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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41 | 세척 조성물 및 방법 | KR1020177017700 | 2009-12-17 | KR1020170078864A | 2017-07-07 | 바수,라자트; 지호우스키,게리; 쿡,케인; 네일워젝,데이비드 |
본발명은이온성계면활성제, 바람직하게는이의플루오르화부를갖는이온성계면활성제, 및하이드로플루오로- 및/또는하이드로클로로플루오로-올레핀으로부터선택된용매를포함하는용매및 세척조성물을제공한다. 또한, 본발명은하이드로플루오로- 또는하이드로클로로플루오로-올레핀및 상기계면활성제를함유하는건조, 드라이클리닝및 방오조성물을제공한다. 또한, 본발명은하이드로플루오로-올레핀또는하이드로클로로플루오로-올레핀및 메탄올, 에탄올또는이소프로판올과같은알코올을함유하는건조조성물을제공한다. | ||||||
42 | 할로겐화 알칸의 선택적 디하이드로할로겐화 방법 | KR1020070109199 | 2007-10-29 | KR101576098B1 | 2015-12-10 | 왕하이유; 퉁쉬에성 |
불소치환체및 비-불소치환체를모두갖는하나이상의알칸으로부터바람직하게고도의전환율및 선택성으로할로겐화올레핀, 바람직하게테트라불소화프로펜(들)을생성하는방법이개시된다. 바람직하게상기방법은촉매반응의사용을포함하며, 여기서상기촉매는활성탄소, 할로겐화단- 및이가금속산화물, 단- 및이가루이스산금속할라이드, 0가금속,및이들의조합으로구성되는그룹으로부터선택된다. | ||||||
43 | 세척 조성물 및 방법 | KR1020117016608 | 2009-12-17 | KR1020110096164A | 2011-08-29 | 바수,라자트; 지호우스키,게리; 쿡,케인; 네일워젝,데이비드 |
본 발명은 이온성 계면활성제, 바람직하게는 이의 플루오르화부를 갖는 이온성 계면활성제, 및 하이드로플루오로- 및/또는 하이드로클로로플루오로-올레핀으로부터 선택된 용매를 포함하는 용매 및 세척 조성물을 제공한다. 또한, 본 발명은 하이드로플루오로- 또는 하이드로클로로플루오로-올레핀 및 상기 계면활성제를 함유하는 건조, 드라이 클리닝 및 방오 조성물을 제공한다. 또한, 본 발명은 하이드로플루오로-올레핀 또는 하이드로클로로플루오로-올레핀 및 메탄올, 에탄올 또는 이소프로판올과 같은 알코올을 함유하는 건조 조성물을 제공한다. | ||||||
44 | C1 탄화수소를 할로겐화 C1 탄화수소로 산화성할로겐화시키는 방법 | KR1020077025568 | 2006-04-25 | KR1020080009707A | 2008-01-29 | 포드콜진사이몬쥐.; 스탱글랜드에릭이.; 쇼웨이저2세알버트이.; 존스마크이. |
An oxidative halogenation process involving contacting methane, a C1 halogenated hydrocarbon, or a mixture thereof with a source of halogen and a source of oxygen, at a molar ratio of reactant hydrocarbon to source of halogen in a feed to the reactor greater than 23/1, and/or at a molar ratio of reactant hydrocarbon to source of oxygen in a feed to the reactor greater than about 46/1; in the presence of a rare earth halide or rare earth oxyhalide catalyst, to produce a halogenated C1 product having at least one more halogen as compared with the C1 reactant hydrocarbon, preferably, methyl chloride. The process can be advantageously conducted to total conversion of source of halogen and source of oxygen. The process can be advantageously conducted with essentially no halogen in the feed to the reactor, by employing a separate catalyst halogenation step in a pulse, swing or circulating bed mode. The production of methyl halide can be integrated into downstream processes for manufacture of valuable commodity chemicals. | ||||||
45 | 과플루오로 알칸 및 할로 과플루오로 알칸, 이들의 전구 물질 및 이들의 제조 방법 | KR1019860002574 | 1986-04-04 | KR1019860008112A | 1986-11-12 | 게라르도카포리치오; 장안젤로바르기기아; 클라우디오토넬리; 비토토르텔리 |
내용 없음 | ||||||
46 | METHOD OF DETECTING PRE-FIRE SITUATIONS ARISING AS A RESULT OF ELECTRICAL CIRCUIT FAULTS | EP16835530.3 | 2016-08-10 | EP3336814A1 | 2018-06-20 | LESIV, Aleksey Valeryevich |
The present invention relates to the field of fire and electric power safety, in particular to methods for detection of pre-fire situations arising from local overheating of electrical equipment, and is intended to prevent fires arising from electrical wiring faults, in particular, faults in wiring devices. The method is based on measuring the content of low-boiling substances in the atmosphere of the protected room, which are enclosed in capsules with an opening temperature in the range of 80-200 ° C, fixed on current-carrying parts, and released into the external environment when these capsules are opened by heating the mentioned parts to the appropriate temperature. The technical result of the claimed solution is to increase the probability of detecting a pre-fire situation at an early stage. |
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47 | 1,1,1,3,3-PENTACHLOROPROPANE PROCESS PURGE STREAM CONCENTRATION USING A SECONDARY REFLUXED EVAPORATOR AND SECONDARY PRODUCT RECOVERY | EP03746914.5 | 2003-02-11 | EP1509485B1 | 2013-03-13 | WILSON, Richard, L.; DAWKINS, John, L.; KLAUSMEYER, Rodney, L.; WELLER, James, J. |
48 | NOVEL CRYSTALLINE ION-ASSOCIATION SUBSTANCE, PROCESS FOR PRODUCING THE SAME, AND POLYMERIZATION INITIATOR | EP00902020.7 | 2000-01-31 | EP1153905A1 | 2001-11-14 | HIWASA, Shin |
