This document discusses reactor design for multiple reactions. It describes types of reactors including batch, semi-batch, plug flow, and continuous stirred-tank reactors (CSTRs). It also covers parameters for reactor design like volume, flow rate, concentrations, kinetics, temperature, and pressure. The document discusses plug flow versus CSTR design and designing for parallel, series, and complex reaction networks. It provides methods for maximizing desired products in multiple reaction systems, including adjusting conditions, choosing proper contacting patterns and reactors, and optimizing space-time or residence time. The document also presents equations for modeling multiple reactions occurring in a CSTR.
This slide completely describes you about the stuff include in it and also everything about chemical engineering. Fluid Mechanics. Thermodynamics. Mass Transfer Chemical Engineering. Energy Engineering, Mass Transfer 2, Heat Transfer,
Difference between batch,mixed flow & plug-flow reactorUsman Shah
This slide completely describes you about the stuff include in it and also everything about chemical engineering. Fluid Mechanics. Thermodynamics. Mass Transfer Chemical Engineering. Energy Engineering, Mass Transfer 2, Heat Transfer,
This slide completely describes you about the stuff include in it and also everything about chemical engineering. Fluid Mechanics. Thermodynamics. Mass Transfer Chemical Engineering. Energy Engineering, Mass Transfer 2, Heat Transfer,
Difference between batch,mixed flow & plug-flow reactorUsman Shah
This slide completely describes you about the stuff include in it and also everything about chemical engineering. Fluid Mechanics. Thermodynamics. Mass Transfer Chemical Engineering. Energy Engineering, Mass Transfer 2, Heat Transfer,
This Presentation gives an overview about the multiple effect evaporators. The intention is also focused on designing principles of Single and Multiple Effect Evaporators
These slides may be used for a part of Advanced level course in Chemical Reaction Engineering. I taught this course to Masters level students covering 1.5 credit hours.
continuous distillation with rectification process and its working principal with diagram and also its use in industrial applications.
design and operations explained.
Introduction to Chemical Reactors and Chemical Reaction EngineeringMuhammad Sajid Liaqat
The presentation covers the following topics developing a conceptual approach to Chemical Reaction Engg.
The rate equation
Reactor Systems
Types of reactors
Reactor design parameter
Fixed bed reactors
Fluidized bed reactors
Stirred tank reactors
Slurry loop reactors
Bubble columns
Mole balances for multiple reactions
Shell and Tube Heat Exchanger in heat TransferUsman Shah
This slide will explain you the chemical engineering terms .Al about the basics of this slide are explain in it. The basics of fluid mechanics, heat transfer, chemical engineering thermodynamics, fluid motions, newtonian fluids, are explain in this process.
Single and multiple effective evaporator (mee)Sumer Pankaj
A multiple-effect evaporator, as defined in chemical engineering, is an apparatus for efficiently using the heat from steam to evaporate water.[1] In a multiple-effect evaporator, water is boiled in a sequence of vessels, each held at a lower pressure than the last. Because the boiling temperature of water decreases as pressure decreases, the vapor boiled off in one vessel can be used to heat the next, and only the first vessel (at the highest pressure) requires an external source of heat. While in theory, evaporators may be built with an arbitrarily large number of stages, evaporators with more than four stages are rarely practical except in systems where the liquor is the desired product such as in chemical recovery systems where up to seven effects are used.
The multiple-effect evaporator was invented by an African-American inventor and engineer Norbert Rillieux. Although he may have designed the apparatus during the 1820s and constructed a prototype in 1834, he did not build the first industrially practical evaporator until 1845. Originally designed for concentrating sugar in sugar cane juice, it has since become widely used in all industrial applications where large volumes of water must be evaporated, such as salt production and water desalination.
Multiple effect evaporation commonly uses sensible heat in the condensate to preheat liquor to be flashed. In practice the design liquid flow paths can be somewhat complicated in order to extract the most recoverable heat and to obtain the highest evaporation rates from the equipment.
