Integrated technology for capturing and mineralizing carbon dioxide
A carbon dioxide and process technology, applied in the field of carbon dioxide capture and mineralization integrated process, can solve the problems of low recycling rate, large energy consumption, high energy consumption for regeneration, and achieve the goal of reducing use, reducing water consumption and high leaching rate. Effect
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Embodiment 1
[0023] An integrated process of carbon dioxide capture and mineralization, comprising the following steps:
[0024] In the first step, the ore or other bulk solid waste rich in calcium and magnesium ions is crushed into solid particles with a particle size of less than 1mm by a pulverizer, and then ground by a ball mill to a mineral powder of less than 75μm. The ore is serpentine. Solid waste for fly ash;
[0025] In the second step, the ore powder is mixed with ammonium bisulfate (NH 4 HSO 4 ) solution reaction, the solid-liquid ratio of the feed is 50g / l, the corresponding NH 4 HSO 4 Solution molarity according to NH 4 HSO 4 The molar ratio of magnesium ions in the ore is 1.4:1. The reaction conditions for ore leaching are 100 ℃, the water vapor pressure is 1 bar, the stirring rate is 800-1200 rpm, and the reaction time is 1 hour. The mud obtained after dissolving the ore is passed through a hydrocyclone or The sedimentation tank realizes solid-liquid separation, and t...
Embodiment 2
[0032] An integrated process of carbon dioxide capture and mineralization, comprising the following steps:
[0033] In the first step, the ore or other bulk solid waste rich in calcium and magnesium ions is crushed into solid particles with a particle size of less than 1.5mm by a pulverizer, and then ground by a ball mill to a mineral powder of less than 150μm. The ore is olivine, and the solid waste For steel slag;
[0034] In the second step, the ore powder is mixed with ammonium bisulfate (NH 4 HSO 4 ) solution reaction, the solid-liquid ratio of the feed is 100g / l, and the corresponding NH 4 HSO 4 Solution molarity according to NH 4 HSO 4 The molar ratio of magnesium ions in the ore is 1.2:1. The reaction conditions for ore leaching are 135°, water vapor pressure 3bar, stirring speed 800-1200rpm, reaction time 1 hour, and the mud obtained after dissolving the ore passes through the hydrocyclone Or the sedimentation tank realizes solid-liquid separation, and the separ...
Embodiment 3
[0041] An integrated process of carbon dioxide capture and mineralization, comprising the following steps:
[0042] In the first step, the ore or other bulk solid waste rich in calcium and magnesium ions is crushed into solid particles with a particle size of 2 mm, and then ground to 300 μm ore powder by a ball mill. The ore is serpentine, and the solid waste is steel slag ;
[0043] In the second step, the ore powder is mixed with ammonium bisulfate (NH 4 HSO 4 ) solution reaction, the solid-liquid ratio of the feed is 150g / l, and the corresponding NH 4 HSO 4 Solution molarity according to NH 4 HSO 4 The molar ratio of magnesium ions in the ore is 1:1. The reaction conditions for ore leaching are 150°, water vapor pressure 4bar, stirring speed 800-1200rpm, reaction time 1 hour, and the mud obtained after dissolving the ore passes through the hydrocyclone Or the sedimentation tank realizes solid-liquid separation, and the separated tailings are coarse silicon powder with...
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