The practical significance of the adjustable ratio of control valves in engineering design
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The adjustable ratio of a control valve is easy to explain: it refers to the ratio of the maximum flow rate to the minimum flow rate that the control valve can regulate. The higher this value, the greater its regulating capability. It can also be found online that \"when the pressure difference across the control valve is constant, the adjustable ratio is referred to as the ideal adjustable ratio; the ideal adjustable ratio equals the ratio of the maximum flow coefficient to the minimum flow coefficient.\" So what does the maximum flow coefficient mean? Does it refer to the flow coefficient at the maximum flow rate specified by the process conditions, or is it the flow coefficient when the valve is fully open, that is, the rated flow coefficient? Or it is the flow coefficient mentioned above in relation to the \"maximum flow rate that can be controlled\"; then where does this \"maximum flow rate value that can be controlled\" come from? Is it calculated or measured? Moreover, in actual engineering design, from the process specifications for control valves provided by design institutes and engineering companies, to the calculation sheets prepared by valve manufacturers, and then to the samples supplied by these manufacturers, it seems that this adjustable ratio R is never mentioned. What is the specific practical significance of this value?Nominal diameter DN×dN | Φ values at various relative openings | Adjustable ratio R
0.1 | 0.2 | 0.3 | 0.4 | 0.5 | 0.6 | 0.7 | 0.8 | 0.9 | 1.0
25 | 2.65 | 4.57 | 7.84 | 12.76 | 17.96 | 25.04 | 35.00 | 49.11 | 74.53 | 103.39 | 51.5
32 | 3.09 | 6.30 | 9.90 | 13.99 | 18.90 | 24.60 | 30.10 | 42.80 | 74.40 | 100.00 | 34.6
40 | 7.44 | 10.28 | 11.52 | 13.22 | 16.88 | 21.92 | 28.82 | 52.84 | 78.92 | 92.00 | 17.4
50 | 7.68 | 11.89 | 14.90 | 18.40 | 22.90 | 29.50 | 37.80 | 53.50 | 70.40 | 98.20 | 14.6
65 | 3.95 | 7.72 | 11.36 | 15.53 | 20.20 | 26.56 | 36.51 | 50.77 | 77.53 | 99.58 | 28.9
80 | 3.34 | 7.64 | 10.49 | 14.63 | 19.85 | 28.00 | 37.75 | 50.28 | 75.49 | 97.25 | 32.4
100 | 4.70 | 7.68 | 10.32 | 14.20 | 18.81 | 27.35 | 37.02 | 52.82 | 72.39 | 97.60 | 27.1
125 | 4.14 | 6.49 | 9.47 | 12.89 | 19.37 | 27.61 | 37.34 | 51.88 | 66.66 | 103.63 | 32.3
150 | 2.55 | 5.70 | 8.50 | 12.42 | 18.17 | 25.45 | 34.98 | 48.48 | 76.74 | 96.81 | 45.7
200 | 12.20 | 16.10 | 20.10 | 25.10 | 32.00 | 46.50 | 75.80 | 100.50 | – | – | 20.0
Table 3: Flow coefficient Φ values and calculated R values for sleeve control valves
Nominal diameter DN×dN | Φ values at various relative openings | Adjustable ratio R
0.1 | 0.2 | 0.3 | 0.4 | 0.5 | 0.6 | 0.7 | 0.8 | 0.9 | 1.0
25 | 4.10 | 7.90 | 12.10 | 16.50 | 20.40 | 29.60 | 42.20 | 61.00 | 81.50 | 103.00 | 30.9
40 (C=16) | 2.12 | 6.06 | 10.00 | 14.31 | 18.75 | 24.75 | 34.50 | 51.06 | 73.75 | 96.88 | 45.3
60 (C=25) | 6.54 | 9.12 | 11.76 | 14.84 | 20.24 | 28.16 | 38.60 | 56.00 | 78.00 | 99.20 | 21.3
50 | 3.10 | 6.45 | 9.90 | 15.05 | 22.48 | 32.50 | 46.50 | 67.50 | 90.50 | 97.75 | 45.2
65 | 3.25 | 6.83 | 10.24 | 14.63 | 20.63 | 27.46 | 40.32 | 58.73 | 86.35 | 107.94 | 41.2
