Preparation method for polyphosphoric acid

A polyphosphoric acid and dilute phosphoric acid technology, applied in the field of phosphorus chemical industry, can solve the problems of high production energy consumption, small mass transfer and heat transfer, easy pressure fluctuation, etc. The effect of production accidents

Active Publication Date: 2014-06-04
绵阳启明星磷化工有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The above-mentioned method for preparing polyphosphoric acid has the following disadvantages: 1, the mixed acid solution of phosphoric acid and phosphorus pentoxide has a high viscosity, which easily causes blockage in the graphite tube, further causing production accidents; 2, the acid solution is heated in the heat exchange tube , the heat is transferred from the wall of the heat exchange tube to the center of the heat exchange tube. Due to the high viscosity of the hot acid liquid, the mass transfer and heat transfer inside the acid liquid are particularly small, so that part of the acid liquid close to the heat exchange tube wall is prone to polymerization, and the obtained Polyphosphoric acid, and part of the

Method used

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  • Preparation method for polyphosphoric acid
  • Preparation method for polyphosphoric acid
  • Preparation method for polyphosphoric acid

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0041] Such as figure 1 As shown, the device for realizing the method for preparing polyphosphoric acid in this embodiment includes a heater 2, a separator 3 and a concentrated acid tank 6, and the inside of the separator 3 is communicated with the vacuum constant pressure device 4; as figure 2 As shown, the heater 2 includes a heat exchange tube 21 and a heat ventilation area, the heat exchange tube 21 is a graphite tube, and the outer wall of the graphite tube is provided with an anti-oxidation coating, and the anti-oxidation coating does not react with the high-temperature flue gas; There is an insulation layer 22 outside the ventilation area, and the heat exchange tube 21 is located in the heat ventilation area; the heat exchange tube 21 is coiled in an S shape in the heat ventilation area, image 3 is a plan view of the upper part of the heat exchange tube 21, Figure 4 It is a bottom view of the lower part of the heat exchange tube 21, the upper outlet 2103 of the heat...

Embodiment 2

[0046] Utilize the method for preparing polyphosphoric acid of the device for preparing polyphosphoric acid of embodiment 1, wherein the heat exchange tube 21 is from the acid inlet 2101 of the heat exchange tube to the acid outlet 2102 of the heat exchange tube, inclined downward at an angle of 1°:

[0047] The dilute phosphoric acid with a mass concentration of 45% from the dilute acid tank 1 enters the heat exchange tube 21 through the acid inlet 2101 of the heat exchange tube. The pressure at the acid inlet 2101 of the heat exchange tube is -594mmHg, and the dilute phosphoric acid passes through the heat ventilation area , that is, inside the insulation layer 22, the heat exchange with the yellow phosphorus waste gas (220°C) in the shell of the heat exchange tube 21 raises the temperature to 210°C. Polyphosphoric acid, the acid liquid exits the heat exchanger 2 from the acid outlet 2102 of the heat exchange tube, and enters the film-hanging tray 5 in the separator 3 through...

Embodiment 3

[0050] Utilize the method for preparing polyphosphoric acid of the device for preparing polyphosphoric acid of embodiment 1, the heat exchange tube 21 is from the acid inlet 2101 of the heat exchange tube to the acid outlet 2102 of the heat exchange tube, and slopes downward at an angle of 3°:

[0051] The dilute phosphoric acid with a mass concentration of 70% from the dilute acid tank 1 enters the heat exchange tube 21 through the acid inlet 2101 of the heat exchange tube. , that is, inside the insulation layer 22, heat exchange with the yellow phosphorus tail gas (200°C) in the shell of the heat exchange tube 21 and raise the temperature to 195°C. Polyphosphoric acid, the acid liquid exits the heat exchanger 2 from the acid outlet 2102 of the heat exchange tube, and enters the film-hanging tray 5 in the separator 3 through the acid inlet pipe 31 of the separator; the vacuum constant pressure device 4 keeps the inside of the separator 3 The constant vacuum is -500mmHg, the p...

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Abstract

The invention relates to the field of phosphorus chemical industry, in particular to a preparation method for polyphosphoric acid. The method for preparing polyphosphoric acid includes: letting dilute phosphoric acid enter a heater through a heat exchange tube acid inlet to be heated to 185DEG C-230DEG C, then discharging the dilute phosphoric acid out of the heater from a heat exchange tube acid outlet, and making the dilute phosphoric acid enter a separator to undergo flash concentration, keeping the vacuum degree in the separator ranging from -500 to -700mmHg, discharging the concentrated acid liquor out of the separator through an acid outlet tube at the lower end of the separator, and leading the concentrated acid liquor into a concentrated acid tank through a concentrated acid tank acid inlet to undergo cooling and storage. The heat exchange tube is coiled in an S shape in the heater, from the heat exchange tube acid inlet to the heat exchange tube acid outlet, the heat exchange tube tilts downward at an angle of 1-3 degrees. The preparation method for polyphosphoric acid provided by the invention has a simple process, can prepare high concentration polyphosphoric acid from dilute phosphoric acid by one-step polymerization. By taking dilute phosphoric acid as the raw material, the acid liquor cannot adhere to the heat exchange tube wall, thus avoiding blocking of the heat exchange tube. Further, the prepared polyphosphoric acid product has uniformly distributed components.

Description

technical field [0001] The invention relates to the field of phosphorus chemical industry, in particular to a method for preparing polyphosphoric acid. Background technique [0002] In the 1930s, the Tennessee Valley Authority Research Institute of the United States found that in orthophosphoric acid (H 3 PO 4 ) and pyrophosphate (H 4 P 2 o 7 ) between liquid phosphoric acid with a eutectic composition. its ωP 2 o 5 is 76% [equivalent to ω (H 3 PO 4 ) is 105%], of which about 49%P 2 o 5 It exists in the form of orthophosphoric acid, 42% is pyrophosphoric acid, and 8% is tripolyphosphoric acid (H 5 P 3 o 10 ), 1% is tetrapolyphosphoric acid (H 6 P 4 o 13 )exist. This mixture of orthophosphoric acid and polyphosphoric acid is called polyphosphoric acid (poly phosphoric acid). [0003] Polyphosphoric acid, also known as tetrapolyphosphoric acid, polyphosphoric acid or polyphosphoric acid, is a colorless, transparent, viscous liquid, easy to deliquescence, non-...

Claims

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Application Information

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IPC IPC(8): C01B25/24
Inventor 唐希勇彭永
Owner 绵阳启明星磷化工有限公司
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