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HuagongsheHuagongshe Chemistry Print Report · For research reference only
HRID 34248Generated: October 25, 2026

Acetone → Cyclohexanone

https://huagongshe.com/reaction/34248

Reaction equation

Participants

RoleNameHCIDCharge
ReactantAcetoneHCID 180—
ReactantNitric AcidHCID 944—
ReactantWaterHCID 962—
ReactantMethyl Ethyl KetoneHCID 6569—
ReactantTetrahydrofuranHCID 8028—
Solvent1-ButanolHCID 263—
SolventEthanolHCID 702—
SolventMethanolHCID 887—
Solvent1-PropanolHCID 1031—
SolventIsopropanolHCID 3776—
Solvent1,4-DioxaneHCID 31275—
ProductCyclohexanoneHCID 7967—
Product1-DecanolHCID 8174—

Reaction Steps

The conditions that can be used above in subjecting the lignin-containing material to reaction with nitric acid must be mild. The reaction can be carried out using an aqueous mixture containing the lignin-containing material and aqueous nitric acid. The nitric acid used can have a concentration of about 5 to about 100 weight percent nitric acid, preferably about 15 to about 70 weight percent nitric acid. The mixture can contain about 0 to about 95 weight percent water, preferably about 40 to about 80 weight percent water. On a weight basis, the lignin-containing material (on a dry basis) and the nitric acid (as 100 percent nitric acid) can be in the range of about 1:0.1 to about 1:10, preferably about 1:1 to about 1:2. The above is mixed while it is maintained in a temperature range of about -10° to about 150° C., preferably about 20° to about 100° C., and a pressure of about 14.5 to about 1000 pounds per square inch gauge, preferably about 14.5 to about 100 pounds per square inch gauge, for about 1 minute to about 10 hours, preferably about 0.5 to about 2 hours. The resulting reaction product is then subjected to extraction with any suitable polar solvent, for example, a ketone, such as acetone, methylethylketone, cyclohexanone, etc., an alcohol, such as methanol, ethanol, normal propanol, isopropanol, butanol, decanol, and mixtures of the lower alcohols, such as those obtained in the industrial production of fuel grade methanol and ethanol, etc., tetrahydrofuran, dioxane, etc., or mixtures thereof. The extraction can be carried out at temperatures in the range of about 0° to about 200° C. and the extraction can be continued until no further extract is obtained. Removal of polar solvent from the extract can be effected by subjecting the extract to drying or distillation. The solid material obtained is the novel alcohol soluble product used herein.

Provenance & Evidence

DOI10.6084/m9.figshare.5104873.v1
Patent numberUS04760803
Source datasetuspto-grants-1988_08
ORD IDord-574db99598fd44cd9dc192255e572cfe
Source noteuspto-grants-1988_08