| 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 | 一种高炉煤气催化燃烧方法 | CN201510246517.3 | 2015-05-15 | CN104864401A | 2015-08-26 | 王爱英; 张天锁; 王罗焕; 王英春 |
| 本发明提出了一种高炉煤气催化燃烧方法，其方法步骤如下：在发电锅炉燃烧器的下方或中心设置高炉煤气火焰发生器；打开高炉煤气燃气供给控制阀，同时给高能点火器供电使其连续发射电弧；在催化反应室内，高炉煤气与空气中的氧气遇到高能点火器发射的电弧发生连锁反应，产生出高炉煤气火焰；高炉煤气火焰发生器喷出的高炉煤气火焰作为伴烧火焰，引燃发电锅炉燃烧器喷出的高炉煤气，发电锅炉运行。本发明的有益效果如下：大幅度降低伴烧燃气成本，使高炉煤气放散燃烧处理运行费用基本为零，节约燃料，提高企业的经济效益。 | ||||||
| 2 | 一种节能煤化工废水深度处理系统及其处理方法 | CN201410713950.9 | 2014-11-28 | CN104402160A | 2015-03-11 | 马涛; 郝春红; 刘强; 鲍利; 苟晓东; 靖玉明 |
| 一种节能煤化工废水处理系统及其处理方法，该系统包括正渗透膜浓缩装置和多效蒸发器，正渗透膜浓缩装置包括FO膜密闭交换箱、汲取液回收利用装置和清水回收装置，FO膜密闭交换箱至少设置一级，汲取液回收利用装置与各级FO膜密闭交换箱分别通过电动阀门连接，清水回收装置与汲取液回收利用装置连接，各级FO膜密闭交换箱依次通过排液电动阀门连接，且均通过超越电动阀门与母液焚烧炉连接。该方法针对煤化工废水的高渗透压特性，通过配制依数性更高的汲取液，利用溶液的依数性差异带来的渗透压差，使煤化工废水得到高效浓缩的同时回收循环利用水资源，产生电能；运行过程实现自动联锁控制，可根据不同进水条件调整运行方式。 | ||||||
| 3 | 使用聚集的太阳光的热氧化器的改进 | CN201180016190.0 | 2011-01-24 | CN102821834A | 2012-12-12 | 勒法特·埃尔·查勒比; 奥弗奈尔·亨利·帕瑞 |
| 本发明公开一种挥发性有机化合物处理设备，用于处理基本上不透明的挥发性有机化合物，所述处理设备包括：挥发性有机化合物在其中被处理的处理腔(24)和太阳能引导装置(8)。太阳能引导装置(8)包括管状结构，所述管状结构具有：第一端部，位于处理腔(24)的外部，并具有第一入口(14)和第二入口(16)，聚集的太阳光通过第一入口被接收，大致光学上透明的气体流通过第二入口被接收。太阳能引导装置(8)具有第二端部(18)，第二端部通向处理腔(24)并且终止在喷嘴中，喷嘴提供用于大致光学上透明的气体和聚集的太阳光的出口。在使用中，光学上透明的气体以射流中排出该装置的第二端部，以在处理腔(24)内的基本不透明的挥发性有机化合物中形成光学上透明的区域，太阳光能够在所述光学上透明的区域中传播。 | ||||||
| 4 | 污染处理装备 | CN201510874468.8 | 2015-11-27 | CN106439825A | 2017-02-22 | 张瑞麟 |
| 一种污染处理装备，它包括污水管、综合污水罐、水泵、预处理装置、电磁阀、止回阀、柱塞计量泵、输水嘴、排烟气管、膨胀节、冷却水套、烘干箱进料管、压缩空气管等，涉及船舶污染处理、工业废渣、废气、医疗垃圾、高浓度有机废水等技术。其内容是，烘干箱、焚烧炉部分的烟筒、排气管两端分别安装小夹板法兰和大夹板法兰，且小夹板法兰的外径略小于大夹板法兰的内径；利用压力锅盖、密封碟、烘干斗面板、弹簧片技术解决运行中烘干斗的密封问题；采用矩形单层隔板结构增加焚烧炉迭层温度的传递，提高排烟气管和烘干箱、焚烧炉间的热传递效率，这样，使得污染处理装备易于安装、密封、节能。 | ||||||
| 5 | 用于煤焦油加工过程挥发性有机物的催化燃烧处理系统 | CN201610129672.1 | 2016-03-08 | CN105536369A | 2016-05-04 | 高家俊; 黄永红; 周全 |
| 本发明公开了一种用于煤焦油加工过程挥发性有机物的催化燃烧处理系统，包括依次连接的废气预处理系统、废气缓冲系统以及废气催化燃烧系统，其中，废气预处理系统包括依次连接的废气吸收装置和用于过滤废气中颗粒物的过滤装置，废气吸收装置包括文氏管、循环槽、吸收塔、液体冷却器以及循环泵；废气缓冲系统包括依次连接的第一风机和气柜；废气催化燃烧系统包括催化反应器以及用于预热催化反应器的管式加热炉。本发明提出的催化燃烧处理系统具有脱除效率高、选择性好、能耗低以及无洗油造成的二次污染的优点。 | ||||||
| 6 | 使用聚集的太阳光的热氧化器的改进 | CN201180016190.0 | 2011-01-24 | CN102821834B | 2014-08-13 | 勒法特·埃尔·查勒比; 奥弗奈尔·亨利·帕瑞 |
| 本发明公开一种挥发性有机化合物处理设备，用于处理基本上不透明的挥发性有机化合物，所述处理设备包括：挥发性有机化合物在其中被处理的处理腔(24)和太阳能引导装置(8)。太阳能引导装置(8)包括管状结构，所述管状结构具有：第一端部，位于处理腔(24)的外部，并具有第一入口(14)和第二入口(16)，聚集的太阳光通过第一入口被接收，大致光学上透明的气体流通过第二入口被接收。太阳能引导装置(8)具有第二端部(18)，第二端部通向处理腔(24)并且终止在喷嘴中，喷嘴提供用于大致光学上透明的气体和聚集的太阳光的出口。在使用中，光学上透明的气体以射流中排出该装置的第二端部，以在处理腔(24)内的基本不透明的挥发性有机化合物中形成光学上透明的区域，太阳光能够在所述光学上透明的区域中传播。 | ||||||
| 7 | 一种垃圾快速焚烧炉 | CN201510278338.8 | 2015-05-27 | CN104819471A | 2015-08-05 | 不公告发明人 |
| 本发明公开了一种垃圾快速焚烧炉，包括炉体、进料通道、污水箱，所述进料通道设置在炉体上部并与炉体内部相连通，在进料通道和炉体连接处设置有密封门，在进料通道内设置有进料传送带，所述进料通道顶部呈圆锥形，在进料通道顶端连接有雾气管道，所述雾气管道另一端与污水箱相连通，所述污水箱与炉体并列设置，在雾气管道内设置有引流风机和折流板，折流板位于污水箱正上方，在炉体内部设置有炉排和焚烧网，本装置通过设置驱动电机转动焚烧网使得掉落在焚烧网上的垃圾均匀铺设，保证垃圾燃烧充分，并且通过在进料通道外部包裹烟气换热管，通过高温烟气加热进料通道内垃圾使垃圾中的水分蒸发，使垃圾干燥，提高燃烧效果，保证垃圾燃烧充分。 | ||||||
| 8 | 一种节能综合化工废水深度处理系统及其处理方法 | CN201410713949.6 | 2014-11-28 | CN104402092A | 2015-03-11 | 马涛; 康兴生; 贾新强; 陈志鸿; 王家国; 刘剑 |
| 一种节能综合化工废水处理系统及其处理方法，该系统包括正渗透膜浓缩装置和多效蒸发器，正渗透膜浓缩装置包括FO膜密闭交换箱、汲取液回收利用装置和清水回收装置，FO膜密闭交换箱至少设置一级，汲取液回收利用装置与各级FO膜密闭交换箱分别通过电动阀门连接，清水回收装置与汲取液回收利用装置连接，各级FO膜密闭交换箱依次通过排液电动阀门连接，且均通过超越电动阀门与母液焚烧炉连接。该方法针对综合化工废水的高渗透压特性，通过配制依数性更高的汲取液，利用溶液的依数性差异带来的渗透压差，使综合化工废水得到高效浓缩的同时回收循环利用水资源，产生电能；运行过程实现自动联锁控制，可根据不同进水条件调整运行方式。 | ||||||
| 9 | 有价物回收装置及回收方法 | CN201280033321.0 | 2012-07-03 | CN103796737A | 2014-05-14 | 冈村聪一郎; 花田隆; 坂本好明 |
