SlideShare a Scribd company logo
Koya University
Faculty of Engineering
Chemical Engineering Department
3rd Stage (2021-2022)
Reactor Laboratory
Lab Report
Number of Experiment: 12
Experiment Name:
Impact of Ethyl Acetate Flow Rate on
Conversion in Plug Flow Reactor Test (21 o
C)
Experiment Date: 02/03/2022
Submitted on: 30/03/2021
Instructor: Mr. Ahmed Abdulkareem Ahmed
Group: A1
Prepared by:
Safeen Yaseen Jafar
Ahmed Mamand Aziz
Ibrahim Ali
Rokan Mohammad Omer
Rivan Dler Ali
Ramazan Shkur Kakl
1
1. Aim of Experiment
➢ Determine Conductivity.
➢ Find out conversion of Plug Flow Reactor (PFR) at 21 o
C with increasing
Ethyl Acetate reactant flowrate.
2. Procedure
1. Prepare 1 L and 0.05 M of NaOH (solution). after it, we need to prepare second reactant
for reaction occur prepare 1 L and 0.05 M of CH3COOHC2H5 (solution) .
2. First of all, in the service units close all valve if open. After that put the bottles in specific
places in service unit. And be careful to that the pipes and valves are connected as well.
3. Turn on the switch control box (power supply).
4. In this experiment we don’t use water bath because it operates under room temperature (20
oC in this experiment).
5. Set the limited flow rate of the reagents before run the steps.
6. Switch on pumps of reactants.
7. Take the reactants from their containers to the Plug Flow Reactor (PFR).
8. Send both of reactants at same time by both reactant hose and reactants enter the reactor
by long tube (inside tube).
9. The reactants react together, and the tube flow as laminar through the packaging and
then after a specific time give us a product.
10. Product will out from the top.
11. In this experiment we increase the flowrate of Ethyl Acetate.
12. To estimate the conductivity, we use the conductivity meter after output of the PFR.
Also, join end of the hose of product with the sensor then the value of conductivity can be
read on the display of the sensor.
13. At the end of the experiment, turn off the pumps.
14. Turn off the power of control interface box.
15. Reactants should be removed from both (1 and 2) reactant bottle container. Then, the
liquids must be kept for following test.
2
3. Tools and Apparatus
Figure 2: Service Unit - Back
Part
Figure 1: Service Unit - Front Part
1
2
4
3
5
6
7
Figure 3: Control Unit/Box
8
10
11
12
Figure 4: Plug Flow Reactor
13
9
14
3
Service Unit, control unit and its parts:
1. Water Bath: is the tank which contain water it used for control temperature of
reactants.
2. Water Bath temperature switch button and controllers.
3. Reactant Container 1: For storage reactant 1.
4. Reactant Container 2: For storage reactant 2.
5. Water Pump AB-1: it used for pumping water.
6. Pump AB-2: It used for pump the reactant 1.
7. Pump AB-3: It used for pump the reactant 2.
8. Pump AB-1 on/off button: It used for switch on or switch of pump AB-1.
9. Power Button: Used to turn on control unit.
10. Temperature Display: For displaying the temperatures
11. Temperature Sensor: for record or estimate temperature.
12. Volumetric Switch Button and Controller: For control the flowrate of reactant.
13. Sensor Selector: it used for select the temperature sensor that you want.
14. Temperature Controller: It can be used when we want to select specified
temperature or control temperature in water bath that we want.
Plug Flow reactor parts:
1. Tube: feeds (reactants) inter the reactor by two of hoses and flow through this
tube and react together.
2. Packaging: These packages are useful for increasing surface area to fast the
reaction or to make more collision number between reactants.
3. Temperature Sensor: it used for record temperature.
4
4. Calculation and Results
We obtained conductivity (λ) value from recording by conductivity meter in lab.
Concentration calculated by this equation:
CA
CAo
=
λ − λ∞
λo − λ∞
* Here we have four values for conductivity (λ)
Conversion calculated by this equation:
X =
CAo
− CA
CAo
CAo = 0.05 M
λo = 14.5 mS
λ∞ = 2.5 µS = 0.0025 mS
λ1 = 0.31 mS , λ2 = 0.25 mS , λ3 = 0.24 mS , λ4 = 0.23 mS
Let’s calculate X for (λ1 = 0.31 mS):
CA
0.05
=
0.31 − 0.0025
14.5 − 0.0025
CA
0.05
= 0.02121055
CA = 0.001060527 M
X =
0.05 − 0.001060527
0.05
X = 0.97878
5
Let’s calculate X for (λ2 = 0.25 mS):
CA
0.05
=
0.25 − 0.0025
14.5 − 0.0025
CA
0.05
= 0.0170719089
CA = 0.000853595 M
X =
0.05 − 0.000853595
0.05
→ 𝐗 = 𝟎. 𝟗𝟖𝟐𝟗
Let’s calculate X for (λ3 = 0.24 mS):
CA
0.05
=
0.24 − 0.0025
14.5 − 0.0025
CA
0.05
= 0.016382134
CA = 0.000819106 M
X =
0.05 − 0.000819106
0.05
→ 𝐗 = 𝟎. 𝟗𝟖𝟑𝟔
Let’s calculate X for (λ4 = 0.23 mS):
CA
0.05
=
0.23 − 0.0025
14.5 − 0.0025
CA
0.05
= 0.01569236
CA = 0.000784618 M
X =
0.05 − 0.0495
0.05
→ 𝐗 = 𝟎. 𝟗𝟖𝟒𝟑
6
5. Discussion
Discussion – Safeen Yaseen Ja’far
This Experiment about Plug Flow reactor or Plug flow reactor (PFR), from
the test we will learn that what is the impact of the increasing flowrate of the
reactant (Ethyl Acetate) on the conversion (X). is after the starting procedure we
estimate conductivity (λ) and main aim of our experiment is that to finding out the
conversion (X) by using conductivity meter firstly and estimate value of
conductivity by this meter. this experiment is under room temperature of 21 o
C
(don’t use water bath) and we used NaOH and Ethyl Acetate (1L and 0.05 M). The
relationship between conductivity and flowrate is vice versa And the relationship
between conductivity and conversion is vice versa. when we increase flowrate λ will
increase then conversion will become more.
After the estimation of (λ) four times (during increasing flowrate) we need
to find the CA by an equation and then we can find X by equation of the conversion.
In previous experiment when we increased the limiting reactant flowrate
conversion will decreased and in this exp will increased. because limiting reactants
gave no more time to reaction and It became complete before completion of the
reaction and it can control the extent of the reaction. but ethyl acetate not like
limiting reactant.
Discussion – Rivan Dler Ali
During this experiment we found conductivity, by conductivity meter then we
convert conductivity to conversion by this equation X=CA0-CA/CA0 at 20C. The
reaction is between NaOH with concentration of 0.05M and second reactant which
is CH3COOHC2H5 with same volume and concentration. First, we put the reactants
below the PFR since putting them above the reactor will cause them to fall quickly
7
and not have enough time to react due to gravity, and then we wait until they reach
the conductivity meter and start reading conductivity (λ) using the conductivity
meter. In this experiment we increased flow rate of Ethyl acetate and we recorded
the conductivity then convert it to concentration by this equation Ca/Ca0= λ- λ∞/
λ0- λ∞ then determined conversion. We did that procedure four times in a row while
increasing flow rate of limiting reactant each time. Concluded that each time we
increased flow rate conversion decreases, because of reaction will not complete
perfectly.
Discussion – Ramazan Shkur Kakl
While conducting the experiment we founded conductivity, then we got
conversion by switching the conductivity with following eq X=CA0-CA/CA0 at
20C. We start with 0.05M NaOH and then prepare the second reactant, which is also
0.05M CH3COOHC2H5. Then, from below, we pour the reactants into the Plug flow
reactor and wait until they reach the reactor's peak, at which point we take a first
reading of conductivity then we convert it to concentration by following equation
Ca/Ca0= λ- λ∞/ λ0- λ∞ at 20C then change it to conversion, result is 0.9984, then
we increased flow rate of Ethyl Acetate 4 times the final result of conversion is 0.997
we noticed that each time we increase flow rate conversion will decrease.
Discussion – Ibrahim Ali
In this experiment we use plug Flow Reactor to our experiment and we want
to Determine Conductivity and Find out conversion of Plug Flow Reactor (PFR) at
21o
C and in the plug Flow Reactor we have the Package inside the tube of reactor
and this package increase cross section area and increase conversion so in this
experiment we increase the mass flow rate and this increasing of mass flow rate is
effect to increasing the conversion.

