Thesis (PhD (Food Science))--University of Stellenbosch, 2006. / High-rate anaerobic bioreactors are used for the treatment of various wastewaters, of which the upflow anaerobic sludge blanket (UASB) bioreactor has the widest application, especially in the food and beverage industries. In an UASB bioreactor sludge develops in a particular granular or flocculent form and the success of the anaerobic process relies on the formation of active and settable granules. These granules are formed by self-aggregation of bacteria that can be divided into different trophic groups that are responsible for the metabolic breakdown of organic substrates. The successful performance of a bioreactor is influenced by the composition of the substrate which subsequently may have an impact on the microbial consortium present in the UASB granules. In order to determine if a change in the structure of the non-methanogenic microbial community takes place, UASB brewery granules were subjected to the sudden addition of different carbon sources at different concentrations. A shift in the microbial community did occur when the granules were subjected to lactate medium (5 g.l-1). No changes in the microbial community were observed when the granules were stressed with glucose medium as carbon source, regardless of an increase in the glucose concentration. In order to better understand the effect that different wastewaters may have on the microbial consortium present in different UASB granules, the polymerase chain reaction (PCR) based denaturing gradient gel electrophoresis (DGGE) technique and sequence analysis were used to fingerprint and identify the Bacteria and Archaea present in either, winery, brewery, distillery or peach-lye canning UASB granules. Each granule type showed distinct PCR-based DGGE fingerprints with unique bands, while other bands were found to be present in all the granules regardless of the wastewater being treated. Bacillus, Pseudomonas, Bacteroides, Enterococcus, Alcaligenes, Clostridium, Shewanella, Microbacterium, Leuconostoc, Sulfurospirillum, Acidaminococcus, Vibrio, Aeromonas, Nitrospira, Synergistes, Rhodococcus, Rhodocyclus, Syntrophobacter and uncultured bacteria were identified, representing different acidogenic, acetogenic and homoacetogenic Bacteria.Different methanogenic bacteria such as Methanosaeta, Methanosarcina, Methanobacterium and uncultured bacteria belonging to the group Archaea were also fingerprinted and identified from different UASB granules. In both these studies a DGGE marker was constructed that may be used to assist in the identification of bacteria. The DGGE marker can also be used to monitor the presence of bacteria over a time period during anaerobic digestion. Bioaugmentation or the enrichment of granules results in tailor-made granules that may be used for the treatment of specific wastewaters. One of the most important contributions to the maintenance and enhancement of UASB granule formation is the inclusion of suitable microbes in the granule structure. Enterobacter sakazakii was isolated from raw winery wastewater and was found to produce sufficient amounts of desired fatty acids. This bacteria was, therefore, incorporated into batch cultured granular sludge. In order to identify and monitor the presence of the incorporated E. sakazakii in the tailor-made granules, 16S rRNA gene sequence primers and PCR conditions were developed. The use of molecular techniques such as PCR-based DGGE and sequence analysis proved to be successful methods to fingerprint and identify the microbial consortium present in the different UASB granules.

