CN208694621U - The system of zeolite runner treating organic exhaust gas by adsorptive-catalytic combustion - Google Patents
The system of zeolite runner treating organic exhaust gas by adsorptive-catalytic combustion Download PDFInfo
- Publication number
- CN208694621U CN208694621U CN201821276142.0U CN201821276142U CN208694621U CN 208694621 U CN208694621 U CN 208694621U CN 201821276142 U CN201821276142 U CN 201821276142U CN 208694621 U CN208694621 U CN 208694621U
- Authority
- CN
- China
- Prior art keywords
- gas
- exhaust gas
- regeneration
- catalytic combustion
- zeolite runner
- 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.)
- Active
Links
- 229910021536 Zeolite Inorganic materials 0.000 title claims abstract description 50
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 title claims abstract description 50
- 239000010457 zeolite Substances 0.000 title claims abstract description 50
- 238000007084 catalytic combustion reaction Methods 0.000 title claims abstract description 37
- 238000011069 regeneration method Methods 0.000 claims abstract description 72
- 230000008929 regeneration Effects 0.000 claims abstract description 71
- 238000006555 catalytic reaction Methods 0.000 claims abstract description 33
- 239000003463 adsorbent Substances 0.000 claims abstract description 30
- 238000010438 heat treatment Methods 0.000 claims abstract description 27
- 238000001816 cooling Methods 0.000 claims abstract description 24
- 238000001179 sorption measurement Methods 0.000 claims abstract description 20
- 238000001514 detection method Methods 0.000 claims abstract description 16
- 238000002485 combustion reaction Methods 0.000 claims abstract description 10
- 238000003795 desorption Methods 0.000 claims description 16
- 239000000835 fiber Substances 0.000 claims description 13
- 229910000975 Carbon steel Inorganic materials 0.000 claims description 3
- 239000010962 carbon steel Substances 0.000 claims description 3
- 239000003365 glass fiber Substances 0.000 claims description 3
- 238000004321 preservation Methods 0.000 claims description 3
- 210000000038 chest Anatomy 0.000 claims 1
- 230000009286 beneficial effect Effects 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 128
- 239000003054 catalyst Substances 0.000 description 10
- 238000005516 engineering process Methods 0.000 description 8
- 230000003647 oxidation Effects 0.000 description 7
- 238000007254 oxidation reaction Methods 0.000 description 7
- 238000012545 processing Methods 0.000 description 7
- 230000009102 absorption Effects 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000000746 purification Methods 0.000 description 4
- 239000012855 volatile organic compound Substances 0.000 description 4
- 229910002092 carbon dioxide Inorganic materials 0.000 description 3
- 238000011161 development Methods 0.000 description 3
- 230000018109 developmental process Effects 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 238000004134 energy conservation Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 229910052697 platinum Inorganic materials 0.000 description 2
- 230000002265 prevention Effects 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 238000002336 sorption--desorption measurement Methods 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 206010067125 Liver injury Diseases 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 231100000315 carcinogenic Toxicity 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 230000002607 hemopoietic effect Effects 0.000 description 1
- 239000010985 leather Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- 210000000653 nervous system Anatomy 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- 210000000056 organ Anatomy 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 238000010422 painting Methods 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 239000010970 precious metal Substances 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 210000002345 respiratory system Anatomy 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- 210000000952 spleen Anatomy 0.000 description 1
- 238000007592 spray painting technique Methods 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Incineration Of Waste (AREA)
Abstract
The utility model discloses a kind of systems of zeolite runner treating organic exhaust gas by adsorptive-catalytic combustion, including pressure fan, exhaust gas pretreatment filters, with adsorption zone, cooling zone and the zeolite of renewing zone runner adsorbent bed, regeneration gas preheating unit, regeneration air stream amount control device, PLC controller, catalysis burning bed and exhaust apparatus；The pressure fan admission line is equipped with flow detector and concentration detection apparatus, the regeneration gas preheating unit includes First Heat Exchanger, burner hearth gas heating pipe and primary heater, and the regeneration air stream amount control device includes the regeneration blower of at least two different air quantity parallel connections.The utility model beneficial effect is that regeneration gas preheating unit is equipped with the mixing of burner hearth gas after burner exhaust heat heat exchange and directly heats, and substantially increases the utilization rate of combustion heat energy, has saved the energy；Regeneration air stream amount control device is rationally controlled cocnentration factor, is successfully managed the exhaust gas of various inlet concentration using the regeneration blower fan group of more different air quantity parallel connections.
Description
Technical field
The utility model relates to the purified treatment field of organic exhaust gas, in particular to a kind of zeolite runner absorption-catalysis combustion
Burn the system of processing organic exhaust gas.
