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1. 发明授权

US5510016A Gasoline upgrading process 失效
标题翻译：汽油升级过程
公开(公告)号：US5510016A
公开(公告)日：1996-04-23
申请号：US303909
申请日：1994-09-09
申请人： Timothy T. Hilbert , Dominick N. Mazzone , Michael S. Sarli
发明人： Timothy T. Hilbert , Dominick N. Mazzone , Michael S. Sarli
IPC分类号： B01J29/40 , C10G35/04 , C10G35/095 , C10G45/08 , C10G53/16 , C10G67/00 , C10G67/16 , C10G69/08 , C10G69/02
CPC分类号： C10G53/16 , C10G35/095 , C10G67/00 , C10G67/16 , C10G69/08 , C10G2300/70
摘要： A process for catalytically desulfurizing cracked fractions in the gasoline boiling range to acceptable sulfur levels uses an initial hydrotreating step to desulfurize the feed with some reduction in octane number, after which the desulfurized material is treated with a self-bound or binder-free zeolite to restore lost octane. The process may be utilized to desulfurize catalytically and thermally cracked naphthas such as FCC naphtha as well as pyrolysis gasoline and coker naphthas, while maintaining octane so as to reduce the requirement for reformate and alkylate in the gasoline blend. The self-bound catalyst offers advantages in activity and permits the process to be carried out at lower temperatures.
摘要翻译：将汽油沸点范围内的裂化馏分催化脱硫至可接受的硫水平的方法使用初始加氢处理步骤以一定量的辛烷值对进料进行脱硫，之后将脱硫物质用自结合或无粘合剂的沸石处理恢复失去的辛烷值。该方法可用于脱硫催化和热裂解石脑油如FCC石脑油以及热解汽油和焦化石脑油，同时保持辛烷值，以减少对汽油混合物中重整产物和烷基化物的需求。自限催化剂具有活性优点，并允许该方法在较低温度下进行。

2. 发明授权

US07902103B2 Structured bodies with siliceous binder 有权
标题翻译：具有硅质粘结剂的结构体
公开(公告)号：US07902103B2
公开(公告)日：2011-03-08
申请号：US12459307
申请日：2009-06-30
申请人： Jean W. Beeckman , Glenn R. Sweeten , Arthur W. Chester , John P. McWilliams , Dominick N. Mazzone
发明人： Jean W. Beeckman , Glenn R. Sweeten , Arthur W. Chester , John P. McWilliams , Dominick N. Mazzone
IPC分类号： B01J29/06 , B01J31/00
CPC分类号： B01J37/0018 , B01J20/183 , B01J29/041 , B01J29/084 , B01J29/40 , B01J29/65 , B01J37/0009 , B01J2229/42 , C04B35/18 , C04B38/0022 , C04B2111/00793 , C08L83/04 , C10G45/04 , C10G49/02 , C04B38/0006 , C04B38/0054 , C08L2666/54 , C08L2666/58
摘要： The invention relates to the use of particulate silicone resins in the absence of added organic solvents with particulate inorganic materials to form structured bodies and in particular molecular sieve containing structured bodies. The silicone resin is used in the form of a particulate with an average particle size of less than 700 um. Upon calcining, the silicone resin is converted to silica which acts as a binder.
摘要翻译：本发明涉及在没有添加的有机溶剂与颗粒状无机材料形成结构体的情况下使用颗粒状有机硅树脂，特别是分子筛含结构体的用途。有机硅树脂以平均粒径小于700μm的颗粒形式使用。煅烧后，将有机硅树脂转化为二氧化硅作为粘合剂。

3. 发明申请

US20090270246A1 Structured bodies with siliceous binder 有权
公开(公告)号：US20090270246A1
公开(公告)日：2009-10-29
申请号：US12459307
申请日：2009-06-30
申请人： Jean W. Beeckman , Glenn R. Sweeten , Arthur W. Chester , John P. McWilliams , Dominick N. Mazzone
发明人： Jean W. Beeckman , Glenn R. Sweeten , Arthur W. Chester , John P. McWilliams , Dominick N. Mazzone
IPC分类号： B01J29/04
CPC分类号： B01J37/0018 , B01J20/183 , B01J29/041 , B01J29/084 , B01J29/40 , B01J29/65 , B01J37/0009 , B01J2229/42 , C04B35/18 , C04B38/0022 , C04B2111/00793 , C08L83/04 , C10G45/04 , C10G49/02 , C04B38/0006 , C04B38/0054 , C08L2666/54 , C08L2666/58
摘要： The invention relates to the use of particulate silicone resins in the absence of added organic solvents with particulate inorganic materials to form structured bodies and in particular molecular sieve containing structured bodies. The silicone resin is used in the form of a particulate with an average particle size of less than 700 um. Upon calcining, the silicone resin is converted to silica which acts as a binder.

