焚燒工藝廢氣處理工業廢氣匯總
濃縮轉輪/焚燒爐rotorconcentrator/oxidizer
濃縮轉輪/焚燒爐系統吸附大風量低濃度揮發性有機化合物(vocs)。再把脫附后小風量高濃度廢氣導入焚燒爐予以分解凈化。大風量低濃度的vocs廢氣，通過一個由沸石為吸附材料的轉輪，vocs經被轉輪吸附區的沸石所吸附后凈化的氣體經煙囪排到大氣，再于脫附區中用180℃~200℃的小量熱空氣，將vocs予以脫附。如此一高濃度小風量的脫附廢氣在導入焚燒爐中予以分解為二氧化碳及水氣，凈化的氣體經煙囪排到大氣。這一濃縮的工藝大大地降低燃料費用。
氯化有機物催化劑焚燒爐
氯化有機物催化劑焚燒爐(chlorinatedcatalyticoxidizer)系統依風量，污染物種類及所需去除效率而設計。
在運行操作時，含vocs的廢氣經氯化有機物催化劑焚燒爐風機抽到系統換熱器中。廢氣通過換熱器的管側，再到燃燒機，此處將廢氣加熱到催化劑反應溫度。含vocs廢氣通過特制的抗鹵化物毒化的催化劑，轉化成二氧化碳，水氣并放出熱。這熱凈化的氣體通過換熱器的殼側，將熱能加熱浸入系統的廢氣，如此可以將燃料費用降到最小，在許多時候，如vocs濃度夠高，可以不需額外燃料系統即可自行運轉。最后如有需要，可裝設恩國洗滌塔以去除無機酸(如hcl，cl2，hbr，br2等)。 套裝洗滌塔(hclscrubbermodule)，套裝洗滌塔出口含hcl或cl2的氣體導入套裝洗滌塔中的驟冷塔，循環汞噴注大量的水進入用超合金(hastelloy)材質的驟冷塔(quenches)。這時水會把熱廢氣降溫并將部分的予以吸收，之后經一氣道進入逆流式的吸收塔。循環吸收溶液從吸收塔頂部的噴嘴噴灑而下，將剩余的充份吸收，然后通過一除水層把水滴去除，再排到大氣。
自動清理陶瓷過濾系統
自動清理陶瓷過濾系統(self-cleaningceramicfilter)系依排風量，污染物種類和所需補及過濾效率有關。系統操作運行時，排自工藝廢氣(含有冷或熱有機粒狀物/有機凝結物質或vocs)。被抽引至陶瓷過濾器中。廢氣通過依粒狀物之例徑大小及捕集效率大小而設計選用的陶瓷板，一組燃燒器，間歇或連續加熱此一陶瓷板，使被捕集于此一陶瓷板的有機粒狀物揮發而進到焚燒爐中，任何無機物被燒成無機灰并掉至腔體底部而予以收集。經揮發的有機物導至焚燒爐中(如催化劑式焚燒爐，直燃式焚燒爐)經焚燒轉化為二氧化碳，水氣和熱氣。
rto蓄熱式焚燒爐
排放自工藝含vocs的廢氣進入雙槽rto，三向切換風閥(poppetvalve)將此廢氣導入rto的蓄熱槽(energyrecoverychamber)而預熱此廢氣，含污染的廢氣被蓄熱陶塊漸漸地加熱后進入燃燒室(combustionchamber)，vocs在燃燒室被氧化而放出熱能于第二蓄熱槽中之陶塊，用以減少輔助燃料的消耗。陶塊被加熱，燃燒氧化后的干凈氣體逐漸降低溫度，因此出口溫度略高于rto入口溫度。三向切換風閥切換改變rto出口/入口溫度。如果vocs濃度夠高，所放出的熱能足夠時，rto即不需燃料。例如rto熱回收效率為95%時，rto出口僅較入口溫度高25℃而已。
蓄熱式催化劑焚燒爐(rco)
排放自工藝含vocs的廢氣進入雙槽rco，三向切換風閥(poppetvalve)將此廢氣導入rco的蓄熱槽(energyrecoverychamber)而預熱此廢氣，含污染的廢氣被蓄熱陶塊漸漸地加熱后進入催化床(catalystbed)，vocs在經催化劑分解被氧化而放出熱能于第二蓄熱槽中之陶塊，用以減少輔助燃料的消耗。陶塊被加熱，燃燒氧化后的干凈氣體逐漸降低溫度，因此出口溫度略高于rco入口溫度。三向切換風閥切換改變rco出口/入口溫度。如果vocs濃度夠高，所放出的熱能足夠時，rco即不需燃料。例如rco熱回收效率為95%時，rco出口僅較入口溫度高25℃而已。
催化劑焚燒爐catalyticoxidizer
