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CONTUFILT-M TUBULAR - The ZERO HOLDUP CATALYST FILTER

Contufilt –M outside-in filtration for polishing and removing solids, carbon and  catalysts in  hydrogenation slurry filtration. The systems are back washable and easy to use and maintain. The mechanism is either to remove the catalyst from fluid streams or re-slurry and send them back to the reactor.

Features and Benefits

The system consists of a number of equally sized pressure vessels each containing an equal area of Porous metal cartridges  arranged in multi-cylindrical form. The vessel performs the specific functions of filtration, in-situ reverse flow, gas assisted discharge of collected catalyst and when required, an in-situ soak to re-slurry the catalyst if required.

The mechanism of filtration is a direct interception of catalyst particles on the surface of the Porous metal filter. This initial capture starts and enhances the capture of all other particles 2 micrometer and larger. This ongoing formation of a surface cake continues to build- up to a depth of 3 mm or greater depending on the cake resistance and characteristic.

At the end of each filter cycle, solids are backwashed off the inside of the elements and discharged as a concentrated slurry or wet cake. 

The porous metal backwash filter system is used in slurry Hydrogenation chemical reactions  to remove catalyst solids for improved product quality and reduced operating costs.

 

Technical Specifications

The housing is  designed for:

The filter housing is made of SS 316 with  Nozzles for inlet, outlet, drain, backwash fluid, vent, and pressure taps with suitable  connection size and type for proper operation as per the flow parameters specified.

 The initial clean pressure drop across the filter elements and housing is around : 300 mBar

The housing is designed and  fabricated, generally  in accordance with the ASME Boiler Pressure Vessel Code, Section VIII, Division 1.

 

Testing if required: Special requirements for non-destructive testing like radiography, liquid penetrant inspection, magnetic particle inspection, leak testing, etc. should be specified as required, and is charged extra. The entire filter system is hydrostatically tested in accordance with ASME Code, Section VIII, Division 1.

A filter element integrity test should be performed on all filter elements prior to shipment using a nondestructive "Bubble Point Test" that has been correlated to a destructive challenge with test contaminant to certify it meets the rated efficiency.

Applications and Uses