CN208279588U - The dewaxing device of camellia oil - Google Patents
The dewaxing device of camellia oil Download PDFInfo
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- CN208279588U CN208279588U CN201820117286.5U CN201820117286U CN208279588U CN 208279588 U CN208279588 U CN 208279588U CN 201820117286 U CN201820117286 U CN 201820117286U CN 208279588 U CN208279588 U CN 208279588U
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- camellia oil
- pipeline
- autoclave body
- dewaxing device
- crystallization kettle
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Abstract
The utility model belongs to food processing technology field more particularly to a kind of dewaxing device of camellia oil.The utility model, including the crystallization kettle being connected to by pipeline and centrifuge mechanism, the bottom end of pipeline one end connection crystallization kettle, the other end is penetrated through to the inside of centrifuge mechanism, control switch is arranged on pipeline, to open or close pipeline, crystal seed is added mechanism and is connected to the top of crystallization kettle.The utility model is using the waxy solid being precipitated in the method removal camellia oil of centrifuge separation, the methods of suction filtration, filters pressing have higher separative efficiency in compared with the prior art, to improve the efficiency of entire dewaxing process, and the utility model enables the wax being present in camellia oil comparatively fast, to be preferably precipitated by the way that the methods of crystal seed, control heat transfer temperature difference is added.
Description
Technical field
The utility model belongs to food processing technology field more particularly to a kind of dewaxing device of camellia oil.
Background technique
Currently, China not only abounds with the healthy grain and oil such as peanut oil, sunflower oil, the camellia with special role is also abounded with
Oil, camellia oil not only eat deliciousness, and full of nutrition, but contain a certain amount of saturation acid esters in camellia oil, i.e., dystectic
Solid fat, such as hard fatty acids, wax etc., when the temperature is low, saturation acid esters can generate flocculation, influence its presentation quality, therefore
Dewaxing treatment can be all carried out in camellia oil process, in the prior art, the waxy solid in camellia oil is general after being precipitated
It is separated by solid-liquid separation using the methods of suction filtration or filters pressing, but the separative efficiency of this separation method is lower, is not suitable for extensive life
It produces.
For example, Chinese utility model patent disclose a kind of camellia oil dewaxing filter press [application number:
201520667879.5], which includes shell, in shell by shelf be equipped with multiple groups filter plate, filter cloth and every
Film, septation are arranged between filter plate and filter cloth, and filter plate, filter cloth and diaphragm form filters pressing chamber, which is characterized in that filters pressing chamber
High pressure fluid entrances and rinse mouth is arranged in top, and high pressure fluid entrances connect holding vessel by circulating line, and holding vessel connection is set
The discharge port in housing bottom is set, force (forcing) pump is set on circulating line, shell side is equipped with sewage draining exit, is provided with pumping on shell
Vacuum port.
The utility model achievees the purpose that separation of solid and liquid by the way of filters pressing, and such production efficiency is lower, nothing
Method adapts to the needs of large-scale production.
Utility model content
The purpose of this utility model is in view of the above-mentioned problems, providing a kind of dewaxing device of camellia oil.
In order to achieve the above objectives, the utility model uses following technical proposal:
A kind of dewaxing device of camellia oil, including the crystallization kettle being connected to by pipeline and centrifuge mechanism, the pipeline
One end is connected to the bottom end of crystallization kettle, and the other end is penetrated through to the inside of centrifuge mechanism, and control switch is arranged on pipeline, to
Open or close pipeline, crystal seed are added mechanism and are connected to the top of crystallization kettle.
In the dewaxing device of above-mentioned camellia oil, the centrifuge mechanism include shell and positioned at interior of shell from
Heart supporting plate, shell are fixed on the rack, and the centrifugation supporting plate is fixedly connected with rotary shaft, and the axial line of rotary shaft with from
The axial line of heart supporting plate is overlapped, and the outlet of pipeline is located at the surface of centrifugation supporting plate, the driving motor being fixed on the rack
It is drivingly connected by transmission belt and rotary shaft, further includes the vertical filter plate that can be rotated synchronously with rotary shaft, the vertical filter plate
One end is fixedly connected with the edge of centrifugation supporting plate.
In the dewaxing device of above-mentioned camellia oil, there is cavity, centrifugation between the vertical filter plate and the inner wall of shell
The bottom of separating mechanism is equipped with oil exit pipe, and described oil exit pipe one end is connected to fuel reserve tank, and the other end is connected to cavity.
In the dewaxing device of above-mentioned camellia oil, the bottom surface of the centrifugation supporting plate is close to one end of rotary shaft in vertical side
Upward height is higher than the height of one end far from rotary shaft in the vertical direction.
In the dewaxing device of above-mentioned camellia oil, the crystallization kettle includes autoclave body and the motor that is connected at the top of autoclave body,
One end of agitating shaft and motor are rotatablely connected, and the other end extends into inside autoclave body, and feed inlet is provided with the top of autoclave body, further includes
It is arranged in the intracorporal heat exchange mechanisms of kettle.
In the dewaxing device of above-mentioned camellia oil, the heat exchange mechanisms include that at least one is located at changing inside autoclave body
Hot coil, the heat exchange coil in the shape of a spiral, and one end perforation autoclave body bottom be connected to heat transferring medium delivery pump, the other end passes through
The top of logical autoclave body is connected to refrigeration case, and the heat transferring medium delivery pump and refrigeration case are interconnected.
It further include on the pipeline being arranged between refrigeration case and heat exchange coil in the dewaxing device of above-mentioned camellia oil
Thermometer.
In the dewaxing device of above-mentioned camellia oil, the agitating shaft side is fixedly connected with several stirring blocks.
In the dewaxing device of above-mentioned camellia oil, it includes crystal seed reservoir that mechanism, which is added, in the crystal seed, the crystal seed storage
Storage bottom is connected to powder delivery pump, and the powder delivery pump is connected to the top of crystallization kettle.
It further include the flow valve being arranged between powder delivery pump and crystallization kettle in the dewaxing device of above-mentioned camellia oil
With flow accumulation indication valve, opening and closing of the flow accumulation indication valve to control flow valve.
Compared with prior art, utility model has the advantages that
1, the utility model is using the waxy solid being precipitated in the method removal camellia oil of centrifuge separation, compared to existing skill
The methods of suction filtration, filters pressing have higher separative efficiency in art, to improve the efficiency of entire dewaxing process.
2, the utility model is by being added the methods of crystal seed, control heat transfer temperature difference, so that being present in the wax in camellia oil
It can comparatively fast, preferably be precipitated.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model；
In figure: mechanism 5, autoclave body 11, motor is added in crystallization kettle 1, centrifuge mechanism 2, pipeline 3, control switch 4, crystal seed
12, agitating shaft 13, feed inlet 14, heat exchange mechanisms 15, heat exchange coil 16, heat transferring medium delivery pump 17, refrigeration case 18, thermometer
19, shell 21, centrifugation supporting plate 22, rack 23, rotary shaft 24, driving motor 25, transmission belt 26, vertical filter plate 27, cavity 28, row
Oil pipe 29, crystal seed reservoir 51, powder delivery pump 52, flow valve 53, flow accumulation indication valve 54, stirring block 131.
Specific embodiment
The utility model is described in more detail with reference to the accompanying drawings and detailed description.
As shown in Figure 1, including the crystallization kettle 1 being connected to by pipeline 3 and centrifuge mechanism 2,3 one end of pipeline connection
The bottom end of crystallization kettle 1, the other end are penetrated through to the inside of centrifuge mechanism 2, and control switch 4 is arranged on pipeline 3, to open
Or closed duct 3, crystal seed are added mechanism 5 and are connected to the top of crystallization kettle 1.
The utility model, in use, controlling organization 4 is closed, after the camellia oil wait dewax is added into crystallization kettle 1, then
Be added the crystal seed that crystal seed is added in mechanism 5, crystallization for a period of time after, open control mechanism 4, the camellia oil after crystallization passes through pipeline
3, which enter to centrifuge mechanism 2, is separated by solid-liquid separation, and middle suction filtration, filters pressing etc. are square compared with the prior art for the method for centrifuge separation
Method has higher separative efficiency, to improve the efficiency of entire dewaxing process.
1 bottom of crystallization kettle is connected to inside centrifuge mechanism 2 by pipeline 3, the control to open or close pipeline 3
Organ 4 is arranged on pipeline 3, and crystal seed is added mechanism 5 and is connected to the top of crystallization kettle 1, in use, controlling organization 4 is closed, it will
After camellia oil wait dewax is added into crystallization kettle 1, add crystal seed be added mechanism 5 in crystal seed, crystallization for a period of time after, beat
Control mechanism 4 is opened, the camellia oil after crystallization enters to centrifuge mechanism 2 by pipeline 3 and is separated by solid-liquid separation, and is centrifugated
Method compared with the prior art in filter, the methods of filters pressing has higher separative efficiency, entirely dewaxed to improve
The efficiency of journey.
Specifically, the centrifuge mechanism 2 includes shell 21 and the centrifugation supporting plate 22 inside shell 21, outside
Shell 21 is fixed in rack 23, and the centrifugation supporting plate 22 is fixedly connected with rotary shaft 24, and the axial line of rotary shaft 24 with
The axial line for being centrifuged supporting plate 22 is overlapped, and the outlet of pipeline 3 is located at the surface of centrifugation supporting plate 22, is fixed in rack 23
Driving motor 25 be drivingly connected by transmission belt 26 and rotary shaft 24, further include the vertical filter that can be rotated synchronously with rotary shaft 24
One end of plate 27, the vertical filter plate 27 is fixedly connected with the edge of centrifugation supporting plate 22, the vertical filter plate 27 and shell 21
There is cavity 28, the bottom of centrifuge mechanism 2 is equipped with oil exit pipe 29, and described 29 one end of oil exit pipe and fuel reserve tank connect between inner wall
Logical, the other end is connected to cavity 28.
Shell 21 is fixed in rack 23, and centrifugation supporting plate 22 is located at the inside of shell 21, and the centrifugation supporting plate 22 is solid
Surely be connected with rotary shaft 24, and the axial line of rotary shaft 24 is overlapped with the axial line of centrifugation supporting plate 22, the outlet of pipeline 3 positioned at from
The surface of heart supporting plate 22, the driving motor 25 being fixed in rack 23 are connected by transmission belt 26 and the driving of rotary shaft 24
It connects, when driving motor 25 starts, being centrifuged supporting plate 22 and rotary shaft 24 can synchronously rotate movement, and further including can be with rotary shaft 24
One end of the vertical filter plate 27 rotated synchronously, the vertical filter plate 27 is fixedly connected with the edge of centrifugation supporting plate 22, described vertical
There is cavity 28, cavity 28 is by oil exit pipe 29 arranged at the bottom and is located at centrifugation between filter plate 27 and the inner wall of shell 21
Fuel reserve tank connection outside separating mechanism 2, in use, the camellia oil after crystallization is delivered on centrifugation supporting plate 22 by pipeline 3,
Start driving motor 25, at this time under the drive of transmission belt 26, centrifugation supporting plate 22, rotary shaft 24 do synchronous turn with vertical filter plate 27
Dynamic movement, the camellia oil after crystallization are fitted in vertical 27 surface of filter plate under the influence of centrifugal force to be separated by solid-liquid separation, liquid
Body portion is thrown out of into cavity 28, then is collected by oil exit pipe 29 into fuel reserve tank.
Preferably, the bottom surface of the centrifugation supporting plate 22 is higher than remote close to the height of one end of rotary shaft 24 in the vertical direction
The height of one end in the vertical direction from rotary shaft 24, the set-up mode that centrifugation supporting plate 22 is inclined outwardly, after can promote crystallization
Camellia oil it is mobile to the direction of vertical filter plate 27, to further increase the rate of filtration, save the time.
Preferably, vertical filter plate 27 is also covered with one layer of filter cloth close to the surface of 24 one side of rotary shaft, separates in this way
Waxy solid can be adhered to filter cloth surface, be conveniently replaceable and clean.
As shown in Figure 1, the crystallization kettle 1 includes autoclave body 11 and the motor 12 being connected at the top of autoclave body 11, agitating shaft 13
One end and motor 12 are rotatablely connected, and the other end extends into inside autoclave body 11, and 13 side of agitating shaft is fixedly connected with several
Stirring block 131, feed inlet 14 are provided with the top of autoclave body 11, further include the heat exchange mechanisms 15 being arranged in autoclave body 11, described to change
Heat engine structure 15 includes the heat exchange coil 16 that at least one is located inside autoclave body 11, and one end penetrates through bottom and the heat exchange of autoclave body 11
Medium delivery pump 17 is connected to, and the top of other end perforation autoclave body 11 is connected to refrigeration case 18,17 He of heat transferring medium delivery pump
Refrigeration case 18 is interconnected.
Motor 12 is equipped at the top of autoclave body 11, one end of agitating shaft 13 and motor 12 are rotatablely connected, and the other end extends into autoclave body
Inside 11,13 side of agitating shaft is fixedly connected with several stirring blocks 131, can 13 revolving speed of agitating shaft under the same conditions
Mixing effect is improved, feed inlet 14 is provided with the top of autoclave body 11, heat exchange coil 16, heat transferring medium delivery pump 17 and refrigeration case 18
It is sequentially communicated to form a circulation, heat exchange coil 16 is at least provided with one and is located inside autoclave body 11, in use, camellia oil is led to
It crosses feed inlet 14 to be added to autoclave body 11, starting motor 12 drives agitating shaft 13 and stirring block 131 to rotate, to realize camellia
Oil is uniformly mixed, and after mixing, adjusting motor 12 reduces the velocity of rotation of agitating shaft 13, starts refrigeration case 18 and crystalline substance is added
Kind carries out crystallization.
Preferably, in the shape of a spiral, heat exchange coil 16 is designed as helical form can increase contact area to the heat exchange coil 16, add
Fast heat transfer rate.
Preferably, further include thermometer 19 on the pipeline being arranged between refrigeration case 18 and heat exchange coil 16, due to
In Crystallization Process, in heat exchange coil 16 temperature of heat transferring medium on crystallization result influence it is very big, if temperature is higher, temperature difference compared with
Small, then crystallization speed is slower, influences crystallization efficiency；If temperature difference is larger, temperature difference is larger, then will lead to crystallization speed quickly,
So that the crystal being precipitated is excessively tiny, larger difficulty is caused to the filtering of next step, therefore controls and exchanges heat in heat exchange coil 16
The temperature of medium is particularly significant, so passing through the thermometer 19 being arranged on the pipeline between refrigeration case 18 and heat exchange coil 15
Real-time measurement goes out the temperature of heat transferring medium in heat exchange coil 16, regulates and controls convenient for user.
As shown in Figure 1, it includes crystal seed reservoir 51,51 bottom of crystal seed reservoir and powder that mechanism 5, which is added, in the crystal seed
Last delivery pump 52 is connected to, and the powder delivery pump 52 is connected to the top of crystallization kettle 1, further includes being arranged in powder delivery pump 52
Flow valve 53 and flow accumulation indication valve 54 between crystallization kettle 1, the flow accumulation indication valve 54 is to control flow
The opening and closing of valve 53.
Crystallization result is also related with the additional amount of crystal seed in addition to related with the temperature of heat transferring medium in heat exchange coil 16, therefore
The utility model controls the additional amount of crystal seed by setting flow valve 53 and flow accumulation indication valve 54, when flow accumulation indicates
When valve 54 shows that the accumulation throughput of crystal seed has reached preset value, by closing flow valve 53 to stop powder delivery pump 52 to knot
The conveying of crystal seed in brilliant kettle 1.
The working principle of the utility model is: in use, closing controlling organization 4, camellia oil is added by feed inlet 14
To autoclave body 11, starting motor 12 drives agitating shaft 13 and stirring block 131 to rotate, to realize being uniformly mixed for camellia oil, mixes
After closing uniformly, adjusting motor 12 reduces the velocity of rotation of agitating shaft 13, starts refrigeration case 18, restarting powder delivery pump 52 will be brilliant
Crystal seed in kind of reservoir 51 is added in autoclave body 11, crystallization for a period of time after, open control mechanism 4, the camellia after making crystallization
Oil is delivered on centrifugation supporting plate 22 by pipeline 3, starts driving motor 25, at this time under the drive of transmission belt 26, is centrifuged supporting plate
22, rotary shaft 24 and vertical filter plate 27 synchronously rotate movement, and the camellia oil after crystallization is fitted in perpendicular under the influence of centrifugal force
To be separated by solid-liquid separation, liquid portion is thrown out of into cavity 28 on straight 27 surface of filter plate, then is collected by oil exit pipe 29 and extremely stored up
In fuel tank, the methods of middle suction filtration, filters pressing have higher separative efficiency to the method for centrifuge separation compared with the prior art, to mention
The high efficiency of entire dewaxing process.
The specific embodiments described herein are merely examples of the spirit of the present invention.The utility model institute
Belonging to those skilled in the art can make various modifications or additions to the described embodiments or using similar
Mode substitute, but without departing from the spirit of the present application or beyond the scope of the appended claims.
Although crystallization kettle 1, centrifuge mechanism 2, pipeline 3, control switch 4, crystal seed, which is used more herein, is added machine
Structure 5, autoclave body 11, motor 12, agitating shaft 13, feed inlet 14, heat exchange mechanisms 15, heat exchange coil 16, heat transferring medium delivery pump 17, system
Ice chest 18, thermometer 19, shell 21, centrifugation supporting plate 22, rack 23, rotary shaft 24, driving motor 25, transmission belt 26, vertical filter
Plate 27, cavity 28, oil exit pipe 29, crystal seed reservoir 51, powder delivery pump 52, flow valve 53, flow accumulation indication valve 54, stirring
The terms such as block 131, but it does not exclude the possibility of using other terms.The use of these items is only for more easily describe
With the essence for explaining the utility model；Being construed as any additional limitation is disagreed with the spirit of the present invention
Back.
Claims (10)
1. a kind of dewaxing device of camellia oil, it is characterised in that: including the crystallization kettle (1) being connected to by pipeline (3) and centrifugation point
It disembarks structure (2), the bottom end of described pipeline (3) one end connection crystallization kettle (1), the other end penetrates through interior to centrifuge mechanism (2)
Portion, control switch (4) are arranged on pipeline (3), and to open or close pipeline (3), mechanism (5) and crystallization kettle is added in crystal seed
(1) top connection.
2. the dewaxing device of camellia oil as described in claim 1, it is characterised in that: the centrifuge mechanism (2) includes outer
Shell (21) and the centrifugation supporting plate (22) for being located at shell (21) inside, shell (21) are fixed on rack (23), the centrifugation
Supporting plate (22) is fixedly connected with rotary shaft (24), and the axial line of rotary shaft (24) is overlapped with the axial line of centrifugation supporting plate (22),
The outlet of pipeline (3) is located at the surface of centrifugation supporting plate (22), and the driving motor (25) being fixed on rack (23) passes through
Transmission belt (26) and rotary shaft (24) are drivingly connected, and further include the vertical filter plate (27) that can be rotated synchronously with rotary shaft (24), institute
The one end for stating vertical filter plate (27) is fixedly connected with the edge of centrifugation supporting plate (22).
3. the dewaxing device of camellia oil as claimed in claim 2, it is characterised in that: the vertical filter plate (27) and shell (21)
Inner wall between there are cavity (28), the bottom of centrifuge mechanism (2) is equipped with oil exit pipe (29), described oil exit pipe (29) one end
It is connected to fuel reserve tank, the other end is connected to cavity (28).
4. the dewaxing device of camellia oil as claimed in claim 2, it is characterised in that: the bottom surface of centrifugation supporting plate (22) is close
The height of one end of rotary shaft (24) in the vertical direction is higher than the height of one end far from rotary shaft (24) in the vertical direction.
5. the dewaxing device of camellia oil as described in claim 1, it is characterised in that: the crystallization kettle (1) includes autoclave body (11)
With the motor (12) being connected at the top of autoclave body (11), one end and motor (12) of agitating shaft (13) are rotatablely connected, and the other end extends
It is internal to enter autoclave body (11), feed inlet (14) is provided with the top of autoclave body (11), further includes the heat exchanger being arranged in autoclave body (11)
Structure (15).
6. the dewaxing device of camellia oil as claimed in claim 5, it is characterised in that: the heat exchange mechanisms (15) include at least one
Root is located at the heat exchange coil (16) internal in autoclave body (11), and in the shape of a spiral, and one end penetrates through autoclave body to the heat exchange coil (16)
(11) bottom is connected to heat transferring medium delivery pump (17), and the top of other end perforation autoclave body (11) is connected to refrigeration case (18),
The heat transferring medium delivery pump (17) and refrigeration case (18) are interconnected.
7. the dewaxing device of camellia oil as claimed in claim 6, it is characterised in that: further include being arranged in refrigeration case (18) and changing
Thermometer (19) on pipeline between hot coil (16).
8. the dewaxing device of camellia oil as claimed in claim 5, it is characterised in that: agitating shaft (13) side is fixedly connected
There are several stirring blocks (131).
9. the dewaxing device of camellia oil as described in claim 1, it is characterised in that: it includes crystalline substance that mechanism (5), which are added, in the crystal seed
Kind of reservoir (51), crystal seed reservoir (51) bottom are connected to powder delivery pump (52), the powder delivery pump (52) and
The top of crystallization kettle (1) is connected to.
10. the dewaxing device of camellia oil as claimed in claim 9, it is characterised in that: further include being arranged in powder delivery pump
(52) flow valve (53) and flow accumulation indication valve (54) between crystallization kettle (1), the flow accumulation indication valve (54) are used
To control the opening and closing of flow valve (53).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820117286.5U CN208279588U (en) | 2018-01-24 | 2018-01-24 | The dewaxing device of camellia oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820117286.5U CN208279588U (en) | 2018-01-24 | 2018-01-24 | The dewaxing device of camellia oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208279588U true CN208279588U (en) | 2018-12-25 |
Family
ID=64747178
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820117286.5U Active CN208279588U (en) | 2018-01-24 | 2018-01-24 | The dewaxing device of camellia oil |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208279588U (en) |
-
2018
- 2018-01-24 CN CN201820117286.5U patent/CN208279588U/en active Active
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