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    • 1. 发明申请
    • PROCESS FOR PREPARING ALKYL ETHERS AND MIXTURES THEREOF
    • 制备烷基醚及其混合物的方法
    • WO1997023438A1
    • 1997-07-03
    • PCT/FI1996000678
    • 1996-12-19
    • NESTE OYTAMMINEN, EsaLINDQVIST, Petri
    • NESTE OY
    • C07C43/04
    • C07C41/42B01D3/009C07C41/06C10L1/023Y02P20/127C07C43/046
    • The invention relates to a process for preparing tertiary alkyl ethers, in particular MTBE, ETBE or mixtures of these ethers with heavier ethers. According to the process the feedstock containing hydrocarbons is fed to a catalytic distillation reactor system, in which the isoolefines, in particular the C4 to C7 isoolefines, of the feed are reacted with an alkanol in the presence of a cation exchange resin in order to produce tertiary alkyl ether products. The reaction product containing the ethers is removed from the distillation system as the bottoms product and, if necessary, it is subjected to an additional treatment for producing a gasoline component. The unreacted alkanol is removed as the overhead product of the distillation. According to the invention, the distillate withdrawn mainly contains an azeotrope of C3 hydrocarbons and alkanol, the C3 amount of which at least approximately corresponds to the C3 hydrocarbon concentration of the hydrocarbon feed, a substantial amount of the unreacted alkanol being removed in the form of said azeotrope. By means of the invention the need for a separate alkanol washing unit is eliminated in the apparatus which considerably reduces apparatus investment costs.
    • 本发明涉及一种制备叔烷基醚,特别是MTBE,ETBE或这些醚与较重醚的混合物的方法。 根据该方法,将含有烃的原料进料到催化蒸馏反应器系统中,其中进料的异烯烃,特别是C4至C7异烯烃在阳离子交换树脂的存在下与烷醇反应,以产生 叔烷基醚产物。 含有醚的反应产物作为塔底产物从蒸馏系统中除去,如果需要,将其进行额外处理以生产汽油组分。 将未反应的链烷醇作为蒸馏塔顶产物除去。 根据本发明,取出的馏出物主要含有C 3烃和链烷醇的共沸物,其C3量至少大约对应于烃进料的C 3烃浓度,大量未反应的链烷醇以 说共沸物。 通过本发明,在装置中消除了对单独的烷醇洗涤单元的需求,这大大降低了设备的投资成本。
    • 2. 发明申请
    • PROCESS FOR PREPARING METHYL ETHERS
    • 制备甲基醚的方法
    • WO1993019032A1
    • 1993-09-30
    • PCT/FI1993000098
    • 1993-03-18
    • NESTE OYTAMMINEN, EsaAITTAMAA, JuhaniJAKKULA, Juha
    • NESTE OY
    • C07C41/06
    • B01D3/009C07C41/06C07C41/42Y02P20/127C07C43/046
    • The invention relates to a process for preparing tertiary methyl ethers. According to the process the feedstock containing hydrocarbons is fed to a catalytic distillation reactor system, in which the isoolefines, in particular the C4 to C7 isoolefines, of the feed are reacted with methanol in the presence of a cation exchange resin in order to produce tertiary methyl ether products. The reaction product containing the ethers is removed from the distillation system as the bottoms product and, if necessary, it is subjected to an additional treatment for producing a gasoline component. The unreacted methanol is removed as the overhead product of the distillation. According to the invention, the distillate withdrawn mainly contains an azeotrope of C4 hydrocarbons and methanol, the C4 amount of which at least approximately corresponds to the C4 hydrocarbon concentration of the hydrocarbon feed, a substantial amount of the unreacted methanol being removed in the form of said azeotrope. By means of the invention the need for a separate methanol washing unit is eliminated in the apparatus which considerably diminishes apparatus investment costs.
