The Principles. Settling velocity can be estimated via a well-known equation known as Stokes Law:

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The Principles of Separation SEDIMENTATION Sedimentation is one of the most versatile separation processes. Pieralisi Vertical Separators (Disc- Stack Separators) are ideally suited to separation processes where the physical characteristics of sedimentation can be applied thanks to density difference. Centrifugal sedimentation is often a very good and economical alternative to other separation processes such as: Filtration: based on particle size, Micro-Filtration: based on particle size in the sub-micron range, ADVANTAGES Separator FPC18 technical drawing Flotation: based on physicalchemical behaviour, i.e. surface tension. In many cases centrifugal sedimentation and another complementary technology are combined to achieve the required process results. The most common advantages of centrifugal sedimentation, more appropriately termed Centrifugal Separation are: compact size of equipment, low capital investments, versatility, ease of use, low operating costs, high performance. The basic principle of separation by sedimentation allows for the simultaneous separation of three different, immiscible substances. PIERALISI Vertical Separators make use of this three-phase separation regime. None of the alternative principles mentioned above can achieve this result. Sedimentation is the physical process whereby suspensions and emulsions (or a combination of both) are exposed to gravitational force, either the earth s gravity or by using a centrifuge. By applying g-force, the droplets and/or particles acquire settling velocity (vg) and are sent to the bottom/wall of the container/centrifuge bowl. Settling velocity (vg) increases with: bigger particle diameter, higher density difference, lower dynamic viscosity of the fluid environment. Settling velocity can be estimated via a well-known equation known as Stokes Law: Sedimentation is used in many industrial processes where it is necessary to separate substances that are mixed together (dispersion). With a suitable recipient and the time needed to complete the sedimentation process, the two or more substances with different densities will be separated (stratified) Separator S300 technical drawing within the recipient, the lightest going to the surface, the heaviest to the bottom. (See illustration below) INCREASING CAPACITY But what can we do if we do not have enough time or if we want to increase capacity? Going back to Stokes Law, to obtain an higher settling velocity and consequently to accelerate the sedimentation process, we can replace gravitational acceleration g by centrifugal acceleration ˆ2 r. The centrifugal acceleration ˆ2 r produced in a Pieralisi Vertical Separator is up to ten thousand times higher than the ordinary force of gravity g. As a consequence, settling velocity is up to ten thousand times faster, and separation can be achieved in a very short time and/or using very small volumes. Modified Stokes Law N.B. Stokes Law can of course only be used when the settling process takes place under conditions when the Reynolds-No. is below 0,25. For higher Reynolds-No., the Grassmann system has to be used, which takes advantage of two dimension-less parameters: the Archimedes number and the Omega number.

Pieralisi Vertical Separators Pieralisi Vertical Separators combine very high rotational speed, a unique design and special materials. They generate a very high centrifugal force which, when used for sedimentation purposes, ensures extremely efficient equipment. The mixture to be separated is forced through a conical disc stack, where multi-layer sedimentation takes place. The separation happens very quickly as the mixture passes through the parallel thin channels of the disc stack. A medium-sized Disc-Stack Separator, when using high centrifugal force, can be compared to the efficiency of a sedimentation tank with a surface area of 60,000 m 2, the same size as 10 football fields. In technical terms, this separator hosts an equivalent settling area of 60,000 m 2. HOW DOES IT WORK? Thousands of g s are produced in the bowl of the Disc Stack Separator, the centrifugal force being the product of the high rotational speed and the large size of the bowl. The rotation is generated by an electric motor connected to the horizontal shaft by means of an elastic coupling or clutch. Thanks to the gear ratio produced by specially-designed gears, the movement is transferred to the vertical shaft. The bowl is assembled on the conical top-end of the vertical shaft. The processing liquid is fed into the centre of the bowl through the stationary feed pipe. Subsequently the inflow is accelerated by means of specially-designed accelerators, forced in the first instance to the perimeter of the bowl, and then through the discs where multi-layer separation takes place. The separated liquid(s) flow to the top of the bowl where they are SECTION OF A BOWL Sludge ports Distributor disc Distributor Feed Outlet light phase Outlet heavy phase discharged by overflow or by centripetal pumps. The solids captured via the described settling process are collected at the perimeter of the bowl, and then discharged intermittently. This discharge is activated by a hydraulic system located underneath Paring disc heavy phase the separation area. In essence, the Paring disc light phase solids are discharged via Disc stack openings at the perimeter of the Sludge space bowl which are opened and closed Ring valve by the down- and upwards movement of either a sliding Operating liquid piston or bowl bottom (see picture). DESIGN FEATURES Construction materials The structural parts of the bowl are made of special stainless steel, the inside parts in contact with the product are made of suitable materials for the processing environment: stainless steel, brass or bronze. The housing of the Vertical Separator is in stainless steel, aluminium, or cast iron. The gear box is made of cast iron or cast iron coated with stainless steel. The gasket material is always selected according to the process. Transmission The movement is always generated by an electric motor and is transmitted by means of: clutch and worm gear, flexible coupling worm gear, set of pulleys and flat belt, rigid coupling and frequency drive. A special transmission version makes use of a high-speed motor coupled directly to the vertical shaft. Feeding and discharge of process liquids The mixture generally is fed in through a stationary feed pipe in the centre of the bowl. The separated liquid may be discharged from the Vertical Separator by an overflow or by a built-in centripetal pump. SPECIAL VERSIONS Sanitary version Specially-designed all-stainless-steel Separators, designed to be used with a CIP cycle for cleaning purposes. This version incorporates a so-called gap-optimised design to allow for easy flushig of all critical sections. ATEX version Specially-designed and certified Vertical Separators, designed to be installed in hazardous areas and for the treatment of potentially inflammable products, i.e. Separators complying with II2G EEx cp IIB TB4. These separators can be purged with nitrogen to minimise the risk of ignition and to fulfil ATEX requirements. Hermetic version Hydro-hermetic device installed inside the bowl, designed to ensure that contact with the surrounding environment is avoided, and to prevent oxidation and gas leaks.

