CN104017618B - A kind of industrial waste oil treatment process - Google Patents
A kind of industrial waste oil treatment process Download PDFInfo
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- CN104017618B CN104017618B CN201410070212.7A CN201410070212A CN104017618B CN 104017618 B CN104017618 B CN 104017618B CN 201410070212 A CN201410070212 A CN 201410070212A CN 104017618 B CN104017618 B CN 104017618B
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Abstract
The open a kind of industrial waste oil treatment process of the present invention, comprises and is dissolved in industrial waste oil by ethylene glycol monobutyl ether, slurries additive agent, stir under normal temperature, form mixed solution, mixed solution adds coal dust and water, continues to stir the not stratified coal water slurry product of formation. this technique not only can turn waste into wealth originally scrapping the waste oil that can not directly discharge, eliminate subsequent disposal expense, the coal water slurry product thermal value simultaneously utilizing industrial waste oil to make also obtains corresponding raising, and couplant stabilization technique provided by the invention thoroughly solves the stability problem of tradition Orgnic Waste Liquid CWS, can also fundamentally solve the system stability problem of product, improve product stability, there is not oily water separation in long-time leaving standstill, it is easy to handling, storage, Cemented filling and atomization space burning etc., can be used for station boiler, Industrial Boiler and Industrial Stoves generation oil, for gas, for coal combustion.
Description
Technical field
The present invention relates to industrial waste oil process field, it is related specifically to the industrial waste oil treatment process using the equipment oil (comprising hydraulic efficiency oil, gear oil etc.) scrapped, industrial used oil, industrial abandoned treated oil etc. above industrial equipments.
Background technology
The various equipment oil (comprising hydraulic efficiency oil, gear oil etc.) must used above industrial machinery, industrial used oil, industrial abandoned treated oil etc.; play the lubrication protection effect to equipment or cutter, but finally these oil products all can cause because of reasons such as being mixed into moisture, mechanical impurity, oxidation, acidifying can not continue use and scrap. Degradation does not reach will scrap when requiring, but because the mineral oil wherein contained and other organic additive compositions, COD value (chemical oxygen demand) is very up to less than direct emission standard. Conventional producer or stealthily discharge, not only causes great destruction, and has offended the corresponding environmental protection laws and regulations of China environment. Give the environmental protection company process of corresponding qualification, but processing costs is high generally at 800-2000 yuan/ton not etc., brings many economical load to enterprise like this. Prior art also has and to process industrial waste oil by coal water slurry, but the fuel value of coal water slurry is not high, thoroughly can not effectively solve the wasting of resources and problem of environmental pollution, and the more important thing is also there is the relatively poor problem of system stability, can there is oily water separation in long-time leaving standstill, be not easy to handling, storage, Cemented filling and atomization space burning etc.
Therefore, need a kind of high performance fuel and its preparation method, can not only effectively process industrial waste oil, improve fuel combustion value, thoroughly can effectively solve the wasting of resources and problem of environmental pollution, moreover it is possible to fundamentally solve the system stability problem of product, it is to increase product stability, there is not oily water separation in long-time leaving standstill, is easy to handling, storage, Cemented filling and atomization space burning etc.
Summary of the invention
In view of this, the object of this patent is to provide a kind of industrial waste oil treatment process. this technique not only can turn waste into wealth originally scrapping the waste oil that can not directly discharge, eliminate subsequent disposal expense, the coal water slurry product thermal value simultaneously utilizing industrial waste oil to make also obtains corresponding raising, and couplant stabilization technique provided by the invention thoroughly solves the stability problem of tradition Orgnic Waste Liquid CWS, can also fundamentally solve the system stability problem of product, improve product stability, there is not oily water separation in long-time leaving standstill, it is easy to handling, storage, Cemented filling and atomization space burning etc., can be used for station boiler, Industrial Boiler and Industrial Stoves generation oil, for gas, for coal combustion.
A kind of industrial waste oil treatment process of the present invention, in industrial waste oil, add ethylene glycol monobutyl ether, slurries additive agent, coal dust, water form not stratified coal water slurry product.
