CN219709439U - Oil gel production equipment - Google Patents
Oil gel production equipment Download PDFInfo
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- CN219709439U CN219709439U CN202320075398.XU CN202320075398U CN219709439U CN 219709439 U CN219709439 U CN 219709439U CN 202320075398 U CN202320075398 U CN 202320075398U CN 219709439 U CN219709439 U CN 219709439U
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- stirring
- extruder
- oleogel
- cylinder
- stirring rod
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- 238000004519 manufacturing process Methods 0.000 title claims abstract description 33
- 238000003756 stirring Methods 0.000 claims abstract description 163
- 238000010438 heat treatment Methods 0.000 claims abstract description 56
- 238000001816 cooling Methods 0.000 claims abstract description 49
- 239000000523 sample Substances 0.000 claims abstract description 22
- 238000010008 shearing Methods 0.000 claims abstract description 19
- 239000000463 material Substances 0.000 claims description 31
- 238000007599 discharging Methods 0.000 claims description 6
- 230000001154 acute effect Effects 0.000 claims description 3
- 235000019198 oils Nutrition 0.000 abstract description 39
- 239000007787 solid Substances 0.000 abstract description 27
- 235000013871 bee wax Nutrition 0.000 abstract description 25
- 239000012166 beeswax Substances 0.000 abstract description 25
- 235000021323 fish oil Nutrition 0.000 abstract description 25
- 239000002994 raw material Substances 0.000 abstract description 10
- 238000001514 detection method Methods 0.000 abstract description 6
- 239000000499 gel Substances 0.000 description 41
- 239000003921 oil Substances 0.000 description 37
- 239000007788 liquid Substances 0.000 description 28
- 230000009471 action Effects 0.000 description 13
- 230000000694 effects Effects 0.000 description 10
- 239000000047 product Substances 0.000 description 10
- 238000007493 shaping process Methods 0.000 description 9
- 238000005520 cutting process Methods 0.000 description 7
- 239000004519 grease Substances 0.000 description 6
- 239000011521 glass Substances 0.000 description 4
- 235000019197 fats Nutrition 0.000 description 3
- 239000007863 gel particle Substances 0.000 description 3
- 239000011259 mixed solution Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- 230000001276 controlling effect Effects 0.000 description 2
- 235000014113 dietary fatty acids Nutrition 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 229930195729 fatty acid Natural products 0.000 description 2
- 239000000194 fatty acid Substances 0.000 description 2
- 150000004665 fatty acids Chemical class 0.000 description 2
- 239000011344 liquid material Substances 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 235000015112 vegetable and seed oil Nutrition 0.000 description 2
- 239000008158 vegetable oil Substances 0.000 description 2
- 239000001993 wax Substances 0.000 description 2
- 241001125048 Sardina Species 0.000 description 1
- 239000002199 base oil Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 235000019512 sardine Nutrition 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 235000021003 saturated fats Nutrition 0.000 description 1
- 150000004671 saturated fatty acids Chemical class 0.000 description 1
- 238000001338 self-assembly Methods 0.000 description 1
- 235000010692 trans-unsaturated fatty acids Nutrition 0.000 description 1
Landscapes
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
The utility model relates to the technical field of oil gel production equipment, in particular to oil gel production equipment, which comprises a stirring cylinder and a cooling cylinder which are communicated with each other; the stirring cylinder is provided with a first feed inlet and a first discharge outlet, and a stirring rod and a heating device which are connected with the output end of the power device are arranged in the stirring cylinder; the cooling cylinder is provided with a second feed inlet and a second discharge outlet, and the second feed inlet is connected with the first discharge outlet through a first extruder; a hardness probe for detecting the hardness of the oil gel is also arranged in the cooling cylinder; the second discharge port is provided with a second extruder for extruding the oleogel out of the cooling cylinder and a cutter for shearing the oleogel. And after the hardness of the solid is tested to be qualified by the hardness probe, the solid is sent out of the cooling cylinder through the second discharge hole by the second extruder. The equipment integrates heating, stirring, cooling, hardness detection and shearing, and the raw materials are added into the equipment to produce the beeswax and fish oil gel with the hardness meeting the requirements and the size specification being consistent, so that the production efficiency and the quality of the fish oil gel are effectively improved.
Description
Technical Field
The utility model relates to the technical field of oil gel production equipment, in particular to oil gel production equipment.
Background
The oil gel grease is a soft solid substance capable of forming certain viscoelasticity and mechanical strength, the special physical and chemical properties of the oil gel grease endow a product with special texture and rheological properties, the oil gel grease system only contains oil gel factors and liquid grease, a small amount of oil gel factors are utilized to interact in a crystallization or self-assembly mode, and the liquid vegetable oil is bound in a certain network structure to lose fluidity, so that a semi-solid viscoelastic system is presented, and the oil gel grease has the advantages of low saturated fat and zero trans fat due to the fact that only a small amount of solid fat exists in the system, and can be applied to a special grease product for food to replace the traditional products of high saturated fatty acid and trans fatty acid.
In recent years, natural waxes have been receiving a great deal of attention in the research field of oil-in-oil gels due to their excellent oil-in-gel properties, and natural waxes are mostly byproducts of food-grade agricultural processing, and have high commercial and economic values. At present, the research of oil gel taking vegetable oil as an oil phase is more mature, and reports on the preparation of the oil gel by using fish oil are more fresh. Sardine oil is used as base oil, beeswax is used as oil gel, and the low-saturated zero-trans fatty acid fish oil gel is prepared and has extremely high market potential as a novel healthy plastic fat to replace the traditional plastic fat. Thus, there is a need for an integrated fish oil gel production facility that is capable of unifying the specifications of the oil gel.
Disclosure of Invention
The utility model provides the oil gel production equipment which integrates stirring, cooling, hardness detection and extrusion shearing, and improves the quality of oil gel by unifying the specifications of oil gel through hardness detection.
In order to solve the technical problems, the utility model adopts the following technical scheme:
an oil gel production device comprises a stirring cylinder and a cooling cylinder which are communicated with each other; the stirring barrel is provided with a first feed inlet and a first discharge outlet, and a stirring rod and a heating device which are connected with the output end of the power device are arranged in the stirring barrel; the cooling cylinder is provided with a second feeding hole and a second discharging hole, and the second feeding hole is connected with the first discharging hole through a first extruder; a hardness probe for detecting the hardness of the oil gel is also arranged in the cooling cylinder; the second discharging hole is provided with a second extruder for extruding the oil gel out of the cooling cylinder and a shearing device for shearing the oil gel.
In the scheme, raw materials such as fish oil, beeswax and the like enter a stirring cylinder through a first feed inlet, wherein the stirring cylinder is used for stirring the fish oil and the beeswax, the beeswax is melted into a liquid state under the action of a heating device, the liquid state is fully mixed with the fish oil under the action of a stirring rod until the stirring mixed solution is clear liquid, and the clear liquid is fed into a cooling cylinder through a first extruder at a first discharge outlet and naturally cooled until the clear liquid is solidified into a solid; and after the hardness of the solid is tested by the hardness probe, the solid is sent out of the cooling cylinder through a second discharge port by a second extruder, and the second discharge port is provided with oil gel particles for shearing the solid into the same specification. The equipment integrates heating, stirring, cooling, hardness detection and shearing, and the raw materials are added into the equipment to produce the beeswax and fish oil gel with the hardness meeting the requirements and the size specification being consistent, so that the production efficiency and the quality of the fish oil gel are effectively improved.
As one preferable scheme, the stirring rod and the stirring cylinder are coaxially arranged, and a plurality of stirring struts extend from the periphery of the stirring rod.
In the scheme, the stirring barrel is cylindrical, the stirring rod and the central axis of the stirring barrel are coaxially arranged, wherein one end of the stirring rod is connected with the output end of the power device and rotates along with the output end of the power device; adding fish oil and beeswax into the stirring barrel, at the moment, starting the heating device to melt the beeswax, and simultaneously starting the power device to drive the stirring rod to stir so as to fully mix the fish oil and the beeswax. The periphery of stirring rod extends has a plurality of stirring branches, and stirring branch can effectively improve stirring effect, increases the area of contact of stirring rod and material, makes it can obtain better stirring effect under the same condition.
As one preferable scheme, the stirring support rod is obliquely arranged, and the included angle between the stirring support rod and the central axis of the stirring rod is an acute angle.
In this scheme, stirring branch slope sets up, makes the stirring rod wholly be the fishbone form, and stirring branch that the slope set up compares with the stirring branch that sets up perpendicularly, and under the same circumstances of stirring branch quantity, the spatial position that the stirring rod can stir is bigger, consequently can further improve stirring effect. The stirring branch that the slope set up can make the mixture of raw materials such as beeswax and fish oil more abundant, and the stirring is also shorter to the time of clarification liquid, reduces power device's energy consumption and has improved the efficiency of stirring.
As one preferable aspect, the heating device includes a heating plate; the heating plate is arranged at the end part of the stirring cylinder.
In this scheme, the hot plate is the ring form, locates the one end relative with the cooling cylinder, and the material starts the hot plate after adding in the churn, and the material can heat with the hot plate contact, along with the stirring of puddler, the beeswax melts gradually, is liquid raw materials and flows back and forth in the heating barrel and heat with the hot plate contact. Wherein, under the action of the heating plate, the temperature in the heating cylinder can reach 80 ℃ which is enough to melt the beeswax into liquid. Specifically, the heating cylinder is made of transparent glass with high temperature resistance and good heat conduction performance into a cylinder with a certain thickness. The transparent glass can be used for a producer to observe the stirring condition of the liquid in the heating barrel in time.
As one preferable scheme, the heating device further comprises a heating wire; the heating wire is arranged on the outer wall of the stirring rod.
In this scheme, add the heater strip on the stirring rod and can effectively increase the area of contact of liquid material and heating device, can make the material reach the temperature of settlement fast in the shorter time, further improve the production efficiency of oleogel.
As one preferable scheme, the first extruder and the second extruder are columnar, and spiral plates are arranged on the peripheries of the first extruder and the second extruder; the first extruder is coaxial with the stirring rod, is connected with the stirring rod and conveys materials from the stirring cylinder to the cooling cylinder along with the stirring rod; the second extruder is coaxially arranged at the second discharge port and externally connected with a driving device for driving the second extruder, and the driving device drives the second extruder to rotate and extrude materials from the second discharge port; the first extruder is provided with a clearance hole used for inserting and assembling the hardness probe along the axis direction.
In this scheme, the periphery of first extruder is equipped with the screw plate, and the screw plate is connected with the stirring rod, rotates along with the stirring rod, and the liquid in the churn carries the liquid to the cooling cylinder in the effect of screw plate and cools off. And after the materials are cooled and solidified in the cooling cylinder, the solid oleogel is conveyed to a second discharge port for shearing by the rotation of a second extruder. The spiral plate can convey the materials forwards through rotation, and the materials gradually move forwards to a designated position for processing under the action of the cylinder wall and the spiral plate until the materials are cooled and solidified and conveyed to the second discharge hole for cutting. The cutter is provided with a plurality of blades, and the blades are driven by the motor to rotate at a constant speed to cut the solid oil gel on the basis of the second discharge hole. The first extruder is provided with a clearance hole for inserting and assembling the hardness probe along the axis direction, one end of the hardness probe, which penetrates through the clearance hole of the first extruder, is connected with the stirring rod, and the other end of the hardness probe stretches into the cooling cylinder to carry out hardness test on products in the cooling cylinder. The hardness probe can be arranged at the top of the inner wall of the cooling cylinder in a telescopic manner along the vertical direction, and the hardness of a product in the cooling cylinder can be tested under the action of driving equipment configured by the hardness probe so as to evaluate the quality of the product.
As one preferable scheme, the second discharging hole is provided with a forming nozzle which is coaxially arranged with the cooling cylinder and connected with the second extruder; the cutter is positioned at the end of the forming nozzle.
In this scheme, shaping mouth can be designed into detachable structure, and the shaping mouth of changing suitable shape according to actual production needs can adjust the shape size of oil gel, and the spiral plate cooperation shaping mouth's of second extruder inner wall can progressively carry solid oil gel to the device outside and cut. In addition, the size of the oleogel can also be adjusted by adjusting the speed at which the blade rotates or the feeding speed of the second extruder. The lower the feeding speed of the second extruder, the larger the shape of the oleogel, whereas the smaller the shape of the oleogel, under the same cutting speed; similarly, under the condition that the feeding speed of the second extruder is the same, the faster the cutting speed is, the smaller the shape of the oleogel is, and conversely, the larger the shape of the oleogel is.
As one preferable mode, the forming nozzle is conical, and the inner diameter is gradually reduced along the conveying direction of the materials.
In this scheme, the internal diameter of conical shaping mouth reduces along the material direction of delivery gradually, and this structure has the pressure boost effect, and when the material gets into the cavity of little interior warp from big interior, under the unchangeable circumstances of other conditions, the pressure of material can be increased, and then makes solid oleogel extrude with certain pressure, forms the solid oleogel unanimous with shaping mouth cross-sectional shape under the effect of shaping mouth, cuts by the cutter again to according to the length that actual needs regulation oleogel was cut.
As one preferable scheme, the power device is a motor; the fixed end of the power device is assembled outside the stirring barrel, and the output end of the power device stretches into the stirring barrel to be connected with the stirring rod.
In this scheme, use the motor as power device in order to drive stirring rod rotation, can also select other types of motors such as servo motor as power device in addition, select suitable power device according to the needs of production process. The motor has the characteristics of light weight, small volume, large output force, high efficiency and the like, and is suitable for driving the stirring rod to rotate so as to stir the materials in the stirring cylinder.
As one preferable scheme, a temperature sensor connected with a temperature control system is arranged in the stirring cylinder, the temperature control system is electrically connected with the heating device, and the heating device is controlled by the temperature control system.
In the scheme, a temperature sensor connected with a temperature control system is arranged in the stirring barrel, the temperature sensor feeds back temperature information to the temperature control system in real time, and the temperature control system controls the power of the heating device according to the temperature information fed back by the temperature sensor, so that the temperature in the stirring barrel is continuously kept in a temperature range, and the working steps of manually controlling the temperature are reduced.
Compared with the prior art, the utility model discloses oil gel production equipment, which has the following beneficial effects: the stirring cylinder is used for stirring the fish oil and the beeswax, the beeswax is melted into a liquid state under the action of the heating device, the liquid state is fully mixed with the fish oil under the action of the stirring rod until the stirring mixed solution is clear liquid, and the clear liquid is sent into the cooling cylinder through the first extruder at the first discharge port to be naturally cooled until the clear liquid is solidified into a solid; and after the hardness of the solid is tested by the hardness probe, the solid is sent out of the cooling cylinder through a second discharge port by a second extruder, and the second discharge port is provided with oil gel particles for shearing the solid into the same specification. The equipment integrates heating, stirring, cooling, hardness detection and shearing, and the raw materials are added into the equipment to produce the beeswax and fish oil gel with the hardness meeting the requirements and the size specification being consistent, so that the production efficiency and the quality of the fish oil gel are effectively improved.
Drawings
Fig. 1 is a schematic overall structure of embodiment 1 of the present utility model.
Fig. 2 is a schematic overall structure of embodiment 2 of the present utility model.
Fig. 3 is a schematic structural view of the first extruder and the second extruder.
Wherein, 1, a stirring cylinder; 2. a cooling cylinder; 3. a first feed port; 4. a first extruder; 5. a hardness probe; 6. a stirring rod; 7. stirring support rods; 8. forming a nozzle; 9. a heating plate; 10. a spiral plate; 11. a second extruder.
Detailed Description
The drawings are for illustrative purposes only and are not to be construed as limiting the present patent; for the purpose of better illustrating the embodiments, certain elements of the drawings may be omitted, enlarged or reduced and do not represent the actual product dimensions; it will be appreciated by those skilled in the art that certain well-known structures in the drawings and descriptions thereof may be omitted. The positional relationship depicted in the drawings is for illustrative purposes only and is not to be construed as limiting the present patent.
The same or similar reference numbers in the drawings of embodiments of the utility model correspond to the same or similar components; in the description of the present utility model, it should be understood that if there are terms "upper", "lower", "left", "right", "long"
The orientation or positional relationship indicated by "short", "top", "bottom", "inside", "outside", etc. is based on the orientation or positional relationship shown in the drawings, and is merely for convenience of describing the present utility model and simplifying the description, rather than indicating or implying that the device or element being referred to must have a specific orientation, be constructed and operated in a specific orientation, so that the terms describing the positional relationship in the drawings are merely for exemplary illustration and are not to be construed as limiting the present patent, and the specific meaning of the terms described above will be understood by those of ordinary skill in the art according to the specific circumstances.
The technical scheme of the utility model is further specifically described by the following specific embodiments with reference to the accompanying drawings:
example 1
As shown in fig. 1, the present embodiment provides an oleogel production apparatus, which comprises a stirring cylinder 1 and a cooling cylinder 2 which are communicated; the stirring cylinder 1 is provided with a first feed inlet 3 and a first discharge outlet, and a stirring rod 6 and a heating device which are connected with the output end of the power device are arranged in the stirring cylinder 1; the cooling cylinder 2 is provided with a second feed inlet and a second discharge outlet, and the second feed inlet is connected with the first discharge outlet through a first extruder 4; a hardness probe 5 for detecting the hardness of the oil gel is also arranged in the cooling cylinder 2; the second discharge port is provided with a second extruder 11 for extruding the oleogel out of the cooling cylinder 2 and a cutter for shearing the oleogel.
Specifically, raw materials such as fish oil and beeswax enter a stirring cylinder 1 through a first feed port 3, wherein the stirring cylinder 1 is used for stirring the fish oil and the beeswax, the beeswax is melted into a liquid state under the action of a heating device, the liquid state is fully mixed with the fish oil under the action of a stirring rod 6 until the stirring mixed solution is a clear liquid, and the clear liquid is fed into a cooling cylinder 2 through a first extruder 4 at a first discharge port and naturally cooled until the clear liquid is solidified into a solid; and after the hardness of the solid is tested to be qualified by the hardness probe 5, the solid is sent out of the cooling cylinder 2 through a second discharge hole by the second extruder 11, and the second discharge hole is provided with an oil gel particle for shearing the solid into the same specification. The equipment integrates heating, stirring, cooling, hardness detection and shearing, and the raw materials are added into the equipment to produce the beeswax and fish oil gel with the hardness meeting the requirements and the size specification being consistent, so that the production efficiency and the quality of the fish oil gel are effectively improved.
Specifically, the stirring rod 6 is coaxially disposed with the stirring cylinder 1, and a plurality of stirring struts 7 extend from the outer periphery of the stirring rod 6. As shown in the figure, the stirring rod 7 is vertically arranged on the periphery of the stirring rod 6, the stirring cylinder 1 is cylindrical, the stirring rod 6 and the central axis of the stirring cylinder 1 are coaxially arranged, one end of the stirring rod 6 is connected with the output end of the power device, and the output end of the follow-up power device rotates; the fish oil and the beeswax are added into the stirring barrel 1, at the moment, the heating device is started to melt the beeswax, and meanwhile, the power device is started to drive the stirring rod 6 to stir so that the fish oil and the beeswax are fully mixed. The periphery of stirring rod 6 extends there is a plurality of stirring branch 7, and stirring branch 7 can effectively improve stirring effect, increases stirring rod 6 and the area of contact of material, makes it can obtain better stirring effect under the same condition.
Further, the heating means comprises a heating plate 9; the heating plate 9 is provided at the end of the stirring cylinder 1. The heating plate 9 is circular, locates the one end opposite with cooling cylinder 2, starts heating plate 9 after the material is added in the churn 1, and the material can heat with heating plate 9 contact, along with stirring of stirring rod 6, the beeswax melts gradually, is liquid raw materials and flows back and forth in the heating barrel and heat in heating plate 9 contact. Wherein the temperature in the cartridge can reach 80 degrees celsius under the influence of the heating plate 9, sufficient to melt the beeswax to the liquid. Specifically, the heating cylinder is made of transparent glass with high temperature resistance and good heat conduction performance into a cylinder with a certain thickness. The transparent glass can be used for a producer to observe the stirring condition of the liquid in the heating barrel in time.
The heating device also comprises a heating wire; the heating wire is arranged on the outer wall of the stirring rod 6. The heating wire is additionally arranged on the stirring rod 6, so that the contact area between the liquid material and the heating device can be effectively increased, the material can quickly reach the set temperature in a shorter time, and the production efficiency of the oleogel is further improved.
Wherein the outer circumferences of the first extruder 4 and the second extruder 11 are provided with spiral plates 10; the first extruder 4 is coaxial with the stirring rod 6 and is connected with the stirring rod 6; the second extruder 11 is externally connected with a driving device for driving the second extruder 11. The periphery of the first extruder 4 is provided with a spiral plate 10, the spiral plate 10 is connected with the stirring rod 6, and rotates along with the stirring rod 6, and liquid in the stirring cylinder 1 is conveyed into the cooling cylinder 2 for cooling under the action of the spiral plate 10. The solid oil gel is conveyed to a second discharge hole for shearing by the rotation of a second extruder 11 after the material is cooled and solidified in the cooling cylinder 2. The spiral plate 10 can convey materials forwards through rotation, and the materials gradually move forwards to a designated position for processing under the action of the cylinder wall and the spiral plate 10 until the materials are cooled and solidified and conveyed to a second discharge hole for cutting. The cutter is provided with a plurality of blades, and the blades are driven by the motor to rotate at a constant speed to cut the solid oil gel on the basis of the second discharge hole. The first extruder 4 is provided with a clearance hole for inserting and assembling the hardness probe 5 along the central axis direction, one end of the hardness probe 5, which passes through the clearance hole of the first extruder 4, is connected with the stirring rod 6, and the other end extends into the cooling cylinder 2 to carry out hardness test on the product in the cooling cylinder 2. The position of the hardness probe 5 can be adjusted adaptively according to the placement mode of the equipment, for example, when the equipment is placed horizontally, the hardness probe 5 can be arranged at the top of the inner wall of the cooling cylinder 2, at this time, the hardness probe 5 can stretch and retract along the vertical direction, and under the action of the driving equipment configured by the hardness probe 5, the hardness test can be performed on the product in the cooling cylinder 2 to evaluate the quality of the product.
Further, the second discharge port is provided with a forming nozzle 8, and the forming nozzle 8 is coaxially arranged with the cooling cylinder 2 and is connected with a second extruder 11; the shears are located at the ends of the forming nozzle 8. The shaping mouth 8 can be designed into detachable structure, and the shaping mouth 8 of changing suitable shape according to actual production needs can adjust the shape size of oil gel, and the spiral plate 10 of second extruder 11 cooperates the inner wall of shaping mouth 8 and can progressively carry solid oil gel to the device outside for cutting. In addition, the size of the oleogel can also be adjusted by adjusting the speed at which the blade rotates or the feeding speed of the second extruder 11. The slower the feeding speed of the second extruder 11, the larger the shape of the oleogel, whereas the smaller the shape of the oleogel, under the same cutting speed; similarly, under the condition that the feeding speed of the second extruder 11 is the same, the faster the cutting speed, the smaller the shape of the oleogel, and conversely, the larger the shape of the oleogel.
The forming nozzle 8 is tapered, and the inner diameter is gradually reduced along the conveying direction of the material. The internal diameter of the conical forming nozzle 8 is gradually reduced along the conveying direction of the material, the structure has a supercharging effect, when the material enters the cavity of the small inner channel from the large inner channel, the pressure of the material is increased under the condition that other conditions are unchanged, so that solid oleogel is extruded out at a certain pressure, the solid oleogel consistent with the section shape of the forming nozzle 8 is formed under the action of the forming nozzle 8, and then the shearing is carried out by the shearing machine, and the shearing length of the oleogel is regulated according to actual needs.
The power device is a motor; the fixed end of the power device is assembled outside the stirring barrel 1, and the output end of the power device extends into the stirring barrel 1 and is connected with the stirring rod 6. The motor is used as a power device to drive the stirring rod 6 to rotate, other types of motors such as a servo motor can be used as the power device, and a proper power device can be selected according to the requirement of the production process. The motor has the characteristics of light weight, small volume, large output force, high efficiency and the like, and is suitable for driving the stirring rod 6 to rotate so as to stir the materials in the stirring cylinder 1.
Example 2
As shown in the figure, this embodiment provides an oil gel production apparatus, which is different from embodiment 1 in that the stirring rod 7 is disposed diagonally, and the angle between the stirring rod 7 and the central axis of the stirring rod 6 is an acute angle. Stirring branch 7 slope sets up, makes stirring rod 6 whole be the fishbone form, and stirring branch 7 that the slope set up compares with stirring branch 7 that set up perpendicularly, and under the same circumstances of stirring branch 7 quantity, stirring rod 6 can stir the spatial position bigger, consequently can further improve stirring effect. The stirring branch 7 that the slope set up can make the mixture of raw materials such as beeswax and fish oil more abundant, and the stirring is also shorter to the time of clarified liquid, reduces power device's energy consumption and has improved the efficiency of stirring.
Example 3
The embodiment provides an oil gel production device, on the basis of embodiment 1 or embodiment 2, a temperature sensor connected with a temperature control system is arranged in a stirring cylinder 1, the temperature control system is electrically connected with a heating device, and the heating device is controlled by the temperature control system.
The temperature sensor connected with the temperature control system is arranged in the stirring barrel 1, the temperature sensor feeds back temperature information to the temperature control system in real time, the temperature control system controls the power of the heating device according to the temperature information fed back by the temperature sensor, so that the temperature in the stirring barrel 1 is continuously kept in a temperature range, and the working steps of manually controlling the temperature are reduced.
It is to be understood that the above examples of the present utility model are provided by way of illustration only and not by way of limitation of the embodiments of the present utility model. Other variations or modifications of the above teachings will be apparent to those of ordinary skill in the art. It is not necessary here nor is it exhaustive of all embodiments. Any modification, equivalent replacement, improvement, etc. which come within the spirit and principles of the utility model are desired to be protected by the following claims.
Claims (10)
1. An oleogel production apparatus, characterized in that: comprises a stirring cylinder (1) and a cooling cylinder (2) which are communicated with each other;
the stirring cylinder (1) is provided with a first feed inlet (3) and a first discharge outlet, and a stirring rod (6) and a heating device which are connected with the output end of the power device are arranged in the stirring cylinder (1);
the cooling cylinder (2) is provided with a second feeding hole and a second discharging hole, and the second feeding hole is connected with the first discharging hole through a first extruder (4); a hardness probe (5) for detecting the hardness of the oil gel is also arranged in the cooling cylinder (2);
the second discharge port is provided with a second extruder (11) for extruding the oleogel out of the cooling cylinder (2) and a shearing device for shearing the oleogel.
2. The oleogel production apparatus as claimed in claim 1, wherein: the stirring rod (6) and the stirring cylinder (1) are coaxially arranged, and a plurality of stirring support rods (7) extend from the periphery of the stirring rod (6).
3. The oleogel production apparatus as claimed in claim 2, wherein: the stirring support rod (7) is obliquely arranged, and the included angle between the stirring support rod (7) and the central axis of the stirring rod (6) is an acute angle.
4. The oleogel production apparatus as claimed in claim 1, wherein: the heating device comprises a heating plate (9); the heating plate (9) is arranged at the end part of the stirring cylinder (1).
5. The oleogel production apparatus as claimed in claim 1, wherein: the heating device also comprises a heating wire; the heating wire is arranged on the outer wall of the stirring rod (6).
6. The oleogel production apparatus as claimed in claim 1, wherein: the first extruder (4) and the second extruder (11) are columnar, and spiral plates (10) are arranged on the periphery of the first extruder and the second extruder; the first extruder (4) is coaxial with the stirring rod (6) and connected with the stirring rod (6) and conveys materials from the stirring cylinder (1) to the cooling cylinder (2) along with the stirring rod (6); the second extruder (11) is coaxially arranged at the second discharge port and is externally connected with a driving device for driving the second extruder (11), and the driving device drives the second extruder (11) to rotate and extrude materials from the second discharge port; the first extruder (4) is provided with a clearance hole used for inserting and assembling the hardness probe (5) along the axial direction.
7. The oleogel production apparatus as claimed in claim 1, wherein: the second discharge hole is provided with a forming nozzle (8), and the forming nozzle (8) is coaxially arranged with the cooling cylinder (2) and is connected with the second extruder (11);
the cutter is positioned at the end of the forming nozzle (8).
8. The oleogel production apparatus as claimed in claim 7, wherein: the forming nozzle (8) is conical, and the inner diameter is gradually reduced along the conveying direction of the material.
9. The oleogel production apparatus as claimed in claim 1, wherein: the power device is a motor; the fixed end of the power device is assembled outside the stirring barrel (1), and the output end of the power device stretches into the stirring barrel (1) to be connected with the stirring rod (6).
10. The oleogel production apparatus as claimed in any one of claims 1-9, wherein: the stirring barrel (1) is internally provided with a temperature sensor connected with a temperature control system, the temperature control system is electrically connected with the heating device, and the heating device is controlled by the temperature control system.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN202320075398.XU CN219709439U (en) | 2023-01-09 | 2023-01-09 | Oil gel production equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN202320075398.XU CN219709439U (en) | 2023-01-09 | 2023-01-09 | Oil gel production equipment |
Publications (1)
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