CN206762316U - A kind of capsaicine subcritical fluid extraction device - Google Patents
A kind of capsaicine subcritical fluid extraction device Download PDFInfo
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- CN206762316U CN206762316U CN201720561337.9U CN201720561337U CN206762316U CN 206762316 U CN206762316 U CN 206762316U CN 201720561337 U CN201720561337 U CN 201720561337U CN 206762316 U CN206762316 U CN 206762316U
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- capsaicine
- extractor
- recycle
- solvent
- evaporator
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Abstract
The utility model discloses a kind of capsaicine subcritical fluid extraction device, including support, extractor, evaporator, recycle heat device and solvent recycle unit, support is cube frame like structure, cradle top is fixedly installed extractor and evaporator, internal stent is fixedly installed recycle heat device and solvent recycle unit, and extractor turns on the evaporator, recycle heat device and solvent recycle unit respectively.Capsaicine is prepared using subcritical fluid extraction technology, is extracted under subcritical environment, extraction temperature is low, does not destroy capsaicine composition, does not aoxidize, and capsaicine leaches complete, internal system heat exchange, and power consumption is low;Technical process is simple, is advantageous to industrialized production;Whole process is completed in the system of closing, environmentally safe.
Description
Technical field
Capsaicine extractive technique field is the utility model is related to, specially a kind of capsaicine subcritical fluid extraction device.
Background technology
Capsaicine also known as capsaicine, popular name Capsaicin is the alkaloid of a kind of phenolic hydroxy group, wherein main being formed by five kinds
Composition, respectively capsaicine, dihydrocapsaicin, nordihydrocapsaicin, homodihydrocapsaicin, homocapsaicin.Capsaicine thermostabilization
Property it is high, sterling be white needle-like crystals under usual conditions, nontoxicity, but excitant is very strong, is soluble in methanol, ethanol, acetone, three
In chloromethanes, dichloromethane, ethyl acetate and alkaline aqueous solution, cold water is insoluble in.The capsicum of low concentration is usually with pigment, with sugar
Body, Phospholipids form the molten thing of violet oil.
Capsaicine is primarily present in the tire reality tissue and chili peel and seed of pepper fruit, and content is 0.05~1.0%,
The difference because of the difference of kind, maturity, weather conditions and soil property etc., is typically accumulated with maturity.It is peppery
Green pepper element is the main matter for causing acid in capsicum, and the content of a ten thousandth can feel obvious pungent in food.
Capsaicine can be used for many fields, and low-purity chilli extract can be widely used in food industry as additive;Purifying
Capsaicine afterwards is wider in pharmaceuticals industry application, such as has notable adjustment effect to angiocarpy, PFT, stomach and intestine function;It can promote
Enter fat metabolism;Acted on easing pain and diminishing inflammation, can be made into potent analgesic;Interior free yl can be suppressed, reduce cell carcinogenesis;With
Morphine shares, and can mitigate the withdrawal syndrome of Morphinoid drug, reduces additive[13];To chronic rheumatic arthritis, ox-hide
Tinea, baldness have good therapeutic action.There is high-purity capsicum cellulose crystal tear-gas to urge the effect of sneezing, military affairs can manufacture tear bombnoun,
Tear-gas rifle and defensive weapon.Capsaicine has the active material for preventing biological attachment, can agriculturally be used as biochemical pesticide, be used for
Pest and mouse, rabbit etc.;It is used for nontoxic antifouling paint additive on ship;Add on cable, optical cable for protection against rodents coating
Add agent;It is used for termite-proof coating etc. on wooden building.
At present, the agent of capsicum stomach strengthening and digestion promoting, capsicum diet food, capsicum health medicine etc. are also among research and development.It is it is expected that domestic
The application of outer capsaicine will rapidly expand and bring wide market prospects.
Conventional high-purity capsaicine extracting method has:Solvent extraction method, adsorpting column chromatography method, supercritical carbon dioxide extracting
Method.
(1)Solvent extraction method:Using scarlet chilli as raw material, extracted after crushed with organic solvent, be concentrated to give one kind
Kermesinus is referred to as capsicum oleoresin, extract yield is generally chilli total amount in the world to orange/red oil
15%.By capsicum oleoresin through ether, ethanol and alkaline aqueous solution, or further extracted with petroleum ether, dichloroethanes equal solvent dense
After contracting, crystallize to obtain thick capsaicine crystallization through petroleum ether or n-hexane.Equipment needed for organic solvent extractionprocess is simple, production cost
It is relatively low, but there is product purity it is poor, have the problems such as peculiar smell, solvent residual amount is high.
(2)Adsorpting column chromatography method:Capsicum oleoresin is extracted with acetone, petroleum ether, 59% ethanol, then knot is used as using ether
Brilliant solvent, obtain thick capsicum cellulose crystal.Crystallized after purification through silica gel column chromatography again, obtain capsaicine sterling.Adsorpting column chromatography method
Recovery rate is relatively low.
(3)Supercritical carbon dioxide extraction method:Fukaya, Kyoo etc. of Japan using supercritical carbon dioxide as solvent, with
Ethanol is entrainer, and temperature is fixed on 50 DEG C, and pressure is 9.8 × l06MPa, be directly isolated to obtain from capsicum 80% or so it is peppery
Green pepper element.Supercritical carbon dioxide extraction method can obtain the capsaicine sterling for having high added value, purity high, but supercritical fluid extracts
Taking technology presently, there are, equipment investment is big, and extraction kettle can not operate continuously, the space-time yield of equipment than relatively low and operation into
The problems such as this is high, thus can be not yet widely used in China in industrial production.
Capsaicine extraction process in China's uses solvent method mostly at present, and extraction step is longer, and crystallization is cumbersome, time-consuming, causes
Resource utilization is low, and cost increases.The universal bad adaptability of extraction process of use, the capsaicine recovery rate of different sources capsicum become
Change is very big, influences industrial-scale production.The adaptability of capsaicin content assay method is also poor, for the capsicum of different sources
And capsaicin product, accuracy, the rate of recovery of its capsaicin content measure change greatly, the final quality determination for influenceing product.Mirror
In above reason, capsicum deep processing producer is more to extract based on capsochrome, and constitute competition fierceness, and annual production only reaches 20 tons
Above production scale could support reluctantly.
The content of the invention
The purpose of this utility model is to provide the equipment that a kind of subcritical fluid extraction technology prepares capsaicine, faced in Asia
Extracted under boundary's environment, extraction temperature is low, does not destroy capsaicine composition, does not aoxidize, and capsaicine leaches complete, internal system heat and handed over
Change, power consumption is low;Technical process is simple, is advantageous to industrialized production;Whole process is completed in the system of closing, to environment without dirt
Dye.Solve that existing extraction process product purity is low, has that peculiar smell, solvent residual amount are high, processing step is longer, crystallization processes are numerous
The problem such as trivial, time-consuming, condition is created for the industrialized production of high-purity capsaicine, to solve what is proposed in above-mentioned background technology
Problem.
To achieve the above object, the utility model provides following technical scheme:A kind of capsaicine subcritical fluid extraction dress
Put, including support, extractor, evaporator, recycle heat device and solvent recycle unit, the support are cube frame-shaped knot
Structure, the cradle top are fixedly installed extractor and evaporator, the internal stent be fixedly installed recycle heat device and
Solvent recycle unit, the extractor turn on the evaporator, recycle heat device and solvent recycle unit respectively.
Preferably, solvent recycle unit includes vavuum pump, compressor, freezing machine and solvent tank, the vavuum pump, compression
Machine, freezing machine and solvent tank are connected in series successively, and the air inlet of the vavuum pump turns on the evaporator, the solvent tank
Liquid outlet connects with the extractor.
Preferably, recycle heat device includes hot-water cylinder and hot recycle pump, the hot-water cylinder and hot recycle pump mutual conduction,
The inlet of the hot-water cylinder turns on the extractor and evaporator respectively, the liquid outlet of hot recycle pump respectively with the extraction
Tank and evaporator conducting.
