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Thesis (M. Sc. (Microbiology)) -- University of Limpopo, 2016 / Smart hydrogels could facilitate immobilisation of cellulases to allow recovery and decrease enzyme cost in the biofuel industry, as they have a soluble-gel transition. The aim of the study was to design and evaluate the use of smart hydrogels for immobilisation of cellulase system that can be recovered after hydrolysis of cellulosic biomass. Cellulases from Aspergillus niger FGSC A733 produced under solid state fermentation and commercial cellulases were used in immobilisation. Various support matrices prepared were poly-N-isopropylacrylamide (p-NIPAAm), poly-N isopropylacrylamide-co-Methacrylic acid (p-NIPAAm-co-MAA) and supermacroporous poly-crosslinked-Acrylamide-co-N,N’-Methylenebisacrylamide (p-crosslinked-AA-co MBA). Cellulases were coupled onto the support matrices by covalent attachment method through reactive groups of N-acryloxysuccinimide (NAS) or Methacrylic acid N-hydroxysuccinimide (NMS). The low critical solution temperature (LCST) of formed p-NIPAAm-co-MAA copolymer was determined by the inflection point method. The shrinking and swelling kinetics and pH sensitivity of p-NIPAAm-co-MAA copolymer and conjugates were characterised using a cloud point method. Hydrolysis of CMC using cellulase-microbeads-p-NIPAAm and cellulase-crosslinked-p-NIPAAm with different percentage gel showed activity trend of 0.05>1>10>5>0.1% and 5>2>10% respectively. HPLC analysis showed that supplementation of β-glucosidase in cellulase-crosslinked-p-NIPAAm conjugates increased glucose by 12 and 14-fold at 30 and 50 °C respectively in the avicel hydrolysate in comparison with no β glucosidase supplementation. In the hydrolysis of avicel using cellulase-crosslinked p-NIPAAm-co-MAA conjugate a total of 13.6 g/L of reducing sugar was liberated after three cycles. In comparison a total of 21.4 g/L of reducing sugars were released from avicel hydrolysis using cellulase-crosslinked-p-AA-co-MBA conjugate after 3 cycles. In contrast, reducing sugars released in thatch grass hydrolysis using free enzyme were 8 times greater than in cellulase-crosslinked-p-AA-co-MBA conjugate. Cellulase crosslinked-p-NIPAAm-co-MAA conjugates were more stable than free enzyme at 50 and 60 °C after 24 hour and 120 minutes of incubation respectively, but lost activities at 65 °C after 120 minute. Therefore the activity loss in the immobilised enzymes was more due to thermal inactivation during precipitation and recovery than incomplete recovery during precipitation cycles. The results show that cellulases immobilised on smart polymers with sol-gel transition could be used in hydrolysis of cellulose due to ease of recovery. Hydrolysis kinetics was efficient for both immobilised enzyme system (cellulase-crosslinked-p-AA-co-MBA and cellulase-crosslinked-p-NIPAAm-co MAA conjugate) since were re-used in hydrolysis of avicel. Therefore the use of these smart polymers for cellulase immobilisation can contribute in cost reduction of the enzymatic hydrolysis process in the biofuel industry. / National Research Foundation (NRF) , University of Limpopo financial aid office and Flemish Interuniversity Council (VLIR-UOS) fo

Atmospheric carbon dioxide levels have been steadily increasing from anthropogenic energy production, development and use. Carbon cycling in the terrestrial biosphere, particularly forest ecosystems, has an important role in regulating atmospheric concentrations of carbon dioxide. US West coast forest management policies are being developed to implement forest bioenergy production while reducing risk of catastrophic wildfire. Modeling and understanding the response of terrestrial ecosystems to changing environmental conditions associated with energy production and use are primary goals of global change science. Coupled carbon-nitrogen ecosystem process models identify and predict important factors that govern long term changes in terrestrial carbon stores or net ecosystem production (NEP). By quantifying and reducing uncertainty in model estimates using existing datasets, this research provides a solid scientific foundation for evaluating carbon dynamics under conditions of future climate change and land management practices at local and regional scales. Through the combined use of field observations, remote sensing data products, and the NCAR CESM/CLM4-CN coupled carbon-climate model, the objectives of this project were to 1) determine the interactive effects of changing environmental factors (i.e. increased CO���, nitrogen deposition, warming) on net carbon uptake in temperate forest ecosystems and 2) predict the net carbon emissions of West Coast forests under future climate scenarios and implementation of bioenergy programs. West Coast forests were found to be a current strong carbon sink after accounting for removals from harvest and fire. Net biome production (NBP) was 26 �� 3 Tg C yr�����, an amount equal to 18% of Washington, Oregon, and California fossil fuel emissions combined. Modeling of future conditions showed increased net primary production (NPP) because of climate and CO��� fertilization, but was eventually limited by nitrogen availability, while heterotrophic respiration (R[subscript h]) continued to increase, leading to little change in net ecosystem production (NEP). After accounting for harvest removals, management strategies which increased harvest compared to business-as-usual (BAU) resulted in decreased NBP. Increased harvest activity for bioenergy did not reduce short- or long-term emissions to the atmosphere regardless of the treatment intensity or product use. By the end of the 21st century, the carbon accumulated in forest regrowth and wood product sinks combined with avoided emissions from fossil fuels and fire were insufficient to offset the carbon lost from harvest removals, decomposition of wood products, associated harvest/transport/manufacturing emissions, and bioenergy combustion emissions. The only scenario that reduced carbon emissions compared to BAU over the 90 year period was a 'No Harvest' scenario where NBP was significantly higher than BAU for most of the simulation period. Current and future changes to baseline conditions that weaken the forest carbon sink may result in no change to emissions in some forest types. / Graduation date: 2013

