CN210697393U - Material feeder for kitchen equipment - Google Patents

Material feeder for kitchen equipment Download PDF

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Publication number
CN210697393U
CN210697393U CN201921063108.XU CN201921063108U CN210697393U CN 210697393 U CN210697393 U CN 210697393U CN 201921063108 U CN201921063108 U CN 201921063108U CN 210697393 U CN210697393 U CN 210697393U
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China
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gas
liquid
solid
cavity
separator
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CN201921063108.XU
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Chinese (zh)
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姚晓宾
李东星
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Zhuhai Unicook Technology Co Ltd
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Zhuhai Unicook Technology Co Ltd
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Abstract

The utility model provides a feeder for kitchen equipment, include: a housing; the storage piece is provided with a storage cavity for storing materials; the separation device can store materials and separate gas in the materials introduced into the separation device; and the power source is connected with the separating device and/or the material storage member and provides power for the movement of the material. The utility model provides the poor problem of material precision is thrown to the feeder among the prior art of having improved.

Description

Material feeder for kitchen equipment
Technical Field
The utility model relates to a kitchen utensils and appliances technical field particularly, relates to a feeder for kitchen equipment.
Background
In the prior art, various seasonings still need to be added manually when a commercial stove cooks, which is tedious. Some commercial kitchen that has the unloading function has set up near-end feeder usually and has been used for buffer memory condiment, and when condiment blows feeder from batching host computer malleation, no matter condiment is solid or liquid, all is mingled with easily and brings into a large amount of gas, when throwing the material, receives the gaseous influence of mingling with and leads to throwing the material inaccurate for the throw material volume of liquid condiment is difficult to accurate control, influences and throws the material precision.
SUMMERY OF THE UTILITY MODEL
A primary object of the present invention is to provide a feeding device for kitchen equipment to improve the problem of poor feeding accuracy of feeding devices in the prior art.
In order to achieve the above object, the utility model provides a feeder for kitchen equipment, include: a housing; the storage piece is provided with a storage cavity for storing materials; the separation device can store materials and separate gas in the materials introduced into the separation device; and the power source is connected with the separating device and/or the material storage member and provides power for the movement of the material.
Further, the separation device comprises: the gas-solid separator is used for storing the solid materials and separating gas in the introduced solid materials; and the gas-liquid separator is used for storing the liquid material and separating gas in the introduced liquid material.
Further, the gas-solid separator includes: the gas-solid separation device comprises a gas-solid shell, a gas-solid separation device and a gas-solid separation device, wherein the gas-solid shell is provided with a gas-solid separation cavity which is provided with a gas-solid feed inlet, a gas-solid discharge outlet and a gas-solid suction inlet; the filtering mechanism is arranged in the gas-solid separation cavity and divides the gas-solid separation cavity into a first cavity for containing materials and a second cavity for extracting gas, the gas-solid feeding hole and the gas-solid discharging hole are located at the first cavity, the gas-solid suction port is located at the second cavity, and the filtering mechanism blocks solid materials from entering the second cavity.
Further, the filter mechanism includes: the mechanism shell is connected with the gas-solid shell; a first filter structure; the second filtration, first filtration and second filtration all set up in the mechanism shell, and first filtration compares the second filtration and is close to first cavity, and the side of first filtration and second filtration has the filtration pore, and the filterable material size of first filtration is greater than the filterable material size of second filtration.
Furthermore, the end face of the first filter structure and/or the second filter structure is a sealed end; or the end face of the first filtering structure and/or the second filtering structure is a non-sealing end, and the size of the material filtered by the end face is smaller than that of the material filtered by the side face.
Further, the end of the first filtering structure, which is far away from the second filtering structure, is a protruding end, at least one part of the protruding end extends into the first cavity, the mechanism shell is provided with a protruding part, at least one part of the protruding part extends into the first cavity, the length of the protruding part extending into the first cavity is greater than the length of the protruding part extending into the first cavity, and the protruding end is accommodated in the protruding part.
Further, the gas-solid separator further includes a cleaning mechanism, the cleaning mechanism including: the cleaning pipeline is detachably arranged at the gas-solid feeding port; the heating element is arranged on the outer side of the gas-solid shell.
Further, the gas-liquid separator includes: the gas-liquid separation device comprises a gas-liquid shell, a gas-liquid separation device and a gas-liquid separation device, wherein the gas-liquid shell is provided with a gas-liquid separation cavity for accommodating materials, and the gas-liquid separation cavity is provided with a gas-liquid feeding hole, a gas-liquid discharging hole and a gas-liquid air suction hole; the gas-liquid suction pipe is communicated with the gas-liquid suction port, at least one part of the gas-liquid suction pipe extends into the gas-liquid separation cavity, and the gas-liquid suction pipe extends into the opening end of the gas-liquid separation cavity and is provided with a stop surface for stopping liquid materials; and the vortex elimination piece is arranged in the gas-liquid separation cavity, and the surface of the vortex elimination piece faces the opening end.
Further, the inner wall surface of the opening end is a stopping surface, the stopping surface is obliquely arranged along the direction of sucking gas by the gas-liquid suction pipe, and the stopping surface is obliquely arranged towards the direction close to the center of the gas-liquid suction pipe.
Further, the end part of the opening end is provided with a flow guide structure, and liquid on the stop surface is gathered to flow down in a flow mode through the flow guide structure.
Furthermore, the vortex elimination piece comprises a vortex elimination part, the vortex elimination part is opposite to the gas-liquid suction pipe, and at least one part of the vortex elimination part protrudes towards the direction close to the gas-liquid suction pipe
Further, the gas-liquid separator also comprises a vortex-preventing piece, the vortex-preventing piece is arranged in the gas-liquid separation cavity and divides the cavity part of the gas-liquid separation cavity close to the gas-liquid discharge hole into a plurality of discharge areas, and each discharge area is communicated with the gas-liquid discharge hole.
