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THEO EORE RETIC TICAL AND EX D EXPE PERI RIMENT ENTAL AL EX EXPL PLORA ORATION TION OF OF OR ORGAN ANIC IC SYNTHE THESIS SIS ROU OUTES ES TO OB O OBTAIN IN NATU TURAL RAL RUB UBBE BER R AN ANAL ALOG OGUE UES David


  1. THEO EORE RETIC TICAL AND EX D EXPE PERI RIMENT ENTAL AL EX EXPL PLORA ORATION TION OF OF OR ORGAN ANIC IC SYNTHE THESIS SIS ROU OUTES ES TO OB O OBTAIN IN NATU TURAL RAL RUB UBBE BER R AN ANAL ALOG OGUE UES David Mauric icio io Ramírez írez Sanchez ez Centro de Bioinformatica y Simulación Molecular, Universidad de Talca, Talca, Chile. Danilo ilo Gonzalez alez Forero Departamento de Química, Facultad de Ciencias, Universidad Nacional de Colombia, Bogotá, Colombia.

  2.  Introduction  Issue  Justification  Objetives  Framework  Methodology  Analysis and Results  Conclusions  Recommendations  References

  3. INTRODUCTION

  4. ISSUE National Industry requires synthetic compounds with a high molecular weight to replace natural rubber with its elasticity, resistency, softness and resilience properties among others. It has theoretical tools that are not normally used in the national industry when the predictability potential they have is not known. The use of these tools in leading countries, has encouraged the development of these new technologies and their application to this industry could prompt more lights on how to improve processes. In this work, the polymers synthesis processes are taken from dienes to obtain compounds similar to E-polyisoprene or natural rubber as a starting point for a theoretical study, using a semi- empirical calculation method and the theory of punctual groups applied to chemistry.

  5. JUSTIFICATION

  6. JUSTIFICATION

  7. OBJECTIVES  Genera neral To explore in a theoretical and experimental way, possible organic synthesis routes to obtain one or more compounds with analogous properties to natural rubber.  Specif ecific ic  Design of synthesis routes for different monomeric units involved in the polymer obtainment.  Theoretical determination of conditions to obtain the polymer(s) of interest.  Design of synthesis routes for the polymer(s) of interest.  Synthesis of polimer(s) of interest based on theoretical and computational studies previously carried out.

  8. FRAMEWORK  Natural Rubber  Used by ancient Mesoamerican Elastic castile

  9. FRAMEWORK Taken from International Rubber Study Group. Distribution of natural rubber global production in 2004 . F taken from http://www.rubberstudy.com/statistics-quarstat.aspx. Statistics summary of world rubber situation

  10. FRAMEWORK

  11. Synthe nthetic tic Rub ubber ber  C.Schonbein (1846) Nitrocellulose  A.Hofmann (1907) First synthetic rubber (Conjugated dienes)  World war two ID Increase of new polymers  Did not replace natural rubber completely  Radial tires, footwear, condoms Taken from International Rubber Study Group. . Distribution of natural rubber global production in 2004 . .

  12. Polimerization types Polyester  Condensation  Ionic  Anionic Poly(acrylonitrile)  Cationic Poly(isobutene)  Free Radicals Synthetic rubber

  13. Condensation H O H O H O - + + H O O H + O H O H O H - n H 2 O - + H O H 2 C O O O + H O H O H + H O O H H H H O + H H O + O + - O + O O - H 2 C O O O H - n H 2 O H O O O H O n

  14. Cationic F F - OH 2 + + H 2 O F B B F F F CH 3 CH 3 F + - OH + H H 2 C H 3 C C F F B - O + F B F CH 3 CH 3 F H CH 3 CH 3 CH 3 CH 3 CH 3 F F - OH + - OH + + H 2 C F B H 3 C C H 3 C C F B F F CH 3 CH 3 CH 3 CH 3 CH 3 n n-1 CH 3 CH 3 CH 3 CH 3 CH 3 CH 3 F F C + B - OH B - OH 2 H 3 C + + F H 3 C F H F CH 3 F CH 3 CH 3 CH 3 CH 2 n-1 H n-1 H

  15. Anionic N - N + K + K + NH 2 - - H 2 C N NH 3 H 2 N CH H 2 N N - H 2 N + CH K + + H 2 C N H 2 C N n + - K H 2 N CH N N N n H 2 N - H 2 N + CH H K + + NH 2 - + K N H N N N N H N N n n

  16. Polymerization Means  Emulsion SBR  Suspension Poly(Vinylacrylate)  Solution  “ Bulk ” Poly(methylmethacrylate)

  17. Emulsion  Virtualy occurs in nanoreactors (micelles)  Water (Non-polluting)  Good heat dissipater  Water Soluble Initiator  Slightly water soluble Monomers  Emulsificant  A colloidal dispersion of water polymer is produced.  There is not precipitation

  18. Solution  Low viscosity obtained solutions  Avoids interweaving  Low reaction rate and low molecular weight  The solvent acts as chain transfer agent  Easy polymer extraction  Precipitation may occur

  19. Suspension  Dispersed monomers by strong agitation  Both monomer and polymer are insoluble in dispersing medium  Polymerization occurs while dispersion  Soluble initiator (peroxides generally)  Aqueous phase  Heat exchange

  20. “ Bulk ”  Conversion of monomers in polymers by heat or radiation  Monomers: liquid, solid or gas  Do not use solvents or dispersing medium  It is not industrially important (small- scale)

  21. Radiopolymerization  Uses an ionizing radiation source  Induces free radicals when initiating polymerization Gamma radiation source 60 60 Co Co

  22. Photopolymerization  Used in dental medicine  Camphoroquinone (photoinitiator agent)

  23. Vul ulcanization canization  Treatment applied to rubber (natural and synthetic)  Generally with S, compounds with S or peroxides among others (based on its final usage)  Crosslinking creation Vulcanización

  24.  Computational Methods  Force Field  Semi-Empirical Methods  MNDO  AM1  PM3

  25. Force Field Energy  The electron energy is a parametric function of nuclear coordinates  Dynamic treatment is relized with classic mechanic tools.  Minimum energy in surface potential is sought translated in a more stable geometry.