Further, this technique comprises the following steps:
A. 0.1-1.5 part ethylene glycol monobutyl ether, 0.1-1.5 part slurries additive agent are dissolved in 5-20 part industrial waste oil, under normal temperature, stir 20-30min with the rotating speed of 4500rpm��5500rpm, form mixed solution;
B: coal dust and the 30-40 part water adding 40-60 part in mixed solution, continues to stir 20-30min and forms not stratified coal water slurry product.
Further, described slurries additive agent is one or more in emulsifying agent, defoamer, described emulsifying agent is one or more mixtures in naphthalene sulfonate, sulfonated lignin, Soxylat A 25-7, carboxylate salt, and described defoamer is waterborne organic silicon defoamer.
Further, described industrial waste oil is one or more in useless equipment oil, used oil, useless treated oil.
The useful effect of the present invention: a kind of industrial waste oil treatment process of the present invention, this technique not only can turn waste into wealth originally scrapping the waste oil that can not directly discharge, eliminate subsequent disposal expense, the coal water slurry product thermal value simultaneously utilizing industrial waste oil to make also obtains corresponding raising, and couplant stabilization technique provided by the invention thoroughly solves the stability problem of tradition Orgnic Waste Liquid CWS, can also fundamentally solve the system stability problem of product, improve product stability, there is not oily water separation in long-time leaving standstill, it is easy to handling, storage, Cemented filling and atomization space burning etc., obtained coal water slurry product is because what utilize is such as be collectively referred to as ester etc. containing mineral oil and some organic additives to scrap industrial waste oil, so it has higher thermal value relative to the coal water slurry obtained with ortho-water, can be used for station boiler, Industrial Boiler and Industrial Stoves generation oil, for gas, for coal combustion.
Embodiment
A kind of industrial waste oil treatment process of the present embodiment, it is characterised in that: this technique comprises the following steps:
A. 0.1-1.5 part ethylene glycol monobutyl ether, 0.1-1.5 part slurries additive agent are dissolved in 5-20 part industrial waste oil, under normal temperature, stir 20-30min with the rotating speed of 4500rpm��5500rpm, form mixed solution;
B: coal dust and the 30-40 part water adding 40-60 part in mixed solution, continues to stir 20-30min and forms not stratified coal water slurry product.
In the present embodiment, described slurries additive agent is one or more in emulsifying agent, defoamer, described emulsifying agent is one or more mixtures in naphthalene sulfonate, sulfonated lignin, Soxylat A 25-7, carboxylate salt, and described defoamer is waterborne organic silicon defoamer.
In the present embodiment; pending industrial waste oil is various equipment oil (comprising hydraulic efficiency oil, gear oil etc.), industry used oil, industrial abandoned treated oil etc.; play the lubrication protection effect to equipment or cutter, but finally these oil products all can cause because of reasons such as being mixed into moisture, mechanical impurity, oxidation, acidifying can not continue use and scrap. Degradation does not reach will scrap when requiring, but because the mineral oil wherein contained and other organic additive compositions, COD value (chemical oxygen demand) is very up to less than direct emission standard.
Below by way of specific embodiment, the present invention is further elaborated.
Embodiment one
A. 1 part of ethylene glycol monobutyl ether, 1 part of slurries additive agent are dissolved in 20 parts of industrial waste oils, under normal temperature, stir 25min with the rotating speed of 5000rpm, form mixed solution;
B: coal dust and the 30 parts of water adding 48 parts in mixed solution, continues to stir 25min and forms not stratified coal water slurry product.
In the present embodiment, described slurries additive agent is one or more in emulsifying agent, defoamer, described emulsifying agent is one or more mixtures in naphthalene sulfonate, sulfonated lignin, Soxylat A 25-7, carboxylate salt, and described defoamer is waterborne organic silicon defoamer.
In the present embodiment, pending industrial waste oil is various equipment oil (comprising hydraulic efficiency oil, gear oil etc.), industry used oil, industrial abandoned treated oil etc.
Embodiment two
A kind of industrial waste oil treatment process of the present embodiment, it is characterised in that: this technique comprises the following steps:
A. 1.2 parts of ethylene glycol monobutyl ethers, 1.5 parts of slurries additive agents are dissolved in 15.5 parts of industrial waste oils, under normal temperature, stir 20min with the rotating speed of 4500rpm��5500rpm, form mixed solution;
B: coal dust and the 35 parts of water adding 46.8 parts in mixed solution, continues to stir 20min and forms not stratified coal water slurry product.
