Dear All,
I would like to discuss regarding some Incident happened in my work area.
A worker was about to purge a line section upstream Booster Compressor using nitrogen gas from our Nitrogen Generation System Unit.
He attached the inlet of 3/4" hose to the outlet of Nitrogen Generation...
Hi @pierreick, thank you for your suggestion. I will try to contact the closetest fire brigade near the shore.
@shvet my goodness, I didnt realize until you replied. I did post in the wrong forum.
@littleInch yes, I am aware that with "normal" pipe, 863 m3/h will need 12-14" pipe size. But I...
Hi all,
Anyone familiar with Fire Fighting Boat services?
We have demand of Firewater for a shore facility 836 m3/h. We have 1x100% firewater tank but our facility is foreseen not enough to fulfill the tank in less than 8 hours as per NFPA codes requirement. Alternatively, we are proposing to...
Hi everyone,
I am currently doing modelling of a firewater system at LNG Terminal & Regas Facility using PIPENET both Spray/Sprinkler module (steady state) and Transient module (dynamic) for surge analysis. This is my first time conducting surge analysis using transient module.
In the...
Hi everyone,
I am currently sizing a vent nozzle of an atmospheric tank contains produced water.
I have followed the API 2000 and already got my vent requirement is 992 Am3/hr of air.
but, I am stuck in the nozzle velocity criteria to determine the size of the nozzle.
does anyone have any...
Dear LittleInch,
yes it said so, but it's supposed to be more than the current gas flow. as the current gas flow is 59.88 MMscfd.
anyway thanks for the hint!
I have resolved it.
you were right, one of the problems here is incorrect density data.
the fluid properties I input, including mass...
Dear LittleInch,
That's the kind of you. Really appreaciate that.
The input are the ones with blue font colour.
When I put 59.88 MMscfd (as it is the initial input) in the yellow coloured column as captured below, the 'Horizontal Gas Velocity - calculated and Conds. in Gas Droplet Fall Times...
Dear LittleInch,
Thank you for your correction. I have typed them wrong in this forum. But I can assure the mass flow input data on the spreadsheet are correct.
The operating pressure is 492 psig; T = 120 F which has been considered in the process simulation prior to obtaining the fluid mass...
Dear members,
Greetings
I am a junior engineer, doing a separator sizing check for the separators that our Client has. I need to determine the maximum capacity of the separator can accomodate in case our Client want to maximize their production in the future.
I am still new to this separator...
