A、f<sub>rsub>ρ<sub>ssub>gL B、f<sub>ρsub>Lρg C、(f<sub>ρsub>-f<sub>rsub>)Lρg D、f<sub>rsub>(ρ<sub>ssub>-ρ)gL
A、f<sub>rsub>ρ<sub>ssub>gL B、f<sub>ρsub>Lρg C、(f<sub>ρsub>-f<sub>rsub>)Lρg D、f<sub>rsub>(ρ<sub>ssub>-ρ)gL
A、F<sub>甲sub>=F<sub>乙sub>ρ<sub>甲sub>〉ρ<sub>乙sub> B、F<sub>甲sub>=F<sub>乙sub>ρ<sub>甲sub>〈ρ<sub>乙sub> C、F<sub>甲sub>〈F<sub>乙sub>ρ<sub>甲sub>〈ρ<sub>乙sub> D、F<sub>甲sub>〈F<sub>乙sub>ρ<sub>甲sub>〉ρ<sub>乙sub>
A、f<sub>rsub>ρ<sub>ssub>gL B、f<sub>ρsub>Lρg C、(f<sub>ρsub>-f<sub>rsub>)Lρg D、f<sub>rsub>(ρ<sub>ssub>-ρ)
A、p=p<sub>0sub>+ 2γ/R’ B、ln(p/p<sub>0sub>)=ΔVapHm(1/T<sub>0sub>- 1/T)/R C、RTln(p/p<sub>0sub>)=2γM/ρR’ D、p=nRT/V
A、ρ<sub>20sub>=ρ<sub>20sub>-r(20-r) B、ρ<sub>20sub>=ρ<sub>20sub>-r(t-20) C、ρ<sub>20sub>=ρ<sub>20sub>+r(t-20) D、ρ<sub>20sub>=ρ<sub>20sub>+r(20-r)
A、H<sub>1sub>>H<sub>2sub>;P<sub>1sub>=P<sub>2sub> B、H<sub>1sub>=H<sub>2sub>;P<sub>1sub>>P<sub>2sub> C、H<sub>1sub>>H<sub>2sub>;P<sub>1sub>>P<sub>2sub> D、H<sub>1sub>=H<sub>2sub>;P<sub>1sub>=P<sub>2sub>
A、在一常压气流干燥器中干燥某种湿物料,已知数据如下:空气进入预热器的温度为15℃,湿含量为0.0073kg<sub>水sub>/kg<sub>绝干空气sub>,空气进干燥器温度为90℃,空气出干燥器温度为50℃。进干燥器物料含水量为0.15kg<sub>水sub>/kg<sub>绝干空气sub>;出干燥器物料含水量为0.01kg<sub>水sub>/kg<sub>绝干空气sub>;干燥器生产能力为237kg/h(按干燥产品计)。若此干燥为等焓过程,湿空气的焓按计算
试求:①水分蒸发量(kg/h)
②空气出干燥器的湿含量(kg<sub>水sub>/kg<sub>绝干空气sub>)
③绝干空气的消耗量(kg<sub>绝干空气sub>/h)
④预热器加入热量(kw)(预热器热损失可忽略)
A、P>P<sub>0sub>,防止Cl<sub>2sub>泄漏 B、P<P<sub>0sub>,防止Cl<sub>2sub>泄漏 C、P>P<sub>0sub>,防止空气混入 D、P<P<sub>0sub>,防止空气混入