Simulation and Experiment of the Homogeneously Catalyzed Production of Terpenyl Amine

Robin Schulz, Laura Sengen, Katja Gießelmann, Sira Hunold, Tim Zeiner

Research output: Contribution to journalArticleResearchpeer-review

Abstract

Continuous terpenyl amine production via a homogeneously catalyzed hydroamination is presented. For the recycling of the catalyst a liquid-liquid system combined with a subsequent acid complexation as capturing step for the terpenyl amine was used. The whole process was run in pilot plant scale. At first, batch experiments were conducted to determine reaction equilibria of the hydroamination and the acid complexation. On this, a process model was developed which is based on equilibrium stages. This process model was validated by running the continuous process and was able to predict the continuous process in good agreement with experimental data. So, it allows a reduction of the experimental effort.

Original languageEnglish
Pages (from-to)947-955
Number of pages9
JournalChemie - Ingenieur - Technik
Volume90
Issue number7
DOIs
Publication statusPublished - 1 Jul 2018

Fingerprint

Complexation
Amines
Acids
Liquids
Pilot plants
Recycling
Experiments
Catalysts

Keywords

  • Continuous process
  • Hydroamination
  • Liquid-liquid system
  • Reactive extraction
  • Simulation

ASJC Scopus subject areas

  • Chemistry(all)
  • Chemical Engineering(all)
  • Industrial and Manufacturing Engineering

Cite this

Simulation and Experiment of the Homogeneously Catalyzed Production of Terpenyl Amine. / Schulz, Robin; Sengen, Laura; Gießelmann, Katja; Hunold, Sira; Zeiner, Tim.

In: Chemie - Ingenieur - Technik, Vol. 90, No. 7, 01.07.2018, p. 947-955.

Research output: Contribution to journalArticleResearchpeer-review

Schulz, Robin ; Sengen, Laura ; Gießelmann, Katja ; Hunold, Sira ; Zeiner, Tim. / Simulation and Experiment of the Homogeneously Catalyzed Production of Terpenyl Amine. In: Chemie - Ingenieur - Technik. 2018 ; Vol. 90, No. 7. pp. 947-955.
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