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Desulfurization of coal by oxidation in alkaline solution PDF

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Iowa State University Capstones, Theses and Retrospective Theses and Dissertations Dissertations 1979 Desulfurization of coal by oxidation in alkaline solution Kang-Chun Chuang Iowa State University Follow this and additional works at:https://lib.dr.iastate.edu/rtd Part of theChemical Engineering Commons, and theOil, Gas, and Energy Commons Recommended Citation Chuang, Kang-Chun, "Desulfurization of coal by oxidation in alkaline solution " (1979).Retrospective Theses and Dissertations. 7272. https://lib.dr.iastate.edu/rtd/7272 This Dissertation is brought to you for free and open access by the Iowa State University Capstones, Theses and Dissertations at Iowa State University Digital Repository. It has been accepted for inclusion in Retrospective Theses and Dissertations by an authorized administrator of Iowa State University Digital Repository. For more information, please [email protected]. INFORMATION TO USERS This was produced from a copy of a document sent to us for microfilming. 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ZEEB ROAD, ANN ARBOR, Ml 48106 18 BEDFORD ROW, LONDON WCIR 4EJ, ENGLAND 8010223 CHUANG, KANG-CHUN DESULFURIZATION OF COAL BY OXIDATION IN ALKALINE SOLUTION Iowa State University PH.D. 1979 University Microfilms In tGr n Qti 0 n & I 300 N. Zeeb Road, Ann Arbor, Ml 48106 18 Bedford Row, London WCIR 4EJ, England PLEASE NOTE; In all cases this material has been filmed in the best possible way from the available copy. Problems encountered with this document have been identified here with a check mark . 1. Glossy photographs [/ 2. Colored illustrations 3. Photographs with dark background 4. Illustrations are poor copy 5. °rint shows through as there is text on both sides of page 6. Indistinct, broken or small print on several pages throughout 7. Tightly bound copy with print lost in spine 8. Computer printout pages with indistinct print 9. Page(s) lacking when material received, and not available from school or author 10. Page(s) seem to be missing in numbering only as text follows 11. Poor carbon copy 12. Not original copy, several pages with blurred type 13. Appendix pages are poor copy 14. Original copy with light type 15. Curling and wrinkled pages 16. Other UniversiN Micrœlnis International 300 N Z:5= RD. ANN AHBOfi Ml JSl06'3131 761-4700 Desulfurization of coal by oxidation in alkaline solution by Kang-Chun Chuang A Dissertation Submitted to the Graduate Faculty in Partial Fulfillment of the Requirements for the Degree of DOCTOR OF PHILOSOPHY Major: Chemical Engineering Approved: Signature was redacted for privacy. In Charge of Major Work Signature was redacted for privacy. For the Major Department Signature was redacted for privacy. For the Graduate College Iowa State University Ames, Iowa 1979 ii TABLE OF CONTENTS Page NOMENCLATURE x ABSTRACT xi INTRODUCTION 1 LITERATURE REVIEW 6 Extraction of Sulfur from Pyrite and Other Sulfide Minerals 6 Desulfurization of Coal 21 Leaching with solutions of ferric sulfate 21 Nitric acid leaching 23 Leaching with dissolved oxygen solutions 24 Atmospheric pressure method 24 Elevated pressure method 25 Hot aqueous solutions 25 Hot aqueous solutions with a promoter 29 Hot alkaline solutions 30 Leaching with caustic solutions 32 Extraction with molten caustic 33 Leciching with aqueous solutions of metal oxides 33 Treatment with gases 34 Sulfur dioxide 34 Chlorine 35 Ozone 35 KVB process 36 Hazen Magnex process 37 Other reviews and monographs 37 EXPERIMENTAL INVESTIGATION 39 Materials and Equipment Used 39 Autoclave 39 Pyrite cleaning apparatus 41 Coal and pyrite feedstock 41 Leaching Procedure 45 Calculations 46 iii EXPERIMENTAL RESULTS AND DISCUSSION 48 Coal Desulfurization 48 Effect of stirring rate 48 Effect of oxygen flow rate 53 Effect of pulp density 53 Effect of leach solution and oxidant 56 Effect of alkali concentration 57 Effect of residence time 59 Effect of temperature 59 Effect of oxygen partial pressure 63 Effect of acid treatment 69 Sodium bicarbonate solution 71 Effect of temperature 71 Effect of concentration 73 Effect of sodium sulfate 73 Comparison of different alkalis 