Multiple-effect evaporation plants in sugar beet factories have up to eight effects. Six effect evaporators are common in the recovery of black liquor in the kraft process for making wood pulp.
Reactores batch quimicos para la industria en campos de ingenieria.pptBastheanFranciscoPin
eactores Discontinuos o Batch: Son recipientes con agitación en el cual se cargan los reactivos y se descargan una vez la reacción ha finalizado. Se caracterizan por no trabajar en condiciones estacionarias. Tanto la temperatura como las composiciones varían constantemente.
This Presentation gives an overview about the multiple effect evaporators. The intention is also focused on designing principles of Single and Multiple Effect Evaporators
These slides may be used for a part of Advanced level course in Chemical Reaction Engineering. I taught this course to Masters level students covering 1.5 credit hours.
continuous distillation with rectification process and its working principal with diagram and also its use in industrial applications.
design and operations explained.
Introduction to Chemical Reactors and Chemical Reaction EngineeringMuhammad Sajid Liaqat
The presentation covers the following topics developing a conceptual approach to Chemical Reaction Engg.
The rate equation
Reactor Systems
Types of reactors
Reactor design parameter
Fixed bed reactors
Fluidized bed reactors
Stirred tank reactors
Slurry loop reactors
Bubble columns
Mole balances for multiple reactions
Shell and Tube Heat Exchanger in heat TransferUsman Shah
This slide will explain you the chemical engineering terms .Al about the basics of this slide are explain in it. The basics of fluid mechanics, heat transfer, chemical engineering thermodynamics, fluid motions, newtonian fluids, are explain in this process.
Single and multiple effective evaporator (mee)Sumer Pankaj
A multiple-effect evaporator, as defined in chemical engineering, is an apparatus for efficiently using the heat from steam to evaporate water.[1] In a multiple-effect evaporator, water is boiled in a sequence of vessels, each held at a lower pressure than the last. Because the boiling temperature of water decreases as pressure decreases, the vapor boiled off in one vessel can be used to heat the next, and only the first vessel (at the highest pressure) requires an external source of heat. While in theory, evaporators may be built with an arbitrarily large number of stages, evaporators with more than four stages are rarely practical except in systems where the liquor is the desired product such as in chemical recovery systems where up to seven effects are used.
The multiple-effect evaporator was invented by an African-American inventor and engineer Norbert Rillieux. Although he may have designed the apparatus during the 1820s and constructed a prototype in 1834, he did not build the first industrially practical evaporator until 1845. Originally designed for concentrating sugar in sugar cane juice, it has since become widely used in all industrial applications where large volumes of water must be evaporated, such as salt production and water desalination.
Multiple effect evaporation commonly uses sensible heat in the condensate to preheat liquor to be flashed. In practice the design liquid flow paths can be somewhat complicated in order to extract the most recoverable heat and to obtain the highest evaporation rates from the equipment.
Multiple-effect evaporation plants in sugar beet factories have up to eight effects. Six effect evaporators are common in the recovery of black liquor in the kraft process for making wood pulp.
Reactores batch quimicos para la industria en campos de ingenieria.pptBastheanFranciscoPin
eactores Discontinuos o Batch: Son recipientes con agitación en el cual se cargan los reactivos y se descargan una vez la reacción ha finalizado. Se caracterizan por no trabajar en condiciones estacionarias. Tanto la temperatura como las composiciones varían constantemente.
Chemical reaction engineering is that engineering activity which is concerned with the exploitation of chemical reactions on commercial scale.
The areas of different fields of science like:
Oil Refining
Pharmaceuticals
Biotechnology
Chemical Industries
Sustainable Development
This slide completely describes you about the stuff include in it and also everything about chemical engineering. Fluid Mechanics. Thermodynamics. Mass Transfer Chemical Engineering. Energy Engineering, Mass Transfer 2, Heat Transfer,
In this Course we get two sections:
Section 1
Introduction and information on the existing reactors
Visual images of reactors
Importance of Reactor Design
Section 2
- The General Mole Balance Equation
- The concept of Generation
- The Accumulation term
- The Design Equations for a Batch Reactor
- The Design Equations for a Continuous Stirred Tank Reactor
- The Design Equations for a Plug Flow Reactor
- The Design Equations for a Packed Bed Reactor
By the end of this block you should be able to differentiate between batch reactors vs. continuous flow reactors.
