CN209416084U - Chemical catalyst calcining and decomposition gas burn all-in-one oven - Google Patents
Chemical catalyst calcining and decomposition gas burn all-in-one oven Download PDFInfo
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- CN209416084U CN209416084U CN201920014584.6U CN201920014584U CN209416084U CN 209416084 U CN209416084 U CN 209416084U CN 201920014584 U CN201920014584 U CN 201920014584U CN 209416084 U CN209416084 U CN 209416084U
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- decomposition gas
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- 238000000354 decomposition reaction Methods 0.000 title claims abstract description 37
- 238000001354 calcination Methods 0.000 title claims abstract description 29
- 239000003054 catalyst Substances 0.000 title claims abstract description 16
- 239000000126 substance Substances 0.000 title claims abstract description 11
- 238000010438 heat treatment Methods 0.000 claims abstract description 16
- 239000000779 smoke Substances 0.000 claims abstract description 14
- 239000000463 material Substances 0.000 claims abstract description 13
- 230000004913 activation Effects 0.000 claims abstract description 11
- 238000007599 discharging Methods 0.000 claims abstract description 6
- 239000007789 gas Substances 0.000 claims description 53
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 13
- 239000003546 flue gas Substances 0.000 claims description 13
- 238000001816 cooling Methods 0.000 claims description 10
- 238000004519 manufacturing process Methods 0.000 claims description 10
- 239000000919 ceramic Substances 0.000 claims description 4
- 238000002485 combustion reaction Methods 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims description 3
- 239000000567 combustion gas Substances 0.000 claims 1
- 230000008901 benefit Effects 0.000 abstract description 6
- 238000000034 method Methods 0.000 description 3
- 241000264877 Hippospongia communis Species 0.000 description 2
- 230000003213 activating effect Effects 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000010304 firing Methods 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 210000000038 chest Anatomy 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000007405 data analysis Methods 0.000 description 1
- 238000012938 design process Methods 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 238000005338 heat storage Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 150000002632 lipids Chemical class 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000012802 pre-warming Methods 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 210000000952 spleen Anatomy 0.000 description 1
- 238000013022 venting Methods 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Abstract
The utility model discloses a kind of calcining of chemical catalyst and decompose gas burning all-in-one oven, it solves the prior art and there is the problems such as taking up a large area, equipment investment is high, it is characterized by: decomposing the row of being provided at the top of section (2) in heating decomposes feed channel (7) and row decomposition gas blower (6), decomposition gas Burning Room (16) are additionally arranged below the device for transporting objects of calcining at constant temperature activation section (3), it is provided on Burning Room (16) and decomposes gas branch pipe, feed channel (8) are decomposed by conveying and are connected with row's decomposition gas blower (6) outlet mouth of pipe；Burning Room discharge flue (11) are provided with below the material transmitting device that preheating section (1) and heating decompose section (2), and are provided with smoke discharging pipe (10) in preheating section (1), which is connected with the smoke exhaust fan (9) for being mounted on furnace roof.Have many advantages, such as structurally reasonable, easy to operate, energy-saving and emission-reduction, there is good Social benefit and economic benefit.
Description
Technical field:
The utility model belongs to Thermal Equipment, and gas is calcined and decomposed particularly with regard to a kind of chemical catalyst and burns one
Body furnace.
Background technique:
The mature equipment that the chemical catalyst calcining furnace of domestic manufacturer's production at present uses has: tunnel oven, shuttle kiln, roller-way
Kiln, mesh-belt kiln etc..Need to add a large amount of organic lipids or various salt in chemical catalyst forming process, it is dry in catalyst
Discharge must be decomposed during calcining and activating, these tail gas are again extremely serious to the pollution of environment, in general factory at this stage
Family requires to spend high cost installation tail gas treatment device.Decomposing gas disposal generally uses spray-absorption, burning disposal, desulfurization de-
Nitre tower processing etc..I.e. catalyst calcination when, be divided into calciner and tail gas treatment device match, that there are equipment investments is big,
The problems such as occupied area is more, energy consumption is high, environmental pollution weight.
