{"id":435,"date":"2025-11-18T12:39:34","date_gmt":"2025-11-18T11:39:34","guid":{"rendered":"https:\/\/sites.unica.it\/hydrochar\/?page_id=435"},"modified":"2026-06-10T15:35:17","modified_gmt":"2026-06-10T13:35:17","slug":"process-water-liquor","status":"publish","type":"page","link":"https:\/\/sites.unica.it\/hydrochar\/wikichar\/hydrothermal-products\/process-water-liquor\/","title":{"rendered":"Process water\/Liquor"},"content":{"rendered":"\n<hr class=\"wp-block-separator aligncenter has-alpha-channel-opacity is-style-wide\" \/>\n\n\n\n<h2 class=\"wp-block-heading\">Origin and Role of Process Water in HTC<\/h2>\n\n\n\n<p>Process water (PW) is a liquid by-product generated during HTC, which involves treating wet biomass or organic waste under subcritical conditions (Boamah and Salaudeen, 2025; Ipiales et al., 2021; Taran et al., 2025). This liquid is separated from the resulting slurry by processes such as filtration or centrifugation after the reaction (Zhi et al., 2024). In terms of volume, it usually represents the dominant fraction of HTC products (Boamah and Salaudeen, 2025). Although it was traditionally considered a secondary waste product, recent studies recognize its value as a co-product rich in dissolved organic and inorganic substances released and transformed from the original feedstock (Chu et al., 2026; Langone and Basso, 2020; Mahata et al., 2026; Pei et al., 2026; Shekoohiyan et al., 2025).<\/p>\n\n\n\n<h2 class=\"wp-block-heading\">Chemical Composition and Variability<\/h2>\n\n\n\n<p>The composition of PW is chemically dense and highly complex. It typically exhibits high levels of total organic carbon (TOC) and chemical oxygen demand (COD) (Chu et al., 2026; Mahata et al., 2026; Zhi et al., 2024). It is also characterized by a high nutrient content, particularly bioavailable ammonium nitrogen and orthophosphate. However, depending on the feedstock type and reaction temperature, it may also carry heavy metals and be highly saline (Chu et al., 2026; Langone and Basso, 2020; Mahata et al., 2026, 2023; Zhang et al., 2025).<\/p>\n\n\n\n<figure class=\"wp-block-image size-full is-resized\"><img loading=\"lazy\" decoding=\"async\" width=\"1184\" height=\"659\" src=\"http:\/\/sites.unica.it\/hydrochar\/files\/2026\/06\/PW_1.jpg\" alt=\"\" class=\"wp-image-1670\" style=\"width:1208px;height:auto\" srcset=\"https:\/\/sites.unica.it\/hydrochar\/files\/2026\/06\/PW_1.jpg 1184w, https:\/\/sites.unica.it\/hydrochar\/files\/2026\/06\/PW_1-300x167.jpg 300w, https:\/\/sites.unica.it\/hydrochar\/files\/2026\/06\/PW_1-1024x570.jpg 1024w, https:\/\/sites.unica.it\/hydrochar\/files\/2026\/06\/PW_1-768x427.jpg 768w\" sizes=\"auto, (max-width: 1184px) 100vw, 1184px\" \/><\/figure>\n\n\n\n<h2 class=\"wp-block-heading\">Environmental Risks and Need for Treatment<\/h2>\n\n\n\n<p>Treatment of HTC PW is necessary, as its direct discharge into the environment may pose significant ecological risks. PW is a highly concentrated effluent which, due to its nutrient load and toxic intermediates, can cause freshwater eutrophication and significant ecotoxicity in aquatic ecosystems (Mahata et al., 2023). The presence of inhibitory and recalcitrant compounds can further disrupt biological systems (Ipiales et al., 2021). Therefore, effective management strategies are required to reduce the organic and mineral content to acceptable levels, ensuring the HTC process remains environmentally safe and economically viable (Mahata et al., 2026).