CN109652205A - Chilli oil extracting system and its production method - Google Patents
Chilli oil extracting system and its production method Download PDFInfo
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- CN109652205A CN109652205A CN201910063735.1A CN201910063735A CN109652205A CN 109652205 A CN109652205 A CN 109652205A CN 201910063735 A CN201910063735 A CN 201910063735A CN 109652205 A CN109652205 A CN 109652205A
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- flue
- boiler
- stirred tank
- pipe
- heating tube
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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
- C11B1/10—Production of fats or fatty oils from raw materials by extracting
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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
-
- 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
Abstract
The present invention relates to a kind of chilli oil extracting systems, including boiler and stirred tank, the circulation pipe of circulation is provided between stirred tank and boiler, circulation pipe includes flowline, oil inlet pipe and heating tube, the heating tube is arranged between the flowline and oil inlet pipe, the heating tube is heated in boiler by boiler, and the flowline and oil inlet pipe are connected to inside the stirred tank；Stirred tank upper end is provided with feed inlet, and feed inlet is hinged with flip lid；Strainer is removably connected in stirred tank, the strainer is arranged between the flowline and oil inlet pipe.By above-mentioned setting, reduce the solid matter content flowed in circulating line, to reduce the phenomenon that solid matter overheats coking in heating tube, improves the quality and mouthfeel of chilli oil.Compared to existing in such a way that worker's manpower stirs, flip lid improves the condition that chilli oil is isolated with external environment, to improve the production sanitary condition in capsicum oil production process, and then improves the quality of chilli oil.
Description
Technical field
Technical field of the present invention, more particularly, to a kind of chilli oil extracting system and its production method.
Background technique
The raw material that chilli oil extraction at present generally uses is capsicum, soybean oil, various seasonings etc., the extraction process of use
Capsicum, soybean oil and seasoning are generally placed on heating stirring in extraction kettle, until effectively by capsaicine in capsicum etc.
Constituents extraction comes out.
Existing extraction kettle includes the heating system below extraction kettle, is generally heated by combustion of fossil fuels etc.,
By the chilli oil of generation from the flowline below extraction kettle after the raw material such as capsicum heating stirring certain time length in extraction kettle
It takes out.It is additionally provided with filter screen in extraction kettle, raw material residue and chilli oil are separated.There is heating not in existing such extraction kettle
, easy hot-spot makes the case where capsicum coking, reduces the quality and mouthfeel of chilli oil；And it is generally logical in existing technique
Worker's stirring paddle stirring is crossed, this agitating mode makes chilli oil exposure in the environment, reduces the quality of chilli oil, and capsicum
Smell is choked nose in oily heating process, is unfavorable for workers ' health, there are certain rooms for improvement for the above deficiency.
Summary of the invention
In view of the deficiencies of the prior art, the present invention intends to provide a kind of chilli oil extracting system and its production
Method makes heating, stirring to capsicum more uniform by way of separating heating and stirring, reduces the feelings of raw material coking
Condition, and process chinese raw materials is relatively isolated with external environment, improves the production sanitary condition of chilli oil.
To achieve the above object, the present invention provides the following technical scheme that
A kind of chilli oil extracting system, including boiler and stirred tank, are provided with circulation between the stirred tank and boiler
Circulation pipe, the circulation pipe include flowline, oil inlet pipe and heating tube, and the heating tube is arranged in the flowline and oil inlet pipe
Between, the heating tube is heated in boiler by boiler, and the flowline and oil inlet pipe are connected to inside the stirred tank, institute
State the level height that flowline is higher than oil inlet pipe and stirred tank communicating position with the level height of stirred tank communicating position；It is described to stir
It mixes kettle upper end and is provided with feed inlet, the feed inlet is hinged with flip lid；The stirring dress being driven by motor is provided in the stirred tank
It sets, strainer is removably connected in the stirred tank, the strainer is arranged between the flowline and oil inlet pipe, and is lower than and stirs
Mix device；The flowing of the circulation liquid in pipe is driven by circulating pump.
By above-mentioned setting, the circulation pipe for the chilli oil that circulates is provided between boiler and stirred tank, circulation pipe is logical
It crosses liquid in circulating pump driving tube to flow, circulation pipe is divided into flowline, oil inlet pipe and heating tube according to position, wherein heating tube position
Between flowline and oil inlet pipe, and heating tube is located in boiler, carries out heating to heating tube by boiler to realization pair
The heating of chilli oil in circulation pipe.Wherein flowline and oil inlet pipe are connected to stirred tank inside, and flowline is arranged and stirs
Mix the communicating position of kettle level height be higher than oil inlet pipe and stirred tank communicating position level height.It is detachable in stirred tank
It is connected to strainer repeatedly, the agitating device being driven by motor is provided in stirred tank, the raw material in stirred tank are caught by strainer
And raw material slag, and by stirred tank solid and liquid separate, agitating device is then used for the raw material and raw material in stirred tank
Slag is stirred, and keeps the extraction to the effective component in capsicum or various seasonings more thorough, so improve produce it is peppery
The quality of green pepper oil.Wherein, strainer being arranged between flowline and oil inlet pipe, solid matter is isolated on the upside of strainer by strainer,
The liquid of circulation pipe, which flows to, enters stirred tank from flowline for chilli oil, passes through strainer, enters in boiler from oil inlet pipe outflow and adds
Heat, then flowed out from flowline, to reduce the solid matter flowed in circulating line by filtering of the strainer to solid matter
Content improves the quality and mouthfeel of chilli oil to reduce the phenomenon that solid matter overheats coking in heating tube.By strainer
Setting contacts below agitating device and not with agitating device, avoids agitating device from tangling with strainer, influences filter effect.Stirring
Kettle upper end is provided with feed inlet, and the disengaging of raw material or raw material slag is passed through from feed inlet, is hinged in feed inlet and blocks feed inlet
Flip lid because being stirred by motor driven agitating device, compared to existing in such a way that worker's manpower stirs, flip lid
The condition that chilli oil is isolated with external environment is improved, to improve the production sanitary condition in capsicum oil production process, in turn
Improve the quality of chilli oil.
The present invention is further arranged, and the boiler includes the flue of shell and setting inside the shell, and the boiler face is opened
Have the fuel port being connected to the burner hearth of the flue, between the flue and boiler jacket between be separated with flue, the flue package
The flue, the flue are provided with smoke pipe, the smoke pipe connection burner hearth and flue, the boiler jacket far from the side of fuel port
Perforation is provided with the cleaning door of connection flue.
By above-mentioned setting, boiler is provided with the flue of shell and setting inside the shell, and boiler face is provided with and flue
The fuel port of burner hearth connection, formation flue spaced apart between flue lateral wall and boiler jacket, flue package flue are set
It sets, flue is provided with several smoke pipes in the side far from fuel port, and smoke pipe is for being connected to burner hearth and flue, to make burner hearth fuel
The high-temperature flue gas generated that burns enters flue from smoke pipe, and boiler jacket perforation is provided with the cleaning door of connection flue, cleaning door with
Smoke pipe forming circuit passes through flue for flue gas.The setting that flue is wrapped up by flue, increases logical circulation road of the flue gas in boiler
Diameter increases time of the high-temperature flue gas in boiler, and forms insulating layer to flue by flue, and then reduces flue gas discharge
Heat when boiler, is deposited in heat in boiler as much as possible, and then improves heating effect of the boiler to heating tube, Yi Jiqi
To the effect for saving fuel.
The present invention is further arranged, and the heating tube winding is arranged on the furnace wall of the flue, and the heating tube is straight
Diameter is greater than the thickness of the furnace wall, and the heating tube protrudes some in burner hearth and flue respectively.
By above-mentioned setting, the form that heating tube is wound is arranged on the furnace wall of flue, and heating tube is arranged
Diameter be greater than furnace wall wall thickness, heating tube and furnace wall are fixed as one, heating tube is protruded to some respectively in furnace
In thorax and flue, even if heating tube distinguishes some and the mouth flue gas in burner hearth and the smoke contacts in flue, to improve
The contact area of flue gas and heating tube keeps heating tube two sides heated, improves the heating surface area of heating tube, and then improve combustion
The heat utilization rate of material, to improve the utilization of fuel in the case that chilli oil in heat cycles pipe is to certain temperature
Rate reduces fuel cost, thereby reduces the production cost of enterprise's production chilli oil.
The present invention is further arranged, and communicating pipe, the connection are provided between the heating tube being wrapped on the furnace wall
Pipe is connected to heating tube head and the tail both ends, is arranged close to fuel port the communicating pipe.
By above-mentioned setting, it is provided with communicating pipe between the heating tube being wrapped on furnace wall, communicating pipe is by heating tube
The connection of head and the tail both ends, to make to be formed into a loop between the heating tube wound, chilli oil can circulate between the circuit of heating tube,
Residence time of the chilli oil in boiler is improved, and then keeps heating more abundant, rate of rise in temperature faster, and improves circulation
More expansion spaces can be reserved for chilli oil heating expansion, reduce impact of the chilli oil expansion to circulating pump.
The present invention is further arranged, and the heating tube top is communicated with flowline, and the heating bottom of the tube is communicated with oil inlet
Pipe.
By above-mentioned setting, because heating tube is wrapped on flue side wall, global shape is similar to flue side wall, and adds
The connection of heat pipe bottom can form circulation loop so that the chilli oil in heating tube be made not flow according to the track of pipeline
It is flowed freely in heating tube.To which flowline to be connected to heating tube top, oil inlet pipe is connected to heating bottom of the tube, makes to recycle
Chilli oil in pipe enters from oil inlet pipe, flows out after being heated in heating tube from flowline, and because chilli oil density with
The raising of temperature gradually decreases, so that the higher chilli oil of temperature can move up, flowline is arranged above oil inlet pipe multiple
Close the proper motion of chilli oil.
The present invention is further arranged, and the flowline is communicated with the escape pipe being vertically arranged, and the escape pipe is provided with gas
The gas outlet of valve, the escape pipe is in communication with the outside, and the height of the gas outlet is much higher than the height of flowline.
By above-mentioned setting, position of the flowline above boiler is communicated with the escape pipe being vertically arranged, escape pipe setting
There is air valve that hole is opened and closed, the gas outlet of escape pipe is connected to external, and gas outlet volume height is much higher than the height of flowline.Outlet
The setting of pipe can open air valve when the chilli oil extracting system is discharged or inputs chilli oil, be used for balanced recycle pipe
Interior air pressure, inputs chilli oil preferably in circulation pipe, and chilli oil is also enable to be discharged when the extracting system is discharged more thoroughly,
Convenient for recycling chilli oil.
The present invention is further arranged, and the strainer is provided with bound edge, and the bound edge is bonded with the stirred tank inner sidewall, institute
It states bound edge and is connected with several connecting rods, several connecting rods are along the circumferential equidistant arrangement of the bound edge, the connecting rod and institute
Stirred tank is stated to be detachably connected.
By above-mentioned setting, strainer is supported by flexible material, is fixed with bound edge flexible in strainer surrounding, bound edge with stir
The fitting of kettle inner sidewall is mixed, several connecting rods are fixed on bound edge, connecting rod is supportted along the circumferential equidistant arrangement of bound edge by connecting rod
Bound edge and strainer are opened, strainer is made to keep certain shape, to be reduced as far as raw material or raw material slag through strainer and stir
The gap between kettle barrel is mixed, filtration of the strainer to raw material or raw material slag is improved.It is provided with connecting rod and stirred tank
It is detachably connected, convenient for user after chilli oil produces, raw material slag is retained in strainer, is lifted strainer and is taken raw material slag
Topple over out, completes the cleaning to raw material slag in stirred tank.
The present invention is further arranged, and the stirred tank inner sidewall is fixed with guide rail along circumferential surface, and the guide rail is arranged described
Below feed inlet, guide rail upper surface is provided with sliding slot along the track of guide rail, and the connecting rod top is respectively and fixedly provided with limited block, the limit
Position block lower end surface is fixed with the sliding block being engaged by clamping with sliding slot, and the limited block is placed on the guide rail, and the sliding block is in institute
State clamping sliding in sliding slot.
By above-mentioned setting, it is fixed with guide rail along circumferential surface in stirred tank inner sidewall, guide rail upper surface is opened along the track of guide rail
There is sliding slot, guide rail is arranged below feed inlet, and connecting rod top is respectively and fixedly provided with limited block, and the spacing between guide rail and flip lid is greater than
The height of limited block.Limited block lower end surface protrusion is fixed with the sliding block being engaged by clamping with sliding slot, is led by the way that limited block to be placed on
On rail, and sliding block and sliding slot clamping are slided, to realize the positioning and sliding to limited block, connecting rod can be slid into not
It on same position, and then realizes the distracted function of strainer, so that strainer is kept certain shape, play better filter effect.
The present invention is further arranged, and is fixed with connecting rope between several limited blocks.
By above-mentioned setting, connecting rope is fixed between several limited blocks, connecting rope both ends disconnect, so as to draw
Connecting rope collapses the limited block being placed on guide rail different location, plays the effect for facilitating and collapsing strainer, and then conveniently
User clears up raw material slag.
A kind of capsicum oil producing method, comprising the following steps:
(1) raw material are processed: cassia bark are smashed in dry chili dissection to pieces, ginger, garlic are clapped flat；
(2) raw material add bubble hair, stand；
(3) raw material and soybean oil mix in stirred tank；
(4) start circulating pump and boiler: driving soybean oil to recycle in the circulation pipe by circulating pump, the boiler is gradually
Heating, heating rate are 50-60 degrees Celsius/hour；
(5) first time constant temperature extracting: 100 degrees Celsius of constant temperature circulatings in the boiler is kept to extract 30 minutes；
(6) second of constant temperature extractings: being arranged heating rate identical with step (4) in the boiler and be warming up to 160 degrees Celsius,
Constant temperature circulating extracts 40 minutes；
(7) boiler is closed, Temperature fall: circulating pump continues working, until oil temperature closes circulating pump when being down to 60 degrees Celsius；
(8) it filters and shifts chilli oil and stored into storage tank.
Pass through above-mentioned setting, the extraction mode of chilli oil persistent loop, by the heating of chilli oil and the stirring of raw material point
It drives row into, so that it is heated more evenly to make chilli oil, and directly solid matter is not heated and can reduce solid matter coking
The case where, to improve the quality and taste of chilli oil.
In conclusion the invention has the following advantages:
1. by setting boiler and stirred tank and the circulation pipe between boiler and stirring, circulation pipe one section of heating tube therein
It is heated in the boiler, strainer is provided in stirred tank, retained raw material and raw material slag in a stirring kettle, to subtract by strainer
Lack and solid matter has been directly heated, being not easy solid, local heating is excessively high to lead to coking, and then improves chilli oil
Quality and mouthfeel；
2. the flue for being less than boiler jacket by being provided with volume in boiler, forms flue, furnace between flue and boiler jacket
Gallbladder is through with smoke pipe connection flue and flue, and boiler jacket is through with the cleaning door being connected to flue, to be formed in boiler
The exhaust gases passes of burner hearth, flue to cleaning door improve path of the high-temperature flue gas in boiler；Heating tube winding is arranged in furnace
On gallbladder wall, and heating tube two sides some be exposed in burner hearth and flue in, in the flue gas and flue in burner hearth
Flue gas directly contacts, to improve the contact area of heating tube and flue gas, improves the transformation efficiency and fuel of heat
Utilization rate reduce the production cost of enterprise so as to make chilli oil increase same temperature with less fuel；
3. by the way that dismountable strainer is arranged, and lifting strainer by connecting rod, compared to existing by manually pulling stirred tank out
The mode of interior raw material slag, reduces the cleaning difficulty of raw material slag, and keeps the cleaning of raw material slag more thorough, and then improves next
Take turns the quality and mouthfeel of the chilli oil of production.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the present embodiment；
Fig. 2 is the cross-sectional view of boiler in the present embodiment；
Fig. 3 is the cross-sectional view of stirred tank in the present embodiment；
Fig. 4 is the enlarged drawing in Fig. 3 at A.
Appended drawing reference: 1, boiler；11, shell；12, flue；121, smoke pipe；13, flue；14, burner hearth；15, cleaning door；
16, fuel port；2, stirred tank；21, it renovates；22, shaft；23, agitating paddle；24, motor；25, guide rail；251, sliding slot；26, it discharges
Pipe；3, circulation pipe；31, flowline；32, oil inlet pipe；33, heating tube；34, communicating pipe；35, escape pipe；4, strainer；41, bound edge；
42, connecting rod；43, limited block；44, sliding block；45, connecting rope.
Specific embodiment
Below in conjunction with attached drawing, invention is further described in detail.
As shown in Figure 1 to Figure 2, a kind of chilli oil extracting system disclosed by the invention and its production method, including 1 He of boiler
Stirred tank 2, the boiler 1 include shell 11 and the flue 13 being arranged in shell 11, and the volume of flue 13 is less than the outer of boiler 1
Shell 11, between flue 13 and shell 11 between be separated with certain distance formed flue 12.Flue 13 and 1 front of boiler are fixed, and boiler 1 is just
Face is provided with the fuel port 16 being connected to inside flue 13, for adding fuel in flue 13.Flue 13 is far from fuel port 16
Side be through with the smoke pipe 121 being connected to flue 12,1 shell of boiler, 11 side is through with the cleaning door 15 of connection flue 12,
To make burner hearth 14, smoke pipe 121, flue 12, the cleaning door 15 of flue 13 form the access to circulate for flue gas, make in burner hearth 14
The flue gas of burning is discharged after smoke pipe 121, flue 12 from cleaning door 15.Make the higher flue gas packet of temperature by the setting of flue 12
Flue 13 is wrapped up in, burner hearth 14 is formed and is kept the temperature, and increases path of the flue gas in boiler 1, temperature when flue gas is discharged is most
It is possibly low, the more heats of flue gas are retained in boiler 1.
The circulation pipe 3 for recycling chilli oil is provided between boiler 1 and stirred tank 2, circulation pipe 3 is according to opposite boiler 1
The difference of location is divided into flowline 31, oil inlet pipe 32 and heating tube 33, and wherein heating tube 33 is arranged in 31 He of flowline
Between oil inlet pipe 32, heating tube 33 is arranged in boiler 1, is heated heating tube 33 in circulation pipe 3 by boiler 1
Chilli oil heated.Flowline 31 and oil inlet pipe 32 are connected to stirred tank 2, wherein the company of flowline 31 and stirred tank 2
The level height of logical position is higher than the communicating position of oil inlet pipe 32 and stirred tank 2.Chilli oil in circulation pipe 3 is driven by circulating pump
Circulation is moved, wherein the circulation path of the chilli oil in circulation pipe 3 are as follows: be circulated in boiler 1 along stirred tank 2 by oil inlet pipe 32
Heating tube 33, chilli oil is flowed out from flowline 31 after heating tube 33 completes heating, inside 31 other end of flowline and stirred tank 2
Connection, forming circuit.
Wherein heating tube 33, which is wrapped like, is fixed on 13 wall of flue, and the diameter that heating tube 33 is arranged is greater than flue 13
The thickness of wall, thus make heating tube 33 13 wall two sides of flue protrude some respectively with flue 12 in flue gas and burner hearth
Smoke contacts in 14.Contact of the heating tube 33 with high-temperature flue gas is increased by the heating tube 33 of winding setting, and then is improved
Heat exchanger effectiveness, wherein heating tube 33 two sides are heated in burner hearth 14 and in flue 12 respectively, are further increased pair
The utilization rate of the heat of flue gas in flue 12 is improving identical chilli oil phase to compare the mode of existing heated on one side
In the case where same temperature, less fuel need to be only used, the utilization rate of fuel is improved, reduce enterprise's production chilli oil
Production.
Heating tube 33 is wrapped like and integrally similar with the shape of flue 13, is provided in the position close to fuel port 16
Communicating pipe 34, communicating pipe 34 are connected to the head and the tail both ends of heating tube 33, so that heating tube 33 itself be made to be formed into a loop, improve capsicum
Cycle period and time of the oil in heating tube 33, and then the heating rate of chilli oil is improved, and make chilli oil in heating tube
The setting of installation pipeline is not circulated in 33.Flowline 31 is connected to the top of heating tube 33, oil inlet pipe 32 is connected to
The bottom of heating tube 33, so that the chilli oil for completing heating pumps out boiler 1 from top, into stirred tank 2, temperature is lower peppery
Green pepper oil enters boiler 1 from bottom and is heated, and the movement of chilli oil is identical as the density stratification direction of chilli oil, temperature compared with
The lower top positioned at heating tube 33 of high chilli oil Density Density, conducive to the circulation of chilli oil.
Flowline 31 is provided with vertical escape pipe 35 above boiler 1, and escape pipe 35 is provided with Air Valve Control escape pipe
35 opening and closing, the gas outlet of escape pipe 35 are connected to external, and the height of gas outlet is arranged much higher than flowline 31
Height.Through the setting of escape pipe 35 when soybean oil or discharge finished product chilli oil is perfused, air valve balanced recycle can be opened
Air pressure in pipe 3, so that it is more smooth to make soybean oil or chilli oil circulate in circulation pipe 3, it is not easy to remain bubble, reduction pair
The damage of circulating pump.
As shown in Figure 3 to Figure 4,2 top of stirred tank is provided with feed inlet, for raw material and clear material raw material slag to be added,
Feed inlet is hinged with covering and covers to feed inlet, improves the isolation effect of the chilli oil and external environment inside stirred tank 2,
To improve the sanitary grade of the chilli oil extracting system, and reduce the popularity taste pair of choking that capsicum generates during heating
The influence of worker.
Stirred tank 2 is provided with agitating device, and agitating device includes protruding into stirred tank 2 with the vertical of the rotation connection of stirred tank 2
Interior shaft 22 is fixed with several agitating paddles 23 in shaft 22, and shaft 22 has motor 24 to be driven, by agitating device to original
Material is stirred, and improves the contact effects of the raw material with soybean oil such as capsicum, and then improve to the effective component in capsicum such as
The extraction effect of capsaicine etc..
Strainer 4 is wherein removably connected in stirred tank 2, strainer 4 is made up of flexible material, and strainer 4 is to raw material
It is filtered with raw material slag, strainer 4 is arranged between flowline 31 and oil inlet pipe 32 and does not contact with agitating device.Strainer 4 four
It is fixed with bound edge 41 week, bound edge 41 is bonded with 2 inner sidewall of stirred tank, reduces raw material and raw material slag out of strainer 4 and stirred tank 2
Gap between side wall passes through.Equidistantly be arranged with several connecting rods 42 along bound edge 41 is circumferential on bound edge 41,42 lower end of connecting rod with
Bound edge 41 is fixed, and 42 upper end of connecting rod is fixed with limited block 43.2 inner sidewall of stirred tank is fixed with guide rail 25, guide rail 25 along circumferential surface
It is arranged below feed inlet, the spacing between guide rail 25 and flip lid 21 is greater than the height of limited block 43, and 25 upper surface of guide rail edge is led
The track of rail 25 is provided with sliding slot 251, and 43 lower end surface of limited block is fixed with the sliding block 44 being engaged by clamping with card slot, by by limited block
43 placements make sliding block 44 be clamped sliding between sliding slot 251 on the slide rail, realize the limit to connecting rod 42, and then pass through company
Extension bar 42 struts strainer 4, keeps the filtering to the solid matter in stirred tank 2.It connects and is fixed between several limited blocks 43
Connecting rope 45,45 both ends of connecting rope disconnect, and so as to be gathered several limited blocks 43 by drawing connecting rope 45, and then realize
Connecting rod 42 and strainer 4 are gathered, it is complete convenient for users to lifting strainer 4 and the raw material slag in strainer 4 being proposed stirred tank 2
The cleaning of raw material slag in pairs of stirred tank 2.
The implementation principle of the present embodiment are as follows:
Using the chilli oil extracting system production chilli oil method the following steps are included:
(1) raw material are processed: by dry chili dissection in 10mm or so size, cassia bark is smashed to pieces in 20mm or so size, ginger,
Garlic is clapped flat；
(2) raw material add bubble hair, stand 20 hours；
(3) raw material being soaked and soybean oil are mixed in stirred tank 2；
(4) start circulating pump and boiler 1: driving soybean oil to recycle in the circulation pipe 3 by circulating pump, the pot is set
Furnace 1 is gradually warmed up, and heating rate is 50-60 degrees Celsius/hour；
(5) first time constant temperature extracting: 100 degrees Celsius of constant temperature circulatings in the boiler 1 is kept to extract 30 minutes；
(6) second of constant temperature extractings: heating rate identical with step (4) in the boiler 1 is arranged, and to be warming up to 160 Celsius
Degree, constant temperature circulating extract 40 minutes；
(7) boiler 1 is closed, Temperature fall: circulating pump continues working 20 hours or so, until closing when oil temperature is down to 60 degrees Celsius
Circulating pump；
(8) it filters and shifts chilli oil and stored into storage tank.
This specific embodiment is only explanation of the invention, is not limitation of the present invention, those skilled in the art
Member can according to need the modification that not creative contribution is made to the present embodiment after reading this specification, but as long as at this
All by the protection of Patent Law in the scope of the claims of invention.
Claims (10)
1. a kind of chilli oil extracting system, including boiler (1) and stirred tank (2), it is characterized in that: the stirred tank (2) and boiler
(1) circulation pipe (3) of circulation is provided between, the circulation pipe (3) includes flowline (31), oil inlet pipe (32) and heating
It manages (33), the heating tube (33) is arranged between the flowline (31) and oil inlet pipe (32), and the heating tube (33) is in pot
It is heated in furnace (1) by boiler (1), the flowline (31) and oil inlet pipe (32) are connected to the stirred tank (2) inside, described
The level height of flowline (31) and stirred tank (2) communicating position is higher than the water of oil inlet pipe (32) and stirred tank (2) communicating position
Flat height；Stirred tank (2) upper end is provided with feed inlet, and the feed inlet is hinged with flip lid (21)；It is set in the stirred tank (2)
It is equipped with the agitating device driven by motor (24), is removably connected with strainer (4) in the stirred tank (2), the strainer (4) sets
It sets between the flowline (31) and oil inlet pipe (32), and is lower than agitating device；The flowing of the interior liquid of the circulation pipe (3) by
Circulating pump driving.
2. chilli oil extracting system according to claim 1, it is characterized in that: the boiler (1) includes shell (11) and sets
The flue (13) in shell (11) is set, boiler (1) front is provided with the combustion being connected to the burner hearth (14) of the flue (13)
Material mouth (16), between the flue (13) and boiler (1) shell (11) between be separated with flue (12), described in the flue (12) package
Flue (13), the flue (13) are provided with smoke pipe (121) far from the side of fuel port (16), and the smoke pipe (121) is connected to burner hearth
(14) and flue (12), boiler (1) shell (11) perforation are provided with the cleaning door (15) of connection flue (12).
3. chilli oil extracting system according to claim 2, it is characterized in that: the heating tube (33) winding is arranged described
On flue (13) wall of flue (13), heating tube (33) diameter is greater than the thickness of the flue (13) wall, the heating tube
(33) some is protruded respectively in burner hearth (14) and flue (12).
4. chilli oil extracting system according to claim 3, it is characterized in that: being wrapped in the heating on the flue (13) wall
It is provided with communicating pipe (34) between pipe (33), the communicating pipe (34) is connected to heating tube (33) head and the tail both ends, the communicating pipe
(34) it is arranged close to fuel port (16).
5. chilli oil extracting system according to claim 4, it is characterized in that: the heating tube (33) top with it is described fuel-displaced
(31) connection is managed, heating tube (33) bottom is connected to the oil inlet pipe (32).
6. chilli oil extracting system according to claim 5, it is characterized in that: the flowline (31) is communicated with and is vertically arranged
Escape pipe (35), the escape pipe (35) is provided with air valve, and the gas outlet of the escape pipe (35) is in communication with the outside, it is described go out
The height of port is much higher than the height of flowline (31).
7. chilli oil extracting system according to claim 1, it is characterized in that: the strainer (4) is provided with bound edge (41), institute
It states bound edge (41) to be bonded with the stirred tank (2) inner sidewall, the bound edge (41) is connected with several connecting rods (42), several described
Connecting rod (42) detachably connects along the circumferential equidistant arrangement of the bound edge (41), the connecting rod (42) with the stirred tank (2)
It connects.
8. chilli oil extracting system according to claim 7, it is characterized in that: the stirred tank (2) inner sidewall is solid along circumferential surface
Surely have guide rail (25), the guide rail (25) is arranged below the feed inlet, track of guide rail (25) upper surface along guide rail (25)
It is provided with sliding slot (251), connecting rod (42) top is respectively and fixedly provided with limited block (43), and limited block (43) lower end surface is fixed with
The sliding block (44) being engaged by clamping with sliding slot (251), the limited block (43) are placed on the guide rail (25), the sliding block (44)
The clamping sliding in the sliding slot (251).
9. chilli oil extracting system according to claim 8, it is characterized in that: being fixed between several limited blocks (43)
Connecting rope (45).
10. it is a kind of using any capsicum oil producing method of claim 1-9, it is characterized in that: the following steps are included:
(1) raw material are processed: cassia bark are smashed in dry chili dissection to pieces, ginger, garlic are clapped flat；
(2) raw material add bubble hair, stand；
(3) raw material and the soybean oil mixing in stirred tank (2)；
(4) start circulating pump and boiler (1): soybean oil circulation in the circulation pipe (3) being driven by circulating pump, institute is set
It states boiler (1) to be gradually warmed up, heating rate is 50-60 degrees Celsius/hour；
(5) first time constant temperature extracting: 100 degrees Celsius of constant temperature circulatings in the boiler (1) is kept to extract 30 minutes；
(6) second of constant temperature extractings: heating rate identical with step (4) in the boiler (1) is arranged, and to be warming up to 160 Celsius
Degree, constant temperature circulating extract 40 minutes；
(7) boiler (1) is closed, Temperature fall: circulating pump continues working, until oil temperature closes circulating pump when being down to 60 degrees Celsius；
(8) it filters and shifts chilli oil and stored into storage tank.
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| CN201910063735.1A CN109652205B (en) | 2019-01-23 | 2019-01-23 | Chilli oil extraction system and production method thereof |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910063735.1A CN109652205B (en) | 2019-01-23 | 2019-01-23 | Chilli oil extraction system and production method thereof |
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| CN109652205A true CN109652205A (en) | 2019-04-19 |
| CN109652205B CN109652205B (en) | 2021-11-30 |
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| CN106350196A (en) * | 2016-08-16 | 2017-01-25 | 张�杰 | System and method for producing chili oil |
| KR101853450B1 (en) * | 2016-11-03 | 2018-04-30 | 진성인덱스트리 주식회사 | Rotary Type Drying Apparatus |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2374813Y (en) * | 1999-03-22 | 2000-04-19 | 宋晓农 | Verticle gas oil heating furnace |
| US7793861B2 (en) * | 2007-01-17 | 2010-09-14 | The Dial Corporation | Piston actuated vapor-dispersing device |
| CN201293458Y (en) * | 2008-11-07 | 2009-08-19 | 徐蓓 | Heat conducting oil heating-furnace |
| KR20110014757A (en) * | 2009-08-06 | 2011-02-14 | 최재교 | Apparatus for loading red pepper powder |
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| CN109652205B (en) | 2021-11-30 |
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