CN103183574A - Composite oil phase for production of ammonium nitrate fuel oil mixture - Google Patents
Composite oil phase for production of ammonium nitrate fuel oil mixture Download PDFInfo
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- CN103183574A CN103183574A CN2013100727488A CN201310072748A CN103183574A CN 103183574 A CN103183574 A CN 103183574A CN 2013100727488 A CN2013100727488 A CN 2013100727488A CN 201310072748 A CN201310072748 A CN 201310072748A CN 103183574 A CN103183574 A CN 103183574A
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- ammonium nitrate
- oil phase
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- fuel oil
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Abstract
The invention discloses a composite oil phase used for the production of an ammonium nitrate fuel oil mixture. The composite oil phase contains 90wt%-95wt% animal oil and 5wt%-10wt% of a surfactant which are mixed together. The composite oil phase is stable in property and low in cost; raw materials are easy to obtain; the ammonium nitrate fuel oil mixture produced by the composite oil phase is stable in property, convenient to store and transport, is suitable for the industrial production, and the explosiveness is improved remarkably.
Description
Technical field
The invention belongs to the industrial explosive field, particularly a kind of compound oil phase for ammonium nitrate-fuel oil mixture production.
Background technology
Ammonium nitrate-fuel oil mixture is because it is simple to operate, production cost is low, obtained using widely, because the present industrial explosive of China is TNT-free explosive, so what research was more aspect ammonium nitrate-fuel oil mixture is that its process aspect is studied, such as CN10150333A, CN101328098A, CN101429081A etc., and fewer to its compound oil phase research, CN101172915A studies its oil phase, because ammonium oils explosive is the mixture of Oxidizing and Reducing Agents, the Oxidizing and Reducing Agents exposure level is relatively low, and it is not very desirable causing its blast performance, seems necessary so the searching suitable oils improves its blast performance.
Existing ammonium oils explosive, comprise that the oil phase material that uses in expanded ammonal, modified ammonium nitrate-fuel oil explosive, porous grain ammonium nitrate-fuel oil mixture and the heavy ammonium oils explosive production all is based on the refining of petroleum product, mainly be diesel oil, paraffin, ceresine etc. are aided with certain additive, such as wood powder etc., perhaps directly carry out the refining of petroleum product composite.Along with petering out of petroleum resources, the cost of refining of petroleum product is more and more higher, causes the oil phase material cost that uses in the present ammonium nitrate-fuel oil mixture too high, and the ammonium nitrate-fuel oil mixture blast performance of making is not very desirable, can not satisfy some solid rock explosion requirements.
Summary of the invention
The object of the present invention is to provide a kind ofly overcome that existing ammonium nitrate-fuel oil mixture oil phase material cost is too high, blast performance is not really desirable, with low cost, superior performance be used for the compound oil phase that ammonium nitrate-fuel oil mixture is produced.
The technical solution that realizes the object of the invention is:
A kind of compound oil phase for ammonium nitrate-fuel oil mixture production contains animal oil 90 ~ 95 wt %, and tensio-active agent 5 ~ 10 wt % make its proportioning sum reach 100% and mix.
The present invention compared with prior art, its remarkable advantage:
Compounded oil phase stable in properties of the present invention, cheap, raw material are easy to get; The ammonium nitrate-fuel oil mixture that uses described compounded oil to produce mutually, stable performance, blast performance has had significant raising, is convenient to store and transportation, is suitable for suitability for industrialized production.
Embodiment
A kind of compound oil phase for ammonium nitrate-fuel oil mixture production of the present invention contains animal oil 90 ~ 95 wt %, and tensio-active agent 5 ~ 10 wt % make its proportioning sum reach 100% and mix.
Described tensio-active agent is this Pan 80.
Described animal oil is one or more mixing animal grease in lard, sheep oil, fish oil, butter or other animal grease.
Embodiment 1
With the lard of 90 wt %, this Pan 80 of 10 wt %, be mixed with compound oil phase.Preparation 5kg ammonium nitrate-fuel oil mixture selects component and proportioning to be: ammonium nitrate 95 wt %, compound oil phase 5 wt %.At first with ammonium nitrate after vacuum puffed, compound oil phase is through heating, temperature is 90 ℃, through fully mixing pack.Density is 0.85g/cm
3, explosion velocity is 3490m/s.
Embodiment 2
With the butter of 95 wt %, this Pan 80 of 5 wt %, be mixed with compound oil phase.Preparation 5kg ammonium nitrate-fuel oil mixture selects component and proportioning to be: ammonium nitrate 95 wt %, compound oil phase 5 wt %.At first with ammonium nitrate after vacuum puffed, compound oil phase is through heating, temperature is 90 ℃, through fully mixing pack.Density is 0.87g/cm
3, explosion velocity is 3520m/s.
Embodiment 3
With the sheep oil of 93 wt %, this Pan 80 of 7 wt %, be mixed with compound oil phase.Preparation 5kg ammonium nitrate-fuel oil mixture selects component and proportioning to be: ammonium nitrate 95 wt %, compound oil phase 5 wt %.At first with ammonium nitrate after vacuum puffed, compound oil phase is through heating, temperature is 90 ℃, through fully mixing pack.Density is 0.87g/cm
3, explosion velocity is 3510m/s.
