Friday, November 26, 2010

Heat Exchanger Fabricator Has Flow Arrangement Options

We have been posting some “behind-the-scenes” and educational information about Heat Exchangers, how they work, what is the science behind them, etc.  And now we want to take a look at “flow arrangement” and how we classify flow arrangement when fabricating our Heat Exchangers.

Parallel flow shell & tube heat exchanger fabrication from Bendel Tank & Heat Exchanger in Charlotte, NC.Basically, there are two primary classifications of heat exchangers according to their flow arrangement. In parallel-flow heat exchangers (at left), the two fluids enter the exchanger at the same end, and travel in parallel to one another to the other side.

In counter-flow heat exchangers (at right) the fluids enter the exchanger from opposite endsCounter current shell & tube heat exchanger fabrication from Bendel Tank & Heat Exchanger in Charlotte, NC.. The counter current design is most efficient, in that it can transfer the most heat from the heat (transfer) medium.

For efficiency, heat exchangers are designed to maximize the surface area of the wall between the two fluids, while minimizing resistance to fluid flow through the exchanger. The exchanger’s performance can also be affected by the addition of fins or corrugations in one or both directions, which increase surface area and may channel fluid flow or induce turbulence.

Cross flow shell & tube heat exchanger fabrication at Bendel Tank & Heat Exchanger in Charlotte, NC.In a cross-flow heat exchanger (at left), the fluids travel roughly perpendicular to one another through the exchanger.

The driving temperature across the heat transfer surface varies with position, but an appropriate mean temperature can be defined. In most simple systems this is the “log mean temperature difference” (LMTD). Sometimes direct knowledge of the LMTD is not available and the NTU (Number of Transfer Units) method is used.

If you would like more information about our Bendel heat exchanger design and fabricating program, please call us at 866-596-5112 or contact  Vince Petrucci or Vivek Patel at Bendel.

 

Wednesday, November 10, 2010

Heat Exchanger Fouling Can be a Nightmare Maintenance Issue with Shell & Tube Heat Exchangers!

Fouling occurs when a fluid goes through the heat exchanger, and the impurities in the fluid precipitate onto the surface of the tubes. Precipitation of these impurities can be caused by:

Heat Exchanger fabrication and manufacturing company Bendel Tank & Heat Exchanger in Charlotte, NC.Effects of fouling are more abundant in the cold tubes of the heat exchanger than in the hot tubes. This is because impurities are less likely to be dissolved in a cold fluid, because for most substances, solubility increases as temperature increases. A notable exception is hard water where the opposite is true.

Fouling reduces the cross sectional area for heat to be transferred and causes an increase in the resistance to heat transfer across the heat exchanger. This is because the thermal conductivity of the fouling layer is low. This reduces the overall heat transfer coefficient and efficiency of the heat exchanger. This in turn, can lead to an increase in pumping and maintenance costs.

The conventional approach to fouling control combines the “blind” application of biocides and anti-scale chemicals with periodic lab testing. This often results in the excessive use of chemicals with the inherent side effects of accelerating system corrosion and increasing toxic waste – not to mention the cost of unnecessary treatments. There are however solutions for continuous fouling monitoring in liquid environments with sensors measuring both fouling thickness and temperature, allowing cleaning effectiveness to be monitored and chemical usage to be minimized.

If you would like more information about our Bendel heat exchanger design and fabricating program, please call us at 866-596-5112 or contact  Vince Petrucci or Vivek Patel at Bendel.  www.bendelcorp.com