published_or_final_version / Civil Engineering / Doctoral / Doctor of Philosophy

<p>This master's theses was carried out on assignment from Stockholm Vatten AB as a part of a project developing new waste water treatment techniques. The goal of the theisis has been to evaluate an anaerobic membrane bioreactor for treatment of waste water from Hammarby Sjöstad. The bioreactor has not been heated and the main interest has been to study the gas production, power consumption and the reduction of organic matter and nutrients.</p><p>The system has been completed with a reverse osmosis unit and a total of four batch runs have been made with good results. The use of reverse osmosis allows nutrient in the waste water to be reintroduced into circulation as the reverse osmosis concentrate can be used as crop nutrient.</p><p>The membrane unit is of VSEP ("Vibratory Shear Enhanced Processing") type and an extensive membrane test has been conducted. This so called L-test helped determine the most suitable type of membrane for the system to allow a higher ±ux and thus lower power consumption. The L-test gave good results and a new membrane with a poresize diameter of 0,45 μm was used.</p><p>The organic load on the bioreactor has been more or less constant, around 0,7 kg COD/day, during the seven weeks of testing. The reduction over the entire system including reverse osmosis has been large, around 99 % regarding organic matter and phosporus and 93 % for nitrogen, making the system suitable for waste water treatment except for high power consumption, around 2 kWh/m3. The production of methanegas has worked although it has been quite low, with average values of 0,13 m3 CH4/kg reduced COD.</p> / <p>Examensarbetet är utfört på uppdrag av Stockholm Vatten AB som en del av det pilotprojekt som utvärderar nya tekniker för avloppsvattenrening för Hammarby Sjöstad. Målsättningen med studien har varit att utvärdera ett system bestående av en anaerob membranbioreaktor för behandling av avloppsvatten från Hammarby Sjöstad. Bioreaktorn har inte varit uppvärmd och det som har studerats är reningseffekten, biogasproduktionen samt energiåtgången.</p><p>Systemet har även innefattat en omvänd osmosanläggning och totalt har fyra försök med denna gjorts med goda resultat. Analyser har koncentrerats till att utvärdera reduktion av organiskt material över membranbioreaktorn och av närsalter och metaller över omvänd osmos anläggningen. Bakgrunden till att använda omvänd osmos är att öka återföringen av näringsämnen från avloppsvatten. Resultatet av försöken med omvänd osmos gav ett koncentrat med högt näringsinnehåll och låg halt av tungmetaller vilket ger möjligheten att sprida det på åkermark.</p><p>Membranenheten är av typen VSEP ("Vibratory Shear Enhanced Processing") och ett membrantest har även utfötts för att finna det membran som passar systemet bäst med avseende på flöde och energiförbrukning. Det så kallade L-testet var omfattande och gav en klar bild över vad som skulle vara det bästa membranet. Det membran som visade sig passa systemet bäst var ett membran med en porstorlek på 0,45 μm. Belastningen av organiskt material på reaktorn under försöksperiodens sju veckor har varit mer eller mindre konstant och låg, cirka 0,7 kg COD/dygn. Reduktionen över hela systemet inklusive omvänd osmosanläggningen med avseende på organiskt material och fosfor har varit mycket hög, omkring 99 %. Reduktionen av kväve var som högst 93 %. Gasproduktionen har fungerat och har i genomsnitt varit omkring 0,13 m3 CH4/kg reducerad COD.</p><p>Energiförbrukningen för systemet i motsvarande fullskala blev omkring 2 kwh/m3.</p>

<p>Chile and Santiago are struggling with heavy environmental problems as a consequence of urbanisation and industrialisation. In the Santiago region the air is seriously contaminated and most of the rivers are classified as heavily polluted.</p><p>The aim of this thesis is to survey the industrial fluid waste situation in the Santiago region and to make suggestions on technological improvements or process changes. The purpose is also to study five different enterprises more closely and to give more detailed suggestions for improvement. Another purpose is to summarize relevant Chilean legislation.