Applications and Technical Features Vertical Disc-Stack Separators are normally designed for one type of separation only, but in some cases, more versatile versions are available that can carry out two different types of separation. Below is a list of the range of disc stacks and bowl designs used for different types of separation. CLARIFICATION PURIFICATION (SEPARATION) CONCENTRATION (SKIMMING) Separation of suspended particles from a liquid (e.g. fruit juices, cell biomass). Separation of a heavy liquid from a main light liquid (e.g. separation of water from lubricating oil). Simultaneous separation of solids is also possible. Concentration of a light liquid dispersed throughout a heavy liquid (e.g. skimming of cream from milk). Simultaneous separation of solids is also possible. PIERALISI Disc-Stack Separators are able to simultaneously process dispersions of two liquids and one solid. The Pieralisi product range offers two main equipment solutions: one with solids retention (requiring manual cleaning) known as the S-Type, and the other with automatic, intermittent solids discharge, known as the FPC-Type. Four different sizes are available for both types of equipment. The tables below show types and sizes, with some general indications of dimensions. Type Bowl Volume [L] Sludge Space Volume [L] Bowl Speed [rpm] max. Hydraulic Capacity [L/h] Dimension L x W x H [m] Mass [kg] SEPARATORS WITH SOLIDS RETAINING BOWL SEPARATORS WITH AUTOMATIC DISCHARGE S200 S250 S300 S400 FPC 6 FPC 12 FPC 18 FPC 24 5 11 25 40 9 14 24 38 2 6 8 12 4 7 12 16 7600 6400 6400 5800 7100 6500 6400 5800 5000 8000 30000 50000 8000 16000 30000 50000 1,0 x 0,7 x 1,2 1,2 x 0,8 x 1,4 1,5 x 0,8 x 1,7 1,7 x 1,0 x 2,0 1,3 x 0,9 x 1,4 1,6 x 1,2 x 1,4 1,7 x 1,3 x 1,7 1,8 x 1,4 x 1,9 300 500 950 1600 1100 1400 2000 2600 AREAS OF APPLICATION FOR PIERALISI SEPARATION SOLUTIONS Environmental Processes treatment and disposal processes of sludge from municipal and industrial waste water drying of animal slurry drying of biomass thermal sludge drying Chemical Processes production processes involving intermediate or end products and integrated recycling and recovery processes processes within HDPE, PVC and PP polymer production production processes for the pharmaceutical and biotech sector minerals and ores production processes production processes for non-fossil fuels, such as biodiesel and ethanol Recycling treatment processes for drilling mud treatment and recovery processes for industrial fluids recycling of polymers and their respective recyclables recycling of service water in industrial processes Oleo-chemistry production processes for oleo-chemistry derivates refining processes for edible vegetable oils, excluding olive oil Mineral- Fuel and Lube Oils Processes purification and conditioning of fuels purification of lube oils treatment and recovery of mineral and fuel oils treatment of slop-oils from refineries and lagoons, of slops from lube oils, of bilge water Animal-Based Products treatment of by-products from the fish-processing and meat-processing industries Food Production processing and recovery of non-liquid food products processing of citrus fruit wine and sugar processing recycling of food-related products Dairy Products and Juices production processes of dairy and cheese products recycling of related waste materials processing of fruit and vegetable juices.

inv inv M70 Separators for Biodiesel - Slop oils - Vegetable oils BIODIESEL HOT SLOP OILS SHELL AND TUBE HEAT EXCHANGER SLOP OIL TO BE TREATED HEAT EXCHANGER PUMPING SKID CLEAN SLOP OIL UNTREATED SLOP OIL OIL TANK M TANK OUTLET POTABLE STEAM GENERATOR DE-EMULSIFIER DOSING UNIT TREATMENT SOLIDS OUTLET SERVICE CRUDE OIL STEAM HOLDING TANK FILTER M M DYN. DYN. MIXER MIXER CONDENSATE GUM CONDITIONING M CONDENSATE STAT. MIXER STEAM BUFFER TANK VEGETABLE OILS: Degumming Neutralization Washing CHILLED W. GUMS GUM SEPARATION WASH- WASHING VACUUM H 3 P O 4 DEGUMMED OIL WASH-W. RECYCLING GUMS 50 % 50 % FLASH DRYING N a O H PROCESS-W. WASTE WASH-W