Refining and recycling equipment for crude glycerine
By designing a refining and recycling equipment for glycerol distillation, using the combination of cooling components and condensation components, the problems of low condensation efficiency and easy rust in the existing technology are solved, and efficient glycerol vapor condensation and purity improvement are achieved.
CN119633433APending Publication Date: 2025-03-18JIANGSU JINQIAO OIL TECH CO LTD
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Patent Information
- Application Number
- CN202411816481.3
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Filing Date
- 2024-12-11
- Publication Date
- 2025-03-18
AI Technical Summary
Technical Problem
In existing glycerol distillation devices, the condensation is cooled by water cooling, which can easily lead to rust after long-term use. The cold water tank needs to be cleaned, otherwise the cooling efficiency will decrease.
Method used
A refined recycling equipment for crude glycerol is designed, using cooling components and condensation components, and the vapor enters the condensation components laterally, increasing the contact area and condensation efficiency to avoid steam reflux.
Benefits of technology
It improves the vapor condensation efficiency, increases the purity collection efficiency of glycerol, avoids the problems of rust and cooling plate cleaning, and improves the reliability and efficiency of the equipment.
✦ Generated by Eureka AI based on patent content.
Abstract
The invention discloses refining and recycling equipment for crude glycerine, and relates to the technical field of crude glycerine refining. According to the refining and recycling equipment for the crude glycerine, pressurized air can be quickly conveyed into a side connecting pipe through a condensation assembly and a hose, the air flow quickly flows in the side connecting pipe, and when the air flow makes contact with protruding threads, the heat exchange area can be increased, and heat absorbed by a condensation pipe is taken away; and then the gas subjected to heat exchange can be conveyed into the insertion pipe A through the insertion pipe B, and the gas subjected to heat exchange is conveyed into the injection cylinder B through the calandria, so that liquid cooling is conveniently avoided, subsequent cooling of the condensation pipe is facilitated, the heat exchange area in the condensation pipe can be increased through the cooling mode, and the heat exchange efficiency of the condensation pipe is improved. Therefore, the heat exchange efficiency is improved, and the condensation pipe can be rapidly cooled in an air cooling mode.
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