Densicat

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    1.The dense loading process

    Reminder of the sock loading process

    During loading

    - Loading is not homogeneous- High void space in the catalyst bed- Reactor capacity not at maximum- Loading rate about 6 to 8 t/h- High risk of catalyst attrition

    - Risk of breakage if the technician walks on thebed during loading

    During operation

    - Preferential channels can form> Higher temperatures> Preferential coking/plugging> Shorter cycle

    - Compaction of the catalyst bed- Increased maintenance budget- Non optimised operation of the loaded catalyst.

    The advantages

    of Densicat/Catapac technologies

    Better dense loading

    During loading

    - More homogenous loading- Lower void space in the catalyst bed

    - 10 to 20% more catalyst can be loaded- Loading rate up to 25 t/h

    During operation

    - Maximum catalyst activity- Homogeneous distribution of the flow in the

    reactor- Reactor at maximum capacity.

    The (PETROVAL) Dense Loading process

    A certified, experienced technician- Trained in the specific characteristics of the reactors- Certification renewed every year

    A certified machine- The latest available technology : Densicat and/or

    Catapac- Full maintenance before each job

    Technical procedure in accordance with

    standards- Catalyst density guaranteed before loading- Machine installed in accordance with PETROVAL

    standards- Inspection and checking of the catalyst bed profile- Fully documented report

    Densicat and/or Catapac :Horizontal orientation of catalyst particles

    Sock loading :Random catalyst particles orientation

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    2.Densicat and Catapac

    Petroval know-how More than 50 reactors / year / PETROVAL technician Each technician is trained for all types of dense loading Density guaranteed

    Flat profile of bed

    Very flexible technologies

    Size and type of reactor- Diameter from 0,4 to 7,5 m.- Reactor types : axial, radial, spherical, multi-bed,

    reactor with excentric manholes ...

    - The only procedures capable of loading very largereactors

    Catalyst flow- From 0,6 to 25 t/h- The only procedures capable of achieving very

    high catalyst flows without causing attrition

    Maximum load volume- These technologies permit loading up to 40cm

    below the distribution tray (depending on reactor

    diameter)

    For efficient dense loading, the PETROVAL

    solution : Densicat, Catapac

    Best possible distribution of catalyst particles

    Efficient for all types of catalyst :

    - Cylindrical extrudes- Trilobe extrudes- Quadrilobe extrudes

    - Spherical- Tablets

    Reduces attrition and dust

    Fast and safe

    Maximum density and levelness of the

    catalyst bed- Better activity and stability of the catalyst bed- Eliminates preferential paths

    Horizontal orientation of the particles

    - Better contact between reactive phases

    High loading rate- High level of activity and better availability of

    the unit

    Densicat

    Catapac

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    3.The technical advantages

    Evolution and product research : Densicat,

    a procedure in constant evolution

    Densicat (a)- Limitation of loading flow below 10 t/h- Densicat loading was limited to reactors with a

    diametre of less than 1,8 m

    Evolution 1 (b)- Optimisation of catalyst distribution by improvement

    of the loading flow- Flow limited to about 15 t/h- Problems observed :Too much catalyst flow in the centre of the reactor,hemispherical distribution not well managed

    Evolution 2 (c)- Modification of the strip layout for more reliable

    permeability during loading.

    - Better distribution. Flat distribution profile with alarge catalyst flow, up to 25 t/h

    Evolution 3In R&D phase.

    Objective 1: load density

    Advantages of dense loading linked todensity- Load density is near to maximum density- The increase in density depends on the type and

    size of the material to be loaded:

    a

    b

    c

    Type Density gained

    Cylindrical extrudes 14 % to 20 %Trilobe extrudes 17 % to 20 %Quadrilobe extrudes 17 % to 21 %Spherical 8 % to 12 %Tablets 12 % to 17 %

    For an existing reactor or for a new reactor, thisincrease in density allows:

    - Either to increase the conversion rate while main-taining the same operating conditions

    - Or to vary the operating conditions to your advan-tage while maintaining the same performance.

    - Technical analysis and preparation of the worksite

    - Choice of technology : Densicat or Catapac

    - Permanent on-site interface with the customer

    - Approval of the customers load targets (density,loading plan, organisation, etc.)

    - Pre-loading report

    - Technical report approved by thePETROVAL technical manager

    Ojective 2 : optimum loading organisation

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    Objective 3: loading homogeneity

    Correct dense loading- The orientation of the particles does not affectthe flow- Orientation of catalyst pellets

    > Horizontal> Perpendicular to the flow

    Concavedense load

    Convexdense load

    Dense load badlydistributed

    PETROVAL : The dense loading specialist Refineries and petrochemical sites

    More than 3 500 projects carried out since the 1990s and more than 1 200 reactors loaded Long term agreements and partnerships with

    > ExxonMobil, Shell, Total, BP> Loading performed in more than 50 countries around the world, on all six continents.

    Examples of poor dense loading

    =37

    =10

    =6 Zone 3

    Zone 2

    Densicat ZoneDensicat Zone Yes Yes

    Zone 2 No Yes

    Zone 3 No No

    Maximum

    density

    Horizontal

    orientation ofthe pellets

    Correct dense loading

    Petroval loading

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    4. Examples of industrial applications

    >PETROVAL quality charter + PETROVAL technology + PETROVAL reactiveness= optimization of maintenance shutdown and catalyst reliability

    ZoneUnit

    Reactor

    Team mobilisedNo. of loading shiftsQuantity loadedLoad heightReactor diametreSame type of loading

    EuropeDGO

    1 bed

    1160 t8,5 m3,5 m125/year

    EuropePowerformer

    Sphrical

    1136 t4,7 m6,3 m10/year

    ZoneUnit

    Reactor

    Team mobilisedNo. of loading shiftsQuantity loadedLoad heightReactor diametreSame type of loading

    EuropeReforming

    Radial

    1125 t10 m2,8 m15/year

    ZoneUnit

    ReactorTeam mobilisedNo. of loading shiftsQuantity loadedLoad heightReactor diametreSame type of loading

    AsiaAmmonia Co

    S2001135 t14 m1,2 m15/year

    ZoneUnitReactor

    Team mobilisedNo. of loading shiftsQuantity loadedLoad heightReactor diametreSame type of loading

    EuropeAnilinTubular(11800 tubes 1)1115 t3 m3,5 m5/year

    ZoneUnit

    ReactorTeam mobilisedNo. of loading shiftsQuantity loadedLoad heightReactor diametreSame type of loading

    AsiaHDT

    3 beds2 (J/N)6*500 t25 m5,7 m137/year

    ZoneUnitReactor

    Team mobilisedNo. of loading shiftsQuantity loadedLoad heightReactor diametreSame type of loading

    USAHDS6 beds

    2 (J/N)10*450 t35 m4,5 m45/year

    ZoneUnit

    Reactor 8 reactors

    Team mobilisedNo. of loading shiftsQuantity loadedLoad heightReactor diametreSame type of loading

    AsiaARDS

    double beds

    4 (J/N)25*800 t20 m4,8 m25/year

    * Internal assembling stations included

    ZoneUnit

    Reactor

    Team mobilisedNo. of loading shiftsQuantity loadedLoad heightReactor diametreSame type of loading

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    PETROVAL SA

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