Thesis (PhD)--Stellenbosch University, 2012. / ENGLISH ABSTRACT: In the developed and developing world, the use of lipids for the production of alkyl esters, also known as biodiesel, showed phenomenal growth during the ten year period up to the end of 2007. The main sources for these lipids are the oils extracted from oil seeds such as soya-, palm-, and rape seed, but other products in the food chain such as waste cooking oil (yellow grease) and animal fats are also used. In Africa and Asia vast tracks of land not previously tilled, are now being cultivated to yield oils which are not edible and in a number of countries intensive research is focused on lipid producing species such as algae. Meanwhile more evidence is coming to the fore pronouncing biodiesel and other first generation biofuels not to be the panacea for the predicament the world is facing on unbridled population growth, energy security concerns and environmental issues such as indirect land use changes, global warming and climate changes. The acceptance of the National Biofuels Industrial Strategy at Cabinet level has not yet resulted in significant commensurate activity in South Africa. The availability, other uses and volumes of selected feed stocks for biodiesel production invite debate on the choice between food- and energy security and the appropriateness of some identified socio-economical and socio-political drivers for a viable industry. Somehow the unique characteristics of South Africa and its resources seem not to feature in debate and constraints on the production of biodiesel, as described in this dissertation. The conventional process routes for commercial biodiesel production are based on a mature technology which has inherent pollution and economical limitations. This called for a detailed critical evaluation on process routes more environmentally friendly or involving fewer unit processes generating more desirable products, albeit with more severe process conditions. By comparison, the homogeneous alkali catalyst alcoholysis (HACA), the enzymatic catalyst alcoholysis (ECA) and the super critical alcoholysis (SCA) process routes as developed in this study, are found to be competitive on total manucturing costs as assessed, if results emanating from selected sensitivity analyses and optimisation studies, are accepted. The total manufacturing and operating costs in the selected process routes as estimated, assuming the same capacities for commercial biodiesel production, are dominated by feed stock costs. Incentives on depreciation and fuel levies are deemed not effective, if costs are compared to the price of fossil diesel at the retail level – October 2011. It is concluded that using the feed stocks indicated in the Strategy, commercial biodiesel production is not economically feasible in South Africa at present. In this study process routes and feed stocks were identified that can change this position. Note should be taken of the intensive research activities being conducted on second generation technologies and biorefineries in the developed world, as discussed in this dissertation. / AFRIKAANSE OPSOMMING: In die ontwikkelde en ontwikkelende wêreld het die gebruik van vette vir die produksie van alkielesters, ook bekend as biodiesel, in die tienjaarperiode tot die einde van 2007 fenomenale groei getoon. Die hoofbronne vir hierdie lipiede is die olies onttrek van oliesade soos soja-, palm-, en raapsaad, maar ander produkte in die voedselketting soos gebruikte kookolie en dierevette word ook gebruik. In Afrika en Asië word uitgestrekte stukke grond voorheen onbewerk, nou bewerk om olies wat nie eetbaar is nie, op te lewer, en in verskeie lande word intensiewe navorsing op vetproduserende spesies soos alge gedoen. Intussen kom meer bewyse na vore wat verklaar dat biodiesel en ander eerste-generasie biobrandstowwe nie die wondermiddel is vir die moeilike posisie wat die wêreld in die gesig staar oor onbeteuelde bevolkingsaanwas, kwellings oor energiesekuriteit en omgewingskwessies soos indirekte grondverbruike, aardverwarming en klimaatsveranderings nie . Die aanvaarding van die Nasionale Biobrandstowwe Industriële Strategie op kabinetsvlak het nog nie verhoogde soortgelyke aktiwiteite in Suid-Afrika tot gevolg gehad nie. Die beskikbaarheid, gebruike en volumes van gekose grondstowwe, lok debatte uit oor die keuse tussen voedsel- en energiesekuriteit en die toepaslikheid van sekere geïndentifiseerde sosio-ekonomiese en sosio-politieke stimulante vir ‘n lewensvatbare nywerheid. Op een of ander manier is die unieke kenmerke van Suid- Afrika en sy bronne nog nie in die debat op die knelpunte van biodiesel nie, soos beskryf in hierdie proefskrif. Die gewone prosesroetes vir kommersiële produksie van biodiesel is gebaseer op ‘n beproefde tegnologie met inherente besoedelings- en ekonomiese beperkings. Dit het gevra vir ‘n uitvoerige kritiese evaluasie van meer omgewingsvriendelike- en minder eenheidsprosesse wat meer gewensde produkte genereer, al is dit met erger prosesbepalings. By vergelyking, is dit bevind dat die homogene alkali-katalisator- alkoholisis (HAKA), ensiem-katalisator-alkoholisis (EKA) en die superkritiese-alkoholisis (SKA) prosesroetes soos in hierdie studie ontwikkel, mededingend is op ‘n totale vervaardigingskoste-vlak, as die resultate wat spruit uit geselekteerde sensiwiteitsanalises en optimiseringsstudies, aanvaar word. Die totale vervaardigings- en bedryfskostes soos beraam vir die gekose prosesroetes vir kommersiële biodieselvervaardiging vir dieselfde deursette, word oorheers deur grondstofkostes. Aansporings op afskrywings en brandstofheffings word gesien as nie effektief nie, as kostes vergelyk word met die prys van fossieldiesel op kleinhandelsvlak – Oktober 2011. Die gevolgtrekking word gemaak dat met die grondstowwe aangedui in die Strategie, kommersiële biodieselvervaardiging tans nie ekonomies gangbaar is vir Suid-Afrika nie. In hierdie studie is prosesroetes en grondstowwe geïdentifiseer wat die posisie kan verander. Kennis moet geneem word van die intensiewe navorsingsaktiwiteite op tweede-geslag tegnologieë en bioraffinaderye in die ontwikkelde wereld, soos in hierdie proefskrif bespreek.

