沸石转轮吸附脱附+CO组合工艺待处理废气经过干式过滤器，由干式过滤器滤除杂质后的废气进入沸石转轮，被沸石转轮吸附处理后的气体达标排入大气中。脱附风机将转轮排放口的一部分气体抽吸出来，经过CO燃烧炉的二级换热器加热后，进入转轮的脱附段，根据转轮脱附进口温度控制电加热器的开启，保证脱附温度≥180。选沸石转轮CO抛装式就找河北清大环保机械有限公司， 沸石浓缩转轮+催化燃烧系统是我司多年来根据实际工程经验所选择出的适合处理大风量、低浓度的挥发性有机废气装置。系统主要由预处理装置、沸石浓缩转轮装置、催化净化装置、风机、烟囱等组成。

The waste gas to be treated by the combination process of zeolite wheel adsorption and desorption+CO passes through a dry filter, and after impurities are filtered out by the dry filter, the waste gas enters the zeolite wheel. The gas that is adsorbed and treated by the zeolite wheel meets the standard and is discharged into the atmosphere. The desorption fan extracts a portion of the gas from the discharge outlet of the impeller, which is heated by the secondary heat exchanger of the CO combustion furnace, and then enters the desorption section of the impeller. The electric heater is controlled to turn on according to the inlet temperature of the impeller desorption, ensuring that the desorption temperature is ≥ 180. If you choose the zeolite wheel CO throwing type, you can find Hebei Qingda Environmental Protection Machinery Co., Ltd. The zeolite concentration wheel+catalytic combustion system is a device that our company has selected for many years based on practical engineering experience, suitable for processing high air volume and low concentration volatile organic waste gas. The system mainly consists of pre-treatment device, zeolite concentration rotary device, catalytic purification device, fan, chimney, etc.

系统原理：主要利用沸石分子筛的多孔吸附性及催化燃烧在温度300-400在催化剂的作用下将有机组分中的C、H化合物氧化成无害的CO2、H2O等。装置原理及特点（1）吸附性能佳：沸石转轮具有与活性炭一样多微孔的吸附特性；

System principle: It mainly utilizes the porous adsorption of zeolite molecular sieves and catalytic combustion to oxidize C and H compounds in organic components into harmless CO2, H2O, etc. under the action of catalysts at temperatures of 300-400. Principle and characteristics of the device (1) Excellent adsorption performance: The zeolite wheel has the same porous adsorption characteristics as activated carbon;

（2）稳定性：蜂窝状沸石转轮具有性能稳定、抗腐蚀和耐高速气流冲击；

(2) Stability: The honeycomb zeolite impeller has stable performance, corrosion resistance, and resistance to high-speed airflow impact;

（3）净化：净化达95%；

(3) Purification: Purification reaches 95%;

（4）再生性能好：沸石转轮吸附饱和后可用热空气脱附再生，沸石转轮+CO撬装式一体机厂家，再生温度较高可达200，因此再生彻底。

(4) Good regeneration performance: After the zeolite wheel is saturated with adsorption, hot air can be used for desorption and regeneration. The manufacturer of the zeolite wheel+CO pry mounted integrated machine has a high regeneration temperature of up to 200, so the regeneration is thorough.

（5）转轮浓缩CO燃烧原理：再生后沸石转轮重新投入使用，通过控制脱附过程流量可将有机废气浓度浓缩10-20倍，脱附气流经催化床的加热器装置加热至300左右，在催化剂作用下起燃，催化燃烧过程净化效率可达97%以上，燃烧后生成RCO2 和H2O 并释放出大量热量，该热量通过催化燃烧床内的热交换器一部分再用来加热脱附出的高浓度废气，沸石转轮+CO撬装式一体机，另外一部分加热室外来的空气做沸石转轮脱附气体使用，一般达到脱附～催化燃烧自平衡过程须启动燃烧器1小时左右。达到热平衡后可关闭电加热装置，沸石转轮+CO撬装式一体机定制，这时再生处理系统靠废气中的做燃料，在无须外加能源基础上使再生过程达到自平衡循环，极大地减少能耗，并且无二次污染的产生，整套吸附和催化燃烧过程由PLC实现自动控制。

(5) The principle of CO concentration combustion by rotary wheel: After regeneration, the zeolite rotary wheel is put back into use. By controlling the flow rate of the desorption process, the concentration of organic waste gas can be concentrated 10-20 times. The desorption gas flows through the heater device of the catalytic bed and is heated to about 300. Under the action of the catalyst, it ignites, and the purification efficiency of the catalytic combustion process can reach over 97%. After combustion, RCO2 and H2O are generated, releasing a large amount of heat, This heat is partially used by the heat exchanger inside the catalytic combustion bed to heat the high concentration exhaust gas that is desorbed. The zeolite wheel+CO pry mounted integrated machine is used, and the air outside the heating chamber is used as the zeolite wheel desorbed gas. Generally, the process of desorbing to catalytic combustion self equilibrium requires the burner to be started for about 1 hour. After reaching thermal equilibrium, the electric heating device can be turned off, and the zeolite wheel+CO pry mounted integrated machine can be customized. At this time, the regeneration treatment system relies on the fuel in the exhaust gas to achieve a self balancing cycle in the regeneration process without the need for additional energy, greatly reducing energy consumption and avoiding the generation of secondary pollution. The entire adsorption and catalytic combustion process is automatically controlled by PLC.

工艺流程:

Process flow:

1）甲方废气先经过干式过滤预处理箱体去除废气中的粉尘等颗粒物，防止该类物质进入到沸石转轮中引起转轮效率下降；

1) The exhaust gas of Party A is first subjected to dry filtration pretreatment box to remove dust and other particulate matter from the exhaust gas, preventing such substances from entering the zeolite wheel and causing a decrease in wheel efficiency;

2）经预处理后的废气，进入沸石转轮吸附区，废气中的VOCs被吸附、净化后直接达标排放，而吸附过VOCs的沸石随转轮转动进入冷却区，在原有废气风量15~25分之一的常温气体作用下冷却下来（110），随后在冷却风机作用下经电加热器预热至脱附温度：180~220（亦可以通过催化床排放高温气体换热预热），将VOCs从沸石中脱附出来，形成小风量、高浓度的VOCs尾气；

2) After pre-treatment, the exhaust gas enters the zeolite wheel adsorption area. VOCs in the exhaust gas are adsorbed and purified before directly meeting the emission standards. Zeolites that have adsorbed VOCs enter the cooling area with the rotation of the wheel, and are cooled by a room temperature gas with an original exhaust gas flow rate of 15-25 times (110). Then, under the action of a cooling fan, they are preheated by an electric heater to a desorption temperature of 180-220 (or can be preheated by discharging high-temperature gas through a catalytic bed for heat exchange), Desorb VOCs from zeolite to form low air volume and high concentration VOCs exhaust gas;

3）脱附产生的高浓尾气（30~60）在CO系统风机作用下经换热器预热升温、电加热器加热至催化剂活性温度（300）后，进入催化床并发生氧化分解反应、同时放出热量，该反应形成的高温尾气再依次与转轮冷却气、脱附气换热后排放。

3) The high concentration exhaust gas (30-60) generated by desorption is preheated and heated by a heat exchanger under the action of a CO system fan, and then heated by an electric heater to the catalyst activity temperature (300). It enters the catalytic bed and undergoes oxidation decomposition reaction, while releasing heat. The high-temperature exhaust gas formed by this reaction is then heat exchanged with the cooling gas and desorption gas of the impeller before being discharged.