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公开(公告)号:US4294687A
公开(公告)日:1981-10-13
申请号:US106973
申请日:1979-12-26
申请人: Ronald Pinaire , Gary L. Everett
发明人: Ronald Pinaire , Gary L. Everett
CPC分类号: C10G45/08 , C10G2400/10
摘要: Heavy gas oil is converted to a high quality, high viscosity index lubricating oil stock by improved contacting with hydrogen in three catalytic stages. The gas oil is first hydrotreated to provide a stock more amenable to subsequent hydrocracking, thus permitting the use of less severe conditions in the latter step. The hydrocracked oil is finally subjected to a hydrogenation step to fully meet remaining lubricating oil specifications.
摘要翻译: 通过在三个催化阶段改善与氢的接触,将重质瓦斯油转化为高质量,高粘度指数的润滑油原料。 瓦斯油首先被加氢处理以提供更适合随后的加氢裂化的原料,从而允许在后一步骤中使用较不苛刻的条件。 加氢裂化油最终经受氢化步骤以完全满足剩余的润滑油规格。
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公开(公告)号:US5294327A
公开(公告)日:1994-03-15
申请号:US945029
申请日:1992-09-15
申请人: Gary L. Everett
发明人: Gary L. Everett
CPC分类号: C10G65/08 , C10G2400/14
摘要: The production of food grade quality white mineral oils from predominantly naphthenic or cycloparaffinic crude distillates heretofore have required acid treating using sulfuric acid followed by neutralization, water wash and possibly finishing step. Herein, however, three stages of hydroprocessing without any solvent extraction or acid treatment prior step are employed to produce the desired food grade quality white mineral oil having a trace of aromatic constituents therewithin. Specific steps are defined in the application in terms of the severity of the hydrogenation in the hydrotreatiang operation at each respective step; as well as the steps of separating gaseous constituents of the hydroprocessing product.
摘要翻译: 迄今为止,主要生产环烷酸或环烷烃原油馏出物的食品级优质白色矿物油需要使用硫酸进行酸处理,然后进行中和,水洗和可能的整理步骤。 然而,本文中,使用没有任何溶剂萃取或酸处理先前步骤的三个阶段的加氢处理来生产其中具有微量芳族成分的所需的食品级质量的白色矿物油。 在各个步骤中,在加氢处理操作中的氢化的严重性方面,在应用中确定了具体步骤; 以及分离加氢产物的气态成分的步骤。
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公开(公告)号:US5558284A
公开(公告)日:1996-09-24
申请号:US331560
申请日:1994-10-20
申请人: Ralph F. Baumung , Gary L. Everett
发明人: Ralph F. Baumung , Gary L. Everett
CPC分类号: B30B3/02 , B02C19/0081 , B30B9/325
摘要: Householders separate metal cans, plastic bottles, containers and similar items from other garbage. The crushing apparatus is carried on the recycling truck, and the driver tosses these items into the apparatus for crushing. The apparatus has a rotating crusher rotor (12) which forms a pinch-throat against a concavely-curved crusher plate (27). A crammer (40) is driven into reciprocation to cram the larger items into the mouth of the pinch-throat. A rubber pad (49) on the crush plate creates friction to assist in the grabbing the item into the mouth.
摘要翻译: PCT No.PCT / CA94 / 00090 Sec。 371日期:1994年10月20日 102(e)日期1994年10月20日PCT 1994年2月23日PCT PCT。 WO94 / 19106 PCT公开号 日期1994年9月1日住户将金属罐,塑料瓶,容器和类似物品与其他垃圾分开。 破碎装置装在回收车上,司机将这些物品扔进破碎设备中。 该设备具有旋转的破碎机转子(12),该转动破碎机转子(12)与凹曲的破碎机板(27)形成一个夹紧的喉部。 一个挤压器(40)被驱动进入往复运动,将较大的物品压入捏喉的口中。 挤压板上的橡胶垫(49)产生摩擦力以帮助将物品抓入口中。
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公开(公告)号:US4325804A
公开(公告)日:1982-04-20
申请号:US207574
申请日:1980-11-17
申请人: Gary L. Everett , William C. Hu
发明人: Gary L. Everett , William C. Hu
IPC分类号: C10G65/12
CPC分类号: C10G65/12 , C10G2400/14
摘要: The preparation of high quality, e.g., high viscosity index, base lubricating oils and white oils, particularly food grade white mineral oils, of suitable viscosity in high yield from a mineral oil distillate of suitable lubricating oil viscosity comprises contacting the distillate with hydrogen in four catalytic stages. The first reaction stage employs hydrocracking conditions. Subsequent reaction stages employ hydrogenation conditions. The second reaction stage, preferably employs a sulfur-resistant hydrogenation catalyst and produces a product suitable as a high quality lubricating oil base stock. The third reaction stage preferably employs a sulfur-resistant hydrogenation catalyst to obtain further aromatic saturation. The final stage employs a selective hydrogenation catalyst, optionally activated with a halogen, and produces a product suitable as a white oil, preferably a food grade white oil.
摘要翻译: 从合适的润滑油粘度的矿物油馏出物制备高品质,例如高粘度指数,基础润滑油和白油,特别是食品级白色矿物油,具有合适的粘度,高产率,包括使馏出物与四氢呋喃接触 催化阶段。 第一反应阶段采用加氢裂化条件。 随后的反应阶段采用氢化条件。 第二反应阶段优选使用耐硫氢化催化剂,并产生适合作为优质润滑油基础油料的产品。 第三反应阶段优选使用耐硫氢化催化剂以获得进一步的芳族饱和。 最终阶段采用选择性氢化催化剂,任选用卤素活化,并产生适合作为白油,优选食品级白油的产物。
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