Jump to content

Ostwald process: Difference between revisions

From Niidae Wiki
imported>Citation bot
Add: bibcode, authors 1-1. Removed parameters. Some additions/deletions were parameter name changes. | Use this bot. Report bugs. | Suggested by Dominic3203 | Category:Chemical processes | #UCB_Category 10/256
 
(No difference)

Latest revision as of 02:51, 15 March 2025

Template:Short description The Ostwald process is a chemical process used for making nitric acid (HNO3).<ref name=Ull>Template:Cite encyclopedia</ref> The Ostwald process is a mainstay of the modern chemical industry, and it provides the main raw material for the most common type of fertilizer production.<ref>Template:Cite book</ref> Historically and practically, the Ostwald process is closely associated with the Haber process, which provides the requisite raw material, ammonia (NH3). This method is preferred over other methods of nitric acid production, in that it is less expensive and more efficient.<ref>Template:Cite web</ref>

Reactions

[edit]

Ammonia is converted to nitric acid in 2 stages.

Initial oxidation of ammonia

[edit]

The Ostwald process begins with burning ammonia. Ammonia burns in oxygen at temperature about Template:Convert and pressure up to Template:Convert<ref>Template:Cite book</ref> in the presence of a catalyst such as platinum gauze, alloyed with 10% rhodium to increase its strength and nitric oxide yield, platinum metal on fused silica wool, copper or nickel to form nitric oxide (nitrogen(II) oxide) and water (as steam). This reaction is strongly exothermic, making it a useful heat source once initiated:<ref name="jones1">Template:Cite book</ref>

Template:Chem2H = −905.2 kJ/mol)

Side reactions

[edit]

A number of side reactions compete with the formation of nitric oxide. Some reactions convert the ammonia to N2, such as:

Template:Chem2

This is a secondary reaction that is minimised by reducing the time the gas mixtures are in contact with the catalyst.<ref>Template:Cite book</ref> Another side reaction produces nitrous oxide:

Template:Chem2H = −1105 kJ/mol)

Platinum-rhodium catalyst

[edit]

The platinum and rhodium catalyst is frequently replaced due to decomposition as a result of the extreme conditions which it operates under, leading to a form of degradation called cauliflowering.<ref name=":02">Template:Cite journal</ref> The exact mechanism of this process is unknown, the main theories being physical degradation by hydrogen atoms penetrating the platinum-rhodium lattice, or by metal atom transport from the centre of the metal to the surface.<ref name=":02" />

Secondary oxidation

[edit]

The nitric oxide (NO) formed in the prior catalysed reaction is then cooled down from around 900˚C to roughly 250˚C to be further oxidised to nitrogen dioxide (NO2)<ref>Template:Cite web</ref> by the reaction:

Template:Chem2H = -114.2 kJ/mol)<ref>Template:Cite journal</ref>

The reaction:

Template:Chem2H = -57.2 kJ/mol)<ref>Template:Cite web</ref>

also occurs once the nitrogen dioxide has formed.<ref name=":0">Template:Citation</ref>

Conversion of nitric oxide

[edit]

Stage two encompasses the absorption of nitrous oxides in water and is carried out in an absorption apparatus, a plate column containing water.Template:Cn This gas is then readily absorbed by the water, yielding the desired product (nitric acid in a dilute form), while reducing a portion of it back to nitric oxide:<ref name="jones1" />

Template:Chem2H = −117 kJ/mol)

The NO is recycled, and the acid is concentrated to the required strength by distillation.

This is only one of over 40 absorption reactions of nitrous oxides recorded,<ref name=":0" /> with other common reactions including:

Template:Chem2

And, if the last step is carried out in air:

Template:Chem2H = −348 kJ/mol).

Overall reaction

[edit]

The overall reaction is the sum of the first equation, 3 times the second equation, and 2 times the last equation; all divided by 2:

Template:Chem2H = −740.6 kJ/mol)

Alternatively, if the last step is carried out in the air, the overall reaction is the sum of equation 1, 2 times equation 2, and equation 4; all divided by 2.

Without considering the state of the water,

Template:Chem2H = −370.3 kJ/mol)

History

[edit]

Template:Expand section Wilhelm Ostwald developed the process, and he patented it in 1902.<ref>Template:Cite patent</ref><ref>Template:Cite patent</ref>

See also

[edit]

References

[edit]

Template:Reflist

[edit]