序号 | 专利名 | 申请号 | 申请日 | 公开(公告)号 | 公开(公告)日 | 发明人 |
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81 | Verfahren zum Herstellen einer Anzündhilfe | EP13153356.4 | 2013-01-30 | EP2623581A1 | 2013-08-07 | Scheichl, Dieter |
Die vorliegende Erfindung schafft ein Verfahren zum Herstellen einer Anzündhilfe (2), mit folgenden Verfahrensschritten: Bereitstellen zumindest eines Holzwolleseils (4); Zerteilen des zumindest einen Holzwolleseils (4) in einzelne Seilabschnitte (10) mittels einer Schneideinrichtung (5); Benetzen einer Mantelfläche (13) und Stirnflächen (14, 15) der einzelnen Seilabschnitte (10) mit einem geschmolzenen Brennstoff; und Abkühlen der einzelnen, mit dem geschmolzenen Brennstoff benetzten Seilabschnitte (10), wobei der Brennstoff erstarrt. |
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82 | Method for enabling the detection of fuel leaking from a fuel cell | EP04789273.2 | 2004-09-30 | EP1673421B1 | 2010-04-07 | REN, Xiaoming; SHUFON, Kevin, J.; KOVACS, Frank, W. |
Fuel mixtures for direct methanol fuel cells are disclosed. The fuels include methanol and additives that react with water to produce methanol and other easily electro-oxidizable compounds including dimethyloxymethane, methylorthoformate, tetramethylorthocarbonate, trimethylborate, and tetramethylorthosilicate. Other additives to improve safety and efficiency of the fuel cell include sulfonated activated carbon particles and metal hydrides, such as LiAlH4, NaBH4, LiBH4, (CH3)2 NHBH3, NaAlH4, B2H6, NaCNBH3, CaH2, LiH, NaH, KH or sodium bis (2-methoxyethoxy) dihydridaluminate. | ||||||
83 | FUEL COMPOSITION IN FUEL CARTRIDGES FOR DMFCS | EP04789273.2 | 2004-09-30 | EP1673421A2 | 2006-06-28 | REN, Xiaoming; SHUFON, Kevin, J.; KOVACS, Frank, W. |
Fuel mixtures for direct methanol fuel cells are disclosed. The fuels include methanol and additives that react with water to produce methanol and other easily electro-oxidizable compounds including dimethyloxymethane, methylorthoformate, tetramethylorthocarbonate, trimethylborate, and tetramethylorthosilicate. Other additives to improve safety and efficiency of the fuel cell include sulfonated activated carbon particles and metal hydrides, such as LiAlH4, NaBH4, LiBH4, (CH3)2 NHBH3, NaAlH4, B2H6, NaCNBH3, CaH2, LiH, NaH, KH or sodium bis (2-methoxyethoxy) dihydridaluminate. | ||||||
84 | Verfahren zur Lagerung bzw. zum Transport von flüssigen Kohlenwasserstoffen | EP92114585.0 | 1992-08-27 | EP0531807B1 | 1995-03-15 | Engelhardt, Fritz, Dr.; Ebert, Gerlinde, Dr.; Hoffmann, Heinz, Prof. Dr.; Platz, Gerhard, Prof. Dr.; Ritschel, Werner, Dr. |
85 | SLURRY DEWATERING AND CONVERSION OF BIOSOLIDS TO A RENEWABLE FUEL | EP05818601.6 | 2005-11-08 | EP1799796B1 | 2018-08-22 | DICKINSON, Norman, L.; BOLIN, Kevin, M.; OVERSTREET, Edward; DOOLEY, Brian |
In the processes for treating municipal sewage and storm water containing biosolids to discharge standards, biosolids, even after dewatering, contain typically about 80% water bound in the dead cells of the biosolids, which gives biosolids a negative heating value. It can be incinerated only at the expense of purchased fuel. Biosolids are heated to a temperature at which their cell structure is destroyed and, preferably, at which carbon dioxide is split off to lower the oxygen content of the biosolids. The resulting char is not hydrophilic, and it can be efficiently dewatered and/or dried and is a viable renewable fuel. This renewable fuel can be supplemented by also charging conventional biomass (yard and crop waste, etc.) in the same or in parallel facilities. Similarly, non-renewable hydrophilic fuels can be so processed in conjunction with the processing of biosolids to further augment the energy supply. | ||||||
86 | LOW-TEMPERATURE SLUSH FLUID PRODUCTION APPARATUS | EP07742269 | 2007-04-24 | EP2028430A4 | 2010-12-01 | KAMIYA TAKANOBU; MAEMURA TAKASHI; NAKAMURA RYO; NAKAMICHI KENJI; KIMURA SEIICHIRO |
87 | TRANSPARENT CANDLE AND METHOD OF MAKING | EP05705998 | 2005-01-21 | EP1749080A4 | 2010-03-17 | ALLISON GERALD; FERNANDEZ ERGINIO; DEAN JONATHAN |
88 | FUEL FOR FUEL CELL, FUEL CELL AND APPLICATION THEREOF | EP04820664 | 2004-12-03 | EP1705740A4 | 2009-02-25 | YAGI MINORU; NISHI TETSUYUKI |
