公开(公告)号：US20110011094A1

公开(公告)日：2011-01-20

申请号：US12888004

申请日：2010-09-22

申请人： Brian W. Hedrick

发明人： Brian W. Hedrick

IPC分类号： F02C3/28 ,  F02C3/20

CPC分类号： C10G11/185 ,  B01J8/1836 ,  B01J8/26 ,  B01J38/12 ,  B01J38/16 ,  B01J38/30 ,  B01J38/36 ,  B01J38/40 ,  B01J38/72 ,  C10G11/182 ,  F01K13/00 ,  Y02E20/344 ,  Y02P30/446

摘要： In at least one embodiment of the present invention, a method of recovering energy from a FCC unit having a reactor and a regenerator for overall CO2 reduction is provided. The method comprises cooling syngas to a predetermined low temperature to define cooled syngas. A turbo-expander including a first compressor is provided. The turbo-expander train is configured to combust and expand gas to drive the first compressor. The cooled syngas is compressed with the first compressor to define compressed syngas. A first stream of gas comprising CO2 and a second stream of gas comprising CO are separated from the compressed syngas. O2 and the first and second streams of gas are introduced to the turbo-expander train. The first stream of gas is expanded and the second stream of gas is combusted and expanded with the O2 to recover energy, driving the first compressor and producing the syngas.

摘要翻译： 在本发明的至少一个实施方案中，提供了一种从具有用于总体CO 2还原的反应器和再生器的FCC装置回收能量的方法。 该方法包括将合成气冷却至预定的低温以限定冷却的合成气。 提供包括第一压缩机的涡轮膨胀机。 涡轮膨胀机列车构造成燃烧和膨胀气体以驱动第一压缩机。 冷却的合成气用第一压缩机压缩以限定压缩的合成气。 包含CO 2的第一气体流和包含CO的第二气体气流与压缩的合成气分离。 O2和第一和第二气体流被引入涡轮膨胀机列车。 第一气体流膨胀，第二气体气体与O2一起燃烧和膨胀以回收能量，驱动第一压缩机并产生合成气。

公开(公告)号：US20100236980A1

公开(公告)日：2010-09-23

申请号：US12408046

申请日：2009-03-20

申请人： Lawrence L. Upson ,  Brian W. Hedrick ,  Keith Allen Couch

发明人： Lawrence L. Upson ,  Brian W. Hedrick ,  Keith Allen Couch

IPC分类号： C10G51/04 ,  B01J8/26

CPC分类号： C10G51/026 ,  C10G11/05 ,  C10G51/06

摘要： One exemplary embodiment can be a process for fluid catalytic cracking. The process can include withdrawing a catalyst from a reaction vessel to replace a catalyst inventory over a period of about 10- about 35 days for maximizing propylene yield.

摘要翻译： 一个示例性实施方案可以是流化催化裂化的方法。 该方法可以包括从反应容器中取出催化剂以在约10-约35天的时间内代替催化剂库存以使丙烯产率最大化。

公开(公告)号：US07767075B2

公开(公告)日：2010-08-03

申请号：US11963101

申请日：2007-12-21

申请人： Brian W. Hedrick

发明人： Brian W. Hedrick

IPC分类号： C10G51/04

CPC分类号： C10G11/18 ,  Y02P30/446

摘要： Systems and methods of reducing refinery carbon dioxide emissions by increasing synthesis gas production in a fluid catalytic cracking unit having a reactor and a regenerator are disclosed. In one example, a method comprises separating spent catalyst from a hydrocarbon product in the reactor, the spent catalyst having trapped hydrocarbon thereon. The method further comprises reacting an additional feed with the spent catalyst in the reactor to deposit additional coke on the spent catalyst, defining a gas product. The method further separating the gas product and the trapped hydrocarbon from the spent catalyst with a stripping gas. The method further comprises removing coke from the spent catalyst in the regenerator, thereby increasing the amount of synthesis gas production.

摘要翻译： 公开了通过在具有反应器和再生器的流化催化裂化装置中增加合成气生产来减少炼油二氧化碳排放的系统和方法。 在一个实例中，一种方法包括从反应器中的烃产物中分离废催化剂，废催化剂上含有捕获的烃。 该方法还包括使另外的进料与反应器中的废催化剂反应以在废催化剂上沉积另外的焦炭，从而限定气体产物。 该方法进一步用汽提气体从废催化剂中分离气体产物和捕获的烃。 该方法还包括从再生器中的废催化剂中除去焦炭，从而增加合成气产量。

公开(公告)号：US20100158764A1

公开(公告)日：2010-06-24

申请号：US12337734

申请日：2008-12-18

申请人： Brian W. Hedrick ,  Daniel B. Gillis

发明人： Brian W. Hedrick ,  Daniel B. Gillis

IPC分类号： B01J19/00

CPC分类号： C10G11/18 ,  C10G45/32 ,  C10G69/04 ,  C10G2300/1033

摘要： A process and apparatus for improving flow properties of crude may include processing a first crude stream, which may in turn include cracking the first crude stream with catalyst to form a cracked stream and spent catalyst, hydrotreating a portion of the cracked stream and then mixing the hydrotreated stream with an unprocessed second crude stream.

