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System for recovering ammonia from rare earth separation waste liquor

A technology for separating waste liquid and recovering ammonia, which is applied in the preparation/separation of ammonia, ammonia compounds, inorganic chemistry, etc. It can solve the problems of high processing cost, environmental pollution, high energy consumption of processing, etc., achieve efficient and thorough recovery, and save steam , the effect of saving energy

Pending Publication Date: 2018-08-31
全南县新资源稀土有限责任公司
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  • Abstract
  • Description
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  • Application Information

AI Technical Summary

Problems solved by technology

A method for reclaiming ammonium chloride as described in the patent application document CN1224694A as the publication number, which obtains ammonium chloride by directly concentrating, evaporating and crystallizing, but this method is because the concentration of ammonium chloride in the waste liquid is low, resulting in The processing cost is high, so it has not been popularized; a kind of recovery method that is recorded in the patent application document CN1504413A as the publication number, it is to add a circulating agent in the ammonium chloride solution, and reclaim ammonia and hydrochloric acid by evaporation, but this method Because the ammoniacal liquor and hydrochloric acid concentration of recovery are too low, useless, so do not obtain industrial application; In addition, the patent document that publication number is CN101475194B also discloses a kind of method that reclaims ammonia from low-concentration ammonium chloride waste water, and this method is Alkaline substances are added to low-concentration ammonium chloride wastewater to generate ammonia water and chloride salts, and then separated and concentrated to obtain valuable ammonia water. This method has been widely used by rare earth separation companies because of its high industrial application value, but Due to the limitations of the current technological process and equipment, this method has the problems of low ammonia yield and high processing energy consumption. The recovery rate of ammonia in this method is only 70.0-80.0%, and the ammonia content in the final discharge is still relatively high. The discharge will still cause certain environmental pollution, and the concentration of ammonia water produced is only 3.0-5.0mol / L, while the steam consumption is ≥1.5 tons / ton of ammonia water
[0004] In view of the above-mentioned problems, it is still difficult to get a better solution under the existing conditions. Therefore, it is urgent to make a breakthrough and improve the recovery process of ammonia in the rare earth industrial waste liquid.

Method used

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  • System for recovering ammonia from rare earth separation waste liquor

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Embodiment 1

[0045] A method for recovering ammonia from rare earth separation waste liquid, such as figure 1 as shown, figure 1 Be the process flow diagram of this embodiment, concrete steps are:

[0046]Step 1, stir evenly; put the ammonium chloride wastewater discharged in the rare earth processing and extraction production with a concentration range of 1.7-2.1mol / L and an acidity range of 0.2-0.3mol / L in the solution pool I1 and stir evenly to obtain the concentration and A solution with a consistent pH.

[0047] Step 2, heating and concentrating; pump the low-concentration ammonium chloride solution obtained in step 1 into the energy-saving concentrator 2 and heat and concentrate it to obtain a high-concentration ammonium chloride solution and place it in the solution pool II3. The concentration of ammonium chloride in the high-concentration ammonium chloride solution is controlled at 3.6mol / L.

[0048] Step 3, replacement reaction; the high-concentration ammonium chloride solution...

Embodiment 2

[0053] A method for recovering ammonia from rare earth separation waste liquid, such as figure 1 as shown, figure 1 Be the process flow diagram of this embodiment, concrete steps are:

[0054] Step 1. Stir evenly; combine ammonium chloride wastewater with a concentration range of 1.8-2.3mol / L and an acidity range of 0.2-2.3mol / L discharged from the rare earth processing and extraction production with a concentration range of 0.4-1.0 discharged from the precipitation production mol / L, neutral to weakly alkaline ammonium chloride wastewater is placed in the solution pool Ⅰ1 and stirred evenly to obtain a solution with the same concentration and pH. The concentration of ammonium chloride wastewater after stirring is 1.9±0.1mol / L , The acidity is 0.3±0.05mol / L.

[0055] Step 2, heating and concentrating; pump the low-concentration ammonium chloride solution obtained in step 1 into the energy-saving concentrator 2 and heat and concentrate it to obtain a high-concentration ammoniu...

Embodiment 3

[0061] A method for recovering ammonia from rare earth separation waste liquid, such as figure 1 as shown, figure 1 Be the process flow diagram of this embodiment, concrete steps are:

[0062] Step 1. Stir evenly; put the ammonium chloride wastewater discharged from the rare earth processing and precipitation production with a concentration range of 0.4-1.0mol / L and a neutral to slightly alkaline acidity in the solution pool I1 and stir evenly to obtain the concentration and pH consistent solution.

[0063] Step 2, heating and concentrating; pump the low-concentration ammonium chloride solution obtained in step 1 into the energy-saving concentrator 2 and heat and concentrate it to obtain a high-concentration ammonium chloride solution and place it in the solution pool II3. The concentration of ammonium chloride in the high-concentration ammonium chloride solution is controlled at 2.6mol / L.

[0064] Step 3, replacement reaction; the high-concentration ammonium chloride solut...

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Abstract

The invention discloses a system for recovering ammonia from rare earth separation waste liquor. The system comprises a solution tank I, an energy-saving concentrator, a solution tank II and other parts, wherein a solution outlet of the solution tank I is connected to a material concentration inlet of the energy-saving concentrator through a pipeline, a material concentration outlet of the energy-saving concentrator is connected to a solution inlet of the solution tank II through the pipeline, and a solution outlet of the solution tank II is connected to a material inlet of a reaction tank through the pipeline. Ammonia is recovered by the system, ammonia recovery rate can be 99.5% or higher, concentration of finally obtained ammonia water reaches 8.0-10.0 mol / L, and recovery is efficient and thorough; meanwhile, according to the method, ammonia nitrogen content of finally discharged wastewater after being treated with the method is smaller than or equal to 5.0 ppm which is far lower than 15.0 ppm specified in national first level discharge standard, and low discharge and low pollution are realized; besides, for operation with the method, only 0.8-1.0 ton of steam is consumed for each ton of the ammonia water, steam needed for the operation is saved greatly, and energy is saved.

Description

technical field [0001] The invention belongs to the field of rare earth separation resource recovery, in particular to a system for recovering ammonia from rare earth separation waste liquid. Background technique [0002] my country is a major producer of rare earths, with an annual output of more than 250,000 tons of rare earths, and a huge amount of mining and processing. In today's rare earth wet separation process, ammonia water saponification and ammonium bicarbonate precipitation are usually used in the rare earth extraction and rare earth precipitation process sections respectively. The ammonia water and ammonium bicarbonate auxiliary materials used in them cause the waste liquid after separation of rare earth elements to contain ammonium chloride, which is rare earth Separation of sources of ammonia nitrogen pollution in waste liquid. The discharge of waste liquid not only causes serious environmental pollution, but also causes a large amount of ammonia to be wasted...

Claims

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Application Information

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IPC IPC(8): C01C1/02
CPCC01C1/022C01C1/026Y02P20/10Y02P20/50
Inventor 樊佐军赵军峰张虎军
Owner 全南县新资源稀土有限责任公司
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