A fuel for fuel cell consisting of an organic fuel which is in the form of a solid molecular compound, such as a clathrate compound. This molecular compound can be produced by catalytic reaction between a molecular compound forming compound and an organic fuel and changes a liquid organic fuel to a solid compound, thereby realizing relatively lightweight and stable storage of the organic fuel. Organic fuel can be easily released from the molecular compound by heating, etc. and can be fed to a fuel electrode of the fuel cell. As a result, not only can the handleability of the fuel for fuel cell consisting of an organic fuel be improved but also the problems of corrosion, fuel freezing, crossover, etc. can be solved. | ||||||
89 | FUEL FOR FUEL CELL, FUEL CELL AND APPLICATION THEREOF | EP04820664.3 | 2004-12-03 | EP1705740A1 | 2006-09-27 | YAGI, Minoru, c/o KURITA WATER INDUSTRIES LTD; NISHI, Tetsuyuki, c/o KURITA WATER INDUSTRIES LTD |
A fuel cell fuel contains an organic fuel used as a fuel for a fuel cell. The organic fuel is in a form of a solid molecular compound, such as an inclusion compound. The molecular compound can be prepared by contact catalytic reaction of a compound for forming the molecular compound and the organic fuel, and allows a liquid organic fuel to be in a solid compound to store the organic fuel stably in a relatively lightweight form. The molecular compound easily releases the organic fuel by, for example, heating, and the organic fuel is supplied to the fuel electrode of a fuel cell. Thus, the handleability of the fuel cell fuel containing the organic fuel can be improved, and the problems of corrosion, freezing of the fuel, crossover, and so forth can be solved. |
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90 | Verfahren zur Lagerung bzw. zum Transport von flüssigen Kohlenwasserstoffen | EP92114585.0 | 1992-08-27 | EP0531807A1 | 1993-03-17 | Engelhardt, Fritz, Dr.; Ebert, Gerlinde, Dr.; Hoffmann, Heinz, Prof. Dr.; Platz, Gerhard, Prof. Dr.; Ritschel, Werner, Dr. |
Die vorliegende Erfindung betrifft die Verwendung von kohlenwasserstoffreichen Gelen als sichere Lager- bzw. Transportform für flüssige Kohlenwasserstoffe sowie ein Verfahren zur sicheren Lagerung bzw. zum sicheren Transport von flüssigen Kohlenwasserstoffen, dadurch gekennzeichnet, daß
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91 | RHEOLOGY CONTROLLED EMULSION | EP90913307 | 1990-07-30 | EP0486612A4 | 1993-03-17 | LOWNDS, C. MICK; GROW, STEVEN, C. |
The present invention relates to an emulsion composition with a polymerizing and/or crosslinking agent and methods for its use in improving the manufacturing, packaging, transporting, storage placement and blasting characteristics of explosives containing an emulsion. The present invention is directed to controlling the rheology of an emulsion or explosive containing an emulsion by polymerizing and/or crosslinking the continuous phase of the emulsion by employing hydroxy-terminated polybutadiene and polymerizing agents and/or maleic anhydride adducted polybutadiene and crosslinking agents. The present invention provides compositions and methods of polymerizing and crosslinking emulsion compositions which result in an emulsion whose rheology may be controllably selected, without compromising the integrity of the explosive reaction. The composition of the present invention is comprised of a water-in-oil emulsion containing a continuous external carbonaceous fuel phase, the fuel phase being at least partially polymerized and/or crosslinked. | ||||||
92 | 연료 조성물 및 이의 제조방법 | KR1020150182061 | 2015-12-18 | KR1020170073310A | 2017-06-28 | 김성균; 김요섭 |
본발명은연료조성물및 이의제조방법에관한것이며, 보다상세하게는 3차원가지구조무기물에액상연료가포획된분말상또는겔상의연료조성물및 이의제조방법에관한것이다. | ||||||
93 | 하이브리드 로켓의 파라핀계 연료 제조방법 | KR1020090008466 | 2009-02-03 | KR100908290B1 | 2009-07-17 | 김진곤; 문희장; 김수종; 조정태 |
A paraffinic fuel manufacturing apparatus for hybrid rockets is provided to enable paraffinic fuel to be solidified when paraffin wax fused by high-pressure gas is pressurized and cooled in a gravity direction under a state of minimizing the contraction of paraffinic fuel in a radial direction. A method for manufacturing paraffinic fuel for hybrid rockets comprises the following steps of: fusing paraffin wax in a fuser; placing the fused paraffin wax in a casting frame; injecting high-pressure gas to the casting frame in order to pressurize the fused paraffin wax to be solidified; and taking the solidified paraffin wax out of the casting frame. The solidifying step minimizes the contraction in a radial direction. | ||||||
94 | 탄수화물 가공 연료 | KR2020070013583 | 2007-08-16 | KR2020090001618U | 2009-02-19 | 류하수 |
