JPS55120690A - Gasification of solid or liquid fuel - Google Patents
Gasification of solid or liquid fuelInfo
- Publication number
- JPS55120690A JPS55120690A JP2730079A JP2730079A JPS55120690A JP S55120690 A JPS55120690 A JP S55120690A JP 2730079 A JP2730079 A JP 2730079A JP 2730079 A JP2730079 A JP 2730079A JP S55120690 A JPS55120690 A JP S55120690A
- Authority
- JP
- Japan
- Prior art keywords
- solid
- liquid fuel
- gasification
- alkali
- stage
- 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.)
- Pending
Links
- 239000000446 fuel Substances 0.000 title abstract 4
- 239000007788 liquid Substances 0.000 title abstract 3
- 239000007787 solid Substances 0.000 title abstract 3
- 238000002309 gasification Methods 0.000 title abstract 2
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 abstract 3
- 239000003513 alkali Substances 0.000 abstract 2
- 150000002736 metal compounds Chemical class 0.000 abstract 2
- 239000000203 mixture Substances 0.000 abstract 2
- 239000000295 fuel oil Substances 0.000 abstract 1
- 238000010438 heat treatment Methods 0.000 abstract 1
- 239000010742 number 1 fuel oil Substances 0.000 abstract 1
Abstract
PURPOSE: To selectively produce H2 and CO at low temperatures, by adding an alkali (alkaline earth) metal compound to a solid or liquid fuel, and effecting the gasification of the fuel in two separate stages under specific conditions.
CONSTITUTION: To a solid or liquid fuel such as coal or heavy oil, there is added 10W1,000wt% of an alkali (alkaline earth) metal compound such as NaOH or KCl. The resulting mixture is gasified either by continuously raising the temperature of the mixture from 300°CW1,000°C, or by stepwise heating, i.e., from 300 to 600°C and a gas comprising a major proportion of CO is produced in the temperature range in the 1st stage and from 800 to 1,000°C in the 2nd stage. A gas comprising major proportion of H2 is produced in the temperature range of 300W600°C of 800W 1,000°C .
COPYRIGHT: (C)1980,JPO&Japio
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2730079A JPS55120690A (en) | 1979-03-09 | 1979-03-09 | Gasification of solid or liquid fuel |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2730079A JPS55120690A (en) | 1979-03-09 | 1979-03-09 | Gasification of solid or liquid fuel |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS55120690A true JPS55120690A (en) | 1980-09-17 |
Family
ID=12217232
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2730079A Pending JPS55120690A (en) | 1979-03-09 | 1979-03-09 | Gasification of solid or liquid fuel |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS55120690A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4432773A (en) * | 1981-09-14 | 1984-02-21 | Euker Jr Charles A | Fluidized bed catalytic coal gasification process |
US5056019A (en) * | 1989-08-29 | 1991-10-08 | Citicorp Pos Information Servies, Inc. | Automated purchase reward accounting system and method |
US5611963A (en) * | 1993-04-08 | 1997-03-18 | Shell Oil Company | Method of reducing halides in synthesis gas |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4966609A (en) * | 1972-09-08 | 1974-06-27 |
-
1979
- 1979-03-09 JP JP2730079A patent/JPS55120690A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4966609A (en) * | 1972-09-08 | 1974-06-27 |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4432773A (en) * | 1981-09-14 | 1984-02-21 | Euker Jr Charles A | Fluidized bed catalytic coal gasification process |
US5056019A (en) * | 1989-08-29 | 1991-10-08 | Citicorp Pos Information Servies, Inc. | Automated purchase reward accounting system and method |
US5611963A (en) * | 1993-04-08 | 1997-03-18 | Shell Oil Company | Method of reducing halides in synthesis gas |
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