CN1158833A - Emulsifier for emulsified explosive and its preparation process - Google Patents
Emulsifier for emulsified explosive and its preparation process Download PDFInfo
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- CN1158833A CN1158833A CN 96100379 CN96100379A CN1158833A CN 1158833 A CN1158833 A CN 1158833A CN 96100379 CN96100379 CN 96100379 CN 96100379 A CN96100379 A CN 96100379A CN 1158833 A CN1158833 A CN 1158833A
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Abstract
Under the action of catalyst, polyhydrocarbon carboxylic acid, acid anhydride or polyol under esterification reaction forms water-in-oil highpolymer emulsifier. The emulsifier has excellent emulsifying property and is suitable for preparing emulsified explosive with high storage stability.
Description
The present invention relates to a kind of emulsifying agent that is used for emulsion explosive and preparation method thereof.
Emulsion explosive mainly is made up of aqueous inorganic oxidizer salt solution, oil phase material and emulsifying agent, and the effect by emulsifying agent makes the oil phase material that is lower than 10w% with the aqueous inorganic oxidizer salt solution emulsification more than the 90w%, forms the emulsifying base of water-in-oil (W/O).Its emulsified particle is polyhedral structure, and is extremely unstable on the thermodynamics, and desire improves its stability must make the emulsifying agent molecule closely arrange its emulsifying film intensity of enhancing, so emulsifying agent is the major cause that influences the emulsion explosive stability in storage.
Emulsifying agent is of a great variety, and emulsifying agent commonly used in emulsion explosive production can be divided into two classes, promptly low molecule emulsifying agent and macromolecule emulsifier.Low molecule emulsifying agent is representative with SP-80.A lot of in the past patents are reported to this.It is that emulsifying agent prepares emulsion explosive that EP0142916 proposes with SP-80, and the compactness of the emulsifying film of its formation and film toughness are all very poor, so stability is very low.For improving emulsifying stability, EP0305104, EP0317221, USP4470855 propose to add emulsion stabilizers such as Zinic stearas, lecithin respectively, USP4482403 proposition SP-80 and sorbitol ester are composite, but because it is low-molecular material, the emulsifying film intensity that forms is very low, does not fundamentally solve the problem of emulsion explosive stability in storage.It is to grow up in recent years that macromolecule emulsifier is used for emulsion explosive production, USP4708753, USP4828633, GB2216128 all proposes carboxylic acid and the polyamine compounds prepared in reaction succimide class emulsifying agent with the replacement of polymer alkyl, because it has macromolecular structure, thereby emulsification film strength and snappiness have been improved greatly, but it is sterically hindered bigger, and hydrophilic radical is few, so emulsifying power is lower, required stirring intensity is higher, must under continuous production line or higher rotation speed, could form the good emulsifying state, in addition, such emulsifying agent high temperature easily decomposes generation ammonia and carbonic acid gas, have certain detonation susceptibility with this process of dynamite substrate for preparing, reduced the safety coefficient of emulsion explosive production.
The object of the present invention is to provide a kind of easy emulsification, be difficult for decomposing, emulsifying stability does not well contain the ester family macromolecule emulsifying agent of succimide group.Another object of the present invention provides a kind of method for preparing macromolecule emulsifier, directly carry out esterification with polyol and poly-hydrocarbon carboxylic acids or acid anhydrides, the hydrophilic radical that increases the emulsifying agent molecule makes emulsifying agent of the present invention possess good emulsifying performance and emulsifying stability simultaneously to improve its emulsifying property.
Consisting of of emulsifying agent of the present invention:
N=1-3 wherein
R
1Be C
50--C
100Alkyl,
R
2, R
3For-CH
2CH
2-or-CH
2CH
2-(OCH
2CH
2) m-m=1-5 or
Or
Each component content is respectively (I) 30w%-60w%, (II) 20w%-60w%, (III) 10w%-40w%, (IV) 10w%-40w%, (V) the poly-hydrocarbon carboxylic acids of 0.05w%-2w% or acid anhydrides and/or polyol.
The preparation method of emulsifying agent of the present invention: in reaction vessel, add poly-hydrocarbon carboxylic acids of reactant or acid anhydrides 60w%-98w%, be preferably 80w%-90w%; Reactant polyol 1w%-40w% is preferably 10w%-20w%.And adding concentration is that 20w%-50w% is preferably the NaOH of 25w%-35w% or KOH aqueous solution 0.05w%-1.5w% is preferably 0.5w%-1.0w% and defoamer 0.01w%-0.5w% is preferably 0.05w%-0.1w%, 100-250 ℃ be preferably 150-200 ℃ and-0.02MPa--0.10MPa is preferably-condition of 0.04MPa--0.08MPa under reaction 2-10 hour, preferably 3--8 hour.
