Jump to content
Main menu
Main menu
move to sidebar
hide
Navigation
Main page
Recent changes
Random page
Help about MediaWiki
Special pages
Niidae Wiki
Search
Search
Appearance
Create account
Log in
Personal tools
Create account
Log in
Pages for logged out editors
learn more
Contributions
Talk
Editing
Methanol
(section)
Page
Discussion
English
Read
Edit
View history
Tools
Tools
move to sidebar
hide
Actions
Read
Edit
View history
General
What links here
Related changes
Page information
Appearance
move to sidebar
hide
Warning:
You are not logged in. Your IP address will be publicly visible if you make any edits. If you
log in
or
create an account
, your edits will be attributed to your username, along with other benefits.
Anti-spam check. Do
not
fill this in!
===From synthesis gas=== Carbon monoxide and hydrogen react over a catalyst to produce methanol. Today, the most widely used catalyst is a mixture of copper and [[zinc oxide]]s, [[catalyst support|supported]] on [[alumina]], as first used by [[Imperial Chemical Industries|ICI]] in 1966. At 5–10 MPa (50–100 atm) and {{convert|250|C}}, the reaction :{{chem2 | CO + 2 H2 -> CH3OH }} is characterized by high selectivity (>99.8%). The production of [[syngas|synthesis gas]] from methane produces three [[Mole (unit)|mole]]s of hydrogen for every mole of carbon monoxide, whereas the synthesis consumes only two moles of hydrogen gas per mole of carbon monoxide. One way of dealing with the excess hydrogen is to inject [[carbon dioxide]] into the methanol synthesis reactor, where it, too, reacts to form methanol according to the equation :{{chem2 | CO2 + 3 H2 -> CH3OH + H2O }} In terms of mechanism, the process occurs via initial conversion of CO into {{chem2|CO2}}, which is then [[hydrogenation|hydrogenated]]:<ref>Deutschmann, Olaf; Knözinger, Helmut; Kochloefl, Karl and Turek, Thomas (2012) "Heterogeneous Catalysis and Solid Catalysts, 3. Industrial Applications" in ''Ullmann's Encyclopedia of Industrial Chemistry''. Wiley-VCH, Weinheim. {{doi|10.1002/14356007.o05_o03}}</ref> :{{chem2 | CO2 + 3 H2 -> CH3OH + H2O }} where the {{chem2|H2O}} byproduct is recycled via the [[water gas shift reaction|water-gas shift reaction]] :{{chem2 | CO + H2O -> CO2 + H2 }} This gives an overall reaction :{{chem2 | CO + 2 H2 -> CH3OH }} which is the same as listed above. In a process closely related to methanol production from synthesis gas, a feed of hydrogen and {{chem2|CO2}} can be used directly.<ref>{{Cite journal|last1=Bozzano|first1=Giulia|last2=Manenti|first2=Flavio|date=2016|title=Efficient methanol synthesis: Perspectives, technologies and optimization strategies|url=https://www.sciencedirect.com/science/article/pii/S0360128515300484|journal=Progress in Energy and Combustion Science|language=en|volume=56|page=76|doi=10.1016/j.pecs.2016.06.001|bibcode=2016PECS...56...71B |issn=0360-1285}}</ref> The main advantage of this process is that [[Carbon capture and storage|captured {{chem2|CO2}}]] and hydrogen sourced from [[Electrolysis of water|electrolysis]] could be used, removing the dependence on fossil fuels.
Summary:
Please note that all contributions to Niidae Wiki may be edited, altered, or removed by other contributors. If you do not want your writing to be edited mercilessly, then do not submit it here.
You are also promising us that you wrote this yourself, or copied it from a public domain or similar free resource (see
Encyclopedia:Copyrights
for details).
Do not submit copyrighted work without permission!
Cancel
Editing help
(opens in new window)
Search
Search
Editing
Methanol
(section)
Add topic