  26. Semi-empirical methods  Decrease of computational cost  Use data obtained experimantally  It has into account only valence electrons  They are parameterized  MNDO ( Modiffed Neglect of Diatomic Overlap ) ( s, p(px, py, pz))  First model (aproximation of two integral electrons)  Problems with predictions  Hydrogen bridges  Low Δ H f reliability  AM1 (Austin Model 1) (S, P(px, py, pz))  Uses a modification of nuclear expresion  Description of hydrogene bridges  Aproximations overexploitation  Adds repulsion function  PM3 (Parametric Model 3) ( s, p(px, py, pz),/d)  Similar to AM1, but different parametrization  Better thermochemical properties prediction  Problems with  Studied molecule ≈ parametrized molecules, reliable results

  27. METHODOLOGY LITERATURE REVIEW PHAS ASE E ONE EXPERIMENTAL EXPLORATION TECHNICAL STUDY OF POSSIBLE SYNTHESIS ROUTES PHASE TWO WO DESIGN OF POSSIBLE SYNTHESIS ROUTES PHAS ASE E THREE EE EXPERIMENTAL TESTING OF SYNTHESIS ROUTES PHASE FOUR FINAL REPORT

  28. RESULTS AND ANALYSIS PHASE ONE  Obtainment of n-butene n-butanol H 2 SO 4 (98%) Heat H 2 SO 4 (98%) 175 ° C-180 ° C 175 °C - 180 °C Dropwise add n-butanol Collect in Frigorífic mixture According to Mezcla frígorifica [H 2 O (s) --NaCl] Diagram n-buteno

  29. O O H + CH 2 OH H OH + O S O H - +  OH O S +  O H H O H 3 C H 3 C H H 3 C O - O S OH O O CH 2 + H 3 C OH H O S  O Rection mechanism to dehidrate n-butanol

  30. PHASE TWO  Theoretical study of possible synthesis routes by semiempirical methods. Condensation.  Ionic  Cationic  Anionic  Free Radicals

  31.  Polimerization by free radicals • Iniciation O O O O O O 2

  32. • Propagation + CH 2 H 2 C O O O O CH 2 + O O CH 2 H 2 C O O CH CH 2 O CH CH 2 H 2 C + O O O n

  33. • Finalization CH 2 CH 2 + O O O O n n O O O O n O CH 2 O O O + O O O O n n

  34. Values of HOMO and LUMO orbitals Orbitales O O 27 28 N ° atomo Atomo HOMO LUMO 13 O O 12 12 C -0.00108 0.31809 25 26 3 13 O -0.01689 -0.10687 15 4 16 25 C 0.00037 0.08477 5 26 O 0.01835 -0.00781 20 17 2 0.06258 -0.07301 27 O 0.00466 -0.28112 19 18 6 28 O 7 14 O 8 radical oxidanilo (fenilcarbonil) Orbitales O 13 N° atomo Atomo HOMO LUMO 3 4 3 C -0.00012 -0.32957 8 C -0.00298 -0.59240 2 5 13 O 0.00258 0.27140 14 O -0.00389 0.42479 7 6 8 CH 2 estireno Orbitales 1,3-butadieno Orbitales N° atomo Atomo HOMO LUMO N° atomo Atomo HOMO LUMO 7 1 C -0.32554 -0.29831 1 C 0.55776 0.56016 1 2 C 0.45588 -0.46489 2 C 0.42639 -0.42306 6 4 2 2 CH 2 3 C 0.29950 0.30725 3 C -0.42713 -0.42420 1 4 C -0.19624 0.20270 4 C -0.55961 0.56195 H 2 C 3 5 3 5 C -0.45539 -0.47282 1,3-butadieno 4 6 C -0.18323 0.19400 estireno 7 C 0.30632 0.31038 8 C -0.47244 0.44930

  35.  Theoretical study of possible synthesis routes by groups theory  Polyestirene obtainment • Phenylcarbonyl radical obtainment from a thermical decomposition of benzoyl peroxide. • Radical 1-phenyl-2-oxi(phenylcarbonyl)]etilo obtainment from phenylcarbonyl radical and styrene. [Chain propagation]. • Polystyrene obtainment from two growing chains and, a growing chain and the phenylcarbonyl radical. [ending]

  36.  SBR obtainment  1,3-butadiene obtainment O O 1. SOCl 2 OH 2. EtOH O CH 3 EtOH H O H 3 C O H 3 O + Na,EtOH O O 2. H 3 O + 1.LiAlH 4 , eter Pirolisis OH H O  H 3 O + H 2 C Destilacion Petroleo CH 2 Pt, eter H 3 C CH 3

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