</p><p>Information, provided by the supervisory authority, about the release of industrial wastewater to rivers has been analysed. Deep interviews have been made with authorities and consultants. Five enterprises have been visited; a brewery, a dairy, a bakery, a producer of cooked meat and a surface treatment industry. The present treatment of the wastewater was studied at the plants and the information was completed with a questionnaire to the responsible at each company.</p><p>The contamination load released to the Chilean rivers is heavy. The rivers in southern Chile receive the biggest loads of BOD and SS and the rivers in central Chile were the most exposed to discharges of the metals Cr, Cu, Zn and CN as well as phenols.</p><p>The industrial discharge into the rivers of Santiago RM and Region VII is also to a large extent characterized by high concentrations of BOD and SS. Large releases of oils and greases, nitrogen and phosphorus are also fairly common, as are too high or too low pH levels. The food industry is the most contaminating sector, but also tanneries have great problems with effluents exceeding limits.</p><p>All five companies visited share the need to take measures towards more water saving technologies. The brewery, the producer of cooked meat and the surface treatment company also need end-of-pipe-treatment of their wastewater. In many cases, the recommended and most economic alternative is to separate the flows with the highest concentration of polluting substances for internal treatment, while releasing the rest of the wastewater to the outside sewage system. The costs of the suggested changes must be balanced against the present costs for treatment of wastewater and remaining solid waste as well as the costs for alternative treatments.</p><p>The economic incentives for Chilean companies to invest in wastewater treatment plants or to optimize the processes until today have been few. Cost reductions may be achieved by savings in water consumption and reuse of raw material. Another motive could be to keep “one step ahead” if the discharge limits in the future are tightened up leading to rising costs.</p> / <p>Chile och Santiago brottas med omfattande miljöproblem till följd av urbanisering och industrialisering. I santiagoregionen är luftföroreningarna svåra och de flesta floderna klassas som gravt förorenade av CONAMA, det chilenska naturvårdsverket.</p><p>Syftet med examensarbetet är att kartlägga situationen i santiagoregionen med avseende på industriell avloppsrening samt att ge förslag på förbättring av teknik eller förändring av processer. Dessutom är syftet att studera fem industrier närmare och att ge mer detaljerade förslag på åtgärder. Syftet är också att ge rekommendationer för fortsatt utveckling av relevant chilensk lagstiftning.</p><p>Uppgifter från tillsynsmyndigheten för utsläpp till ytvattendrag har studerats och djupintervjuer har gjorts med myndigheter och konsulter. Fem olika industrier besöktes; ett bryggeri, ett mejeri, ett bageri, ett charkuteri samt en ytbehandlingsindustri. Nuvarande hantering av processvattnet studerades på plats och med hjälp av ett frågeformulär kompletterades uppgifterna av ansvariga på företagen.</p><p>Föroreningsbelastningen på Chiles floder är stor. Floderna i södra delen av landet tar emot störst mängder organiskt material och suspenderat material medan centrala Chiles floder är värst drabbade av utsläpp av metallerna Cr, Cu, Zn och CN samt utsläpp av fenoler. Utsläppen från industrin till floderna i Region Metropolitana och Region VII kännetecknas också i stor utsträckning av höga halter BOD och suspenderat material. Relativt vanligt är också stora utsläpp av oljor och fetter, kväve, fosfor samt för höga eller låga för pH-värden. Det är främst flera olika typer av livsmedelsindustri, som har de största utsläppen till floderna, men även garverierna har stora problem med överskridande av gränsvärden.</p><p>Gemensamt för de fem besökta företagen är att vattenbesparande åtgärder bör vidtas för att minska volymen avloppsvatten som går till extern eller intern behandling. Bryggeriet, charkuterifabriken och ytbehandlaren behöver även end-of-pipe-rening. Det kan ofta vara lämpligt och mer ekonomiskt att avskilja de flöden som har högst halt av föroreningar till den interna reningsanläggningen. Resten av avloppet kan i vissa fall släppas ut på avloppsnätet. Kostnader för föreslagna åtgärder måste vägas mot aktuella kostnader för behandling av avlopp och restprodukter, samt kostnader för alternativa behandlingar.</p><p>Incitamenten, bl a de ekonomiska, för chilenska företag att skaffa eget reningsverk eller att resurseffektivisera produktionen har hittills varit små. Kostnadsminskningar kan uppnås genom sänkt vattenförbrukning samt återanvändning av råmaterial. Ytterligare en drivkraft kan vara att ”ligga steget före” om utsläppskraven i framtiden skärps och kostnaderna därmed ökar.</p>

