| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 141 | Of petroleum acid neutralization how to use the overbased detergents | JP51049197 | 1996-08-23 | JP2000512318A | 2000-09-19 | アンダーソン・ミカエル・ピー; ゴルバティー・マーチン・エル; サーベイジ・デビッド・ダブリュー; サルトリ・グイド; バリンガー・ブルース・エッチ; ブラム・ソウル・シー; マーテラ・デビッド・ジェー; ラマナラヤナン・トリクル・エー |
| (57)【要約】 本発明は、酸性全原油又はその留分を、典型的に２００℃より低い適当な高温度で、典型的に０．２５：１〜１０：１の中和量の過塩基性化洗浄剤と接触させることによって、その酸性度を低下又は除去するための、ナフテン酸含有全原油又はその留分の処理方法に関する。 この方法は、処理した原油中のエマルジョンの形成に付随する材料取り扱い問題を減少させるという追加の利点を有する。 | ||||||
| 142 | Process and device for converting heavy oil into fluid fuel for generating unit | JP28488798 | 1998-10-07 | JP2000109850A | 2000-04-18 | OTA KAZUAKI; HANZAWA MASATOSHI; TANAKA AKIRA |
| PROBLEM TO BE SOLVED: To efficiently and easily gasify heavy oils and convert them into light oils, to inhibit facility corrosion and environmental pollution by easily converting metal components or sulfuric components contained in heavy oils into harmless inorganic salts and removing them, and to alleviate efforts for maintenance and increase the electric power generation efficiency of electric power generating devices. SOLUTION: A heavy oil, water and an alkali are maintained at the supercritical state of water and decomposed in a supercritical reactor 24 to generate a light oil component, a hydrocarbon gas, a metal oxide, an alkaline salt and supercritical water. The obtained decomposed product is maintained in an extractor 25 at a temperature and pressure equal to or below the subcritical state of water to extract a hydrocarbon gas, a light oil component and moisture from the decomposed product. The extracted hydrocarbon gas, light oil component and moisture are vapor-liquid separated by a vapor-liquid separator 27 into a hydrocarbon gas, a light oil component and moisture. The separated light oil component and moisture are separated into a light oil component and water by an oil-water separator 28. COPYRIGHT: (C)2000,JPO | ||||||
| 143 | Method of reducing crude oil acid content and corrosive | JP51049097 | 1996-08-23 | JP2000503040A | 2000-03-14 | アンダーソン・ミカエル・ピー; ゴルバティー・マーチン・エル; サーベイジ・デビッド・ダブリュー; サルトリ・グイド; バリンガー・ブルース・エッチ; ブラム・ソウル・シー; マーテラ・デビッド・ジェー; ラナマナヤナン・トリクル・エー |
| (57)【要約】 本発明は、適当な量の第ＩＡ族又は第ＩＩＡ族の酸化物、水酸化物及び水和物を添加することによって、その酸性度及び腐食性を低下又は除去するための、酸性原油又はその留分の処理方法に関する。 この方法は、液体溶媒を使用して酸性原油を処理することに付随する材料取り扱い問題を減少させるとともにエマルジョン形成を減少させる追加の利点を有する。 | ||||||
| 144 | Desulfurization of non-condensable gases from the crude oil vacuum distillation | JP50589896 | 1995-07-20 | JPH10506364A | 1998-06-23 | ズァコヴァル，ジーリ |
| (57)【要約】 原油重質成分の減圧蒸留のガス生成物を脱硫するための方法および装置。 脱硫すべき初期ガス混合物（８）は非凝縮性のガスで、硫化水素を含有する。 ガス−液接触塔（２）には第１および第２区画（３、４）があり、それらの区画は組織化または不規則充填物の充填床を有している。 充填床は潅液装置（１８）の下方に支持されており、この潅液装置が充填床の湿潤を促すが、塔を通過するガスの圧力低下は最小限になっている。 初期ガス混合物は乾燥され、塔の第１区国（３）に導入される（１４）。 同様に、塔の第１区画には、初期ガス混合物中に存在する硫化水素量と反応するための化学量論量を含む新鮮なアンモニア溶液（９）が導入される。 最終的に、塔の第１区画は第２アンモニア溶液を受けるが、これは塔の第２区画から第１区画へと送り込まれる。 | ||||||
