Triple-Effect Evaporator: Introduction

preview_player
Показать описание
Check out our Separations and Mass Transfer playlist at
Рекомендации по теме
Комментарии
Автор

If boiling point in second effect is lower then first effect, then why do we use steam in second effect, bcoz feed in second effect is alredy at higher temp then boiling point i.e. t1>t2

zenithpatel
Автор

what's about "mix feed" and "parallel feed"
i wanna know those equation for calculation, please

pploy-yydt
Автор

Does this only work for processes where you’re concentrating a solid, and would expect 0% product to be coming through in the vapor stream?

michaelmolter
Автор

I believe q can’t be same at all areas since there is always some losses as stem gets does not compeltely condensed.

We must take that too in calculation

farahsa
Автор

Your video on backwards flow dilute solution is more realistic to real life use.
Counter flow design is always the goal with heat exchanging.

curtis
Автор

hello sir
want to ask you about how you find steam flow rate to 1st effect by energy balance using steam table

JINAl
Автор

How can l calculate the changer when we have anumbers not just the mechanisum😧💔

engzahraa
Автор

I'm looking for the material about Falling Film Evaporator. Anyone have?

tuanphamquoc
Автор

How to find optimum number of effects any formula

anukritisingh
Автор

Is there a reason why saturated steam is used instead of superheated steam to evaporate the liquid solution? 

IRuvJndL
Автор

OUR invention avoids the extra-energy needed for water boiling and the safety problems associated with the old systems

fahmylina
Автор

How it's possible that liquid 2 and vapor 2 be cooler than V1 and T1? Who received that energy? I'd think that T2 would be equal to T1 because you are "heating" a liquid with a Vapor, both at the same temperature. I mean, temperature vapor inlet = temperature liquid inlet and the result is temperature vapor outlet = temperature liquid outlet, T1>T2, WTF?

davidvalero