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 耐热燃料活化物质的安装方法以及燃烧装置 CN200980138517.4 2009-09-15 CN102165261A 2011-08-24 高桥清太郎; 伊东正浩
发明提供一种耐热燃料活化物质的安装方法以及燃烧装置。在将耐热性的燃料活化物质安装于锅炉等燃烧装置时,通过采用的适宜的安装方法即适宜的安装位置和安装面积来使燃烧活化效果迅速稳定并且廉价地使燃烧活化效果发挥发挥出来。当将在电磁波长为3μm~20μm的区域中具有0.85以上的光谱辐射率的耐热燃料活化物质安装到燃烧设备时,在比燃烧器的燃烧火焰的产生部位靠向后方的燃烧室外部或内部并且是温度为300℃以下的位置,以成为如下位置的50%以上的面积安装耐热燃料活化物质:该位置相当于燃烧圆锥部投影部分。
2 用于处理燃料以增加其发热量的装置 CN201380013031.4 2013-03-05 CN104160132A 2014-11-19 奥雷尔·埃纳凯
发明涉及一种用于处理燃料以增加它们的发热量的装置。根据所要求保护的发明的装置具有壳体(15)和取样管(10),其间放置有一些励磁单元(A),该励磁单元(A)中的每一个连接至沿螺旋路径前进通过取样管(10)的两根配线(11和12)中的每一根。
3 耐热燃料活化物质的安装方法以及燃烧装置 CN200980138517.4 2009-09-15 CN102165261B 2013-08-07 高桥清太郎; 伊东正浩
发明提供一种耐热燃料活化物质的安装方法以及燃烧装置。在将耐热性的燃料活化物质安装于锅炉等燃烧装置时,通过采用的适宜的安装方法即适宜的安装位置和安装面积来使燃烧活化效果迅速稳定并且廉价地使燃烧活化效果发挥发挥出来。当将在电磁波长为3μm~20μm的区域中具有0.85以上的光谱辐射率的耐热燃料活化物质安装到燃烧设备时,在比燃烧器的燃烧火焰的产生部位靠向后方的燃烧室外部或内部并且是温度为300℃以下的位置,以成为如下位置的50%以上的面积安装耐热燃料活化物质:该位置相当于燃烧圆锥部投影部分。
4 浆的制备装置及方法 CN201410698369.4 2014-11-27 CN105695008A 2016-06-22 余量; 薛俊利; 吕静; 毕喜婧; 朱迪恩·波林·奥本海姆
发明揭示浆的制备装置及方法,其中提供的一种水煤浆的制备装置包括:预处理装置,用来接收原煤和微波吸收剂,并用来混合所述微波吸收剂和原煤,所述微波吸收剂包括细渣和炭黑中的至少一种;微波产生装置,用来微波处理来自所述预处理装置的所述微波吸收剂和原煤的混合物;及制浆机,用来利用微波处理后的所述混合物制备水煤浆。本发明也提供了一种水煤浆制备方法。
5 化学燃料调节和激活 CN201380070307.2 2013-11-12 CN104919168A 2015-09-16 罗伊·爱德华·麦卡利斯特
公开了用于化学活化燃料以在内燃机中喷射和点火的方法、系统和设备。在一个方面中,一种引起燃烧的方法,包括将中间燃料物质转变为包括自由基的成分。中间燃料物质由使用燃料的化学转化形成,以及中间燃料物质具有相对于燃料的点火能量的较低的点火能量;将成分喷射入发动机燃烧室;以及在燃烧室中提供包括化剂的气态流体,以与成分在燃烧反应中反应,其中,成分的燃烧反应发生在相对于燃料物质的燃烧反应的能量平的减少的能量水平。
6 ADVANCED COAL UPGRADING PROCESS FOR A POWER STATION US13148945 2010-11-17 US20110314730A1 2011-12-29 Rodolfo Antonio M. Gomez
A coal or carbonaceous material upgrading process for power station use, the process comprising a number of steps. First comminuting the coal or carbonaceous to a comminuted material. Second pre-treating the comminuted coal with a pulsing single frequency microwave and vacuum to reduce its water and oxygen content; the pre-treating stage being carried out at a temperature of up to 180 C Third, treating the pre-treated comminuted material with a pulsing single frequency microwave energy under vacuum to optimize the volatile organic materials; the treatment stage being carried out at a temperature of up to 350 C. Next pyrolyzing the treated coal with a pulsing single frequency microwave and vacuum to produce a hot gas and a solid carbon residue; the pyrolyzing stage is carried out at a temperature of up to 720 C. The solid carbon residue can then be separated from the hot gas, the volatile organic materials condensed to produce a liquid hydrocarbon product and a gas product; and the solid material and the gas product fed to a power station to produce electricity therefrom. The microwave energy applied at each of the stages has a single frequency of 100 megahertz to 300 gigahertz, has circular polarisation, and is pulsed at a frequency of 2 to 50 kilohertz. The pre-treatment step, the treatment step, and the pyrolysis step can be done under vacuum.
