公开(公告)号：US4479809A

公开(公告)日：1984-10-30

申请号：US449110

申请日：1982-12-13

Applicant: Everett M. Johnson ,  Warren G. Schlinger

Inventor： Everett M. Johnson ,  Warren G. Schlinger

IPC: C10J3/84 ,  C10J3/08

CPC classification number: C10J3/84 ,  C10J3/74 ,  C10J3/78 ,  C10J2300/093 ,  C10J2300/1628 ,  Y10S48/02

Abstract: A slag trap structure is for use where synthesis gas is generated having small particulate slag entrained therewith. It has a high pressure shell with a body of water at the bottom for quenching and removing the slag. There is a coaxial inner wall to direct the flow of synthesis gas and slag down from an inlet at the top toward the body of water. And there is an outlet spaced substantially above the level of the water to cause reversal of the gas and slag flow. Also, there is means for recirculating some clean gas in conjunction with the inner wall to direct a swirling flow that confines the downward flow centrally in the vessel.

Abstract translation: 渣捕获结构用于在其中产生具有夹带的小颗粒渣的合成气的情况下。 它具有高压壳体，底部有一个水体，用于淬火和除渣。 有一个同轴的内壁，用于将合成气和渣的流向从顶部的入口向水体向下引导。 并且存在明显高于水平高度的出口以引起气体和渣流的反转。 而且，存在用于将一些清洁气体与内壁一起再循环的装置，以引导将向下的流动中心限制在容器中的旋流。

公开(公告)号：US4158948A

公开(公告)日：1979-06-26

申请号：US934120

申请日：1978-08-16

Applicant: Warren G. Schlinger

Inventor： Warren G. Schlinger

IPC: C10J3/46 ,  C10G1/00 ,  C10G1/06 ,  F02G3/00 ,  C10J3/00

CPC classification number: C10G1/002 ,  Y02E20/16

Abstract: Solid carbonaceous fuels are converted into gaseous fuels by a process comprising liquefying at least a portion of the solid fuel, subjecting a portion of the high boiling product to gasification with substantially pure oxygen to provide hydrogen for the liquefaction, subjecting the balance of the high boiling product to gasification with air to provide a gaseous product used as the stripping medium to remove lighter boiling materials from the liquefaction product and recovering fuel gas from the stripping zone overhead.

Abstract translation: 固体碳质燃料通过包括液化至少一部分固体燃料的方法转化为气体燃料，使一部分高沸点产物用基本上纯的氧气气化以提供用于液化的氢气，使高沸点 产物用空气气化以提供用作汽提介质的气态产物，以从液化产物中除去较轻的沸腾物质并从汽提塔顶部回收燃料气体。

公开(公告)号：US4121912A

公开(公告)日：1978-10-24

申请号：US793008

申请日：1977-05-02

Applicant: Everett M. Barber ,  James R. Muenger ,  David L. Alexander ,  Warren G. Schlinger

Inventor： Everett M. Barber ,  James R. Muenger ,  David L. Alexander ,  Warren G. Schlinger

IPC: C10J3/46 ,  F02C3/20 ,  C10J3/00 ,  C01B2/14 ,  C10J3/16

CPC classification number: F02C3/20 ,  C10J3/485 ,  C10J3/74 ,  C10J3/78 ,  C10J3/84 ,  C10K1/003 ,  C10K1/101 ,  C10K1/16 ,  C10K3/04 ,  C10J2300/092 ,  C10J2300/093 ,  C10J2300/0943 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0976 ,  C10J2300/1671 ,  C10J2300/1675 ,  C10J2300/1807 ,  C10J2300/1846 ,  C10J2300/1884 ,  C10J2300/1892 ,  Y02P20/131

Abstract: Power is developed by an expansion turbine in which the working fluid is a gaseous mixture comprising all of the hot raw gas stream leaving an unpacked partial oxidation gas generator, after removing if present a portion of the entrained solids, in admixture with a temperature moderating stream. A molal increase is associated with the partial oxidation process. Power is obtained from this molal increase in addition to the power obtained from the elevated pressure and sensible heat in the hot raw partial oxidation product gas. The temperature moderating stream may comprise a recycle portion of the turbine exhaust gas stream after being cooled, cleaned, optionally water-gas shifted or purified, or both, and recompressed. Alternatively, the recycle gas stream may be mixed with water, steam, or both. In one embodiment the temperature moderating stream comprises liquid water or condensate produced in the process. Auxiliary gas compressors for recompressing said recycle gas, and optionally for compressing a free-oxygen containing gas for use in the gas generation zone may be driven by said expansion turbine. Similarly, an electric generator may be coupled to the turbine shaft.

