公开(公告)号：US20120152058A1

公开(公告)日：2012-06-21

申请号：US13404835

申请日：2012-02-24

申请人： Peter Joel Meschter ,  Paul Stephen Dimascio

发明人： Peter Joel Meschter ,  Paul Stephen Dimascio

IPC分类号： C22B7/04

CPC分类号： C10L9/10 ,  C10J3/57 ,  C10J2200/09 ,  C10J2300/09 ,  C10J2300/0916 ,  C10J2300/093 ,  C10J2300/0943 ,  C10J2300/0983 ,  C10L5/00 ,  C10L5/366 ,  C10L10/04 ,  Y02P20/145

摘要： Embodiments disclosed herein provide hydrocarbon additives and methods of making and using the same. The additives are suitable for use in conjunction with gasifiers, furnaces, or other high-temperature vessels. The additives may be part of an input stream to a reaction vessel of a hydrocarbon gasifier. The additives may include materials that at least partially reduce the infiltration of slag into the refractory material.

摘要翻译： 本文公开的实施方案提供烃添加剂及其制备和使用方法。 这些添加剂适用于与气化炉，熔炉或其他高温容器结合使用。 添加剂可以是到烃类气化器的反应容器的输入流的一部分。 添加剂可以包括至少部分地减少熔渣渗透到耐火材料中的材料。

公开(公告)号：US07575612B2

公开(公告)日：2009-08-18

申请号：US11263270

申请日：2005-10-31

申请人： Paul Steven Wallace

发明人： Paul Steven Wallace

IPC分类号： B01J8/00

CPC分类号： B01J4/001 ,  B01J4/002 ,  B01J19/26 ,  B01J2219/00119 ,  C10J3/485 ,  C10J3/506 ,  C10J2200/152 ,  C10J2300/09 ,  C10J2300/093 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0973 ,  C10J2300/1606 ,  C10J2300/165 ,  C10J2300/1668 ,  C10J2300/1675 ,  C10J2300/1678 ,  Y02E20/18

摘要： Methods and systems for decomposing ammonia in a gasifier are provided. The system includes a gasifier including a pressure vessel and an injection nozzle extending through the pressure vessel and including a nozzle tip at a distal end of the injection nozzle, the injection nozzle further includes a passage configured to direct a fluid stream including ammonia proximate the nozzle tip such that the fluid stream including ammonia facilitates reducing a temperature of at least a portion of the nozzle tip.

摘要翻译： 提供了在气化器中分解氨的方法和系统。 该系统包括气化器，其包括压力容器和延伸穿过压力容器并且在喷嘴的远端处包括喷嘴尖端的喷嘴，喷嘴还包括通道，该通道构造成在喷嘴附近引导包括氨的流体流 使得包括氨的流体流有助于降低喷嘴尖端的至少一部分的温度。

公开(公告)号：US20050124842A1

公开(公告)日：2005-06-09

申请号：US10498700

申请日：2002-12-10

申请人： Jacques Paris ,  Jean-Raymond Costes

发明人： Jacques Paris ,  Jean-Raymond Costes

IPC分类号： B01J19/08 ,  B02C19/18 ,  B09B5/00 ,  C10J3/18 ,  G21F9/30 ,  G21F9/00

CPC分类号： C10J3/723 ,  B02C19/18 ,  B02C2019/183 ,  C10J3/18 ,  C10J2200/12 ,  C10J2200/33 ,  C10J2300/09 ,  G21F9/30 ,  G21Y2004/60

摘要： A process for the treatment of a nuclear graphite contaminated with radioelements includes subjecting the graphite, immersed in a medium containing water, to high-voltage pulses. The pulses have sufficient energy for electric arcs to be initiated and to break the constituent bonds of the water molecules and the carbon-carbon bonds of the graphite. The number of high-voltage pulses is determined so as to convert the graphite into gas.

摘要翻译： 用于处理被放射性元素污染的核石墨的方法包括将浸入含水介质的石墨进行高压脉冲。 脉冲具有足够的能量来启动电弧并破坏水分子的组成键和石墨的碳 - 碳键。 确定高压脉冲的数量以将石墨转化为气体。

公开(公告)号：US20040045272A1

公开(公告)日：2004-03-11

申请号：US10451727

申请日：2003-06-25

发明人： Norihisa Miyoshi ,  Seiichiro Toyoda ,  Kei Matsuoka

IPC分类号： F02C003/28

CPC分类号： C10J3/56 ,  C10J3/463 ,  C10J2300/09 ,  C10J2300/0916 ,  C10J2300/093 ,  C10J2300/0973 ,  C10J2300/0993 ,  C10J2300/165 ,  C10J2300/1687 ,  C10J2300/1838 ,  C10J2300/1853 ,  F01K23/067 ,  F23C10/12 ,  F23C2206/00 ,  F23G5/027 ,  F23G5/30 ,  F23G2203/503 ,  Y02E20/12 ,  Y02E20/16 ,  Y02E20/18 ,  Y02P20/129