Thesis (PhD)--Stellenbosch University, 2013. / ENGLISH ABSTRACT: The extraction of hemicelluloses prior to pulping that would have been dissolved in black liquor during pulping process, is an attractive alternative for pulp and paper mills as they, in addition to their core products, can increase their revenue by producing biofuels, biopolymers, paper additives and other chemicals. However, the amount of hemicelluloses extracted will be limited by the requirement to maintain pulp yield and pulp quality in comparison to existing pulping processes. In the present study, mild alkaline (NaOH) and dilute sulphuric acid conditions were used to extract hemicelluloses from Eucalyptus grandis, giant bamboo (Bambusa balcooa) and sugarcane (Saccharum officinarum) bagasse (SCB) prior to kraft or sodaAQ pulping processes. The effects of catalyst concentration, temperature and reaction time on hemicelluloses pre-extraction were studied, using a statistical experimental design to investigate conditions under which hemicelluloses could be extracted prior to alkaline pulping with minimal interference on cellulose (glucan) content. Subsequently, selected pre-extracted materials were subjected to kraft or sodaAQ pulping to evaluate the effect of the hemicelluloses pre-extraction on cooking chemicals, pulp yield and properties. This study also included evaluation of hot water hemicelluloses pre-extraction of SCB as it was part of a dilute sulphuric acid experimental design. The pulp yield, cooking chemicals and handsheet strength properties were compared with those obtained from kraft or sodaAQ pulping of non extracted raw materials. The results showed that alkaline pre-extraction options investigated preserves the pulp yield with minimal effect on handsheet strength properties depending on the choice of the subsequent pulping method while a fraction of xylan was extracted in polymeric form. In addition, less active alkali was required to delignify the xylan extracted materials. The integration of hemicelluloses pre-extraction by alkaline methods into a kraft pulping process was preferred for giant bamboo and E. grandis since it maintained pulp yields at desired industrial levels of 50%, and pulps within a bleachable kappa number range. Another advantage observed was the reduction in total cooking active alkali required to delignify alkaline extracted giant bamboo or E. grandis by 8or 3 percentage points respectively. However, the compromise to maintain the pulp yield was obtained when only 13.6% or 12.4% polymeric xylan was solubilised from giant bamboo or E. grandis respectively. Slight improvement in burst index of the handsheet was observed for extracted giant bamboo. On the other hand, pulp viscosity was increased by 13% due to the removal of low molecular weight hemicelluloses, while the breaking strength of the handsheet was also increased by 8.9% for pulps produced from extracted E. grandis. In the case of sugarcane bagasse, hemicelluloses pre-extraction by alkaline methods integrated well with the sodaAQ pulping process. It enabled a xylan recovery of 69.1%, while providing pulp with higher screened pulp yield (45.0%), with an advantageous decrease in kappa number (15.5). The handsheet tear index was superior without reduction in viscosity compared to pulp produced from non extracted SCB. On the contrary, results obtained from optimised dilute sulphuric acid pre-extraction of all the tested feedstocks were found to negatively impact subsequent kraft or sodaAQ pulping processes resulting in lower pulp yields and poorer strengths properties. Nonetheless, the differences were better when sodaAQ pulping was used compared to kraft pulping. SodaAQ protects the carbohydrates against the peeling reaction under alkaline medium. Conversely, pre-extraction of SCB with hot water resulted in low concentration of xylooligomers (5.7%), while the subsequent sodaAQ pulping resulted in no pulp yield reduction. The tear index and optical brightness of the handsheet papers produced from hot water extracted SCB were slightly improved while the breaking length, tensile and burst indexes were similar to those of pulps produced from non extracted SCB fibres. Of equal importance were the observed higher tear and burst indexes of handsheets produced from giant bamboo compared to E. grandis for both extracted and non extracted materials prepared under similar pulping processes. The advantage of bamboo was due to the larger fibre length and different morphological properties to those of hardwoods. However, the pulps produced from giant bamboo showed higher kappa numbers than those pulps produced from E. grandis due to the high condensation behaviour of bamboo lignins under alkaline conditions. Higher kappa numbers explained the higher demand for subsequent bleaching chemicals. In conclusion, the pulp mill biorefinery concept through hemicelluloses pre-extraction with NaOH can be achieved with modified kraft pulping or the sodaAQ pulping processes, but it depends on the type of raw material, extraction method and quality and performance requirements of a particular paper. The low pulping chemicals demand, comparable pulp yields and the improvement in some physico-chemical properties of the pulps from preextracted materials were observed. Furthermore, owing to xylan pre-extraction a larger amount of (extracted) material could be loaded into the digester as when non-extracted materials were used. / AFRIKAANSE OPSOMMING: Ekstraksie van hemiselluloses wat tydens verpulping in die swartloog opgelos word, bied ‘n aantreklike alternatief aan pulp- en papiermeulens om, addisioneel tot hul hoofprodukte, hul inkomste deur die vervaardiging van biobrandstowwe, biopolimere, papierbymiddels en ander chemikalië, daardeur te kan verhoog. Die hoeveelheid hemiselluloses wat ge-ekstraheer kan word, sal egter beperk word deur die vereiste dat pulpopbrengs en –kwaliteit tydens bestaande verpulpingsprosesse gehandhaaf moet word. In hierdie ondersoek is matige alkaliese (NaOH) en verdunde swawelsuurtoestande gebruik om hemiselluloses vóór kraft- of natriumantrakinoonverpulping uit Eucalyptus grandis, reuse bamboes (Bambusa balcooa) en suikerriet (Saccharum officinarum) bagasse, mee te ekstraheer. Die invloed van katalisatorkonsentrasie, temperatuur en reaksietyd is mbv ‘n statistiese, eksperimentele ontwerp ondersoek om die toestande te bepaal waaronder hemiselluloses, met minimale effek op die sellulose (glukaan) –inhoud, vóór alkaliese verpulping ge-ekstraheer kan word. Die pre-ge-ekstraheerde materiale, met hoë glukaan- en voldoende hemisellulosesinhoud, is vervolgens aan kraft- en natriumantrakinoonverpulping onderwerp om die invloed van pre-ekstraksie van hemiselluloses op die verpulpingsreagense, pulpopbrengs en - eienskappe vas te stel. Hierdie studie het ook die evualering van warmwater hemisellulosespre-ekstraksie