80 | 4.20 | 7.67 | 11.10 | 14.97 | 21.05 | 29.70 | 40.60 | 60.50 | 80.10 | 92.60 | 29.9
100 | 3.57 | 7.37 | 11.03 | 15.21 | 21.80 | 30.39 | 44.13 | 64.90 | 82.06 | 93.23 | 34.9
125 (C=250) | 3.69 | 7.00 | 10.80 | 15.24 | 21.20 | 29.80 | 41.60 | 59.60 | 87.60 | 102.80 | 36.9
125 (C=370) | 3.34 | 7.14 | 10.84 | 15.19 | 21.89 | 31.62 | 45.95 | 65.41 | 82.43 | 93.24 | 37.5
200 | 3.17 | 6.90 | 10.79 | 15.66 | 22.41 | 31.90 | 42.76 | 60.34 | 81.21 | 96.03 | 37.8
300 | 3.31 | 6.92 | 10.54 | 14.54 | 20.23 | 28.62 | 43.85 | 64.23 | 82.31 | 94.08 | 38.3
Table 4: Flow coefficient Φ values and calculated R values for Fisher’s ED-type sleeve valves
Nominal diameter DN×dN | Φ values at various relative openings | Adjustable ratio R
0.1 | 0.2 | 0.3 | 0.4 | 0.5 | 0.6 | 0.7 | 0.8 | 0.9 | 1.0
1*1/4×1*5/16 | 0.783 | 1.54 | 2.20 | 2.89 | 4.21 | 5.76 | 7.83 | 10.9 | 14.1 | 17.2 | 27.4
1*1/2×1*7/8 | 1.52 | 2.63 | 3.87 | 5.41 | 7.45 | 11.2 | 17.4 | 24.5 | 30.8 | 35.8 | 36.3
2×2*5/16 | 1.66 | 2.93 | 4.66 | 6.98 | 10.8 | 16.5 | 25.4 | 37.3 | 50.7 | 59.7 | 57.6
2*1/2×2*7/8 | 3.43 | 7.13 | 10.8 | 15.1 | 22.4 | 33.7 | 49.2 | 71.1 | 89.5 | 99.4 | 41.3
3×3*7/16 | 4.32 | 7.53 | 10.9 | 17.1 | 27.2 | 43.5 | 66.0 | 97.0 | 120 | 136 | 54.2
4×4*3/8 | 5.85 | 11.6 | 18.3 | 30.2 | 49.7 | 79.7 | 125 | 171 | 205 | 224 | 64.8
6×7 | 12.9 | 25.8 | 43.3 | 67.4 | 104 | 162 | 239 | 316 | 368 | 394 | 47.1
8×8 L=2 | 18.5 | 38.0 | 58.4 | 86.7 | 130 | 189 | 268 | 371 | 476 | 567 | 41.9
8×8 L=3 | 27.0 | 58.1 | 105 | 188 | 307 | 478 | 605 | 695 | 761 | 818 | 43.1
By comparing the R values of the two series of control valves in Table 2 and Table 3, it can be seen that the R values for various specifications of two-seat control valves exhibit relatively large deviations, whereas those for sleeve control valves show smaller deviations. This is consistent with the different error criteria used for flow characteristics in the design of these two types of valves: the double-seat control valve uses 10% of the maximum flow value as the allowable deviation range for the flow value per stroke, whereas the sleeve valve employs the slope method specified in the international IEC standards to calculate the deviation in flow characteristics. Clearly, the latter method is better than the former at ensuring that the R value meets the design requirements, which also demonstrates the superiority of the IEC standard slope method. Comparing Tables 2, 3, and 4 also shows that the R value of domestically produced control valves is lower than that of imported control valves; the average R value for domestic two-seat valves is 30.5, while the average R value for sleeve valves is 36.2 ; The average value of Fisher Company’s ED type cartridge valve R = 45.9. The R values of the domestic sleeve valves and Fisher’s ED type sleeve valves during the working stroke range (h=0.2~0.8) were calculated using equation (10), and these values were compared with those at full stroke; the results are shown in Tables 5 and 6. It can be seen that the R value during the working stroke of the domestically produced cartridge valves is close to the R value for the