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 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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Publication Details

Journal
Case Studies in Thermal Engineering
Published
2025-04-29
DOI
https://doi.org/10.1016/j.csite.2025.106191
Citations
1
Primary Topic
Thermochemical Biomass Conversion Processes
Type
article
Field-Weighted Citation Impact
0.67

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article

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

Songkran Wiriyasart, Sommas Kaewluan, Sittinun Tawkaew, Nathawat Unsomsri et al.
1 citations
Case Studies in Thermal Engineering
Thermochemical Biomass Conversion Processes
0.67
article

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

Songkran Wiriyasart, Sommas Kaewluan, Sittinun Tawkaew, Nathawat Unsomsri, Pathipan Manchit, Puthanate Tabrak
article en
1 citations

Abstract

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 %.

Case Studies in Thermal EngineeringVol. 71
Srinakharinwirot University
Openalex Percentile: Top 32%
Thermochemical Biomass Conversion Processes
0.67
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Performance analysis of cross-draft biomass gasifier and synthesis gas burner as heat source for small ceramic kilns — Songkran Wiriyasart, Sommas Kaewluan, et al. · Case Studies in Thermal Engineering (2025) | TGRS Research Map | TGRS