Carboxylic acid or acid anhydrides that the poly-alkyl of reactant replaces, preferably di-carboxylic acid or acid anhydrides can be selected toxilic acid, maleic anhydride, fumaric acid, pentanedioic acid, hexanodioic acid for use, preferably select maleic anhydride for use.
The carboxylic acid that the poly-alkyl of reactant replaces or the substituent carbonatoms of acid anhydrides are at least 50, preferably select polyisobutene for use, and its number-average molecular weight can be selected 700-2500 for use, selects for use 800-1500 better.
The carboxylic acid that the poly-alkyl of reactant replaces is preferably selected the polyisobutenyl maleic anhydride for use, and its saponification value can be selected 50-109mgKOH/g for use, preferably selects 60-90mgKOH/g for use.
The polyisobutenyl maleic anhydride is to utilize the C4 fraction to make polyisobutene under the effect of lewis acid catalyst, mixes at a certain temperature with maleic anhydride and feed chlorine reaction simultaneously to make product.Referring to GB-1162436, this patent is not discussed in detail.
The reactant polyol is one or more polyol, and its hydroxyl value is at least 2.
The reactant polyol comprises HO-(CH
2CH
2O) n-H n=1-6 wherein, best n=2-3, trolamine, glycerine.
The defoamer that reacts used can be selected polyethers or silicone oil defoamer for use, preferably selects the silicone oil defoamer for use.
Emulsifying agent of the present invention has well emulsify performance and emulsifying stability, has good detonation property and stability in storage with the emulsion explosive of its preparation, and emulsification condition is mild.In addition, emulsifying agent of the present invention does not contain diimide group, and is at high temperature more stable, can not decompose generation gas, and the process of dynamite substrate sensitivity of preparation is lower, so better with the emulsion explosive production security of emulsifying agent preparation of the present invention.In addition, emulsifying agent preparation method of the present invention is simple, and raw material is easy to get, and need not reaction process is carried out precision control.
Below by specific examples the present invention is described.
Example 1
With the 200.6g saponification value is that polyisobutenyl maleic anhydride (Mn=978) the 21.0g glycol ether of 68.5mgKOH/g and 2g30%NaOH solution mix, and adds the 0.14g silicon oil foam killer. heat and vacuumize, reaction finished in 3 hours under 200 ℃-0.08MPa.Product property sees Table 1.
Example 2
With the 200.6g saponification value is polyisobutenyl maleic anhydride (Mn=930), 30.0g triglycol and the mixing of 1.5g30%NaOH solution of 75.5mgKOH/g, adds the 0.14g silicon oil foam killer.Heating also vacuumizes, and 150 ℃-0.06MPa reaction 5 hours, product property saw Table 1.
Example 3
With the 300g saponification value is alpha-olefin fumaric acid (Mn=902), 20g glycerine and the mixing of 1.5g30%NaOH solution of 85.5mgKOH/g, adds the 0.14g silicon oil foam killer.Heating also vacuumizes, and finishes in 4 hours in 250 ℃-0.04MP reaction, and product property sees Table 1.
Example 4
With the 300g saponification value is polyisobutenyl maleic anhydride (Mn=998), 10.0g trolamine, 15g glycol ether and the mixing of 2.0g30%NaOH solution of 70.5mgKOH/g, adds the 0.14g silicon oil foam killer.Heating also vacuumizes, and finishes in 8 hours in 100 ℃-0.08MP reaction, and product property sees Table 1.
