CN205878190U - Heat accumulation formula heating power oxidation equipment - Google Patents
Heat accumulation formula heating power oxidation equipment Download PDFInfo
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- CN205878190U CN205878190U CN201620832702.0U CN201620832702U CN205878190U CN 205878190 U CN205878190 U CN 205878190U CN 201620832702 U CN201620832702 U CN 201620832702U CN 205878190 U CN205878190 U CN 205878190U
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- regenerator
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- pass
- blowback
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Abstract
The utility model discloses a heat accumulation formula heating power oxidation equipment belongs to organic waste gas treatment facility field, including intake pipe, blast pipe, blowback trachea, regenerator no. 1, regenerator no. 2, regenerator no. 3 and combustion chamber, regenerator no. 1, regenerator no. 2 and regenerator no. 3 respectively with the combustion chamber intercommunication, be equipped with the heat exchange in the regenerator and pack, the intake pipe is connected through bye -pass and regenerator no. 1, regenerator no. 2, regenerator no. 3 respectively, is equipped with waste gas admission valve, filter and the draught fan that admits air on the intake pipe main line, the blast pipe is connected through bye -pass and regenerator no. 1, regenerator no. 2, regenerator no. 3 respectively, is equipped with exhaust draught fan and row air control valve on the blast pipe main line, the blowback tracheorrhaphy do not passes through bye -pass and regenerator no. 1, regenerator no. 2, regenerator no. 3 is connected, blowback trachea main line connect to the exhaust draught fan with arrange the blast pipe between air control valve on. Heat in this equipment is relapseed cyclic utilization, energy saving, green.
Description
Technical field
This utility model relates to a kind of heat accumulating type heating power oxidation furnaces, belongs to organic waste gas treatment equipment field.
Background technology
Heat accumulating type heating power oxidation (Regenerative Thermal Oxidizer, be called for short RTO), be by high-temperature oxydation with
Heat storage technology ties a kind of organic waste gas treatment equipment of platform mutually.Traditional automobile and machinery manufacturing industry, paint line and drying room, electronics
The production processes such as manufacturing industry, printed substrate (PCB), Electric Manufacture industry, magnet wire insulation, light industry all can produce organic waste
Gas, directly burns waste gas during traditional method, is converted into safe gas and steam, then discharges in an atmosphere, and reacts
During the amount of heat that produces can not reclaim, cause the waste of heat, meanwhile, in waste gas heating combustion process, need to expend
The substantial amounts of energy.
Summary of the invention
The problem existed for above-mentioned prior art, this utility model provides a kind of heat accumulating type heating power oxidation furnaces, equipment
In heat be repeatedly recycled, save the energy, environmental protection.
To achieve these goals, a kind of heat accumulating type heating power oxidation furnaces that this utility model uses, including air inlet pipe, row
Trachea, blowback trachea, regenerator one, regenerator two, regenerator three and combustor, described regenerator one, regenerator two and accumulation of heat
Room three respectively with combustion chamber, be provided with heat exchange filler in regenerator；
Described air inlet pipe is connected with regenerator one, regenerator two, regenerator three by bye-pass respectively, air inlet pipe bye-pass
And it is provided with intake valve one between regenerator one, between described air inlet pipe bye-pass and regenerator two, is provided with intake valve two, described air inlet pipe
Being provided with intake valve three between bye-pass and regenerator three, air inlet pipe main line is provided with gas inlet valve, filter and air inlet air inducing
Machine；
Described exhaustor is connected with regenerator one, regenerator two, regenerator three by bye-pass respectively, exhaustor bye-pass
And it is provided with air bleeding valve one between regenerator one, between described exhaustor bye-pass and regenerator two, is provided with air bleeding valve two, described exhaustor
Being provided with air bleeding valve three between bye-pass and regenerator three, exhaustor main line is provided with aerofluxus air-introduced machine and gas exhausting valve；
Described blowback trachea is connected with regenerator one, regenerator two, regenerator three by bye-pass respectively, blowback tracheal branches
It is provided with back-flushing valve one between pipeline and regenerator one, between blowback trachea bye-pass and regenerator two, is provided with back-flushing valve two, described blowback
Being provided with back-flushing valve three between tracheal branches pipeline and regenerator three, described blowback trachea main line is provided with blowback control valve, described instead
Gas blow pipe main line is connected on the exhaustor between aerofluxus air-introduced machine and gas exhausting valve.
As improvement, in described regenerator one, it is provided with thermal storage ceramic body one, in regenerator two, is provided with thermal storage ceramic body two, store
Thermal storage ceramic body three it is provided with in hot cell three.