You should be familiar with the General Mole Balance Equation and how to apply it to every reactor.
You should know or at least get to know the Mole Balance Equations or Design Equations of each reactor in the Course.
INTRODUCTION
COMPARISION BETWEEN FIXED BED VS FLUIDISED BED REACTOR
SELECTION CRITERIA FOR CATALYST REACTOR
DESIGN OF CATALYST REACTOR
DESIGN OF DEACTIVATION OF CATALYST
Macroeconomics- Movie Location
This will be used as part of your Personal Professional Portfolio once graded.
Objective:
Prepare a presentation or a paper using research, basic comparative analysis, data organization and application of economic information. You will make an informed assessment of an economic climate outside of the United States to accomplish an entertainment industry objective.
Introduction to AI for Nonprofits with Tapp NetworkTechSoup
Dive into the world of AI! Experts Jon Hill and Tareq Monaur will guide you through AI's role in enhancing nonprofit websites and basic marketing strategies, making it easy to understand and apply.
Honest Reviews of Tim Han LMA Course Program.pptxtimhan337
Personal development courses are widely available today, with each one promising life-changing outcomes. Tim Han’s Life Mastery Achievers (LMA) Course has drawn a lot of interest. In addition to offering my frank assessment of Success Insider’s LMA Course, this piece examines the course’s effects via a variety of Tim Han LMA course reviews and Success Insider comments.
Biological screening of herbal drugs: Introduction and Need for
Phyto-Pharmacological Screening, New Strategies for evaluating
Natural Products, In vitro evaluation techniques for Antioxidants, Antimicrobial and Anticancer drugs. In vivo evaluation techniques
for Anti-inflammatory, Antiulcer, Anticancer, Wound healing, Antidiabetic, Hepatoprotective, Cardio protective, Diuretics and
Antifertility, Toxicity studies as per OECD guidelines
Read| The latest issue of The Challenger is here! We are thrilled to announce that our school paper has qualified for the NATIONAL SCHOOLS PRESS CONFERENCE (NSPC) 2024. Thank you for your unwavering support and trust. Dive into the stories that made us stand out!
Instructions for Submissions thorugh G- Classroom.pptxJheel Barad
This presentation provides a briefing on how to upload submissions and documents in Google Classroom. It was prepared as part of an orientation for new Sainik School in-service teacher trainees. As a training officer, my goal is to ensure that you are comfortable and proficient with this essential tool for managing assignments and fostering student engagement.
Operation “Blue Star” is the only event in the history of Independent India where the state went into war with its own people. Even after about 40 years it is not clear if it was culmination of states anger over people of the region, a political game of power or start of dictatorial chapter in the democratic setup.
The people of Punjab felt alienated from main stream due to denial of their just demands during a long democratic struggle since independence. As it happen all over the word, it led to militant struggle with great loss of lives of military, police and civilian personnel. Killing of Indira Gandhi and massacre of innocent Sikhs in Delhi and other India cities was also associated with this movement.
Synthetic Fiber Construction in lab .pptxPavel ( NSTU)
Synthetic fiber production is a fascinating and complex field that blends chemistry, engineering, and environmental science. By understanding these aspects, students can gain a comprehensive view of synthetic fiber production, its impact on society and the environment, and the potential for future innovations. Synthetic fibers play a crucial role in modern society, impacting various aspects of daily life, industry, and the environment. ynthetic fibers are integral to modern life, offering a range of benefits from cost-effectiveness and versatility to innovative applications and performance characteristics. While they pose environmental challenges, ongoing research and development aim to create more sustainable and eco-friendly alternatives. Understanding the importance of synthetic fibers helps in appreciating their role in the economy, industry, and daily life, while also emphasizing the need for sustainable practices and innovation.