<p>All products will eventually end up as waste, which in a sustainable society has to be handled in an efficient and environment friendly way. This report focuses on waste fractions meant for combustion, often difficult to characterize. However, more homogeneous fractions that are treated biologically are also discussed.</p><p>The study concerns the region of Borås, Sweden, where the waste plant Sobacken has provided a good starting point. On this site, fuel to the Energy-from-Waste plant of Borås Energi is prepared and the biological waste is treated through anaerobic digestion.</p><p>One important part of the study has been to collect experience-based knowledge from the technical staff at Sobacken and Borås Energi. This information was compiled into an overview of wanted and unwanted fractions to the preparation plant and the boilers respectively. The purpose of this overview is to complement existing delivery terms and thereby facilitate an increased quality of the fuel from the suppliers.</p><p>A significant element of the analysis has been to characterize the content of the industrial waste sent to Sobacken for combustion. Chemical analyses of the prepared fuel as well as the conducted waste component analysis indicate a heterogeneous composition of the waste. A heterogeneous fuel often results in an uneven combustion, leading to higher emissions and an unwanted variation in the energy production.</p><p>Through the waste component analysis, a comprehensive picture of the waste composition was attained. Materials non-valid for delivery mostly consisted of wet domestic waste (biodegradable materials), but some hazardous waste was also found. The results of the waste component analysis were communicated to the involved suppliers and this has already resulted in a considerable reduction of the amount of biodegradable waste in the deliveries of industrial waste.</p> / <p>Förr eller senare blir alla produkter avfall, som i ett uthålligt samhälle måste hanteras på ett resurssnålt och miljövänligt sätt. Det här arbetet är främst inriktat mot de svåridentifierade fraktionerna som är ämnade för förbränning, men berör även de mer homogena fraktionerna som behandlas biologiskt genom rötning.</p><p>Arbetet har utförts i Boråsregionen där Sobackens avfallsanläggning, med beredning av avfallsbränsle till Borås Energis två FB-pannor och rötkammare, har utgjort en naturlig utgångspunkt.</p><p>Ett stort inslag i arbetet var sammanställning av erfarenhetsbaserade kunskaper hos driftteknikerna på beredningsanläggningen, liksom hos Anders Johnsson på Borås Energi. På detta sätt erhölls viktig information om både bra och dåliga fraktioner, för såväl avfallskross som för pannor. Dessa fakta har bland annat använts för att sätta samman en översikt över önskade respektive oönskade fraktioner. Översikten är tänkt som komplement till befintliga leveransregler, i syfte att förenkla för avfallsleverantörerna.</p><p>Stor vikt har lagts vid att försöka kartlägga sammansättningen av det verksamhetsavfall som kommer in till Sobackens beredningsanläggning. Både kemiska analyser av bränsleprov och utförd plockanalys visar på en heterogen sammansättning i avfallet. Ett heterogent bränsle brinner i många fall ojämt, vilket resulterar i högre emissionsnivåer samt en icke-önskvärd variation i energiproduktion.</p><p>I och med plockanalysen erhölls en övergripande bild av förbränningsavfallets sammansättning. Det icke leveransgilla materialet som påträffades utgjordes främst av blött hushållsavfall (biologiskt nedbrytbart material), men även av en del elektronik påträffades. Efter avslutad analys kommunicerades erhållna resultat med aktuella leverantörer, vilket hittills har resulterat i en betydande minskning av biologiskt nedbrytbart material i verksamhetsavfallet.</p>

