<HashMap><database>biostudies-literature</database><scores/><additional><submitter>Zhou S</submitter><funding>Key Technologies Research and Development Program</funding><funding>National Key Research and Development Program of China</funding><funding>China Three Gorges Corporation</funding><pagination>100259</pagination><full_dataset_link>https://www.ebi.ac.uk/biostudies/studies/S-EPMC11490804</full_dataset_link><repository>biostudies-literature</repository><omics_type>Unknown</omics_type><volume>25</volume><pubmed_abstract>High solid anaerobic digestion (HSAD) achieves the benefits of high volumetric loading rates and lower reject water production, which, however, results in much more concentrated reject water with a remarkable increase in organics and nitrogen compared with that from conventional AD with low solid content. The high concentrations of ammonium (2000-3500 mg/L) and COD (3000-4000 mg/L) were reported to exert inhibition on anammox bacteria (AnAOB), posing challenges to the application of the partial nitritation/anammox (PN/A). To date, no cases of PN/A process start-up for sludge HSAD reject water were reported. This study demonstrated the start-up process of a 480 m&lt;sup>3&lt;/sup>/d PN/A project without anammox sludge inoculation and treating HSAD reject water from a centralized dewatered sludge treatment plant. The project did not construct new infrastructures but utilized previously constructed tanks to upgrade the process from existing short-cut nitrification-denitrification to a two-stage PN/A process. Although no external anammox sludge inoculation was performed to save seeding sludge cost, the start-up was successfully achieved in about 9 months (273 days) based on a three-step method of "AnAOB enrichment - sludge acclimation - capacity doubling". During start-up, the relative abundance of AnAOB (Candidatus_&lt;i>Kuenenia&lt;/i>) increased from near zero to 12.0%. After start-up, the total inorganic nitrogen (TIN) removal load reached 0.74 kgN/(m&lt;sup>3&lt;/sup>•d), with a total nitrogen removal efficiency of over 90%. Compared to the traditional nitrification-denitrification process, the PN/A process remarkably reduces the addition of organic chemicals and aeration energy consumption, saving approximately 4.2 million yuan (RMB) in operational costs annually. In summary, this research provides a full-scale reference for the start-up of the PN/A process treating sludge HSAD reject water.</pubmed_abstract><journal>Water research X</journal><pubmed_title>Start-up of a full-scale two-stage partial nitritation/anammox (PN/A) process treating reject water from high solid anaerobic sludge digestion (HSAD).</pubmed_title><pmcid>PMC11490804</pmcid><funding_grant_id>202403018</funding_grant_id><funding_grant_id>2020YFC1908702</funding_grant_id><pubmed_authors>Yang J</pubmed_authors><pubmed_authors>Zhou S</pubmed_authors><pubmed_authors>Zhang Y</pubmed_authors><pubmed_authors>Gu G</pubmed_authors><pubmed_authors>Xu E</pubmed_authors><pubmed_authors>Chen X</pubmed_authors><pubmed_authors>Wang X</pubmed_authors><pubmed_authors>Wang H</pubmed_authors><pubmed_authors>Gong H</pubmed_authors><pubmed_authors>Zhu D</pubmed_authors><pubmed_authors>Dai X</pubmed_authors></additional><is_claimable>false</is_claimable><name>Start-up of a full-scale two-stage partial nitritation/anammox (PN/A) process treating reject water from high solid anaerobic sludge digestion (HSAD).</name><description>High solid anaerobic digestion (HSAD) achieves the benefits of high volumetric loading rates and lower reject water production, which, however, results in much more concentrated reject water with a remarkable increase in organics and nitrogen compared with that from conventional AD with low solid content. The high concentrations of ammonium (2000-3500 mg/L) and COD (3000-4000 mg/L) were reported to exert inhibition on anammox bacteria (AnAOB), posing challenges to the application of the partial nitritation/anammox (PN/A). To date, no cases of PN/A process start-up for sludge HSAD reject water were reported. This study demonstrated the start-up process of a 480 m&lt;sup>3&lt;/sup>/d PN/A project without anammox sludge inoculation and treating HSAD reject water from a centralized dewatered sludge treatment plant. The project did not construct new infrastructures but utilized previously constructed tanks to upgrade the process from existing short-cut nitrification-denitrification to a two-stage PN/A process. Although no external anammox sludge inoculation was performed to save seeding sludge cost, the start-up was successfully achieved in about 9 months (273 days) based on a three-step method of "AnAOB enrichment - sludge acclimation - capacity doubling". During start-up, the relative abundance of AnAOB (Candidatus_&lt;i>Kuenenia&lt;/i>) increased from near zero to 12.0%. After start-up, the total inorganic nitrogen (TIN) removal load reached 0.74 kgN/(m&lt;sup>3&lt;/sup>•d), with a total nitrogen removal efficiency of over 90%. Compared to the traditional nitrification-denitrification process, the PN/A process remarkably reduces the addition of organic chemicals and aeration energy consumption, saving approximately 4.2 million yuan (RMB) in operational costs annually. In summary, this research provides a full-scale reference for the start-up of the PN/A process treating sludge HSAD reject water.</description><dates><release>2024-01-01T00:00:00Z</release><publication>2024 Dec</publication><modification>2026-06-30T03:10:19.648Z</modification><creation>2026-06-29T03:09:54.723Z</creation></dates><accession>S-EPMC11490804</accession><cross_references><pubmed>39429521</pubmed><doi>10.1016/j.wroa.2024.100259</doi></cross_references></HashMap>