More Related Content

Similar to RD Lab - Exp-12 - G-A1.pdf

reactor lab single CSTR reactor.pdf
reactor lab single CSTR reactor.pdfreactor lab single CSTR reactor.pdf
reactor lab single CSTR reactor.pdf
DimaJawhar
 
reactor design lab continuous stirred tank reactor
reactor design lab continuous stirred tank reactorreactor design lab continuous stirred tank reactor
reactor design lab continuous stirred tank reactor
DimaJawhar
 
RD Lab - Exp-04 - G-A1.pdf
RD Lab - Exp-04 - G-A1.pdfRD Lab - Exp-04 - G-A1.pdf
RD Lab - Exp-04 - G-A1.pdf
Safeen Yaseen Ja'far
 
Chemical Reaction Engineering Lab v3.0
Chemical Reaction Engineering Lab v3.0Chemical Reaction Engineering Lab v3.0
Chemical Reaction Engineering Lab v3.0Michael Garibaldi
 
Chemical Kinetics in Unit Processes
Chemical Kinetics in Unit ProcessesChemical Kinetics in Unit Processes
Chemical Kinetics in Unit Processes
Rahul Gaur
 
Conductivity measurement water-base(temperature is not included)
Conductivity measurement water-base(temperature is not included)Conductivity measurement water-base(temperature is not included)
Conductivity measurement water-base(temperature is not included)
sarkawtn
 
Conductivity measurement in CSTR water-base(according to temperature)
Conductivity measurement in CSTR water-base(according to temperature)Conductivity measurement in CSTR water-base(according to temperature)
Conductivity measurement in CSTR water-base(according to temperature)
sarkawtn
 
Rea 2.ppt
Rea 2.pptRea 2.ppt
Rea 2.ppt
SurafelMustefa1
 
Auto catalytic reactions presentation
Auto catalytic reactions presentationAuto catalytic reactions presentation
Auto catalytic reactions presentation
Rai Amad Ud Din
 
kineticsmeasurement.pdf
kineticsmeasurement.pdfkineticsmeasurement.pdf
kineticsmeasurement.pdf
NandiniGattadahalli
 
Reaction Engineering
Reaction Engineering Reaction Engineering
Reaction Engineering
odeliachancee
 
Lab 2.docx
Lab 2.docxLab 2.docx
Lab 2.docx
MadhumitaKumar1
 
Effect of Operating Conditions on CSTR performance: an Experimental Study
Effect of Operating Conditions on CSTR performance: an Experimental StudyEffect of Operating Conditions on CSTR performance: an Experimental Study
Effect of Operating Conditions on CSTR performance: an Experimental Study
IJERA Editor
 