<p>Hammarby Sjöstad is a new district in southern Stockholm. A main objective with the Sjöstad project was to halve the environmental impact compared to other construction work. The environmental goals involve a halved water consumption rate, a local treatment of storm water and trials aiming to extract nutrients from the waste water. Sjöstadsverket is an experimental treatment plant used for testing new treatment processes for domestic waste water from Hammarby Sjöstad. The results are to be compared with the conventional process used at Henrikdals treatment plant today. Two aerobic and two anaerobic main treatment processes are to be tested before decision of full scale is taken in 2005.</p><p>Anaerobic treatment without heating, as a way to reduce the content of organic material in the waste water, consumes less energy than conventional methods. Anaerobic reactors are usually operated at 37°C. It is possible to attain a high COD-reduction at lower temperatures, assumed a longer contact time between biomass and waste water. In an Upflow Anaerobic Sludge Blanket (UASB) - reactor the microorganisms form granules with excellent sedimentation properties. The granules are floating with the waste water flowing upwards through the reactor. This makes it possible to reduce the COD-content despite a short hydraulic retention time in the reactor.</p><p>The two UASB-reactors examined in this thesis is a part of the pilot plant. The thesis shows how the startup of the reactors has functioned and evaluates the possibility to reduce the contence of different COD-fractions with this technique.The domestic waste water temperature has during the experiment period dropped from 23°C to 18°C. The total COD-content of the untreated waste water is 567 mg/l. Before the anaerobic step the water is pre-treated by adding of flocculation chemicals and sedimentation. The total amount of suspended material is reduced by 50 % in the pre-treatment and the load on the UASB-reactors is 100 mg/l. With a hydrologic retention time of 2,4 h the pre-treatment and the two-step anaerobic reactor has reduced 64 % of the total COD-content. Over the anaerobic treatment step the COD-reduction was 49 %. The reduction of dissolved COD (<0, 45 μm) was 59 %. When operated in series the main part of the soluble CODreduction has taken place in the first reactor. After more than six months operation there is still a granulated sludge in the reactors and tests show a high metanogenic activity. Gas production from the reactors has been observed but not measured quantitatively.</p><p>The results from this thesis show that anaerobic treatment with a UASB-process functions without heating for the household waste water from Hammarby Sjöstad. The anaerobic process should be combined with pre-treatment and supplementary treatment to reduce the remaining COD and the nitrogen and phosphorus content.</p> / <p>Hammarby Sjöstad i södra Stockholm är en stadsdel under framväxt. Tanken bakom Sjöstadsprojektet var att halvera miljöpåverkan jämfört med annan nybyggnation. Bland annat anges i miljömålen halverad vattenförbrukning, lokal hantering av dagvatten och försök med utvinning av växtnäringsämnen ur avloppsvattnet. Sjöstadsverket är en del av detta projekt; en försöksanläggning för reningen av avloppsvattnet från hushållen i Hammarby Sjöstad. Två aeroba och två anaeroba linjer ska utvärderas innan beslut om full skala tas år 2005.</p><p>Anaerob rening utan uppvärmning är ett resurssnålt sätt att minska innehållet av organiskt material i avloppsvattnet. Anaeroba reaktorer drivs vanligen vid ca 37°C. Det är möjligt att nå en hög reduktion av organiskt material även vid lägre temperaturer, förutsatt en längre kontakttid mellan biomassa och avloppsvatten. I en Upflow Anaerobic Sludge Blanket (UASB)-reaktor utnyttjas mikroorganismernas förmåga att bilda granuler, vilka svävar med avloppsvattnet som flödar uppåt genom reaktorn. Det gör det möjligt att reducera vattnets innehåll av organiskt material trots en kort hydraulisk uppehållstid i reaktorn. I detta examensarbete studeras de två UASB-reaktorer som ingår som en del i pilotanläggningen vid Sjöstadsverket. Examensarbetet visar hur uppstarten av reaktorerna fungerat och utvärderar möjligheten att reducera avloppsvattnets olika fraktioner av COD med denna teknik.