Hi guys,
I really need help here as I need to find a vendor or technology that offers a process heater equipment that runs on crude oil as the fuel (and in my case its heavy oil with API density of around 13 to 16 deg. API).
I have tried searching it in the internet but perhaps it must be my...
Hi guys,
I need some kind assistance here regarding any literature or website that contains information regarding petroleum product blending process scheme which produces black product and white product, i.e fuel oil from black product and MOGAS RON 92, RON 97 from white product. Or if you guys...
Hi guys,
I need some kind assistance here regarding any literature or website that contains information regarding petroleum product blending process scheme which produces black product and white product, i.e fuel oil from black product and MOGAS RON 92, RON 97 from white product. Or if you guys...
Hi TD2K,
Thanks for your input. We design the vessel (fuel gas scrubber) with a liquid trap/auto drainer on the liquid line instead of putting LCV with on/off operation based on the liquid level inside the vessel. This is because the liquid drop off from the gas stream is fairly small in the...
If i have liquid trap installed on the liquid outlet line (i.e. fuel gas scrubber liquid outlet), do i need LSLL for the vessel for tripping of the unit due to low low liquid level inside the vessel?
Thanks jsummerfield!!
But for the records here (i already mentioned it in petroleum production engineering forum), we do not have any petroleum engineer or that related to it that can answer my curiosity. All my leads and seniors answered me well but as far as i know their explanation still on...
Hi guys,
Thanks for the infos.
Leonardt,
Actually we are an offshore topsides engineering design company. Most of our design scope is just the facilities of the topsides, i.e. processing facilities like wellhead control panel with the wellhead control philosophy, the production manifolds, and...
Hi guys.
Thanks again Antman25 and dadfap. Since you guys are petroleum background (and i am not..), do you guys know any internet website that offers information on well killing operations. I have tried so many times (using google) but there is no websites that offer much information on this...
Thanks dadfap,
Is this well killing performed during the abandonment of the wells sort of like we seal the wells?
I am sorry for asking more because I am a young design engineer and this terms and its concerns is my very first time encounter. We don't have drilling engineer or petroleum...
Hullo guys,
I have been asking around this question in this forum but seems nobody knows about it. The platform that I am involve in designing it has five slots of wellheasd for well fluids and one wellhead for well kill operations.
What is well kill operations and how it works? I even went to...
Hi MortenA,
Thanks for the info. Actually I am not working on the platform. We are engaged in a platform design project at this moment of time. So this is my very first time to encounter such term.
TQ.
Hi guys,
The platform that we are currently working on has 6 slots of wellhead. 5 for the well fluids and the remaining one is for the well kill operations.
What is it (well kill operations)? and how does it works?
Resizal
Hi guys,
Currently I am involve in designing a drilling/riser platform. In our platform we have 6 slots for wellhead. 5 will be used for well fluids and the remaining one is for well kill operations.
Can anyone tell me what is well kill operations and how it is works? Please I need guidance...
Hi guys,
Recently i have discussion with my collegues about control valve. As far as I am concerns, in API RP 14E the most suitable control valve is globe type. But according to my colleagues, sometimes we use ball too as control valve whenever we have shearing effect in the flow.
My question...
Hi guys..
Thanks guys. Smckennz, thanks for the info. But there is still one issue need to be addressed, shearing effect? What is it actually? What it has to do with ball valve selection as a control valve?
I need help guys, please.
Reiszal
Hi guys,
As far as I am concerns, from API RP 14E, the most suitable valve type for control valve is Globe type. But after awhile I have come to know that sometimes we do use ball valve as control valve. But it is not very often. One of my colleagues told me that we use control valve of ball...
Hi Senno,
Thanks for the info. Actualy I do have that Gas Properties v1.5.1 registered in our HYSYS software. And yes you are very right, that extension can give us both info, the water dewpoint and the HC dew point. The reason why I wanna use other alternatives of determining water dew point is...
Hullo guys,
I am checking the efficiency of the TEG dehydration module that has been designed by previous consultant. One of the way is to check the water dew point of the export gas / condensate from our Central Processing Platform to the onshore terminal.
Can anyone in here advice me or share...
Hi ixchawla!
This subject really interests me. In fact I am doing a process simulation for one of our new gas platform design job at this very moment of time. I just wanna share the idea and knowledge that I had gathered. Feel free for you guys to criticise and comment.
Yes, HYSYS so far so...
