CN108636389A - Activated carbon adsorption exhaust gas desorption cracking harmless treatment device and method - Google Patents
Activated carbon adsorption exhaust gas desorption cracking harmless treatment device and method Download PDFInfo
- Publication number
- CN108636389A CN108636389A CN201810633527.6A CN201810633527A CN108636389A CN 108636389 A CN108636389 A CN 108636389A CN 201810633527 A CN201810633527 A CN 201810633527A CN 108636389 A CN108636389 A CN 108636389A
- Authority
- CN
- China
- Prior art keywords
- desorption
- valve
- heat preservation
- activated carbon
- catalytic bed
- 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
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/34—Regenerating or reactivating
- B01J20/3416—Regenerating or reactivating of sorbents or filter aids comprising free carbon, e.g. activated carbon
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
- F23G7/07—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases in which combustion takes place in the presence of catalytic material
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2207/00—Control
- F23G2207/10—Arrangement of sensing devices
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2207/00—Control
- F23G2207/10—Arrangement of sensing devices
- F23G2207/101—Arrangement of sensing devices for temperature
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Environmental & Geological Engineering (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Analytical Chemistry (AREA)
- Organic Chemistry (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
The present invention proposes activated carbon adsorption exhaust gas desorption cracking harmless treatment device and method.It is related to environmental protection technical field of air purification.Including device and method two parts.Heat preservation desorption case rear portion is equipped with explosion relief door, last one of barrier as security protection system, the exhaust outlet for being catalyzed combustion box is equipped with combustable gas concentration alarm, combustable gas concentration in moment detection stove when work, detect the burning degree of organic solvent, pernicious gas is avoided to enter atmosphere pollution environment, while organic solvent is carried out harmless treatment by activated carbon adsorption exhaust gas desorption cracking harmless treatment device, the heat generated using the calorific value of organic solvent burning carries out activated carbon desorption, with recycling energy, avoid secondary pollution, the characteristics of clean environment firendly, it will be reused after regenerating active carbon, extend the service life of activated carbon, make to extend in replacement cycle from several weeks of activated carbon and replace within 2 to four years once, substantially reduce the operating cost for more renewing activated carbon, favorably promote the use of.
Description
Technical field：
The present invention relates to environmentally friendly technical field of air purification, specifically activated carbon adsorption exhaust gas desorption cracking is innoxious
Processing unit and method.
Background technology：
Current domestic organic waste gas processing equipment 70% of going is to utilize active carbon adsorption, because of activated carbon adsorption dead weight
Just reach saturation state after 25% organic exhaust gas, no longer there is adsorption capacity, need replacing new activated carbon or desorption and regeneration, have
Solvent is burnt by catalysis into harmless treatment, and burning generates a large amount of thermal energy, is dispersed into air therewith, waste of energy.
Invention content：
To solve the above-mentioned problems, the present invention provides activated carbon adsorption exhaust gas desorption cracking harmless treatment device and side
Method.
The technical scheme is that：Activated carbon adsorption exhaust gas desorption cracking harmless treatment device, including heat preservation desorption
Case, heat preservation desorption case are rock wool heat-preservation+steel structural form, and skeleton is inner frame, and side is equipped with one group of gate, are split manually
Door, chamber body rear portion are equipped with explosion relief door, desorption bed are set in heat preservation desorption case, be respectively equipped on the shell of heat preservation desorption case desorption case into
Mouthful valve and desorption case outlet valve, desorption case inlet valve are connected to by pipeline and mend low temperature valve, mend low temperature valve by pipeline connect it is explosion-proof mend it is cold
Wind turbine, the desorption case inlet valve is connected to by pipeline mends low temperature valve, and the pipeline is cold with bypass valve, drain valve, heat exchanger simultaneously
Matchmaker's pipeline is connected to, the outlet of heat exchanger refrigerant pipe connection heat preservation catalysis combustion box, heat preservation catalysis combustion box import and electric heater
Outlet conduit is connected to, and electric heater inlet pipeline connects explosion-proof desorption fan outlet after being connect with heat exchanger heat medium passage, explosion-proof
Desorption fan inlet pipeline is connected to bypass valve, desorption case outlet valve, balanced valve respectively, wherein on the outside of drain valve and balanced valve
It is connected to outside atmosphere.
