Lynne Wong's PhD thesis

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is prepared by dissolving 800 g potassium iodide in 500 mL of warm distilled water. The juice preservative is applied at a rate of 0.5 mL per litre of sample. 2.1.2 Equipment A heavy duty universal model 264 Jeffco cutter-grinder (Fig 2.1) with a 7500 W, three phase motor, was suitable for shredding the sugar cane stalk. A cane chipper (Fig 2.2) with four steel blades bolted onto a horizontal, cylindrical shaft, which rotates at a high speed, was used to shred cane into pieces about 2 – 3 cm long. Cane was fed manually to the electrically-driven rotating knives. Juice was expressed from the cane by means of a Pinette Emidecau hydraulic press (Fig 2.3) capable of exerting a pressure of up to 25 MPa to sample contained in a stainless steel cup. A Schmidt and Haensch DUR W2 sugar refractometer (Fig 2.4) was used to measure the refractive index of sugar solutions and displayed the results as dissolved solids (g) in 100 g solution (Brix). A Schmidt and Haensch Saccharomat sugar polarimter (Fig 2.5) was used to measure the pol and Clerget sucrose of mixed juice, and pol in bagasse, cane, dry leaf, green leaf and in tops. A Dionex high performance ion chromatograph (Fig 2.6) equipped with an eluant degas module model EDM-2 and a pulsed amperometric detector was used to determine glucose, fructose and sucrose. Separation was achieved at ambient temperature on a Dionex CarboPac PA1 column of 250 mm length and 4 mm internal diameter. The column was preceded by a guard column packed with the same material. Sodium hydroxide solution (150 mmol L -1 ) was used as eluant at a flow rate of 1 mL per minute. 31
Figure 2.1. Jeffco cutter grinder. Figure 2.2. Cane chipper. Figure 2.3. Pinette Emidecau Press. Figure 2.4. Sugar refractometer. Figure 2.5. Sugar polarimeter Figure 2.6. High Performance Ion Chromatograph. 32
Page 1 and 2:
THE BRIX-FREE WATER CAPACITY AND SO
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dissolved and hydrated waters, and
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ACKNOWLEDGEMENTS I am particularly
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Page 1.5 THE DELETERIOUS EFFECTS OF
Page 9 and 10:
Page 2.2 THE PHENOMENON OF BRIX-FRE
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Page 3.4.3.3 Cane tops 83 3.4.4 Cha
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4.3.3 Temperature at which Brix-fre
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4.6.1 Materials 143 4.6.1.1 Samples
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CHAPTER 6. PROPERTIES OF THE SORBED
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APPENDIX 3. CALCULATIONS LEADING TO
Page 21 and 22:
LIST OF FIGURES Page Figure 1.1. Fi
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Figure 3.1. Glucose and fructose an
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Figure 5.11. Residual plots for the
Page 27 and 28: total adsorbed water (m) and the pr
Page 29 and 30: Table 2.18. Moisture content in sug
Page 31 and 32: Page Table 4.4. Results of the dete
Page 33 and 34: Page Table 4.24. Analysis of varian
Page 35 and 36: Page Table 5.13. Table 5.14. Equili
Page 37 and 38: Table 6.3. Heat of sorption of the
Page 39 and 40: GLOSSARY OF TERMS Absorption is the
Page 41 and 42: Filterability of a raw sugar is mea
Page 43 and 44: Sorption is the generic term used w
Page 45 and 46: LIST OF MAIN SYMBOLS Symbol Descrip
