This lab report summarizes an experiment examining the impact of ethyl acetate flow rate on conversion in a plug flow reactor at 21°C. Students measured conductivity at four increasing flow rates and calculated conversion using conductivity readings. Results showed conversion decreased as flow rate increased, because higher flow rates gave reactants less time to fully react before exiting the reactor. The experiment helped students learn how conversion in a plug flow reactor is affected by changing an inlet flow rate.
Aim:
The aim of this experiment is to determine the conversion of our reactants by using conductivity meter in the reactor which the reaction takes place which is a CSTR reactor.
Introduction:
In our experiment a reaction takes place between two reactants in a CSTR reactor, first reactant is the strong base (NaOH) and second reactant is the weak Acid which is (CH3CO2CH2CH3) to produce (CH3COONa) and (CH3CH2OH) and water.
But since one of reactant is weak (CH3CO2CH2CH3) this means our reactants won't fully react and convert into our product which means we don't have a 100% conversion like we have between two strong reactants.
So, in order to find conversion, we have to divide the concentration of the reactants reacted by the concentration of the reactant in our reactor as the term of conversion suggests.
In order to find concentration, we use conductivity meter which measures the amount of free ions in our reactor.
This way can find conductivity to find concentration which gives us the key to find conversion.
4
Tools:
o CSTR reactor:
Our CSTR reactor is continuous and we add the reactants together continuously. Before the reactants run out, we read the (λ) ،And we read the (T) . Our reactor has a capacity of one liter ، and has a thermometer ، and has a vent valve.
5
o Conductivity meter:
Is a tool to measure the amount of free ions in a liquid or solution which uses a small amount of electricity to use how much ions will carry the charge.
6
o service unit:
Our service unit for this experience holds the both of the tanks of both reactants, and the pumps which is needed for each tank to the inlet of the reactor.
7
o Control unit:
For this experiment the control unit provides power and electricity to our reactor But not the conductivity meter because it works on its own.
o Tank:
The tank provide store service to our reactant before being added to our reactor, which is located in unit service.
8
o Pumps:
The pumps are our helpful tool which add our reactants to the reactor, which is located in unit service but is controlled in and turned on and off in control unit.
9
Procedure:
1.Temperature sensor Ts.4/on T=18: reaction Dane isothermally.
2. stirrer A A1 on
3. Flow rate: on both reactants should inter in The reactor at The same Flow rate Conversion is not Function of Flow rate in This experiment
4. vent valve: It is opened when the reactants. reach The level needs to be closed.
5. The level adjust into another tank over Flow draining it.
6. when continuously adjusting level occurred Conductivity is read when It becomes constant in The conductivity meter.
reactor design lab continuous stirred tank reactorDimaJawhar
Aim:
The aim of this experiment is to determine the conversion of our reactants by using conductivity meter in the reactor which the reaction takes place which is a CSTR reactor.
Introduction:
In our experiment a reaction takes place between two reactants in a CSTR reactor, first reactant is the strong base (NaOH) and second reactant is the weak Acid which is (CH3CO2CH2CH3) to produce (CH3COONa) and (CH3CH2OH) and water.
But since one of reactant is weak (CH3CO2CH2CH3) this means our reactants won't fully react and convert into our product which means we don't have a 100% conversion like we have between two strong reactants.
So, in order to find conversion, we have to divide the concentration of the reactants reacted by the concentration of the reactant in our reactor as the term of conversion suggests.
In order to find concentration, we use conductivity meter which measures the amount of free ions in our reactor.
This way can find conductivity to find concentration which gives us the key to find conversion.
4
Tools:
o CSTR reactor:
Our CSTR reactor is continuous and we add the reactants together continuously. Before the reactants run out, we read the (λ) ،And we read the (T) . Our reactor has a capacity of one liter ، and has a thermometer ، and has a vent valve.
5
o Conductivity meter:
Is a tool to measure the amount of free ions in a liquid or solution which uses a small amount of electricity to use how much ions will carry the charge.
6
o service unit:
Our service unit for this experience holds the both of the tanks of both reactants, and the pumps which is needed for each tank to the inlet of the reactor.
7
o Control unit:
For this experiment the control unit provides power and electricity to our reactor But not the conductivity meter because it works on its own.
o Tank:
The tank provide store service to our reactant before being added to our reactor, which is located in unit service.
