专利快速检索-快速检索全球专利，免费商用专利数据库-IPRDB

1. 发明申请

US20060283776A1 Bitumen Production-Upgrade with Common or Different Solvents 有权
标题翻译：沥青生产升级与普通或不同溶剂
公开(公告)号：US20060283776A1
公开(公告)日：2006-12-21
申请号：US11160366
申请日：2005-06-21
申请人： Rashid Iqbal , Anshumali , Raymond Floyd
发明人： Rashid Iqbal , Anshumali , Raymond Floyd
IPC分类号： C10C3/00 , C10G1/00 , B01J8/04
CPC分类号： C10G21/003 , C10G21/28 , C10G31/08 , C10G2300/1033 , C10G2300/203 , C10G2300/206 , C10G2300/207 , C10G2300/208 , C10G2300/308 , C10G2300/4081 , C10G2300/44 , C10G2300/802 , C10G2300/805
摘要： Disclosed is a process for the upgrading of heavy oils and bitumens, where the total feed to the process can include heavy oil or bitumen, water, and diluent. The process can include the steps of solvent deasphalting 110 the total feed 105 to recover an asphaltene fraction 116, a deasphalted oil fraction 118 essentially free of asphaltenes, a water fraction 112, and a solvent fraction 114. The process allows removal of salts from the heavy oils and bitumens either into the aqueous products or with the asphaltene product.
摘要翻译：公开了一种重质油和沥青改质方法，其中该方法的总进料可包括重油或沥青，水和稀释剂。该方法可以包括将总进料105溶剂脱沥青的步骤，以回收沥青质馏分116，基本不含沥青质的脱沥青油馏分118，水馏分112和溶剂馏分114.该方法允许从重油和沥青进入含水产品或沥青质产品。

2. 发明申请

US20060062635A1 CONCENTRATED BUOYANCY SUBSEA PIPELINE APPARATUS AND METHOD 有权
标题翻译：浓缩的BUOYANCY SUBSEA管道装置和方法
公开(公告)号：US20060062635A1
公开(公告)日：2006-03-23
申请号：US10711489
申请日：2004-09-21
申请人： John Mungall , Khamir Joshi , Craig Lamison
发明人： John Mungall , Khamir Joshi , Craig Lamison
IPC分类号： F16L1/00
CPC分类号： F16L1/20 , F16L1/14
摘要： Various apparatuses and methods to traverse an undersea topographic feature (12) with a subsea pipeline (18) are disclosed. The apparatuses and methods of the present invention accomplish this task through the use of a concentrated buoyancy scheme (10). The invention disclosed can allow more efficient and cost effective traversal of hostile terrain for subsea pipelines at great depths while minimizing the risk of rupturing the pipeline (18) or negatively impacting the surrounding undersea environment.
摘要翻译：公开了用海底管道（18）横穿海底地形特征（12）的各种装置和方法。本发明的装置和方法通过使用集中的浮力方案（10）来完成这个任务。所公开的发明可以更有效和成本有效地跨越海底管线在较大深度的敌对地形，同时最小化破裂管道（18）的风险或对周围海底环境的负面影响。

