Lubricant production process
    31.
    发明授权
    Lubricant production process 失效
    润滑油生产过程

    公开(公告)号:US4919788A

    公开(公告)日:1990-04-24

    申请号:US260857

    申请日:1988-10-21

    IPC分类号: C10G45/64 C10G65/04 C10G67/04

    摘要: A process for producing lubricant oils of low pour point and high viscosity index by first carrying out a partial dewaxing of a lubricant base stock in an initial catalytic dewaxing operation, followed by a selective dewaxing step. The initial catalytic dewaxing step is carried out using a large pore, high silica zeolite dewaxing catalyst such as high silica Y or zeolite beta which dewaxes by isomerizing the waxy components of the base stock to less waxy brance chain isoparaffins but the severity of the operation is controlled so as to effect only a partial removal of the waxy components. Further removal of the waxy components is effected during the subsequent dewaxing step which is selective for the removal of the more waxy n-paraffin components, leaving the branched chain isoparaffins which contribute to a high VI in the product. The selective dewaxing step may be either a solvent, e.g. MEK dewaxing operation or a catalytic dewaxing using a highly shape selective zeolite such as ZSM-22 or ZSM-23. The severity of the initial catalytic dewaxing operation may be controlled so as to effect a net increase in the content of isoparaffins and because of the selective nature of the solvent dewaxing step, this increased isoparaffins concentration may be retained, producing a product of high VI. The pour point of the feedstock is preferably reduced during the initial catalytic dewaxing step to a value which is no lower than 10.degree. F. and preferably no lower than 20.degree. F., above the target pour point for the products. Generally, this will entail a reduction of at least 10.degree. F. and preferably at least 20.degree. F. in the pour point of the feed.

    摘要翻译: 首先在初始催化脱蜡操作中进行润滑剂原料的部分脱蜡,然后进行选择性脱蜡步骤,生产低倾点和高粘度指数的润滑油的方法。 初始催化脱蜡步骤使用大孔,高二氧化硅沸石脱蜡催化剂如高二氧化硅Y或沸石β进行,该脱蜡通过使基础油料的蜡质组分异构化成较少的蜡状分支链异链烷烃,但操作的严重性是 被控制以仅影响蜡组分的部分去除。 在随后的脱蜡步骤中进一步除去蜡状组分,该脱蜡步骤选择性地除去更多的蜡状正链烷烃组分,留下有助于产物中高VI的支链异链烷烃。 选择性脱蜡步骤可以是溶剂,例如 MEK脱蜡操作或使用ZSM-22或ZSM-23等高选择性沸石的催化脱蜡。 可以控制初始催化脱蜡操作的严重性,以便实现异链烷烃含量的净增加,并且由于溶剂脱蜡步骤的选择性,可以保留这种增加的异链烷烃浓度,从而产生高VI的产物。 原料的倾点优选在初始催化脱蜡步骤期间降低至不低于产物的目标倾点的10°F,优选不低于20°F的值。 通常,这将导致在进料的倾点下降至少10°F,优选至少降低20°F。

    Process configuration for producing high viscosity lubricating oils
    32.
    发明授权
    Process configuration for producing high viscosity lubricating oils 失效
    生产高粘度润滑油的工艺配置

    公开(公告)号:US4913794A

    公开(公告)日:1990-04-03

    申请号:US379511

    申请日:1989-07-13

    IPC分类号: C10G27/12 C10G71/00

    CPC分类号: C10G71/00 C10G2400/10

    摘要: A process is disclosed for improving the Viscosity Index of a hydrocarbon lubricating oil comprising the steps of providing a flow reactor having separate first and second inlet ports for the separate co-injection of lubricating oil and an organic peroxide, charging said lubricating oil and said organic peroxide of said flow reactor through said first and second inlet ports respectively, controlling the relative flowrates of said lubricating oil and organic peroxide reactants together with the total volumetric flowrate through said flow reactor to maintain a flow regime which favors diffusional mixing between said organic peroxide and said lubricating oil, and maintaining said organic peroxide and said lubricating oil under conversion conditions including temperatures of between about 50.degree. and 300.degree. C. and pressure sufficient to maintain said lubricating oil and said organic peroxide substantially in the liquid phase. Controlling the flow regime to favor diffusional rather than convective mixing between the lubricating oil and the organic peroxide has surprisingly been found to markedly enhance Viscosity Index improvement.

