Key engineering innovations in industrial-scale cyclohexanone production via cyclohexene esterification–reduction

Clicks: 1
ID: 324183
2026
Article Quality & Performance Metrics
Overall Quality
Not rated
Combines reader engagement with the AI quality analysis. This article has not been analysed, so there is no overall score — reader engagement is measured and shown alongside.
AI Quality Assessment
Not analyzed
Readership in this journal

Ranked #232 of 261 articles by views in national science review

Most read Least read

Bar heights use a square-root scale. Only the 120 most-read articles are drawn; the journal has 261 in total.

Mint this article as an NFT
Not yet minted

Create a permanent, verifiable on-chain record of this article on the Scimatic Network. The NFT is held in your Journament account, and you can withdraw it to your own wallet at any time.

5 SUSD one-off · no wallet required
Abstract
Abstract Conventional industrial technologies for cyclohexanone production, a key precursor to ε-caprolactam, primarily cyclohexane oxidation (CHA-Ox) and cyclohexene hydration (CHE-Hydr), are constrained by an inherent trade-off between conversion and selectivity. This leads to low carbon atom utilization or high energy intensity, together with substantial environmental burdens. The cyclohexene esterification–reduction (CHE-ER) route, first proposed by the Research Institute of Petroleum Processing (RIPP), delivers exceptional conversion and selectivity and therefore offers a promising platform for next-generation cyclohexanone production. However, the central challenge has been to translate the intrinsic advantages of this chemistry into a process that is simultaneously economically competitive and environmentally sustainable. Here we report a set of critical chemical engineering innovations that streamline process design and substantially reduce energy consumption. By leveraging the inertness of cyclohexane during cyclohexene esterification, we designed a new extraction system that selectively separates benzene from its partial hydrogenation products. We further implemented a hybrid reactor configuration integrating a fixed-bed reactor with a catalytic reactive distillation reactor for cyclohexene esterification with acetic acid. In addition, we identified and strategically harnessed the beneficial roles of cyclohexane in facilitating reaction heat dissipation and excess acetic acid separation. These innovations have been successfully deployed in a 400 kt yr–1-capacity industrial plant for cyclohexanone production via the CHE-ER route, affording nearly complete cyclohexene conversion and cyclohexyl acetate selectivity above 99.0%. This work establishes a new-generation of industrial technology for cyclohexanone production that maximizes economic benefit, while minimizes energy demand and environmental impacts associated with conventional processes.
Reference Key
openalex_W7201879776 Use this key to autocite in the manuscript while using SciMatic Manuscript Manager or Thesis Manager
Authors Baoning Zong, Dongqiang Ma, Yanqiang Shi, Junqi Zhao, Bin Sun, Langyou Wen, Wencheng Tang, Zhaoli Yang, Minghua Qiao
Journal national science review
Year 2026
DOI
10.1093/nsr/nwag465
URL
Keywords Keywords not found

Citations

No citations found. To add a citation, contact the admin at info@scimatic.org

No comments yet. Be the first to comment on this article.