Doruk Apt
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1 TB
DAĞITIM HATTI BORUSU TS 301 'E GÖRE 5 6 7 8 9 W Pr/L Pr Ksi Pr m/s mbar/m mbar mbar 3.05 0.02965 0.58114 5.7 0.21051 2.85 0.02525 0.01263 0 0.00000 2.55 0.02120 0.08268 1.2 0.03098 2.1 0.01410 0.04230 0 0.00000 2.36 0.02520 0.07560 0.5 0.01106 1.9 0.02060 0.06180 0.5 0.00717 1.7 0.02340 0.02574 2.7 0.03098 1.7 0.02340 0.03276 2.7 0.03098 1.7 0.02340 0.02574 2.9 0.03327 1.7 0.02340 0.03276 2.9 0.03327 1.7 0.02340 0.05850 3.5 0.04016 1.7 0.02340 0.00468 2.3 0.02639 1.7 0.02340 0.09360 3.2 0.03671 2.7 0.07620 0.10668 0.5 0.01447 1.9 0.04050 0.12150 2.1 0.03010 1.18 0.01234 0.01481 2.3 0.01271
2 3 4 V L DN m³/h m mm 1 24.5 19.60 50 2 22.5 0.50 50 3 20.5 3.90 50 4 16.5 3.00 50 5 11.8 3.00 40 6 7 3.00 32 7 3.5 1.10 25 8 3.5 1.40 25 9 3.5 1.10 25 10 3.5 1.40 25 11 3.5 2.50 25 12 3.5 0.20 25 13 3.5 4 25 14 3.5 1.4 20 15 2.5 3 20 16 1.6 1.2 20 KRİTİK HAT KOLON 1+2+11 D:3 13+14+15
0.85893 < 1 UYGUNDUR 0.42306 < 0,8 UYGUNDUR
10 h 1.20 0.00 3.20 3.00 3.00 3.00 -0.20 -0.20 -0.20 -0.20 -0.10 -0.20 0.50 0.00 -1.00 -1.20
11 Pa mbar -0.0480 0.0000 -0.1280 -0.1200 -0.1200 -0.1200 0.0080 0.0080 0.0080 0.0080 0.0040 0.0080 -0.0200 0.0000 0.0400 0.0480
12 ΣPt mbar 0.74365 0.01263 -0.01434 -0.07770 -0.03334 -0.05103 0.06472 0.07174 0.06701 0.07403 0.10266 0.03907 0.11031 0.12115 0.19160 0.07552
10 9 8 7 5 4 3 2 1
24.5 22.5 20.5 18.5 14 11.8 9.5 7 3.5
KSİ DEĞERİ TESPİT FORMU 6 7 8 9 10 11 12 13 14 15 1 1 1 1 1 1 1 1 1 1 1 1 3 8 4
EKLEME PARÇALARI
ζ
REDÜKSİYON DİRSEK 90º T PARÇA DÜZ GEÇİŞ KURUVA TE TE PARÇASI DİRSEK 45º KÜRESEL VANA DİŞLİ DİRSEK TE PARÇASI ZIT AKIŞLI KSİ TOPLAMI
1 2 3 4 5 0.5 1 0.4 10 3 0 1.5 1 1 1.3 1 1 1 1 0.3 4 0.5 1 1 1 1 1 1 1 1 0.5 1.5 5.7 0.0 1.2 0.0 0.5 0.5 2.7 2.7 2.9 2.9 3.5 2.3 3.2 0.5 2.1
16 1
1 1
2.3
1 TB
2 V m³/h 16.5 14 11.8 9.5 7 3.5 3.5 3.5 3.5
1 2 3 4 5 6 7 8 9 KRİTİK HAT 1+2+3+7 0.9075
3 L m 12.8 2.5 5.1 3 3 3 1.2 1.2 0.2
DAĞITIM HATTI BORUSU TS 301 'E GÖRE 4 5 6 7 DN W Pr/L Pr mm m/s mbar/m mbar 40 3.3 0.0475 0.6080 40 2.8 0.0348 0.0870 40 2.36 0.0252 0.1285 40 1.9 0.02 0.0504 32 1.9 0.02 0.0618 32 1 0.01 0.0171 25 1.7 0.02 0.0281 25 1.7 0.02 0.0281 25 1.7 0.02 0.0047
8 Ksi 5.7 0 1.2 0 0.5 0.5 2.7 2.7 2.9
9 Pr mbar 0.2464 0.0000 0.0265 0.0000 0.0072 0.0020 0.0310 0.0310 0.0333
10 h m 2.9 0 3.5 3 3 3 -0.2 -0.2 -0.2
11 Pa mbar -0.1160 0.0000 -0.1400 -0.1200 -0.1200 -0.1200 0.0080 0.0080 0.0080
12 ΣPt mbar 0.7384 0.0870 0.0151 -0.0696 -0.0510 -0.1009 0.0671 0.0671 0.0460
