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1. Rate Constant Determination for Saponification in Batch & CSTR February 17, 2005
Presentation by Trevor Binney
2. Group Members Jay Berndt Me Eric Houchin
Operations Manager Team Leader Safety Coordinator
3. Presentation Plan Familiarize audience with saponification
Discuss the project objectives
Overview of process and equipment used
Batch and CSTR kinetic data results
Difficulties encountered during lab work
Give recommendations for future work
Answer any questions the audience have
4. 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
5. What is Saponification,and what is it used for? http://www.dictionary.com/ defines saponification as: A reaction in which an ester is heated with an alkali, such as sodium hydroxide, producing a free alcohol and an acid salt, especially alkaline hydrolysis 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.
6. Project Objectives Our team was asked to meet several goals while running saponification experiments
Develop conductivity calibration curves for the reactants used in the process. (NaOH & EtAc)
Verify feed concentration through standardization using titration
Determine the true rate constant for reaction in a batch reactor
Obtain reaction rate data for the CSTR as a function of the solution residence time
7. Safety Considerations NaOH- Corrosive
EtOH & EtAc- Flammable
EtAc will corrode various plastics
Standard PPE worn, as well as face shield and rubber 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
8. 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
9. Conductivity Probe Calibration
10. Conductivity Probe Calibration
11. Xa & Conc Solved w/ Conductivity NaOH conductivity: 214*(conc NaOH) mS/m
NaAc conductivity: 78*(conc NaAc) mS/m
EtAc & EtOH conductivity: negligible
Overall conductivity: Ca0*(214-136*Xa)
Where Xa = (Ca0 Ca) / Ca0
12. Continuous Stirred Tank Reactor
13. CSTR procedure Enter setpoint temperatures using set point 2
Drain reactant tanks as much as possible
Prepare three liters of reactant solutions
Fill tanks equally and heat to set temp
Make sure the bottom reactor drain is closed
Turn on the CSTR stirring device
Open the flow valves to equal levels
Wait until SS reached and record conductivity using a calibrated conductivity probe
14. Batch Reactor and Heating Bath
15. Batch Procedure Preheat bath to desired reaction temp
Prepare the NaOH and ethyl acetate solutions
Fill two erlenmeyer flasks, one with NaOH and the other with EtAc
Allow reactants to heat to desired temp
Pour one flask into the other submerged flask
Using the conductivity probe, record conductivities of the solution every 15 seconds
Record data until the conductivity stabilizes
16. 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
17. Results and Conclusions
18. Results and Conclusions
19. 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 Chemical Society of Japan k = 0.112 L/mol*sec
According to this source, the rate constant we determined was about 59% too large
A possible reason for this is that the EtAc solution concentration was higher than predicted
20. CSTR Results and Conclusions Data recorded was very inconsistent
For equal feed concentrations, we had runs that 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 the final lab period to focus on Batch data
21. 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 literature
k30 = 0.178 L/mol*sec < k45 =0.192 L/mol*sec
Experimental E = 4040 J/mol
22. 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 experimental rate constant to that in literature
Batch data fairly reproducible and precise
CSTR data and operation inconsistent
23. 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
24. 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 during lab prior to running the labs
Make an in depth Design of Experiment before entering the lab
25. References Levenspiel, Octave. Chemical Reaction Engineering, 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 the Alkaline Hydrolysis of Ethyl Acetate. Bulletin of the Chemical Society of Japan. 39: 1837-1839
http://www.woodlandsinstruments.com/conductivity_values.htm
26. Questions ??