Method for manufacturing rare earth saponifier using barium sulfide
A technology of saponification agent and barium sulfide, applied in the chemical field, can solve the problems of poor recycling efficiency and low value, and achieve the effect of increasing efficiency
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Embodiment 1
[0024] a. Add 25g of black ash with a BaS content of 60% into hot water at 55°C to 85°C, stir for 15min and filter to prepare 100ml of BaS solution with a concentration of 150g / L. Take 1.5M P 507 Put 330ml into a 500ml reactor, add the above-mentioned BaS solution, stir and react at a temperature of 18-40°C for 10min and statically separate into layers. produced H 2 S gas is introduced into 18ml aqueous solution containing 3.6g NaOH through a catheter with negative pressure for absorption. Separate the stratified barium soap for later use, and heat the water phase at the same time, the released H 2 S gas is also introduced into NaOH solution for absorption.
[0025] b. Take 37ml of rare earth solution with a concentration of 1.6M and PH=1~2 and add the above barium soap P 570 In the medium, the temperature is between 18°C and 40°C, the reaction is stirred for 15 to 20 minutes, the static layer is separated, and the water phase contains BaCl 2 About 36ml, evaporated to d...
Embodiment 2
[0028] a. Slowly add 2.5T black ash with a BaS content of 60% into hot water at a temperature of 55°C-85°C, stir for 50-70min, and the water volume is 9m 3 , filter, wash the filter residue with water, and adjust it to a concentration of 150g / L and a volume of 10m 3 Backup.
[0029] b. Introduce the above-mentioned BaS solution as a barium soap liquid into the grouping production process of rare earth extraction of praseodymium and neodymium, wherein P 507 The concentration of the rare earth solution is 1.47M, the flow rate is 110L / min; the BaS flow rate is 31.2L / min, the concentration of the rare earth solution is 1.6M, the pH=1~2, and the flow rate is 12.4L / min.
[0030] The H produced during barium soap formation 2 S is mixed with a NaOH solution with a concentration of 20% to 30% in a Venturi reactor and sprayed for absorption, and at the same time, the H released by heating its water phase 2 S gas is also absorbed by Venturi reactor to prepare NaHS.
[0031] In the pr...
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