Calculation of Kv value Medium Saturated Liquids steam RECOMMENDED FLOW VELOCITIES AT THE INLET OF VALVE, FOR THE SIZING OF NOMINAL PIPE SIZE :

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Transcription:

DT SHEET FOR CONTROL VLVES VLVE SIZING The valve sizing is based on the calculation of the Kv coefficient. The Kv represents the quantity of water, expressed in cubic meters (m3) at 15ºC, that flows through the valve with a pressure drop of 1 bar, in one hour period. The formulas, below indicated, allow the Kv calculation in accordance with the type of fluid and it s operating condition. fter the Kv calculation, the corresponding Kvs is available from the valve data sheet. If real operating data have been used for the calculation, as a rule the calculated Kv should be around 70% to 80% of the selected valve Kvs in order to guaranty proper regulation of maximum flow rate at the given operating conditions preventing that sometimes some precautionary additions will result in undesirable valve over sizing. t the same time it is necessary to check whether the minimum flow rate can be even regulated or not considering the chose valve rangeability. For critical applications,(critical flow velocities, for example), noise prediction, etc, please fill the data sheet available in the next page and submit it to our technical department for proper selection using our software. a) b) Pressure Drop P Dp P Dp Calculation of Kv value Medium Saturated Liquids steam d1 Kv Q1 Dp 1000 Q Kv,4 Dp P Q Kv 11, Q3 Kv 514 Gases d T Dp P Q Kv 3 d T 57 Remarks: For superheated steam and other fluids please consult. a) Subcritical pressure drop: downstream absolute pressure more than 50% of the absolute upstream pressure in the valve. b) Supercritical pressure drop: downstream absolute pressure is equal or less than 50% of the upstream absolute pressure in the valve. Kv Flow coefficient m3/h Upstream absolute pressure bar P Downstream absolute pressure bar Dp Pressure drop ( P) bar Q1 Flow rate m3/h Q Flow rate Kgs/h Q3 Flow rate N.m3/h (0ºC 1013 mbar) d1 Specific weight of liquid Kg/m3 d Specific weight of gas Kg/m3 T bsolute temperature (T=73 + t ºC) ºK t Fluid temperature ºC RECOMMENDED FLOW VELOCITIES T THE INLET OF VLVE, FOR THE SIZING OF NOMINL PIPE SIZE : Liquids :,5 m/s ; Gases : 0m/s ; Saturated steam : 5 m/s ; Superheated steam : 50m/s 437

SUPERCRITICL PRESSURE DROP When pressure ratio is supercritical, speed of flow reaches acoustic velocity at the narrowest section causing higher level of noisiness, cavitation or flashing, the single or double perforated trim design is recommended. INHERENT FLOW CHRCTERISTICS Kv Kv 0 H PT PL On-off, the flow rate changes from 0 to 100% - fully open or fully closed control. Linear, the flow capacity or Kv increases linearly with valve travel. The flow is directely proportional to the valve travel.recommended when there are no relevant variations in differential pressure or flow rates EQP Equal-percentage, for equal increments of valve plug travel the change in flow rate with respect to travel may be expressed as a constant percent of the flow rate at the time of the change. t constant differential pressure, the valve travel increase of 10% usually corresponds to a flow rate increase equal to 50% of the valve flow preceding the variation. The change in flow rate observed with respect to travel will be relatively small when the valve plug is near it s seat and relatively high when the valve plug is nearly wide open. Recommended when there are wide variations in flow rate or differential pressure. 438

CONTROL VLVES General Information TWO WY VLVES pplication: On/off, control of flow, pressure, temperature. Fig.1 THREE WY MIXING VLVES pplication: Mixing of two streams y-pass at heat exchangers Fig. THREE WY DIVERTING VLVES pplication: Diverting of two streams y-pass at heat exchangers * Diverting into two different systems (* The mixing design is recommended, see Fig.6) Fig.3 439

TYPICL REGULTION LOOPS Fig.4 TYPICL REGULTION LOOPS Two-way valve arrangement Fluid : saturated steam Three way mixing valve arrangement (mixing regulation) Fluids: water, diathermic oil, Fig.5 Three way mixing valve arrangement (diverting regulation) Fluids: water, diathermic oil, Fig.6 Three way diverting valve arrangement Fluids: water, diathermic oil, Fig.7 Two-way valve arrangement Fluids: water, diathermic oil, 440

