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1. 发明授权

US09499405B2 Process for producing sulfuric acid with low levels of niter 有权
标题翻译：生产硫酸水平低的方法
公开(公告)号：US09499405B2
公开(公告)日：2016-11-22
申请号：US14642840
申请日：2015-03-10
申请人： E I DU PONT DE NEMOURS AND COMPANY
发明人： Hasan Dindi
IPC分类号： C01B17/90 , C01B17/94
CPC分类号： C01B17/90
摘要： This disclosure relates to a process for producing sulfuric acid with reduced levels of niter. The process involves (a) providing an absorption tower wherein sulfur trioxide is absorbed in a sulfuric acid feed having a first sulfuric acid solution to produce a sulfuric acid effluent having (i) a second sulfuric acid solution which has a higher concentration than the first sulfuric acid solution, (ii) a niter concentration greater than about 5 ppm (as NO3), and (iii) a temperature greater than 100° C.; and (b) contacting a first purifying agent comprising sulfamic acid and a second purifying agent comprising hydrogen peroxide with the sulfuric acid effluent to form a treated sulfuric acid effluent, the treated sulfuric acid effluent being maintained at a temperature of greater than 100° C. for a maintenance period of at least about 1 minute.
摘要翻译：本公开涉及一种生产硫酸水平降低的方法。该方法包括（a）提供吸收塔，其中三氧化硫被吸收在具有第一硫酸溶液的硫酸进料中以产生硫酸流出物，其具有（i）比第一硫酸更高的浓度的第二硫酸溶液酸溶液，（ii）大于约5ppm的硝酸盐浓度（作为NO 3），和（iii）大于100℃的温度; 和（b）使包含氨基磺酸的第一纯化剂和包含过氧化氢的第二纯化剂与硫酸流出物接触以形成经处理的硫酸流出物，处理的硫酸流出物保持在大于100℃的温度。维持期至少约1分钟。

2. 发明授权

US09365782B2 Hydroprocessing light cycle oil in liquid-full reactors 有权
公开(公告)号：US09365782B2
公开(公告)日：2016-06-14
申请号：US14816287
申请日：2015-08-03
申请人： E I DU PONT DE NEMOURS AND COMPANY
发明人： Hasan Dindi , Alan Howard Pulley , Thanh Gia Ta , Vincent Adam Kuperavage, Jr.
IPC分类号： C10G65/12 , C10G45/22 , C10G7/00 , C10G47/00
CPC分类号： C10G65/12 , C10G7/00 , C10G45/22 , C10G47/00 , C10G2300/1037 , C10G2300/1044 , C10G2300/1051 , C10G2300/4081 , C10G2400/04
摘要： A process for the hydroprocessing of a low-value light cycle oil (LCO) hydrocarbon feed to provide a high-value diesel-range product. The process comprises a hydrotreatment stage followed by a hydrocracking stage, each of which is conducted under liquid-full reaction conditions wherein substantially all the hydrogen supplied to the hydrotreating and hydrocracking reactions is dissolved in the liquid-phase hydrocarbon feed. Ammonia and optionally other gases formed during hydrotreatment are removed in a separation step prior to hydrocracking. The LCO feed is advantageously converted to diesel in high yield with little loss of hydrocarbon to naphtha.

3. 发明授权

US08815202B2 Process for producing sulfuric acid with low levels of nitrogen oxides 有权
标题翻译：生产硫酸含量低的氮氧化物的方法
公开(公告)号：US08815202B2
公开(公告)日：2014-08-26
申请号：US13969836
申请日：2013-08-19
申请人： E I du Pont de Nemours and Company
发明人： Hasan Dindi , Donald James Loftus
IPC分类号： C01B17/69 , C01B17/90 , C01B17/94
CPC分类号： C01B17/94 , C01B17/90
摘要： A process for producing sulfuric acid with reduced levels of nitrogen oxides (NOx) within a typical sulfuric acid production line. A hydrazine source material can be mixed with a sulfuric acid effluent at a temperature of at least about 90° C. for a period of at least 1 minute to reduce the level of NOx is the sulfuric acid effluent.
摘要翻译：在典型的硫酸生产线中生产具有降低的氮氧化物（NOx）水平的硫酸的方法。肼源材料可以在至少约90℃的温度下与硫酸流出物混合至少1分钟的时间，以降低NOx的水平是硫酸流出物。

4. 发明申请

US20140056802A1 PROCESS FOR PRODUCING SULFURIC ACID WITH LOW LEVELS OF NITROGEN OXIDES 有权
标题翻译：生产含低氮氧化物的硫酸的方法
公开(公告)号：US20140056802A1
公开(公告)日：2014-02-27
申请号：US13969836
申请日：2013-08-19
申请人： E I DU PONT DE NEMOURS AND COMPANY
发明人： Hasan Dindi , Donald James Loftus
IPC分类号： C01B17/94
CPC分类号： C01B17/94 , C01B17/90
摘要： A process for producing sulfuric acid with reduced levels of nitrogen oxides (NOx) within a typical sulfuric acid production line. A hydrazine source material can be mixed with a sulfuric acid effluent at a temperature of at least about 90° C. for a period of at least 1 minute to reduce the level of NOx is the sulfuric acid effluent.
摘要翻译：在典型的硫酸生产线中生产具有降低的氮氧化物（NOx）水平的硫酸的方法。肼源材料可以在至少约90℃的温度下与硫酸流出物混合至少1分钟的时间，以降低NOx的水平是硫酸流出物。

