Hello,
I'm working on a project where a Plate Steam Condensor is used to heat district water for urban houses.
In short, I have:
- superheated steam of 42 bar(g) @ 430 C and condensate of approximately 7 bar(g).
- The supply must be 1 MWth to 50 MWth
- District water pressure is at minimum...
We at work have a discussion about the gas buffering in a pipeline.
The case:
We have a 100 km pipeline 30" with no output @ 25 bar(g). What will happen with the pressure at the end of the pipeline if we assume an output of 10 m/s @ 25 bar(g) (=x kg/hour) by opening a valve and an input of x...
Hi All,
I have a relative small question, but I can't find the answer!
We are going to install a compressor (No vendor selected yet) which will have a various demand and will go off line every night.
In the contract we have is a statement that we must meet a technical availability of 99% for...
Hi All,
This question is a bit frustrating since I am thinking about it all day!
The problem: I have a pipeline of 5000 meter, on one side I have a compressor and on the other side I have a consumer. In one scenario I have an equilibrium and for instance the pressure at the consumer is 4,7...
Hi all,
I have a question, does anyone know if the following components can be filtered with an active coal filter?
NOx
Ethylene
Methane
If not, is there a way to filter these components? (Catalytic Oxidation for instance?)
Thanks in advance.
Regards,
Eltjo
Hi all,
In order to check a compressor offer I want to calculate the kW needed to raise the pressure.
In short, I do not trust the stated 480 kW of Horsepower.
The compressor needs to compress 10.000 kg/hour CO2 @ 55 C saturated with water (about 670 kg/hour of water --> Total flow is 10.680...