RD Lab - Exp-07 - G-A1.pdf
RD Lab - Exp-07 - G-A1.pdfRD Lab - Exp-07 - G-A1.pdf
RD Lab - Exp-07 - G-A1.pdf
Safeen Yaseen Ja'far
 
Auto catalytic reactions presentation
Auto catalytic reactions presentationAuto catalytic reactions presentation
Auto catalytic reactions presentation
Rai Amad Ud Din
 
Fast Slow Timescale Analysis.1
Fast  Slow Timescale Analysis.1Fast  Slow Timescale Analysis.1
Fast Slow Timescale Analysis.1
ahmad bassiouny
 

Similar to RD Lab - Exp-12 - G-A1.pdf (20)

experiment Cstr 40l
experiment Cstr 40lexperiment Cstr 40l
experiment Cstr 40l
 
reactor lab single CSTR reactor.pdf
reactor lab single CSTR reactor.pdfreactor lab single CSTR reactor.pdf
reactor lab single CSTR reactor.pdf
 
reactor design lab continuous stirred tank reactor
reactor design lab continuous stirred tank reactorreactor design lab continuous stirred tank reactor
reactor design lab continuous stirred tank reactor
 
GroupW _Kinetics
GroupW _KineticsGroupW _Kinetics
GroupW _Kinetics
 
RD Lab - Exp-04 - G-A1.pdf
RD Lab - Exp-04 - G-A1.pdfRD Lab - Exp-04 - G-A1.pdf
RD Lab - Exp-04 - G-A1.pdf
 
Chemical Reaction Engineering Lab v3.0
Chemical Reaction Engineering Lab v3.0Chemical Reaction Engineering Lab v3.0
Chemical Reaction Engineering Lab v3.0
 
Reaction rates
Reaction ratesReaction rates
Reaction rates
 
Reactor Design 9
Reactor Design 9Reactor Design 9
Reactor Design 9
 
Chemical Kinetics in Unit Processes
Chemical Kinetics in Unit ProcessesChemical Kinetics in Unit Processes
Chemical Kinetics in Unit Processes
 
Conductivity measurement water-base(temperature is not included)
Conductivity measurement water-base(temperature is not included)Conductivity measurement water-base(temperature is not included)
Conductivity measurement water-base(temperature is not included)
 
Conductivity measurement in CSTR water-base(according to temperature)
Conductivity measurement in CSTR water-base(according to temperature)Conductivity measurement in CSTR water-base(according to temperature)
Conductivity measurement in CSTR water-base(according to temperature)
 
Rea 2.ppt
Rea 2.pptRea 2.ppt
Rea 2.ppt
 
Auto catalytic reactions presentation
Auto catalytic reactions presentationAuto catalytic reactions presentation
Auto catalytic reactions presentation
 
kineticsmeasurement.pdf
kineticsmeasurement.pdfkineticsmeasurement.pdf
kineticsmeasurement.pdf
 
Reaction Engineering
Reaction Engineering Reaction Engineering
Reaction Engineering
 
Lab 2.docx
Lab 2.docxLab 2.docx
Lab 2.docx
 
Effect of Operating Conditions on CSTR performance: an Experimental Study
Effect of Operating Conditions on CSTR performance: an Experimental StudyEffect of Operating Conditions on CSTR performance: an Experimental Study
Effect of Operating Conditions on CSTR performance: an Experimental Study
 
RD Lab - Exp-07 - G-A1.pdf
RD Lab - Exp-07 - G-A1.pdfRD Lab - Exp-07 - G-A1.pdf
RD Lab - Exp-07 - G-A1.pdf
 
Auto catalytic reactions presentation
Auto catalytic reactions presentationAuto catalytic reactions presentation
Auto catalytic reactions presentation
 
Fast Slow Timescale Analysis.1
Fast  Slow Timescale Analysis.1Fast  Slow Timescale Analysis.1
Fast Slow Timescale Analysis.1
 

More from Safeen Yaseen Ja'far

Safeen Yaseen-Assignment-1 (TC Unit).pdf
Safeen Yaseen-Assignment-1 (TC Unit).pdfSafeen Yaseen-Assignment-1 (TC Unit).pdf
Safeen Yaseen-Assignment-1 (TC Unit).pdf
Safeen Yaseen Ja'far
 
Assignment 1 - Application of Numerical Analysis.pdf
Assignment 1 - Application of Numerical Analysis.pdfAssignment 1 - Application of Numerical Analysis.pdf
Assignment 1 - Application of Numerical Analysis.pdf
Safeen Yaseen Ja'far
 
Safeen Yaseen-Assignment-1 (HAZOP).pdf
Safeen Yaseen-Assignment-1 (HAZOP).pdfSafeen Yaseen-Assignment-1 (HAZOP).pdf
Safeen Yaseen-Assignment-1 (HAZOP).pdf
Safeen Yaseen Ja'far
 
Assignment 1 - Application of Simulation Software.pdf
Assignment 1 - Application of Simulation Software.pdfAssignment 1 - Application of Simulation Software.pdf
Assignment 1 - Application of Simulation Software.pdf
Safeen Yaseen Ja'far
 
Assignment 1 - Crude Oil Desalting Unit.pdf
Assignment 1 - Crude Oil Desalting Unit.pdfAssignment 1 - Crude Oil Desalting Unit.pdf
Assignment 1 - Crude Oil Desalting Unit.pdf
Safeen Yaseen Ja'far
 
Process Control-Paraphrased.pdf
Process Control-Paraphrased.pdfProcess Control-Paraphrased.pdf
Process Control-Paraphrased.pdf
Safeen Yaseen Ja'far
 