催化劑焚燒爐的設計是依廢氣風量，vocs濃度及所需知破壞去除效率而定。操作時含vocs的廢氣用系統風機導入系統內的換熱器，廢氣經由換熱器管側(tubeside)而被加熱后，再通過燃燒器，這時廢氣已被加熱至催化分解溫度，再通過催化劑床，催化分解會釋放熱能，而vocs被分解為二氧化碳及水氣。之后此一熱且經凈化氣體進入換熱器之殼側(shellside)將管側(tubeside)未經處理的voc廢氣加熱，此換熱器會減少能源的消耗，最后，凈化后的氣體從煙囪排到大氣中。
直燃式焚燒爐的設計是依廢氣風量，vocs濃度及所需知破壞去除效率而定。操作時含vocs的廢氣用系統風機導入系統內的換熱器，廢氣經由換熱器管側(tubeside)而被加熱后，再通過燃燒器，這時廢氣已被加熱至催化分解溫度(650~1000℃)，并且有足夠的留置時間(0.5~2.0秒)。這時會發生熱反應，而vocs被分解為二氧化碳及水氣。之后此一熱且經凈化氣體進入換熱器之殼側(shellside)將管側(tubeside)未經處理的voc廢氣加熱，此換熱器會減少能源的消耗(甚至于某適當的vocs濃度以上時便不需額外的燃料)，最后，凈化后的氣體從煙囪排到大氣中。
直接燃燒焚燒爐directfiredthermaloxidizer-dfto
有時直接燃燒焚燒爐源于后燃燒器(after-burner)，直接燃燒焚燒爐使用經特別設計的燃燒器以加熱高濃度的廢氣到ㄧ預先設的溫度，于運轉時廢氣被導入燃燒室(burnerchamber)。燃燒器將vocs及有毒空氣污染物分解為無毒的物質(二氧化碳及水)并放出熱，凈化后的氣體可再由一熱回收系統以達節能的需求。
rotor concentrator / incinerator rotorconcentrator / oxidizer
rotor concentrator / incinerator system adsorption air volume low concentration of volatile organic compounds (vocs). after a small amount of wind then desorbed gas is introduced into a high concentration of incinerators decomposition purification. low wind concentration of vocs emissions, by a zeolite adsorbent material for the wheel, vocs are adsorbed by the zeolite after adsorption zone runner purified gas to the atmosphere through the chimney, and then by desorption zone at 180 ℃ ~ a small amount of hot air 200 ℃ will be desorbed vocs. such a high concentration of small amounts of desorbed gas in the air introduced into the incinerator to be decomposed into carbon dioxide and water vapor, purified gas through the chimney into the atmosphere. the enrichment process greatly reduced fuel costs.
the catalyst of chlorinated organics incinerator
chlorinated organics catalyst incinerator (chlorinatedcatalyticoxidizer) system by air flow, contaminant species and required removal efficiency and design.
