Dursun Kahraman

1 TB

2 V m³/h

1 14 2 11.8 3 9.5 4 7 5 3.5 6 3.5 7 3.5 8 3.5 KRİTİK HAT KOLON 1+2+3+6

DAĞITIM HATTI BORUSU TS 301 3 4 5 6 L DN W Pr/L m mm m/s mbar/m 9.1 40 2.8 0.03480 9.4 40 2.36 0.02520 3 32 2.6 0.03650 3 32 1.9 0.02340 3.9 32 1 0.02340 0.9 25 1.7 0.02340 0.4 25 1.7 0.02340 0.2 25 1.7 0.02340 0.5103 < 1 UYGUNDUR

'E GÖRE 7 Pr mbar 0.31668 0.23688 0.10950 0.07020 0.09126 0.02106 0.00936 0.00468

8 Ksi 3.3 1.9 0.5 0 1.2 1.4 2.7 2.7

9 Pr mbar 0.10271 0.04201 0.01342 0.00000 0.00476 0.01606 0.03098 0.03098

10 h 1.80 4.10 3.00 3.00 3.00 -0.20 -0.20 -0.20

11 12 Pa ΣPt mbar mbar -0.0720 0.34739 -0.1640 0.11489 -0.1200 0.00292 -0.1200 -0.04980 -0.1200 -0.02398 0.0080 0.04512 0.0080 0.04834 0.0080 0.04366

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 7

KSİ DEĞERİ TESPİT FORMU 2 3 4 5 6 1 1 4 3 1

7 1 1

8 1 1

1

1

1

1

1 1

1

3.3 1.9 0.5 0.0 1.2 1.4 2.7 2.7

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 0.8474

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 3.3 1.9 0.5 0 1.2 1.4 2.7 2.7 #REF!

9 Pr mbar 0.1427 0.0591 0.0111 0.0000 0.0172 0.0056 0.0310 0.0310 #REF!

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 0.6347 0.1461 -0.0004 -0.0696 -0.0410 -0.0973 0.0671 0.0671 #REF!