Background technique
With China's economy, industrialized fast development, atmosphere polluting problem is outstanding day by day, a large amount of rows of organic exhaust gas
It puts, compromises atmospheric environment, constrain economic sustainable development.Organic exhaust gas is mainly derived from petrochemical industry, pharmacy, printing, painting
Dress, spray painting, leather processing, experimental branch line, plastic processing etc. are related to the production process of the industry using a large amount of organic solvents, at
Divide complicated, inflammable, explosive and have certain toxicity, can not only pollute atmospheric environment, generate photochemical fog, destroy ozone layer,
Also the respiratory system of people can be caused to stimulate, influence the nervous system and hemopoietic system of people, the organs such as damage liver, spleen cause
It is malicious, carcinogenic or even dead.In this context, the prevention and cure of pollution of organic exhaust gas obtain the most attention of society.It is 2016, new " big
Gas prevention and cure of pollution method " for the first time the property of will volatilize organic compound (VOCs) be included in supervision scope, embody country organic exhaust gas is controlled
The resolution and dynamics of reason.
Multinomial technology has been developed for the processing of organic exhaust gas at present, according to principle difference can be divided into recycling class technology and
Eliminate class technology, recycling class technology mainly includes absorption, absorptions, condensation, UF membrane etc., elimination class technology mainly include burn,
Impulse electric corona, low-temperature plasma, photochemical catalytic oxidation, ozone oxidation, biological treatment etc..More with organic waste-gas purification standard
Strictly, single technology has been relatively inaccessible to expected requirement, to reduce processing cost, improves treatment effeciency, more combines work
Skill is gradually applied in reality.Therefore, while development technology, have to different air quantity and concentration organic exhaust gas relatively strong
Applicability meets that clean manufacturing requires, the purification techniques of energy conservation type increasingly obtains the high praise of VOCs treatment industry.
CN 103394270B discloses a kind of movable integral organic waste gas treatment device, which is integrated design
On moveable mobile holder, absorbing unit is the rotary-type structure of continuous rotation, and organic exhaust gas passes through runner adsorbent bed, lived
Property charcoal or molecular sieve absorption after by high altitude discharge pipeline qualified discharge, device is using the fresh wind of heating to the progress of runner adsorbent bed
It is desorbed, the exhaust gas after desorption is heated to react generation carbon dioxide and water, the medium temperature of generation into catalysis burning bed with after heat exchange
Organic exhaust gas after the pre- thermal desorption of flue gas utilization heat exchanger.Device has mobility, treatment effeciency high, can be used for environmental pollution
The emergency processing of burst accident.But the device is designed to movable integral, has to the processing of Wind Volume organic exhaust gas
Limitation；Furthermore it as desorption wind after device is directly heated using surrounding air, is influenced vulnerable to ambient environmental factors and heats energy
It consumes higher.
CN 106039995A discloses a kind of integral type VOCs Adsorption Concentration-catalyzing oxidizing degrading rotary wheel device and its work
Skill, runner are divided into adsorption zone and catalysis oxidation area, difunctional adsorption catalyst are uniformly attached on runner, and catalysis oxidation area enters
Mouth is connected with heater, and device is under adsorption-regeneration cycles operation, it can be achieved that the continuity of VOCs purifies in industrial tail gas.But
It is that the catalysis oxidation area temperature of the runner of device is up to 150~300 DEG C, into after adsorption zone, is easy to cause shadow to adsorption effect
It rings；Meanwhile catalysis oxidation area has high temperature air air-flow to continuously pass through, and organic pollutant is easily caused just to be desorbed without catalysis oxidation
It takes away, it is not up to standard to may result in outlet drain.
Utility model content
In view of the deficienciess of the prior art, the purpose of this utility model is to provide a kind of high applicabilities, high purification effect
The system of the zeolite runner treating organic exhaust gas by adsorptive-catalytic combustion of rate and energy conservation type.
