SlideShare a Scribd company logo
1 of 10
Download to read offline
1
Koya University
Faculty of Engineering
Chemical Engineering Department
3rd Stage (2021-2022)
Reactor Laboratory
Lab Report
Number of Experiment: 10
Experiment Name:
Plug Flow Reactor - Conversion Test (20 o
C)
Experiment Date: 16/02/2022
Submitted on: 23/02/2021
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. Aim of Experiment
➢ Determine Conductivity.
➢ Find out conversion of Plug Flow Reactor (PFR) at 20 o
C.
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. 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.
12. At the end of the experiment, turn off the pumps.
13. Turn off the power of control interface box.
14. Reactants should be removed from both (1 and 2) reactant bottle container. Then, the
liquids must be kept for following test.
3
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
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 Packaging are used for increase the surface area and it cause to
fast the reaction or to make more collision number between reactants.
3. Temperature Sensor: it used for record temperature.
5
4. Calculation and Results
We obtained conductivity value from recording by conductivity meter in lab.
Concentration calculated by this equation:
CA
CAo
=
λ − λ∞
λo − λ∞
Conversion calculated by this equation:
X =
CAo
− CA
CAo
Let’s calculate X:
λo = 14.5 mS
λ∞ = 2.5 µS = 0.0025 mS
λ = 0.5 mS
CAo = 0.05 M
CA
0.05
=
0.5 − 0.0025
14.5 − 0.0025
CA
0.05
= 0.034316
CA = 0.0017158 M
X =
0.05 − 0.0495
0.05
X = 0.965
6
As a result for this experiment and previous experiments here we make a table that
shows us differences between quality or conversion rate (under the room
temperature)in different types of the reactors, as following:
Types of reactor Conversion Rate
Batch Flow Reactor 0.996
Continuous Stirred Tank Reactor (CSTR) 0.880
CSTR in Series 0.890
Tubular Flow Reactor (TFR) 0.917
Laminar Flow Reactor (LFR) 0.999
Plug Flow Reactor (PFR) 0.965
7
5. Discussion
Discussion – Safeen Yaseen Ja’far
This Experiment about Plug Flow reactor or in short (PFR), estimate
conductivity 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. In this experiment under room temperature of 20 o
C we used NaOH and
Ethyl Acetate (1L and 0.05 M). After the estimation of (λ) we need to find the CA
by an equation and then we can find X by equation of the conversion.
As we see in the result of our experiment and previous experiments there are
different values of conversion rate means the conversion rate change by changing
the reactor type. If we see the values, we learn that some reactor type better than
some other reactor types, for example TFR or PFR better than CSTR means we
can place the TFR or PFR instead of some CSTR reactors.
However, we have some error in this experiment because maybe we don’t
have exact conversion of the 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 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 the recent experiment the conversion shows that it varies
each time with reactor changing, according to conversion table that Laminar Flow
Reactor (LFR) with conversion of 0.999 is first place and in second place Batch
8
Flow Reactor with conversion of 0.996 and in third place Plug Flow Reactor (PFR)
with conversion of 0.965. the conversion changes and a lot of things have impact
on it for example the type of reaction, reactants, production rate and a lot more.
Discussion – Ahmed Mamand Aziz
Throughout this experiment is about Plug reactor (PFR), we were
determined the conductivity & conversion at 20 oC, the solution of reactant was
between {Sodium hydroxide and Ethyl acetate} in the reactant input tube. Each
reactant prepared in 1 L contain of 0.05M. Read directly the value of conductivity-
by-conductivity meter that is equal to 0.5mS and these values are given
λ∞=0.0025mS, λo=14.5mS. Then we found conversion that is explained in
calculation by the way we have already have a value of λ∞=0.0025mS and
λo=14.5 and we found the value of λ in the experiment that is equal to 0.5mS and
also, we have the value of CAo =0.05, then we could find the value of
CA=0.34316. finally, by using the value of CA and CAo we were found
conversion equal to (0.965).
Also, about the difference between the reactant conversion that is required to
compare between them, if we sort them from top to bottom, the first one is LFR
that have the highest conversion rate between them, second one is batch reactor
BR, third one is PFR, forth one is TFR, sixth one is CSTR in series, and last one is
CSTR.
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 laminar flow
9
reactor and wait until they reach the reactor's peak, at which point we take a single
reading because the reactor is already at steady state at 20C. Finally, we convert
conductivity to concentration using the equation Ca/Ca0=λ0-λ/λ0-λ∞. During the
previous experiment the conversion demonstrate that it changes each time with the
reactor being changed. With the information that we got from the conversion table
we can confirm that (LFR) laminar flow reactor is at first place with 0.999
conversion rate, while the batch flow reactor with conversion rate of 0.996 got the
second place. The third place goes to Plug flow reactor with conversion of 0.965.
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
20 C and in the Plug Flow Reactor we have the catalyst inside the device this
catalyst increase cross section area and increase conversion and in this experiment
we t we have two reactant we use 0.05 M NaOH and 0.05 M of CH3COOHC2H5
to occur conversion and after a specific time we start to read the conductivity-by-
conductivity meter. Also, during experiment we do in past by the different device
we can focus in the rate of conversion occur during the experiment from different a
device so we can note Laminar Flow Reactor (LFR) is the best device to occur
conversion and after that Batch Flow Reactor after that Plug (Plug) Flow Reactor
(PFR) and after that Tubular Flow Reactor (TFR) and after that Continuous Stirred
Tank Reactor (CSTR) and finally CSTR in Series.
Discussion – Rokan Mohammad
10
During this experiment we learn about the Plug reactor (PFR), at
temperature (20 oC) and inertial concentration is (CAo)=0.05M and 1L for the
(CH3COOC2H5 and NAOH). We calculated conductivity by conductivity meter,
we read this value directly and equal to 0.5mS also, determined conversion (X) by
using (conductivity and CA) so is equal to 0.965. First determine the concentration
(CA) is equal to 0.34316 by using the values of conductivities λ= 2.8mS this is
found in our experiment λ∞=0.0025, λo=14.5 and there are given for using to
determining CA, following that by using CA and CAo could find the conversion.
Also, if we rank them from top to bottom, the first one is LFR, which has the
greatest conversion rate between them, the second one is batch reactor BR, third
one is PFR, fourth one is TFR, sixth one is CSTR in series, and last one is CSTR.

