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New technology of applying double-effect forced circulation concentration method in production of ammonium phosphate

A technology of forced circulation and production process, which is applied in the direction of phosphate, phosphorus oxyacid, etc., can solve the problems of multiple heating steps, complicated heating environment, difficult control of supersaturation changes, and short equipment operation cycle, so as to achieve the increase of equipment operation cycle , reduce the number and height of equipment used, and significantly increase production capacity

Inactive Publication Date: 2012-08-22
GANSU WENGFU CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, the domestic production methods of ammonium phosphate are mainly the traditional method and the slurry method. During the concentration process of these two production methods, there are many heating steps and the heating environment is complicated, and it is not easy to control the temperature. The more the temperature changes during production, the more the supersaturation changes. The more difficult it is to control, a large number of tiny crystal nuclei will easily form a scale layer on the tube wall, thereby blocking the heat exchange tubes, resulting in a short operating cycle of the equipment during the production process and requiring frequent maintenance
Cause a lot of waste of manpower and material resources, virtually increase the production cost

Method used

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  • New technology of applying double-effect forced circulation concentration method in production of ammonium phosphate
  • New technology of applying double-effect forced circulation concentration method in production of ammonium phosphate
  • New technology of applying double-effect forced circulation concentration method in production of ammonium phosphate

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0023] Such as figure 1 Shown is a two-effect forced circulation concentration method applied to the new process of ammonium phosphate production:

[0024] a. dilute phosphoric acid (P 2 o 5 Content 23%) is forced to circulate between heater 1 and flash chamber 2, dilute phosphoric acid is heated to 70°C for flash evaporation, the gas-liquid phase is separated in the flash chamber, and the P in the liquid phase phosphoric acid is 2 o 5 Enter the reaction chamber 3 after the content is raised to 29%;

[0025] b. P in reaction chamber 3 2 o 5 Phosphoric acid with a content of 29% reacts with ammonia gas to form a monoammonium phosphate slurry with a neutralization degree of 1.02; the generated reaction heat concentrates the monoammonium phosphate slurry, making the monoammonium phosphate slurry P 2 o 5 content rose to 31%;

[0026] c. The 31% monoammonium phosphate slurry is forced to circulate between the heater 4 and the flash chamber 5 at a heating temperature of 1...

Embodiment 2

[0030] Such as figure 1 Shown is a two-effect forced circulation concentration method applied to the new process of ammonium phosphate production:

[0031] a. dilute phosphoric acid (P 2 o 5 Content 25%) is forced to circulate between the heater 1 and the flash chamber 2, dilute phosphoric acid is heated to 74°C for flash evaporation, the gas-liquid phase is separated in the flash chamber, and the P in the liquid phase phosphoric acid is 2 o 5 Enter the reaction chamber 3 after the content is raised to 27%;

[0032] b. P in reaction chamber 3 2 o 5 Phosphoric acid with a content of 27% reacts with ammonia gas to form a monoammonium phosphate slurry with a neutralization degree of 1.01; the generated reaction heat concentrates the monoammonium phosphate slurry, making the monoammonium phosphate slurry P 2 o 5 content rose to 34%;

[0033] c. The 34% monoammonium phosphate slurry is forced to circulate between the heater 4 and the flash chamber 5 at a heating temperat...

Embodiment 3

[0037] Such as figure 1 Shown is a two-effect forced circulation concentration method applied to the new process of ammonium phosphate production:

[0038] a. dilute phosphoric acid (P 2 o 5 Content 24%) is forced to circulate between the heater 1 and the flash chamber 2, dilute phosphoric acid is heated to 72°C for flash evaporation, the gas-liquid phase is separated in the flash chamber, and the P in the liquid phase phosphoric acid is 2 o 5 After the content is increased to 30%, it enters the reaction chamber 3;

[0039] b. P in reaction chamber 3 2 o 5 Phosphoric acid with a content of 30% and slag acid in the concentration section (P 2 o 5 content of 37%) and react with gas ammonia to form a monoammonium phosphate slurry with a neutralization degree of 0.99; the generated reaction heat concentrates the monoammonium phosphate slurry, increasing the P2O5 content of the monoammonium phosphate slurry to 32%;

[0040] c. The 32% monoammonium phosphate slurry is forc...

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Abstract

The invention provides a new technology of applying the double-effect forced circulation concentration method in the production of ammonium phosphate, which comprises the steps of carrying out double-effect forced circulation flash distillation on phosphoric acid slurry, removing excess moisture in the phosphoric acid slurry and reacting with neutralizing slurry so as to generate intermediate slurry, enabling the intermediate slurry to be reacted with ammonia gas to generate a product, carrying out one-effect forced circulation flash distillation on the product slurry, further preparing qualified monoammonium phosphate slurry, drying and granulating by a fluid bed, packaging and weighing. Heat quantity generated by neutralization reaction is taken as a one-effect flash distillation heat source, and the excess heat in the one-effect flash distillation process is taken as a double-effect flash distillation heat source. With the adoption of the new technology, the heating steps in the production process are reduced, the quantity and height of devices used are decreased, heat energy is used reasonably, and energy consumption is reduced. The temperature difference between an inlet and an outlet of a heater is only 1-3 DEG C, degree of supersaturation can be controlled effectively, and scaling of the pipe wall of a heat exchanger is reduced. The forced circulation can enable the circulation speed of liquid phase to improve greatly, wash the wall pipe, and play an important role in reducing the scaling. The cycle of operation of a device is increased greatly, productive capacity is improved obviously, and the production cost is reduced effectively.

Description

technical field [0001] The invention relates to a process for producing ammonium phosphate, in particular to a new process in which a two-effect forced circulation concentration method is applied to produce ammonium phosphate. Background technique [0002] The degree of supersaturation is the driving force for the crystallization of the solute from the solution. The higher the degree of supersaturation, the faster the formation of crystal nuclei. At present, the domestic production methods of ammonium phosphate are mainly the traditional method and the slurry method. During the concentration process of these two production methods, there are many heating steps and the heating environment is complicated, and it is not easy to control the temperature. The more the temperature changes during production, the more the supersaturation changes. The more difficult it is to control, a large number of tiny crystal nuclei will easily form a scale layer on the tube wall, thereby blockin...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B25/28
Inventor 高源张胜葛洪均杨瑞山
Owner GANSU WENGFU CHEM
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