The heat preservation is catalyzed combustion box, including shell, and insulating layer is set in shell, catalytic bed, catalytic bed are equipped in shell
PT type thermocouples are equipped with, flammable gas alarm is equipped in the outer outlet of heat preservation catalysis combustion box.
Catalyst is using cordierite honeycomb ceramic body as first vector, and γ-Al2O3 are Second support, with noble metal platinum
It is main active component with palladium.
Activated carbon adsorption exhaust gas desorption cracking method for innocent treatment, comprises the steps of：
1, heat preservation desorption case (1) gate (14) is opened, flatcar cart.Activated charcoal to be desorbed (has been adsorbed full
With) tile and pile up onto flatcar.Flatcar is pushed into heat preservation desorption case (1), and gate (14) are closed tightly.
2, start automatic desorption button.Bypass valve (10) automatically turns on, remaining valve is in closed state, explosion-proof desorption
Wind turbine (5) starts automatically, and electric heater (11) starts automatically, and system is in catalytic bed automatic preheating state.Pre- Warm status catalysis
Bed tempertaure, which reaches 250 DEG C and keeps the temperature preheating in 30 minutes, to be terminated.
3, system is automatically into desorption combustion state after catalytic bed preheats.Desorption case inlet valve (9) and desorption case go out
Mouth valve (3) automatically turns on, and bypass valve (10) is automatically closed, and hot-air enters heat preservation desorption case (1) and heats activated carbon, with temperature
Degree increases, and the organic solvent in activated carbon is deviate from enters catalytic bed through heat exchanger, electrical heating room, when concentration and temperature reach anti-
When answering condition, organic exhaust gas is in catalytic bed reactive combustion.
4, the concentration and temperature of organic solvent gradually rise, and when catalytic bed temperature reaches 250~300 DEG C, catalytic bed is opened
Beginning combustion reaction mends low temperature valve (8) and mends air-cooler (2) automatic opening, and control heat preservation desorption case (1) interior temperature is no more than 130 DEG C.
When catalytic bed temperature reaches 350 DEG C, drain valve (4) automatically turns on, and excessive heat in system is discharged, and is generated using waste gas burning
Hot-air by heat exchanger (12) enter heat preservation desorption case (1) recycle, at this time electric heater (11) stop, not needing
External heat, single desorption, desorption time are 3-4 hours, and the ceramic honeycomb body noble metal catalyst service life of inside filling is
6000 hours；
5, at the end of desorption catalyzing, balanced valve (6) and drain valve (4) automatically turn on, at remaining valve and electric heater
Catalytic bed is recycled to by extraneous air, catalytic bed is cooled down under the action of explosion-proof desorption wind turbine (5) in closed state, it is empty
Gas is discharged outdoor by drain valve (4)；Catalytic bed is in the state of cooling at this time, is cooled to 65 DEG C hereinafter, catalytic bed cooling terminates.
6, after catalytic bed cooling, case inlet valve (9), desorption is desorbed automatically into desorption case cooling stage in system
Case outlet valve (3), mend low temperature valve (8), balanced valve (6) is in open state remaining valve and is closed.Mend air-cooler (2) certainly
Dynamic to start, entering drawing by extraneous air makes activated charcoal cool down, and air is discharged by balanced valve (6), when desorption box temperature degree
50 DEG C are dropped to, desorption case cooling stage terminates.
7, gate (14) are opened, flatcar is hauled out from heat preservation desorption case (1), the activated charcoal after desorption is transported.It is flat
Vehicle pushes back, and gate is closed, and operation terminates.
