环境工程学报
環境工程學報
배경공정학보
CHINESE JOURNAL OF ENVIRONMENTAL ENGINEERING
2010年
4期
909-914
,共6页
蒋旭光%费振伟%陆胜勇%李春雨%安春国%池涌%严建华%俞恺%潘金华%施政
蔣旭光%費振偉%陸勝勇%李春雨%安春國%池湧%嚴建華%俞愷%潘金華%施政
장욱광%비진위%륙성용%리춘우%안춘국%지용%엄건화%유개%반금화%시정
危险废物%回转式流化冷渣%升温曲线%热解%污染物排放
危險廢物%迴轉式流化冷渣%升溫麯線%熱解%汙染物排放
위험폐물%회전식류화랭사%승온곡선%열해%오염물배방
hazardous waste%rotary fluidizing and ash-cooling%temperature curve%pyrolysis%pollutant emission
危险废物的处理和处置是摆在我国各级市政府面前的紧迫任务.然而我国已经运行的危险废物焚烧装置普遍存在回转窑挂壁结渣、热灼减率偏高和污染排放超标等问题,作者通过将回转窑和流化床特点相结合的方法提出了一种新型危险废物回转式流化冷渣多段焚烧处置装置.该装置采用回转窑(一燃室)、二燃室和流化床结合的热解-流化焚烧工艺,特别是采用控制窑头温度避免了回转窑挂壁结渣;采用流化冷渣装置延长未燃烬渣的焚烧时间,解决了热灼减率偏高问题;水冷式烟气急冷装置可以将烟气温度从1100℃降到200℃,防止了二恶英的尾部低温再生成.该系统运行稳定可靠,可以处理医疗垃圾和大多数的固态和液态危险废物,实现了烟气污染物尤其是二恶英排放达到国家标准的目标.同时对该系统运行时窑头温度分布、二燃室炉膛出口氧量变化、回转窑和炉膛升温特性、燃烧室外壁温度分布等几方面运行数据都进行了详细的介绍,为危险废物焚烧炉的运行提供了宝贵的经验数据.
危險廢物的處理和處置是襬在我國各級市政府麵前的緊迫任務.然而我國已經運行的危險廢物焚燒裝置普遍存在迴轉窯掛壁結渣、熱灼減率偏高和汙染排放超標等問題,作者通過將迴轉窯和流化床特點相結閤的方法提齣瞭一種新型危險廢物迴轉式流化冷渣多段焚燒處置裝置.該裝置採用迴轉窯(一燃室)、二燃室和流化床結閤的熱解-流化焚燒工藝,特彆是採用控製窯頭溫度避免瞭迴轉窯掛壁結渣;採用流化冷渣裝置延長未燃燼渣的焚燒時間,解決瞭熱灼減率偏高問題;水冷式煙氣急冷裝置可以將煙氣溫度從1100℃降到200℃,防止瞭二噁英的尾部低溫再生成.該繫統運行穩定可靠,可以處理醫療垃圾和大多數的固態和液態危險廢物,實現瞭煙氣汙染物尤其是二噁英排放達到國傢標準的目標.同時對該繫統運行時窯頭溫度分佈、二燃室爐膛齣口氧量變化、迴轉窯和爐膛升溫特性、燃燒室外壁溫度分佈等幾方麵運行數據都進行瞭詳細的介紹,為危險廢物焚燒爐的運行提供瞭寶貴的經驗數據.
위험폐물적처리화처치시파재아국각급시정부면전적긴박임무.연이아국이경운행적위험폐물분소장치보편존재회전요괘벽결사、열작감솔편고화오염배방초표등문제,작자통과장회전요화류화상특점상결합적방법제출료일충신형위험폐물회전식류화랭사다단분소처치장치.해장치채용회전요(일연실)、이연실화류화상결합적열해-류화분소공예,특별시채용공제요두온도피면료회전요괘벽결사;채용류화랭사장치연장미연신사적분소시간,해결료열작감솔편고문제;수랭식연기급랭장치가이장연기온도종1100℃강도200℃,방지료이악영적미부저온재생성.해계통운행은정가고,가이처리의료랄급화대다수적고태화액태위험폐물,실현료연기오염물우기시이악영배방체도국가표준적목표.동시대해계통운행시요두온도분포、이연실로당출구양량변화、회전요화로당승온특성、연소실외벽온도분포등궤방면운행수거도진행료상세적개소,위위험폐물분소로적운행제공료보귀적경험수거.
The treatment and disposal of hazardous wastes are currently the urgent task of many cites in our country. Now there are many problems such as slagging in rotary kiln inside wall, high loss-on-ignition and high pollution emission existing in most of conventional hazardous waste incinerators. A muhi-incineration system of rotary fluidizing and ash-cooling for hazardous waste was developed by the combination of rotary kiln and fluidized bed. The incineration system includes primary chamber (rotary kiln), fluidized bed and secondary chamber.The problem of slagging in rotary kiln inside wall can be solved by the controlling of temperature at the rotary kiln inlet, the residence time of the incombustible slag can be prolonged by using the fluidizing and the ash-cooling device, so the problem of high value of the loss-on-ignition can be solved. The flue gas temperature can be lowered directly from 1100℃ to 200 ℃ by the flue gas quenching facility, thus the low-temperature regeneration of dioxin are prevented. Medical waste and majority of solid and liquid hazardous wastes can be disposed by the stable system. The levels of flue gas pollutants emitted from the stack especially dioxin meet national emission limits set by the Chinese EPA. The operation data of temperature distribution at the rotary kiln inlet, oxygen content at the outlet of secondary chamber with time, temperature changing with time of rotary kiln and furnace temperature distribution at the outlet of chamber are described, valuable experience data for the operation of hazardous waste incinerator can be referred for commercial incineration plants.