when you run the operation by the exhaust gas catalyst of chlorinated organics incinerator blower system containing vocs evacuated heat exchanger. pipe-side exhaust gas through the heat exchanger, to the burner, where the catalyst is heated to the reaction temperature of the exhaust gas. exhaust gases containing vocs by a special anti-halide catalyst poisoning, into carbon dioxide, water vapor and emit heat. this hot purified gas through the shell side of the heat exchanger, the exhaust gas heat heating immersion systems, so fuel costs can be reduced to a minimum, in many cases, such as vocs concentration is high enough, you can no additional fuel system to run itself . finally, if necessary, can be installed anguil scrubber to remove inorganic acid (such as hcl, cl2, hbr, br2, etc.). hydrogen chloride suit scrubber (hclscrubbermodule), gaseous hydrogen chloride suit scrubber outlet containing hcl or cl2 introducing hydrogen chloride suit scrubber quench tower, circulating mercury injection amount of water entering with superalloy (hastelloy) material quench tower ( quenches). then the water will cool the hot exhaust gases and hydrogen chloride to be absorbed part, after a stretch through the tract into the counterflow absorber. circulating the absorption solution from the absorber spray nozzle at the top, fully absorb the remaining hydrogen chloride, and then a layer to remove water droplets removed, then vented to the atmosphere.
ceramic filter automatic clean-up system
automatic clean-up ceramic filter system (self-cleaningceramicfilter) exhaust system according to the amount and types of pollutants required to fill and filtration efficiency related. operating system is running, exhaust gas from the process (cold or hot containing organic particulate matter / organic coagulant substance or vocs). by evacuating to the ceramic filter. example path through the exhaust gas according to the size and the size of the particulate matter collection efficiency of the design chosen ceramic plate, a burner, a batch or a continuous heating the ceramic plates that trapped here a ceramic plate and volatile organic particulate matter into the incinerator and be collected by any of the inorganic ashes and inorganic burned off to the bottom of the cavity. by volatile organic compounds lead to the incinerator (catalyst incinerator, direct-fired incinerator) by incineration is converted to carbon dioxide, water vapor and heat.
rto regenerative thermal oxidizer
emissions from process exhaust gases containing vocs into the double slot rto, three-way switching valve (poppetvalve) this gas is introduced into the storage tank rto (energyrecoverychamber) and preheat the exhaust gas, containing contaminated waste gas is gradually heated regenerative ceramic block after entering the combustion chamber (combustionchamber), vocs are oxidized in the combustion chamber and heat energy is released in the second heat storage tank of the ceramic block, to reduce the consumption of auxiliary fuel. ceramic block is heated, clean combustion gas after oxidation gradually lowering the temperature, so the outlet temperature slightly higher than the rto inlet temperature. three-way switching valve is switched to change the rto outlet / inlet temperature. if vocs concentration is high enough, the released heat enough, rto ie without fuel. for example rto heat recovery efficiency of 95%, rto inlet temperature higher than the export only 25 ℃ only.
regenerative catalyst incinerator (rco)
emissions from process exhaust gases containing vocs into the double slot rco, three-way switching valve (poppetvalve) this gas is introduced into the storage tank rco (energyrecoverychamber) and preheat the exhaust gas, containing contaminated waste gas is gradually heated regenerative ceramic block after entering the catalytic bed (catalystbed), vocs by decomposition catalyst in the oxidation of heat energy is released in the second heat storage tank of the ceramic block, to reduce the consumption of auxiliary fuel. ceramic block is heated, clean combustion gas after oxidation gradually lowering the temperature, so the outlet temperature slightly higher than the inlet temperature of the rco. three-way switching valve is switched to change the rco outlet / inlet temperature. if vocs concentration is high enough, the released heat enough, rco ie without fuel. for example rco heat recovery efficiency of 95%, rco export only higher than the inlet temperature is 25 ℃ only.
