Abstract
This paper evaluates the technical and economic feasibility of using a steam accumulator in the thermal hydrolysis process for the treatment of sludge. The increase in the efficiency of anaerobic digestion and biogas valorisation through the combined use of heat and power engines was studied based on scenarios from the wastewater treatment plant of the city of Burgos (Spain). These scenarios were evaluated based on the installation of steam accumulation to average the thermal needs of the process. Biogas production was estimated based on the plant’s operating conditions between 2011 and 2016. Results indicated a process enhancement from 33 to 100% due to a better use of exhaust gases. Consequently, increases of 20.0% in the net biogas and 13.1% in electrical energy production were obtained, along with decreases of 66.8% in the thermal power needs and 61.9% in the biogas consumed by the recovery boiler. The economic savings were 98,213 €/year, due to a decrease in the need to purchase electrical energy from the network. The return on investment period was 2 years after introducing a steam accumulator to the process and replacing the boiler with a new, smaller one.
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Abbreviations
- BP:
-
Biogas production of the digesters (m3/day) reported at STP (0 °C and 100 kPa)
- CHP:
-
Combined heat and power
- C F :
-
Annual cash flow (€)
- Cp W :
-
Specific heat capacity of water (4.186 kJ/kg °C)
- D l :
-
Degree of loading of the engines (%)
- Dsr:
-
Degree of steam release (kg/h m2)
- Ds max :
-
Maximum degree of steam release (kg/h m2)
- E g :
-
Thermal power recovered from the exhaust gases in the recovery boiler (kW)
- E p :
-
Electrical power generated by the engines (kW)
- fc :
-
Filling coefficient
- F Eg :
-
Mass flow of exhaust gases of the Guascor engines (kg/s)
- Fs :
-
Steam flow of the thermal hydrolysis process (kg/h)
- FSA:
-
Free surface area of water (m2)
- Fs acum :
-
Mass flow of steam provided by the steam accumulator (kg/h)
- Fs boiler :
-
Mass flow of steam provided by the boiler (kg/h)
- F W_feed :
-
Flow of feed water (kg/s)
- I 0 :
-
Initial capital invested (€)
- LHV:
-
Low heating value of the biogas (kJ/m3)
- L s :
-
Thermal power of live steam obtained in the recovery boiler at 190.2 °C (kW)
- Ms:
-
Mass of steam needed for the thermal hydrolysis process (kg)
- m sat_water :
-
Saturated water stored in the accumulator (kg)
- N :
-
Number of engines
- P acc :
-
Pressure of the accumulator (kPa)
- P VS :
-
Daily mass flow of volatile solids (VS) of primary sludge (kg/day)
- SMPp, SMPw :
-
Specific methane production of primary sludge and WAS (m3 CH4/kg VS)
- T 0 :
-
Temperature of the feeding water (15 °C)
- T fw :
-
Preheating temperature of feed water (°C)
- THSA:
-
Thermal hydrolysis and steam accumulator scenario
- THP:
-
Thermal hydrolysis plant
- t inj :
-
Injection time of live steam per hydrolysis cycle (min)
- t cycle :
-
Total time of the reactor cycle (min)
- T in, T out :
-
Inlet temperature and outlet temperature of the recovery boiler of exhaust gases (°C)
- TpB cons :
-
Consumption of thermal power derived from biogas needed for the engines and the recovery boiler (kW)
- TpB dig :
-
Thermal power of the biogas produced (kW)
- TpB eng :
-
Thermal power associated with biogas available for the engines (kW)
- TpB rb-av :
-
Average thermal power of the biogas consumed in the recovery boiler (kW)
- Tp W :
-
Thermal power of feed water (kW)
- V acum :
-
Volume of the accumulator (m3)
- WAS:
-
Waste activated sludge
- W VS :
-
Daily mass flow of volatile solids (VS) of WAS sludge (kg/day)
- ∆h :
-
Change in enthalpy of water associated with difference in pressure
- η rb :
-
Efficiency performance of the recovery boiler (%)
- η b :
-
Efficiency performance of the burner in the recovery boiler (%)
- λ water]1260 :
-
Enthalpy of water evaporation at 1260 kPa
- ρ :
-
Density of water (kg/m3)
References
Abu-Nada E, Al-Hinti I, Al-Sarkhi A, Akash B (2006) Thermodynamic modeling of spark-ignition engine: effect of temperature dependent specific heats. Int Commun Heat Mass 33(10):1264–1272. https://doi.org/10.1016/j.icheatmasstransfer.2006.06.014
Barber W (2016) Thermal hydrolysis for sewage treatment: a critical review. Water Res 104:53–71. https://doi.org/10.1016/j.watres.2016.07.069