7 化学燃料の調整及び活性化 JP2015542026 2013-11-12 JP2015536405A 2015-12-21 エドワード マキャリスター、ロイ
内燃機関における噴射及び点火のために燃料を化学的に活性化するための方法、システム及びデバイスが開示される。1つの態様では、燃焼を開始する方法は、化学的に活性な燃料、酸化体、イオン、又はラジカルのうちの少なくとも1つを含む成分に中間燃料物質を変換することであって、中間燃料物質が、燃料を使用して化学転換により形成され、中間燃料物質の点火エネルギーが、燃料の点火エネルギーよりも低い、変換することと、成分を燃焼チャンバへと噴射することと、燃焼反応において成分と反応するように、酸化体を含む気体流体を燃焼チャンバに提供することとを含み、成分の燃焼開始反応が、燃料の燃焼反応のエネルギーレベルに対して低減されたエネルギーレベルで生じる。
8 耐熱燃料活性化物質の装着方法及び燃焼装置 JP2010530710 2009-09-15 JPWO2010035423A1 2012-02-16 清太郎 高橋; 伊東 正浩; 正浩 伊東
ボイラ等の燃焼装置に対して耐熱性の燃料活性化物質を装着するに際して、適切な装着方法すなわち適切な装着場所と装着面積を採ることで燃焼活性化効果を迅速に安定してかつ安価に発揮させる。電磁波長3μm〜20μmの領域で、分光放射率が0.85以上を有する耐熱燃料活性化物質を燃焼装置に装着する場合において、耐熱燃料活性化物質を、バーナーの燃焼火炎の発生部位よりも後方の燃焼室外部又は内部であり、温度が300℃以下の場所であり、かつ燃焼コーン投影部分に相当する場所の50%以上となる面積で、装着させる。
9 INSTALLATION FOR TREATING A FUEL TO INCREASE ITS CALORIC POWER EP13766155.9 2013-03-05 EP2825750A1 2015-01-21 Enache, Aurel
The invention refers to an installation for treating fuels to increase their caloric power. The installation, according to the claimed invention has a housing (15) and a coupon (10) between which there are place some excitation units (A), each of these are attached to each of two wires (11 and 12) which follow a spiral path through the coupon (10).
10 CHEMICAL FUEL CONDITIONING AND ACTIVATION US14954870 2015-11-30 US20160319735A1 2016-11-03 Roy Edward McAlister
Methods, systems, and devices are disclosed for chemically activating a fuel for injection and ignition in a combustion engine. In one aspect, a method to initiate combustion includes transforming an interim fuel substance into constituents including radicals, the interim fuel substance formed by a chemical conversion using a fuel, in which the interim fuel substance has a lower ignition energy than that of the fuel, injecting the constituents into a combustion chamber of an engine, and providing a gaseous fluid including oxidants in the combustion chamber to react with the constituents in a combustion reaction, in which the combustion reaction of the constituents occurs at a reduced energy than that of a combustion reaction of the fuel substance.
11 Advanced coal upgrading process for a power station US13148945 2010-11-17 US09187697B2 2015-11-17 Rodolfo Antonio M. Gomez
A coal or carbonaceous material upgrading process for power station use, the process comprising a number of steps. First comminuting the coal or carbonaceous to a comminuted material. Second pre-treating the comminuted coal with a pulsing single frequency microwave and vacuum to reduce its water and oxygen content; the pre-treating stage being carried out at a temperature of up to 180 C. Third, treating the pre-treated comminuted material with a pulsing single frequency microwave energy under vacuum to optimize the volatile organic materials; the treatment stage being carried out at a temperature of up to 350 C. Next pyrolyzing the treated coal with a pulsing single frequency microwave and vacuum to produce a hot gas and a solid carbon residue; the pyrolyzing stage is carried out at a temperature of up to 720 C. The solid carbon residue can then be separated from the hot gas, the volatile organic materials condensed to produce a liquid hydrocarbon product and a gas product; and the solid material and the gas product fed to a power station to produce electricity therefrom. The microwave energy applied at each of the stages has a single frequency of 100 megahertz to 300 gigahertz, has circular polarisation, and is pulsed at a frequency of 2 to 50 kilohertz. The pre-treatment step, the treatment step, and the pyrolysis step can be done under vacuum.
12 CHEMICAL FUEL CONDITIONING AND ACTIVATION US13843976 2013-03-15 US20140130756A1 2014-05-15 Roy Edward McAlister
Methods, systems, and devices are disclosed for chemically activating a fuel for injection and ignition in a combustion engine. In one aspect, a method to initiate combustion includes transforming an interim fuel substance into constituents including radicals, the interim fuel substance formed by a chemical conversion using a fuel, in which the interim fuel substance has a lower ignition energy than that of the fuel, injecting the constituents into a combustion chamber of an engine, and providing a gaseous fluid including oxidants in the combustion chamber to react with the constituents in a combustion reaction, in which the combustion reaction of the constituents occurs at a reduced energy than that of a combustion reaction of the fuel substance.
