First, by using the dry or wet filtration method, Remove the small particles from the exhaust gas, Make the organic waste gas meet the cleanliness requirements of the zeolite runner adsorption; The method of heating up and humidity reduction again, Make the organic waste gas meet the humidity requirements of the stone rotary wheel adsorption, Through the action of the fan, Pretreated organic waste gas through the adsorption zone of the zeolite wheel, Organic molecules are captured by the unique adsorption holes of the zeolite wheel, The standard adsorbed gas is discharged directly into the chimney, After a certain period of adsorption, Zeolite wheel adsorption area will be adsorption saturation, this moment, Using small heat (200-230℃) over the stripping zone of the zeolite wheel, The organic matter is removed from the zeolite and burned into the RTO high temperature (750℃) by the fan method, To regenerate the zeolite, So cycle, Since the zeolite is purged by a hot wind, The temperature becomes high enough to absorb organic matter, At this time, the zeolite needs to be cooled to cool it to room temperature, Ensure its adsorption efficiency.

Step 1: adsorption concentrated flue gas is adsorbed through the zeolite in the runner, and the clean exhaust gas is discharged into the atmosphere by the system extraction and frequency conversion fan; the adsorbent can provide a large amount of gas contact with the zeolite surface area, and the runner continues to rotate at a speed of 1~6 revolutions.

Step 2: the VOCs in the desattachment wheel is concentrated into a saturated zeolite area, and the heat current provided by the heat exchanger (about 200℃) is used for desattachment. After the desattachment, the cooling area is cooled to normal temperature with normal temperature air, and then rotated to the adsorption concentration area.

> The material itself is not combustible, can be used safely at 600℃ ambient temperature, hydrophobic products

> With excellent de-attachment performance, in about 300 °℃, de-attachment time, complete, no secondary pollution.

> Is the best material to replace honeycomb activated carbon, can be high temperature stripping, desorption thoroughly.

> Product size: can be determined according to customer needs

Combination 1: Zeolite rotating wheel + RCO

Zeolite runner + RCO is mainly composed of zeolite runner concentration (adsorption area, stripping area, cooling area), stripping system, pretreatment device, preheating device, catalytic combustion device and explosion-proof device.

Process features:

(1) Establishment of internal bypass circulation in the adsorption zone.When the waste gas does not reach the standard after adsorption through the adsorption area, it enters the bypass cycle and conducts adsorption treatment again.The basic idea of this bypass internal circulation is to eliminate the existing pollution and then absorb the new pollution.

(2) Establishment of cooling air bypass.In the case of very complex working conditions, the VOCs concentration may rise sharply. At this time, some cooling wind is introduced into the adsorption area to reduce the detached air volume, and the fresh air is supplemented after heat transfer 2 to maintain the air volume into the catalytic reactor within the preset range.The basic idea of this bypass is to dilute the high concentration of VOCs with fresh air, so from the effect, this method will also extend the governance time.

(3) Compared with the traditional process, the whole system adopts the design of induced draft fan to facilitate the regulation of bypass.Remove the cooling blower for the catalytic combustion device, treat the symptoms and control the VOCs concentration in the runner.

(4) The electric auxiliary heat system is removed from the catalytic combustion chamber, by heating the air from heat transfer 2 to the VOCs combustion temperature, and stabilizing the temperature of the catalytic combustion chamber within the range of 500℃ ~600℃.

(5) The runner speed is easy to adjust, so in the case of 2, the runner speed can be appropriately increased to reduce the amount of VOCs adsorption per unit time per unit area, so as to ensure the safety of the system.

Combination 2: zeolite runner + RTO

Zeolite runner + RTO process is mainly composed of zeolite runner concentration (adsorption area, stripping area, cooling area), heat storage system, regenerative combustion system (RTO furnace body, ceramic heat storage body, combustion system, etc.) and control system and other parts.

Process Flow:

Adsorption and deattachment: zeolite sieve wheel adsorption concentration system uses adsorption & amp; & amp; cooling this continuous process, adsorption concentration of VOCs waste gas, zeolite sieve wheel is divided into three functional areas: adsorption zone, deattachment zone and cooling zone, and cooling area.The exhaust gas enters the adsorption area of the zeolite molecular sieve wheel, and the VOCs is adsorbed and removed by the zeolite molecular sieve and discharged after purification.VOCs adsorbed in the molecular sieve wheel is deannexed and concentrated in the detachment zone after about 200oC small air volume.The regenerated zeolite sieve wheel is cooled in the cooling zone so repeatedly.

Thermal storage combustion: the high concentration of small air volume waste gas after deattachment enters the RTO treatment system and first enters the ceramic dielectric layer of RTO heat storage chamber A. The ceramic releases heat and the temperature decreases, while the organic waste gas absorbs heat and the temperature increases. After leaving the waste gas enters the oxidation chamber at a higher temperature.In the oxidation chamber, the organic exhaust gas is heated by the burner to a set oxidation temperature above 800oC, so that the VOCs is decomposed into carbon dioxide and water.

Suitable for high volume, low concentration, including: printing, large spraying workshop, furniture, chips, liquid crystal LED industry and other production places.