the catalyst incinerator catalyticoxidizer
the catalyst incinerator is designed according to the exhaust air flow, vocs concentration and destruction removal efficiency required to be known. operation with exhaust gas heat exchanger into the system within the wind turbine system containing the vocs, after the exhaust gas is heated by the heat exchanger tube side (tubeside), then through the burner, then the exhaust gas had been heated to a temperature of the catalytic decomposition, and then by catalyst bed catalytic decomposition releases heat, and vocs are decomposed into carbon dioxide and water vapor. after a hot and purified gas into the shell side of the heat exchanger (shellside) heating the tube voc exhaust side (tubeside) untreated, this heat exchanger will reduce energy consumption, and finally, purified gas from the chimney vented to the atmosphere.
direct-fired incinerator is designed according to the exhaust air flow, vocs concentration and destruction removal efficiency required to be known. operation with exhaust gas heat exchanger into the system within the wind turbine system containing the vocs, after the exhaust gas is heated by the heat exchanger tube side (tubeside), then through the burner, when the exhaust gas has been heated to the catalytic decomposition temperature (650 ~ 1000 ℃), and sufficient retention time (0.5 to 2.0 seconds). then undergo thermal reactions, and vocs are decomposed into carbon dioxide and water vapor. after a hot and purified gas into the shell side of the heat exchanger (shellside) the tube side (tubeside) untreated voc gas heating, the heat exchanger will reduce energy consumption (more than adequate even certain vocs concentration when they do not need additional fuel), and finally, purified gas from the chimney into the atmosphere.
direct fired incinerator directfiredthermaloxidizer-dfto
sometimes directly from the combustion incinerator afterburner (after-burner), direct fired incinerator using specially designed burners to heat the exhaust gas to a high concentration ㄧ preset temperature, when in operation the exhaust gas is introduced into the combustion chamber (burnerchamber ). burner vocs and toxic air pollutants decomposed into non-toxic substances (carbon dioxide and water) and release heat, the gas can be further purified by a heat recovery system to achieve energy needs.
關鍵詞：焚燒爐 催化劑 換熱器 洗滌塔 吸收塔
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濃縮轉輪/焚燒爐系統吸附大風量低濃度揮發性有機化合物(vocs)。再把脫附后小風量高濃度廢氣導入焚燒爐予以分解凈化。大風量低濃度的vocs廢氣，通過一個由沸石為吸附材料的轉輪，vocs經被轉輪吸附區的沸石所吸附后凈化的氣體經煙囪排到大氣，再于脫附區中用180℃~200℃的小量熱空氣，將vocs予以脫附。如此一高濃度小風量的脫附廢氣在導入焚燒爐中予以分解為二氧化碳及水氣，凈化的氣體經煙囪排到大氣。這一濃縮的工藝大大地降低燃料費用。
氯化有機物催化劑焚燒爐
氯化有機物催化劑焚燒爐(chlorinatedcatalyticoxidizer)系統依風量，污染物種類及所需去除效率而設計。
