Hydrothermal carbonization (HTC) is a process where elevated temperature and pressure is used in order to convert biomass to hydrochar, a coal-like substance with good dewatering properties and many potential uses. HTC can be used to treat digestate from anaerobic digestion, but the process water that remains after the hydrochar has been recovered needs to be treated further in the wastewater treatment plant. In order to make HTC more competitive compared to other sludge treatments it is important to find a good use for the process water. The main objective of this master thesis was to investigate the effects of recirculating HTC process water to the anaerobic digestion. To achieve the objective, both theoretical calculations and experimental trials were performed. The experimental trials were conducted with an Automatic Methane Potential Test System (AMPTS II) in order to investigate the anaerobic digestion in laboratory scale. In the first trial, three substrates, process water, hydrochar, and primary sludge were tested for their biochemical methane potential (BMP). All substrates were mixed with inoculum. Process water had a BMP of 335 ± 10 % NmL/gvs (normalized CH4 production in mL per g added VS (volatile solids)), hydrochar had BMP of 150 ± 5 % NmL/gvs, and primary sludge had a BMP of 343 ± 2 % NmL/gvs. The methane production was almost the same for process water as for primary sludge i.e. no inhibitory effects could be seen when process water was mixed with only inoculum. In the second trial, a more realistic scenario was tested where process water was co-digested with primary sludge at different ratios. The results from the second trial were not statistically reliable and therefore cannot be used on their own to determine with certainty if the process water could have an inhibitory effect in a full-scale anaerobic digester. However, the combined results from both trials indicate that it is unlikely that the process water would have an inhibitory effect. The possible increase in methane yield, if the digestate from a biogas facility was treated in full-scale implementation of the HTC process, was calculated theoretically. The produced process water would have the capacity to increase the methane production with approximately 10 % for a biogas facility. For the calculations, the BMP for process water was assumed to be 335 NmL/gvs and no synergetic effects was considered.

This thesis focuses on modeling the primary sludge in the thickening process at Henrikdals wastewater treatment plant in Stockholm, Sweden. The thickening process is one of the core processes at the wastewater treatment plant, where the goal is to thicken a residual product called primary sludge. Two thickener belts are used to thicken the sludge gravimetrically. Polymer is also added to increase the dewaterability and to thicken the sludge. The thickness of the sludge is measured by the total solids content (TS) in the sludge and is measured with total solid measurement sensors. These sensors have, however, been shown to be inaccurate. A long short-term memory network (LSTM) and a feed-forward neural network were compared by using sensor and instrument data to predict the TS in the thickened primary sludge. To validate the performance of the models, manual laboratory testing samples were compared with the predictions of the models. Simulations in Simulink were also performed with the intent of simulating the thickening process. By using a machine learning model that could predict the TS, hypotheses regarding reductions in the polymer dosage were explored. A feed-forward and feedback control strategy in combination with the LSTM architecture were used and it was shown that the TS of the thickened sludge could be controlled by regulating the polymer dosage. Thus, using a feedback control strategy gives further opportunities for the wastewater treatment plant to choose whether a lower polymer consumption or a higher TS is preferred, as these two variables correlate with each other. / Syftet med detta arbete var att ta fram maskininlärningsmodeller av primärslamsförtjockningen på Henriksdals avloppsreningsverk i Stockholm, Sverige. Förtjockningsprocessen är en av de viktigaste delerna i avloppsreningsverk, där målet är att förtjocka en restprodukt som kallas primärslam. Förtjockningen sker i två separata linjer. Polymer tillsätts och slammet förtjockas genom gravimetrisk avvattning på ett silband. Slammets torrsubstanshalt (TS) är ett mått på slammets tjockhet och beräknas med hjälp av att använda sensorer. Dessa sensorer har dock visats sig vara opålitliga. Genom att använda tillgänglig process-, maskin- och instrumentdata så har en long short-term memory (LSTM) arkitektur och ett framkopplat neuralt nätverk jämförts för att uppskatta torrsubstansen i primärslammet. Manuell provtagning och labbanalys utfördes för att validera prestandan i de två modellerna. Hypoteser kring att kunna optimera TS-halten eller minska polymerförbrukningen utforskades genom att simulera processen i Simulink. Resultaten visade att användandet av en fram och återkopplingsregulator tillsammans med en LSTM arkitektur kan minska polymerförbrukningen och kan ge en jämnare TS-halt i det förtjockade slammet. Däremot måste en avvägning mellan hög TS-halt och låg polymerförbrukning göras, då dessa två variabler korrelerar med varandra

