sap on present
TRANSCRIPT
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Rate Constant Determination for
Saponification in Batch & CSTR
February 17, 2005
Presentation by Trevor Binney
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Group Members
Jay Berndt Me Eric Houchin
Operations Manager Team Leader Safety Coordinator
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Nomenclature
CSTR- Continuous Stirred Tank Reactor
EtAc- Ethyl Acetate
NaAc- Sodium Acetate
EtOH- Ethyl Alcohol (Ethanol) PPE- Personal Protective Equipment
Soln- Solution
Xa- Extent of Reaction of NaOH Conc- Concentration in mol/L
Ca- mol/L NaOH
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What is Saponification,and what is it used for?
http://www.dictionary.com/defines saponificationas: A reaction in which an ester is heated withan alkali, such as sodium hydroxide, producing a
free alcohol and an acid salt, especially alkalinehydrolysis of a fat or oil to make soap.
EtAc + NaOH NaAc + EtOH
CH3COOC2H5 + NaOH
CH3COONa + C2H5OH Saponification is primarily used for the
production of soaps.
http://www.dictionary.com/http://www.dictionary.com/ -
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Project Objectives
Our team was asked to meet several goalswhile running saponification experiments
1. Develop conductivity calibration curves for thereactants used in the process. (NaOH & EtAc)
2. Verify feed concentration throughstandardization using titration
3. Determine the true rate constant for reaction ina batch reactor
4. Obtain reaction rate data for the CSTR as afunction of the solution residence time
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Safety Considerations
NaOH- Corrosive
EtOH & EtAc- Flammable
EtAc will corrode various plastics
Standard PPE worn, as well as face shield andrubber gloves for handling dangerous chemicals.
Clean up spills and broken glass immediately
Be aware of where other people in the lab are Open windows for ventilation and work under
the fume hood when mixing solutions
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Assumptions
Conductivities EtAc & EtOH negligible
Solution inside the CSTR is well mixed
Solution inside batch reactor well mixed Ethyl acetate bottle wasnt contaminated
Liquid pulled from the 1 M EtAc is 1 M
The CTSR flow meters were accurate Conductivity linearly proportional to Conc
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Conductivity Probe Calibration
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Conductivity Probe Calibration
NaOH Conductivity vs Concentration
y = 214.03x
0
10
20
30
40
50
60
0 0.05 0.1 0.15 0.2 0.25 0.3
Molarity NaOH
Conductivity(mho
)
Literature Data
Calibration
Linear (LiteratureData)
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Continuous Stirred Tank Reactor
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CSTR procedure
1. Enter setpoint temperatures using set point 2
2. Drain reactant tanks as much as possible
3. Prepare three liters of reactant solutions
4. Fill tanks equally and heat to set temp5. Make sure the bottom reactor drain is closed
6. Turn on the CSTR stirring device
7. Open the flow valves to equal levels8. Wait until SS reached and record conductivityusing a calibrated conductivity probe
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Batch Reactor and Heating Bath
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Batch Procedure
1. Preheat bath to desired reaction temp
2. Prepare the NaOH and ethyl acetate solutions
3. Fill two erlenmeyer flasks, one with NaOH and
the other with EtAc
4. Allow reactants to heat to desired temp
5. Pour one flask into the other submerged flask
6. Using the conductivity probe, recordconductivities of the solution every 15 seconds
7. Record data until the conductivity stabilizes
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Equations Used for Data Analysis
Arrhenius law: k = k0e-E/RT
ln(k2/k1)=E/R*(1/T1 1/T2)
Ca0*(214-136*Xa)
Xa = (Ca0 Ca)/Ca0 Ca = (Cond/Ca0 214)*Ca0/136 + Ca0
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Results and Conclusions
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Results and Conclusions
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Results and Conclusions
(k) Determined rate constant for saponification
Experimental k = 0.178 L/mol*sec @ 30 C
Experimental k = 0.192 L/mol*sec @ 45 C
As listed in in the Bulletin of the ChemicalSociety of Japan k = 0.112 L/mol*sec
According to this source, the rate constant wedetermined was about 59% too large
A possible reason for this is that the EtAc solutionconcentration was higher than predicted
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CSTR Results and Conclusions
Data recorded was very inconsistent
For equal feed concentrations, we had runsthat yielded conductivities of 6-7 mS and also
3 mS/m, with no results falling in between Reagent bottle contamination?
Inability to completely drain feed tanks
Difficulty in maintaining stirring speed
CSTR operations were abandoned for thefinal lab period to focus on Batch data
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Temperature Dependence Results
Multiple trials were run at both 30 & 45 C
Arrhenius law: k = k0e-E/RT
Rewritten: ln(k2/k1)=E/R*(1/T1 1/T2) R = 8.314 J/mol*K
E = Activation energy of this reaction
We were unable to find the value for E in literaturek30 = 0.178 L/mol*sec < k45 =0.192 L/mol*sec
Experimental E = 4040 J/mol
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Overall Conclusions
Saponification rxn is a 2nd order reversible reaction
(1/Ca vs time linear at low time)
-Ra = k*Ca*Cb
Considerable error comparing experimentalrate constant to that in literature
Batch data fairly reproducible and precise
CSTR data and operation inconsistent
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Difficulties Encountered During Lab
Creation and mixing of ethyl acetate solns
Attempted creation of 1 M stock solution
Attempted to dissolve 9.6 g EtAc/100 mL
Max Solubility of EtAc in water is 8 g/100 mL
Possible reagent bottle contamination
Evident through formation of unknown precipitate
CSTR temperature reading inconsistency Inability to completely drain CSTR tanks
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Recommendations For Future Work
Do research before entering the lab
Become familiar with analytical equipment
Begin trials with CSTR as early as
possible
Split up tasks for each person to do duringlab prior to running the labs
Make an in depth Design of Experimentbefore entering the lab
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References
Levenspiel, Octave. Chemical ReactionEngineering, Third Edition. USA: John Wiley &Sons, 1999.
Levenspiel, Octave. The Chemical Reactor
Omnibook. Corvallis, OR: OSU Book Stores, 2002. Pecaj, Arta. Personal Interview. February 16, 2005.
Tsujikawa, H. and Inoue, H. 1965. The Rate of theAlkaline Hydrolysis of Ethyl Acetate. Bulletin of the
Chemical Society of Japan. 39: 1837-1839 http://www.woodlandsinstruments.com/conductivity_
values.htm
http://www.woodlandsinstruments.com/conductivity_values.htmhttp://www.woodlandsinstruments.com/conductivity_values.htmhttp://www.woodlandsinstruments.com/conductivity_values.htmhttp://www.woodlandsinstruments.com/conductivity_values.htm -
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Questions ??