More Related Content

Similar to RD Lab - Exp-10 - 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
 
Chemical Reaction Engineering Lab v3.0
Chemical Reaction Engineering Lab v3.0Chemical Reaction Engineering Lab v3.0
Chemical Reaction Engineering Lab v3.0
Michael Garibaldi
 
reactor design batch reactor
reactor design batch reactorreactor design batch reactor
reactor design batch reactor
DimaJawhar
 
Research Project Submission
Research Project SubmissionResearch Project Submission
Research Project Submission
Kelvin Obareti
 

Similar to RD Lab - Exp-10 - G-A1.pdf (20)

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
 
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
 
Chemical Reaction Engineering Lab v3.0
Chemical Reaction Engineering Lab v3.0Chemical Reaction Engineering Lab v3.0
Chemical Reaction Engineering Lab v3.0
 
Reactor Design 9
Reactor Design 9Reactor Design 9
Reactor Design 9
 
Lab cstr in series
Lab cstr in seriesLab cstr in series
Lab cstr in series
 
Thermo qbank2
Thermo qbank2Thermo qbank2
Thermo qbank2
 
reactor design batch reactor
reactor design batch reactorreactor design batch reactor
reactor design batch reactor
 
experiment Cstr 40l
experiment Cstr 40lexperiment Cstr 40l
experiment Cstr 40l
 
Space time and Space velocity, CSTR
Space time and Space velocity, CSTRSpace time and Space velocity, CSTR
Space time and Space velocity, CSTR
 
Auto catalytic reactions presentation
Auto catalytic reactions presentationAuto catalytic reactions presentation
Auto catalytic reactions presentation
 
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
 
Multiple reactors
Multiple reactorsMultiple reactors
Multiple reactors
 
Research Project Submission
Research Project SubmissionResearch Project Submission
Research Project Submission
 
Ammonia converter
Ammonia converterAmmonia converter
Ammonia converter
 
Rea 2.ppt
Rea 2.pptRea 2.ppt
Rea 2.ppt
 
investrigatory project in chemistry
investrigatory project in chemistryinvestrigatory project in chemistry
investrigatory project in chemistry
 
Auto catalytic reactions presentation
Auto catalytic reactions presentationAuto catalytic reactions presentation
Auto catalytic reactions presentation
 