    摘要翻译: 公开了一种用于改进烃类润滑油的粘度指数的方法,该方法包括以下步骤:提供具有单独的第一和第二入口的流动反应器,用于单独共同注入润滑油和有机过氧化物,将所述润滑油和所述有机物 所述流动反应器分别通过所述第一和第二入口过氧化物,控制所述润滑油和有机过氧化物反应物的相对流速以及通过所述流动反应器的总体积流量,以保持有利于所述有机过氧化物和 所述润滑油,并且在包括约50℃至300℃的温度的转化条件下保持所述有机过氧化物和所述润滑油以及足以使所述润滑油和所述有机过氧化物基本上处于液相的压力。 令人惊讶地发现控制流动状态以有利于润滑油和有机过氧化物之间的扩散而不是对流混合,显着提高了粘度指数的改善。

    Process for hydroisomerization and etherification of isoalkenes
    35.
    发明授权
    Process for hydroisomerization and etherification of isoalkenes 失效
    异烯烃加氢异构化和醚化的方法

    公开(公告)号:US5609654A

    公开(公告)日:1997-03-11

    申请号:US455746

    申请日:1995-05-31

    CPC分类号: C07C41/06

    摘要: A process for production of alkyl tertiary alkyl ethers in C.sub.4 + hydrocarbon streams rich in isoolefins, typically containing catalyst deactivating amounts of dienes and/or compounds containing heteroatoms. The process is especially advantageous in extending the cycle length for the zeolite catalyzed etherification of isoolefins in C.sub.4 + FCC gasoline by reducing catalyst aging. It has been discovered that if hydrogen is cofed with the alkanol and C.sub.4 + isoolefin rich feedstreams to an etherification reaction catalyzed by acidic zeolite wherein the zeolite has been impregnated with a noble metal the rate of catalyst aging or deactivation is substantially lowered. The process is especially effective, i.e., catalyst aging is particularly reduced, when hydrogen is cofed to an etherification reaction using acidic zeolite Beta catalyst containing palladium.

    摘要翻译: 在富含异烯烃的C4 +烃流中生产烷基叔烷基醚的方法,通常含有催化剂失活量的二烯和/或含杂原子的化合物。 该方法特别有利于通过降低催化剂老化来延长C4 + FCC汽油中异烯烃沸石催化醚化的循环长度。 已经发现,如果氢气与链烷醇和C 4 +异烯烃富集的原料流共沸到由酸性沸石催化的醚化反应,其中沸石已经用贵金属浸渍,则催化剂老化或失活的速率显着降低。 当使用含钯的酸性沸石β催化剂将氢气共沸至醚化反应时,该方法特别有效,即催化剂老化特别降低。

    Gasoline upgrading by aromatics amination
    36.
    发明授权
    Gasoline upgrading by aromatics amination 失效
    通过芳烃胺化提炼汽油

    公开(公告)号:US5284984A

    公开(公告)日:1994-02-08

    申请号:US998807

    申请日:1992-12-29

    摘要: A method for upgrading an aromatics-containing charge composition boiling in the gasoline boiling range comprises i) contacting the charge composition with a nitrating agent under nitrating conditions to form a product comprising nitrated aromatics; ii) hydrogenating a feed containing the product of i) under conditions sufficient to substantially reduce the nitro group of the nitrated aromatics so as to form a product comprising aromatic amines, water and heavy amines; and iii) removing the water and heavy amines from the product of step ii) to provide a gasoline boiling range product of an octane rating greater than the charge composition.

    摘要翻译: 一种用于升级汽油沸程沸腾的含芳烃的电荷组分的方法包括:i)在硝化条件下使电荷组合物与硝化剂接触以形成包含硝化芳族化合物的产物; ii)在足以基本上还原硝化芳族化合物的硝基的条件下氢化含有i)产物的进料,以形成包含芳族胺,水和重胺的产物; 和iii)从步骤ii)的产物中除去水和重胺,以提供辛烷值等于大于电荷组成的汽油沸程产物。

    Process for the hydration of olefins
    37.
    发明授权
    Process for the hydration of olefins 失效
    烯烃水合方法

    公开(公告)号:US5231233A

    公开(公告)日:1993-07-27

    申请号:US878278

    申请日:1992-05-04

    IPC分类号: C07C29/04 C07C41/05

    CPC分类号: C07C41/05 C07C29/04

    摘要: There is provided a process for converting light olefin to alcohol(s), ether(s) or mixtures of alcohol(s) and ether(s) which comprises contacting a feed containing at least one light olefin with water in the vapor and/or liquid phase under olefin hydration conditions in the presence of MCM-36 as olefin hydration catalyst to produce said alcohol(s) and/or ether(s).