8
o Pumps:
The pumps are our helpful tool which add our reactants to the reactor, which is located in unit service but is controlled in and turned on and off in control unit.
9
Procedure:
1.Temperature sensor Ts.4/on T=18: reaction Dane isothermally.
2. stirrer A A1 on
3. Flow rate: on both reactants should inter in The reactor at The same Flow rate Conversion is not Function of Flow rate in This experiment
4. vent valve: It is opened when the reactants. reach The level needs to be closed.
5. The level adjust into another tank over Flow draining it.
6. when continuously adjusting level occurred Conductivity is read when It becomes constant in The conductivity meter.
10
Calculation:
11
Discussion:
Sntia louay
Discussion:
What is a continuous stirred tank reactor?
(CSTR) is a type of chemical reactor that is widely used in industrial processes to produce chemicals, pharmaceuticals, and other products.
Is concentration constant in a CSTR?
The essential idea involved in the operation of a CSTR is that, after the passage of sufficient time, the concentrations of the
This presentation discusses the various uses of chemical kinetics involved in the unit processes involved in most of the industries these days. I have discussed all the basics and also included 4 examples with detailed description.
Effect of Operating Conditions on CSTR performance: an Experimental StudyIJERA Editor
In this work, Saponification reaction of ethyl acetate by sodium hydroxide is studied experimentally in a continuous stirred tank reactor at 1 atmospheric pressure. The aim of this study is to investigate the influence of operating conditions on the conversion and specific rate constant. The parameters considered for analysis are temperature, feed flow rate, residence time, volume of reactor and stirrer rate. The steady state conversion of 0.45 achieved after a period of 30 minutes. Conversion decreases with increase of reactant flow rate due to decrease of residence time. The stirrer rate has a positive effect on the conversion and rate constant. Specific rate constant and conversion increase with temperature within the studied temperature range. Within the range of reactor volume selected for analysis, conversion increases with increase in reactor volume. The results obtained in this study may be helpful in maximizing the conversion of ethyl acetate saponification reaction at industrial scale in a CSTR.
Aim:
The aim of this experiment is to determine the conversion of our reactants by using conductivity meter in the reactor which the reaction takes place which is a CSTR reactor.
Introduction:
In our experiment a reaction takes place between two reactants in a CSTR reactor, first reactant is the strong base (NaOH) and second reactant is the weak Acid which is (CH3CO2CH2CH3) to produce (CH3COONa) and (CH3CH2OH) and water.
But since one of reactant is weak (CH3CO2CH2CH3) this means our reactants won't fully react and convert into our product which means we don't have a 100% conversion like we have between two strong reactants.
So, in order to find conversion, we have to divide the concentration of the reactants reacted by the concentration of the reactant in our reactor as the term of conversion suggests.
In order to find concentration, we use conductivity meter which measures the amount of free ions in our reactor.
This way can find conductivity to find concentration which gives us the key to find conversion.
4
Tools:
o CSTR reactor:
Our CSTR reactor is continuous and we add the reactants together continuously. Before the reactants run out, we read the (λ) ،And we read the (T) . Our reactor has a capacity of one liter ، and has a thermometer ، and has a vent valve.
5
o Conductivity meter:
Is a tool to measure the amount of free ions in a liquid or solution which uses a small amount of electricity to use how much ions will carry the charge.
6
o service unit:
Our service unit for this experience holds the both of the tanks of both reactants, and the pumps which is needed for each tank to the inlet of the reactor.
7
o Control unit:
For this experiment the control unit provides power and electricity to our reactor But not the conductivity meter because it works on its own.
o Tank:
The tank provide store service to our reactant before being added to our reactor, which is located in unit service.
8
o Pumps:
The pumps are our helpful tool which add our reactants to the reactor, which is located in unit service but is controlled in and turned on and off in control unit.
9
Procedure:
1.Temperature sensor Ts.4/on T=18: reaction Dane isothermally.
2. stirrer A A1 on
3. Flow rate: on both reactants should inter in The reactor at The same Flow rate Conversion is not Function of Flow rate in This experiment
4. vent valve: It is opened when the reactants. reach The level needs to be closed.
