Thesis - faculty.ait.ac.th - Asian Institute of Technology

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Table B-1 Leachate Characteristic of the Primary Sources and the Feed Pathumthani Landfill Site Ram-Indra Transfer Station Feed Sample No. NH4 + -N TKN COD NH4 (mg/L) (mg/L) (mg/L) + -N TKN COD NH4 (mg/L) (mg/L) (mg/L) + -N TKN COD (mg/L) (mg/L) (mg/L) 1 2,184 2,349 5,410 349 1,292 87,200 1,831 2,013 7,412 2 1,820 1,968 3,660 333 1,247 85,020 1,537 1,719 7,521 3 1,691 1,882 4,230 319 1,652 73,840 1,562 1,848 7,692 4 1,691 1,882 4,100 336 1,249 32,190 1,604 1,893 8,195 5 1,781 2,050 3,940 448 1,361 34,280 1,669 1,957 7,200 6 1,756 2,019 4,170 333 1,226 33,330 1,753 1,982 7,000 7 1,607 1,884 3,288 409 921 31,151 1,417 1,750 7,233 8 1,719 2,044 3,243 434 879 32,432 1,442 1,764 7,135 146
Table B-2 Acclimation of Mixed Yeast Sludge to Landfill Leachate Containing High Organic and Ammonia Concentration Time COD (mg/L) COD Removal MLSS F/M ratio (days) Influent Effluent (%) (mg/L) (d -1 ) 1 3,800 2,090 45 3,750 1.01 3 3,800 1,710 55 3,933 0.97 6 4,000 1,440 64 4,233 0.94 9 4,000 1,320 67 4,533 0.88 12 4,150 1,287 69 4,800 0.86 14 4,150 1,245 70 5,367 0.77 17 4,320 1,210 72 5,633 0.77 21 4,320 1,166 73 6,240 0.69 25 4,800 1,296 73 6,560 0.73 29 4,800 1,248 74 6,740 0.71 35 4,800 1,200 75 7,040 0.68 39 5,530 1,438 74 7,540 0.73 42 5,530 1,327 76 8,167 0.68 44 5,,530 1,272 77 8,667 0.64 46 6,105 1,526 75 9,800 0.62 50 6,105 1,404 77 10,450 0.58 52 7,071 1,697 76 10,750 0.66 54 7,071 1,838 74 11,240 0.63 56 7,300 1,898 74 11,400 0.64 58 7,300 1,825 75 11,950 0.61 61 7,300 1,898 74 11,850 0.62 67 7,300 1,825 75 11,700 0.62 147
Page 1 and 2:
APPLICATION OF MEMBRANE BIOREACTOR
Page 3 and 4:
Abstract Landfill leachate is a com
Page 5 and 6:
Table of Contents Chapter Title Pag
Page 7 and 8:
4.5.6 Cost Analysis for Operation 1
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4.4 Effect of Free Ammonia Concentr
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4.16 COD Concentration in the Influ
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MWCO Molecular Weight Cut-off MWW M
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1.1 Background Chapter 1 Introducti
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generally unsuccessful in removal o
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2.1 Introduction Chapter 2 Literatu
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In the municipal solid waste landfi
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COD/TOC, VS/FS and VFA/TOC ratios o
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Table 2.3 presents the general leac
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Ground water 2.7.1 Seasonal Variati
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Table 2.5 Variation of COD, BOD & B
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entails the re-circulation of leach
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Table 2.8 Summary of Biokinetic Coe
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that extensive loss of nitrogen (up
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ammonia could only be achieved when
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Table 2.10 Treatment Efficiencies o
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Activated Carbon Adsorption Granula
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Colloidal material as well as metal
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iologically, physical-chemical proc
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Ammonia Stripping Air stripping of
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These systems are land intensive wh
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the biological treatment can be rep
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Table 2.16 Typical Leachate Composi
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influent reached 200 mg/L. For the
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Table 2.18 Advantages and Disadvant
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through the effluent. Different ope
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Mixed Liquor Suspended Solids and D
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2.12 Yeasts 2.12.1 Introduction The
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Nishihara ESRC Ltd. (2001) studied
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nitrification-denitrification proce
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Table 3.1 Composition of Simulated
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3.4.1 Ammonia Toxicity The experime
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Figure 3.4 Experiments Conducted to
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Leachate Option Ammonia Stripping R
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MW larger than 50 kDa, (2) MW betwe
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Figure 3.7 Flowchart Showing Ammoni
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Chapter 4 Results and Discussion 4.