Plant Design Report-Oil Refinery.pdf
Plant Design Report-Oil Refinery.pdfPlant Design Report-Oil Refinery.pdf
Plant Design Report-Oil Refinery.pdf
Safeen Yaseen Ja'far
 
Eng Economics-Report-Safeen Yaseen.pdf
Eng Economics-Report-Safeen Yaseen.pdfEng Economics-Report-Safeen Yaseen.pdf
Eng Economics-Report-Safeen Yaseen.pdf
Safeen Yaseen Ja'far
 
Applied of Statistics in Quality Control-Safeen Yaseen.pdf
Applied of Statistics in Quality Control-Safeen Yaseen.pdfApplied of Statistics in Quality Control-Safeen Yaseen.pdf
Applied of Statistics in Quality Control-Safeen Yaseen.pdf
Safeen Yaseen Ja'far
 
HTR Lab - Exp-03 - G-A2.pdf
HTR Lab - Exp-03 - G-A2.pdfHTR Lab - Exp-03 - G-A2.pdf
HTR Lab - Exp-03 - G-A2.pdf
Safeen Yaseen Ja'far
 
HTR Lab - Exp-02b - G-A2.pdf
HTR Lab - Exp-02b - G-A2.pdfHTR Lab - Exp-02b - G-A2.pdf
HTR Lab - Exp-02b - G-A2.pdf
Safeen Yaseen Ja'far
 
HTR Lab - Exp-02a - G-A2.pdf
HTR Lab - Exp-02a - G-A2.pdfHTR Lab - Exp-02a - G-A2.pdf
HTR Lab - Exp-02a - G-A2.pdf
Safeen Yaseen Ja'far
 
HTR Lab - Exp-01 - G-A1.pdf
HTR Lab - Exp-01 - G-A1.pdfHTR Lab - Exp-01 - G-A1.pdf
HTR Lab - Exp-01 - G-A1.pdf
Safeen Yaseen Ja'far
 
EXPERIMENT HEAT-CONDUCTION.pdf
EXPERIMENT HEAT-CONDUCTION.pdfEXPERIMENT HEAT-CONDUCTION.pdf
EXPERIMENT HEAT-CONDUCTION.pdf
Safeen Yaseen Ja'far
 
RD Lab - Exp-06 - G-A1.pdf
RD Lab - Exp-06 - G-A1.pdfRD Lab - Exp-06 - G-A1.pdf
RD Lab - Exp-06 - G-A1.pdf
Safeen Yaseen Ja'far
 
RD Lab - Exp-01 - G-A1.pdf
RD Lab - Exp-01 - G-A1.pdfRD Lab - Exp-01 - G-A1.pdf
RD Lab - Exp-01 - G-A1.pdf
Safeen Yaseen Ja'far
 
Natural Gas Dehydration Processes.pdf
Natural Gas Dehydration Processes.pdfNatural Gas Dehydration Processes.pdf
Natural Gas Dehydration Processes.pdf
Safeen Yaseen Ja'far
 
HTR Report - Energy Storage.pdf
HTR Report - Energy Storage.pdfHTR Report - Energy Storage.pdf
HTR Report - Energy Storage.pdf
Safeen Yaseen Ja'far
 
Applied of Statistics in Quality Control-Safeen Yaseen.pdf
Applied of Statistics in Quality Control-Safeen Yaseen.pdfApplied of Statistics in Quality Control-Safeen Yaseen.pdf
Applied of Statistics in Quality Control-Safeen Yaseen.pdf
Safeen Yaseen Ja'far
 
Env. Eng. 21-22-Ass-Acid Rain-26-Mar.pdf
Env. Eng. 21-22-Ass-Acid Rain-26-Mar.pdfEnv. Eng. 21-22-Ass-Acid Rain-26-Mar.pdf
Env. Eng. 21-22-Ass-Acid Rain-26-Mar.pdf
Safeen Yaseen Ja'far
 

More from Safeen Yaseen Ja'far (20)

Safeen Yaseen-Assignment-1 (TC Unit).pdf
Safeen Yaseen-Assignment-1 (TC Unit).pdfSafeen Yaseen-Assignment-1 (TC Unit).pdf
Safeen Yaseen-Assignment-1 (TC Unit).pdf
 
Assignment 1 - Application of Numerical Analysis.pdf
Assignment 1 - Application of Numerical Analysis.pdfAssignment 1 - Application of Numerical Analysis.pdf
Assignment 1 - Application of Numerical Analysis.pdf
 
Safeen Yaseen-Assignment-1 (HAZOP).pdf
Safeen Yaseen-Assignment-1 (HAZOP).pdfSafeen Yaseen-Assignment-1 (HAZOP).pdf
Safeen Yaseen-Assignment-1 (HAZOP).pdf
 
Assignment 1 - Application of Simulation Software.pdf
Assignment 1 - Application of Simulation Software.pdfAssignment 1 - Application of Simulation Software.pdf
Assignment 1 - Application of Simulation Software.pdf
 
Assignment 1 - Crude Oil Desalting Unit.pdf
Assignment 1 - Crude Oil Desalting Unit.pdfAssignment 1 - Crude Oil Desalting Unit.pdf
Assignment 1 - Crude Oil Desalting Unit.pdf
 
Process Control-Paraphrased.pdf
Process Control-Paraphrased.pdfProcess Control-Paraphrased.pdf
Process Control-Paraphrased.pdf
 
Plant Design Report-Oil Refinery.pdf
Plant Design Report-Oil Refinery.pdfPlant Design Report-Oil Refinery.pdf
Plant Design Report-Oil Refinery.pdf
 