<p>Käppala wastewater treatment plant situated on the island of Lidingö northeast of Stockholm is running a project during 2004 and 2005 with the purpose to map out the capacity of anaerobic digestion in the digesters that treat primary and excess sludge. The purpose of this thesis work, which is part of that project, was to characterize the present anaerobic digestion process and to investigate its capacity to treat other organic wastes such as restaurant waste and waste from water works. To decide the potential of both methane and biogas production from different substrates batch laboratory tests were carried out. To imitate the anaerobic digestion process at Käppala continuous tests with small scale reactors were carried out. These reactors were later fed with restaurant waste.</p><p>The batch laboratory tests showed that primary sludge had a potential biogas and methane production of 0,62 and 0,35 Ndm3/g VS respectively after 40 days of digestion. After 15 to 20 days of digestion (average retention time in the digester at Käppala wastewater treayment plant that treats primary sludge) the biogas production was between 0,55 and 0,60 Ndm3/g VS, which is within the range of the production at the digester that treats the primary sludge. This leads to the conclusion that the digestion of primary sludge is well functioning at the plant.</p><p>Batch laboratory tests showed that excess sludge had a potential biogas and methane production of 0,31 and 0,16 Ndm3/g VS respectively after 40 days of digestion.</p><p>Batch laboratory tests with restaurant waste showed a potential biogas and methane production of 0,81 and 0,38 Ndm3/g VS respectively after 47 days of digestion. This means that the total production of methane gas can increase with 7-8 per cent with an annual load of 3500 tonnes of restaurant waste (estimated amount of available restaurant waste). Tests to imitate transport of restaurant waste with influent wastewater showed that 35-60 per cent of the increase of gas production would be “washed out” if the waste was tranported this way to the plant.</p><p>Batch laboratory tests with waste from water works showed that no gas was produced from this substrate.</p><p>The continuous tests with small scale reactors which were fed with restaurant waste resulted in an increase of biogas production with 12 per cent (corresponding to an annual load of 3500 tonnes of restaurant waste) compared to the present process.</p> / <p>Avloppsreningsverket Käppalaverket på Lidingö driver under år 2004-2005 ett projekt med syftet att kartlägga rötningskapaciteten i den befintliga anläggningen där primär- och överskottsslam behandlas i två rötkammare. Syftet med examensarbetet, som är en del av kartläggningsprojektet, var att karakterisera Käppalaverkets nuvarande rötningsprocess och undersöka processens kapacitet att behandla organiskt avfall i form av restaurangavfall och vatttenverksslam. För att bestämma potentialen hos olika substrat har satsvisa utrötningar genomförts. För att efterlikna processen på Käppalaverket har kontinuerliga försök med små reaktorer bedrivits. Till dessa reaktorer har sedan restaurangavfall tillsats.</p><p>De satsvisa utrötningarna av primärslam visade en potentiell bio- respektive metangasproduktion om 0,62 respektive 0,35 Ndm3/g VS efter 40 dagars utrötning. Efter 15-20 dagars utrötning (som är den genomsnittliga uppehållstiden i Käppalaverkets rötkammare där primärslammet behandlas) var biogasproduktionen mellan 0,55 och 0,60 Ndm3/g VS, vilket är inom samma intervall som vid den verkliga driften av rötkamrarna vid Käppalaverket. Detta betyder att utrötningen av primärslammet fungerar bra vid Käppalaverket.</p><p>De satsvisa utrötningarna av överskottsslammet visade en potentiell bio- respektive metangasproduktion om 0,31 respektive 0,16 Ndm3/g VS efter 40 dagars utrötning.</p><p>För restaurangavfallet visade de satsvisa utrötningarna på en potentiell bio- respektive metangasproduktion om 0,81 respektive 0,38 Ndm3/g VS efter 47 dagars utrötning.</p><p>Detta innebär att den totala metangasproduktionen vid Käppalaverket skulle kunna ökas med 7-8 procent om 3500 ton restaurangavfall skulle tas emot årligen (uppskattad mängd restaurangavfall som finns att tillgå). Försök att efterlikna transport av restaurangavfallet via avloppsledningsnätet visade dock att 35-60 procent av den ökade metangasproduktionen skulle ”tvättas ur” om avfallet fördes till verket via avloppsledningsnätet.</p><p>Försöken med satsvis utrötning av vattenverksslam visade att detta substrat inte bidrar med någon produktion av biogas eller metangas.</p><p>De kontinuerliga försöken med tillsats av restaurangavfall (motsvarande en årlig belastning med 3500 ton) resulterade i en ökning av biogasproduktionen med 12 procent.</p>