Midterm review
Midterm reviewMidterm review
Midterm review
 

More from 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

UNIT-V FMM.HYDRAULIC TURBINE - Construction and working
UNIT-V FMM.HYDRAULIC TURBINE - Construction and workingUNIT-V FMM.HYDRAULIC TURBINE - Construction and working
UNIT-V FMM.HYDRAULIC TURBINE - Construction and working
rknatarajan
 
Call for Papers - Educational Administration: Theory and Practice, E-ISSN: 21...
Call for Papers - Educational Administration: Theory and Practice, E-ISSN: 21...Call for Papers - Educational Administration: Theory and Practice, E-ISSN: 21...
Call for Papers - Educational Administration: Theory and Practice, E-ISSN: 21...
Christo Ananth
 
result management system report for college project
result management system report for college projectresult management system report for college project
result management system report for college project
Tonystark477637
 

Recently uploaded (20)

The Most Attractive Pune Call Girls Manchar 8250192130 Will You Miss This Cha...
The Most Attractive Pune Call Girls Manchar 8250192130 Will You Miss This Cha...The Most Attractive Pune Call Girls Manchar 8250192130 Will You Miss This Cha...
The Most Attractive Pune Call Girls Manchar 8250192130 Will You Miss This Cha...
 
Top Rated Pune Call Girls Budhwar Peth ⟟ 6297143586 ⟟ Call Me For Genuine Se...
Top Rated  Pune Call Girls Budhwar Peth ⟟ 6297143586 ⟟ Call Me For Genuine Se...Top Rated  Pune Call Girls Budhwar Peth ⟟ 6297143586 ⟟ Call Me For Genuine Se...
Top Rated Pune Call Girls Budhwar Peth ⟟ 6297143586 ⟟ Call Me For Genuine Se...
 
UNIT-V FMM.HYDRAULIC TURBINE - Construction and working
UNIT-V FMM.HYDRAULIC TURBINE - Construction and workingUNIT-V FMM.HYDRAULIC TURBINE - Construction and working
UNIT-V FMM.HYDRAULIC TURBINE - Construction and working
 
Introduction to IEEE STANDARDS and its different types.pptx
Introduction to IEEE STANDARDS and its different types.pptxIntroduction to IEEE STANDARDS and its different types.pptx
Introduction to IEEE STANDARDS and its different types.pptx
 
Processing & Properties of Floor and Wall Tiles.pptx
Processing & Properties of Floor and Wall Tiles.pptxProcessing & Properties of Floor and Wall Tiles.pptx
Processing & Properties of Floor and Wall Tiles.pptx
 
High Profile Call Girls Nagpur Isha Call 7001035870 Meet With Nagpur Escorts
High Profile Call Girls Nagpur Isha Call 7001035870 Meet With Nagpur EscortsHigh Profile Call Girls Nagpur Isha Call 7001035870 Meet With Nagpur Escorts
High Profile Call Girls Nagpur Isha Call 7001035870 Meet With Nagpur Escorts
 
Call for Papers - Educational Administration: Theory and Practice, E-ISSN: 21...
Call for Papers - Educational Administration: Theory and Practice, E-ISSN: 21...Call for Papers - Educational Administration: Theory and Practice, E-ISSN: 21...
Call for Papers - Educational Administration: Theory and Practice, E-ISSN: 21...
 
Introduction and different types of Ethernet.pptx
Introduction and different types of Ethernet.pptxIntroduction and different types of Ethernet.pptx
Introduction and different types of Ethernet.pptx
 
KubeKraft presentation @CloudNativeHooghly
KubeKraft presentation @CloudNativeHooghlyKubeKraft presentation @CloudNativeHooghly
KubeKraft presentation @CloudNativeHooghly
 
Call Girls Pimpri Chinchwad Call Me 7737669865 Budget Friendly No Advance Boo...
Call Girls Pimpri Chinchwad Call Me 7737669865 Budget Friendly No Advance Boo...Call Girls Pimpri Chinchwad Call Me 7737669865 Budget Friendly No Advance Boo...
Call Girls Pimpri Chinchwad Call Me 7737669865 Budget Friendly No Advance Boo...
 
