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International Journal of Technology Enhancements and Emerging Engineering Research

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IJTEEE >> Volume 2 - Issue 9, September 2014 Edition



International Journal of Technology Enhancements and Emerging Engineering Research  
International Journal of Technology Enhancements and Emerging Engineering Research

Website: http://www.ijteee.org

ISSN 2347-4289



Modelling Of Non-Isothermal Plug Flow Reactor Adsorption Tower For Sulpur Trioxide Hydration Using Vanadium Catalyst

[Full Text]

 

AUTHOR(S)

Goodhead T.O, Abowei M.F.N

 

KEYWORDS

Keywords : Sulphur , Vanadium Catalyst, Modelling , Plug Flow Reactor

 

ABSTRACT

ABSTRACT: An isothermal plug flow reactor for the production of sulphuric acid over a range of degree of conversion, XA = 0.95 to 0.99 and reactor diameter, Di = 0.05 to 0.1m have been designed. The reactor which operates at atmospheric pressure is capable of producing 10,000 metric tons per annum. This reactor is designed with hastelloy because it possesses an excellent corrosion and sulphuric acid resistance properties. The reactor performance models are simulated with the aid of a Computer using MATLAB (R2007b).The results provided information for the functional parameters for the reactor which include; the reactor volume, space time, space velocity, rate of heat generation per unit volume of reactor, pressure drop, and length of reactor. The relationship between these parameters and the degree of conversion are presented graphically.

 

REFERENCES

[1] Chenier, P. J. (1987), Survey of industrial chemistry, John Wiley & Sons, New York, pp45-47.

[2] Green Wood, N. W., and Earnshaw, A. (1984). Che-mistry of the Elements pp. 837-845 Pergamon Press, Oxford UK.

[3] Charles G. Hill, jr (1977), An Introduction to chemi-cal engineering Kinetics & Reactor design, 1st edition, John Wiley & Sons USA, pp5-16, pp509-523.

[4] Faith, K. C. (1965), Industrial Chemistry, Third edi-tion pp. 747 -755, John Wiley 8 Sons New York.

[5] Abowei, M. F.N. (1989). Computer-aided design of heat exchanger for P.F. reactor in the addition of ethylene oxide. Part 1: Design equation development. Modeling, simulation and control, B. AMSE press, vol. 25, no. 4, pp. 15-24.

[6] Goodhead, T. O; Dagde, K. K.,(2011) Adsorption of Acetic Acid, Cadmmium ions, Lead ions and Iodine Using Activated Carbon from Waste Wood and Rice Husks, ‘’Journal of Applied Sciences and Environmental Management, 15 (2) 407-411’’

[7] Goodhead, T. O; Dagde, K. K.(2011) Potentials of Caustic Potash (KOH) Production From Cocoa Pod Husk,’’Journal of the Nigerian Society of Chemical Engineers, 27: 2, 86-96’’.

[8] Duecker and West (1975), Manufacture of Sulphuric acid, Reinhold, New York.

[9] Internet: Sulhuric acid-Wikipedia, free Encyclopedia http://en.wikipedia. Org/wiki/sulphuric acid.

[10] Austin, G. T. (1984), Shreve’s Chemical process in-dustrial. Fifth edition, publisher McGraw-Hill, pp370-345.
[11] Gibney, S. C., and Ferracid, G. (1994) Photocata-lysed Oxidation, Journal of Horganic Chemistry, Vol. 37, pp. 6120-6124.

[12] Goodhead, T. O; Ozubu, O. I., (2012) Design of a Feed Preheater for the fluid catalytic Cracking unit,’’Journal of Nigerian Society of the Chemical Engineers, 27: 130-42’’.

[13] Erikson, T. E. (1974), Chem Soc, Faraday Trans. I, 70, 203.

[14] Huie, R.E. and Neta. P.J. (1985), Phys Chem. 89, 3918.

[15] Marokuma, k., Mugurama, C.J. Am. Chem Soc. 1994, 116,10316.

[16] Fogler, H. S. (1994) Elements of Chemical Reaction Engineering. 2nd edition Prentice-Hall Inc., India.

[17] Forment, G. F. Modeling of Catalyst Deactivation, Applied Cataly sis A: General, 211 (1.2): pp. 117 – 128, 2001.

