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BIOREACTOR STUDIES OF HETEROLOGOUS
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nie University of Waterloo requin%
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ate depended on activities of the p
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Acknowiedgments Fmt of aü, 1 am ve
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2.6. Concluding Rernarks ..........
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5.3.3. Simlilated Results for Prese
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Table 1.1. Table 1.2. Table 1.3. Ta
- Page 15 and 16: Figure 2.1. Figure 3.1. Figure 3.2.
- Page 17 and 18: during Continuous Culture in Airlif
- Page 19 and 20: Figure 5.3. Comparison between Mode
- Page 21 and 22: Cell Systern at Glucose Feed Concen
- Page 23 and 24: a .......... growth ratio (dimensio
- Page 25 and 26: Y, ... ethanol yield for fermentati
- Page 27 and 28: foreign plasmids. One major chalien
- Page 29 and 30: than the denanired, inclusion body
- Page 31 and 32: Table 1.2. Strategies for Enhancing
- Page 33 and 34: Table 1.3. Host Cek, Pfasmids, Gene
- Page 35 and 36: 1.4. Immo bilized-Cell Bioreactors
- Page 37 and 38: 1. Study the gmwth characteristics,
- Page 39 and 40: plasmid are used; or chromaromal DN
- Page 41 and 42: 2.2.1. Genetic Factors 2.2.1.1. Pid
- Page 43 and 44: 1- fkquently than a plasmid with Io
- Page 45 and 46: Da Silva and Bailey (1991) used the
- Page 47 and 48: LEU2 or TRPI is cloned into the aux
- Page 49 and 50: eported reduced stabiliity in the s
- Page 51 and 52: on metabolic pathways. In the ferme
- Page 53 and 54: OC), oniy about 35% of the populati
- Page 55 and 56: loss @) is dehned as the probabilit
- Page 57 and 58: + s Dilution Rate = p' = CI,- - K*+
- Page 59 and 60: concentration couid Iead to coexist
- Page 61 and 62: that factors other than immobiiizat
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- Page 69 and 70: Aerobic fermentation osing iamnobih
- Page 71 and 72: (ranghg h m 1 to 7) on citric acid
- Page 73 and 74: celi fraction decreases monotonicai
- Page 75 and 76: (1987) model aliows for plasmid ins
- Page 77 and 78: affect plasmid stability have ben o
- Page 79 and 80: CEtAPTER 3 MATERIALS AND METHODS 3.
- Page 81 and 82: stiU deleted hm the plasmid. Such p
- Page 83 and 84: 1) Reagent solution preparation was
- Page 85 and 86: nonse1ective agar plates, but only
- Page 87 and 88: working Liquid volume. The aeration
- Page 89 and 90: 3.5. UNnobilized Ceil Culture 35.1.
- Page 91 and 92: 3.52 Cd Lmmobiiization Yeast attach
- Page 93 and 94: 3.6. Experimental Error and Reprodu
- Page 95 and 96: -0-Cell(1) +Total CeII (2) 4- Ethan
- Page 97 and 98: * . I I a O 2 4 6 8 10 12 14 Batche
- Page 99 and 100: Cell Maso, Glucose and EthanoI(g1L)
- Page 101 and 102: 4.2.2. Batch CuIture in Stirreà-Ta
- Page 103 and 104: [t ~lucoamylase (ALR) -e Glucoamyla
- Page 105 and 106: The finai giucoamyiase concentratio
- Page 107 and 108: Bentley and Kompala, 1989; Satyagal
- Page 109 and 110: 160 First ExponenUaI Phase 1 -c ALR
- Page 111 and 112: Figure 4hl. Pathways of Yeast Intem
- Page 113 and 114: fermentation (using nitrogen spargi
- Page 115 and 116: 43. Continuous Suspension Culture C
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Figure 4.9. Continuous Suspension C
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1 +Enzyme +Fradlan of PBC +CeIl Mas
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Figures 4.12 and 4.13 show that by
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Fi- 4.13. Cornparison of Glu~iase C
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where 6 = p- - p' + pp*, which is a
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Figure 4-14. Effeds of Dilution Rat
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Impoolsup et ai. (1989a) and Hardji
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Figure 4.16. dB/dt versus B Plots a
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Figure 4.17. Totai Cell Mas at Diff
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another recombinant yeast (impoolsu
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other recombinant yeast under nonse
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4.3.4. Effixt of Dilution Rate On R
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Figure 4.18- Etlects of Mluiioa Rat
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Number of Generations - - - - - - *
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B Table 4.5. Metabolic Pathway Anal
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concentration. But this may be more
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[+ Enzyme (ALR) + Enzyme (STR) +Fra
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necessary for host ce& to grow in t
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Glucoamylase ConcentraUon (unltsll)
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[a Selective Medium A Nonseiective
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5.1 Introduction CHAPTER 5 MODELING
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handle. excess glucose is femented
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The carbon fluxes h m the three met
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53. Modei Simulation in Batch CuItu
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Table 5.1. Summary of Parameters fo
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1 n Glucose o Cell Mass O Ethano1 A
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detennined in the cunent study, the
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Figure 5.4. Cornparison between Mod
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equations are üsted in Appendix G.
