CONDENSATE POLISHING: Basic Principles
Fossil-fuelled (coal, oil, gas) and nuclear power stations produce electricity with turbines powered with high pressure steam. A schematic representation of this steam circuit is shown in the picture below. After going through the turbine, the steam is condensed and recycled.
To avoid deposits on the turbine blades and corrosion in the steam circuit, the steam must be extremely pure. However, being permanently recycled, the condensate collects corrosion and erosion products from the boiler and pipework, as shown in the picture. The contaminants in the condensate must have a concentration of a few µg/L (ppb) or less. Therefore, the condensate, in many (but not all) power stations, is treated with ion exchange resins, ion exchange being the only process capable of achieving these low residual values.
Many new power stations are being built, particularly in emerging countries such as India and China, so that the number of condensate polishing project has increased tremendously since the beginning of the 21st Century. Whilst ion exchange processes for water demineralisation were mainly developed in Europe, the champions of condensate polishing design are largely American.
Duties of a condensate polisher
The condensate polisher must fulfill two simultaneous duties:
- it must remove the "crud", wich is suspended solids (mostly metal oxides) resulting from corrosion and erosion;
- it must also remove any dissolved solids originating from the make-up water, possible leaks of the condenser, or from regeneration of the ion exchange resins.
This means that the polisher must perform filtration and demineralisation at the same time.
Most power stations use ammonia or amines to condition the water and steam circuit to reduce corrosion. As a result, the ionic load on the condensate polishing resin is largely cationic, and ammonium ions are removed together with lower concentrations of cations and anions in the condensate polisher.
In view of the low salinity of the water to be treated, mixed bed polishers are used in over 90 % of the cases. These units are usually designed for a high specific flow rate (80 to 120 bed volumes per hour). In large power stations, the flow rate through each condensate polishing unit is often 600 to 1000 m3/h. When the operating pressure is not too high, cylindrical vessels are used, but at 4 MPa (40 bar) or above, spherical vessels are necessary to keep the shell thickness within reasonable limits.
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A cylindrical MB unit
A spherical MB unit
Other polisher designs are mentioned in the page about ion exchange columns.
In most cases, regeneration is external. This has two purposes:
- to avoid accidental ingress of regenerant chemicals in the water and steam circuit;
- to design the operating unit without internals, and with a low bed depth producing a relatively low pressure drop, whilst the regeneration station is designed with narrower columns and a high bed depth facilitating resin separation.
The principle of external regeneration is shown below. Exhausted resin is transferred hydraulically from the operating unit to the regeneration station, and a fresh regenerated resin charge is transferred back immediately.
Condensate polishing system with external regeneration
The regeneration station has typically three columns, the first one (CRT = cation regeneration tower) used for backwash, cleaning and separation of the mixed resins and regeneration of the cation exchanger, the second one (ART = anion regeneration tower) for regeneration of the anion exchanger, and the last one (MSV = mixing and storage vessel) for mixing, fast rinse and storage of the regenerated resin.
© François de Dardel