College Call Girls Nashik Nehal 7001305949 Independent Escort Service Nashik
College Call Girls Nashik Nehal 7001305949 Independent Escort Service NashikCollege Call Girls Nashik Nehal 7001305949 Independent Escort Service Nashik
College Call Girls Nashik Nehal 7001305949 Independent Escort Service Nashik
 
MANUFACTURING PROCESS-II UNIT-1 THEORY OF METAL CUTTING
MANUFACTURING PROCESS-II UNIT-1 THEORY OF METAL CUTTINGMANUFACTURING PROCESS-II UNIT-1 THEORY OF METAL CUTTING
MANUFACTURING PROCESS-II UNIT-1 THEORY OF METAL CUTTING
 
result management system report for college project
result management system report for college projectresult management system report for college project
result management system report for college project
 
Porous Ceramics seminar and technical writing
Porous Ceramics seminar and technical writingPorous Ceramics seminar and technical writing
Porous Ceramics seminar and technical writing
 
MANUFACTURING PROCESS-II UNIT-5 NC MACHINE TOOLS
MANUFACTURING PROCESS-II UNIT-5 NC MACHINE TOOLSMANUFACTURING PROCESS-II UNIT-5 NC MACHINE TOOLS
MANUFACTURING PROCESS-II UNIT-5 NC MACHINE TOOLS
 
Water Industry Process Automation & Control Monthly - April 2024
Water Industry Process Automation & Control Monthly - April 2024Water Industry Process Automation & Control Monthly - April 2024
Water Industry Process Automation & Control Monthly - April 2024
 
(ANVI) Koregaon Park Call Girls Just Call 7001035870 [ Cash on Delivery ] Pun...
(ANVI) Koregaon Park Call Girls Just Call 7001035870 [ Cash on Delivery ] Pun...(ANVI) Koregaon Park Call Girls Just Call 7001035870 [ Cash on Delivery ] Pun...
(ANVI) Koregaon Park Call Girls Just Call 7001035870 [ Cash on Delivery ] Pun...
 
BSides Seattle 2024 - Stopping Ethan Hunt From Taking Your Data.pptx
BSides Seattle 2024 - Stopping Ethan Hunt From Taking Your Data.pptxBSides Seattle 2024 - Stopping Ethan Hunt From Taking Your Data.pptx
BSides Seattle 2024 - Stopping Ethan Hunt From Taking Your Data.pptx
 
(INDIRA) Call Girl Aurangabad Call Now 8617697112 Aurangabad Escorts 24x7
(INDIRA) Call Girl Aurangabad Call Now 8617697112 Aurangabad Escorts 24x7(INDIRA) Call Girl Aurangabad Call Now 8617697112 Aurangabad Escorts 24x7
(INDIRA) Call Girl Aurangabad Call Now 8617697112 Aurangabad Escorts 24x7
 
Roadmap to Membership of RICS - Pathways and Routes
Roadmap to Membership of RICS - Pathways and RoutesRoadmap to Membership of RICS - Pathways and Routes
Roadmap to Membership of RICS - Pathways and Routes
 