As improvement, described filter uses two-layer to filter, and one layer is metal gauze, and one layer is filter cotton.
As improvement, being further connected with fresh air pipeline between described gas inlet valve and filter, described fresh air pipeline is provided with newly
Wind control valve.
Compared with prior art, the beneficial effects of the utility model are:
1) this equipment is as an entirety, thermal storage ceramic body, preheating device, combustor is formed a whole, and forms one
Individual volume is little, compact conformation, and air-flow runs smooth organism；It is furnished with pipeline blowback cleaning function simultaneously, will remain in pipeline
Waste gas carries out purified treatment, improves exhaust purification efficiency.
2) using preheating and accumulation of heat to replace handoff technique, be allowed to have higher heat exchange efficiency, efficiency is up to more than 90%,
Energy-efficient performance is notable, and environmental protection.
3) low by impurities concentration in the gas of discharge after burning disposal: VOCs < 120mg/Nm, CO < 100 mg/
Nm, NOx < 100mg/Nm, safety and environmental protection.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model；
In figure: 1, regenerator one, 2, regenerator two, 3, regenerator three, 4, combustor, 5, gas inlet valve, 6, filter,
7, air inlet air-introduced machine, 8, intake valve one, 9, Xingfeng capsule valve, 10, back-flushing valve one, 11, intake valve two, 12, back-flushing valve two, 13,
Intake valve three, 14, back-flushing valve three, 15, blowback control valve, 16, air bleeding valve one, 17, air bleeding valve two, 18, air bleeding valve three, 19, row
Gas air-introduced machine, 20, gas exhausting valve.
Detailed description of the invention
For making the purpose of this utility model, technical scheme and advantage of greater clarity, below by drawings and Examples,
This utility model is further elaborated.However, it should be understood that specific embodiment described herein is only in order to solve
Release this utility model, be not limited to scope of the present utility model.
As it is shown in figure 1, a kind of heat accumulating type heating power oxidation furnaces, including air inlet pipe, exhaustor, blowback trachea, regenerator one
1, regenerator 22, regenerator 33 and combustor 4, described regenerator 1, regenerator 22 and regenerator 33 respectively with combustor
4 connections, are provided with heat exchange filler in regenerator；
Described air inlet pipe is connected with regenerator 1, regenerator 22, regenerator 33 by bye-pass respectively, and air inlet pipe is propped up
It is provided with intake valve 1 between pipeline and regenerator 1, between described air inlet pipe bye-pass and regenerator 22, is provided with intake valve 2 11, institute
Stating and be provided with intake valve 3 13 between air inlet pipe bye-pass and regenerator 33, air inlet pipe main line is provided with gas inlet valve 5, filters
Device 6 and air inlet air-introduced machine 7；
Described exhaustor is connected with regenerator 1, regenerator 22, regenerator 33 by bye-pass respectively, and exhaustor props up
It is provided with air bleeding valve 1 between pipeline and regenerator 1, between described exhaustor bye-pass and regenerator 22, is provided with air bleeding valve 2 17,
Being provided with air bleeding valve 3 18 between described exhaustor bye-pass and regenerator 33, exhaustor main line is provided with aerofluxus air-introduced machine 19 He
Gas exhausting valve 20；
Described blowback trachea is connected with regenerator 1, regenerator 22, regenerator 33 by bye-pass respectively, blowback air
It is provided with back-flushing valve 1 between pipe bye-pass and regenerator 1, between blowback trachea bye-pass and regenerator 22, is provided with back-flushing valve two
12, it is provided with back-flushing valve 3 14 between described blowback trachea bye-pass and regenerator 33, described blowback trachea main line is provided with blowback
Control valve 15, described blowback trachea main line is connected on the exhaustor between aerofluxus air-introduced machine 19 and gas exhausting valve 20.
As the improvement of embodiment, it is provided with thermal storage ceramic body one in described regenerator 1, in regenerator 22, is provided with accumulation of heat
Ceramic body two, is provided with thermal storage ceramic body three in regenerator 33, by the effective accumulation of heat of thermal storage ceramic body, preserve heat.
As the improvement of embodiment, described filter 6 uses two-layer to filter, and one layer is metal gauze, and one layer is filter cotton,
It is effective to clear up stickum and dust impurities in gas.
As the improvement of embodiment, between described gas inlet valve 5 and filter 6, it is further connected with fresh air pipeline, described fresh wind tube
Road is provided with Xingfeng capsule valve 9.It is passed through by controlling new wind, incinerator preheating before device power-up.
