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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