Table 1. examples preparation emulsifying agent performance
Emulsifying agent of the present invention as can be seen from Table 1 has higher viscosity and hydroxyl value, and acid number is also lower, is suitable for preparing the emulsion explosive of high storage stability.
| Kinematic viscosity (100 ℃ of mm 2/s) | Saponification value (mgKOH/g) | Acid number (mgKOH/g) | Hydroxyl value (mgKOH/g) | |
| Example 1 | ????2105.6 | ????60.5 | ????15.6 | ????98.7 |
| Example 2 | ????1700.5 | ????68.8 | ????16.7 | ????105.8 |
| Example 3 | ????2215.1 | ????62.3 | ????13.2 | ????112.6 |
| Example 4 | ????2463.5 | ????63.2 | ????12.9 | ????96.7 |
Emulsifying agent of the present invention is pressed the preparation test that surface compositions carries out emulsion explosive respectively under 800 rev/mins, 1700 rev/mins, 2900 rev/mins rotating speed.The results are shown in Table 2.Not only be suitable for high rotating speed by data emulsifying agent more of the present invention, and the emulsion explosive for preparing still has good blast performance and stability under middle and slow speed of revolution.The sensitivity of the emulsifying base of emulsifying agent preparation of the present invention in addition is lower, and security is better.
Preparation of emulsifying explosive: ammonium nitrate 66
SODIUMNITRATE 15
Water 12
Compound wax 4.5
Emulsifying agent 2
Help emulsion * 0.5
Perlite 4
Annotate: the emulsion that helps of explosive 1, explosive 2, explosive 3, explosive 4, relatively 1 employing is the AS agent, and the emulsion that helps that comparative example 2 adopts is Yelkin TTS.
The explosive property test of table 2. emulsifying agent
| Explosive 1 | Explosive 2 | Explosive 3 | Explosive 4 | Compare 1 | Compare 2 | ||
| Emulsifying agent | Example 1 | Example 2 | Example 3 | Example 4 | T-152 | SP-80 | |
| Induced detonation (mm) | 800 rev/mins | ??30 | 30 | ???30 | ????30 | ??20 | ??40 |
| 1700 rev/mins | ??50 | 50 | ???50 | ????50 | ??30 | ??50 | |
| 2900 rev/mins | ??70 | 80 | ???80 | ????80 | ??80 | ??70 | |
| Emulsifying base sensitivity (mm) * 1 | 800 rev/mins | Miss-fire | Miss-fire | Miss-fire | Miss-fire | Miss-fire | Miss-fire |
| 1700 rev/mins | ??200 | 200 | ???200 | ???200 | ??150 | ??200 | |
| 2900 rev/mins | ??150 | 150 | ???150 | ???150 | ??80 | ??120 | |
| The high cold cycle of explosive (individual) * 2 (50 ℃ of 8h/-25 ℃ 16h) | 800 rev/mins | ??10 | 9 | ???11 | ???10 | ??5 | ??5 |
| 1700 rev/mins | ??35 | 34 | ???35 | ???33 | ??18 | ??8 | |
| 2900 rev/mins | ??43 | 40 | ???44 | ???46 | ??45 | ??10 |
Annotate: T-152 is a succimide family macromolecule emulsifying agent, and Lanzhou refinery head factory additive subsidiary factory produces.
SP-80 is a dehydrating sorbitol monooleate, and experiment chemical plant, Yantai produces.
* 1. process of dynamite substrate sensitivity are to be represented by the critical diameter of the process of dynamite substrate of 8# blasting cap initiation under 100 ℃ condition.Critical diameter represents that greatly then the sensitivity of process of dynamite substrate is more little, and security is good more, and vice versa.
* the high cold cycle of 2. emulsion explosives is a main method estimating the emulsion explosive stability in storage, and the high more stability in storage of then representing of cycle number is good more.
Claims (13)
1. macromolecule emulsifier that is used for emulsion explosive is characterized in that consisting of:
N=1-3 wherein
R
1Be C
50--C
100Alkyl,
R
2, R
3For-CH
2CH
2-or-CH
2CH
2-(OCH
2CH
2) m-m=1-5 or
Or
Each component content is respectively (I) 30w%-60w%, (II) 20w%-60w%, (III) 10w%-40w%, (IV) 10w%-40w%, (V) the poly-hydrocarbon carboxylic acids of 0.05w%-2w% or acid anhydrides and/or polyol.
2. preparation method of emulsifying agent according to claim 1, it is characterized in that in reaction vessel, adding poly-hydrocarbon carboxylic acids of reactant or acid anhydrides 60w%-98w%, reactant polyol 1w%-40w%, and to add concentration be the NaOH of 20w%-50w% or the defoamer of KOH aqueous solution 0.05w%-1.5w% and 0.05w%-0.5w%, 100-250 ℃ and-the 0.02MPa--0.10MPa condition under reaction 2-10 hour.