Combustor 4, regenerator, before carrying out exhaust-gas treatment, are first preheated by body of heater；After preheating, by exhaust gas source
Access device.This equipment working state is one-in-and-one-out, air inlet or give vent to anger and all should meet waste gas and have to pass through thermal-flame
Burn and purify；First, opening gas inlet valve 5, waste gas flows through intake valve 1 and enters regenerator 1, in regenerator 1
The thermal storage ceramic body one preheated in advance carries out heat exchange, and after intensification, waste gas entrance oxidizing chamber 4 burns, and generates carbon dioxide with water also
Release heat energy, the high-temperature gas of purification leaves combustor 4, enters regenerator two 2(the most cooled in circulation above), release
Heat, discharges after cooling, and regenerator 22 rises intermediate temperature regenerator (for next circulating-heating waste gas) after absorbing amount of heat, place
After reason, gas leaves regenerator 22, controls to enter air through aerofluxus air-introduced machine 19 and gas exhausting valve 20.Generally aerofluxus
Temperature is higher about about 45～55 DEG C than intake air temperature.
After circulation completes, air inlet once switches with valve of giving vent to anger, and enters next one circulation, and waste gas is by regenerator 22
Entering, regenerator 33 is discharged.Before handover, cleaned gas coordinates control through blowback control valve 15, back-flushing valve 3 14
Enter regenerator 33 purging and remain in pipeline and indoor Organic substance.The purifying rate that so can make waste gas is higher, can reach 98-99%
Above.Replace and so forth.
In one cycle of operation, each valve switch state such as following table:
| Regenerator | One | Two | Three | One | Two | Three | One | Two | Three |
| Intake valve | Open | Open | Open | ||||||
| Air bleeding valve | Open | Open | Open | ||||||
| Back-flushing valve | Open | Open | Open |
The foregoing is only preferred embodiment of the present utility model, not in order to limit this utility model, all at this
Any amendment, equivalent or the improvement etc. made within the spirit of utility model and principle, should be included in this utility model
Protection domain within.
Claims (4)
1. a heat accumulating type heating power oxidation furnaces, it is characterised in that include air inlet pipe, exhaustor, blowback trachea, regenerator one
(1), regenerator two (2), regenerator three (3) and combustor (4), described regenerator one (1), regenerator two (2) and regenerator three
(3) connect with combustor (4) respectively, in regenerator, be provided with heat exchange filler；
Described air inlet pipe is connected with regenerator one (1), regenerator two (2), regenerator three (3) by bye-pass respectively, air inlet pipe
It is provided with intake valve one (8) between bye-pass and regenerator one (1), between described air inlet pipe bye-pass and regenerator two (2), is provided with air inlet
Valve two (11), is provided with intake valve three (13) between described air inlet pipe bye-pass and regenerator three (3), air inlet pipe main line is provided with useless
Gas intake valve (5), filter (6) and air inlet air-introduced machine (7)；
Described exhaustor is connected with regenerator one (1), regenerator two (2), regenerator three (3) by bye-pass respectively, exhaustor
It is provided with air bleeding valve one (16) between bye-pass and regenerator one (1), between described exhaustor bye-pass and regenerator two (2), is provided with aerofluxus
Valve two (17), is provided with air bleeding valve three (18) between described exhaustor bye-pass and regenerator three (3), exhaustor main line is provided with row
Gas air-introduced machine (19) and gas exhausting valve (20)；
Described blowback trachea is connected with regenerator one (1), regenerator two (2), regenerator three (3) by bye-pass respectively, blowback
It is provided with back-flushing valve one (10) between tracheal branches pipeline and regenerator one (1), is provided with anti-between blowback trachea bye-pass and regenerator two (2)
Blowing valve two (12), be provided with back-flushing valve three (14) between described blowback trachea bye-pass and regenerator three (3), described blowback trachea is responsible for
Road is provided with blowback control valve (15), and described blowback trachea main line is connected between aerofluxus air-introduced machine (19) and gas exhausting valve (20)
Exhaustor on.
A kind of heat accumulating type heating power oxidation furnaces the most according to claim 1, it is characterised in that in described regenerator one (1)
It is provided with thermal storage ceramic body one, is provided with thermal storage ceramic body two in regenerator two (2), in regenerator three (3), is provided with thermal storage ceramic body three.
A kind of heat accumulating type heating power oxidation furnaces the most according to claim 1, it is characterised in that described filter (6) uses
Two-layer filters, and one layer is metal gauze, and one layer is filter cotton.