13 Methods and systems for briquetting solid fuel US12247004 2008-10-07 US08585786B2 2013-11-19 J. Michael Drozd; Steven L. Lawson; Michael C. Druga; Frederick Christopher Lang; Jan M. Surma; Herbie L. Bullis
In embodiments of the present invention improved capabilities are described for a system and method for briquetting solid fuel before or after treatment with electromagnetic energy. In the system and method, solid fuel is transported through a continuous feed solid fuel treatment facility, treated using electromagnetic energy, and briquetted after treatment.
14 燃料を処理して、当該燃料の発熱量を増加させる装置 JP2015500387 2013-03-05 JP2015517077A 2015-06-18 エナシェ,オウレル
本発明は、燃料を処理して、当該燃料の発熱量を増加させる装置に関する。本発明に係る装置は、ハウジング(15)とクーポン(10)とを有し、ハウジング(15)とクーポン(10)との間にはいくつかの励振器(A)が配置され、各励振器(A)は、クーポン(10)に沿って螺旋軌道を描くワイヤ(11および12)に各々取り付けられている。
15 CHEMICAL FUEL CONDITIONING AND ACTIVATION EP13854103 2013-11-12 EP2917552A4 2016-08-03 MCALISTER ROY EDWARD
16 METHOD OF AFFIXING HEAT-RESISTANT FUEL ACTIVATION SUBSTANCE AND COMBUSTION DEVICE EP09815845.4 2009-09-15 EP2336640A1 2011-06-22 TAKAHASHI, Seitaro; ITO, Masahiro

A heat-resistant fuel-activating substance is affixed to a combustion device such as a boiler in an adequate manner, that is, the substance is affixed in an adequate position over an adequate area, whereby the effect of activating combustion is rapidly, stably, and inexpensively produced. A heat-resistant fuel-activating substance having a spectral emissivity of 0.85 or higher at electromagnetic wavelengths in the range of 3-20 µm is affixed to a combustion device so that the heat-resistant fuel-activating substance is disposed in a position which is located outside or inside the combustion chamber at the back of the flame-generating portion of the burner and rises to at most 300°C in temperature and that the substance occupies at least 50% of the area of the projected part of the combustion cone.

17 Chemical fuel conditioning and activation US13843976 2013-03-15 US09200561B2 2015-12-01 Roy Edward McAlister
Methods, systems, and devices are disclosed for chemically activating a fuel for injection and ignition in a combustion engine. In one aspect, a method to initiate combustion includes transforming an interim fuel substance into constituents including radicals, the interim fuel substance formed by a chemical conversion using a fuel, in which the interim fuel substance has a lower ignition energy than that of the fuel, injecting the constituents into a combustion chamber of an engine, and providing a gaseous fluid including oxidants in the combustion chamber to react with the constituents in a combustion reaction, in which the combustion reaction of the constituents occurs at a reduced energy than that of a combustion reaction of the fuel substance.
18 Installation for Treating a Fuel to Increase its Caloric Power US14380240 2013-03-05 US20150003489A1 2015-01-01 Aurel Enache
The invention refers to an installation for treating fuels to increase their caloric power. The installation, according to the claimed invention has a housing (15) and a coupon (10) between which there are place some excitation units (A), each of these as are attached to each of two wires (11 and 12) which follow a spiral path through the coupon (10).
19 Apparatus and Method for Processing any Fluid or Mixture of Fluids or any Gas or Mixture of Gases such as Air, and in Particular, a Mixture of Fluid or Gaseous Hydrocarbons with Air US14270829 2014-05-06 US20140330052A1 2014-11-06 Marina Sarti Pascoli
An apparatus for improving the combustion of a mixture of fluid or gaseous hydrocarbon with combustion air comprising, an inner tube for receiving the flow of said mixture, the inner tube having at both sides two fittings or couplers; a central magnetic ring for generating an axial magnetic field in the vicinity of the center of said inner tube two magnetic rings located on both sides and held at a predetermined distance from said central magnetic ring; a first connecting bridge allowing a magnetic connection of the two magnetic rings but without connection with said central magnetic ring; and two connection bridges allowing a magnetic connection between said central magnetic ring and each of the magnetic rings at both ends.
20 METHOD OF AFFIXING HEAT-RESISTANT FUEL ACTIVATION SUBSTANCE AND COMBUSTION DEVICE US13121373 2009-09-15 US20110223550A1 2011-09-15 Seitaro Takahashi; Masahiro Ito
A heat-resistant fuel-activating substance is affixed to a combustion device such as a boiler in an adequate manner, that is, the substance is affixed in an adequate position over an adequate area, whereby the effect of activating combustion is rapidly, stably, and inexpensively produced. A heat-resistant fuel-activating substance having a spectral emissivity of 0.85 or higher at electromagnetic wavelengths in the range of 3-20 μm is affixed to a combustion device so that the heat-resistant fuel-activating substance is disposed in a position which is located outside or inside the combustion chamber at the back of the flame-generating portion of the burner and rises to at most 300° C. in temperature and that the substance occupies at least 50% of the area of the projected part of the combustion cone.
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