• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    A catalytic process for treating a mercaptan-containing sour petroleum distillate is disclosed. The distillate is contacted with a weakly basic anion exchange resin to separate a portion of the mercaptan content and substantially all of the acidic catalyst toxins or toxin precursors. The resulting distillate is subsequently treated in contact with a supported metal phthalocyanine catalyst in admixture with an oxidizing agent and an alkaline solution to convert the residual mercaptans to innocuous disulfides.
    公开号:SU784792A3
    申请号:SU782619153
    申请日:1978-05-23
    公开日:1980-11-30
    发明作者:Гарольд Джозеф Карлсон Дэвид
    申请人:Юоп Инк (Фирма)；
    IPC主号:
    专利说明:

    ny amine as a functional group.
    Pretreatment of the feedstock is carried out at a pressure of 1-100 atm.
    In this case, sulfur compounds, mercaptans, and virtually all catalytic acid poisons — mainly phenolic substances, which either act as catgetizing oxides — are either adsorbed or oxidized to catalytic oxides during subsequent catalytic oxidation. The contacting is carried out for a time equivalent to the spatial velocity of the feedstock per hour 0.5-5.0. The regeneration of the anion exchange resin can be carried out in known ways.
    Thus, the regeneration is carried out by rinsing the resin in a solution that is mixed with a distillate, usually in methanol, after which the regeneration is carried out by passing an aqueous caustic solution or an ammonium solution over the resin. After the final rinsing in water, before re-using the resin, the rinsing is again carried out in methanol.
    The treated feedstock is then subjected to oxidation in the presence of a catalyst based on cobalt deposited on a substrate in combination with an oxidizing agent and an alkaline solution, pH 9-14.
    The oxidation is carried out at 10-250 ° C and a pressure of 1-100 atm for a time equivalent to the spatial speed of the raw material per hour, which is 0.5-5.0.
    As a catalyst used in the described method, it is possible to use a catalyst containing a phthalocyanine of a metal of the III group, such as phthalocyanine cobalt of iron, rhodium, nickel, platinum, palladium, ruthenium, osmium, iridium, or mixtures of these compounds. Other metal phthalocyanines can also be used, including the phthalocyanines of magnesium, titanium, hafnium, vanadium tantalum, molybdenum, manganese, copper, silver, tin, and similar compounds. Preferably, metal sulfthal derivatives, such as phthalocyanine cobalt monosulfate, phthalocyanine cobalt disulfonate or mixtures thereof, are used.
    It is also possible to use carboxylated derivatives. The catalyst support may contain any of various types of charcoal obtained from the destructive distillation of wood, peat, nut shell lignin, bones and other carbonaceous substances, with activated charcoal being preferred. It is useful to use activated carbons derived from plants when processing peat and wood; coals obtained by treating petroleum soot.
    Such clays and silicates, for example, diatomic lands, fuller's earth, diatomaceous earth, clay attapulgus, feldspar, montmorylnite, haloisite, kaolin and other similar substances, as well as those existing in natural form or in a layer of artificially refractory inorganic oxides, are used as substrates for the catalyst. such as alumina, silica, zirconia, boron oxide, etc., or combinations of these oxides, such as silica, alumina, silica, zirconia, alumina, zirconia, etc. The choice of material is carried out based on the specific conditions of the oxidation process. For example, when processing distilled petroleum products containing sulfur compounds, the solid absorbent material that is the substrate must be insoluble in these products and, moreover, neutral to the effects of aqueous solutions of caustic soda and distilled petroleum products under their processing conditions. Catalyst based on metal phthalocyanine, deposited on a substrate, contains 0.000110 wt.% Metal phthalocyanine.
    Oil distillation products containing sulfur compounds differ dramatically from each other in composition depending on the oil from which the distillates are obtained, the boiling range of the distillate, and the method of treating the oil, as a result of which this distillate is obtained.