    • 本发明涉及一种制备叔甲基醚的方法。 根据该方法,将含有烃的原料进料到催化蒸馏反应器系统中,其中进料的异烯烃,特别是C4至C7异烯烃在阳离子交换树脂的存在下与甲醇反应,以产生叔 甲醚产品。 含有醚的反应产物作为塔底产物从蒸馏系统中除去,如果需要,将其进行额外处理以生产汽油组分。 作为蒸馏塔顶产物除去未反应的甲醇。 根据本发明,取出的馏出物主要含有C 4烃和甲醇的共沸物,其C4量至少大约对应于烃进料的C4烃浓度,大量未反应的甲醇以 说共沸物。 通过本发明,在装置中消除了对单独的甲醇洗涤单元的需求,这显着地减少了设备投资成本。
    • 3. 发明申请
    • PROCESS AND APPARATUS FOR PREPARING TERTIARY ALKYL ETHERS
    • 制备碱性烷基醚的方法和装置
    • WO1993019031A1
    • 1993-09-30
    • PCT/FI1993000097
    • 1993-03-18
    • NESTE OYAITTAMAA, JuhaniEILOS, IstoJAKKULA, JuhaLINDQVIST, Petri
    • NESTE OY
    • C07C41/06
    • C07C41/42B01D3/009C07C41/06Y02P20/127Y10S203/06Y10S203/17Y10S203/20C07C43/046
    • The invention concerns a process and an apparatus for preparing tertiary ethers. According to the process, C4 to C6 isoolefins and possibly heavier olefins contained in the feedstock are reacted with lower aliphatic alcohols, in particular methanol or ethanol, in a catalytic distillation reactor system in order to produce the corresponding ethers. According to the invention, the reaction between the isoolefins and the alcohols is essentially carried out in at least one reactor (5-7) of the kind, which is combined with a distillation column (3) intended for product separation, by conducting at least a part of the liquid flow of the column through the reactor and returning it to a lower tray than the one from which it was taken. At least half of cation exchange resin is placed in the side reactor (5-7). In the process according to the invention, the catalyst can be rapidly changed without stopping the process. In order to improve conversion additional alcohol can be fed to at least one of the side reactors.
    • 本发明涉及一种制备叔醚的方法和装置。 根据该方法,原料中所含的C4至C6异烯烃和可能较重的烯烃在催化蒸馏反应器系统中与低级脂族醇,特别是甲醇或乙醇反应,以产生相应的醚。 根据本发明,异烯烃和醇之间的反应基本上在至少一个与用于产物分离的蒸馏塔(3)组合的反应器(5-7)中进行,至少通过至少 柱的液体流的一部分通过反应器并将其返回到比从其取出的塔的下部托盘。 将至少一半的阳离子交换树脂置于侧反应器(5-7)中。 在根据本发明的方法中,可以快速改变催化剂而不停止该方法。 为了改善转化率,另外的醇可以进料至至少一个侧反应器。
    • 4. 发明申请
    • PROCESS FOR PREPARING ALKYL ETHERS AND MIXTURES THEREOF
    • 制备烷基醚及其混合物的方法
    • WO1997030960A1
    • 1997-08-28
    • PCT/FI1997000120
    • 1997-02-21
    • NESTE OYKOSKINEN, MattiLINDQVIST, PetriJÄRVELIN, HarriAITTAMAA, Juhani
    • NESTE OY
    • C07C41/06
    • C07C41/42C07C41/06C07C43/046
    • The invention concerns a process for preparing a tertiary alkyl ether product. The process comprises reacting the isoolefins of an olefinic hydrocarbon feedstock in a reaction zone (1 - 3) with an alkanol to form a reaction mixture, which is subjected to distillation in a first distillation zone (4). The bottoms product of the first distillation contains the ether(s), whereas the overhead stream contains unreacted alkanol and a mixture of light hydrocarbons. The overhead stream is subjected to a second distillation in a second distillation zone (15). The overhead product of the second distillation mainly contains the lightest hydrocarbons and a small amount of alkanol, and the bottoms product contains an essentially oxygenate-free hydrocarbon stream which can be used as such for alkylation. In order to increase the conversion of the process, a side drawoff is withdrawn from the second distillation zone (15) and recirculated to the reaction zone (1 - 3).