It is for technical solution used by realization the purpose of this utility model:
The utility model relates to a kind of systems of zeolite runner treating organic exhaust gas by adsorptive-catalytic combustion, including pressure fan
(exclusive pull exhaust gas), exhaust gas pretreatment filters (exclusive cooling exhaust gas, de- exhaust gas and dust), have adsorption zone, cooling zone and
Zeolite runner adsorbent bed (the exclusive adsorption/desorption that integrates realizes exhaust gas concentration), the regeneration gas preheating unit of renewing zone are (exclusive
Preheat regeneration gas), regeneration air stream amount control device (exclusive adjustings exhaust gas cocnentration factor), PLC controller (it is exclusive automatically control entirely
System operation), catalysis burning bed (exclusive to exhaust gas carry out catalyst combustion reaction) and exhaust apparatus (exclusive exhaust gas high altitude discharge)；
The regeneration gas preheating unit includes First Heat Exchanger, burner hearth gas heating pipe and primary heater, the burner hearth gas heating tube
Road one end connection catalysis burning bed, the other end are connected to the pipeline between First Heat Exchanger and primary heater；The pressure fan,
Exhaust gas pretreatment filters are sequentially connected, and the outlet pipe of the exhaust gas pretreatment filters is divided into two-way, are turned all the way with zeolite
Adsorption zone, the exhaust apparatus of wheel adsorbent bed are sequentially connected, the cooling zone of another way and zeolite runner adsorbent bed, First Heat Exchanger,
Primary heater, renewing zone, regeneration air stream amount control device, catalysis burning bed, First Heat Exchanger and exhaust apparatus are sequentially connected；
The PLC controller respectively with pressure fan, exhaust gas pretreatment filters, regeneration gas preheating unit, regeneration air stream amount control device,
It is catalyzed burning bed connection.
Exhaust gas is entered by admission line, is divided into two strands after exhaust gas pretreatment filters by pressure fan, first strand useless
Gas adjusts flow by regeneration air stream amount control device, into the cooling zone blow it is cold after, add by regeneration gas preheating unit
Desorption gas is formed after heat, the renewing zone is desorbed, and the desorption concentration exhaust gas of formation enters catalysis by regenerating blower fan group
Burning bed completes catalyst combustion reaction and forms CO2With 270, the high-temperature gas of formation is after First Heat Exchanger by exhaust apparatus
Qualified discharge；Second strand of exhaust gas is directly entered the adsorption zone, directly through exhaust apparatus qualified discharge after being adsorbed by zeolite.
Further, the regeneration air stream amount control device includes the regeneration blower of at least two different air quantity parallel connections, institute
It states regeneration blower to be connected with the PLC controller, is successively arranged flow along airintake direction on every regeneration fan air inlet pipeline
Detection device and the solenoid valve being connected with the PLC controller, every regeneration blower outlet tube road also are provided with and the PLC
The connected solenoid valve of controller；The pressure fan admission line is equipped with flow detector and is connected with the PLC controller
Concentration detection apparatus.The difference for the inlet gas concentration that the PLC controller is detected according to the concentration detection apparatus, control is again
The solenoid valve and regeneration blower of angry volume control device are to adjust air-flow size.
Further, the exhaust gas pretreatment filters include the gas cooling device set gradually along airintake direction and fibre
Dimensional filter device；It is respectively equipped with hygrometer at the air inlet of fibre filter and gas outlet, in going out for fibre filter
It is additionally provided with thermocouple at port, is additionally provided with differential pressure indicator on the fibre filter.The differential pressure indicator is for feedback fibers filtering dress
The stopping state set.
Further, the zeolite runner adsorbent bed by rotation rate-controllable driver frequency control；The zeolite runner
The adsorption zone optimal adsorption temperature of adsorbent bed is 20~40 DEG C；The best desorption temperature in renewing zone of the zeolite runner adsorbent bed is
150~200 DEG C.
Further, it is pretreated that the cooling air-flow that the cooling zone of the zeolite runner adsorbent bed uses leads directly from exhaust gas
The exhaust piping that filter is connected with zeolite runner adsorbent bed, the cooling air air-flow control the control of regeneration gas flow by PLC controller
Device processed is adjusted.
Further, the burner hearth gas heating pipe of the regeneration gas preheating unit is equipped with the 5th solenoid valve, the burner hearth
The pipeline that gas heating pipe gas outlet is connected with primary heater air inlet is equipped with the second thermocouple, and the primary heater goes out
Port pipeline is equipped with third thermocouple, and the 5th solenoid valve, the second thermocouple, third thermocouple and primary heater are divided equally
It is not connected with PLC controller.After the burner hearth gas Hybrid Heating that PLC controller is detected according to the second thermocouple, third thermocouple
The 5th solenoid valve of airflow temperature-control opening degree, adjust burner hearth throughput size, and then adjust primary heater use
Power.
Further, the renewing zone gas outlet pipeline of the zeolite runner adsorbent bed is equipped with the 4th thermocouple.It is described useless
In the outlet pipe of gas pretreatment filters, the exhaust gas interior all the way being connected with the cooling zone of zeolite runner adsorbent bed is by regeneration
After gas preheating unit, formed desorption gas, the renewing zone of the zeolite runner adsorbent bed is desorbed, after desorption exhaust gas concentration with
The cocnentration factor of inlet gas concentration is 10~20 times.