DAĞITIM HATTI BORUSU TS 301 'E GÖRE 5 6 7 8 9 W Pr/L Pr Ksi Pr m/s mbar/m mbar mbar 3.05 0.02965 0.58114 5.7 0.21051 2.85 0.02525 0.01263 0 0.00000 2.55 0.02120 0.08268 1.2 0.03098 2.1 0.01410 0.04230 0 0.00000 2.36 0.02520 0.07560 0.5 0.01106 1.9 0.02060 0.06180 0.5 0.00717 1.7 0.02340 0.02574 2.7 0.03098 1.7 0.02340 0.03276 2.7 0.03098 1.7 0.02340 0.02574 2.9 0.03327 1.7 0.02340 0.03276 2.9 0.03327 1.7 0.02340 0.05850 3.5 0.04016 1.7 0.02340 0.00468 2.3 0.02639 1.7 0.02340 0.09360 3.2 0.03671 2.7 0.07620 0.10668 0.5 0.01447 1.9 0.04050 0.12150 2.1 0.03010 1.18 0.01234 0.01481 2.3 0.01271
2 3 4 V L DN m³/h m mm 1 24.5 19.60 50 2 22.5 0.50 50 3 20.5 3.90 50 4 16.5 3.00 50 5 11.8 3.00 40 6 7 3.00 32 7 3.5 1.10 25 8 3.5 1.40 25 9 3.5 1.10 25 10 3.5 1.40 25 11 3.5 2.50 25 12 3.5 0.20 25 13 3.5 4 25 14 3.5 1.4 20 15 2.5 3 20 16 1.6 1.2 20 KRİTİK HAT KOLON 1+2+11 D:3 13+14+15
0.85893 < 1 UYGUNDUR 0.42306 < 0,8 UYGUNDUR
10 h 1.20 0.00 3.20 3.00 3.00 3.00 -0.20 -0.20 -0.20 -0.20 -0.10 -0.20 0.50 0.00 -1.00 -1.20
11 Pa mbar -0.0480 0.0000 -0.1280 -0.1200 -0.1200 -0.1200 0.0080 0.0080 0.0080 0.0080 0.0040 0.0080 -0.0200 0.0000 0.0400 0.0480
12 ΣPt mbar 0.74365 0.01263 -0.01434 -0.07770 -0.03334 -0.05103 0.06472 0.07174 0.06701 0.07403 0.10266 0.03907 0.11031 0.12115 0.19160 0.07552
10 9 8 7 5 4 3 2 1
24.5 22.5 20.5 18.5 14 11.8 9.5 7 3.5
KSİ DEĞERİ TESPİT FORMU 6 7 8 9 10 11 12 13 14 15 1 1 1 1 1 1 1 1 1 1 1 1 3 8 4
EKLEME PARÇALARI
ζ
REDÜKSİYON DİRSEK 90º T PARÇA DÜZ GEÇİŞ KURUVA TE TE PARÇASI DİRSEK 45º KÜRESEL VANA DİŞLİ DİRSEK TE PARÇASI ZIT AKIŞLI KSİ TOPLAMI
1 2 3 4 5 0.5 1 0.4 10 3 0 1.5 1 1 1.3 1 1 1 1 0.3 4 0.5 1 1 1 1 1 1 1 1 0.5 1.5 5.7 0.0 1.2 0.0 0.5 0.5 2.7 2.7 2.9 2.9 3.5 2.3 3.2 0.5 2.1
16 1
1 1
2.3
1 TB
2 V m³/h 16.5 14 11.8 9.5 7 3.5 3.5 3.5 3.5
1 2 3 4 5 6 7 8 9 KRİTİK HAT 1+2+3+7 0.9075
3 L m 12.8 2.5 5.1 3 3 3 1.2 1.2 0.2
DAĞITIM HATTI BORUSU TS 301 'E GÖRE 4 5 6 7 DN W Pr/L Pr mm m/s mbar/m mbar 40 3.3 0.0475 0.6080 40 2.8 0.0348 0.0870 40 2.36 0.0252 0.1285 40 1.9 0.02 0.0504 32 1.9 0.02 0.0618 32 1 0.01 0.0171 25 1.7 0.02 0.0281 25 1.7 0.02 0.0281 25 1.7 0.02 0.0047
8 Ksi 5.7 0 1.2 0 0.5 0.5 2.7 2.7 2.9
9 Pr mbar 0.2464 0.0000 0.0265 0.0000 0.0072 0.0020 0.0310 0.0310 0.0333
10 h m 2.9 0 3.5 3 3 3 -0.2 -0.2 -0.2
11 Pa mbar -0.1160 0.0000 -0.1400 -0.1200 -0.1200 -0.1200 0.0080 0.0080 0.0080
12 ΣPt mbar 0.7384 0.0870 0.0151 -0.0696 -0.0510 -0.1009 0.0671 0.0671 0.0460
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