Summary of the invention:
The purpose of this utility model is to provide a kind of structurally reasonable, production simply, saves the energy, reduces investment, saving
Land used protects the chemical catalyst calcining of environment and decomposition gas to burn all-in-one oven.
The technical solution of the utility model is: it includes decomposing section, calcining at constant temperature activation section, cooling by preheating section, heating
The furnace body and device for transporting objects and be made of burner, gas pipeline, combustion-supporting air piping and combustion fan that cooling section is constituted
The composition such as burner decomposes the row of being provided at the top of section in heating and decomposes feed channel and row's decomposition gas blower, arranges decomposition gas blower
Air inlet mouth of pipe by row decompose feed channel with heating decomposition section burner hearth communicate.In the device for transporting objects of calcining at constant temperature activation section
Lower section is additionally arranged decomposition gas Burning Room, is provided on Burning Room and decomposes gas branch pipe, decomposes feed channel and row's decomposition gas by conveying
Blower outlet mouth of pipe is connected.The indoor residence time is being burned in order to improve incineration flue gas, ceramic honey comb is equipped in Burning Room
The flue gas residence wall of heat storage production.Burning Room is provided with below the material transmitting device that preheating section and heating decompose section to discharge fume
Channel, and it is provided with smoke discharging pipe in preheating section, which is connected with the smoke exhaust fan for being mounted on furnace roof.
The utility model has the beneficial effects that: due to being additionally arranged decomposition gas Burning Room in furnace body calcining at constant temperature activation section,
Calcining and decomposing gas is directly carried out to burning disposal meet the requirement of environmental protection, UTILIZATION OF VESIDUAL HEAT IN outlet again in calcining furnace, greatlys save and accounts for
Ground, energy consumption and equipment investment.With structurally reasonable, production is simple, the saving energy, reduces and invests, saves the area, protects environment etc.
Advantage, incineration flue gas utilization rate are up to 80~90%, compared with the energy that traditional handicraft and equipment have saved 35% or so, have good
Social benefit and economic benefit, market prospects are very wide.
The utility model is described in further detail with reference to the accompanying drawing.
Detailed description of the invention:
Fig. 1 is the utility model principle schematic diagram；
Fig. 2 is the utility model schematic view of the front view.
In figure: 1 is preheating section, and 2 decompose section for heating, and 3 be calcining at constant temperature activation section, and 4 be cooling down section, and 5 be material
Conveying device, 6 be row's decomposition gas blower, and 7 decompose feed channel for row, and 8 decompose feed channel for conveying, and 9 be smoke exhaust fan, and 10 be row
Smoke pipeline, 11 be Burning Room discharge flue, and 12 be gas pipeline, and 13 be combustion-supporting air piping, and 14 be combustion fan, and 15 be burner,
16 be Burning Room.
Specific embodiment:
As shown in Figure 1, chemical catalyst calcining and decompose gas burn all-in-one oven be by preheating section 1, heating decompose section 2,
Calcining at constant temperature activation section 3, cooling down section 4 constitute furnace body and device for transporting objects 5 and by burner 15, gas pipeline 12,
The compositions such as the burner that combustion-supporting air piping 13 and combustion fan 14 are constituted decompose the row's of being provided with decomposition gas at the top of section 2 in heating
The air inlet mouth of pipe of pipeline 7 and row's decomposition gas blower 6, row's decomposition gas blower 6 decomposes feed channel 7 by row and 2 furnace of section is decomposed in heating
Thorax communicates.It is additionally arranged decomposition gas Burning Room 16 below the device for transporting objects of calcining at constant temperature activation section 3, is arranged on Burning Room 16
Decomposition gas branch pipe decomposes feed channel 8 by conveying and is connected with decomposition gas blower 6 outlet mouth of pipe is arranged.In preheating section 1 and heating point
It solves and is provided with Burning Room discharge flue 11 below the material transmitting device of section 2, and be provided with smoke discharging pipe 10 in preheating section 1, it should
Smoke discharging pipe 10 is connected with the smoke exhaust fan 9 for being mounted on furnace roof.
