A.1 754.8 B.1 826.2 C.1 805.7 D.1 922.6
A.1.85 B.2.06 C.2.77 D.2.96
A.1 826 B.1 857 C.1 938 D.1 905
A.1.718 B.1.816 C.1.927 D.1.906
A.0.35 B.0.42 C.0.490 1 D.0.510 9
A.0.803 7 B.0.852 6 C.0.880 9 D.0.9 125
A.38 116 J/kg B.39 256 J/kg C.30 000 J/kg D.40 526 J/kg
A.120.6 B.151.05 C.160.2 D.162.8
A.65.6% B.69.1% C.72.5 % D.75.6%
A.0.5% B.1% C.1.5% D.2%
A.129.051 J/kg B.12.9 J/kg C.1 290.5 J/kg D.129 051 J/kg
A.125 mm B.138 mm C.140 mm D.146 mm
A.3.155 B.3.162 C.3.188 D.3.176
某一φ159×4.5、工作压力为1MPa的水平蒸汽管道,在两支架之间有一个Q=80kg重阀门,布置如下图所示,已知管道单位长度计算荷载为(管材重+保温重+冷凝水重)325N/m,阀门与相邻支架间距为L1=2m,L2=6m,支架A、B垂直荷载各为()。
A.A B.B C.C D.D
已知液化石油气在15℃时的液相各组分的摩尔成分(%)为=47.39%,=52.61%,则15℃时气、液相平衡状态下的气相各组分的摩尔成分(%)为()。
A.72.13%,24.83% B.72.15%,30.06% C.52.89%,27.85% D.52.89%,30.06%
A.22 000 m3/h B.23 654 m3/h C.24 500 m3/h D.28 098 m3/h
A.5~6 B.4~5 C.3~4 D.2~3
A.5.82 W/mm2,0.68 B.6.01 W/mm2,0.68 C.6.01 W/mm2,0.82 D.5.82 w/mm2,0.82
A.1.02 B.1.15 C.1.18 D.1.25
A.0.6% B.1.0% C.1.4% D.1.8%
A.150 B.200 C.250 D.300
A.3 066 m3/h B.3 200 m3/h C.3 305 m3/h D.3 726 m3/h