Dear all
I'm part of a team working to convert a batch process into an online and continuous process. Please could you give me some ideas of instrumentation to measure the weight of the raw materials (Dust or granulates ) to feed in the process?
We are trying to change the way we weigh this raw...
Ok Thank you
I want to clhorinate at 1.2 ppm, 40 cubic meter of water, but i want to add chlorine in the piping after the pump that is going to send the water to the tank instead of install another line of chlorine to the top of the tank and feed in the surface of water.
Regrads
Do you think it could be necessary to use a Venturi tube or feeder, the problem is that i'm going to use a Pump and put the feed after the pump to improve the mixing.
Hi everybody, could you please tell me if is possible to feed sodium hypochlorite on a piping line to chlorinate and mix before send this water to another tank, what tool or technology should i use?
Best regards
Sergio Avila
Hi everybody, could you please tell me if is possible to feed sodium hypochlorite on a piping line to chlorinate and mix before send this water to another tank, what tool or technology should i use?
Best regards
Sergio Avila
Dear All
A cleinte give me a temperature for calaculation of the heating load less than the temperature for the cooling load, what should i do to use the recirculation load or use the cooling load to calculate the flow in the AHU?
Thanks in advance
Sergio Avila
Hi to everybody
It is possible to justify the evaluation of HEPA filter's integrity using a san f the Filter by a particle counter instead of the procedure by ISO 14644-3?
Thanks in advance
Sergio Avila
I have a doubt:
If a have a negative pressure in a room, does it suppose that i have a negative air change?
Because my extraction is bigger than my inyection of air to the room. these is rigth or not?
I have to report my air changes in a pharma instalation and i have that doubt.
Please help...
Hi everibody
I want to know if there is a recommended practice to choose the air filter efficiency for a dust collector in a pharma facility of solids?, It is not a potent active facility, just commun API.
Thanks a lot.
Sergio Avila
Hi Everybody
Could you help me?, i need to know the recommended air eficiency of filters for a dust collection system in a pharmaceutical facility.
Is there a standad or a recommended practice?
Thanks a lot.
Sergio Avila
Is it Correct to calculate six sigma parameters in process that are controled by a PLC.
Example i use an Oven where i steriliza ampoules, i read with dataloggers the temperature inside oven´s chamber.
Must i calculate the Cp, Cpk and others measures of capability process?
We have a VHP Isolator, where we use a HP 31%, but in the market there is no more HP of that concentration, only 35%.
Must we califiate again the process with this new HP concentration?
Must we change the recipe´s parameters?
Thanks in advance.
Sergio Ávila
Hi everybody
Someone know how to use a negative exponential distribution as a function to have control limits?, or know a good article or url about this distribution?
Thanks in advance.
Sergio Ávila
Hi
Is it true that we muss change HEPA filters if there is a change of 10% in the pressure? it means the filters is satured with dust?
Which standar gives that infomation?
Thanks a lot
Sergio Ávila
Is it true we muss change HEPA filter if there is a change in the pressure of the filter of 10%?
Which standar have the information about that?
Thanks a lot?
Sergio
I´m Méxican, but i want to inmigrate to Canada, What pages for a job seeking do you recommend to me.
I´n Pharmaceutical Engenier and have 5 years of experience in contamination control and critical systems.
Thanks
I read all the messages and i think the same it is a big challenge that you face, but i think the next page can help you a lot: http://www.picscheme.org/, and http://www.ivthome.com/
just keep it easy
I hope you may do it all right.
Fenixseravgon
