Ahmet Serbest

1 TB

2 V m³/h 9.5 7 3.5 3.5 3.5 3.5 3.5 2.5 1.6

1 2 3 4 5 6 7 8 9 KRİTİK HAT KOLON 1+4+6 DAİRE 2 11+12+14

DAĞITIM HATTI BORUSU TS 301 3 4 5 6 L DN W Pr/L m mm m/s mbar/m 12.2 32 2.6 0.03650 3 32 1.9 0.02060 3 32 1 0.00570 2 25 1.7 0.02340 2 25 1.7 0.02340 1.5 25 1.7 0.02340 2.6 20 2.7 0.07620 3.3 20 1.9 0.04050 1.5 15 2.24 0.08368 0.4665 < 1 UYGUNDUR #REF! < 0,8 UYGUNDUR

'E GÖRE 7 Pr mbar 0.44530 0.06180 0.01710 0.04680 0.04680 0.03510 0.19812 0.13365 0.12552

8 Ksi 4.5 0 0.4 1.4 2.7 3.5 2.1 1.7 3.5

9 Pr mbar 0.12077 0.00000 0.00159 0.01606 0.03098 0.04016 0.06078 0.02436 0.06972

10 h 2.10 3.00 3.00 -0.20 -0.20 -0.10 0.40 -1.00 -1.20

11 12 Pa ΣPt mbar mbar -0.0840 0.48207 -0.1200 -0.05820 -0.1200 -0.10131 0.0080 0.07086 0.0080 0.08578 0.0040 0.07926 -0.0160 0.24290 0.0400 0.19801 0.0480 0.24324

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 3 4 5 6 7 1 1 1 1 1 1 1 3 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 8 9 0.5 1 0.4 10 3 3 0 1.5 1.3 1 1 1 0.3 0.5 1 1 1 1 1 1 0.5 1.5 4.5 0.0 0.4 1.4 2.7 3.5 2.1 1.7 3.5

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 0.8311

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 4.5 0 0.4 1.4 2.7 3.5 2.1 1.7 3.5

9 Pr mbar 0.1945 0.0000 0.0088 0.0201 0.0387 0.0139 0.0241 0.0195 0.0402

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 0.6865 0.0870 -0.0026 -0.0495 -0.0195 -0.0890 0.0602 0.0556 0.0528