Eng Economics-Report-Safeen Yaseen.pdf
Eng Economics-Report-Safeen Yaseen.pdfEng Economics-Report-Safeen Yaseen.pdf
Eng Economics-Report-Safeen Yaseen.pdf
 
Applied of Statistics in Quality Control-Safeen Yaseen.pdf
Applied of Statistics in Quality Control-Safeen Yaseen.pdfApplied of Statistics in Quality Control-Safeen Yaseen.pdf
Applied of Statistics in Quality Control-Safeen Yaseen.pdf
 
HTR Lab - Exp-03 - G-A2.pdf
HTR Lab - Exp-03 - G-A2.pdfHTR Lab - Exp-03 - G-A2.pdf
HTR Lab - Exp-03 - G-A2.pdf
 
HTR Lab - Exp-02b - G-A2.pdf
HTR Lab - Exp-02b - G-A2.pdfHTR Lab - Exp-02b - G-A2.pdf
HTR Lab - Exp-02b - G-A2.pdf
 
HTR Lab - Exp-02a - G-A2.pdf
HTR Lab - Exp-02a - G-A2.pdfHTR Lab - Exp-02a - G-A2.pdf
HTR Lab - Exp-02a - G-A2.pdf
 
HTR Lab - Exp-01 - G-A1.pdf
HTR Lab - Exp-01 - G-A1.pdfHTR Lab - Exp-01 - G-A1.pdf
HTR Lab - Exp-01 - G-A1.pdf
 
EXPERIMENT HEAT-CONDUCTION.pdf
EXPERIMENT HEAT-CONDUCTION.pdfEXPERIMENT HEAT-CONDUCTION.pdf
EXPERIMENT HEAT-CONDUCTION.pdf
 
RD Lab - Exp-06 - G-A1.pdf
RD Lab - Exp-06 - G-A1.pdfRD Lab - Exp-06 - G-A1.pdf
RD Lab - Exp-06 - G-A1.pdf
 
RD Lab - Exp-01 - G-A1.pdf
RD Lab - Exp-01 - G-A1.pdfRD Lab - Exp-01 - G-A1.pdf
RD Lab - Exp-01 - G-A1.pdf
 
Natural Gas Dehydration Processes.pdf
Natural Gas Dehydration Processes.pdfNatural Gas Dehydration Processes.pdf
Natural Gas Dehydration Processes.pdf
 
HTR Report - Energy Storage.pdf
HTR Report - Energy Storage.pdfHTR Report - Energy Storage.pdf
HTR Report - Energy Storage.pdf
 
Applied of Statistics in Quality Control-Safeen Yaseen.pdf
Applied of Statistics in Quality Control-Safeen Yaseen.pdfApplied of Statistics in Quality Control-Safeen Yaseen.pdf
Applied of Statistics in Quality Control-Safeen Yaseen.pdf
 
Env. Eng. 21-22-Ass-Acid Rain-26-Mar.pdf
Env. Eng. 21-22-Ass-Acid Rain-26-Mar.pdfEnv. Eng. 21-22-Ass-Acid Rain-26-Mar.pdf
Env. Eng. 21-22-Ass-Acid Rain-26-Mar.pdf
 

Recently uploaded

English lab ppt no titlespecENG PPTt.pdf
English lab ppt no titlespecENG PPTt.pdfEnglish lab ppt no titlespecENG PPTt.pdf
English lab ppt no titlespecENG PPTt.pdf
BrazilAccount1
 
weather web application report.pdf
weather web application report.pdfweather web application report.pdf
weather web application report.pdf
Pratik Pawar
 
Fundamentals of Electric Drives and its applications.pptx
Fundamentals of Electric Drives and its applications.pptxFundamentals of Electric Drives and its applications.pptx
Fundamentals of Electric Drives and its applications.pptx
manasideore6
 
CME397 Surface Engineering- Professional Elective
CME397 Surface Engineering- Professional ElectiveCME397 Surface Engineering- Professional Elective
CME397 Surface Engineering- Professional Elective
karthi keyan
 
Sachpazis:Terzaghi Bearing Capacity Estimation in simple terms with Calculati...
Sachpazis:Terzaghi Bearing Capacity Estimation in simple terms with Calculati...Sachpazis:Terzaghi Bearing Capacity Estimation in simple terms with Calculati...
Sachpazis:Terzaghi Bearing Capacity Estimation in simple terms with Calculati...
Dr.Costas Sachpazis
 
Hybrid optimization of pumped hydro system and solar- Engr. Abdul-Azeez.pdf
Hybrid optimization of pumped hydro system and solar- Engr. Abdul-Azeez.pdfHybrid optimization of pumped hydro system and solar- Engr. Abdul-Azeez.pdf
Hybrid optimization of pumped hydro system and solar- Engr. Abdul-Azeez.pdf
fxintegritypublishin
 
Pile Foundation by Venkatesh Taduvai (Sub Geotechnical Engineering II)-conver...
Pile Foundation by Venkatesh Taduvai (Sub Geotechnical Engineering II)-conver...Pile Foundation by Venkatesh Taduvai (Sub Geotechnical Engineering II)-conver...
Pile Foundation by Venkatesh Taduvai (Sub Geotechnical Engineering II)-conver...
AJAYKUMARPUND1
 
J.Yang, ICLR 2024, MLILAB, KAIST AI.pdf
J.Yang,  ICLR 2024, MLILAB, KAIST AI.pdfJ.Yang,  ICLR 2024, MLILAB, KAIST AI.pdf
J.Yang, ICLR 2024, MLILAB, KAIST AI.pdf
MLILAB
 
Standard Reomte Control Interface - Neometrix
Standard Reomte Control Interface - NeometrixStandard Reomte Control Interface - Neometrix
Standard Reomte Control Interface - Neometrix
Neometrix_Engineering_Pvt_Ltd
 
