Disclosure of Invention
The utility model aims to provide a mixing and stirring structure for walnut oil production and an oil press thereof, so as to solve at least one technical problem in the prior art. The utility model discloses a mix stirring structure all has advantages such as stirring ability reinforce, the homogeneity of mixing is high, is applicable to the mixing stirring when the processing of walnut kernel single product, or walnut kernel and other a plurality of oil crop multiparticle water substitution method.
In order to solve the technical problems, the utility model provides a mixing and stirring structure for walnut oil production, which comprises the following components: the stirring assembly, the vertical stirring tank, the heated water storage tank and the metering pump;
the heating water storage tank is used for heating water to a set temperature;
the heating water storage tank is communicated with the vertical stirring tank through a waterway;
the metering pump is arranged on the water path and is used for pumping hot water with a set proportion into the vertical stirring tank;
the stirring assembly includes: stirring paddles; one end of the stirring paddle is inserted into the vertical stirring tank to be rotationally arranged;
the stirring paddle rotates in the vertical stirring tank and simultaneously rotates along the circumferential direction of the vertical stirring tank.
Preferably, the stirring assembly comprises: the device comprises a main motor, a self-rotation motor, a driving connecting piece and a circumferential rotating shaft; the main motor is in driving connection with the self-rotation motor through a driving connecting piece; the self-rotation motor is in driving connection with the stirring paddle through a circumferential rotating shaft.
Preferably, the method further comprises: colloid mill; the discharge gate of colloid mill orientation vertical agitator tank is opened and is set up.
Preferably, the colloid mill comprises: a blanking guide plate; one end of the blanking guide plate is connected with a blanking opening of the colloid mill, and the other end of the blanking guide plate is obliquely arranged on the top surface of the vertical stirring tank in an extending way.
Preferably, the vertical stirring tank comprises a heating interlayer; the heating interlayer cover is arranged on the outer side wall of the vertical stirring tank.
Preferably, the device further comprises a heating oil storage tank and an oil pump;
the heating oil storage tank is communicated with the heating interlayer through an oil way;
the oil pump is arranged on the oil path and used for forcing oil to circulate between the heating oil storage tank and the heating interlayer so as to heat the vertical stirring tank.
Preferably, an electric heater and a second temperature sensor are arranged in the heating oil storage tank;
the second temperature sensor is arranged on a pipeline which is communicated with the heating interlayer and the heating oil storage tank;
the electric heater is arranged in the heating oil storage tank.
Preferably, it comprises: a first temperature sensor, a display; the display is respectively and electrically connected with the first temperature sensor, the second temperature sensor and the metering pump; the first temperature sensor is arranged in the vertical stirring tank.
The second aspect of the application provides an oil press that adopts above-mentioned walnut oil production to use mixed stirring structure, and it still includes: a receiving assembly; the receiving component is arranged on the bottom surface of the vertical stirring tank and is communicated with the vertical stirring tank.
Preferably, the material receiving assembly comprises: a blanking pipe, a gate valve and a receiving barrel; the blanking pipe is arranged on the bottom surface of the vertical stirring tank; the receiving barrel is arranged opposite to the blanking pipe; the gate valve is arranged on the blanking pipe.
Preferably, the material receiving assembly comprises: a filter screen; the filter screen is arranged on the top surface of the receiving barrel.
The beneficial effects that this application can produce include:
1) This application is through adopting vertical agitator tank to set up the rotation in the jar internal and around the circumference pivot at jar internal edge jar body circumference pivoted stirring rake, realize the quick even mix of a large amount of walnut kernel powder and water in the jar body, effectively improve walnut kernel oil extraction throughput and extraction efficiency, can avoid producing the stirring dead angle. The walnut kernel powder can be treated for 20kg once by adopting the device, the treatment capacity is far higher than that of the existing oil press with a horizontal structure, the treatment efficiency is higher, and the time required from blanking to oil outlet is effectively shortened.
The method is applicable to the mixing and stirring of the walnut kernel single-product water substitution processing, and is also applicable to the mixing and stirring of the walnut kernel and a plurality of other oil crops when the water substitution processing is adopted.
2) This application is through the downward extrusion walnut meat powder of the stirring rake of vertical setting to utilize gravity, effectively improve the oil yield, and can realize the oil extraction in the stirring, need not to stir the back oil extraction alone again, shorten the time of extracting oil.