5. The level adjust into another tank over Flow draining it.
6. when continuously adjusting level occurred Conductivity is read when It becomes constant in The conductivity meter.
reactor design lab continuous stirred tank reactorDimaJawhar
Aim:
The aim of this experiment is to determine the conversion of our reactants by using conductivity meter in the reactor which the reaction takes place which is a CSTR reactor.
Introduction:
In our experiment a reaction takes place between two reactants in a CSTR reactor, first reactant is the strong base (NaOH) and second reactant is the weak Acid which is (CH3CO2CH2CH3) to produce (CH3COONa) and (CH3CH2OH) and water.
But since one of reactant is weak (CH3CO2CH2CH3) this means our reactants won't fully react and convert into our product which means we don't have a 100% conversion like we have between two strong reactants.
So, in order to find conversion, we have to divide the concentration of the reactants reacted by the concentration of the reactant in our reactor as the term of conversion suggests.
In order to find concentration, we use conductivity meter which measures the amount of free ions in our reactor.
This way can find conductivity to find concentration which gives us the key to find conversion.
4
Tools:
o CSTR reactor:
Our CSTR reactor is continuous and we add the reactants together continuously. Before the reactants run out, we read the (λ) ،And we read the (T) . Our reactor has a capacity of one liter ، and has a thermometer ، and has a vent valve.
5
o Conductivity meter:
Is a tool to measure the amount of free ions in a liquid or solution which uses a small amount of electricity to use how much ions will carry the charge.
6
o service unit:
Our service unit for this experience holds the both of the tanks of both reactants, and the pumps which is needed for each tank to the inlet of the reactor.
7
o Control unit:
For this experiment the control unit provides power and electricity to our reactor But not the conductivity meter because it works on its own.
o Tank:
The tank provide store service to our reactant before being added to our reactor, which is located in unit service.
8
o Pumps:
The pumps are our helpful tool which add our reactants to the reactor, which is located in unit service but is controlled in and turned on and off in control unit.
9
Procedure:
1.Temperature sensor Ts.4/on T=18: reaction Dane isothermally.
2. stirrer A A1 on
3. Flow rate: on both reactants should inter in The reactor at The same Flow rate Conversion is not Function of Flow rate in This experiment
4. vent valve: It is opened when the reactants. reach The level needs to be closed.
5. The level adjust into another tank over Flow draining it.
6. when continuously adjusting level occurred Conductivity is read when It becomes constant in The conductivity meter.
10
Calculation:
11
Discussion:
Sntia louay
Discussion:
What is a continuous stirred tank reactor?
(CSTR) is a type of chemical reactor that is widely used in industrial processes to produce chemicals, pharmaceuticals, and other products.
Is concentration constant in a CSTR?
The essential idea involved in the operation of a CSTR is that, after the passage of sufficient time, the concentrations of the
This presentation discusses the various uses of chemical kinetics involved in the unit processes involved in most of the industries these days. I have discussed all the basics and also included 4 examples with detailed description.
Effect of Operating Conditions on CSTR performance: an Experimental StudyIJERA Editor
In this work, Saponification reaction of ethyl acetate by sodium hydroxide is studied experimentally in a continuous stirred tank reactor at 1 atmospheric pressure. The aim of this study is to investigate the influence of operating conditions on the conversion and specific rate constant. The parameters considered for analysis are temperature, feed flow rate, residence time, volume of reactor and stirrer rate. The steady state conversion of 0.45 achieved after a period of 30 minutes. Conversion decreases with increase of reactant flow rate due to decrease of residence time. The stirrer rate has a positive effect on the conversion and rate constant. Specific rate constant and conversion increase with temperature within the studied temperature range. Within the range of reactor volume selected for analysis, conversion increases with increase in reactor volume. The results obtained in this study may be helpful in maximizing the conversion of ethyl acetate saponification reaction at industrial scale in a CSTR.
Sachpazis:Terzaghi Bearing Capacity Estimation in simple terms with Calculati...Dr.Costas Sachpazis
Terzaghi's soil bearing capacity theory, developed by Karl Terzaghi, is a fundamental principle in geotechnical engineering used to determine the bearing capacity of shallow foundations. This theory provides a method to calculate the ultimate bearing capacity of soil, which is the maximum load per unit area that the soil can support without undergoing shear failure. The Calculation HTML Code included.