[18] Levenspeil Octave (1999), Chemical Reaction Engi-neering, 3rd Ed tion, John Wiley & Sons USA, pp55-80

[19] Coulson, J. M., Richardson, J. F. (1978), Chemical Engineering, vol.2, 3rd Edition, Pergamon press Inc., New York, pp.529-530, 547-550.

[20] Coulson J. M., Richardson J. F. “Chemical Engineering” Vol. 3, 2nd Edition, Pergramon Press Inc. New York (1979). Pp. 3 -10, 36 -42.

[21] Goodhead, T. O; Digitemie, M. T., (2012) Design of a fixed bed plug flow reactor for Ammonia synthesis. ‘’Journal of current Engineering and Applied science, 3: 1’’.

[22] Fair, G. M. Geyer, J.C.; and Oken D.A. (1968): Water Purification and waste water treatment, and disposal, volume 2. Water and waste water Engineering, New York Wiley.

[23] Goodhead, T. O; Abo, F. A., (2012) Design of a packed bed reactor for the production of Vinyl chloride monomer. ‘’African journal of engineering, 5: 8 207-226’’.

[24] Dewachtere, N.V., Santaella, F., Froment, G. F., Application of a single event kinetic Model in the simulation of an industrial Riser Reactor for the Catalytic Cracking of Vacuum Gas Oil, Chemical Engineering Science, 54: pp. 3653-3660,1999.

[25] Ancheya – Juarez, J. C., A. Strategy for Kinetic Parameter Estimation in the Fluid Catalytic Cracking Process, Ind. Eng. Chem. Res., 36 (12): pp 5170- 5174, 1997.


[26] Blanding, F. H., Reaction Rates in Catalytic Cracking of Petroleum, Industrial and Engineering Chemistry, 45 (6) pp 1186-1197, 1953.

[27] Charles G. Hill, jr (1977), An Introduction to chemical engineering Kinetics & Reactor design, 1st edition, John Wiley & Sons USA, pp5-16, pp509-523.

[28] Geankoplis, Tansport Processes and unit Opera-tions, 3rd Editions Prentice hall, Englewood Cliffs, N. J. 1993.

[29] Corma, A., Melo, F. V., Sauvanaud, L., Kinetic and Decay Cracking Model for a Micordowner unit, Ap-plied Catalysis A: General, 287 (1): pp 34 -36, 2005.

[30] Bird, Stewart, and Lightfoot, Transport Phenomena, Wiley, NY (1960). Calderbank, P. H., (1953) Chem. Eng. Prog. 49(585).

[31] Dagde, K. K., Akpa, J. G., Puyate, Y. T., Oboho, E. O., Five – Lump Kinetic Model for Fluid Catalytic Cracking of Gas-Oil in a Fluidized bed Reactor, Journal of the Nigerian Society of Chemical Engineers pp. 1- 19, 2009.

[32] Dagde, Kenneth Kekpugile, Goodhead ThankGod Oweifa (2013) Analysis of Mass Transfer During Mi-crowave drying of Yam Slabs, “American Journal of Engineering Research (AJER), 11.2, 61-70”.

[33] Christenson, G., Apelian, M. R., Hickey, K. J., Jaffe, S. B., Future Directions in Modeling of the FCC Process: An Emphasis on Product Quality, Chemical Engineering Science, 54:pp. 2753-2764, 1999.

[34] Danner and Daubert, Manual for predicting Chemical Process design data, Alche, New York, 1983.

[35] Dupain, x. Gfamas, E. D., Madon. R., Kelkar, C. P., Makkee, M., Moulijn, J. A., Aromatic Gas Oil Cracking under realistic FCC conditions in a Microriser Reactor, Fuel, 82: pp 1559-1569, 2003.

[36] Foust, A.S., et al, Principles of Unit Operations, 1st Edition, John Wiley & Sons Inc. Pennsylvania, (1960) pp. 223-225.

[37] Goodhead, T. O; Nkwo, F. C., (2012) Design of an isothermal packed bed reactor for the Production of acrylonitrile. ‘’African journal of Engineering, 5: 8 99-116’’.

[38] Goodhead, T. O; Abia, U. A., (2012) The influence of conductive heat transfer on Structural integrity of flat horizontal metal plate. ‘’Journal of current Engineering And Applied science, 3 1’’.