摘要
设计制作了处理气量为33000m3/h的两台串联的碟—环式气体换热器,以代替转化系统原有的两台圆缺式气体换热器。新换热器的实测传热系数为205W/(m2·K),提高了847%;管程总阻力为686Pa,壳程总阻力为771Pa,分别降低650%和601%。两年来运行情况良好。
Two gas gas heat exchangers, arranged in series, with disk doughnat baffles and capacity of 33*!000 *!m 3/h gas were designed and made to replace existing ones with segmental baffles The new heat exchangers have practical overall heat transfer coefficient of 20 5*!W/(*!m 2·K),up 84 7%,and total pressure drop of 686 Pa on the tube side and 771 Pa on the shell side, respectively down 65 0% and 60 1%.They have operated well for two years
出处
《硫酸工业》
CAS
1999年第1期43-45,共3页
Sulphuric Acid Industry