Processing method of recycled illegal cooking oil

A processing method and technology for waste oil, which are applied in the recovery of fat oil/fatty acid from waste, recovery of fatty substances, and recycling technology, etc., can solve the problems of raising livestock with garbage, etc., and achieve the effects of low cost, low energy consumption and simple process.

Inactive Publication Date: 2012-01-04
HEILONGJIANG CHUNYI ENVIRONMENTAL PROTECTION TECH DEV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At the same time, problems such as waste oil on the dining table and food waste feeding livestock have also arisen.
At present, there is no unified method to deal with or recycle waste oil in our country.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0015] (1) First filter impurities and deacidify the collected waste oil, swill oil, and waste fat oil;

[0016] (2) Place waste oil, swill, and waste fat oil in the reaction kettle again, add 3% white clay and 0.5% phosphoric acid, mix, heat and stir. The heating temperature is between 80° C., and the heating and stirring time is 0.5 hour;

[0017] (3) Heat the evenly stirred material, settle and decompose, cool naturally to 34°C, settle and separate phases, and then filter to obtain liquid oil and semi-solid white clay, gutter oil, swill oil, and oil acid value of waste oil From 3.5mg / koh / g to 0.9mg / koh / g;

[0018] (4), the semi-solid white clay is dried or naturally dried;

[0019] (5), then put the liquid oil and semi-solid clay in the reaction kettle, add 3% cationic active emulsifier, stir at 50°C for 20 minutes at high speed to micro-emulsify fatty acids and triglycerides, then add ionic catalysts to stabilize 0.1% agent, under the pressure condition of 100Mpa pressur...

Embodiment 2

[0021] (1) First filter impurities and deacidify the collected waste oil, swill oil, and waste fat oil;

[0022] (2) Place waste oil, swill, and waste fat oil in the reaction kettle, add 4.5% clay and 1% phosphoric acid, mix and heat and stir evenly. The heating temperature is between 90° C., and the heating and stirring time is 1 hour;

[0023] (3) Heat the evenly stirred material, settle and decompose, cool naturally to 36°C, settle and separate phases, and then filter to obtain liquid oil and semi-solid white clay, gutter oil, swill oil, and oil acid value of waste oil From 3.5mg / koh / g to 1.2mg / koh / g;

[0024] (4), the semi-solid white clay is dried or naturally dried;

[0025] (5), then put the liquid oil and semi-solid clay in the reaction kettle, add 3% cationic active emulsifier, stir at 65°C for 35 minutes at high speed to micro-emulsify fatty acid and triglyceride, then add ionic catalyst to stabilize 0.1% of the agent, under the pressure condition of 120Mpa pressur...

Embodiment 3

[0027] (1) First filter impurities and deacidify the collected waste oil, swill oil, and waste fat oil;

[0028] (2) Place waste oil, swill, and waste fat oil in the reaction kettle again, add 6% clay and 1.5% phosphoric acid, mix and heat and stir evenly. The heating temperature is between 100° C., and the heating and stirring time is 1.2 hours;

[0029] (3) Heat the evenly stirred material, settle and decompose, cool naturally to 37°C, settle and separate phases, and then filter to obtain liquid oil and semi-solid white clay, gutter oil, swill oil, and oil acid value of waste oil From 3.5mg / koh / g to 1.4mg / koh / g;

[0030] (4), the semi-solid white clay is dried or naturally dried;

[0031] (5), then put the liquid oil and semi-solid clay in the reaction kettle, add 3% cationic active emulsifier, stir at 80°C for 50 minutes at high speed to micro-emulsify fatty acids and triglycerides, then add ionic catalysts to stabilize 0.1% agent, under the pressure condition of 150Mpa, ...

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PUM

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Abstract

The invention relates to a processing method of recycled illegal cooking oil, which comprises the following steps of: firstly, filtering impurities of collected illegal cooking oil, swilling oil and waste oil and depickling the collected illegal cooking oil, swilling oil and waste oil, then placing the collected illegal cooking oil, swilling oil and waste oil in an agitated reactor, adding 3-6% of carclazyte and 0.5-1.5% of phosphoric acid, mixing, heating and uniformly stirring, heating the uniformly stirred materials, naturally cooling to 34 DEG C-37 DEG C after settling and decomposing, filtering to obtain liquid oil and semi-solid carclazyte after settling and splitting phase, wherein the acid value of oil of the illegal cooking oil, swilling oil and waste oil is reduced from 3.5mg/koh/g to 0.9-1.4mg/koh/g, drying or naturally drying the semi-solid carclazyte in air, then placing the liquid oil and the semi-solid carclazyte in the agitated reactor, adding 3% of cation expression activity emulsifying agent, stirring at high speed for 20-50 minutes at the temperature of 50 DEG C-80 DEG C to enable fatty acid and triglyceride to be micro-emulsified, then adding 0.1% of ionic catalysis stabilizing agent, under the condition of 100-150Mpa pressure, and finally pumping hydrogen for 15-25 minutes by 0.5 per cubic meter per second to obtain biomass fuel. The processing method has the advantages of simple process, low cost, little energy consumption and high efficiency.

Description

technical field [0001] The invention relates to a treatment method for recovered waste oil. Background technique [0002] Our country has a large population, the consumption of vegetable oil and food is huge, and a large amount of catering waste is produced. In our country, catering waste can reach tens of millions of tons every day. Therefore, the developed catering industry in our country makes the output of catering oil extremely large, causing serious environmental pollution. . At the same time, problems such as the use of waste oil on the dining table and food waste to feed livestock have also arisen. At present, my country does not have a unified method to process or recycle waste oil. Contents of the invention [0003] The object of the present invention is to overcome the weak point that exists in the above-mentioned technology, and provides a kind of treatment method of recovering waste oil. [0004] In order to achieve the above object, the technical scheme ad...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C11B3/00C11B3/04C11B13/00C11B3/10C11C3/12C10L1/02
CPCY02W30/74
Inventor 李毅付英春于俊洲张震岩冯传江
Owner HEILONGJIANG CHUNYI ENVIRONMENTAL PROTECTION TECH DEV
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