    The described method is especially effective in the treatment of distillates of oil having high boiling points, including, in particular, kerosene and jet fuel. These petroleum-distilled products containing sulfur compounds, whose boiling points are quite high, usually contain a greater amount of hardly oxidizable mercaptans, i.e. caustic-insoluble, highly branched thiols and aromatic thiols, in particular, high molecular weight tertiary and multifunctional mercaptans. In the latter case, difficulties arise due to the presence of acidic and carbon-free impurities, usually phenol compounds, which are found in such distillates in high concentrations.
    Q The described method can be used to treat petroleum products having a low temperature, containing sulfur compounds, such as gaseous, gasoline and other
    5 fractions of oil.
    权利要求:
    Claims (1)
    [1]
    Claim
    The method of purification of oil distillates from sulfur compounds and catalytic poisons by pretreating the feedstock 40 and oxidizing the treated feedstock with oxygen in the presence of a metal phthalocyanine catalyst in an alkaline medium, characterized in that, in order to increase the efficiency of the process, the feedstock is pretreated by contacting the latter with a weakly basic anion exchange resin, which is a porous matrix based on styrene-divinylbenzene poly50 measure with transverse bonds Containing as functional group a tertiary amine.
    类似技术:
    公开号 | 公开日 | 专利标题
    SU784792A3|1980-11-30|Method of purifying oil distillates from sulfuric compounds and catalyst poisons
    US4124494A|1978-11-07|Treating a petroleum distillate with a supported metal phthalocyanine and an alkanolamine hydroxide
    US4485007A|1984-11-27|Process for purifying hydrocarbonaceous oils
    US4124531A|1978-11-07|Catalytic composite for the treatment of sour petroleum distillates
    US4913802A|1990-04-03|Process for sweetening a sour hydrocarbon fraction
    US4498978A|1985-02-12|Catalytic oxidation of mercaptan in petroleum distillate
    US4238320A|1980-12-09|Denitrogenation of shale oil
    CA1224771A|1987-07-28|Catalytic oxidation of mercaptan in petroleumdistillate
    RU1826987C|1993-07-07|Method of purification of high-sulfur hydrocarbon fraction containing mercaptan
    US4207173A|1980-06-10|Sweetening of hydrocarbon distillates utilizing a tetra-alkyl guanidine with phthalocyanine catalyst
    US4107078A|1978-08-15|Preparation of a supported metal phthalocyanine catalyst
    US4260479A|1981-04-07|Catalytic oxidation of mercaptan in sour petroleum distillate
    CA1081152A|1980-07-08|Mercaptan conversion process for a petroleum distillate charge stock
    US4100057A|1978-07-11|Method of treating a sour petroleum distillate
    US4206043A|1980-06-03|Conversion of mercaptans contained in a sour petroleum distillate
    US6485633B2|2002-11-26|Process for the demercaptanization of petroleum distillates
    IL24118A|1969-02-27|Process for reactivating a solid phthalocyanine catalyst
    US4168245A|1979-09-18|Preparation of a supported metal phthalocyanine catalyst
    GB2027049A|1980-02-13|Process for Treating a Sour- Petroleum Distillate
    US4121999A|1978-10-24|Catalytic oxidation of petroleum distillates with charcoal and with supported metal phthalocyanine
    CN111278952A|2020-06-12|Catalytic system and method for removing heteroatom compounds from hydrocarbon streams
    CA1132933A|1982-10-05|Conversion of mercaptans contained in asour petroleum distillate
    US2081309A|1937-05-25|Process for treating oils
    CA1093492A|1981-01-13|Process for sweetening sour hydrocarbon distillates
    KR810000938B1|1981-08-22|A process for treating a sour petroleum distillate
    同族专利:
    公开号 | 公开日
    HU180971B|1983-05-30|
    IE781016L|1978-11-23|