Hybrid optimization of pumped hydro system and solar- Engr. Abdul-Azeez.pdffxintegritypublishin
Advancements in technology unveil a myriad of electrical and electronic breakthroughs geared towards efficiently harnessing limited resources to meet human energy demands. The optimization of hybrid solar PV panels and pumped hydro energy supply systems plays a pivotal role in utilizing natural resources effectively. This initiative not only benefits humanity but also fosters environmental sustainability. The study investigated the design optimization of these hybrid systems, focusing on understanding solar radiation patterns, identifying geographical influences on solar radiation, formulating a mathematical model for system optimization, and determining the optimal configuration of PV panels and pumped hydro storage. Through a comparative analysis approach and eight weeks of data collection, the study addressed key research questions related to solar radiation patterns and optimal system design. The findings highlighted regions with heightened solar radiation levels, showcasing substantial potential for power generation and emphasizing the system's efficiency. Optimizing system design significantly boosted power generation, promoted renewable energy utilization, and enhanced energy storage capacity. The study underscored the benefits of optimizing hybrid solar PV panels and pumped hydro energy supply systems for sustainable energy usage. Optimizing the design of solar PV panels and pumped hydro energy supply systems as examined across diverse climatic conditions in a developing country, not only enhances power generation but also improves the integration of renewable energy sources and boosts energy storage capacities, particularly beneficial for less economically prosperous regions. Additionally, the study provides valuable insights for advancing energy research in economically viable areas. Recommendations included conducting site-specific assessments, utilizing advanced modeling tools, implementing regular maintenance protocols, and enhancing communication among system components.
About
Indigenized remote control interface card suitable for MAFI system CCR equipment. Compatible for IDM8000 CCR. Backplane mounted serial and TCP/Ethernet communication module for CCR remote access. IDM 8000 CCR remote control on serial and TCP protocol.
• Remote control: Parallel or serial interface.
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• Remote control system for accessing CCR and allied system over serial or TCP.
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Technical Specifications
Indigenized remote control interface card suitable for MAFI system CCR equipment. Compatible for IDM8000 CCR. Backplane mounted serial and TCP/Ethernet communication module for CCR remote access. IDM 8000 CCR remote control on serial and TCP protocol.
Key Features
Indigenized remote control interface card suitable for MAFI system CCR equipment. Compatible for IDM8000 CCR. Backplane mounted serial and TCP/Ethernet communication module for CCR remote access. IDM 8000 CCR remote control on serial and TCP protocol.
• Remote control: Parallel or serial interface
• Compatible with MAFI CCR system
• Copatiable with IDM8000 CCR
• Compatible with Backplane mount serial communication.
• Compatible with commercial and Defence aviation CCR system.
• Remote control system for accessing CCR and allied system over serial or TCP.
• Indigenized local Support/presence in India.
Application
• Remote control: Parallel or serial interface.
• Compatible with MAFI CCR system.
• Compatible with IDM8000 CCR.
• Compatible with Backplane mount serial communication.
• Compatible with commercial and Defence aviation CCR system.
• Remote control system for accessing CCR and allied system over serial or TCP.
• Indigenized local Support/presence in India.
• Easy in configuration using DIP switches.
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Final project report on grocery store management system..pdfKamal Acharya
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This document will discuss each of the underlying technologies to create and implement an e- commerce website.
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It is always satisfying when we can help solve complex challenges like this. Do your systems also need a check-up or optimization? Give us a call!
Work done in cooperation with James Malloy and David Moelling from Tetra Engineering.
More examples of our work https://www.r-r-consult.dk/en/cases-en/
Overview of the fundamental roles in Hydropower generation and the components involved in wider Electrical Engineering.
This paper presents the design and construction of hydroelectric dams from the hydrologist’s survey of the valley before construction, all aspects and involved disciplines, fluid dynamics, structural engineering, generation and mains frequency regulation to the very transmission of power through the network in the United Kingdom.
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Collaborators and co editors: Charlie Sims and Connor Healey.
(C) 2024 Robbie E. Sayers
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The automated cosmetic shop management system should deal with the automation of general workflow and administration process of the shop. The main processes of the system focus on customer's request where the system is able to search the most appropriate products and deliver it to the customers. It should help the employees to quickly identify the list of cosmetic product that have reached the minimum quantity and also keep a track of expired date for each cosmetic product. It should help the employees to find the rack number in which the product is placed.It is also Faster and more efficient way.
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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.