3) This application adopts the agitator tank of vertical setting, and the discharging pipe that the accessible bottom was seted up goes out oil in proper order and slag tap, utilizes gravity automatic discharging when slag tap, simple structure, oil outlet, slag tap efficient, and the discharge and the recovery of waste water after being convenient for wash.
Detailed Description
The following description of the embodiments of the present utility model will be made apparent and fully in view of the accompanying drawings, in which some, but not all embodiments of the utility model are shown. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
In the description of the present utility model, it should be noted that the directions or positional relationships indicated by the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", etc. are based on the directions or positional relationships shown in the drawings, are merely for convenience of describing the present utility model and simplifying the description, and do not indicate or imply that the devices or elements referred to must have a specific orientation, be configured and operated in a specific orientation, and thus should not be construed as limiting the present utility model. Furthermore, the terms "first," "second," and "third" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.
In the description of the present utility model, it should be noted that, unless explicitly specified and limited otherwise, the terms "mounted," "connected," and "connected" are to be construed broadly, and may be either fixedly connected, detachably connected, or integrally connected, for example; can be mechanically or electrically connected; can be directly connected or indirectly connected through an intermediate medium, and can be communication between two elements. The specific meaning of the above terms in the present utility model will be understood in specific cases by those of ordinary skill in the art.
The utility model is further illustrated with reference to specific embodiments.
As shown in fig. 1-3, the mixing and stirring structure for walnut oil production provided in this embodiment includes a casing 1: a stirring assembly, a vertical stirring tank 43, a metering pump 41, and a heated water storage tank 42; the heating water storage tank 42 is used for storing purified water required by oil extraction by a water substitution method, the heating module in the heating water storage tank 42 heats the purified water to a set temperature, and then the heated purified water is pumped into the vertical stirring tank 43 through a pipeline and the metering pump 41 on the pipeline.
The heating water storage tank 42 may be a commercially available heating water storage tank 42 with an internal electric heater 442 and a water storage function.
The vertical stirring tank 43 is provided with an opening on the top surface of the vertical structure, so that the stirring assembly is convenient to be inserted into the stirring tank for stirring, and meanwhile, materials are convenient to be manually added or powder falls into the tank body after grinding. And the vertical structure is adopted, so that the single treatment capacity is conveniently increased, and the volume of the tank body and the size of a stirring paddle used by the tank body are adjusted according to the change of the treatment capacity, so that the oil pressing operation of mixing walnut kernel powder and water is realized.
Adopt the vertical structure jar body, the stirring rake that stirring assembly contains inserts jar internal rotation setting, and during the stirring, stirring rake periphery is less with jar internal wall clearance, produces the extrusion force to the mixed material after the rotation mix, realizes better oil yield, and jar body volume is big, only needs to select the stirring rake that matches stirring power with it can realize the single processing of a large amount of materials, is favorable to improving the single throughput of walnut kernel.
The stirring assembly is arranged at the upper part of the vertical stirring tank 43; the stirring assembly includes: stirring paddles and driving components thereof; the driving part is suspended on the top of the vertical stirring tank 43; and is in driving connection with the stirring paddle; the stirring paddle extends into the tank body. The driving component drives the stirring paddle to rotate in the tank body and rotate along the circumferential direction of the vertical stirring tank 43 so as to improve the comprehensive stirring of the materials in the tank body and avoid residual mixing dead angles.
The drive assembly may be a combination of drive components commonly used in the art, including, for example: a main motor 21, a rotation motor 222, a driving link 223, and a circumferential rotation shaft 221; the main motor 21 is in driving connection with the self-rotation motor 222 through a driving connection piece 223; the rotation motor 222 is in driving connection with the stirring paddle through the circumferential rotation shaft 221. The drive connection 223 used may in particular be a chain.
According to the process requirement, a heating interlayer 44 can be arranged on the outer wall of the vertical stirring tank 43, and heating oil is used as a heat conducting medium to regulate the temperature of the treated material. In one embodiment, a heating interlayer 44 is disposed on the outer wall of the vertical stirring tank 43, and the heating interlayer 44 is connected with a heating oil storage tank 441 through a pipeline to heat the inside of the vertical stirring tank 43. The heating oil storage tank 441 may be a tank structure in which an electric heating element is provided.