摘要翻译： 用于改善粗品流动性质的方法和设备可包括加工第一原油流，其还可包括用催化剂裂化第一原油流以形成裂化料流和废催化剂，加氢处理裂化物流的一部分，然后将 加氢处理的流与未加工的第二原油流。

公开(公告)号：US20100126621A1

公开(公告)日：2010-05-27

申请号：US12323101

申请日：2008-11-25

申请人： Mark Van Wees ,  Joseph M. Slaughter ,  Brian W. Hedrick ,  Brian H. Johnson

发明人： Mark Van Wees ,  Joseph M. Slaughter ,  Brian W. Hedrick ,  Brian H. Johnson

IPC分类号： B65B3/04

CPC分类号： B01D3/008

摘要： A liquid distribution device including a liquid distributor having an inlet pipe connected to a piping manifold that further includes a plurality of liquid distribution pipes each liquid distribution pipe including an inlet connected to the piping manifold and an outlet, and a liquid impact portion having a plurality of pans located in close proximity to the outlet of one or more of the liquid distribution pipes.

摘要翻译： 一种液体分配装置，包括具有连接到管道歧管的入口管的液体分配器，所述入口管还包括多个液体分配管，每个液体分配管包括连接到管道歧管的入口和出口，以及具有多个 位于一个或多个液体分配管的出口附近的平底锅。

公开(公告)号：US07699974B2

公开(公告)日：2010-04-20

申请号：US11962740

申请日：2007-12-21

申请人： Brian W. Hedrick

发明人： Brian W. Hedrick

IPC分类号： C10J3/00

CPC分类号： C10G11/182 ,  B01J8/1836 ,  B01J8/26 ,  B01J38/12 ,  B01J38/16 ,  B01J38/30 ,  B01J38/36 ,  B01J38/40 ,  B01J38/72 ,  C10G11/185 ,  F01K13/00 ,  F02C3/22 ,  F02C6/04 ,  F02C6/10 ,  Y02E20/344 ,  Y02P30/446

摘要： In at least one embodiment of the present invention, a method of heating a FCC unit having a regenerator and a reactor having overall CO2 reduction is provided. The method comprises compressing syngas to define compressed syngas. Separating a first stream of gas comprising CO2 from the compressed syngas. A second stream of gas comprising O2 is expanded with the first stream of gas to produce a feed gas. The feed gas is introduced to the regenerator at gasification conditions to burn coke from coke heavy spent catalyst advanced from the reactor, producing syngas and heat for operating the reactor at reaction temperatures.

摘要翻译： 在本发明的至少一个实施方案中，提供了一种加热具有再生器的FCC单元和具有总体CO 2还原的反应器的方法。 该方法包括压缩合成气以限定压缩的合成气。 从压缩的合成气分离包含CO 2的第一气体流。 包含O 2的第二气体气流与第一气体气流一起膨胀以产生进料气体。 在气化条件下，将进料气体引入再生器，以将焦炭从反应器中排出的焦炭废废催化剂中燃烧，产生合成气，并在反应温度下操作反应器。

公开(公告)号：US20090158661A1

公开(公告)日：2009-06-25

申请号：US11962763

申请日：2007-12-21

申请人： Brian W. Hedrick

发明人： Brian W. Hedrick

IPC分类号： C10J3/00 ,  B01J8/00

CPC分类号： C10G11/185 ,  B01J8/1836 ,  B01J8/26 ,  B01J38/12 ,  B01J38/16 ,  B01J38/30 ,  B01J38/36 ,  B01J38/40 ,  B01J38/72 ,  C10G11/182 ,  F01K13/00 ,  Y02E20/344 ,  Y02P30/446

摘要： In at least one embodiment of the present invention, a method of recovering energy from a FCC unit having a reactor and a regenerator for overall CO2 reduction is provided. The method comprises cooling syngas to a predetermined low temperature to define cooled syngas. A turbo-expander including a first compressor is provided. The turbo-expander train is configured to combust and expand gas to drive the first compressor. The cooled syngas is compressed with the first compressor to define compressed syngas. A first stream of gas comprising CO2 and a second stream of gas comprising CO are separated from the compressed syngas. O2 and the first and second streams of gas are introduced to the turbo-expander train. The first stream of gas is expanded and the second stream of gas is combusted and expanded with the O2 to recover energy, driving the first compressor and producing the syngas.

