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pierreick sir why is the engineering dpt. actually we are having engineering & projects department for developing engineering related SOP. In our company we are the operating personnel of Purified Water generation & distribution system.

it is our recent SOP prepared for new plant but we provide RO water instead of DM water for Purified water feed purposes.

Pierre sir can i upload our SOP for purified water generation system ?

LittleInch sir Thanks for your information and it is Active Pharmaceutical Ingredient. In future i will use the full form.

pierreick sir the website you have provided is excellent for me. https://pharmadevils.com/urs-for-purified-water-generation-storage-distribution-system/ it is really very informative and exactly i am in the position to do all the qualification like URS, DQ,IQ and OQ.

bimr sir it will help me a lot. thank you.

pierreick sir i didn't know about them. can you please refer me some site to learn the basics Drug master file for your product.

jhnblgr we have to apply for FDA regulatory after commissioning and it is a greenfield project.

This is not a job for a mechanic. i am a project engineer and involving in basic design so i was asked to order the system. share with us the specification. The specification i have is just plant capacity from my stakeholders.

Hi Professionals I need your help in designing purified water generation system to our plant, we are manufacturing API product and we have set 4000 LPH RO system as a feed water for PW generation system but i don't have further how to develop the process and arrange things to initiate...

I have attached the COOLING TOWER PIPING

pierreick thanks for sharing the docuemnts. i am referring them now

GD2 i have shared the data for our pump. it is spx flow make and model NCP-65-40-160-C

Little inch I need basics of pumps and factors influencing pump discharge pressure

Could u please explain me a little bit

4 m down From pump eye. Unfortunately the pump cure is not available but Vendor told me the shut off head is 32 meters

Pump rated flow rate is 45 m3/hr Suction pressure is 0.29 barg Manifold is 4 meter frome the pump eye

Littleinch The inlet pressure is - 0.264 barg The flow is not zero. Pump rpm is 2900 rpm Our gauge is gauge pressure not absolute DIagram is bit tough to time taken

Hi It is room temperature fluid Centrifugal pump Pump head is 25 meter (2.5 bar) Cooling tower pump Header size is 3" Branch size is 1.5" We are getting 3.5 bar pressure at reactor manifold? Is it possible to get 3.5 bar pressure at 2.5 bar head centrifugal pump ? Fluid temp is room...

thanks for correction As 0.4 Nm3/hr is 0.68 ACFM. and as you told 1.5 bar A is 44.2951 inches Hg. V2= (1.92/41.29) * 0.68 = 0.0316 ACFM. 0.0537 Nm3/hr. I think i should have read them again and clear the calculation part.