Can Reheating Steam Locally Improve Air Outlet Temperature in Heat Exchangers?

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Discussion Overview

The discussion revolves around the challenges of improving air outlet temperature in heat exchangers used in a tin plating line, particularly in the context of reduced steam pressure and temperature. Participants explore various methods to locally reheat steam or enhance heat exchanger efficiency to achieve desired air temperatures for drying processes.

Discussion Character

  • Technical explanation
  • Debate/contested
  • Experimental/applied

Main Points Raised

  • Rob describes the current situation with reduced steam pressure leading to lower steam inlet temperatures and seeks advice on locally reheating steam to improve air outlet temperatures.
  • Russ questions the relationship between steam pressure and superheat, suggesting that reducing pressure may lead to a loss of flow rate, which reheating may not resolve.
  • Rob clarifies that the steam is saturated and acknowledges the impact of pressure on temperature, noting the original specifications for the heat exchanger and current performance metrics.
  • Another participant suggests that reducing air flow could increase air temperature but would decrease the total heating value due to less air being heated.
  • There is a mention of ensuring no air is trapped in the heat exchanger to maintain efficiency.
  • Participants propose various solutions, including larger heat exchangers, higher pressure boilers, or alternative heating methods such as electric elements.
  • One participant raises the idea of using exhaust air to preheat incoming air through an air-to-air heat exchanger as a potential energy-saving measure.

Areas of Agreement / Disagreement

Participants express differing views on the best approach to improve air outlet temperatures, with no consensus on a single solution. Various methods are proposed, but the effectiveness and feasibility of these methods remain contested.

Contextual Notes

Participants acknowledge limitations related to steam pressure, heat exchanger efficiency, and the potential need for additional equipment or modifications. There are unresolved technical details regarding the implementation of proposed solutions.

rnmconnor
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Our tin plating line has several of these. Original design was superheated steam to 300 degrees celsius, but the plant reduced steam pressure and now our steam inlet temperature is much lower (less than 150 degrees celsius). Inlet air is what we want to heat up for the drying. It comes in between 15 degrees celsius in winter to up to 40 degrees celsius in the summer.

Since I am limited to steam inlet temperature being lower, is there a simple way to locally heat the steam again to make my outlet air temperature higher? Would an tankless boiler be effective? I have a tank of condensate at about 100 degrees celsius in the basement below the line, but I am no better off unless I can heat this up to superheated steam again, but at least I have a source to start from. Any feedback would be great!

Thanks;
Rob
 
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Why would reducing the pressure reduce the superheat? Or do you really mean saturated steam? The main problem with reducing pressure is generally a loss of flow rate and adding superheat won't fix that. Can you increase the pipe size?
 
Hi Russ;

Thanks for your response.

I guess my numbers are off. I am new to the area and still coming up to speed with the equipment.

You are right, it is saturated steam, and the temperature follows the steam table. Reduce the pressure and temperature goes as well. From what I am told, looking at the drawings as well, the original spec on the steam to air heat exchanger was 150 psi for steam at 366 deg. F. But they applied 250 psi saturated steam into the system, which was over 400 deg. F, my guess is with a high temperature like that, it doesn't matter so much efficiency wise for the heat exchanger, you could get outlet air temperature at 250 to 300 F no problem. But now with saturated steam pressure at 100 PSI we are seeing steam inlet temperature of 300 deg F in and outlet temp of 295 F on the piping. Our air outlet temp is only 146 deg. F

The heat exchanger has been rebuilt once. We were thinking of adding a tankless boiler locally since there is no plant plantwise to increase steam pressure. Somehow we have to boost either steam inlet temperature or heat exchanger efficiency to get the maximum out of air outlet temperature. If we need to go back to the drawing board to increase the heat exchanger iefficiency, then that may be our best cost effective option.

Regards;
Rob
 
Reducing the Air flow will increase the Air temp but the heat output of the heat exchanger will drop badly.Ie must less air coming off at a higher temp. less total heating value of said air as there is less of it. Make sure there is no air trapped in the heat exchanger (steam side) Don't burn yourself I know nothing about how to do that.
 
I guess if the end bends pipe temp. matches the saturation temp. for the pressure of the steam there will be no air trapped.
 
otherwise some one is going to have to spend some money bigger heat exchangers or another one in series in the air flow, a higher pressure boiler or perhaps one could add electric elements or heat some other way.
 
Can exhaust air from the system be used to preheat the incoming air in a air to air heat exchanger to save heaps of energy?
 

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