Further, the magazine includes: the storage shell is provided with a storage cavity; the diffusion structure is used for detecting the material quantity, the diffusion structure is connected with the material storage shell, at least one part of the diffusion structure extends into the material storage cavity, the diffusion structure detects the material quantity in the material storage cavity, a material supplementing signal is sent when the material quantity is lower than a low preset value, and an overflow signal is sent when the material quantity is higher than a high preset value.
Further, the bottom end of the diffusion structure is close to the bottom surface of the storage cavity, or the bottom end of the diffusion structure is in contact with the bottom surface of the storage cavity.
Further, the storage cavity is provided with an overflow port for the outflow of materials.
Use the technical scheme of the utility model, through setting up storage spare and separator, wherein the storage spare is used for storing some materials that the measurement need not carry out gas separation, for example edible oil, sesame oil etc., separator is used for storing the material that needs carry out gas separation, and can separate out the gas separation who is mingled with in the material, when the material is thrown to needs, let in the separator with the material, separator separates out the gas separation in with the material, the material after the separation can throw the material, because no longer be mingled with impurity such as gas in the material, therefore can guarantee to throw the accuracy of material, realize that the feeder accuracy throws the material. The different storage modes are set according to the different types of the materials, the universality of the feeder is improved, meanwhile, the separating device avoids the influence of gas mixed in the materials on the feeding precision, the feeding precision is guaranteed, the waste of the materials is reduced, and the liquid materials and the solid materials are used, so that the application range is improved.
Drawings
The accompanying drawings, which form a part of the present application, are included to provide a further understanding of the invention, and are incorporated in and constitute a part of this specification, illustrate embodiments of the invention and together with the description serve to explain the invention and not to limit the invention. In the drawings:
fig. 1 shows a schematic structural view of a feeder of the present invention;
FIG. 2 shows a front view of FIG. 1;
FIG. 3 shows a top view of FIG. 1;
FIG. 4 shows a rear view of FIG. 1;
FIG. 5 shows a schematic diagram of the gas-solid separator of the feeder of FIG. 1;
FIG. 6 shows an exploded view of the gas-solid separator of FIG. 5;
FIG. 7 shows a side cross-sectional view of the gas-solid separator of FIG. 5;
FIG. 8 shows an exploded view of the filter mechanism of FIG. 6;
FIG. 9 shows a schematic diagram of the gas-liquid separator of the feeder of FIG. 1;
FIG. 10 shows an exploded view of the gas-liquid separator of FIG. 9;
FIG. 11 shows a side cross-sectional view of the gas-liquid separator of FIG. 9;
FIG. 12 shows a schematic view of the suction duct of the gas-liquid separator of FIG. 10;
FIG. 13 shows a schematic view of the structure of the vortex breaker of the gas-liquid separator of FIG. 10;
FIG. 14 shows a schematic view of the vortex breaker of the gas-liquid separator of FIG. 10;
figure 15 shows a schematic view of the magazine portion of the feeder of figure 1; and
fig. 16 shows a cross-sectional view of the magazine of fig. 15.
Wherein the figures include the following reference numerals:
100. a housing; 200. a material storage member; 210. a material storage shell; 211. a material storage cavity; 2111. a material storage feeding hole; 2112. a material storing and discharging port; 2113. an overflow port; 220. a diffuser structure; 230. a liquid level meter; 240. a flow guide pipe; 300. a gas-solid separator; 310. a gas-solid shell; 311. a gas-solid separation chamber; 3111. a gas-solid feed inlet; 3112. a gas-solid discharge port; 3113. a gas-solid air suction port; 3114. a first cavity; 3115. a second cavity; 3116. a gas-solid gas inlet; 312. a material containing part; 313. an installation part; 314. a covering part; 320. a filtering mechanism; 321. a mechanism housing; 3211. a protruding portion; 322. a first filter structure; 323. a second filter structure; 324. a cover body; 330. a gas-solid pressure relief valve; 340. a mounting structure; 400. a gas-liquid separator; 410. a gas-liquid housing; 411. a gas-liquid separation chamber; 4111. a gas-liquid feed inlet; 4112. a gas-liquid discharge port; 4113. a gas-liquid air suction port; 4114. a gas-liquid exhaust port; 412. a transition section; 420. a gas-liquid suction pipe; 421. a stop surface; 422. a flow guide structure; 430. a vortex breaker; 431. a vortex elimination part; 432. a support portion; 440. a vortex breaker; 450. a gas-liquid pressure relief valve; 500. a flow meter; 610. a negative pressure control switch; 620. a negative pressure regulator; 630. a positive pressure control switch; 640. a positive pressure regulator; 650. an electromagnetic valve; 660. a straight-through ball valve; 710. a gear pump.
Detailed Description
It should be noted that the embodiments and features of the embodiments in the present application may be combined with each other without conflict. The present invention will be described in detail below with reference to the accompanying drawings in conjunction with embodiments.
It is noted that, unless otherwise indicated, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this application belongs.
In the present application, where the contrary is not intended, the use of directional words such as "upper, lower, top and bottom" is generally with respect to the orientation shown in the drawings, or with respect to the component itself in the vertical, perpendicular or gravitational direction; likewise, for ease of understanding and description, "inner and outer" refer to the inner and outer relative to the profile of the components themselves, but the above directional words are not intended to limit the invention.
In order to improve the poor problem of material precision of feeding device among the prior art, the utility model provides a feeding device for kitchen equipment.
A feeder for a kitchen appliance as shown in fig. 1 to 4, comprising a housing 100, at least one storage member 200, a separating device and a power source, the storage member 200 having a storage chamber 211 for storing material; the separation device can store materials and separate gas in the materials introduced into the separation device; the power source is connected to the separating apparatus and/or the storage member 200 and provides power for movement of the material.
This embodiment is through setting up storage piece 200 and separator, wherein storage piece 200 is used for storing some materials that the measurement need not carry out gas separation, for example edible oil, sesame oil etc., separator is used for storing the material that needs carry out gas separation, and can separate out the gas separation that mix with in the material, when the material is thrown to needs, let in separator with the material, separator separates out the gas separation in with the material, the material after the separation can throw the material, because no longer be mixed with impurity such as gas in the material, therefore can guarantee the accuracy of throwing the material, realize that the feeder accurately throws the material. The different storage modes are set according to the different types of the materials, the universality of the feeder is improved, meanwhile, the separating device avoids the influence of gas mixed in the materials on the feeding precision, the feeding precision is guaranteed, the waste of the materials is reduced, and the liquid materials and the solid materials are used, so that the application range is improved.