Käppala wastewater treatment plant situated on the island of Lidingö northeast of Stockholm is running a project during 2004 and 2005 with the purpose to map out the capacity of anaerobic digestion in the digesters that treat primary and excess sludge. The purpose of this thesis work, which is part of that project, was to characterize the present anaerobic digestion process and to investigate its capacity to treat other organic wastes such as restaurant waste and waste from water works. To decide the potential of both methane and biogas production from different substrates batch laboratory tests were carried out. To imitate the anaerobic digestion process at Käppala continuous tests with small scale reactors were carried out. These reactors were later fed with restaurant waste. The batch laboratory tests showed that primary sludge had a potential biogas and methane production of 0,62 and 0,35 Ndm3/g VS respectively after 40 days of digestion. After 15 to 20 days of digestion (average retention time in the digester at Käppala wastewater treayment plant that treats primary sludge) the biogas production was between 0,55 and 0,60 Ndm3/g VS, which is within the range of the production at the digester that treats the primary sludge. This leads to the conclusion that the digestion of primary sludge is well functioning at the plant. Batch laboratory tests showed that excess sludge had a potential biogas and methane production of 0,31 and 0,16 Ndm3/g VS respectively after 40 days of digestion. Batch laboratory tests with restaurant waste showed a potential biogas and methane production of 0,81 and 0,38 Ndm3/g VS respectively after 47 days of digestion. This means that the total production of methane gas can increase with 7-8 per cent with an annual load of 3500 tonnes of restaurant waste (estimated amount of available restaurant waste). Tests to imitate transport of restaurant waste with influent wastewater showed that 35-60 per cent of the increase of gas production would be “washed out” if the waste was tranported this way to the plant. Batch laboratory tests with waste from water works showed that no gas was produced from this substrate. The continuous tests with small scale reactors which were fed with restaurant waste resulted in an increase of biogas production with 12 per cent (corresponding to an annual load of 3500 tonnes of restaurant waste) compared to the present process. / Avloppsreningsverket Käppalaverket på Lidingö driver under år 2004-2005 ett projekt med syftet att kartlägga rötningskapaciteten i den befintliga anläggningen där primär- och överskottsslam behandlas i två rötkammare. Syftet med examensarbetet, som är en del av kartläggningsprojektet, var att karakterisera Käppalaverkets nuvarande rötningsprocess och undersöka processens kapacitet att behandla organiskt avfall i form av restaurangavfall och vatttenverksslam. För att bestämma potentialen hos olika substrat har satsvisa utrötningar genomförts. För att efterlikna processen på Käppalaverket har kontinuerliga försök med små reaktorer bedrivits. Till dessa reaktorer har sedan restaurangavfall tillsats. De satsvisa utrötningarna av primärslam visade en potentiell bio- respektive metangasproduktion om 0,62 respektive 0,35 Ndm3/g VS efter 40 dagars utrötning. Efter 15-20 dagars utrötning (som är den genomsnittliga uppehållstiden i Käppalaverkets rötkammare där primärslammet behandlas) var biogasproduktionen mellan 0,55 och 0,60 Ndm3/g VS, vilket är inom samma intervall som vid den verkliga driften av rötkamrarna vid Käppalaverket. Detta betyder att utrötningen av primärslammet fungerar bra vid Käppalaverket. De satsvisa utrötningarna av överskottsslammet visade en potentiell bio- respektive metangasproduktion om 0,31 respektive 0,16 Ndm3/g VS efter 40 dagars utrötning. För restaurangavfallet visade de satsvisa utrötningarna på en potentiell bio- respektive metangasproduktion om 0,81 respektive 0,38 Ndm3/g VS efter 47 dagars utrötning. Detta innebär att den totala metangasproduktionen vid Käppalaverket skulle kunna ökas med 7-8 procent om 3500 ton restaurangavfall skulle tas emot årligen (uppskattad mängd restaurangavfall som finns att tillgå). Försök att efterlikna transport av restaurangavfallet via avloppsledningsnätet visade dock att 35-60 procent av den ökade metangasproduktionen skulle ”tvättas ur” om avfallet fördes till verket via avloppsledningsnätet. Försöken med satsvis utrötning av vattenverksslam visade att detta substrat inte bidrar med någon produktion av biogas eller metangas. De kontinuerliga försöken med tillsats av restaurangavfall (motsvarande en årlig belastning med 3500 ton) resulterade i en ökning av biogasproduktionen med 12 procent.