In the present embodiment, described slurries additive agent is one or more in emulsifying agent, defoamer, described emulsifying agent is one or more mixtures in naphthalene sulfonate, sulfonated lignin, Soxylat A 25-7, carboxylate salt, and described defoamer is waterborne organic silicon defoamer.
In the present embodiment; pending industrial waste oil is various equipment oil (comprising hydraulic efficiency oil, gear oil etc.), industry used oil, industrial abandoned treated oil etc.; play the lubrication protection effect to equipment or cutter, but finally these oil products all can cause because of reasons such as being mixed into moisture, mechanical impurity, oxidation, acidifying can not continue use and scrap. Degradation does not reach will scrap when requiring, but because the mineral oil wherein contained and other organic additive compositions, COD value (chemical oxygen demand) is very up to less than direct emission standard.
Embodiment three
A kind of industrial waste oil treatment process of the present embodiment, it is characterised in that: this technique comprises the following steps:
A. 0.8 part of ethylene glycol monobutyl ether, 1 part of slurries additive agent are dissolved in 14 parts of industrial waste oils, under normal temperature, stir 20-30min with the rotating speed of 4500rpm��5500rpm, form mixed solution;
B: coal dust and the 34.2 parts of water adding 50 parts in mixed solution, continues to stir 20-30min and forms not stratified coal water slurry product.
In the present embodiment, described slurries additive agent is one or more in emulsifying agent, defoamer, described emulsifying agent is one or more mixtures in naphthalene sulfonate, sulfonated lignin, Soxylat A 25-7, carboxylate salt, and described defoamer is waterborne organic silicon defoamer.
In the present embodiment; pending industrial waste oil is various equipment oil (comprising hydraulic efficiency oil, gear oil etc.), industry used oil, industrial abandoned treated oil etc.; play the lubrication protection effect to equipment or cutter, but finally these oil products all can cause because of reasons such as being mixed into moisture, mechanical impurity, oxidation, acidifying can not continue use and scrap. Degradation does not reach will scrap when requiring, but because the mineral oil wherein contained and other organic additive compositions, COD value (chemical oxygen demand) is very up to less than direct emission standard.
In above-described embodiment, additive is generally emulsifying agent, defoamer etc., but adds pigment, mask agent, other functional additives, all the character of the present invention is not had substantial effect, only adds for not congenerous alternative.
In above-described embodiment, it is possible to adopt other defoamers that can realize same goal of the invention.
The characteristic of the waste oil coal water slurry that the industrial waste oil treatment process of above-described embodiment obtains sees the following form:
| Embodiment | Calorific value | Rheological | Efficiency of combustion |
| Embodiment one | 19.8MJ/�K | B level | 98.9 |
| Embodiment two | 22.0MJ/�K | B level | 99.1 |
| Embodiment three | 22.6MJ/�K | B level | 98.7 |
The stability of the high performance fuel (coal water slurry) that above-described embodiment is obtained all can reach more than B level. Detection method is: gets a small amount of sample, is placed in sealed vessel, quiet a surname's for some time, then observes its analysis regimen condition, precipitation situation, slurry body regenerative power, withered property, mobility etc.
Carry out respectively testing as follows by the waste liquor coal liquid obtained by the process of water-based metal working fluid process for treating waste liquor in above-described embodiment:
Measuring the concentration of waste liquor coal liquid in advance, then get six bottles, (quantitatively filling 200ml in every bottle, sealing) leaves standstill, and within every 15 days, gets one bottle and measures change in concentration. Measuring method is: the slurry concentration measuring upper strata 50ml and orlop 50ml.
Two, experimental result
1, the change of upper strata 50ml: the time is more long, the concentration of slurry is more and more lower, and the fastest change in first 10 days, change is little afterwards.
2, the change of lower floor 50ml: the fastest change in first 10 days, changes more and more less afterwards and tends to be steady.
3, in 3 months, hard-caked sediment does not occur, stability very good is described.
A level: stability is best, slurry body keeps original state, is uniformly distributed, and produces without analysis water and precipitation.
, there is the generation of a small amount of analysis water or soft precipitation in B level: stability is better.