Top 10 Oil and Gas Projects in Saudi Arabia 2024.pdf
Top 10 Oil and Gas Projects in Saudi Arabia 2024.pdfTop 10 Oil and Gas Projects in Saudi Arabia 2024.pdf
Top 10 Oil and Gas Projects in Saudi Arabia 2024.pdf
Teleport Manpower Consultant
 
Final project report on grocery store management system..pdf
Final project report on grocery store management system..pdfFinal project report on grocery store management system..pdf
Final project report on grocery store management system..pdf
Kamal Acharya
 
block diagram and signal flow graph representation
block diagram and signal flow graph representationblock diagram and signal flow graph representation
block diagram and signal flow graph representation
Divya Somashekar
 
The Benefits and Techniques of Trenchless Pipe Repair.pdf
The Benefits and Techniques of Trenchless Pipe Repair.pdfThe Benefits and Techniques of Trenchless Pipe Repair.pdf
The Benefits and Techniques of Trenchless Pipe Repair.pdf
Pipe Restoration Solutions
 
Design and Analysis of Algorithms-DP,Backtracking,Graphs,B&B
Design and Analysis of Algorithms-DP,Backtracking,Graphs,B&BDesign and Analysis of Algorithms-DP,Backtracking,Graphs,B&B
Design and Analysis of Algorithms-DP,Backtracking,Graphs,B&B
Sreedhar Chowdam
 
CFD Simulation of By-pass Flow in a HRSG module by R&R Consult.pptx
CFD Simulation of By-pass Flow in a HRSG module by R&R Consult.pptxCFD Simulation of By-pass Flow in a HRSG module by R&R Consult.pptx
CFD Simulation of By-pass Flow in a HRSG module by R&R Consult.pptx
R&R Consult
 
一比一原版(SFU毕业证)西蒙菲莎大学毕业证成绩单如何办理
一比一原版(SFU毕业证)西蒙菲莎大学毕业证成绩单如何办理一比一原版(SFU毕业证)西蒙菲莎大学毕业证成绩单如何办理
一比一原版(SFU毕业证)西蒙菲莎大学毕业证成绩单如何办理
bakpo1
 
HYDROPOWER - Hydroelectric power generation
HYDROPOWER - Hydroelectric power generationHYDROPOWER - Hydroelectric power generation
HYDROPOWER - Hydroelectric power generation
Robbie Edward Sayers
 
ML for identifying fraud using open blockchain data.pptx
ML for identifying fraud using open blockchain data.pptxML for identifying fraud using open blockchain data.pptx
ML for identifying fraud using open blockchain data.pptx
Vijay Dialani, PhD
 
Cosmetic shop management system project report.pdf
Cosmetic shop management system project report.pdfCosmetic shop management system project report.pdf
Cosmetic shop management system project report.pdf
Kamal Acharya
 
Water Industry Process Automation and Control Monthly - May 2024.pdf
Water Industry Process Automation and Control Monthly - May 2024.pdfWater Industry Process Automation and Control Monthly - May 2024.pdf
Water Industry Process Automation and Control Monthly - May 2024.pdf
Water Industry Process Automation & Control
 

Recently uploaded (20)

English lab ppt no titlespecENG PPTt.pdf
English lab ppt no titlespecENG PPTt.pdfEnglish lab ppt no titlespecENG PPTt.pdf
English lab ppt no titlespecENG PPTt.pdf
 
weather web application report.pdf
weather web application report.pdfweather web application report.pdf
weather web application report.pdf
 
Fundamentals of Electric Drives and its applications.pptx
Fundamentals of Electric Drives and its applications.pptxFundamentals of Electric Drives and its applications.pptx
Fundamentals of Electric Drives and its applications.pptx
 
CME397 Surface Engineering- Professional Elective
CME397 Surface Engineering- Professional ElectiveCME397 Surface Engineering- Professional Elective
CME397 Surface Engineering- Professional Elective
 
Sachpazis:Terzaghi Bearing Capacity Estimation in simple terms with Calculati...
Sachpazis:Terzaghi Bearing Capacity Estimation in simple terms with Calculati...Sachpazis:Terzaghi Bearing Capacity Estimation in simple terms with Calculati...
Sachpazis:Terzaghi Bearing Capacity Estimation in simple terms with Calculati...
 
Hybrid optimization of pumped hydro system and solar- Engr. Abdul-Azeez.pdf
Hybrid optimization of pumped hydro system and solar- Engr. Abdul-Azeez.pdfHybrid optimization of pumped hydro system and solar- Engr. Abdul-Azeez.pdf
Hybrid optimization of pumped hydro system and solar- Engr. Abdul-Azeez.pdf
 
Pile Foundation by Venkatesh Taduvai (Sub Geotechnical Engineering II)-conver...
Pile Foundation by Venkatesh Taduvai (Sub Geotechnical Engineering II)-conver...Pile Foundation by Venkatesh Taduvai (Sub Geotechnical Engineering II)-conver...
Pile Foundation by Venkatesh Taduvai (Sub Geotechnical Engineering II)-conver...
 
