GATE3
Mechanical
- Jan 22, 2011
- 3
BATCH HEATER
Hi, everybody
I am try to size a plate heat exchanger for a Batch heater. The problem is that I stack to find the final temperatures.
Note: I found a software that calculated the temperature but I don’t understand how.
BATCH DATA
Batch Content=1000 Kg
Heating Milk From tinitial=4DegCtfinal=94DegC In 30min
Specific Heat Of Milk Cpc=3950 J/KgK @49 DegC
Density of Milk ρ=1013 Kg/m3 @49 DegC
Milk Circulated via a pump through the PHEX and back
to the tank with a flow rate mc=2.78 kg/s
Heating Medium DATA
Hot Water @ T1=97DegC
Specific Heat Of Hot Water Cp=4220J/KgK @ 97 DegC
Density of Hot Water ρ=960Kg/m3@ 97 DegC
Hot Water flow rate mh=4 kg/s
Solution
Heat Duty Qduty=MC*ΔT/ Heating time
Qduty=(1000*3950*(94-4)/(30*60))/1000=197.5Kw
Qduty=mh*Cph*(T1-T2)=>T2=T1-Q/mh*Cph
T2=97-((197.5*1000)/(4*4220))=85.29DegC
T2=85.29DegC
Qduty=m *Cpc*(t2-t1)
(t2-t1)=Q/m*Cpc=(197.5*1000)/(2.78*3950)
(t2-t1)=ΔT=17.98DegC
I try many solutions but I stack again and again and as i realized (I’AM NOT SURE) that the program include efficiency and from the Equation n=Qduty/Qmax calculated the Qmax .
Known The Qmax and from the usual equation calculated t1=T1-(Qmax/mc*Cpc)=70.79DegC and with combination of ΔT=17.98DegC=t2-t1 found the t2=17.98DegC+70.79=88.77DegC but again I don’t understand how calculated the efficiency in order to found the Qmax. Or how to find the Qmax to find the efficiency.
I try to calculated the Qmax with Qmax=mc*Cpc*(T1-t1) but is to high.
Software Results
n, efficiency=68%
Product inlet Temp=70.79 DegC
Product Outlet Temp=88.77 DegC
Please Advice how can I calculated the final temperatures .
Note: Area And Overall Heat Transfer Of PHEX are Unknown.
Hi, everybody
I am try to size a plate heat exchanger for a Batch heater. The problem is that I stack to find the final temperatures.
Note: I found a software that calculated the temperature but I don’t understand how.
BATCH DATA
Batch Content=1000 Kg
Heating Milk From tinitial=4DegCtfinal=94DegC In 30min
Specific Heat Of Milk Cpc=3950 J/KgK @49 DegC
Density of Milk ρ=1013 Kg/m3 @49 DegC
Milk Circulated via a pump through the PHEX and back
to the tank with a flow rate mc=2.78 kg/s
Heating Medium DATA
Hot Water @ T1=97DegC
Specific Heat Of Hot Water Cp=4220J/KgK @ 97 DegC
Density of Hot Water ρ=960Kg/m3@ 97 DegC
Hot Water flow rate mh=4 kg/s
Solution
Heat Duty Qduty=MC*ΔT/ Heating time
Qduty=(1000*3950*(94-4)/(30*60))/1000=197.5Kw
Qduty=mh*Cph*(T1-T2)=>T2=T1-Q/mh*Cph
T2=97-((197.5*1000)/(4*4220))=85.29DegC
T2=85.29DegC
Qduty=m *Cpc*(t2-t1)
(t2-t1)=Q/m*Cpc=(197.5*1000)/(2.78*3950)
(t2-t1)=ΔT=17.98DegC
I try many solutions but I stack again and again and as i realized (I’AM NOT SURE) that the program include efficiency and from the Equation n=Qduty/Qmax calculated the Qmax .
Known The Qmax and from the usual equation calculated t1=T1-(Qmax/mc*Cpc)=70.79DegC and with combination of ΔT=17.98DegC=t2-t1 found the t2=17.98DegC+70.79=88.77DegC but again I don’t understand how calculated the efficiency in order to found the Qmax. Or how to find the Qmax to find the efficiency.
I try to calculated the Qmax with Qmax=mc*Cpc*(T1-t1) but is to high.
Software Results
n, efficiency=68%
Product inlet Temp=70.79 DegC
Product Outlet Temp=88.77 DegC
Please Advice how can I calculated the final temperatures .
Note: Area And Overall Heat Transfer Of PHEX are Unknown.