3. 发明授权

US06902593B2 Separation device to remove fine particles 有权
标题翻译：分离装置去除细颗粒
公开(公告)号：US06902593B2
公开(公告)日：2005-06-07
申请号：US10248875
申请日：2003-02-26
申请人： Richard B. Miller , Eusebius Gbordzoe , Yong-Lin Yang , Suisheng M. Dou , David Lee Johnson
发明人： Richard B. Miller , Eusebius Gbordzoe , Yong-Lin Yang , Suisheng M. Dou , David Lee Johnson
IPC分类号： B04C3/04 , B01D45/14 , B01J8/00 , B04C3/06 , B04C5/14 , B04C5/181 , B04C5/24 , B04C5/30 , B01D45/12
CPC分类号： B04C5/181 , B01D45/14 , B01J8/0055 , B04C5/14 , B04C5/30
摘要： A multi-cyclone gas/solids separator with reduced solids re-entrainment is disclosed. The separator uses a plurality of cyclones spaced horizontally apart from adjacent cyclones to process flue gas containing residual catalyst fines. Each cyclone has a body that has a feed inlet end for admitting gas and entrained solids into an annular space defined by a sidewall of the cyclone body and a cylindrical gas outlet tube axially aligned with the cyclone body. A solids outlet at an opposing end of the cyclone body has a tangential outlet for solids and a minor amount of gas through a sidewall of the cyclone body. A gas reflux opening is axially aligned with the outlet tube. The plurality of cyclones share both a common catch chamber for solids discharged from the solids outlet, and a common manifold for gas and entrained solids. A plurality of shields are positioned in the catch chamber to inhibit discharge of solids from the tangential outlet of the adjacent cyclones into a vicinity of an inlet of the gas reflux opening.
摘要翻译：公开了具有减少的固体再夹带的多旋风分离器气/固分离器。分离器使用与相邻旋风分离器水平分开的多个旋风分离器来处理含有残留催化剂细粉的烟道气。每个旋风分离器具有一个主体，该主体具有用于将气体和夹带的固体引入由旋风分离器主体的侧壁限定的环形空间和与旋风分离器主体轴向对准的圆柱形气体出口管的进料端。在旋风分离器主体的相对端处的固体出口具有用于固体的切向出口和通过旋风器主体的侧壁的少量气体。气体回流开口与出口管轴向对准。多个旋风分离器共享用于从固体出口排出的固体的公共捕获室，以及用于气体和夹带固体的公共歧管。多个屏蔽件位于捕获室中以阻止固体从相邻旋风分离器的切向出口排出到气体回流开口的入口附近。

4. 发明申请

US20040177555A1 PARTIAL OXIDATION REFORMER-REFORMING EXCHANGER ARRANGEMENT FOR HYDROGEN PRODUCTION 有权
标题翻译：用于氢生产的部分氧化改质改质交换器装置
公开(公告)号：US20040177555A1
公开(公告)日：2004-09-16
申请号：US10708606
申请日：2004-03-15
申请人： KELLOGG BROWN AND ROOT, INC.
发明人： Stanislaus A. Knez , Avinash Malhotra , David P. Mann , Martin J. Van Sickels
IPC分类号： B01J008/00
CPC分类号： C01B3/36 , B01J8/067 , B01J2208/00309 , B01J2208/0053 , B01J2219/00024 , C01B3/382 , C01B3/384 , C01B3/48 , C01B2203/0233 , C01B2203/025 , C01B2203/0283 , C01B2203/0475 , C01B2203/0844 , C01B2203/1241 , C01B2203/141 , C01B2203/142 , Y02P20/124
摘要： Low-energy hydrogen production is disclosed. A reforming exchanger is placed in parallel with a partial oxidation reactor in a new hydrogen plant with improved efficiency and reduced steam export, or in an existing hydrogen plant where the hydrogen capacity can be increased by as much as 20-30 percent with reduced export of steam from the hydrogen plant.
摘要翻译：公开了低能氢生产。在新的氢气厂中，重整交换器与部分氧化反应器平行放置，效率提高，蒸汽输出降低，或者在现有氢气厂中，氢气容量可以增加20-30％，减少出口来自氢电厂的蒸汽。

