 2009-11-23 | US20110290162A1 | 2011-12-01 | Yeong Min Jeon |
| The present invention relates to a carbon treatment system for supplying decomposition heat to waste tires. The carbon treatment system of the present invention comprises: a carbon storage tank which receives carbon separated from a thermal decomposition furnace for thermally decomposing waste tires and which stores the received carbon; a burner which receives oil or gas contained in the steam generated during a process of thermally decomposing waste tires, and burns the received oil or gas; and a combustion furnace arranged at one side of the burner to burn the carbon supplied by the carbon storage tank using the burner as an ignition source and to supply heat generated during the combustion to the thermal decomposition furnace. The thus-configured system of the present invention completely burns the carbon separated from waste tires to prevent contamination and reutilizes the heat generated during combustion to maximize the economical operation thereof, and therefore is of great industrial usefulness. | ||||||
| 15 | Verbrennungsanlage | EP13005633.6 | 2013-12-04 | EP2746661A2 | 2014-06-25 | Kaiser, Sebastian; Wojik, Axel; Encic, Heinz; Glössl, Martin |
Bei einer Verbrennungsanlage (1) zum Verbrennen von Zusatzbrennstoffen mit einem ersten Zug (2), mit wenigstens einem Hauptbrenner (6) zum Verbrennen eines Hauptbrennstoffs und mit einem Wirbelbett (5) oder einem Rost, werden beim Verbrennen der Zusatzbrennstoffe mit einem Zusatzbrenner (8) entstehende Aschen mit einer Leiteinrichtung (11, 12) in einen vom Hauptbrenner (6) separierten Bereich geleitet.
|
||||||
| 16 | Brennstoffmatte | EP00810458.0 | 2000-05-26 | EP1158242A1 | 2001-11-28 | Burkart, Candid |
Es wird zwecks Beschleunigung und Unterstützung der thermischen Oxidation eines Leichnams und zur Reduktion der Emissionen der Einäscherung eine Brennmatte (1) in Form eines flächigen Gebildes vorgeschlagen. Die Brennmatte besteht aus Kunststoff (2), vorzugsweise aus Kunststoff thermoplastischer Art, und dient zur Aufnahme von Metallpartikeln (3) aus Be, Mg, Ca, Sr, Ba, B, Al, Ga, In und Tl oder ihrer Legierung nebst anderen Substanzen (4), die so in den Kunststoff (2) eingeschlossen sind, dass weder die Lagerung der Brennmatte, noch ihre Handhabung noch der Abbrand im Ofen irgendwelche Gefahren pyrotechnischer Art bedeuten können. Zur Benützung wird die Brennmatte vorzugsweise auf den Leichnam gelegt und mit dem Leichnam in die Kammer der Einäscherung geschoben und dort verbrannt. |
||||||
| 17 | VERFAHREN ZUR VERWERTUNG VON PHOSPHORHALTIGEN ABFÄLLEN | EP13716180.8 | 2013-02-19 | EP2817564A2 | 2014-12-31 | Mallon, Joachim; Schaaf, Michael; Scheidig, Klaus |
| The invention relates to a method for utilizing phosphorous-containing wastes in facilities for the exclusive energy recovery of said wastes, such as mono-incinerators for sewage sludge and/or animal meal, during the co-incineration in power plants or during additional firings in cement industry furnaces or comparable furnaces of other branches of industry, in which method an installation for melt gasification of P-containing substances is integrated into existing or new facilities of said kind. Depending on the composition of the P-containing substance, said installation generates a metal melt, a lime-silico-phosphate-containing slag low in heavy metals, and a fuel gas, and the fuel gas is supplied as fuel to the facilities for the exclusive energy recovery. | ||||||
| 18 | FLUIDIZED BED GASIFICATION COMBUSTION FURNACE | EP97910620.0 | 1997-11-04 | EP1030150A1 | 2000-08-23 | NAGATO, Shuichi; OSHITA, Takahiro; MIYOSHI, Norihisa; TOYODA, Seiichiro; HOSODA, Shugo; KASHIMA, Nobutaka; NARUSE, Katsutoshi |
A gasification furnace and a combustion furnace are integrated with each other to form a single fluidized-bed gasification and combustion furnace in which unburned char generated in the gasification furnace is combusted in the combustion furnace, and the thus generated heat of combustion is utilized as a heat source for gasification. The fluidized-bed gasification and combustion furnace (1) comprises a gasification furnace (3) and a combustion furnace (4) which are divided by a first partition wall (2). In the gasification furnace (3), a revolving flow of the fluidized medium is formed by diffusion devices (32, 33) provided on furnace bottoms, and an upward flow of the fluidized medium partly flows in the combustion furnace (4). The combustion furnace (4) is divided into a main combustion chamber (6) and a heat recovery chamber (7) by a second partition wall (5). In the main combustion chamber (6), a revolving flow of the fluidized medium is formed by diffusion devices (34, 35) provided on furnace bottoms, and an upward flow of the fluidized medium partly flows in the heat recovery chamber (7). |
||||||
| 19 | Verfahren und Vorrichtung zum Verbessern des Bettmasse-Ausbrandes bei Wirbelschichtfeuerungen | EP91110461.0 | 1991-06-25 | EP0489226A1 | 1992-06-10 | Eickenberg, Leonhard |
Verfahren und Vorrichtung zum Verbessern des Bettmasse-Ausbrandes bei Feuerungen mit zirkulierender Wirbelschicht, bei denen wenigstens ein Teil des im Filter (6) anfallenden Flugstaubs einer Schmelzkammerfeuerung zugeführt und dort bei so hoher Temperatur nachverbrannt wird, daß die Asche schmilzt und sich als flüssige Schlacke abziehen läßt. Die Rauchgase der Schmelzkammer (12) werden der Wirbelschichtfeuerung in einer Zone mit Sauerstoffmangel zugeführt, so daß die im Rauchgas enthaltenen Schadstoffe in der Wirbelschichtfeuerung beseitigt werden. |
||||||
| 20 | 유동층가스화 연소로 | KR1020007004822 | 1997-11-04 | KR1020010031757A | 2001-04-16 | 나가토슈이치; 오시타다카히로; 미요시노리히사; 도요다세이이치로; 호소다슈고; 가시마노부타카; 나루세가츠토시 |
| 가스화로와연소로가일체화되어있고, 가스화로에서발생한미연숯을연소로에서연소시키고, 이연소열을가스화용열원으로서이용할수 있는유동층가스화연소로이다. 유동층가스화연소로(1)는제 1 칸막이벽(2)에의하여분할된가스화로(3)와연소로(4)를구비하고있다. 가스화로(3)에있어서는노바닥에있는산기장치(32, 33)에의하여유동매체의선회류가형성되고, 상승류의일부는연소로(4)로유입된다. 연소로(4)는제 2 칸막이벽(5)에의하여주연소실(6)과열회수실(7)로분할되어있다. 주연소실(6)에있어서는노바닥에있는산기장치(34, 35)에의하여유동매체의선회류가형성되고, 상승류의일부는열회수실(7)로유입된다. | ||||||
