Klaren International develops self-cleaning heat exchangers for zero-fouling operation. In the self-cleaning heat exchangers a fluidized bed of solid particles is used at the tube side where the fouling liquid flows through. The solid particles create a scouring effect on the tube wall surface which removes the developing fouling layer. In this way severe fouling of shell and tube heat exchangers is prevented. Either new or revamped heat exchanger solutions with a zero-fouling configuration can be realized in all types of industries.
Why self-cleaning heat exchangers?
Enhanced productivity
Sustainable
Better energy performance
In a self-cleaning heat exchanger the tubes remain clean and therefore the heat transfer can kept constant which improves the energy performance:
- A shell and tube heat exchanger to cool quench water had a decrease in heat transfer coefficient of 50% within 20 days of operation. With a self-cleaning heat exchanger, the heat transfer coefficient remained constant.
- Because of the lower fluid velocities and shorter tube length in most applications the pumping power required is reduced. In the apllication mentioned above the reduction was more than 50%.
- Applying the self-cleaning fluidized bed technology for an evaporator that concentrates waste water allows to reach higher solid concentrations in the recirculation flow without incurring in fouling problems as compared to falling film evaporators. This results in a higher water recovery and a drastic reduction of the blow down. When adding a spray dryer to come to Zero Liquid Discharge the overall energy consumption of the self-cleaning unit combined with the spray dryer is only 60% of the energy consumption of the falling film unit combined with the spray dryer. Main reason for this is that with the technology of Klaren International the waste water can be further concentrated meaning a smaller volume flow as blow down requiring less energy for spray drying.
- A shell and tube heat exchanger uses water to recover heat from an exothermic reaction. The heat is used elsewhere in the process. Fouling on the chemical component side of the heat exchanger causes a decrease on heat transfer coefficient which results in a decreasing heat recovery capacity. As the fouling layer develops an increasing amount of make-up steam has to be used to further heat the process elsewhere. With a self-cleaning heat exchanger the heat recovery form the exothermic reaction remains constant and no steam has to be used.
Enhanced productivity
A self-cleaning heat exchanger needs not to be taken out of production for cleaning, therefore the capacity remains constant and in some cases the production yield can be increased, which enhances the productivity:
- With fouling of heat exchangers the period between two cleanings can range from a year to 4 hours. In most cases cleaning means a stop in operation with as a consequence a loss of production. If a stop in operation is not allowed, it is usually decided to install redundant equipment. Choosing for redundancy means an additional investment.
- It is known that in case of fouling in crude oil pre-heaters, installed upstream the refinery furnace, the required inlet temperature of the distillation column cannot be met and thus the throughput needs to be reduced to meet the required inlet temperatures. Obviously, reducing the throughput directly affects the production output and the revenues of the refinery. With a self-cleaning heat exchanger there is no downtime for cleaning nor is it required to install redundant equipment and throughput can remain constant.
Sustainable
When using the self-cleaning heat exchanger technology chemicals are not required as online additives or needed for cleaning purposes. Therefore, there are no hazardous waste streams from cleaning which makes the heat exchanger more sustainable:
- All MSF plants for sea water desalination use a chemical additive to suppress fouling or scaling of sea water in the condenser section or the top brine heater. Already in the late 1970’s at the Island of Texel a MSF plant with a vertical orientation has been built and operated that applied a fluidized bed in the tubes of the condenser and final heater and could run without the need of chemicals to prevent scaling.
- PTA coolers face a major issue of fouling. A major PTA producer has to clean the PTA coolers every 6 hours. Cleaning of these PTA coolers is done using chemical solutions i.e. caustic solution (5% w/w caustic @ 80 deg C). After cleaning they have to dispose the caustic solution which contains valuable terephthalic acid crystals. Replacing the existing PTA coolers with the self- cleaning coolers will enable the PTA producer to skip the caustic cleaning of the heat exchanger and thus there will be no disposal of the cleaning solution.
Compact design
Because of a constant heat transfer in the self-cleaning heat exchanger, over dimensioning of the heat transfer surface is not required which results in a more compact design of the heat exchanger:
- With a heat exchanger application known to foul, the required surface of the heat exchanger is normally calculated by adding a fouling factor to the heat transfer coefficient. Fouling factors can easily be 2 to 5 *10-4 m2K/W. Starting with an overall heat transfer coefficient of 2000 W/m2K, the heat transfer over time will drop to 1500 W/m2K or in the worst case to only 1000 W/m2K. So, for the same heat capacity, the heat exchanger needs an overdesign of 30 to 100% to meet the required capacity over time. With the self-cleaning heat exchanger overdesign is not required leading to a more compact design.
- Besides the scouring effect of the particles, the fluidized bed in the fluid stream has an additional effect. The chaotic movement of the particles also breaks down the boundary layer and thereby strongly improves the heat transfer with a factor of around 4 at the same fluid velocity. Because the self-cleaning heat exchanger normally applies lower velocities the heat transfer improves with around 20% compared to that of a regular shell and tube heat exchanger.
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