Model | Ev capacity | Steam consumption kg/h | Each effect vacuum, mmHg | Each effect temp. ℃ | Steam pres. | Feed DS,% | Discharge DS, % | ||||
1st effect | 2nd effect | 3rd effect | 1st effect | 2nd effect | 3rd effect | ||||||
HM-CC1.0-T | 1000.0 | 330-400 | 300 | 510 | 750 | 85 | 76.0 | 55 | 0.5-0.6 | 5-6 | 55-65 |
HM-CC3.0-T | 3000.0 | 990-1200 | |||||||||
HM-CC4.5-T | 4500.0 | 1485-1800 | |||||||||
HM-CC6.0-T | 6000.0 | 1980-2400 | |||||||||
HM-CC9.0-T | 9000.0 | 2970-3600 | |||||||||
HM-CC12.0-T | 12000.0 | 3960-4800 | |||||||||
HM-CC15.0-T | 15000.0 | 4950-6000 | |||||||||
HM-CC20.0-T | 20000.0 | 6600-8000 | |||||||||
It is used for the products with general requirements on crystal shape and size, and can achieve high concentration discharging.
According to the characteristics of materials and the evaporation capacity, it can be designed as a single-effect or multi-effect evaporative crystallization system.
The unique design of the crystallizer can meet the intermittent crystallization, semi-continuous crystallization and continuous crystallization system. It can meet the continuous feed, continuous discharge process requirements.
The whole process system evaporates under the vacuum condition, with relatively low temp., fast evaporation speed, high evaporation concentration, and the relatively high viscosity of the liquid material is not easy to scale or block, which can achieve the maximum crystal ratio under the same energy consumption.