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REGENERATIVE AIR COOLER (UNDER THE GUIDENCE OF-PROFF. H.P GUPTA) SUBMITTED BY: YAMIKA PATEL SUMIT SINGH PREM KUMAR PARUL DIXIT

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Page 1: regenerative air cooler

REGENERATIVE AIR COOLER(UNDER THE GUIDENCE OF-PROFF. H.P

GUPTA)

SUBMITTED BY:YAMIKA PATELSUMIT SINGHPREM KUMARPARUL DIXIT

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MONTH JUNE-AUG.2013

SEPT-NOV 2013

JANAURY 2014

FEB 2014

MARCH 2014

APRIL2014

ACTIVITY

1st

Data search and study

ACTIVITY2nd

Selection of materials & design layout

ACTIVITY3rd

Design & Assembling of parts

ACTIVITY4th

Assembling continued…

ACTIVITY5th

Testing of system

ACTIVITY6th

Preparation of report

PROJECT SCHEDULE FORMAT

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REGENERATIVE AIR COOLER

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Main Components Of The Regenerative Air Cooler Are:1. Blower2. Blower3. Motor4. Duct5. Water Pad 6. Heat Exchanger7. Water Pad 8. Water Tank9. Water Pump

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MATERIAL SELECTION:

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HEAT EXCHANGER

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FABRICATION OF THE HEAT EXCHANGER

Obtain MS rods for studs

Order GI sheets for

heat exchanger

Obtain insulation

for HE

Purchase adhesive

Manufacture 5 studs

Cut the sheets and drill holes

Cut the insulation into

proper size

Assemble the heat exchanger

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TOP VIEW OF REGENERATIVE AIR COOLER

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RIGHT HAND SIDE OF REGENERATIVE AIR COOLER

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LEFT HAND SIDE VIEW OF REGENERATIVE AIR COOLER

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FRONT VIEW OF REGENERATIVE AIR COOLER

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BACK SIDE VIEW OF REGENERATIVE AIR COOLER

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MOTOR PERFORMANCE CHARECTORISTICS:POWER=95 WBLADE VELOCITY=

ПDN/60=П×.18×1300/60=12.25 m/secAC SUPPLY=230 VCURRENT=.4 ampFREQUENCY=50 Hz

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 CALCULATION FOR BLOWER 2 Entering Air velocity, Vin= 6.62 m/sec Inlet area, Ain=П/4(.16^2+.12^2) Ain=.0314 m2

 Q = Ain×Vin By applying Bernoulli’s equation Q=const Q= .208 m3/sec=12.4 m3/min Outlet area, out=.13×.13= .0169 m2 Exit Air velocity, Vout=Q/A=.208/.0169=12.3 m/sec

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CALCULATION FOR DUCT 

Inlet area, Ain=.13×.13= .0169 m2 Entering Air velocity, Vin=Q/A=.208/.0169=12.3 m/sec By applying Bernoulli’s equation Q=constant Q= .208 m3/sec=12.4 m3/min Outlet area, Aout=.205×.13=.02665 m2

 Exit Air velocity, Vout =Q/A=.208/.02665 = 7.8 m/sec

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CALCULATION FOR WATER PAD DBT1=38°C WBT1=21°C RH1=20% H1=60.25 KJ/Kg of air Spe. Vol, Vs1=.89 m3/Kg DBT2=36.5°C WBT2=27°C RH2=50%

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H2=85 KJ/Kg of air SPE. VOL, Vs2=.91 m3/Kg Mass of Air Supplied ma=Q/Vs=12.8/.91=14.06Kg/min Ma=.234 Kg/sec 

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CALCULATION FOR HEAT EXCHANGER  TH1=38°C TH2=? TC1=36.5°C TC2=? Capacity rate of air, (C) min=ma

U=

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H=40, l=.0005, k=52

U= =19.996

A=16(l × b) =16(.23×.23) =.8464  UA=19.996×.8464=16.92

N=70.58

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ε=.92 TH1=38°C TH2=? TC1=36.5°C TC2=?

ε =

ε =

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(38-36.5) ε =38- TH2   (38-36.5) ε =38- TH2  1.5× .92= 38- TH2  1.38 = 38- TH2   TH2 =36.62 °C   1.38 = TC2-36.5   TC2=37.88°C Temp. Of atm air, TH1=38°C Temp. Of treated atm air, TH2=36.62°C Temp. Of cooled air from water pad, TC1=36.5°C Temp. Of exit air, TC2=37.88°C

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1.Refrigeration and air conditioning………………..Khurmi and Gupta2. Refrigeration and air conditioning………………..Arora and Domkundwar 3. Refrigeration and air conditioning………………..C.P. Arora 4. Refrigeration and air conditioning………………..P.L. Balany

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