2024.06.01 Introducing a competency framework for languag learning materials ...Sandy Millin
http://sandymillin.wordpress.com/iateflwebinar2024
Published classroom materials form the basis of syllabuses, drive teacher professional development, and have a potentially huge influence on learners, teachers and education systems. All teachers also create their own materials, whether a few sentences on a blackboard, a highly-structured fully-realised online course, or anything in between. Despite this, the knowledge and skills needed to create effective language learning materials are rarely part of teacher training, and are mostly learnt by trial and error.
Knowledge and skills frameworks, generally called competency frameworks, for ELT teachers, trainers and managers have existed for a few years now. However, until I created one for my MA dissertation, there wasn’t one drawing together what we need to know and do to be able to effectively produce language learning materials.
This webinar will introduce you to my framework, highlighting the key competencies I identified from my research. It will also show how anybody involved in language teaching (any language, not just English!), teacher training, managing schools or developing language learning materials can benefit from using the framework.
2024.06.01 Introducing a competency framework for languag learning materials ...
Cre1
1. Design for Mutiple Reactions
PRESENTED BY:
NAME :
CLASS ROLL NO:
UNV ROLL NO:
PAPER NAME :
PAPER CODE :
DEPARTMEN :
2. Types of reactors
1.Batch- uniform composition everywhere in
reactor but changes with time
2. Semi batch- in semi-batch one reactant will
be added when reaction will proceed
3. Continuous reactor
a.Mixed flow- this is uniformly mixed ,
same composition everywhere, within the
reactor and at exit
b. Plug flow- flow of fluid through reactor with
order so that only lateral mixing is possible
3. Reactor design parameter
Reactor design basically means which type and size of
reactor and method of operation we should employ for
a given conversation
Parameters
• Volume of reactor
• Flow rate
• Concentration of feed
• Reaction kinetic
• Temperature
• pressure
4. Plug flow and mixed flow reactor design
Mixed flow reactor design
Applying mass balance performance
equation for mixed flow reactor
Plug flow reactor design
Performance equation for plug flow reactor
5. Plug flow vs CSTR
•
•
•
•
For any particular duty and for all
positive reaction order the volume of
mixed flow reactor will always be grater
then plug flow
Area under curve in figure is very small
for plug flow as compared to mixed flow
so volume is small for plug flow.
When conversion is small, the reactor
performance is only slightly affected by
flow type. the perforation ratio very
rapidly at high conversion.
Density variation during reaction affects
design, however it is normally of
secondary importance compared to the
difference in flow type.
6. Multiple reactor system
•
•
•
b
e
Number of plug flow reactor
in series are theoretically
same as equivalent volume
of a single plug flow reactor.
Number of mixed flow
reactor of equal size in
series may be used when we
need high conversion and
can’t perform in a single
reactor.
From the given graph, for
first order reaction,
conversion for series of
equal size reactor can
find
7. Mixed flow reactor of different size in series
•
•
•
•
•
From the fig it is clear that for plug flow
reactor volume can be find by dashed
area and for mixed flow whole area.
When we are have to use mixed flow
reactor, then we can use different size
mixed flow reactor so, that over all
volume would be small
To optimized or to find how different size
of mixed flow reactor should used we
have to maximized lower dashed
rectangle.
This optimization gives the slope of
diagonal of the rectangle should be equal
to slope of curve at intersection of these
two reactor.
Levenspiel , has proved that after overall
economic consideration equal size
reactors in series are economical.
8. Design for parallel
reaction
•
•
•
When a reactant gives two product
(desired, and undesired)simultaneously
with different rate constant then this is
called a parallel reaction.
To keep maximum amount of desired
product we can take following steps.
• Ifa1>a2or the desired reaction is of higher
order then keep reactant concentration
high for high product concentration.
If a1<a2 than for desired reaction keep
reactant concentration low.
• For a1=a2 change in reactant
concentration will not affect the product
then, because rate constant k1and k2are
different at different temperature so, we
can keep our temperature such that
desired product will be high or use of
catalyst would be a option which are
9. Reactor design for multiple
reaction
•
•
In multiple reaction reactor design contacting pattern is most important
factor to get a particular product.