在運行操作時，含vocs的廢氣經氯化有機物催化劑焚燒爐風機抽到系統換熱器中。廢氣通過換熱器的管側，再到燃燒機，此處將廢氣加熱到催化劑反應溫度。含vocs廢氣通過特制的抗鹵化物毒化的催化劑，轉化成二氧化碳，水氣并放出熱。這熱凈化的氣體通過換熱器的殼側，將熱能加熱浸入系統的廢氣，如此可以將燃料費用降到最小，在許多時候，如vocs濃度夠高，可以不需額外燃料系統即可自行運轉。最后如有需要，可裝設恩國洗滌塔以去除無機酸(如hcl，cl2，hbr，br2等)。 套裝洗滌塔(hclscrubbermodule)，套裝洗滌塔出口含hcl或cl2的氣體導入套裝洗滌塔中的驟冷塔，循環汞噴注大量的水進入用超合金(hastelloy)材質的驟冷塔(quenches)。這時水會把熱廢氣降溫并將部分的予以吸收，之后經一氣道進入逆流式的吸收塔。循環吸收溶液從吸收塔頂部的噴嘴噴灑而下，將剩余的充份吸收，然后通過一除水層把水滴去除，再排到大氣。
自動清理陶瓷過濾系統
自動清理陶瓷過濾系統(self-cleaningceramicfilter)系依排風量，污染物種類和所需補及過濾效率有關。系統操作運行時，排自工藝廢氣(含有冷或熱有機粒狀物/有機凝結物質或vocs)。被抽引至陶瓷過濾器中。廢氣通過依粒狀物之例徑大小及捕集效率大小而設計選用的陶瓷板，一組燃燒器，間歇或連續加熱此一陶瓷板，使被捕集于此一陶瓷板的有機粒狀物揮發而進到焚燒爐中，任何無機物被燒成無機灰并掉至腔體底部而予以收集。經揮發的有機物導至焚燒爐中(如催化劑式焚燒爐，直燃式焚燒爐)經焚燒轉化為二氧化碳，水氣和熱氣。
rto蓄熱式焚燒爐
排放自工藝含vocs的廢氣進入雙槽rto，三向切換風閥(poppetvalve)將此廢氣導入rto的蓄熱槽(energyrecoverychamber)而預熱此廢氣，含污染的廢氣被蓄熱陶塊漸漸地加熱后進入燃燒室(combustionchamber)，vocs在燃燒室被氧化而放出熱能于第二蓄熱槽中之陶塊，用以減少輔助燃料的消耗。陶塊被加熱，燃燒氧化后的干凈氣體逐漸降低溫度，因此出口溫度略高于rto入口溫度。三向切換風閥切換改變rto出口/入口溫度。如果vocs濃度夠高，所放出的熱能足夠時，rto即不需燃料。例如rto熱回收效率為95%時，rto出口僅較入口溫度高25℃而已。
蓄熱式催化劑焚燒爐(rco)
排放自工藝含vocs的廢氣進入雙槽rco，三向切換風閥(poppetvalve)將此廢氣導入rco的蓄熱槽(energyrecoverychamber)而預熱此廢氣，含污染的廢氣被蓄熱陶塊漸漸地加熱后進入催化床(catalystbed)，vocs在經催化劑分解被氧化而放出熱能于第二蓄熱槽中之陶塊，用以減少輔助燃料的消耗。陶塊被加熱，燃燒氧化后的干凈氣體逐漸降低溫度，因此出口溫度略高于rco入口溫度。三向切換風閥切換改變rco出口/入口溫度。如果vocs濃度夠高，所放出的熱能足夠時，rco即不需燃料。例如rco熱回收效率為95%時，rco出口僅較入口溫度高25℃而已。
催化劑焚燒爐catalyticoxidizer
催化劑焚燒爐的設計是依廢氣風量，vocs濃度及所需知破壞去除效率而定。操作時含vocs的廢氣用系統風機導入系統內的換熱器，廢氣經由換熱器管側(tubeside)而被加熱后，再通過燃燒器，這時廢氣已被加熱至催化分解溫度，再通過催化劑床，催化分解會釋放熱能，而vocs被分解為二氧化碳及水氣。之后此一熱且經凈化氣體進入換熱器之殼側(shellside)將管側(tubeside)未經處理的voc廢氣加熱，此換熱器會減少能源的消耗，最后，凈化后的氣體從煙囪排到大氣中。
直燃式焚燒爐的設計是依廢氣風量，vocs濃度及所需知破壞去除效率而定。操作時含vocs的廢氣用系統風機導入系統內的換熱器，廢氣經由換熱器管側(tubeside)而被加熱后，再通過燃燒器，這時廢氣已被加熱至催化分解溫度(650~1000℃)，并且有足夠的留置時間(0.5~2.0秒)。這時會發生熱反應，而vocs被分解為二氧化碳及水氣。之后此一熱且經凈化氣體進入換熱器之殼側(shellside)將管側(tubeside)未經處理的voc廢氣加熱，此換熱器會減少能源的消耗(甚至于某適當的vocs濃度以上時便不需額外的燃料)，最后，凈化后的氣體從煙囪排到大氣中。
直接燃燒焚燒爐directfiredthermaloxidizer-dfto
有時直接燃燒焚燒爐源于后燃燒器(after-burner)，直接燃燒焚燒爐使用經特別設計的燃燒器以加熱高濃度的廢氣到ㄧ預先設的溫度，于運轉時廢氣被導入燃燒室(burnerchamber)。燃燒器將vocs及有毒空氣污染物分解為無毒的物質(二氧化碳及水)并放出熱，凈化后的氣體可再由一熱回收系統以達節能的需求。
rotor concentrator / incinerator rotorconcentrator / oxidizer
rotor concentrator / incinerator system adsorption air volume low concentration of volatile organic compounds (vocs). after a small amount of wind then desorbed gas is introduced into a high concentration of incinerators decomposition purification. low wind concentration of vocs emissions, by a zeolite adsorbent material for the wheel, vocs are adsorbed by the zeolite after adsorption zone runner purified gas to the atmosphere through the chimney, and then by desorption zone at 180 ℃ ~ a small amount of hot air 200 ℃ will be desorbed vocs. such a high concentration of small amounts of desorbed gas in the air introduced into the incinerator to be decomposed into carbon dioxide and water vapor, purified gas through the chimney into the atmosphere. the enrichment process greatly reduced fuel costs.