In order to realize better process parameter control, temperature sensors are respectively arranged in the vertical stirring tank 43 and the heating oil storage tank 441; the power distribution box 23 is internally provided with a PLC control module, and the PLC control module is respectively and electrically connected with each temperature sensor and the electric heater 442 to realize the control of the technological parameters of each link.
In one embodiment, the display 33 is electrically connected to the first temperature sensor 431, the second temperature sensor 443, and the metering pump 41, respectively. The second temperature sensor 443 is disposed on a pipeline that communicates with the heating oil tank 441 and the heating interlayer 44, and is used for detecting the temperature of the heating oil flowing into the heating interlayer 44, and feeding back to the display 33, and the temperature and the flow rate of each link can be displayed by the display 33, so that an operator can perform manual adjustment according to the needs, for example, the operator can control the start and stop of the electric heater 442 in the heating oil tank 441 according to the needs.
In order to improve the integration level of the device, a colloid mill 31 can be arranged in the shell 1, so that the walnut kernels are integrally processed, after the walnut kernel raw materials are added into the colloid mill 31 and ground into powder, the powder falls into a vertical stirring tank 43 from a discharge hole, manual transportation is not needed, the production efficiency is improved, and the labor cost is reduced. In one embodiment, the method comprises the following steps: and one end of the blanking guide plate 32 is connected with a blanking opening of the colloid mill 31, and the other end of the blanking guide plate 32 is obliquely arranged on the top surface of the vertical stirring tank 43 in an open and extending way, so that automatic blanking is realized.
The vertical stirring tank 43 can utilize gravity to realize automatic discharging, power is not required to be additionally provided, discharging efficiency is high, after tank body treatment capacity is large, the volume of the tank body is increased, the size of a discharging pipe 45 arranged on the bottom surface of the tank body is increased, automatic discharging of slag can be realized, and waste water is discharged after operation of the subsequent cleaning tank body.
In one embodiment, the blanking assembly includes: connect material subassembly, connect material subassembly specifically to include: a blanking pipe 45, a gate valve 46 and a receiving barrel 47; the blanking pipe 45 is arranged on the bottom surface of the vertical stirring tank 43; the receiving bowl 47 is disposed directly opposite the blanking tube 45.
In one embodiment, the blanking assembly includes: a screen 48; the filter screen 48 is disposed on the top surface of the receiving barrel 47, and filtering of oil residues contained in the oil can be achieved by adopting the filter screen 48. The walnut oil produced by the device can be obtained by filtering without the subsequent purifying and impurity removing process, and has simple process and good effect.
In one embodiment, the method comprises the following steps: a plurality of rollers 11; the rollers 11 are symmetrically arranged on the bottom surface of the casing 1 in pairs. Realizing the rapid transfer of the equipment.
In one embodiment, the method comprises the following steps: a motor frame 211 and a distribution box 23; the main motor 21 is suspended on the top surface of the vertical stirring tank 43 through a motor frame 211; the relevant power supply components and cables of the equipment are accommodated in the distribution box 23, so that maintenance is convenient, and safe production is realized.
In one embodiment, the receiving barrel 47 is of an open structure, the filter screen 48 is a detachable bracket, and the filter screen 48 can be placed or inserted into the open top surface of the receiving barrel 47.
The embodiment also discloses an oil press adopting the mixing and stirring structure for walnut oil production.
This embodiment is through adopting vertical agitator tank to set up the rotation in the jar internal and around circumference pivot in jar internal along jar body circumference pivoted stirring rake, realize the internal a large amount of walnut kernel powder of jar and the quick, evenly mixing mix of water, effectively improve walnut kernel oil extraction throughput and extraction efficiency, can avoid producing the stirring dead angle.
The walnut kernel powder can be treated for 20kg once by adopting the device, the treatment capacity is far higher than that of the existing oil press with a horizontal structure, the treatment efficiency is higher, and the time required from blanking to oil outlet is effectively shortened.
Finally, it should be noted that: the above embodiments are only for illustrating the technical solution of the present utility model, and not for limiting the same; although the utility model has been described in detail with reference to the foregoing embodiments, it will be understood by those of ordinary skill in the art that: the technical scheme described in the foregoing embodiments can be modified or some or all of the technical features thereof can be replaced by equivalents; such modifications and substitutions do not depart from the spirit of the utility model.