<\/p>\n\n\n\n<h2 class=\"wp-block-heading\">Reuse and Valorization Pathways<\/h2>\n\n\n\n<p>The reuse and valorization of PW are important for closing loops within a circular bioeconomy, and there are several forms of these processes. The recirculation of the aqueous phase into the HTC reactor has been identified as a key strategy that serves to reduce the consumption of fresh water. The utilization of organic acids as an in-situ catalyst has been demonstrated to enhance hydrochar yields and fuel properties (Boamah and Salaudeen, 2025). Anaerobic digestion of PW represents another significant pathway, converting a high organic load into methane-rich biogas. In this context, HTC functions as a thermal hydrolysis pretreatment, solubilizing organic matter and thereby facilitating biological degradation (Ipiales et al., 2021; Kwapi\u0144ska et al., 2025). In the field of agriculture, PW can be valorized as a liquid fertilizer or biostimulant, with the objective of promoting soil microbial diversity and crop yields. However, it is important to note that dilution is essential in order to mitigate phytotoxicity and salt stress (Chu et al., 2026; Mahata et al., 2026). The recovery of specific nutrients, such as phosphorus, through the process of struvite precipitation can achieve up to 99% phosphorus recovery (Chu et al., 2026).<\/p>\n\n\n\n<h2 class=\"wp-block-heading\">Strategic Relevance and Future Perspectives<\/h2>\n\n\n\n<p>Overall, the status of PW from HTC has shifted from that of problematic waste to a strategic resource for bioenergy and nutrient recovery. Due to its highly variable composition, which depends strictly on the types of feedstocks used and the specific operating conditions, successful valorization requires the development of integrated, tailored management technologies. To advance HTC towards successful industrial-scale application, future efforts must prioritize detailed characterization, optimization of treatment routes and the establishment of clear regulatory frameworks. Harnessing all HTC fractions effectively, particularly the liquid phase, is key to creating a sustainable cycle of value in waste management.<\/p>\n\n\n\n<h2 class=\"wp-block-heading\"><strong>\ud83d\udcd6\u00a0References<\/strong><\/h2>\n\n\n\n<p>Boamah, N.N., Salaudeen, S.A., 2025. Process water from the hydrothermal carbonization of biomass: A review on the characterization, applications, and potential for future work. Journal of Water Process Engineering. <a href=\"https:\/\/doi.org\/10.1016\/j.jwpe.2025.108531\">https:\/\/doi.org\/10.1016\/j.jwpe.2025.108531<\/a><\/p>\n\n\n\n<p>Chu, Q., Liu, X., Feng, Y., Li, D., Yin, S., Chen, C., Sha, Z., 2026. Process water from hydrothermal carbonization: from waste to liquid fertilizer and soil health amendment in circular bioeconomy. Biochar. <a href=\"https:\/\/doi.org\/10.1007\/s42773-026-00614-y\">https:\/\/doi.org\/10.1007\/s42773-026-00614-y<\/a><\/p>\n\n\n\n<p>Ipiales, R.P., de la Rubia, M.A., Diaz, E., Mohedano, A.F., Rodriguez, J.J., 2021. Integration of hydrothermal carbonization and anaerobic digestion for energy recovery of biomass waste: An overview. Energy and Fuels. <a href=\"https:\/\/doi.org\/10.1021\/acs.energyfuels.1c01681\">https:\/\/doi.org\/10.1021\/acs.energyfuels.1c01681<\/a><\/p>\n\n\n\n<p>Kwapi\u0144ska, M., Burke, N., Leahy, J.J., 2025. Hydrothermal carbonization and pyrolysis of dairy processing sludge for improved nutrient management in agriculture: Current state-of-the-art. Chemical Engineering Journal Advances. <a href=\"https:\/\/doi.org\/10.1016\/j.ceja.2025.100888\">https:\/\/doi.org\/10.1016\/j.ceja.2025.100888<\/a><\/p>\n\n\n\n<p>Langone, M., Basso, D., 2020. Process waters from hydrothermal carbonization of sludge: Characteristics and possible valorization pathways. Int. J. Environ. Res. Public Health 17, 1\u201331. <a href=\"https:\/\/doi.org\/10.3390\/ijerph17186618\">https:\/\/doi.org\/10.3390\/ijerph17186618<\/a><\/p>\n\n\n\n<p>Mahata, S., Majee, P., Bhar, R., Mondal, A., Yadav, B.K., Dubey, B.K., 2026. Decoding the Valorization of Hydrothermal Carbonization Process Water: From Chemical Complexity to Circular Waste-Management Pathways. ACS ES and T Engineering. <a href=\"https:\/\/doi.org\/10.1021\/acsestengg.5c01034\">https:\/\/doi.org\/10.1021\/acsestengg.5c01034<\/a><\/p>\n\n\n\n<p>Mahata, S., Periyavaram, S.R., Akkupalli, N.K., Srivastava, S., Matli, C., 2023. A review on Co-Hydrothermal carbonization of sludge: Effect of process parameters, reaction pathway, and pollutant transport. Journal of the Energy Institute. <a href=\"https:\/\/doi.org\/10.1016\/j.joei.2023.101340\">https:\/\/doi.org\/10.1016\/j.joei.2023.101340<\/a><\/p>\n\n\n\n<p>Pei, L., Wufuer, R., Duo, J., Duan, P.