the catalyst of chlorinated organics incinerator
chlorinated organics catalyst incinerator (chlorinatedcatalyticoxidizer) system by air flow, contaminant species and required removal efficiency and design.
when you run the operation by the exhaust gas catalyst of chlorinated organics incinerator blower system containing vocs evacuated heat exchanger. pipe-side exhaust gas through the heat exchanger, to the burner, where the catalyst is heated to the reaction temperature of the exhaust gas. exhaust gases containing vocs by a special anti-halide catalyst poisoning, into carbon dioxide, water vapor and emit heat. this hot purified gas through the shell side of the heat exchanger, the exhaust gas heat heating immersion systems, so fuel costs can be reduced to a minimum, in many cases, such as vocs concentration is high enough, you can no additional fuel system to run itself . finally, if necessary, can be installed anguil scrubber to remove inorganic acid (such as hcl, cl2, hbr, br2, etc.). hydrogen chloride suit scrubber (hclscrubbermodule), gaseous hydrogen chloride suit scrubber outlet containing hcl or cl2 introducing hydrogen chloride suit scrubber quench tower, circulating mercury injection amount of water entering with superalloy (hastelloy) material quench tower ( quenches). then the water will cool the hot exhaust gases and hydrogen chloride to be absorbed part, after a stretch through the tract into the counterflow absorber. circulating the absorption solution from the absorber spray nozzle at the top, fully absorb the remaining hydrogen chloride, and then a layer to remove water droplets removed, then vented to the atmosphere.
ceramic filter automatic clean-up system
automatic clean-up ceramic filter system (self-cleaningceramicfilter) exhaust system according to the amount and types of pollutants required to fill and filtration efficiency related. operating system is running, exhaust gas from the process (cold or hot containing organic particulate matter / organic coagulant substance or vocs). by evacuating to the ceramic filter. example path through the exhaust gas according to the size and the size of the particulate matter collection efficiency of the design chosen ceramic plate, a burner, a batch or a continuous heating the ceramic plates that trapped here a ceramic plate and volatile organic particulate matter into the incinerator and be collected by any of the inorganic ashes and inorganic burned off to the bottom of the cavity. by volatile organic compounds lead to the incinerator (catalyst incinerator, direct-fired incinerator) by incineration is converted to carbon dioxide, water vapor and heat.
