Butterfly Valve Flow Coefficient Kv & Pressure Drop Reference Data
All concentric lug butterfly valves and wafer butterfly valves are equipped with complete opening-angle Kv flow coefficient table and GPM-PSI pressure drop nomograph, supporting metric & imperial dual-system pipeline design calculation for global industrial projects. Flow coefficient Kv represents the fluid throughput capacity of the valve; higher Kv value brings lower pipeline pressure loss and less operation energy consumption.
1. Kv Value Table at Different Opening Angle (DN50 ~ DN600, 10°~90° Full Open)
| DN | 10° | 20° | 30° | 40° | 50° | 60° | 70° | 80° | 90° Full Open |
|---|---|---|---|---|---|---|---|---|---|
| 50 | 0.1 | 5 | 12 | 24 | 45 | 64 | 90 | 125 | 135 |
| 65 | 0.2 | 8 | 20 | 37 | 65 | 98 | 144 | 204 | 220 |
| 80 | 0.3 | 12 | 22 | 39 | 70 | 116 | 183 | 275 | 302 |
| 100 | 0.5 | 17 | 36 | 78 | 139 | 230 | 364 | 546 | 600 |
| 125 | 0.8 | 29 | 61 | 133 | 237 | 392 | 620 | 930 | 1022 |
| 150 | 2 | 45 | 95 | 205 | 366 | 605 | 958 | 1437 | 1579 |
| 200 | 3 | 89 | 188 | 408 | 727 | 1202 | 1903 | 2854 | 3136 |
| 250 | 4 | 151 | 320 | 694 | 1237 | 2047 | 3240 | 4859 | 5340 |
| 300 | 5 | 234 | 495 | 1072 | 1911 | 3162 | 5005 | 7507 | 8250 |
| 350 | 6 | 338 | 715 | 1549 | 2761 | 4568 | 7230 | 10844 | 11917 |
| 400 | 8 | 464 | 983 | 2130 | 3797 | 6282 | 9942 | 14913 | 16388 |
| 450 | 11 | 615 | 1302 | 2822 | 5028 | 8320 | 13168 | 19752 | 21705 |
| 500 | 14 | 791 | 1674 | 3628 | 6465 | 10698 | 16931 | 25396 | 27908 |
| 600 | 24 | 1222 | 2587 | 5605 | 9989 | 16528 | 26157 | 39236 | 43116 |
Table Instruction: Small opening 10°~30° for precise flow throttling; medium opening 40°~70° for circulating water regulation; 90° full open delivers maximum Kv value with minimum flow resistance for main pipeline isolation.
2. GPM & PSI Pressure Drop Nomograph Chart
Figure 1: Flow Rate & Pressure Drop Nomograph for Concentric Butterfly Valve
The pressure drop curve chart adopts US imperial units, with horizontal axis for flow rate GPM and vertical axis for differential pressure (PSI / Feet water head). Diagonal slant lines correspond to matching Kv/Cv flow coefficients, helping North American and ANSI standard clients quickly calculate pipeline medium pressure loss.
- Horizontal axis: Flow range 100 ~ 100,000 Gallons Per Minute, covers DN50~DN600 full size flow demand;
- Vertical axis dual units: PSI pressure difference and Feet water head, convenient for direct conversion of pipeline design parameters;
- Operation logic: Locate flow GPM vertically intersect Kv diagonal line, horizontally read pressure drop value to judge system energy loss.
3. Combined Application of Kv Table & Pressure Drop Curve
- Step 1: Confirm working opening angle (throttling / full open), extract Kv value from the table;
- Step 2: Convert metric Kv to US Cv via formula: Cv = Kv × 1.156;
- Step 3: Match Cv diagonal line on the GPM-PSI nomograph, calculate actual pipeline differential pressure;
- Step 4: If pressure drop exceeds design allowable value, upgrade to larger DN butterfly valve to raise overall Kv flow capacity.
Catalog Technical Tips
- Kv test standard: Clean water 15°C, SG=1, comply with EN 12266-1 & ISO5211;
- Avoid long-term stable operation under 10°~20° small opening, high pressure drop will cause cavitation and seal abrasion;
- The pressure drop nomograph only applies to liquid medium; gas & steam flow calculation requires special gas coefficient formula;
- We provide dual system flow data to meet metric European projects and imperial US standard engineering selection demands.






