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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 ??