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1. 发明申请

WO2016030495A1 PROCESS FOR CONTROLLING THE POROSITY OF CARBON BLACKS 审中-公开
标题翻译：控制炭黑的多孔性的方法
公开(公告)号：WO2016030495A1
公开(公告)日：2016-03-03
申请号：PCT/EP2015/069720
申请日：2015-08-28
申请人： ORION ENGINEERED CARBONS GMBH
发明人： VOGLER, Conny , TIMMERMANS, Eddy , SCHINKEL, Arndt-Peter
IPC分类号： C09C1/50 , C08K3/04 , C08L21/00
CPC分类号： C09C1/50 , B01D46/00 , B01D53/047 , B01D53/22 , B01D2253/102 , B01D2256/10 , B01D2257/104 , C01P2006/12 , C01P2006/19 , C08K3/04 , C08K2201/006 , C08L21/00 , F23J15/00 , F23J2217/60
摘要： The present invention relates to a furnace black having a STSA surface area of at 130 m 2 /g to 350 m 2 /g wherein - the ratio of BET surface area to STSA surface area is less than 1.1 if the STSA surface area is in the range of 130 m 2 /g to 150 m 2 /g, - the ratio of BET surface area to STSA surface area is less than 1.2 if the STSA surface area is greater than 150 m 2 /g to 180 m 2 /g, -the ratio of BET surface area to STSA surface area is less than 1.3 if the STSA surface area is greater than 180 m 2 /g; and the STSA surface area and the BET surface area are measured according to ASTM D 6556 and to a furnace process wherein the stoichiometric ratio of combustible material to O 2 when forming a combustion gas stream is adjusted to obtain a k factor of less than 1.2 and the inert gas concentration in the reactor is increased while limiting the CO 2 amount fed to the reactor. Also provided is an apparatus for conducting the process according to the present invention.
摘要翻译：本发明涉及STSA表面积为130m 2 / g〜350m 2 / g的炉黑，其中如果STSA表面积在以下范围内，则BET表面积与STSA表面积的比例小于1.1 130 m2 / g至150 m2 / g， - 如果STSA表面积大于150 m2 / g至180 m2 / g，则BET表面积与STSA表面积的比例小于1.2，BET表面积如果STSA表面积大于180 m2 / g，STSA表面积小于1.3; 并且根据ASTM D 6556测量STSA表面积和BET表面积，以及炉法，其中调节形成燃烧气体流时可燃材料与O 2的化学计量比以获得小于1.2的ak因子和惰性反应器中的气体浓度增加，同时限制供给反应器的CO 2量。还提供了用于进行根据本发明的方法的装置。

2. 发明申请

WO2008104766A1 RESIDENCE CHAMBER FOR PRODUCTS OF COMBUSTION 审中-公开
标题翻译：燃烧产物居住室
公开(公告)号：WO2008104766A1
公开(公告)日：2008-09-04
申请号：PCT/GB2008/000655
申请日：2008-02-27
申请人： BIOFLAME LIMITED , GRUNDMANN, Matthias
发明人： GRUNDMANN, Matthias
IPC分类号： F23G7/06 , F23J15/02 , B04C5/12
CPC分类号： F23G7/06 , B04C5/103 , B04C5/13 , B04C5/185 , B04C7/00 , F23J15/02 , F23J2217/40 , F23J2217/60
摘要： A residence chamber (1) for use in treating products of combustion is disclosed. The chamber comprises a first chamber (10), having a gas inlet (12) and a gas outlet (14), and a baffle (16), The baffle is located in the first chamber part and is arranged so as to cause gas entering the chamber through the inlet to travel initially in a first helical path and subsequently in a second helical path. The second helical path is in a second opposed axial direction and is inside the first helical path. The gas is arranged to exit the first chamber part through the outlet.
摘要翻译：公开了一种用于处理燃烧产物的居住室（1）。所述室包括具有气体入口（12）和气体出口（14）的第一室（10）和挡板（16）。所述挡板位于所述第一室部分中并且被布置成使气体进入通过入口的腔室最初以第一螺旋路径行进，随后在第二螺旋路径中行进。第二螺旋路径处于第二相对的轴向方向并且在第一螺旋路径的内部。气体被布置成通过出口离开第一室部分。

