material balance for multi-unit operations
TRANSCRIPT
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Material Balance for
Multi-Unit Operations
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Process Flow sheet Flow Chart)
1. Process Information: key properties data, market conditions, techniinformation, etc., are collected.
2. Input /Output Diagram: All major inputs and outputs streams and thstoichiometric balances are illustrated, according to the potential chemipathways.
3. Functions Diagram: All the major functions of the process and materiflow to and from those functions are specified. The functions include reacti
boxes, separation boxes, finishing boxes, etc.
4. Operations Diagram: Detail technologies used such as types of reactoperating conditions, etc. are specified.
5. Process Flow sheet: Details for each function are described, ready to use.
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Process Flowsheet Development
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Function Diagram
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Operation Diagram
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Process Flow sheet
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MB for Multiple Units Process
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Example on MB for Multi-units Process
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Recycle System
The stream containing the recycled material is kno
as a recycle stream.
Because of relatively high cost of industrial feerecycle of unused reactants/feed is a commpractice.
Recovery of catalyst, circulation of working fluidilution of process streams, control of procvariables, etc., are all reasons for applicationsrecycle system.
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Recycle with Chemical Reaction
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Bypass and Purging
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Bypassing wastewater to waste Lagoon
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Limiting reactant
In practice a reactant may be used in excess of thestoichiometric quantity for various reasons. In this casthe other reactant is limiting i.e. it will limit the yield oproduct(s)
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Excess reactant
A reactant is in excess if it is present in a quantity
greater than its stoichiometric proportion.% excess = [(moles supplied stoichiometric
moles)/stoichiometric moles] x 100
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Conversion
Fractional conversion = amount reactant
consumed/amount reactant supplied % conversion = fractional conversion x 100
Note: conversion may apply to single pass reactorconversion or overall process conversion
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Yield
Yield = (moles product/moles limiting reactant
supplied) x s.f. x 100
Where s.f. is the stoichiometric factor = stoichiometrimoles reactant required per mole product
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Multiple Reactions
There are four basic type of multiple reactions: series, parallel, complex, and indepe
Parallel reactions competing reaction)
A
k1
k2 C
B
Series reactions consecutive reaction)
Ak1 k2
CB
The reactant is consumed by two different reaction pathways to form different pro
The reactant forms an intermediate product, where reacts further to form another
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Complex reactions
ECA
DCBA
OHHCCHOCHHC
HCHOCHOHHC
OHHCOHHC
264342
2352
24252
Involving a combination of both series and parallel reactions
Independent reactions
FED
CBA
42143188
6324123215
HCHCHC
HCHCHC
Occurring at the same time but neither the products nor reactants react with thems
or one another.
formation of butadiene from ethanol
cracking of crude oil to form gasoline
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Selectivity tells us how one product is favored over another when we ha
multiple reactions. We can quantify the formation of Desired product (D
with respect to Undesired product (U) by defining the selectivity and yie
of the system.
The instantaneous selectivity of D with respective to U is the ratio of the rate
formation of D to the rate of formation of U.
UDS
/
~
Overall selectivity
Selectivity
/ =
=
=
=
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Selectivity
Selectivity = (moles product/moles reactant converted) x s.f. x
OR
Selectivity = moles desired product/moles byproduct
Where s.f. is the stoichiometric factor = stoichiometric moles reactant re
mole product
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Selectivity and YieldInstantaneous Overall
Selectivity:
Yield:
Example: desired product ,
undesired product ,
To keep the selectivity of the desired products high withrespect to the undesired products, carry out the reactioat high concentration of A and low concentration of B. Ahigh selectivity can easily be achieved in a semibatchreactor where B is fed slowly compared to A.
rD k
1CA
2CB
rU k
2CACB
2