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8/3/2019 Evaporator and Its Types
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Evaporator and its types
Awais Ahmad 41
Irfan Shafiq 09
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Evaporator
It is a equipment that is used to turn the liquid in anychemical or substance to gaseous state.
The basic example is Air conditioning
in this phenomena or process evaporator consist ofa liquid that takes heat of air and convert itself into
gaseous form, allowing cold air to circulate.
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Uses
Food and drink industry ( transportation of icecream)
Pharmaceutical industries(removes excess moisture
which makes a more easily handled product andimproves product stability).
As a heat exchanger in industry
Sugar industry
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Working of evaporator
The solution containing the desired product is fedinto the evaporator and passes a heat source.
The applied heat converts the water in the solutioninto vapor.
The vapor is removed from the rest of the solutionand is condensed while the now concentratedsolution is either fed into a second evaporator or isremoved. The evaporator as a machine generally
consists of four sections. The heating section consists of parallel tubes but
others have plates or coils.
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Working of evaporator
The concentrating and separating section removesthe vapor being produced from the solution.
The condenser condenses the separated vapor, thenthe vacuum or pump provides pressure to increase
circulation.
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Types of evaporators
Natural circulation evaporator Natural circulation evaporators are based on the
natural circulation of the product caused by thedensity differences that arise from heating.
After the water begins to boil, bubbles will rise andcause circulation, facilitating the separation of theliquid and the vapor.
The amount of evaporation that takes place depends
on the temperature difference between the steamand the solution.
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Natural circulation evaporator
If tubes are not well immersed then circulation will becompromised.
So forced circulation is introduced by a pump due to
which good circulation is achieved at hightemperature.
But steam consumption is increased.
Circulation evaporators can operate over a widerange of concentration and thick liquor in single unit.
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Falling film evaporator
This type of evaporator is generally made of longtubes (48 meters in length) which are surrounded
by steam jackets.
The uniform distribution of the solution is important
when using this type of evaporator. The solution enters and gains velocity as it flows
downward. This gain in velocity is attributed to thevapor being evolved against the heating medium,
which flows downward as well. (video)
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Climbing film evaporator
These vertical evaporator are with upward flow ofliquid
Steam in the shell and liquid in pipe.
Separator to remove entrained liquid from the vapor
Inlets for steam and liquid are provided
Outlets are provided for vapor and non condensablegases
They are 25-50mm in dia
3-10m long
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Climbing film evaporator
Feed is entered into the system Concentrated liquor is withdrawn from bottom of
heater
The mixture of liquid and vapor from top of the tube
flows into separator, where its velocity is greatlyreduced
This aids in eliminating liquid droplets
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Multiple-effect evaporators
Unlike single-stage evaporators, theseevaporators can be made of up to sevenevaporator stages or effects.
The energy consumption for single-effect
evaporators is very high and makes up most ofthe cost for an evaporation system.
Putting together evaporators saves heat andthus requires less energy. Adding one evaporator
to the original decreases the energyconsumption to 50% of the original amount.
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Adding another effect reduces it to 33% and soon. A heat saving % equation can be used toestimate how much one will save by adding acertain amount of effects
The number of effects in a multiple-effectevaporator is usually restricted to seven becauseafter that, the equipment cost starts catching upto the money saved from the energy requirement
drop.
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types of feeding
There are two types of feeding that can be usedwhen dealing with multiple-effect evaporators.
Forward feeding Backward feeding.
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Forward feeding takes place when the productenters the system through the first effect, whichis at the highest temperature.
The product is then partially concentrated as
some of the water is transformed into vapor andcarried away. It is then fed into the second effectwhich is a little lower in temperature.
The second effect uses the heated vapor createdin the first stage as its heating source (hence thesaving in energy expenditure).
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The combination of lower temperatures andhigher viscosities in subsequent effects providesgood conditions for treating heat-sensitiveproducts like enzymes and proteins.
In using this system, an increase in the heatingsurface area of subsequent effects is required.
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backward feeding.
In this process, the dilute products is fed into the lasteffect with has the lowest temperature and is
transferred from effect to effect with the temperatureincreasing.
The final concentrate is collected in the hottest effectwhich provides an advantage in that the product ishighly viscous in the last stages so the heat transferis considerably better...
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FORCED-CIRCULATION EVAPORATOR
Natural circulation evaporators are economical,but they cannot be used in quite a few situation:
If the solution is viscous, the circulation velocityremains low which greatly reduces the heat
transfer coefficient If the solution contains suspended solid particles
(it may occur in a crystallizing evaporator) or ifthere is a possibility of salting out of a solute,settling of particles is very likely to occurbecause of too low a velocity attainable in anatural circulation unit.
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While handling the solution of aheat sensitive material, the time of contact of thesolution with the hot surface of a tube should below. This is possible only by maintaining a high
velocity of the liquid in the tubes which is notpossible in a natural circulation evaporator. Thevelocity through the tubes is be enhanced in aforced circulation unit by employing a pump.
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