3. 发明申请

WO1998015357A1 BARRIER DISCHARGE CONVERSION OF SO2 AND NOx TO ACIDS 审中-公开
标题翻译：二氧化硫和氮氧化物的阻碍物排放转化为酸
公开(公告)号：WO1998015357A1
公开(公告)日：1998-04-16
申请号：PCT/US1997018263
申请日：1997-10-09
申请人： ZERO EMISSIONS TECHNOLOGY INC. , ALIX, Francis, R. , NEISTER, S., Edward , MCLARNON, Christopher, R.
发明人： ZERO EMISSIONS TECHNOLOGY INC.
IPC分类号： B03C03/00
CPC分类号： B03C3/017 , B01D53/32 , B01D53/73 , B01D2257/302 , B01D2257/404 , B01D2257/602 , B03C3/01 , B03C3/013 , B03C3/016 , B03C3/16 , C01B17/74 , C01B21/38 , C01G13/02 , F01N3/01 , F23J15/006 , F23J15/025 , F23J2215/10 , F23J2215/20 , F23J2215/60 , F23J2217/102 , F23J2217/40 , F23J2217/60 , Y02A50/2357 , Y02T10/20
摘要： A process and apparatus for reducing particulate, nitrogen oxides ("NOx"), sulfur dioxide ("SO2"), and mercury ("Hg") emissions from the combustion exhaust of fossil fuel fired plants while producing an end product that is commercially useful, comprising the steps of oxidizing Hg, NOx and SO2 using a barrier, pulse, corona, or electron beam electrical discharge apparatus (100) to produce HgO and the acids HNO3 and H2SO4 collecting the HgO, acids and particulates in a wet ESP (120), and separating the particulates from the collected acid mixture, then separating and concentrating the acids for industrial use.
摘要翻译：一种用于减少来自化石燃料燃烧厂的燃烧废气的颗粒状，氮氧化物（“NOx”），二氧化硫（“SO2”）和汞（“Hg”）排放的方法和装置，同时产生商业上有用的最终产物包括以下步骤：使用阻挡层，脉冲，电晕或电子束放电装置（100）氧化Hg，NO x和SO 2，以产生HgO，并且将酸性HNO 3和H 2 SO 4在湿ESP中收集HgO，酸和微粒（120 ），并将颗粒与收集的酸混合物分离，然后分离和浓缩工业用酸。

4. 发明申请

WO2013171711A2 HEATING PELLET STOVE OR BOILER EQUIPPED WITH A CLEANING SYSTEM 审中-公开
标题翻译：加热小桶或锅炉配有清洁系统
公开(公告)号：WO2013171711A2
公开(公告)日：2013-11-21
申请号：PCT/IB2013054013
申请日：2013-05-16
申请人： UNGARO SRL
发明人： UNGARO ANTONIO
IPC分类号： F23J1/02
CPC分类号： F23J1/02 , F23J1/04 , F23J2217/60 , F23L17/005
摘要： Heating pellet stove or boiler equipped with a cleaning system comprising a hearth (1), a suction fan (2), a flue (3), characterized by the fact that in combination comprises also a first compartment (4) that collects the ash of the hearth (1), a second compartment (5) that collects the dust positioned under the suction fan (2) of the fumes, a third compartment (6) that collects the dust positioned at the base of the flue (3) and that the third compartment is equipped with a scraping means (8) controlled from outside through a handle (9) and that the first, the second and the third compartment (4, 5, 6) may be each provided with a hole connected to a suction system for the removal of ash and dust.
摘要翻译：配备有包括炉底（1），吸风扇（2），烟道（3）的清洁系统的加热颗粒炉或锅炉，其特征在于，组合还包括第一室（4），其收集炉床（1），收集位于烟气吸入风扇（2）下方的灰尘的第二室（5），收集位于烟道（3）底部的灰尘的第三室（6）第三隔间配备有从外部通过手柄（9）控制的刮擦装置（8），并且第一，第二和第三隔室（4,5,6）可以各自设置有连接到吸力系统除灰和灰尘。