van suikerrietbagasse, wat deel is van ‘n verdunde swawelsuur eksperimentele uitleg, ingesluit. Pulpopbrengs, die hoeveelheid verpulpingsreagense en handveleienskappe van dieselfde materiale wat nie vooraf ge-ekstraheer is nie, is vergelyk. Die resultate toon dat alkaliese pre-ekstraksie metodes wat ondersoek is die pulpopbrengs met minimale effek op handvel sterkte-eienskappe afhangende van die keuse van daaropvolgende pulpmetode kon handhaaf terwyl ‘n fraksie van xilaan in polimeriese vorm ge-ekstraheer is. Addisioneel, is minder aktiewe alkali benodig om die xilaan ge-ekstraheerde materiale te delignifiseer. Die integrasie van hemisellulosespre-ekstraksie dmv alkaliese metodes tydens ‘n kraft verpulpingsproses is vir reuse bamboes en E. grandis verkies omdat pulpopbrengste op ideale industriële vlakke van 50% gehandhaaf en is en pulp in ‘n bleikbare kappa nommergebied interval kon lewer. ‘n Verdere voordeel wat waargeneem is was die vermindering in die totale gekookte aktiewe alkali benodig vir reuse bamboes of E. grandis met 8 of 3 persentasiepunte onderskeidelik. Die kompromie om die pulpopbrengs te handhaaf is verkry toe slegs 13.6% of 12.4% polimeriese xilaan opgelos is vanuit reuse bamboes of E. grandis onderskeidelik. ‘n Effense verbetering in bars-indeks van die handvelle is waargeneem vir ge-ekstraheerde reuse bamboes. Pulpviskositeit het met 13% gestyg agv die verwydering van die lae molekulêre massa hemiselluloses, terwyl breeksterkte van handvelle ook met 8.9% toegeneem het vir pulp verkry uit pre-gekstraheerde E. grandis. NaOH pre-ekstraksie van 69.1% xilaan (droë massa) uit suikerriet bagasse (SCB) het ‘n hoër natriumantrakinoon, gesifte pulpopbrengs gelewer (45.0%) met ‘n verbeterde afname in kappa-getal (15.5) en uitstekende skeursterkte sonder verlaging in viskositeit, soos vergelyk met nie-ge-ekstraheerde suikkerrietbagasse. Daarteenoor het die resultate verkry met die geoptimeerde verdunde swawelsuur preekstraksie van al die getoetste rumateriale getoon om‘n negatiewe effek te gehad het op die daaropvolgende kraft- of natriumantrakinoonverpulping dws het laer pulpopbrengste en swakker sterkte-eienskappe opgelewer. Die verskille was nietemin kleiner toe natriumantrakinoonverpulping ipv kraftverpulping gebruik is. Antrakinoon beskerm die koolhidrate teen die afskilreaksie in alkaliese medium. Daarteenoor het pre-ekstraksie van suikerrierbagasse met warm water tot 'n lae hoeveelheid (5.7%) xilaanoligomere gelei, terwyl die daaropvolgende natriumantrakinoonverpulping geen verlaging in pulpopbrengs veroorsaak het nie. Skeursterkte en optiese helderheid van handvelle wat uit warm water ge-ekstraheerde suikerrietbagasse vervaardig is, het ietwat verbeter terwyl breek-, trek- en barssterkte dieselfde was as van suikerrietbagasse pulp wat nie ge-ekstraheer is nie. Net so belangrik was die waargenome hoër skeur- en barsindekse van handvelle vervaardig van reuse bamboes in vergelyking met E. grandis van beide geekstraheerde en nie ge-ekstraheerde materiale voorberei onder dieselfde verpulpings toestande. Bamboes se sterker eienskappe was as gevolg van die hoër vesellengte en ander morfologiese eienskappe as diévan loofhout. Pulp wat vervaardig is van reuse bamboes het ‘n hoër kappanommer getoon as pulp van E. grandis as gevolg van die hoë kondensasiegedrag van bamboeslignien onder alkaliese toestande. Hoër kappanommers kon die gepaardgaande hoër aanvraag vir bleikchemikalieë verklaar. Ten slotte, die pulpmeul bio-raffinaderykonsep nl. deur hemisellulosesekstraksie met NaOH gekombineer met óf ‘n gemodifiseerde kraft verpulping óf ‘n gemodifiseerde natriumantrakinoon verpulping, is wel uitvoerbaar. Dit word egter sterk beïnvloed deur die tipe ru-materiaal en die ekstraksie-metode gebruik, asook deur die kwaliteits- en gebruiksvereistes van verskillende tipes papier. ‘n Lae aanvraag vir verpulpingschemikalieë, vergelykbare pulpopbrengste en die verbetering in fisies-chemiese eienskappe van pulp vanaf pre-ge-ekstraheerde materiale is waargeneem. Verder kon, as gevolg van xilaan ekstraksie, meer ge-ekstraheerde materiaal in die verteerder gelaai word as wanneer nie-ge-ekstraheerde materiaal gebruik is.

Thesis (MScEng)--Stellenbosch University, 2013. / ENGLISH ABSTRACT: Whereas fuel used for transport and electricity production are mainly fossil–derived, there has recently been an increased focus on bio-fuels due to the impact of fossil derived fuel on the environment as well as the increased energy demand worldwide, concomitant with the depletion of fossil fuel reserves. Paper sludge produced by paper mills are high in lignocellulose and represents a largely untapped feedstock for bio-energy production. The aim of this study was to determine the composition, fermentability and optimum paper sludge loading and enzyme dosage for producing ethanol from paper sludge. This information was used to develop a model of the process in Aspen Plus®. The mass and energy balances obtained from the Aspen Plus® model were used to develop equipment specifications which were used to source equipment cost data. A techno-economic model was developed from the equipment cost data to assess the economic viability of the simultaneous saccharification and fermentation (SSF) process utilising paper sludge as feedstock. Nine paper sludge samples obtained from Nampak Tissue (Pty) Ltd. were evaluated in terms of ethanol production and those samples yielding the highest and lowest ethanol titres were selected for optimisation. This allowed for the determination of a range of ethanol concentrations and yields, expressed as percentage of the theoretical maximum, which could be expected on an industrial scale. Response surface methodology was used to obtain quadratic mathematical models to determine the effects of solid loading and cellulase dosage on ethanol production and ethanol yield from paper sludge during anoxic fed-batch fermentations using Saccharomyces cerevisiae strain MH1000. This approach was augmented with a multi response optimisation approach incorporating a desirability function to determine the optimal solid loading and cellulase dosage in fed-batch SSF cultures. The multi response optimisation revealed that an optimum paper sludge loading of 21% (w/w) and a cellulase loading of 14.5 FPU g-1 be used regardless of the paper sludge sample. The fact that one optimal enzyme dosage and paper sludge loading is possible, regardless the paper sludge feed stock, is attractive since the SSF process can be controlled efficiently, while not requiring process alterations to optimize ethanol production when different batches of paper sludge are processed. At the optimum paper sludge loading and cellulase dosage a minimum ethanol concentration of 47.36 g l-1 (84.69% of theoretical maximum) can be expected regardless of the paper sludge used. An economic assessment