3. by the described method of claim 2, it is characterized in that poly-hydrocarbon carboxylic acids of reactant or acid anhydrides 80w%-90w%, reactant polyol 10w%-20w%, and to add concentration be the NaOH of 25w%-35w% or the defoamer of KOH aqueous solution 0.5w%-1.0w% and 0.05w%-0.1w%, 150-200 ℃ and-the 0.04MPa--0.08MPa condition under reaction 3-8 hour.
4. by claim 2 or 3 described methods, it is characterized in that di-carboxylic acid or acid anhydrides that poly-hydrocarbon carboxylic acids of reactant or acid anhydrides replace for one or more alkyl.
5. by claim 2 or 3 described methods, it is characterized in that poly-hydrocarbon carboxylic acids of reactant or acid anhydrides are carboxylic acid or the acid anhydrides that polyisobutene replaces.
6. by claim 2 or 3 described methods, it is characterized in that reactant gathers hydrocarbon carboxylic acids or acid anhydrides is selected toxilic acid, maleic anhydride, fumaric acid, pentanedioic acid, hexanodioic acid for use.
7. by claim 2 or 3 described methods, it is characterized in that poly-hydrocarbon carboxylic acids of reactant or acid anhydrides are maleic anhydrides.
8. by the described method of claim 7, it is characterized in that poly-hydrocarbon carboxylic acids of reactant or acid anhydrides are the polyisobutenyl maleic anhydrides, its saponification value is 50-109mgKOH/g.
9. by the described method of claim 8, it is characterized in that poly-hydrocarbon carboxylic acids of reactant or acid anhydrides are the polyisobutenyl maleic anhydrides, its saponification value is 60-90mgKOH/g.
10. by claim 2 or 3 described methods, it is characterized in that the reactant polyol, contain 2 hydroxyls at least.
11., it is characterized in that the reactant polyol is trolamine, glycerine, HO-(CH by claim 2 or 3 described methods
2CH
2-O) n-H n=1-6 wherein.
12., it is characterized in that the reactant polyol is trolamine, glycerine, HO-(CH by claim 2 or 3 described methods
2CH
2-O) n-H n=2-3 wherein.
13., it is characterized in that used defoamer is polyethers or silicon oil foam killer by claim 2 or 3 described methods.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN96100379A CN1067039C (en) | 1996-01-17 | 1996-01-17 | Emulsifier for emulsified explosive and its preparation process |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN96100379A CN1067039C (en) | 1996-01-17 | 1996-01-17 | Emulsifier for emulsified explosive and its preparation process |
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| Publication Number | Publication Date |
|---|---|
| CN1158833A true CN1158833A (en) | 1997-09-10 |
| CN1067039C CN1067039C (en) | 2001-06-13 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN96100379A Expired - Lifetime CN1067039C (en) | 1996-01-17 | 1996-01-17 | Emulsifier for emulsified explosive and its preparation process |
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| Country | Link |
|---|---|
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Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101152992B (en) * | 2006-09-29 | 2011-05-04 | 鞍钢集团矿业公司 | Emulsifying blasting agent produced on blasting agent mixing vehicle |
| CN101152993B (en) * | 2006-09-29 | 2011-08-17 | 鞍钢集团矿业公司 | Emulsifying agent for emulsification blasting agent mixing vehicle and synthesizing method thereof |
| CN102424516A (en) * | 2011-09-26 | 2012-04-25 | 江西省安全生产科学技术研究中心 | Desensitizing agent for reducing mechanical sensitivity of pyrotechnic composition |
| CN102584502A (en) * | 2012-01-12 | 2012-07-18 | 南京理工大学 | Method for preparing macromolecular emulsifying agent |
| CN102675006A (en) * | 2012-06-11 | 2012-09-19 | 江南大学 | Emulsifier for emulsion explosive and preparation method for emulsifier |
| CN102976877A (en) * | 2012-12-24 | 2013-03-20 | 江南大学 | Novel emulsifier for emulsion explosive and preparation method of novel emulsifier |
| CN103755503A (en) * | 2014-01-23 | 2014-04-30 | 葛洲坝易普力股份有限公司 | Polymer emulsifier for mixed emulsified explosive and preparation method of polymer emulsifier |
