CN103848704A - Application of recovered oil - Google Patents
Application of recovered oil Download PDFInfo
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- CN103848704A CN103848704A CN201210520477.3A CN201210520477A CN103848704A CN 103848704 A CN103848704 A CN 103848704A CN 201210520477 A CN201210520477 A CN 201210520477A CN 103848704 A CN103848704 A CN 103848704A
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- Prior art keywords
- oil
- recovered oil
- explosive
- refiltered
- application
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Abstract
The invention relates to application of recovered oil, provides an application of recovered oil for preparing a special oil phase of a porous granular ammonium nitrate-fuel oil explosive and aims at effectively preventing the recovered oil from flowing to dinning tables and achieving no secondary pollution of wastes. A method for preparing the special oil phase of the porous granular ammonium nitrate-fuel oil explosive from the recovered oil comprises the following steps: on the basis of taking the recovered oil as a raw material, heating the recovered oil to the range from 40 DEG C to 60 DEG C, putting the heated recovered oil in an oscillating treater and carrying out oscillating treatment for 2.0-3.0 hours at a temperature within a range from 40 DEG C to 60 DEG C, and then standing and keeping a constant temperature for 10 minutes to 60 minutes. The application of the recovered oil has the advantages that the recovered oil is added to the porous granular ammonium nitrate-fuel oil explosive with the same effect just like adding diesel oil, the recovered oil is burnt thoroughly without influence on the ecology of the surrounding, and meanwhile, the recovered oil can be effectively prevented from flowing to the catering industry.
Description
Affiliated technical field
The present invention relates to a kind of oily application of regaining.
Background technology
Porous particulated ammonium oil explosive is to be invented by one company of the U.S. last century.This Explosive Technology is simple, and employment is few, essential safety, and less energy-consumption, outstanding feature is, with low cost, simple for production, insensitiveness relatively, the outdoor bulk blasting occasion that is adapted at wide aperture, large dose is used.Porous and granular ammonium nitrate has determined that to the characterization of adsorption of diesel oil and oil phase mixed process processed is both simple and quick.This explosive production, easy to use, Min Bao producer can be directly to engineering site and puddles, and reduce many transportations, store middle-chain, but this explosive uses diesel oil amount large, causes production cost to go up year by year along with International Crude Oil rises steadily.Refiltered oil has part to be back to food-processing or catering industry after processing, pollutes.In order to make refiltered oil utilization of waste material, prior art is generally that chemical treatment is processed as diesel oil.
Up to the present, also there is not the research report as the special oil phase of porous particulated ammonium oil explosive about refiltered oil.
Summary of the invention
The technical problem to be solved in the present invention is: provide a kind of refiltered oil as the application of preparing the special oil phase of porous particulated ammonium oil explosive, effectively contain that it flows to dining table, reaches refuse non-secondary pollution.
The present invention also provides a kind of method that refiltered oil is prepared the special oil phase of porous particulated ammonium oil explosive of applying.
In order to solve the problems of the technologies described above, the present invention is achieved through the following technical solutions:
In one aspect of the invention, provide a kind of application of refiltered oil, described refiltered oil is as the application of preparing the special oil phase of porous particulated ammonium oil explosive.
In another aspect of this invention, a kind of method that refiltered oil is prepared the special oil phase of porous particulated ammonium oil explosive of applying is provided, take refiltered oil as raw material, refiltered oil is heated to 40 ℃--after 60 ℃, put into oscillation treatment device, be 40 ℃ in temperature--60 ℃ after oscillation treatment 2.0-3.0 hour, leave standstill constant temperature 10-60 minute.
The present invention's application refiltered oil is prepared the method for the special oil phase of porous particulated ammonium oil explosive, and said oscillation treatment device is a kind of electromagnetic oscillation equipment, outreaches two wires and vibration ball by equipment.
The present invention's application refiltered oil is prepared the method for the special oil phase of porous particulated ammonium oil explosive, and said oscillation treatment is directly vibration ball to be put into refiltered oil, discharges electromagnetic oscillation ripple, and electromagnetic oscillation frequency is 50-100 hertz.
The invention has the beneficial effects as follows:
1, the present invention compared with prior art has the beneficial effect that cost is low, and data are as follows:
Porous particulated ammonium oil explosive proportioning is: porous and granular ammonium nitrate 88%-94%, diesel oil 6%-12%.It is 8%-10% left and right that intermediate value is got by general producer.
Calculate by producing 10000 tons of porous particulated ammonium oil explosives per year: with 1000 tons of diesel oil, existing diesel oil insurance and freight (CIF) is 8900 yuan/ton, and annual diesel oil expense is 8,900,000 yuan; Existing market refiltered oil is 5500 yuan/ton, adds electromagnetic treatment, packing, labor wage, charges for water and electricity, trucking costs, overheads uses tricks to increase by 1000 yuan/ton.Cost price is at 6500 yuan/ton, and sale price, by 8500 yuan/ton, is produced 1000 tons of refiltered oils, and gross profit, 2,000,000 yuan of left and right, is processed per year 2000 tons of refiltered oils and calculated, and gross profit can reach more than 400 ten thousand yuan.