In the embodiment, the separation device comprises a gas-solid separator 300 and a gas-liquid separator 400, wherein the gas-solid separator 300 stores solid materials and separates gas in the solid materials introduced into the gas-solid separator 300; the gas-liquid separator 400 is used to store the liquid material and separate the gas from the liquid material introduced therein. Thus, the gas-solid separator 300 and the gas-liquid separator 400 enable solid materials and liquid materials to be stored, separated by gas, fed and the like independently, the feeding device can be applied to the solid materials and the liquid materials, mutual interference between the solid materials and the liquid materials is avoided, and feeding accuracy is guaranteed.
The gas-solid separator 300 shown in fig. 5 to 8 comprises a gas-solid housing 310 and a filtering mechanism 320, wherein the gas-solid housing 310 has a gas-solid separation cavity 311, and the gas-solid separation cavity 311 has a gas-solid inlet 3111, a gas-solid outlet 3112 and a gas-solid suction inlet 3113; the filtering mechanism 320 is disposed in the gas-solid separation cavity 311, and divides the gas-solid separation cavity 311 into a first cavity 3114 for accommodating solid materials and a second cavity 3115 for extracting gas, the gas-solid feed port 3111 and the gas-solid discharge port 3112 are disposed at the first cavity 3114, the gas-solid suction port 3113 is disposed at the second cavity 3115, and the filtering mechanism 320 prevents the solid materials from entering the second cavity 3115.
In the embodiment, the filtering mechanism 320 is provided, the filtering mechanism 320 divides the gas-solid separation cavity 311 into a first cavity 3114 and a second cavity 3115, wherein, the first cavity 3114 can be filled with solid materials through the gas-solid feed inlet 3111, the feeding is realized through a gas-solid discharge port 3112, the second cavity 3115 can suck gas through a gas-solid suction port 3113, thereby generating negative pressure in the gas-solid separation cavity 311, the negative pressure drives the solid material to move from the first cavity 3114 to the second cavity 3115, during the movement, the solid material is filtered by the filtering mechanism 320 to remain in the first cavity 3114, and gas entrained in the solid material can pass through the filter mechanism 320 into the second chamber 3115, and is sucked away by the gas-solid air suction port 3113, thus the gas mixed in the solid material can be separated from the solid material, and the feeding can be realized through the gas-solid discharge port 3112 after the separation is finished. The gas in the solid material is separated and discharged by the arrangement mode, the condition that the feeding materials are inaccurate due to the interference of mixed gas in the feeding process of the feeding machine is avoided, the feeding precision is improved, and the cooking effect is ensured. Meanwhile, the gas-solid separator 300 can play a role in buffering solid materials, so that the solid materials are prevented from being conveyed to the gas-solid separation cavity 311 all the time, the gas is too much, and even the gas-solid separation cavity 311 is cracked, so that potential safety hazards are generated. The solid material is equivalent to temporary buffer memory in gas-solid separator 300, waits for to throw the material instruction, and at this in-process, the proportioning machine can be for other separators transported substance material, separates the procedure, and a plurality of gas-solid separators 300 work simultaneously like this makes proportioning machine work efficiency improve, and the efficiency of culinary art execution is also high. In addition, the negative pressure feeding is adopted, and the quantitative function is realized, so that the weight of the solid materials required in the menu is converted into a pressure value corresponding to the negative pressure, then the corresponding pressure value is output, and the same amount of solid materials are sucked into the gas-solid separator 300.
As shown in FIG. 8, the filter mechanism 320 comprises a mechanism housing 321, a first filter structure 322 and a second filter structure 323, wherein the mechanism housing 321 is connected with the gas-solid housing 310; first filtration 322 and second filtration 323 all set up in mechanism shell 321, and first filtration 322 compares second filtration 323 and is close to first cavity 3114, and the material size that first filtration 322 filters is greater than the material size that second filtration 323 filters.
Specifically, solid material passes through first filtration 322 and second filtration 323 in proper order, first filtration 322 plays prefilter's effect, its mainly used filters the great solid material of granule, second filtration 323 plays the effect of strengthening the filtration, its mainly used filters the less solid material of granule, most large granule solid can be strained in first filtration 322's filtration, avoid being attached to second filtration 323 by the solid material that absorbs and influence the filter effect of second filtration 323, cause second filtration 323 to block up even, influence the gaseous exhaust condition, and simultaneously, can also play gas buffering effect, avoid the air current of second filtration 323 to lead to the fact the wind to block up suddenly, guarantee the filter effect of filter mechanism 320. The solid materials are sequentially filtered according to the size of the solid materials by the arrangement mode. Thereby the graded filtration to solid material has been realized, has guaranteed the filter effect, has improved filterable efficiency. And the setting up of mechanism shell 321 can make things convenient for the installation of filter mechanism 320 on the one hand, realizes integrating of filter mechanism 320, and on the other hand can play certain guard action to first filtration 322 and second filtration 323, prevents that first filtration 322 and second filtration 323 from influencing the filter effect because the exogenic action leads to unexpected damage, guarantees the reliability of filter mechanism 320. Preferably, the mechanism housing 321 has a reinforced rib structure to make the filter mechanism 320 more robust. In this embodiment, the first filter structure 322 and the second filter structure 323 are provided with filter holes, and accordingly, the size of the filter holes of the first filter structure 322 is larger than that of the filter holes of the second filter structure 323, but the above-mentioned effects may also be achieved by other manners.
Preferably, the first filter structure 322 is a screen and the second filter structure 323 is a filter element. The meshes of the filter screen are larger, and the filter holes of the filter element are smaller, so that the graded filtration is realized. Of course, the first filter structure 322 and the second filter structure 323 may be replaced with other filter elements as needed.