본 고안은 탄수화물( 당류, 녹말류, 셀룰로스류, 리그닌류등의 식물체의 구성 물질)를 가공하여 각종 연료로 사용하기 위한 것으로 특히 탄수화물의 산(Acid) 에스테르화한 연료에 관한 것이다. 탄수화물이란 당류, 녹말류, 셀룰로스류, 리그닌류등 식물체의 구성 물질을 말한다. | ||||||
95 | 휴대용 반고형 연료 조성물 | KR1019940022539 | 1994-09-07 | KR1019960010837A | 1996-04-20 | 박병구 |
저온 착화레인니트로셀루로스, 결합제인 칼복시 메칠셀루로스 연료물질인 알콜 및 왁스, 연소매개체인 목분 또는 펄프분말, 연소촉진제인 실록산으로 조성된 휴대용 반고형 연료조성물에 관한 것이다. | ||||||
96 | 조명용 연료 | KR1019920015663 | 1992-08-29 | KR1019930004444A | 1993-03-22 | 오까다도오루 |
내용 없음. | ||||||
97 | SLURRY DEWATERING AND CONVERSION OF BIOSOLIDS TO A RENEWABLE FUEL | EP05818601 | 2005-11-08 | EP1799796A4 | 2012-10-31 | DICKINSON NORMAN L; BOLIN KEVIN M; OVERSTREET EDWARD; DOOLEY BRIAN |
98 | LOW-TEMPERATURE-SLUSH-FLUID PRODUCING APPARATUS | EP07742269.9 | 2007-04-24 | EP2028430B1 | 2012-06-13 | KAMIYA, Takanobu; MAEMURA, Takashi; NAKAMURA, Ryo; NAKAMICHI, Kenji; KIMURA, Seiichiro; KAWASAKI, Shuichi |
A low-temperature slush fluid production apparatus that attains an increase of weight solidification ratio of slush fluid. There is provided low-temperature slush fluid production apparatus (1) comprising heat exchanger (12) with heat transfer plane (11) disposed in low-temperature fluid (L) of liquid form held within vessel (10); slush fluid production unit (2) equipped with scraping means (13) for scraping off any low-temperature fluid of solid form produced on the surface of the heat transfer plane (11); and extremely low temperature fluid generating unit (3) adapted to supply an extremely low temperature fluid whose temperature is lower than that of the low-temperature fluid (L) of liquid form held within the vessel (10) to the inside of the heat transfer plane (11), wherein not only the flow rate and temperature of the extremely low temperature fluid flowing into the inside of the heat transfer plane (11) but also the rotational speed or reciprocation speed of the scraping means (13) is regulated in accordance with the particle diameter of low-temperature fluid of solid form scraped off by the scraping means (13). | ||||||
99 | LOW-TEMPERATURE SLUSH FLUID PRODUCTION APPARATUS | EP07742269.9 | 2007-04-24 | EP2028430A1 | 2009-02-25 | KAMIYA, Takanobu; MAEMURA, Takashi; NAKAMURA, Ryo; NAKAMICHI, Kenji; KIMURA, Seiichiro |
A low-temperature-slush-fluid producing apparatus capable of achieving an increased weight solidification rate of slush fluid is provided. A low-temperature-slush-fluid producing apparatus 1 includes a slush-fluid producing unit 2 that includes a heat exchanger 12 having a heat-transfer surface 11 and disposed in a liquid-phase low-temperature fluid L stored in a container 10 and scraping means 13 for scraping a solid-phase low-temperature fluid formed on a surface of the heat-transfer surface 11; and a cryogenic-fluid generating unit 3 for supplying into the interior of the heat-transfer surface 11 a cryogenic fluid having a lower temperature than the liquid-phase low-temperature fluid L stored in the container 10. The low-temperature-slush-fluid producing apparatus 1 is configured so that the flow rate and temperature of the cryogenic fluid flowing into the interior of the heat-transfer surface 11 and the rotational speed or reciprocating speed of the scraping means 13 can be adjusted based on the particle size of the solid-phase low-temperature fluid scraped by the scraping means 13. |
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100 | SLURRY DEWATERING AND CONVERSION OF BIOSOLIDS TO A RENEWABLE FUEL | EP05818601.6 | 2005-11-08 | EP1799796A2 | 2007-06-27 | DICKINSON, Norman, L.; BOLIN, Kevin, M.; OVERSTREET, Edward; DOOLEY, Brian |
In the processes for treating municipal sewage and storm water containing biosolids to discharge standards, biosolids, even after dewatering, contain typically about 80% water bound in the dead cells of the biosolids, which gives biosolids a negative heating value. It can be incinerated only at the expense of purchased fuel. Biosolids are heated to a temperature at which their cell structure is destroyed and, preferably, at which carbon dioxide is split off to lower the oxygen content of the biosolids. The resulting char is not hydrophilic, and it can be efficiently dewatered and/or dried and is a viable renewable fuel. This renewable fuel can be supplemented by also charging conventional biomass (yard and crop waste, etc.) in the same or in parallel facilities. Similarly, non-renewable hydrophilic fuels can be so processed in conjunction with the processing of biosolids to further augment the energy supply. |