Need help to find a steam compressor

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Discussion Overview

The discussion revolves around the search for a steam compressor or system capable of compressing very low pressure steam (2.56 kPa) to 1 bar and above. Participants explore various options, manufacturers, and technical considerations related to steam compression, particularly in the context of open cycle and hybrid OTEC (Ocean Thermal Energy Conversion) plants.

Discussion Character

  • Exploratory
  • Technical explanation
  • Debate/contested

Main Points Raised

  • The original poster (OP) seeks a steam compressor system that can handle low pressure steam, acknowledging that achieving a high compression ratio may require multiple sets in series.
  • Some participants suggest looking at various manufacturers and products, including Penberthy eductors and Nash liquid ring pumps, but express concerns about their applicability to low pressure steam.
  • One participant mentions that many manufacturers focus on higher pressure steam and may not cater to the OP's specific needs.
  • There is a discussion about the mechanical work required to compress gases and the potential inefficiencies of certain systems, such as ejectors or eductors, which may use more steam than they produce.
  • Participants reference specific OTEC experiments and systems, discussing the configuration and stages of compressors used in those contexts.
  • Some participants express frustration with manufacturers who do not provide suitable options or adequate customer support for low pressure applications.
  • There is a mention of alternative methods like Mechanical Vapour Compression (MVC) or Mechanical Vapour Recompression (MVR) as preferred options over ejectors.

Areas of Agreement / Disagreement

Participants do not reach a consensus on the best approach or available solutions for the OP's requirements. Multiple competing views exist regarding the suitability of different compressor types and manufacturers, and the discussion remains unresolved.

Contextual Notes

Participants highlight limitations in available products for low pressure steam compression and the challenges in finding manufacturers willing to accommodate such specifications. There are also unresolved questions about the efficiency and practicality of different compression methods.

Who May Find This Useful

This discussion may be of interest to engineers, researchers, and practitioners involved in thermal energy systems, particularly those focused on low pressure steam applications and OTEC technologies.

pranj5
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At present, I am looking for a steam compressor or steam compressor system that can compress very low pressure steam (2.56 kPa) to 1 bar and above. I know well that such high compression ratio will be impossible for a single set to achieve, therefore it more than one sets have to set in series that's welcome too.
To be precise, I am looking for steam compressor system(s) that can compress steam as said above. Such sets were and still are used in open cycle and/or hybrid OTEC plants.
If anybody can refer a company that can manufacture such sets, I will be grateful to him/her.
 
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I am not sure, but you might try Alibaba.com/showroom/steam-compressor.html
 
Thanks! I have tried them but they aren't worth the effort. Most of them are in the field of higher pressure steam compression i.e. moe than one bar is the starting pressure.
 
Both TLV and Spilling deal with higher pressure steam. They don't deal with such low pressure steam.
 
Are you removing air from a condenser ?
It takes a lot of mechanical work to compress a gas. That's why we condense the steam before pumping it back up to boiler pressure.
Probably you know better than to contemplate an over unity steam system.

The links i gave you came from searches on "condenser air ejector" and "eductor"
which turn up plenty of other manufacturers.
 
I want something similar to used in open cycle OTEC experiments like http://www.otecnews.org/articles/vega/07_landbased_OTEC.html . Kindly look at the compressor system fitted to the Condenser of this experiment.
 
Last edited by a moderator:
pranj5 said:
http://www.otecnews.org/articles/vega/07_landbased_OTEC.html . Kindly look at the compressor system fitted to the Condenser of this experiment.

http://www.otecnews.org/articles/vega/07_landbased_OTEC.html
returns
upload_2016-5-17_19-56-22.png
 
Last edited by a moderator:
  • #11
Hmm not a lot to go on there
The basic compressor system has four stages with direct contact coolers in-between. The fourth stage compressor takes the non-condensables from the third stage. The discharge from the fourth stage is re-injected at 30 kPa into the warm water effluent returning from the second stage evaporator. A fifth stage compressor is also provided to alternately bypass the re-injection scheme and discharge into the atmosphere. The first four stages are centrifugal, whereas the fifth stage is a positive displacement type.
and that's all they tell us about it ?
Clearly it's rotating machinery
and it's for venting noncondensibles.
in my plant we used a three stage steam eductor
but we never had 4°C seawater, maybe 15°C for a day in a severe winter . So we had higher absolute pressure.

I would call a sales rep for such machinery , ask him for a brochure on what he sells ,
Tell him you're looking for a ~100hp condenser air ejector that'll pump from saturation at 4°C to atmosphere.
I didn't see a mass flow rate for anything but cooling water to the intercooler and that'll probably be his first question.

In my plant we had a visit from a Nash salesman pushing water ring compressors for air ejector duty.
But why would we trade a simple steam jet eductor with no moving parts for a complex rotating machine that has bearings, seals, motors and electrical controls to maintain ?

Sorry i can't help more.
I've heard of other plants that use Nash water ring compressors for that application . Any manufacturer's sales rep should be more than happy to help you spec a suitable machine.

old jim
 
  • #12
Not only non-condensables, but also the non-condensed steam too that is 5% of the steam produced at the Evaporator. I don't want something that can compress steam from 5C level, 20C level will be enough for me. I have contacted a few manufacturers but all said that the pressure level (20C saturation pressure level) is too low for them to manufacture anything even if that means putting more than one machine in series.
 
  • #13
pranj5 said:
Not only non-condensables, but also the non-condensed steam too that is 5% of the steam produced at the Evaporator.
Well sure, that's why there are intercoolers and vent condensers to recover that heat of vaporization.

pranj5 said:
I have contacted a few manufacturers but all said that the pressure level (20C saturation pressure level) is too low for them to manufacture anything even if that means putting more than one machine in series

Chalk them of your list. Either they don't have what you need or the sales reps aren't helpful enough. Part of that job is educating customers.
Search on keywords from links like these to teach your search engine where are the right social circles.

http://www.graham-mfg.com/usr/pdf/TechLibVacuum/218.PDF

http://www.fluid-technology.com/product/ejectors-and-condensers/

http://spxheattransfer.com/products/detail/steam-jet-air-ejectors
 
  • #14
Ejectors or eductors aren't my preference. They use more steam than they produce. I prefer mechanical means like MVC (Mechanical Vapour Compression) or MVR (Mechanical Vapour Recompression).
 
  • #15
pranj5 said:
Ejectors or eductors aren't my preference. They use more steam than they produce.
They don't produce any .
I prefer mechanical means like MVC (Mechanical Vapour Compression) or MVR (Mechanical Vapour Recompression).

call Nash.
 
  • #16
I want to mean the steam they produce by evaporating in vacuum. And, by the way, who is Nash?
 
  • #18
Thanks! I have contacted them and hope to get some reply. In the meantime, if you know some other sources, kindly send that to me.
 
  • #19
I have contacted them but don't get any reply so far.
 
  • #20
This thread is dead, the last post was more than a year ago and it looks to me like the OP has been banned.
 
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