76 Removal of organic sulfur from precleaned coal 78 Two-step leaching 84 Desulfurization of Coal-Derived Pyrite 87 Conversion-time data 87 Modeling 88 Reaction kinetics 88 Selection of a model 99 Effective diffusivity calculation 104 Effect of Temperature 108 Effect of Oxygen Partial Pressure 110 Effect of Particle Size 114 CONCLUSIONS AND RECOMMENDATIONS 118 Conclusions 118 Coal desulfurization 118 Pyrite desulfurization 120 Recommendations 121 Coal desulfurization 121 Pyrite desulfurization 122 iv LITERATURE CITED 123 ACKNOWLEDGMENTS 130 APPENDIX A. EXPERIMENTAL CONDITIONS AND RESULTS OBTAINED FOR COAL DESULFURIZATION 131 APPENDIX B. STATISTICAL ANALYSIS OF COAL DATA 155 APPENDIX C. DETERMINATION OF SULFUR IN LIQUID SAMPLES 163 Procedure 163 Calculation Method 164 Sample Calculation of Sulfur Content 164 APPENDIX D. EXPERIMENTAL CONDITIONS AND RESULTS OBTAINED FOR PYRITE DESULFURIZATION 166 APPENDIX E. NONLINEAR REGRESSION ANALYSIS OF PYRITE LEACHING DATA 170 V LIST OF FIGURES Page Figure 1. Schematic diagram of experimental apparatus 40 Figure 2. Pyrite cleaning apparatus 42 Figure 3. Effect of agitator speed on the removal of sulfur from coal for 50 Ib./sq. in. (absolute) oxygen partial pressure 50 Figure 4. The interaction of agitator speed and oxygen partial pressure on pyritic sulfur removal 51 Figure 5. Effect of oxygen flow rate on leaching of coal 54 Figure 6. Effect of pulp density on leaching of coal 55 Figure 7. Effect of sodium carbonate concentration on oxy- desulfurization of coal 58 Figure 8. Effect of leaching time on oxydesulfurization of coal 60 Figure 9. Desulfurization of coal as a function of tempera­ ture at 50 Ib./sq. in. (absolute) oxygen pressure 61 Figure 10. Desulfurization of coal as a function of tempera­ ture at 200 Ib./sq. in. (absolute) oxygen pressure 62 Figure 11. Effect of oxygen partial pressure on oxydesulfuriza­ tion of Lovilia coal 65 Figure 12. Effect of oxygen partial pressure on leaching of Western Kentucky coal 66 Figure 13. Effect of oxygen partial pressure on oxydesulfuriza­ tion of Western Kentucky coal by leaching with alkaline, neutral or acidic solutions 68 Figure 14. Effect of temperature on leaching of coal with sodium bicarbonate solution 72 Figure 15. Effect of sodium bicarbonate concentration on leaching of coal 74 Figure 16. Effect of O2 pressure and reaction time on organic sulfur removal at 1200C 81 vi Figure 17. Effect of O2 pressure and time on organic sulfur removal at 2000C 82 Figure 18. Organic sulfur removal versus heating value loss 83 Figure 19. Total sulfur conversion versus reaction time for coarse particles 89 Figure 20. Total sulfur conversion versus reaction time for fine particles 90 Figure 21. Partially reacted pyrite from chemical leaching of c>-)a.l. A hematite (Fe203) reaction rim is indicated by the arrows 92 Figure 22. The photomicrograph of a large leached pyrite particle. P = unreacted pyrite. H = the reac­ tion rim of hematite 94 Figure 23. Representation of shrinking unreacted core model for single particles 96 Figure 24. gCXg) and p(Xg) versus reaction time for coarse particles 102 Figure 25. g(Xg) and p(Xg) versus reaction time for fine particles 103 Figure 26. Arrhenius plot for the temperature effect 109 Figure 27. Effect of oxygen pressure on pyrite leaching 111 Figure 28. Effect of oxygen partial pressure on sulfur conversion 113 Figure 29. Effect of particle size on sulfur conversion 115 Figure 30. Time for complete reaction of ppyyi rite (T)v ersus square of the particle size (R/) 117 Figure B-1. Response of high sulfur coals to leaching condi­ tions 157 Figure B-2. Effect of sulfur content on response of high sulfur coals to different leaching conditions 158 Figure B-3. Response of low sulfur coals to leaching condi­ tions 160 Figure B-4. Effect of sulfur content on response of low sulfur coals to different leaching conditions 161

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Among the difficulties are the stability of the sulfur oxides, the relatively low concentration of sulfur oxides in the stack gas, and the waste disposal problem. Besides, like coal gasification and liquefaction, the cost of flue gas desulfurization is relatively high. Recently, the development of
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