Page 47 and 48: s c s Slope of Caurie I isotherm pl
Page 49 and 50: number of 255, and cane land covere
Page 51 and 52: Nouvelle Mon In Trésor ustrie and
Page 53 and 54: Figure 1.3. Cane sampling by core s
Page 55 and 56: In Mauritius, most of the sugar fac
Page 57 and 58: are: cane tops, dry and green leave
Page 59 and 60: 1.4 TRENDS IN CANE QUALITY RECEIVED
Page 61 and 62: campaign was launched to encourage
Page 63 and 64: The level of extraneous matter in c
Page 65 and 66: In Australia (Cargill, 1976), cane
Page 67 and 68: The effect of soil on factory perfo
Page 69 and 70: leaves increased the level of impur
Page 71 and 72: • From 1976 to 1980, when the pro
Page 73 and 74: Clerget purity of molasses 40 Clerg
Page 75 and 76: CHAPTER 2. IMPACT OF EXTRANEOUS MAT
Page 77: Since the extrapolated purity of mo
Page 81 and 82: 2.1.4 Results The analytical result
Page 83 and 84: Table 2.3. Analytical results of re
Page 85 and 86: Table 2.5. Composition of dry trash
Page 87 and 88: Table 2.7. Predicted factory perfor
Page 89 and 90: Boiling house recovery 91.0 89.8 89
Page 91 and 92: 0 5 10 15 20 % EM in cane y = 0.572
Page 93 and 94: % EM in cane 0 5 10 15 20 0 -2 -4 -
Page 95 and 96: 1 y = 0.020 (% D) R 2 = 1.00 = 0.03
Page 97 and 98: % EM in cane 0 5 10 15 20 0 -2 y =
Page 99 and 100: esulting in 0.015 unit sucrose loss
Page 101 and 102: 2.2.1 Experimental procedure Cane m
Page 103 and 104: filter paper, rejecting the first f
Page 105 and 106: Table 2.9. Effect of increased addi
Page 107 and 108: Table 2.11. Effect of increased add
Page 109 and 110: Table 2.13. Effect of increased add
Page 111 and 112: various components such as stalk fi
Page 113 and 114: in the presence of dry leaves, if c
Page 115 and 116: Table 2.17. Moisture content in sug
Page 117 and 118: CHAPTER 3. SEPARATION OF THE SUGAR
Page 119 and 120: Table 3.1. It can be seen that the
Page 121 and 122: Table 3.2. Fibrous physical composi
Page 123 and 124: R 579 R 570 M 1557/70 M 1400/86 74
Page 125 and 126: loosen the fibre. The woody core is
Page 127 and 128: agitate the mixture in the pot, and
Page 129 and 130:
Figure 3.7. Custom-built fibre-pith
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The extraction of fibres starting f
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pre-treatment in a Jeffco cutter-gr
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Figure 3.19. Stalk cake washed free
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not have many dry leaves attached t
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Table 3.5. Masses of cane samples a
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Table 3.7. Masses of cane samples a
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Table 3.9. Masses of cane component
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3 57.6 126.3 23.7 97.2 31.1 53.8 11
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Table 3.12. Material loss (%) from
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3.5.3 Fibre/pith ratios in cane com
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Table 3.15. Effect of extraneous ma
Page 153 and 154:
Snow (1974) investigated the season
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from Figure 2.9 that the change in
Page 157 and 158:
Table 3.18. Fibre % cane results by
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110
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(a). Dry leaf (b). Green leaf (c).
