CN102500130A - First-stage rutin extraction equipment - Google Patents
First-stage rutin extraction equipment Download PDFInfo
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- CN102500130A CN102500130A CN2011103339856A CN201110333985A CN102500130A CN 102500130 A CN102500130 A CN 102500130A CN 2011103339856 A CN2011103339856 A CN 2011103339856A CN 201110333985 A CN201110333985 A CN 201110333985A CN 102500130 A CN102500130 A CN 102500130A
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- rutin
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- current extraction
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Abstract
The invention discloses first-stage rutin extraction equipment. A screw type thrust is connected with a backflow ultrasonic extraction pipe, the backflow ultrasonic extraction pipe is connected with a slag discharge mechanism and a revolving barrel type filter, the revolving barrel type filter is connected with an extract liquid storage tank, the extract liquid storage tank is connected with a revolving disc type filter, and the revolving disc type filter is connected with a gelatin and pigment separating mechanism. Compared with the prior art, the first-stage rutin extraction equipment can realize continuous production, is high in automation degree, and can increase rutin extraction purity and extraction rate.
Description
Technical field
The present invention relates to the extraction field of rutin, exactly be meant a kind of first order rutin extraction equipment.
Background technology
Rutin is a kind of light yellow acicular crystal (water), fusing point 176-8 ℃, clinically is used to prevent and treat cerebral hemorrhage, hypertension, retinal hemorrhage, purple scar and acute bleeding nephritis, also as food antioxidant and pigment.Its pharmacological action is: rutin belongs to vitamin drug, and the effect that reduces capillary permeability and fragility is arranged, and keeps and recover the normal elasticity of capillary.The production technology of rutin is mainly accomplished by operations such as alcohol extracting, extraction, chromatography, crystallizations.But existing rutin extraction automation degree of equipment is low, and the rutin purity of extraction is not high and recovery rate is lower, needs to improve.
Summary of the invention
To above-mentioned defective, the technical problem that the present invention solves is to provide a kind of first order rutin to extract equipment, can produce continuously, and automaticity is high, can improve dna purity and the recovery rate of rutin.
In order to solve above technical problem; First order rutin provided by the invention is extracted equipment; Comprise spiral propeller, adverse current Extraction by Ultrasound pipeline, slagging device, cylinder-rotating filter, extract storage tank, rotating disk type filter and glue, pigment separating mechanism; Said spiral propeller is connected with said adverse current Extraction by Ultrasound pipeline, and said adverse current Extraction by Ultrasound pipeline is connected with said slagging device, said adverse current Extraction by Ultrasound pipeline is connected with said cylinder-rotating filter, said cylinder-rotating filter is connected with said extract storage tank, said extract storage tank is connected with said rotating disk type filter, said rotating disk type filter is connected with glue, pigment separating mechanism.
Preferably, said adverse current Extraction by Ultrasound pipeline comprises immersion pipeline section and ultrasonic pipeline section.
Preferably, said first order rutin is extracted equipment and also comprises the deionized water storage tank, and said deionized water storage tank is connected with said adverse current Extraction by Ultrasound pipeline.
Preferably, be provided with heat exchanger and flowmeter between said deionized water storage tank and the said adverse current Extraction by Ultrasound pipeline.
Preferably, said slagging device is provided with extruder, and said extruder is connected with said adverse current Extraction by Ultrasound pipeline.
Preferably, said slagging device is provided with return duct, and said return duct is connected with said adverse current Extraction by Ultrasound pipeline.
Preferably, said spiral propeller is provided with feed hopper.
Preferably, said first order rutin is extracted equipment and also comprises slag-discharging device, and said slag-discharging device is connected with said rotating disk type filter.
First order rutin provided by the invention is extracted equipment; Said spiral propeller is connected with said adverse current Extraction by Ultrasound pipeline, and said adverse current Extraction by Ultrasound pipeline is connected with said slagging device, said adverse current Extraction by Ultrasound pipeline is connected with said cylinder-rotating filter, said cylinder-rotating filter is connected with said extract storage tank, said extract storage tank is connected with said rotating disk type filter, said rotating disk type filter is connected with glue, pigment separating mechanism.Compared with prior art, first order rutin provided by the invention is extracted equipment, can produce continuously, and automaticity is high, can improve dna purity and the recovery rate of rutin.
Description of drawings
Fig. 1 extracts the structural representation of equipment for first order rutin among the present invention.
Wherein, respectively be denoted as among the figure:
1-adverse current Extraction by Ultrasound pipeline;
The spiral propeller of 2-;
3-deionized water storage tank;
4-cylinder-rotating filter;
The 5-heat exchanger;
The 6-flowmeter;
The 7-extruder;
8-extract storage tank;
The 9-slag-discharging device;
10-rotating disk type filter;
The ultrasonic pipeline section of 11-;
12-soaks pipeline section;
The 13-jet chimney;
14-extracts the material outlet;
The 15-charging aperture;
The 16-return duct;
The 17-feed hopper;
18-glue, pigment separating mechanism;
The 19-elevator.