    FI62856C|1983-03-10|
    ATA373978A|1981-01-15|
    IT7823671D0|1978-05-22|
    IN149145B|1981-09-26|
    ES470081A1|1979-01-01|
    BE867386A|1978-09-18|
    DD137725A5|1979-09-19|
    CS207616B2|1981-08-31|
    AT363575B|1981-08-10|
    IL54733A|1981-07-31|
    NL7805511A|1978-11-27|
    GB1602390A|1981-11-11|
    NO781760L|1978-11-24|
    DE2822235A1|1978-11-30|
    JPS5729512B2|1982-06-23|
    AR227870A1|1982-12-30|
    BR7803245A|1979-01-02|
    PL111177B1|1980-08-30|
    GR64876B|1980-06-06|
    TR19966A|1980-06-02|
    RO75843A|1981-02-28|
    IT1121201B|1986-03-26|
    EG13862A|1982-09-30|
    US4113604A|1978-09-12|
    CA1100079A|1981-04-28|
    FR2392103A1|1978-12-22|
    PL207036A1|1979-02-26|
    IL54733D0|1978-07-31|
    FR2392103B1|1983-12-23|
    JPS53147702A|1978-12-22|
    IE47054B1|1983-12-14|
    FI62856B|1982-11-30|
    DE2822235C2|1982-12-09|
    FI781618A|1978-11-24|
    MX147667A|1983-01-04|
    YU120878A|1982-08-31|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    FR1100026A|1954-02-20|1955-09-15|Exxon Standard Sa|Process for softening petroleum gasolines using anion exchange resins, and regeneration of said resins|
    US3108081A|1959-07-17|1963-10-22|Universal Oil Prod Co|Catalyst and manufacture thereof|
    US3108948A|1960-05-09|1963-10-29|Petrolite Corp|Petroleum refining|
    US3144403A|1961-11-24|1964-08-11|Sun Oil Co|Sweetening hydrocarbons|
    US3130148A|1962-06-22|1964-04-21|Universal Oil Prod Co|Treating hydrocarbon distillates|
    US3392111A|1967-06-16|1968-07-09|Howe Baker Eng|Regeneration of ion exchange catalyst in sweetening process|
    US3454488A|1967-09-27|1969-07-08|William R Lewis|Sweetening process utilizing ion exchange compositions|
    FR1602191A|1968-12-31|1970-10-19|US4206043A|1978-11-06|1980-06-03|Uop Inc.|Conversion of mercaptans contained in a sour petroleum distillate|
    US4378305A|1980-12-10|1983-03-29|Uop Inc.|Catalytic composite particularly useful for the oxidation of mercaptans and the removal of gums contained in a sour petroleum distillate|
    US4298502A|1978-11-06|1981-11-03|Uop Inc.|Catalytic composite particularly useful for the oxidation of mercaptans and the removal of gums contained in a sour petroleum distillate|
    DE3008284C2|1980-03-04|1982-11-04|UOP Inc., 60016 Des Plaines, Ill.|Process for treating an acidic mercaptan-containing petroleum distillate to convert the mercaptans|
    JPH0132277B2|1980-03-24|1989-06-30|Uop Inc|
    US4647367A|1985-12-23|1987-03-03|Uop Inc.|Antifouling agents for prevention of unwanted coke formation in reactors|
    US4753722A|1986-06-17|1988-06-28|Merichem Company|Treatment of mercaptan-containing streams utilizing nitrogen based promoters|
    EP0337837B1|1988-04-14|1990-08-29|Societe Nationale Elf Aquitaine |Process for the preparation of organic disulfides and polysulfides|
    US8323603B2|2004-09-01|2012-12-04|Sud-Chemie Inc.|Desulfurization system and method for desulfurizing a fuel stream|
    US7780846B2|2004-09-01|2010-08-24|Sud-Chemie Inc.|Sulfur adsorbent, desulfurization system and method for desulfurizing|
    US20060283780A1|2004-09-01|2006-12-21|Sud-Chemie Inc.,|Desulfurization system and method for desulfurizing a fuel stream|
    US20060043001A1|2004-09-01|2006-03-02|Sud-Chemie Inc.|Desulfurization system and method for desulfurizing afuel stream|
    WO2011114352A2|2010-03-17|2011-09-22|Indian Oil Corporation Limited|Process for selective removal of mercaptan from aviation turbine fuel |
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    US05/799,825|US4113604A|1977-05-23|1977-05-23|Process for treating a sour petroleum distillate with anion exchange resin and with metal phthalocyanine catalyst|
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