    • 本发明涉及一种制备叔烷基醚产物的方法。 该方法包括使反应区(1-3)中的烯烃原料的异烯烃与烷醇反应以形成反应混合物,其在第一蒸馏区(4)中进行蒸馏。 第一次蒸馏的塔底产物含有醚,而顶部物流含有未反应的链烷醇和轻烃的混合物。 塔顶流在第二蒸馏区(15)中进行第二次蒸馏。 第二次蒸馏的塔顶产物主要含有最轻的烃和少量的链烷醇,底部产物含有基本上不含氧的烃流,可用于烷基化。 为了增加该方法的转化率,从第二蒸馏区(15)中取出侧抽出物并再循环至反应区(1-3)。
    • 5. 发明申请
    • PROCESS FOR PREPARING TERTIARY ALKYL ETHERS
    • 制备仲胺醇的方法
    • WO1997023437A1
    • 1997-07-03
    • PCT/FI1996000677
    • 1996-12-19
    • NESTE OYLINDQVIST, Petri
    • NESTE OY
    • C07C43/04
    • C07C41/06C07C41/42C07C43/046
    • A process for preparing tertiary alkyl ethers comprises the steps of reacting C4-7 isoolefins of an olefinic hydrocarbon feedstock with an alkanol in the presence of a first catalyst in a reaction zone to form a reaction mixture containing a tertiary alkyl ether or a mixture of tertiary alkyl ethers, feeding the reaction mixture to a distillation column, distilling the reaction mixture and recovering the alkyl ether(s) with the bottoms product of the distillation. An azeotrope formed by unreacted C4 hydrocarbons and the alkanol is withdrawn as an overhead product of the distillation. According to the invention, a part of the liquid flow of the column is withdrawn to form a side drawoff, and the side drawoff is recirculated to the reaction zone. As a result, the conversion of the reactive C6 hydrocarbons is increased and the operating cost of the ethers process is reduced.
    • 制备叔烷基醚的方法包括以下步骤:在反应区中,在第一催化剂存在下使烯烃原料的C 4-7异烯烃与链烷醇反应,形成含有叔烷基醚或叔烷基醚的混合物的反应混合物 将反应混合物进料到蒸馏塔中,蒸馏反应混合物并用蒸馏塔底产物回收烷基醚。 由未反应的C 4烃和链烷醇形成的共沸物作为蒸馏塔顶馏出物排出。 根据本发明,塔的液体流的一部分被抽出以形成侧抽屉,并且侧抽屉被再循环到反应区。 结果,反应性C6烃的转化率增加,并且醚过程的操作成本降低。
    • 8. 发明申请
    • ADDITIVES USABLE IN PREPARATION OF ALKENYL SUCCINIC ANHYDRIDE
    • 添加剂可用于制备烷基苯甲酸酐
    • WO1997023474A1
    • 1997-07-03
    • PCT/FI1996000657
    • 1996-12-12
    • NESTE OYMÄKIPEURA, PetriKAPANEN, MikaTULISALO, JukkaKOSKIMIES, Salme
    • NESTE OY
    • C07D307/60
    • C07C51/567C07C57/13
    • In the preparation of alkenyl succinic anhydride (ASA) from an olefinically unsaturated hydrocarbon and a maleic anhydride, additives are used in the preparation reaction in order to improve the yield of the product and to reduce side reactions. According to the present invention, quinone and hydroquinone derivatives as well as dialkyl sulfoxides and transition-metal acetylacetonate have such properties. The amounts to be added are approx. 0.01-2 mol % of the amount of maleic anhydride. The olefin is preferably a straight-chain alpha -olefin or a straight-chain or branched internal olefin having a chain length of 6-20 carbon atoms. The olefin may also be a polyolefin, in which case the preferred molecular weight is 900-1500. The preparation process may be of the batch type or the semi-batch type, and the maleic anhydride and the additive may be added in several batches or as a continuous feed which may be even or variable. The ASA obtained by the process may be used in particular as an additive in foods, for hydroxy sizing of paper, or as a dispersing agent in lubricants.