Pm (bar) Pa (bar) T ( C) PHYSICL PROPERTIES OF STURTED STEM V (m 3 /Kg) he (Kcal/Kg) he (KJ/Kg) r (Kcal/Kg) r (KJ/Kg) hg (Kcal/Kg) hg (KJ/Kg) 0,00 1,013 100,0 1,673 100,1 419,1 539,4 58,4 639,5 677,5 0,05 1,063 101,4 1,601 101,5 45,0 538,4 54, 639,9 679,1 0,10 1,113 10,6 1,533 10,8 430,4 537,7 51, 640,5 681,6 0,15 1,163 105,1 1,471 104,1 435,8 536,9 47,9 641,0 683,7 0,0 1,13 106, 1,414 105,3 440,9 536, 45,0 641,5 685,8 0,30 1,313 107,4 1,31 107,6 450,5 534,7 38,7 64,3 689, 0,40 1,413 109,5 1,5 109,8 459,7 533,3 3,8 643,1 69,5 0,50 1,513 111,6 1,149 111,9 468,5 531,9 7,0 643,8 695,5 0,60 1,613 113,5 1,038 113,8 476,5 530,6 1,5 644,4 698,0 0,70 1,713 115,4 1,04 115,7 484,4 59,5 16,9 645, 701,3 0,80 1,813 117,1 0,971 117,5 491,9 58,3 11,9 645,8 703,8 0,90 1,913 118,8 0,93 119, 499,1 57,1 06,9 646,3 705,9 1,00,013 10,4 0,881 10,8 505,8 56,0 0,3 646,8 708,0 1,10,113 11,9 0,841 1,4 51,5 55,1 198,5 647,5 711,0 1,0,13 13,4 0,806 14,0 519, 54,1 194,3 648,1 713,5 1,30,313 14,9 0,773 15,4 55,0 53,1 190,1 648,5 715,1 1,40,413 16,3 0,743 16,8 530,9 5, 186,3 649,0 717, 1,50,513 17,6 0,714 18,1 536,3 51,1 181,7 649, 718,1 1,60,613 18,9 0,689 19,5 54, 50,4 178,8 649,9 71,0 1,70,713 130,1 0,665 130,7 547, 519,5 175,0 650, 7,3 1,80,813 131,4 0,643 13,0 55,7 518,6 171,3 650,6 73,9 1,90,913 13,5 0,6 133, 557,7 517,8 167,9 651,0 75,6,00 3,013 133,7 0,603 134,4 56,7 517,0 164,6 651,4 77,3,0 3,13 135,9 0,568 136,6 571,9 515,5 158,3 65,1 730,,40 3,413 138,0 0,536 138,8 581,1 514,0 15,0 65,8 733,1,60 3,613 140,0 0,509 140,8 589,5 51,6 146, 653,4 735,7,80 3,813 141,9 0,483 14,8 597,9 511, 140,3 654,0 738, 3,00 4,013 143,7 0,461 144,7 605,8 509,9 134,8 654,6 740,7 3,0 4,13 145,4 0,440 146,4 61,9 508,6 19,4 655,0 74,4 3,40 4,413 147, 0,4 148, 60,5 507,4 14,4 655,6 744,9 3,60 4,613 148,8 0,405 149,9 67,6 506,1 118,9 656,0 746,5 