Next Article in Journal
Characterization and Assessment of a Novel Plate and Frame MD Module for Single Pass Wastewater Concentration–FEED Gap Air Gap Membrane Distillation
Next Article in Special Issue
Hydrogen Production via Steam Reforming: A Critical Analysis of MR and RMM Technologies
Previous Article in Journal
Highly Selective Oxygen/Nitrogen Separation Membrane Engineered Using a Porphyrin-Based Oxygen Carrier
Previous Article in Special Issue
Theoretical Evaluation of Graphene Membrane Performance for Hydrogen Separation Using Molecular Dynamic Simulation
 
 
Article
Peer-Review Record

Techno-Economic Assessment in a Fluidized Bed Membrane Reactor for Small-Scale H2 Production: Effect of Membrane Support Thickness

Membranes 2019, 9(9), 116; https://doi.org/10.3390/membranes9090116
by Gioele Di Marcoberardino 1, Jasper Knijff 2, Marco Binotti 3, Fausto Gallucci 2 and Giampaolo Manzolini 3,*
Reviewer 1: Anonymous
Reviewer 2: Anonymous
Membranes 2019, 9(9), 116; https://doi.org/10.3390/membranes9090116
Submission received: 6 August 2019 / Revised: 3 September 2019 / Accepted: 3 September 2019 / Published: 6 September 2019

Round 1

Reviewer 1 Report

The projection price (target price) of hydrogen is 2$/kg but here we can see other values such as 3$/kg and 5$/kg. Comment on this. Table 1 needs further information such as thermal expansion, strength, creep, yield, pore size. A discussion on elemental analysis of the ceramic support can clarify the type of the ceramic. Qualitative comparison is not scientific. Authors could do the comparison in the text and remove the table. More elaboration on Fig. 1 is required. The assumption list and also the method of solution must be further discussed. Which software was employed to solve the equations? (7)-(9) need proper support or citations from the literature. Validation of the model against the experimental data is required to show the reliability of the model. Fig 8: The layout of the system must be further described. Type of the HEX, burner, separator and other units should be discussed. For example, for separator, is it just a thermodynamic separator or there is a specific configuration considered for it? What is the amortising period for the assessment of the process? Table 9: What is the reference case for the cost assumption given in Table 9? Provide the citation. A sensitivity analysis is required between LCOH and the cost assumptions used in Table 9 .

Author Response

Please see the attachment

Author Response File: Author Response.docx

Reviewer 2 Report

Techno-economic assessment on support thickness 3 for Pd-membrane in fluidized bed reactor for small 4 scale H2 production review

The manuscript presents an interesting topic in the techno-economic assessment in different membranes, however, in my opinion, minor corrections in the manuscript should be done before considering it for publication.

I suggest that the authors get editing help from someone with full professional proficiency in English to revise the entire English writing through the manuscript The novelty needs to be highlighted in the introduction as I struggled to find the novelty In your introduction section, you mentioned “Hydrogen has a higher energy density” which is full picture as the energy density of hydrogen compressed at 700 bar is 9.17 MJ/L, while it is 35.8 MJ/L for diesel at atmospheric pressure, so in term of safety and energy density, hydrogen fuel is in favourable, please comment it in the manuscript. In your introduction section, you mentioned the methane in biogas applications, however, you also need to mention the methane slip challenge as well.

 

 

Author Response

please see the attachment

Author Response File: Author Response.docx

Round 2

Reviewer 1 Report

Authors have addressed my comments. Paper can be accepted now.

Back to TopTop