rto regenerative thermal oxidizer
emissions from process exhaust gases containing vocs into the double slot rto, three-way switching valve (poppetvalve) this gas is introduced into the storage tank rto (energyrecoverychamber) and preheat the exhaust gas, containing contaminated waste gas is gradually heated regenerative ceramic block after entering the combustion chamber (combustionchamber), vocs are oxidized in the combustion chamber and heat energy is released in the second heat storage tank of the ceramic block, to reduce the consumption of auxiliary fuel. ceramic block is heated, clean combustion gas after oxidation gradually lowering the temperature, so the outlet temperature slightly higher than the rto inlet temperature. three-way switching valve is switched to change the rto outlet / inlet temperature. if vocs concentration is high enough, the released heat enough, rto ie without fuel. for example rto heat recovery efficiency of 95%, rto inlet temperature higher than the export only 25 ℃ only.
regenerative catalyst incinerator (rco)
emissions from process exhaust gases containing vocs into the double slot rco, three-way switching valve (poppetvalve) this gas is introduced into the storage tank rco (energyrecoverychamber) and preheat the exhaust gas, containing contaminated waste gas is gradually heated regenerative ceramic block after entering the catalytic bed (catalystbed), vocs by decomposition catalyst in the oxidation of heat energy is released in the second heat storage tank of the ceramic block, to reduce the consumption of auxiliary fuel. ceramic block is heated, clean combustion gas after oxidation gradually lowering the temperature, so the outlet temperature slightly higher than the inlet temperature of the rco. three-way switching valve is switched to change the rco outlet / inlet temperature. if vocs concentration is high enough, the released heat enough, rco ie without fuel. for example rco heat recovery efficiency of 95%, rco export only higher than the inlet temperature is 25 ℃ only.
the catalyst incinerator catalyticoxidizer
the catalyst incinerator is designed according to the exhaust air flow, vocs concentration and destruction removal efficiency required to be known. operation with exhaust gas heat exchanger into the system within the wind turbine system containing the vocs, after the exhaust gas is heated by the heat exchanger tube side (tubeside), then through the burner, then the exhaust gas had been heated to a temperature of the catalytic decomposition, and then by catalyst bed catalytic decomposition releases heat, and vocs are decomposed into carbon dioxide and water vapor. after a hot and purified gas into the shell side of the heat exchanger (shellside) heating the tube voc exhaust side (tubeside) untreated, this heat exchanger will reduce energy consumption, and finally, purified gas from the chimney vented to the atmosphere.
direct-fired incinerator is designed according to the exhaust air flow, vocs concentration and destruction removal efficiency required to be known. operation with exhaust gas heat exchanger into the system within the wind turbine system containing the vocs, after the exhaust gas is heated by the heat exchanger tube side (tubeside), then through the burner, when the exhaust gas has been heated to the catalytic decomposition temperature (650 ~ 1000 ℃), and sufficient retention time (0.5 to 2.0 seconds). then undergo thermal reactions, and vocs are decomposed into carbon dioxide and water vapor. after a hot and purified gas into the shell side of the heat exchanger (shellside) the tube side (tubeside) untreated voc gas heating, the heat exchanger will reduce energy consumption (more than adequate even certain vocs concentration when they do not need additional fuel), and finally, purified gas from the chimney into the atmosphere.
direct fired incinerator directfiredthermaloxidizer-dfto
sometimes directly from the combustion incinerator afterburner (after-burner), direct fired incinerator using specially designed burners to heat the exhaust gas to a high concentration ㄧ preset temperature, when in operation the exhaust gas is introduced into the combustion chamber (burnerchamber ). burner vocs and toxic air pollutants decomposed into non-toxic substances (carbon dioxide and water) and release heat, the gas can be further purified by a heat recovery system to achieve energy needs.
關鍵詞：焚燒爐 催化劑 換熱器 洗滌塔 吸收塔
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