Method for producing site mixed and charged emulsion explosive by utilizing waste engine oil
An emulsion explosive, on-site mixing technology, applied in explosives and other directions, can solve problems such as resource waste and environmental hazards, and achieve the effect of reducing production costs
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Embodiment 1
[0022] 1800 kilograms of water, 7050 kilograms of industrial ammonium nitrate, and 500 kilograms of industrial sodium nitrate are put into the water compatibility tank B1 for stirring and heating in sequence, and heated to 80°C to prepare an aqueous solution for subsequent use;
[0023] The waste oil used needs to be separated from water and filtered to remove water and impurities before use. During implementation, 150 kilograms of emulsifier and 450 kilograms of treated waste oil were put into the oil phase melting tank A1 according to the weight ratio, stirred and heated to 40° C. to prepare an oil phase solution for subsequent use;
[0024] In the foaming agent tank D, a 30% sodium nitrite aqueous solution with a concentration of 50 kg is configured;
[0025] The prepared water phase solution is pumped into the water phase tank B, and the oil phase solution is pumped into the oil phase tank A;
[0026] The water phase and the oil phase are continuously pumped in a ratio of...
Embodiment 2
[0029] In the early stage of implementation, the waste oil was separated from oil and water and filtered to remove moisture and impurities. Its flash point was greater than 210 °C;
[0030] The water of 1800 kilograms, the industrial ammonium nitrate of 7050 kilograms, the industrial sodium nitrate of 500 kilograms are put into the water phase dissolving tank B1 in order and stirred and heated, and heated to 80 ℃ to prepare the aqueous phase solution for subsequent use;
[0031] 170 kilograms of emulsifier and 430 kilograms of treated waste oil were put into oil phase melting tank A1, stirred and heated to 40° C. to prepare an oil phase solution for later use.
[0032] In the foaming agent tank D, configure 50 kg of 30% sodium nitrite aqueous solution;
[0033] The prepared water phase solution is pumped into the water phase tank B, and the oil phase solution is pumped into the oil phase tank A;
[0034] The water phase and the oil phase are continuously pumped in a ratio of ...
Embodiment 3
[0037] In the early stage of implementation, the waste oil was separated from oil and water and filtered to remove moisture and impurities. Its flash point was greater than 210 °C;
[0038] By weight proportioning 1800 kilograms of water, 7050 kilograms of industrial ammonium nitrate, 500 kilograms of industrial sodium nitrate are sequentially put into the water compatibility tank B1 for stirring and heating, heated to 80 ℃ and prepared into an aqueous solution for subsequent use;
[0039] 185 kilograms of emulsifier and 415 kilograms of treated waste oil were put into oil phase melting tank A1, stirred and heated to 40° C. to prepare an oil phase solution for later use.
[0040] In the foaming agent tank D, configure 50 kg of 30% sodium nitrite aqueous solution;
[0041] The prepared water phase solution is pumped into the water phase tank B, and the oil phase solution is pumped into the oil phase tank A;
[0042] The water phase and the oil phase are continuously pumped in ...
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