Hydrocarbon cracking and reforming process
    1.
    发明授权
    Hydrocarbon cracking and reforming process 失效
    烃裂解和重整过程

    公开(公告)号:US5100534A

    公开(公告)日:1992-03-31

    申请号:US609553

    申请日:1990-11-06

    IPC分类号: C10G57/00 C10L1/02

    CPC分类号: C10G57/00 C10L1/023

    摘要: An improved process for upgrading paraffinic naphtha to high octane fuel by contacting a naphtha feedstock, such as virgin naphtha feedstock stream containing predominantly C.sub.7 -C.sub.12 alkanes and naphthenes, with solid medium pore acid zeolite cracking catalyst under low pressure selective cracking conditions effective to produce at least 10 wt % selectivity C.sub.4 -C.sub.5 isoalkene. Cracking effluent is separated to obtain a light olefinic fraction rich in C.sub.4 -C.sub.5 isoalkene and a C.sub.6 + liquid fraction of enhanced octane value containing less than 50 wt % aromatic hydrocarbons. In a multistage operation enhanced octane products are obtained by etherifying the isoalkene fraction and by contacting the C.sub.6 + normally liquid fraction with reforming catalyst under moderate reforming conditions at elevated temperature to obtain a reformate product of enhanced octane value.

    摘要翻译: 将石脑油原料(如含有主要为C 7 -C 12烷烃和环烷烃的原始石脑油原料流)与固体中孔孔酸沸石裂化催化剂接触的改进方法,该方法是在低压选择性裂解条件下有效生产 至少10重量%的选择性C4-C5异烯烃。 裂解流出物被分离以获得富含C4-C5异烯烃的轻烯烃馏分和含有小于50重量%芳烃的增强辛烷值的C6 +液体馏分。 在多级操作中,通过醚化异烯烃馏分并且在中等重整条件下在升高的温度下使C6 +正常液体馏分与重整催化剂接触获得增强的辛烷值产物,以获得增强的辛烷值的重整产物。

    Process for production of iso-olefin and ether
    2.
    发明授权
    Process for production of iso-olefin and ether 失效
    异烯烃和醚的生产方法

    公开(公告)号:US5100533A

    公开(公告)日:1992-03-31

    申请号:US607952

    申请日:1990-11-01

    IPC分类号: C10G57/00 C10L1/02

    CPC分类号: C10L1/023 C10G57/00

    摘要: Process and apparatus for upgrading paraffinic naphtha to high octane fuel by contacting a fresh virgin naphtha feedstock stream medium pore acid cracking catalyst comprising MCM-22 zeolite under low pressure selective cracking conditions effective to produce increased yield of total C4-C5 branched aliphatic hydrocarbhons. The preferred feedstock is straight run naptha containing C7+ alkanes, at least 15 wt % C7+ cycloaliphatic hydrocarbons and less than 20% aromatics, which can be converted with a fluidized bed catalyst in a vertical riser reactor during a short contact period.The isoalkene products of cracking are etherified to provide high octane fuel components.

    摘要翻译: 通过在低压选择性裂解条件下接触包含MCM-22沸石的新鲜原始石脑油原料流介质孔隙酸裂解催化剂,有效地产生总C4-C5支链脂族烃的产率提高,将石蜡石脑油升级成高辛烷值燃料的方法和设备。 优选的原料是含有C7 +烷烃,至少15重量%的C7 +脂环族烃和少于20%的芳族化合物的直馏石脑油,其可以在短时间接触期间在垂直提升管反应器中用流化床催化剂转化。 裂化的异烯烃产物被醚化以提供高辛烷值的燃料成分。

    Process for improving olefin etherification catalyst life
    3.
    发明授权
    Process for improving olefin etherification catalyst life 失效
    改进烯烃醚化催化剂寿命的方法