    • 在由烯属不饱和烃和马来酸酐制备链烯基琥珀酸酐(ASA)时,在制备反应中使用添加剂以提高产物的产率并减少副反应。 根据本发明,醌和氢醌衍生物以及二烷基亚砜和过渡金属乙酰丙酮化物具有这样的性质。 添加量约为。 0.01-2摩尔%的马来酸酐。 烯烃优选为直链α-烯烃或链长为6-20个碳原子的直链或支链内烯烃。 烯烃也可以是聚烯烃,在这种情况下,优选的分子量为900-1500。 制备方法可以是间歇式或半批式,并且马来酸酐和添加剂可以分批加入或作为可以均匀或可变的连续进料。 通过该方法获得的ASA可特别用作食品中的添加剂,用于纸张的羟基上浆或作为润滑剂中的分散剂。
    • 9. 发明申请
    • PROCESS FOR PREPARATION OF POLY-N-BUTENES HAVING HIGH VISCOSITY
    • 制备具有高粘度的聚N-丁烯的方法
    • WO1996026913A1
    • 1996-09-06
    • PCT/FI1995000106
    • 1995-02-27
    • NESTE OYKAPANEN, MikaHALME ErkkiKOSKIMIES Salme
    • NESTE OY
    • C07C02/20
    • C07C2/04C07C2527/1213C07C2531/02C07C2531/04
    • The application relates to a process for the oligomerization of olefins, preferably a hydrocarbon blend which contains 1-butenes and/or 2-butenes, for example the so-called Raffinate II stream and cyclic aromatic or alicyclic hydrocarbons, by means of BF3 and a cocatalyst. The aromatic hydrocarbon may preferably be styrene, alpha-methyl styrene, alkyl styrene, or a blend thereof, and the alicyclic hydrocarbon may be vinyl cyclohexane, vinyl cyclohexene, or a blend thereof. The cocatalyst is an aliphatic alcohol, carboxylic acid or inorganic acid. The oligomerization may be carried out with or without a medium, at a temperature above 0 DEG C, by adjusting the pressure to 1-10 bar by means of BF3 gas. The oligomer prepared by the process may be used as a solvent or an additive in fuels or lubricants, in surfactants, in white and cosmetic oils requiring extra purity, and in PVC and polyolefin plastics. In polyester and vinyl ester resins this oligomer can be used for replacing in part the monomer (e.g. styrene), thus reducing monomer evaporation and to inhibit shrinkage at the hardening stage, and it also improves the optical properties of the said resins.
    • 本申请涉及烯烃低聚的方法,优选含有1-丁烯和/或2-丁烯的烃共混物,例如所谓的残液II类和环状芳族或脂环族烃,通过BF 3和 助催化剂。 芳族烃可以优选为苯乙烯,α-甲基苯乙烯,烷基苯乙烯或其共混物,脂环族烃可以是乙烯基环己烷,乙烯基环己烯或其共混物。 助催化剂是脂族醇,羧酸或无机酸。 通过用BF 3气调节压力至1-10巴,可以在高于0℃的温度下使用或不用介质进行低聚。 通过该方法制备的低聚物可以用作燃料或润滑剂,表面活性剂,需要额外纯度的白色和化妆油以及PVC和聚烯烃塑料中的溶剂或添加剂。 在聚酯和乙烯基酯树脂中,该低聚物可用于部分单体(例如苯乙烯)的替代,从而减少单体蒸发并抑制硬化阶段的收缩,并且还改善了所述树脂的光学性能。