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dry fibre, or a factor, is used in
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Steuerwald (1912) applied sucrose s
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solution/fibre ratio was lowered fr
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leave some residual moisture on the
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instead of 150 g of 10° Brix sucro
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Table 4.2. Determination of Brix-fr
Page 175 and 176:
Table 4.3. Comparison of Brix-free
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Table 4.4. Results of the determina
Page 179 and 180:
In order to test for homogeneity of
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Table 4.7. Results of the repeat de
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The experiment was repeated with th
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e any residual moisture in the samp
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By means of the same technique, Won
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was still hot. Since the filter was
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value determined could be corrected
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Qin and White’s finding was confi
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A sample size of 3.5 g with 75 g co
Page 197 and 198:
Figure 4.4. Fibre samples drying in
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- One large fibre sample (rind) of
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Table 4.18. Brix-free water values/
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Table 4.20. Brix-free water values/
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4.7.3 Statistical analysis It is es
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Table 4.23. Analysis of variance (B
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pointing out that at 52 weeks old,
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The crop of R 570 sampled in 2001 w
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4.7.4. Estimated Brix-free water co
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The main difference in the two sets
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Table 4.27. Predicted Brix-free wat
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4.8 SUMMARY AND CONCLUSIONS An anal
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component parts, and verify the Bri
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3) Thermodynamic, water in equilibr
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Langmuir (1916, 1917, 1918) propose
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to determine the moisture sorption
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Table 5.1. Some commonly used isoth
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Lomauro et al. (1985) found that wi
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and on agricultural products such a
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Bruijn (1963) studied the mass incr
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After measuring the EMC of dry corn
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approached, that is, either by adso
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Table 5.4. Water activity (a w ) of
Page 243 and 244:
5.6.3 Procedure to determine equili
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5.6.4 Results and discussion An exa
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Table 5.8. Equilibrium moisture con
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Table 5.10. Equilibrium moisture co
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Table 5.12. Equilibrium moisture co
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30 o C 45 o C 55 o C 60 o C Water w
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m/m of 96% activity, a w (g/100g dr
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vaporisation generally decreases fr
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30 o C isotherm 45 o C isotherm 55
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4 0 Stalk fibre 5 0 Stalk pith 5 0
Page 263 and 264:
5.6.4.4 Fitting of sorption models
Page 265 and 266:
Table 5.19. Parameters of the sorpt
Page 267 and 268:
Page 269 and 270:
Page 271 and 272:
Page 273 and 274:
Page 275 and 276:
Modified GAB Kuhn Iglesias - Chirif
Page 277 and 278:
Table 5.28. Classification of resid
Page 279 and 280:
Stalk fibre Stalk pith Rind fibre 4
Page 281 and 282:
5.6.4.5 Calculated EMC values of re
Page 283 and 284:
Table 5.30. Calculated equilibrium
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m/m of 96% Table 5.32. Calculated e
Page 287 and 288:
Table 5.33. Parameters of the Hailw
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CHAPTER 6. PROPERTIES OF THE SORBED
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where m is the equilibrium moisture
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Page 297 and 298:
6.2 THE NUMBER OF ADSORBED MONOLAYE
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6.3 TOTAL SOLID SURFACE AREA AVAILA
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Thus, for each cane component of ea
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abscissa. For each moisture level (
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Page 307 and 308:
A similar procedure was followed to
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10 0 Stalk fibre Stalk pith Rind fi
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Moreover, if T β > T hm the proces
Page 313 and 314:
Table 6.5. Characteristic parameter
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Binding energy/kJ (kg mol) -1 2 0 0
Page 317 and 318:
6.8 CALCULATION OF BOUND WATER AND
Page 319 and 320:
The values of K 1 , K 2 and W were
Page 321 and 322:
Table 6.7. Separation of the total
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Table 6.7. (Contd.) Sample 30 o C 4
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3 0 S talk fibre 4 0 Stalk pith 3 0
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3 0 Reconstituted cane at 30 o C 3
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when water is added to dry wood, wh
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It is evident that in some cases ma
Page 333 and 334:
The number of adsorbed monolayers,
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Data in Tables 2.9 and 2.11 show th
Page 337 and 338:
particular fibre is systematically
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Anon. (1985b). Laboratory manual fo
Page 341 and 342:
Blanchi R.H. and A.G. Keller (1952)
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Day D.L. and G.L. Nelson (1965). De
Page 345 and 346:
Heyrovsky J. (1970). Determination
Page 347 and 348:
Kuhn I.J. (1964). A new theoretical
Page 349 and 350:
Madamba P.S., R.H. Driscoll and K.A
Page 351 and 352:
Prinsen Geerligs, H.C. (1897). Stud
Page 353 and 354:
Sing K.S.W., D.H. Everett, R.A.W. H
Page 355 and 356:
Van der Pol C., C.M. Young and K. D
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Lynne Wong's PhD thesis

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