was conducted to ascertain whether ethanol production from paper sludge using SSF is economically viable. Three scenarios were investigated. In the first scenario revenue was calculated from the ethanol sales linked to the basic fuel price, whereas in the second and third scenarios liquefied petroleum gas (LPG) consumption at the paper mill was replaced with anhydrous and 95% ethanol respectively. In all the cases, paper sludge feed rates of 15, 30 and 50 t d-1 were used. The production of ethanol from paper sludge for ethanol sales (scenario 1) resulted in higher IRR and NPV values, as well as shorter payback periods, compared to replacement of LPG at the paper mill (scenarios 2 and 3). At an assumed enzyme cost of $ 0.90 gal-1 (R 2.01 litre-1), IRR values of 11%, 22% and 30% were obtained at paper sludge feed rates of 15, 30 and 50 t d-1. A sensitivity analysis performed on the total capital investment and enzyme cost revealed that the SSF process is only economically viable at a paper sludge feed rate of 50 t d-1 irrespective of the variation in capital investment. For the SSF process to be economically viable the enzyme costs must be lower than $ 0.70 gal-1 (R 1.56 litre-1) and $ 1.20 gal-1 (R 2.68 litre-1) for paper sludge feed rates of 30 and 50 t d-1 respectively. The SSF process at a paper sludge feed rate of 15 t d-1 was not economically viable even assuming a zero enzyme cost. A Monte Carlo simulation revealed that the SSF process is economically viable at a paper sludge feed rate of 50 t d-1 as a mean IRR value of 32% were obtained with a probability of 26% to attain an IRR value lower than 25%. The SSF process at lower paper sludge loadings is not economically viable as probabilities of 70% and 95% were obtained to attain IRR values lower than 25% at paper sludge feed rates of 30 and 15 t d-1 respectively. From this study it can be concluded that paper sludge is an excellent feedstock for ethanol production for the sales of ethanol at a paper sludge feed rate in excess of 50 t d-1 with the added environmental benefit of reducing GHG emissions by 42.5%. / AFRIKAANSE OPSOMMING: Aangesien dat brandstof vir vervoer en energie meestal vanaf fossiel afgeleide bronne kom, is daar onlangs ʼn groter fokus op bio-brandstowwe as gevolg van die impak van fossiel afgeleide brandstowwe op die omgewing en 'n verhoogde aanvraag na energie wêreldwyd, gepaardgaande met die uitputting van fossielbrandstof-reserwes. Papier slyk geproduseer deur papier meule is hoog in lignosellulose en verteenwoordig 'n grootliks onontginde grondstof vir etanol produksie. Die doel van die studie was om vas te stel wat die samestelling, fermenteerbaarheid, optimale papier slyk en ensiem ladings is vir die vervaardiging van etanol uit papier slyk. Die inligting was gebruik om 'n model van die proses in Aspen Plus® te ontwikkel. Die massa-en energiebalanse wat verkry is van die Aspen Plus® model was gebruik om toerusting spesifikasies te ontwikkel wat gebruik was om toerusting kostes te bereken. ‘n Tegno-ekonomiese model is ontwikkel om die ekonomiese lewensvatbaarheid van die gelyktydige versuikering en fermentasie proses “SSF” wat gebruik maak van papier slyk as grondstof te assesseer. Nege papier slyk monsters verkry vanaf Nampak Tissue (Pty) Ltd. is geëvalueer in terme van etanol produksie. Die monsters wat die hoogste en laagste etanol konsentrasies opgelewer het, is geselekteer vir optimalisering omdat dit toegelaat het vir die vasstelling van etanol konsentrasies en opbrengste, uitgedruk as persentasie van die teoretiese maksimum, wat verwag kan word in industrie. Reaksie oppervlak metodologie “RSM” is gebruik om wiskundige modelle te ontwikkel om die impak van papier slyk lading en sellulase dosis op etanol produksie en etanol opbrengs te assesseer. Die RSM is aangevul met 'n multi effek optimiserings benadering wat 'n wenslikheid funksie inkorporeer om die optimale papier slyk lading en sellulase dosis in gevoerde-enkellading SSF kulture te bepaal. Die multi effek optimalisering het getoon dat 'n optimale papier slyk lading van 21% (w/w) en 'n sellulase dosis van 14.5 FPU g-1 gebruik moet word, ongeag van die papier slyk monster. Die feit dat die optimale ensiem dosis en papier slyk lading dieselfde is ongeag die papier slyk monster, is aantreklik aangesien die SSF proses meer doeltreffend beheer kan word omdat proses veranderinge nie nodig is om die proses te optimaliseer nie. By die optimale papier slyk lading en sellulase dosis kan 'n minimum etanol konsentrasie van 47.36 g l-1 (84,69% van die teoretiese maksimum) verwag word ongeag van die papier slyk wat gebruik word. 'n Ekonomiese evaluasie is gedoen om vas te stel of etanol produksie vanaf papier slyk met behulp van SSF ekonomies lewensvatbaar is. Drie moontlikhede is ondersoek. In die eerste moontlikheid is die inkomste bereken vanaf etanol verkope gekoppel aan die basiese brandstofprys, terwyl in die tweede en derde moontlikhede, LPG by die papier meul vervang is met anhidriese en 95% etanol onderskeidelik. In al die gevalle was daar gebruik gemaak van papier slyk voer tempo’s van 15, 30 en 50 t d-1. Die produksie van etanol uit papier slyk vir verkope (moontlikheid 1) het gelei tot hoër IRR en die NPV waardes, sowel as korter terugverdien tydperke, in vergelyking met die vervanging van LPG by die papier meul (moontlikhede 2 en 3). Met ʼn ensiem koste van $ 0.90 gal-1 (R 2.01 litre-1) is IRR-waardes van 11%, 22% en 30% verkry teen papier slyk voer tempo’s van 15, 30 en 50 t d-1 onderskeidelik. 'n Sensitiwiteitsanalise uitgevoer op die totale kapitale belegging en ensiem koste het aan die lig gebring dat 'n SSF proses slegs ekonomies lewensvatbaar is op 'n papier slyk voer tempo van 50 t d-1 ongeag van die variasie in die kapitale belegging. Vir die SSF proses om ekonomies lewensvatbaar te wees, moet die ensiem kostes laer wees as $ 0.70 gal-1 (R 1.56 liter-1) en $ 1.20 gal-1 (R 2.68 liter-1) vir papier slyk voer tempo’s van onderskeidelik 30 en 50 t d-1. Die SSF proses was op 'n papier slyk voer tempo van 15 t d-1 nie ekonomies lewensvatbaar nie, selfs teen 'n ensiem koste van nul. 'n Monte Carlo-simulasie het getoon dat die SSF proses ekonomies lewensvatbaar is met 'n papier slyk voer tempo van 50 t d-1 omdat 'n gemiddelde IRR-waarde van 32% verkry is met 'n waarskynlikheid van 26% om 'n IRR-waarde laer as 25% te verkry. Die SSF proses teen papier slyk voer tempo’s van 30 en 15 t d-1 is nie ekonomies lewensvatbaar nie omdat waarskynlikhede van 70% en 95% onderskeidelik verkry is om IRR-waardes laer as 25% te kry. Daar kan van die studie afgelei word dat papier slyk 'n uitstekende grondstof is vir die produksie van etanol mits 'n papier slyk voer tempo van meer as 50 t d-1 bereik kan word. Die produksie van etanol vanaf papier slyk het die bykomende voordeel dat kweekhuis gasse (GHG) met 42.5% verminder word.

