首页> 外国专利> Oxidn.- and cold-stable middle distillates prodn. - from mineral oil fractions by hydrocracking using hydrocracking catalyst and hydrotreating using borosilicate pentasil zeolite

Oxidn.- and cold-stable middle distillates prodn. - from mineral oil fractions by hydrocracking using hydrocracking catalyst and hydrotreating using borosilicate pentasil zeolite

机译:氧化稳定和冷稳定的中间馏分-通过使用加氢裂化催化剂进行加氢裂化和使用硼硅酸钾五元硅沸石进行加氢处理,从矿物油馏分中分离出

摘要

Oxidn-stable and cold-stable base oils and middle distillates are produced from mineral oil fractions boiling in the range above 350 deg C. The novelty is that the mineral oil fraction is converted on a hydrocracking catalyst under hydrocracking conditions to 20-80 wt% components boiling below 360 deg C, the reactor charge is sepd in a high pressure separator into liq and gaseous phase. In a second stage of the process, the whole reactor charge or only the liq phase, directly or after distilling off the components boiling below 360 deg C is treated with hydrogen in the presence of a catalyst contg a crystalline borosilicate pentasil-type zeolite, Al203 or amorphous aluminosilicate as carrier and metal(s) from gp VIb or VIII and P, at 200-450 deg C and 20-150 bar. After distilling off the hydrogenation prod a middle distillate boiling in the range 180-360 deg C with a pour pt below -30 deg C and an oxidn-stable residue with a bpt above 360 deg C, VI 110-135 and pour pt below -12 deg C is obtd.
机译:氧化稳定和冷稳定的基础油和中间馏分是由沸点在350℃以上的矿物油馏分生产的。新颖的是,矿物油馏分在加氢裂化条件下通过加氢裂化催化剂转化为20-80 wt%当组分沸腾到360℃以下时,将反应器进料在高压分离器中分离成液相和气相。在该方法的第二阶段中,直接或在蒸馏掉沸点低于360℃的组分后,将整个反应器装料或仅液相用氢气处理,该催化剂在含有结晶硼硅酸五硅锰型沸石Al 2 O 3的催化剂的存在下进行。或无定形硅铝酸盐作为载体和金属,来自gp VIb或VIII和P,温度为200-450℃,压力为20-150 bar。蒸馏出氢化产物后,中间馏分沸点在180-360℃范围内,倾点低于-30℃,氧化稳定的残渣的bpt高于360℃,VI 110-135,倾点低于-超过12℃。

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