The present invention has the advantages that：Heat preservation desorption case rear portion is equipped with explosion relief door, most as security protection system
One of barrier afterwards, the exhaust outlet for being catalyzed combustion box are equipped with combustable gas concentration alarm, flammable in moment detection stove when work
Gas concentration detects the burning degree of organic solvent, and pernicious gas is avoided to enter atmosphere pollution environment, and activated carbon adsorption exhaust gas is de-
While organic solvent is carried out harmless treatment by attached cracking harmless treatment device, generated using the calorific value of organic solvent burning
Heat carry out activated carbon desorption, there is recycling energy, avoid secondary pollution, clean environment firendly the characteristics of, by activated carbon
It is reused after regeneration, extends the service life of activated carbon, replacement cycle from several weeks of activated carbon is made to extend to 2 to four years more
It changes once, substantially reduces the operating cost for more renewing activated carbon, favorably promote the use of.
Description of the drawings：
Fig. 1 is the structural schematic diagram of the present invention；
Attached drawing 2 is desorption bed heating process flow diagram in the present invention；
Attached drawing 3 is catalytic bed preheating procedure flow diagram in the present invention；
Attached drawing 4 is catalytic combustion process flow diagram in the present invention；
Attached drawing 5 is catalytic bed cooling process flow diagram in the present invention；
Attached drawing 6 is desorption bed cooling process flow diagram in the present invention；
Attached drawing 7 is the structural schematic diagram of heat preservation catalysis combustion box in the present invention.
Case outlet valve, 4- drain valves, the explosion-proof desorption wind of 5- is desorbed in 1- heat preservations desorption case, the explosion-proof benefit air-coolers of 2-, 3- in figure
Machine, 6- balanced valves, 7- heat preservation catalysis combustion box, 8- benefit low temperature valves, 9- desorption case inlet valves, 10- bypass valves, 11- electric heaters,
12- heat exchangers, 13- is quick-fried to let out door, the gates 14-, 15- shells, 16- insulating layers, 17- catalytic beds, and mouth, 19- fuel gas are arranged outside 18-
Alarm, 20-PT type thermocouples.
Specific implementation mode：
The invention will be further described below in conjunction with the accompanying drawings：
Shown in Fig. 1 combinations Fig. 2~6, activated carbon adsorption exhaust gas desorption cracking harmless treatment device, including heat preservation desorption
Case 1, heat preservation desorption case 1 are rock wool heat-preservation+steel structural form, and skeleton is inner frame, and side is equipped with one group of gate 14, are right manually
It opens the door, chamber body rear portion is equipped with explosion relief door 13, and desorption bed is set in heat preservation desorption case 1, is respectively equipped on the shell of heat preservation desorption case 1 de-
Attached case inlet valve 9 and desorption case outlet valve 3, desorption case inlet valve 9 is connected to by pipeline mends low temperature valve 8, mends low temperature valve 8 and is connected by pipeline
Connect mend air-cooler 2, the desorption case inlet valve 3 by pipeline be connected to mend low temperature valve 8, the pipeline simultaneously with bypass valve 10, discharge
Valve 4, the connection of 12 refrigerant pipe of heat exchanger, 12 refrigerant pipe of heat exchanger connection heat preservation catalysis combustion box 7 export, heat preservation catalysis burning
7 import of case is connected to 11 outlet conduit of electric heater, and 11 inlet pipeline of electric heater connects after being connect with 12 heat medium passage of heat exchanger
Quick-fried desorption wind turbine 5 is taken over control to export, explosion-proof 5 inlet pipeline of desorption wind turbine respectively with bypass valve 10, case outlet valve 3, balanced valve 6 is desorbed
Connection, wherein drain valve 4 and 6 outside of balanced valve are connected to outside atmosphere.
The heat preservation is catalyzed combustion box 7, including shell 15, and insulating layer 16 is set in shell 15, catalysis is equipped in shell 15
Bed 17, catalytic bed 17 are equipped with the detection catalysis ignition temperature of PT types thermocouple 20, and catalysis ignition temperature reaches setting value, is passed through useless
Gas combustion catalysis, the outer outlet 18 of heat preservation catalysis combustion box 7 is interior to be equipped with the detection burning adequacy of flammable gas alarm 19, prevents
The outer pollution discharging environment of insufficient exhaust gas that only burns.