5. 发明申请

US20060135830A1 SELECTIVE HYDROGENATION OF ALPHA-METHYL-STYRENE TO CUMENE 有权
标题翻译： ALPHA-METHYL-STYRENE选择性氢化成CUMENE
公开(公告)号：US20060135830A1
公开(公告)日：2006-06-22
申请号：US10905177
申请日：2004-12-20
申请人： Ronald Birkhoff , Clive Griffiths , Kiran Shah , Anand Subramanian
发明人： Ronald Birkhoff , Clive Griffiths , Kiran Shah , Anand Subramanian
IPC分类号： C07C5/10 , B01J8/04
CPC分类号： C07C5/03 , C07C7/163 , Y02E60/324 , Y02P20/52 , C07C15/085
摘要： A process for the selective hydrogenation of alpha-methyl-styrene (AMS) to cumene in a two catalyst system is disclosed. A crude cumene feed stream containing up to 10% AMS by weight is supplied to the first reaction zone 112 and mixed with hydrogen in a first catalyst bed 118 containing a nickel catalyst, converting from 70 to 95 percent of the AMS to cumene. Cumene and remaining AMS are separated from hydrogen in a liquid take off tray 120. The first reaction zone 112 5effluent is supplied to a second reaction zone 114, where the effluent and hydrogen gas are mixed in a second catalyst bed 126 containing a noble-metal catalyst to substantially convert any remaining AMS to cumene. Cumene is collected, separated from the hydrogen, and can be resupplied to the hydrogenation reactor 110, or supplied as feed to a phenol synthesis loop.
摘要翻译：公开了在二催化剂体系中α-甲基 - 苯乙烯（AMS）选择性氢化为枯烯的方法。将含有高达10重量％AMS的粗异丙基苯进料流供应到第一反应区112，并在含有镍催化剂的第一催化剂床118中与氢混合，将70-95％的AMS转化为异丙基苯。在液体取出托盘120中，将Cumene和剩余的AMS与氢气分离。将第一反应区112 5流出物供应到第二反应区域114，其中流出物和氢气在含有贵金属催化剂的第二催化剂床126中混合以将任何剩余的AMS基本上转化为枯烯。收集赤藓烯，与氢分离，并且可以重新供应到氢化反应器110，或作为进料提供给酚合成回路。

6. 发明申请

US20060049082A1 SELF-STRIPPING FCC RISER CYCLONE 有权
标题翻译：自卸式FCC升级器
公开(公告)号：US20060049082A1
公开(公告)日：2006-03-09
申请号：US10711308
申请日：2004-09-09
申请人： Phillip Niccum , Iwan Chan , Richard Miller , Steven Tragesser
发明人： Phillip Niccum , Iwan Chan , Richard Miller , Steven Tragesser
IPC分类号： C10G11/00 , B01J8/18
CPC分类号： B01J8/28 , B01J8/0055 , B01J8/388 , B04C5/18 , B04C9/00 , B04C2009/008 , C10G11/18 , C10G2300/4056 , C10G2300/4093
摘要： Apparatus and method are provided for separating and stripping suspensions comprising catalyst particles transported in vapors from the fluid catalytic cracking riser/reactor. Particles are disentrained from vapor in a vortex zone 112 of the primary cyclonic separator 100. The disentrained particles enter a stripping zone 126, wherein the particles are contacted with a stripping gas 136 to recover vapors entrained and adsorbed onto the catalyst. The stripping gas 136 enters stripping zone 126 via perforations in the wall of the cyclone 100. The stripping gas 136 limits the residual catalytic conversion of hydrocarbon vapors and formation of delta-coke on the catalyst. Stripped catalyst is delivered from the cyclone stripping zone 126 via a dipleg 130 connected to a bottom of the cyclone 100, and enters an FCC stripping vessel. Solids-lean stripping gas and vapors from the catalyst particles are blended with the carrier fluid and discharged from the cyclone.
摘要翻译：提供了用于分离和汽提悬浮液的装置和方法，所述悬浮液包含从流体催化裂化提升管/反应器以蒸汽输送的催化剂颗粒。主旋涡分离器100的涡流区112中的蒸气分离颗粒。脱盐颗粒进入汽提区126，其中颗粒与汽提气体136接触以回收夹带并吸附到催化剂上的蒸气。汽提气体136通过旋风分离器100的壁中的穿孔进入汽提区126。汽提气体136限制了烃蒸气的残留催化转化和δ-焦炭在催化剂上的形成。剥离的催化剂通过连接到旋风分离器100的底部的三通130从旋风分离器剥离区126输送，并进入FCC汽提容器。来自催化剂颗粒的贫贫汽提气体和蒸气与载体流体混合并从旋风分离器中排出。

