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Method for preparing high-concentration calcium chloride solution by decomposing ammonium chloride with lime powder

A technology of calcium chloride solution and lime powder, applied in the direction of calcium/strontium/barium chloride, calcium/strontium/barium halide, etc., can solve the problems of waste, large discharge of waste liquid, pollute the environment, etc., and reduce steam The effect of reducing consumption and emissions

Active Publication Date: 2014-04-30
QINGDAO SODA ASH IND DEV CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Ammonia-alkali white mud is mainly produced in the distillation recovery process of ammonia and brine refining process, and the distillation waste liquid is about 9~10m 3 / t of soda ash, about 200~300kg dry base lime mud / t of soda ash is produced, and the waste liquid contains about 10% calcium chloride and about 5% sodium chloride. Due to the large amount of waste liquid discharge, it is difficult to achieve thorough treatment. It pollutes the environment and also leads to the waste of substances such as sodium chloride and calcium chloride
At present, most ammonia-alkali enterprises use the waste liquid recovery method to produce calcium chloride, but this method is to directly evaporate the distillation waste liquid after clarification and purification. Due to the low concentration of calcium chloride (about 10%), the steam consumption is large and the cost is high.

Method used

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  • Method for preparing high-concentration calcium chloride solution by decomposing ammonium chloride with lime powder

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0021] As shown in the flow chart, add 95% ammonium chloride 300kg / h from the ammonium chloride silo 1 and send the lime powder (CaO content 77.32%) 215kg / h from the lime powder silo 2 into the mixing conveying auger 15 for mixing Then enter the first-stage reactor 3, and add 0.24m at the same time 3 The / h light liquid is fully mixed and partially reacted by stirring, the reaction temperature is 89.5 °C, the excess CaO of lime powder in the first-stage reaction liquid is 9.91%, and it is sent to the top of the first-stage distillation tower 7 by the first-stage delivery pump 4 and from the second-stage distillation tower. The mixed gas of the steam of 8 and ammonia is contacted in countercurrent for heat and mass transfer, the temperature of the first-stage distillate overflowing from the bottom of the first-stage distillation tower 7 is 118.1°C, and the first-stage distillate overflows from the bottom of the first-stage distillation tower The second stage reactor 5 reacts fu...

Embodiment 2

[0023] As shown in the flow chart, add 95% ammonium chloride 300kg / h from the ammonium chloride silo 1 and send the lime powder (CaO content 75.76%) 210kg / h from the lime powder silo 2 into the mixing conveying auger 15 for mixing Then enter the first-stage reactor 3, and add 0.25m 3 The / h light liquid is fully mixed and partially reacted by stirring. The reaction temperature is 79.7 ° C. The excess CaO of lime powder in the first-stage reaction liquid is 5.30%. The mixed gas of steam of 8 and ammonia is contacted in countercurrent for heat and mass transfer, the temperature of the first-stage distillate overflowing from the bottom of the first-stage distillation tower 7 is 117.6°C, and the first-stage distillate overflows from the bottom of the first-stage distillation tower The second stage reactor 5 reacts further, in order to ensure the ammonium chloride decomposition reaction, add 7.8kg / h steam in the second stage reactor 5, the temperature is 114.7 ℃. The reaction liqu...

Embodiment 3

[0025] As shown in the flow chart, add 95% ammonium chloride 200kg / h from ammonium chloride silo 1 and send lime powder (CaO content 80.26%) 128kg / h from lime powder silo 2 into the mixing conveyor auger 15 for mixing Then enter the first-stage reactor 3, and add 0.20m 3 The / h light liquid is fully mixed and partially reacted by stirring. The reaction temperature is 70.7 ° C. The excess CaO of lime powder in the first-stage reaction liquid is 3.21%. The mixed gas of 8 steam and ammonia is contacted in countercurrent for heat and mass transfer. The temperature of the first-stage distillate overflowing from the bottom of the first-stage distillation tower 7 is 117.2°C, and the first-stage distillate overflows from the bottom of the first-stage distillation tower to The second stage reactor 5 reacts further, in order to ensure the ammonium chloride decomposition reaction, add 5.4kg / h steam in the second stage reactor 5, the temperature is 100.8 ℃. The reaction liquid in the sec...

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Abstract

The invention discloses a method for preparing high-concentration calcium chloride solution by decomposing ammonium chloride with lime powder. The method is characterized by including steps of mixing wet ammonium chloride in soda production process II with lime powder to feed into a primary reactor, adding light liquid from a light liquid distillation tower for sufficient reaction, subjecting generated primary reaction liquid to ammonia distillation process by a primary distillation tower, subjecting primary distillation liquid overflowing into a secondary reactor for subsequent reaction, and pumping generated secondary reaction liquid for ammonia distillation in a secondary distillation tower, and subjecting the obtained secondary distillation liquid to flash steam distillation to obtain high-concentration calcium chloride solution. The high-concentration calcium chloride solution is fed to a calcium chloride production system by a concentrated-calcium conveying pump, gas discharged by the secondary distillation tower is used as heat source for ammonia distillation of the primary distillation tower, and ammonia gas of the primary distillation tower and the light liquid distillation tower is recovered by an ammonia cooler and fed to an ammonia absorption tower. The method for preparing high-concentration calcium chloride solution has the advantages that concentration of the calcium chloride solution can reach 38% or above, ammonia content is lower than 100mg / L, consumption of 0.5MPa steam for producing double-water calcium chloride per ton is reduced by more than 30% as compared with before, and discharge of dry white-base mud is reduced by about 30% as well.

Description

technical field [0001] The invention relates to a method for preparing high-concentration calcium chloride solution by using lime powder to decompose ammonium chloride. Background technique [0002] As the world's largest soda ash producer, my country's current annual output of soda ash has reached more than 20 million tons. There are three production methods: ammonia soda method, combined soda method and trona method, of which the ammonia soda method accounts for 20~40% of the total output about. Ammonia-alkali white mud is mainly produced in the distillation recovery process of ammonia and brine refining process, and the distillation waste liquid is about 9~10m 3 / t of soda ash, about 200~300kg dry base lime mud / t of soda ash is produced, and the waste liquid contains about 10% calcium chloride and about 5% sodium chloride. Due to the large amount of waste liquid discharge, it is difficult to achieve thorough treatment. Pollution of the environment also leads to the wast...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01F11/24
Inventor 尹小春于英明徐志国丁珊修高山刘晓莉宋焱李家强赵建国牟国宪
Owner QINGDAO SODA ASH IND DEV CO LTD
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