Catalyst is using cordierite honeycomb ceramic body as first vector, and γ-Al2O3 are Second support, with noble metal platinum
It is main active component with palladium, noble metal platinum and palladium have high activity, high purification efficiency, high temperature resistant and long life, simultaneously
It releases energy, energy is replaced by heat-exchange device, be used for the energy of maintained equipment spontaneous combustion, water is resolved by the effect of catalyst
And carbon dioxide.
Activated carbon adsorption exhaust gas desorption cracking method for innocent treatment, comprises the steps of：
1, heat preservation desorption case (1) gate (14) is opened, flatcar cart.Activated charcoal to be desorbed (has been adsorbed full
With) tile and pile up onto flatcar.Flatcar is pushed into heat preservation desorption case (1), and gate (14) are closed tightly.
2, start automatic desorption button.Bypass valve (10) automatically turns on, remaining valve is in closed state, explosion-proof desorption
Wind turbine (5) starts automatically, and electric heater (11) starts automatically, and system is in catalytic bed automatic preheating state.Pre- Warm status catalysis
Bed tempertaure, which reaches 250 DEG C and keeps the temperature preheating in 30 minutes, to be terminated.
3, system is automatically into desorption combustion state after catalytic bed preheats.Desorption case inlet valve (9) and desorption case go out
Mouth valve (3) automatically turns on, and bypass valve (10) is automatically closed, and hot-air enters heat preservation desorption case (1) and heats activated carbon, with temperature
Degree increases, and the organic solvent in activated carbon is deviate from enters catalytic bed through heat exchanger, electrical heating room, when concentration and temperature reach anti-
When answering condition, organic exhaust gas is in catalytic bed reactive combustion.
4, the concentration and temperature of organic solvent gradually rise, and when catalytic bed temperature reaches 250~300 DEG C, catalytic bed is opened
Beginning combustion reaction mends low temperature valve (8) and mends air-cooler (2) automatic opening, and control heat preservation desorption case (1) interior temperature is no more than 130 DEG C.
When catalytic bed temperature reaches 350 DEG C, drain valve (4) automatically turns on, and excessive heat in system is discharged, and is generated using waste gas burning
Hot-air by heat exchanger (12) enter heat preservation desorption case (1) recycle, at this time electric heater (11) stop, not needing
External heat, single desorption, desorption time are 3-4 hours, and the ceramic honeycomb body noble metal catalyst service life of inside filling is
6000 hours；
5, at the end of desorption catalyzing, balanced valve (6) and drain valve (4) automatically turn on, at remaining valve and electric heater
Catalytic bed is recycled to by extraneous air, catalytic bed is cooled down under the action of explosion-proof desorption wind turbine (5) in closed state, it is empty
Gas is discharged outdoor by drain valve (4)；Catalytic bed is in the state of cooling at this time, is cooled to 65 DEG C hereinafter, catalytic bed cooling terminates.
6, after catalytic bed cooling, case inlet valve (9), desorption is desorbed automatically into desorption case cooling stage in system
Case outlet valve (3), mend low temperature valve (8), balanced valve (6) is in open state remaining valve and is closed.Mend air-cooler (2) certainly
Dynamic to start, entering drawing by extraneous air makes activated charcoal cool down, and air is discharged by balanced valve (6), when desorption box temperature degree
50 DEG C are dropped to, desorption case cooling stage terminates.
7, gate (14) are opened, flatcar is hauled out from heat preservation desorption case (1), the activated charcoal after desorption is transported.It is flat
Vehicle pushes back, and gate is closed, and operation terminates.
The high-concentration organic waste gas of activated carbon adsorption is introduced into catalysis burning unit, waits for that concentration and temperature reach reaction and requires
When, water and carbon dioxide are resolved by the effect of catalyst, released energy simultaneously, energy is replaced by heat-exchange device, is used for
The energy of maintained equipment spontaneous combustion.
