序号 专利名 申请号 申请日 公开(公告)号 公开(公告)日 发明人
121 MX17624979 1979-01-10 MX149175A 1983-09-15 FRAME ROBERT ROY
122 REMOVAL OF NON-PARAFFINIC HYDROCARBONS FROM PARAFFINIC HYDROCARBONS CA301728 1978-04-21 CA1113880A 1981-12-08 ABRAMOVICI MIRON; RYLANDER PAUL N; VIANI UMBERTO
REMOVAL OF NON-PARAFFINIC HYDROCARBONS FROM PARAFFINIC HYDROCARBONS Non-paraffinic hydrocarbons, such as aromatic hydrocarbons, in a stream of paraffinic hydrocarbons are removed by contacting the paraffinic hydrocarbon stream with an oxidation system comprising an aqueous solution of hypochlorite, such as sodium hypochlorite, and a ruthenium species, such as ruthenium dioxide, as the oxidation catalyst. The ruthenium species is oxidized by the hypochlorite to a higher oxidation state with resulting selective oxidation of the non-paraffinic hydrocarbons to water-soluble non-paraffinic compounds and/or CO2. A stream of paraffinic hydrocarbons substantially free of nonparaffinic hydrocarbons is recoverable..
123 TREATING SOUR PETROLEUM DISTILLATES AU4308279 1979-01-03 AU518640B2 1981-10-08 FRAME R R
124 PURIFYING PARAFFINS BY SELECTIVE OXIDATION OF NONPARAFFINIC IMPURITIES GB1619078 1978-04-25 GB1583118A 1981-01-21
125 UN PROCEDIMIENTO PARA TRATAR UN DESTILADO DE PETROLEO AGRIO QUE CONTIENE MERCAPTANOS ES476663 1979-01-09 ES476663A1 1979-06-16
Procedimiento para tratar un destilado de petróleo agrio que contiene mercaptanos, que comprende pasar dicho destilado en mezcla con un agente oxidante, a través de un lecho fijo de un catalizador de ftalocianina metálica soportado, en presencia de un haluro de alcanolamina entremezclado con un reactivo alcalino, teniendo dicho haluro de alcanolamina la fórmula estructural **fórmula** dónde R es un radical alcohileno que contiene hasta aproximadamente 3 átomos de carbono, Y es un radical hidroxilo o hidrógeno y X es cloruro, bromuro, fluoruro o yoduro.
126 IT1919879 1979-01-10 IT7919198D0 1979-01-10
127 continuous process for separating non-paraffinic hydrocarbons of paraffinic hydrocarbons FR7812388 1978-04-26 FR2388876A1 1978-11-24
<P>Procédé continu pour séparer des hydrocarbures non-paraffiniques d'hydrocarbures paraffiniques. </P><P>Selon la présente invention, un courant, tel qu'un courant d'hydrocarbures contenant des hydrocarbures aliphatiques saturés en même temps que des composés non-saturés et/ou non-aliphatiques, est mis en contact avec un mélange comprenant un composé du ruthénium à un bas degré d'oxydation, et une solution aqueuse d'hypochlorite. Le composé du ruthénium, en présence de la solution aqueuse d'hypochlorite, est transformé en un composé du ruthénium d'un degré d'oxydation plus élevé. A son tour, le composé du ruthénium d'un degré d'oxydation plus élevé oxydé sélectivement les composés autres que les hydrocarbures aliphatiques saturés, tels que les composes aromatiques et les hydrocarbures aromatiques. </P><P>Application à l'oxydation sélective d'un type d'hydrocarbures en presence d'un autre type d'hydrocarbures.</P>
128 A method for separating hydrocarbons non paraffinic paraffinic hydrocarbons FR7812386 1978-04-26 FR2388875A1 1978-11-24
<P>La présente invention concerne la séparation d'hydrocarbures non-paraffiniques d'hydrocarbures paraffiniques. Des hydrocarbures non-paraffiniques, tels que des hydrocarbures aromatiques, dans un courant d'hydrocarbures paraffiniques sont éliminés par mise en contact du courant d'hydrocarbures paraffiniques avec un système oxydant comprenant une solution aqueuse d'hypochlorite, comme d'hypochlorite de sodium, et un compose du ruthénium, comme du dioxyde de ruthénium, comme catalyseur d'oxydation. Le composé du ruthénium est oxydé par l'hypochlorite à un degré d'oxydation plus élevé avec pour résultat une oxydation sélective des hydrocarbures non-paraffiniques en composés non-paraffiniques solubles dans l'eau et/ou en CO2 . </P><P>On peut ainsi recueillir un courant d'hydrocarbures paraffiniques sensiblement exempt d'hydrocarbures non-paraffiniques.</P>
129 A process for the removal of non-paraffinic hydrocarbons from paraffinic hydrochlorofluorocarbons DE2818823 1978-04-28 DE2818823A1 1978-11-02 ABRAMOVICI MIRON; RYLANDER PAUL N; VIANI UMBERTO
130 Improvement in the refining of hydrocarbons FR1084027D 1953-09-25 FR1084027A 1955-01-14
131 Способ очистки бензинов и подобных углеводородов SU301927 1940-02-04 SU70743A1 1947-11-30 VISHNEVSKIJ N E
132 Improvements in the refining of liquid hydrocarbons FR549963D 1922-04-08 FR549963A 1923-02-23
133 PROCESS FOR REMOVING MERCURY FROM CRUDE OIL EP18846865.6 2018-08-01 EP3668634A1 2020-06-24 LAMBERTSSON, Lars, T.; LORD, Charles, J.; BJÖRN, Erik, L.; FRECH, Wolfgang
Methods, systems and designs are provided for removing mercury from crudes. Crude oil containing a synthetic reducing agent is heated to a temperature above 100° C. and held at that temperature for a specified period of time to convert all of the forms of mercury in the oil into the elemental mercury form. The elemental mercury is then stripped from the crude oil by e.g., flashing the hot oil and/or contacting it with a gas phase.