A polymerization initiator for cationically polymerizable organic substances which comprises a crystalline ion-association substance having such a unique property that it can initiate not only photopolymerization but thermal polymerization when used in polymerizing a cationically polymerizable organic substance. The crystalline ion-association substance is represented by the general formula (I): |
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49 | TERMINAL CHLORINATION OF NORMAL ALKANE HYDROCARBONS | EP89909319 | 1989-07-13 | EP0427782A4 | 1991-11-21 | TURRO, NICHOLAS, J.; FEHLNER, JAMES, R. |
Normal alkane hydrocarbons are chlorinated with high terminal selectivity by pre-adsorbing the hydrocarbons into a pentasil zeolite. | ||||||
50 | Method and apparatus for detoxicating halide of nitrogen or carbon | EP90400371.2 | 1990-02-12 | EP0384802A1 | 1990-08-29 | Hirase, Ikuo; Petitjean, Mathieu |
A nitrogen halide or carbon halide gas is caused to pass through a packed layer in which at least one granular material selected from the group consisting of silicon, molybdenum, tungsten, molybdenum silicide, and tungsten silicide is heated, so that the halide gas and granular material react with each other. The reaction product is treated with an alkali. In this manner, a toxic halide gas can be detoxicated with high efficiency. |
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51 | Verfahren zur Herstellung von Hexachlorethan aus Hexachlorbutadien | EP87100830.6 | 1987-01-22 | EP0235535A1 | 1987-09-09 | Sticken, Gerhard, Dr. |
Zur Herstellung von Hexachlorethan wird gasförmiges Chlor mit flüssigem Hexachlorbutadien in Gegenwart von Sauerstoff umgesetzt. Als Sauerstofflieferant kann Luft eingesetzt werden. Der Druck des Reaktionssystems liegt zwischen 1 und 50 bar (abs.), die Reaktionstemperatur zwischen 100 °C und der Siedetemperatur der flüssigen Phase bei dem jeweils festgelegten Druck. |
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52 | Halogenated hydrocarbons | EP86302937.7 | 1986-04-18 | EP0204413A1 | 1986-12-10 | Mills, John Frederick David; Richardson, Michael Thomas; Madeley, John Robert |
A chlorinated paraffins composition of low or zero toxicity comprising a chlorinated mixture of a C12 paraffin and one or more paraffins of chain length greater than 12 carbon atoms and containing from 20 to 70% by weight chlorine based on the chlorinated paraffins; preferably a chlorinated mixture of C12, C13, C14 and optionally C15 paraffins. |
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53 | Verfahren zur Stabilisierung von Polychloralkanen und Stabilisatorkombinationen | EP79100109.2 | 1979-01-15 | EP0003140A1 | 1979-07-25 | Landau, Helmut |
Die Erfindung betrifft Stabilisatorkombinationen für die Hochtemperaturstabilisierung von Polychloralkanen, die aus 10 bis 90 Gew.-% einer Epoxyverbindung und 90 bis 10 Gew.-% eines tertiären Esters der phosphorigen Säure bestehen. |
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54 | 펜타 할로 에탄의 불소화 방법 | KR1019890009110 | 1989-06-28 | KR1019900000317A | 1990-01-30 | 리오어네스트맨저; 밸리유르노트말리가르주나라오 |
내용 없음 | ||||||
55 | 1,1,1-트리 플루오로 디클로로 에탄 및 1,1,1,2- 테트라 플루올로 클로로 에탄의 개선된 제조 방법 | KR1019880013781 | 1988-10-21 | KR1019890006550A | 1989-06-14 | 윌리엄헨리검프리췻; 리오우어네스트맨저; 벨류어노트말리카주너라오 |
내용 없음 | ||||||
56 | 연속적 불소화 방법 | KR1019840003522 | 1984-06-22 | KR100023971B1 | 1987-08-06 | 프레더릭크윌리엄마더 |
57 | 브로모 트리 플루오 메탄의 제법 | KR1019850007865 | 1985-10-24 | KR1019860003187A | 1986-05-21 | 레슬리부르게스; 귀퀜틴말링 |
내용 없음 | ||||||
58 | 올레핀계 모노 첨가 생성물과 이와 반응적인 텔로겐의 제조 방법 | KR1019840003900 | 1984-07-05 | KR1019850001143A | 1985-03-16 | ㅅ콧트샌트포드우두아드 |
내용없음 | ||||||
59 | 연속적 불소화 방법 | KR1019840003522 | 1984-06-22 | KR1019850000378A | 1985-02-27 | 프레더릭크윌리엄마더 |
내용없음. | ||||||
60 | Method of detoxifying a harmful compound by using an alkylating composition and the composition | JP2006118388 | 2006-04-21 | JP4802036B2 | 2011-10-26 | 浩一郎 中村; 新二郎 堂見; 晋司 神谷; 晶光 菱沼 |