J.Yang, ICLR 2024, MLILAB, KAIST AI.pdf
J.Yang,  ICLR 2024, MLILAB, KAIST AI.pdfJ.Yang,  ICLR 2024, MLILAB, KAIST AI.pdf
J.Yang, ICLR 2024, MLILAB, KAIST AI.pdf
 
Standard Reomte Control Interface - Neometrix
Standard Reomte Control Interface - NeometrixStandard Reomte Control Interface - Neometrix
Standard Reomte Control Interface - Neometrix
 
Top 10 Oil and Gas Projects in Saudi Arabia 2024.pdf
Top 10 Oil and Gas Projects in Saudi Arabia 2024.pdfTop 10 Oil and Gas Projects in Saudi Arabia 2024.pdf
Top 10 Oil and Gas Projects in Saudi Arabia 2024.pdf
 
Final project report on grocery store management system..pdf
Final project report on grocery store management system..pdfFinal project report on grocery store management system..pdf
Final project report on grocery store management system..pdf
 
block diagram and signal flow graph representation
block diagram and signal flow graph representationblock diagram and signal flow graph representation
block diagram and signal flow graph representation
 
The Benefits and Techniques of Trenchless Pipe Repair.pdf
The Benefits and Techniques of Trenchless Pipe Repair.pdfThe Benefits and Techniques of Trenchless Pipe Repair.pdf
The Benefits and Techniques of Trenchless Pipe Repair.pdf
 
Design and Analysis of Algorithms-DP,Backtracking,Graphs,B&B
Design and Analysis of Algorithms-DP,Backtracking,Graphs,B&BDesign and Analysis of Algorithms-DP,Backtracking,Graphs,B&B
Design and Analysis of Algorithms-DP,Backtracking,Graphs,B&B
 
CFD Simulation of By-pass Flow in a HRSG module by R&R Consult.pptx
CFD Simulation of By-pass Flow in a HRSG module by R&R Consult.pptxCFD Simulation of By-pass Flow in a HRSG module by R&R Consult.pptx
CFD Simulation of By-pass Flow in a HRSG module by R&R Consult.pptx
 
一比一原版(SFU毕业证)西蒙菲莎大学毕业证成绩单如何办理
一比一原版(SFU毕业证)西蒙菲莎大学毕业证成绩单如何办理一比一原版(SFU毕业证)西蒙菲莎大学毕业证成绩单如何办理
一比一原版(SFU毕业证)西蒙菲莎大学毕业证成绩单如何办理
 
HYDROPOWER - Hydroelectric power generation
HYDROPOWER - Hydroelectric power generationHYDROPOWER - Hydroelectric power generation
HYDROPOWER - Hydroelectric power generation
 
ML for identifying fraud using open blockchain data.pptx
ML for identifying fraud using open blockchain data.pptxML for identifying fraud using open blockchain data.pptx
ML for identifying fraud using open blockchain data.pptx
 
Cosmetic shop management system project report.pdf
Cosmetic shop management system project report.pdfCosmetic shop management system project report.pdf
Cosmetic shop management system project report.pdf
 
Water Industry Process Automation and Control Monthly - May 2024.pdf
Water Industry Process Automation and Control Monthly - May 2024.pdfWater Industry Process Automation and Control Monthly - May 2024.pdf
Water Industry Process Automation and Control Monthly - May 2024.pdf
 

