Absorption liquid used for purifying hydrogen phosphide by wet-catalytic oxidation
A technology of wet catalytic oxidation and liquid absorption, applied in chemical instruments and methods, separation of dispersed particles, separation methods, etc., can solve the problems of secondary pollution of phosphorus-containing activated carbon, high reaction temperature, etc., and achieve easy separation and recovery, simple components, easily accessible effects
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Embodiment 1
[0012] Absorption liquid: Weigh 0.3375g CuCl 2 Dissolve in 100mL distilled water, stir well to dissolve, and make 0.025mol / L CuCl 2 Solution, add 0.1mol / L HCl solution, adjust the pH to 4, and obtain the absorption solution.
[0013] Reaction conditions: Take 50mL of the prepared absorption solution and pour it into the bubbling reactor, the pH of the gas composition at the inlet of the reactor 3 1000mg / m 3 , O 2 1% (volume ratio), N 2 As carrier gas, the total gas flow rate is 200mL / min, and the reaction temperature is 50°C.
[0014] Purification effect: Under this condition, the purification efficiency of phosphine in the initial reaction is low, only 32%. As the reaction progresses, the purification efficiency increases, and the purification efficiency reaches 90% in 2 hours, and continues to rise, and the purification efficiency reaches a maximum of 97.53%. Then it gradually decreased, and the purification efficiency was still above 70% at 190 minutes.
Embodiment 2
[0016] Absorption solution: Weigh 0.8g CuSO 4 Dissolve in 100mL distilled water, stir well to dissolve, and make 0.05mol / L CuSO 4 The solution is the obtained absorption liquid.
[0017] Reaction conditions: Take 50mL of the prepared absorption solution and pour it into the bubbling reactor, the pH of the gas composition at the inlet of the reactor 3 900mg / m 3 , O 2 1% (volume ratio), N 2 As carrier gas, the total gas flow rate is 300mL / min, and the reaction temperature is 50°C.
[0018] Purification effect: Under this condition, the initial purification efficiency of phosphine reaches 93.92%. As the reaction progresses, the purification efficiency increases. The concentration of phosphine at the outlet is 0 at 40 minutes, and the 100% purification efficiency drops rapidly after 2 hours. The purification efficiency is above 30%.
Embodiment 3
[0020] Absorbing solution: Weigh 0.376g Cu(NO 3 ) 2 Dissolve in 100mL distilled water, fully stir to dissolve, and make 0.02mol / L Cu(NO 3 ) 2 solution, add 0.1mol / L HNO 3 solution, adjust the pH to 5, and obtain an absorption solution.
[0021] Reaction conditions: Take 50mL of the prepared absorption solution and pour it into the bubbling reactor, the pH of the gas composition at the inlet of the reactor 3 800mg / m 3 , O 2 3% (volume ratio), N 2 As carrier gas, the total gas flow rate is 100 mL / min, and the reaction temperature is 50 °C.
[0022] Purification effect: Under this condition, the initial purification efficiency of phosphine is 46.03%. As the reaction proceeds, the purification efficiency increases rapidly. After 40 minutes, the purification efficiency rises to 94.96%, and the purification efficiency continues to rise, reaching 100% in 80 minutes. The purification efficiency began to decrease after 7 hours, and the purification efficiency dropped to 42.67%...
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