C level: slurry stability is poor, has precipitation to produce, has analysis water, density distribution uneven, and renewable through stirring, good flowing properties, slurry body is even.
D level: stability is worst, density distribution is obviously uneven, and producing hard-caked sediment cannot regenerate.
As seen from the above-described embodiment, and for above technique effect, the proportioning of embodiment two and processing parameter, it may also be useful to effect is best, is obviously better than other embodiment, is the best.
What finally illustrate is, above embodiment is only in order to illustrate the technical scheme of this patent and unrestricted, although this patent being described in detail with reference to better embodiment, it will be understood by those within the art that, the technical scheme of this patent can be modified or equivalent replace (such as adding proportion have that adjust, industrial waste oil product source may be other mechanical means sources a little etc. such as civilian machinery), and not departing from objective and the scope of technical solution of the present invention, it all should be encompassed in the middle of the right of the present invention.
Claims (2)
1. an industrial waste oil treatment process, it is characterised in that: this technique comprises the following steps:
A. 0.1-1.5 part ethylene glycol monobutyl ether, 0.1-1.5 part slurries additive agent are dissolved in 5-20 part industrial waste oil, under normal temperature, stir 20-30min with the rotating speed of 4500rpm��5500rpm, form mixed solution;
B. in mixed solution, add coal dust and 30-40 part water of 40-60 part, continue to stir 20-30min and form not stratified coal water slurry product;
Described slurries additive agent is one or more in emulsifying agent, defoamer; Described emulsifying agent is one or more mixtures in naphthalenesulfonate, sulfonated lignin, Soxylat A 25-7, carboxylate salt; Described defoamer is waterborne organic silicon defoamer.
2. industrial waste oil treatment process according to claim 1, it is characterised in that: described industrial waste oil is one or more in useless equipment oil, used oil, useless treated oil.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201410070212.7A CN104017618B (en) | 2014-02-27 | 2014-02-27 | A kind of industrial waste oil treatment process |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410070212.7A CN104017618B (en) | 2014-02-27 | 2014-02-27 | A kind of industrial waste oil treatment process |
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| CN104017618A CN104017618A (en) | 2014-09-03 |
| CN104017618B true CN104017618B (en) | 2016-06-01 |
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| CN105925327A (en) * | 2016-04-26 | 2016-09-07 | 太原理工大学 | Coal-based three phase hybrid fuel prepared from waste engine oil |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1099064A (en) * | 1993-06-01 | 1995-02-22 | 株式会社阿罗马化学机械工业 | Combustion method of water-in-oil type emulsified fuel |
| CN101092578A (en) * | 2006-06-21 | 2007-12-26 | 颜春夏 | Composite fuel with high heat value and preparation method |
| CN101358137A (en) * | 2008-09-28 | 2009-02-04 | 广州恒雅环保科技有限公司 | Sludge liquid fuel and preparation method thereof |
| CN102051242A (en) * | 2010-12-17 | 2011-05-11 | 贵阳超群实业有限公司 | Oil-water coal slurry and preparation method thereof |
-
2014
- 2014-02-27 CN CN201410070212.7A patent/CN104017618B/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1099064A (en) * | 1993-06-01 | 1995-02-22 | 株式会社阿罗马化学机械工业 | Combustion method of water-in-oil type emulsified fuel |
| CN101092578A (en) * | 2006-06-21 | 2007-12-26 | 颜春夏 | Composite fuel with high heat value and preparation method |
| CN101358137A (en) * | 2008-09-28 | 2009-02-04 | 广州恒雅环保科技有限公司 | Sludge liquid fuel and preparation method thereof |
| CN102051242A (en) * | 2010-12-17 | 2011-05-11 | 贵阳超群实业有限公司 | Oil-water coal slurry and preparation method thereof |
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| CN104017618A (en) | 2014-09-03 |
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Address after: Guangdong Province, Dongguan City Industrial Road 523808 Songshan Lake Science and Technology Industrial Park No. 6 Applicant after: AMER TECHNOLOGY CO.,LTD. Address before: 523808 Guangdong province Dongguan City Songshan Lake Science and Technology Industrial Park Road No. 6 Applicant before: DONGGUAN AMER LUBRICANT TECHNOLOGY Co.,Ltd. |
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Granted publication date: 20160601 |