</p><p>Temperaturen på vattnet från hushållen har under försöksperioden sjunkit från 23°C till 18°C. Det obehandlade avloppsvattnet har en total COD-halt kring 567 mg/l. Innan det anaeroba reningssteget förbehandlas vattnet genom sedimentering och inblandning av flockningskemikalier. Den totala mängden suspenderat material halveras i förbehandlingen och belastningen på UASB-reaktorerna är kring 100 mg /l. Efter förbehandling är vattnets COD-koncentration ca 400 mg/l. Med en hydraulisk uppehållstid på 2,4 timmar har en COD-reduktion på 64 % uppnåtts i hela systemet, dvs. försedimentering och två-stegs UASB-reaktor. Över det anaeroba reningssteget var reduktionen av COD 49 %. Reduktionen av löst COD (<0, 45 μm) i UASB-reaktorerna var 59 %. Vid seriell drift har merparten av lösligt COD reducerats i den första reaktorn. Efter nio månaders drift finns fortfarande ett granulärt slam i båda reaktorerna. Tester visar på en hög metanogen aktivitet. Gasproduktion har observerats i reaktorerna men inte kunnat mätas kvantitativt.</p><p>Resultaten från detta examensarbete indikerar att anaerob rening med en UASB-process fungerar utan uppvärmning för avloppsvattnet från hushållen i Hammarby Sjöstad. Den anaeroba behandlingen bör kompletteras med förbehandling samt en kompletterande behandling för att minska kvarvarande COD och reducera kväve och fosfor.</p>

The aim of the investigation was to compare the performance of an anaerobic baffled reactor (ABR) with a completely mixed anaerobic reactor (CMAR). The ABR was operated with a hydraulic retention time (HRT) of 20 h while the CMAR was operated at 20 d. A control experiment was conducted with a CMAR operated at a constant hydraulic retention time and substrate feed concentration. During the first phase, the start-up performance of the ABR and CMAR were compared. In the second phase of the study the steady state COD removals were compared. The laboratory completely mixed anaerobic reactor was a 20L glass vessel with a stirrer coming in through the neck. A second type of reactor, anaerobic baffled reactor (ABR) was also operated. The ABR was a rectangular perspex box with internal vertical baffles alternately hanging and standing. The baffles divide the reactor into eight compartments with a total working volume of 7.5 L. Each baffle is angled at about 45Q to distribute the flow towards the centre of the upcomer. The reactors were seeded with raw sewage and allowed to stand for 3 days after which a continous feed of sucrose and basal salts was commenced. The initial HRT for the ABR and the CMAR were 60 h and 30 days respectively. When the reactors reached steady state (pH, gas production, gas composition and alkalinity), the HRT was reduced in a stepwise fashion (ABR 60 h to 35 h to 20 h and CMAR 35 d to 30 d to 20 d). At the final HRT the COD removals were similar (67 %). The ABR took 120 d to attain final steady state while the CMAR took 200 d. The organic loading tests were undertaken with a stepwise increase (doubling) in the influent substrate concentration. The feeding commenced at an organic loading rate (OLR) of 4.8 kg/m(3).d for the ABR. The flow rate (HRT) into both reactors and other parameters were kept constant (HRT of 20 h and 20 d for ABR and CMAR respectively). The substrate concentration was increased from 4 gCOD/L (4.8 kg/m(3).d) to 64 gCOD/L (76.8 kg/m(3).d) for the ABR. For the CMAR it was increased from 4 gCOD/L (0.25 kg/m(3).d) to 32 gCOD/L (2 kg/m(3).d). The method used was to increase the organic loading rate until the reactors failed. Since the two reactors had different operating HRTs, the tests began when both had the same COD removal rate of about 60 % COD reduction. The same parameters as in the start-up period were monitored for both reactors. The CMAR had a COD removal efficiency ca. 70 %, which did not fluctuate when OLR was increased. The ABR reached a maximum COD removal of 80 %. An increase in the OLR led to an initial decrease in the COD removal until the biomass recovered and the high COD (80 %) removal rates resumed. The ABR reached a maximum OLR of 76.8 kg/m(3).d whilst the CMAR reached a maximum OLR of 2.0 kg/m(3).d. The investigations showed that the ABR could be operated at higher organic loads than the CMAR and give the same organic removal rate. This verified the importance of increasing the SRT/HRT ratio in anaerobic reactors. The CMAR, however, proved to be stable to changes in the influent feed strength, as there was no immediate noticeable changes in the gas production. / Thesis (M.Sc.Eng.)-University of Natal, Durban, 2000.

