公开(公告)号：US3980451A

公开(公告)日：1976-09-14

申请号：US570127

申请日：1975-04-21

申请人： Joseph F. McMahon

发明人： Joseph F. McMahon

IPC分类号： C01B3/22 ,  C01B3/36 ,  C10J3/46 ,  C10G13/30

CPC分类号： C10J3/00 ,  C01B3/22 ,  C01B3/36 ,  C10J3/466 ,  C10J3/485 ,  C10J3/721 ,  C10J3/76 ,  C10J3/84 ,  C10J2300/093 ,  C10J2300/0943 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0976 ,  C10J2300/1807 ,  C10J2300/1884 ,  C10J2300/1892

摘要： A process for the gasification of carbonaceous materials to produce a high B.T.U. gaseous product is disclosed. The process includes the partial oxidation of a fluid hydrocarbon to produce a gaseous mixture of carbon monoxide and hydrogen, followed by contacting the gaseous mixture with a relatively cool, finely-divided carbonaceous solid material. The resulting gas-solid mixture is then passed along with a carbonaceous feed into a high velocity transfer line reactor furnace, and the solid material is removed from the gas-solid mixture which emerges from the reactor furnace. The present invention is particularly well suited for the hydrogasification of high boiling, carbon-rich feedstocks such as reduced crude oils.

摘要翻译： 一种用于气化碳质材料以产生高B.T.U.的方法。 公开了气态产物。 该方法包括流体烃的部分氧化以产生一氧化碳和氢气的气体混合物，然后将气体混合物与相对冷却的细碎碳质固体材料接触。 然后将所得气体 - 固体混合物与含碳进料一起通入高速传输线反应器炉中，并将固体物质从从反应器炉出来的气固混合物中除去。 本发明特别适用于高沸点富碳原料如还原原油的加氢气化。

公开(公告)号：US4696679A

公开(公告)日：1987-09-29

申请号：US790675

申请日：1985-10-23

申请人： Marilena Albulescu ,  Joseph F. McMahon

发明人： Marilena Albulescu ,  Joseph F. McMahon

IPC分类号： B03C3/00 ,  B01D50/00 ,  B01D51/00 ,  B01D51/02 ,  B01D51/10 ,  C10J3/02 ,  C10J3/84 ,  C10K1/02 ,  C10K1/04

CPC分类号： C10J3/84 ,  C10J3/02 ,  C10J3/721 ,  C10K1/026 ,  C10K1/028 ,  C10J2300/093 ,  C10J2300/1884

摘要： The present invention cleans gas produced from solid carbonaceous materials in a two stage gas producer. Second stage gas from the gas producer is passed through a first precipitator to remove oil mist and particulates from the second stage gas. First stage gas from the gas producer is passed through a cyclone to remove particulates from the first stage gas. The first stage gas from the cyclone is cooled and then mixed with the second stage gas from the first precipitator. The temperature of the gas mixture is maintained at least at the temperature of the second stage gas. The gas mixture is cooled to a temperature in the range of about 25.degree. F. to about 125.degree. F. above the water dew point of the gas mixture. The cooled gas mixture is subsequently passed through a second precipitator to remove oil mist and particulates from the gas mixture and to yield an industrial usable gas.

摘要翻译： 本发明在两级气体生产者中清洁由固体碳质材料产生的气体。 来自气体生产者的第二级气体通过第一除尘器以除去来自第二级气体的油雾和颗粒。 来自气体生产者的第一级气体通过旋风分离器以除去第一级气体中的微粒。 来自旋风分离器的第一级气体被冷却，然后与来自第一除尘器的第二级气体混合。 气体混合物的温度至少保持在第二级气体的温度。 将气体混合物冷却至高于气体混合物的水露点的约25°F至约125°F的温度。 冷却的气体混合物随后通过第二除尘器以从气体混合物中除去油雾和颗粒并产生工业上可用的气体。

公开(公告)号：US4400309A

公开(公告)日：1983-08-23

申请号：US330540

申请日：1981-12-14

申请人： Joseph F. McMahon ,  Peter Steiner

发明人： Joseph F. McMahon ,  Peter Steiner

IPC分类号： C10G11/20 ,  B01J12/00 ,  B01J23/755 ,  B01J35/02 ,  C01B3/38 ,  C01B3/40 ,  D05B19/00 ,  B01J23/74

CPC分类号： C01B3/40 ,  B01J12/007 ,  B01J19/2425 ,  B01J23/755 ,  B01J35/02 ,  C01B3/38 ,  C01B3/384 ,  D05B19/00 ,  B01J2219/00094 ,  B01J2219/30284 ,  C01B2203/0233 ,  C01B2203/085 ,  C01B2203/1052 ,  C01B2203/1241 ,  C01B2203/1247 ,  C01B2203/127 ,  C01B2203/1619 ,  C01B2203/1623 ,  C01B2203/1628 ,  C01B2203/169 ,  Y02P20/52

摘要： A catalyst is provided for reforming hydrocarbon with steam, comprising a nickel containing catalyst in the form of an activated elongated strip.

摘要翻译： 提供催化剂用于用蒸汽重整烃，包括活化的细长条形式的含镍催化剂。

公开(公告)号：US4119349A

公开(公告)日：1978-10-10

申请号：US844629

申请日：1977-10-25

申请人： Peter Albulescu ,  Joseph F. McMahon

发明人： Peter Albulescu ,  Joseph F. McMahon

IPC分类号： E21B43/247 ,  E21B43/34 ,  E21C41/24 ,  E21B43/24 ,  E21C41/10

CPC分类号： E21B43/247 ,  E21B43/34 ,  E21C41/24

摘要： Gaseous and liquid products discharged from the outlet of an in-situ retort for the retorting of oil shale are delivered into an underground separating chamber located substantially at the level of the bottom of the retort. The lower portion of the separating chamber is divided by a weir into a first sump adjacent the inlet end of the separating chamber and a second sump adjacent the outlet end of the separating chamber. Oil and water separate in the first sump and the oil overflows the weir into the second sump. Water is withdrawn at a level below the oil in the first sump and pumped to the surface. Oil is withdrawn from the second sump and pumped to the surface separately from the water.

摘要翻译： 从用于蒸馏油页岩的原位蒸馏出口排出的气体和液体产物被输送到基本上位于蒸馏器底部水平面的地下分离室。 分离室的下部被堰分隔成邻近分离室的入口端的第一贮槽和邻近分离室的出口端的第二贮槽。 油和水在第一个贮槽中分离，油溢出堰进入第二个贮槽。 水在第一个贮槽中的油位以下被抽出并泵送到表面。 油从第二个贮槽中抽出并与水分开泵送到地面。