| 145 | New decomposition method of crude oil | JP23963996 | 1996-07-15 | JPH1030093A | 1998-02-03 | KUNO MASAYA |
| PROBLEM TO BE SOLVED: To remove sulfur, a metal compound, etc., from a crude oil and use the residue as a fertilizer source. SOLUTION: A crude oil is desalted, brought into contact with a large amount of ammonia to transfer sulfur compounds and metal compounds to an ammonia side as ammonium salts and a complex salt mixture. In the operation, an iron- based or a luthenium-based catalyst is used as the catalyst, the catalyst is arbitrarily used since a carbon steel and an alloy are used for a heat exchanger, a reactor, pipings, etc. The separation of the sulfur compounds and the metal compounds from the crude oil is carried out by a water washing column and impurities are introduced to an ammonia water side. In the separation, the impurities eventually contain ammonia, Fe, water, minerals, sulfur and heavy hydrocarbons, made into an excellent fertilizer source, conveniently laid under the ground so as to green a desert and are effectively mixed with grass peat, etc. | ||||||
| 146 | Liquid dehalogenizing agent, its manufacture and method to dehalogenize out of waste oil | JP2233590 | 1990-02-02 | JPH0390173A | 1991-04-16 | MANFUREETO NOIMAN; HAINTSUUBUERUNAA FUOOGESU |
| PURPOSE: To obtain dehalogenizing agent convenient to handle, hard to oxidize nor hydrolyze by containing respectively specific amount of specific alkaline metal alcoholate, alcohol, specific polyether and non-halogen hydrocarbon oil. CONSTITUTION: Liquid dehalogenizing agent is to contain 30 to 70% of alkaline metal alcoholate having 6 to 20 carbon atoms, 0 to 12% of alcohol having 6 to 20 carbon atom, 5 to 40% of formula 1 polyether and 10 to 65% of non- halogen hydrocarbon oil. To produce liquid dehalogenizing agent, the alkaline metal alcoholate that many contain a small amount of alcohol is dissolved with the formula 1 polyether at 100 to 200°C. Next mixed up with is the non- halogen hydrocarbon oil, desirably at 100 to 160°C. Amount of respective factor to mix up should follow the above mentioned percentage to produce the liquid dehalogenizing agent. This product, liquid under room temperature is able to dehalogenize the waste oil. COPYRIGHT: (C)1991,JPO | ||||||
| 147 | Method of regenerating treatment of waste oil | JP9816088 | 1988-04-22 | JPH01271487A | 1989-10-30 | NIHONGI TOKIHIRO; INADA SACHIKO; YAMAGUCHI KEN |
