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Sewage sludge and digestate gasification in an atmospheric fluidized bed gasifier

The result's identifiers

  • Result code in 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>

  • Result on the web

    <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>

Alternative languages

  • Result language

    angličtina

  • Original language name

    Sewage sludge and digestate gasification in an atmospheric fluidized bed gasifier

  • Original language description

    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.

  • Czech name

  • Czech description

Classification

  • Type

    J<sub>imp</sub> - Article in a specialist periodical, which is included in the Web of Science database

  • CEP classification

  • OECD FORD branch

    20704 - Energy and fuels

Result continuities

  • Project

    <a href="/en/project/EF16_019%2F0000753" target="_blank" >EF16_019/0000753: Research centre for low-carbon energy technologies</a><br>

  • Continuities

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

Others

  • Publication year

    2023

  • Confidentiality

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

Data specific for result type

  • Name of the periodical

    Biomass Conversion and Biorefinery

  • ISSN

    2190-6815

  • e-ISSN

    2190-6823

  • Volume of the periodical

    May

  • Issue of the periodical within the volume

    May

  • Country of publishing house

    DE - GERMANY

  • Number of pages

    9

  • Pages from-to

    „“-„“

  • UT code for WoS article

    000980332700001

  • EID of the result in the Scopus database

    2-s2.0-85158047185