Performance analysis of cross-draft biomass gasifier and synthesis gas burner as heat source for small ceramic kilns

The traditional biscuit firing process typically uses LPG, firewood, or electricity as a heat source. This research explores the application of a cross-draft biomass gasifier to generate and combust synthesis gas from rubberwood scraps as a heat source for small ceramic kilns. The firing program con...

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Main Authors: Puthanate Tabrak, Nathawat Unsomsri, Pathipan Manchit, Sittinun Tawkaew, Songkran Wiriyasart, Sommas Kaewluan
Format: Article
Language:English
Published: Elsevier 2025-07-01
Series:Case Studies in Thermal Engineering
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Online Access:http://www.sciencedirect.com/science/article/pii/S2214157X25004514
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author Puthanate Tabrak
Nathawat Unsomsri
Pathipan Manchit
Sittinun Tawkaew
Songkran Wiriyasart
Sommas Kaewluan
author_facet Puthanate Tabrak
Nathawat Unsomsri
Pathipan Manchit
Sittinun Tawkaew
Songkran Wiriyasart
Sommas Kaewluan
author_sort Puthanate Tabrak
collection DOAJ
description The traditional biscuit firing process typically uses LPG, firewood, or electricity as a heat source. This research explores the application of a cross-draft biomass gasifier to generate and combust synthesis gas from rubberwood scraps as a heat source for small ceramic kilns. The firing program consists of two stages. In the first stage, rubberwood scraps are burned with primary air in the gasifier, causing the equivalence ratio (ER) to decrease from 2.07 to 1.36. During this stage, the kiln's internal temperature rises from room temperature to 400 °C. In the second stage, synthesis gas from the gasifier is burned at the burner with secondary air, reducing the ER from 1.68 to 1.18 and increasing the kiln temperature from 400 °C to 800 °C. Gas emission analysis showed that carbon monoxide (CO) remained below 690 ppm, while nitrogen oxides (NOx) peaked at 225 ppm at kiln temperatures above 400 °C. The final biscuit product exhibited a shrinkage of 2.69 %, a density of 1.71 g/mL, and a water absorption rate of 18.51 %.
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publishDate 2025-07-01
publisher Elsevier
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series Case Studies in Thermal Engineering
spelling doaj-art-e631c9644ddf40e0b2b71a2ac2bc1ea22025-08-20T03:18:23ZengElsevierCase Studies in Thermal Engineering2214-157X2025-07-017110619110.1016/j.csite.2025.106191Performance analysis of cross-draft biomass gasifier and synthesis gas burner as heat source for small ceramic kilnsPuthanate Tabrak0Nathawat Unsomsri1Pathipan Manchit2Sittinun Tawkaew3Songkran Wiriyasart4Sommas Kaewluan5Biofuel and Bioenergy Technology Research and Development Laboratory (BBT R&D), Department of Mechanical Engineering, Faculty of Engineering, Srinakharinwirot University,ThailandBiofuel and Bioenergy Technology Research and Development Laboratory (BBT R&D), Department of Mechanical Engineering, Faculty of Engineering, Srinakharinwirot University,ThailandBiofuel and Bioenergy Technology Research and Development Laboratory (BBT R&D), Department of Mechanical Engineering, Faculty of Engineering, Srinakharinwirot University,ThailandDepartment of Chemical Engineering, Faculty of Engineering, Srinakharinwirot University, 63 Rangsit-Nakhonnayok Rd., Ongkharak, Nakhon-nayok, 26120, ThailandThermal Solution and Energy Technology Research and Development Laboratory (TSET R&D), Department of Mechanical Engineering, Faculty of Engineering, Srinakharinwirot University, ThailandBiofuel and Bioenergy Technology Research and Development Laboratory (BBT R&D), Department of Mechanical Engineering, Faculty of Engineering, Srinakharinwirot University,Thailand; Corresponding author.The traditional biscuit firing process typically uses LPG, firewood, or electricity as a heat source. This research explores the application of a cross-draft biomass gasifier to generate and combust synthesis gas from rubberwood scraps as a heat source for small ceramic kilns. The firing program consists of two stages. In the first stage, rubberwood scraps are burned with primary air in the gasifier, causing the equivalence ratio (ER) to decrease from 2.07 to 1.36. During this stage, the kiln's internal temperature rises from room temperature to 400 °C. In the second stage, synthesis gas from the gasifier is burned at the burner with secondary air, reducing the ER from 1.68 to 1.18 and increasing the kiln temperature from 400 °C to 800 °C. Gas emission analysis showed that carbon monoxide (CO) remained below 690 ppm, while nitrogen oxides (NOx) peaked at 225 ppm at kiln temperatures above 400 °C. The final biscuit product exhibited a shrinkage of 2.69 %, a density of 1.71 g/mL, and a water absorption rate of 18.51 %.http://www.sciencedirect.com/science/article/pii/S2214157X25004514Crossdraft gasifierSynthesis gasGasificationBiscuit firingRubberwood scraps
spellingShingle Puthanate Tabrak
Nathawat Unsomsri
Pathipan Manchit
Sittinun Tawkaew
Songkran Wiriyasart
Sommas Kaewluan
Performance analysis of cross-draft biomass gasifier and synthesis gas burner as heat source for small ceramic kilns
Case Studies in Thermal Engineering
Crossdraft gasifier
Synthesis gas
Gasification
Biscuit firing
Rubberwood scraps
title Performance analysis of cross-draft biomass gasifier and synthesis gas burner as heat source for small ceramic kilns
title_full Performance analysis of cross-draft biomass gasifier and synthesis gas burner as heat source for small ceramic kilns
title_fullStr Performance analysis of cross-draft biomass gasifier and synthesis gas burner as heat source for small ceramic kilns
title_full_unstemmed Performance analysis of cross-draft biomass gasifier and synthesis gas burner as heat source for small ceramic kilns
title_short Performance analysis of cross-draft biomass gasifier and synthesis gas burner as heat source for small ceramic kilns
title_sort performance analysis of cross draft biomass gasifier and synthesis gas burner as heat source for small ceramic kilns
topic Crossdraft gasifier
Synthesis gas
Gasification
Biscuit firing
Rubberwood scraps
url http://www.sciencedirect.com/science/article/pii/S2214157X25004514
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AT pathipanmanchit performanceanalysisofcrossdraftbiomassgasifierandsynthesisgasburnerasheatsourceforsmallceramickilns
AT sittinuntawkaew performanceanalysisofcrossdraftbiomassgasifierandsynthesisgasburnerasheatsourceforsmallceramickilns
AT songkranwiriyasart performanceanalysisofcrossdraftbiomassgasifierandsynthesisgasburnerasheatsourceforsmallceramickilns
AT sommaskaewluan performanceanalysisofcrossdraftbiomassgasifierandsynthesisgasburnerasheatsourceforsmallceramickilns