| PURPOSE: To attain effective utilization of resources and obtain a regenerated oil with a high utility value, by a process comprising simultaneously adding phosphoric acid and a particular anionic surfactant or a nonionic surfactant to waste oil, blending, neutralizing, adding a cationic polymer coagulant and performing solid-liq. separation. CONSTITUTION: 0.5-1.0 part of phosphoric acid (B) and 0.1-1.0 part of surfactant (C) selected from a member (a) selected from anionic surfactants of the formulae I-III (wherein each of R 1R 3 is a 7-20 C alkyl, M 1 is H or M 2, M 2 is Na, K, Ca or NH 4; and n is 6-20) and a nonionic surfactant (b) of the formula IV (wherein R 4 is R 1; p is 1 or 2; and m is n) are simultaneously added to 100 pts. waste oil (A), and they are blended with each other. Subsequently, an alkali compd. (e.g., NaOH) (D) and water are added, and blended at 80-90°C for at least 30min. to effect neutralization. Thereafter, 0.05-0.2 part of a cationic polymer coagulant (e.g., an epichlorohydrin condensation product of a polyamide from diethanolamine and adipic acid) is added. Finally, solid-liq. separation is performed by filtration, centrifugation, etc., to recover in a high yield of 80-90% a regenerated oil with a low ash content. COPYRIGHT: (C)1989,JPO&Japio | ||||||
| 148 | Improvement of thermal stability of jet fuel sweetened by catalytic oxidation | JP22734888 | 1988-09-10 | JPH01113492A | 1989-05-02 | EDOWAADO JIYOOJI BARII; JIYOSEFU JIYOOJI BENDORAITEISU; PERII UIRIAMU KAAKURIN; DEBITSUDO ANDORIYUU PATSUPARU |
| PURPOSE: To improve the thermal stability of jet fuel sweetened by catalytic oxidation by washing the fuel with an aq. caustic alkali, then washing with water and drying the same. CONSTITUTION: The jet fuel is sweetened by prewashing the jet fuel with the dilute caustic alkali in a prewashing device 11, then mixing the jet fuel with air, introducing the mixture into a reactor 12 and subjecting the mixture to the catalytic oxidation in the presence of a catalyst (e.g. cobalt phthalocyanine). The sweetened jet fuel is then introduced through a settler 13 into a washing device 14 and is washed with the aq. strongly caustic alkali. The jet fuel is then washed with water in a washing vessel 15 and is passed through a salt filter base 16, by which the jet fuel is dehydrated. The dehydrated jet fuel is passed through a clay filter device 1 where an oil-soluble surfactant is removed, by which the jet fuel having the improved thermal stability is obtd. COPYRIGHT: (C)1989,JPO | ||||||
| 149 | Decomposition of polyhalogenated aromatic compound | JP1967687 | 1987-01-31 | JPS62192179A | 1987-08-22 | FUIRITSUPU NERI |
| 150 | JPS5439402B1 - | JP10665670 | 1970-12-02 | JPS5439402B1 | 1979-11-28 | |
| 151 | JPS5347241B2 - | JP8325075 | 1975-07-07 | JPS5347241B2 | 1978-12-20 | |
| 152 | JPS5336483B1 - | JP4215671 | 1971-06-15 | JPS5336483B1 | 1978-10-03 | |
| 153 | Desulfurization of heavy oils | JP11204376 | 1976-09-17 | JPS5336503A | 1978-04-04 | KIMOTO SANEMI; NAKAMURA TAKUJI; NAGASAKI KAZUYUKI |
