Расход и скорость клапана в основном зависят от диаметра клапана, также связаны с сопротивлением конструкции клапана среде и неразрывно связаны с такими факторами, как давление клапана, температура и концентрация среды.
Какова именно связь между ними?
The flow channel area of a valve is directly related to flow velocity and flow rate, and flow velocity and flow rate are two mutually dependent quantities. When the flow rate is constant, the flow velocity is larger, and the channel area can be smaller; If the flow velocity is low, the runner area can be larger. Conversely, a large flow channel area has a lower flow velocity; The smaller the flow channel area, the higher the flow velocity.
If the medium has a high flow velocity, the valve diameter can be smaller, but resistance loss is greater and the valve is prone to damage. High flow velocity can cause static electricity effects on flammable and explosive media, posing dangers; If the flow rate is too low, efficiency is low and uneconomical. For media with high viscosity and explosive value, a lower flow rate should be used. For oils and liquids with high viscosity, the flow rate should be adjusted according to viscosity, generally 0.1~2m/s.
Generally, the flow rate is known, and the flow rate can be determined by experience. The nominal diameter of the valve can be calculated by analyzing flow rate and flow rate.
Valves with the same diameter may have different structural types, resulting in different fluid resistance. Under the same conditions, the greater the valve’s resistance coefficient, the more the flow rate and flow rate of the fluid through the valve decrease; The lower the valve resistance coefficient, the less the flow rate and flow rate of fluid passing through the valve decrease.
Overview of Common Flow Rates for Various Media
| Название жидкости |
Условия использования |
Flow rate
(m/s) |
| Насыщенный пар |
DN>200
DN=200～100
DN<100 |
30~40
25~35
15~30 |
| Перегретый пар |
DN>200
DN=200～100
DN<100 |
40～60
30～50
20~40 |
| Пар низкого давления |
p<1,0 (абсолютное давление) |
15~20 |
| Пар среднего давления |
P=1,0～4,0(абсолютное давление) |
20～40 |
| Пар высокого давления |
P=4,0～12,0 (абсолютное давление) |
40～60 |
| Сжатый газ |
Vacuum
P≤0.3（Gauge pressure）
P=0.3～0.6（Gauge pressure）
P=0.6～1.0（Gauge pressure）
P=1.0～2.0（Gauge pressure）
P=2.0～3.0（Gauge pressure）
P=3.0～30.0（Gauge pressure） |
5~10
8~12
10～20
10~15
8~12
3~6
0.5~3 |
| Кислород |
P=0～0.05（Gauge pressure）
P=0.05~0.6（Gauge pressure）
P=0.6～1.0（Gauge pressure）
P=1.0~2.0（Gauge pressure）
P=2.0～3.0（Gauge pressure） |
5~10
7~8
4~6
4~5
3~4 |
| Угольный газ |
|
2,5~15 |
| Полуводяной газ |
Р = 0,1–0,15 (манометрический) |
10~15 |
| Природный газ |
|
30 |
| Азот |
P = 5–10 (абсолютный) |
15~25 |
| Аммиак |
Vacuum
P < 0.3 (gauge)
P < 0.6 (gauge)
P ≤ 2 (gauge) |
15~25
8~15
10～20
3~8 |
| Ацетиленовая вода |
|
30
5~6 |
| Ацетилен газ |
p < 0.01 (gauge)
p < 0.15 (gauge)
p < 2.5 (gauge) |
3~4
4~8
5 |
| Дым |
Gas
Liquid |
10~25
1.6 |
| Сероводород |
Gas
Liquid |
20
1.5 |
| Жидкий криптон |
Vacuum
P ≤ 0.6 (gauge)
P ≤ 2.0 (gauge) |
0.05～0.3
0.3~0.8
0.8~1.5 |
| аргиоксид натрия |
Concentration 0–30%
Concentration 30%–50%
Concentration 50%–73% |
2
1.5
1.2 |
| Серная кислота |
Concentration 88%–93%
Concentration 93%–100% |
1.2
1.2 |
| Соляная кислота |
|
1,5 |
| Water and viscosity
Similar liquids |
P = 0.1–0.3 (gauge pressure)
P ≤ 1.0 (gauge pressure)
P ≤ 8.0 (gauge pressure)
P ≤ 20–30 (gauge pressure)
Heating network circulating water, cooling water
Pressure return water
Non-pressurized return water |
0.5～2
0.5~3
2~3
2~3.5
0.3～1
0.5~2
0.5~1.2 |
| Водопроводная вода |
Main pipe P = 0.3 (gauge pressure)
Branch pipe P = 0.3 (gauge pressure) |
1.5～3.5
1~1.5 |
| Питательная вода котла |
|
>3 |
| Конденсат пара |
|
0,5~1,5 |
| Конденсат |
Гравитационный поток |
0,2~0,5 |
| Перегретая вода |
|
2 |
| Морская вода, слабощелочная вода |
P < 0,6 (избыточное давление) |
1,5~2,5 |
Note:
The unit for DN value is: mm; The unit of Rho value is: MPa.
Gate valves have a low resistance coefficient, only within the range of 0.1~1.5; large-diameter gate valves have a resistance coefficient of 0.2~0.5; shrink-mouth gate valves have a higher resistance coefficient.
The resistance coefficient of globe valves is much higher than that of gate valves, generally between 4~7. Y-type globe valves (DC type) have the lowest resistance coefficient, between 1.5~2.
Forged steel globe valves have the highest resistance coefficient, sometimes reaching as high as 8.
The resistance coefficient of check valves depends on their structure: swing check valves are usually about 0.8~2, with multi-disc swing check valves having a higher resistance coefficient; lifting type check valves have the highest resistance coefficient, up to 12. The plug valve has a low resistance coefficient, usually about 0.4~1.2.
The resistance coefficient of diaphragm valves is generally around 2.3. The resistance coefficient of butterfly valves is low, generally within 0.5. The resistance coefficient of ball valves is the lowest, generally around 0.1.
The resistance coefficient of the above valve is the value when the valve is fully open.
При выборе диаметра клапана следует учитывать точность обработки клапана, отклонения размеров и другие факторы. Диаметр клапана должен иметь определенный запас, обычно 15%. В реальной эксплуатации диаметр клапана определяется диаметром технологического трубопровода.
