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公开(公告)号：US5965783A
公开(公告)日：1999-10-12
申请号：US759771
申请日：1996-12-03
摘要： A process for producing a synthetic hydrocarbon product is provided comprising contacting under isomerization conditions an olefin feed comprising linear olefins with a catalyst comprising an intermediate pore size molecular sieve, wherein the catalyst is substantially free of Group VIII metals. The synthetic hydrocarbon product exhibits a low pour point and low toxicity to marine life.
摘要翻译： 提供一种生产合成烃产物的方法，包括在异构化条件下使包含线性烯烃的烯烃进料与包含中等孔径分子筛的催化剂接触，其中催化剂基本上不含VIII族金属。 合成烃产品具有低的倾点和对海洋生物的低毒性。
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公开(公告)号：US5933102A
公开(公告)日：1999-08-03
申请号：US935468
申请日：1997-09-24
申请人： Stephen J. Miller , Michael S. West
发明人： Stephen J. Miller , Michael S. West
IPC分类号： H03K17/96
CPC分类号： G06F3/044 , H03K17/962 , H03K17/9622 , H03K2017/9602
摘要： A touch sensor switch that responds to touching, or even to the proximity of an object, is disclosed. The switch includes a number of capacitance elements, or touch pads, that produce an effective capacitance dependent upon the physical proximity of the object. A microcontroller under control of a program stored in a read-only memory causes its I/O port to set a transient voltage on each capacitance element as a logic level. Each transient voltage is at variance with the capacitive element's preferred voltage level. The program then reads the I/O port, and hence the logic levels of the capacitance elements, as the capacitive elements revert to their preferred voltage levels, and calculates the proximity of the object, or touching, from relationships among recorded signals. The circuit may also be embodied in an application specific integrated circuit.
摘要翻译： 公开了一种触摸传感器开关，其响应于触摸或甚至对象的接近。 开关包括多个电容元件或触摸板，其产生取决于物体的物理接近度的有效电容。 在存储在只读存储器中的程序的控制下的微控制器使其I / O端口将每个电容元件上的瞬态电压设置为逻辑电平。 每个瞬态电压与电容元件的优选电压电平不一致。 然后，程序读取I / O端口，并因此读取电容元件的逻辑电平，因为电容元件恢复到其优选的电压电平，并根据记录的信号之间的关系计算对象或触摸的接近度。 电路也可以体现在专用集成电路中。
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公开(公告)号：US5741759A
公开(公告)日：1998-04-21
申请号：US716119
申请日：1996-09-19
CPC分类号： C09K8/26 , C09K8/34 , C09K8/36 , C10G45/64 , Y10S507/905
摘要： The present invention relates to synthetic hydrocarbons produced by skeletal isomerization, and the isomerization process. The products are especially useful as the continuous phase of a drilling fluid, for example when prepared from C.sub.14 to C.sub.18 linear alpha-olefins via isomerization or hydroisomerization, and as lube oils. The present invention also relates to a process for producing synthetic hydrocarbons by skeletally isomerizing C.sub.12+ olefins over a catalyst comprising an intermediate pore size molecular sieve, with or without Group VIII metals under skeletal isomerization conditions which result in little, preferably in substantially no, olefin cracking or oligomerization.
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94.发明授权Method for controlling multistage aromatization process to give high aromatic barrel per calendar day throughput 失效用于控制多级芳构化方法以使日历日产量高的芳香桶的方法
公开(公告)号：US5407558A
公开(公告)日：1995-04-18
申请号：US734265
申请日：1991-07-22
摘要： A method is provided of selecting operating parameters for an aromatization process having at least penultimate and final stages, each containing a respective catalyst, for optimum aromatic barrel per calendar day (AB/CD) production of product having a selected RON and/or over a particular run length. The catalyst lives are determined at constant LHSV for the penultimate and final stage catalysts for a given feed RON to each stage as a function of the change in RON from that of the feed to that of the C.sub.5+ effluent from the respective stage. The penultimate stage C.sub.5+ effluent RON is selected to be such that the lives of the catalysts in each stage are substantially equal. Preferably the yield of C.sub.5+ effluent from each stage and the life of the catalyst used in each stage is determined as a function of the pressure of that stage. The operating pressures of the stages are then selected to be within about 30% of that which gives the highest AB/CD.
摘要翻译： 提供了一种方法，其选择具有至少倒数第二和最后阶段的芳构化方法的操作参数，每个步骤包含相应的催化剂，用于每个日历日（AB / CD）产生具有选定RON和/或 特定跑步长度。 对于给定进料RON到每个阶段的倒数第二阶段催化剂和最终阶段催化剂，催化剂寿命作为从进料的RON变化到来自各个阶段的C5 +流出物的RON变化的函数来确定。 选择倒数第二级C5 +流出物RON使得每个阶段的催化剂的寿命基本相等。 优选地，每个阶段的C5 +流出物的产率和每个阶段中使用的催化剂的寿命作为该阶段的压力的函数来确定。 然后将级的操作压力选择为提供最高AB / CD的操作压力的约30％。
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公开(公告)号：US5246566A
公开(公告)日：1993-09-21
申请号：US905713
申请日：1992-06-29
申请人： Stephen J. Miller
发明人： Stephen J. Miller
CPC分类号： B01J29/064 , B01J29/7284 , B01J29/7292 , B01J29/7484 , B01J29/7492 , B01J29/85 , C10G2400/10
摘要： The present invention relates to a process for producing a lube oil having a low pour point and excellent viscosity and viscosity index comprising isomerizing a waxy feed over a catalyst comprising a molecular sieve having generally oval 1-D pores having a minor axis between about 4.2 .ANG. and about 4.8 .ANG. and a major axis between about 5.4 .ANG. and about 7.0 .ANG. and at least one group VIII metal. SAPO-11, SAPO-31, SAPO-41, ZSM-22, ZSM-23 and ZSM-35 are examples of useful catalysts.
