PRODUCTION OF PHENOL AND ACETONE BY CUMENE PEROXIDATION PROCESS REFERENCES: EQUATIONS USED [A] – Eq. 41 Pg. 394 from
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PRODUCTION OF PHENOL AND ACETONE BY CUMENE PEROXIDATION PROCESS
REFERENCES: EQUATIONS USED
[A] – Eq. 41 Pg. 394 from Levenspiel O. Chemical Reaction Engineering 3rd Edition. (). John Wiley and Sons [B] - Eqn. 6.2 Pg. 182 from Alkylation of Benzene by Propylene to Cumene [C] – Eqn. 6.5 Pg. 182 from Alkylation of Benzene by Propylene to Cumene [D] – Eqn. 12.3b Pg. 648 from R.K Sinnott, Chemical Engineering Design Vol. 6. (2005).Elsevier ButterworthHeinemann. Oxford [E] – Pg. 676 from R.K Sinnott, Chemical Engineering Design Vol. 6. (2005).Elsevier ButterworthHeinemann. Oxford [F] – http://www.eng-tips.com/viewthread.cfm?qid=69206 [G] – http://enggyd.blogspot.com/2010/07/shell-and-tube-reactor-design.html [H] – Pg. 675 from R.K Sinnott, Chemical Engineering Design Vol. 6. (2005).Elsevier ButterworthHeinemann. Oxford [I] – Eqn. 12.21 Pg. 672 from R.K Sinnott, Chemical Engineering Design Vol. 6. (2005).Elsevier ButterworthHeinemann. Oxford [J] – Eqn. 12.22 Pg. 672 from R.K Sinnott, Chemical Engineering Design Vol. 6. (2005).Elsevier ButterworthHeinemann. Oxford [K] – Eqn. 12.25 Pg. 675 from R.K Sinnott, Chemical Engineering Design Vol. 6. (2005).Elsevier ButterworthHeinemann. Oxford [L] – Eqn. 12.20 Pg. 635 from R.K Sinnott, Chemical Engineering Design Vol. 6. (2005).Elsevier ButterworthHeinemann. Oxford [M] – Eqn. 4.9-5 Pg. 271 from Geankoplis et.al. Transport Processes and Unit Operation 3rd Edition. (1993). Prentice Hall Inc. New Jersey [N] - Eqn. 11.89 Pg. 577 from Gerhart E, Fixed Bed Reactors. Institit fur Chemische Verfahrenstechnik, University of Stuttgart. Germany [O] – Eqn. 12.26 Pg. 675 from R.K Sinnott, Chemical Engineering Design Vol. 6. (2005).Elsevier ButterworthHeinemann. Oxford [P] – Eqn. 13.43 Pg. 819 from R.K Sinnott, Chemical Engineering Design Vol. 6. (2005).Elsevier ButterworthHeinemann. Oxford [Q] – Eqn. 13.39a Pg. 815 from R.K Sinnott, Chemical Engineering Design Vol. 6. (2005).Elsevier Butterworth- Heinemann. Oxford
EQUIPMENT DESIGN
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PRODUCTION OF PHENOL AND ACETONE BY CUMENE PEROXIDATION PROCESS
[R] – Pg. 19 from NPTEL – Chemical Engineering – Chemical Engineering Design II: Module No. 2
REFERENCES FOR VALUES USED
[1], [2] – Pg. 110 from Chauvel A. et al Petrochemical Processes: Technical and Economic Characteristics (1989).Editions Technip. Paris [3] – Pg. 182 from Alkylation of Benzene by Propylene to Cumene [4] – Pg. 185 from Alkylation of Benzene by Propylene to Cumene [5] – Gathered using DWSIM: NRTL Thermodynamic Package (For Liquids); Peng-Robinson Thermodynamic Package (For Gases); Steam-Tables Thermodynamic Package (For water); Nested Loops Flash Algorithm [6] – Table 6.7 Pg. 185 from Alkylation of Benzene by Propylene to Cumene
[7] – Pg. 213 from Gerhart E, Fixed Bed Reactors. Institit fur Chemische Verfahrenstechnik, University of Stuttgart. Germany [8] – Table 12.3 Pg. 645 from R.K Sinnott, Chemical Engineering Design Vol. 6. (2005).Elsevier ButterworthHeinemann. Oxford
[9] – Table 12.4 Pg. 649 from R.K Sinnott, Chemical Engineering Design Vol. 6. (2005).Elsevier ButterworthHeinemann. Oxford
EQUIPMENT DESIGN
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PRODUCTION OF PHENOL AND ACETONE BY CUMENE PEROXIDATION PROCESS
[10] – Fig. 12.9 Pg. 646 from R.K Sinnott, Chemical Engineering Design Vol. 6. (2005).Elsevier ButterworthHeinemann. Oxford
[11] – Pg. 7 from NPTEL – Chemical Engineering – Chemical Engineering Design II: Module No. 2 [12] – Pg. 652 from R.K Sinnott, Chemical Engineering Design Vol. 6. (2005).Elsevier ButterworthHeinemann. Oxford
EQUIPMENT DESIGN
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PRODUCTION OF PHENOL AND ACETONE BY CUMENE PEROXIDATION PROCESS
[13] – Fig. 12.29 Pg. 673 from R.K Sinnott, Chemical Engineering Design Vol. 6. (2005).Elsevier ButterworthHeinemann. Oxford
[14] – Fig. 12.29 Pg. 673 from R.K Sinnott, Chemical Engineering Design Vol. 6. (2005).Elsevier ButterworthHeinemann. Oxford [15] – Table. 12.6 Pg. 662 from R.K Sinnott, Chemical Engineering Design Vol. 6. (2005).Elsevier Butterworth- Heinemann. Oxford
EQUIPMENT DESIGN
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PRODUCTION OF PHENOL AND ACETONE BY CUMENE PEROXIDATION PROCESS
[16] – Pg. 652 from R.K Sinnott, Chemical Engineering Design Vol. 6. (2005).Elsevier ButterworthHeinemann. Oxford [17] – Table 12.30 Pg. 674 from R.K Sinnott, Chemical Engineering Design Vol. 6. (2005).Elsevier Butterworth- Heinemann. Oxford
[18] – Table 13.20 Pg. 812 from R.K Sinnott, Chemical Engineering Design Vol. 6. (2005).Elsevier Butterworth- Heinemann. Oxford
EQUIPMENT DESIGN
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PRODUCTION OF PHENOL AND ACETONE BY CUMENE PEROXIDATION PROCESS
[19] – Corrosion Allowance; Pressure Vessel Handout.pdf
[20] – Pg. 233 from Datta A., Process Engineering and Design using Visual Basic. (2008). CRC Press. United States Of America.
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