2011 Feb Dewaxing Aids

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2011 Feb Dewaxing Aids

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  • Dewaxing Aids

    Increased Profitability

    by Optimizing Wax/Oil

    Separation

    Evonik RohMax Additives GmbH. London, 25th of February 2011

    Andr Unglert Technical Sales Manager

  • 1. Group I Base Oil and Waxes

    2. Solvent Dewaxing and

    Dewaxing Aids (DWAs)

    3. Case Studies

  • 328,5 million tonnes per year*

    570.000 barrels per day*

    2010

    * Source: LubesnGreases, January 2011, Vol. 17, Issue 1

    2020

    -25%

    21 million tonnes per year*

    420.000 barrels per day*

    Group I Capacities in 20XX

    Bright Stocks and Heavy

    Grades

    High Quality Waxes

    High Oil Yields

    High Throughputs

    Lower Oil-in-wax

    20XX

  • 4Consequences for Group I Refineries

    Close or

    Shut-down

    Optimize

    Convert

    Wait and See

    Group II and

    III or Fuels

    Focus on

    Bright StocksFocus on

    Waxes

    Tailored

    Dewaxing Aids

    Group I

    Refineries

  • 1. Group I Base Oil and Waxes

    2. Solvent Dewaxing and

    Dewaxing Aids (DWAs)

    3. Case Studies

  • 6 Separation of lube oil from wax

    Precipitation of wax crystals in a chilled solvent

    system

    MEK/toluene, propane, MIBK

    Filtration under specific operating conditions in a

    rotary drum filter

    - vacuum pressure,

    - drum rotation interval,

    - solvent wash conditions,

    - filter wash interval

    Solvent removal from oil and wax

    Solvent Dewaxing General Info

  • 7RaffinateRaffinate

    Filtrate ( Oil / Solvent )Filtrate ( Oil / Solvent )

    Slack waxSlack wax

    Cold solventCold solvent

    Process Operation

    Process variables:

    Filtration temperature

    Solvent ratio

    Drum rotation interval

    Solvent wash conditions

    Process outcomes:

    Filtration rate

    Oil yield

    Oil-in-wax content

    Costs

  • 8RaffinateRaffinate

    Filtrate ( Oil / Solvent )Filtrate ( Oil / Solvent )

    Slack waxSlack wax

    Cold solventCold solvent

    Improved Process with DWAs

    Potential benefits on

    process outcomes:

    Filtration rate

    Oil yield

    Oil-in-wax content

    Costs

  • 9 PAMA dewaxing aids are based on variable chemistry

    R = alkyl side chain with

    varying chain length

    Higher alkyl side chains

    interact with higher paraffins

    Lower alkyl side chains

    interact with lower waxes

    Side chain distribution can

    be designed to give the

    best match

    O O

    R

    The Chemistry behind our DWAs

    Raffinate Paraffin Distribution

    Tailored DWA Side Chain Distribution

  • 10

    Dewaxing Mechanism (1/2)

  • 11

    Raffinate Raffinate Filtrate ( Oil / Solvent ) Filtrate ( Oil / Solvent )

    Slack wax Slack wax

    Cold solventCold solvent

    Dewaxing Mechanism (2/2)

    +70+70CC --2020CC

    Without a

    dewaxing aid -

    Crystalline

    network

    With a dewaxing aid

    - More uniform sized

    wax crystals

    Cross-polarized microscopic pictures from the solution at -20C

  • 12

    A Successful Project Approach

    Understanding

    Needs

    Laboratory

    Testing

    Plant

    Trial

    Apply optimized

    laboratory

    screening

    techniques

    Identify most

    promising

    dewaxing aid

    Characterize

    refinery

    processes

    Get samples of

    the raffinates

    Identify

    improvement

    levers

    Agree upon

    targets

    Confirm the

    performance

    in the field

    On-site

    Support by

    DWA experts

  • 1. Group I Base Oil and Waxes

    2. Solvent Dewaxing and

    Dewaxing Aids (DWAs)

    3. Case Studies

  • 14

    Case Study 1 Bright Stock (BS)

    DEWAXING AID Pump

  • 15

    Case Study 1 Bright Stock (BS)

    Oil Yield (%)

    Without

    DWA

    870

    1250

    78,0

    82,329% Oil

    in Wax

    Wax Yield (%)

    Throughput or

    Feed Rate (m/day)

    With

    DWA

    Without

    DWA

    With

    DWA

    22,0

    17,7 12% Oil

    in Wax

    > 40%

  • 16

    Case Study 2 Bright Stock (BS)

    Oil Yield (%)450

    510

    72

    62 Throughput or

    Feed Rate (m/day)

    Without

    DWA

    With

    DWA

    Without

    DWA

    With

    DWA

    14%

  • 17

    Case Study 2 Heavy Grade

    Oil Yield (%)

    500

    585

    67

    71

    Throughput or

    Feed Rate (m/day)

    Without

    DWA

    With

    DWA

    Without

    DWA

    With

    DWA

    17%

  • 18

    Conclusion

    Increased

    Oil Yield

    Improved

    Wax Quality

    Total

    Added

    Value

    Increased

    Throughput