Further preferably, the outer surface of the filter element of the second filter structure 323 is a circumference surrounded by one pleat and one pleat, so that the contact area with the solid material is increased, the second filter structure 323 can filter more solid materials, the filter efficiency is higher, and the filter effect is better.
It should be noted that the present embodiment is described by taking two-stage filtering as an example, that is, two-stage filtering implemented by the first filtering structure 322 and the second filtering structure 323. In addition to this arrangement, a filter structure may be added as needed, for example, a third filter structure, a fourth filter structure, etc., and the sizes between the filter holes of the filter structures are preferably sequentially decreased in a direction from the first cavity 3114 to the second cavity 3115, so as to implement the step filtration.
In this embodiment, the side surfaces of the first filter structure 322 and the second filter structure 323 are respectively provided with filter holes, and the gas flows from the outer side surface to the inner side surface through the filter holes, and then flows from the inner side surface to the second cavity 3115, accordingly, the outer side surfaces of the first filter structure 322 and the second filter structure 323 and the inner wall surface of the mechanism housing 321 are arranged at intervals, and form a channel for the gas to pass through, so as to provide a space for the gas to flow and part of the solid material to move. Like this, because the filtration pore sets up in the side, therefore gaseous can only be by the side through first filtration 322 and second filtration 323, make the terminal surface of first filtration 322 and second filtration 323 can play certain effect of blockking to the solid material, reduce the quantity of the solid material of inhaling on the filtration 320, also further reduced the filtration volume of filtration 320, avoid the unexpected possibility through filtration 320 of solid material, avoid too much solid material to block up first filtration 322 and second filtration 323 simultaneously, guarantee the filter effect.
Preferably, the end faces of the first filter structure 322 and the second filter structure 323 are sealed ends, that is, neither gas nor solid material can pass through the end faces of the first filter structure 322 and the second filter structure 323, so as to improve the blocking effect of the end faces on the solid material, and ensure that most of the solid material is filtered while the exhaust gas is not blocked. Certainly also can set to non-sealed end at first filtration 322 and second filtration 323's terminal surface, for example, seted up the filtration pore on the terminal surface, it needs to be noted that, the filtration pore size of terminal surface needs to be less than the filtration pore size of side, make the filterable material size of terminal surface be less than the filterable material size of side, just so can play the effect of blockking to the solid material, otherwise the solid material can directly pass through the great filtration pore of size on the terminal surface, and can not pass through the less filtration pore of size on the side, not only play the effect of blockking the solid material, can influence the filter effect on the contrary. Other structures may be used instead of the filter holes. In this embodiment, the first filtering structure 322 and the second filtering structure 323 both adopt the above-mentioned arrangement manner in which the filtering holes are formed on the side surfaces, and of course, the first filtering structure 322 or the second filtering structure 323 may also adopt the arrangement manner, that is, the first filtering structure 322 is set as a common filtering net, the second filtering structure 323 adopts the above-mentioned arrangement manner in which the side surfaces are filtered, or the second filtering structure 323 is set as a common filtering net, and the first filtering structure 322 adopts the above-mentioned arrangement manner in which the side surfaces are filtered. Furthermore, the first filter structure 322 may have other filter element configurations. The filter screen can be an injection molding piece with a closed middle part and a filter screen structure at the periphery to form a structure similar to a poached egg, and can also be filter screens in other forms.
The first filtering structure 322 and the second filtering structure 323 of the embodiment are in a column shape, the circumferential surfaces of the first filtering structure 322 and the second filtering structure 323 are side surfaces, and filtering holes are uniformly distributed on the entire circumferential surface to improve the filtering efficiency.
In this embodiment, since the second filter structure 323 needs a larger contact area to exhaust more gas, the diameter of the first filter structure 322 is smaller than that of the second filter structure 323, one end of the first filter structure 322, which is away from the second filter structure 323, is an extended end, at least a portion of the extended end extends into the first cavity 3114, a protruding portion 3211 is disposed on an end surface of the mechanism housing 321, which is away from the second cavity 3115, at least a portion of the protruding portion 3211 extends into the first cavity 3114, the extended end is accommodated in the protruding portion 3211, and the length of the protruding portion 3211 extending into the first cavity 3114 is greater than the length of the extended end extending into the first cavity 3114. The arrangement of the extending end and the extending portion 3211 enables the first filtering structure 322 to be deeper into the first cavity 3114, solid materials in ascending airflow can be blocked to a great extent during air suction, gas mixed in the solid materials can be separated more effectively, the extending portion 3211 on the mechanism shell 321 can play a certain protection role on the extending end, a filtering hole is formed in the side wall of the extending end, a gap is formed between the extending portion 3211 and the extending end, the gas and the sucked partial solid materials enter the gap through the end portion of the extending portion 3211, so that the gas can only pass through the side face of the first filtering structure 322, and the blocking effect on large-particle solid materials is improved.
Preferably, the second filter structure 323 has filter holes smaller than the smallest diameter of the solid material, and the second filter structure 323 has an overall size larger than half the diameter of the gas-solid separator 300.
Optionally, the protruding portion 3211 may be configured to be a cylinder with a wide top and a narrow bottom, that is, the opening at the bottom end of the protruding portion 3211 is narrow, and the opening at the butt joint of the top end and the second filtering structure 323 is wide, and this configuration enables the protruding portion 3211 to block more solid materials from entering the filtering mechanism 320, so as to improve the blocking effect on large-particle solid materials. Correspondingly, the second filtering structure 323 can also be set to be in a shape with a wide bottom and a narrow top, and most of large-particle solid materials are filtered out by the first filtering structure 322, so the second filtering structure 323 is set to be in a form with a wide bottom and a narrow top and does not affect the filtering effect, the inclined side wall can block more solid materials, meanwhile, the setting mode is also beneficial to gas passing through the second filtering structure 323, the second filtering structure 323 can enter gas as much as possible, and the blocking effect of the inclined side wall is matched, so that as much gas as possible is pumped away and solid materials are left.
