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LPG Purification with zeolite 13X and 3A molecular sieve

Table of Contents

Customer Background

Combined use of 3A & 13X molecular sieves with activated carbon in LPG purification removes H₂S, odor, and moisture, preventing pipeline blockage.

An LPG refinery faced issues with H₂S, mercaptans, moisture, and heavy hydrocarbons in its product stream—leading to equipment corrosion, odor, and catalyst poisoning. Traditional adsorbents couldn’t effectively remove all impurities. A three-stage adsorption process using activated carbon, 13X, and 3A molecular sieves was adopted for deep desulfurization, dehydration, and heavy hydrocarbon removal.

Process Overview

1.LPG Feed Composition & Targets

Impurity                            Before (ppm)                          Target (ppm) 
H₂S                                     200                                             < 0.5 
CH₃SH                                50                                               < 1                                                                              H₂O                                     100                                             < 5      
C5+                                     300                                             < 10 

2.Three-Stage Adsorption Design

  • Stage 1 – Activated Carbon:
    Removes C5+ hydrocarbons and partial sulfur compounds.
    Prevents clogging and protects downstream adsorbents.
  • Stage 2 – 13X Molecular Sieve:
    Removes H₂S, mercaptans, and moisture.
    High sulfur capacity (4–6 wt%), reduces water to <10 ppm.
  • Stage 3 – 3A Molecular Sieve:
    Final dehydration to <5 ppm H₂O.
    Selective to water, prevents LPG loss and freezing.

3.Regeneration Methods

  • Activated Carbon: Hot N₂ or steam (150–200°C)
  • Zeolite 13X: High-temp N₂ (250–300°C)
  • Zeolite 3A: Low-temp purge (180–220°C)

Results

Impurity                                        Before (ppm)                              After (ppm)
H₂S                                                200                                                < 0.5
CH₃SH                                           50                                                  < 1
H₂O                                                100                                                < 3
C5+                                                300                                                < 10

Benefits

  • 30% lower operating cost than traditional processes.
  • Longer adsorbent life (Carbon: 1 yr, 13X: 3 yrs, 3A: 5 yrs).
  • Reduced waste—saves ~¥800,000/year in alkali treatment.
  •  Meets GB 11174-2011 and reduces SO₂ emissions.

Application Scope & Value

Ideal for   

  • LPG/natural gas purification (refineries, depots)
  • Raw gas (propylene, butene) purification
  • Autogas treatment

Optimization Tips:

  • Adjust desiccants 13X loading based on sulfur content.
  • Use TSA (Temperature Swing Adsorption) for efficiency.
  • Monitor pressure drop to prevent bed clogging.

Conclusion

The 13X + 3A + activated carbon process offers a cost-effective, environmentally friendly solution for ultra-deep LPG purification, making it suitable for high-standard energy and chemical applications.

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