    摘要翻译: 提供了将轻烯烃转化为醇,醚或醇和醚的混合物的方法,其包括使含有至少一种轻质烯烃的进料与蒸气中的水接触和/或 在作为烯烃水合催化剂的MCM-36存在下,在烯烃水合条件下制备所述醇和/或醚。

    Catalysts/process to synthesize alkylated naphthalene synthetic fluids
with increased alpha/beta isomers for improving product qualities
    38.
    发明授权
    Catalysts/process to synthesize alkylated naphthalene synthetic fluids with increased alpha/beta isomers for improving product qualities 失效
    合成具有增加的α/β异构体的烷基化萘合成流体的催化剂/方法,以改善产品质量

    公开(公告)号:US5177284A

    公开(公告)日:1993-01-05

    申请号:US705997

    申请日:1991-05-28

    摘要: This application discloses critical parameters, including process conditions and catalysts which effect the alpha:beta ratio of alkylated naphthalene isomers. The use of low alkylation temperatures and of low acidity zeolite catalysts (e.g. steamed USY and zeolite beta) lead to an increase in the alpha:beta ratio. The alkylated naphthalene fluids with higher alpha:beta ratio exhibited significantly enhanced product qualities, including thermal and oxidative stabilities.

    摘要翻译: 本申请公开了影响烷基化萘异构体的α:β比的关键参数,包括工艺条件和催化剂。 使用低烷基化温度和低酸度沸石催化剂(例如蒸煮的USY和沸石β)导致α:β比例的增加。 具有较高α:β比率的烷基化萘液显示出显着提高的产品质量,包括热和氧化稳定性。

    Catalytic olefin upgrading process using synthetic mesoporous
crystalline material
    39.
    发明授权
    Catalytic olefin upgrading process using synthetic mesoporous crystalline material 失效
    催化烯烃升级过程采用合成介孔结晶材料

    公开(公告)号:US5134242A

    公开(公告)日:1992-07-28

    申请号:US718884

    申请日:1991-06-21

    摘要: A process for upgrading aliphatic 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 new process is provied for catalytic oligomerization of lower olefin component in paraffin-containing mixed aliphatic feedstock which comprises contacting the 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 execellent conversion of lower olefins at pressure of about 100-13,000 pKa range and moderate space velocity. Oligomers of propene produced over MCM-41, when reacted under cracking/disproportionation conditions yield a propylene-rich mixture which is separated as a C.sub.3 stream, and C.sub.6 + isoalkenes are recovered 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升级含有低级烯烃的脂肪原料的方法。 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。 提出了一种新的方法,用于在含链烷烃的混合脂族原料中的低级烯烃组分的催化低聚,其包括在催化转化条件下使原料与具有基本上由均匀孔组成的六方蜂窝晶格结构的具有MCM-41结构的酸性金属硅酸盐固体催化剂 在约20至100埃的范围内。 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范围和适度的空间速度的压力下进行低级烯烃的非常好的转化。 在裂解/歧化条件下反应时,MCM-41产生的丙烯的低聚物产生作为C3流分离的富丙烯混合物,以良好的收率回收C6 +异烯烃。

    Stabilization of polyalpha-olefins
    40.
    发明授权
    Stabilization of polyalpha-olefins 失效
    聚α-烯烃的稳定化

    公开(公告)号:US5107049A

    公开(公告)日:1992-04-21

    申请号:US593171

    申请日:1990-10-05

    摘要: The thermal stability of poly alpha-olefin (PAO) lubricant basestocks are improved by reacting an aromatic compound with the alpha-olefin oligomer. The PAO materials are prepared by oligomerization of olefins such as 1-decene in the presence of a Lewis acid oligomerization catalyst. The resulting lubricant basestock product exhibits high viscosity, viscosity index and low pour point in addition to the unique enhancement in thermal stability. The reaction between the PAO and the aromatic is carried out in the presence of a solid, cyrstalline alkylation catalyst identified by a specific X-ray diffraction pattern. The preferred catalyst for this purpose is the material known as MCM-22.

    摘要翻译: 通过使芳族化合物与α-烯烃低聚物反应来改善聚α-烯烃(PAO)润滑剂基础油料的热稳定性。 在路易斯酸低聚催化剂存在下,通过烯烃如1-癸烯的低聚制备PAO材料。 除了独特的热稳定性提高之外,所得润滑剂基础油产品显示出高粘度,粘度指数和低倾点。 PAO和芳族化合物之间的反应是在特定X射线衍射图谱鉴定的固体,Cyrstalline烷基化催化剂的存在下进行的。 用于该目的的优选催化剂是称为MCM-22的材料。