2, the application method of refiltered oil is simple, and the oil phase performance of preparation is good
Sewer oil is nearly all made up of middle longer chain fatty acid and glycerine, and glycerine claims again glycerol, and redox reaction all can occur after being heated for lipid acid and glycerol, particularly contains the unsaturated free fatty acids of two keys.Molecular formula is as follows:
CH3-COOH+CL2P CI---CH2---COOH+HCL
Used oil molecular formula is as follows:
Electronic oscillation frequency is: 50-80 hertz
Before vibration, sewer oil viscosity is: 750mm
2/ S (40 ℃)
After vibration, sewer oil viscosity is: 100mm
2/ S (40 ℃)
No matter still detect data from outward appearance, before and after vibration, sewer oil is obviously thinning, change former sewer oil thickness, muddy, gluey outward appearance and intrinsiccharacteristic, make the sewer oil after vibration be transparent and there is fabulous mobility liquid, this just in time meets the quality requirement of porous particulated ammonium oil explosive to oil phase product, require oil phase to there is fabulous mobility, flammable, and there is certain coating function, just by having changed the sticky nature of refiltered oil, in addition refiltered oil itself has combustibility, therefore the refiltered oil after electromagnetic oscillation becomes the best substitute of main subsidiary material one diesel oil in porous particulated ammonium oil explosive.
Because main raw material(s) multi-hole nitramines in porous particulated ammonium oil explosive has blast performance, it has been outward combustion-supporting effect that diesel oil bag is attached to multi-hole nitramines particle, require evenly abundant coated porous ammonium nitrate particle of diesel oil, so require diesel oil must dilute and good fluidity, and by refiltered oil electromagnetic oscillation, cut off the longer molecular chain of refiltered oil, make refiltered oil thinning, improve refiltered oil flowing property, make it in porous particulated ammonium oil explosive, reach diesel oil substitute effect.Use diesel production porous particulated ammonium oil explosive identical with my company's special oil production porous particulated ammonium oil explosive result of use by user, quality level is identical, without using difference, but uses me can significantly reduce explosive production enterprise production cost in the company's special oil.
3, refiltered oil application of the present invention has the effect of environmental protection:
Combustion-supporting effect because refiltered oil is added in porous and granular ammoniumnitrate explosives, porous particulated ammonium oil explosive is fully burning in engineering explosion, and discharge blasting energy, reach blasting work object, diesel oil effect is the same with adding, and refiltered oil is fully burnt, on ecological without impact around, can effectively stop it to flow to catering industry, this invention be a contribution greatly to people's food sanitation and health simultaneously.
Therefore, the present invention compared with prior art, for further reducing production costs, rational exploitation and utilization sewer oil, swill wet goods refiltered oil, thoroughly effectively contain that it flows to dining table, reach refuse non-secondary pollution, low cost recycling, guarantee to produce a kind of steady quality is provided for porous particulated ammonium oil explosive, price is suitable, seriation, stdn, normalized oil phase material.Through reaction, the special oil phase of a kind of easy to use, moderate, stay-in-grade porous particulated ammonium oil explosive of formation that is in harmonious proportion.
The application of refiltered oil of the present invention, the physical parameter that application refiltered oil is prepared the special oil phase of porous particulated ammonium oil explosive be outward appearance without macroscopic impurity, without moisture, flash-point is not less than 60 ℃, zero pour is not higher than-10 ℃.
Embodiment
Embodiment 1
Sewer oil is being prepared the application of the special oil phase of porous particulated ammonium oil explosive.
Take the sewer oil that reclaims as raw material, the sewer oil of recovery is poured in heating tank, be heated to 40 ℃--60 ℃ time, putting into oscillation treatment device, constant temperature to 40 ℃--60 ℃ of oscillation treatment are after 2 hours, leave standstill constant temperature 10 minutes.
Embodiment 2
Swill oil is being prepared the application of the special oil phase of porous particulated ammonium oil explosive.
Take the swill oil that reclaims as raw material, the swill oil of recovery is poured in heating tank, be heated to 40 ℃--60 ℃ time, putting into oscillation treatment device, constant temperature to 40 ℃--60 ℃ of oscillation treatment are after 3 hours, leave standstill constant temperature 35 minutes.
Embodiment 3
Reclaim and mix assorted oil in the application of preparing the special oil phase of porous particulated ammonium oil explosive.
Take the sewer oil that reclaims as raw material, by assorted the mixing of recovery oily pouring in heating tank,--60 ℃ time, putting into oscillation treatment device, constant temperature to 40 ℃--the 60 ℃ of oscillation treatment that are heated to 40 ℃, after 2 hours, leave standstill constant temperature 60 minutes.
