1 TB
2 V m³/h 9.5 7 3.5 3.5 3.5 3.5 1.6 1.6 2.5
1 2 3 4 5 6 7 8 9 KRİTİK HAT KOLON 1+2+4 DAİRE 2 5+6+7+8
3 L m 8.5 0.3 1 0.7 9 1.2 4.4 0.3 1
DAĞITIM HATTI BORUSU TS 301 'E GÖRE 4 5 6 7 8 9 DN W Pr/L Pr Ksi Pr mm m/s mbar/m mbar mbar 32 2.6 0.03650 0.31025 2 0.05367 32 1.9 0.02060 0.00618 0 0.00000 25 1.7 0.02340 0.02340 1.4 0.01606 25 1.7 0.02340 0.01638 2.3 0.02639 25 1.7 0.02340 0.21060 4.8 0.05507 20 2.7 0.07620 0.09144 0.9 0.02605 20 1.18 0.01234 0.05430 1.2 0.00663 15 2.24 0.08368 0.02510 1 0.01992 20 1.9 0.04050 0.04050 1.8 0.02580 0.3489 < 1 UYGUNDUR 0.4771 < 0,8 UYGUNDUR
10 h 2.30 0.00 -0.70 -0.70 1.50 0.00 -0.90 -0.30 -1.00
11 Pa mbar -0.0920 0.0000 0.0280 0.0280 -0.0600 0.0000 0.0360 0.0120 0.0400
12 ΣPt mbar 0.27192 0.00618 0.06746 0.07077 0.20567 0.11749 0.09693 0.05702 0.10630
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
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
0.5 0.4 0 1.5 1.3 0.3 0.5 0.5 1.5
1 5
2
KSİ DEĞERİ TESPİT FORMU 3 4 5 6 7 1 1 1 1 12 1 3
8 1
1 1
1
9
1 1
1
2.0 0.0 1.4 2.3 4.8 0.9 1.2 1.0 1.8
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 0.7348
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 2 0 1.4 2.3 4.8 0.9 1.2 1 1.8
9 Pr mbar 0.0865 0.0000 0.0310 0.0330 0.0688 0.0036 0.0138 0.0115 0.0207
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 0.5785 0.0870 0.0195 -0.0366 0.0106 -0.0993 0.0498 0.0476 0.0333