Embodiment 4
With the fish oil of 95 wt %, this Pan 80 of 5 wt %, be mixed with compound oil phase.Preparation 10kg porous grain ammonium nitrate-fuel oil mixture selects component and proportioning to be: porous grain ammonium nitrate 94 wt %, compound oil phase 6 wt %.Compound oil phase is through heating, and temperature is 90 ℃, and porous grain ammonium nitrate carries out preheating, and the control temperature is mixed the back pack about 45 ℃.Density is 0.90g/cm
3, explosion velocity is 3660m/s.
Embodiment 5
With the sheep oil of 95 wt %, this Pan 80 of 5 wt %, be mixed with compound oil phase.Preparation 10kg ammonium nitrate-fuel oil mixture, select component and proportioning to be: ammonium nitrate 93 wt %, compound oil phase 7 wt %, at first with ammonium nitrate after vacuum puffed, compound oil phase is through heating, temperature is 90 ℃, pulverizes the back and packs through mixing.Density is 0.89g/cm
3, explosion velocity is 3730m/s.
Embodiment 6
With the lard of 93 wt % and the mixing oil of butter, this Pan 80 of 7wt %, be mixed with compound oil phase, lard 50 wt %, butter 50 wt %.Preparation 10kg ammonium nitrate-fuel oil mixture, select component and proportioning to be: ammonium nitrate 93 wt %, compound oil phase 7 wt %, at first with ammonium nitrate after vacuum puffed, compound oil phase is through heating, temperature is 90 ℃, pulverizes the back and packs through mixing.Density is 0.89g/cm
3, explosion velocity is 3780m/s.
Embodiment 7
With the sheep of 93 wt % oil and the mixing oil of fish oil, this Pan 80 of 7wt %, be mixed with compound oil phase, the oily 50 wt % of sheep, fish oil 50 wt %.Preparation 10kg ammonium nitrate-fuel oil mixture, select component and proportioning to be: ammonium nitrate 93 wt %, compound oil phase 7 wt %, at first with ammonium nitrate after vacuum puffed, compound oil phase is through heating, temperature is 90 ℃, pulverizes the back and packs through mixing.Density is 0.89g/cm
3, explosion velocity is 3770m/s.
Claims (3)
1. one kind is used for the compound oil phase that ammonium nitrate-fuel oil mixture is produced, and it is characterized in that contain animal oil 90 ~ 95 wt %, tensio-active agent 5 ~ 10 wt % make its proportioning sum reach 100% and mix.
2. a kind of compound oil phase for ammonium nitrate-fuel oil mixture production according to claim 1 is characterized in that described tensio-active agent is this Pan 80.
3. a kind of compound oil phase for ammonium nitrate-fuel oil mixture production according to claim 1 and 2 is characterized in that, described animal oil is lard, sheep oil, fish oil, butter or one or more mixing animal grease wherein.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013100727488A CN103183574A (en) | 2013-03-07 | 2013-03-07 | Composite oil phase for production of ammonium nitrate fuel oil mixture |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013100727488A CN103183574A (en) | 2013-03-07 | 2013-03-07 | Composite oil phase for production of ammonium nitrate fuel oil mixture |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN103183574A true CN103183574A (en) | 2013-07-03 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2013100727488A Pending CN103183574A (en) | 2013-03-07 | 2013-03-07 | Composite oil phase for production of ammonium nitrate fuel oil mixture |
Country Status (1)
| Country | Link |
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Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1144792A (en) * | 1995-09-05 | 1997-03-12 | 冶金工业部长沙矿冶研究院 | Powdered ammonium nitrate explosive containing stabilizer and its preparing process |
| CN101475424A (en) * | 2009-01-24 | 2009-07-08 | 湖南南岭民用爆破器材股份有限公司 | High power emulsified explosive |
-
2013
- 2013-03-07 CN CN2013100727488A patent/CN103183574A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1144792A (en) * | 1995-09-05 | 1997-03-12 | 冶金工业部长沙矿冶研究院 | Powdered ammonium nitrate explosive containing stabilizer and its preparing process |
| CN101475424A (en) * | 2009-01-24 | 2009-07-08 | 湖南南岭民用爆破器材股份有限公司 | High power emulsified explosive |
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Owner name: INNER MONGOLIA OTOG BANNER SHENG AN JIU ERJIU CHEM Free format text: FORMER OWNER: XU CHANG Effective date: 20150202 |
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Free format text: CORRECT: ADDRESS; FROM: 210009 NANJING, JIANGSU PROVINCE TO: 016064 ORDOS, INNER MONGOLIA AUTONOMOUS REGION |
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Effective date of registration: 20150202 Address after: 016064 the Inner Mongolia Autonomous Region Erdos city Etuokeqi sanbeiyangchang two kilometers east Applicant after: Inner Mongolia Etuoke County Sheng'an No.929 Chemical Co., Ltd. Address before: 210009, Hunan Road building, building 22, building A, Phoenix Square, No. 1, Gulou District, Jiangsu, Nanjing, Jiangsu Applicant before: Xu Chang |
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Application publication date: 20130703 |