5. 发明授权

US10005971B2 Gas oil hydroprocess 有权
公开(公告)号：US10005971B2
公开(公告)日：2018-06-26
申请号：US15444363
申请日：2017-02-28
申请人： E I DU PONT DE NEMOURS AND COMPANY
发明人： Hasan Dindi , Thanh Gia Ta , Vincent Adam Kuperavage, Jr. , Alan Howard Pulley , Scott Louis Webster
IPC分类号： C10G65/12
CPC分类号： C10G65/12 , C10G45/02 , C10G45/08 , C10G47/00 , C10G47/06 , C10G47/20 , C10G47/36 , C10G2300/1059 , C10G2300/802 , C10G2400/04
摘要： A process for the hydroprocessing of a gas oil (GO) hydrocarbon feed to provide high yield of a diesel fraction. The process comprises a liquid-full hydrotreating reaction zone followed by a liquid-full hydrocracking reaction zone. A refining zone may be integrated with the hydrocracking reaction zone. Ammonia and other gases formed during the hydrotreatment are removed in a separation step prior to hydrocracking.

6. 发明授权

US09139783B2 Hydroprocessing light cycle oil in liquid-full reactors 有权
标题翻译：液体反应堆中的加氢轻循环油
公开(公告)号：US09139783B2
公开(公告)日：2015-09-22
申请号：US14051495
申请日：2013-10-11
申请人： E I DU PONT DE NEMOURS AND COMPANY
发明人： Hasan Dindi , Alan Howard Pulley , Thanh Gia Ta , Vincent Adam Kuperavage, Jr.
IPC分类号： C10G57/00 , C10G65/12 , C10G45/22 , C10G7/00
CPC分类号： C10G65/12 , C10G7/00 , C10G45/22 , C10G47/00 , C10G2300/1037 , C10G2300/1044 , C10G2300/1051 , C10G2300/4081 , C10G2400/04
摘要： A process for the hydroprocessing of a low-value light cycle oil (LCO) hydrocarbon feed to provide a high-value diesel-range product. The process comprises a hydrotreatment stage followed by a hydrocracking stage, each of which is conducted under liquid-full reaction conditions wherein substantially all the hydrogen supplied to the hydrotreating and hydrocracking reactions is dissolved in the liquid-phase hydrocarbon feed. Ammonia and optionally other gases formed during hydrotreatment are removed in a separation step prior to hydrocracking. The LCO feed is advantageously converted to diesel in high yield with little loss of hydrocarbon to naphtha.
摘要翻译：一种用于低价值轻循环油（LCO）烃进料加氢处理以提供高价值柴油范围产品的方法。该方法包括加氢处理阶段，随后是加氢裂化阶段，每个步骤在液体完全反应条件下进行，其中供应到加氢处理和加氢裂化反应的基本上所有氢气都溶解在液相烃进料中。在加氢处理之前，氨和任选的其它气体在分离步骤中被除去。有利地，LCO进料以高产率转化为柴油，几乎没有烃与石脑油的损失。

7. 发明授权

US09783746B2 Process for improving cold flow properties and increasing yield of middle distillate feedstock through liquid full hydrotreating and dewaxing 有权
公开(公告)号：US09783746B2
公开(公告)日：2017-10-10
申请号：US15285803
申请日：2016-10-05
申请人： E I DU PONT DE NEMOURS AND COMPANY
发明人： Hasan Dindi , Sandeep Palit , Alan Howard Pulley , Luis Eduardo Murillo , Thanh Gia Ta , Brian Boeger
IPC分类号： C10G65/04 , C10G45/22 , C10G45/58 , C10G45/60 , C10G45/62 , C10G45/64 , C10G49/20 , C10G49/22 , C10L1/08 , C10L10/14 , C10L10/16
CPC分类号： C10G65/043 , C10G45/22 , C10G45/58 , C10G45/60 , C10G45/62 , C10G45/64 , C10G49/20 , C10G49/22 , C10G2300/1048 , C10G2300/1055 , C10G2300/202 , C10G2300/301 , C10G2300/304 , C10G2300/4006 , C10G2300/42 , C10G2300/44 , C10G2300/802 , C10G2400/04 , C10L1/08 , C10L10/14 , C10L10/16 , C10L2200/0446 , C10L2270/026
摘要： Novel liquid-full process for improving cold flow properties and increasing yield of middle distillate fuel feedstock by hydrotreating and dewaxing the feedstock in liquid-full reactors.