RD Lab - Exp-12 - G-A1.pdf

  • 1. Koya University Faculty of Engineering Chemical Engineering Department 3rd Stage (2021-2022) Reactor Laboratory Lab Report Number of Experiment: 12 Experiment Name: Impact of Ethyl Acetate Flow Rate on Conversion in Plug Flow Reactor Test (21 o C) Experiment Date: 02/03/2022 Submitted on: 30/03/2021 Instructor: Mr. Ahmed Abdulkareem Ahmed Group: A1 Prepared by: Safeen Yaseen Jafar Ahmed Mamand Aziz Ibrahim Ali Rokan Mohammad Omer Rivan Dler Ali Ramazan Shkur Kakl
  • 2. 1 1. Aim of Experiment ➢ Determine Conductivity. ➢ Find out conversion of Plug Flow Reactor (PFR) at 21 o C with increasing Ethyl Acetate reactant flowrate. 2. Procedure 1. Prepare 1 L and 0.05 M of NaOH (solution). after it, we need to prepare second reactant for reaction occur prepare 1 L and 0.05 M of CH3COOHC2H5 (solution) . 2. First of all, in the service units close all valve if open. After that put the bottles in specific places in service unit. And be careful to that the pipes and valves are connected as well. 3. Turn on the switch control box (power supply). 4. In this experiment we don’t use water bath because it operates under room temperature (20 oC in this experiment). 5. Set the limited flow rate of the reagents before run the steps. 6. Switch on pumps of reactants. 7. Take the reactants from their containers to the Plug Flow Reactor (PFR). 8. Send both of reactants at same time by both reactant hose and reactants enter the reactor by long tube (inside tube). 9. The reactants react together, and the tube flow as laminar through the packaging and then after a specific time give us a product. 10. Product will out from the top. 11. In this experiment we increase the flowrate of Ethyl Acetate. 12. To estimate the conductivity, we use the conductivity meter after output of the PFR. Also, join end of the hose of product with the sensor then the value of conductivity can be read on the display of the sensor. 13. At the end of the experiment, turn off the pumps. 14. Turn off the power of control interface box. 15. Reactants should be removed from both (1 and 2) reactant bottle container. Then, the liquids must be kept for following test.
  • 3. 2 3. Tools and Apparatus Figure 2: Service Unit - Back Part Figure 1: Service Unit - Front Part 1 2 4 3 5 6 7 Figure 3: Control Unit/Box 8 10 11 12 Figure 4: Plug Flow Reactor 13 9 14
  • 4. 3 Service Unit, control unit and its parts: 1. Water Bath: is the tank which contain water it used for control temperature of reactants. 2. Water Bath temperature switch button and controllers. 3. Reactant Container 1: For storage reactant 1. 4. Reactant Container 2: For storage reactant 2. 5. Water Pump AB-1: it used for pumping water. 6. Pump AB-2: It used for pump the reactant 1. 7. Pump AB-3: It used for pump the reactant 2. 8. Pump AB-1 on/off button: It used for switch on or switch of pump AB-1. 9. Power Button: Used to turn on control unit. 10. Temperature Display: For displaying the temperatures 11. Temperature Sensor: for record or estimate temperature. 12. Volumetric Switch Button and Controller: For control the flowrate of reactant. 13. Sensor Selector: it used for select the temperature sensor that you want. 14. Temperature Controller: It can be used when we want to select specified temperature or control temperature in water bath that we want. Plug Flow reactor parts: 1. Tube: feeds (reactants) inter the reactor by two of hoses and flow through this tube and react together. 2. Packaging: These packages are useful for increasing surface area to fast the reaction or to make more collision number between reactants. 3. Temperature Sensor: it used for record temperature.
  • 5. 4 4. Calculation and Results We obtained conductivity (λ) value from recording by conductivity meter in lab. Concentration calculated by this equation: CA CAo = λ − λ∞ λo − λ∞ * Here we have four values for conductivity (λ) Conversion calculated by this equation: X = CAo − CA CAo CAo = 0.05 M λo = 14.5 mS λ∞ = 2.5 µS = 0.0025 mS λ1 = 0.31 mS , λ2 = 0.25 mS , λ3 = 0.24 mS , λ4 = 0.23 mS Let’s calculate X for (λ1 = 0.31 mS): CA 0.05 = 0.31 − 0.0025 14.5 − 0.0025 CA 0.05 = 0.02121055 CA = 0.001060527 M X = 0.05 − 0.001060527 0.05 X = 0.97878
  • 6. 5 Let’s calculate X for (λ2 = 0.25 mS): CA 0.05 = 0.25 − 0.0025 14.5 − 0.0025 CA 0.05 = 0.0170719089 CA = 0.000853595 M X = 0.05 − 0.000853595 0.05 → 𝐗 = 𝟎. 𝟗𝟖𝟐𝟗 Let’s calculate X for (λ3 = 0.24 mS): CA 0.05 = 0.24 − 0.0025 14.5 − 0.0025 CA 0.05 = 0.016382134 CA = 0.000819106 M X = 0.05 − 0.000819106 0.05 → 𝐗 = 𝟎. 𝟗𝟖𝟑𝟔 Let’s calculate X for (λ4 = 0.23 mS): CA 0.05 = 0.23 − 0.0025 14.5 − 0.0025 CA 0.05 = 0.01569236 CA = 0.000784618 M X = 0.05 − 0.0495 0.05 → 𝐗 = 𝟎. 𝟗𝟖𝟒𝟑
  • 7. 6 5. Discussion Discussion – Safeen Yaseen Ja’far This Experiment about Plug Flow reactor or Plug flow reactor (PFR), from the test we will learn that what is the impact of the increasing flowrate of the reactant (Ethyl Acetate) on the conversion (X). is after the starting procedure we estimate conductivity (λ) and main aim of our experiment is that to finding out the conversion (X) by using conductivity meter firstly and estimate value of conductivity by this meter. this experiment is under room temperature of 21 o C (don’t use water bath) and we used NaOH and Ethyl Acetate (1L and 0.05 M). The relationship between conductivity and flowrate is vice versa And the relationship between conductivity and conversion is vice versa. when we increase flowrate λ will increase then conversion will become more. After the estimation of (λ) four times (during increasing flowrate) we need to find the CA by an equation and then we can find X by equation of the conversion. In previous experiment when we increased the limiting reactant flowrate conversion will decreased and in this exp will increased. because limiting reactants gave no more time to reaction and It became complete before completion of the reaction and it can control the extent of the reaction. but ethyl acetate not like limiting reactant. Discussion – Rivan Dler Ali During this experiment we found conductivity, by conductivity meter then we convert conductivity to conversion by this equation X=CA0-CA/CA0 at 20C. The reaction is between NaOH with concentration of 0.05M and second reactant which is CH3COOHC2H5 with same volume and concentration. First, we put the reactants below the PFR since putting them above the reactor will cause them to fall quickly
  • 8. 7 and not have enough time to react due to gravity, and then we wait until they reach the conductivity meter and start reading conductivity (λ) using the conductivity meter. In this experiment we increased flow rate of Ethyl acetate and we recorded the conductivity then convert it to concentration by this equation Ca/Ca0= λ- λ∞/ λ0- λ∞ then determined conversion. We did that procedure four times in a row while increasing flow rate of limiting reactant each time. Concluded that each time we increased flow rate conversion decreases, because of reaction will not complete perfectly. Discussion – Ramazan Shkur Kakl While conducting the experiment we founded conductivity, then we got conversion by switching the conductivity with following eq X=CA0-CA/CA0 at 20C. We start with 0.05M NaOH and then prepare the second reactant, which is also 0.05M CH3COOHC2H5. Then, from below, we pour the reactants into the Plug flow reactor and wait until they reach the reactor's peak, at which point we take a first reading of conductivity then we convert it to concentration by following equation Ca/Ca0= λ- λ∞/ λ0- λ∞ at 20C then change it to conversion, result is 0.9984, then we increased flow rate of Ethyl Acetate 4 times the final result of conversion is 0.997 we noticed that each time we increase flow rate conversion will decrease. Discussion – Ibrahim Ali In this experiment we use plug Flow Reactor to our experiment and we want to Determine Conductivity and Find out conversion of Plug Flow Reactor (PFR) at 21o C and in the plug Flow Reactor we have the Package inside the tube of reactor and this package increase cross section area and increase conversion so in this experiment we increase the mass flow rate and this increasing of mass flow rate is effect to increasing the conversion.