RD Lab - Exp-10 - G-A1.pdf

  • 1. 1 Koya University Faculty of Engineering Chemical Engineering Department 3rd Stage (2021-2022) Reactor Laboratory Lab Report Number of Experiment: 10 Experiment Name: Plug Flow Reactor - Conversion Test (20 o C) Experiment Date: 16/02/2022 Submitted on: 23/02/2021 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. 2 1. Aim of Experiment ➢ Determine Conductivity. ➢ Find out conversion of Plug Flow Reactor (PFR) at 20 o C. 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. 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. 12. At the end of the experiment, turn off the pumps. 13. Turn off the power of control interface box. 14. Reactants should be removed from both (1 and 2) reactant bottle container. Then, the liquids must be kept for following test.
  • 3. 3 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. 4 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 Packaging are used for increase the surface area and it cause to fast the reaction or to make more collision number between reactants. 3. Temperature Sensor: it used for record temperature.
  • 5. 5 4. Calculation and Results We obtained conductivity value from recording by conductivity meter in lab. Concentration calculated by this equation: CA CAo = λ − λ∞ λo − λ∞ Conversion calculated by this equation: X = CAo − CA CAo Let’s calculate X: λo = 14.5 mS λ∞ = 2.5 µS = 0.0025 mS λ = 0.5 mS CAo = 0.05 M CA 0.05 = 0.5 − 0.0025 14.5 − 0.0025 CA 0.05 = 0.034316 CA = 0.0017158 M X = 0.05 − 0.0495 0.05 X = 0.965
  • 6. 6 As a result for this experiment and previous experiments here we make a table that shows us differences between quality or conversion rate (under the room temperature)in different types of the reactors, as following: Types of reactor Conversion Rate Batch Flow Reactor 0.996 Continuous Stirred Tank Reactor (CSTR) 0.880 CSTR in Series 0.890 Tubular Flow Reactor (TFR) 0.917 Laminar Flow Reactor (LFR) 0.999 Plug Flow Reactor (PFR) 0.965
  • 7. 7 5. Discussion Discussion – Safeen Yaseen Ja’far This Experiment about Plug Flow reactor or in short (PFR), estimate conductivity 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. In this experiment under room temperature of 20 o C we used NaOH and Ethyl Acetate (1L and 0.05 M). After the estimation of (λ) we need to find the CA by an equation and then we can find X by equation of the conversion. As we see in the result of our experiment and previous experiments there are different values of conversion rate means the conversion rate change by changing the reactor type. If we see the values, we learn that some reactor type better than some other reactor types, for example TFR or PFR better than CSTR means we can place the TFR or PFR instead of some CSTR reactors. However, we have some error in this experiment because maybe we don’t have exact conversion of the 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 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 the recent experiment the conversion shows that it varies each time with reactor changing, according to conversion table that Laminar Flow Reactor (LFR) with conversion of 0.999 is first place and in second place Batch
  • 8. 8 Flow Reactor with conversion of 0.996 and in third place Plug Flow Reactor (PFR) with conversion of 0.965. the conversion changes and a lot of things have impact on it for example the type of reaction, reactants, production rate and a lot more. Discussion – Ahmed Mamand Aziz Throughout this experiment is about Plug reactor (PFR), we were determined the conductivity & conversion at 20 oC, the solution of reactant was between {Sodium hydroxide and Ethyl acetate} in the reactant input tube. Each reactant prepared in 1 L contain of 0.05M. Read directly the value of conductivity- by-conductivity meter that is equal to 0.5mS and these values are given λ∞=0.0025mS, λo=14.5mS. Then we found conversion that is explained in calculation by the way we have already have a value of λ∞=0.0025mS and λo=14.5 and we found the value of λ in the experiment that is equal to 0.5mS and also, we have the value of CAo =0.05, then we could find the value of CA=0.34316. finally, by using the value of CA and CAo we were found conversion equal to (0.965). Also, about the difference between the reactant conversion that is required to compare between them, if we sort them from top to bottom, the first one is LFR that have the highest conversion rate between them, second one is batch reactor BR, third one is PFR, forth one is TFR, sixth one is CSTR in series, and last one is CSTR. 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 laminar flow
  • 9. 9 reactor and wait until they reach the reactor's peak, at which point we take a single reading because the reactor is already at steady state at 20C. Finally, we convert conductivity to concentration using the equation Ca/Ca0=λ0-λ/λ0-λ∞. During the previous experiment the conversion demonstrate that it changes each time with the reactor being changed. With the information that we got from the conversion table we can confirm that (LFR) laminar flow reactor is at first place with 0.999 conversion rate, while the batch flow reactor with conversion rate of 0.996 got the second place. The third place goes to Plug flow reactor with conversion of 0.965. 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 20 C and in the Plug Flow Reactor we have the catalyst inside the device this catalyst increase cross section area and increase conversion and in this experiment we t we have two reactant we use 0.05 M NaOH and 0.05 M of CH3COOHC2H5 to occur conversion and after a specific time we start to read the conductivity-by- conductivity meter. Also, during experiment we do in past by the different device we can focus in the rate of conversion occur during the experiment from different a device so we can note Laminar Flow Reactor (LFR) is the best device to occur conversion and after that Batch Flow Reactor after that Plug (Plug) Flow Reactor (PFR) and after that Tubular Flow Reactor (TFR) and after that Continuous Stirred Tank Reactor (CSTR) and finally CSTR in Series. Discussion – Rokan Mohammad
  • 10. 10 During this experiment we learn about the Plug reactor (PFR), at temperature (20 oC) and inertial concentration is (CAo)=0.05M and 1L for the (CH3COOC2H5 and NAOH). We calculated conductivity by conductivity meter, we read this value directly and equal to 0.5mS also, determined conversion (X) by using (conductivity and CA) so is equal to 0.965. First determine the concentration (CA) is equal to 0.34316 by using the values of conductivities λ= 2.8mS this is found in our experiment λ∞=0.0025, λo=14.5 and there are given for using to determining CA, following that by using CA and CAo could find the conversion. Also, if we rank them from top to bottom, the first one is LFR, which has the greatest conversion rate between them, the second one is batch reactor BR, third one is PFR, fourth one is TFR, sixth one is CSTR in series, and last one is CSTR.