full stroke, with no significant change; the average value of R is 34.2. In contrast, the R value during the working stroke of Fisher’s cartridge valves is significantly higher than the R value for the full stroke, with an average value of R of 60.5. Increasing the R value of the working stroke segment has the advantage of better meeting the requirements of automatic control systems; it also increases the flow coefficient at an opening degree of 80%, thereby significantly enhancing the flow capacity of the valve when it is fully open. Through the analysis and comparison of R values, it is shown that there is a certain gap in the design level of control valves between domestic and international manufacturers. Table 5: R values of domestic sleeve control valves. Stroke stages of sleeve valves; R values for various specifications of sleeve valves. Average R value: 20, 40; C=16: 40; C=25: 50, 65, 80, 100, 125; C=250: 125; C=370: 200, 300. For full stroke: 30.9, 45.3, 21.3, 45.2, 41.2, 29.9, 34.9, 36.9, 37.5, 37.8, 38.3, 36.2. When h=0.2~0.8: 26.9, 28.9, 20.5, 49.2, 33.4, 29.5, 35.4, 33.0, 39.2, 35.2, 38.4, 34.2. Table 6: R values of Fisher company’s sleeve valves. Stroke stages of sleeve valves; R values for various specifications of sleeve valves. Average R value: 1*1/4×1*5/1, 1*1/2×1*7/8, 2×2*5/16, 2*1/2×2*7/8, 3×3*7/16, 4×4*3/8, 6×7, 8×8L=2, 8×8L=3. For full stroke: 27.4, 35.3, 57.6, 41.3, 54.2, 64.8, 67.1, 41.9, 43.1, 45.9. When h=0.2~0.8: 25.8, 41.5, 69.7, 46.2, 78.1, 99.7, 69.0, 45.0, 69.7, 60.5. 4. Understanding of IEC 534—2—4 (draft): Paragraph 3.3 of IEC 534—2—4 (draft) specifies the equal percentage flow characteristic as follows: “Between h=0.2 and h=0.8, the difference between the logarithms of any two adjacent flow coefficient values should be within the range of 0.13 to 0.2.” “For values below h=0.2, these two values are 0.13 and 0.25 respectively ; For values above h=0.8, these figures should correspond to 0.03 and 0.2”. Here, the selection of the range for deviations in flow characteristics should be considered as being determined by the range of values for R. Calculating accordingly: for R=20, 0.1×logR=0.13; for R=100, 0.1×logR=0.20; for R=300, 0.1×logR=0.25; and for R=2, 0.1×logR=0.03. In other words, the deviations in flow characteristics are actually restricted within certain ranges for R values, specifically, h=0.2~0.8 and R=20~80 ; h=0.8~1.0, R=2~100 ; h=0~0.2, R=20~300 ; This requirement of the IEC reflects the use of the R value as a characteristic parameter of the flow characteristic curve, and it implements the design concept that different R values can be adopted across the entire range of motion. The national standard GB 4213—84 \"General Technical Requirements for Pneumatic Control Valves\" differs to some extent from the IEC standard on this issue. A thorough discussion of the relationship between the R value and the flow coefficient is of significance for the design, manufacturing, and application of control valves. It is also essential for advancing the fundamental theoretical research on control valves and improving the level of design and manufacturing of such valves in our country