Golgappa.net | Golgappa.org | BagIndia.net | BodyIndia.Com | CabIndia.net | CarsBikes.net | CarsBikes.org | CashIndia.net | ConsumerIndia.net | CookingIndia.net | DataIndia.net | DealIndia.net | EmailIndia.net | FirstTablet.com | FirstTourist.com | ForsaleIndia.net | IndiaBody.Com | IndiaCab.net | IndiaCash.net | IndiaModel.net | KidForum.net | OfficeIndia.net | PaysIndia.com | RestaurantIndia.net | RestaurantsIndia.net | SaleForum.net | SellForum.net | SoldIndia.com | StarIndia.net | TomatoCab.com | TomatoCabs.com | TownIndia.com
Interested to Buy Any Domain ? << Click Here >> for more details...

Difine flashing , Cavitaion & Noise?
how to minimize these effects

Answer Posted / www.islamqa.com

# Flashing: it's formation of vapour bubbles in liquid
stream as valve cause pressure drop to the liquid below its
vaporization pressure.

# Cavitation: it's formation and collapse of vapor bubbles,
collapse occures due to pressure recovery at valve
downstream which cause bubbles to implode, giving microjets
and very high pressure waves (in range 100000 psi).

# Noise: is a result of turbulent fields generated through
the flow stream caused by many parameters:

- pipeline restrictions (orifice, valves, ..)
- pressure fluctuation
- unstable flow and very high flow velocity

and the noise radiation depends on pipeline material and
diameter and thickness.



# Here is the main guidelines to avoid flashing and
cavitation:

# To avoid flashing:
====================

1 - valve selection with high Fl.
Fl:valve pressure recovery coefficient, and this introduced
by MASONILIAN as: Fl=(P1-P2/P1-Pvc)^.5 - and Fl max is 1.

where FISHER introduced Km =(P1-P2/P1-Pv) - and this is a
valve parameter presented by vendor and it's calculated by
lab tests, and usin Km we can get allowable(P1-P2) which
will not cause flashing.

2 - using anti cavitation trim, which generate multi vena
contracta points in the presuure profile, and this prevent
pressure drop below Pv.

3 - To cool down the process material to make Pv very low.

4 - To change the valve position to another place with high
pressure, to make pressure drop through the valve away from
PV.


And anyway if there is no escape from flashing, it's better
to sustain flashing within the valve to assure that we will
not have a cavitation when pressure recover, and liquid can
be recovered and bubbles can implode any other place away
from the valve.

and this can be achieved by heating up the process liquid
so we raise Pv, and a good indication for us to be sure
that flash will be sustained is p2, as we can know P2 at
downstream pipeline and make sure that it's below Pvc of
the process liquid.

Regards,

Ahmed Sabry
Control and Instrumentation Engineer
GPC - General Petroleum Company
ahmedsabry.online@gmail.com
CELL.: 00 2 0121367310

Is This Answer Correct ?    6 Yes 0 No



Post New Answer       View All Answers


Please Help Members By Posting Answers For Below Questions

Working principle of magnetic flow meter ......and calibration procedure of e+h magnetic flowmeter...

2350


Why not come out analog output in ABB EL3020 when display show correct value

1890


How many interlocks at turbine side?

1935


why we us isolation barrier in hazardous area how it works to protect the area and please clarify its current flow.

1957


DEAR SIR/MADAM MY NAME IS ARKAPROVA BHATTACHARYYA.I AM A FRESHER INSTRUMENTATION ENGINEER.CAN YOU PLEASE SEND SOME QUESTION PAPERS OF GRADUATE ENGINEER TRAINEE EXAM OF DVC(DAMODAR VALLY CORPORATION).MY EMAIL IDs ARE arka_aec@rediffmail.com.

1904


How do you identify an orifice in the pipeline?

1258


What is the use of single seated valve?

1077


anybody having Qatar Petroleum questions for instrument Technician offshore ....please send me

6035


How to find out the current of two motors having same power consumption but different RPM?

2019


What are the key features of a Distributed Control System? describing the various layers (sensor through to business system interfaces) as well as the hardware, software and security aspects of the DCS.

2226


In turbine what does term CDP, NI, NH, HSSOC means.

2596


i have been asked by QAFCO to appear for interview for thy post of Instrument Designer(INTOOLS)..i m engineering graduate with 5 years exp. in design engineering.Will this job profile suit me??i need all ur help n suggestions for thy same?

2231


how do calibrate the valves.. with clear manual

2089


kindly sent some demo question and answer

2071


How works weighfeeders in cement industry? what is the working principle?

2043