4. 发明授权

US06294077B1 Production of high viscosity lubricating oil stock with improved ZSM-5 catalyst 有权
标题翻译：生产具有改进的ZSM-5催化剂的高粘度润滑油原料
公开(公告)号：US06294077B1
公开(公告)日：2001-09-25
申请号：US09496693
申请日：2000-02-02
申请人： Richard C. Dougherty , Dominick N. Mazzone , Richard F. Socha , Hye Kyung Cho Timken
发明人： Richard C. Dougherty , Dominick N. Mazzone , Richard F. Socha , Hye Kyung Cho Timken
IPC分类号： C10G7302
CPC分类号： C10M101/02 , C10G2400/10 , C10M2203/1025 , C10N2220/028 , C10N2270/00 , C10N2220/022
摘要： The present invention is a process for producing a high viscosity index and low pour point lubricating oil base stock which comprises catalytically converting a hydrotreated hydrocarbon lube oil feedstock containing waxy paraffins in the presence of hydrogen and in the presence of a low acidity ZSM-5 catalyst having a highly dispersed noble metal component. The ZSM-5 catalyst is subjected to controlled acidity reduction to an alpha value below 15 prior to incorporation of the noble metal component.
摘要翻译：本发明是一种生产高粘度指数和低倾点润滑油基础油料的方法，其包括在氢气存在下和在低酸性ZSM-5催化剂存在下催化转化含有蜡质链烷烃的加氢处理的烃类润滑油原料具有高度分散的贵金属组分。在引入贵金属组分之前，将ZSM-5催化剂进行受控的酸度降低至低于15的α值。

5. 发明授权

US5401389A Gasoline-cycle oil upgrading process 失效
标题翻译：汽油循环油升级过程
公开(公告)号：US5401389A
公开(公告)日：1995-03-28
申请号：US133942
申请日：1993-10-12
申请人： Dominick N. Mazzone , Samual A. Tabak , Hye Kyung C. Timken
发明人： Dominick N. Mazzone , Samual A. Tabak , Hye Kyung C. Timken
IPC分类号： C10G69/08 , C10G69/00 , C10G69/02
CPC分类号： C10G69/08
摘要： Light cycle oil (LCO) is upgraded to a low sulfur gasoline by co-processing the LCO with a cracked, sulfur-containing olefinic naphthas by hydrodesulfurization followed by treatment over an acidic catalyst comprising zeolite beta with a metal hydrogenation component such as molybdenum. The treatment over the acidic catalyst in the second step restores the octane loss which takes place as a result of the hydrogenative treatment and results in a low sulfur gasoline product with an octane number comparable to that of the feed naphtha. The zeolite beta catalyst is active for conversion of the higher boiling portions of the feed to products of low sulfur content in the gasoline boiling range.
摘要翻译：将轻循环油（LCO）升级为低硫汽油，通过加氢脱硫，然后用包含沸石β的酸性催化剂与金属氢化组分如钼进行处理，将裂化的含硫烯烃石脑油与LCO共处理。在第二步骤中对酸性催化剂的处理恢复了由于氢化处理而发生的辛烷值损失，并导致具有与进料石脑油相当的辛烷值的低硫汽油产物。沸石β催化剂对于将汽油沸点范围内的较低沸点部分转化为低硫含量的产物是有活性的。