5. 发明申请

WO2011162023A1 ガス処理システム审中-公开
标题翻译：气体加工系统
公开(公告)号：WO2011162023A1
公开(公告)日：2011-12-29
申请号：PCT/JP2011/060255
申请日：2011-04-27
申请人：エドワーズ株式会社 , 中山泉 , 高橋克典
发明人：中山　泉 , 高橋　克典
IPC分类号： F23G7/06 , B01D53/46 , B01D53/68 , F23J15/08
CPC分类号： B01D47/00 , B01D53/323 , B01D53/68 , B01D2252/103 , B01D2257/2047 , B01D2257/553 , B01D2258/0216 , B01D2259/80 , F23G7/065 , F23J15/006 , F23J15/06 , F23J2217/102 , F23J2217/60 , F23J2219/80 , Y02C20/30
摘要：【課題】配管を含むガス処理システム全体の低価格化、コンパクト化、メンテナンス性の向上を図るのに好適なガス処理システムを提供する。【解決手段】ガス処理システム１は、半導体材料ガスであるシランや、プラズマＣＶＤ装置等の密閉チャンバＣ１、Ｃ２…Ｃｎ内を例えばプラズマでクリーニングする際のクリーニングガスとして使用するＮＦ３、ＣＦ４、Ｃ２Ｆ６、ＳＦ６、ＣＨＦ３、ＣＦ６等のガス状フッ化物を被処理ガスとし、これらの被処理ガスに対して燃焼分解及び洗浄集塵を行う水冷燃焼式除害装置２と、燃焼分解及び洗浄集塵後の処理ガスに対して電気集塵を行う電気集塵装置３と、電気集塵後の処理ガスを工場スクラバー設備５へ送る配管４と、を備えるものとする。
摘要翻译：提供一种气体处理系统，其适于实现包括管道的整个气体处理系统的成本降低，尺寸减小和可靠性的提高。一种气体处理系统（1）具有：水冷燃烧式危害除去装置（2），其具有作为半导体材料气体的硅烷和诸如NF3，CF4，C2F6，SF6，CHF3等气态氟化物，或CF6，当等离子体CVD装置等的封闭室（C1，C2 ... Cn）的内部被等离子体作为待处理气体清洁时，将其用作清洁气体，进行燃烧分解和清洗集尘待处理的气体; 电除尘装置（3），其在燃烧分解和清洗集尘后对处理气体进行集尘; 以及用于将电集尘后的处理气体送到工厂洗涤设备（5）的管道（4）。

6. 发明申请

WO1989008225A1 A FLUID BED COOLER, A FLUID BED COMBUSTION REACTOR AND A METHOD FOR THE OPERATION OF A SUCH REACTOR 审中-公开
标题翻译：流体床冷却器，流化床燃烧反应器和这种反应器的操作方法
公开(公告)号：WO1989008225A1
公开(公告)日：1989-09-08
申请号：PCT/DK1989000049
申请日：1989-03-03
申请人： AALBORG BOILERS A/S , HYLDGAARD, Niels, Joergen
发明人： AALBORG BOILERS A/S
IPC分类号： F23C11/02
CPC分类号： F28D13/00 , F22B31/0084 , F23C10/005 , F23C10/08 , F23C2206/103 , F23J2217/60
摘要： A fluid-bed combustion reactor (51) comprising a substantially vertical reactor chamber with a first inlet (9) at the reactor chamber lower portion (52) for the introduction of liquid and/or solid particulate material, and a second inlet (22) at a level below the first inlet for the introduction of gas for fluidization of particulate material within the reactor in order to maintain a primary fluid bed, an exhaust duct (28) at the reactor chamber upper portion for the withdrawal of exhaust gas and particles from the reactor, and a fluid-bed cooler (42) for particulate material, formed as an upwards open vessel with generally closed bottom and side walls and arranged so as to collect a portion of particulate material (64, 65) from the reactor chamber upper portion, said cooler comprising heat transfer means (43) such as tubes carrying a heat transfer medium at the inside and having said particulate material flowing at the outside, said cooler comprising at least one conduit (56) for the controlled returning of particulate material from the cooler to the primary fluid bed, and said cooler haing inlets at the bottom wall (68) for introduction of gas for fluidization of particulate material. The heat transfer means are divided into at least two sections, and the inlets for fluidization gas are divided into sections corresponding with the heat transfer means sections and provided with separate control means for the inflow of fluidization gas into each section.

