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Sewage sludge and digestate gasification in an atmospheric fluidized bed gasifier

Identifikátory výsledku

  • Kód výsledku v IS VaVaI

    <a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F00216305%3A26210%2F23%3APU148153" target="_blank" >RIV/00216305:26210/23:PU148153 - isvavai.cz</a>

  • Výsledek na webu

    <a href="https://link.springer.com/article/10.1007/s13399-023-04276-9" target="_blank" >https://link.springer.com/article/10.1007/s13399-023-04276-9</a>

  • DOI - Digital Object Identifier

    <a href="http://dx.doi.org/10.1007/s13399-023-04276-9" target="_blank" >10.1007/s13399-023-04276-9</a>

Alternativní jazyky

  • Jazyk výsledku

    angličtina

  • Název v původním jazyce

    Sewage sludge and digestate gasification in an atmospheric fluidized bed gasifier

  • Popis výsledku v původním jazyce

    The gasification of sewage sludge (SS) and digestate was investigated in a pilot-scale fluidized bed gasifier with an outputof 100 kWt. The treatment of these by-products is an ongoing challenge for sustainable development. SS and digestate aremost commonly used as fertilizers. However, regulations restrict their use, mainly because of the content of heavy metals,pathogens and bacteria. Gasification of these by-products instead of application to agricultural land seems to be more effi-cient, as the syngas can subsequently be used for combined heat and power (CHP) generation. A series of measurementswere carried out to get a better understanding of the gasification process of these fuels and to study the effects of gasifyingagent on the syngas composition, particulate matter (PM) and tar. The produced syngas and tar were analyzed using a gaschromatograph with mass spectrometry (GC–MS). The results showed that no ash slagging was observed and therefore itis feasible to operate digestate and SS gasification at 750°C. The lower heating value (LHV) of the syngas from digestateand SS with air as the gasifying agent is comparable, 4.06 MJ·Nm−3 for digestate and 4.11 MJ·Nm−3 for SS. The additionof steam had a positive effect on the amount of tar and the tar dew point, which was below 150°C. Tar reduction in digestatewas 5037.3 mg·Nm−3 to 3566.3 mg·Nm−3 and in SS 7447.7 mg·Nm−3 to 3390.3 mg·Nm−3. Furthermore, the concentrationsof the individual tar compounds were determined and subsequently divided into tar classes.

  • Název v anglickém jazyce

    Sewage sludge and digestate gasification in an atmospheric fluidized bed gasifier

  • Popis výsledku anglicky

    The gasification of sewage sludge (SS) and digestate was investigated in a pilot-scale fluidized bed gasifier with an outputof 100 kWt. The treatment of these by-products is an ongoing challenge for sustainable development. SS and digestate aremost commonly used as fertilizers. However, regulations restrict their use, mainly because of the content of heavy metals,pathogens and bacteria. Gasification of these by-products instead of application to agricultural land seems to be more effi-cient, as the syngas can subsequently be used for combined heat and power (CHP) generation. A series of measurementswere carried out to get a better understanding of the gasification process of these fuels and to study the effects of gasifyingagent on the syngas composition, particulate matter (PM) and tar. The produced syngas and tar were analyzed using a gaschromatograph with mass spectrometry (GC–MS). The results showed that no ash slagging was observed and therefore itis feasible to operate digestate and SS gasification at 750°C. The lower heating value (LHV) of the syngas from digestateand SS with air as the gasifying agent is comparable, 4.06 MJ·Nm−3 for digestate and 4.11 MJ·Nm−3 for SS. The additionof steam had a positive effect on the amount of tar and the tar dew point, which was below 150°C. Tar reduction in digestatewas 5037.3 mg·Nm−3 to 3566.3 mg·Nm−3 and in SS 7447.7 mg·Nm−3 to 3390.3 mg·Nm−3. Furthermore, the concentrationsof the individual tar compounds were determined and subsequently divided into tar classes.

Klasifikace

  • Druh

    J<sub>imp</sub> - Článek v periodiku v databázi Web of Science

  • CEP obor

  • OECD FORD obor

    20704 - Energy and fuels

Návaznosti výsledku

  • Projekt

    <a href="/cs/project/EF16_019%2F0000753" target="_blank" >EF16_019/0000753: Centrum výzkumu nízkouhlíkových energetických technologií</a><br>

  • Návaznosti

    P - Projekt vyzkumu a vyvoje financovany z verejnych zdroju (s odkazem do CEP)

Ostatní

  • Rok uplatnění

    2023

  • Kód důvěrnosti údajů

    S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů

Údaje specifické pro druh výsledku

  • Název periodika

    Biomass Conversion and Biorefinery

  • ISSN

    2190-6815

  • e-ISSN

    2190-6823

  • Svazek periodika

    May

  • Číslo periodika v rámci svazku

    May

  • Stát vydavatele periodika

    DE - Spolková republika Německo

  • Počet stran výsledku

    9

  • Strana od-do

    „“-„“

  • Kód UT WoS článku

    000980332700001

  • EID výsledku v databázi Scopus

    2-s2.0-85158047185