Researchers at Rhodes University conducted investigations into the anaerobic co-disposal of primary sewage sludge (PSS) and high sulphate acid mine drainage (AMD) resulting in the development of the Rhodes BioSURE Process® which forms the basis for the operation of a pilot recycling sludge bed reactor (RSBR). Further research has been conducted by researchers at the University of Cape Town (UCT), with the principle aim of determining the rate of hydrolysis of PSS under rnethanogenic, acidogenic and sulphate reducing conditions in laboratory-scale anaerobic digesters. The University of Cape Town's Anaerobic Digestion Model No.1 (UCTADMI) which integrates various biological anaerobic processes for the production of methane was extended with the development of a mathematical model incorporating the processes of biosulphidogenic reduction and the biology of sulphate reducing bacteria (SRB). Kinetic parameters used in the model were obtained from SOtemann et al. (2005b) and Kalyuzhnyi et al. (1998). The WEST® software was used as a platform in translation of the basic UCTADMI from AQUASIM, and subsequently applied to data sets from UCT laboratory experiments. Incomplete closure of mass balances was attributed to incorrect reaction stoichiometry inherited through translation of the AQUASIM model into WEST®. The WEST® implementation of the model to the experimental methanogenic systems gave fairly close correlations between predicted and measured data for a single set of stoichiometric and kinetic constants, with regressed hydrolysis rate constants. Application of the extended UCTADMI to experimental sulphidogenic systems demonstrated simulation results reasonably close to measured data, with the exception of effluent soluble COD and sulphate concentrations. Except for a single system with a high COD:Sat ratio, sulphidogens are out competed for substrate by methanogens within the model. Therefore the model does not properly represent the competition between methanogenic and sulphidogenic organism groups. Trends observed in application of the model to available pilot plant RSBR data were similar to those observed in sulphidogenic systems, resulting in methanogens out-competing sulphidogens. The model was used as a tool to explore various scenarios regarding operation of the pilot plant. Based on the work conducted in this study, various areas for further information and research were highlighted and recommended. / Thesis (M.Sc.Eng.)-University of KwaZulu-Natal, Durban, 2009.

Today's society is facing major challenges. In order to reduce the climate impact fossil fuels should be replaced with fuels that do not contribute to the greenhouse effect. The growing population generates organic waste originating from industry and households so called organic fraction of municipal solid waste (OFMSW). Through anaerobic digestion, waste can be utilized to produce energy-rich methane gas. In this way, waste can be a resource instead of a burden on society. The purpose of this project is to investigate the methane yield of source-sorted organic fraction of municipal solid waste (SS-OFMSW) pretreated with screw crush technology and methane yield at the co-digestion of food waste and biosludge from paper mills. SS-OFMSW which is either pre-treated in a screw crusher or a Food Waste Mill and a mixture of SS-OFMSW and biosludge from paper mills digested in a semi - continuous wet process under mesophilic conditions with a retention time of 20 days. Screw crush technique gave a slurry with a methane yield of about 440-490 mL / g VS, which was slightly higher than the yield of 300-350 mL / g VS from the slurry pretreated with Food Waste Mill. The methane concentration was slightly higher for slurry pretreated with Food Waste Mill, 74% in average compared with 68% for slurry pretreated with screw crush. Biosludge from paper mills is an organic waste that can be digested in order to produce biogas. The sludge is poor in nutrients and methane yield at individual anaerobic digestion of paper mill sludge is relatively low. In this study, biosludge was co-digested with SS-OFMSW. The mixture with the proportions 1:1 by g VS gave a methane yield of about 420-480 mL / g VS which is higher than the constituent substrates digested separately. Co-digestion gave a methane concentration at 80% which is also higher than at the individual anaerobic digestion of substrates.

