Problem on Humidity - Process Calculations & Thermodynamics (PCT). Please refer same.
If you wish to be part of detailed understanding of concepts through an interactive sessions, please register to ATTEMPT Batch#02 Course (April to October 2021).
Write us at attempttosucceed@gmail.com or comment below so that we can revert back to you.
Environmental comparison mailer vs. boxPAC Worldwide
A cosmetic customer of ours came to us wanting to switch to a more environmentally friendly option to ship their product in. The Jumbojacket 1/2" bubble mailer was the perfect solution. The 1/2" bubble would protect their product just as a box with void fill, plus it would drastically decrease their environmental impact both in the manufacturing of the package plus the waste saved by downsizing to a mailer vs. a box with void fill. Here you'll see the comparison of both packaging options.
www.pac.com
info@pac.com
Problem on Humidity - Process Calculations & Thermodynamics (PCT). Please refer same.
If you wish to be part of detailed understanding of concepts through an interactive sessions, please register to ATTEMPT Batch#02 Course (April to October 2021).
Write us at attempttosucceed@gmail.com or comment below so that we can revert back to you.
Environmental comparison mailer vs. boxPAC Worldwide
A cosmetic customer of ours came to us wanting to switch to a more environmentally friendly option to ship their product in. The Jumbojacket 1/2" bubble mailer was the perfect solution. The 1/2" bubble would protect their product just as a box with void fill, plus it would drastically decrease their environmental impact both in the manufacturing of the package plus the waste saved by downsizing to a mailer vs. a box with void fill. Here you'll see the comparison of both packaging options.
www.pac.com
info@pac.com
HEAT TRANSFER : STEADY STATE HEAT CONDUCTION NUMERICALS part3PRAMOD MAURYA
NUMERICAL SOLUTION FROM MUMBAI UNIVERSITY QUESTION PAPERS
.An electric cable of 20 mm diameter is insulated with rubber, which is exposed to atmosphere at 30°C. Calculate the most economical thickness of rubber insulation (k = 0.175 W/m.K). When cable surface temperature with and without insulation is at 70°C. Also calculate the percentage increase in heat dissipation and current carrying capacity when most economical thickness is provided. Take heat transfer coefficient, h = 9.3 W/m2.K.
Proje Kontrol Açıklamalı El Kitabı v.02.01Yusuf Yıldız
Bu kitapçık T.M.M.O.B İnşaat Mühendisleri Odası İzmir ve Bursa Şubeleri tarafından, statik proje hazırlayan üyelerimize bir yol göstermesi ve kontrol hizmetinin daha sağlıklı yapılabilmesi için hazırlanmıştır.
HEAT TRANSFER : STEADY STATE HEAT CONDUCTION NUMERICALS part3PRAMOD MAURYA
NUMERICAL SOLUTION FROM MUMBAI UNIVERSITY QUESTION PAPERS
.An electric cable of 20 mm diameter is insulated with rubber, which is exposed to atmosphere at 30°C. Calculate the most economical thickness of rubber insulation (k = 0.175 W/m.K). When cable surface temperature with and without insulation is at 70°C. Also calculate the percentage increase in heat dissipation and current carrying capacity when most economical thickness is provided. Take heat transfer coefficient, h = 9.3 W/m2.K.
Proje Kontrol Açıklamalı El Kitabı v.02.01Yusuf Yıldız
Bu kitapçık T.M.M.O.B İnşaat Mühendisleri Odası İzmir ve Bursa Şubeleri tarafından, statik proje hazırlayan üyelerimize bir yol göstermesi ve kontrol hizmetinin daha sağlıklı yapılabilmesi için hazırlanmıştır.
With great pleasure and enthusiasm, Thermodyne Engineering Systems present you with the maiden edition of our Thermodyne Boiler Bible. With an industrial presence of 24 years and serving a vast variety of clients the undersigned felt a special bond of respect and gratitude for all of you who made us grow with yourselves.for More Detail visit our website http://www.thermodyneboilers.com/
1. Gösterim
Uzunluk
Alan
Hacim
Kütle
Yo¤unluk
H›z
Debi
Bas›nç
Enerji Is›
Güç
Is› gücü
So¤utma
Özgül ›s›
Is› ak›s›
Is› Geçifl
Katsay›s›
Is› ‹letim
Katsay›s›
Is› Geçifl
Direnci
Is› ‹letim
Direnci
S›cakl›k
L
A, F
V
m
d
w, V
V, Q
P
E, W, Q
P
C, Cp
q
K
k
1/K
1/k
T
m
m2
m3
L
g
kg
kg / m3
m / s
m3 / s
Pa
bar
mbar
N / m2
kJ
kWh
kJ / h
kW
kJ / kgK
kJ / m2h
W / m2
W/ m2K
W/mK
m2K / W
K
in
ft
sq in
sq ft
acre
cu in
cu ft
gal
oz
lb
lb / cu ft
ft / min
cfm
psi
in H2O
lb / ft2
Btu
Btu / h
HP
ton ref.
