A crystallization cooler and its method for extending the operation period of an external circulation type crystallizer
An operation cycle and cooler technology, applied in the chemical industry, can solve problems affecting supersaturation, deterioration of heat transfer performance, crystallizer shutdown, etc., and achieve the effects of eliminating scaling, small temperature difference between inside and outside, and reducing heat exchange area
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0025] The piperazine solution at 60°C is cooled and crystallized by a DTB crystallizer at 20°C, and the traditional tubular cooler and the crystallization cooler of the present invention are respectively used for cooling and crystallization. The traditional shell and tube cooler is directly cooled with cooling water at 6-10°C. The working fluid of the crystallization cooler of the present invention is dimethyl ether, and the temperature of the freezing water is 6-10°C. The circulating material entering the crystallization cooler is 4800kg / h piperazine solution at 23°C. The flow of chilled water is controlled through the control loop formed by the regulating valve 18 and the temperature control indicator 19, so that the evaporation temperature of the working fluid is controlled at 18°C, so that The circulating material is cooled to 20°C and enters the crystallizer.
[0026] After 112 hours of operation of the traditional shell-and-tube cooler, the cooler was blocked and unabl...
Embodiment 2
[0028] As described in Example 1, the traditional tubular cooler and the crystallization cooler of the present invention are respectively used for cooling and crystallization, and the crystallization process conditions and control mode are the same as in Example 1, except that the working fluid of the present invention is Methylal.
[0029] After the traditional shell-and-tube cooler was operated for 102 hours, the cooler was blocked and could not operate; after the crystallization cooler of the present invention was operated for 200 hours, no obvious fouling was found when the crystallization cooler was disassembled.
Embodiment 3
[0031] As described in Example 1, the traditional tubular cooler and the crystallization cooler of the present invention are respectively used for cooling and crystallization, and the crystallization process conditions and control mode are the same as in Example 1, except that the working fluid of the present invention is Methyl tert-butyl ether.
[0032] After 95 hours of operation of the traditional shell-and-tube cooler, the cooler was blocked and unable to operate; after the crystallization cooler of the present invention was operated for 200 hours, no obvious fouling was found when the crystallization cooler was disassembled.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 