Bertanza G, Canato M, Heimersson S, Laera G, Salvetti R, Slavik E, Svanström M (2015) Techno-economic and environmental assessment of sewage sludge wet oxidation. Environ Sci Pollut Res 22(10):7327–7338. https://doi.org/10.1007/s11356-014-3378-6
Biglia A, Comba L, Fabrizio E, Gay P, Aimonino D (2017) Steam batch thermal processes in unsteady state conditions: modelling and application to a case study in the food industry. Appl Therm Eng 118:638–651. https://doi.org/10.1016/j.applthermaleng.2017.03.004
Burcat A, Ruscic B (2005) Third millennium ideal gas and condensed phase thermochemical database for combustion with updates from active thermochemical tables, Argonne National Laboratory, report number ANL-05/20. http://www.ipd.anl.gov/anlpubs/2005/07/53802.pdf. Accessed 10 Nov 2017
Cao J (2000) Optimization of thermal storage based on load graph of thermal energy system. Int J Thermodyn 3(2):91–97
Carrère H, Dumas C, Battimelli A, Batstone DJ, Delgenès JP, Steyer JP, Ferrer I (2010) Pretreatment methods to improve sludge anaerobic degradability: a review. J Hazard Mater 183(1–3):1–15. https://doi.org/10.1016/j.jhazmat.2010.06.129
Chauzy J, Dimassimo R, Kline M, Howell G (2014) What is the best arrangement for implementing THP (thermal hydrolysis process) on my sludge treatment facilities? Proc Water Environ Fed 15:5181–5193. https://doi.org/10.2175/193864714815938814
Divyalakshmi P, Murugan D, Sivarajan M, Sivasamy A, Saravanan P, Rai CL (2017) Optimization and biokinetic studies on pretreatment of sludge for enhancing biogas production. Int J Environ Sci Technol 14(4):813–822. https://doi.org/10.1007/s13762-016-1191-0
Fernández-Polanco D, Tatsumi H (2016) Optimum energy integration of thermal hydrolysis through pinch analysis. Renew Energy 96:1093–1102. https://doi.org/10.1016/j.renene.2016.01.038
Haider M, Werner A (2013) An overview of state of the art and research in the fields of sensible, latent and thermo-chemical thermal energy storage. Elektrotech Inftech 130(6):153–160. https://doi.org/10.1007/s00502-013-0151-3
Ibrahima H, Ilincaa A, Perron J (2008) Energy storage systems—characteristics and comparisons. Renew Sustain Energy Rev 12(5):1221–1250. https://doi.org/10.1016/j.rser.2007.01.023
Jafarinejad S (2017) Cost estimation and economical evaluation of three configurations of activated sludge process for a wastewater treatment plant (WWTP) using simulation. Appl Water Sci 7(5):2513–2521. https://doi.org/10.1007/s13201-016-0446-8
Khana I, Othmanb M, Hashim H, Matsuurad T, Ismailb A, Rezaei-DashtArzhandib M, Azeleeb I (2017) Biogas as a renewable energy fuel—a review of biogas upgrading, utilisation and storage. Energy Convers Manag 150:277–294. https://doi.org/10.1016/j.enconman.2017.08.035
Kuravi S, Trahan J, Goswami D, Rahman M, Stefanakos E (2013) Thermal energy storage technologies and systems for concentrating solar power plants. Prog Energy Combust 39(4):285–319. https://doi.org/10.1016/j.pecs.2013.02.001
Lozano MA (1998) Cogeneración. Departamento de Ingeniería Mecánica, Universidad de Zaragoza (revisión 2014). https://publicationslist.org/data/miguel.a.lozano/ref-183/Cogeneracion%201998%. Accessed 05 Dec 2017
Magrí A, Giovannini F, Connan R, Bridoux G, Béline F (2017) Nutrient management from biogas digester effluents: a bibliometric-based analysis of publications and patents. Int J Environ Sci Technol 14(8):1739–1756. https://doi.org/10.1007/s13762-017-1293-3
Martínez EJ, Gil MV, Rosas JG, Moreno R, Mateos R, Morán A, Gómez X (2017) Application of thermal analysis for evaluating the digestion of microwave pre-treated sewage sludge. J Therm Anal Calorim 127(2):1209–1219. https://doi.org/10.1007/s10973-016-5460-4
Metcalf E, Eddy E (2003) Wastewater engineering: treatment and reuse. McGrawHill Inc., New York
Molinos-Senante M, Hernandez-Sancho F, Sala-Garrido R (2014) Benchmarking in wastewater treatment plants: a tool to save operational costs. Clean Technol Environ 16(1):149–161. https://doi.org/10.1007/s10098-013-0612-8
Nazari L, Yuan Z, Santoro D, Sarathy S, Ho D, Batstone D, Xu C, Ray M (2017) Low-temperature thermal pre-treatment of municipal wastewater sludge: process optimization and effects on solubilization and anaerobic degradation. Water Res 113:111–123. https://doi.org/10.1016/j.watres.2016.11.055