Thesis (MEng)--Stellenbosch University, 2014. / ENGLISH ABSTRACT: It was found that bacterial sludge from anaerobic water treatment systems is produced internationally at a rate of 60 grams per person per day and the accumulation of the potentially hazardous by-product has become of increasing concern. The produced bacterial sludge is frequently pumped into dams, dried out and used as agricultural fertilizer. This bacterial sludge is expected to have a relatively high heating value and as such, has the potential to produce energy from the biomass. It is, therefore, advisable to utilize this energy potential as an alternative to conventional sludge disposal. This project aimed to improve the yield of syngas by optimizing the reactor design to partially oxidize bacterial sludge using a sonochemical reactor that is operated at bulk atmospheric conditions. The effect of different conditions was investigated and the optimum settings for syngas production were found by investigating temperature, pressure and the effect of the amplitude of operation that regulates the energy input by the ultrasonic equipment. The optimum conditions were used to investigate the kinetics involved in this process as well as to determine the energy consumption by the process. It was also required to study the feasibility of partially oxidizing bacterial sludge using a sonochemical reactor instead of conventional steam gasification and also as an alternative means of sludge disposal. By eliminating this pollutant source, the future environmental threat posed by an increasing population size will be minimized and energy will be utilized from a thus-far wasted energy source. The syngas that is produced is used as a green alternative to fossil fuels in the Gas-to-Liquids (GTL) process to produce liquids fuels. A thus-far wasted energy source will be consumed and fossil fuels can be saved in the process. It was found that the maximum hydrogen mole percentage produced is 0.141 mole % of the vapour phase with the maximum carbon monoxide mole percentage in the vapour phase at 1.896 mole %. This shows an improvement on work conducted by Beyers (2011) of 59 % for hydrogen, 92% for carbon monoxide and a reduction of 49 % for carbon dioxide. A kinetic study of the process indicated that the rate equations that describe the hydrogen and carbon monoxide production are zero order and, therefore, independent of initial concentration of the sludge. The rate constants were 0.0146 (mol % hydrogen/s) and 0.0183 (mol % hydrogen/s) for hydrogen and carbon monoxide, respectively. It was found that the most severe change to the higher heating value of the feed was a mere 0.27 mJ/kg from an original value of 9.81 mJ/kg. This therefore confirms that the reaction has not proceeded to completion. The statistical model predicted a maximum value for hydrogen production at 0.151 mole % in the product gas, 0.01 mole % from the measured maximum. It was also found that hydrogen is produced during the sonolysis of distilled water and that this confirms that the hydrogen production during partial oxidation of the sludge sample comes mainly from the water present in the sludge. The hydrogen produced when only using water, was found to be 0.127 mole % and when using the active sludge, the value was 0.116 mole % hydrogen in the vapour phase. The thermal decomposition of calcium carbonate in the lime that is used to treat the pH of the unit where the sludge originates from, followed by the formation of carbon monoxide during the Boudouard reaction, led to an increased amount of carbon monoxide present in the product gas. Ultrasonic intensity is defined as the amount of energy that is transferred to the sample per cubic meter of the internal surface area of the reactor vessel. It was found that the intensity that was delivered to the reactant was lower than expected as the reactor was operating at an efficiency of only 36%. The design intensity was 1.44 W/m2 and the actual delivered intensity was 0.52 W/m2. Based on a maximum yield of 0.00012 Nm3/kg, the cost of syngas production under the conditions described by this study, would amount to R 19.98/Nm3. This cost only implicates the operational expenses and does not take further downstream processing and initial capital investment repayments into account. Conventional steam gasification at a yield of 0.67 Nm3/kg has an operational syngas production cost of R 1.48/Nm3. This process was therefore found to not be economically feasible as the cost of utilizing ultrasound as opposed to normal steam gasification is more than ten times more expensive. It was concluded that the process was successfully optimized by the redesigning of the reactor and that carbon dioxide production was limited by excluding oxygen from the feed gas. It was also concluded that the sonolysis of water and the thermal decomposition of calcium carbonate, followed by the conversion of carbon dioxide to carbon monoxide, supplements the syngas production under the current operational conditions. Based on the production of no methane during the course of this study, the sonochemical process can be tied into the GTL process after the steam reforming unit. Due to the relatively high carbon dioxide content, the process will need to join the main feed gas stream that is fed into the carbon dioxide removal unit before it enters the GTL process to correct the desired feed gas ratio. Based on the very low syngas yields, the low hydrogen to carbon monoxide ratio in comparison to the required ratio of 2 as well as the high energy intensity required for this process, it can be concluded that the partial oxidation of biomass sludge in a sonochemical reactor is not feasible as an alternative technology to conventional steam gasification. The operating costs of the sonochemical unit would be nearly ten times that of steam gasification and is therefore concluded to not be a competitive technology to conventional steam gasification. It is recommended that the reactor design is reinvestigated to improve the delivered ultrasound intensity as well as the surface area where the ultrasonic waves are intensified. This would eliminate dead-zones. It was also recommended that the argon gas is continuously bubbled through the reactant mixture during experiments to eliminate the degassing effect caused when the ultrasound is initially emitted. The gas outlet of the process can then be connected to an online gas chromatograph (GC) with a thermal conductivity detector (TCD) and flame ionization detector (FID) methanizer in series as the TCD does not destroy the sample and this setup would improve the analytical process. The production of carbon monoxide from lime as well as the production of hydrogen from water during sonolysis needs to be investigated. The effect of radicals can also be studied by the addition of a radical scavenger to the process. It is recommended that the experimental design is reinvestigated and a design that will deliver similar information utilizing fewer data points should be chosen. Based on this model as well as further kinetic testing, it is recommended that a complete ASPEN model is developed to simulate the energy requirements to tie the ultrasonic process into the commercial plant. Based on this model, a complete feasibility study can then be conducted to determine the capital costs involved, the operating costs, the repayment period as well as taking the current costs of sludge disposal into account. / AFRIKAANSE OPSOMMING: Daar is gevind dat bakteriele slik internasionaal geproduseer word