Further, it is set on the pipeline that regeneration air stream amount control device gas outlet is connected with catalysis burning bed air inlet
There is fire arrester；The catalysis burning bed includes the second heat exchanger, catalytic combustion burner and the secondary heater being sequentially connected；Described
Two heat exchangers, catalytic combustion burner and secondary heater are wrapped in carbon steel interior of shell.
Further, the catalysis burning bed includes the second heat exchanger being sequentially connected, catalytic combustion burner and the second heating
Device；The pipeline that the secondary heater is connected with catalytic combustion burner is equipped with the 5th thermocouple, the secondary heater and the
Five thermocouples are connected with PLC controller, and (gas flow temperature is adjusted after the heating that the PLC controller is detected according to the 5th thermocouple
Secondary heater uses power)；The catalytic combustion burner is equipped with the 6th thermocouple, the 6th thermocouple and PLC controller
It is connected.6th thermocouple is connected with PLC controller, for feeding back temperature in burner hearth at any time.
Further, the catalysis burning bed includes the second heat exchanger being sequentially connected, catalytic combustion burner and the second heating
Device；The First Heat Exchanger, burner hearth gas heating pipe, primary heater, the second heat exchanger, secondary heater and the catalysis
The gas pipeline that burning bed is connected with First Heat Exchanger is all made of glass fibre package heat preservation.
Further, the catalysis burning bed selects honeycomb noble metal catalyst, the catalyst active component be Pd,
Pt or Co.
Compared with prior art, the utility model have it is following the utility model has the advantages that
1. each unit that the system of the utility model uses is worked in coordination in a specific sequence, synergistic effect, final to realize
High applicability, high purification efficiency.For each specific unit, exhaust gas pretreatment filtration is led directly from by the desorption gas of renewing zone
The pipeline of device gas outlet reduces the air-intake load of whole system and will not shadow compared to the technology directly drawing air and being desorbed
Ring desorption effect.
2. the utility model is additionally arranged burner hearth gas heating pipe between the heat exchanger and heater of regeneration gas pre-heating system,
One of burner hearth gas is increased after heat exchange and mixes direct-fired process, mentions the utilization rate of catalytic combustion thermal energy significantly
Height also reduces required for heater using power, realizes energy saving purpose.
3. regeneration air stream amount control system is made of the regeneration fan parallel-connection of more different air quantity, blower and its front and back are regenerated
The concentration detection apparatus that the solenoid valve and pressure fan admission line being equipped with are equipped with is connected with PLC controller, according to different
Inlet gas concentration can open suitable regeneration blower to adjust the flow of regeneration gas, so that the cocnentration factor of exhaust gas after desorption is controlled,
In the system of the utility model, suitable cocnentration factor is 10~20 times, and the design of more regeneration fan parallel-connections farthest mentions
High applicability of the system to the organic exhaust gas of various inlet air quantity and concentration.
Detailed description of the invention
Upon reading the detailed description of non-limiting embodiments with reference to the following drawings, other spies of the utility model
Sign, objects and advantages will become more apparent upon:
Fig. 1 is that the system flow of the zeolite runner treating organic exhaust gas by adsorptive-catalytic combustion of the utility model and structure are shown
It is intended to；
Wherein, 1 is pressure fan admission line, and 2 be concentration detection apparatus, and 3 be pressure fan, and 4 be gas cooling device,
5 be fibre filter, and 6 be differential pressure indicator, and 7 be exhaust gas pretreatment filters, and 8 be zeolite runner adsorbent bed, and 8a is absorption
Area, 8b are renewing zone, and 8c is cooling zone, and 9 be driver, and 10 be First Heat Exchanger, and 11 be burner hearth gas heating pipe, 12
It is regeneration gas preheating unit for primary heater, 13,14 is regenerate blower, and 15 be regeneration air stream amount control device, and 16 are
Fire arrester, 17 be PLC controller, and 18 be the second heat exchanger, 19 be secondary heater, 20 is catalytic combustion burner, 21 be to urge
Change burning bed, 22 be exhaust apparatus, and 23 be first flow detection device, and 24 be second flow detection device, and 25 be third
Flow detector, 26 be the first hygrometer, and 27 be the second hygrometer, and 28 be the first thermocouple, and 29 be the second thermocouple,
30 be third thermocouple, and 31 be the 4th thermocouple, and 32 be the 5th thermocouple, and 33 be the 6th thermocouple, and 34 be the first electromagnetism
Valve, 35 be second solenoid valve, and 36 be third solenoid valve, and 37 be the 4th solenoid valve, and 38 be the 5th solenoid valve.