| CN104610482A (en) * | 2015-02-09 | 2015-05-13 | 巴彦淖尔盛安化工有限责任公司乌拉特中旗分公司 | Method for preparing polyisobutene maleic anhydride tripropamol amine ester |
| CN105272784A (en) * | 2015-07-23 | 2016-01-27 | 浏阳金科新材料有限公司 | Composite oil phase for preparing bulk emulsion explosive for upward hole package |
| CN106045797A (en) * | 2016-05-24 | 2016-10-26 | 江南大学 | Emulsifying agent for emulsion explosive, and preparation method thereof |
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Families Citing this family (1)
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| CN102718613B (en) * | 2012-07-03 | 2014-09-03 | 保利民爆济南科技有限公司 | Half-esterification high polymer emulsifying agent for industrial explosives |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA1162744A (en) * | 1982-02-02 | 1984-02-28 | Howard A. Bampfield | Emulsion explosive compositions and method of preparation |
| US4931110A (en) * | 1989-03-03 | 1990-06-05 | Ireco Incorporated | Emulsion explosives containing a polymeric emulsifier |
-
1996
- 1996-01-17 CN CN96100379A patent/CN1067039C/en not_active Expired - Lifetime
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| CN101152992B (en) * | 2006-09-29 | 2011-05-04 | 鞍钢集团矿业公司 | Emulsifying blasting agent produced on blasting agent mixing vehicle |
| CN102424516B (en) * | 2011-09-26 | 2013-06-05 | 江西省安全生产科学技术研究中心 | Desensitizing agent for reducing mechanical sensitivity of pyrotechnic mixture |
| CN102424516A (en) * | 2011-09-26 | 2012-04-25 | 江西省安全生产科学技术研究中心 | Desensitizing agent for reducing mechanical sensitivity of pyrotechnic composition |
| CN102584502A (en) * | 2012-01-12 | 2012-07-18 | 南京理工大学 | Method for preparing macromolecular emulsifying agent |
| CN102584502B (en) * | 2012-01-12 | 2014-06-04 | 南京理工大学 | Method for preparing macromolecular emulsifying agent |
| CN102675006A (en) * | 2012-06-11 | 2012-09-19 | 江南大学 | Emulsifier for emulsion explosive and preparation method for emulsifier |
| CN102675006B (en) * | 2012-06-11 | 2016-03-02 | 江南大学 | A kind of emulsifier for emulsion explosive and preparation method thereof |
| CN102976877A (en) * | 2012-12-24 | 2013-03-20 | 江南大学 | Novel emulsifier for emulsion explosive and preparation method of novel emulsifier |
| CN102976877B (en) * | 2012-12-24 | 2015-08-05 | 江南大学 | A kind of emulsifier for emulsion explosive and preparation method thereof |
| CN103755503A (en) * | 2014-01-23 | 2014-04-30 | 葛洲坝易普力股份有限公司 | Polymer emulsifier for mixed emulsified explosive and preparation method of polymer emulsifier |
| CN103755503B (en) * | 2014-01-23 | 2016-03-30 | 葛洲坝易普力股份有限公司 | A kind of the mixed loading emulsion explosive macromolecule emulsifier and preparation method thereof |
| CN104610482A (en) * | 2015-02-09 | 2015-05-13 | 巴彦淖尔盛安化工有限责任公司乌拉特中旗分公司 | Method for preparing polyisobutene maleic anhydride tripropamol amine ester |
| CN105272784A (en) * | 2015-07-23 | 2016-01-27 | 浏阳金科新材料有限公司 | Composite oil phase for preparing bulk emulsion explosive for upward hole package |
| CN105272784B (en) * | 2015-07-23 | 2017-09-01 | 浏阳金科新材料有限公司 | A kind of composite oil phase for being used to prepare the bulk emulsifying explosive of upward hole powder charge |
| CN106045797A (en) * | 2016-05-24 | 2016-10-26 | 江南大学 | Emulsifying agent for emulsion explosive, and preparation method thereof |
| CN108191997A (en) * | 2018-01-18 | 2018-06-22 | 广州崇轩信息科技有限公司 | A kind of emulsifier and preparation method thereof |
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Owner name: CHINA PETROCHEMICAL CORPORATION; CHINA PETROLEUM & Free format text: FORMER NAME OR ADDRESS: CHINA PETRO-CHEMICAL CORP.; FUSHUN PETROCHEMICAL INSTITUTE., CHINA PETROCHEMICAL CORP. |
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Patentee after: China Petrochemical Group Corp. Patentee after: Sinopec Group Fushun Research Institute of Petroleum and Petrochemicals Patentee before: China Petrochemical Corporation Patentee before: Fushun Research Inst. of Petroleum Processing, China Petro-chem. Corp. |
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