- A.52m<SUP>3</SUP>
- B.60.48m<SUP>3</SUP>
- C.72.56m<SUP>3</SUP>
- D.80m<SUP>3</SUP>
- A.320
- B.300
- C.450
- D.620
- A.7.76L/s
- B.5.28L/s
- C.4.25L/s
- D.7.21L/s
- A.32
- B.128
- C.45
- D.320
- A.32.5
- B.33.1
- C.35.6
- D.28.7
- A.排水立管内水流为断续非均匀流
- B.排水立管内最大免压值的大小与排水横支管的高度、排水量的大小和通气量大小有关
- C.排水立管内为水气两相流
- D.排水立管内的最大负压往往发生在立管底部
- A.0.06m
- B.0.20m
- C.0.10m
- D.0.26m
- A.2.16m<SUP>3</SUP>/h
- B.3.25m<SUP>3</SUP>/h
- C.1.68m<SUP>3</SUP>/h
- D.2.42m<SUP>3</SUP>/h
- A.73.8mH<SUB>2</SUB>O
- B.71.74mH<SUB>2</SUB>O
- C.75.6mH<SUB>2</SUB>O
- D.78.9mH<SUB>2</SUB>O
- A.1200
- B.1300
- C.1500
- D.1600
- A.1.865m
- B.1.520m
- C.1.858m
- D.1.627m
- A.24
- B.32
- C.48
- D.56
- A.1.767g/h
- B.17.67g/h
- C.1767g/h
- D.17670g/h
- A.92.3%
- B.91.55%
- C.94.6%
- D.95.82%
- 15
-
已知某城市污水处理厂的最大设计流量为0.6m3/s,设最大设计流量时的停留时间t= 2min,最大设计流量时水平流速v=0.1m/s,有效水深h=2m,则曝气沉砂池的池总宽度和池长分别为( )m。
- A.4,10
- B.3,12
- C.5,10
- D.4,12
- A.25.32L/s
- B.26.12L/s
- C.21.23L/s
- D.35.86L/s
- A.15.8×10<SUP>4</SUP>
- B.14.4×10<SUP>4</SUP>
- C.25×10<SUP>4</SUP>
- D.20×10<SUP>4</SUP>
- A.500%
- B.400%
- C.300%
- D.200%
- A.40L/s
- B.52L/s
- C.60L/s
- D.78L/s
- A.50%
- B.25%
- C.27%
- D.36%
- A.44.8
- B.35.6
- C.26.4
- D.45.9
- A.49578.5m<SUP>3</SUP>/d
- B.49758.5m<SUP>3</SUP>/d
- C.57152.5m<SUP>3</SUP>/d
- D.57172.5m<SUP>3</SUP>/d
- A.8.652mm/s
- B.9.537mm/s
- C.6.353mm/s
- D.7.262mm/s
- A.14.46×10<SUP>4</SUP>m<SUP>3</SUP>/d
- B.13.95×10<SUP>4</SUP>m<SUP>3</SUP>/d
- C.12.21×10<SUP>4</SUP>m<SUP>3</SUP>/d
- D.15.28×10<SUP>4</SUP>m<SUP>3</SUP>/d
- A.32
- B.53
- C.46
- D.30