Paragraph 1.3. 1 41 5 6' 1.9 10 111 112 113 14 115 E After the diffuser selection and the specification of the required exhaust flow, th Hucts connecting the centrifugal fan is designed using a duct sizer program. Addition d loss through the duct is considered to be about 1 Pa/m or 0.12 inch Wc/100 ft[10] w is then calculated using this program, as depicted in Figure 3-6 below. Exit DesignTools DuctSizer... Print Clear Units About 20°C Air STP X Fluid density Fluid viscosity Specific Heat Energy factor 1.2014 kg/m² 0.0643 kg/m-h 1.0048 kJ/kg*C 1.21 W/C-L/s Flow rate 900 L/s Head loss Pa/m Velocity 7.355 m/s Equivalent 573.5 mm diameter Flow Area Duct size Equivalent Diameter Fluid velocity Reynolds Number Friction factor 283,930 500 mm X 550 mm 573.1 mm 0.2580 m² 7.364 m/s 0.01753 Velocity Pressure Head Loss 32.5862 Pa 0.998 Pa/m Aduct = Apipe = π X² (3-6) Where Re: Reynold Number V: Velocity 771 Aduct Apipe Area of duct and pipe m² deqivelent pipe Equivalent diameter of pipe with same area of duct (m^2) Then the equivalent diameter is 0.59 m Then the Reynold number is 435000, this show that the flow is turbulent then using the moody chart. And the relative pipe equivalent roughness is about 0.05[12]. Then refer to the moody chart as shown in Figure 3-9[13]. Moody Diagram
Paragraph 1.3. 1 41 5 6' 1.9 10 111 112 113 14 115 E After the diffuser selection and the specification of the required exhaust flow, th Hucts connecting the centrifugal fan is designed using a duct sizer program. Addition d loss through the duct is considered to be about 1 Pa/m or 0.12 inch Wc/100 ft[10] w is then calculated using this program, as depicted in Figure 3-6 below. Exit DesignTools DuctSizer... Print Clear Units About 20°C Air STP X Fluid density Fluid viscosity Specific Heat Energy factor 1.2014 kg/m² 0.0643 kg/m-h 1.0048 kJ/kg*C 1.21 W/C-L/s Flow rate 900 L/s Head loss Pa/m Velocity 7.355 m/s Equivalent 573.5 mm diameter Flow Area Duct size Equivalent Diameter Fluid velocity Reynolds Number Friction factor 283,930 500 mm X 550 mm 573.1 mm 0.2580 m² 7.364 m/s 0.01753 Velocity Pressure Head Loss 32.5862 Pa 0.998 Pa/m Aduct = Apipe = π X² (3-6) Where Re: Reynold Number V: Velocity 771 Aduct Apipe Area of duct and pipe m² deqivelent pipe Equivalent diameter of pipe with same area of duct (m^2) Then the equivalent diameter is 0.59 m Then the Reynold number is 435000, this show that the flow is turbulent then using the moody chart. And the relative pipe equivalent roughness is about 0.05[12]. Then refer to the moody chart as shown in Figure 3-9[13]. Moody Diagram
Elements Of Electromagnetics
7th Edition
ISBN:9780190698614
Author:Sadiku, Matthew N. O.
Publisher:Sadiku, Matthew N. O.
ChapterMA: Math Assessment
Section: Chapter Questions
Problem 1.1MA
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I want the method to calculate the Reynolds number, where did this number 435,000 come from(Marked in red) ?
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