Vid tillverkning av massa och papper förorenas årligen 505 miljoner kubikmeter vatten som måste renas innan det släpps tillbaka till omgivningen. Vid reningen avskiljs först stora partiklar som sedan avvattnas och förbränns. Vattnet som blir kvar genomgår ytterligare en rening, varvid det bildas bioslam. Bioslammet innehåller mycket intracellulärt vatten, vilket gör det kostsamt och energikrävande att avvattna. Det är även sedan 2005 förbjudet att dumpa organiskt material, varför en mer ekonomiskt attraktiv behandling av slammet är anaerob nedbrytning. I denna nedbrytning omvandlas det organiska materialet till metan och koldioxid där metanet är den eftertraktade gasen. Bioslammet innehåller dock partiklar såsom träfiberrester och mikroorganismer med komplex struktur och är näringsfattigt. Någon form av sönderdelande förbehandling underlättar därför rötningsprocessen. I detta projekt undersöktes termisk förbehandling i kombination med kemisk förbehandling på bioslam från Stora Enso Skoghalls bruk på Hammarö. Själva rötningen skedde i två omgångar varav den första omgången med termisk förbehandling vid 70C och den andra vid 140C. Den kemiska förbehandlingen skedde med tillsats av lut (natriumhydroxid), kalk (kalciumhydroxid) och syra (fosforsyra) vid pH 9 och 11 för baserna och pH 2 och 4 för syran. Även neutrala prov (endast värmebehandling) och ett blankprov (ingen förbehandling) gjordes. Bioslammet ympades med kommunalt slam från Fiskartorpets reningsverk i Kristinehamn som har en mesofil bakteriekultur. Rötningen varade i 19 dagar per omgång i en temperatur på 35C och skedde satsvis i E-kolvar försedda med påsar för gasuppsamling. Totalt rötades 42 prov per omgång som utgjordes av sju mätpunkter á sex replikat för goda statistiska underlag. Resultaten gav en indikation för högst metanproduktion för proven behandlade med kalk vid 140C och för provet utan kemisk förbehandling vid 140C. Lägst produktion hade det kalkbehandlade provet vid pH 9 och 70C följt av blankprovet. Lutproven gav lägre metanproduktion vid 140C än vid 70C och fosforsyran hade så gott som oförändrad produktion mellan temperaturerna. Gemensamt för alla prover som behandlats vid 70C var att de fick en högre procentandel metan då de behandlats vid 140C. De resultat som erhållits är dock osäkra då det i vissa fall var stor spridning mellan provens biogasproduktion inom de enskilda förbehandlingsområdena. / In the pulp and paper process 505 million tons of water are polluted annually, which has to be purified before it is returned to the surrounding lakes. When the water is treated bigger particles are first separated to form sludge, then dewatered and finally incinerated. The excess water is further treated were a type of sludge  bio sludge  is formed. The bio sludge contains high concentration of intracellular water, why it is expensive and energy demanding to dewater. It is also forbidden to dump organic waste since 2005, why a more economically attractive treatment of the water is anaerobic digestion. In the digestion organic compounds is converted into methane and carbon dioxide where the methane is the desired gas. The bio sludge also contains fiber residues and microorganisms with complex structure and is nutrient-poor, which makes it hard to digest. Some kind of disintegrating pretreatment is needed and co-digestion with a more nutrient-rich sludge to facilitate the digestion process. In this project thermal pretreatment in combination with chemical pretreatment was examined on bio sludge from Stora Enso Skoghalls bruk at Hammarö. The anaerobe digestion was done by two rounds whereof the first round thermal pretreated at 70C and the second at 140C. The chemical pretreatment was done by additive of sodium hydroxide, calcium hydroxide and phosphoric acid at pH 9 and 11 for the bases and pH 2 and 4 for the acid. Also neutral samples (no chemical pretreatment) and a reference sample (no pretreatment) were done. The bio sludge were co-digested with municipal sludge from Fiskartorpets reningsverk in Kristinehamn which has a mesophilic bacterial culture. The anaerobic digestion lasted for 19 days per round at a temperature of 35C and were done batch wise in E-flasks provided with a small bag for gas collection. Totally 42 samples were made per round which consisted of seven measurement points and six replicates each for a good statistical basis. The results gave an indication of the highest methane production for the samples treated with calcium hydroxide at 140C and the neutral sample treated at 140C. The sample treated with calcium hydroxide at pH 9 and 70C gave the lowest production of methane followed by the reference sample. The samples treated with sodium hydroxide gave a lower methane production at 140C than at 70C while the acid treated samples had almost the same production at the two different temperatures. All the samples had in common a higher proportion of methane in the biogas when treated at 140C than at 70C. The results should be taken with caution since the distribution amongst the samples within the same pretreatment method sometimes is very high.