Neumann P, Pesante S, Venegas M, Vidal G (2016) Developments in pre-treatment methods to improve anaerobic digestion of sewage sludge. Rev Environ Sci Bio Technol 15(2):173–211. https://doi.org/10.1007/s11157-016-9396-8
Oakland D (2004) Steam accumulation gives CHP an added push to halt climate change, https://www.homeaccentstoday.com/file/12083-chp.pdf. Accessed 27 Aug 2017
Pérez-Elvira SI, Diez PN, Fernández-Polanco F (2006) Sludge minimisation technologies. Rev Environ Sci Bio Technol 5(4):375–398. https://doi.org/10.1007/s11157-005-5728-9
Pérez-Elvira SI, Fernández-Polanco F, Fernández-Polanco M, Rodríguez P, Rouge P (2008) Hydrothermal multivariable approach: full-scale feasibility study. Electron J Biotechnol 11(4):7–8. https://doi.org/10.2225/vol11-issue4-fulltext-14
Pilli S, Yan S, Tyagi RD, Surampalli RY (2015) Thermal pretreatment of sewage sludge to enhance anaerobic digestion: a review. Crit Rev Environ Sci Technol 45(6):669–702. https://doi.org/10.1080/10643389.2013.876527
Ruffino B, Campo G, Cerutti A, Zanetti M, Lorenzi E, Scibilia G, Genon G (2016) Preliminary technical and economic analysis of alkali and low temperature thermo-alkali pretreatments for the anaerobic digestion of waste activated sludge. Waste Biomass Valoris 7(4):667–675. https://doi.org/10.1007/s12649-016-9537-x
Sapkaite I, Barrado E, Fdz-Polanco F, Pérez-Elvira SI (2017) Optimization of a thermal hydrolysis process for sludge pre-treatment. J Environ Manag 192:25–30. https://doi.org/10.1016/j.jenvman.2017.01.043
Spiraxsarco (2017) Steam accumulators, http://www.spiraxsarco.com/Resources/Pages/Steam-Engineering-Tutorials/the-boiler-house/steam-accumulators.aspx. Accessed 27 Aug 2017
Steinmann W, Eck M (2006) Buffer storage for direct steam generation. Sol Energy 80(10):1277–1282. https://doi.org/10.1016/j.solener.2005.05.013
Stevanovic V, Maslovaric B, Prica S (2012) Dynamics of steam accumulation. Appl Therm Eng 37:73–79. https://doi.org/10.1016/j.applthermaleng.2012.01.007
Stevanovic VD, Petrovic MM, Milivojevic S, Maslovaric B (2015) Prediction and control of steam accumulation. Heat Transf Eng 36:498–510. https://doi.org/10.1080/01457632.2014.935226
Sun B, Guo J, Lei Y, Yang L, Li Y, Zhang G (2015) Simulation and verification of a non-equilibrium thermodynamic model for a steam catapult’s steam accumulator. Int J Heat Mass Transf 85:88–97. https://doi.org/10.1016/j.ijheatmasstransfer.2015.01.120
Thomas A (1996) Design methodology for a small solar steam generation system using the flash boiler concept. Energ Convers Manag 37(1):1–15. https://doi.org/10.1016/0196-8904(95)00022-6
Tyagi VK, Lo SL (2011) Application of physico-chemical pretreatment methods to enhance the sludge disintegration and subsequent anaerobic digestion: an up to date review. Rev Environ Sci Bio Technol 10(3):215. https://doi.org/10.1007/s11157-011-9244-9
Wenqiang S, Yuhao H, Yanhui W (2017) Operation optimization of steam accumulators as thermal energy storage and buffer units. Energies 10(1):1–16. https://doi.org/10.3390/en10010017
Zhang G, Sun B, Li Y, Ma H, Liu C, Wang Y (2013) Simulation study on influencing factors of rapid steam-charging process in steam accumulator. Appl Mech Mater 281:563–567. https://doi.org/10.4028/www.scientific.net/AMM.281.563
Zhen G, Lu X, Kato H, Zhao Y, Li YY (2017) Overview of pretreatment strategies for enhancing sewage sludge disintegration and subsequent anaerobic digestion: current advances, full-scale application and future perspectives. Renew Sustain Energy Rev 69:559–577. https://doi.org/10.1016/j.rser.2016.11.187
Acknowledgements
The author wishes to thank the plant manager of the Burgos WWTP for the great support during the implementation of this research. This research was possible thanks to financial support from Ministerio de Economía y Competitividad and ERDF through Project UNLE15-EE-3070.
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García-Cascallana, J., Borge-Díez, D. & Gómez, X. Enhancing the efficiency of thermal hydrolysis process in wastewater treatment plants by the use of steam accumulation. Int. J. Environ. Sci. Technol. 16, 3403–3418 (2019). https://doi.org/10.1007/s13762-018-1982-6
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DOI: https://doi.org/10.1007/s13762-018-1982-6