- A.50L/min
- B.70L/min
- C.80L/min
- D.90L/min
- A.150mm
- B.100mm
- C.120mm
- D.80mm
- A.1
- B.2
- C.3
- D.4
- A.0.4L/s
- B.0.5L/s
- C.0.6L/s
- D.0.71L/s
- A.83
- B.85
- C.835
- D.853
- A.0.000025
- B.0.000035
- C.0.000045
- D.0.000075
- A.165800m<SUP>3</SUP>/h
- B.170900m<SUP>3</SUP>/h
- C.172800m<SUP>3</SUP>/h
- D.182600m<SUP>3</SUP>/h
- A.368000m<SUP>3</SUP>/h
- B.432000m<SUP>3</SUP>/h
- C.456000m<SUP>3</SUP>/h
- D.462000m<SUP>3</SUP>/h
- A.-l℃
- B.-2℃
- C.0℃
- D.1℃
- A.320
- B.330
- C.350
- D.380
- A.R12采用回热循环制冷系数提高
- B.R717采用回热循环制冷系数提高
- C.R12采用回热循环制冷系数下降
- D.R717采用回热循环制冷系数不变
- A.44.3
- B.44.6
- C.45.2
- D.46.8
- A.3.60
- B.3.78
- C.3.96
- D.4.48
- A.8.5m
- B.8.9m
- C.2m
- D.9.6m
- A.2726
- B.2528
- C.2623
- D.2684
- A.38.7%
- B.42.9%
- C.45.6%
- D.46.2%
- A.119Pa/m
- B.1.20Pa/m
- C.1.22Pa/m
- D.1.25Pa/m
- A.88.2%
- B.88.5%
- C.88.7%
- D.89.2%
- A.0.3
- B.0.5
- C.0.1
- D.0.4
- 20
-
某排气系统中S02浓度为50g/m3,用水吸收SO2,吸收塔在t=20℃,P=101325Pa工况下工作,若相平衡系数m=38,则水中可能达到的SO2最大浓度为( )kmolSO2/ kmolH2O。
- A.3.2×10<SUP>-4</SUP>
- B.3.8×10<SUP>-4</SUP>
- C.4.2×10<SUP>-4</SUP>
- D.4.7×10<SUP>-4</SUP>
- A.0.15m<SUP>2</SUP>
- B.0.18m<SUP>2</SUP>
- C.0.20m<SUP>2</SUP>
- D.0.25m<SUP>2</SUP>
- A.52.8
- B.62.5
- C.51.7
- D.79.2
- A.2.4
- B.24
- C.240
- D.3.6
- A.5663t
- B.5826t
- C.4729t
- D.4500t
- A.2587.6Pa/m
- B.368.7Pa/m
- C.582.6Pa/m
- D.776.9Pa/m