6. 发明授权

US5302769A Process for making alkylated polycyclic aromatics 失效
标题翻译：制备烷基化多环芳烃的方法
公开(公告)号：US5302769A
公开(公告)日：1994-04-12
申请号：US986187
申请日：1992-12-07
申请人： David O. Marler , Dominick N. Mazzone , L. Deane Rollmann
发明人： David O. Marler , Dominick N. Mazzone , L. Deane Rollmann
IPC分类号： C07C6/12 , C10G29/20 , C07C2/66 , C07C15/24 , C07C15/27
CPC分类号： C07C6/126 , C10G29/205
摘要： A polycyclic aromatic is contacted with an alkyl-substituted single ring aromatic, such as toluene, o-, m- or p-xylene or mesitylene, over a catalyst comprising a zeolite, such as zeolite beta, USY or ZSM-5 to alkylate the polycyclic aromatic. The polycyclic aromatic can be a fused polynuclear aromatic, e.g. phenanthrene, or an assembly of two or more cyclic systems, e.g. biphenyl. The polycyclic aromatic can also include carbocyclic systems such as fluorene and naphthalene or heterocyclic systems such as benzothiophene and dibenzothiophene. The polycyclic aromatic can be derived from a cycle oil, coker gas oil, extract of lubricant solvent refining or crude distillate fraction. The transalkylating agent can be derived from a reformate, pyrolysis gasoline or coker naphtha.
摘要翻译：使多环芳族化合物与烷基取代的单环芳族化合物如甲苯，邻 - ，间 - 或对 - 二甲苯或均三甲苯在包含沸石如β沸石，USY或ZSM-5沸石的催化剂上接触，将多环芳香族。多环芳族化合物可以是稠合多核芳族化合物。菲或两个或更多个环状体系的组合，例如。联苯。多环芳族还可以包括碳环体系如芴和萘，或杂环体系如苯并噻吩和二苯并噻吩。多环芳烃可以衍生自循环油，焦化瓦斯油，润滑剂溶剂精制或粗馏分馏提取物。烷基转移剂可以由重整油，热解汽油或焦化石脑油衍生而来。

7. 发明授权

US08298451B2 Reformer distillate as gassing additive for transformer oils 有权
标题翻译：改性馏分作为变压器油的加气添加剂
公开(公告)号：US08298451B2
公开(公告)日：2012-10-30
申请号：US12584312
申请日：2009-09-03
申请人： S. Darden Sinclair , Martin A. Krevalis , Dominick N. Mazzone , Jean-Luc Martin , Louis F. Burns
发明人： S. Darden Sinclair , Martin A. Krevalis , Dominick N. Mazzone , Jean-Luc Martin , Louis F. Burns
IPC分类号： H01B3/24 , C10L1/00 , B01J29/70
CPC分类号： C10M169/04 , C10M2203/06 , C10M2203/1006 , C10M2203/104 , C10N2230/02 , C10N2230/10 , C10N2240/201 , C10N2270/00
摘要： This invention relates to reformer distillates as gassing additives for transformer oils. The reformer distillates have a 1-ring and 2-ring aromatics content of at least 98%, and are added such that the transformer oil contains less than 10 wt % of reformer distillate. The invention also relates to a method for preparing transformer oils containing reformer distillates and having excellent gassing tendency, oxidative stability, viscosity and volatility.
摘要翻译：本发明涉及重整器馏出物作为变压器油的放气添加剂。重整器馏出物具有至少98％的1-环和2-环芳族化合物含量，并加入，使得变压器油含有小于10重量％的重整器馏出物。本发明还涉及一种用于制备含有重整器馏出物的变压器油的方法，并且具有优异的放气倾向，氧化稳定性，粘度和挥发性。

8. 发明申请

US20100059725A1 Reformer distillate as gassing additive for transformer oils 有权
标题翻译：改性馏分作为变压器油的加气添加剂
公开(公告)号：US20100059725A1
公开(公告)日：2010-03-11
申请号：US12584312
申请日：2009-09-03
申请人： S. Darden Sinclair , Martin A. Krevalis , Dominick N. Mazzone , Jean-Luc Martin , Louis F. Burns
发明人： S. Darden Sinclair , Martin A. Krevalis , Dominick N. Mazzone , Jean-Luc Martin , Louis F. Burns
IPC分类号： H01B3/22
CPC分类号： C10M169/04 , C10M2203/06 , C10M2203/1006 , C10M2203/104 , C10N2230/02 , C10N2230/10 , C10N2240/201 , C10N2270/00
摘要： This invention relates to reformer distillates as gassing additives for transformer oils. The reformer distillates have a 1-ring and 2-ring aromatics content of at least 98%, and are added such that the transformer oil contains less than 10 wt % of reformer distillate. The invention also relates to a method for preparing transformer oils containing reformer distillates and having excellent gassing tendency, oxidative stability, viscosity and volatility.
摘要翻译：本发明涉及重整器馏出物作为变压器油的放气添加剂。重整器馏出物具有至少98％的1-环和2-环芳族化合物含量，并且加入使得变压器油含有小于10重量％的重整器馏出物。本发明还涉及一种用于制备含有重整器馏出物的变压器油的方法，并且具有优异的放气倾向，氧化稳定性，粘度和挥发性。