7. 发明申请

US20050115484A1 SEMISUBMERSIBLE TRIMARAN 有权
公开(公告)号：US20050115484A1
公开(公告)日：2005-06-02
申请号：US10708531
申请日：2004-03-10
申请人： John Leitch , Harvey McBee , Jan Veldwijk , Douglass Williams
发明人： John Leitch , Harvey McBee , Jan Veldwijk , Douglass Williams
IPC分类号： B63B1/00 , B63B1/10 , B63B1/12 , B63B35/44 , B63B35/50
CPC分类号： B63B35/44 , B63B1/107 , B63B35/50 , B63B39/03
摘要： A semisubmersible trimaran for use in an afloat sea base is disclosed. The trimaran has an upper deck structure 12 supported on a longitudinal center hull 26 and column-stabilized, longitudinal outrigger pontoons 28. The center hull 26 and pontoon columns 38 and 40 have a reduced waterplane area for minimizing motion during operations. The trimaran has a transit draft 37 for deployment at full waterplane area, and an operating draft 36 with a reduced waterplane area for damping motion. The vessel can be deployed with a transit drive 42 on the hull 26, and dynamically positioned at a destination for operations. Multiple trimarans can be assembled to provide an extended upper surface, including a landing area for fixed-wing aircraft.
摘要翻译：公开了一种用于漂浮海底的半潜式三体船。三体船具有支撑在纵向中心船体26和柱稳定的纵向外伸支架28上的上甲板结构12.中心船体26和浮筒柱38和40具有减少的水翼面积，以最小化运行期间的运动。三体船有一个运输草案37，用于全水面区域的部署，以及一个减少水面面积用于阻尼运动的运行草图36。船舶可以与船体26上的运输驱动器42一起部署，并且动态地定位在目的地用于操作。可以组装多个三体船以提供延长的上表面，包括用于固定翼飞机的着陆区域。

8. 发明申请

US20050086864A1 LOW PRESSURE DROP REFORMING EXCHANGER 有权
标题翻译：低压减压换向阀
公开(公告)号：US20050086864A1
公开(公告)日：2005-04-28
申请号：US10905460
申请日：2005-01-05
申请人： Robert Burlingame , Thomas Czuppon , Larry Hackemesser
发明人： Robert Burlingame , Thomas Czuppon , Larry Hackemesser
IPC分类号： B01J8/00 , B01J8/02 , B01J8/06 , B01J19/30 , B01J23/755 , B01J35/02 , C01B3/38
CPC分类号： B01J8/0292 , B01J8/008 , B01J8/067 , B01J19/30 , B01J23/755 , B01J35/026 , B01J2208/00221 , B01J2208/00309 , B01J2208/00495 , B01J2208/0053 , B01J2219/30223 , B01J2219/30242 , B01J2219/32296 , C01B3/382 , C01B3/384 , C01B2203/0844 , C01B2203/141 , C01B2203/142 , C01B2203/82 , Y02P20/52
摘要： Disclosed are a syngas production process and a reforming exchanger 100. The process involves passing a first portion of hydrocarbon feed mixed with steam and oxidant through an autothermal catalytic steam reforming zone to form a first reformed gas of reduced hydrocarbon content, passing a second portion of the hydrocarbon feed mixed with steam through an endothermic catalytic steam reforming zone to form a second reformed gas of reduced hydrocarbon content, and mixing the first and second reformed gases and passing the resulting gas mixture through a heat exchange zone for cooling the gas mixture and thereby supplying heat to the endothermic catalytic steam reforming zone. The endothermic catalytic steam reforming zone and the heat exchange zone are respectively disposed tube side and shell side within a shell-and-tube reforming exchanger 100. The reforming exchanger 100 comprises a plurality of tubes 118 packed with low pressure drop catalyst-bearing monolithic structures 200 wherein an inside diameter of the tubes 118 is less than 4 times a maximum edge dimension of the catalyst structures 200.
摘要翻译：公开了合成气生产方法和重整换热器100。该方法包括使与蒸汽和氧化剂混合的烃进料的第一部分通过自热催化蒸汽重整区，以形成具有降低的烃含量的第一重整气体，使与蒸汽混合的烃进料的第二部分通过吸热催化蒸汽重整形成还原烃含量的第二重整气体，并混合第一和第二重整气体，并使得到的气体混合物通过热交换区，用于冷却气体混合物，从而向吸热催化蒸汽重整区供热。吸热催化蒸汽重整区和热交换区分别设置在管 - 管重整交换器100内的管侧和壳侧。重整交换器100包括填充有低压降催化剂承载整体结构200的多个管118，其中管118的内径小于催化剂结构200的最大边缘尺寸的4倍。