Specific embodiment
The utility model is described in detail combined with specific embodiments below.Following embodiment will be helpful to this field
Technical staff further understands the utility model, but does not limit the utility model in any form.It should be pointed out that ability
For the those of ordinary skill in domain, without departing from the concept of the premise utility, various modifications and improvements can be made.
These are all within the protection scope of the present invention.
Embodiment
As shown in Figure 1, the system of the zeolite runner treating organic exhaust gas by adsorptive-catalytic combustion of the utility model includes exclusive
Pull the pressure fan 3 of exhaust gas, exclusive cooling exhaust gas, de- exhaust gas and dust exhaust gas pretreatment filters 7, it is exclusive collect adsorption/desorption in
One realize exhaust gas concentration with adsorption zone, cooling zone and the zeolite of renewing zone runner adsorbent bed 8, exclusive preheating regeneration gas
Regeneration gas preheating unit 13, the exclusive regeneration air stream amount control device 15 for adjusting exhaust gas cocnentration factor, the entire system of exclusive automatic control
The PLC controller 17 of system operation, the exclusive catalysis burning bed 21 and the high idle discharge of exclusive exhaust gas that catalyst combustion reaction is carried out to exhaust gas
The exhaust apparatus 22 put.The pressure fan admission line 1 is equipped with first flow detection device 23 and concentration detection apparatus 2, institute
Stating regeneration gas preheating unit 13 includes First Heat Exchanger 10, burner hearth gas heating pipe 11 and primary heater 12, the burner hearth gas
11 one end of heating pipe connection catalysis burning bed 21, the other end are connected to the pipe between First Heat Exchanger 10 and primary heater 12
Road；The pressure fan 3, exhaust gas pretreatment filters 7 are sequentially connected, and the outlet pipe of the exhaust gas pretreatment filters 7 is divided into
Two-way is sequentially connected with the adsorption zone 8a of zeolite runner adsorbent bed 8, exhaust apparatus 22 all the way, and another way and zeolite runner adsorb
The cooling zone 8c of bed 8, First Heat Exchanger 10, primary heater 12, renewing zone 8b, regeneration air stream amount control device 15, catalysis combustion
Bed 21, First Heat Exchanger 10 and exhaust apparatus 22 is burnt to be sequentially connected；The PLC controller 17 is located with pressure fan 3, exhaust gas in advance respectively
Filter 7, regeneration gas preheating unit 13, regeneration air stream amount control device 15, catalysis burning bed 21 is managed to connect.
The regeneration air stream amount control device 15 includes the regeneration blower fan group 14 of at least two different air quantity parallel connections；It is described
PLC controller 17 is connected with the control valve on each pipeline.
For the adsorption effect for ensuring zeolite runner adsorbent bed 8, the exhaust gas pretreatment filters 7 are successively set along airintake direction
There are gas cooling device 4 and fibre filter 5, the first hygrometer 26, the are being respectively equipped at air inlet and gas outlet
Two hygrometers 27, gas outlet are equipped with the first thermocouple 28；It is additionally provided with differential pressure indicator 6 on the fibre filter 5, for feeding back fibre
The stopping state of dimensional filter device.
To ensure that absorption, regeneration and the cooling procedure of zeolite runner adsorbent bed 8 reach expected requirement, driver 9 can
Frequency control revolving speed；Meanwhile adsorption zone 8a optimal adsorption temperature be 20~40 DEG C, the best desorption temperature of renewing zone 8b be 150~
200℃。
Exhaust gas is entered by pressure fan admission line 1, is divided into two strands after exhaust gas pretreatment filters 7 by pressure fan 3,
First strand of exhaust gas adjusts flow by regeneration air stream amount control device 15, and the cooling zone 8c into zeolite runner adsorbent bed 8 is blown
After cold, desorption gas is formed after the heating of regeneration gas preheating unit 13, the renewing zone 8b of zeolite runner adsorbent bed 8 is taken off
Attached, the desorption concentration exhaust gas of formation enters catalysis burning bed 21 by regeneration blower 14, completes catalyst combustion reaction and forms CO2With
270, the high-temperature gas of formation is after the First Heat Exchanger 10 of regeneration gas preheating unit 13 by 22 qualified discharge of exhaust apparatus；The
Two strands of exhaust gas are directly entered the adsorption zone 8a of zeolite runner adsorbent bed 8, directly reach through exhaust apparatus 22 after being adsorbed by zeolite
Mark discharge.
