Integration of MFI Zeolite Membranes in the Light Gasoline Isomerisation Process - Archive ouverte HAL Access content directly
Journal Articles Oil & Gas Science and Technology - Revue d'IFP Energies nouvelles Year : 2009

Integration of MFI Zeolite Membranes in the Light Gasoline Isomerisation Process

(1) , (1)
1
A. Baudot
  • Function : Correspondent author

Abstract

Tests aiming at separating normal pentane from a light gasoline isomerate through a MFI zeolite composite membrane were carried out. The performances of this membrane sample were studied as a function of total hydrocarbon pressure upstream of the membrane as well as the temperature. Maximal permeate flux, close to 2 kg/m2.h, was observed at 250°C - 2 bar total hydrocarbon pressure. The normal pentane weight fraction was more than threefold higher in the permeate than in the feed. In a second step, a fully heat-integrated light gasoline isomerisation process loop integrating a MFI zeolite membrane-based separation was simulated and optimised. Integration of MFI zeolite membranes in this process proved to be valuable only if their cost is lower than 1000 EURO/m2.
Fichier principal
Vignette du fichier
ogst09047.pdf (592.01 Ko) Télécharger le fichier
Origin : Publication funded by an institution
Loading...

Dates and versions

hal-02001593 , version 1 (31-01-2019)

Identifiers

Cite

A. Baudot, L. Bournay. Integration of MFI Zeolite Membranes in the Light Gasoline Isomerisation Process. Oil & Gas Science and Technology - Revue d'IFP Energies nouvelles, 2009, 64 (6), pp.759-771. ⟨10.2516/ogst/2009073⟩. ⟨hal-02001593⟩

Collections

IFP OGST
18 View
114 Download

Altmetric

Share

Gmail Facebook Twitter LinkedIn More