The extension portion 3211 of the present embodiment is detachably disposed on the mechanism housing 321, and more specifically, the extension portion 3211 is mounted on the mechanism housing 321 through a threaded structure, and when the first filter structure 322 needs to be replaced, the extension portion 3211 is screwed down to replace the first filter structure 322, so as to facilitate assembly and disassembly. And sealing members such as sealing rings may be disposed at the installation position of the protruding portion 3211 to ensure that gas and fine solid materials are not filtered from the gap beyond the first filtering structure 322.
The mechanism housing 321 of the filter mechanism 320 of the present embodiment is an open side at an end far from the protruding portion 3211, the second filter structure 323 is installed into the mechanism housing 321 or removed from the mechanism housing 321 through the open side, and the filter mechanism 320 further includes a cover 324, and the cover 324 is detachably disposed at the open side of the mechanism housing 321, so as to shield the open side, so that the second filter structure 323 can be stably disposed in the mechanism housing 321. When the filter mechanism 320 needs to be replaced, the cover 324 is opened, and the filter mechanism 320 can be taken out integrally, so that the replacement and the maintenance are convenient. The cover 324 is preferably threadably connected to the mechanism housing 321. A through hole for gas to pass through is formed in the cover 324, and the size of the through hole is smaller than the outer diameter of the second filter structure 323 and approximately equal to the inner diameter of the second filter structure 323, so that the gas passing through the side surface of the second filter structure 323 enters the second cavity 3115 through the inner cavity of the second filter structure 323 and the through hole in the cover 324. In addition, a handle can be arranged on the cover 324, and the filter mechanism 320 can be integrally moved by the handle, so that the filter mechanism is convenient to install and take out. A sealing member such as a sealing ring may be disposed between the cover 324 and the mechanism housing 321 to ensure a sealing effect.
As shown in fig. 5 to 7, the gas-solid separator 300 is vertically arranged, and the first cavity 3114 is located below the second cavity 3115, so that when solid materials are added into the first cavity 3114 through the gas-solid feed inlet 3111, the solid materials are kept in the first cavity 3114 under the action of gravity, and the solid materials can move upwards only when negative pressure is introduced, and when negative pressure is not introduced any more, part of the solid materials can automatically fall back to the bottom of the first cavity 3114 under the action of gravity, thereby reducing the solid materials attached to the filtering mechanism 320. In addition, the bottom of first cavity 3114 is hourglass hopper-shaped, and gas-solid discharge gate 3112 is located the bottom of first cavity 3114 to solid material realizes throwing the material in the automatic whereabouts under the action of gravity when gas-solid discharge gate 3112 is opened, guarantees simultaneously that solid material can go out under the whole, avoids solid material to remain. Of course, the first cavity 3114 may be formed in a cylindrical shape having the same upper and lower diameters, or in other shapes.
Preferably, the gas-solid feed port 3111 is located on the top side of the first cavity 3114, and the axis of the gas-solid feed port 3111 is parallel to the tangent of the gas-solid housing 310 at the gas-solid feed port 3111, that is, the gas-solid feed port 3111 introduces solid material into the first cavity 3114 along the tangent of the circumference of the gas-solid housing 310, so that the solid material is added into the first cavity 3114 from the top of the first cavity 3114, enters the first cavity 3114 along the tangent, and spirally descends along the inner wall, and is separated by being thrown to the inner wall surface by the rotational motion caused by the tangential introduction of air flow, so as to disperse the solid material with larger inertial centrifugal force, and lose inertia after the solid material hits the inner wall, and fall freely, at this time, part of gas is mixed in the solid material, and the gas mixed in the solid material can be extracted by inputting negative pressure through the gas-solid suction port 3113, the purpose of gas-solid separation is better realized.
Optionally, the inner wall of the gas-solid separation chamber 311 is made of a non-stick coating, an organosilicon material, or the like, so as to further reduce the residue of solid materials on the inner wall.
In this embodiment, the gas-solid separation chamber 311 further has a gas-solid inlet 3116, and the gas-solid inlet 3116 is located at the second chamber 3115. After the gas-solid suction port 3113 inputs negative pressure to extract gas in the solid material, positive pressure is input into the gas-solid separation cavity 311 through the gas-solid inlet 3116, and the gas with positive pressure makes the solid material attached to the filtering mechanism 320 and deposited in the filtering mechanism 320 be blown into the first cavity 3114, so that the solid material is prevented from being deposited on the filtering mechanism 320, the utilization rate of the solid material is improved, and almost all the solid material can be used for feeding. The gas-solid inlet 3116 and the gas-solid inlet 3113 can be interchanged, or only one common inlet is provided, and the functions of gas suction and gas inlet are realized by controlling inlet negative pressure or inlet positive pressure through a valve.
Optionally, the gas-solid separator 300 further comprises a gas-solid pressure relief valve 330, the gas-solid pressure relief valve 330 is communicated with the gas-solid separation cavity 311, when positive pressure is introduced into the gas-solid separation cavity 311 through the gas-solid gas inlet 3116 until the pressure reaches a preset value, the gas-solid pressure relief valve 330 is automatically jacked open by the pressure, gas in the gas-solid separation cavity 311 is directly discharged, and danger caused by overlarge pressure in the gas-solid separation cavity 311 is avoided. The specific numerical value is set correspondingly according to the actual situation.
Preferably, gas-solid relief valve 330 and second cavity 3115 intercommunication, like this, gas-solid relief valve 330 is when being backed up, and only the gas of second cavity 3115 can be discharged through gas-solid relief valve 330, and the solid material in first cavity 3114 can not directly be discharged from gas-solid relief valve 330, avoids the solid material in first cavity 3114 to discharge from gas-solid relief valve 330 and cause the problem of solid material loss.
In this embodiment, the gas-solid housing 310 includes a material containing portion 312, a mounting portion 313 and a covering portion 314, the material containing portion 312, the mounting portion 313 and the covering portion 314 are sequentially connected from bottom to top, the material containing portion 312 has a first cavity 3114, and the filtering mechanism 320 is mounted on the mounting portion 313; the cover portion 314 is a cover, connected to the mounting portion 313, and forms a second cavity 3115 together with the mounting portion 313. Sealing elements such as sealing rings can be additionally arranged between the covering part 314 and the mounting part 313 and between the mounting part 313 and the material containing part 312 so as to ensure the whole sealing performance of the gas-solid separation cavity 311 and ensure the effect of pumping gas. Through adopting the components of a whole that can function independently setting up with gas-solid casing 310, be convenient for install the inside parts of gas-solid casing 310 such as filter mechanism 320 in gas-solid casing 310, establish portion 314 with the lid and open and can wholly take out filter mechanism 320 and change and maintain to greatly reduced change and the required time of maintenance and vigor. The material containing part 312 and the mounting part 313 of the present embodiment are both cylindrical, and the material containing part 312, the mounting part 313 and the cover arranging part 314 are all detachably connected, preferably in threaded connection, so that the gas-solid separator 300 is integrally connected in a threaded manner, and fasteners such as screws are not required to be additionally arranged, and the gas-solid separator is convenient and reliable to assemble and disassemble. Of course, instead of using a screw connection, a screw or bolt connection may be used. Of course, in addition to the method of connecting the components by screw threads, other methods such as bolts and screws may be used to connect some of the components.
It should be noted that, although the material containing portion 312 and the mounting portion 313 in the gas-solid separator 300 shown in the drawings of the present embodiment are connected by bolts, a screw connection is preferred.
Optionally, the gas-solid separator 300 further comprises a mounting structure 340 for connection with an external device, the mounting structure 340 being connected with the gas-solid housing 310. The two opposite sides of the gas-solid casing 310 are respectively provided with a plate-shaped member as a mounting structure 340, the plate-shaped member is provided with a connecting hole connected with an external device such as a stand, and the gas-solid separator 300 can be mounted on the stand through a bolt. The mounting structure 340 is not limited to the plate-like member, and may be other members, and the mounting position is not limited to the two opposite sides of the gas-solid housing 310, and may be provided with only one or more members, and may be provided in other arrangement, as long as the gas-solid separator 300 can be mounted and fixed.
In this embodiment, the gas-solid separator 300 further includes a cleaning mechanism, the cleaning mechanism includes a cleaning pipeline and a heating element for conveying cleaning liquid, the cleaning pipeline is detachably installed at the gas-solid feed port 3111, when the interior of the gas-solid separator 300 needs to be cleaned, the cleaning pipeline is butted at the gas-solid feed port 3111, cleaning liquid such as water is introduced for cleaning, and the cleaning liquid can be discharged from the gas-solid discharge port 3112 at the bottom; the heating member sets up in the gas-solid casing 310 outside, and after the washing is accomplished, heats gas-solid separation chamber 311 through starting the heating member, promotes remaining liquid evaporation in the gas-solid separation chamber 311, is favorable to the pipeline cleaning, can increase the precision that solid material was thrown material to reduce solid material collision friction and produce static.
Preferably, the heating member surrounds the outside of the first cavity 3114, so as to heat the whole outside of the first cavity 3114, thereby ensuring the heating effect on the first cavity 3114 and avoiding the liquid residue. Of course, the heating member may heat only a portion of the outside of the first cavity 3114. The heating member preferred is heating silica gel gasket, and direct adhesion is on the lateral wall of first cavity 3114, just control when needing the heating and start, simple structure, low cost, it is convenient to maintain.
The gas-solid separator 300 is used as follows:
when gas-solid separation is needed, a gas-solid feed port 3111 of the gas-solid separator 300 and a gas-solid suction port 3113 of the gas-solid separator 300 are opened, negative pressure gas is introduced into the gas-solid separation cavity 311 through the gas-solid suction port 3113, the solid materials are sucked into the gas-solid separation cavity 311 from the gas-solid feed port 3111 through the negative pressure gas, and when the solid materials enter the gas-solid separation cavity 311, the gas in the solid materials is separated and sucked away by the negative pressure gas, so that the gas-solid separation is realized; after gas separation is completed, the gas-solid feeding port 3111 and the gas-solid suction port 3113 are closed, the gas-solid discharging port 3112 of the gas-solid separator 300 and the gas-solid gas inlet 3116 of the gas-solid separator 300 are opened, positive pressure gas is introduced into the gas-solid separation cavity 311 through the gas-solid gas inlet 3116, the positive pressure gas can blow down materials remained on the filtering mechanism 320, on the other hand, the solid materials can be fed from the gas-solid discharging port 3112, and the solid materials are prevented from being accumulated on the gas-solid discharging port 3112 to affect feeding. The duration of the positive pressure and the negative pressure can be correspondingly set according to the quantity and other parameters of the materials.
When needing to wash, will wash pipeline butt joint gas-solid feed inlet 3111 department, let in water and wash, wash accomplish the back, water from the gas-solid discharge gate 3112 of bottom discharge can, then restart the heating member and heat gas-solid separation chamber 311, with remaining liquid evaporation can.
When the parts need to be removed and replaced, the cover part 314 at the top is screwed off, the filter mechanism 320 is integrally lifted up and taken out through the handle on the cover body 324, then the cover body 324 is screwed off, the second filter structure 323 can be taken out and replaced, the extension part 3211 is screwed off, the first filter structure 322 can be taken out and replaced, and the gas-solid separator 300 does not need to be removed.
The gas-liquid separator 400 shown in fig. 9 to 14 includes a gas-liquid housing 410, a gas-liquid suction pipe 420 and a vortex breaker 430, wherein the gas-liquid housing 410 has a gas-liquid separation chamber 411 for accommodating liquid materials, and the gas-liquid separation chamber 411 has a gas-liquid inlet 4111, a gas-liquid outlet 4112 and a gas-liquid suction port 4113; the gas-liquid suction pipe 420 is communicated with the gas-liquid suction port 4113, at least one part of the gas-liquid suction pipe 420 extends into the gas-liquid separation chamber 411, and the open end of the gas-liquid suction pipe 420 extending into the gas-liquid separation chamber 411 is provided with a stop surface 421 for stopping liquid materials; the vortex breaker 430 is disposed in the gas-liquid separation chamber 411 with a surface of the vortex breaker 430 facing the open end.
In this embodiment, by providing the gas-liquid suction port 4113 and the gas-liquid suction pipe 420, when liquid material is introduced into the gas-liquid separation chamber 411 from the gas-liquid feed port 4111, negative pressure is input into the gas-liquid separation chamber 411 through the gas-liquid suction port 4113 and the gas-liquid suction pipe 420, the negative pressure sucks gas in the liquid material, and the gas in the liquid material is separated by discharging through the gas-liquid suction pipe 420 and the gas-liquid suction port 4113, in this process, the negative pressure gas will also suck part of liquid into the gas-liquid suction pipe 420, so that the gas-liquid suction pipe 420 extends into the open end of the gas-liquid separation chamber 411, that is, the gas and the sucked liquid enter the end of the gas-liquid suction pipe 420 and is provided with the stop surface 421, so that the sucked liquid will adhere to the stop surface 421 due to inertia and flow back into the gas-liquid separation chamber 411 downward along the stop surface 421, thereby, meanwhile, the vortex elimination piece 430 can reduce the influence of the tail of the central air flow vortex of the gas-liquid suction pipe 420 on the separated liquid in the gas-liquid separation cavity 411, and further prevent the liquid from entering the gas-liquid suction pipe 420 and being taken away along with the air flow. Above-mentioned mode of setting up comes out the gas separation in with liquid material, avoids mixing with the gas in liquid material to throwing the influence of material precision to prevent that liquid from smuggleing secretly entering into gas-liquid breathing pipe 420 along with the condition that the air current was taken away, reduce the waste of liquid material, avoid liquid to produce liquid rotation and influence exhaust speed's problem in gas-liquid discharge gate 4112 department simultaneously. Meanwhile, the gas-liquid separator 400 can play a role in buffering liquid materials, and avoids the situation that materials are conveyed to the gas-liquid separation cavity 411 all the time, so that the gas is too much, and even the gas-liquid separation cavity 411 is cracked, thereby generating potential safety hazards. Liquid material is equivalent to temporary buffer memory in vapour and liquid separator 400 the inside, waits for throw the material instruction, and at this in-process, the proportioning machine can be for other separators transported substance material, separates the procedure, and a plurality of separators simultaneous working make proportioning machine work efficiency high, cooks the efficiency of execution also high. In addition, the negative pressure feeding is adopted, and the quantitative function is realized, so that the weight of the liquid material required in the menu is converted into a pressure value corresponding to the negative pressure, then the corresponding pressure value is output, and the same amount of liquid material is sucked and enters the gas-liquid separator 400.
As shown in fig. 11 and 12, the segment of the gas-liquid suction pipe 420 of the present embodiment extending into the gas-liquid separation chamber 411 is vertically disposed, the open end is the bottom end of the segment, the inner wall surface of the open end is the stopper surface 421, and the stopper surface 421 is obliquely disposed, along the direction of sucking gas by the gas-liquid suction pipe 420, the stopper surface 421 inclines towards the direction close to the center of the gas-liquid suction pipe 420, that is, the stopper surface 421 inclines towards the direction close to the center of the gas-liquid suction pipe 420 from bottom to top, so that the range of gas entering the gas-liquid suction pipe 420 is gradually reduced, thus, when liquid material is entrained in gas, gas can smoothly change the motion trajectory along with the inclination of the stopper surface 421, and the motion trajectory of the liquid material is not easily changed due to inertia effect, and thus the liquid material is stopped by the stopper surface 421 and attached to be accumulated on the stopper surface 421, and can, thereby re-collecting into the separated liquid and reducing the loss of liquid material. If the straight cylinder-shaped gas-liquid suction pipe 420 is arranged, the sucked liquid material directly enters into the gas-liquid suction pipe 420 along the gas-liquid suction pipe 420 to form a short circuit, and the liquid material is lost along with the discharge of gas.
Alternatively, the number of the stop surfaces 421 may be one or more, when there is one stop surface 421, the stop surface 421 may be provided on only one side in the circumferential direction of the gas-liquid suction pipe 420, or the stop surface 421 is provided as an arc surface, the arc surface is provided along the circumferential direction of the opening end, in this embodiment, it is preferable that the stop surface 421 is provided as a circumferential surface, and when there are a plurality of stop surfaces 421, the side edges of the stop surfaces 421 may be sequentially connected, and the stop surfaces are provided along the circumferential direction of the gas-liquid suction pipe 420. The stop surfaces 421 are preferably arranged in the circumferential range of the gas-liquid suction pipe 420, so that liquid materials sucked into the gas-liquid suction pipe 420 from various positions of the opening end can be effectively stopped, and the stop effect is ensured.
Optionally, the shape of the opening end has multiple setting modes according to actual conditions, for example, the opening end is set to be a circular truncated cone or a truncated pyramid, the embodiment is preferably set to be a flared shape, and the opening end can be integrally attractive and elegant while the processing is convenient.
In this embodiment, the end of the open end has a flow guide structure 422, and the liquid on the stop surface 421 is collected into a stream by the flow guide structure 422.
Specifically, the end of the opening end is the bottom surface of the opening end, a toothed flow guide structure 422 is arranged at the bottom surface, liquid materials on the stop surface 421 flow downwards onto the flow guide structure 422 along the stop surface 421, the liquid materials are converged into large liquid drops through the flow guide structure 422 and fall off from the gas-liquid suction pipe 420 to be converged with separated liquid, the arrangement of the flow guide structure 422 can accelerate the process that liquid films on the stop surface 421 are converged to form liquid drops, and the problem of liquid material loss is effectively solved. The diversion structure 422 of the present embodiment is preferably configured to be serrated, and sharp corners of the serrations face downward, so that the liquid film flows to the sharp corners along the serrated slope, which is beneficial to converging the liquid film at the serrated sharp corners to form larger droplets to drop, and accelerates the process of converging the liquid film into droplets. Of course, instead of a sharp corner, an arc-shaped surface or a flat surface may be used.
The diversion structure 422 of this embodiment is provided with the round along the circumference of gas-liquid suction pipe 420, just so can all play the effect of assembling to the liquid film in each position on backstop surface 421, reduces the loss of liquid material. Of course, the arrangement may be performed according to the arrangement position of the stop surface 421. For example, if the stopper surface 421 is provided only on one side of the gas-liquid suction pipe 420, the flow guide structure 422 may be provided only on the bottom surface of the one side.