8. 发明授权

US09617485B2 Gas oil hydroprocess 有权
公开(公告)号：US09617485B2
公开(公告)日：2017-04-11
申请号：US14481952
申请日：2014-09-10
申请人： E I DU PONT DE NEMOURS AND COMPANY
发明人： Hasan Dindi , Thanh Gia Ta , Vincent Adam Kuperavage, Jr. , Alan Howard Pulley , Scott Louis Webster
IPC分类号： C10G65/12 , C10G45/02 , C10G45/08 , C10G47/00 , C10G47/06 , C10G47/20 , C10G47/36
CPC分类号： C10G65/12 , C10G45/02 , C10G45/08 , C10G47/00 , C10G47/06 , C10G47/20 , C10G47/36 , C10G2300/1059 , C10G2300/802 , C10G2400/04
摘要： A process for the hydroprocessing of a gas oil (GO) hydrocarbon feed to provide high yield of a diesel fraction. The process comprises a liquid-full hydrotreating reaction zone followed by a liquid-full hydrocracking reaction zone. A refining zone may be integrated with the hydrocracking reaction zone. Ammonia and other gases formed during the hydrotreatment are removed in a separation step prior to hydrocracking.

9. 发明授权

US09499750B2 Process for improving cold flow properties and increasing yield of middle distillate feedstock through liquid full hydrotreating and dewaxing 有权
标题翻译：通过液体全加氢处理和脱蜡改善中间馏分原料的冷流特性和提高产率的方法
公开(公告)号：US09499750B2
公开(公告)日：2016-11-22
申请号：US14208258
申请日：2014-03-13
申请人： E I DU PONT DE NEMOURS AND COMPANY
发明人： Hasan Dindi , Sandeep Palit , Alan Howard Pulley , Luis Eduardo Murillo , Thanh Gia Ta , Brian Boeger
IPC分类号： C10G65/04 , C10G45/22 , C10G45/58 , C10G45/60 , C10G45/62 , C10G45/64 , C10G49/20 , C10G49/22 , C10L1/08
CPC分类号： C10G65/043 , C10G45/22 , C10G45/58 , C10G45/60 , C10G45/62 , C10G45/64 , C10G49/20 , C10G49/22 , C10G2300/1048 , C10G2300/1055 , C10G2300/202 , C10G2300/301 , C10G2300/304 , C10G2300/4006 , C10G2300/42 , C10G2300/44 , C10G2300/802 , C10G2400/04 , C10L1/08 , C10L10/14 , C10L10/16 , C10L2200/0446 , C10L2270/026
摘要： Novel liquid-full process for improving cold flow properties and increasing yield of middle distillate fuel feedstock by hydrotreating and dewaxing the feedstock in liquid-full reactors.
摘要翻译：用于通过在液体反应器中加氢处理和脱蜡原料来改善冷流特性和提高中间馏分燃料原料的产率的新型全液化方法。

10. 发明授权

US09212323B2 Liquid-full hydrotreating and selective ring opening processes 有权
标题翻译：全液相加氢处理和选择性开环方法
公开(公告)号：US09212323B2
公开(公告)日：2015-12-15
申请号：US14335058
申请日：2014-07-18
申请人： E I DU PONT DE NEMOURS AND COMPANY
发明人： Hasan Dindi , Thanh Gia Ta
IPC分类号： C10G45/02 , C10G45/08 , C10G45/22 , C10G45/48 , C10G45/58 , C10G45/60 , C10G65/08 , C10G65/12 , C10G69/02 , C10G45/50 , C10G45/54 , C10G65/04
CPC分类号： C10G45/02 , C10G45/08 , C10G45/22 , C10G45/48 , C10G45/50 , C10G45/54 , C10G45/58 , C10G45/60 , C10G65/043 , C10G65/08 , C10G65/12 , C10G69/02 , C10G2300/202 , C10G2300/307 , C10G2300/308 , C10G2300/4018 , C10G2300/4081 , C10G2300/802 , C10G2400/04
摘要： This disclosure relates to liquid-full processes for hydroprocessing a light cycle oil (LCO). The processes involve hydrotreatment followed by selective ring opening in the presence of hydrotreating catalyst and selective ring opening catalyst respectively. The selective ring opening catalyst can be either zeolite ring opening catalyst or amorphous ring opening catalyst. In aspects of zeolite ring opening catalyst, the volume ratio of the total amount of the zeolite ring opening catalyst to the total amount of the hydrotreating catalyst is from about 0.2 to about 1.5. In aspects of amorphous ring opening catalyst, the volume ratio of the total amount of the amorphous ring opening catalyst to the total amount of the hydrotreating catalyst is from about 0.2 to about 3.
摘要翻译：本公开涉及用于加氢处理轻质循环油（LCO）的液体充分方法。该方法包括加氢处理，然后在加氢处理催化剂和选择性开环催化剂存在下选择性开环。选择性开环催化剂可以是沸石开环催化剂或无定形开环催化剂。在沸石开环催化剂方面，沸石开环催化剂的总量与加氢处理催化剂总量的体积比为约0.2至约1.5。无定形开环催化剂方面，无定形开环催化剂的总量与加氢处理催化剂总量的体积比为约0.2至约3。

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