序号 专利名 申请号 申请日 公开(公告)号 公开(公告)日 发明人
161 Gasification-combined power plant US248426 1994-05-24 US5440873A 1995-08-15 Hiromichi Toda; Shigeyasu Ishigami; Norihisa Kobayashi; Takaaki Furuya; Jun Izumi
The gasification-combined power plant of the present invention has a structure wherein a fuel gas is generated by partially oxidizing a carbon-containing fuel 2 with an oxygen-containing gas 3 in the gasification apparatus 1, the sensible heat of the fuel gas is recovered by the heat exchanger 4, char and dust are removed from the fuel gas by the dust collector 5, trace gas components, such as H.sub.2 S and NH.sub.3, are simultaneously removed from the waste gas by the gas separation apparatus 6 based on dry physical adsorption of these components (for example, by a pressure swing adsorption method), the thus separated and removed gas containing high concentrations of trace gas components, such as H.sub.2 S and NH.sub.3, is denitrated and desulfurized by the gas disposal apparatus 7 and then is discharged from the chimney 13 into the atmosphere. With the simultaneous removal of the trace gas components at a high temperature from the fuel gas produced by the gasification apparatus, this plant simultaneously achieves both a high heat efficiency for the gasification-combined power plant as a whole and the reduction of sulfur oxides and nitrogen oxides in the combustion waste gas from the gas turbine.
162 Process for gasification of coal utilizing reactor protected interally with slag coalescing materials US372806 1989-06-29 US4959080A 1990-09-25 Charles V. Sternling
A process and reaction for the gasification of coal disclosed, the invention being characterized by the provision in each of a plurality of layers of slag coalescing materials on the inner liner of the reactor to provide a protective coating on the wall or walls of the reactor.
163 Process for purifying and cooling a hot gas US220449 1988-07-13 US4874402A 1989-10-17 Jacobus E. Vogel
A process for cooling and cleaning a hot fly ash containing synthesis gas wherein the gas is first passed through a cooler, the bulk of the fly ash being separated from the cooled gas in a cyclone, whereupon the gas is further cleaned in a water scrubber. At least a part of the fly ash/water slurry obtained in the scrubber is injected into the crude synthesis gas and the fly ash particles are agglomerated in the hot crude gas and/or in the slurry by adding a binder, e.g., water glass.
164 High temperature removal of H.sub.2 S from reducing gas US867323 1978-01-05 US4207298A 1980-06-10 Donald C. Erickson
High temperature reducing gas is scrubbed of H.sub.2 S and other gaseous sulfur compounds at high temperature (>800.degree. K.) in a highly efficient regenerative process. The scrubbing is effected in at least two sequential stages. The first stage scrubbing medium is a molten salt comprised essentially of molten alkali carbonates, sulfides, and hydroxides. The second stage is optionally either a metallic melt comprised of copper or a second molten salt. The copper melt is regenerated with air. The salt melts are regenerated with steam and/or CO.sub.2. When two or more salt stages are used, they are regenerated stagewise countercurrently to the scrubbing sequence.
165 Method and apparatus for separating and collecting fine particles in gas with stream of falling molten metal drops US31600372 1972-12-18 US3823530A 1974-07-16 MIYASHITA T; CHAUSSY L
A method and apparatus for separating fine particles such as soot contained in hot gases, in which the gas is passed upward countercurrently to contact with the descending molten metal drops, whereby fine particles contained in the gas are attached to the falling molten metal drops and are thus separated from the gas.
166 Separation of gaseous materials by isothermal expansion in a sub-region of a gas-solid phase region US37134864 1964-06-01 US3324668A 1967-06-13 JOHN LOHRENZ; HASZ JOHN W; DEW JOHN N; BRAY BRUCE G
167 Coke-oven gas by-product recovery US70166633 1933-12-09 US2010003A 1935-08-06 JOSEPH BECKER
168 Recovery of tar acids, etc. US56527031 1931-09-26 US2002704A 1935-05-28 PARMELEE MILLER STUART
169 Process for removing suspended solids and liquids from gases and vapors US39090329 1929-09-07 US1844851A 1932-02-09 HARMON ROBERT R
170 Process and apparatus for cracking oil US42787420 1920-12-02 US1835809A 1931-12-08 POLLOCK ROBERT T
171 Recovery of ammonia and other products from coke oven gases US20636527 1927-07-16 US1826561A 1931-10-06 PARMELEE MILLER STUART
172 Process for fractionation of coke oven gas US27235528 1928-04-23 US1821170A 1931-09-01 RICHARD LINDE
173 Process of treating sulphur bearing gases US23487227 1927-11-21 US1807528A 1931-05-26 HIATT WILLIAM G
174 Gas cleaner US25144128 1928-02-02 US1797906A 1931-03-24 PICKERING DOVEL JAMES
175 Apparatus for the recovery of dry distillation material US11328526 1926-06-02 US1774554A 1930-09-02 LUDWIG HONIGMANN; FRIEDRICH BARTLING
176 Breeze collector US1262125 1925-03-02 US1589375A 1926-06-22 DIETZSCH WILLIAM F
177 Gas equalizer and soot collector for gas producers US51819521 1921-11-28 US1541650A 1925-06-09 MATHESON JAMES H
178 Process of purifying combustible gas US62921323 1923-03-31 US1514889A 1924-11-11 BROWN RALPH L; ODELL WILLIAM W
179 보일러내에서 에너지를 생산하고 배출을 감소시키기 위하여 연료들의 상승적 혼합물을 이용하는 공정 KR1020167005582 2014-07-30 KR1020160096584A 2016-08-16 존스턴,데이비드앤드류; 푸칼러스,린지랜달
주연소공정으로부터의배출물들이포획, (연소쳄버에도달하기이전에이른연소를회피하기위하여)냉각, 압축, 마그네가스와의혼합및 보조연소쳄버내에서재-연소된다.
180 고로가스의 분리방법 KR1020107020239 2009-03-17 KR101244129B1 2013-03-14 나카가와츠구히코; 하라오카타카시; 키시모토아키라; 사이마히토시
고로가스의 분리방법은 고로 노정으로부터 배출되는 고로가스를 2단의 가스분리정제장치를 사용하여 각 성분을 주체로 하는 가스로 분리함에 있어서, 1단째의 가스분리정제장치(S1)에 의해, 고로가스를, 이산화탄소 및 불가피적 불순물 가스 성분으로 이루어지는 가스와, 질소 및 일산화탄소 및 불가피적 불순물 가스 성분으로 이루어지는 가스로 분리하고, 2단째의 가스분리정제장치(S2)에 의해, 상기 1단째의 가스분리정제장치에 의해 분리된, 질소 및 일산화탄소 및 불가피적 불순물 가스 성분으로 이루어지는 가스를, 질소 및 불가피적 불순물 가스 성분으로 이루어지는 가스와, 일산화탄소 및 불가피적 불순물 가스 성분으로 이루어지는 가스로 분리한다.
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