摘要
随着站外油井措施增产,为了满足处理需求,转油站处理工艺、处理能力及运行参数等出现不适应,四合一淤泥沉积、烟火管外壁结垢降低其加热效率。因此,通过调整多台四合一并联运行,并与闲置加热炉和新建掺水炉串联运行等工艺优化,分别满足含水油外输和掺水温度要求,使得外输温度降低了15℃而达标外输;及时采取对四合一清淤除垢,提高加热效率10.56%;根据各掺水集油环生产情况优化进站温度,以达到提质增效作用。
In order to meet the demand of treatment,the treatment technology,treatment capacity and operation parameters of the oil transfer station are not adapted to meet the demand of treatment.The heating efficiency of the oil transfer station is reduced by four-in-one silt deposition and scaling on the outer wall of the fireworks pipe.Therefore,by adjusting several four-in-one parallel operation,and running in series with idle heating furnace and newly built water mixing furnace,and other process optimization,the external temperature requirements of water-bearing oil and water mixing are respectively met,and the external temperature is reduced by 15℃to meet the external temperature standards.At the same time,the four in one desilting and descaling were adopted to improve the heating efficiency by 10.56%.The inlet temperature was optimized according to the production situation of each water-mixed oil collecting ring to achieve the effect of improving quality and efficiency.
作者
谢正芳
XIE Zhengfang(NO.9 Oil Production Plant in Daqing Oilfield)
出处
《石油石化节能》
2022年第3期4-7,I0002,共5页
Energy Conservation in Petroleum & PetroChemical Industry
关键词
处理工艺优化
低温集输
加热效率
加热炉
转油站
process optimization
low temperature gathering and transportation
heating efficiency
heating furnace
transfer station