    公开(公告)号:US5300126A

    公开(公告)日:1994-04-05

    申请号:US963955

    申请日:1992-10-19

    摘要: A method is disclosed for the pretreatment of olefinic hydrocarbon feedstock to remove conjugated dienes and/or basic nitrogen compounds that deactivate acidic catalyst particles used in olefin conversion processes by reacting the dienes with one or more dienophiles to form the corresponding Diels-Alder adduct, followed by catalytic conversion of the olefinic hydrocarbon feedstock containing the adduct. The formation of the Diels-Alder adduct essentially eliminates the role of dienes in the feedstock as catalyst deactivating agents. When maleic anhydride (MA) is employed as the dienophile, basic nitrogen reacts with maleic anhydride, or with the tetrahydrophthalic anhydride adduct, to lower the amount of catalyst deactivating basic nitrogen compounds in the feedstock. Where the olefin conversion process comprises etherification of isoolefins with alkanol in a C.sub.4 + or C.sub.5 + olefinic hydrocarbon feedstream to produce a gasoline boiling range product enriched in oxygen and rich in high octane value alkyl tertiary alkyl ethers, it has been discovered that the adduct, particularly those adducts formed with MA, is in the gasoline boiling range and contributes usefully to the oxygen enrichment of the gasoline and to octane value.

    摘要翻译: 公开了一种用于预处理烯烃原料以除去共轭二烯和/或碱性氮化合物的方法,其通过使二烯与一种或多种亲双烯体反应形成相应的狄尔斯 - 阿尔德加合物,使烯烃转化过程中使用的酸性催化剂颗粒失活,随后 通过催化转化含有加合物的烯烃原料。 Diels-Alder加合物的形成基本上消除了二烯在原料中作为催化剂失活剂的作用。 当使用马来酸酐(MA)作为亲二烯体时,碱性氮与马来酸酐或四氢邻苯二甲酸酐加合物反应,以降低原料中催化剂失活碱性氮化合物的量。 当烯烃转化方法包括在C4 +或C5 +烯烃原料流中异构烯烃与烷醇的醚化以产生富含氧并富含高辛烷值烷基叔烷基醚的汽油沸程产物时,已经发现加合物,特别是那些 与MA形成的加合物处于汽油沸点范围内,有助于汽油的富氧和辛烷值。

    Selective cracking and etherification of olefins
    4.
    发明授权
    Selective cracking and etherification of olefins 失效
    烯烃的选择性裂化和醚化

    公开(公告)号:US5264635A

    公开(公告)日:1993-11-23

    申请号:US770215

    申请日:1991-10-03

    CPC分类号: C07C6/04 C07C41/06

    摘要: A selective alkene upgrading process wherein a mixture of intermediate molecular weight monoalkenes comprising at least one linear alkene component and at least one tertiary alkene component is contacted under selective olefin interconversion conditions with medium pore, shape selective acid catalyst, such as MCM-22 aluminosilicate zeolite, thereby converting at a major amount of linear intermediate alkene to lower alkene while leaving tertiary alkene substantially unconverted. In the preferred embodiments, the process interconversion conditions comprise reaction temperature in the range of about 300.degree. C. to 550.degree. C., pressure in the range of 100 kpa to 1000 kPa, thereby selectively converting at least 60% (net) of linear intermediate alkene while converting less than 20% (net) of branched alkene. By etherifying at least a portion of the unconverted tertiary alkene, an oxygenated fuel having enhanced octane rating is obtained. Cracked lower olefins may be recovered for upgrading.

    摘要翻译: 选择性烯烃改质方法,其中包含至少一种直链烯烃组分和至少一种叔烯烃组分的中等分子量单烯烃的混合物在选择性烯烃相互转化条件下与中孔,形状选择性酸催化剂如MCM-22铝硅酸盐沸石 ,从而将主要量的线性中间体烯转化为低级烯烃,同时使叔烯烃基本上未转化。 在优选的实施方案中,工艺互转条件包括在约300℃至550℃范围内的反应温度,在100kpa至1000kPa范围内的压力,由此选择性地将至少60%(净)的线性 中间烯烃,同时转化少于20%(净)的支链烯烃。 通过醚化至少一部分未转化的叔烯烃,获得具有增强的辛烷值的含氧燃料。 可以回收裂解的低级烯烃进行升级。

