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Heat energy recovery method for combining heat-process phosphoric acid and polyphosphoric acid micro absorption and device thereof

A thermal phosphoric acid and heat energy recovery technology, which is applied in the steam generation method using heat carrier, phosphoric acid, phosphorus oxyacid, etc. Recycling etc.

Active Publication Date: 2017-09-26
贵州东晟捷能科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] Invention patent CN102910602A double-zone high-efficiency recovery of yellow phosphorus combustion heat energy device proposes a heat energy recovery device similar to a phosphorus-burning boiler, without considering the recovery of high-temperature tail gas heat energy and hydration reaction heat
Therefore, the temperature of the material in the absorption process must be increased, which in turn requires the selection of more expensive equipment materials
For large equipment, material upgrade means increased investment in equipment, which will weaken the benefits of heat recovery

Method used

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  • Heat energy recovery method for combining heat-process phosphoric acid and polyphosphoric acid micro absorption and device thereof
  • Heat energy recovery method for combining heat-process phosphoric acid and polyphosphoric acid micro absorption and device thereof
  • Heat energy recovery method for combining heat-process phosphoric acid and polyphosphoric acid micro absorption and device thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0043]For every ton of phosphorus-containing phosphoric acid or polyphosphoric acid produced, the air quality required for the combustion of the by-product tail gas produced by the electric furnace method is 34 tons, the air quality required for yellow phosphorus combustion is 5 tons, and the air quality for heat recovery is 15 tons. tons, the water quality for heat recovery is 5 tons.

[0044] Used micro-absorption-heat exchanger 2, the hydraulic radius of the reaction plate parallel channel is 0.1mm, the hydraulic radius of the dispersion hole is 0.01mm, the angle between the axis of the dispersion hole and the parallel channel axis is 20°, and the residence time of the material is 0.1s; the heat exchange plate is a cavity with a gap of 0.1mm or a parallel channel with a hydraulic radius of 0.1mm.

Embodiment 2

[0046] For every ton of phosphoric acid or polyphosphoric acid containing phosphorus, the air quality required for the combustion of the by-product tail gas produced by the electric furnace method is 52 tons, the air quality required for yellow phosphorus combustion is 10 tons, and the air quality for heat recovery is 40 tons. tons, the water quality for heat recovery is 30 tons.

[0047] For the micro-absorption-heat exchanger 2 used, the hydraulic radius of the reaction plate parallel channel is 10mm, the hydraulic radius of the dispersion hole is 2mm, the angle between the axis of the dispersion hole and the parallel channel axis is 55°, and the residence time of the material is 5s; The heat exchange plates are cavities with a gap of 10 mm or parallel channels with a hydraulic radius of 10 mm.

Embodiment 3

[0049] For every ton of phosphorus-containing phosphoric acid or polyphosphoric acid produced, the air quality required for the combustion of the by-product tail gas produced by the electric furnace method is 70 tons, the air quality required for yellow phosphorus combustion is 15 tons, and the air quality for heat recovery is 70 tons. tons, the water quality for heat recovery is 50 tons.

[0050] In the micro-absorption-heat exchanger 2 used, the hydraulic radius of the reaction plate parallel channel is 20mm, the hydraulic radius of the dispersion hole is 4mm, the angle between the axis of the dispersion hole and the parallel channel axis is 90°, and the residence time of the material is 10s; The heat exchange plates are cavities with a gap of 20 mm or parallel channels with a hydraulic radius of 20 mm.

[0051] Through the tests of Examples 1, 2, and 3, the above-mentioned test data can all have a relatively good test structure, which meets the production requirements of ph...

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Abstract

The invention discloses a heat energy recovery method for combining heat-process phosphoric acid and polyphosphoric acid micro absorption and a device thereof. According to the method, a micro absorption heat exchanger is used for recovering heat of reaction heat of phosphorus pentoxide and water; the heat of furnace slag is recovered through a furnace slag heat recovery device; the recovered heat of the reaction heat and the heat of the furnace slag are simultaneously connected into an air heat exchanger to prepare hot soft water; the hot soft ware is conveyed to a yellow phosphorus furnace and a phosphorus furnace tail gas boiler through pipelines for overheating steam; through combining the reaction heat, the furnace slag heat, the byproduct tail gas combustion heat and the yellow phosphorus combustion heat, the efficient recovery and utilization of the heat energy is realized. The goals of producing heat-process phosphoric acid or polyphosphoric acid by low energy consumption and recovering the combustion heat of the byproduct tail gas of the yellow phosphorus, the combustion heat of the yellow phosphorus, the reaction heat of phosphorus pentoxide and water, the solidification heat and the sensible heat of the furnace slag at the same time can be achieved; the recovery efficiency is high; the energy sources can be favorably saved; the production cost is effectively reduced.

Description

technical field [0001] The invention relates to a method and a device for micro-absorption combined thermal energy recovery of thermal phosphoric acid and polyphosphoric acid, and belongs to the technical field of low-energy production thermal phosphoric acid or polyphosphoric acid technology and the comprehensive recovery and recovery of heat energy in the production process. Background technique [0002] Phosphoric acid is an important chemical intermediate product, and it is a common raw material for the synthesis of most phosphates and some phosphoric esters and other phosphorus compounds. It is widely used in food, medicine, electronics, petroleum, metallurgy, chemical industry and other industries. According to the production process, The sources of phosphoric acid are wet process phosphoric acid and hot process phosphoric acid. Wet-process phosphoric acid uses strong acid—usually sulfuric acid, but also nitric acid, hydrochloric acid, fluosilicic acid and phosphate ro...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B25/20C01B25/24F22B1/18F22B31/08
CPCC01B25/20C01B25/24F22B1/1807F22B31/08Y02E20/30Y02P20/10Y02P20/129
Inventor 杜强王邵东权晓威
Owner 贵州东晟捷能科技有限公司
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