The specific embodiment
For those skilled in the art can understand technical scheme provided by the present invention better, set forth below in conjunction with specific embodiment.
See also Fig. 1, this figure is the structural representation that first order rutin is extracted equipment among the present invention.
First order rutin provided by the invention is extracted equipment; Comprise spiral propeller 2, adverse current Extraction by Ultrasound pipeline 1, slagging device, cylinder-rotating filter 4, extract storage tank 8, rotating disk type filter 10; Spiral propeller 2 is connected with adverse current Extraction by Ultrasound pipeline 1, and adverse current Extraction by Ultrasound pipeline 1 is connected with slagging device, adverse current Extraction by Ultrasound pipeline 1 is connected with cylinder-rotating filter 4, cylinder-rotating filter 4 is connected with extract storage tank 8, extract storage tank 8 is connected with rotating disk type filter 10, rotating disk type filter 10 is connected with glue, pigment separating mechanism 18.Slag-discharging device 9 is connected with rotating disk type filter 10.
Adverse current Extraction by Ultrasound pipeline 1 comprises immersion pipeline section 12 and ultrasonic pipeline section 11.Spiral propeller 2 is provided with feed hopper 17, and feed hopper 17 is used to receive the sophora bud of steaming that charging aperture 15 is carried.Deionized water storage tank 3 is connected with adverse current Extraction by Ultrasound pipeline 1, is provided with heat exchanger 5 and flowmeter 6 between deionized water storage tank 3 and the adverse current Extraction by Ultrasound pipeline 1.Heat exchanger 5 is connected with jet chimney 13.Slagging device is provided with extruder 7 and return duct 16, and extruder 7 is connected with adverse current Extraction by Ultrasound pipeline 1, and return duct 16 is connected with adverse current Extraction by Ultrasound pipeline 1.Extruder 7 also is provided with and extracts material outlet 14, is used to discharge the sophora bud that has extracted.
The workflow that first order rutin provided by the invention is extracted equipment is following:
1, gets into feed hopper 17 through the sophora bud after the dry blowing automatically through charging aperture 15;
2, the sophora bud gets into spiral propeller 2, gets into ultrasonic pipeline section 11 again and soaks water back 12, and soaking temperature is 28-32 ℃, and the reverse entering of steam is soaked water back 12 and heated;
3, after the process deionized water immersion heating, the sophora bud process elevator 19 automatic liftings except that glue get into extruders 7, and the sophora bud entering extraction after the extruding is expected to export 14 next link and extracted;
4, the solution entering cylinder-rotating filter 4 after the immersion sophora bud carries out the one-level filtration;
5, one-level filtrating gets into extract storage tank 8, gets into rotating disk type filter 10 again and carries out cascade filtration;
6, secondary filtrating gets into glue, pigment separating mechanism 18 separates, and the dregs of a decoction get into slag-discharging device 9 and carry out deslagging.
Compared with prior art, first order rutin provided by the invention is extracted equipment, can produce continuously, and automaticity is high, can improve dna purity and the recovery rate of rutin.
To the above-mentioned explanation of the disclosed embodiments, make this area professional and technical personnel can realize or use the present invention.Multiple modification to these embodiment will be conspicuous concerning those skilled in the art, and defined General Principle can realize under the situation that does not break away from the spirit or scope of the present invention in other embodiments among this paper.Therefore, the present invention will can not be restricted to these embodiment shown in this paper, but will meet and principle disclosed herein and features of novelty the wideest corresponding to scope.
Claims (8)
1. a first order rutin is extracted equipment; It is characterized in that; Comprise spiral propeller, adverse current Extraction by Ultrasound pipeline, slagging device, cylinder-rotating filter, extract storage tank, rotating disk type filter and glue, pigment separating mechanism; Said spiral propeller is connected with said adverse current Extraction by Ultrasound pipeline, and said adverse current Extraction by Ultrasound pipeline is connected with said slagging device, said adverse current Extraction by Ultrasound pipeline is connected with said cylinder-rotating filter, said cylinder-rotating filter is connected with said extract storage tank, said extract storage tank is connected with said rotating disk type filter, said rotating disk type filter is connected with glue, pigment separating mechanism.
2. first order rutin according to claim 1 is extracted equipment, it is characterized in that, said adverse current Extraction by Ultrasound pipeline comprises immersion pipeline section and ultrasonic pipeline section.
3. first order rutin according to claim 1 is extracted equipment, it is characterized in that also comprise the deionized water storage tank, said deionized water storage tank is connected with said adverse current Extraction by Ultrasound pipeline.
4. first order rutin according to claim 3 is extracted equipment, it is characterized in that, is provided with heat exchanger and flowmeter between said deionized water storage tank and the said adverse current Extraction by Ultrasound pipeline.
5. first order rutin according to claim 1 is extracted equipment, it is characterized in that said slagging device is provided with extruder, and said extruder is connected with said adverse current Extraction by Ultrasound pipeline.
6. first order rutin according to claim 1 is extracted equipment, it is characterized in that said slagging device is provided with return duct, and said return duct is connected with said adverse current Extraction by Ultrasound pipeline.
7. first order rutin according to claim 1 is extracted equipment, it is characterized in that said spiral propeller is provided with feed hopper.
8. first order rutin according to claim 1 is extracted equipment, it is characterized in that also comprise slag-discharging device, said slag-discharging device is connected with said rotating disk type filter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011103339856A CN102500130A (en) | 2011-10-28 | 2011-10-28 | First-stage rutin extraction equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011103339856A CN102500130A (en) | 2011-10-28 | 2011-10-28 | First-stage rutin extraction equipment |
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| CN102500130A true CN102500130A (en) | 2012-06-20 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
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| CN2011103339856A Pending CN102500130A (en) | 2011-10-28 | 2011-10-28 | First-stage rutin extraction equipment |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103830932A (en) * | 2012-11-28 | 2014-06-04 | 东北林业大学 | Tunnel type ultrasonic triple-effect reflux extraction system |
| CN105001667A (en) * | 2014-08-10 | 2015-10-28 | 王选明 | System for rapidly extracting natural plant pigments |
| CN105062123A (en) * | 2014-08-10 | 2015-11-18 | 王选明 | Equipment for rapidly extracting pigments from rhododendron simsii planch |
| CN106675085A (en) * | 2014-08-10 | 2017-05-17 | 王选明 | System for quickly extracting pigment from azalea flowers |
| CN109400570A (en) * | 2018-12-25 | 2019-03-01 | 江苏哈工药机科技股份有限公司 | A kind of extraction system of anthocyanidin |
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| CN1373128A (en) * | 2002-01-07 | 2002-10-09 | 王经安 | Enzyme-removing degumming process of preparing rutin |
| CN201320417Y (en) * | 2008-12-17 | 2009-10-07 | 济宁金百特工程机械有限公司 | Reverse-flow ultrasonic extracting machine set |
| CN101818184A (en) * | 2010-05-04 | 2010-09-01 | 河南青纯生物科技有限公司 | Method for extracting rutin from sophora japonica |
| CN202315396U (en) * | 2011-10-28 | 2012-07-11 | 四川省砚山中药饮片有限公司 | First-stage rutin extraction equipment |
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2011
- 2011-10-28 CN CN2011103339856A patent/CN102500130A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1373128A (en) * | 2002-01-07 | 2002-10-09 | 王经安 | Enzyme-removing degumming process of preparing rutin |
| CN201320417Y (en) * | 2008-12-17 | 2009-10-07 | 济宁金百特工程机械有限公司 | Reverse-flow ultrasonic extracting machine set |
| CN101818184A (en) * | 2010-05-04 | 2010-09-01 | 河南青纯生物科技有限公司 | Method for extracting rutin from sophora japonica |
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| 易克传等: "超声波强化逆流提取机及提取试验", 《农业机械学报》, vol. 38, no. 12, 31 December 2007 (2007-12-31), pages 109 - 128 * |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103830932A (en) * | 2012-11-28 | 2014-06-04 | 东北林业大学 | Tunnel type ultrasonic triple-effect reflux extraction system |
| CN105001667A (en) * | 2014-08-10 | 2015-10-28 | 王选明 | System for rapidly extracting natural plant pigments |
| CN105062123A (en) * | 2014-08-10 | 2015-11-18 | 王选明 | Equipment for rapidly extracting pigments from rhododendron simsii planch |
| CN105001667B (en) * | 2014-08-10 | 2016-10-26 | 重庆雅香美源生态农业科技有限公司 | The system of rapid extraction natural plant pigment |
| CN106675085A (en) * | 2014-08-10 | 2017-05-17 | 王选明 | System for quickly extracting pigment from azalea flowers |
| CN106675085B (en) * | 2014-08-10 | 2019-01-15 | 三门华迈化工产品有限公司 | A kind of system for from the middle rapidly extracting pigment of azalea |
| CN109400570A (en) * | 2018-12-25 | 2019-03-01 | 江苏哈工药机科技股份有限公司 | A kind of extraction system of anthocyanidin |
| CN109400570B (en) * | 2018-12-25 | 2023-12-22 | 江苏哈工药机科技股份有限公司 | Anthocyanin extraction system |
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Application publication date: 20120620 |