    Hydroisomerization process for pour point reduction of long chain alkyl
aromatic compounds
    8.
    发明授权
    Hydroisomerization process for pour point reduction of long chain alkyl aromatic compounds 失效
    长链烷基芳族化合物倾点降低的加氢异构化方法

    公开(公告)号:US5157187A

    公开(公告)日:1992-10-20

    申请号:US636828

    申请日:1991-01-02

    IPC分类号: C10M127/04

    CPC分类号: C10M127/04 C10M2203/06

    摘要: There is provided a method for reducing the pour point of an alkyl aromatic lube base stock by hydroisomerizing alkyl side groups on alkyl aromatic compounds. The alkyl aromatic, compounds may be alkylated naphthalenes. The hydroisomerization reaction may take place over a catalyst comprising zeolite beta and platinum.

    摘要翻译: 提供了一种通过烷基芳族化合物上的烷基侧基加氢异构化来降低烷基芳族润滑剂基础油料的倾点的方法。 烷基芳族化合物可以是烷基化萘。 加氢异构化反应可以在包含β沸石和铂沸石的催化剂上进行。

    Multistage olefin upgrading process using synthetic mesoporous
crystalline material
    9.
    发明授权
    Multistage olefin upgrading process using synthetic mesoporous crystalline material 失效
    使用合成介孔结晶材料进行多级烯烃升级工艺

    公开(公告)号:US5134241A

    公开(公告)日:1992-07-28

    申请号:US718879

    申请日:1991-06-21

    摘要: A process for upgrading olefinic feedstocks containing lower olefins employing new synthetic catalyst of ultra-large pore crystalline material. The new crystalline material exhibits unusually large sorption capacity demonstrated by its benzene adsorption capacity of greater than about 15 grams benzene/100 grams at 50 torr and 25.degree. C., a hexagonal electron diffraction pattern that can be indexed with a d.sub.100 value greater than about 18 Angstrom Units and a hexagonal arrangement of uniformly sized pores with a maximum perpendicular cross section of at least about 13 Angstrom units. A multistage process is provided for catalytic oligomerization of lower olefin which comprises contacting olefinic feedstock under catalytic conversion conditions with acid metallosilicate solid catalyst having the structure of MCM-41 with hexagonal honeycomb lattice structure consisting essentially of uniform pores in the range of about 20 to 100 Angstroms. The oligomerization reaction is very selective, especially when conducted at temperature of about 40.degree. to 250.degree. C., yielding branched intermediate olefins. Low severity reaction permits excellent conversio of lower olefins at pressure of about 100-13,000 pKa range and moderate space velocity. Intermediate oligomers produced over MCM-41, when reacted under cracking/disproportionation conditions yield etherifiable C.sub.4 + isoalkenese in good yield.

    摘要翻译: 一种使用新型超大孔结晶材料合成催化剂来提纯含有低级烯烃的烯烃原料的方法。 新的结晶材料表现出非常大的吸附能力,其吸附能力在50托和25℃时苯吸附能力大于约15克苯/ 100克,可以用大于约100的d100值进行指数的六方电子衍射图 18埃单位和具有至少约13埃单位的最大垂直截面的均匀尺寸孔的六边形排列。 提供了用于低级烯烃催化低聚的多级方法,其包括在催化转化条件下使烯属原料与具有MCM-41结构的酸性金属硅酸盐固体催化剂接触,其中六方蜂窝晶格结构基本上由约20至100范围内的均匀孔组成 埃 低聚反应非常有选择性,特别是当在约40℃至250℃的温度下进行时,产生支链中间体烯烃。 低强度反应允许在约100-13000pKa范围的压力和适度的空间速度下的低级烯烃的优异转录。 在裂化/歧化条件下反应时,MCM-41产生的中间体低聚物以良好的产率得到可醚化的C4 +异烯烃。