Claims (4)
1. an application for refiltered oil, is characterized in that: described refiltered oil is as the application of preparing the special oil phase of porous particulated ammonium oil explosive.
2. apply the method that refiltered oil is prepared the special oil phase of porous particulated ammonium oil explosive for one kind, it is characterized in that: take refiltered oil as raw material, refiltered oil is heated to 40 ℃--after 60 ℃, put into oscillation treatment device, be 40 ℃ in temperature--60 ℃ after oscillation treatment 2.0-3.0 hour, leave standstill constant temperature 10-60 minute.
3. method according to claim 2, is characterized in that: said oscillation treatment device is a kind of electromagnetic oscillation equipment, outreaches two wires and vibration ball by equipment.
4. method according to claim 2, is characterized in that.Said oscillation treatment is directly vibration ball to be put into refiltered oil, discharges electromagnetic oscillation ripple, and electromagnetic oscillation frequency is 50-100 hertz.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210520477.3A CN103848704A (en) | 2012-11-30 | 2012-11-30 | Application of recovered oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210520477.3A CN103848704A (en) | 2012-11-30 | 2012-11-30 | Application of recovered oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN103848704A true CN103848704A (en) | 2014-06-11 |
Family
ID=50856875
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201210520477.3A Pending CN103848704A (en) | 2012-11-30 | 2012-11-30 | Application of recovered oil |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103848704A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104211549A (en) * | 2014-09-04 | 2014-12-17 | 葛洲坝易普力股份有限公司 | Preparation method of mixed-charged emulsion explosive |
| CN106673928A (en) * | 2016-12-21 | 2017-05-17 | 福建海峡科化股份有限公司 | High-temperature sensitized emulsion explosives and preparation method thereof |
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| WO1998015521A1 (en) * | 1996-10-10 | 1998-04-16 | Isis Pharma Gmbh | New pentaerythritol derivatives, their production and use and intermediates for their synthesis |
| CN1227209A (en) * | 1998-10-28 | 1999-09-01 | 准格尔煤炭工业公司 | Anfo explosive and its producing process |
| CN201435000Y (en) * | 2009-07-16 | 2010-03-31 | 葛洲坝易普力股份有限公司 | Full automatic field mixed loading emulsion explosive truck control device |
| CN101898922A (en) * | 2010-08-24 | 2010-12-01 | 新疆天河化工有限公司 | Swill-cooked dirty oil expanded explosive and production method thereof |
| CN101898923A (en) * | 2010-08-24 | 2010-12-01 | 新疆天河化工有限公司 | Industrial waste oil expanded explosive and production method thereof |
| CN102504930A (en) * | 2011-10-28 | 2012-06-20 | 连力生 | Spent lubrication oil regeneration device with ultrasonic membrane separator |
| CN102504942A (en) * | 2011-10-25 | 2012-06-20 | 李文东 | Process for preparing high quality tea oil |
| US20120180915A1 (en) * | 2007-06-28 | 2012-07-19 | Maxam North America | Explosive emulsion compositions and methods of making the same |
-
2012
- 2012-11-30 CN CN201210520477.3A patent/CN103848704A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1998015521A1 (en) * | 1996-10-10 | 1998-04-16 | Isis Pharma Gmbh | New pentaerythritol derivatives, their production and use and intermediates for their synthesis |
| CN1227209A (en) * | 1998-10-28 | 1999-09-01 | 准格尔煤炭工业公司 | Anfo explosive and its producing process |
| US20120180915A1 (en) * | 2007-06-28 | 2012-07-19 | Maxam North America | Explosive emulsion compositions and methods of making the same |
| CN201435000Y (en) * | 2009-07-16 | 2010-03-31 | 葛洲坝易普力股份有限公司 | Full automatic field mixed loading emulsion explosive truck control device |
| CN101898922A (en) * | 2010-08-24 | 2010-12-01 | 新疆天河化工有限公司 | Swill-cooked dirty oil expanded explosive and production method thereof |
| CN101898923A (en) * | 2010-08-24 | 2010-12-01 | 新疆天河化工有限公司 | Industrial waste oil expanded explosive and production method thereof |
| CN102504942A (en) * | 2011-10-25 | 2012-06-20 | 李文东 | Process for preparing high quality tea oil |
| CN102504930A (en) * | 2011-10-28 | 2012-06-20 | 连力生 | Spent lubrication oil regeneration device with ultrasonic membrane separator |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104211549A (en) * | 2014-09-04 | 2014-12-17 | 葛洲坝易普力股份有限公司 | Preparation method of mixed-charged emulsion explosive |
| CN106673928A (en) * | 2016-12-21 | 2017-05-17 | 福建海峡科化股份有限公司 | High-temperature sensitized emulsion explosives and preparation method thereof |
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Application publication date: 20140611 |