CN106350196A - System and method for producing chili oil - Google Patents
System and method for producing chili oil Download PDFInfo
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- CN106350196A CN106350196A CN201610674281.8A CN201610674281A CN106350196A CN 106350196 A CN106350196 A CN 106350196A CN 201610674281 A CN201610674281 A CN 201610674281A CN 106350196 A CN106350196 A CN 106350196A
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- Prior art keywords
- frying
- chilli oil
- fructus capsici
- airing
- extraction
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- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B1/00—Production of fats or fatty oils from raw materials
- C11B1/02—Pretreatment
- C11B1/04—Pretreatment of vegetable raw material
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23D—EDIBLE OILS OR FATS, e.g. MARGARINES, SHORTENINGS, COOKING OILS
- A23D9/00—Other edible oils or fats, e.g. shortenings, cooking oils
- A23D9/007—Other edible oils or fats, e.g. shortenings, cooking oils characterised by ingredients other than fatty acid triglycerides
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23D—EDIBLE OILS OR FATS, e.g. MARGARINES, SHORTENINGS, COOKING OILS
- A23D9/00—Other edible oils or fats, e.g. shortenings, cooking oils
- A23D9/02—Other edible oils or fats, e.g. shortenings, cooking oils characterised by the production or working-up
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23D—EDIBLE OILS OR FATS, e.g. MARGARINES, SHORTENINGS, COOKING OILS
- A23D9/00—Other edible oils or fats, e.g. shortenings, cooking oils
- A23D9/02—Other edible oils or fats, e.g. shortenings, cooking oils characterised by the production or working-up
- A23D9/04—Working-up
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B1/00—Production of fats or fatty oils from raw materials
- C11B1/10—Production of fats or fatty oils from raw materials by extracting
- C11B1/104—Production of fats or fatty oils from raw materials by extracting using super critical gases or vapours
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B1/00—Production of fats or fatty oils from raw materials
- C11B1/10—Production of fats or fatty oils from raw materials by extracting
- C11B1/108—Production of fats or fatty oils from raw materials by extracting after-treatment, e.g. of miscellae
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B3/00—Refining fats or fatty oils
- C11B3/12—Refining fats or fatty oils by distillation
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B9/00—Essential oils; Perfumes
- C11B9/02—Recovery or refining of essential oils from raw materials
- C11B9/022—Refining
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B9/00—Essential oils; Perfumes
- C11B9/02—Recovery or refining of essential oils from raw materials
- C11B9/025—Recovery by solvent extraction
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B9/00—Essential oils; Perfumes
- C11B9/02—Recovery or refining of essential oils from raw materials
- C11B9/027—Recovery of volatiles by distillation or stripping
Abstract
The invention discloses a system and a method for producing chili oil. The system comprises a stir-frying device, an airing device, a smashing device, a frying device, an ultrasonic device, a rectifying device, an extracting device and a separating device. The method includes stir-frying, airing, smashing, frying, ultrasonic treatment, extracting, separating and refining. The system and the method have the advantages that various processing devices are effectively connected with one another, accordingly, the chili oil can be basically automatically produced, large quantities of labor and materials can be reduced, and the production cost can be saved to a great extent; stir-fried chili is aired, accordingly, the uniform content of moisture in the chili can be advantageously controlled, and the oil yield of the chili can be increased; chili powder is subjected to ultrasonic treatment at first, accordingly, the extraction time of the chili powder can be shortened to a great extent, release of oil in cells can be enhanced under vibration effects of ultrasonic waves, a large quantity of oil can be extracted in a promoted manner, and the oil yield of the chili can be increased; peculiar smell in the chili oil can be effectively removed by means of rectifying treatment, and accordingly the quality and aroma of the chili oil can be improved.
Description
Technical field
The present invention relates to edible fat production technical field, it particularly relates to a kind of chilli oil production system and its production
Method.
Background technology
Fructus Capsici is Solanaceae capsicum plants, originates in Central and South America.Because it is nutritious, delicious flavour, and each in the world
Ground is extensively planted, and its yield is only second to Fructus Lycopersici esculenti in solanaceous vegetable.Fructus Capsici is rich in capsaicin, capsorubin, beta-carotene, big
The multiple nutritional components such as the vitamin c of amount.China is Fructus Capsici big producing country, occupies first place in the world, growing area be mainly distributed on Hunan,
Sichuan, Guizhou etc. save.Fructus Capsici is a kind of vegetable of homovitamin c content, wherein contains capsaicin thus has pungent, Ke Yizeng
Plus the appetite of people, Fructus Capsici have fat-reducing, delay atherosclerosiss, reduce cardiopathic effect.Fructus Capsici is due to moisture
Height, be difficult preserve, typically by Fructus Capsici be dried process and chilli preserve, and chilli exist added value relatively low, storage
The shortcomings of space is big, product form is simple.And Fructus Capsici is processed into chilli oil, the original nutritional labeling of Fructus Capsici not only can be retained
And mouthfeel, and make it more preferably delicious, and be easy to store.
At present, chilli oil is mainly prepared using organic solvent extractionprocess by domestic manufacturing enterprise of certain scale.Used
Organic solvent mostly be ethanol, acetone, ether, ethyl acetate, hexane etc..After chilli is pulverized, multiple with organic solvent
Leaching, combining extraction liquid, can be obtained by mainly containing the mixture of capsaicin and capsochrome, the wind of Fructus Capsici after recycling design
Taste material enters in mixture substantially, these mixture blend with base oil again preparation chilli oil.Existing method is prepared peppery
Not only extraction yield is low for green pepper oil, and contains a certain amount of dissolvent residual and special odor etc., its matter in the Fructus Capsici oil product being obtained
Figureofmerit is difficult to meet the requirement of user, have impact on the utilization of Fructus Capsici, constrain chilli oil in the food industry further should
With.In extraction process, loss of effective components is big, few due to heating in production process, and its fragrance matter generates less, lacks chilli oil
Distinctive fragrance.
Content of the invention
In view of this, it is an object of the invention to provide a kind of system that can improve chilli oil extraction yield and fragrance and its
Production method.
The present invention solves above-mentioned technical problem by the following technical programs:
A kind of chilli oil production system, including frying apparatus, airing device, reducing mechanism, frying device, Vltrasonic device,
Rectifier unit, extraction equipment and segregation apparatuss, frying apparatus are arranged on airing device side, and airing device is arranged on parch
The lower section of device material outlet；Reducing mechanism is arranged on airing device opposite side, and the crushing groove of reducing mechanism is arranged on airing
The lower section of device material outlet；The pulverizing trench bottom of reducing mechanism is provided with material outlet, frying device is arranged on pulverizing dress
Put below material outlet；Vltrasonic device is arranged on frying device side, and Vltrasonic device bottom is provided with material outlet, extraction dress
Put the side being arranged on Vltrasonic device, and extraction equipment is connected by pipeline with Vltrasonic device, material passes through pipeline from ultrasonic dress
It is transported in extraction equipment in putting；It is provided with segregation apparatuss below extraction equipment, rectifier unit is connected on segregation apparatuss.
Described frying apparatus include speed adjusting gear, cylinder, support, roller, charging aperture and discharging opening, and speed adjusting gear is arranged
On support, cylinder is arranged on the roller of speed adjusting gear, and electric furnace is arranged on support, and charging aperture and discharging opening are separately positioned on
The both sides of cylinder.
Described airing device includes bracing frame and airing groove, and airing groove is arranged on bracing frame, and airing trench bottom is arranged
There is air vent, the size of this air vent is advisable to guarantee that Fructus Capsici will not pass through from this hole.
Described reducing mechanism includes crushing groove, motor, pulverizes bar and support bar, and support bar is arranged on crushing groove, electricity
Machine is arranged on support bar, and the top pulverizing bar is arranged on motor, and bottom is arranged in crushing groove.
Described pan-fried frying apparatus include bracing frame, electric furnace and pan-fried frying pan, and pan-fried frying pan is arranged on bracing frame, and pan-fried frying pan is just
Lower section is provided with electric furnace.
Described extraction equipment includes extraction tank, refrigeration machine, carbon dioxide steel cylinder and filter, and filter two ends connect respectively
Connect carbon dioxide steel cylinder and refrigeration machine, refrigeration machine is connected by pipeline with extraction tank.
The production method of described chilli oil comprises the following steps:
(1) parch: the red chilli that will be singled out is cut into the Fructus Capsici section of 3～5cm length, is then placed in frying in frying apparatus
System, adjusts temperature and is 120～180 DEG C, and the rotating speed of cylinder is 100～300r/min, and the parch time is 30～50min；
(2) airing: Fructus Capsici good for parch is sent in airing device and carries out airing, adjust temperature and be 20～40 DEG C, relatively
Humidity is 40～60%, and the time is 10～30min；
(3) pulverize: the Fructus Capsici after airing is sent in reducing mechanism and pulverizes, obtain the Fructus Capsici powder that fineness is 30～50 mesh；
(4) fry: Fructus Capsici powder is sent in frying device and be fried, the temperature of frying is 180～240 DEG C, the time is
10～20min；
(5) supersound process: the Fructus Capsici powder after frying is sent into and carries out supersound process in Vltrasonic device, control the work(of ultrasound wave
Rate is 50～300w, and process time is 20～40min；
(6) extract: the Fructus Capsici powder after supersound process is sent in extraction equipment, is passed through liquid carbon dioxide and carries out supercritical
Extraction, extraction temperature is 40～60 DEG C, extracting pressure 20～30mpa, flow 0.3～0.4m3/ h, extraction time is 2～4h；
(7) separate: the material of extraction gained is sent in segregation apparatuss, carbon dioxide separation out and is recycled,
Obtain thick chilli oil；
(8) refine: by thick chilli oil send into rectifier unit in, temperature be 120～150 DEG C, vacuum be 150～
In the rectifier unit of 250pa, distillation 30～50min carries out de- abnormal flavour, obtains final product.
In described step (1), the red chilli that will be singled out is cut into the Fructus Capsici section of 4cm length, is then placed in frying apparatus
Middle parch, adjusts temperature and is 150 DEG C, and the rotating speed of cylinder is 200r/min, and the parch time is 40min.
In described step (2), Fructus Capsici good for parch is sent in airing device and carries out airing, adjust temperature and be 30 DEG C, phase
It is 50% to humidity, the time is 20min.
In described step (4), Fructus Capsici powder is sent in frying device and be fried, the temperature of frying is 200 DEG C, the time is
15min.
In described step (5), the Fructus Capsici powder after frying is sent into and in Vltrasonic device, carries out supersound process, control ultrasound wave
Power is 200w, and process time is 30min.
In described step (6), the Fructus Capsici powder after supersound process is sent in extraction equipment, is passed through liquid carbon dioxide and carries out
Supercritical extraction, extraction temperature is 50 DEG C, extracting pressure 25mpa, flow 0.35m3/ h, extraction time is 3h.
In described step (8), by thick chilli oil send into rectifier unit in, temperature be 130 DEG C, vacuum be 200pa
In rectifier unit, distillation 40min carries out de- abnormal flavour, obtains final product.
The beneficial effects of the present invention is:
1st, the present invention pass through by frying apparatus, airing device, reducing mechanism, frying device, Vltrasonic device, rectifier unit,
Extraction equipment and segregation apparatuss effectively couple together, and substantially achieve automated production, reduce substantial amounts of manpower and materials,
Greatly save the cost of production.
2nd, the frying apparatus of the present invention are drum-type, by controlling certain rotating speed and temperature so that the Fructus Capsici of parch
Moisture ratio is more uniform, is conducive to follow-up processing, improves the quality of chilli oil.
3rd, the present invention, by the Fructus Capsici after parch is carried out airing, is conducive to controlling the moisture of Fructus Capsici uniform, test
Show, control Fructus Capsici uniform moisture to be conducive to improving the oil yield of Fructus Capsici, be conducive to containing the moisture of Fructus Capsici by airing moisture regain
Amount controls uniformly, to increase the oil yield of Fructus Capsici.
4th, the present invention, by first Fructus Capsici powder being carried out supersound process, is imitated using ultrasonic cavitation effect, heat effect and machinery
Effect, when the ul-trasonic irradiation of big energy is in Fructus Capsici powder, makes the cell wall of Fructus Capsici powder and organism rupture in moment, significantly
Shorten the extraction time of Fructus Capsici powder, the effect of vibration of ultrasound wave strengthens the release of intracellular oil content, promote more oils
It is extracted out, thus improve the oil yield of Fructus Capsici.
5th, the present invention passes through for thick chilli oil to carry out rectification process under vacuum conditions, can be effectively by chilli oil
Abnormal flavour removes, and improves quality and the fragrance of chilli oil.
More than synthesis, using the chilli oil of chilli oil method of the present invention production, extraction yield is 12.2～13.8%, chilli oil
Color be peony, there is strong fragrant spicy, and no other abnormal flavour.
Brief description
Fig. 1 is the structural representation of chilli oil production system of the present invention.
In figure: 1～frying apparatus；101～support；102～speed adjusting gear；103～charging aperture；104～cylinder；105～
Electric furnace；106～roller；107～discharging opening；2～airing device；201～airing groove；202～bracing frame；3～reducing mechanism；
301～motor；302～support bar；303～crushing groove；304～pulverize bar；4～frying device；401～decoct frying pan；402～electricity
Stove；403～bracing frame；5～rectifier unit；6～Vltrasonic device；7～segregation apparatuss；8～extraction equipment；801～carbon dioxide
Steel cylinder；802～extraction tank；803～filter；804～refrigeration machine.
Specific embodiment
Those skilled in the art understands for convenience, below in conjunction with embodiment and accompanying drawing, the present invention is done further
Description.Embodiment is only illustration to this invention, is not limitation of the invention, does not make to illustrate in embodiment
Step is all prior art, and here is not described in detail.
Embodiment one
As shown in figure 1, a kind of chilli oil production system, including frying apparatus 1, airing device 2, reducing mechanism 3, frying dress
Put 4, Vltrasonic device 6, rectifier unit 5, extraction equipment 8 and segregation apparatuss 7.
Described frying apparatus 1 include speed adjusting gear 102, electric furnace 105, cylinder 104, support 101, roller 106, charging aperture
103 and discharging opening 107, speed adjusting gear 102 is arranged on support 101, and cylinder 104 is arranged on the roller 106 of speed adjusting gear 102
On, electric furnace 105 is arranged on support 101, and charging aperture 103 and discharging opening 107 are separately mounted to the both sides of cylinder 104.
Described airing device 2 includes bracing frame 202 and airing groove 201, and airing groove 201 is arranged on bracing frame 202, stand
Groove 201 bottom of drying in the air is provided with air vent, and the size of this air vent is advisable with guaranteeing that Fructus Capsici will not pass through from this hole.
Described reducing mechanism 3 includes crushing groove 303, motor 301, pulverizes bar 304 and support bar 302, and support bar 302 is pacified
It is contained on crushing groove 303, motor 301 is arranged on support bar 302, the top pulverizing bar 304 is arranged on motor 301, bottom
It is arranged in crushing groove 303.
Described pan-fried frying apparatus 4 include bracing frame 403, electric furnace 402 and pan-fried frying pan 401, and pan-fried frying pan 401 is arranged on bracing frame
On 403, the underface of pan-fried frying pan 401 is provided with electric furnace 402.
Described extraction equipment 8 includes extraction tank 802, refrigeration machine 804, carbon dioxide steel cylinder 801 and filter 803, mistake
Filter 803 two ends connect carbon dioxide steel cylinder 801 and refrigeration machine 804 respectively, and refrigeration machine 804 passes through pipeline with extraction tank 802
Connect.
Frying apparatus 1 are arranged on airing device 2 side, and airing device 2 is arranged under frying apparatus 1 material outlet
Side so that material from the discharging opening of frying apparatus 1 out after can enter directly into airing device 2；Reducing mechanism 3 is arranged on
Airing device 2 opposite side, and the crushing groove 303 of reducing mechanism 3 is arranged on the lower section of airing device 2 material outlet, so that material
From airing device 2 out after can enter directly into reducing mechanism 3 and pulverized；Crushing groove 303 bottom in reducing mechanism 3
Have material outlet, frying device 4 is arranged on below reducing mechanism 3 material outlet, so that material is after reducing mechanism 3 is out
Enter directly in frying device 4；Vltrasonic device 6 is arranged on frying device 4 side, is provided with material in Vltrasonic device 6 bottom
Outlet, extraction equipment 8 is arranged on the side of Vltrasonic device 6, and extraction equipment 8 is connected by pipeline with Vltrasonic device 6, and material leads to
Piping is transported in extraction equipment 8 from Vltrasonic device 6；Segregation apparatuss 7 are installed below extraction equipment 8, material can
Enter directly in segregation apparatuss 7 from extraction equipment 8, rectifier unit 5 is connected on segregation apparatuss 7, material can fill from separating
Put and enter directly in 7 in rectifier unit 5.
Embodiment two
The production method of chilli oil:
(1) parch: the red chilli that will be singled out is cut into the Fructus Capsici section of 3cm length, is then placed in parch in frying apparatus,
Adjust temperature and be 120 DEG C, the rotating speed of cylinder is 100r/min, and the parch time is 30min；
(2) airing: Fructus Capsici good for parch is sent in airing device and carries out airing, adjust temperature and be 20 DEG C, relative humidity
For 40%, the time is 10min；
(3) pulverize: the Fructus Capsici after airing is sent in reducing mechanism and pulverizes, obtain the Fructus Capsici powder that fineness is 30 mesh；
(4) fry: Fructus Capsici powder is sent in frying device and is fried, the temperature of frying is 180 DEG C, the time is 10min；
(5) supersound process: the Fructus Capsici powder after frying is sent into and carries out supersound process in Vltrasonic device, control the work(of ultrasound wave
Rate is 50w, and process time is 20min；
(6) extract: the Fructus Capsici powder after supersound process is sent in extraction equipment, is passed through liquid carbon dioxide and carries out supercritical
Extraction, extraction temperature is 40 DEG C, extracting pressure 20mpa, flow 0.3m3/ h, extraction time is 2h；
(7) separate: the material of extraction gained is sent in segregation apparatuss, carbon dioxide separation out and is recycled,
Obtain thick chilli oil；
(8) refine: by thick chilli oil send into rectifier unit in, temperature be 120 DEG C, vacuum be 150pa rectification dress
Put middle distillation 30min and carry out de- abnormal flavour, obtain final product.
In described step (1), the red chilli that will be singled out is cut into the Fructus Capsici section of 4cm length, is then placed in frying apparatus
Middle parch, adjusts temperature and is 150 DEG C, and the rotating speed of cylinder is 200r/min, and the parch time is 40min.
The chilli oil producing through test, the present embodiment, extraction yield is 12.2%, and the color of chilli oil is peony, has
Strong fragrant spicy, and no other abnormal flavour.
Embodiment three
(1) parch: the red chilli that will be singled out is cut into the Fructus Capsici section of 5cm length, is then placed in parch in frying apparatus,
Adjust temperature and be 180 DEG C, the rotating speed of cylinder is 300r/min, and the parch time is 50min；
(2) airing: Fructus Capsici good for parch is sent in airing device and carries out airing, adjust temperature and be 40 DEG C, relative humidity
For 60%, the time is 30min；
(3) pulverize: the Fructus Capsici after airing is sent in reducing mechanism and pulverizes, obtain the Fructus Capsici powder that fineness is 50 mesh；
(4) fry: Fructus Capsici powder is sent in frying device and is fried, the temperature of frying is 240 DEG C, the time is 20min；
(5) supersound process: the Fructus Capsici powder after frying is sent into and carries out supersound process in Vltrasonic device, control the work(of ultrasound wave
Rate is 300w, and process time is 40min；
(6) extract: the Fructus Capsici powder after supersound process is sent in extraction equipment, is passed through liquid carbon dioxide and carries out supercritical
Extraction, extraction temperature is 60 DEG C, extracting pressure 30mpa, flow 0.4m3/ h, extraction time is 4h；
(7) separate: the material of extraction gained is sent in segregation apparatuss, carbon dioxide separation out and is recycled,
Obtain thick chilli oil；
(8) refine: by thick chilli oil send into rectifier unit in, temperature be 150 DEG C, vacuum be 250pa rectification dress
Put middle distillation 50min and carry out de- abnormal flavour, obtain final product.
The chilli oil producing through test, the present embodiment, extraction yield is 12.7%, and the color of chilli oil is peony, has
Strong fragrant spicy, and no other abnormal flavour.
Example IV
(1) parch: the red chilli that will be singled out is cut into the Fructus Capsici section of 4cm length, is then placed in parch in frying apparatus,
Adjust temperature and be 150 DEG C, the rotating speed of cylinder is 200r/min, and the parch time is 40min；
(2) airing: Fructus Capsici good for parch is sent in airing device and carries out airing, adjust temperature and be 30 DEG C, relative humidity
For 50%, the time is 20min；
(3) pulverize: the Fructus Capsici after airing is sent in reducing mechanism and pulverizes, obtain the Fructus Capsici powder that fineness is 40 mesh；
(4) fry: Fructus Capsici powder is sent in frying device and is fried, the temperature of frying is 200 DEG C, the time is 15min；
(5) supersound process: the Fructus Capsici powder after frying is sent into and carries out supersound process in Vltrasonic device, control the work(of ultrasound wave
Rate is 200w, and process time is 30min；
(6) extract: the Fructus Capsici powder after supersound process is sent in extraction equipment, is passed through liquid carbon dioxide and carries out supercritical
Extraction, extraction temperature is 50 DEG C, extracting pressure 25mpa, flow 0.35m3/ h, extraction time is 3h；
(7) separate: the material of extraction gained is sent in segregation apparatuss, carbon dioxide separation out and is recycled,
Obtain thick chilli oil；
(8) refine: by thick chilli oil send into rectifier unit in, temperature be 130 DEG C, vacuum be 200pa rectification dress
Put middle distillation 440min and carry out de- abnormal flavour, obtain final product.
The chilli oil producing through test, the present embodiment, extraction yield is 13.8%, and the color of chilli oil is peony, has
Strong fragrant spicy, and no other abnormal flavour.
The above, be only the preferable example of the present invention, and not the present invention is made with any pro forma restriction, any does not take off
From technical solution of the present invention content, any simple modification above example made according to the technical spirit of the present invention, conversion material
Material equivalent variations and modification, all still fall within the range of technical solution of the present invention.
Claims (10)
1. a kind of chilli oil production system it is characterised in that: include frying apparatus (1), airing device (2), reducing mechanism (3),
Frying device (4), Vltrasonic device (6), rectifier unit (5), extraction equipment (8) and segregation apparatuss (7), frying apparatus (1) set
Put in airing device (2) side, and airing device (2) is arranged on the lower section of frying apparatus (1) material outlet；Reducing mechanism (3)
It is arranged on airing device (2) opposite side, and reducing mechanism (3) is arranged on the lower section of airing device (2) material outlet；Pulverizing dress
Put (3) bottom and have material outlet, frying device (4) is arranged on below reducing mechanism (3) material outlet；Vltrasonic device (6) sets
Put in frying device (4) side, Vltrasonic device (6) bottom is provided with material outlet, extraction equipment (8) is arranged on Vltrasonic device
(6) side, and extraction equipment (8) is connected by pipeline with Vltrasonic device (6)；It is provided with below extraction equipment (8) and separate
Device (7), rectifier unit (5) is connected on segregation apparatuss (7).
2. chilli oil production system as claimed in claim 1 it is characterised in that: described frying apparatus (1) include speed adjusting gear
(102), electric furnace (105), cylinder (104), support (101), roller (106), charging aperture (103) and discharging opening (107), speed governing
Mechanism (102) is arranged on support (101), and cylinder (104) is arranged on the roller (106) of speed adjusting gear (102), electric furnace
(105) it is arranged on support () 101, charging aperture (103) and discharging opening (107) are separately positioned on the both sides of cylinder (104).
3. chilli oil production system as claimed in claim 1 it is characterised in that: described reducing mechanism (3) includes crushing groove
(303), motor (301), pulverizing bar (304) and support bar (302), support bar (302) is arranged on crushing groove (303), electricity
Machine (301) is arranged on support bar (302), and the top pulverizing bar (304) is arranged on motor (301), and bottom is arranged on pulverizing
In groove (303).
4. chilli oil production system as claimed in claim 1 it is characterised in that: described extraction equipment (8) includes extraction tank
(802), refrigeration machine (804), carbon dioxide steel cylinder (801) and filter (803), filter (803) two ends connect two respectively
Carbonoxide steel cylinder (801) and refrigeration machine (804), refrigeration machine (804) is connected by pipeline with extraction tank (802).
5. chilli oil production system as described in Claims 1 to 4 any one produce chilli oil method it is characterised in that:
Comprise the following steps:
(1) parch: the red chilli that will be singled out is cut into the Fructus Capsici section of 3～5cm length, is then placed in parch in frying apparatus,
Adjust temperature and be 120～180 DEG C, the rotating speed of cylinder is 100～300r/min, and the parch time is 30～50min；
(2) airing: Fructus Capsici good for parch is sent in airing device and carries out airing, adjust temperature and be 20～40 DEG C, relative humidity
For 40～60%, the time is 10～30min；
(3) pulverize: the Fructus Capsici after airing is sent in reducing mechanism and pulverizes, obtain the Fructus Capsici powder that fineness is 30～50 mesh；
(4) fry: Fructus Capsici powder to be sent in frying device and be fried, the temperature of frying is 180～240 DEG C, the time is 10～
20min；
(5) supersound process: the Fructus Capsici powder after frying is sent into and carries out supersound process in Vltrasonic device, the power of control ultrasound wave is
50～300w, process time is 20～40min；
(6) extract: the Fructus Capsici powder after supersound process is sent in extraction equipment, is passed through liquid carbon dioxide and carries out supercritical extraction
Take, extraction temperature is 40～60 DEG C, extracting pressure 20～30mpa, flow 0.3～0.4m3/ h, extraction time is 2～4h；
(7) separate: the material of extraction gained is sent in segregation apparatuss, carbon dioxide separation out and is recycled, obtains slightly
Chilli oil；
(8) refine: by thick chilli oil send into rectifier unit in, temperature be 120～150 DEG C, vacuum be 150～250pa's
In rectifier unit, distillation 30～50min carries out de- abnormal flavour, obtains final product.
6. chilli oil production system as claimed in claim 5 produce chilli oil method it is characterised in that: described step (1)
In, the red chilli that will be singled out is cut into the Fructus Capsici section of 4cm length, is then placed in parch in frying apparatus, and adjusting temperature is 150
DEG C, the rotating speed of cylinder is 200r/min, and the parch time is 40min.
7. chilli oil production system as claimed in claim 5 produce chilli oil method it is characterised in that: described step (2)
In, good for parch Fructus Capsici is sent in airing device and carries out airing, adjusts temperature and be 30 DEG C, relative humidity is 50%, the time is
20min.
8. chilli oil production system as claimed in claim 5 produce chilli oil method it is characterised in that: described step (4)
In, Fructus Capsici powder is sent in frying device and is fried, the temperature of frying is 200 DEG C, the time is 15min.
9. chilli oil production system as claimed in claim 5 produce chilli oil method it is characterised in that: described step (5)
In, the Fructus Capsici powder after frying is sent into and in Vltrasonic device, carries out supersound process, the power controlling ultrasound wave is 200w, process time
For 30min.
10. chilli oil production system as claimed in claim 5 produce chilli oil method it is characterised in that: described step (6)
In, the Fructus Capsici powder after supersound process is sent in extraction equipment, is passed through liquid carbon dioxide and carries out supercritical extraction, extraction temperature
For 50 DEG C, extracting pressure 25mpa, flow 0.35m3/ h, extraction time is 3h.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610674281.8A CN106350196A (en) | 2016-08-16 | 2016-08-16 | System and method for producing chili oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610674281.8A CN106350196A (en) | 2016-08-16 | 2016-08-16 | System and method for producing chili oil |
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ID=57844821
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| CN201610674281.8A Pending CN106350196A (en) | 2016-08-16 | 2016-08-16 | System and method for producing chili oil |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109652205A (en) * | 2019-01-23 | 2019-04-19 | 广州市国味油脂食品有限公司 | Chilli oil extracting system and its production method |
| CN114317100A (en) * | 2022-01-14 | 2022-04-12 | 四川省食品发酵工业研究设计院有限公司 | Ultrasonic-assisted supercritical extraction tank and preparation method of Sichuan-type chili red oil |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101341966A (en) * | 2008-09-08 | 2009-01-14 | 四川大学 | Lixiviation apparatus for zanthoxylum oil and digestion method |
| CN102807770A (en) * | 2012-07-30 | 2012-12-05 | 江苏科技大学 | Method for preparing paprika red pigment by ultrasonic pre-treatment |
| CN202777912U (en) * | 2012-08-25 | 2013-03-13 | 遵义轩瑞生物科技有限公司 | Device for supercritical CO2 extraction of capsicum oleoresin |
| CN103749743A (en) * | 2013-10-12 | 2014-04-30 | 晨光生物科技集团股份有限公司 | Spicy flavor seasoning oil and preparation method thereof |
| CN104605303A (en) * | 2015-01-16 | 2015-05-13 | 四川川北凉粉饮食文化有限公司 | Chili oil and preparation method thereof |
| CN204560809U (en) * | 2014-03-27 | 2015-08-19 | 成都金大洲实业发展有限公司 | The flow-line equipment of a kind of flavored oils automation processing |
| CN204837813U (en) * | 2015-06-29 | 2015-12-09 | 贵州安顺春来茶业有限公司 | Novel roasting machine |
-
2016
- 2016-08-16 CN CN201610674281.8A patent/CN106350196A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101341966A (en) * | 2008-09-08 | 2009-01-14 | 四川大学 | Lixiviation apparatus for zanthoxylum oil and digestion method |
| CN102807770A (en) * | 2012-07-30 | 2012-12-05 | 江苏科技大学 | Method for preparing paprika red pigment by ultrasonic pre-treatment |
| CN202777912U (en) * | 2012-08-25 | 2013-03-13 | 遵义轩瑞生物科技有限公司 | Device for supercritical CO2 extraction of capsicum oleoresin |
| CN103749743A (en) * | 2013-10-12 | 2014-04-30 | 晨光生物科技集团股份有限公司 | Spicy flavor seasoning oil and preparation method thereof |
| CN204560809U (en) * | 2014-03-27 | 2015-08-19 | 成都金大洲实业发展有限公司 | The flow-line equipment of a kind of flavored oils automation processing |
| CN104605303A (en) * | 2015-01-16 | 2015-05-13 | 四川川北凉粉饮食文化有限公司 | Chili oil and preparation method thereof |
| CN204837813U (en) * | 2015-06-29 | 2015-12-09 | 贵州安顺春来茶业有限公司 | Novel roasting machine |
Non-Patent Citations (1)
| Title |
|---|
| 袁超等: "《辣椒红色素的超声波提取及稳定性研究》", 《河南农业大学学报》 * |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109652205A (en) * | 2019-01-23 | 2019-04-19 | 广州市国味油脂食品有限公司 | Chilli oil extracting system and its production method |
| CN109652205B (en) * | 2019-01-23 | 2021-11-30 | 广州市国味油脂食品有限公司 | Chilli oil extraction system and production method thereof |
| CN114317100A (en) * | 2022-01-14 | 2022-04-12 | 四川省食品发酵工业研究设计院有限公司 | Ultrasonic-assisted supercritical extraction tank and preparation method of Sichuan-type chili red oil |
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