2017
DOI: 10.1016/j.ijhydene.2017.09.056
|View full text |Cite
|
Sign up to set email alerts
|

Operational experiences of PEMFC pilot plant using low grade hydrogen from sodium chlorate production process

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
1
1
1
1

Citation Types

0
6
0

Year Published

2018
2018
2024
2024

Publication Types

Select...
8

Relationship

0
8

Authors

Journals

citations
Cited by 21 publications
(6 citation statements)
references
References 24 publications
0
6
0
Order By: Relevance
“…where, P H 2 O is the saturation pressure of water vapor in atm, given in Equation (8). RH a and RH c are relative humidity of vapor at anode and cathode respectively [41].…”
Section: Output Voltage Of Pem Fuel Cellmentioning
confidence: 99%
See 1 more Smart Citation
“…where, P H 2 O is the saturation pressure of water vapor in atm, given in Equation (8). RH a and RH c are relative humidity of vapor at anode and cathode respectively [41].…”
Section: Output Voltage Of Pem Fuel Cellmentioning
confidence: 99%
“…For these reasons, the hydrogen-fueled cars on the global market have been fed by PEMFCs, where they participate in about 90% of fuel cell research and development [6]. For instance, in Finland, a substantial amount of hydrogen is extracted as a byproduct in industrial factories that specialize in chlorine and sodium chlorate, whereas the hydrogen quality is adequate for employment as a sustainable fuel in PEMFCs [7,8]. As a result, this hydrogen can be used in PEMFC power plants that operate at partial loading conditions, and so they can yield an important quick load cover in power systems, besides other renewable energy sources [9][10][11][12].…”
Section: Introductionmentioning
confidence: 99%
“…The two following mechanisms are well-known in the chemical industry under the form of the chlor-alkali process 58 and the chlorate production process. 59 The only difference between direct seawater electrolysis and the mentioned industrial processes is that the industrial ones use saturated and purified brines, containing NaCl or KCl, depending on the desired type of caustic or chlorate. 60 Both processes, chlor-alkali and chlorate production, share the same redox reactions, defined by the following equations: Anode:…”
Section: Technologiesmentioning
confidence: 99%
“…The first route follows the mechanisms that are explained in the Low-temperature electrolysis. The two following mechanisms are well-known in the chemical industry under the form of the chlor-alkali process and the chlorate production process . The only difference between direct seawater electrolysis and the mentioned industrial processes is that the industrial ones use saturated and purified brines, containing NaCl or KCl, depending on the desired type of caustic or chlorate .…”
Section: Suitable Seawater Electrolysis Technologiesmentioning
confidence: 99%
“…17 Indeed, reduction of the degradation in the case of ageing under reformate are mostly considered through the adaptation of the operating conditions such as air bleeding, temperature or humidity control, cleaning procedures including stops or pure hydrogen feeding to remove the CO adsorbed. More recent papers present interesting long-term durability studies with contamination issues at stack or system level but with air contaminant 18 or with only non-controlled CO traces, 19 thus allowing few direct comparison with studies conducted at stack level with CO content representative of a reformate stationary case. 20,21 Recently, focus has also been put on the analysis of the heterogeneities of degradation thanks to local post mortem analyses performed in different zones of the aged MEAs 25,26 or thanks to in situ measurements techniques allowing direct information about local performance or electrochemical properties.…”
mentioning
confidence: 99%