3,80 4,813 150,4 0,389 151,5 634,3 505,0 114,3 656,5 748,6 4,00 5,013 15,0 0,374 153,1 641,0 503,8 109,3 656,9 750,3 4,0 5,13 153,4 0,361 154,6 647,3 50,7 104,7 657,3 75,0 4,40 5,413 154,8 0,348 156,1 653,6 501,6 100,1 657,7 753,7 4,60 5,613 156, 0,336 157,6 659,8 500,6 095,9 658, 755,8 4,80 5,813 157,6 0,35 159,0 665,7 499,5 091,3 658,5 757,0 5,00 6,013 158,9 0,315 160,3 671,1 498,5 087,1 658,8 758,3 5,50 6,513 16,1 0,9 163,6 685,0 496,1 077,1 659,7 76,0 6,00 7,013 165,0 0,7 166,7 697,9 493,8 067,4 660,5 765,4 6,50 7,513 167,8 0,55 169,6 710,1 491,6 058, 661, 768,3 7,00 8,013 170,5 0,40 17,4 71,8 489,4 049,0 661,8 770,8 7,50 8,513 173,0 0,7 175,1 733,1 487,4 040,6 66,5 773,8 8,00 9,013 175,4 0,15 177,6 743,6 485,4 03,3 663,0 775,8 8,50 9,513 177,7 0,04 180,0 753,6 483,5 04,3 663,5 777,9 9,00 10,013 180,0 0,194 18,3 763,3 481,6 016,4 663,9 779,6 9,50 10,513 18,1 0,185 184,6 77,9 479,8 008,8 664,4 781,7 10,00 11,013 184,1 0,177 186,8 78,1 478,0 001,3 664,8 783,4 11,00 1,013 188,0 0,163 190,9 799,3 474,6 1987,1 665,5 786,3 1,00 13,013 191,7 0,151 194,8 815,6 471,4 1973,7 666, 789, 13,00 14,013 195,1 0,141 198,5 831,1 468,3 1960,7 666,8 791,8 14,00 15,013 198,3 0,13 0,0 845,7 465,3 1948,1 667,3 793,9 15,00 16,013 01,4 0,14 05,3 859,6 46,5 1936,4 667,8 795,9 16,00 17,013 04,4 0,117 08,5 87,9 459,7 194,7 668, 797,6 17,00 18,013 07, 0,110 11,5 885,5 457,0 1913,4 668,5 798,9 18,00 19,013 09,9 0,105 14,4 897,8 454,4 190,5 668,8 800,1 19,00 0,013 1,5 0,100 17, 909,4 451,8 1891,6 669,0 801,0 0,00 1,013 15,0 0,095 0,0 91,1 449,4 1881,5 669,4 80,6 1,00,013 17,3 0,090,6 93,0 447,0 1871,5 669,6 803,5,00 3,013 19,6 0,087 5,1 94,4 444,6 1861,5 669,7 803,9 3,00 4,013 1,8 0,083 7,6 95,9 44, 1851,4 669,8 804,3 4,00 5,013 4,0 0,080 30,0 963,0 440,0 184, 670,0 805, 5,00 6,013 6,1 0,077 3,3 97,6 437,7 183,6 670,0 805, 441