Heat preservation desorption case rear portion is catalyzed combustion box equipped with explosion relief door as last one of barrier of security protection system
Exhaust outlet is equipped with combustable gas concentration alarm, and combustable gas concentration in moment detection stove, detects organic solvent when work
Burning degree avoids pernicious gas from entering atmosphere pollution environment, and activated carbon adsorption exhaust gas desorption cracking harmless treatment device will
While organic solvent carries out harmless treatment, the heat generated using the calorific value of organic solvent burning carries out activated carbon desorption,
With recycling energy, avoid secondary pollution, clean environment firendly the characteristics of, will be reused after regenerating active carbon, extend and live
Property charcoal service life, make to extend in replacement cycle from several weeks of activated carbon and replace within 2 to four years primary, substantially reduce and more renew
The operating cost of activated carbon, is favorably promoted the use of.
Claims (2)
1. a kind of activated carbon adsorption exhaust gas desorption cracking harmless treatment device, including heat preservation desorption case (1), it is characterised in that：
Heat preservation desorption case (1) is rock wool heat-preservation+steel structural form, and skeleton is inner frame, and side is equipped with one group of gate (14), is right manually
It opens the door, chamber body rear portion is equipped with explosion relief door (13), and heat preservation, which is desorbed in case (1), sets desorption bed, on the shell of heat preservation desorption case (1) respectively
Equipped with desorption case inlet valve (9) and desorption case outlet valve (3), desorption case inlet valve (9) is connected to by pipeline and mends low temperature valve (8), is mended
Low temperature valve (8) is connected by pipeline mends air-cooler (2), and the desorption case inlet valve (9) is connected to by pipeline and mends low temperature valve (8), should
Pipeline is connected to bypass valve (10), drain valve (4), heat exchanger (12) refrigerant pipe simultaneously, the connection of heat exchanger (12) refrigerant pipe
Heat preservation catalysis combustion box (7) exports, and heat preservation catalysis combustion box (7) import is connected to electric heater (11) outlet conduit, electrical heating
Device (11) inlet pipeline connects explosion-proof desorption wind turbine (5) outlet, explosion-proof desorption wind turbine after being connect with heat exchanger (12) heat medium passage
(5) inlet pipeline is connected to bypass valve (10), desorption case outlet valve (3), balanced valve (6) respectively, wherein drain valve (4) peace
It is connected to outside atmosphere on the outside of weighing apparatus valve (6).
The heat preservation catalysis combustion box (7), including shell (15), shell (15) is interior to set insulating layer (16), is set in shell (15)
There are catalytic bed (17), catalytic bed (17) to be equipped with PT types thermocouple (20), the outer outlet (18) of heat preservation catalysis combustion box (7) is interior
Equipped with flammable gas alarm (19).
Catalyst is using cordierite honeycomb ceramic body as first vector, and γ-Al2O3 are Second support, with noble metal platinum and palladium
For main active component.