摘要： The present invention relates to a method and apparatus for effectively utilizing thermal energy possessed by a high-temperature combustion gas discharged from a combustor and utilizing high-temperature oxygen contained in the high-temperature combustion gas discharged from the combustor. A fluidized-bed gasification apparatus for gasifying combustibles in a fluidized-bed furnace comprises a gasification furnace (2) for gasifying combustibles therein, and a combustion furnace (1) for combusting combustible components therein. The fluidized medium moves between the gasification furnace (2) and the combustion furnace (1), and exhaust gas discharged from another combustor is utilized as a fluidizing gas in the combustion furnace (1).

摘要翻译： 本发明涉及一种有效利用由燃烧器排出的高温燃烧气体所具有的热能并利用从燃烧器排出的高温燃烧气体中所含的高温氧的方法和装置。 用于在流化床炉中气化可燃物的流化床气化装置包括用于气化可燃物的气化炉（2）和用于在其中燃烧可燃组分的燃烧炉（1）。 流化介质在气化炉（2）和燃烧炉（1）之间移动，从另一个燃烧器排出的排气用作燃烧炉（1）中的流化气体。

公开(公告)号：US08333951B2

公开(公告)日：2012-12-18

申请号：US12311919

申请日：2007-10-16

申请人： Heinz-Juergen Muehlen

发明人： Heinz-Juergen Muehlen

IPC分类号： C01B3/26

CPC分类号： C10B47/44 ,  C10J3/12 ,  C10J3/14 ,  C10J3/66 ,  C10J2300/09 ,  C10J2300/0916 ,  C10J2300/0993 ,  Y02E50/14 ,  Y02P20/129 ,  Y02P20/145

摘要： A method produces a product gas rich in hydrogen. A starting material including carbon is split via pyrolysis, and the resulting gas is mixed with water vapor to increase the hydrogen content and heated. The heat necessary comes from the combustion of the produced pyrolysis coke. The heat necessary for individual process steps is fed via a heat transfer medium circuit having a heating zone heated via flue gas from the pyrolysis coke firing. The gas/water vapor mixture is subsequently heated in a reaction zone. The heat transfer medium heats the starting material in a pyrolysis zone indirectly, without directly contacting the starting material, is cooled in a cooling zone, and subsequently returns to the beginning of the circuit. Upstream of the heating zone, the heat transfer medium is preheated via the hot product gas.

摘要翻译： 一种方法产生富含氢的产物气体。 通过热解将包含碳的原料分解，并将所得气体与水蒸汽混合以增加氢含量并加热。 所需的热量来自所生产的热解焦炭的燃烧。 单个工艺步骤所需的热量通过具有通过烟道气从热解焦炭燃烧加热的加热区域的传热介质回路进料。 随后在反应区中加热气/水蒸气混合物。 传热介质在热解区内间接加热起始材料，而不直接接触原料，在冷却区中冷却，然后返回到回路的开头。 在加热区的上游，传热介质通过热产物气体预热。

公开(公告)号：US20090249691A1

公开(公告)日：2009-10-08

申请号：US11883442

申请日：2006-02-01

申请人： Toru Akiyama ,  Fumihiko Kiso ,  Shinji Tanaka ,  Hirofumi Okazaki ,  Fumihiko Hanayama ,  Kazunori Sato ,  Takahiro Nishida ,  Hiroshi Takezaki ,  Akio Ueda ,  Makoto Takeda

发明人： Toru Akiyama ,  Fumihiko Kiso ,  Shinji Tanaka ,  Hirofumi Okazaki ,  Fumihiko Hanayama ,  Kazunori Sato ,  Takahiro Nishida ,  Hiroshi Takezaki ,  Akio Ueda ,  Makoto Takeda

IPC分类号： C10J3/06 ,  C10J3/20

CPC分类号： F23G5/02 ,  C10J3/487 ,  C10J3/506 ,  C10J2200/15 ,  C10J2300/09 ,  C10J2300/0903 ,  C10J2300/0909 ,  C10J2300/093 ,  C10J2300/1807 ,  F23G2201/301 ,  F23G2201/40 ,  F23G2201/80

