摘要
在140kt/a硫酸装置上,利用热管技术回收三氧化硫气体的中温余热。回收的蒸汽压力为500kPa,蒸发量1.2~1.6t/h。投资的回收年限21个月。
Middle-level heat was recoverd from SO3 with heat pipe to generate 1.2-1.6t/h
of steam at 500kPa in a 140kt/a sulphuric
acid unit. The return period of the investment is 21 months.
出处
《硫酸工业》
CAS
1989年第6期16-18,64,共4页
Sulphuric Acid Industry