Abstract translation: 功率由膨胀涡轮机开发，其中工作流体是气体混合物，其包含离开未包装的部分氧化气体发生器的所有热原料气流，如果存在一部分夹带的固体，则与温度调节流 。 molal增加与部分氧化过程相关。 除了从热原料部分氧化产物气体中的升高的压力和显热产生的功率之外，还可以从该摩尔增加获得功率。 温度调节流可以包括涡轮废气流的再循环部分，在冷却，清洁，任选水煤气转移或净化之后，或两者都被再压缩。 或者，循环气流可以与水，蒸汽或两者混合。 在一个实施方案中，温度调节流包括在该过程中产生的液态水或冷凝物。 用于再压缩所述再循环气体的辅助气体压缩机，并且可选地用于压缩用于气体产生区域的含游离氧气体可以由所述膨胀涡轮机驱动。 类似地，发电机可以联接到涡轮机轴。

公开(公告)号：US4052176A

公开(公告)日：1977-10-04

申请号：US617630

申请日：1975-09-29

Applicant: Edward T. Child ,  Warren G. Schlinger ,  George N. Richter

Inventor： Edward T. Child ,  Warren G. Schlinger ,  George N. Richter

IPC: B01D53/14 ,  C01B3/52 ,  E21B43/16 ,  E21B43/40 ,  B01D53/04

CPC classification number: C01B3/52 ,  B01D53/1406 ,  B01D53/1456 ,  B01D53/1493 ,  E21B43/164 ,  E21B43/40 ,  C01B2203/0415 ,  C01B2203/047 ,  C01B2203/0475 ,  C01B2203/0485 ,  C01B2203/049 ,  Y02C10/06 ,  Y02P90/70

Abstract: A raw synthesis gas feed stream, e.g., gaseous mixtures comprising H.sub.2 and CO and containing gaseous impurities including CO.sub.2, H.sub.2 S, COS, and mixtures thereof (acid gas) and CH.sub.4, optionally in admixture with a CO-rich gas stream produced subsequently in the process, is introduced into a water-gas shift reactor to produce H.sub.2 and CO.sub.2. Acid gases are then removed to produce a stream of purified synthesis gas by contacting the process gas stream with a first liquid solvent absorbent such as methanol, N-methyl-pyrrolidone, or dimethyl ether of polyethylene glycol. An H.sub.2 -rich gas stream may be obtained by removing CO from the purified synthesis gas stream. This may be done by physical absorption in a second liquid solvent absorbent comprising an aqueous solution of cuprous ammonium acetate. By regenerating the second liquid solvent, the aforesaid CO-rich stream may be produced. The first liquid solvent absorbent may be desorbed of said acid gas and regenerated for reuse by such techniques as flashing plus reboiling or stripping. Advantageously, the gas used for stripping the first liquid solvent absorbent may be a portion of the synthesis gas feed either before or after removal of said acid-gas, or a portion of said H.sub.2 -rich product gas. The CO.sub.2 -rich gas optionally in admixture with stripping gas which is produced during the regeneration of said first liquid solvent absorbent may be injected into a subterranean oil reservoir to effect secondary or tertiary recovery of oil. Optionally, H.sub.2 S may be in admixture with said CO.sub.2 -rich gas mixture.

公开(公告)号：US3620700A

公开(公告)日：1971-11-16

申请号：US3620700D

申请日：1969-08-15

Applicant: WARREN G SCHLINGER ,  WILLIAM L SLATER ,  ROGER M DILLE ,  JOSEPH P TASSONEY

Inventor： SCHLINGER WARREN G ,  SLATER WILLIAM L ,  DILLE ROGER M ,  TASSONEY JOSEPH P

IPC: B01D53/34 ,  C01B3/36 ,  C01B3/50 ,  B01D15/00 ,  C01B2/14 ,  C02B1/14

CPC classification number: C01B3/36 ,  B01D53/34 ,  C01B3/50 ,  C01B2203/049

Abstract: Free carbon soot entrained in the product gas of a free-flow synthesis gas generator is recovered in a sedimentation vessel as part of a thickened dispersion of solids in water from which clear supernatant water is easily separated by supplying particulate petroleum coke to the sedimentation vessel or to the reaction zone of said gas generator as a portion of the fuel, or by mixing the carbon soot-water dispersion in the sedimentation vessel with a thickened water slurry of unconverted petroleum coke such as produced by quenching in water the product gas of a second free-flow synthesis gas generator in which the fuel comprises raw particulate petroleum coke and the thickened underflow from said sedimentation vessel.