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1.发明公开Process for cracking a hydrocarbon feedstock to obtain gasoline and olefins and upgrading the olefins to improve the total gasoline yield 失效一种用于烃原料生产汽油和烯烃裂解过程，和烯烃的处理，以改善总汽油产率。
公开(公告)号：EP0311375A1
公开(公告)日：1989-04-12
申请号：EP88309278.5
申请日：1988-10-05
发明人： Child, Jonathan Edward , Schipper, Paul Herbert , Sapre, Ajit Vishwanath , Kushnerick, John Douglas
摘要： Improved processes are disclosed for increasing gasoline yield from a gas oil at a constant riser top temperature by introducing a quench fluid, such as liquid water, butane, or lighter hydrocarbons or an alcohol or ether into a riser downstream of the site where the gas oil and/or catalyst are injected. In another embodiment of the invention the introduction of quench fluid, acting as a heat sink, can be used to increase octane number while avoiding significant formation of wet gas as is observed when higher octane number is achieved by generally increasing the overall riser temperature. This invention further provides an integrated process wherein the C 4 - product from an FCC riser unit which is limited to a predetermined top temperature maintained by injecting a quench fluid intermediate the inlet and outlet of the FCC riser is combined and contacted with a zeolite catalyst in a turbulent fluid bed under conditions of severity to upgrade the light olefin-containing gas to heavier hydrocarbons, especially gasoline.
摘要翻译： 改进的处理盘游离缺失用于通过引入骤冷流体，颜色以恒定的提升管顶部温度从气体油增加汽油产率：诸如液态水，丁烷或更轻的烃或为醇或醚进入位点下游的立管，其中瓦斯油 和/或催化剂被注入。 在本发明的引入骤冷流体的另一实施例，作为一个散热片，可用于增加辛烷值，同时避免如观察-当更高辛烷值通过基因拉力增加整体提升管温度来实现湿气体的显著形成。 本发明还提供集成的过程，以从在FCC提升管单元所有worin的C4产物它被限制为通过注入骤冷流体的中间入口和FCC提升管的出口维持一个顶预定温度为合并，并用在所涉及的沸石催化剂接触 严重程度的含轻烯烃的气体升级到更重的烃的条件下，湍流流化床，爱特别是汽油。
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2.发明公开Catalytic cracking process using cross-flow regenerator 失效Katalytisches Krackverfahren mit einem Querstrom-Regenerator。
公开(公告)号：EP0427451A1
公开(公告)日：1991-05-15
申请号：EP90311943.6
申请日：1990-10-31
CPC分类号： B01J8/0015 , C10G11/182
摘要： An improved process and apparatus are disclosed for fluidized bed catalyst regeneration in a cross-flow type regenerator. A baffled coked catalyst inlet located within the dense bed of catalyst disperses and distributes coked catalyst flow in a direction generally normal to the direction of flow in the catalyst inlet. The baffle significantly reduces the stagnant regions in the bed.
摘要翻译： 公开了一种用于横流式再生器中的流化床催化剂再生的改进方法和装置。 位于催化剂密实床内的带挡板的焦化催化剂入口分散并在大致垂直于催化剂入口流动方向的方向上分配焦化催化剂流。 挡板显着减少了床上的停滞区域。
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公开(公告)号：EP0088494A1
公开(公告)日：1983-09-14
申请号：EP83300359.3
申请日：1983-01-25
CPC分类号： C07C1/20 , C07C2529/06 , Y02P20/52 , Y02P20/582 , Y02P30/42 , C07C11/02
摘要： In the conversion of methanol into ethylene, methanol is catalytically dehydrated and the ether product is converted into olefins at predetermined conversion over a zeolite catalyst. The zeolite catalyst is arranged as a plurality of beds with alternate cooling zones. The temperature rise in each bed is .not greater than the methanol to ethylene sensitivity parameter and each cooling zone reduces the temperature by the same amount. The total number of beds is at least equal to the ratio of total adiabatic temperature increase at the predetermined conversion to the sensitivity parameter.
摘要翻译： 在将甲醇转化为乙烯时，甲醇被催化脱水，醚产物在沸石催化剂上以预定的转化率转化为烯烃。 沸石催化剂被布置为具有交替冷却区的多个床。 每个床中的温度升高不大于甲醇对乙烯敏感性参数，每个冷却区将温度降低相同的量。 床的总数至少等于预定转换时的绝热温度增加与灵敏度参数之比。
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4.发明公开Catalytic cracking process and apparatus with improved catalyst flow in swirl regenerators 失效用于与在Wirbelregenerator改进的流动催化裂化方法和设备。
公开(公告)号：EP0427450A1
公开(公告)日：1991-05-15
申请号：EP90311942.8
申请日：1990-10-31
CPC分类号： B01J8/0015 , C10G11/182 , Y10S502/515
摘要： An improved process and apparatus are disclosed for fluidized catalytic cracking of hydrocarbons using a swirl type catalyst regenerator. Multiple, symmetrically spaced spent catalyst inlets are provided for addition of coked catalyst to the regenerator. Preferably, a single catalyst outlet, for withdrawal of regenerated catalyst, is provided in the center of the regenerator. Use of multiple symmetrical inlets and a central catalyst outlet greatly reduce stagnant regions in the bed.