Preferably, extractor is the cylindrical structure of traverse, and extraction pot bottom is fixed on the cradle top, the extraction
Tank lateral ends are provided with slag-drip opening, and the slag-drip opening is circle, and slag-drip opening outer ledge optional position is hinged with dodge gate, described
Dodge gate lateral profile is identical with the slag-drip opening lateral profile.
Preferably, in addition to supersonic generator, the supersonic generator are fixedly installed on the cradle top, ultrasound
Wave producer turns on the extractor.
Compared with prior art, the beneficial effects of the utility model are:
(1)The cooperation that the utility model passes through support, extractor, evaporator, recycle heat device and solvent recycle unit
Practicality, capsaicine is prepared using subcritical fluid extraction technology, is extracted under subcritical environment, extraction temperature is low, does not destroy peppery
Green pepper element composition, do not aoxidize, capsaicine leaches complete, internal system heat exchange, and power consumption is low;Technical process is simple, is advantageous to industry
Metaplasia is produced;Whole process is completed in the system of closing, environmentally safe.Solve existing extraction process product purity it is low,
Have that peculiar smell, solvent residual amount are high, processing step is longer, crystallization processes are cumbersome, the problem such as time-consuming, are the industry of high-purity capsaicine
Metaplasia production creates condition.
(2)Extraction temperature is low under subcritical environment, does not destroy capsaicine composition, does not aoxidize, and capsaicine leaches complete, power consumption
It is low, it is environmentally safe.Subcritical fluid extraction technology can continuous production.Extraction rate is fast, efficiency high, can be suitably used for modernizing
Consecutive production.Extraction accessory substance is comprehensively utilized, and is processed into the various food such as chilli powder, chilli cake, capsicum haw sheet, whole
Individual production process is without waste discharge.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the embodiment of the utility model is carried out
Clearly and completely describing, it is clear that described embodiment is only the utility model part of the embodiment, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made
The every other embodiment obtained, belong to the scope of the utility model protection.
Referring to Fig. 1, the utility model provides a kind of technical scheme:A kind of capsaicine subcritical fluid extraction device, bag
Support 1, extractor 2, evaporator 3, recycle heat device 4 and solvent recycle unit 5 are included, the support 1 is cube frame-shaped knot
Structure, the top of support 1 are fixedly installed extractor 2 and evaporator 3, recycle heat dress are fixedly installed inside the support 1
Put 4 and solvent recycle unit 5, the extractor 2 respectively with the evaporator 3, recycle heat device 4 and solvent recycle unit 5
Conducting.It is practical by the cooperation of support 1, extractor 2, evaporator 3, recycle heat device 4 and solvent recycle unit 5, utilize Asia
Supercritical fluid extraction technology prepares capsaicine, is extracted under subcritical environment, and extraction temperature is low, does not destroy capsaicine composition, no
Oxidation, capsaicine leach complete, internal system heat exchange, and power consumption is low;Technical process is simple, is advantageous to industrialized production;Entirely
Process is completed in the system of closing, environmentally safe.Solve that existing extraction process product purity is low, has peculiar smell, solvent
Residual quantity is high, processing step is longer, and crystallization processes are cumbersome, the problem such as time-consuming, are that the industrialized production of high-purity capsaicine is created
Condition.
Therein, solvent recycle unit 5 includes vavuum pump 5a, compressor 5b, freezing machine 5c and solvent tank 5d, the vacuum
Pump 5a, compressor 5b, freezing machine 5c and solvent tank 5d are connected in series successively, air inlet and the evaporator of the vavuum pump 5a
3 conductings, the liquid outlet of the solvent tank 5d connect with the extractor 2.
Recycle heat device 4 includes hot-water cylinder 4a and hot recycle pump 4b, the hot-water cylinder 4a and hot recycle pump 4b phase mutual conductances
Logical, the inlet of the hot-water cylinder 4a turns on the extractor 2 and evaporator 3 respectively, hot recycle pump 4b liquid outlet difference
Turned on the extractor 2 and evaporator 3.
Simultaneously, extractor 2 is the cylindrical structure of traverse, and the bottom of extractor 2 is fixed on the top of support 1, institute
State the lateral ends of extractor 2 and be provided with slag-drip opening 6, the slag-drip opening 6 is circle, and the outer ledge optional position of slag-drip opening 6 is hinged with
Dodge gate 7, the lateral profile of dodge gate 7 are identical with the lateral profile of slag-drip opening 6.
And also include supersonic generator 8 in the utility model, supersonic generator 8 is fixedly installed on the support
1 top, supersonic generator 8 turn on the extractor 2.It is low that extraction temperature under subcritical environment can be given full play of, no
Destroy capsaicine composition, do not aoxidize, capsaicine leaches completely, and power consumption is low, environmentally safe to wait many advantages.Subcritical fluids
Abstraction technique can continuous production.Extraction rate is fast, efficiency high, can be suitably used for modernizing consecutive production.Accessory substance is extracted to carry out
Comprehensive utilization, is processed into the various food such as chilli powder, chilli cake, capsicum haw sheet, whole production process is without waste discharge.
While there has been shown and described that embodiment of the present utility model, for the ordinary skill in the art,
It is appreciated that these embodiments can be carried out with a variety of changes in the case where not departing from principle of the present utility model and spirit, repaiied
Change, replace and modification, the scope of the utility model are defined by the appended claims and the equivalents thereof.
Claims (5)
- A kind of 1. capsaicine subcritical fluid extraction device, it is characterised in that:Including support, extractor, evaporator, recycle heat Device and solvent recycle unit, the support are cube frame like structure, and the cradle top is fixedly installed extractor and steaming Send out tank, the internal stent is fixedly installed recycle heat device and solvent recycle unit, the extractor respectively with the steaming Send out tank, recycle heat device and the conducting of solvent recycle unit.
- A kind of 2. capsaicine subcritical fluid extraction device according to claim 1, it is characterised in that:The solvent circulation Equipment includes vavuum pump, compressor, freezing machine and solvent tank, and the vavuum pump, compressor, freezing machine and solvent tank are serial successively Connection, the air inlet of the vavuum pump turn on the evaporator, and the liquid outlet of the solvent tank connects with the extractor.
- A kind of 3. capsaicine subcritical fluid extraction device according to claim 1, it is characterised in that:The recycle heat Device includes hot-water cylinder and hot recycle pump, the hot-water cylinder and hot recycle pump mutual conduction, and the inlet of the hot-water cylinder is distinguished Turned on the extractor and evaporator, the liquid outlet of hot recycle pump turns on the extractor and evaporator respectively.
- A kind of 4. capsaicine subcritical fluid extraction device according to claim 1, it is characterised in that:The extractor is The cylindrical structure of traverse, extraction pot bottom are fixed on the cradle top, and the extractor lateral ends are provided with slag-drip opening, institute Slag-drip opening is stated as circle, slag-drip opening outer ledge optional position is hinged with dodge gate, the dodge gate lateral profile and the row Cinder notch lateral profile is identical.
- A kind of 5. capsaicine subcritical fluid extraction device according to claim 1, it is characterised in that:Also include ultrasonic wave Generator, the supersonic generator are fixedly installed on the cradle top, and supersonic generator turns on the extractor.
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CN201720561337.9U CN206762316U (en) | 2017-05-19 | 2017-05-19 | A kind of capsaicine subcritical fluid extraction device |
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CN201720561337.9U CN206762316U (en) | 2017-05-19 | 2017-05-19 | A kind of capsaicine subcritical fluid extraction device |
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CN201720561337.9U Expired - Fee Related CN206762316U (en) | 2017-05-19 | 2017-05-19 | A kind of capsaicine subcritical fluid extraction device |
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2017
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Granted publication date: 20171219 Termination date: 20180519 |