科技风
科技風
과기풍
TECHNOLOGY WIND
2015年
12期
64-65
,共2页
变换冷凝液%工艺冷凝液%汽提%节能%环保
變換冷凝液%工藝冷凝液%汽提%節能%環保
변환냉응액%공예냉응액%기제%절능%배보
trans for mati oncondensate%processcondensate%steamstripping%energysaving%environmental protection
变换冷凝液COD2300mg/L，NH3- N1200mg/L，超过污水处理进口指标，为此根据目前焦炉气制合成氨工艺、设备现状和工艺模拟数据，提出变换冷凝液具体处理方案，回收汽提气用于焦炉气转化，节约水和蒸汽资源。
變換冷凝液COD2300mg/L，NH3- N1200mg/L，超過汙水處理進口指標，為此根據目前焦爐氣製閤成氨工藝、設備現狀和工藝模擬數據，提齣變換冷凝液具體處理方案，迴收汽提氣用于焦爐氣轉化，節約水和蒸汽資源。
변환냉응액COD2300mg/L，NH3- N1200mg/L，초과오수처리진구지표，위차근거목전초로기제합성안공예、설비현상화공예모의수거，제출변환냉응액구체처리방안，회수기제기용우초로기전화，절약수화증기자원。
The trans for mati oncondensatecan'tbetreated because of high COD and NH3- Nconcentration. According to the currentsituation of syn-thetic ammonia process with coke oven gas, equipment, analysis results of process simulation, the process of condensate treatment is proposed, by which recovers trippinggas for cokeoveng astrans for mation and savesteam and waterres ources.
