公开(公告)号：US5295350A

公开(公告)日：1994-03-22

申请号：US904635

申请日：1992-06-26

Applicant: Edward T. Child ,  William L. Lafferty, Jr. ,  Robert M. Suggitt ,  Frederick C. Jahnke

Inventor： Edward T. Child ,  William L. Lafferty, Jr. ,  Robert M. Suggitt ,  Frederick C. Jahnke

IPC: F02C3/22 ,  F01K23/06 ,  F02C7/143 ,  F02C7/22 ,  F17C9/04 ,  F02C1/00 ,  F02G3/00

CPC classification number: F25J3/04018 ,  F01K23/068 ,  F17C9/04 ,  F25J3/0403 ,  F25J3/0406 ,  F25J3/04157 ,  F25J3/04545 ,  F25J3/04575 ,  F25J3/04606 ,  F25J3/04618 ,  F17C2205/0326 ,  F17C2221/033 ,  F17C2223/0161 ,  F17C2223/033 ,  F17C2225/0123 ,  F17C2225/036 ,  F17C2227/0135 ,  F17C2227/0316 ,  F17C2227/0323 ,  F17C2227/0332 ,  F17C2227/0339 ,  F17C2227/0393 ,  F17C2265/05 ,  F17C2265/068 ,  F17C2265/07 ,  F25J2210/62 ,  F25J2230/02 ,  F25J2230/04 ,  F25J2270/42 ,  F25J2270/904 ,  Y02E20/18

Abstract: Mechanical and electrical power are produced along with synthesis or fuel gas by the partial oxidation process with integrated combustion and steam turbines. By-product vaporized liquefied natural gas for feed to a pipeline for gas consumers is obtained by heat exchange with heat containing streams from the partial oxidation gasification and gas cleaning and purification zone; and optionally from heat containing streams from combustion and/or steam turbine zones which are integrated with said partial oxidation process. Heat from the combustion turbine exhaust gas is used as follows: (1) superheat steam for use in a steam turbine; (2) preheat water saturated clean sulfur-free synthesis or fuel gas with or without supplemental methane enrichment; (3) preheat oxygen gas for said partial oxidation zone; and (4) vaporize LNG. Pre, inter, and after stages of an air compressor are cooled by indirect heat exchange with LNG which is thereby warmed or vaporized.

Abstract translation: 通过部分氧化过程与综合燃烧和蒸汽轮机一起产生机械和电力以及合成或燃料气体。 通过与来自部分氧化气化和气体净化和净化区的含有热的物流进行热交换，获得副产气化的液化天然气用于供给燃气消耗者的管道的进料; 并且任选地从与所述部分氧化过程相结合的来自燃烧和/或蒸汽涡轮机区域的含热气流中获得。 来自燃气轮机废气的热量如下使用：（1）用于汽轮机的过热蒸汽; （2）预热水饱和干净的无硫合成气或有或没有补充甲烷浓缩的燃气; （3）预热所述部分氧化区的氧气; 和（4）蒸发LNG。 空气压缩机的前，后和后阶段通过与LNG的间接热交换而被冷却，由此被加热或蒸发。

公开(公告)号：US4399314A

公开(公告)日：1983-08-16

申请号：US344333

申请日：1982-02-01

Applicant: Edward T. Child

Inventor： Edward T. Child

IPC: C10G1/00 ,  C10G1/04

CPC classification number: C10G1/002

Abstract: An integrated process for the production of fuels from tar sands in which bitumen is recovered from the tar sand by a hot-water separation step, recovered bitumen is converted in a hydroconversion step to gaseous and liquid fuels, carbonaceous residue from the bitumen conversion step is gasified with oxygen to produce synthesis gas, hot synthesis gas from the gasification step is water washed, hot water from the water wash step provides hot water for the separation step, and synthesis gas from the gasification step provides hydrogen for the bitumen conversion step. Soot recovered from the synthesis gas in the water wash step is transferred to the bitumen in the separation step and ultimately consumed in the process. Water contaminants from the tar sand separation step are largely eliminated in the gasification step.

Abstract translation: 通过热水分离步骤从沥青砂中回收沥青的沥青砂生产燃料的综合方法，回收沥青在加氢转化步骤中转化为气态和液态燃料，沥青转化步骤中的碳质残渣为 用氧气气化生成合成气，气化步骤中的热合成气进行水洗，水洗步骤中的热水为分离步骤提供热水，气化步骤的合成气为沥青转化步骤提供氢气。 在水洗步骤中从合成气中回收的烟灰在分离步骤中转移到沥青中，并最终在该过程中消耗。 来自焦油砂分离步骤的水污染物在气化步骤中大部分被消除。