I have done the second part of the question with a plant feed of 0.45L/h. I assumed they meant the fertiliser feed, am I right?
I am just stuck on the first part, determine the concentration at the outlet using a component material balance around the fertiliser feed. I don't know if the original question data will be needed. I put a picture of the original question too.
thanks
I think you are confused about calculating the concentration in mole/volume or may be not.Hope you might be knowing that density is also a representation of concentration ,so we use specific term for both like Molar density for concentration while mass density for simple density kg/volume and thus both are interrelated.
Now coming to the question,for solving it one must know the fundamentals i.e. density or concentration is an intesive property.So if we add certain mass or moles of any solute to the water definitely it will change the concentration because the number of molesor mass has been increased now and hence the concentration is changed.But when we will take out some volume from a particular solution of solute,then also the concentration of solute will not change in the solution or the volume which is taken out because the mass or moles of solute has been distributed through out the solution uniformly and we represent concentration per unit volume so that remains unchanged in that case.
So in this problem once the mass of fertiliser has been added to the water, it will be distributed uniformly throught and hence the concentration of fertiliser remains the same after mixing and is equal to concentration in any row.Hence finding out the concentration at outlet A itself means finding out the concentration before the water is distributed to any row of tomato.
I have done the second part of the question with a plant feed of 0.45L/h. I...
Please help with this question regarding the design of a
forward-feed double effect evaporator. Will really appreciate
it.
(I've edited by typing out the questions, so the question is now
clearer.)
Please provide a proposal for the design of a forward-feed
double effect evaporator (Figure 1), for which operating conditions
are given below.
Figure 1: Schematic diagram of forward-feed
double effect evaporator
Configuration: Forward-feed double effect evaporator
Number of effects: 2
Feed:
Feed material: Aqueous high molecular weight solution
Flow...
Please help with this question regarding the design of a
forward-feed double effect evaporator. Will really appreciate
it.
(I've edited by typing out the questions, so the question is now
clearer.)
Please provide a proposal for the design of a forward-feed
double effect evaporator (Figure 1), for which operating conditions
are given below.
Figure 1: Schematic diagram of forward-feed
double effect evaporator
Configuration: Forward-feed double effect evaporator
Number of effects: 2
Feed:
Feed material: Aqueous high molecular weight solution
Flow...
I am having trouble in understanding this question. The second
photo is part b of the question. Any help would be
appreciated!
Four Hfr strains of E.ole known to transfer thier genetic material during conjugation in different sequences. Given the time of entry of the markers into the F-recipient, construct a genetic map which includes all of these markers, starting with arg as number 1 and phe as number 11.(Not all markers were assayed in each strain, remember the E.coli...
10. Write a one-page summary of the attached paper? INTRODUCTION Many problems can develop in activated sludge operation that adversely affect effluent quality with origins in the engineering, hydraulic and microbiological components of the process. The real "heart" of the activated sludge system is the development and maintenance of a mixed microbial culture (activated sludge) that treats wastewater and which can be managed. One definition of a wastewater treatment plant operator is a "bug farmer", one who controls the aeration...