2. activated carbon adsorption exhaust gas desorption cracking method for innocent treatment, it is characterised in that comprise the steps of：
S1, heat preservation desorption case (1) gate (14) is opened, flatcar cart, by activated charcoal (adsorption saturation) to be desorbed
In tiling stacking to flatcar, flatcar is pushed into heat preservation desorption case (1), and gate (14) are closed tightly；
S2, start automatic desorption button, bypass valve (10) automatically turns on, remaining valve is in closed state, explosion-proof desorption wind
Machine (5) starts automatically, and electric heater (11) starts automatically, and system is in catalytic bed automatic preheating state, pre- Warm status catalytic bed
Temperature, which reaches 250 DEG C and keeps the temperature preheating in 30 minutes, to be terminated；
System is automatically into desorption combustion state after S3, catalytic bed preheating：Case inlet valve (9) and desorption case outlet valve is desorbed
(3) it automatically turns on, bypass valve (10) is automatically closed, and hot-air enters heat preservation desorption case (1) and heats activated carbon, with temperature liter
Height, the organic solvent in activated carbon is deviate from enters catalytic bed through heat exchanger, electrical heating room, when concentration and temperature reach reaction item
When part, organic exhaust gas is in catalytic bed reactive combustion；
S4, the concentration of organic solvent and temperature gradually rise, and when catalytic bed temperature reaches 250~300 DEG C, catalytic bed starts to fire
Reaction is burnt, low temperature valve (8) is mended and mends air-cooler (2) automatic opening, control heat preservation desorption case (1) interior temperature is no more than 130 DEG C；When urging
Change drain valve (4) when bed tempertaure reaches 350 DEG C to automatically turn on excessive heat discharge, the heat for utilizing waste gas burning to generate in system
Air enters heat preservation desorption case (1) by heat exchanger (12) and recycles, and electric heater (11) stops at this time, does not need additional
Heat, single desorption, desorption time are 3-4 hours, and the ceramic honeycomb body noble metal catalyst service life of inside filling is 6000
Hour；
S5, at the end of desorption catalyzing, balanced valve (6) and drain valve (4) automatically turn on, remaining valve and electric heater are in and close
Closed state is recycled to catalytic bed by extraneous air, catalytic bed is cooled down under the action of explosion-proof desorption wind turbine (5), and air is logical
It is outdoor to cross drain valve (4) discharge；Catalytic bed is in the state of cooling at this time, is cooled to 65 DEG C hereinafter, catalytic bed cooling terminates；
After S6, catalytic bed cooling, automatically into desorption case cooling stage, desorption case inlet valve (9), desorption case go out system
Mouthful valve (3), mend low temperature valve (8), balanced valve (6) is in open state remaining valve and is closed.Air-cooler (2) is mended to open automatically
Dynamic, entering drawing by extraneous air makes activated charcoal cool down, and air is discharged by balanced valve (6), when desorption box temperature degree drops to
50 DEG C, desorption case cooling stage terminates；
S7, gate (14) are opened, flatcar is hauled out from heat preservation desorption case (1), the activated charcoal after desorption is transported.Flatcar pushes away
It returns, gate is closed, and operation terminates.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810633527.6A CN108636389A (en) | 2018-06-20 | 2018-06-20 | Activated carbon adsorption exhaust gas desorption cracking harmless treatment device and method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810633527.6A CN108636389A (en) | 2018-06-20 | 2018-06-20 | Activated carbon adsorption exhaust gas desorption cracking harmless treatment device and method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108636389A true CN108636389A (en) | 2018-10-12 |
Family
ID=63752922
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810633527.6A Pending CN108636389A (en) | 2018-06-20 | 2018-06-20 | Activated carbon adsorption exhaust gas desorption cracking harmless treatment device and method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108636389A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111467928A (en) * | 2020-04-17 | 2020-07-31 | 重庆三峡环保（集团）有限公司 | Method and system for treating organic waste gas sprayed in automobile industry based on activated carbon adsorption concentration-catalytic combustion technology |