9. 发明授权

US07326818B2 Selectivation of molecular sieve catalysts and use therof in hydrocarbon conversion 有权
标题翻译：选择分子筛催化剂，并在烃转化中使用
公开(公告)号：US07326818B2
公开(公告)日：2008-02-05
申请号：US10641604
申请日：2003-08-15
申请人： Jean W. Beeckman , William G. Borghard , Arthur W. Chester , Robert A. Crane , Owen C. Feeley , John C. Fried , Dominick N. Mazzone , Glenn R. Sweeten
发明人： Jean W. Beeckman , William G. Borghard , Arthur W. Chester , Robert A. Crane , Owen C. Feeley , John C. Fried , Dominick N. Mazzone , Glenn R. Sweeten
IPC分类号： C07C5/00
CPC分类号： B01J29/40 , B01J2229/12 , B01J2229/18 , B01J2229/40 , B01J2229/42 , C07C6/123 , C07C2521/08 , C07C2529/40 , Y02P20/52 , Y10S585/906 , C07C15/08
摘要： In a process for preparing a selectivated catalyst composition useful in the disproportionation of toluene, a catalyst comprising an acidic molecular sieve is contacted with a boron compound at a temperature in excess of 500° C.; and the resultant catalyst is then contacted with a medium containing hydrogen ions to at least partially restore the acid activity of the molecular sieve.
摘要翻译：在制备可用于甲苯歧化的选择性催化剂组合物的方法中，包含酸性分子筛的催化剂在硼氢化合物与超过500℃的温度下接触; 然后使得到的催化剂与含有氢离子的介质接触，至少部分地恢复分子筛的酸活性。

10. 发明授权

US06190532B1 Production of high viscosity index lubricants 有权
标题翻译：生产高粘度指数润滑剂
公开(公告)号：US06190532B1
公开(公告)日：2001-02-20
申请号：US09439666
申请日：1999-11-15
申请人： Thomas F. Degnan , Dominick N. Mazzone
发明人： Thomas F. Degnan , Dominick N. Mazzone
IPC分类号： C10G1301
CPC分类号： B01J29/86 , B01J29/7415 , C10G2400/10
摘要： Petroleum waxes are converted to high viscosity index lubricants by a hydroisomerization process in which the wax feed is subjected to hydroisomerization over a low acidity molecular sieve isomerization catalyst (the molecular sieve being preferably a zeolite) which effects a preferential isomerization on the paraffin components in the feed to less waxy, high VI isoparaffins. The hydroisomerization is operated at high pressure, at least 1000 psig hydrogen partial pressure (reactor inlet) using a zeolite catalyst, preferably a noble metal containing zeolite beta catalyst which contains boron as a framework component of the zeolite to give a low alpha value, typically below 10. The hydroisomerization is carried out at with a 650° F.+ conversion in the range of 10 to 40 weight percent of the feed. A final dewaxing step to target pour point may be used with relatively low loss, typically no more than 15 weight percent, during this dewaxing. The final products typically have VI values in excess of 125 and usually in the range of 130 to and are characterized by exceptional stability.
摘要翻译：石油蜡通过加氢异构化方法转化为高粘度指数润滑剂，其中蜡进料在低酸度分子筛异构化催化剂（分子筛优选沸石）上进行加氢异构化，其在饲料较少蜡状，高VI异链烷烃。加氢异构化使用沸石催化剂，优选包含硼作为沸石骨架组分的硼沸石催化剂的高压，至少1000psig氢分压（反应器入口）进行操作，以产生低α值，通常加氢异构化在650°F +转化率的范围内在进料的10至40重量％的范围内进行。在该脱蜡过程中，目标倾点的最终脱蜡步骤可以使用相当低的损失，通常不超过15重量％。最终产品通常具有超过125的VI值，通常在130的范围内，并且具有特别的稳定性。

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