GB737070A - Improvements in the gasification of pulverulent to granular fuels - Google Patents
Improvements in the gasification of pulverulent to granular fuelsInfo
- Publication number
- GB737070A GB737070A GB33457/53A GB3345753A GB737070A GB 737070 A GB737070 A GB 737070A GB 33457/53 A GB33457/53 A GB 33457/53A GB 3345753 A GB3345753 A GB 3345753A GB 737070 A GB737070 A GB 737070A
- Authority
- GB
- United Kingdom
- Prior art keywords
- exothermic
- gasifying agent
- gasifying
- fuel
- pulverulent
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 239000000446 fuel Substances 0.000 title abstract 7
- 238000002309 gasification Methods 0.000 title abstract 4
- 239000003795 chemical substances by application Substances 0.000 abstract 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract 2
- 238000000034 method Methods 0.000 abstract 2
- 229910052760 oxygen Inorganic materials 0.000 abstract 2
- 239000001301 oxygen Substances 0.000 abstract 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 abstract 1
- 239000012159 carrier gas Substances 0.000 abstract 1
- 239000000571 coke Substances 0.000 abstract 1
- 239000000428 dust Substances 0.000 abstract 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/46—Gasification of granular or pulverulent flues in suspension
- C10J3/48—Apparatus; Plants
- C10J3/50—Fuel charging devices
- C10J3/506—Fuel charging devices for entrained flow gasifiers
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
- C10J2300/0913—Carbonaceous raw material
- C10J2300/093—Coal
- C10J2300/0933—Coal fines for producing water gas
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
Abstract
737,070. Gasifying pulverulent fuels. BADISCHE ANILIN- & SODAFABRIK AKT.-GES. Dec. 2, 1953 [Dec. 11, 1952], No. 33457/53. Class 55 (1). In a process of gasifying, in a flame, pulverulent fuels with endothermic and exothermic gasifying agents, the exothermic gasifying agent is divided into two streams before introduction into the gasification chamber, one stream being introduced with or without the endothermic gasifying agent and with a direction of flow parallel to the flow of the fuel, and the other stream alone and with a direction of movement having a component perpendicular to the direction of flow of the fuel and the first stream of exothermic gasifying agent, the size of the two streams of exothermic gasifying agent being adjusted to correspond to the ignition properties of the fuel. As shown in the drawing, pulverulent fuel is introduced in a carrier gas, for example air, through a conduit 1 which is arranged in a gasifying chamber and defines therewith an annular chamber 2 into which is introduced part of the exothermic gasifying agent together with steam or carbon di-oxide. The remainder of the exothermic gasifying agent is introduced through a pipe 3 concentric with conduit 1 and having at its lower end a baffle 4 which deflects the exothermic gasifying agent into the streams entering through 1 and 2. The process is controlled by observation of the wall temperatures of the gasification chamber. In an example, 200 kilograms of coke dust were supplied per hour to the gasification chamber; 40 cubic metres of oxygen and 62 cubic metres of steam were passed in through the annular chamber 2 and 90 cubic metres of oxygen through the central pipe 3.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE737070X | 1952-12-11 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB737070A true GB737070A (en) | 1955-09-21 |
Family
ID=6642484
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB33457/53A Expired GB737070A (en) | 1952-12-11 | 1953-12-02 | Improvements in the gasification of pulverulent to granular fuels |
Country Status (2)
| Country | Link |
|---|---|
| FR (1) | FR1089366A (en) |
| GB (1) | GB737070A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| NL183096C (en) * | 1979-06-13 | 1988-07-18 | Shell Int Research | BURNER FOR THE PARTIAL BURNING OF A FINE DISTRIBUTED OXYGEN FUEL AND MODERATOR GAS. |
| CN106147865B (en) * | 2016-07-19 | 2019-10-01 | 陕西中核交大超洁能源技术有限公司 | The method and apparatus of continuous supercritical water double tube reactor gasification organic matter |
-
1953
- 1953-12-02 GB GB33457/53A patent/GB737070A/en not_active Expired
- 1953-12-11 FR FR1089366D patent/FR1089366A/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| FR1089366A (en) | 1955-03-16 |
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