9. 发明申请

US20040182002A1 Autothermal Reformer-Reforming Exchanger Arrangement for Hydrogen Production 有权
标题翻译：用于氢气生产的自热重整器改造器换热器排列
公开(公告)号：US20040182002A1
公开(公告)日：2004-09-23
申请号：US10708583
申请日：2004-03-12
申请人： KELLOGG BROWN AND ROOT, INC.
发明人： Avinash Malhotra , James Hanlan Gosnell
IPC分类号： C01B003/26 , B01J008/00
CPC分类号： B01J8/0488 , B01J8/0496 , B01J8/065 , B01J8/067 , B01J2208/00309 , B01J2208/00504 , B01J2208/0053 , B01J2219/00006 , C01B3/382 , C01B3/384 , C01B3/48 , C01B2203/0233 , C01B2203/0244 , C01B2203/0283 , C01B2203/0405 , C01B2203/042 , C01B2203/0844 , C01B2203/141 , C01B2203/142 , C01B2203/82 , H01M8/0618 , H01M8/0668 , Y02P20/129
摘要： Low-energy, low-capital hydrogen production is disclosed. A reforming exchanger 14 is placed in parallel with an autothermal reformer (ATR) 10 to which are supplied a preheated steam-hydrocarbon mixture. An air-steam mixture is supplied to the burner/mixer of the ATR 10 to obtain a syngas effluent at 650null-1050null C. The effluent from the ATR is used to heat the reforming exchanger, and combined reformer effluent is shift converted and separated into a mixed gas stream and a hydrogen-rich product stream. High capital cost equipment such as steam-methane reformer and air separation plant are not required.
摘要翻译：披露了低能耗，低资本的氢气生产。重整交换器14与自热重整器（ATR）10平行放置，向其供应预热的蒸汽 - 烃混合物。将空气 - 蒸汽混合物供应到ATR 10的燃烧器/混合器，以在650℃-1050℃下获得合成气流出物。来自ATR的流出物用于加热重整交换器，并且组合的重整器流出物被转换和分离成混合气流和富氢产物流。不需要高成本设备，如蒸汽 - 甲烷重整器和空气分离设备。

10. 发明申请

US20060210361A1 CONTINUOUSLY PRESSURIZED PIPELINE 有权
标题翻译：连续加压管道
公开(公告)号：US20060210361A1
公开(公告)日：2006-09-21
申请号：US10907041
申请日：2005-03-17
申请人： Craig Lamison
发明人： Craig Lamison
IPC分类号： F16L1/00 , F16L35/00
CPC分类号： F16L1/165 , F16L1/161 , F16L1/203 , Y10T137/6116
摘要： A pipeline segment 5, used for the manufacture of a thin-walled underwater pipeline 50, is disclosed. Terminal pipe sections 20 are at either end of main pipe section 10. Terminal pipe sections 20 are thick-walled or otherwise resistant to collapse due to external pressure. A pressure isolation device 30 maintains an internal pressure in main pipe section 10 above a shutoff pressure. A pressure compensation system 35 can protect main pipe section 10 from collapse due to external pressure. Pipeline segments 5 can be manufactured by connecting and winding stalks 100 onto storage device 110 forming main pipe section 10. Terminal pipe section 20 can be connected to the lead end of main pipe section 10, and main pipe section 10 can be unwound from storage device 110 while towing.
摘要翻译：公开了一种用于制造薄壁水下管线50的管线段5。端子管段20位于主管段10的任一端。端子管段20由于外部压力而是厚壁的或以其他方式抵抗塌缩的。压力隔离装置30将主管部10中的内部压力保持在切断压力以上。压力补偿系统35可以保护主管段10不受外部压力的压缩。管线段5可以通过将杆100连接和缠绕到形成主管段10的存储装置110上来制造。端子管部分20可以连接到主管部分10的引导端，并且主管部分10可以在牵引时从存储装置110退绕。

你已经成功收藏专利！

检索式保存成功!

IPRDB

热门服务

关于我们

友情链接

联系方式