如何使用流量系数
How to use Cv
法门流量系数(Cv)是表示阀门通过流体能力的数值。Cv越大,在给定压降下阀门能够通过的流体就越多。Cv值1表示当通过压降为1 PSI时,阀门每分钟流过1加仑15oC的水。Cv值350表示当通过压降为1 PSI时,阀门每分钟流过350加仑15oC的水。
Valve coefficient (Cv) is a number which represents a valve's ability to pass flow. The bigger the Cv, the more flow a valve can pass with a given pressure drop. A Cv of 1 means a valve will pass 1 gallon per minute (gpm) of 60oF water with a pressure drop (dp) of 1 PSI across the valve. A Cv of 350 means a valve will pass 350 gpm of 60oF water with a dp of 1 PSI.
公式1
FORMULA 1
流速:磅/小时(蒸汽或水)
FLOW RATE LBS/HR (Steam or Water)
在此: Where: |
dp | = | 压降,单位:PSI |
dp | = | pressure drop in PSI |
F | = | 流速,单位:磅/小时 |
F | = | flow rate in lbs./hr. |
= | 比容积的平方根,单位:立方英尺/磅 (阀门下游) | |
= | square root of a specific volume in ft3/lb. (downstream of valve) |
公式2
FORMULA 2
流速:加伦/分钟(水或其它液体)
FLOW RATE GPM (Water or other liquids)
在此: Where: |
dp | = | 压降,单位:PSI |
dp | = | pressure drop in PSI |
Sg | = | 比重 |
Sg | = | specific gravity |
Q | = | 流速,单位:加伦/分钟 |
Q | = | flow rate in GPM |
局限性
LIMITATIONS
上列公式在下列条件下无效:
Above formulas are not valid under the following conditions:
例子
EXAMPLE
F | = | 5,000,000 |
= | 0.137 (从水温为400oF的表中得到) | |
= | 0.137 (from chart for water at 400oF) | |
Cv | = | 9150 (来自本页) |
Cv | = | 9150 (from page 26) |
F | = | 500,000 |
= | 0.785 (来自900oF, 1200 PSIG蒸汽表) | |
= | 0.785 (from chart for steam at 900oF, 1200 PSIG) | |
= | = 2.24 | |
最接近的、较大的Cv是DN250压力等级Class 2500闸阀,其Cv是3130。这里是压降小于5 PSIG的最小的阀门。
The closest higher Cv is a 10" Class 2500 gate with a Cv of 3130. This is the smallest valve with a pressure drop less than 5 PSIG.
水和蒸汽的备选特性 Selected Properties of Water and Steam |
水的(下游) For Water (Downstream) | ||||||
所有压力等级 All Pressures | 温度(oF) Temperature (oF) | |||||
100 | 200 | 300 | 400 | 500 | 600 | |
0.127 | 0.129 | 0.132 | 0.137 | 0.143 | 0.154 |
蒸汽的(下游) For Steam (Downstream) | ||||||||
压力 PSIG Pressure PSIG | 温度(oF) Temperature (oF) | |||||||
Sat | 500 | 600 | 700 | 800 | 900 | 1000 | 1100 | |
100 200 300 400 500 600 700 800 900 1000 1100 1200 1300 1400 1600 1800 2000 2500 3000 4000 5000 6000 | 1.97 1.46 1.21 1.06 0.950 0.865 0.801 0.747 0.701 0.662 0.628 0.598 0.570 0.545 | 2.20 1.61 1.30 1.11 0.979 0.895 | 2.32 1.68 1.38 1.19 1.06 0.960 0.880 0.815 0.759 0.710 0.670 0.629 0.590 0.559 | 2.44 1.77 1.46 1.26 1.12 1.02 0.941 0.875 0.821 0.773 0.732 0.695 0.662 0.633 0.58 0.54 0.50 0.41 0.31 0.17 0.16 0.16 | 2.54 1.85 1.52 1.32 1.18 1.08 0.994 0.926 0.870 0.816 0.781 0.745 0.710 0.683 0.63 0.59 0.55 0.48 0.42 0.32 0.24 0.19 | 2.64 1.95 1.60 1.38 1.23 1.13 1.04 0.972 0.914 0.865 0.823 0.785 0.752 0.723 0.67 0.63 0.59 0.52 0.46 0.38 0.32 0.28 | 2.74 2.00 1.65 1.43 1.28 1.17 1.08 1.01 0.955 0.917 0.872 0.813 0.789 0.752 0.70 0.66 0.62 0.55 0.49 0.42 0.36 0.32 | 2.84 2.07 1.71 1.47 1.33 1.22 1.12 1.05 0.99 0.94 0.90 0.86 0.83 0.79 0.74 0.69 0.65 0.58 0.52 0.44 0.39 0.35 |
阀座端口流速计算 下列公式可以用来计算任何阀门的阀座流速:
例: 解:
例: 解:
局限性 流速公式在下列条件下无效:
注意 在确定止回阀通径时,最适宜的工作流速应该位于这些范围内:
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球形止回阀,截止止回阀,提升式止回阀的流量特性曲线 小于全开状态的估计流量系数Cv |
表中所列流量系数仅适用于全开状态下的阀门。不是全开状态的流量系数可以采用适用于提升式阀瓣止回阀和截止阀的流量特性曲线进行估算。不建议将闸阀用在节流应用中。 例: |
解: 查询图2,全开状态的1/4时阀门的比率是52%. 因此计算1/4全开的流量系数Cv为: Copyright ©2006-2024 Xuda Fluid all rights reserved 苏ICP备16042488号 |