摘要翻译： 一种改进的方法和装置，光盘为游离缺失使用旋流型催化剂再生器的烃的流化催化裂化。 提供了另外的焦化催化剂的再生器多，对称间隔废催化剂入口。 优选地，单个催化剂出口，用于再生的催化剂的撤出，是在再生器的中心设置。 多个对称的进气口和使用中央出口催化剂大大减少在床上停滞区域。
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公开(公告)号：EP0088495B1
公开(公告)日：1985-09-11
申请号：EP83300360.1
申请日：1983-01-25
CPC分类号： C07C1/20 , C07C2529/06 , Y02P20/52 , Y02P30/42 , C07C11/04
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6.发明公开
公开(公告)号：EP0889016A1
公开(公告)日：1999-01-07
申请号：EP98305188.9
申请日：1998-06-30
发明人： Motoyuki, Masahiro, Osaka Branch Kobe Steel Ltd. , Yamamoto, Koji, Kobe Corp.Res.Lab. Kobe Steel Ltd. , Sapre, Ajit Vishwanath , McWilliams, John Paul
CPC分类号： C07C15/24 , C07C2/66 , C07C6/126 , C07C2529/70
摘要： 2,6-Dialkylnaphthalene is prepared from a feedstock comprising naphthalene and an alkylating agent, by a process comprising the steps:
(I) transalkylating isomers of dialkylnaphthalene and naphthalene to produce monoalkylnaphthalene and isomers of dialkylnaphthalene;
(II) separating the product obtained in step (I) into naphthalene, monoalkylnaphthalene, dialkylnaphthalene and other components;
(III) alkylating the monoalkylnaphthalene fraction from step (II) with an alkylating agent to produce dialkylnaphthalene; and
(IV) separating 2,6-dialkylnaphthalene from the dialkylnaphthalene fraction in step (II),
wherein at least step (I) or step (III) is conducted in the presence of a catalyst having a composition comprising a synthetic zeolite having an X-ray diffraction pattern with an interplanar d-spacing (Å) 12.36 ± 0.4 11.03 ± 0.2 8.83 ± 0.14 6.18 ± 0.12 6.00 ± 0.10 4.06 ± 0.07 3.91 ± 0.07 3.42 ± 0.06.摘要翻译： 2,6-二烷基萘由包含萘和烷基化剂的原料通过包括以下步骤的方法制备：（I）将二烷基萘和萘的异构体转烷基化以产生单烷基萘和二烷基萘的异构体; （II）将步骤（I）中获得的产物分离成萘，单烷基萘，二烷基萘等组分; （III）用烷基化剂将步骤（II）中的单烷基萘馏分烷基化以制备二烷基萘; 和（IV）在步骤（II）中从二烷基萘馏分中分离2,6-二烷基萘，其中至少步骤（I）或步骤（III）在具有包含具有X 具有晶面d间距的阵列衍射图（ANGSTROM）
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公开(公告)号：EP0088494B1
公开(公告)日：1985-05-02
申请号：EP83300359.3
申请日：1983-01-25
CPC分类号： C07C1/20 , C07C2529/06 , Y02P20/52 , Y02P20/582 , Y02P30/42 , C07C11/02
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公开(公告)号：EP0088495A1
公开(公告)日：1983-09-14
申请号：EP83300360.1
申请日：1983-01-25
CPC分类号： C07C1/20 , C07C2529/06 , Y02P20/52 , Y02P30/42 , C07C11/04
摘要： Stable thermal operation of the conversion of a lower aliphatic alcohol alone or as a mixture with its corresponding ether is achieved in a cooled tubular reactor having a diameter and a length which will maintain the ratio of the rate of change or heat generation within the reactor with respect to temperature to the rate of change of heat removal by cooling with respect to temperature at a value not greater than unity.
摘要翻译： 在具有直径和长度的冷却管式反应器中实现单独的或与其相应的醚的混合物的低级脂族醇的转化的稳定的热操作，其将保持反应器内的变化率或发热率与反应器中的比例 通过相对于不大于1的值的温度进行冷却来解决温度对散热变化率的影响。
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