When implementing the utility model, by taking 62m muffle mesh-belt kiln as an example: expanding in the calcining at constant temperature activation section 3 of mesh-belt kiln and increase
If Burning Room 16, it will heat up to decompose by air-introduced machine 6 and be burned in section decomposition gas feeding Burning Room 16, general organic matter incineration temperature
At 500~600 DEG C, salt or other oxides need 800~900 DEG C of burnings, and chemical catalyst calcination temperature generally exists
500~700 DEG C.Therefore it is distinguished in the design process according to different product different decomposition object, when incineration temperature is higher than calcining temperature
The thickness and material of flame isolation layer are considered when spending；When burning required temperature and being lower than calcination temperature, directly improving incineration temperature makes point
Burning of venting one's spleen is faster more abundant.Flue gas after burning can be discharged out of the furnace by bottom flue gas passage in burner preheating section, flue gas
To material bed carry out radiant heating in bottom flue gas passage 11.
Its process is:
(1) calcining and activating furnace is heated up to decompose product in section 2 and heat up 200~250 DEG C of decomposed tail gas and contain organic compounds pumping
It is sent out to burning in Burning Room 16；
(2) decomposition gas organic exhaust gas burns the heat supply calcining at constant temperature activation section 3 generated and uses, and calcining required temperature is
600 DEG C or so；Improve incineration temperature when heat is inadequate, when heat superelevation adds muffle heat preservation, makes to calcine section moderate temperature；
(3) honeycomb ceramic heat accumulator is added in Burning Room 16, is burning the indoor residence time to improve incineration flue gas,
It is burned to achieve the effect that improve decomposition gas；
(4) 200 DEG C or so low-temperature flue gas are discharged out of the furnace from low-temperature prewarming section 1 by smoke exhaust fan 9.
Catalyst decomposition product Correlative data analysis is provided by owner, decomposition product warp >=850 DEG C can reach after high temperature incineration
National environmental standard, design catalyst decompose feeding burner hearth after gas is extracted out by blower and make burning disposal.It is decomposed in view of burning
The temperature of gas is higher than production temperature, special to have been moved off material furnace zone with the kiln and make exhaust gas incineration area, i.e. kiln 49m
It is set as decomposing gas incineration section to 53m, because material calcining area (traditional kiln is cooling section herein) has been left in this region,
Influence of the temperature to material can accomplish the firing and cooling that do not influence material by scientific selection and reasonable masonry construction.
The decomposition gas burn down mode is better than free-standing flue gas incineration furnace, because of the decomposition gas incineration section and production burner hearth
It is not only to have connected together but also relatively independent organism, the high-temperature gas generated when burning and decomposing gas is to walk roaster hearth warp
Smoke exhaust fan discharge, therefore its utilization rate of waste heat is greatly improved (utilization rate up to 85%~95%), and free-standing flue gas burns
The waste heat of furnace is often directly emptied, and heat utilization efficiency and environment protecting are also unsatisfactory.
The kiln 49m to 53m is used as by the decomposition gas incineration section decomposes gas incineration area, will with two high-power burners
The temperature of area jian be raised to >=850 DEG C for burn decompose gas, for make decompose gas be heated more evenly in the area, jian uses bee
Nest ceramics have made 7 flue gas residence walls, and decomposition gas is made to be appropriately extended by the time of high temperature incineration and burn more equal
It is even.
