Powder Explosion Inhibitor Prepared from Waste Incinerator Slag: Applied to Explosion Suppression of Oil Shale Dust Explosion
Round 1
Reviewer 1 Report
At this point in the development of science in the world, the authors' studies are relevant for industry. The article is presented as a completed scientific work. However, I have a few points to make. These notes are presented in the attached file.
Comments for author File: 
Comments.pdf
Author Response
Please see the attachment.
Author Response File: Author Response.pdf
Reviewer 2 Report
Powder Explosion Inhibitor Prepared from Waste Incinerator Slag: Applied to Explosion Suppression of Oil Shale Dust Explosion is very interesting paper. Some improvement is required!
Line 13: Abstract: In this paper, an application method of waste incinerator slag (based on following oxides:.....)
Line 22: MSA-NaHCO3 (Please to write full name for MSA)
Line 36: dust explosion accidents in industrial production (which type of dust?)
Line 56: composite powder (which type of composite?)
Line 79: PH value (pH value)
LIne 151: Hence from the SEM diagrams (please to add a particle size of composite), the composite powder explosion inhibitor prepared by WCSC method is more efficacious.
Line 285: The flame length of oil shale dust reduces with increasing amount of slag-based composite powder in all cases (in which range (ratio)? what are limitations?)
Line 344: Figure 12. The SEM image of explosion residues after explosion inhibition (can you add EDX (or XRD) analysis of the the explosion residues?)
Line 359: Combustion reaction insufficient, resulting in a lower CO2 content and a higher CO content (please to write a combustion reaction in order to understand it)
Line 387: MSA-NaHCO3 composite powder explosion inhibitor generates
gas (which type of gas? What is composition of gas?)
Line 403: The TG curve shows that decomposition begins at around 100 °C and ends at 186 °C (in which time period)
Author Response
Please see the attachment.
Author Response File: Author Response.pdf