It is all provided on every regeneration fan air inlet and gas outlet pipeline in parallel in the regeneration air stream amount control device 15
There are solenoid valve, respectively the first solenoid valve 34, second solenoid valve 35, third solenoid valve 36, the 4th solenoid valve 37, the regeneration wind
Flow detector is equipped with before the first, second solenoid valve 34,35 that machine air inlet duct is equipped with, respectively second flow detects
Device 24, third flow detector 25, first, second, third and fourth solenoid valve 34,35,36,37 and regeneration blower 14 with
PLC controller is connected；First flow detection device 23 that the pressure fan admission line 1 is equipped with, concentration detection apparatus 2 are distinguished
It is connected with PLC controller, according to the difference of inlet gas concentration, by the first and second of PLC controller control regeneration gas control unit 15,
Three, four solenoid valves 34,35,36,37 and regeneration blower 14 make exhaust gas after desorption reach suitable concentration to adjust air-flow size
Than reasonable cocnentration factor is 10~20 times.Applicability of the realization system to the exhaust gas of different air quantity concentration.
The burner hearth gas heating pipe 11 of the regeneration gas preheating unit 13 is equipped with the 5th solenoid valve 38, and the burner hearth gas adds
The pipeline that 11 gas outlet of heat pipeline is connected with 12 air inlet of primary heater is equipped with the second thermocouple 29, the primary heater
12 gas outlet pipelines are equipped with third thermocouple 30, the 5th solenoid valve 38, the second thermocouple 29, third thermocouple 30 and the
One heater 12 is connected with PLC controller respectively, according to the 5th solenoid valve of airflow temperature-control after burner hearth gas Hybrid Heating
38 opening degree, adjusting burner hearth throughput size, and then adjusting primary heater 12 use power, realize to make full use of and urge
Change the purpose of combustion heat energy and saves the energy.
To the concentration detection apparatus 2 in regeneration air stream amount control device 15 in this present embodiment, second flow detection device
24, third flow detector 25, first flow detection device 23 and PLC controller 17, those skilled in the art can roots
These components are realized according to the prior art, such as are bought.
To ensure safety, the admission line of the catalysis burning bed 21 is equipped with fire arrester 16.
The catalysis burning bed is made of the second heat exchanger 18, catalytic combustion burner 20 and secondary heater 19, and described second
Heat exchanger 18, secondary heater 19 and catalytic combustion burner 20 are wrapped in carbon steel interior of shell.
To ensure that there is certain temperature, secondary heater 19 and catalytic combustion burner 20 before exhaust gas enters catalytic combustion burner 20
Connected pipeline is equipped with the 5th thermocouple 32, and the secondary heater 19 and the 5th thermocouple 32 are connected with PLC controller, root
Secondary heater 19, which is adjusted, according to gas flow temperature after heating uses power；For the operational safety for ensuring catalytic combustion burner 20, set in furnace
There is the 6th thermocouple 33, the 6th thermocouple 33 is connected with PLC controller, feeds back temperature in burner hearth at any time.
It is converted completely to ensure exhaust gas in the catalytic combustion burner 20, catalyst uses honeycomb precious metal catalyst in furnace
Agent, the catalyst active component are Pd, Pt or Co etc..
For ensure exhaust gas in the loss by reducing thermal energy when heating pipe and equipment in whole system to the greatest extent, described the
One heat exchanger 10, burner hearth gas heating pipe 11, primary heater 12, the second heat exchanger 18, secondary heater 19, and catalysis combustion
It burns the gas pipeline that bed 21 is connected with First Heat Exchanger 10 and is all made of glass fibre package heat preservation.
Specific embodiment of the utility model is described above.It is to be appreciated that the utility model not office
It is limited to above-mentioned particular implementation, those skilled in the art can make various deformations or amendments within the scope of the claims,
This has no effect on the substantive content of the utility model.
Claims (10)
1. a kind of system of zeolite runner treating organic exhaust gas by adsorptive-catalytic combustion, which is characterized in that including pressure fan, exhaust gas
Pretreatment filters, with adsorption zone, cooling zone and the zeolite of renewing zone runner adsorbent bed, regeneration gas preheating unit, regeneration gas
Volume control device, PLC controller, catalysis burning bed and exhaust apparatus；The regeneration gas preheating unit include First Heat Exchanger,
Burner hearth gas heating pipe and primary heater, burner hearth gas heating pipe one end connection catalysis burning bed, the other end are connected to
Pipeline between First Heat Exchanger and primary heater；The pressure fan, exhaust gas pretreatment filters are sequentially connected, the exhaust gas
The outlet pipe of pretreatment filters is divided into two-way, and adsorption zone, the exhaust apparatus with zeolite runner adsorbent bed are sequentially connected all the way,
The cooling zone of another way and zeolite runner adsorbent bed, First Heat Exchanger, primary heater, renewing zone, regeneration gas flow control fill
It sets, be catalyzed burning bed, First Heat Exchanger and exhaust apparatus and be sequentially connected；The PLC controller is located with pressure fan, exhaust gas in advance respectively
Manage filter, regeneration gas preheating unit, regeneration air stream amount control device, catalysis burning bed connection.