-G., Elendu, C.C., Yang, F., Wang, S., Liu, Y., Edna, O.U., Wang, X., 2026. Machine learning-enhanced life cycle assessment of hydrothermal carbonization for agro-waste valorization: Innovations in sustainable soil remediation. Ind. Crops Prod. 241, 122704. <a href=\"https:\/\/doi.org\/10.1016\/j.indcrop.2026.122704\">https:\/\/doi.org\/10.1016\/j.indcrop.2026.122704<\/a><\/p>\n\n\n\n<p>Shekoohiyan, S., Sajadi, A., Moussavi, G., Heidari, M., 2025. Hydrothermal carbonization of plastic wastes and effect of influential parameters on performance and challenges: a review. International Journal of Environmental Science and Technology. <a href=\"https:\/\/doi.org\/10.1007\/s13762-025-06394-5\">https:\/\/doi.org\/10.1007\/s13762-025-06394-5<\/a><\/p>\n\n\n\n<p>Taran, J., Bhar, R., Jha, H., Kuila, S.K., Samal, B., Pradhan, R., Dubey, B.K., 2025. Synthetic coalification of microalgae through hydrothermal carbonization: strategies for enhanced hydrochar characteristics and technological advancements. Bioresour. Technol. <a href=\"https:\/\/doi.org\/10.1016\/j.biortech.2025.132542\">https:\/\/doi.org\/10.1016\/j.biortech.2025.132542<\/a><\/p>\n\n\n\n<p>Zhang, B., Syed, N.R., Zhang, J., Ma, X., Xu, Q., 2025. A systematic review on nitrogen control during hydrothermal carbonization of sewage sludge under PRISMA guidelines. J. Anal. Appl. Pyrolysis. <a href=\"https:\/\/doi.org\/10.1016\/j.jaap.2025.106965\">https:\/\/doi.org\/10.1016\/j.jaap.2025.106965<\/a><\/p>\n\n\n\n<p>Zhi, Y., Xu, D., Jiang, G., Yang, W., Chen, Z., Duan, P., Zhang, J., 2024. A review of hydrothermal carbonization of municipal sludge: Process conditions, physicochemical properties, methods coupling, energy balances and life cycle analyses. Fuel Processing Technology. <a href=\"https:\/\/doi.org\/10.1016\/j.fuproc.2023.107943\">https:\/\/doi.org\/10.1016\/j.fuproc.2023.107943<\/a><\/p>\n","protected":false},"excerpt":{"rendered":"<p>Origin and Role of Process Water in HTC Process water (PW) is a liquid by-product generated during HTC, which involves treating wet biomass or organic waste under subcritical conditions (Boamah and Salaudeen, 2025; Ipiales et al., [&hellip;]<\/p>\n","protected":false},"author":3514,"featured_media":0,"parent":407,"menu_order":0,"comment_status":"closed","ping_status":"closed","template":"","meta":{"footnotes":""},"class_list":["post-435","page","type-page","status-publish","hentry"],"_links":{"self":[{"href":"https:\/\/sites.unica.it\/hydrochar\/wp-json\/wp\/v2\/pages\/435","targetHints":{"allow":["GET"]}}],"collection":[{"href":"https:\/\/sites.unica.it\/hydrochar\/wp-json\/wp\/v2\/pages"}],"about":[{"href":"https:\/\/sites.unica.it\/hydrochar\/wp-json\/wp\/v2\/types\/page"}],"author":[{"embeddable":true,"href":"https:\/\/sites.unica.it\/hydrochar\/wp-json\/wp\/v2\/users\/3514"}],"replies":[{"embeddable":true,"href":"https:\/\/sites.unica.it\/hydrochar\/wp-json\/wp\/v2\/comments?post=435"}],"version-history":[{"count":6,"href":"https:\/\/sites.unica.it\/hydrochar\/wp-json\/wp\/v2\/pages\/435\/revisions"}],"predecessor-version":[{"id":1671,"href":"https:\/\/sites.unica.it\/hydrochar\/wp-json\/wp\/v2\/pages\/435\/revisions\/1671"}],"up":[{"embeddable":true,"href":"https:\/\/sites.unica.it\/hydrochar\/wp-json\/wp\/v2\/pages\/407"}],"wp:attachment":[{"href":"https:\/\/sites.unica.it\/hydrochar\/wp-json\/wp\/v2\/media?parent=435"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}