deur anaerobiese waterbehandelingseenhede teen ‘n tempo van 60 gram per person per dag en dat die opberging van hierdie gevaarlike byproduk ‘n groeiende probleem word. Die geproduseerde bakteriele slik word in damme gestoor, uitgedroog of gebruik as kunsmis in die landbou bedryf. Daar word vermoed dat hierdie baketriele slik oor ‘n hoe verwarmings waarde beskik en het daarom die potensiaal om energie te produseer uit die biomassa. Daarom is dit voorgestel om alternatiewe prosesse te ondersoek om van hierdie slik ontslae te raak en moontlik die energie wat beskikbaar is te gebruik. Die projek is daarop gefokus om die produksie van syngas te verbeter deur die reaktorontwerp te optimeer deur gebruik te maak van parsiele oksidasie van slik onder atmosferiese kondisies deur klankgolwe te gebruik. Die effek van verskillende operasionele kondisies is ondersoek en die optimale vlakke van syngas produksie is gevind deur temperatuur, druk en amplitude wat die hoeveelheid energie wat oorgedra word aan die reaktor reguleer, te ondersoek. Die optimale kondisies is ook gebruik om die kinetiese aspekte van die proses te ondersoek en ook om te kyk wat die sisteem se energie benodighede behels. Die haalbaarheid om baketriele slik parsieel te oksideer in ‘n sonochemiese reaktor is vergelyk met dit van konvensionele stoom vergassing van die biomassa en is ook ondersoek as ‘n alternatief om van die slik ontslae te raak. Deur die slik te verwyder as ‘n potensiele bron van besoedeling, kan die toekomstige omgewing’s risiko wat deur die toename in die bevolkkingsgroote tot gevolg is, verwyder word deur ‘n energie bron te gebruik wat tot dusver geignoreer is. Die syngas wat geproduseer word kan dan gebruik word in die “Gas-to-Liquids” (GTL) process om vloeistof brandstowwe te produseer. Dus sal ‘n omgewingsrisiko verminder word, ‘n energiebron word benuttig wat nooit van tevore benuttig is nie en fosiel brandstowwe kan gespaar word. Die maksimum waterstof wat geproduseer is, was 0.141 mol % in die gas fase met ‘n maksimum waarde vir koosltof monoksied van 1.896 mol % in die gas fase. Dit toon ‘n verbetering van 59 % vir waterstof, 92 % vir koolstof monoksied en ‘n vermindering van 49% in die koolstof dioksied wat deur Beyers (2011) geproduseer is. Die kinetiese studie het ondervind dat die “rate equation” van waterstof en koolstofmonoksied beskryf word deur nul-orde kinetika. Hierdie konstantes was 0.0146 (mol % waterstof/s) en 0.0183 (mol % waterstof/s) vir waterstof en koolstofmonoksied. Daar is ook gevind dat die grootste moontlik verandering in die hoe verwarmings waarde van die biomassa is ‘n skamele 0.27 mJ/kg van die oorspronklike waarde van 9.81 mJ/kg. Hierdie waarneming staaf dus die uitkoms dat die reaksie dus nie tot die einde verloop het nie. Die statistiese model het ‘n maksimum van 0.151 mol % voorspel wat 0.01 mol % meer was as die waarde wat gemeet is. Dit is ook gevind dat waterstof geproduseer word deur die sonoliese van water en dat hierdie bykomende waterstof deel uitmaak van die produkgas aangesien die slik grootliks uit water bestaan.Die hoveelheid waterstof in die gas fase wat geproduseer is tydens sonoliese van ‘n suiwer water monster, was 0.127 mol %. Die hoeveelheid waterstof in die gas fase wanneer die slik behandel is ten optimal kondisies, was 0.116 mol % gemiddeld. Die hitte degradering van kalsium karbonaat wat teenwoordig is in die kalk wat gebruik word om die pH van die produksie eenheid te reguleer, gevolg deur die Boudouard reaksie, het tot gevolg dat addisionele koolstof monoksied ook gevorm word. Ultrasoniese intensiteit kan gedefineer word as die hoeveelheid energy wat oorgedra word aan ‘n reaktant gebasseer op die oppervlak area aan die binnekant van die reaktor. Die intensiteit waarteen die voermateriaal blootgestel word aan die klankgolwe was laer as verwag met ‘n 36 % effektiwiteit. Die ontwerp spesifiseer ‘n intensiteit van 1.44 W/m2 en die intensiteit wat fisies gelewer is, was 0.521 W/m2. Die maksimum produksie van syngas was 0.00012 Nm3/kg, wat lei tot ‘n operasionele koste van R 19.98/Nm3 onder die kondisies van hierdie studie. Hierdie koste neem nie die oorsponkilke kapitaal vir die konstruksie, of die koste van verdere behandelik van die gas, in ag nie. Konvensionele stoom vergassing teen ‘n opbrengs van 0.67 Nm3/kg het ‘n operasionele koste van R 1.48/Nm3 tot gevolg. Die proses is dus ekonomies nie ‘n aantreklike opsie nie aangesien die kostes van syngas produksie met ultraklank meer as tien keer meer is as konvensionele stoom vergassing. Daar is tot die gevolgtrekking gekom dat die reaktor optimering suksesvol was en deur geen stuurstof te voer nie, die koolstofdioksied persentasie verminder is. Daar is ook tot die gevolgtrekking gekom dat die sonoliese van water, en die hitte degradering van kalsium karbonaat, gevolg deur die Boudouard reaksie, die syngas produksie supplementeer. Aangesien geen metaan gedurende hierdie studie geproduseer is nie, kan die sonochemiese proses inskakel by die GTL aanleg na die stoom hervormingseenhed. As gevolg van die hoe koolstofdioksied konsentrasie, sal die prosesstroom gemeng moet word met die produk stroom uit die stoom hervormings proses, wat gevoer word na die koolstofdioksied verwyderings eenheid. Hierdie eenheid is daarvoor verantwoordelik om die korrekte verhouding van gasse vir die GTL voer stroom te reguleer. Gebasseer op die baie lae syngas opbrengs, die lae waterstof tot koolstofmonoksied verhouding en die hoe energie behoeftes, is daar tot die gevolgtrekking gekom dat die parsiele oksidasdie van die biomassa in ‘n sonochemiese reaktor nie ‘n haalbare alternatief is vir konvensionele stoom vergassing nie. Die operasionele koste van die sonochemiese eenheid is ongeveer tien keer meer as die van stoom vergassing en daarom is die proses nie kompeterend nie. Daar word voorgestel dat die reaktor ontwerp hersien word om die gelewerde intensiteit te verbeter, sowel as om die kontak area waar die klankgolwe gekonsentreer is, te vergroot. Dit sal dooie sones uitskakel. Daar word ook voorgestel dat argon gas gedurende die eksperiment aanhoudende geborrel word deur die reaktant vloeistof in die reaktor om die ontgassingseffek uit te skakel sodra die klankgolwe aangeskakel word. Die gas uitlaat kan dan inlyn gekoppel word aan ‘n gas chromatograaf met ‘n termiese geleidings detektor (TCD) en ‘n vlam ionisasie detektor (FID) met metaan omskakeling, aangesien die TCD nie die monster vernietig nie. Hierdie opstelling behoort analitiese methodes te verbeter. Die produksie van koolstofmonoksied uit kalk sowel as die produksie van waterstof uit water gedurende sonoliese, moet verder ondersoek word. Die effek van radikale kan ook verder bestudeer word deur die gebruik van ‘n radikaal rower gedurende die proses. Daar word ook voorgestel dat die statistiese ontwerp herondersoek word sodat minder eksperimente gebruik kan word om soortgelyke resultate te bekom met minder data punte. Gebasseer op hierdie nuwe model en ‘n kinetiese studie, word dit aangeraai dat ‘n volledige ASPEN model gebou word om te simuleer hoe hierdie sonochemiese eenheid sal inskakel met die kommersiele eenheid. Dit sal dan moontlik wees om die energie benodighede van die proses te verstaan en gebasseer daarop, kan ‘n volledige haalbaarheid studie gedoen word wat kyk na oorspronklike installasie kostes, onderhouskostes, operasionele kostes sowel as die terugbetaling van die konstruksie kostes. Dan kan ‘n vergelyking getref word met die huidige kostes om van hierdie slik ontslae te raak en om die slik as ‘n brandstof te benut.

