darbaz khasraw

Mr. darbaz khasraw

orcid

Research Focus & Metrics

Academic Career Length

6Years (2021-Present)

(Calculated once Scilit publication data is synced: current year − year of first publication + 1)

Representative Publications

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13 April 2024 in Fuel
Verified
Journal Article
Closed access
DKdarbaz khasraw
darbaz khasraw
CMCiarán Martin
Ciarán Martin
JHJulian Herbert
Julian Herbert
ZLZushu Li
Zushu Li

10 August 2022 in Metallurgical and Materials Transactions B
Verified
Journal Article
Open access
PDF file
DKdarbaz khasraw
darbaz khasraw
ZYZhiming Yan
Zhiming Yan
JHJohannes L. T. Hage
Johannes L. T. Hage
KMKoen Meijer
Koen Meijer
ZLZushu Li
Zushu Li
To investigate the use of biomass in the novel HIsarna technology, the reduction of FeO in the slag by chars produced from thermal coal (TC), charcoal (CC), and Bana grass char (BGC) was studied. A drop tube furnace coupled with a quadrupole mass spectrometer (DTF-QMS) was employed to study the injection of chars into pre-melted slag in the temperature range between 1450 °C and 1525 °C. The reduction rate was calculated from evolved gases and the extent of FeO reduction was confirmed by wavelength-dispersive X-ray fluorescence (WDXRF). The FeO reduction proceeds through two stages, starting with a rapid reduction, which is dependent on the carbon type, and followed by gradual leveling off. The reduction rate with the charcoal char (CC) was the highest, over 60 pct reduction was achieved in the first 500 seconds at 1500 °C, while ~ 50 and 40 pct achieved with TC and BGC chars, respectively, for the same reaction time. The kinetic analysis suggests that the first and second stages of the reaction can be described by the second-order (F2) and three-dimensional diffusion (D3) models, respectively. The apparent activation energy values for the first stage were 290, 229 and 267 kJ/mol for reactions with TC, CC and BGC chars, while 265, 369, and 282 kJ/mol were obtained for the second stage. Based on the experimental data and kinetic results, it can be concluded that the first stage is controlled by chemical reactions on the carbon surface, and the second stage is influenced by a mixed-controlling mechanism.

9 November 2021 in Metals
Verified
Journal Article
Open access
PDF file
SZShuo Zhao
Shuo Zhao
ZLZushu Li
Zushu Li
RXRenze Xu
Renze Xu
DKdarbaz khasraw
darbaz khasraw
GSGaoyang Song
Gaoyang Song
DXDong Xu
Dong Xu
Al2O3, Al2O3·TiN, Al2O3·MgO, and CaO·2Al2O3 are four different types of inclusions in high Al steels. To improve the steel cleanness level, the effective removal of such inclusions during secondary refining is very important, so these inclusions should be removed effectively via inclusion dissolution in the slag. The dissolution behavior of Al2O3, Al2O3·TiN, Al2O3·MgO, and CaO·2Al2O3 in CaO-SiO2-Al2O3-MgO slags, as well as the steel-slag reaction, was investigated using laser scanning confocal microscopy (LSCM) and high-temperature furnace experiments, and thermodynamic calculations for the inclusion in steel were carried out by FactSage 7.1. The results showed that Al2O3·TiN was observed to be completely different from the other oxides. The composite oxides dissolved quickly in the slags, and the dissolution time of the inclusions increased as their melting point increased. SiO2 and B2O3 in the slag were almost completely reacted with [Al] in steel, so the slags without SiO2 showed a positive effect for avoiding the formation of Al2O3 system inclusions and promoting inclusions dissolution as compared with SiO2-rich slags. The steel-slag reaction was also found to influence the inclusion types in steel significantly. Because of the rapid absorption of different inclusions in the slag, it was found that the dissolution time of inclusions mainly depends on the diffusion in the molten slag.

1 May 2021 in Fuel
Verified
Journal Article
Closed access
DKdarbaz khasraw
darbaz khasraw
SSStephen Spooner
Stephen Spooner
HHHans Hage
Hans Hage
KMKoen Meijer
Koen Meijer
ZLZushu Li
Zushu Li

7 August 2025 in Bioresource Technology
Verified
Journal Article
Open access
CDChay A. Davies-Smith
Chay A. Davies-Smith
JHJulian Herbert
Julian Herbert
CMCiarán Martin
Ciarán Martin
DKdarbaz khasraw
darbaz khasraw
DWDavid Warren-Walker
David Warren-Walker
RBRakesh Bhatia
Rakesh Bhatia
Biochar has potential applications in steelmaking processes, but faces technical challenges such as low material density, high alkali content, and high reactivity compared to coal. This study explores converting the solid residue, following hydrothermal pretreatment-steam explosion (HTP-SE) of Miscanthus and other biomass feedstocks, into biochar to facilitate the replacement of coal in blast furnace and electric arc furnace operations. It is the first to demonstrate the enhanced combustion characteristics of pretreated fibre and the compatibility of the biochar for use in steelmaking. Biomass from birch, miscanthus, wheat straw, both untreated and pretreated, was evaluated. HTP-SE was conducted at 192 °C and 1.3 MPa, conditions aligned with hemicellulose extraction for application in biobased products. Biochars were produced at temperatures ranging from 300 °C to 550 °C. HTP-SE increased the carbon, hydrogen, and energy content by approximately 10%, 8%, and up to 5 MJ/kg, respectively, while reducing ash quantity by up to 45%. In addition, it reduced the alkali and phosphorus content from the solid fraction into aqueous phase. Gas analysis indicated that HTP-SE enhanced the energy content of pyrolysis syngas. Thermogravimetric studies revealed that pretreated biochars exhibited significantly lower reactivity with carbon dioxide compared to untreated counterparts, approaching the reactivity of coal. This was attributed to increased aromaticity, C=C bonding, cross-linkages enriching lignin and by the removal of hemicellulose through HTP-SE. Overall, the upgraded biochar addresses key limitations of conventional biochar and shows strong potential as a substitute to replace injection coal entirely in both blast and electric arc furnaces.

3 June 2026
Verified
Book Chapter
Closed access
PDF file
MAMasoud Ahmadinia
Masoud Ahmadinia
SSStephen Spooner
Stephen Spooner
DKdarbaz khasraw
darbaz khasraw
MKMarcos Kauffman
Marcos Kauffman
GGGraham Giles
Graham Giles
BSBhavik Shah
Bhavik Shah