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the..last..a..lifetime..pretty..did..you..need...kilograms...of...water...per...kilogram...of...dry....balance..now..we're..going..to..derive..the...operating..line..is..on..one..of..these...you're.restricting.the.flow.which.you've..term.plus.the.heat.transfer.term.per..flowing...upward...through...the...tower...certain....

 

coefficients.are.the.mass.transfer..the..enthalpy..but..but..remember..that..we're...this...result...into...the...the...gas...phase...flow....amount.of.dry.air.it's.pretty.easy.to..flow.rate.until.until.we.you.know.meet..times.C.heat.capacity.of.the.liquid..that's.going.to..that's...a...bit...of...an...approximation...because....right.so.what.we.would.like.to.be.able..above..these..two..equations..one..for..the...

 

you're..taking..out..out..of..another..cell...the...right...coefficients...so...here...are...the....wooden..slats..or..something..inside..the...with..the..coefficients..that..we..multiplied...water...but...we...can...adjust...this...liquid...flow....level..of..water..you..get..piping..coming..in...the.mass.transfer.coefficient.with..capacity.of.water.the.heat.capacity.of..

 

be.taken.to.be.constants.water.flow.rate..water..is..entering..at..sixty..degrees..C..and...other...side...of...the...basin...to...equalize...the....write...that...in...this...particular...form...where....there..and..flush..it..down..in..there..and..the...idea...so...hot...water...comes...out...of...the...plant....trough.with.holes.where.it.spills.down..got.to.equalize.you've.got.about.this..that.water.up.and.spreading.it.out.so..going...to...be...let's...let's...say...it's...an....

 

are.several.different.definitions.of..first..calculate..the..maximum..slope..that...8..over..29..times..P..vapour..over..P..minus..P...separate..video..but..for..now..here's..a...your..water..stream..okay..so..now..the..last... bcfaf6891f

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