In irreversible reaction in series like
•
the mixing of fluid of different composition is the key to formation of
intermediate. The maximum possible amount of intermediate is
obtained if fluid of different composition and different stage of
conversation are not allowed to mixed.
In series of reaction if intermediate reactant is our desired product
than semi batch reactor will be used.
10. Irreversibleseries-parallel reaction
•
•
Multiple reaction that consist of steps in
series and steps in parallel reaction.
In these reaction proper contacting
pattern is very important.
• The general representation of these
reaction are
• reaction is parallel witHere the h respect
to reactant B and in series with A.
Halogenations of alkane is a
example of this kind of
reaction where reaction is
parallel with respect to
halogen
11. Reaction type
•
•
•
•
•
• Chemical kinetics of reaction can be known by knowing
the type of reaction
For reactor selection reaction type will tell us about heat of
reaction either reaction is endothermic or exothermic.
Selectivity is defined as reaction rate ratio for two parallel
reaction.
Catalyst are used to increase reaction rate and selectivity
for a specific reaction.
We can determine what type of catalyst will be used.
Reaction temperature range will be determined.
12. Reactor type
• Reactor may be a plug flow or mixed flow or batch
flow reactor or other.
• Contacting pattern of reaction will be known.
• In case of expensive catalyst and high heat transfer
rate required, mixed flow(fludized bed) reactor are
used.
• For high mass transfer plug flow (packed bed) reactor
will be used.
13. Parallel rxns (competing rxns)
B
A
C
A + B
A + C
C + D
E
A
D
B + C
E + F
k1
k2
Definition of Multiple Reaction
• Series rxns (consecutive rxns)
• A k1
B
k2
C
• Complex rxns (Parallel + Series rxns)
k1
k2
Independent rxns
k1
k2
14. Maximizing the desired product in series reaction
A
k1
B
k2
C
In parallel rxns, maximize the desired product
by adjusting the reaction conditions
by choosing the proper reactor
In series rxns, maximize the desired product
by adjusting the space-time for a flow reactor
by choosing real-time for a batch reactor
15. If the first reaction (formation of B) is fast and the reaction to form C is
slow, a large yield of B can be achieved.
However, if the reaction is allowed to proceed for a long time in a
batch reactor or if the tubular flow reactor is too long, the desired product
B will be converted to C.
In no other type reaction is exactness in the calculation of the time
needed to carry out the reaction more important than in series reactions.
Maximizing the desired product in series reaction
k1 k2
A B C
Desired Product
I f t hefirst reaction is slow and second reaction
is fast,it will be extremely difficult to produce species B.
16. Reaction paths for different ks in series reaction
A B C
k1 k2
~1
2
2
1
1
k
k1
k1
k2
k
k1
A C
B
1
'
2
'
For k1/k2>1, a
Large quantity of B
Can be obtained
For k1/k2<1, a
Little quantity of B
Can be obtained 1st rxn is slow
2nd rxn is fast
'
3
Long rxn time in batch or long tubular reactor
-> B will be converted to C
17. Multiple reactions in a CSTR
Rearranging yields where
After writing a mole balance on each species in the reaction set, we substitute for concentrations
in the respective rate laws.
If there is no volume change with reaction, we use concentrations, Cj, as variables.
If the reactions are gas-phase and there is volume change, we use molar flow rates, Fj as
variables.
q reactions in gas-phase with N different species to be solved
rj
For a CSTR, a coupled set of algebraic eqns analogous to PFR differential eqns must be solved.
Fj
V
Fj0
Fj rjVFj0
q
f j (C1 , C2 ,...,CN ) rij
i1
rj
T
T0
T
NN
T
T0
T
j
q
i1
T0
T
T0
T
10 1 1 i1 1
CT 0
F
FN
C , ,
F
F1
FN r V V fFN0
CT 0
F
FN
C , ,
F
F1
Fj rjV V fFj0
, , C
FF
F FN
F F r V V r V f 1
C