7. 发明申请

WO2014102624A1 SYSTEM FOR GENERATING STEAM 审中-公开
标题翻译：蒸汽发生系统
公开(公告)号：WO2014102624A1
公开(公告)日：2014-07-03
申请号：PCT/IB2013/054500
申请日：2013-05-31
申请人： BABU, Sudarshan Anantharam
发明人： BABU, Sudarshan Anantharam
IPC分类号： F22B1/00 , F23J15/04 , F22D5/00 , F22D1/24
CPC分类号： F23B60/02 , F22B1/02 , F22D1/18 , F23J15/04 , F23J2215/50 , F23J2217/60 , F23J2219/40
摘要： A system for generating steam includes a steam generation unit (104). The steam generation unit (104) comprises a plurality of immersed water pipes (804) and a steam generator core (806). The immersed water pipes (804) are configured to receive water to be heated. The steam generator core (806) is configured to receive heat retention material, receive the immersed water pipes (804), wherein the immersed water pipes (804) are immersed in the heat retention material received by the steam generator core (806) and be heated by combustion of fossil fuel, thereby heating the heat retention material, which in turn heats the water in the immersed water pipes (804), thereby generating steam.
摘要翻译：一种用于产生蒸汽的系统包括蒸汽发生单元（104）。蒸汽发生单元（104）包括多个浸入式水管（804）和蒸汽发生器芯（806）。浸入式水管804被构造成接收待加热的水。蒸汽发生器芯（806）构造成接收保温材料，接收浸入的水管（804），其中浸入的水管（804）浸入由蒸汽发生器芯（806）容纳的保温材料中，并且通过化石燃料的燃烧加热，从而加热保温材料，其又加热浸入的水管（804）中的水，由此产生蒸汽。

8. 发明申请

WO2012120933A1 塩素バイパス排ガスの処理装置及び処理方法审中-公开
标题翻译：用于处理氯离子排气的装置和方法
公开(公告)号：WO2012120933A1
公开(公告)日：2012-09-13
申请号：PCT/JP2012/051519
申请日：2012-01-25
申请人：太平洋セメント株式会社 , 寺崎淳一 , 鈴木崇幸
发明人：寺崎　淳一 , 鈴木　崇幸
IPC分类号： C04B7/60 , B01D53/50 , B01D53/78 , B09B3/00 , F23J15/00
CPC分类号： F23J15/006 , B01D53/501 , B01D2251/404 , B01D2251/604 , B01D2257/302 , B01D2258/0233 , C04B7/364 , F23J2215/20 , F23J2217/50 , F23J2217/60 , F27B7/20 , F27D17/008
摘要：【課題】塩素バイパス排ガスを、セメント焼成系の熱損失を増加させることなく、セメント焼成系の安定運転を確保しながら、低コストで処理する。【解決手段】セメントキルン２の窯尻から最下段サイクロンに至るまでのキルン排ガス流路より燃焼ガスの一部Ｇを冷却しながら抽気し、抽気ガスＧ１から塩素バイパスダストＤ６を回収する塩素バイパス設備１に付設され、回収された塩素バイパスダストにアルカリ剤を添加しながらスラリー化する第１の溶解槽１２と、第１の溶解槽で生成されたスラリーＳ１を固液分離する固液分離装置１３と、固液分離装置で生成されたケークＣ１を再溶解させる第２の溶解槽１４と、第２の溶解槽で生成された再溶解後のスラリーＳ２を塩素バイパス設備の排ガスＧ４に接触させ、排ガスの脱硫を行う脱硫塔１１とを備える塩素バイパス排ガスの処理装置。
摘要翻译： [问题]以低成本处理氯旁路废气，而不增加水泥燃烧系统的热损失，同时确保水泥燃烧系统的安全运行。 [解决方案]一种用于处理与旁路系统（1）相关联的氯旁路废气的装置，其从来自水泥窑（2）的窑底的窑尾气体通道冷却并提取燃烧气体的一部分（G）到达最低旋风分离器，并且从提取气体（G1）中回收氯旁路灰尘（D6），该装置包括：第一溶解槽（12），用于在回收的氯旁路粉尘中添加碱剂; 用于分离在第一溶解槽中产生的浆料（S1）中的固体和液体的固液分离装置（13）; 用于再溶解在固液分离装置中产生的滤饼（C1）的第二溶解槽（14）; 和脱硫塔（11），用于在第二溶解槽中产生的再溶解后与氯旁通系统的废气（G4）接触浆料（S2）并对排气进行脱硫。