| 本发明提供一种有价物回收装置，能够将设备成本及运转成本抑制得低，能减轻二次燃烧后的气体处理负担。其解决方案是有价物回收装置（1），具备附设于水泥烧成装置（2）的焙烧炉（11），和将焙烧炉的排气返回到水泥烧成装置的返还路径（12）。通过在回收有价物的焙烧炉有效利用在水泥烧成装置中产生的热，变得不需要用于燃烧炉的燃料供给设备，并且能将运转成本抑制得低。能够通过存在于水泥烧成装置内的大量CaO来处理氧化气体，变得不需要用于处理氧化气体的特别的处理装置，与已往相比较，可大幅地降低设备成本及运转成本。焙烧炉能够从下部取入热，并能将焙烧炉的排气经由返还路径返回到水泥烧成装置的800℃以上的温度区域。 | ||||||
| 10 | THERMAL OXIDISERS, USING CONCENTRATED SUNLIGHT | US13575014 | 2011-01-24 | US20130053613A1 | 2013-02-28 | Rifat Al Chalabi; Ophneil Henry Perry |
| A VOC treatment apparatus is provided for treating substantially opaque VOCs and comprises a processing chamber (24) in which VOCs are treated; and a solar energy introducing device (8). The solar energy introducing device (8) comprises a tubular structure having a first end located external to the processing chamber (24) and having a first inlet (14) through which concentrated sunlight is received and a second inlet (16) through which a flow of substantially optically transmittant gas is received. The solar energy introducing device (8) has a second end (18) that opens into the processing chamber (24) and terminates in a nozzle providing an outlet for the substantially optically transmittant gas and the concentrated sunlight. In use the optically transmittant gas exits the second end of the device in a jet to create an optically transmittant zone in the substantially opaque VOCs within the processing chamber (24), in which zone the sunlight can travel. | ||||||
| 11 | Method of and apparatus for thermal degradation of waste | US26495 | 1998-02-19 | US6101958A | 2000-08-15 | Ralf Beckmann; Arvid Christmann; Joachim Dohmann; Kai Keldenich; Rolf Kummel; Frank Niermann; Wilhelm Ruben; Johannes Seippel |
| A method of and an apparatus for the thermal degradation of refuse, garbage and other waste material in which the waste material stream is reacted with air or oxygen in a reaction chamber for pyrolysis, destructive distillation or incineration of the waste material. The released thermal energy, spatial temperature distribution or outlet gas temperature is measured and used to control a feeder which supplies particles of a supplemental fuel, itself recovered from a waste material separate from the waste material stream, to the reaction chamber. | ||||||
| 12 | Thermal oxidisers, using concentrated sunlight | US13575014 | 2011-01-24 | US08524187B2 | 2013-09-03 | Rifat Al Chalabi; Ophneil Henry Perry |
| A VOC treatment apparatus is provided for treating substantially opaque VOCs and comprises a processing chamber (24) in which VOCs are treated; and a solar energy introducing device (8). The solar energy introducing device (8) comprises a tubular structure having a first end located external to the processing chamber (24) and having a first inlet (14) through which concentrated sunlight is received and a second inlet (16) through which a flow of substantially optically transmittant gas is received. The solar energy introducing device (8) has a second end (18) that opens into the processing chamber (24) and terminates in a nozzle providing an outlet for the substantially optically transmittant gas and the concentrated sunlight. In use the optically transmittant gas exits the second end of the device in a jet to create an optically transmittant zone in the substantially opaque VOCs within the processing chamber (24), in which zone the sunlight can travel. | ||||||
