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Composite oil phase for emulsified explosive and preparation method of composite oil phase as well as emulsion matrix and emulsified explosive

A technology of emulsified explosives and composite oil phase, which is applied in explosives, non-explosive/non-thermal agent components, offensive equipment, etc. It can solve the problems of poor fluidity at room temperature, low storage stability, and low emulsifying power, and achieve compatibility Good, excellent storage stability, strong emulsifying ability

Active Publication Date: 2019-10-22
北矿亿博(沧州)科技有限责任公司 +2
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The purpose of the present invention is to overcome the disadvantages of low emulsifying power, poor room temperature fluidity and low storage stability of the existing composite oil phase for emulsion explosives, and provide a kind of oil with good room temperature fluidity, adjustable viscosity, low surface tension and strong emulsifying ability. Composite oil phase for emulsion explosive of the present invention, preparation method thereof, emulsion matrix and emulsion explosive

Method used

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  • Composite oil phase for emulsified explosive and preparation method of composite oil phase as well as emulsion matrix and emulsified explosive
  • Composite oil phase for emulsified explosive and preparation method of composite oil phase as well as emulsion matrix and emulsified explosive
  • Composite oil phase for emulsified explosive and preparation method of composite oil phase as well as emulsion matrix and emulsified explosive

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preparation example Construction

[0073] figure 1 is a flowchart illustrating a method of preparing an emulsifier according to the present invention.

[0074] refer to figure 1, according to the present invention, the method of making the above-mentioned emulsifier includes: reacting polyhydric alcohol and fatty acid under the action of a catalyst in an organic solvent (step S1: preparation of polyhydric alcohol fatty acid ester); adding carboxyl modified After the silicone oil has been reacted for a predetermined time, it is filtered and the solvent is removed under reduced pressure (step S2) to obtain an emulsifier.

[0075] In step S1, mix 1-100 parts by weight of polyol, 1-5 parts by weight of catalyst and 1-300 parts by weight of organic solvent, raise the temperature to 100°C-150°C, Then add 1-200 parts by weight of fatty acid dropwise, then continue to heat up to 150°C-180°C, and react for 2 hours-4 hours, so as to obtain a mixture by esterifying polyhydric alcohol and fatty acid. After the reaction ...

Embodiment 1

[0125] Embodiment 1: Preparation of composite oil phase for emulsion explosive

[0126] Heat 4.5 parts by weight of composite wax (purchased from Sinopec Nanyang Paraffin Wax Fine Chemical Factory) to 120°C to melt, then add 60 parts by weight of 46# engine oil, 8 parts by weight of methyl oleate and 25 parts by weight of prepared The silicone emulsifier prepared in Example 1 was stirred at 75°C for 2 hours until uniform, and finally 2.5 parts by weight of zinc stearate was added, stirred and cooled to obtain a composite oil phase for emulsified explosives. The content of each component is shown in Table 3, and the corresponding performance results are shown in Table 4.

Embodiment 2

[0127] Embodiment 2: the preparation of composite oil phase for emulsion explosive

[0128] Heat 2.0 parts by weight of composite wax (purchased from Sinopec Nanyang Paraffin Wax Fine Chemical Factory) to 120°C to melt, then add 60 parts by weight of 46# engine oil, 10 parts by weight of methyl oleate and 25 parts by weight of prepared The silicone emulsifier prepared in Example 2 was stirred at 80°C for 2 hours until uniform, and finally 3.0 parts by weight of zinc stearate was added, stirred and cooled to obtain a composite oil phase for emulsified explosives. The content of each component is shown in Table 3, and the corresponding performance results are shown in Table 4.

[0129] In order to verify better the performance of the composite oil phase according to the emulsion explosive of the present invention, use sorbitan oleate (Span 80) and polyisobutylene succinimide polymer emulsifier (T154) to carry out as emulsifier Compared.

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Abstract

The invention discloses a composite oil phase for emulsified explosive and a preparation method of the composite oil phase as well as an emulsion matrix and the emulsified explosive. The composite oilphase for the emulsified explosive is prepared from the following components in parts by weight: 1 to 30 parts of organosilicon emulsifier, 3 to 60 parts of base oil, 1 to 10 parts of fatty acid ester, 0 to 5 parts of viscosity modifier and 0 to 3 parts of an oil phase stabilizer. According to the composite oil phase for the emulsified explosive, disclosed by the invention, all the components have good compatibility, and the viscosity of the oil phase can be adjusted according to use requirements; in addition, the composite oil phase has the advantages of higher hydrophobicity, high and low temperature resistance and better flowability at normal temperature.

Description

technical field [0001] The invention belongs to the field of emulsified explosive compositions, in particular to a composite oil phase for emulsified explosives, a preparation method thereof, an emulsified matrix and emulsified explosives. Background technique [0002] Emulsion explosive is a W / O industrial explosive prepared by emulsification technology with ammonium nitrate aqueous solution as the dispersed phase and oil phase as the continuous phase. Due to its good water resistance, storage stability and detonation performance in It has been widely recognized at home and abroad, and its output has grown rapidly in recent years. The essence of emulsion explosives is that the ammonium nitrate solution is emulsified by an emulsifier to form internal phase particles, which are tightly wrapped in the oil layer by the oil phase to form a stable emulsion. In actual production, in order to enhance the convenience and safety of production operations, emulsifiers, hydrocarbon fue...

Claims

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Application Information

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IPC IPC(8): C06B23/00
CPCC06B23/00
Inventor 叶辉马平谭本岭崔刚郝会娟王肇中查正清
Owner 北矿亿博(沧州)科技有限责任公司