HCBBS Forum (English)
Submit Chemical Projects / Find Solutions
Amplify Your Requirements on a Broader Chemical Platform *Engineering · Technology · Equipment · Solutions*
Submit Request

Is the temperature superheated after depressurization of saturated steam?

2018-07-23View Original

Thread Content

Dear experts, could you please help calculate how much the temperature will be superheated after depressurization, assuming an isenthalpic process? The saturated steam pressure is 25 barg before depressurization, with a flow rate of 1200 kg/h; after depressurization, the pressure drops to 12 barg Please help calculate it ;
Reply #22018-07-23
Two methods are determined. The first is software simulation, and the second is querying using software for steam properties
Reply #32018-07-23
Two methods are determined. The first is software simulation, and the second is querying using software for steam properties
Reply #42018-07-23
Does anyone have the Aspen software to help with the simulation? Thanks
Reply #52018-08-06
The depressurization of steam simply means that the pressure decreases while the temperature remains unchanged. However, compared to the vapor pressure at that pressure level, the temperature is too high; that’s why it’s called superheated steam... For example, the saturation temperature of steam at 41K is 253°C. When the pressure is reduced to 30K (the normal saturation temperature being 234°C), the actual temperature still remains at 253°C... This is 253–234 = 19 degrees higher than the theoretical value, meaning the steam is superheated by 19 degrees...
Reply #62018-08-12
There is a Morrell curve that can be used for comparison
Reply #72018-08-13
I have steam calculation software; feel free to message me if you need it
Reply #82018-09-18
When steam is depressurized, the pressure drops, but the temperature remains unchanged, right?... Why do some people still claim that the temperature also decreases? A utility plant produces steam at high pressure and high temperature, while you use steam at relatively lower pressure. Isn’t it necessary to install a pressure control valve and a desuperheater? Is it required to add water to lower the temperature? Then why lower the temperature? It’s because after depressurization, the temperature becomes superheated. Do you understand? What happens when there is superheating? Your pipelines and equipment surely have specified design temperatures, right? I have no objection to criticizing others... but please make sure you understand things first, okay?
Reply #92018-09-20
It’s overheating; it’s a cooling process after passing through the pressure relief valve

Submit a Project

**Looking for Chemical Technology, Equipment & Solutions?** No Registration Required Broader Platform Exposure | Global Chemical Service Provider Connections

Submit Request — Free Consultation

Disclaimer

This is an automated machine translation of the original thread. Some technical terms may have inaccuracies; the original text shall prevail. Click "View Original" at the top right to access the source page, which supports IP-based automatic real-time language translation. Please watch out for contact details and sales inducements to prevent fraud. All content and translations are for reference only, representing solely the poster's personal views. For enquiries, email service@hcbbs.com.