| CN112076586A (en) * | 2020-07-23 | 2020-12-15 | 苏州罗克韦尔智能科技有限公司 | Catalytic combustion device and waste gas treatment method thereof |
| CN112555868A (en) * | 2020-07-20 | 2021-03-26 | 孙昊 | Activated carbon regeneration waste gas incineration purification vehicle |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106310832A (en) * | 2016-10-19 | 2017-01-11 | 烟台三立彩钢结构有限公司 | Novel dedusting cabinet |
| CN107261747A (en) * | 2017-08-08 | 2017-10-20 | 广州云汇能源环保科技有限公司 | A kind of volatile organic waste gas high efficiency purifying processing device |
| CN207401320U (en) * | 2017-10-31 | 2018-05-25 | 成都晟蓝环保科技有限公司 | A kind of activated carbon is desorbed equipment |
| CN208542214U (en) * | 2018-06-20 | 2019-02-26 | 大庆北油工程技术服务有限公司 | Activated carbon adsorption waste gas desorption cracking harmless treatment device |
-
2018
- 2018-06-20 CN CN201810633527.6A patent/CN108636389A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106310832A (en) * | 2016-10-19 | 2017-01-11 | 烟台三立彩钢结构有限公司 | Novel dedusting cabinet |
| CN107261747A (en) * | 2017-08-08 | 2017-10-20 | 广州云汇能源环保科技有限公司 | A kind of volatile organic waste gas high efficiency purifying processing device |
| CN207401320U (en) * | 2017-10-31 | 2018-05-25 | 成都晟蓝环保科技有限公司 | A kind of activated carbon is desorbed equipment |
| CN208542214U (en) * | 2018-06-20 | 2019-02-26 | 大庆北油工程技术服务有限公司 | Activated carbon adsorption waste gas desorption cracking harmless treatment device |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111467928A (en) * | 2020-04-17 | 2020-07-31 | 重庆三峡环保（集团）有限公司 | Method and system for treating organic waste gas sprayed in automobile industry based on activated carbon adsorption concentration-catalytic combustion technology |
| CN112555868A (en) * | 2020-07-20 | 2021-03-26 | 孙昊 | Activated carbon regeneration waste gas incineration purification vehicle |
| CN112076586A (en) * | 2020-07-23 | 2020-12-15 | 苏州罗克韦尔智能科技有限公司 | Catalytic combustion device and waste gas treatment method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100540119C (en) | A kind of color-coating waste gas heat recovery method | |
| CN108636389A (en) | Activated carbon adsorption exhaust gas desorption cracking harmless treatment device and method | |
| CN205155984U (en) | Handle heat accumulation formula catalysis direct combustion system of VOCs waste gas | |
| CN206469276U (en) | A kind of heat accumulating type catalytic burning device | |
| CN110878943A (en) | Waste incineration system and efficient incineration control method | |
| CN203442846U (en) | Integral type organic waste gas thermal storage catalytic reaction device | |
| CN205878188U (en) | Organic waste gas treatment and recovery system | |
| CN108826323A (en) | A kind of catalysis burning waste gas processing system for medium and small air quantity | |
| CN109268106A (en) | One kind clearing up regenerated device and method for DPF or automotive catalytic converter | |
| CN208542214U (en) | Activated carbon adsorption waste gas desorption cracking harmless treatment device | |
| CN102865584B (en) | Seriation L-type non-phase transformation super heat-conductive pipe heat reclamation type VOCs incinerator | |
| CN208253609U (en) | A kind of printing machine VOCs concentration paddy electricity balance RTO processing system | |
| CN203517822U (en) | Catalytic combustion photo-catalyst waste gas treatment device | |
| CN205535842U (en) | Two room heat accumulation after burner of domestic waste | |
| CN202132955U (en) | Organic exhaust-gas treatment and heat energy recycling system | |
| CN101936535A (en) | Painted steel strip roasting method for heating exhaust gas with far infrared electric heating tube and catalytically incinerating exhaust gas at low temperature and catalytic oxidizer thereof | |
| CN107138019A (en) | A kind of volatile organic compounds purifier | |
| CN208727116U (en) | A kind of coating production line waste gas purification by adsorbsion device | |
| CN105864805A (en) | Regenerative thermal oxidation pyrolysis waste gas treatment and utilization system | |
| CN106955568A (en) | A kind of PS editions drying production line organic waste gas treatment system and handling process | |
| CN206235134U (en) | Drying system | |
| CN216281443U (en) | Organic waste gas catalytic oxidation combustion apparatus | |
| CN207893773U (en) | A kind of organic exhaust gas heating power oxidation unit | |
| CN210441668U (en) | Kiln tail gas waste heat cyclic utilization system is fired to ancient building blue brick | |
| CN209246087U (en) | Low-temperature environment-friendly cracking apparatus |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20181012 |