摘要翻译： 在本发明的至少一个实施方案中，提供了一种从具有用于总体CO 2还原的反应器和再生器的FCC装置回收能量的方法。 该方法包括将合成气冷却至预定的低温以限定冷却的合成气。 提供包括第一压缩机的涡轮膨胀机。 涡轮膨胀机列车构造成燃烧和膨胀气体以驱动第一压缩机。 冷却的合成气用第一压缩机压缩以限定压缩的合成气。 包含CO 2的第一气体流和包含CO的第二气体气流与压缩的合成气分离。 O2和第一和第二气体流被引入涡轮膨胀机列车。 第一气体流膨胀，第二气体气体与O2一起燃烧和膨胀以回收能量，驱动第一压缩机并产生合成气。

公开(公告)号：US20080152552A1

公开(公告)日：2008-06-26

申请号：US11643554

申请日：2006-12-21

申请人： Brian W. Hedrick ,  Gavin P. Towler

发明人： Brian W. Hedrick ,  Gavin P. Towler

IPC分类号： F27B15/08

CPC分类号： F27B15/08 ,  B01J8/26 ,  C10G11/02 ,  C10G11/18 ,  Y02P30/446

摘要： Systems and methods of reducing carbon dioxide emissions in a fluid catalytic cracking unit are disclosed. In one example, the method comprises mixing spent catalyst from the reactor and regenerated catalyst from the regenerator to define a catalyst feed. The method further comprises introducing the catalyst feed in the reactor of the unit to react with a reactor feedstock. The catalyst feed has a reactor pass to regenerator pass ratio of between about 5:1 and 15:1 under gasification conditions in the regenerator, thereby reducing carbon dioxide emissions.

摘要翻译： 公开了在流化催化裂化装置中减少二氧化碳排放的系统和方法。 在一个实例中，该方法包括将来自反应器的废催化剂和来自再生器的再生催化剂混合以限定催化剂进料。 该方法还包括将催化剂进料引入单元的反应器中以与反应器原料反应。 催化剂进料在再生器的气化条件下具有通过至约5:1至15:1之间的再生器通过比的反应器，由此减少二氧化碳排放。

公开(公告)号：US07316733B1

公开(公告)日：2008-01-08

申请号：US11040898

申请日：2005-01-21

申请人： Brian W. Hedrick ,  Richard A. Johnson, II ,  Paul A. Sechrist ,  Hadjira Iddir

发明人： Brian W. Hedrick ,  Richard A. Johnson, II ,  Paul A. Sechrist ,  Hadjira Iddir

IPC分类号： B01D45/12

CPC分类号： B01D45/12

摘要： A third stage separator vessel includes a diffuser to promote uniform flow among an array of separation cyclones in the vessel. The vessel has an inlet to receive a gas stream containing solid particles, and the diffuser is mounted at the inlet so that at least some of the stream passes through the diffuser. In an embodiment, a gap between the diffuser and the inlet causes some of the gas stream to flow over an outer surface of the diffuser. The diffuser preferably includes a perforated plate mounted across a wide end of a frustoconical portion. The plate has a plurality of openings through which the flow passes. The openings in the plate have various sizes and positions to direct a greater amount of flow through radially outward portions of the plate than from a central portion of the plate.

摘要翻译： 第三级分离器容器包括扩散器以促进容器中的分离旋风分离器之间的均匀流动。 容器具有用于接收含有固体颗粒的气流的入口，并且扩散器安装在入口处，使得至少一些流通过扩散器。 在一个实施例中，扩散器和入口之间的间隙使得一些气流在扩散器的外表面上流动。 扩散器优选地包括穿过截头圆锥形部分的宽端安装的多孔板。 该板具有多个开口，流过该开口。 板中的开口具有各种尺寸和位置，以引导比板的中心部分更大量的流过板的径向向外的部分。

公开(公告)号：US06797026B2

公开(公告)日：2004-09-28

申请号：US10691266

申请日：2003-10-22

申请人： Paul A. Sechrist ,  Brian W. Hedrick

发明人： Paul A. Sechrist ,  Brian W. Hedrick

IPC分类号： B01D4512

CPC分类号： B04C3/06 ,  B04C3/04 ,  C10G11/182 ,  Y02A50/2327 ,  Y02A50/2354

摘要： A novel cyclone is disclosed that is effective for separating, from a contaminated gas stream, solid particulates having diameters as low as 4 to 5 microns. When multiple cyclones of the present invention are affixed between upper and lower tube sheets in a separator device, fine particle removal is possible to the extent required 1) by stringent regulations governing particulate emissions into the atmosphere, or 2) to prevent damage to turbine blades in downstream power recovery equipment. The cyclones are especially relevant to the problem of removing catalyst fines from refinery effluents, most notably fluid catalytic cracking (FCC) regenerator flue gas. The cyclone separation efficiency is enhanced through the use of 1) a uni-directional flow of gas from the contaminated gas inlet to the clean gas outlet and 2) discharge openings on the surface of the cyclone body that allow ejection of solid particulates.

摘要翻译： 公开了一种新颖的旋风分离器，其有效地从被污染的气流中分离具有低至4至5微米直径的固体微粒。 当本发明的多个旋风分离器固定在分离器装置中的上管板和下管板之间时，可通过严格的规定来控制微粒排放到大气中，或者2）防止损坏涡轮叶片 在下游电力回收设备。 旋风分离器与从炼油厂废水中除去催化剂细粉，特别是流化催化裂化（FCC）再生器烟道气的问题特别相关。 通过使用1）从污染气体入口到清洁气体出口的单向气流，以及2）允许喷射固体颗粒物的旋风体的表面上的排放口，提高了旋风分离效率。