2. the system of zeolite runner treating organic exhaust gas by adsorptive-catalytic combustion as described in claim 1, which is characterized in that institute
State the regeneration blower that regeneration air stream amount control device includes at least two different air quantity parallel connections, the regeneration blower and the PLC
Controller be connected, on every regeneration fan air inlet pipeline along airintake direction be successively arranged flow detector and with the PLC
The connected solenoid valve of controller, every regeneration blower outlet tube road also are provided with the solenoid valve being connected with the PLC controller；
The concentration detection apparatus that the pressure fan admission line is equipped with flow detector and is connected with the PLC controller.
3. the system of zeolite runner treating organic exhaust gas by adsorptive-catalytic combustion as described in claim 1, which is characterized in that institute
Stating exhaust gas pretreatment filters includes the gas cooling device set gradually along airintake direction and fibre filter；In fiber mistake
It filters and is respectively equipped with hygrometer at the air inlet and gas outlet of device, be additionally provided with thermocouple at the gas outlet of fibre filter,
Differential pressure indicator is additionally provided on the fibre filter.
4. the system of zeolite runner treating organic exhaust gas by adsorptive-catalytic combustion as described in claim 1, which is characterized in that institute
Zeolite runner adsorbent bed is stated by the driver frequency control of rotation rate-controllable；The adsorption zone of the zeolite runner adsorbent bed is most preferably inhaled
Enclosure temperature is 20~40 DEG C；The best desorption temperature in renewing zone of the zeolite runner adsorbent bed is 150~200 DEG C.
5. the system of zeolite runner treating organic exhaust gas by adsorptive-catalytic combustion as described in claim 1, which is characterized in that institute
The cooling air-flow for stating the cooling zone use of zeolite runner adsorbent bed leads directly from exhaust gas pretreatment filters and zeolite runner adsorbs
The connected exhaust piping of bed, the cooling air air-flow are adjusted by PLC controller control regeneration air stream amount control device.
6. the system of zeolite runner treating organic exhaust gas by adsorptive-catalytic combustion as described in claim 1, which is characterized in that institute
The burner hearth gas heating pipe for stating regeneration gas preheating unit is equipped with the 5th solenoid valve, the burner hearth gas heating pipe gas outlet and the
The connected pipeline of one heater air inlet is equipped with the second thermocouple, and primary heater gas outlet pipeline is equipped with third heat
Galvanic couple, the 5th solenoid valve, the second thermocouple, third thermocouple and primary heater are connected with PLC controller respectively.
7. the system of zeolite runner treating organic exhaust gas by adsorptive-catalytic combustion as described in claim 1, which is characterized in that institute
The renewing zone gas outlet pipeline for stating zeolite runner adsorbent bed is equipped with the 4th thermocouple.
8. the system of zeolite runner treating organic exhaust gas by adsorptive-catalytic combustion as described in claim 1, which is characterized in that institute
It states regeneration air stream amount control device gas outlet and is equipped with fire arrester with the pipeline that burning bed air inlet is connected is catalyzed；The catalysis combustion
Burning bed includes the second heat exchanger, catalytic combustion burner and the secondary heater being sequentially connected；Second heat exchanger, catalytic combustion burner
Carbon steel interior of shell is wrapped in secondary heater.
9. the system of zeolite runner treating organic exhaust gas by adsorptive-catalytic combustion as described in claim 1, which is characterized in that institute
Stating catalysis burning bed includes the second heat exchanger, catalytic combustion burner and the secondary heater being sequentially connected；The secondary heater with
The pipeline that catalytic combustion burner is connected is equipped with the 5th thermocouple, the secondary heater and the 5th thermocouple and PLC controller
It is connected；The catalytic combustion burner is equipped with the 6th thermocouple, and the 6th thermocouple is connected with PLC controller.