9. 发明申请

WO2011005131A2 INSTALLATION AND PROCEDURE FOR THE TREATMENT OF DOMESTIC AND INDUSTRIAL WASTE 审中-公开
标题翻译：处理国内和工业废物的安装和程序
公开(公告)号：WO2011005131A2
公开(公告)日：2011-01-13
申请号：PCT/RO2009/000023
申请日：2009-11-30
申请人： S.C. HELLENIC TILER INVEST SRL , MUSCALU, Vasile
发明人： MUSCALU, Vasile
CPC分类号： F23G5/006 , F23G5/02 , F23G5/46 , F23G2201/80 , F23G2206/203 , F23J2217/50 , F23J2217/60 , Y02E20/12
摘要： The invention refers to a plant and a procedure for treatment in continuous flow of garbage and industrial waste containing rubber, plastics, metals, pulp and other components resulting from household consumption or industrial use. The problem solved by the group of inventions, according to claimed inventions, is that domestic and industrial waste containing rubber and plastic is treated with the reduction of hazardous emissions resulting from combustion with the recovery of a fuel gas component by washing the smoke in water and placing the dirty water from smoke washing into a reactor, for chemical and physical transformations. It was unexpectedly found that waste recovery, due to the washing of smoke 'with water, whose pH is maintained at a value of 2... 5, such residues are retained by the liquid environment so that it is possible to treat the multi- phase system in a field where a certain energy expressed in eV/cm exists. Following this treatment, gas is generated, which contains hydrogen, oxygen and carbon in an atomic state, the temperature gradient decreases with a constant value forming an amorphous carbon deposit which is recovered, and gas is used as fuel gas... Thermal energy is recovered from the hot smoke at the boiler exit by means of a heat economizer which turns steam into gas at a certain temperature, gas composed of hydrogen and oxygen and which is used to maintain a constant temperature inside the boiler for household waste incineration when other domestic waste with low heating power is burned in the boiler.
摘要翻译：本发明涉及一种用于在家用消费或工业用途中产生的橡胶，塑料，金属，纸浆和其它成分的垃圾和工业废物的连续流动中的处理和处理程序。根据所要求的发明，由发明组解决的问题是，含有橡胶和塑料的家用和工业废物通过在水中洗涤烟雾来回收燃料气体成分而减少由燃烧产生的危险废气，将脏水从烟雾中放入反应器，进行化学和物理转换。意外地发现废物回收由于pH值维持在2〜5左右而被水清洗，这种残留物被液体环境所保留，存在以eV / cm表示的一定能量的场中的相位系统。在这种处理之后，产生气体，其含有原子状态的氢，氧和碳，温度梯度随恒定值而降低，形成无定形碳沉积物，回收，并将气体用作燃料气体。热能是从锅炉出口处的热烟回收，通过将蒸汽转变成一定温度的气体，由氢气和氧气组成的气体，用于在锅炉内保持恒温，用于家庭废物焚烧时的其他国内在锅炉中燃烧具有低加热功率的废物。

10. 发明申请

WO2008128390A1 活塞式节能除尘系统审中-公开
公开(公告)号：WO2008128390A1
公开(公告)日：2008-10-30
申请号：PCT/CN2007/002480
申请日：2007-08-17
申请人：韩贵胜
发明人：韩贵胜
IPC分类号： B01D50/00 , B01D47/02 , F04B19/22 , F23L15/04
CPC分类号： F23L15/04 , B01D47/021 , F23J15/006 , F23J15/022 , F23J15/06 , F23J2217/50 , F23J2217/60 , F23J2219/70 , Y02E20/348
摘要： A piston type energy-saving dust collecting system includes a piston type dust collector (201), a heat exchanger (202), a heat radiator (208) and a dust collecting pool (209). The piston type dust collector transmits the flue dust into said heat exchanger (202), making said flue dust exchange heat with the ambient air through the helical type air pipe (203). The heated air is transmitted into the burner (206) so as to increase the temperature of the air blown into the burner (206), increase the temperature of the burner (206) and save energy. After decreasing the temperature of the flue dust, the flue dust is transmitted into said heat radiator (208) and the temperature of said flue dust is further decreased. Then the flue dust is sent into the dust collecting pool (209). Finally, the flue dust enters the funnel (2010) through the pipeline and is discharged from the funnel (2010).

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