Cemal Yaman
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1 TB
2 3 V L m³/h m 1 3.5 0.8 2 2.5 4.2 3 1.6 13.0 4 1.6 1.2 KRİTİK HAT D:2 1+3+4
DAĞITIM HATTI BORUSU TS 301 'E GÖRE 4 5 6 7 8 9 10 11 DN W Pr/L Pr Ksi Pr h Pa mm m/s mbar/m mbar mbar mbar 20 2.7 0.07620 0.06096 0.9 0.02605 0.50 -0.0200 20 1.9 0.04050 0.17010 3.2 0.04586 -1.00 0.0400 20 1.18 0.01234 0.16042 4.3 0.02377 0.20 -0.0080 15 2.24 0.08368 0.10042 1 0.01992 -1.20 0.0480 0.41153 < 0,8 UYGUNDUR
12 ΣPt mbar 0.06701 0.25596 0.17619 0.16834
10 9 8 7 5 4 3
24.5 22.5 20.5 18.5 14 11.8 9.5
EKLEME PARÇALARI REDÜKSİYON DİRSEK 90º T PARÇA DÜZ GEÇİŞ KURUVA TE TE PARÇASI DİRSEK 45º KÜRESEL VANA DİŞLİ DİRSEK TE PARÇASI ZIT AKIŞLI KSİ TOPLAMI
KSİ DEĞERİ TESPİT FORMU 1 2 3 4 0.5 1 1 0.4 1 3 7 0 1.5 1.3 0.3 0.5 1 1 0.5 1.5 1 1 0.9 3.2 4.3 1.0
ζ
1 TB 1 2 3 4 5 6 7 8 9 KRİTİK HAT 1+2+3+7
2 V m³/h 16.5 14 11.8 9.5 7 3.5 3.5 3.5 3.5 #REF!
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 0.9 3.2 4.3 1 #REF! #REF! #REF! #REF! #REF!
9 Pr mbar 0.0389 0.0996 0.0951 0.0143 #REF! #REF! #REF! #REF! #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 0.5309 0.1866 0.0836 -0.0553 #REF! #REF! #REF! #REF! #REF!
2 3 V L m³/h m 1 3.5 0.8 2 2.5 4.2 3 1.6 13.0 4 1.6 1.2 KRİTİK HAT D:2 1+3+4
DAĞITIM HATTI BORUSU TS 301 'E GÖRE 4 5 6 7 8 9 10 11 DN W Pr/L Pr Ksi Pr h Pa mm m/s mbar/m mbar mbar mbar 20 2.7 0.07620 0.06096 0.9 0.02605 0.50 -0.0200 20 1.9 0.04050 0.17010 3.2 0.04586 -1.00 0.0400 20 1.18 0.01234 0.16042 4.3 0.02377 0.20 -0.0080 15 2.24 0.08368 0.10042 1 0.01992 -1.20 0.0480 0.41153 < 0,8 UYGUNDUR
12 ΣPt mbar 0.06701 0.25596 0.17619 0.16834
10 9 8 7 5 4 3
24.5 22.5 20.5 18.5 14 11.8 9.5
EKLEME PARÇALARI REDÜKSİYON DİRSEK 90º T PARÇA DÜZ GEÇİŞ KURUVA TE TE PARÇASI DİRSEK 45º KÜRESEL VANA DİŞLİ DİRSEK TE PARÇASI ZIT AKIŞLI KSİ TOPLAMI
KSİ DEĞERİ TESPİT FORMU 1 2 3 4 0.5 1 1 0.4 1 3 7 0 1.5 1.3 0.3 0.5 1 1 0.5 1.5 1 1 0.9 3.2 4.3 1.0
ζ
1 TB 1 2 3 4 5 6 7 8 9 KRİTİK HAT 1+2+3+7
2 V m³/h 16.5 14 11.8 9.5 7 3.5 3.5 3.5 3.5 #REF!
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 0.9 3.2 4.3 1 #REF! #REF! #REF! #REF! #REF!
9 Pr mbar 0.0389 0.0996 0.0951 0.0143 #REF! #REF! #REF! #REF! #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 0.5309 0.1866 0.0836 -0.0553 #REF! #REF! #REF! #REF! #REF!
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