10. the system of zeolite runner treating organic exhaust gas by adsorptive-catalytic combustion as described in claim 1, which is characterized in that institute
Stating catalysis burning bed includes the second heat exchanger, catalytic combustion burner and the secondary heater being sequentially connected；The First Heat Exchanger, furnace
Thorax gas heating pipe, primary heater, the second heat exchanger, secondary heater and the catalysis burning bed and First Heat Exchanger phase
Gas pipeline even is all made of glass fibre package heat preservation.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821276142.0U CN208694621U (en) | 2018-08-08 | 2018-08-08 | The system of zeolite runner treating organic exhaust gas by adsorptive-catalytic combustion |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821276142.0U CN208694621U (en) | 2018-08-08 | 2018-08-08 | The system of zeolite runner treating organic exhaust gas by adsorptive-catalytic combustion |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208694621U true CN208694621U (en) | 2019-04-05 |
Family
ID=65941883
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821276142.0U Active CN208694621U (en) | 2018-08-08 | 2018-08-08 | The system of zeolite runner treating organic exhaust gas by adsorptive-catalytic combustion |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208694621U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108854446A (en) * | 2018-08-08 | 2018-11-23 | 浙江省环境工程有限公司 | The system of zeolite runner treating organic exhaust gas by adsorptive-catalytic combustion |
| CN113769539A (en) * | 2021-10-29 | 2021-12-10 | 天津天迈节能设备有限公司 | Zeolite runner all-in-one machine and waste gas treatment process method |
-
2018
- 2018-08-08 CN CN201821276142.0U patent/CN208694621U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108854446A (en) * | 2018-08-08 | 2018-11-23 | 浙江省环境工程有限公司 | The system of zeolite runner treating organic exhaust gas by adsorptive-catalytic combustion |
| CN108854446B (en) * | 2018-08-08 | 2024-05-28 | 浙江省环境工程有限公司 | System for zeolite runner adsorption-catalytic combustion handles organic waste gas |
| CN113769539A (en) * | 2021-10-29 | 2021-12-10 | 天津天迈节能设备有限公司 | Zeolite runner all-in-one machine and waste gas treatment process method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN108854446A (en) | The system of zeolite runner treating organic exhaust gas by adsorptive-catalytic combustion | |
| CN208824192U (en) | A high-efficiency adsorption and desorption catalytic combustion treatment system for VOCs waste gas | |
| CN105749695B (en) | A kind of low concentration, Wind Volume, high peculiar smell exhaust gas concentration energy equipment and its technique | |
| CN108273358B (en) | Organic waste gas treatment system and treatment method thereof | |
| CN105371286A (en) | Preheat type catalytic combustion system for purifying volatile organic waste gas | |
| CN211084096U (en) | System for treating high-boiling-point organic waste gas by zeolite rotary wheel adsorption-catalytic combustion | |
| CN103920362A (en) | Exhaust gas treatment device and method by virtue of online desorption and degradation | |
| CN205760438U (en) | A kind of activated carbon adsorption concentration for processing VOCs and the integrating device of regenerative thermal oxidizer | |
| CN204485594U (en) | Based on color-coating line exhaust-gas treatment and the heat recovery system of concentration runner and RTO | |
| CN104474844A (en) | Color-coating line waste gas treatment and heat recovery method and system based on concentration rotating wheels and RTO (regenerative thermal oxidizer) | |
| CN107694282A (en) | Utilize the technique and device of activated carbon processing organic exhaust gas | |
| CN206617949U (en) | Lacquer spraying waste gas charcoal absorption desorption catalyzing burner | |
| CN204494431U (en) | Based on color-coating line exhaust-gas treatment and the heat recovery system of thermal accumulating incinerator | |
| CN104696972A (en) | Color coating line waste-gas-treating and heat-recovering method and system based on regenerative thermal oxidizer | |
| CN111672265A (en) | A volatile organic compound waste gas treatment system | |
| CN109701358B (en) | Organic waste gas adsorption and catalytic combustion combined system and process thereof | |
| CN208694621U (en) | The system of zeolite runner treating organic exhaust gas by adsorptive-catalytic combustion | |
| TW201027008A (en) | Temperature-control device in the processing system of volatile organic exhaust gas, and method thereof | |
| CN104096450A (en) | Efficient rotating wheel adsorption device for waste gas treatment | |
| CN101893248A (en) | Energy-saving device of volatile organic waste gas treatment system | |
| CN105240864A (en) | Catalytic combustion system and catalytic combustion method | |
| WO2022142424A1 (en) | Voc treatment rotating-wheel system and voc treatment method | |
| CN206613339U (en) | New RTO catalytic combustion systems | |
| CN211725246U (en) | VOCs adsorbs-catalytic combustion system | |
| CN205424950U (en) | Purify volatile organic exhaust gas's preheating -type catalytic combustion system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |