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Author Biography
Prof. Dr. Ravindra Pogaku is a Professor ofChemical and Bioprocess Engineering atUniversity Malaysia Sabah. He is now the Directorfor Oil and Gas Engineering Studies and TrainingUnit at the School of Engineering and InformationTechnology, University Malaysia Sabah (UMS).Pogaku Ravindra’s work has appeared in more than200 publications and 4 patents in ISI/SCI/Scopusjournals. He has published eight books, six bookchapters and edited two scientific books. Prof.Pogaku is also on the Editorial Board of several
international journals and has reviewed over 500 journal manuscripts for reputedinternational journals. He has delivered various keynotes, plenary lectures, andchaired the prestigious conferences, seminars, workshops, technical events bothnationally and internationally. He has been honored with senior membership ofAmerican Institute of Chemical Engineers for his credentials in the field of chemicaland bioprocess engineering. He was a Visiting Scientist at Cornell University. Hewas UNESCO consultant. Prof. Ravindra is bestowed with the distinguishedChemical Engineer Award from the Indian Institute of Chemical Engineers, India.He has been recognized with Excellence Award consecutively for the last three yearsfrom the University Malaysia Sabah. Prof. Pogaku Ravindra is awarded with goldand silver medals for his research contribution for bioprocess industry at Geneva andMalaysia.
Prof. Dr. Ravindra PogakuProfessor of Chemical and Bioprocess Engineering
UNESCO energy consultant; Editor in Chief BMBRDirector Oil and Gas Engineering Studies and Training Unit
Phone: 088-320533/320000 (ext 3661)Fax: 088-320539/320348
Email: [email protected] or [email protected]
R. Pogaku et al. (eds.), Developments in Sustainable Chemicaland Bioprocess Technology, DOI: 10.1007/978-1-4614-6208-8,� Springer Science+Business Media New York 2013
409
Prof. Dr. Awang Bono
Awang Bono (BSc., PhD.) is a Separation Science and Technology Professor atUniversiti Malaysia Sabah (UMS). Prof. Bono completed his PhD work fromChemical Engineering Department, University of Surrey, United Kingdom in 1986and has been involving in teaching, research as well as industry for more than 20years. To date, he has over 150 scientific publications. Currently, Prof. Bono isserving as a Deputy Dean at School of Engineering and Information Technology,UMS.
Associate Professor Dr. Chu Chi Ming
Christopher Chi-Ming Chu is the Head of Chemical Engineering Programme at theSchool of Engineering, Universiti Malaysia Sabah. He received his B.Sc. andPh.D. from the University of Birmingham, United Kingdom. His main researchinterest is in thermal systems and currently works on chimney performanceenhancement using wire mesh and passive cooling systems. He is the Head ofThermal and Environment Group in the Material and Mineral Research Unit. Hehas published and reviewed international journal papers and conferences.
410 Author Biography
Index
AAbyssomicins, 204Acclimatization process, KRW
adaptation process, 63COD removal efficiency, 62–63genotype appearance, 63inoculums, 61microorganisms, 60sample analysis, 62SBR system, 61–62
Acetone-butanol-ethanol (ABE) fermentationacidogenic phase, 35clostridia strains, 35POME, Clostridium acetobutylicum
ABE recovery, 40bacteria growth profiles, 38liquid–liquid extraction, 37–38microbes and media, 37pH and reducing sugar profiles, 38process and analysis, 37solvent productions, 39sterilized POME supernatant vs. sludge,
38–39product recovery, 36solventogenic phase, 35–36
Acetonitrile (MeCN), 152, 229, 243Acid rains, 296Acidic sodium chlorite treatment, 278, 278f,
279f, 280Acidified sodium chlorite, 272Acidogenesis, 4Acoustic cavitation, mechanical effect of, 251
solvent penetration and capillary effects,251
Actinomycetes, 204–205antibiotics, 204anticancer drug, 204
marine actinomycetes. See Marineactinomycetes
parameter study, 205Actinomycetes isolation agar (AIA), 205Activated carbon preparation, waste
rubber tireadsorption, 372chemical activation, ZnCl2
activation temperature, 375activation time, 375–376adsorption, 373ash content, 376impregnation ratio effect, 373, 375methodology, 373–374moisture content, 376morphological study, 376–377scanning electron microscopy, 374surface area analysis, 374, 377–378
2,4-dichlorophenol, 372recycling, 372
Adsorbents, 104, 119, 296adsorption of H2S by, 298–300batch adsorption studies, 120–121bleaching adsorbents, 303, 304characterization of, 297porous adsorbents, 304, 306
Aeromicrobium marinum, 204Algae, 174, 356Alginate, 132t, 160, 201
j-carrageenan/alginate matrix, 199, 202sodium alginate, 198, 200, 202
Alkali treatment, 272, 274, 275, 277f, 278f,279f, 280
purpose of, 356–357of seaweed, 357–358semi-refined and refined carrageenan, 356variation of KOH concentration, 359
R. Pogaku et al. (eds.), Developments in Sustainable Chemicaland Bioprocess Technology, DOI: 10.1007/978-1-4614-6208-8,� Springer Science+Business Media New York 2013
411
Alkaloids, 228, 235a-amylase production
in batch cultures, 165–166of B. subtilis 168 (pKTH10), 166fcomparison of sulphonated PolyHIPE
(SPHPs), 167tin immobilized cultures, 165–166
of B. subtilis 168 (pKTH10), 165fin steady-state, 169
a-lactalbumin (a-lac), 154heat stability of, 155percentage denaturation of, 154f
comparison with b-lactoglobulin, 155f5-aminolevulinic acid (ALA), in solid-state
fermentation, 174in tetrapyrrole compounds production, 174extraction and determination of, 176by Rhodopseudomonas palustris. See
Solid-state fermentation (SSF)kinetics of, 178t
Anaerobic digested sludge dewaterabilityanalytical methods, 13dual conditioning effect
capillary suction time, 13–14cation type effect, 15–16low molecular weight chitosan, 16
materials, 13polymer type and dosage, 14–15pre-treatment, 12sludge characteristion, 13sludge conditioning, 12sludge handling cost, 11–12
Anaerobic digestion, 12, 43, 296and colourants, 4–5of POME, 3organic matter reduction, 3–4
Anaerobically treated palm oil mill effluent(AnPOME)
coagulation/flocculation ofdecolourisation, 5Fenton process, 5metal coagulants and polymers, 6molasses wastewater, treatment of, 6sewage sludge, 6–7ultrafiltration of, 5
Antimicrobial activity studyCynodon dactylon crude extract, 233tCynodon dactylon EtOH- and EA
SPE-based extraction, 234tdisc diffusion bioassay, crude
extract, 231–232, 234McFarland standard, 231Mueller–Hinton Agar (MHA) medium,
231
extraction yield, 231thin-layer chromatographic (TLC)
bioassay, 231Artificially structured microbial consortia
(ASMC), 66Aspergillus niger, 230, 231, 350, 351
potato dextrose agar (PDA), 230potato dextrose broth (PDB), 230on surface of LDPE films, 352fthin-layer chromatographic bioassay
of, 232fAureoverticillatam, 204
BBacillus amyloliquefaciens a-amylase AmyQ,
165Bacillus cereus, 230, 233t, 234tBacillus sp., 63, 66Bacillus subtilis, 160, 230, 233t, 234tB. subtilis 168 (pKTH10) strain, 161, 165,
165f, 167tBaker’s yeast fermentation, dynamic
metabolism of, 220–221Batch process, 211–212
stages, 215Batch process modeling, 212–214
Arrhenius equation, 213schematic of, 213f
Batch productivity optimizationfor exothermic process, 212
b-1,3-glucanase, 288b-lactoglobulin (b-lg), 154
percentage denaturation of, 154fcomparison with a-lactalbumin, 155f
thermal denaturation of, 155Biodegradable plastics, 348–349Biodiesel production
biocatalyst for, 200from crude Jatropha curcas oil, 201fimmobilized lipase in, 201–202
Bioethanol productionfirst-generation biofuel, 130oil palm trunk (OPT) sap
ANOVA and model development,21–23
biomass preparation, 20characteristics, 19culture preparation and fermentation,
20–21face-centered CCD design layout, 21,
22graph-based discussion and model
validation, 23–24
412 Index
one-factor-at-a-time method, 20response surface methodology, 20statistical design of experiment method,
20pretreatment, 19–20seaweed
alkaline pre-treatment, 130–131fermentation, 131, 134pre-treatment reviews, 132–133saccharification pre-treatment, 130
Biofilms, 65–66biodegradability study, 350
results, 351–353formation of, 67for green packaging, starch-based,
348–349immobilization and, 68–69mechanical testing, 350
results, 350–351reactor and treatment system, 67–68sample preparation, 349
Biogas, 44, 45, 46, 297, 298biogas desulfurization, 296from manure digestion, 296and natural gas, 295–296sulfur capacity of fresh zeolite, 299, 299fH2S, 296, 299
Biological evolution theory, 214Bio-oil, 182
higher heating value (HHV), 184Karl Fischer titration (KFT) method, 184straw bio-oil and wood bio-oil, 185
DTG curves of, 186fTGA curves of, 185f
weight change of, 185Bio-oil production
Jatropha curcas, pyrolysisbio-oil yield, 84empirical correlations, 86experimental tests, 83materials, 82–83product characterisation, 85–86thermo-gravimetric analysis, 82
waste chicken fats, pyrolysisGC–MS and FTIR analysis, 75product yield, 75–76pyro-oil characterisation, 76–78raw materials, 74torrefied biomass, 74, 75ZSM-5 catalyst, 74–75
Black pepperbioactive compounds, solubility
of, 266–267pressure, 266, 267f
solvent temperature, 266, 267fdiffusion rate, 268diffusivity, 268–269extraction, 263mass transfer of, 267mass transfer rate in SC
period, 267–268Sarawak black peppers, 265SFE process of, 264solubility of, 266, 267f, 269transition time, 267
Bleaching, 303Bleaching clays, 303Bleaching earth, 304
calcinations of, 309natural bleaching earth (clay), 308–309porous characteristics of, 306, 306t
Bovine serum albumin (BSA), 53, 152, 154,163, 192, 193, 194, 289, 292
Bradford’s assay, 289Brunauer–Emmett–Teller (BET) approach,
305analysis, 306–308model, 374surface area, 308, 309, 374, 376, 378
Buckwheat hulls, hemicellulose from, 251Burkholderia cepacia (B. cepacia) lipase, 198,
200, 201, 202
CCaprolactones, 204CO2 separation of PEI/PEG
CMS membranesgas permeation properties, 332–333materials, 330microstructure properties, 331–332morphological structure, 333, 334procedure, 331phenolic resin-derived carbon
membrane, 330Carbon membrane, 327
performance of, 323porous structure of, 322production of, 324
carbolite vertical furnace, 324Carbon molecular sieve (CMS) membranes
CO2 separation. See Pyrolysis soaking timeproperties, 330
Carrageenan, 133t, 160classification, 356colorimetric determination of, 253effect of ultrasonic wave amplitude on, 254extraction, 130, 131
Index 413
Carrageenan (cont.)functional group composition, KOH
3,6-anhydrogalactose content, 358, 362FTIR spectrum, 358–360galactose-4-sulphate, 361–362gel strength, 359methodology, 358sulphate content, 358–359
iota-carrageenan. See Iota-carrageenaniota-type carrageenan, 356j-carrageenan, 198, 200, 201j-carrageenan/alginate matrix, 199, 202kappa-type carrageenan, 356lambda carrageenan, 356standard kappa-carrageenan, 357at various amplitude, 255fat various temperatures, 254f
Cellulase production, 54EFB. See Solid-state fermentation (SSF)by GDX02, 55, 56in SSF, 52
Cellulose, 52, 242, 272acidic sodium chlorite treatment, 278, 279fbiofuel, 130content analysis, 273, 273tdelignification process, 272, 274–275
acidic sodium chlorite, 275LPO with iron catalyst, 275Organosolv, 275purity of cellulose, 279frange and level of factors for experi-
mental design, 275tdemand, 272extraction methods, optimization of,
281–282extraction process, 276tfitted models for, 276thigher purity of, 280hydrogen bonding in, 247liquid phase oxidation (LPO), 279–280production, effects on, 55purity cellulose of Organosolv, 277, 278f,
279fyield of acidic sodium chlorite, 280
Central composite design (CCD), 243Chinicomycins, 204Chitinases, 287
hevamine, 288Chitosan, 6, 12, 13, 14, 15f, 160
absorbents, 104anaerobic digested sludge dewaterability,
16effect of cation type on dual conditioning
of sludge, 15–16
Chlorophyll, 174, 307Claus process, 296Conversion determination coefficient, 244Cynodon dactylon (L.) Pers. (bermuda), 228
broad-spectrum antibiotic compounds in,236
cardiac glycosides, 235collection, 229extraction, 229
susceptibility of gram-positive and -negative bacteria, 235
solid-phase extraction, 229with different solvents, 231textraction yield, 231separation of bioactive compounds by
TLC, 232fStrataTM-X 33 lm Polymeric Sorbent
reverse-phase (Phenomenex) car-tridges, 229
thin-layer chromatographic bioassay of,232f
DDarwin’s natural selection concept, 214Delignification processes, 272, 274, 277f, 278f,
279fby Design Expert software, 275, 276t
Design Expert software, 275, 340, 344v6.0.8, 243version 7.1.6, 21, 24
Design of experiment (DOE), 20, 21t, 82, 243Dielectrophoresis (DEP)
ASMC construction, utilitzation of wire-cloth for
analytical method, 68biofilms reactor and treatment system,
67–68COD, removal efficiency of, 69immobilization, 67medium, composition of, 67microorganisms, 66–67pH effect, 69–70wirecloth, 67
positive effect, 68use of, 66
Dietzia, 204Diffusion-controlled period (DC), 264
mass transfer rate and mass transfer coef-ficient for, 268t
Dimensionally stable anodes (DSAs), 90Divinylbenzene (DVB), 161D-optimal design, 275, 282
by Design Expert software, 275, 276t
414 Index
RSM, 340Drug-resistant pathogens, 228Dry adsorption process, 296
carbon-based materials, 296metal-based materials, 296polymeric materials, 296porous materials, 296
Dual-conditioning mechanism, 16anaerobic digested sludge dewaterability
capillary suction time, 13–14cation type effect, 15–16low molecular weight chitosan, 16
Dual-mode controller (DM), 212performance of, 216f
proposed DM, 217tDye-sensitized solar cell (DSSC), 313
components of, 314electrolyte, 316photoanode, 315photocathode, 316–317photosensitizer, 314–315
nonnatural-based DSSCs, type of counterelectrode for, 317t
performanceby different types of electrolytes, 317twith different thin films and thickness,
316tsimplified mechanism of, 314fand silicon-based solar cell, 313
EEco-composite materials, 242Eichhornia crassipes, 5Electrolyte, 93, 314, 314f, 316
concentration and removal %, 94ttype of counter-electrode for, 317t
Empty fruit bunch (EFB), 29, 175oil palm empty fruit bunch, 52. See also
Empty palm oil fruit bunch (EFB)under solid-state fermentation (SSF) pro-
cess, 174Empty palm oil fruit bunch (EFB)
cellulase production, Aspergillus sp.GDX02
b-glucosidase, 54biomass, effects of, 55carbon sources, 52EFB saccharification, 53, 56enzyme assay, 53enzyme extraction, 53fermentation process, 52initial moisture content, 55lignocellulose, 52
nitrogen source concentration, 55protein determination, 53xylanase activity, 54
composting processexperimental material, 29mesophilic bacterial consortium prepa-
ration, 29pH, 28, 30–32procedure, 29–30sampling and analysis, 30substrate moisture, 28, 30–31temperature, 28, 30, 32
incineration and mulching, 28Entrapped lipase, leakage of, 199, 200Environmental Quality Regulation 1996 by
Malaysian Government, 321Enzymatic devulcanization, 191Enzymes, 12, 160. See also Hydrolases
extraction, 53genetically modified microorganisms, 160industrial enzymes, SSF in, 52saccharification rate of GDX02 cellulase,
56various immobilization methods for, 198
Escherichia coli (E. coli), 134, 173, 174, 228,230, 233t, 234t
Ethanol, 37, 39, 47, 130, 193, 221concentration profiles of, 224f, 225C. dactylon crude extracts
antimicrobial activity of, 233textraction yield of, 231t
in disc diffusion bioassay (crude extract),231
fermentation process, 223GC SRI 8600C, 45in preparation samples for SEM analysis,
163–164from seaweed, 130
fermentation of, 131, 133t, 134separation of bioactive compounds from,
232fin thin-layer chromatographic bioassay,
230, 231, 232ftransesterification of crude JCO, 199
Eucheuma denticulatum, 250Extracted PKC cellulose, FTIR analysis of,
280–281, 281f, 282Extraction
and calcination, 305of C. dactylon, 229and determination of 5-aminolevulinic
acid, 176of enzyme, 53of hydrolases, 289, 290, 293
Index 415
Extraction (cont.)of iota-carrageenan, 254liquid–liquid extraction, 38–39solid-phase extraction, 229ultrasonic-assisted, 139ultrasound-assisted, 252–253yield, 231
of C. dactylon
FFe/Ti-NaY heterogeneous catalysts
advantages, 98catalyst preparation, 98–99decolorization efficiency
of Amaranth, 99–101drawbacks, 98fast charge carrier
recombination, 98sonocatalytic process, 99
Fed-batch application in industrial bioprocess,219–220
Ferric chloride, 6, 194Flash pyrolysis
bio-oil, 182oil production, 183
physicochemical properties, 184tFlavonoid microencapsulation, Orthosiphon
stamineuschemicals, 138–139field emission scanning electron
microscope, 140HPLC analysis, 139moisture content, 140, 141particle morphology, 142–143plant material, 139spray drying, 140total flavonoid content, 139–142ultrasonic-assisted extraction, 139WPI to maltodextrin ratio, 142
Flavonoids, 138, 143, 228, 235microencapsulation of, 143total content, 139–140, 141, 142f
Formaldehyde-based adhesives, 338Fossil fuels, 74, 81, 82, 295, 296Fourier transform infrared (FTIR)
spectroscopy (FTIR), 273, 357, 367carrageenan functional group composition,
358–360of semi-refined carrageenan at various
KOH concentrations, 359fof cellulose obtained from PKC
under different conditions, 281fof extracted PKC cellulose, 280
and GC–MS, waste chicken fat pyrolysis,75
MPA, PNIPA polymerizationband characteristics, 368–369, 369fmethodology, 368
Fresh palm kernel (Elaeisguineensis var. te-nera), 273
analysis of cellulose content and hemicel-lulose released, 273
isopropanol, 273Freundlich isotherm, 121, 122, 123f, 125, 376,
377, 378Fulvic acid-like substances, 4, 7
GGelatine, 160Gel-filtration chromatography (GFC), 291Gelidium amansii, 131, 132t, 133tGenetic algorithm (GA), 212
performance of, 216fproposed GA, 217t
Genetic algorithm modelling, 214–215chromosome, 214crossover operation, 215
Ginseng roots and cultured cells, saponinsfrom, 251
Glass fibre-reinforced polymer (GFRP)material
mechanical property, 395properties, 395seawater and weathering degradation test,
395layup fabrication technique, 396mass gain and immersion period,
397–398microscopic examination, 398salinity etching effects, 397specimen preparation, 396water absorption and micrographic
tests, 396–397Global warming, 321, 329Glucose, 24, 29, 46, 52, 223, 244t
activity of b-glucosidase, 53, 55in Alaria crassifolia, 132tin batch fermentation of thermophilic
anaerobic sludge, 48fon beta-glucosidases, 56fconcentration profiles of, 224fcontent extraction, 242in Gelidium amansii, 132t, 133tin hydrogen production, 47in Saccharomyces cerevisiae, 133ttotal content analysis, 243
416 Index
in Ulva pertusa, 132tyield, 53
Glycosides, 5, 228cardiac glycosides, 235
HHeme, 174Hemicellulose, 3, 4, 52, 84, 242, 247, 251,
272, 280analysis of hemicelluloses released, 273hemicellulose-free PKC fiber, 274, 281in raw POME, 36removal processes, 274, 275–276, 275t,
276t, 277f, 281talkali treatment, 274hot water treatment, 274range and level of factors for experi-
mental design, 275tregression analyses, 275
removal time (HRT), 275Hevamine, 288Hevea brasiliensis, 286
latex in, 287–288, 293purification of patatin-like protein from,
291lipid acyl hydrolase (LAH), 290screening for, 290f
Hevea Cathepsin G, 288Hexagonal mesoporous molecular sieves
(HMS) silica, 304BET analysis, 306–308bleaching and regeneration (solvent
extraction and calcination), 305characterization, 305DFT differential pore volume distribution,
307, 307fdosage of acid and ratio of bleaching
material, 307, 307tporous characteristics and bleaching earth,
306tregenerability of, 308–309SEM images of, 306fsynthesis of, 304–305
High internal phase (HIPE) route, 160, 161,164
Hollow fiber production, 323dope composition, 323tspinning conditions, 234t
Hot water treatment, 272, 274hemicellulose removal from PKC with,
277fin purity of cellulose, 279fin yield of cellulose, 278f
LPO with, 280Organosolv with, 280
Humic acid, 28, 112, 113, 116like substance, 7
Hydrochloric acid (HCl), 32, 108, 176, 242,274, 277, 289, 373
Tris–HCl, 291, 293H2S adsorption test, 297
adsorption by adsorbents, 297time duration between experiments
(TDBE), 297Hydrolases
extraction, 289, 290qualitation of purity by SDS-PAGE, 292
lipolytic acyl hydrolase (LAH) activity,292
quantitation of protein by Bradford’s Pro-tein Assay, 292
screening, 290–291lipid acyl hydrolase (LAH), 290, 290f
separation by SephacrylTM S-200 Gel Fil-tration, 291–292
elution pattern of, 291fskim latex serum, types of proteins
in, 287–288use in industries, 287
Hydrolysis, 163, 195, 199, 201, 395acid hydrolysis, 130, 132t, 134alkaline hydrolysis, 134anaerobic digestion mechanism, 4cationic hydrolysis products, 15, 16enzymatic hydrolysis, 130, 131, 132t, 134,
347hydrolases in, 287of plant fibre, 202treatment process, 243
IIB-00208, 204Immobilization methods for enzymes
adsorption, 198covalent binding, 198cross-linking, 198entrapment, 198
entrapped lipase, leakageof, 199, 200
of lipase, 198–199, 200lipase activity, 198
reusability, 199, 201transesterification process
parameters, 199Immobilization of lipase, 198–199
lipase activity, 198
Index 417
Immobilized B. subtilis cells. See also Immo-bilized cell technology
morphology of, 166–167Immobilized cell reactor, preparation of, 162Immobilized cell technology, 160
immobilized matrices for cell support, 160production of a-amylase by, 161
In vitro antimicrobial activity. See Cynodondactylon (L.) Pers. (bermuda)
Industrial enzymes, 160. See also a-amylaseproduction; Hydrolases; Skim latexserum
Interfacial polymerization (IP) techniqueBPA toxicity, 112methodology, 113polyamide membrane, 112polyester thin film composite membrane
performance testingcharacteristics, 113materials, 112–113membrane permeability study, 114–115NOM solution model, 113, 116salt and organic removal, 113–114salt rejection study, 115–116salt solutions, 113triethanolamine, 112
Interpenetrating polymer networks (IPNs), 198Iota-carrageenan (i-carrageenan), 250
colorimetric determination of, 253correlation of solid–liquid mass transfer
coefficient, 257–260experimental and predicted mass
transfer coefficients, comparison,260f
Fick’s second law of unidirectionaldiffusion, 257
seaweed particles swelling diameter,258
solid–liquid mass transfer coefficient,259
effect of particle diameter on, 256–257at different diameter of seaweed parti-
cles, 256fequilibrium yield, 257fp and q values of, 257fseaweed particles swelling, 257f
effect of temperature on, 255–256at different temperatures of, 256f
extraction from seaweed, 251extraction yield, 254
effect of ultrasonic wave amplitude on,254–255
extraction time at different amplitudesof ultrasound, 255f
at various temperatures, 254fsolid–liquid mass transfer coefficient, 251ultrasonic waves, determination of ampli-
tude of, 253intensity of ultrasound, 253
ultrasound-assisted extraction, 252experimental apparatus used for, 252f
Iota-type carrageenan, 356Isopropanol, 161, 273
JJapanese Industrial Standard (JIS 5908-1994),
340Japanese Standard JIS8101, 273Jatropha curcas (J. curcas) oil (JCO),
197–198Jatropha curcas pressed cake
bio-oil production, 82empirical correlations, 86product characterisation, 85–86pyrolysis, 83yield, 84
physicochemical properties, 83t
KKaolin hollow tube microstructure
advantage, 381applications, 381k/p ratio effects
dry jet wet spinning, 383hydrodynamically unstable viscous fin-
gering, 386materials, 382powder characterization, 382, 384scanning electron microscope, 383–384SEM images, 385spinning solution preparation, 382–383spongelike structure, 386viscosity measurement, 383, 385–386
j-carrageenan, 198Kappa-type carrageenan, 356Kenaf, 242
2D contour plot and 3D response surface,246f
biomass, 245cellulose, 242glucose content extraction from, 242hemicelluloses, 242
418 Index
hydrogen bonding, 247hydrolysis treatment process, 243lignin, 242total glucose content analysis, 243
Kenaf-retting wastewater (KRW)acclimatization, activated sludge
adaptation process, 63COD removal efficiency, 62–63genotype appearance, 63inoculums, 61microorganisms, 60sample analysis, 62SBR system, 61–62
characteristics of, 61components, 59, 60
Klebsiella spp., 230, 233t, 234, 234tKuster’s agar (KUA), 205
LLambda carrageenan, 356Langmuir isotherm, 121, 122fLatex serum. See Skim latex serumLaticifers, 287Lead ion adsorption, activated carbon
adsorbent, 120aqueous solution, 120batch adsorption studies, 120–121isotherms
Freundlich isotherm, 121Langmuir isotherm, 121results, 122–123
kineticspseudo-first and second order models,
121results, 123–124
thermodynamicsenthalpy and entropy, 122Gibbs free energy, 122results, 124
Lignin, 4–5, 242, 272, 273tin palm kernel cake (PKC), 338removal process, 130
Lignocellulosic material, 242Lipid acyl hydrolase (LAH), 290, 290f, 292,
293Liquid phase oxidation (LPO), 272, 279–280
with alkali pretreatment, 281fLow-density polyethylene/tapioca starch-
based biofilm preparationbiodegradation analysis
fungi growth, 351–353methodology, 350
mechanical testingelongation at break, 350, 351methodology, 350polymer compatibility, 350–351tensile strength, 350, 351
sample preparation, 349Luria–Bertani medium, 161
MMaillard reaction, 5, 7Malaysia, 19, 28, 190
biodiesel production company, 82crude palm oil production in, 304palm oil mill industry in, 3
Maltodextrin, 153a-lac denaturation, 154b-lg denaturation, 155reducing protein denaturation, 156
Marine actinomycetes, 204–205growth, influence of
incubation temperature on, 207–208incubation time on, 209isolation media on, 206pH on, 206seasalt concentration on, 208
isolation from marine sponge, 207fMarine sponge, mesophyll part of, 205Marinophilus, 204Mass transfer, 267
rate, 268tMass transfer coefficients, 264–265, 268t, 269
correlation of solid–liquid efficient,257–260
Medicinal plants, 228Melamine–urea–formaldehyde resin, 338, 339Melanoidin, 4, 5, 7Membrane characterization
permeance P (in GPU), 324, 327fthermogravimetric analysis, 324
Membrane technology, in gas processing, 3223-Mercaptopropionic acid (MPA), PNIPA
polymerizationFourier transform infrared spectroscopy
band characteristics, 368–269methodology, 368
LCST of PNIPAmethodology, 368phase transition, 369
Methanogenesis, 4Micrococcus sp., 66Mixture. See Whey protein isolate (WPI)Multistep action (MSA) Q-learning, 222
Index 419
NNatural gas sweetening, 296Natural gas utilization, 322Natural rubber (cis-1,4-polyisoprene), 286
hevein, 288processing, 286–287proteins in, 287
N-isopropylacrylamide (NIPAAm), 366NiTi alloy
advantages, 389–390applications, 389solid-state synthesis
methodology, 390Ni–Ti binary alloy system, 390primary and secondary reactions, 393SEM micrograph, 390, 391sintering, 391–393XRD spectra, 391, 392
N-methyl-2-pyrrolidone (NMP), 323, 331,382, 383
OOil palm trunk (OPT) sap
bioethanol production, 22ANOVA and model development,
21–23biomass preparation, 20culture preparation and fermentation,
20–21face-centered CCD design layout, 21,
22graph-based discussion and model val-
idation, 23–24one-factor-at-a-time method, 20pretreatment, 19–20statistical design of experiment method,
20characteristics, 19
Oil-free PKC fiber (PKC), analysis of, 273,273t
One-factor-at-a-time (OFAT) method, 20Organosolv processes, 272, 274, 275t, 280
delignification, 276twith organic acids, 277, 278fpurity of cellulose using, 279f
Orthosiphon stamineus leavesbioactive compounds, 138flavonoid degradation, spray drying
chemicals, 138–139field emission scanning electron
microscope, 140HPLC analysis, 139methodology, 140
moisture content, 140, 141particle morphology, 142–143plant material, 139total flavonoid content, 139–142ultrasonic-assisted extraction, 139WPI to maltodextrin ratio, 142
Oxoid nutrient broth, 66
PPalm kernel cake (PKC), 272, 273, 338
alkali-pretreated PKC, 277, 280analysis of, 273textracted PKC cellulose, 280–281FTIR spectra of cellulose, 281fhemicellulose removal from, 277fhemicellulose-free fiber, 274hot water-pretreated PKC, 278, 280oil-free fiber. See Oil-free PKC fiber
(PKC), analysis ofpowder, preparation of, 339purity of cellulose PKC, 279utilization of, 339on water absorption of particleboard, 342
optimization of process factors withproperties of particleboard with, 344
on static bending test (MOE and MOR)of particleboard, 343–344
on thickness swelling of particleboard,343
Palm oil mill effluent (POME)ABE fermentation, Clostridium
acetobutylicumABE recovery, 40bacteria growth profiles, 38liquid–liquid extraction, 37–38microbes and media, 37pH and reducing sugar profiles, 38process and analysis, 37solvent productions, 39sterilized POME supernatant vs. sludge,
38–39anaerobic digester, 297anaerobic digestion and colourants
lignin, 4–5mechanism, 4melanoidin, 5tannins, 5
anaerobically treated, 4. See also Anaero-bically treated palm oil mill effluent(AnPOME)
characteristics, 36hazardous characteristics, 104hydraulic retention time, 104
420 Index
oil and solid separation, H3PO4 effectdegumming, 105emulsifying activities and viscosity,
105higher temperature effect, 106methodology, 105–106neutralization, 105oil flotation rate, 105–108
raw, 4thermophilic hydrogen production
analytical method, 45batch fermentation, 45, 47–48cultural conditions, 46–47fermentation substrate preparation, 44hydrogen yield and production rate,
45–46seed sludge preparation, 44serum bottle experiments, 45
Particle swelling, 251, 395, 398of seaweeds, 256, 257f, 258swelling behavior of particles, 259
Particleboard productionapplications, 338formaldehyde-based adhesives, 338palm kernel cake (PKC) filter
ANOVA results, 341–342experimental design, 340lipid in, 338MUF resin preparation, 339preparation of, 339process factor optimization, 344protein content, 338static bending test, 343–344thickness swelling of particleboard, 343water absorption, 342
production and characterization, 340production of, 338
Petroleum-based fuels, 242Phenol, 161
adsorption of, 273ring, 372
Phenolics, 228, 235phenolic compounds, 372
Phosphoric acid (H3PO4)degumming process, 105neutralization, 105oil and solid separation, POME
degumming, 105emulsifying activities and viscosity,
105higher temperature effect, 106methodology, 105–106neutralization, 105
oil flotation rate, 105–108Photoanode, 313, 314, 315
material (size)/modification, 316tPhotocathode, 316–317, 317tPhotosensitizer, 314–315Photosynthetic bacteria, 174Plastics, 242, 338, 348–349
biodegradable plastics, 348, 349injection-moulded plastics, 348synthetic plastics, 348
Poly(N-isopropylacrylamide) (PNIPA)applications, 366characterization, 368polymerization
chain transfer agent, 366–367FTIR, 367–369materials, 3673-MPA. See 3-Mercaptopropionic acid
(MPA), PNIPA polymerizationPNIPA synthesis, 367telomerization, 366UV–vis spectrophotometer, 367
synthesis, 366Polycyclic aromatic hydrocarbons (PAHs)
characteristics, 90occupational exposures, 89oxidation, electrochemical process
anode effect, 92dimensionally stable anodes, 90electrochemical cell, 91electrode preparation, 91energy consumption (EC), 92, 95field emission scanning electron
microscopy, 91instantaneous current efficiency (ICE),
92, 95pH and electrolyte effect, 93–94selected ion monitoring (SIM) mode,
91Ti/SnO2 electrode structure, 92–93
Polyetherimide (PEI), 323CO2 separation. See Pyrolysis soaking timepolyethylene glycol (PEG) based CMS
membrane. See CO2 separation ofPEI/PEG CMS membranes
properties, 330Polyethylenimine, 66PolyHIPE (PHP) discs, 162, 163PolyHIPE (PHP) matrix, 160, 161, 163
polymer matrix, architecture of, 164characteristics of, 165t
sulphonated matrix. See Sulphonated PHPs(SPHPs)
Index 421
Polynomial regression model, 244Polyolefin, 348Polyvinylpyrrolidone (PVP), 323, 326, 327,
332Potassium persulfate, 161Propionic acid bacteria, 174Protein denaturation, 138, 142, 152, 155, 156Pseudomonas aeruginosa (P. aeruginosa),
228, 230, 232, 233t, 234, 234tPurification, 6
of active ingredients of plantmaterial, 250
of gases, 297of high value biomolecules, 366industrial water purification activities, 11methods for fermentation processes, 36partial purification of hydrolases protein,
291of seawater, 373steps on pooled fractions, 293
Pyrethrum flowers, pyrethrins from, 251Pyrolysis
Jatropha curcas, bio-oil productionbio-oil yield, 84empirical correlations, 86experimental tests, 83materials, 82–83product characterisation, 85–86thermo-gravimetric analysis, 82
waste chicken fats, bio-oil productionGC–MS and FTIR analysis, 75product yield, 75–76pyro-oil characterisation, 76–78raw materials, 74torrefied biomass, 74, 75ZSM-5 catalyst, 74–75
Pyrolysis centrifuge reactor (PCR), 182schematic diagram of, 182f
QQ-learning (QL) algorithm, 220, 221Q-learning-based controller, 222–223
for fed-batch yeast fermentation, 219–220baker’s yeast fermentation, dynamic
metabolism of, 220–221methodology, 221multistep action Q-learning, 222process flow diagram, 222f
Quantificationof a-amylase assays, 163of protein, 163of released cell numbers and cell dry
weight, 162–163
RRhodopseudomonas palustris (R. palustris),
174. See also Solid-state fermenta-tion (SSF)
cell growth determination, 176effect of initial pH, moisture content, and
incubation period on the productionof ALA, 177–178, 178t
Raw seaweed (Eucheuma denticulatum), 252,357
Recombinant plasmid pKTH10, 165Response surface methodology (RSM), 20,
275, 339D-optimal design, 275, 340RSM model, 21–23, 245t
Rhodococcus, 66, 204Rhodobacter capsulatus, 174Rhodobacter sphaeroides, 174Rubber waste, 190
SSabah sea area, 205fSaccharomyces cerevisiae (S. cerevisiae), 20
in anaerobic fermentation, 131ethanol production, 131, 134fermentation efficiency of, 23fermented seaweed (Laminaria japonica)
waste hydrolysate, 134in seaweed fermentation, 133t
Salinibacterium, 204Salinispora, 204Salvia officinalis L., polysaccharides from, 251Sarawak black peppers, 265Scanning electron microscopy (SEM),
325–326determination of pore and interconnect size
by, 162of hollow fiber membranes, 325f
Seaweedsbioethanol production
alkaline pre-treatment, 130–131fermentation, 131, 134pre-treatment reviews, 132–133saccharification pre-treatment, 130
carrageenan. See Carrageenanclassification, 356micrograph, NiTi alloy synthesis, 390, 391SEM analysis, preparation of matrix sam-
ples for, 163–164Semi-refined carrageenan (SRC) production
alkali treatment, 356–357KOH treatment
FTIR spectrum, 358–360
422 Index
functional group composition, 358,360–362
methodology, 357–358seaweed preparation, 357
Semporna, 204, 205, 209Sequencing batch reactor (SBR) system,
61–62Simultaneous thermal analysis, 184Single gas permeability test, 324, 326–327Skim latex serum, 287. See also Hydrolases
biochemical analyses, 289dye-binding method of Bradford’s
assay, 289quantitation of activity by hydrolases
assay, 289chromatography gel formation, 289enzymes in, 288Hevea Cathepsin G, 288types of proteins in, 287–288
Solar crops dryer, chimney effectair flow rate, 146air velocity, 146burner capacity, 146design layout, 147methodology, 148modified and conventional chimney
estimated draft, 148mechanical system, 149simulation program, 149
transparent and drying bed area, 146Solar energy, 146
conversion, 318photocathode in, 316–317
Solar radiation, 146Solid-state fermentation (SSF), 174
advantages, 52cell growth determination, 176–177cellulase production, EFB
b-glucosidase, 54biomass, effects of, 55carbon sources, 52EFB saccharification, 53, 56enzyme assay, 53enzyme extraction, 53fermentation process, 52initial moisture content, 55lignocellulose, 52nitrogen source concentration, 55protein determination, 53xylanase activity, 54
empty fruit bunch (EFB) under, 174incubation periods, 176initial moisture contents, 176
in ALA production, 177, 177f
initial pH, 176in ALA production, 177, 177f
preparation of starter culture and, 175R. palustris NRRL-B4276, 175
Solubility-controlled period (SC), 264mass transfer rate and mass transfer coef-
ficient for, 268tSolwaraspora, 204Sorbitanmonooleate (Span 80), 161Sovova’s model, 264Soxhlet extractor, 305, 309, 339Soybeans, oil from, 251Staphylococcus aureus (S. aureus), 228, 230,
232, 233t, 234, 234tStarch casein agar (SCA), 205Starch-degrading bacterium, 160, 164Streptococcus pneumonia, 230, 231, 233t, 234tStreptococcus pyogenes, 230, 233t, 234tStreptomyces, 204Styrene, 161
divinylbenzene polyHIPEs, 165Sulfhydryl-disulfide interchange reactions, 155Sulphonated PHPs (SPHPs), 164
characteristics of, 165telectron micrograph of cross section of,
168fmicrostructure of, 164f
Sulphonated polyHIPE polymer matrix, prep-aration of, 161
Sulphuric acid (H2SO4), 161, 242Supercritical fluid extraction (SFE), 263
of black pepper using CO2 as the solvent,264
and experimental procedure, 265equipment setup, 266f
Superoxide dismutase (SOD), 288Survival of the fittest, 214
TTannins, 4, 5, 7, 228, 235Terpenoids, 228, 235Test microorganisms, 230Tetrathionate hydrolase, 191
activity, 194–195assay, 193specific activity of, 195
Thermogravimetric analysis (TGA), 326–327,326f
experiments, 182, 185Thermophilic hydrogen production, POME
analytical method, 45batch fermentation, 45, 47–48cultural conditions, 46–47
Index 423
Thermophilic hydrogen production, POME(cont.)fermentation substrate preparation, 44hydrogen yield and production rate, 45–46seed sludge preparation, 44serum bottle experiments, 45
Thiobacillus ferrooxidans, 191cultivation of, 192growth of, absorbance at 440 nm, 194propagation of, 192secreted tetrathionate hydrolase by, 191
activity of enzyme, 194specific activity of, 195, 195fS4-intermediary pathway, 195
Trifluoroacetic acid (TFA), 152, 153Trioxacarcins, 204Trypsin inhibitor, 287
UUltra-performance liquid chromatography
(UPLC) analysis, 152, 153, 154, 156for protein content in WPI, 154
Ultrasonication, 251, 255ultrasonic extraction, 254
of i-carrageenan, 260ultrasonic method, 191, 331ultrasonic waves, 253, 255, 259
amplitude, effect of, 254, 259ultrasonic-assisted extraction, 139ultrasonic-assisted technology, 250ultrasonicator, 256
Ultrasound (US). See also Ultrasonicationamplitude of, 255fexperimental apparatus used for, 252fextraction, 256, 257intensity of, 253, 254ultrasound-accelerated process, 98ultrasound-assisted extraction, 252–253waves, 97–98, 252
VVerrucosispora, 204Vinylpyridine, 161Vitamin B12, 174Vulcanized scrap tires, 190–191
devulcanization process, 191
optical density, 192protein assay, 192–193protein content determination,
192–193, 194tetrathionate hydrolase assay, 193, 194Thiobacillus ferrooxidans in, 191
safe recycling method, search for, 191
WWastewater treatment using wirecloth elec-
trode. See Dielectrophoresis (DEP)Whey protein isolate (WPI), 138, 152
thermal denaturation, 152whey proteins and maltodextrin mixture,
143WPI solution, preparation, 153
degree denaturation of, 154kinetic study design and heat treatment,
153UPLC analysis, 153
Williamsia maris, 204Woad seeds, oil from, 251
XXRD spectra, 392f
NiTi alloy synthesis, 391, 392
YYeast. See also Baker’s yeast fermentation,
dynamic metabolism of; Q-learn-ing-based controller
concentration profiles of, 224ffermentation process, dynamics of, 220
ZZeolites, 296
breakthrough sulfur capacity, 299–300,299f
chemical compositions of, 298tand H2S concentrations, time evolution of,
299tZSM-5 catalyst, 74–75
424 Index