摘要翻译： 本发明涉及一种制备具有低倾点和优异的粘度和粘度指数的润滑油的方法，其包括将蜡质原料异构化在包含分子筛的催化剂上，所述分子筛具有通常为椭圆形的1-D孔隙，所述分子筛具有约4.2N 约4.8 ANGSTROM，大约5.4 ANGSTROM和约7.0 ANGSTROM和至少一个VIII族金属之间的长轴。 SAPO-11，SAPO-31，SAPO-41，ZSM-22，ZSM-23和ZSM-35是有用的催化剂的实例。
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公开(公告)号：US5182012A
公开(公告)日：1993-01-26
申请号：US678678
申请日：1991-04-01
IPC分类号： B01J29/035 , C10G35/095
CPC分类号： B01J29/035 , C10G35/095
摘要： The preferred reforming and/or benzene production catalyst is an intermediate pore size zeolite which has a high degree of crystallinity and a small crystallite size. The reforming or benzene production process using the catalyst is preferably run without added hydrogen, and at low pressures and temperatures.
摘要翻译： 优选的重整和/或苯生产催化剂是具有高结晶度和小晶粒尺寸的中孔孔径沸石。 使用催化剂的重整或苯生产方法优选在不添加氢气的情况下运行，并且在低压和低温下进行。
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公开(公告)号：US5158665A
公开(公告)日：1992-10-27
申请号：US733590
申请日：1991-07-22
申请人： Stephen J. Miller
发明人： Stephen J. Miller
摘要： A method is disclosed for preparing a silicoaluminophosphate molecular sieve, characterized in that the P.sub.2 O.sub.5 to alumina mole ratio at the surface is about 0.85 or less, the P.sub.2 O.sub.5 to aluminia mole ratio of the bulk is 0.94 or greater and the silicon content at the surface is greater than that of the bulk, from a reaction mixture containing particles less than 80 microns in diameter.
摘要翻译： 公开了一种制备硅铝磷酸盐分子筛的方法，其特征在于表面处的P 2 O 5与氧化铝摩尔比为约0.85或更小，本体的P2O5与氧化铝摩尔比为0.94或更大，并且表面的硅含量为 大于体积的反应混合物，其直径小于80微米的反应混合物。
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98.发明授权Staged catalyst reforming to produce optimum octane barrel per calendar day reformate production 失效分阶段催化剂改造生产最佳的OCTANE BARREL每日历改造生产
公开(公告)号：US5073250A
公开(公告)日：1991-12-17
申请号：US488333
申请日：1990-03-02
IPC分类号： C10G59/02
CPC分类号： C10G59/02
摘要： A naphtha feed is contacted in a penultimate reforming stage under catalytic reforming conditions with a first catalyst. The effluent from the penultimate reforming stage is contacted in a final reforming stage under catalytic reforming conditions and at substantially the same pressure as is maintained in the penultimate reforming stage with a second catalyst. The reforming pressure is selected to provide optimal OB/CD production of product reformate of a desired RON from the final stage.
摘要翻译： 在催化重整条件下，在第二催化剂的倒数第二重整阶段，使石脑油进料接触。 倒数第二重整阶段的流出物在最终重整阶段在催化重整条件下和与第二催化剂在倒数第二重整阶段保持的基本相同的压力下接触。 选择重整压力以从最终阶段提供期望RON的产物重整产物的最佳OB / CD生产。
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公开(公告)号：US4921594A
公开(公告)日：1990-05-01
申请号：US86118
申请日：1987-08-17
申请人： Stephen J. Miller
发明人： Stephen J. Miller
IPC分类号： C10G45/62 , B01J29/85 , C10G20060101 , C10G45/64 , C10G47/00 , C10G49/02 , C10G65/12 , C10M177/00
摘要： Lubricating oils are prepared by a process whereby a hydrocarbonaceous feedstock is hydrocracked and subsequently dewaxed over a crystalline silicoaluminophosphate SAPO-11 containing platinum and/or palladium.
摘要翻译： 润滑油通过一种方法制备，其中烃类原料被加氢裂化，随后在包含铂和/或钯的结晶硅铝磷酸SAPO-11上脱蜡。
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公开(公告)号：US4795546A
公开(公告)日：1989-01-03
申请号：US78614
申请日：1987-07-28
申请人： Stephen J. Miller
发明人： Stephen J. Miller
CPC分类号： C10G29/205 , C10G29/20 , C10G69/02 , C10G69/04
摘要： A process for improving the storage stability of hydrocracked neutral oil lubricating oil stocks comprising a dewaxing step utilizing a high silica zeolite catalyst to produce a dewaxer effluent and two stabilizing steps utilizing hydrofinishing and nonhydrogenative stabilization by an acidic catalyst.
摘要翻译： 一种提高加氢裂化中性油润滑油料储存稳定性的方法，其包括使用高二氧化硅沸石催化剂的脱蜡步骤以产生脱蜡剂流出物，以及利用通过酸性催化剂进行加氢精制和非氢化稳定化的两个稳定步骤。
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