Btu / lb 0
F
Btu / hft2
Btu/h ft2 0
F
Btu/h ft F
h ft2 F/Btu
0
F
m
m2
m3
L
g
kg
kg / m3
m / s
m3 / h
m3 / s
L / s
kg / cm2
kg / m2
mmSS
atm
kcal
kcal / h
Kcal / kg 0
C
kcal / m2h
kcal/m2h 0
C
kcal/mh °C
m2h °C/ kcal
°C
1 m = 39,37 in 1 in = 25,4 mm
1 m = 3,281 ft 1 ft = 30,48 cm
1 km = 0,6214 kara mili 1 mil (kara) = 1,60934 km
1 km = 0,5396 deniz mili 1 mil (deniz) = 1,85318 km
1 m2 = 1550 sq in 1 sq in = 645,16 mm2
1 m2 = 10,764 sq ft 1 sq ft = 0,0929 m2
1 ha = 10000 m2 1 acre = 0,40468 ha
1 ha = 2,471 acre 1 sq mile = 2,58999 km2
1 m3 = 1000 L 1 U.S. barrel = 42 U.S.gal
1 L = 61,024 cu in 1 cu in = 16,3871 cm3
1 L = 0,2642 gal 1 cu ft = 0,02831 m3
1 m3 = 35,315 cu ft 1 gal = 3,78541 L
1 kg = 35,274 oz 1 oz = 28,3495 g
1 kg = 2,2046 lb 1 lb = 0,4536 g
1 g = 15,432 grain 1 lb = 16 oz
1 kg/m3 = 0,06243 lb/cuft
1 m/s = 196,85 ft/min 1 km/h = 0,6214 mph
1 km/h = 0,54 Kn 1 ft/min = 0,508 cm/s
1 m3/s = 3600 m3/h 1 cu ft/min = 28,3171 L/min
1 m3/h = 0,5886 cfm 1 cu ft/min = 1,700 m3/h
1 m3/h = 4,403 gal/min 1 gal/min = 0,272 m3/h
1 Pa = 1 N/m2 1 mbar = 100 Pa
1 bar = 100.000 Pa 1 bar = 14,504 psi
1 bar = 0,987 atm 1 kPa = 7,50062 mmHg
1 mbar = 10,19 mmSS 1 in H2O = 249,089 Pa
1 mmSS = 9,87 Pa 1 mbar = 0,4015 in H2O
1 bar = 14,504 psi 1 bar = 1,02 kg/cm2
1 mbar = 2,089 lb/ft2
1 lb/ft2
= 47,88 N/m2
1 kWh = 3600 kJ 1 kJ = 0,2388 kcal
1 kWh = 860 kcal 1 kcal = 4,1868 kJ
1 kJ = 0,948 Btu 1 Btu = 1,055 kJ
1 kcal = 3,97 Btu 1 Btu = 0,252 kcal
1 kW = 1 kJ/s 1 HP = 735,5 W
1 kW = 860 kcal/h 1 HP = 632 kcal/h
1 kW = 3415 Btu/h 1 Btu/h = 0,252 kcal/h
1 kW = 1,341 HP 1 kcal/h = 3,97 Btu/h
1 kW = 0,2843 tons of refrigeration
1 ton ref. = 3,517 kW 1 ton ref. = 3024 kcal/h
1 kJ/kgK = 4,187 kcal/kg 0
C 1 kJ/kg0
K = 0,2388 Btu/lb 0
F
1 W/ m2 = 3,6 kJ/ m2h 1 kJ/m2 = 0,0881 Btu/ft2
1 W/ m2 = 0,86 kcal/m2h 1 W/ m2 = 0,317 Btu/hft2
1 W/ m2K = 0,1761 Btu/h ft2 0
F 1 Btu/h ft2 0
F = 5,678 W/m 2
K
1 W/ m2K = 0,86 kcal/m2h 0
C
1 W /mK = 0,578 Btu/h ft F 1 Btu/h ft F = 1,7296 W/mK
1 W/mK = 0,86 kcal/ mh 0
C 1 kcal/ mh 0
C = 1,162 W/mK
1 h ft2 F/Btu = 0,1761 m2K/W
1 m2K / W = 1,162 m2h 0
C / kcal
1 mK/W = 1,7296 h ft F/BTU 1 h ft F/BTU = 0,5782 mK/W
1 mK/W = 1,162 mh 0
C / kcal
0
C = ( 0
F-32 ) . 5/ 9 0
F= 0
C. 9/ 5 +32 K = 273+0
C
Dönüflüm
SI
Büyüklük
22- B‹R‹M DÖNÜfiÜMLER‹
Sembol
Metrik I-P
629