A kind of heat accumulating type heating power oxidation furnaces the most according to claim 1, it is characterised in that described gas inlet valve (5)
And being further connected with fresh air pipeline between filter (6), described fresh air pipeline is provided with Xingfeng capsule valve (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620832702.0U CN205878190U (en) | 2016-08-03 | 2016-08-03 | Heat accumulation formula heating power oxidation equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620832702.0U CN205878190U (en) | 2016-08-03 | 2016-08-03 | Heat accumulation formula heating power oxidation equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205878190U true CN205878190U (en) | 2017-01-11 |
Family
ID=57701677
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620832702.0U Expired - Fee Related CN205878190U (en) | 2016-08-03 | 2016-08-03 | Heat accumulation formula heating power oxidation equipment |
Country Status (1)
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|---|---|
| CN (1) | CN205878190U (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106765220A (en) * | 2017-01-20 | 2017-05-31 | 山西亚乐士环保技术股份有限公司 | Five Room regenerative thermal oxidizers |
| CN106907721A (en) * | 2017-03-15 | 2017-06-30 | 苏州克兰茨环境科技有限公司 | A kind of collecting and distributing type exhaust treatment system and processing method |
| CN107051116A (en) * | 2017-06-01 | 2017-08-18 | 上海盛剑环境系统科技有限公司 | A kind of organic waste gas treatment system |
| CN108278621A (en) * | 2018-01-30 | 2018-07-13 | 青岛万泰源环保设备工程有限公司 | A kind of heat accumulating type catalytic burning stove |
| CN108278620A (en) * | 2018-01-30 | 2018-07-13 | 南通三信塑胶装备科技股份有限公司 | A kind of cylindrical type regenerative oxidation system |
| CN109899812A (en) * | 2019-03-19 | 2019-06-18 | 南京晨光集团有限责任公司 | A kind of anti-coking blocking heat accumulating type organic exhaust gas oxidation furnace |
| CN110360578A (en) * | 2019-06-03 | 2019-10-22 | 扬州成威涂装设备有限公司 | A kind of heat accumulating type thermal oxidizer with high thermal uniformity thermal-insulation baffle plate device |
| CN111207401A (en) * | 2019-12-31 | 2020-05-29 | 北京东方雨虹防水技术股份有限公司 | Heat accumulating type oxidation furnace and dirt removing and anti-blocking process |
| CN112097277A (en) * | 2020-09-15 | 2020-12-18 | 广州华科环保工程有限公司 | Heat storage combustion system and method for organic waste gas |
-
2016
- 2016-08-03 CN CN201620832702.0U patent/CN205878190U/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106765220A (en) * | 2017-01-20 | 2017-05-31 | 山西亚乐士环保技术股份有限公司 | Five Room regenerative thermal oxidizers |
| CN106907721A (en) * | 2017-03-15 | 2017-06-30 | 苏州克兰茨环境科技有限公司 | A kind of collecting and distributing type exhaust treatment system and processing method |
| CN107051116A (en) * | 2017-06-01 | 2017-08-18 | 上海盛剑环境系统科技有限公司 | A kind of organic waste gas treatment system |
| CN108278621A (en) * | 2018-01-30 | 2018-07-13 | 青岛万泰源环保设备工程有限公司 | A kind of heat accumulating type catalytic burning stove |
| CN108278620A (en) * | 2018-01-30 | 2018-07-13 | 南通三信塑胶装备科技股份有限公司 | A kind of cylindrical type regenerative oxidation system |
| CN109899812A (en) * | 2019-03-19 | 2019-06-18 | 南京晨光集团有限责任公司 | A kind of anti-coking blocking heat accumulating type organic exhaust gas oxidation furnace |
| CN110360578A (en) * | 2019-06-03 | 2019-10-22 | 扬州成威涂装设备有限公司 | A kind of heat accumulating type thermal oxidizer with high thermal uniformity thermal-insulation baffle plate device |
| CN111207401A (en) * | 2019-12-31 | 2020-05-29 | 北京东方雨虹防水技术股份有限公司 | Heat accumulating type oxidation furnace and dirt removing and anti-blocking process |
| CN111207401B (en) * | 2019-12-31 | 2022-03-18 | 北京东方雨虹防水技术股份有限公司 | Heat accumulating type oxidation furnace and dirt removing and anti-blocking process |
| CN112097277A (en) * | 2020-09-15 | 2020-12-18 | 广州华科环保工程有限公司 | Heat storage combustion system and method for organic waste gas |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170111 Termination date: 20200803 |