JPS6475808A - Temperature distribution uniformizing method for fluidized bed type incinerator - Google Patents
Temperature distribution uniformizing method for fluidized bed type incineratorInfo
- Publication number
- JPS6475808A JPS6475808A JP23046187A JP23046187A JPS6475808A JP S6475808 A JPS6475808 A JP S6475808A JP 23046187 A JP23046187 A JP 23046187A JP 23046187 A JP23046187 A JP 23046187A JP S6475808 A JPS6475808 A JP S6475808A
- Authority
- JP
- Japan
- Prior art keywords
- circulation
- grains
- bed
- grain
- grain size
- 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
Landscapes
- Fluidized-Bed Combustion And Resonant Combustion (AREA)
Abstract
PURPOSE:To enable easy and reliable uniformization of temperature distribution in an incinerator vessel, by a method wherein an inactive granular solid is formed with fluidization grains with a relatively large grain size and circulation grains with a small grain size, and the upper part of a free board chamber is allowed to communicate with a bed part through a circulation grain circulating pipe in which a cyclone is situated. CONSTITUTION:A bed 39 is formed to the lower part of an incinerator vessel 35 by means of an inactive granular solid 37 formed by silicon oxide, and forms a fluidized bed. The upper part of a free board chamber 41 is allowed to communicate with a bed 39 part, a circulation grain circulating piping 55 in which a cyclone 53 is situated is provided, and circulation grains are circulated through the circulation grain circulating piping 55. The inactive granular solid 37 by which the bed 39 is formed is composed of fluidization grains with a relatively large size and circulation grains with a small grain size, the grain size of the circulation grain is 50-100mum, and the total weight of the circulation grains amount to 10-15% of a total weight of the fluidization grains per an incinerator floor area.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23046187A JPS6475808A (en) | 1987-09-14 | 1987-09-14 | Temperature distribution uniformizing method for fluidized bed type incinerator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23046187A JPS6475808A (en) | 1987-09-14 | 1987-09-14 | Temperature distribution uniformizing method for fluidized bed type incinerator |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6475808A true JPS6475808A (en) | 1989-03-22 |
Family
ID=16908214
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP23046187A Pending JPS6475808A (en) | 1987-09-14 | 1987-09-14 | Temperature distribution uniformizing method for fluidized bed type incinerator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6475808A (en) |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5257085A (en) * | 1975-10-21 | 1977-05-11 | Battelle Development Corp | Fluidized bed operation method |
JPS54107474A (en) * | 1978-01-12 | 1979-08-23 | Battelle Development Corp | Operation of fluidized bed apparatus |
-
1987
- 1987-09-14 JP JP23046187A patent/JPS6475808A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5257085A (en) * | 1975-10-21 | 1977-05-11 | Battelle Development Corp | Fluidized bed operation method |
JPS54107474A (en) * | 1978-01-12 | 1979-08-23 | Battelle Development Corp | Operation of fluidized bed apparatus |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
ES8802213A1 (en) | Process and fluidised-bed reactor for biological treatment, especially for the treatment of water. | |
ATE91777T1 (en) | BUBBLE LAYER CHAMBER. | |
FI880717A (en) | Swirl Floor System | |
NO851253L (en) | DEVICE AND PROCEDURE FOR INTRODUCING A POWDER WITH CATALYTIC ACTIVITY IN A POLYMERIZATION REACTOR | |
ES8702800A1 (en) | Circulating fluidized bed reactor temperature control | |
DE3368318D1 (en) | Fast fluidized bed boiler | |
IT1150650B (en) | FLUID BED REACTOR | |
GB1482869A (en) | Fluidization apparatus | |
PL310976A1 (en) | Method of and apparatus for circulating solids in a fluidised bed reactor | |
ATE163218T1 (en) | METHOD AND DEVICE FOR GENERATING HEAT IN A FLUIDIZED BED REACTOR | |
ZA904661B (en) | Process and apparatus for regulating or checking the thermal level of a pulverulent solid incorporating a heat exchanger with fluidized bed compartments | |
BR8108766A (en) | DEVICES IN OR RELATING TO FLUIDIZED BEDS | |
CA2158846A1 (en) | Method and apparatus for circulating solid material in a fluidized bed reactor | |
ES415938A1 (en) | Method of and apparatus for fluidizing solid particles | |
HUT61912A (en) | Method and apparatus for generating reaction between a gas and a material consists of solid particles in a closed space | |
EP0181626A3 (en) | Boiler plant for a combustion chamber comprising a plurality of fluid bed stages, and method for its control and regulation | |
JPS6475808A (en) | Temperature distribution uniformizing method for fluidized bed type incinerator | |
ES2108450T3 (en) | PROCEDURE AND APPARATUS FOR PROCESSING BEDDING MATERIAL IN FLUIDIZED BED REACTORS. | |
ES2014629A6 (en) | Controlled discharge from a standpipe containing particulate materials | |
JPS6475809A (en) | Fluidized bed type waste incinerating device | |
JPS5630523A (en) | Fluidized bed type thermal reaction furnace | |
JPS6454104A (en) | Fluidized-bed combustion equipment | |
JPS5347377A (en) | Preventing method for generation of lump at outlet part of feed nozzles for raw materials | |
JPS6446576A (en) | Fluidized bed furnace | |
SU125547A1 (en) | Combined reactor-coke heater for the process of continuous coking of oil residues in the fluidized coke fluid bed |