
基本信息:
- 专利标题: 一种废液三相低温蒸发系统及方法
- 专利标题(英):Waste liquid three-phase low-temperature evaporation system and method
- 申请号:CN201811209872.3 申请日:2018-10-17
- 公开(公告)号:CN109292857A 公开(公告)日:2019-02-01
- 发明人: 汪小刚 , 罗卫坤
- 申请人: 广东上典环境保护工程有限公司
- 申请人地址: 广东省佛山市南海区桂城街道深海路17号瀚天科技城A区8号楼十三楼1308单元
- 专利权人: 广东上典环境保护工程有限公司
- 当前专利权人: 汪小刚
- 当前专利权人地址: 广东省佛山市南海区桂城街道深海路17号瀚天科技城A区8号楼十三楼1308单元
- 主分类号: C02F1/04
- IPC分类号: C02F1/04
The invention discloses a waste liquid three-phase low-temperature evaporation system, which comprises a low-temperature evaporator, a combustion chamber and an intelligent control cabinet. A waste liquid tank is connected to the low-temperature evaporator through a pipeline. The pipeline connected at the upper end of the low-temperature evaporator penetrates through a No. 1 first heat exchanger to be connected to a No.1 separator, the lower end of which is connected to a water storage tank. The pipeline connected at the upper end of the No.1 separator penetrates through a No.3 heat exchangerto be connected to the combustion chamber. An intake pipe penetrates through the No.1 heat exchanger and the No.2 heat exchanger to be connected to the combustion chamber. The low-temperature evaporator is connected to a No. 2 separator through a pipeline. The lower end of the No.2 separator is connected to a condensed wastewater tank, which is connected to the combustion chamber. The pipeline connected at the upper end of the No.2 separator penetrates through the No.3 heat exchanger to be connected to the combustion chamber, the upper end of which is connected to an exhaust dust. The invention has the following advantages: by evaporation and concentration of waste liquid for decrement, the generated combustible waste gas undergoes separation and high-temperature combustion, heat generatedby the waste gas combustion is fully utilized, and waste heat can be recovered to save energy; and there is no secondary pollution.
IPC结构图谱:
C | 化学;冶金 |
--C02 | 水、废水、污水或污泥的处理 |
----C02F | 水、废水、污水或污泥的处理 |
------C02F1/00 | 水、废水或污水的处理C02F3/00至C02F9/00优先 |
--------C02F1/02 | .加热法 |
----------C02F1/04 | ..蒸馏或蒸发 |