134 PREPARATION OF ALKYLATION FEED EP09818197.7 2009-09-04 EP2334761B1 2019-05-22 CROSS, William, M., Jr.; SMITH, Lawrence, A., Jr.; PODREBARAC, Gary, G.
135 PROCESS FOR REMOVING HEAVY METALS FROM FLUIDS EP11841430.9 2011-11-16 EP2640810B1 2016-03-02 YEAN, Sujin
136 METHOD AND SYSTEM FOR OXIDATIVELY INCREASING CETANE NUMBER OF HYDROCARBON FUEL EP10816773 2010-09-10 EP2478075A4 2013-07-24 KIN MENG CHAN; KAMALUL ARIFIN YUSOF; SHAHRUL NIZA BIN ABDUL RAHIM; MD ASRAFF BIN ABDUL KARIM; ROGER KAI LOTT
137 Method for desulfurization of hydrocarbon oils EP10183804.3 2010-09-30 EP2305779A3 2011-12-14 Haitko, Deborah Ann; Osaheni, John Aibangbee; Soloveichik, Grigorii Lev

Provided herein are processes for desulfurization of a hydrocarbon oil. The processes (100) comprise providing a hydrocarbon oil comprising sulfur impurities (101) and mixing the oil with a phase transfer agent and a source of hypochlorite ions to provide a mixture (102). The mixture separates into an aqueous hypochlorite phase and a nonpolar oil phase (103). The hypochlorite phase may then be removed from the oil phase, and the oil phase centrifuged and separated from any precipitate, thereby providing a cleaned oil phase.

138 PREPARATION OF ALKYLATION FEED EP09818197.7 2009-09-04 EP2334761A2 2011-06-22 CROSS, William, M., Jr.; SMITH, Lawrence, A., Jr.; PODREBARAC, Gary, G.
A process for treating an alkylation feedstock comprising olefins, n-alkanes, iso-alkanes, and impurities including one or more of butadiene, oxygenates, nitrogen- containing compounds, and sulfur-containing compounds, the process including: contacting an alkylation feedstock containing at least one of oxygenates and nitrogen-containing compounds with water to produce a hydrocarbon fraction having a reduced concentration of the at least one of oxygenates and nitrogen-containing compounds and an aqueous fraction comprising at least a portion of the at least one of oxygenates and nitrogen-containing compounds; separating water from the hydrocarbon fraction having a reduced concentration to produce a hydrocarbon fraction having a reduced water content; contacting the hydrocarbon fraction having a reduced water content with an oligomerization catalyst in a first oligomerization reaction zone under oligomerization conditions to react at least a portion of the olefins to form a reactor effluent comprising olefin oligomers; and feeding at least a portion of the reactor effluent to an alkylation unit.
139 PROCESS FOR REMOVING METAL IONS FROM CRUDE OIL EP01931866.6 2001-05-17 EP1294827A1 2003-03-26 COLLINS, Ian Ralph; DUNCUM, Simon Neil; OSBORNE, Christopher George
A process for removing metal ions from crude oil comprising contacting a non-ionic amphiphilic solvent with the crude oil, optionally, in the presence of water, so as to produce a metal ion-containing phase, and separating the metal ion-containing phase from the crude oil.
140 PROCESS FOR REDUCING THE ACIDITY OF OIL EP00931456.8 2000-05-30 EP1194505A1 2002-04-10 COLLINS, Ian Ralph; DUNCUM, Simon Neil; OSBORNE, Christopher George
The present invention provides a process for de-acidifying crude oil and/or crude oil distillate, said process comprising: (a) contacting crude oil and/or crude oil distillate with a Group IIA metal hydroxide in the presence of water, wherein water is present in a concentration of 0.01 to 100 wt.% of the crude oil and/or crude oil distillate; and (b) introducing a demulsifier to the mixture of crude oil and/or crude oil distillate, Group IIA metal hydroxide and water, in an amount effective to cause the mixture to separate into an oil-rich phase, an aqueous phase and an interface layer disposed between the oil-rich phase and aqueous phase.
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