Process for producing jet fuel with ZSM-22 containing catalist
    51.
    发明授权
    Process for producing jet fuel with ZSM-22 containing catalist 失效
    用含有催化剂的ZSM-22生产喷气燃料的方法

    公开(公告)号:US4717465A

    公开(公告)日:1988-01-05

    申请号:US915935

    申请日:1986-10-06

    摘要: A novel process is disclosed for the production of high boiling jet fuels which comprises contacting a chargestock with an end boiling point of about 750.degree. F. with ZSM-22 under carefully controlled conditions of temperature and pressure and blending the 330.degree. F. plus fraction with a conventional jet fuel in order to obtain a product having acceptable jet fuel properties and having a high boiling range.

    摘要翻译: 公开了一种用于生产高沸点喷气燃料的新方法,其包括在精心控制的温度和压力条件下将具有约750°F的终沸点的电荷料与ZSM-22接触,并将330°F加级分 使用常规的喷气燃料,以获得具有可接受的喷气燃料性能并具有高沸点范围的产品。

    Manufacture of hydrocracked low pour lubricating oils
    57.
    发明授权
    Manufacture of hydrocracked low pour lubricating oils 失效
    加氢裂化低润滑油的制造

    公开(公告)号:US4283271A

    公开(公告)日:1981-08-11

    申请号:US158980

    申请日:1980-06-12

    IPC分类号: C10G47/16 C10G65/12 C10G49/22

    CPC分类号: C10G65/12 C10G2400/10

    摘要: Hydrocracked, low pour lubricating oils of good stability are manufactured by passing a suitable hydrocarbon feed sequentially through a hydrocracking zone, a catalytic dewaxing zone, and a hydrotreating zone, all at high pressure and in that order, and with separation of hydrocrackate from recycle hydrogen prior to dewaxing. Only clean makeup hydrogen is fed to the dewaxer, passed through the hydrotreater, and then on to the hydrocracker, thereby providing an exceptionally efficient process.

    摘要翻译: 通过使合适的烃进料依次通过加氢裂化区,催化脱蜡区和加氢处理区,全部以高压和依次顺序,并将氢化裂解物从再循环氢气中分离出来制备具有良好稳定性的加氢裂化低倾点润滑油 脱蜡之前。 只有干净的补充氢气才能进入脱蜡机,通过加氢处理器,然后再加到加氢裂化器上,从而提供了非常有效的工艺。

    Conversion of synthesis gas to high octane predominantly olefinic naphtha
    59.
    发明授权
    Conversion of synthesis gas to high octane predominantly olefinic naphtha 失效
    合成气转化为高辛烷值主要是烯烃石脑油

    公开(公告)号:US4172843A

    公开(公告)日:1979-10-30

    申请号:US926987

    申请日:1978-07-21

    IPC分类号: B01J29/40 B01J29/46 C07C1/04

    摘要: An improved method is disclosed for converting synthesis gas to hydrocarbon mixtures wherein the syngas is contacted with a special catalyst comprising a crystalline zeolite having a silica-to-alumina ratio of greater than 200 (including zeolites containing essentially no alumina) and an (R.sub.2 O+ M.sub.2 /.sub.n O): SiO.sub.2 ratio of less than 1.1:1 where M is a metal other than a metal of Group IIIA, n is the valence of said metal, and R is an alkyl ammonium radical, said organosilicate being characterized by a specified x-ray diffraction pattern. In a specific embodiment of this invention, synthesis gas is contacted with a catalyst comprising an intimate mixture of said crystalline zeolite catalyst and iron-containing, Fischer-Tropsch catalyst to produce a liquid hydrocarbon product having a boiling range of less than 400.degree. F. at a 90 percent overhead and being a predominantly olefinic product, wherein the structure of the olefins is substantially branched chain with internally-positioned double bonds.

    摘要翻译: 公开了一种用于将合成气转化为烃混合物的改进方法,其中合成气与包含二氧化硅与氧化铝之比大于200的结晶沸石(包括基本上不含氧化铝的沸石)和(R2O + M2 / nO):SiO 2比小于1.1:1,其中M是除IIIA族金属以外的金属,n是所述金属的化合价,R是烷基铵基团,所述有机硅酸盐的特征在于指定的x- 射线衍射图。 在本发明的具体实施方案中,使合成气与包含所述结晶沸石催化剂和含铁的费 - 托催化剂的紧密混合物的催化剂接触,以产生沸点低于400°F的液体烃产物。 在90%的开销下,并且主要是烯烃产物,其中烯烃的结构基本上是支链的,内部定位的双键。