A kind of sour natural gas mining wastewater treatment method
A technology for mining sewage and treatment methods, applied in mining wastewater treatment, water/sewage treatment, water/sewage multi-stage treatment, etc. High and wide range of effects
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Embodiment 1
[0050] Such as figure 1 As shown in Table 4, take the sulfur-containing natural gas mining sewage whose main components are shown in Table 4 as raw water, add NaOH and Na 2 CO 3 Remove solid waste such as calcium and magnesium, adjust the pH to 11.23, and use a high-pressure pump to control the pressure at 6MPa to pressurize into the DTRO system. The DTRO permeate enters the low-pressure RO system for further desalination. The DTRO concentrate is collected for use, and pumped into the 500L evaporation device. The DTRO concentrated liquid is concentrated by vacuum evaporation, and the boiling point is controlled above 45°C, and the condensed water is collected. When the volume of the concentrated feed liquid is concentrated to 90L, the 90L concentrated feed liquid is transferred to a 100L evaporator to continue vacuum evaporation and concentration, and the boiling point is controlled above 45°C. Concentrate until the salt crystals are precipitated, and dehydrate and dry the sa...
Embodiment 2
[0052] Such as figure 1 As shown in Table 4, take the sulfur-containing natural gas mining sewage whose main components are shown in Table 4 as raw water, add NaOH and Na 2 CO 3 Remove solid waste such as calcium and magnesium, adjust the pH to 11.35, and use a high-pressure pump to control the pressure at 6MPa to pressurize into the DTRO system. The DTRO permeate enters the low-pressure RO system for further desalination. The DTRO concentrate is collected for use, and pumped into the 500L evaporation device. Concentrated liquid, vacuum evaporation and concentration, control the boiling point above 85°C, collect condensed water, when the volume of the concentrated feed liquid is concentrated to 90L, transfer 90L of concentrated feed liquid to a 100L evaporator to continue vacuum evaporation and concentration, control the boiling point above 85°C, concentrate until Salt crystals are precipitated, and the salt slurry is dehydrated and dried. Evaporate the mother liquor to adju...
Embodiment 3
[0054] Such as figure 1 As shown in Table 4, take the sulfur-containing natural gas mining sewage whose main components are shown in Table 4 as raw water, add NaOH and Na 2 CO 3 Remove solid waste such as calcium and magnesium, adjust the pH to 11.23, use a high-pressure pump to control the pressure of 7MPa to pressurize into the DTRO system, and the DTRO permeate will enter the low-pressure RO system for further desalination. Concentrate, vacuum evaporation and concentration, control the boiling point above 45°C, collect condensed water, when the volume of the concentrated feed liquid is concentrated to 90L, transfer 90L of concentrated feed liquid to a 100L evaporator to continue vacuum evaporation and concentration, control the boiling point above 45°C, concentrate until Precipitate salt crystals, dehydrate and dry the salt slurry to obtain salt products. Evaporate the mother liquor to adjust the pH value to 3, and use micro-electrolysis to catalyze the oxidation reaction...
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