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Plant extraction equipment with efficient liquid-residue separation function

A technology for liquid residue separation and plant extraction, applied in solid solvent extraction, chemical/physical process, dissolution and other directions, can solve the problem that the degree of solvent convection cannot be greatly increased, the degree of solvent convection cannot be greatly improved, and cannot be maximized. To improve the leaching effect and other issues, to achieve the effect of speeding up the leaching rate, improving the leaching effect, and improving the pressure effect

Active Publication Date: 2021-05-25
深圳市颐品生物科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] During the leaching process of the existing herbal medicinal materials, they need to be pulverized to make the particle size of the medicinal materials smaller, thereby increasing the contact area with the leaching solvent and increasing the diffusion rate. The leaching of more mucus will increase the viscosity between the herbal medicines; the leaching rate of the herbal medicines is positively correlated with the convective diffusion coefficient, and the convective diffusion coefficient increases with the increase of the convection degree of the solvent, and the convective diffusion coefficient is the largest in turbulent flow , in order to increase the convective diffusion coefficient, most of the existing leaching processes have agitation, and the agitation mechanism is generally divided into two types, one is the stirring blade, but under the action of the viscosity and friction of the herbal medicine, the blade It can only affect the nearby botanicals, and most of the agitated botanicals will rotate synchronously with the paddles, and only a part of the botanicals will have obvious relative dislocation movement, and the degree of convection of the solvent penetrating into the medicinals cannot be achieved. The other is the agitating helical blade, the helical blade can pump the herbal medicine upwards to the top first, and then discharge it to the surroundings, so as to increase the convection of the solvent, but it also affects the viscosity and friction of the herbal medicine. Under the action of the propeller, the herbal medicinal materials input into the spiral blades will be transported upward synchronously, and only a part of the herbal medicinal materials will produce obvious relative dislocation movement, and the convection degree of the solvent cannot be greatly improved. Although the existing propeller blades and helical blades It can improve the degree of convection of botanicals, but the range of influence is small, and the leaching rate cannot be maximized
[0003] Long-term leaching often leads to the dissolution of a large amount of impurities, and some active ingredients are decomposed by the enzymes together, which affects the quality of the leaching solution; The pressure will make the medicinal material tissues accumulate and become compact, which will affect the stirring in the above-mentioned leaching process. Stirring and pressure will affect each other, which is not conducive to leaching. The combined effect of stirring and pressure cannot be realized in the existing devices. effect, does not maximize leaching

Method used

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  • Plant extraction equipment with efficient liquid-residue separation function
  • Plant extraction equipment with efficient liquid-residue separation function
  • Plant extraction equipment with efficient liquid-residue separation function

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031] Embodiment 1, the technical solution it solves is, a kind of plant extraction equipment with high-efficiency liquid slag separation function, comprises vertical leaching barrel 1 and heating barrel 2, and leaching barrel 1 is placed on heating barrel 2 and leaching The openings of the barrel 1 and the heating barrel 2 are opposite, the leaching barrel 1 and the heating barrel 2 are coaxially sealed and connected, and the coaxial sealing and rotating connection of the leaching barrel 1 is connected with the rotating shaft 3 placed in the leaching barrel 1, and the lower end of the rotating shaft 3 A conical body 4 with an upward apex is coaxially connected. The cone 4 is placed at the bottom of the leaching barrel 1 and separates the leaching barrel 1 from the heating barrel 2. A plurality of filter holes 5 are evenly distributed on the cone 4. The leaching The barrel 1 and the heating barrel 2 are connected through the filter hole 5, the outer edge of the cone 4 is in sl...

Embodiment 2

[0035] Embodiment 2, on the basis of Embodiment 1, the end of the rotating shaft 6 close to the rotating shaft has a plurality of fan blades 18 uniformly distributed in the air passage 8, and the plurality of fan blades 18 constitute a shaftless fan .

[0036] When in use, the vaporized leaching solvent is discharged into the air passage 8 of the rotating shaft 6 under the action of the air pump, and the vaporized leaching solvent pushes the fan blade 18 to rotate, so that the rotating shaft 6 rotates with the fan blade 18, and the rotating shaft drives The rotation of the helical blades 9 realizes the effect of the external force forcibly driving the helical blades 9 to stir the botanical medicinal materials, and prevents the botanical medicinal materials from blocking the gap between two adjacent helical blades 9 so that the helical blades 9 cannot rotate.

Embodiment 3

[0037] Embodiment 3, on the basis of Embodiment 1, the transmission mechanism includes a first bevel gear 19 placed above the pressing plate 17 and coaxially connected with the pressing plate 13, between the first bevel gear 19 and the pressing plate 17 Slidingly connected along the radial direction of the pressure plate 13, the end of the pressure piece 17 away from the axis of the pressure plate 13 has a stopper 20, and the lower end of the first bevel gear 19 has two stoppers that match the stopper 20 and are respectively placed on both sides of the stopper 20 Block 21, the space between the two limiting blocks 21 forms a chute 22, the length direction of the chute 22 is along the radial direction of the pressure plate 13, the stopper 20 is placed in the chute 22 and can be moved along the length direction of the chute 22 Sliding, the inner diameter of the first bevel gear 19 is greater than the inner diameter of the pressing plate 13, and the pressing plate 13 is rotatably ...

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Abstract

The invention discloses plant extraction equipment with an efficient liquid-residue separation function, and effectively solves the technical problem that pressure application and stirring cannot be performed simultaneously in a vegetable medicinal material leaching process by an existing device. The plant extraction equipment can apply pressure to vegetable medicinal materials while stirring the vegetable medicinal materials. During pressure application, the pressure application range is enlarged, and stirring is stopped. During stirring, the stirring range is enlarged, and the pressure application range is reduced. The conflict of the two processes is ingeniously avoided, and the adjusting processes are automatically carried out without manual participation.

Description

technical field [0001] The invention relates to the technical field of plant medicinal material extraction equipment, in particular to plant extraction equipment with high-efficiency liquid slag separation function. Background technique [0002] During the leaching process of the existing herbal medicinal materials, they need to be pulverized to make the particle size of the medicinal materials smaller, thereby increasing the contact area with the leaching solvent and increasing the diffusion rate. The leaching of more mucus will increase the viscosity between the herbal medicines; the leaching rate of the herbal medicines is positively correlated with the convective diffusion coefficient, and the convective diffusion coefficient increases with the increase of the convection degree of the solvent, and the convective diffusion coefficient is the largest in turbulent flow , in order to increase the convective diffusion coefficient, most of the existing leaching processes have ...

Claims

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Application Information

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IPC IPC(8): B01D11/02B01F13/10B01F15/00B01F15/02
CPCB01D11/02B01F33/833B01F35/187B01F35/754
Inventor 张滕飞
Owner 深圳市颐品生物科技有限公司
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