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ADSORPTIVE DESULPHURISATION

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Title: ADSORPTIVE DESULPHURISATION


1
ADSORPTIVE DESULPHURISATION
  • National Centre for Catalysis Research, IIT Madras

2
Summary of Research Project on Adsorptive
Desulphurisation
  • Activated Carbons from commercial sources , and
    Zeolites were screened for their adsorption
    characteristics of sulfur compounds in Diesel.
  • Zeolites not considered for further studies for
    the following
  • 1. Poor Adsorption characteristics for
    diesel
  • desulfurisation.
  • 2. Inorganic porous material like Zeolites
    require
  • higher severity and Hydrogen for
    activation.

3
Summary of Research Project on Adsorptive
Desulphurisation
  • Activated Carbon requires appropriate
    modification to enhance capacity for adsorptive
    desulfurisation.
  • Modification of carbon is aimed for
  • 1. Textural properties improvement
  • 2. Functionalisation with Oxygen
  • Treatment with Nitric acid followed by Argon
    activation standardized for modifying carbon
  • Effectiveness for Adsorptive Desulphurisation
    studies was studied
  • The adsorbents were characterised in detail using
    XRD,FT-IR, SEM etc. to understand their
    properties

4
Summary of Research Project on Adsorptive
Desulphurisation
  • Adsorption studies were carried out on modified
    Carbon with CBR Diesel as feed in
  • 5 10 gms Scale
  • Modified Carbon could desulfurise 700 ppm feed
    sulfur to below 300 ppm
  • Preliminary studies indicate treat ratio of 1 m3
    CBR Diesel to 250 kg of adsorbents .

5
Summary of Research Project on Adsorptive
Desulphurisation
  • Regeneration of Adsorbents
  • - Gas Based Regeneration using Hydrogen
  • - Solvent Based Regeneration
    (Toluene)Solvent based regeneration using
    Toluene is found to be effective
  • Several cycles of Adsorption and regeneration
    was studied on modified carbon and the
    performance of fresh and solvent regenerated
    adsorbents were found similar

6
Summary of Research Project on Adsorptive
Desulphurisation
  • Toluene is recoverable by simple flash
    distillation of spent liquid obtained during
    regeneration of modified carbon after adsorption
    cycle.
  • Recovered Toluene is free of sulfur impurities
    and diesel hydrocarbons - Suitable again for
    regeneration cycle of modified carbon

7
Path Forward for ADS Studies
  • Designing a bench scale unit for continuous
    studies with 200 500 ml adsorbent loading
  • Validating lab scale Adsorption/ regeneration
    capacities on continuous flow mode operation
  • Collecting Data for scale up to Demo unit By
    studying progression of Adsorption/Desorption
    Breakthrough point,number of cycles,
    Regenerability of adsorbents, Regeneration time
    and solvent recovery studies.

8
Bench Scale unit in operation at CPCL RD for
Adsorptive Desulphurisation Studies
9
Properties of CBR Diesel used in bench scale
studies
10
Adsorption studies in continuous reactor using
modified carbon(Calgon Corpn.)
11
Studies on ADS in Continuous mode operation
  • Desulphurisation of Diesel was effective in the
    continuous flow mode operation also
  • However liquid hold up in the unit is relatively
    high, which in turn affects solvent regeneration
    and subsequent cycle of adsorption.
  • Liquid hold up in the bench scale reactor is the
    major constraint in studying the performance and
    cycle length of adsorbent.

12
Studies on ADS in Continuous mode operation
  • Adsorbent carbon selected for modification had a
    Granular Size of 0.8mm 1.2mm with Surface Area
    of 950 m2/gm and Pore Volume of 0.45cc/gm
  • Modification improved the surface properties with
    enhanced SA of 1080 m2/gm and PV of 0.6 cc/gm.
    However Particle size reduced with over 20
    passing through 0.7 mm sieve.

13
Studies on ADS in Continuous mode operation
  • The reduction in particle size resulted in larger
    retention of liquids (feed diesel) in
    intra-particle voids
  • Either retaining the granular size during
    modification or extrudating the adsorbent carbon
    are the available options for minimising the
    liquid hold up
  • Liquid Hold up vitiates study on the adsorption
    progression as well as Hydrocarbon mix up during
    solvent regeneration

14
Adsorbent Carbon requirement for continuous
operation
  • Liquid hold up is as high as 125 ml in our
    continuous flow experiments with 250 g adsorbent
    in a fixed bed unit.
  • Studies initiated to reduce liquid hold up by
    changing to extrudate form of the adsorbent
  • Unit for making adsorbent carbon in extrudate
    form is procured by IIT M
  • Preliminary studies for forming extrudates
    without loss of crush strength is in progress at
    IIT M . Various binders are being tried to form
    extrudates

15
Plan for further work
  • Extrudates of Adsorbent Carbon with optimum
    physical strength will be prepared with or
    without binders
  • Continuous mode of Adsorption/Regeneration
    studies will be carried out using the extrudates.
  • Based on the results obtained in the continuous
    unit at CPCL , the basis for design of
    demonstration unit will be firmed up.
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