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Low-cost and high-efficiency supercritical spray drying method and equipment for slurry

A drying method and technology of spray drying tower are applied in the field of low-cost and high-efficiency supercritical spray drying of slurry, which can solve the problems of unsuitability for large-scale production, complex equipment cost, low production efficiency, etc., and achieve the technological method and equipment performance. The effect of low consumption, simple equipment and high thermal efficiency

Active Publication Date: 2018-01-09
西安安聚德纳米科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

These high-viscosity slurries are not suitable for drying by traditional methods, because the nano-powders will form agglomerated particles and blocks that are difficult to disperse. The current production efficiency of supercritical drying is low, and it is not suitable for large-scale production. For heating, the thermal efficiency is low, the equipment is complicated and the cost is high

Method used

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  • Low-cost and high-efficiency supercritical spray drying method and equipment for slurry
  • Low-cost and high-efficiency supercritical spray drying method and equipment for slurry
  • Low-cost and high-efficiency supercritical spray drying method and equipment for slurry

Examples

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Embodiment 1

[0038] image 3 It is a kind of supercritical spray drying equipment used in the present invention, which is suitable for continuous drying process. The equipment includes a supercritical generating device for preheating and pressurizing the slurry to reach a supercritical state, a spray drying tower 5, a powder storage tank 6, a cyclone separator 7, a filter bag separator 8, and a condensation recovery tower 9. The bottom of the spray drying tower is connected to the powder storage tank, and the powder storage tank is connected to the second vacuum pump 12; the top of the spray drying tower is connected to the cyclone separator. Outlet and bottom outlet, the top outlet of the cyclone separator is connected to the filter bag separator, the bottom outlet of the cyclone separator and the filter bag separator are both connected to the powder storage tank, and the first outlet of the filter bag separator is connected to the condensation recovery tower , the outlet of the condensa...

Embodiment 2

[0042] Figure 4 Another supercritical spray drying equipment used in the present invention is suitable for batch drying. Compared with Embodiment 1, this equipment does not use a high-pressure pump and a heater, but an autoclave.

[0043] The equipment includes a supercritical generating device for preheating and pressurizing the slurry to reach a supercritical state, a spray drying tower 5, a powder storage tank 6, a cyclone separator 7, a filter bag separator 8, and a condensation recovery tower 9. The bottom of the spray drying tower is connected to the powder storage tank, and the powder storage tank is connected to the second vacuum pump 12; the top of the spray drying tower is connected to the cyclone separator. Outlet and bottom outlet, the top outlet of the cyclone separator is connected to the filter bag separator, the bottom outlet of the cyclone separator and the filter bag separator are both connected to the powder storage tank, and the first outlet of the filter...

Embodiment 3

[0046] Example 3 Low-cost and high-efficiency supercritical spray drying of slurry

[0047] The dry material is nano iron oxide ethanol slurry with a mass ratio of 10%, and the viscosity at room temperature is 1000cP. The supercritical temperature and pressure of ethanol are 241°C and 6.3MPa, respectively. This slurry uses image 3 In the continuous production process shown, the slurry is boosted to 8MPa by a high-pressure pump, and then heated to 250°C by a heater. The temperature of the spray drying tower is 65°C and the pressure is 50kPa (about 0.5 atmospheric pressure), which is lower than the saturated vapor pressure at this temperature, so there is no condensation and condensation in the spray drying tower, and the set temperature of the condensation recovery tower is -10°C , The vapor pressure is about 0.8kPa, and 95% of the vapor is recovered as a solvent. The pressure of the vacuum pump is set at 47kPa, and the pressure loss of the low-pressure system from the spra...

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Abstract

The invention relates to a size drying and separating method, in particular to a low-cost high-efficiency supercritical fluid spray drying method and device for size.According to the method, the size to be dried is heated and pressurized to the super-critical state of an adopted solvent, then atomization is conducted in a spray drying tower to achieve gas-solid separation quickly, powder is separated from solvent vapor through multi-stage recovery, and the solvent vapor is recovered through condensation.The large-scale production capacity of high-pressure spray drying and the product dispersion easiness of supercritical drying are combined to meet the requirement for drying of different kinds of size, and the solvent content of the size to be processed can be over 95%; due to the fact that the liquid size is only heated to supercritical temperature and pressure, heat conduction speed is high, indirect heating conducted through a drying medium is not adopted, heat efficiency is high, and the method and device are suitable for large-scale production; furthermore, due to the fact the heating process is conducted in an airtight mode in the absence of heating medium air, no combustion explosion risk exists, and the requirement for drying of flammable and combustible organic materials is met.

Description

technical field [0001] The invention relates to a slurry drying and separation method, in particular to a low-cost and high-efficiency supercritical spray drying method and equipment for slurry. Background technique [0002] Most drying processes use a medium to dry materials. The common medium is hot air. If the material to be dried contains organic solvents, the mixture of air and flammable organic solvents may catch fire, burn and explode. Therefore, vacuum drying or inert gas circulation drying is a commonly used process in this case. There is no convective heat conduction of gas in a vacuum state, and the heating efficiency is low. Although the boiling point of the liquid can be lowered, the heat transfer speed is a lawful process of drying, so the overall drying speed is still very slow. Through nitrogen, CO 2 , argon and other inert gas circulation heating and drying and solvent recovery, since the inert gas needs to be heated by a heat source, it is indirect heating...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D1/18
CPCB01D1/18
Inventor 邓超然张亚妮
Owner 西安安聚德纳米科技有限公司
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