Incineration temperature due to decomposing gas is higher than production temperature and is herein cooling section by original design, in order to
The cooling of material is not influenced, the design selects the covering thermal insulation layer of quality refractory thermal insulation board work decomposition gas incineration section in this section,
And cooling air hose is added in kiln tail, make material reaches original design temperature from kiln temperature degree.
2000~8000m3/h of waste gas decomposition is generated when calcined catalyst on an hourly basis as reference, because of the larger warp of its air quantity
Be afraid of effectively be digested by burner hearth and influence firing temperature when crossing burner hearth, therefore be provided with what past burner hearth leaked out at kiln 49m
Control valve, and the resisting blower of the extra air quantity of extraction, when production, are comprehensively utilized the two to balance furnace pressure, are made
Temperature in burner hearth is controllably run (note: resisting blower herein is opened and do not opened and determined by furnace pressure) by production curve.
In order to show the pressure working condition for decomposing gas incineration section in real time, a U-shaped pressure is installed at the 49m of kiln
Count the pressure working condition to show this section.
Claims (2)
1. a kind of calcining of chemical catalyst and decompose gas and burn all-in-one oven, it include decomposed by preheating section (1), heating section (2),
The furnace body and device for transporting objects (5) and by burner (15), combustion gas that calcining at constant temperature activation section (3), cooling down section (4) are constituted
The burner composition that pipeline (12), combustion-supporting air piping (13) and combustion fan (14) are constituted, it is characterised in that: decomposed in heating
The row of being provided with decomposes feed channel (7) and row decomposition gas blower (6) at the top of section (2), and the air inlet mouth of pipe of row decomposition gas blower (6) passes through
Row decomposes feed channel (7) and communicates with heating decomposition section (2) burner hearth, below the device for transporting objects of calcining at constant temperature activation section (3)
It is additionally arranged decomposition gas Burning Room (16), is provided on Burning Room (16) and decomposes gas branch pipe, feed channel (8) and row are decomposed by conveying
Decomposition gas blower (6) outlet mouth of pipe is connected；It is provided with below the material transmitting device that preheating section (1) and heating decompose section (2)
Burning Room discharge flue (11), and smoke discharging pipe (10) are provided in preheating section (1), the smoke discharging pipe (10) and it is mounted on furnace roof
Smoke exhaust fan (9) be connected.
2. chemical catalyst calcining according to claim 1 and decomposition gas burn all-in-one oven, it is characterised in that: burning
Flue gas residence wall equipped with honeycomb ceramic heat accumulator production in room (16).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920014584.6U CN209416084U (en) | 2019-01-05 | 2019-01-05 | Chemical catalyst calcining and decomposition gas burn all-in-one oven |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920014584.6U CN209416084U (en) | 2019-01-05 | 2019-01-05 | Chemical catalyst calcining and decomposition gas burn all-in-one oven |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209416084U true CN209416084U (en) | 2019-09-20 |
Family
ID=67942662
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920014584.6U Withdrawn - After Issue CN209416084U (en) | 2019-01-05 | 2019-01-05 | Chemical catalyst calcining and decomposition gas burn all-in-one oven |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209416084U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109579554A (en) * | 2019-01-05 | 2019-04-05 | 黄冈市中洲安信窑炉有限公司 | Chemical catalyst calcining and decomposition gas burn all-in-one oven |
-
2019
- 2019-01-05 CN CN201920014584.6U patent/CN209416084U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109579554A (en) * | 2019-01-05 | 2019-04-05 | 黄冈市中洲安信窑炉有限公司 | Chemical catalyst calcining and decomposition gas burn all-in-one oven |
| CN109579554B (en) * | 2019-01-05 | 2023-11-07 | 黄冈市中洲安信窑炉有限公司 | Integrated furnace for calcining chemical catalyst and decomposing gas for burning |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20190920 Effective date of abandoning: 20231107 |
|
| AV01 | Patent right actively abandoned |
Granted publication date: 20190920 Effective date of abandoning: 20231107 |
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| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |