CN108309086B

CN108309086B - Food processing machine

Info

Publication number: CN108309086B
Application number: CN201710028672.7A
Authority: CN
Inventors: 王旭宁; 张文凡; 薛领珑
Original assignee: Joyoung Co Ltd
Current assignee: Joyoung Co Ltd
Priority date: 2017-01-16
Filing date: 2017-01-16
Publication date: 2021-10-08
Anticipated expiration: 2037-01-16
Also published as: CN108309086A

Abstract

The invention relates to a small kitchen appliance, in particular to a food processor, which comprises a container and is characterized in that: the container is including the crushing chamber that is located the container bottom, set up in the backward flow chamber of crushing chamber top and be used for the intercommunication to smash the mouth that gathers class of chamber and backward flow chamber, it is provided with crushing blade to smash the intracavity, the capacity in crushing chamber is 22mL ~380mL, be provided with the water level identification line on the lateral wall in backward flow chamber, the outside that is located the container is provided with the circulation line that will smash chamber and backward flow chamber intercommunication, circulation line's entry is located smashes the intracavity, circulation line's export is located the backward flow intracavity, and circulation line's export is not higher than the setting of water level identification line. Compared with the prior art, the bean curd machine has the advantages of simple structure, low cost, capability of effectively reducing foams, capability of intensively crushing materials, high crushing efficiency, no bean curd phenomenon and convenience in cleaning.

Description

Food processing machine

Technical Field

The invention relates to a small household appliance for a kitchen, in particular to a food processor.

Background

The utility model discloses a structure of circulating processor is disclosed in the utility model patent of patent number "CN 201220102774.1", the name is "circulating processor", and the container bottom of this processor is provided with cutting blade and mill, is provided with a circulating line in the handle of container lateral part to be provided with the loading system in the bottom of mill and pressurize the thick liquid, make the thick liquid get into in the circulating line, in the backward flow mouth at circulating line top flowed back to the container again, realize the circulation cutting and the grinding of material.

In the above structure, the grinding and crushing of the grinding disc are completed under the condition that the rotating speed is lower than 6000r/min, and a pressurizing mechanism (an upper conical disc, a lower conical disc or a pressurizing pump) is needed to pressurize the slurry below the grinding disc so as to enable the slurry to enter the circulating pipeline and flow back to the container from the return port at the top of the circulating pipeline, so the circulating type conditioner has a complex structure and higher cost. And if no pressurizing mechanism is provided, the conditioner can not realize circular cutting and grinding of the slurry inside and outside the circulating pipeline during pulping. Meanwhile, the cutting blade is arranged at the top of the grinding disc, when the conditioner works, the mixture of the material flowing out of the backflow port and water is in an unordered state and is scattered onto the cutting blade from all directions above, and the material is thrown away from the periphery and the upper part of the container after being collided by the cutting blade, so that the material is difficult to enter the grinding disc for grinding, and the grinding disc is arranged at the bottom of the container, and large material particles which are not cut can not enter the grinding disc even in the whole pulping process. Therefore, the grinding efficiency of the conditioner is low, and the conditioner can not generate large material particles after long-time grinding.

Disclosure of Invention

The invention aims to provide the food processor which has high crushing efficiency, high circulation speed, simple structure, convenient cleaning and lower cost, and can effectively reduce foam.

In order to achieve the purpose, the invention adopts the following technical scheme: a food processor comprising a container, characterized in that: the container is including the crushing chamber that is located the container bottom, set up in the backward flow chamber of crushing chamber top and be used for the intercommunication to smash the mouth that gathers class of chamber and backward flow chamber, it is provided with crushing blade to smash the intracavity, the capacity in crushing chamber is 22mL ~380mL, be provided with the water level identification line on the lateral wall in backward flow chamber, the outside that is located the container is provided with the circulation line that will smash chamber and backward flow chamber intercommunication, circulation line's entry is located smashes the intracavity, circulation line's export is located the backward flow intracavity, and circulation line's export is not higher than the setting of water level identification line.

Furthermore, the vertical height from the flow gathering port to the water level marking line is H1, the vertical height from the top end of the outlet of the circulating pipeline to the water level marking line is H, and H/H1 is more than or equal to 0.3 and less than or equal to 0.8.

Further, H/H1=0.5~ 0.75.

Furthermore, the outlet of the circulating pipeline is arranged on the side wall of the backflow cavity, the vertical height from the top end of the outlet to the water level identification line is H, and H is larger than or equal to 10mm and smaller than or equal to 100 mm.

Further, when the slurry discharged from the outlet of the circulation line is discharged in an inclined upward direction from the horizontal plane, H is at least more than 10 mm.

Further, when the slurry discharged from the outlet of the circulation line is discharged obliquely downward from the horizontal plane, H is at least less than 100 mm.

Further, the vertical spray angle formed by the slurry sprayed out of the outlet of the circulating pipeline and the horizontal plane is theta, wherein theta is more than or equal to 0 and less than or equal to 60 degrees.

Furthermore, an outlet of the circulating pipeline is arranged on the side wall of the return cavity, when the circulating pipeline is vertically projected on a horizontal plane, a connecting line from the center of the outlet to the center of the return cavity is L1, during circulating pulping, the pulp sprayed out of the outlet is in an inclined spraying state with L1, and a horizontal spraying angle formed by the sprayed pulp and L1 is beta, wherein beta is more than or equal to 0 and less than or equal to 60 degrees;

or the return cavity is provided with an inclined section inclined relative to a vertical plane, and the outlet of the circulating pipeline is arranged on the inclined section.

Further, an inlet of the circulating pipeline is arranged on the side wall of the crushing cavity, the inlet of the circulating pipeline comprises an inlet upper edge and an inlet lower edge, and the crushing blade is positioned in a vertical area of a horizontal plane corresponding to the inlet upper edge and the inlet lower edge;

or the inlet of the circulating pipeline is arranged on the side wall of the crushing cavity, and a material blocking part is arranged at the inlet;

or the distance from the tail end of the crushing blade to the inner side wall of the crushing cavity is a, wherein a is more than or equal to 1mm and less than or equal to 15 mm;

or the inlet of the circulating pipeline is arranged on the side wall of the crushing cavity, the inlet of the circulating pipeline comprises an inlet upper edge and an inlet lower edge, the crushing blade is positioned in a vertical area of a horizontal plane corresponding to the inlet upper edge and the inlet lower edge, the inlet lower edge is flush with the bottom surface of the crushing cavity, the height of the inlet is h1, the height from the lower end surface of the crushing blade to the inlet lower edge is h2, and h2 is more than or equal to 1/4h 1.

Furthermore, the area of the opening part of the flow gathering port is smaller than that of the opening part of any horizontal section on the backflow cavity below the outlet of the circulating pipeline.

After adopting above-mentioned technical scheme, because the container has crushing chamber and backward flow chamber, smashes the chamber and communicates through gathering the mouth with the backward flow chamber, consequently, can concentrate from the thick liquid of backward flow chamber backward flow and smash the intracavity through gathering the mouth of flowing back, gather the mouth of flowing back and have the gathering material, guarantee that the material can both flow into through gathering the mouth of flowing back and smash the intracavity and participate in smashing. Simultaneously, because the capacity in crushing chamber only has 22mL ~380mL, the space is less, and smash the blade and be located crushing intracavity, therefore, the material that flows in from converging the mouth can concentrate crushing at crushing intracavity, and the material is when smashing the intracavity and concentrate crushing, because it has thick liquid to flow into from converging the mouth in the backward flow chamber to smash the chamber to last, the material of smashing the intracavity receives the thick liquid pressure effect of converging the mouth top, the material is difficult to run out and enter into the backward flow chamber from smashing the chamber, consequently, the material is concentrated in crushing intracavity and is concentrated kibbling efficiency height. Secondly, when the materials vertically fall onto the crushing blade from the flow gathering port, the cutting edge of the crushing blade can cut and crush the inflowing materials at the first time, so that the probability of the materials being cut by the crushing blade is greatly improved, and therefore, the food processing machine does not have the condition of large materials when crushing the materials. In addition, at crushing intracavity, when the motor drives crushing blade high-speed rotatory, crushing blade can drive thick liquid stream and make high-speed centrifugal motion, because the entry of circulating line sets up in crushing intracavity, makes the thick liquid stream of centrifugal motion and can receive inertial force effect to enter into the circulating line from the entrance to, because crushing blade continuously makes high-speed rotary motion, the thick liquid stream that enters into the circulating line before subsequent thick liquid stream can continuously promote flows back to the backward flow intracavity from the exit. Therefore, the crushing blade of the food processor provided by the invention has a strong water pushing circulation function while crushing materials, and can ensure that slurry can circulate inside and outside the circulation pipeline. Compared with the prior art, the food processor needs no pressurizing mechanism such as a pressurizing pump, has simple structure and lower cost, and can automatically clean.

Meanwhile, the outlet of the circulating pipeline in the prior art is generally arranged above the water level identification line, when the soybean milk is made to circulate, a large amount of air can be brought into and mixed with the soybean milk in the backflow cavity when the soybean milk sprayed from the outlet of the circulating pipeline flows back to the backflow cavity under the action of gravity, so that more soybean milk foam in the backflow cavity is caused, the soybean milk is not beneficial to foam wrapping and the non-crushed materials continue to participate in the circular crushing, meanwhile, in the process of boiling and making the soybean milk, the false anti-overflow phenomenon is easily caused, the soybean milk is not boiled, and the potential safety hazard of food exists. The outlet of the circulating pipeline is arranged at a position which is not higher than the water level identification line, so that the slurry flowing back from the outlet can not bring a large amount of air to be mixed with the slurry in the backflow cavity, the amount of foams is greatly reduced, and when the outlet of the circulating pipeline is positioned below the water level identification line, the slurry flow jetted from the outlet of the circulating pipeline can block and slow down the slurry flow rotating at high speed in the backflow cavity, and meanwhile, the slurry flow jetted at high speed also has a turbulence effect.

Drawings

The invention will be further described with reference to the accompanying drawings in which:

FIG. 1 is a schematic structural diagram according to a first embodiment of the present invention;

FIG. 2 is a schematic structural diagram according to a second embodiment of the present invention;

FIG. 3 is a schematic view showing the structure of a crushing blade according to the second embodiment;

FIG. 4 is a schematic structural diagram of a third embodiment of the present invention;

FIG. 5 is an enlarged view of the structure at A in FIG. 4;

FIG. 6 is a schematic cross-sectional view of the horizontal plane M in FIG. 4;

FIG. 7 is a plan view of a crushing apparatus according to the third embodiment;

FIG. 8 is an enlarged view of the structure at B in FIG. 4;

FIG. 9 is a schematic structural diagram of a fourth embodiment of the present invention;

FIG. 10 is a schematic structural diagram of a fifth embodiment of the present invention;

FIG. 11 is a schematic structural view of a fifth embodiment of a stationary knife;

FIG. 12 is a schematic structural view of the fifth embodiment of the moving blade;

FIG. 13 is a schematic structural diagram of a sixth embodiment of the present invention;

FIG. 14 is a schematic view of the structure of the moving blade of FIG. 13;

FIG. 15 is an enlarged view of the structure of FIG. 13 at C;

FIG. 16 is a schematic cross-sectional view of the horizontal plane M in FIG. 13;

FIG. 17 is a top view of a crushing apparatus according to a sixth embodiment;

FIG. 18 is an enlarged view of the structure of FIG. 13 at D;

FIG. 19 is a schematic structural diagram of a seventh embodiment of the present invention;

FIG. 20 is an exploded view of the reducing assembly of FIG. 19;

fig. 21 is a schematic structural view of the moving blade of fig. 19.

Detailed Description

The first embodiment is as follows:

fig. 1 is a schematic structural diagram of a first embodiment of the present invention. The utility model provides a food preparation machine, this food preparation machine's reducing mechanism, includes container 1, sets up crushing blade 2 in container 1 and with the circulation pipeline 3 of container upper and lower intercommunication, crushing blade 2 passes through motor 4 and drives, circulation pipeline 3 sets up in the container outside, container 1 is including the crushing chamber 11 that is located the container bottom, be located the backward flow chamber 12 of crushing chamber 11 top and the mouth 13 that gathers that feeds through crushing chamber 11 and backward flow chamber 12, crushing blade 2 is located crushing chamber 11, just it sets up in the top of crushing blade 2 to gather mouthful 13, the entry 31 of circulation pipeline is located crushing chamber 11, the export 32 of circulation pipeline is located backward flow chamber 12.

The food processing machine in the embodiment is a soybean milk machine, the soybean milk machine is provided with a machine head I and a cup body II, wherein the cup body II is of a double-layer structure and comprises an inner cup body and a shell 10, the container 1 is the inner cup body of the soybean milk machine, a circulating pipeline 3 is hidden in an interlayer between the inner cup body and the shell 10, and a motor 4 is arranged inside the machine head I. In this embodiment, the area of the opening of the fluid collecting port 13 is smaller than the area of the opening of any horizontal section on the return cavity 12 below the outlet 32 of the circulation line. And, a water level marking line 90 is provided on the inner wall of the container 1, and the outlet 32 of the circulation line is positioned below the water level marking line 90. The volume of the pulverization chamber 11 in this embodiment is only 22 mL-380 mL.

In this embodiment, because the container has crushing chamber and backward flow chamber, smashes the chamber and communicates through converging the mouth with the backward flow chamber to, the oral area of converging the mouth area and being less than arbitrary horizontal cross-section's oral area on the backward flow chamber of circulating line export below, consequently, the thick liquid of following backward flow chamber backward flow can concentrate through converging the mouth and flow back to crushing intracavity, and it has the gathering material to converge the mouth, guarantees that the material can both flow into through converging the mouth and smashes the intracavity and participate in crushing. Simultaneously, because the capacity in crushing chamber only has 22mL ~380mL, the space is less, and smash the blade and set up in smashing the intracavity, consequently, the material that flows in from the mouth of converging can concentrate crushing at smashing the intracavity, and the material is when smashing the intracavity and concentrate crushing, because it has thick liquid to flow into from the mouth of converging to smash the chamber to last in the backward flow chamber, the material of smashing the intracavity receives the thick liquid pressure effect of the mouth top of converging, the material is difficult to run out and enter into the backward flow chamber from smashing the chamber, consequently, the material is concentrated in smashing the intracavity and is concentrated kibbling efficiency height. Secondly, because the flow gathering port is arranged above the crushing blades, when the materials vertically fall into the crushing blades from the flow gathering port, the cutting edges of the crushing blades can cut and crush the flowing materials at the first time, so that the probability of cutting the materials by the crushing blades is greatly improved, and the condition of large materials cannot exist when the soybean milk machine of the embodiment crushes the materials. In addition, at crushing intracavity, when the motor drives crushing blade high-speed rotatory, crushing blade can drive thick liquid stream and make high-speed centrifugal motion, because the entry of circulating line sets up in crushing intracavity, makes the thick liquid stream of centrifugal motion and can receive inertial force effect to enter into the circulating line from the entrance to, because crushing blade continuously makes high-speed rotary motion, the thick liquid stream that enters into the circulating line before subsequent thick liquid stream can continuously promote flows back to the backward flow intracavity from the exit. Therefore, the crushing blade of the embodiment has a strong water pushing circulation function while crushing materials, and can ensure that slurry can circulate inside and outside the circulation pipeline. Compared with a conditioning machine in the prior art, the soymilk machine of the embodiment needs no pressurizing mechanism such as a pressurizing pump, and has the advantages of simple structure, lower cost and capability of automatic cleaning.

Meanwhile, the outlet of the circulating pipeline in the prior art is generally arranged above the water level identification line, when the soybean milk is made to circulate, a large amount of air can be brought into and mixed with the soybean milk in the backflow cavity when the soybean milk sprayed from the outlet of the circulating pipeline flows back to the backflow cavity under the action of gravity, so that more soybean milk foam in the backflow cavity is caused, the soybean milk is not favorable for the non-crushed materials in the foam to continuously participate in the circulating crushing, meanwhile, the false anti-overflow phenomenon is easily caused in the boiling and pulping process, the soybean milk is not boiled, and the potential safety hazard of food exists. And the food preparation machine of this embodiment sets up circulating line's export in being less than the water level sign line, therefore, the thick liquid that flows back from the export can not bring into a large amount of air and the thick liquid mixture of backward flow intracavity, thereby great reduction the quantity that the foam appears, and, when circulating line's export was located the below of water level sign line, the thick liquid stream that erupts from the circulating line export can have to block the high-speed rotatory thick liquid stream in the backward flow intracavity, slow down rotation and vortex effect, at this moment, the thick liquid stream that is located the backward flow intracavity is owing to lose the centrifugal rotation effect, thereby it continues to participate in the circulation crushing to flow in the crushing intracavity from gathering the mouth more easily, corresponding further promotion the material by the kibbling efficiency of circulation, and simultaneously, during the slurrying, the thick liquid surface is also more steady, difficult to take place the thick liquid splash phenomenon.

In this embodiment, only one circulation line is provided, but a plurality of circulation lines may be provided. Meanwhile, for the embodiment, when the top end of the outlet of the circulating pipeline is flush with the water level mark line, the mixing of air and slurry can be greatly reduced, but the mixing is much worse than the mixing under the water level mark line. It should be noted that, for the present embodiment, there may be one or more water level identification lines disposed on the side wall of the volume, and when there are more water level identification lines, the outlet of the circulation pipeline is required to be at least lower than the lowest water level, such as: the volume of the pulping liquid in this embodiment is 600mL to 1300mL, and there are three water level lines, 600mL, 1000mL and 1300mL, in this embodiment, the water level identification line is a water level identification area identified between the 600mL water level line and the 1300mL water level line, and the outlet of the circulation pipeline is lower than the lowest water level line (the lower end of the water level identification area). In addition, in this embodiment, the area of the opening of the flow gathering port is smaller than the area of the opening of any horizontal cross section on the backflow cavity below the outlet of the circulation pipeline, so that the slurry flow ejected from the outlet of the circulation pipeline can enter the crushing cavity through the flow gathering effect of the flow gathering port. In addition, in the embodiment, the height difference between the outlet of the circulating pipeline and the inlet of the circulating pipeline is generally 30 mm-180 mm. It should be noted that, for this embodiment, another coarse crushing blade may be disposed above the crushing blade, and the coarse crushing blade may be located outside the crushing cavity. In addition, the structure and parameters of the present embodiment can be applied to other embodiments of the present invention.

Example two:

fig. 2 and 3 are schematic structural diagrams of a second embodiment of the present invention. The difference from the first embodiment is that: the food processor in this embodiment is of a bottom-mounted motor structure, the fluid collecting port 13 is tubular, the fluid collecting port 13 has a water inlet end 131 and a water outlet end 132, the water inlet end 131 is disposed in the fluid returning chamber 12, and the water outlet end 132 is disposed in the pulverizing chamber 11. And, be provided with play thick liquid mouth 33 and control valve 34 on the circulating line 3, play thick liquid mouth 33 and circulating line 3 intercommunication, control valve 34 is used for controlling the play thick liquid of play thick liquid mouth 33, and control valve 34 sets up between play thick liquid mouth 33 and circulating line 3. By arranging the control valve 34 and the pulp outlet 33, after pulping is finished, a user can directly pour the drink by controlling the control valve 34.

Meanwhile, in order to increase the water pushing circulation effect of the crushing blade on the slurry, the crushing blade 2 in the embodiment has a water pushing part on the slurry besides a cutting part on the material, wherein the cutting part is a cutting edge 21 of the crushing blade, and the water pushing part is a pushing blade 22 arranged at the tail end of the crushing blade 2, because the pushing blade 22 is vertically arranged relative to the cutting edge 21, in the rotating process of the crushing blade 2, the pushing blade 22 can push the slurry into the circulation pipeline 3 by larger pushing force, so that the circulation speed of the slurry is faster, and the crushing efficiency is higher. It can be understood that, for this embodiment and other embodiments of the present invention, a plurality of crushing blades may also be provided, and the end portions of some of the crushing blades may extend out of the flow gathering port into the backflow cavity to play a role in enhancing turbulent flow; it is of course also possible to use a single crushing blade, which is partly located in the crushing chamber and whose end extends out of the flow collection opening into the return chamber.

In addition, the inlet 31 of the circulating pipeline is arranged on the side wall of the crushing cavity 11, the inlet 31 of the circulating pipeline comprises an inlet upper edge 311 and an inlet lower edge 312, and the crushing blade 2 is positioned in a vertical area N of a horizontal plane corresponding to the inlet upper edge 311 and the inlet lower edge 312. When smashing blade 2 and setting up in this regional N, when smashing blade 2 rotatory, the thick liquid stream that push away the horizontal promotion of blade 22 received centrifugal force effect, can directly get rid of in the circulating line 3 to the hindrance that receives when having reduced thick liquid stream cyclic motion, correspondingly also increaseed the circulation efficiency of thick liquid stream.

In this embodiment, set the mouth of converging to the tubular structure, the thick liquid gets into from the end of intaking, flows out from the play water end, and the material has the effect that gravity accelerates at the in-process through the mouth of converging, behind the material and the thick liquid impact crushing blade that accelerate, the efficiency of smashing of improvement material of ability bigger degree. Meanwhile, the flow gathering port is arranged to be of a tubular structure, the material in the crushing cavity can be prevented from rebounding to the backflow cavity after colliding with the crushing blade, and severe splashing caused by collision of the crushing blade on the serous fluid in the crushing cavity can be prevented, so that scalding accidents of consumers are caused.

In the present embodiment, the cutting portion and the water pushing portion of the crushing blade are not limited to the cutting edge and the pushing blade in the present embodiment, and other configurations are possible, for example, the crushing blade includes a cutting blade for cutting a material and a blade disposed below the cutting blade, and both the blade and the cutting blade are fixed to a motor shaft or a rotating shaft. In addition, in order to further improve the circulation efficiency of the materials in the circulation pipeline, for the embodiment, the rotating speed of the motor can be increased. According to the research of the inventor, the load rotation speed of the motor is preferably more than 8000r/min for the structure that the slurry is circularly crushed inside and outside the circulating pipeline by the rotation of the crushing blade, wherein the load rotation speed of the motor used in the embodiment is 10000r/min, 12000r/min, 16000r/min and 20000 r/min. Meanwhile, the inventor also finds that the water pushing circulation effect of the crushing blades on the slurry can be correspondingly improved by reducing the capacity of the crushing cavity. For the embodiment, the volume of the crushing cavity is generally 22 mL-380 mL, wherein if the pulping amount of the container is 600 mL-1300 mL, the volume of the crushing cavity is preferably 50 mL-180 mL; when the pulping amount of the container is more than 1300mL, the capacity of the crushing cavity is preferably 100 mL-300 mL. If the capacity of the crushing cavity is larger than 400mL, the diameter of the crushing blade needs to be set larger at the moment, so that the materials can be crushed in the crushing cavity in a concentrated mode, the load born by the corresponding motor is increased, the use requirement on the motor is also improved, and the cost of the whole machine is obviously increased. If the diameter of the crushing blade is not increased, the effect of the crushing blade on the concentrated crushing of the materials is poor, and the efficiency of the crushing blade in centrifugal water pushing is also reduced.

In this embodiment, the vertical height from the top end of the flow gathering port to the water level mark line is H1, and the vertical height from the top end of the outlet of the circulation pipeline to the water level mark line is H (wherein, the calculation rule of H and H1 is that if there is one water level mark line, the calculation is performed from the bottom end of the water level mark line, and if there are multiple water level lines, the calculation is performed from the water level mark area where the liquid level between the highest water level and the lowest water level is actually located). The inventors of the present invention found through their studies that H/H1=0.3 to 0.8 is required for the structure of the present embodiment. Because, if H/H1 is less than 0.3, the outlet of the corresponding circulation line is located very close to the liquid level below the water level mark line, at this time, if the motor load rotation speed exceeds 20000r/min, the slurry ejected from the outlet of the circulation line may penetrate the liquid level to be ejected due to the large energy, and when the slurry falls back to the return chamber, a large amount of air is still brought in, and accordingly, the foam is increased. Meanwhile, if the H/H1 is larger than 0.8, the outlet of the circulating pipeline is positioned below the water level identification line and is relatively far away from the liquid level, the slurry above the outlet can effectively prevent the slurry ejected from the outlet from rushing out of the liquid level, and meanwhile, material particles close to the liquid level cannot smoothly flow back to the crushing cavity from the flow gathering port due to the ejection blocking effect of the outlet of the circulating pipeline, so that the material crushing is poor. Therefore, for this embodiment, requirement H/H1=0.3~0.8, in this within range, both can guarantee that the thick liquid does not produce too much foam, can also guarantee simultaneously that the material can not appear smashing bad phenomenon, meanwhile, lie in this within range, the thick liquid stream that erupts from the circulation pipeline export still has the thick liquid stream that slows down the backward flow intracavity and the effect of vortex, can guarantee that thick liquid and material can be more quick get into from gathering the mouth and smash the intracavity participation circulation and smash. In the present embodiment, H/H1 is preferably 0.5 to 0.75.

It should be noted that the above structural modifications and parameter selection of the present embodiment can also be applied to other embodiments of the present invention.

Example three:

as shown in fig. 4, 5 and 6, it is a schematic structural diagram of a third embodiment of the present invention. The difference from the second embodiment is that: in this embodiment, the bottom of the backflow cavity 12 has a flow collecting part 14 protruding toward the center of the container, the top surface of the flow collecting part 14 is inclined downwards relative to the horizontal plane, and the inclination angle α of the flow collecting part 14 relative to the horizontal plane is generally less than 80 °. Because the flow gathering part 14 is in an inverted cone shape, the backflow materials and slurry can be collected, so that the materials can flow in from the flow gathering port more easily. Meanwhile, the top of the crushing cavity 11 is provided with a shielding part 15 for limiting the material in the crushing cavity 11 (the shielding part 15 can further prevent the material from being ejected out of the crushing cavity 11 after being collided by the crushing blades), wherein the flow gathering port 13 is arranged through the flow gathering part 14 and the shielding part 15. The lower edge 312 of the inlet of the circulation pipeline in the embodiment is flush with the bottom surface of the crushing cavity 11, and the inlet 31 of the circulation pipeline is provided with the material blocking piece 5, so that the material blocking piece 5 can prevent large materials from entering the circulation pipeline without being crushed, and the risk of blocking the circulation pipeline is caused. In addition, a heating device 6 is arranged outside the return cavity 12, and the heating device 6 is positioned below the outlet 32 of the circulating pipeline.

In this embodiment, the flow gathering mouth is square, and when thick liquid was spouted to the backward flow chamber from circulation line's export, thick liquid can be rotary motion along the inner wall in backward flow chamber. Because the flow gathering port is square, when the slurry rotates to the flow gathering port, the slurry collides with the corner of the flow gathering port to generate turbulence, so that the slurry can enter the crushing cavity more easily. If the converging port is circular, the rotating slurry flow may be thrown out by centrifugal force and not easily enter the pulverization chamber, and therefore, for this embodiment, the converging port may have other non-circular structures including a square shape.

In this embodiment, the area of the opening of the fluid trap is S1, and the rotation area of the crushing blade is S2. The inventor of the present invention found, according to the research, that for this embodiment, in order to ensure that the material and the slurry can flow into the crushing cavity through the flow gathering port to participate in the circular crushing, it is required that S1/S2 is not less than 0.25 and not more than 4, because when S1/S2 is less than 0.25, the area of the mouth of the flow gathering port is small, the inflow amount of the material and the slurry will be less than the inflow amount of the slurry in the crushing cavity flowing into the circulation pipeline, and at this time, the phenomenon of idle driving exists in the crushing cavity, which is not only not favorable for the crushing of the material, but also may even generate the noise of idle driving of the motor when the crushing is serious. If S1/S2 is greater than 4, the area of the mouth of the corresponding flow gathering port is much larger than the rotating area of the crushing blade, and at this time, the material flowing in from the flow gathering port may enter from the edge of the flow gathering port and cannot be collided and cut by the crushing blade, and the phenomenon of bean curd exists after the pulping. When the capacities of the crushing chambers are different, the ratio of S1/S2 is also different, and when the capacity of the crushing chamber is smaller, S1 is generally required to be larger than S2, for example, S1/S2 is 1.25, 1.5, 1.75, 2 and 2.5. If the volume of the pulverizing chamber is relatively large, it is generally required that S1 is smaller than S2, such as S1/S2 is 0.3, 0.4, 0.5, 0.6, 0.7, 0.8, 0.9, etc. Further, the present inventors have found, based on the study, that in the present embodiment, when the volume of the crushing chamber is 60mL to 100mL, the area of the flow-gathering port is generally slightly smaller than the rotating area of the crushing blade.

Simultaneously, in this embodiment, the terminal inside wall distance to crushing chamber of smashing the blade is a to the requirement, and 1mm is no less than a and is no more than 15mm, because, when this within range, not only can guarantee that the material that falls into from the mouth that gathers flows can all basically be smashed the blade cutting, in addition, can also guarantee to smash the blade and have sufficient drive force to the thick liquid, realize the thick liquid at the circulation pipeline internal and external circulation.

In the embodiment, the height of the inlet of the circulation pipeline is h1, and the height from the lower end surface of the crushing blade to the lower edge of the inlet is h2, wherein h2 is required to be more than or equal to 1/4h 1. Because, in this embodiment, the lower edge of the inlet is parallel to the bottom of the container, if h2 is smaller than 1/4h1, the crushing blade is closer to the bottom of the container, and during the high-speed rotation of the crushing blade, negative pressure is generated in the region below the crushing blade, the smaller h2 is, the larger negative pressure is, and the slurry above the crushing blade cannot be filled into the region due to the negative pressure, so that a vacuum region is formed in the region below the crushing blade, which is not beneficial to cutting and crushing materials by the crushing blade, and is also not beneficial to pushing and circulating the slurry by the crushing blade. It should be noted that, for example, the crushing blade may be disposed above the upper edge of the inlet, and the crushing blade may have a water pressing portion, and when the crushing blade rotates at a high speed, the slurry is driven to rotate below the crushing blade, and when the slurry rotates to the inlet of the circulation pipe, the rotating slurry may continuously flow into the inlet of the circulation pipe due to a centrifugal force, and at this time, the water pressing portion of the crushing blade may have a water pushing function for pushing the slurry, and the water pressing portion may also be regarded as the water pushing portion of the crushing blade. The aim of circularly crushing the slurry in the container inside and outside the circulating pipeline can be fulfilled.

As shown in fig. 7, which is a top view of the food processor of this embodiment, when the vertical projection is on the horizontal plane, the line from the center of the outlet to the center of the container is L1, when the circular pulping process is performed, the pulp ejected from the outlet and L1 are in an inclined spraying state, and the ejected pulp and L1 form a horizontal spraying angle β. The present inventors have found, based on the study, that when the outlet of the circulation line is set so that the angle β is formed between the ejected slurry and L1, the side wall of the tank can be cleaned when the water flow is ejected from the outlet, and the slurry flows down the side wall of the return chamber when the ejected slurry is ejected, so that the splashing phenomenon is less likely to occur. Also, the present inventors have found from the studies that 0. ltoreq. beta. ltoreq.60 ° is required for the present embodiment. It should be noted that, under this structure, the thick liquid stream that jets from the exit of circulating line can carry out violent rotation in the backward flow intracavity, if at this moment, if the direction of rotation of thick liquid stream is opposite with the direction of rotation of crushing blade, this rotatory thick liquid stream is favorable to offsetting the rotational speed of backward flow intracavity thick liquid to can get into crushing intracavity more easily to the material, and meanwhile, this rotatory thick liquid stream still can have the effect of vortex to the thick liquid stream of crushing intracavity, thereby further promote the cutting efficiency of crushing blade to the material.

Fig. 8 is a front view of the food processor of the present embodiment. When the circular pulping is carried out, the pulp sprayed out of the outlet is in a downward inclined spraying state with the horizontal plane, and the sprayed pulp and the horizontal plane form a vertical spraying angle theta. Because the slurry jetted from the outlet is in an inclined downward jetting state, the slurry can be enabled to be disorderly and disturbed when entering the flow gathering port, and the slurry flow rotating in the backflow cavity can be enabled to be prevented from rotating when entering the flow gathering port. Also, the present inventors have found from the research that 0. ltoreq. theta. ltoreq.60 deg. is required for the present embodiment.

The inventor of the present invention found that if the slurry ejected from the outlet of the circulation pipeline is in an inclined downward ejection state with respect to the horizontal plane, the vertical height H of the top end of the outlet from the water level mark line is at least less than 100mm, and if H is greater than 100mm, the slurry is circularly disturbed below the liquid level because the outlet is located below the water level mark line, and the outlet is ejected downward in an inclined manner, so that the liquid level is relatively in a stable state.

It should be noted that the slurry flow ejected from the outlet may also be in an obliquely upward ejection state from the horizontal plane, and in this case, the vertical ejection angle θ formed with the horizontal plane should be at least less than 60 °. The inventor discovers through research that if the grout ejected from the outlet of the circulating pipeline is in an upward inclined ejection state with the horizontal plane, H is at least larger than 10mm, if H is smaller than 10mm, the phenomenon of excessive foam can also occur, because the ejection angle of the outlet is inclined upwards, the height of the grout above the outlet is not enough to block the energy of the grout ejected from the outlet, the grout flow penetrates through the liquid level to go out, when the grout flow falls back under the action of gravity, a large amount of air can be brought into the grout to be mixed with the grout in a backflow cavity, the liquid level is caused to generate a large amount of foam, the circulation of the grout is not facilitated, the phenomenon of false overflow prevention is easily caused during boiling and pulping, and potential safety hazards exist.

Therefore, under the structure of the embodiment, for comprehensive consideration, H is generally required to be more than or equal to 10mm and less than or equal to 100mm, wherein H is preferably 50 mm-80 mm.

For this embodiment, when the outlet of circulation pipeline had both formed the horizontal injection angle with the backward flow chamber lateral wall, had formed the vertical injection angle again, the thick liquid stream of injection not only can disturb the thick liquid stream of making rotary motion in the backward flow chamber, the cutting efficiency of promotion crushing blade to the material that can also be great. Of course, it should be noted that the outlet of the circulation line may be mounted on the side wall of the return chamber in only one of the above-described horizontal spray angle and vertical spray angle.

As shown in fig. 8, an inclined section 19 inclined with respect to the vertical plane is also provided in the lower part of the return chamber, and the outlet 32 of the circulation line is provided in this inclined section 19. It should be noted that, for this inclined section, it is required that its inclination angle γ =0~80 relative to the vertical plane, because inclination angle γ is too big, and when being greater than 80, because the thick liquid has the viscidity, the gravity of material granule itself can be overcome to the material granule that is located on the inclined section under the effect of viscous force to the effect that the material rolls from the inclined section and gets into the mouth that gathers materials can weaken relatively.

In addition, for this embodiment, the heating device is disposed on the sidewall of the return cavity and below the outlet of the circulation pipeline, and mainly considers that the slurry in the return cavity is relatively thin compared with the slurry in the crushing cavity, so that the phenomenon of pan pasting is not easily caused during heating. And when making many people's drink, can directly add water and blend in the backward flow intracavity, at this moment, can directly heat the backward flow chamber, heating efficiency is higher. Certainly, also can set up another heating device on the outer wall in crushing chamber, can further promote this food preparation machine's heating efficiency, realize quick slurrying. In the present embodiment, the arrangement of the heating device is not limited to the structure of the present embodiment, and the present embodiment can be applied to any heating method in the related art. It should be further noted that the flow collecting part in the embodiment is inclined downward relative to the horizontal plane, and when the flow collecting part is parallel to the horizontal plane, the pulping effect of the embodiment can be realized, at this time, the phenomenon of slag accumulation at the corner of the flow collecting part, particularly the corner where the flow collecting part is connected with the backflow cavity, is not favorable for the material to enter the flow collecting opening for internal circulation, and at this time, if the turbulence effect of the slurry in the backflow cavity is increased, the phenomenon of material slag accumulation can be solved.

The present embodiment has the same beneficial effects as the above embodiments, and the details are not repeated herein. It should be noted that, for the above structural changes and selection of parameters of the present embodiment, other embodiments of the present invention may be applicable.

It is also possible for the food processor of the invention to employ other comminution structures than comminution blades, for example where the comminution means is shear comminution or the like.

When the crushing device is a shearing crushing device, the food processor can adopt the following structure, for example:

the utility model provides a food processor, includes the container and with the circulation pipeline of container upper and lower intercommunication, be provided with the reducing mechanism that drives through the motor in the container, the container is including the crushing chamber that is located the container bottom, be located the backward flow chamber and the converging of intercommunication crushing chamber and backward flow chamber of crushing chamber top and draw together mouthful, reducing mechanism sets up in crushing intracavity, and reducing mechanism including being fixed in the epaxial moving knife of motor and being fixed in the stationary knife of crushing intracavity, it shears the smashing to form the material with the stationary knife cooperation to move the knife, it sets up in the top of moving the knife to gather the mouth, circulation pipeline's entry is located crushing intracavity, circulation pipeline's export is located the backward flow intracavity, the mouth area of gathering the mouth is less than the arbitrary horizontal cross-section's on the backward flow chamber of circulation pipeline export below oral area.

Furthermore, the bottom of the backflow cavity is provided with a flow gathering part protruding towards the center of the container, and the flow gathering port penetrates through the flow gathering part.

Further, the flow collecting part is inclined downwards relative to the horizontal plane.

Furthermore, crushing chamber top is provided with the shielding part of injecing the material in crushing intracavity, it sets up to gather the mouth and run through the shielding part.

Furthermore, the flow gathering port is tubular, the flow gathering port is provided with a water inlet end and a water outlet end, the water inlet end is arranged in the backflow cavity, and the water outlet end is positioned in the crushing cavity;

alternatively, the flow gathering port is non-circular.

Further, the fixed cutter is a shearing cylinder, shearing holes are formed in the side wall of the shearing cylinder, and the shearing cylinder is fixed to the bottom of the crushing cavity.

Furthermore, the movable knife is blade-shaped and comprises a transverse cutting edge and a shearing edge bent downwards relative to the cutting edge, and the shearing edge is matched with a shearing hole in the shearing cylinder to form shearing matching;

or, the movable cutter is in a cylindrical shape, the movable cutter comprises a shearing inner cylinder matched with the shearing cylinder and a cutting blade fixed on a motor shaft, a shearing inner hole corresponding to the shearing hole is formed in the shearing inner cylinder, and the shearing inner cylinder and the cutting blade are integrally formed.

Further, the stationary knife comprises a cylindrical static grinding part and a disc-shaped static shearing part, the static grinding part is of a penetrating structure, static grinding teeth are arranged on the inner wall of the static grinding part, the static shearing part is located at the bottom of the static grinding part, downward convex static shearing teeth are arranged at the bottom of the static shearing part, the movable knife comprises a movable grinding part matched with the static grinding part and a movable shearing part matched with the static shearing part, the movable shearing part is located at the bottom of the movable grinding part, the movable shearing part is disc-shaped, the top of the movable shearing part is provided with an inner ring tooth sheared with the inner side of the static shearing tooth, an outer ring tooth sheared with the outer side of the static shearing tooth and a shearing groove located between the inner ring tooth and the outer ring tooth, the static shearing tooth is inserted into the shearing groove, the movable grinding part is columnar, the movable grinding part is sleeved on the inner side of the static grinding part, the movable grinding part comprises a grinding base body and an extrusion head arranged at the top of the grinding base body, the outer wall of the grinding base body is provided with movable grinding teeth corresponding to the static grinding teeth, and the extrusion head and the static grinding teeth form extrusion fit.

Furthermore, an outlet of the circulating pipeline is arranged on the side wall of the return cavity, when the circulating pipeline is vertically projected on a horizontal plane, a connecting line from the center of the outlet to the center of the container is L1, during circulating pulping, the pulp sprayed out of the outlet is in an inclined spraying state with L1, and a horizontal spraying angle formed by the sprayed pulp and L1 is beta, wherein beta is more than or equal to 0 and less than or equal to 60 degrees;

or the outlet of the circulating pipeline is arranged on the side wall of the return cavity, when the pulping is circulated, the pulp sprayed from the outlet is in an inclined downward spraying state with the horizontal plane, and the vertical spraying angle formed by the sprayed pulp and the horizontal plane is theta, wherein theta is more than or equal to 0 and less than or equal to 60 degrees;

or the inlet of the circulating pipeline is arranged on the side wall of the crushing cavity, and the material blocking part is arranged at the inlet.

Further, the load rotating speed of the motor is at least 10000 r/min;

or the circulating pipeline is provided with a pulp outlet nozzle and a control valve, the pulp outlet nozzle is communicated with the circulating pipeline, the control valve is used for controlling pulp outlet of the pulp outlet nozzle, and the control valve is arranged between the pulp outlet nozzle and the circulating pipeline;

or a heating device is arranged outside the reflux cavity and is positioned below the outlet of the circulating pipeline;

or the volume of the crushing cavity is 52-380 mL.

An embodiment in which the crushing apparatus is a shear crushing structure on the basis of the present invention will be described below.

Example four:

fig. 9 is a schematic structural diagram of a fourth embodiment of the present invention. A food processor comprises a container 1a, a crushing device 2a arranged in the container 1a and a circulating pipeline 3a for communicating the container up and down, wherein the crushing device 2a is driven by a motor 4a, the circulating pipeline 3a is arranged outside the container, the container 1a comprises a crushing cavity 11a positioned at the bottom of the container, a backflow cavity 12a positioned above the crushing cavity 11a and a flow gathering port 13a communicated with the crushing cavity 11a and the backflow cavity 12a, the crushing device 2a is arranged in the crushing cavity 11a, the crushing device 2a comprises a movable knife 21a fixed on a motor shaft and a fixed knife 22a fixed in the crushing cavity, the movable knife 21a and the fixed knife 22a are matched to shear and crush materials, the flow gathering port 13a is arranged above the movable knife 21a, and an inlet 31a of the circulating pipeline is positioned in the crushing cavity 11a, the outlet 32a of the circulation line is positioned in the return cavity 12a, a water level mark line 90a is arranged on the inner wall of the container 1a, and the outlet 32a of the circulation line is positioned below the water level mark line 90 a.

The food processing machine in the embodiment is a soybean milk machine, the soybean milk machine is provided with a machine head I and a cup body II, wherein the cup body II is of a double-layer structure and comprises an inner cup body and a shell 10a, the container 1a is the inner cup body of the soybean milk machine, a circulating pipeline 3a is hidden in an interlayer between the inner cup body and the shell 10a, and a motor 4a is arranged inside the machine head I. In this embodiment, the area of the opening of the fluid collecting port 13a is smaller than the area of the opening of any horizontal section of the return chamber 12a below the outlet 32a of the circulation line.

In this embodiment, because the container has crushing chamber and backward flow chamber, smashes the chamber and communicates through converging the mouth with the backward flow chamber to, the oral area of converging the mouth area and being less than arbitrary horizontal cross-section's oral area on the backward flow chamber of circulating line export below, consequently, the thick liquid of following backward flow chamber backward flow can concentrate through converging the mouth and flow back to crushing intracavity, and it has the gathering material to converge the mouth, guarantees that the material can both flow into through converging the mouth and smashes the intracavity and participate in crushing. Simultaneously, the reducing mechanism sets up in smashing the intracavity, consequently, can concentrate in less crushing intracavity from the material that gathers the mouth and flow into and smash, and the material is when smashing the intracavity and concentrating the crushing, because it has the thick liquid to flow into from gathering the mouth and smashes the chamber to last in the backward flow chamber, the material that smashes the intracavity receives the thick liquid pressure effect of gathering the mouth top, the material is difficult to run out and enter into the backward flow chamber from smashing the chamber in, consequently, the material is concentrated in smashing the intracavity and is concentrated kibbling efficiency height. In addition, in the crushing cavity, when the motor drives the movable cutter to rotate at a high speed, the movable cutter can drive the slurry flow to do high-speed centrifugal motion, the inlet of the circulating pipeline is arranged in the crushing cavity, the slurry flow doing the centrifugal motion can enter the circulating pipeline from the inlet under the action of inertia force, and the subsequent slurry flow can continuously push the slurry flow entering the circulating pipeline before to flow back to the backflow cavity from the outlet due to the continuous high-speed rotating motion of the movable cutter. Therefore, the movable knife of the food processor in the embodiment has a strong water pushing circulation function while crushing materials, and can ensure that the slurry can circulate inside and outside the circulation pipeline. Compared with the prior art, the food processor of the embodiment needs to be provided with the grinding disc and the pressurizing mechanism, has simple structure and lower cost, and can carry out automatic cleaning.

In this embodiment, the stationary knife is fixed in the bottom of aircraft nose, and the stationary knife forms the shearing to the material with moving the sword cooperation and smashes. In this embodiment, only one circulation line is provided, but a plurality of circulation lines may be provided. Moreover, for the technical effects produced by the embodiment, other embodiments of the present invention also have the advantages that will not be described in detail when describing the effects of other embodiments. It should be noted that, in this embodiment, the selection of the proportional relation value between the vertical height H from the top end of the outlet of the circulation pipeline to the water level identification line and the vertical height H1 from the top end of the flow gathering port to the water level identification line may also refer to the relation value in the above embodiment, and the generated technical effects are the same as those in the above embodiment, and are not described herein again. Moreover, it should be noted that the structural changes and parameter selection of the present embodiment can also be applied to the fifth to seventh embodiments.

Example five:

fig. 10, 11 and 12 are schematic structural diagrams of a fifth embodiment of the present invention. The difference from the fourth embodiment is that: the food processor in this embodiment is of a bottom-mounted motor structure, the fluid collecting port 13a is tubular, the fluid collecting port 13a has a water inlet end 131a and a water outlet end 132a, the water inlet end 131a is disposed in the backflow cavity 12a, and the water outlet end 132a is disposed in the pulverizing cavity 11 a. The circulation pipeline 3a is provided with a slurry outlet nozzle 33a and a control valve 34a, the slurry outlet nozzle 33a is communicated with the circulation pipeline 3a, the control valve 34a is used for controlling slurry outlet of the slurry outlet nozzle 33a, and the control valve 34a is arranged between the slurry outlet nozzle 33a and the circulation pipeline 3 a. By arranging the control valve 34a and the pulp outlet 33a, after pulping is finished, a user can directly pour the drink by controlling the control valve 34 a.

The fixed knife 22a in this embodiment is a shearing cylinder, the side wall of the shearing cylinder is provided with a shearing hole 221a, the shearing cylinder is fixed at the bottom of the crushing cavity 11a, in addition, the movable knife 21a is blade-shaped, the movable knife 21a comprises a transverse cutting edge 211a and a shearing edge 212a bent downwards relative to the cutting edge 211a, and the shearing edge 212a is matched with the shearing hole 221a on the shearing cylinder to form shearing matching.

In this embodiment, the inlet of circulation pipeline sets up on the lateral wall of smashing the chamber, and cuts the entry setting that the hole just faces circulation pipeline, and material and thick liquid after cuting like this receive the centrifugal thrust effect of moving the sword, can directly enter into circulation pipeline, and the resistance that the thick liquid stream received is less. And, in this embodiment, set the mouth of converging to the tubular structure, the thick liquid gets into from the end of intaking, flows from the end of going out, and the material has the effect that gravity accelerates at the in-process through the mouth of converging, and behind the cutting edge on the impact sword of material and thick liquid that has accelerated, can the bigger degree carry out coarse crushing to the material for the material after coarse crushing can enter into the cooperation of shearing edge and shearing hole and cut crushing, can smash the material more in the degree like this, promotes the crushing efficiency of material. Meanwhile, the flow gathering port is arranged to be of a tubular structure, the materials in the crushing cavity can be prevented from rebounding to the backflow cavity after colliding with the movable knife, and severe splashing caused by collision of cutting edges on the serous fluid in the crushing cavity can be prevented, so that scalding accidents of consumers are caused.

It should be noted that, for the embodiment, the rotation speed of the motor can also be increased in order to further increase the circulation efficiency of the material in the circulation pipeline. The inventor finds that the load rotating speed of the motor is more than 10000r/min according to research, and the slurry can be better circulated inside and outside the circulating pipeline. Meanwhile, the inventor finds that the reduction of the capacity of the crushing cavity can correspondingly improve the circulation efficiency of the slurry according to the research, and the centrifugal pushing efficiency of the moving blade on the slurry is higher. For the present embodiment, the volume of the pulverizing cavity is generally 52mL to 380mL, wherein if the pulping amount of the container is 600mL to 1300mL, the volume of the pulverizing cavity is preferably 52mL to 180 mL; when the pulping amount of the container is more than 1300mL, the capacity of the crushing cavity is preferably 100 mL-300 mL. It should be noted that the above structural modifications and parameter selection of the present embodiment can also be applied to other embodiments of the present invention.

Example six:

fig. 13, 14, 15 and 16 are schematic structural views illustrating a sixth embodiment of the present invention. The difference from the fifth embodiment is that: in this embodiment, the bottom of the backflow cavity 12a has a flow collecting portion 14a protruding toward the center of the container, the top surface of the flow collecting portion 14a is inclined downward relative to the horizontal plane, and the inclination angle of the flow collecting portion 14a relative to the horizontal plane is generally less than 80 °. Because the flow gathering part 14a is in an inverted cone shape, the backflow materials and slurry can be collected, so that the materials can flow in from the flow gathering port more easily. Meanwhile, the top of the crushing cavity 11a is provided with a shielding part 15a for limiting the material in the crushing cavity 11a (the shielding part 15a can further prevent the material from being ejected out of the crushing cavity 11a after being collided by the knife), wherein the flow gathering port 13a is arranged through the flow gathering part 14a and the shielding part 15 a. The inlet 31a of the circulation pipeline in this embodiment is arranged on the side wall of the crushing cavity 11a, and the inlet 31a of the circulation pipeline is provided with the material blocking member 5a, and the material blocking member 5a can prevent large materials from entering the circulation pipeline without being crushed, so that the risk of blocking the circulation pipeline is caused. In addition, a heating device 6a is arranged outside the return cavity 12a, and the heating device 6a is positioned below the outlet 32a of the circulating pipeline.

In this embodiment, the movable blade is in a cylindrical shape, the movable blade includes a shearing inner cylinder 213a matched with the shearing cylinder and a cutting blade 214a fixed on the motor shaft, a shearing inner hole 215a corresponding to the shearing hole is formed in the shearing inner cylinder 213a, and the shearing inner cylinder 213a and the cutting blade 214a are integrally formed. It should be noted that, for this embodiment, a blade-like structure may be further disposed on the outer wall of the shearing cylinder, and the circulation rate of the slurry inside and outside the circulation pipeline is increased by using the strong water pushing effect of the blades.

In this embodiment, the arrangement of the outlet of the circulation line is also an important structure of this embodiment. When the container cover is arranged on the top of the container, the outlet of the circulating pipeline can be arranged on the container cover or directly penetrates through the container cover to extend into the backflow cavity. For this embodiment, the outlet of the circulation line is arranged on the side wall of the return chamber.

As shown in fig. 17, which is a top view of the food processor of this embodiment, when the vertical projection is on the horizontal plane, the line from the center of the outlet to the center of the container is L1, when the circulating pulping process is performed, the pulp ejected from the outlet and L1 are in an inclined spraying state, and the ejected pulp and L1 form a horizontal spraying angle β. The present inventors have found, according to the research, that when the outlet of the circulation line is arranged so that the sprayed slurry is at an angle β to L1, the side wall of the tank can be cleaned by the sprayed slurry from the outlet, and the sprayed slurry is less likely to splash when flowing down the side wall of the return chamber. Under the condition of ensuring safety, the container can be cleaned. Also, the present inventors have found from the studies that 0. ltoreq. beta. ltoreq.60 ° is required for the present embodiment. In this configuration, the slurry flow jetted from the outlet of the circulation line is vigorously rotated in the return chamber, and if the rotational direction of the slurry flow is opposite to the rotational direction of the movable blade, the rotating slurry flow is advantageous to further disturb the slurry flow in the pulverization chamber, thereby further improving the efficiency of pulverizing the material.

Fig. 18 is a front view of the food processor of the present embodiment. When the circular pulping is carried out, the pulp sprayed out of the outlet is in a downward inclined spraying state with the horizontal plane, and the sprayed pulp and the horizontal plane form a vertical spraying angle theta. Because the thick liquid that erupts from the exit can make rotary motion along the inner wall of backward flow chamber, and the thick liquid is the decurrent injection state of slope, can realize that the thick liquid is when entering into the mouth that gathers streams, and the thick liquid stream of slope injection can be to the thick liquid stream of rotation disorder, vortex to guarantee that thick liquid stream no longer takes place rotary motion when entering into the mouth that gathers streams. Also, the present inventors have found from the research that 0. ltoreq. theta. ltoreq.60 deg. is required for the present embodiment.

For the embodiment, when the outlet of the circulating pipeline and the side wall of the return cavity form a horizontal spray angle and a vertical spray angle, the sprayed slurry flow can disturb the slurry flow which does rotary motion in the return cavity, and the cutting efficiency of the cutting blade on the material can be greatly improved. Of course, it should be noted that the outlet of the circulation line may be mounted on the side wall of the return chamber in only one of the above-described horizontal spray angle and vertical spray angle.

Example seven:

fig. 19, 20 and 21 are schematic structural views of a seventh embodiment of the present invention. The present embodiment is different from the sixth embodiment in the structure of the shearing and crushing device: the fixed cutter comprises a cylindrical static grinding part 23a and a disc-shaped static shearing part 24a, the static grinding part 23a is of a penetrating structure, static grinding teeth 231a are arranged on the inner wall of the static grinding part 23a, the static shearing part 24a is positioned at the bottom of the static grinding part 23a, downward convex static shearing teeth 241a are arranged at the bottom of the static shearing part 24a, the movable cutter comprises a movable grinding part 25a matched with the static grinding part 23a and a movable shearing part 26a matched with the static shearing part 24a, the movable shearing part 26a is positioned at the bottom of the movable grinding part 25a, the movable shearing part 26a is disc-shaped, the top of the movable shearing part 26a is provided with inner ring teeth 261a sheared with the inner side of the static shearing teeth 241a, outer ring teeth 262a sheared with the outer side of the static shearing teeth 241a and shearing grooves 263a positioned between the inner ring teeth 261a and the outer ring teeth 262a, the static shearing teeth 241a are inserted into the shearing grooves 263a, the movable grinding part 25a is columnar, the movable grinding part 25a is sleeved on the inner side of the static grinding part 23a, the movable grinding part 25a comprises a grinding base body 251a and an extrusion head 252a arranged at the top of the grinding base body 251a, the outer wall of the grinding base body 251a is provided with movable grinding teeth 2511a corresponding to the static grinding teeth 231a, and the extrusion head 252a and the static grinding teeth 231a are in extrusion fit. Meanwhile, an impeller 27a is also arranged at the bottom of the dynamic shearing part 26a, and the impeller 27a can improve the circulation rate of the pulp flow.

In this embodiment, the extrusion head carries out first coarse grinding with moving grinding tooth cooperation to the material, the bold material is extruded and is smashed, the material after crushing enters into the grinding district between moving grinding tooth and the quiet grinding tooth, carry out the coarse grinding of second way and grind, after the coarse grinding of second way, the bottom of the mixture driven grinding portion of material and thick liquid flows out, enter into the shearing district of inner circle tooth and quiet shearing tooth and begin to carry out first fine crushing, meanwhile, the material that flows out from the inner circle tooth still can receive the second way fine shearing of quiet shearing tooth and outer circle tooth and smash. After the four steps of crushing, the mixture of the material and the serous fluid can just enter from the inlet of the circulating pipeline arranged on the side wall of the crushing cavity, and because the movable knife is driven by the motor shaft, the subsequent serous fluid continuously pushes the serous fluid flow to flow into the backflow cavity from the outlet of the circulating pipeline under the continuous action of centrifugal force, and the circular crushing is continuously carried out. Therefore, the reducing mechanism of this embodiment is higher to the crushing efficiency of material, and the thick liquid drink taste that makes is exquisite, need not filter the dregs of beans completely. It should be noted that, in this embodiment, two coarse pulverization and two fine pulverization are provided, so that the pulverization efficiency is higher, and the material is pulverized more finely, and for this embodiment, the coarse pulverization and the fine pulverization may be both provided together, or the coarse pulverization and the like are not provided.

The food processor of the invention can be of a structure with a motor arranged at the bottom or at the top. Moreover, the novel food processor can be a soybean milk machine or other food processors without heating function. It will be appreciated by those skilled in the art that the present invention includes, but is not limited to, those illustrated in the accompanying drawings and described in the foregoing detailed description. Any modification which does not depart from the functional and structural principles of the present invention is intended to be included within the scope of the claims.

The food processor of the invention can be of a structure with a motor arranged at the bottom or at the top. Moreover, the food processor of the invention can be a soybean milk machine, and can also be other food processors without heating function. It will be appreciated by those skilled in the art that the present invention includes, but is not limited to, those illustrated in the accompanying drawings and described in the foregoing detailed description. Any modification which does not depart from the functional and structural principles of the present invention is intended to be included within the scope of the claims.

Claims

1. A food processor comprising a container, characterized in that: the container comprises a crushing cavity positioned at the bottom of the container, a backflow cavity arranged above the crushing cavity and a flow gathering port used for communicating the crushing cavity with the backflow cavity, a crushing blade is arranged in the crushing cavity, the capacity of the crushing cavity is 22-380 mL, a water level identification line is arranged on the side wall of the backflow cavity, a circulating pipeline for communicating the crushing cavity with the backflow cavity is arranged on the outer side of the container, the inlet of the circulating pipeline is positioned in the crushing cavity, the outlet of the circulating pipeline is positioned in the backflow cavity, and the outlet of the circulating pipeline is not higher than the water level identification line;

the vertical spraying angle formed by the slurry sprayed out of the outlet of the circulating pipeline and the horizontal plane is theta, wherein theta is more than or equal to 0 and less than or equal to 60 degrees;

or the outlet of the circulating pipeline is arranged on the side wall of the return cavity, when the vertical projection is on the horizontal plane, the connecting line from the center of the outlet to the center of the return cavity is L1, when in circulating pulping, the pulp sprayed out of the outlet is in an inclined spraying state with L1, and the horizontal spraying angle formed by the sprayed pulp and L1 is beta, wherein the beta is more than or equal to 0 and less than or equal to 60 degrees.

2. The food processor of claim 1, wherein: the vertical height from the flow gathering port to the water level marking line is H1, the vertical height from the top end of the outlet of the circulating pipeline to the water level marking line is H, and H/H1 is more than or equal to 0.3 and less than or equal to 0.8.

3. The food processor of claim 2, wherein: H/H1 is 0.5-0.75.

4. The food processor of claim 1, wherein: the outlet of the circulating pipeline is arranged on the side wall of the backflow cavity, the vertical height from the top end of the outlet to the water level identification line is H, and H is larger than or equal to 10mm and smaller than or equal to 100 mm.

5. The food processor of claim 1, wherein: when the slurry discharged from the outlet of the circulation line is discharged in an inclined upward direction from the horizontal plane, H is at least more than 10 mm.

6. The food processor of claim 1, wherein: when the slurry discharged from the outlet of the circulation line is discharged in an inclined downward state from the horizontal plane, H is at least less than 100 mm.

7. A food processor as claimed in any one of claims 1 to 6, wherein: the backflow cavity is provided with an inclined section inclined relative to a vertical plane, and an outlet of the circulating pipeline is arranged on the inclined section.

8. A food processor as claimed in any one of claims 1 to 6, wherein: the inlet of the circulating pipeline is arranged on the side wall of the crushing cavity, the inlet of the circulating pipeline comprises an inlet upper edge and an inlet lower edge, and the crushing blade is positioned in a vertical area of a horizontal plane corresponding to the inlet upper edge and the inlet lower edge;

9. A food processor as claimed in any one of claims 1 to 6, wherein: the area of the opening of the flow gathering port is smaller than that of the opening of any horizontal section on the backflow cavity below the outlet of the circulating pipeline.