摘要： Apparatus for gasifying a solid fuel that supplies a solid fuel such as coal by dry condition to a gasification furnace of an entrained-bed type is constructed so as to be able to collect the char discharged from the gasification furnace and re-supply the char to the furnace without using a lock hopper and without changing the char into slurry form.The char discharged from the gasification furnace along with produced gases 53 produced in the gasification furnace is brought into contact with water by a gas cooler 9 and collected. After being dehydrated by a dehydrator 10, the collected char is loaded into a mill 2 or a raw-coal bunker 1. For loading into the raw-coal bunker 1, the char is dried by a drying machine 14, preferably, after the dehydration.According to the present invention, a mixture of the collected char and water can be re-supplied to the gasification furnace without using a lock hopper or a dry feeder. After being dehydrated, the char preferably is further dried and then supplied to the gasification furnace. Since a great deal of moisture is not supplied to the inside of the gasification furnace, it is possible to prevent a temperature of the gasification furnace from decreasing, and thus improve gas conversion efficiency.

摘要翻译： 将通过干燥状态将固体燃料例如煤供给到固定床型的气化炉的固体燃料的装置被构造成能够收集从气化炉排出的炭并将炭再供给 炉子不使用封闭料斗，而不改变焦炭成浆状。 从气化炉排出的焦炭以及在气化炉中产生的生成气体53通过气体冷却器9与水接触并收集。 在脱水机10脱水后，收集的炭被装载到磨机2或原煤仓1中。为了装载到原煤仓1中，优选用干燥机14干燥焦炭，脱水后 。 根据本发明，可以将收集的炭和水的混合物重新供给气化炉，而不使用锁定料斗或干式进料器。 脱水后，优选进一步干燥，然后供给到气化炉。 由于不向气化炉内部供给大量的水分，因此能够防止气化炉的温度下降，从而提高气体转换效率。

公开(公告)号：US20090217588A1

公开(公告)日：2009-09-03

申请号：US12395372

申请日：2009-02-27

申请人： Edwin J. Hippo ,  Pattabhi K. Raman

发明人： Edwin J. Hippo ,  Pattabhi K. Raman

IPC分类号： C10L3/00

CPC分类号： C10J3/00 ,  C10J2300/09 ,  C10J2300/0916 ,  C10J2300/093 ,  C10J2300/0983 ,  C10J2300/0986 ,  Y02P20/145

摘要： Continuous processes are provided for converting a carbonaceous feedstock comprising biomass containing alkali metal, non-biomass components, and at least one gasification catalyst including an alkali metal recovered from solid char, into a plurality of gaseous products including methane and at least one or more of hydrogen, carbon monoxide, and other higher hydrocarbons.

摘要翻译： 提供了连续方法，用于将包含含有碱金属，非生物质组分的生物质的碳质原料和包含从固体炭回收的碱金属的至少一种气化催化剂转化为多种气态产物，包括甲烷和至少一种或多种 氢，一氧化碳和其他高级烃。

公开(公告)号：US07456226B2

公开(公告)日：2008-11-25

申请号：US10582699

申请日：2004-12-13

申请人： Norbert Topf ,  Guenter Liebisch

发明人： Norbert Topf ,  Guenter Liebisch

IPC分类号： C07C27/00

CPC分类号： C10J3/482 ,  C10J3/06 ,  C10J3/54 ,  C10J2300/09 ,  C10J2300/0909 ,  C10J2300/0973 ,  C10J2300/1284 ,  C10J2300/16 ,  C10J2300/1637 ,  C10J2300/1659 ,  C10J2300/1665 ,  C10J2300/1671 ,  C10J2300/1684 ,  C10J2300/1884 ,  C25B1/04 ,  C25B15/08 ,  Y02E60/366 ,  Y02P20/129

摘要： The invention relates to a method and installation for producing liquid energy carriers from a solid carbon carrier by means of gasifying a solid carbon carrier. The installation is at least comprised of a drying device, a gasification apparatus, a synthesizing device for synthesizing the liquid energy carrier, a device for effecting the electrolysis of water for producing oxygen serving as a gasification agent and hydrogen for the synthesis process, and of a combustion apparatus, which is connected to the output of the gasification apparatus for carbon-containing gasification residues and to the oxygen outlet of the device for effecting the electrolysis of water. According to the invention, at least a portion of the waste steam from the drying device and at least a portion of the residual gas arising during synthesis are fed to the gasification process in the gasification apparatus. In addition, the carbon-containing residuals from the gasification apparatus and a portion of the oxygen produced in the device for effecting the electrolysis of water can be fed to a combustion apparatus, and the carbon dioxide-containing and oxygen-containing waste gas from the combustion apparatus can be fed to the combustion apparatus in the form of a gasification agent.

