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System for preparing micro particles with hydraulic cavitation reinforcing supercritical auxiliary atomizing and its method

A hydraulic cavitation and supercritical technology, which is applied in the direction of liquid separation into beads and granulation, can solve problems such as long residence time, early precipitation of solutes, and impact on product quality

Inactive Publication Date: 2007-10-17
ZHEJIANG UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although the SAA technology has been improved compared with the original CAN-BD process, there are still problems such as the slow mass transfer rate of supercritical carbon dioxide and solution between the two phases in the saturator, resulting in low mixing efficiency and long residence time. It is easy to cause early precipitation of solutes and affect product quality

Method used

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  • System for preparing micro particles with hydraulic cavitation reinforcing supercritical auxiliary atomizing and its method
  • System for preparing micro particles with hydraulic cavitation reinforcing supercritical auxiliary atomizing and its method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0023] Embodiment 1: the preparation of levofloxacin hydrochloride microparticles

[0024] First prepare an appropriate amount of levofloxacin hydrochloride methanol solution with a concentration of 2mg / ml, and preheat the solution to 40°C with a water bath; adjust the inner diameter of the nozzle to 200μm; turn on the compressor, and heat the CO in the buffer tank 2 Increase the pressure to 8MPa, heat the temperature control box to 40°C; set the temperature control of the precipitator to 60°C, and feed 40NL / min of nitrogen preheated to 60°C. Then feed 60g / min CO into the hydraulic cavitation mixer 2 Fluid, the copper sieve plate porosity (single hole) is 1 / 8; The hydraulic cavitation mixer is boosted to 8MPa, then pumps into the levofloxacin hydrochloride methanol solution of 25ml / min in the hydraulic cavitation mixer, and the residence time is 40 ~60 seconds, the pressure of the hydraulic cavitation mixer is accurately controlled at 8MPa (±0.1MPa); after the mist droplets a...

Embodiment 2

[0025] Embodiment 2: Preparation of polylactic acid microparticles

[0026]First prepare an appropriate amount of polylactic acid dichloromethane solution with a concentration of 6mg / ml, and preheat the solution to 40°C with a water bath; adjust the inner diameter of the nozzle to 100μm; turn on the compressor, and heat the CO in the buffer tank. 2 Increase the pressure to 8MPa, heat the temperature control box to 40°C; set the temperature control of the precipitator to 70°C, and feed 40NL / min of nitrogen preheated to 70°C. Then feed 50g / min CO into the hydraulic cavitation mixer 2 Fluid, the porosity of the copper sieve plate (8 round holes of 1mm) is 0.32; the hydraulic cavitation mixer is boosted to 8MPa, and then 35ml / min of polylactic acid dichloromethane solution is pumped into the hydraulic cavitation mixer, The residence time is 40-60 seconds, and the pressure of the hydraulic cavitation mixer is precisely controlled at 8MPa (±0.1MPa); after the mist droplets appear a...

Embodiment 3

[0027] Embodiment 3: the preparation of aspirin microparticles

[0028] First prepare an appropriate amount of aspirin ethanol solution with a concentration of 2mg / ml, and preheat the solution to 60°C with a water bath; adjust the inner diameter of the nozzle to 200μm; turn on the compressor, and heat the CO in the buffer tank. 2 Increase the pressure to 9MPa, heat the temperature control box to 60°C; set the temperature control of the precipitator to 90°C, and inject 50N L / min of hot nitrogen preheated to 90°C. Then feed 65g / min CO into the hydraulic cavitation mixer 2 Fluid, copper sieve plate porosity (single hole) is 1 / 10; boost the hydraulic cavitation mixer to 9MPa, then pump 40ml / min aspirin ethanol solution into the hydraulic cavitation mixer, the residence time For 40 to 60 seconds, the pressure of the hydraulic cavitation mixer is precisely controlled at 9MPa (±0.1MPa); after mist droplets appear at the outlet of the nozzle, the vacuum pump is turned on, and the sol...

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Abstract

The invention discloses a system of waterpower cavitation enhanced supercritical assistant pulverization preparing particle and a method thereof, which has the following character that: (1) sieve plate is mounted in the waterpower cavitation mixer to form cavity, inanition and cavum in the miscible liquid flow of supercritical CO2 and solution to realize the rapid mixture thereof, and to make the meltage of the supercritical CO2 in the solution approach the equilibrium solubility; (2) the mixture of the supercritical CO2 and solution is sprinkled into the precipitator by nozzle to form secondary liquid drop, which is heat transfer and mass transfer with N2 to make the liquid vaporize, and then get particle; (3) the particle is collected using the sintered plate mounted on the bottom of the precipitator; (4) the mixing gas of CO2, N2 and solvent enter into the condenser, and the solvent is reclaimed and recycling. The operating condition of the invention is relative mildness, the operating process is simple, the residual of the solvent is low, and the size distribution of the product is narrow. The invention can be used for grain diminution of various of material.

Description

technical field [0001] The invention relates to a system and a method for preparing microparticles by hydraulic cavitation enhanced supercritical atomization. Background technique [0002] At present, the methods of particle preparation mainly include mechanical pulverization, liquid anti-solvent method, spray drying method and freezing method. Although these methods are simple to operate, there are some shortcomings and deficiencies, such as large amount of organic solvent, high content of residual organic solvent in the product, serious heat-sensitive degradation of the solute to be micronized, etc. The most important thing is that these methods are difficult to control the product. particle size, distribution and product morphology. Although these methods still play an important role in the production of bulk petrochemical products, in recent years, with the increasing demand for food and medicine (variety, quality), these traditional methods have become increasingly dif...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J2/02
Inventor 关怡新蔡美强姚善泾朱自强
Owner ZHEJIANG UNIV
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