Low tar yield and high energy conversion efficiency in a continuous pyrolysis reactor with modified ribbon screw conveyor

Anıl Ünsaç*, Hasan Can Okutan, Nilgün Karatepe

*Bu çalışma için yazışmadan sorumlu yazar

Araştırma sonucu: Dergiye katkıMakalebilirkişi

2 Atıf (Scopus)

Özet

The high temperature batch and continuous pyrolysis of rice husk, sewage sludge, composite waste, hazelnut and apricot kernel shell were performed at 850 °C in a rotating batch reactor and a continuous reactor with a modified ribbon screw conveyor. Batch results were used in the continuous reactor design and comparison. At the continuous pyrolysis experiments, mixing and conveying efficiency of screw and thermal cracking performance of reactor, heated gas line and cyclone were investigated. Each material was fed into the reactor continuously with a feed rate of 4.5 kg/h for 3.5 h, and then the pipelines and reactor were monitored and collected tar and char were analyzed. The mixing unit and uninterrupted heated system showed excellent performance on tar reduction and tar yields were lower than 1.7 % for all materials. Separation of char dust from the gas without tar condensation in a heated cyclone prevented blocking in gas lines. With the secondary reactions syngas energy conversion efficiency for rice husk, sewage sludge, composite waste, hazelnut shell, and apricot kernel shell were 67.76 %, 59.22 %, 76.35 %, 56.96 %, 61.98 % respectively. With the new design with a modified ribbon screw, different types of materials were decomposed with minimum char yield in less than 15 min without mechanical problems. The high capacity of the installed reactor as 1–10 kg/h moved the technology readiness level (TRL) to 5 and set an example for demonstration in operational environment.

Orijinal dilİngilizce
Sayfa (başlangıç-bitiş)1332-1343
Sayfa sayısı12
DergiInternational Journal of Hydrogen Energy
Hacim53
DOI'lar
Yayın durumuYayınlandı - 31 Oca 2024

Bibliyografik not

Publisher Copyright:
© 2023 Hydrogen Energy Publications LLC

Finansman

This work made use of Synthetic Fuels and Chemicals Technology Center Facilities at Istanbul Technical University. The authors would like to express their appreciation and gratitude to Presidency of the Republic of Turkey Strategy and Budget Presidency for providing the funding of ITU Synthetic Fuels and Chemicals Technology Center Project (grant number 2016K121250). This work made use of Synthetic Fuels and Chemicals Technology Center Facilities at Istanbul Technical University. The authors would like to express their appreciation and gratitude to Presidency of the Republic of Turkey Strategy and Budget Presidency for providing the funding of ITU Synthetic Fuels and Chemicals Technology Center Project (grant number 2016K121250 ).

FinansörlerFinansör numarası
International Technological University2016K121250
Istanbul Teknik Üniversitesi

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