齐鲁石油化工
齊魯石油化工
제로석유화공
QILU PETROCHEMICAL TECHNOLOGY
2014年
4期
285-289
,共5页
高传成%马传波%王付印
高傳成%馬傳波%王付印
고전성%마전파%왕부인
催化裂化%烟气脱硫%粉尘
催化裂化%煙氣脫硫%粉塵
최화열화%연기탈류%분진
catalytic and cracking%smoke desulfurization%dust
恒源石化在0．3 Mt／a的 TMP 催化裂化装置采用钠镁法湿式烟气脱硫技术，新建1套烟气脱硫除尘装置。工业运行结果表明，钠镁法烟气脱硫除尘装置具有良好的操作弹性，运行经济可靠。净化后烟气中的SO2浓度最低能达到3 mg／m3，SO2脱除率达到99．9％，净化烟气平均粉尘含量16．3 mg／m3，优于设计值。实现了高效连续运行，可控外排废气中的各项指标满足排放要求。
恆源石化在0．3 Mt／a的 TMP 催化裂化裝置採用鈉鎂法濕式煙氣脫硫技術，新建1套煙氣脫硫除塵裝置。工業運行結果錶明，鈉鎂法煙氣脫硫除塵裝置具有良好的操作彈性，運行經濟可靠。淨化後煙氣中的SO2濃度最低能達到3 mg／m3，SO2脫除率達到99．9％，淨化煙氣平均粉塵含量16．3 mg／m3，優于設計值。實現瞭高效連續運行，可控外排廢氣中的各項指標滿足排放要求。
항원석화재0．3 Mt／a적 TMP 최화열화장치채용납미법습식연기탈류기술，신건1투연기탈류제진장치。공업운행결과표명，납미법연기탈류제진장치구유량호적조작탄성，운행경제가고。정화후연기중적SO2농도최저능체도3 mg／m3，SO2탈제솔체도99．9％，정화연기평균분진함량16．3 mg／m3，우우설계치。실현료고효련속운행，가공외배폐기중적각항지표만족배방요구。
A new smoke desulfurization dedusting unit by adopting sodium magnesium wet type desulfurization technology was built on 0.3 Mt/a TMP catalytic and cracking plant of Hengyuan Petrochemical Company .The industrial running results showed that the new built des-ulfurization dedusting unit had good operational flexibility and economic stability .Minimum con-tent of SO2 in the purified smoke could reach 3 mg/m3 and the removal rate was 99.9%.The av-erage dust content of the purified smoke was 16.3 mg/m3 and preceded the design value .Each control index on the discharged exhaust gas of the TMP catalytic and cracking unit after reforma-tion met the discharge standard requirement , which realized high efficient and continuous run-ning.