Thesis (MEng)--Stellenbosch University, 2014. / ENGLISH ABSTRACT: The complexity of adopting a new crop-based biodiesel feedstock into South Africa given the prevailing environmental, economic and social concerns facing the country are addressed in this study by utilising a Systems Thinking approach. Solaris is a new variety of Tobacco developed specifically as an energy crop over the last twelve years by Italian companies Plantechno and Sunchem. Small-scale trials have been underway over the last year in the Loskop Valley farming community in the Limpopo Province of South Africa. These trials have been managed by the newly-formed local entity, Toboil (Pty) Ltd. In order to assess the viability of introducing Solaris into Loskop in terms of addressing the current diesel and electricity needs of the community and larger over-arching biofuel goals of South Africa, the full System Dynamic Modelling process was employed. This included significant research, stakeholder engagement, a Systems Thinking workshop as well as model development and simulation using the System Dynamics programming tool, Vensim. Following the simulation of various scenarios, it was determined that in order for Solaris implementation to have the greatest impact on the diesel and electricity independence desires of the community, as well as maximising job creation and avoided greenhouse gas emissions, the first five to ten years of implementation may only achieve low to moderate profitability. It was further concluded that if crop-based biofuels are to help meet the rural development goals of South Africa then significant investment and skills transfer is required. In order to address both of these, a modular development process is advocated and should be aided and mentored by members of the commercial farming industry. / AFRIKAANSE OPSOMMING: Die kompleksiteit van die aanvaarding van ‘n nuwe oes-gebaseerde bio diesel roumateriaal in Suid-Afrika in die heersende omgewings-, ekonomiese- en sosiale kommer wat die land ervaar, word in hierdie studie aangespreek deur gebruik te maak van ‘n Sistemiese Denke Benadering (Systems Thinking approach) Solaris is ‘n nuwe variasie Tabak wat deur twee Italiaanse maatskappye Plantechno en Sunchem oor die afgelope twaalf jaar spesifiek as ‘n bron van energie ontwikkel is. Kleinskaalse proewe is gedurende die afgelope jaar in die Loskop Vallei Landbougemeenskap in die Limpopo-provinsie van Suid-Afrika gedoen. Hierdie proewe word onder die toesig van die nuut gevormde plaaslike entiteit, Toboil (Pty) Ltd uitgevoer. Aansienlike navorsing, die aktiewe deelname van die onderskeie belanghebbende partye, ‘n Sistemiese Denke werkswinkel sowel as die ontwerp van ‘n simulasie model deur die gebruik van Sisteem Dinamieke Programerings program, naamlik Vensim, is ingespan om die lewensvatbaarheid van die moontlike aanplanting van Solaris te beoordeel. Die spesifieke gemeenskap se huidige behoeftes aan diesel en elektrisiteit sowel as Suid-Afrika se breër doelwitte aangaande bio-brandstowwe was as die grondslag gebruik waarop die volle Sistemiese Denke Benadering toegepas is. In Loskop omgewing was verskeie moontlike scenarios beproef en daar is op grond daarvan vasgestel dat ten einde die grootste moontlike inpak te maak op die afhanlikheid van diesel en elektrisiteit behoeftes van die gemeenskap, sowel as om die grootste moontlik werkskepping potensiaal te verwesenlik – terwyl die afskeiding van kweekhuis gasse verhoed word - die eerste vyf tot tien jaar van implementering baie lae winsgrens tot gevolg sal hê. Daar is ook verder afgelei dat afsienbare beleggings en opleiding benodig gaan word indien aangeplante bio-brandstowwe aangewend sou word om die landelike ontwikkelingsdoelwitte in Suid-Afrika te verwesenlik. Ten einde beide hierdie doelwitte aan te spreek, word ‘n modulêre ontwikkelings proses aanbeveel waar gevestigde lede van die kommersiële lanbou industrie, bystand en leierskap voorsien.

Thesis (MScEng (Process Engineering))--Stellenbosch University, 2008. / This report covers the development of a biofuels engine testing facility at Stellenbosch University. The motivation for the project was three fold: a) a desire to establish biofuels and engine testing know-how; b) to test the performance characteristics of biodiesel; and c) make a facility available for future research. The two main conclusions drawn from the initial test results are: 1) the test cell is fully operational and 2) biodiesel can be substituted for mineral diesel. To the author’s knowledge this is the first biofuel specific engine testing facility in South Africa. After a literature study the test cell was realised in three phases. • Firstly, the hardware layout was designed and the necessary equipment was sourced from respectable suppliers including the judicious use of good qaulity second hand components to minimize capital cost. • The test cell was then instrumented with new sensors. Key components among these are the K-type thermocouples, barometric pressure, humidity, oil pressure and an Allen-Bradley programmable controller to serve as a data acquisition card. Two software programs were chosen, ETA for the control of the test cell and RSLogix to program the programmable logic controller (PLC). • The complete system was then integrated, debugged and validated. The design methods and procedures have been documented throughout the project along with user manuals to facilitate further research. To determine the difference in combustion parameters between biodiesel and mineral diesel an autonomous power curve test was conducted. This revealed little difference in terms of performance between the two fuels, although biodiesel had on average a marginal 0.4% decrease in power over mineral diesel. The fuel consumption for pure biodiesel was found to be higher, which is as expected as it is has a lower calorific value than mineral diesel. As a final validation, an energy balance was conducted. Here the calculated calorific value of biodiesel was compared to the results from a calorie bomb test, and the two results were found to be within 2% of each of other. / Centre for Renewable and Sustainable Energy Studies

Thesis (MScAgric (Agricultural Economics)--University of Stellenbosch, 2009. / The growing scarcity of fossil energy, expressed by rising real prices, justifies an investigation into the viability of utilising alternative, sustainable energy sources. Another motivation is to mitigate CO2 pollution resulting from using fossil fuels, causing climate change. Biomass has the potential to become a major global primary energy source during the next century. In South Africa, a limited amount of land is suitable for high‐potential biomass energy sources like sugar cane or grain. Large areas of South Africa are, however, dry and more suitable for woody biomass production. Cultivating trees in short‐rotation‐system plantations provides a sustainable and effective way of producing biomass. The first part of this study investigated the physical capacity of the Cape Winelands District Municipality (CWDM) for woody biomass production in short‐rotation systems, based on a land availability assessment using Geographic Information Systems (GIS). The CWDM comprises about 2.3 million hectares, of which about 175 000 ha with a slope of less than 35% have been identified as suitable for woody biomass production. Within the CWDM, the following land use classes were excluded: nonagricultural land, such as urban areas, bare rock and mines; ecologically sensitive areas; as well as areas with slope gradients that are too steep for biomass production, due to limited accessibility and trafficability. This was followed by an assessment of suitable tree species and their productivity rates – also using GIS with climate data (i.e. temperature extremes, frost and mean annual precipitation) and terrain data. By combining the identified biomass production sites with the productivity rates of the identified species, an annual supply of woody biomass for energy generation at a medium productivity of about 1 412 000 tonnes of fresh biomass is expected, using exotic species like Eucalyptus claducalyx ( and about 1 306 000 tonnes, using indigenous species like Acacia karoo).