1.
We have a plate heat exchanger as a reactor feed/effluent heat ...
We have a plate heat exchanger as a reactor feed/effluent heat exchanger in DHT ... shape) is installed upstream the exchanger on the reactor effluent line. ...
2.
Neutralizing amines are used in PH control in crude distillation ...
At crude distillation overhead systems neutralizing amines are commonly injected together with oil-soluble filming amines to give a good corrosion ...
3.
Applying relief load calculation methods
Case study compares dynamic simulation vs conventional unbalanced heat method for relief load calculations in a naphtha hydrotreater, focusing on the ...
4.
Applying relief load calculation methods
Case study compares dynamic simulation vs conventional unbalanced heat method for relief load calculations in a naphtha hydrotreater, focusing on the ...
5.
This question is related with capacity estimation for safety ...
This question is related with capacity estimation for safety relief valve for external fire case for heavy oil services. Typical VDU bottoms stream which is ...
6.
What are the most important automation and control components ...
What are the most important automation and control components being incorporated into new projects to help operating companies increase capacity and meet ...
7.
Evidence of MDEA degradation in tail gas treating plants.
To download the full version of this article please subscribe to ePTQ. Go Back. James E Critchfield and James L Jenkins, Huntsman Corporation ...
8.
A coalescer is required to be installed in straight run kero line ...
The friction caused by passage of kerosene through the run down filter and coalescer media may build up an electrostatic charge which in the right ...
9.
Catalyst vendors differ in their philosophies for catalyst ...
Multiple catalyst-layered systems can provide an advantage. However, these loadings can easily become overly complex and create opportunities for improper ...
10.
In a particular complex onshore gas plant, flare network purge is ...
<br/>I would like to know what would be the risk of stopping all N2 purge gas and starting fuel gas purge. This would lead to the flare network being purged ...