Pm bar 0.4 0.6 0.8 1 1.5.5 3 4 5 6 7 8 9 10 1 14 16 18 0 MSS FLOWRTES OF STURTED STEM FOR DIFFERENT VELOCITIES IN PIPES DIN448 - STNDRD v FLOWRTE Kgs / h m/s DN DN DN DN DN DN DN DN DN DN DN DN DN DN 15 0 5 3 40 50 65 80 100 15 150 00 50 300 15 10 17 8 48 64 103 171 36 397 600 878 1476 346 3319 5 17 9 47 80 107 171 85 393 66 1000 1464 459 3911 553 40 8 46 75 18 171 74 456 68 1058 1601 34 3935 657 8851 15 1 0 33 56 76 11 0 78 468 708 1036 1741 769 3917 5 0 34 55 94 16 0 336 463 781 1181 177 90 4615 658 40 33 54 89 151 0 34 538 741 149 1889 764 4644 7384 10445 15 13 35 60 81 130 16 97 501 757 1108 186 960 4187 5 36 59 101 135 16 360 495 835 16 1846 3103 4934 6979 40 35 58 95 161 16 346 575 79 1335 019 954 4964 7894 11166 15 14 4 39 67 89 143 38 37 55 835 11 05 363 4615 5 4 40 65 111 149 38 396 546 90 1391 035 340 5438 769 40 38 64 104 178 38 381 634 873 147 6 356 5471 8700 1307 15 18 9 48 8 110 176 93 404 681 1030 1507 53 406 5694 5 30 49 80 137 184 94 489 673 1135 1716 511 419 6710 9491 40 47 79 19 19 94 470 783 1078/ 1816 746 4018 6751 10735 15185 15 1 35 57 97 131 09 347 478 806 119 1784 998 4767 6743 5 35 58 95 16 18 348 579 797 1344 03 973 4996 7945 1138 40 56 93 15 59 348 557 97 176 150 35 4757 7994 1711 17980 15 4 40 66 11 151 41 401 553 931 1409 061 3463 5506 7789 5 41 67 110 187 51 40 669 91 155 348 3435 5771 9177 198 40 65 108 176 300 40 643 1070 1474 484 3756 5495 934 14684 0770 15 8 46 75 17 171 73 454 66 1055 1595 333 391 635 880 5 46 76 15 1 85 455 757 1043 1758 658 3889 6535 1039 14699 40 73 1 199 339 455 78 11 1669 813 453 63 10456 1667 3519 15 34 56 9 157 11 337 560 771 1300 1966 876 4833 7685 10871 5 57 94 154 61 351 561 934 186 167 377 4794 8055 1809 18119 40 90 150 46 418 561 898 1494 057 3467 543 7670 1888 0495 8990 15 40 67 109 186 50 400 665 916 1544 334 3415 5738 915 1907 5 67 111 18 310 417 666 1109 157 573 3890 569 9564 1508 151 40 107 178 9 496 667 1066 1774 443 4116 64 9107 1530 4333 3440 15 47 77 17 16 89 463 770 1061 1788 703 3955 6646 10568 14948 5 78 19 11 359 48 77 184 1768 979 4505 659 11076 17613 4913 40 14 06 338 575 77 135 054 89 4767 708 10546 177 8180 39861 15 53 88 144 44 38 55 873 10 06 3064 448 753 11977 16941 5 88 146 39 407 547 875 1455 004 3377 5106 7470 1553 19961 835 40 141 34 383 65 875 1399 38 306 540 8170 11953 0084 31937 45176 15 59 98 160 73 366 586 975 134 61 340 5003 8407 13369 18911 5 98 163 67 455 610 976 164 37 3769 5700 8339 1401 8 31518 40 157 61 47 77 977 156 599 3579 6031 910 1334 40 35651 5049 15 65 109 178 30 406 649 1080 1487 506 3790 5545 9318 14816 0958 5 109 181 96 504 676 108 1800 479 4177 6317 94 1559 4694 34930 40 174 89 474 806 108 1731 880 3966 6683 10107 14787 4847 39510 55888 15 7 119 195 331 445 711 1184 1630 747 4154 6078 101 1639 971 5 119 198 34 55 741 1186 1973 717 4578/ 693 1019 1701 7066 3885 40 191 317 519 884 1186 1897 3157 4347 735 11077 1607 733 43305 6155 15 84 139 8 388 51 834 1388 1911 30 4869 714 11971 19036 696 5 140 3 380 647 869 1390 313 3185 5367 8115 11873 19951 3176 44877 40 4 37 608 1036 1390 4 3700 5095 8587 1985 18998 319 50761 71803 15 96 160 61 444 596 954 1587 186 3683 5570 8150 13694 1776 3080 5 160 66 435 740 994 1590 645 3643 6139 984 13583 83 3693 51336 40 56 45 696 1185 1591 544 433 589 983 14854 173 36517 58068 8138 15 108 180 94 501 673 1076 1791 466 4156 684 9194 15450 4567 34751 5 181 300 491 835 11 1794 985 4110 696 10474 1534 5749 40945 57918 40 89 480 785 1337 1794 870 4775 6576 1108 16758 4518 41199 65513 9668 15 11 01 38 559 750 1199 1995 748 4631 7003 1045 1715 7375 387 5 01 334 547 931 150 1999 336 4580 7718 11671 17075 869 4565 64537 40 3 535 875 1489 000 3198 531 738 1348 18673 730 45907 73000 10359 15 134 363 617 89 136 05 3037 5118 7740 1134 1907 3056 4798 5 3 369 604 109 1381 09 3676 506 8530 1899 18873 3171 5047 71330 40 356 591 967 1646 10 3535 5881 8099 13648 0639 30196 50740 80684 11418 44