| 13 | Rotary kiln incinerator | US805698 | 1997-02-25 | US5727483A | 1998-03-17 | Kang-Shin Chen; Chung-Hsing Wu |
| A rotary incinerator for disposal of industrial waste is provided. The incinerator is slopedly and rotatably disposed to a slant support and has a plurality of spirally arranged tubular conveying ribs on entire inner periphery for squeezedly transmitting the incinerating waste from the lower portion to an exit in the tapered upper end so that the waste is stirred while incinerating and the slag and ash are automatically discharged via the exit, a combustion system worked together with a ventilation system at a lower end for supplying the flame and the fresh air into the incinerator, a drive system for driving the incinerator to rotate and a control device for controlling the operation of the above recited elements. The improvement is characterized in safe and rapid incineration of the industrial waste, therefore, economical. | ||||||
| 14 | Verfahren zur Regelung der Temperatur in thermischen Abfallbehandlungsanlagen und Abfallbehandlungsanlage | EP98101427.7 | 1998-01-28 | EP0860657A2 | 1998-08-26 | Beckmann, Ralf; Kümmel, Rolf, Prof. Dr.; Seippel, Johannes; Christmann, Arvid; Dohmann, Joachim, Dr.; Keldenich, Kai, Dr.; Niermann, Frank, Dr.; Rüben, Wilhelm |
Zur Regelung der Temperatur in thermischen Abfallbehandlunganlagen bestehend aus einem Reaktionsraum (1) und einem nachgeschalteten Abhitzekessel (2) wird als Zusatzbrennstoff ein aus Abfallstoffen gewonnener Substitutbrennstoff in staubförmiger, pulvriger oder körniger Form verwendet. Dieser Substitutbrennstoff (7) wird getrennt von den Abfallstoffen in den Reaktionsraum nach Maßgabe der Feuerleistung des Reaktionsraumes und/oder der Temperatur (9,11) am Austritt des Reaktionsraumes eingetragen. |
||||||
| 15 | 有価物回収装置 | JP2011147845 | 2011-07-04 | JP5697251B2 | 2015-04-08 | 岡村 聰一郎; 花田 隆 |
| 16 | Device for recovering valuables and recovery method | JP2011147845 | 2011-07-04 | JP2013014802A | 2013-01-24 | OKAMURA SOICHIRO; HANADA TAKASHI |
| PROBLEM TO BE SOLVED: To provide a device for recovering valuables, which can reduce operation cost and reduce a burden of gas treatment after secondary combustion.SOLUTION: The device for recovering valuables 1 includes a waste roasting furnace 11 disposed in a cement firing device 2 and a returning path for returning exhaust gas from the roasting furnace to the cement firing device. The exhaust gas from the roasting furnace can be returned via the returning path to a region of the cement firing device where the temperature is 800°C or higher. The roasting furnace can be used as a reverberatory furnace for heating wastes W in a hearth by reflecting heat generated in the cement firing device, thereby constructing an interior of the roasting furnace to face the region of 800°C or higher temperature. The roasting furnace may also be used as a fixed furnace 23 for heating the wastes with combustion gas from the cement firing device, thereby constructing an isolation site for the combustion gas from the cement firing device to be present in an area where the temperature is 500-1200°C. | ||||||
| 17 | VALUABLE SUBSTANCE RECOVERY DEVICE AND RECOVERY METHOD | EP12807052 | 2012-07-03 | EP2730329A4 | 2015-05-27 | OKAMURA SOUICHIROU; HANADA TAKASHI; SAKAMOTO YOSHIAKI |
