Spray roasting hydrochloric acid regeneration method and system for ferric oxide powder with high specific surface area
A high specific surface area, iron oxide powder technology, applied in iron oxide, chemical instruments and methods, iron oxide/iron hydroxide, etc., can solve the problem of low BET value of iron oxide powder, improve BET value and ensure system operation , The effect of stable and controllable concentration
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Embodiment 1
[0042] like figure 2 As shown, the present embodiment relates to a method for regeneration of hydrochloric acid by spray roasting, comprising the steps of:
[0043] (1) Contains FeCl 2 , FeCl 3 、H 2 All the waste acid solution of O directly enters the pre-concentrator 4 to be heated and concentrated, and after being pressurized by the pre-concentrator circulation pump 6 and the roaster feed pump 7 on the roaster feed line 8, it enters the roaster 2 in the form of high-pressure injection. Burn the waste acid at high temperature (burning temperature 650~720°C), and the following chemical reactions occur during the burning process:
[0044] 2FeCl 2 + 2H 2 O + 1 / 2O 2 = Fe 2 o 3 ↓ + 4 HCl ↑;
[0045] 2FeCl 3 + 3 H 2 O = Fe 2 o 3 ↓ + 6 HCl.
[0046] (2) The high-temperature flue gas produced by the above-mentioned roasting furnace 2 enters the pre-concentrator 4, and exchanges heat with the waste acid solution in the pre-concentrator 4 as a high-temperature heat so...
Embodiment 2
[0051] The embodiment of the present invention relates to a spray roasting hydrochloric acid regeneration method of iron oxide powder with high specific surface area, which can at least solve some problems existing in the prior art. This method is basically the same as the steps of the spray roasting hydrochloric acid regeneration method in the above-mentioned embodiment 1, and the specific steps are not repeated here; this method has been improved on the basis of embodiment 1, specifically: image 3 As shown, the waste acid solution is divided into an independent first pipeline 14 and a second pipeline 16 before entering the pre-concentrator 4, and enters the roaster 2 and the pre-concentrator 4 respectively, and the waste acid solution entering the pre-concentrator 4 is heated After being concentrated, it is mixed with the spent acid solution in the first pipeline 14 and enters the roaster 2 . Because a certain amount of unconcentrated spent acid solution has been added thro...
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