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a dilution rate at which the giucoa
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[ o Expetfmental data -Simuiated mt
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The effixts of dilution rate on the
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Ttme (hrs) 1 a Enzyme A Phsrnid-Bea
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It may take several generations for
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understanding of the nature of the
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On the other hand. the net accumula
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Differentiating Equation (6.20) res
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Enyme collcentration m the t>ioreac
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Glucoamylase Concentration (units/L
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50 100 150 200 Time (hrs) 1 O Free
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F i 6.6. Cornparison of Fnx Cd Mars
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. - O 50 100 150 200 250 nme (hrs)
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Nasi et ai.. 1988) and recombinant
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estimated by using Equation (6.24)
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[a lmmobilked System O Free System
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oxidation pathway. W~th increasing
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O 50 100 150 200 250 300 Tirne (hrs
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epeated batch fermentations, the fe
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Glucoamylase Concentration (unitslL
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6) Suitable for repeated-batch and
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ecause glucose fermentation dominat
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cells. Tests of the proposed model
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7.2. Recommendations The foUowing f
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APPENDIX A: PLASMID MAP FOR pGAC9 l
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where Bi (Biot number) = - ks De @
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APPENDK C. EFFECTS OF INITIAL GLUCO
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Figure C.2. Effect of Initial Gluco
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Figure C.4 Effect of Initial Glucos
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APPENDLX D. COMPARISON OF ORIGINAL
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(continue)
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(continue)
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(continue)
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E.2. Batch Fermentation with Recomb
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(continue)
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(continue) tfhJ 0.5 10.5 12.75 12.5
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(continue)
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E.3.2. Experimental Data (Parker an
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Run No: CALE (Selected Strain. D =
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Run No: CALR 5 (Original Suain, D =
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Run No: CSTR3 (Selected Suain, D =
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(continue)
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Run No: CICR2 (Selected Suain, D =
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Run No: CiCR4 (Selected Suain, D =
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Eh. Repeated Batch Culture in hmobi
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APPENDIX F. C CODE FOR THE PROPOSED
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* the initial data */ /* gening the
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* getting the founh term in R-K met
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I*Plasrnid-bearing ceU concentratio
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* Func tion C 1 */ îloat C l(float
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APPEMIM G. EXAMPLES OF MAPLE V CODE
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REFERENCES Ataai. MM. and Shuler. M
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Caunt, P.. hpoolsup, A.. and Greenf
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cuitanes of E. coli BZ18@TG 201) wi
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Gabrieisen. O.S. et aL (1990), Effi
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Huang, C-T., Peretti, S.W., and Bry
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Kim, B.G. and Shuler, M.L. (1990a),
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Lee, S.B.. Ryu, D.D.Y., seigel, R,
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Nasri, M., Sayadi. S.. Barbotin, J.
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Pin, S.J. and Kmwski. W.M. (1970),
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Seo, I-H. and Bailey. J.E. (1985).
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Tumer. B.G., Avgerinos G-C.? Melnic
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Yu, J. and Tang, X (Editor, 1991),