| 18 | VALUABLE SUBSTANCE RECOVERY DEVICE AND RECOVERY METHOD | EP12807052.1 | 2012-07-03 | EP2730329A1 | 2014-05-14 | OKAMURA Souichirou; HANADA Takashi; SAKAMOTO Yoshiaki |
[PROBLEM] To provide a valuable substance recovery device, etc. that can keep equipment costs and operation costs low and can reduce a burden of gas processing after secondary combustion. [SOLUTION] A valuable substance recovery device 1 provided with a calcining furnace 11 that is attached to a cement firing device 2 and a return path 12 for returning an exhaust gas from the calcining furnace to the cement firing device. By effectively utilizing heat generated by the cement firing device in the calcining furnace for recovering valuable substances, equipment for supplying fuel for the calcining furnace becomes unnecessary and operation costs can be kept low. Acidic gases can be processed using a large amount of CaO present inside the cement firing device, making special processing device for processing the acidic gases unnecessary and making it possible to reduce equipment costs and operation costs significantly compared to the past. The calcining furnace is able to take in heat from a lower portion thereof and discharge the same from the return path, and can return the calcining furnace exhaust gas to an 800°C or higher temperature region of the cement firing device via the return path. |
||||||
| 19 | IMPROVEMENTS IN THERMAL OXIDISERS, USING CONCENTRATED SUNLIGHT | EP11702486.9 | 2011-01-24 | EP2528678A1 | 2012-12-05 | Chalabi, Rifat Al; Perry, Ophneil Henry |
| A VOC treatment apparatus is provided for treating substantially opaque VOCs and comprises a processing chamber (24) in which VOCs are treated; and a solar energy introducing device (8). The solar energy introducing device (8) comprises a tubular structure having a first end located external to the processing chamber (24) and having a first inlet (14) through which concentrated sunlight is received and a second inlet (16) through which a flow of substantially optically transmittant gas is received. The solar energy introducing device (8) has a second end (18) that opens into the processing chamber (24) and terminates in a nozzle providing an outlet for the substantially optically transmittant gas and the concentrated sunlight. In use the optically transmittant gas exits the second end of the device in a jet to create an optically transmittant zone in the substantially opaque VOCs within the processing chamber (24), in which zone the sunlight can travel. | ||||||
| 20 | Verfahren zur Regelung der Temperatur in thermischen Abfallbehandlungsanlagen und Abfallbehandlungsanlage | EP98101427.7 | 1998-01-28 | EP0860657A3 | 1999-06-30 | Beckmann, Ralf; Kümmel, Rolf, Prof. Dr.; Seippel, Johannes; Christmann, Arvid; Dohmann, Joachim, Dr.; Keldenich, Kai, Dr.; Niermann, Frank, Dr.; Rüben, Wilhelm |
Zur Regelung der Temperatur in thermischen Abfallbehandlunganlagen bestehend aus einem Reaktionsraum (1) und einem nachgeschalteten Abhitzekessel (2) wird als Zusatzbrennstoff ein aus Abfallstoffen gewonnener Substitutbrennstoff in staubförmiger, pulvriger oder körniger Form verwendet. Dieser Substitutbrennstoff (7) wird getrennt von den Abfallstoffen in den Reaktionsraum nach Maßgabe der Feuerleistung des Reaktionsraumes und/oder der Temperatur (9,11) am Austritt des Reaktionsraumes eingetragen. |
||||||
QQ群二维码
意见反馈
意见反馈