Calculate Vaporisation rate (Boil-up Rate) from a batch reactor

[@saikiranampolu9652]

Ajay sir i am very happy that finally you started KZbin we are waiting eagerly

[@dhruvkumarmangukiya3628]

Sir u r doing grate work please add more videos

[@rahulthakor14]

Can you pls explain ANFD complete design with drying rate calculation

[@Niju82]

Sir, What if we use a band heater instead of steam jacket. What will be the LMTD.

[@pappalasunilkumar4805]

sir,why we are consider mλ only for heat demand .why we are not considered M*Cp*deltT Or (M*Cp*deltT+ mλ)

[@gauravjoshi4832]

Hllo Sir if I'm using ceramic band heater for reactor heating for boiling off water what temp will be considered for lmtd calculation

[@venkateshkademane2098]

sir,we wish u heathy wealth

[@pharmaengineering]

Thanks for your wishes mate

[@ramtilakpasupula3352]

Nice 👌

[@silambarasan.s7521]

Sir if lmtd increase y overall heat transfer coefficient will reduce

[@venkateshkademane2098]

do you have any online or paid membership programme for answering our questions?

[@mabasith3877]

Please add more topics

[@dhruvkumarmangukiya3628]

Ty so much

[@SAHILPATIL-se4fb]

In 2nd case what if we use hot water what would be the u value and how u relate lmtd in that case?

[@venkateshkademane2098]

sir,how if heating is double limpet and heating by thermic fluid?

[@ramtilakpasupula3352]

Please explain column design. No theoretical plates and dia of column q line

[@dhruvkumarmangukiya3628]

In atmospheric distillation If i consider toulene as liquid phase having inside temprature 30℃ then what is my LMTD ? OR WHAT IS my demand is it m Cp ∆T + mL ?

[@pharmaengineering]

Hii Dhruv, Toluene boils at 110 C during normal distillation i.e., at 760 mmHg, So for estimating LMTD you can take 30C as initial temperature and 110 C as final temperature and the jacket utility temperature remains the same (if it's steam)

[@bhagathk822]

Required more videos sir

[@pharmaengineering]

We are on it

[@rupaadireddy7708]

How to calculate boilup for distilation col

[@pharmaengineering]

Calculate the boil-up from the kettle or reboiler which could give you an idea about the boil-up that enters the column and then estimate the pressure drop across column, that would give you the vapor rate at column exit.