+86 19150187139
Working exchange capacity refers to the exchange capacity of an ion exchange resin under operating conditions. It is the exchange capacity achieved when exchanged ions begin to appear in the filtrate during the ion exchange reaction process in an ion exchange device. This is the exchange capacity used in actual engineering operations.
Generally, working exchange capacity is expressed in two ways:
1. Mass expression: This refers to the exchange capacity per unit mass of dry resin, expressed as milliequivalents per gram (g) (dry resin).
2. Volume expression: This refers to the exchange capacity per unit volume of resin after full swelling, expressed as milliequivalents per milliliter (wet resin). Because resins are mostly used in exchange columns and towers, volumetric exchange capacity is more commonly used in practice.
Working exchange capacity is related not only to the physicochemical properties of the resin itself but also to the operating conditions. These conditions mainly include:
1. The initial operating state of the resin, i.e., the degree of regeneration. For a given resin bed, the degree of regeneration is related to the ionic composition and distribution of the resin before regeneration, as well as the type, dosage, and concentration of the regenerant, and the temperature and flow rate of the regenerant solution.
2. The working conditions of the resin include solution composition, flow rate, temperature, effluent composition, resin bed height, and equipment operation.
The factors affecting the working exchange capacity of ion exchange resins include some that can be controlled manually, some that are determined during production (such as flow rate, effluent quality, and resin bed height), and some that are determined by natural conditions (such as raw water composition). Therefore, the working exchange capacity is not a constant value. The working exchange capacity of the same resin will vary depending on the water treatment process. The working exchange capacity of the same resin in different locations cannot be compared directly. Therefore, the design and operation level of a water treatment system and equipment cannot be judged solely by its working exchange capacity. In a water treatment system, the limit of the resin's working exchange capacity is the equilibrium exchange capacity under that water quality (with the same inlet and outlet water composition). Therefore, the actual working exchange capacity will inevitably be lower than the dry equilibrium exchange capacity.