Hi
I'm currently looking into optimising the cooling system on one of our process plants and I have a question I hope someone can help me with.
The cooling system is a tempered loop (i.e. warm water from process is recycled into cold water into process to prevent freezing of materials in cool ambient conditions) and has a dedicated mechanical draft cooling tower (3.5MW) to perform the cooling. Due to significant plant uprates in the past the tower is underspecified for the duty it is seeing and there is scope to change the operation of the tower to try to cope with this.
The tower is designed for 500m3/hr with inlet temp to the tower of 25.1'C and return 19.0'C in summer and 16'C in winter, with a wet bulb of 17'C.
What I basically want to know is if I increase the outlet water temp of the tower (and hence the inlet temp to the tower) to say 23'C will I see an increase in the DT across the tower and if so how much?
There is data missing for the tower such as air-flow through the tower so a 'first principals' calc is no use. What I really need is a simple correlation of how changing only tower water outlet temp affects deltaT over tower and hence duty.
Any help on this would be excellent.
Cheers
Shaun.
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Cooling Tower Operation
Started by Guest_TwistedEcho_*, Feb 28 2006 09:02 AM
1 reply to this topic
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#1
Guest_TwistedEcho_*
Posted 28 February 2006 - 09:02 AM
#2
Posted 06 March 2006 - 07:09 AM
Hi,
Present "Approach"(temperature difference between the cold water and dew point) is 19-17 or 2 ℃ and "Range"(temperature differenct between hot water and cold water) is 25.1-19 or 6.1 ℃ in summmer.
Now you are going to increase the COLD cooling water temperature(T1) from 19 to 23 ℃. Then the HOT cooling water temparature(T2) shall be 23+6.1= 29.1℃ assuming the cooling duty in the "tempered water system" remain unchanged. The "Approach" will become 23-17= 6℃.
The governing equation for the cooling tower calculation was given by Merkel expressed as:
K*a*V/L=Integral(T1 to T2)dT/(hs-hw) ------(1)
where, K*a*V/L= characteristic factor of cooling tower
K=Mass-transfer coefficient, a=contact area per tower volume, V=active cooling volume per plan area, L=water rate per plan area, T1=COLD water temperature, T2=HOT water temperature, hs=enthalpy of saturated air at the same local temperaure T of water. hw=enthalpy of hot air/moisture mixture in equlibrium with water at local temperature T.
Refer to Perry's CEH 6th ed. pp12-13~14 for details and the sketch attacked.
The term (hs-hw) makes a kind of "driving force" in the cooling tower. As the "Approach" increases, the driving force (hs-hw) increases, but the value K*a*L/G will not be changed. The idea that the factor will not change could be employed for the estimation of variables such as Hot Air Temperature and L/G ratio.
You must first check the present hot air temperature which is not given in your question. The point "D" shall be determined from the present "Hot Air Temperature". Calculate the area of the shape "A-B-C-D" in the attached drawing, then move C to C", A to A", but the "Range" is the still the same 6.1℃. Find A"-B"-C"-D" to get the same area as A-B-C-D.
L/G Ratio can be greatly increased by decreasing G(Air Rate). L/G ratio is the slope of the Operating Line.
It seems to be a quite complicate job.
Present "Approach"(temperature difference between the cold water and dew point) is 19-17 or 2 ℃ and "Range"(temperature differenct between hot water and cold water) is 25.1-19 or 6.1 ℃ in summmer.
Now you are going to increase the COLD cooling water temperature(T1) from 19 to 23 ℃. Then the HOT cooling water temparature(T2) shall be 23+6.1= 29.1℃ assuming the cooling duty in the "tempered water system" remain unchanged. The "Approach" will become 23-17= 6℃.
The governing equation for the cooling tower calculation was given by Merkel expressed as:
K*a*V/L=Integral(T1 to T2)dT/(hs-hw) ------(1)
where, K*a*V/L= characteristic factor of cooling tower
K=Mass-transfer coefficient, a=contact area per tower volume, V=active cooling volume per plan area, L=water rate per plan area, T1=COLD water temperature, T2=HOT water temperature, hs=enthalpy of saturated air at the same local temperaure T of water. hw=enthalpy of hot air/moisture mixture in equlibrium with water at local temperature T.
Refer to Perry's CEH 6th ed. pp12-13~14 for details and the sketch attacked.
The term (hs-hw) makes a kind of "driving force" in the cooling tower. As the "Approach" increases, the driving force (hs-hw) increases, but the value K*a*L/G will not be changed. The idea that the factor will not change could be employed for the estimation of variables such as Hot Air Temperature and L/G ratio.
You must first check the present hot air temperature which is not given in your question. The point "D" shall be determined from the present "Hot Air Temperature". Calculate the area of the shape "A-B-C-D" in the attached drawing, then move C to C", A to A", but the "Range" is the still the same 6.1℃. Find A"-B"-C"-D" to get the same area as A-B-C-D.
L/G Ratio can be greatly increased by decreasing G(Air Rate). L/G ratio is the slope of the Operating Line.
It seems to be a quite complicate job.
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