Specification for ED Plant
- Feed
to ED Plant ------20000 lph,
- Feed
concentration of whey 17-18%, & 7.2 % ash /TS.
- De-mineralization
of whey after NF ---- 35%.
- De-mineralization
of whey after ED ---- 90%.
- Possibility
to allow C.I.P for all the product inlet and outlet pipes threw ED from
external source.
- Whey
inlet should have the safety filters (duplex) with auto change over
arrangement, with feed back of pressure difference.
- All
the valves and fittings should be of sanitary design and of reputed make.
- All
the circulation & pressure pumps should be of reputed make &
sanitary design.
- Control
system should be Control room based, preferable PLC (S-7-400) with SCADA,
Siemens, two number of PC for operation.
- All the instruments should be of E& H
or equivalent make.
- All the frequency converter should be –
Allen-Bradley, Dan Foss,
- Guarantee of consistency for the out put
mineral profile, based on the mineral profile given for feed to ED.
- Guarantee for the concentration
De-mineralization of whey.
- Offer
should include the separate offer for supply of RO for the treatments of
ED brine.
- Operating
cost per day should be attached with the offer. ED and RO separately.
Operating cost must include the replacement cost of Membrane, maintenance,
cleaning chemical cost per day. Power consumed and installed.
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