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COD Removal Effeciency (%) COD Remo
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MLSS (mg/L) 14000 12000 10000 8000
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Specific Growth Rate ( d -1 ) 0.50
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change in the predominant species w
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Table 4.4 Effect of Free Ammonia Co
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Table 4.5 Substrate Utilization by
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4.3.1 Initial Membrane Resistance P
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when compared with the present stud
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COD Removal Efficiency (%) 90 80 70
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(2) TKN Removal Efficiency Prior to
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As there was no significant improve
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The probable reason for frequent fo
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Ammonia Concentration (mg/L) Ammoni
Page 109 and 110: concentration after treatment. Othe
Page 111 and 112: After the chemical cleaning of the
Page 113 and 114: emoval of 38%. A higher removal in
Page 115 and 116: Influent BOD (mg/L) Influent BOD (m
Page 117 and 118: (3) TKN Removal Efficiency The TKN
Page 119 and 120: Figure 4.34 gives the overall TKN r
Page 121 and 122: fraction and slowly biodegradable C
Page 123 and 124: BOD (mg/L) BOD (mg/L) 6000 5000 400
Page 125 and 126: Figure 4.39 Molecular Weight Cut-of
Page 127 and 128: COD (mg/L) 8000 6000 4000 2000 COD
Page 129 and 130: Though, the obtained COD removal ef
Page 131 and 132: cake used on the top of the membran
Page 133 and 134: Chapter 5 Conclusions and Recommend
Page 135 and 136: 0.02, respectively. This can be con
Page 137 and 138: References Abeling, U., and Seyfrie
Page 139 and 140: Brown, M.J., and Lester, J.N., 1980
Page 141 and 142: Diamadopoulos, E., 1994. Characteri
Page 143 and 144: Grady, C.P.L., Daigger, G.T., and L
Page 145 and 146: Keenan, J.D., Steiner, R.L., and Fu
Page 147 and 148: Martin, G.M.A., Auzmenti, A.I., and
Page 149 and 150: Pohland, F.G., and Harper, S.R., 19
Page 151 and 152: Shin, H.S., An, H., Kang, S.T., Cho
Page 153 and 154: Visvanathan, C., Ben Aim, R., and P
Page 155 and 156: Appendix A Pictures of Experiments
Page 157 and 158: Raw Leachate YMBR Effluent BMBR Eff
Page 159: Appendix B Leachate Characteristics
Page 163 and 164: Appendix C Experimental Data of Bio
Page 165 and 166: y: Where: OUR at line g: This is th
Page 167 and 168: Table C-3 Experimental Results for
Page 169 and 170: Appendix D Membrane Resistance Stud
Page 171 and 172: Table D-3 Experimental Data for Det
Page 173 and 174: Table D-4 Experimental Data for Det
Page 175 and 176: Pressure (kPa) Pressure (kPa) 25 20
Page 177 and 178: Appendix E MBR without Ammonia Stri
Page 179 and 180: Day HRT (h) pH COD (mg/L) Feed Reac
Page 181 and 182: Day HRT (h) pH COD (mg/L) Feed Reac
Page 183 and 184: Table E-3 Variation in TMP with Tim
Page 185 and 186: Appendix F Ammonia Stripping Studie
Page 187 and 188: Table F-5 Pilot Scale Study on Ammo
Page 189 and 190: Table G-1 Feed, Reactor and Effluen
Page 191 and 192: Table G-3 Feed, Reactor and Effluen
Page 193 and 194: Appendix H Other Studies 179
Page 195 and 196: Table H-2 Membrane Resistance of th
Page 197: Table H-6 Chemical Cost for the Yea
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Thesis - faculty.ait.ac.th - Asian Institute of Technology

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