CN102851064B - 可燃废油连续净化蒸馏装置 - Google Patents

可燃废油连续净化蒸馏装置 Download PDF

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CN102851064B
CN102851064B CN201210314626.0A CN201210314626A CN102851064B CN 102851064 B CN102851064 B CN 102851064B CN 201210314626 A CN201210314626 A CN 201210314626A CN 102851064 B CN102851064 B CN 102851064B
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evaporating pot
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CN102851064A (zh
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刘建波
李玉坤
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Ruixin Environmental Technology Minquan County Co ltd
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Abstract

一种可燃废油连续净化蒸馏装置,包括蒸发罐、热风预热器、蒸馏器及燃烧炉组成,导油管一端连接蒸发罐上部,另一端连接热风预热器,废油输油管接口经输油泵连接热风预热器;渣油管一端连接在蒸发罐底部,另一端连接在蒸馏器进口上,出热油气管一端连接在蒸馏器上,另一端连接在蒸发器上部,蒸馏器上的热风出口连接在热风预热器上,出渣口设在蒸馏器末端下部;出油气管连接在蒸发罐顶部。本发明的设备制造简单,工艺易行,且操作方便,可实现连续化生产,产量大、工作效率高,蒸馏充分不产生废渣油,不造成环境二次污染,经济效益和社会效益显著。

Description

可燃废油连续净化蒸馏装置
技术领域
本发明涉及一种可燃废油连续净化蒸馏装置。
背景技术
废旧橡胶、废塑料热裂解生产出来的基础油,以及废机油等废油只能作为工业锅炉和其他燃油锅炉的燃料,不能用于其他更精细的发动机燃烧,大大降低了油品的价值、并造成不同程度的能源浪费,湿法蒸馏又要剩余30%左右的渣油,剩余的渣油还要进行二次裂解,所以增大了不必要的生产成本,还会造成环境的二次污染。
发明内容
本发明要解决的技术问题是:设计一种可燃废油连续净化蒸馏装置,将废燃油通过净化蒸馏,使轻重组份分开,提取出可用于精细发动机的近似国标汽油、柴油的清洁能源,既可提高油品的品质增大经济效益,又不造成环境的二次污染。
解决本发明问题所采取的技术方案是:该装置包括蒸发罐、热风预热器、蒸馏器及燃烧炉组成,导油管一端连接蒸发罐上部,另一端连接热风预热器,废油输油管接口经输油泵连接热风预热器;渣油管一端连接在蒸发罐底部,另一端连接在蒸馏器进口上,出热油气管一端连接在蒸馏器上,另一端连接在蒸发罐上部,蒸馏器上的热风出口连接在热风预热器上,出渣口设在蒸馏器末端下部;出油气管连接在蒸发罐顶部。
在蒸发罐下部设有一根回油管,经输油泵连接热风预热器。
首先点燃燃烧炉使蒸馏器的内部温度上升至150℃,这时开启输油泵使废油通过热风预热器进入蒸发罐,蒸发的热油气体从蒸发罐上部的出油气口流出进入冷凝系统,蒸发罐下部没蒸发的废油一部分通过回油管打循环回热风预热器,另一部分进入蒸馏器蒸馏,蒸馏后的灰渣从出渣口排出,不再有蒸不净的渣油产生。
本发明的积极效果是:设备制造成本低,工艺简单易行,且操作方便,可实现连续化生产,产量大、工作效率高,蒸馏充分不产生废渣油,不造成环境二次污染,经济效益和社会效益0显著。
附图说明
 附图1为本发明结构示意图。
具体实施方式
本发明装置如图1所示,该装置包括蒸发罐2、热风预热器10、蒸馏器7及燃烧炉8组成,导油管3一端连接蒸发罐2上部,另一端连接热风预热器10,废油输油管接口12经输油泵11连接热风预热器10;回油管5一端连接在蒸发罐2下部,另一端经输油泵11连接热风预热器10;渣油管6一端连接在蒸发罐2底部,另一端连接在蒸馏器7进口上,出热油气管4一端连接在蒸馏器7上,另一端连接在蒸发罐2上部,蒸馏器7上的热风出口经热风管9连接在热风预热器10上,出渣口13设在蒸馏器7末端下部;出油气管1连接在蒸发罐2顶部。
首先点燃燃烧炉8、温度上升至150℃开启输油泵11,同时打开回油管5和渣油管6上的阀门并启动蒸发器7的主动电机,打开蒸馏器7出渣口13;废油进入热风预热器10再经导油管3进入蒸发罐2,蒸发罐2下部没蒸发的废油一部分通过回油管5和热风预热器10再循环,另一部分进入蒸馏器7蒸馏,蒸馏产生的热油气进入蒸发罐2,蒸馏的热油气和热风预热器产生的热油气同时从蒸发罐2上部的出油气管1流出进入冷凝系统;蒸馏后的灰渣从出渣口13排出,不再有蒸不净的渣油产生。

Claims (2)

1.一种可燃烧废油连续净化蒸馏装置,其特征在于:该装置包括蒸发罐、热风预热器、蒸馏器及燃烧炉组成,导油管一端连接蒸发罐上部,另一端连接热风预热器,废油输油管接口经输油泵连接热风预热器;渣油管一端连接在蒸发罐底部,另一端连接在蒸馏器进口上,出热油气管一端连接在蒸馏器上,另一端连接在蒸发器上部,蒸馏器上的热风出口连接在热风预热器上,出渣口设在蒸馏器末端下部;出油气管连接在蒸发罐顶部。
2.根据权利要求1所述的可燃烧废油连续净化蒸馏装置,其特征在于:在蒸发罐下部设有一根回油管,经输油泵连接热风预热器。
CN201210314626.0A 2012-08-30 2012-08-30 可燃废油连续净化蒸馏装置 Active CN102851064B (zh)

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