摘要翻译： 本发明涉及一种通过气化固体碳载体从固体碳载体生产液体能量载体的方​​法和装置。 该装置至少包括干燥装置，气化装置，用于合成液体能量载体的合成装置，用于产生用作气化剂的氧的电解电解和用于合成过程的氢的装置，以及 燃烧装置，其连接到用于含碳气化残渣的气化装置的输出端和用于进行电解的装置的氧气出口。 根据本发明，来自干燥装置的废蒸汽的至少一部分和合成期间产生的至少一部分残留气体被供给到气化装置中的气化过程。 此外，来自气化装置的含碳残渣和用于实现水的电解的装置中产生的一部分氧气可以被供给到燃烧装置，并且来自所述二氧化碳的含氧废气 燃烧装置可以以气化剂的形式供给到燃烧装置。

公开(公告)号：US06585884B1

公开(公告)日：2003-07-01

申请号：US10272709

申请日：2002-10-17

申请人： Warden W. Mayes, Jr.

发明人： Warden W. Mayes, Jr.

IPC分类号： B01J3820

CPC分类号： C10J3/482 ,  B01J8/26 ,  B01J29/90 ,  B01J38/34 ,  B01J38/40 ,  B01J2219/0004 ,  C10G11/182 ,  C10J3/54 ,  C10J3/56 ,  C10J2300/09 ,  C10J2300/0943 ,  C10J2300/0959 ,  C10J2300/0973 ,  C10J2300/0983 ,  C10J2300/16 ,  Y02P20/52 ,  Y02P20/584 ,  Y02P30/446

摘要： The present invention provides a method of producing a synthesis gas from a regeneration of spent cracking catalyst. The method includes introducing a spent cracking catalyst into a first regeneration zone in a presence of a first oxygen and carbon dioxide atmosphere and at a first regeneration temperature. For example, a temperature that does not exceed about 1400° F., and more preferable a temperature that ranges from about 1150° F. to about 1400° F., may be used as the first regeneration temperature. The method further includes introducing the spent cracking catalyst from the first regeneration zone into a second regeneration zone in a presence of a second oxygen and carbon dioxide atmosphere, and producing a synthesis gas from cracking deposits located on the spent cracking catalyst within the second regeneration zone at a second regeneration temperature substantially greater than said first regeneration temperature. In a preferred embodiment, the second regeneration temperature ranges from about 1500° F. to about 1800°, and in a related embodiment is about 1800° F.

公开(公告)号：US06491810B1

公开(公告)日：2002-12-10

申请号：US09704085

申请日：2000-11-01

申请人： Warden W. Mayes, Jr.

发明人： Warden W. Mayes, Jr.

IPC分类号： B01J3820

CPC分类号： C10J3/482 ,  B01J8/26 ,  B01J29/90 ,  B01J38/34 ,  B01J38/40 ,  B01J2219/0004 ,  C10G11/182 ,  C10J3/54 ,  C10J3/56 ,  C10J2300/09 ,  C10J2300/0943 ,  C10J2300/0959 ,  C10J2300/0973 ,  C10J2300/0983 ,  C10J2300/16 ,  Y02P20/52 ,  Y02P20/584 ,  Y02P30/446

摘要： The present invention provides a method of producing a synthesis gas from a regeneration of spent cracking catalyst. The method includes introducing a spent cracking catalyst into a first regeneration zone in a presence of a first oxygen and carbon dioxide atmosphere and at a first regeneration temperature. For example, a temperature that does not exceed about 1400° F., and more preferable a temperature that ranges from about 1150° F. to about 1400° F., may be used as the first regeneration temperature. The method further includes introducing the spent cracking catalyst from the first regeneration zone into a second regeneration zone in a presence of a second oxygen and carbon dioxide atmosphere, and producing a synthesis gas from cracking deposits located on the spent cracking catalyst within the second regeneration zone at a second regeneration temperature substantially greater than said first regeneration temperature. In a preferred embodiment, the second regeneration temperature ranges from about 1500° F. to about 1800°, and in a related embodiment is about 1800° F.

摘要翻译： 本发明提供从废裂化催化剂的再生生产合成气的方法。 该方法包括在第一氧气和二氧化碳气氛的存在下并在第一再生温度下将废裂化催化剂引入第一再生区。 例如，可以使用不超过约1400°F的温度，更优选约1150°F至约1400°F范围内的温度作为第一再生温度。 该方法还包括在第二氧气和二氧化碳气氛的存在下将废裂化催化剂从第一再生区引入第二再生区，以及由位于第二再生区内的废裂化催化剂上的裂解沉积物产生合成气 在基本上大于所述第一再生温度的第二再生温度下。 在优选的实施方案中，第二再生温度范围为约1500°F至约1800°，在相关实施方案中为约1800°F