| PURPOSE: To desulfurize a heavy oil without causing degrading the quality, by adding an alkali metal hydroxide to the petroleum heavy oil having a specific carbon residue value, and heat-treating the mixture. COPYRIGHT: (C)1978,JPO&Japio | ||||||
| 154 | Neutralizing agent for crude oil | JP8325075 | 1975-07-07 | JPS526704A | 1977-01-19 | KAWAUCHI TOORU |
| PURPOSE: Specific amine compound is added to crude oil to neutralize inorganic chlorides in the oil. COPYRIGHT: (C)1977,JPO&Japio | ||||||
| 155 | 하나 이상의 티올 화합물을 산화시키는 방법 | KR1020157023020 | 2014-02-07 | KR1020150121000A | 2015-10-28 | 터텔조나단앤드류; 카라직자스나; 트럭코제씨이 |
| 한가지예시적인실시예는알칼리스트림으로부터하나이상의티올화합물을산화시키는방법일수 있다. 방법은알칼리스트림을포함하는혼합스트림을본체와목부를포함하는산화용기로안내하는단계를포함할수 있다. 흔히, 본체는하나이상의패킹요소를포함하고목부는패킹, 분배기및 메시를포함한다. 방법은산화된알칼리스트림을제1 챔버와제2 챔버를포함하는분리용기로안내하는단계를더 포함할수 있다. 일반적으로, 제1 챔버는코팅된메시를포함한다. | ||||||
| 156 | 석유 원유의 부식성 및 산성을 감소시키는 방법 | KR1019980701353 | 1996-08-23 | KR100451325B1 | 2004-12-17 | 블룸사울씨; 앤더슨마이클피; 라마나라야난트리커에이; 사르토리가이도; 사바지데이비드더블유; 고바티마틴엘; 발링거브루스에이치; 마텔라데이비드제이 |
| PCT No. PCT/US96/13688 Sec. 371 Date Sep. 15, 1998 Sec. 102(e) Date Sep. 15, 1998 PCT Filed Aug. 23, 1996 PCT Pub. No. WO97/08270 PCT Pub. Date Mar. 6, 1997The invention relates to processes for treating acidic crudes of fractions thereof to reduce or eliminate their acidity and corrosivity by addition of suitable amounts of Group IA of Group IIA oxides, hydroxides and hydrates. The process has the additional benefits of reducing materials handling problems associated with treating acidic crude oils using liquid solvents and in reducing emulsion formation. | ||||||
| 157 | 알칸올아민 계내의 포말 형성을 억제하는 방법 | KR1020007002706 | 1998-07-21 | KR1020010023984A | 2001-03-26 | 하트,폴,알. |
| 아민유닛의탈거장치에서포말형성을억제하는방법이개시되어있다. 포말비형성해유화제를아민유닛의흡수기에도입되는액상, 압축탄화수소스트림또는상기흡수기에도입되거나빠져나오는유기아민수용액스트림에첨가하면, 아민유닛탈거장치내포말형성이억제된다. 탈거장치내포말형성은흡수기에서의해유화제처리를통해탈거장치로도입되는알칼리성아민스트림중의탄화수소비말동반을억제함으로써억제된다. | ||||||
| 158 | 원유의 산 함량 및 부식성을 감소시키는 공정 | KR1019980704317 | 1996-08-23 | KR1019990044704A | 1999-06-25 | 사토리귀도; 사바즈데이비드더블유; 고바티마틴엘; 발린거브루스에이치; 블룸사울씨; 앤더슨마이클피; 라마나라야난트리커에이; 마텔라데이비드제이 |
| 본 발명은 적당한 양의 1A족 또는 2A족 산화물, 수산화물 및 수화물을 첨가함으로써 산성 및 부식성을 감소 또는 제거하기위한 산성 원유 또는 그의 분획물의 처리 공정에 관한 것이다. 상기 공정은 액체 용매를 사용하여 산성 원유를 처리하는 것과 결부된 문제를 취급함에 있어서 물질을 감소시키고 유화액 형성을 감소시키는 추가의 이점을 갖는다. | ||||||
| 159 | 원유 중의 가수분해성 양이온의 감소 방법 | KR1019960008270 | 1996-03-26 | KR1019960034369A | 1996-10-22 | 폴엠.린데머쓰 |
| 본 발명은 아크릴산, 메타크릴산, 술포메틸화 폴리아크릴아미드 및 아미노메탄 포스폰산 개질된 아크릴산 및 이들의 알칼리 금속 및 암모늄 염으로 이루어진 군에서 선택된 단량체 단위를 20몰% 이상 함유하는 수용성 음이온성 중합체를 100 내지 5,000ppm 함유한 수성 용액으로 원유를 처리함으로써 원유에 함유된 가수분해성 양이온을 원유로부터 제거하는 방법에 관한 것이다. 가수분해성 양이온을 제거함으로써 후속적인 정제시 처리된 오일과 접촉하는 금속 표면에서 발생하는 부식이 감소된다. | ||||||
| 160 | 탄화수소유로부터 할로겐화 방향족 화합물을 제거하는 방법 | KR1019940700374 | 1993-01-11 | KR1019940702214A | 1994-07-28 | 슈우지키따무라; 쯔네오야노; 후미오타니모또 |
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