Abstract

For ethylene/ethane separation, a CMS (carbon molecular sieve) membrane was developed with a PAN (polyacrylonitrile) polymer precursor on an alumina support. To provide an excellent thermal property to PAN precursor prior to the pyrolysis, the stabilization as a pre-treatment process was carried out. Tuning the stabilization condition was very important to successfully preparing the CMS membrane derived from the PAN precursor. The stabilization and pyrolysis processes for the PAN precursor were finely tuned, and optimized in terms of stabilization temperature and time, as well as pyrolysis temperature, heating rate, and soaking time. The PAN stabilized at >250 °C showed improved thermal stability and carbon yield. The CMS membrane derived from stabilized PAN showed reasonable separation performance for ethylene permeance (0.71 GPU) and ethylene/ethane selectivity (7.62), respectively. Increasing the pyrolysis temperature and soaking time gave rise to an increase in the gas permeance, and a reduction in the membrane selectivity. This trend was opposite to that for the CMS membranes derived from other polymer precursors. The optimized separation performance (ethylene permeance of 2.97 GPU and ethylene/ethane selectivity of 7.25) could be achieved at the pyrolysis temperature of 650 °C with a soaking time of 1 h. The separation performance of the CMS membrane derived from the PAN precursor was comparable to that of other polymer precursors, and surpassed them regarding the upper bound trade off.

Highlights

  • The olefin/paraffin separation using a conventional distillation process requires high energy consumption due to their similar physical properties [1,2,3]

  • A carbon molecular sieve membrane has shown excellent olefin/paraffin separation performance, which was attributed to the rigid pore structure [7]

  • The CMS membranes derived from various polymers of intrinsic microporosity (PIM) precursors showed high ethylene/ethane separation performance of 10–44 barrer, and 6.29–17.9 for ethylene permeability and ethylene/ethane selectivity, respectively [33,34,35]

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Summary

Introduction

The olefin/paraffin separation using a conventional distillation process requires high energy consumption due to their similar physical properties [1,2,3]. The CMS membranes derived from various PIM precursors (such as PIM-1, PIM-6FDA, and PIM-cyclodextrin) showed high ethylene/ethane separation performance of 10–44 barrer, and 6.29–17.9 for ethylene permeability and ethylene/ethane selectivity, respectively [33,34,35]. To optimize the separation performance of CMS membranes derived from various polymer precursors for olefin/paraffin separation, many researchers have studied several effective pyrolysis factors, such as heating rate, soaking time, pyrolysis temperature, and gas atmosphere. To optimize the ethylene/ethane separation performance of a PAN-based CMS membrane, we finely tuned and optimized the stabilization and pyrolysis processes in terms of the stabilization temperature and time, as well as the pyrolysis temperature, soaking time, and heating rate. The helium (99.9999%), argon (99.9999%), and ethylene/ethane mixture (80/20 mol%) were supplied by Joongang Industrial Gas Co. (Daejeon, Korea)

Preparation of PAN-Based CMS Membranes
Characterizations
Structure of CMS Composite Membranes
Conclusions
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