As shown in fig. 10 and 13, the vortex breaker 430 includes a vortex breaker 431, the vortex breaker 431 faces the gas-liquid intake pipe 420, and at least a portion of the vortex breaker 431 protrudes in a direction close to the gas-liquid intake pipe 420.
Specifically, the vortex elimination part 431 is formed by a plate-shaped member, the vortex elimination part 431 is over against the center of the gas-liquid suction pipe 420, the vortex elimination part 431 can eliminate the influence of the tail part of a central airflow vortex on the separated liquid in the gas-liquid separation cavity 411, if the vortex elimination part 431 is not arranged, airflow vortex can be generated at the position right below the gas-liquid suction pipe 420 under the action of negative pressure of the gas-liquid suction pipe 420, the airflow vortex can extend to the bottom of the gas-liquid separation cavity 411 from top to bottom, disturbance is generated on the separated liquid at the bottom of the gas-liquid separation cavity 411, even the liquid is sucked up under the action of the airflow vortex, and the sucked up liquid material can directly enter the gas-liquid suction pipe 420 and be sucked away to cause loss because the center of the gas-liquid suction pipe 420 is not provided with; after the vortex elimination part 431 is arranged, the vortex elimination part 431 can block the generated airflow vortex from extending downwards, so that the airflow vortex can only extend to the vortex elimination part 431 and cannot influence the separated liquid at the bottom of the gas-liquid separation cavity 411, and the sucked liquid around the central axis of the gas-liquid suction pipe 420 is stopped by the vortex elimination part 431 when moving upwards, so that the part of the liquid cannot be directly sucked away by the gas-liquid suction pipe 420 through the center of the gas-liquid suction pipe 420, and the loss of liquid materials is reduced; the vortex elimination portion 431 has a similar function to the stopper surface 421 and the inner wall surface of the convex portion in the direction close to the gas-liquid suction pipe 420, and the liquid material moving upward is attached to and accumulated on the inner wall surface of the convex portion, flows downward along the inner wall surface, and is condensed into liquid drops to be gathered at the bottom of the gas-liquid separation chamber 411. The arrangement mode eliminates the influence of the tail part of the central air flow vortex of the gas-liquid suction pipe 420 on the separated liquid in the gas-liquid separation cavity 411, and prevents the liquid material from entering the gas-liquid suction pipe 420 and being taken away along with the air flow.
Preferably, the portion of the vortex elimination portion 431 protruding therefrom is tapered such that the inner wall surface of the protruding portion is also inclined, thereby serving the purpose of sufficiently stopping the liquid moving upward, as with the stop surface 421. And the top of the cone is arc-shaped instead of plane, so that airflow vortex can be removed more effectively to achieve the effect of flow guiding. The cone may be a cone or a pyramid, but may also be a truncated cone, a truncated pyramid, or other shapes.
It should be noted that, in consideration of the problem of the processing process, the top of the inner wall surface of the protruding portion of the vortex-reducing portion 431 is formed into a circular arc shape in this embodiment to facilitate the processing, but it is preferable to form the top of the inner wall surface of the protruding portion of the vortex-reducing portion 431 into a pointed shape to improve the converging action of the inner wall surface and accelerate the process of converging the liquid film on the inner wall surface into liquid droplets.
In addition to the above-mentioned arrangement manner of the vortex reducing member 430, the vortex reducing member 430 may be arranged as a planar plate member, and the surface of the planar plate member facing the opening end can also block the airflow vortex, thereby avoiding the influence of the airflow vortex on the separated liquid; alternatively, the vortex breaker 430 may be reversed, and the protruding portion of the vortex breaker 431 may protrude downward, thereby preventing the airflow from swirling. Furthermore, the vortex breaker 430 may also be an elastic component, which may be made of an elastic material or an injection molded material, so that the vortex breaker 430 automatically changes its convex portion upward or downward according to the air flow direction, for example: when the negative pressure sucks the material into the gas-liquid separator 400, the gas-liquid separator 400 separates gas and liquid, and the protruding part of the vortex eliminating piece 430 protrudes upwards due to the action of the negative pressure; when the positive pressure blows, the convex portion of the vortex breaker 430 protrudes downward. The arrangement of the present application is preferred.
In the present embodiment, the vortex elimination portion 431 is provided coaxially with the gas-liquid intake pipe 420, and the diameter of the vortex elimination portion 431 is smaller than the maximum diameter of the opening end. Thus, when the liquid film on the stop surface 421 stops to form liquid drops which are separated from the gas-liquid suction pipe 420 and drop, the liquid drops are not blocked by the vortex-eliminating part 431 and directly drop to the bottom of the gas-liquid separation cavity 411 to be gathered with separated liquid, so that the situation that the liquid stopped by the stop surface 421 is sucked into the gas-liquid suction pipe 420 again in the dropping process is avoided, the liquid stopping effect is ensured, and the loss of liquid materials is further reduced.
In this embodiment, the vortex breaker 430 further includes a supporting portion 432 supporting the vortex breaking portion 431, the supporting portion 432 includes a ring and a plurality of ribs, the ring is connected with the gas-liquid housing 410, the vortex breaking portion 431 is located in the ring, the ring is connected with the vortex breaking portion 431 through the ribs, the plurality of ribs are generally arranged, and the plurality of ribs are arranged along the circumferential direction of the vortex breaking portion 431 at intervals, so that a channel is formed between the outer ring, the ribs and the vortex breaking portion 431, and gas mixed in the liquid material, the sucked liquid material and liquid dropping from the gas-liquid suction pipe 420 can move up and down through the channel. The support part 432 provides support for the vortex elimination part 431, so that the vortex elimination part 431 can be mounted in the middle of the gas-liquid separation chamber 411 under the support of the support part 432, and a channel can be provided for the up-and-down circulation of gas and liquid materials, and the influence on normal circulation caused by the shielding of the vortex elimination piece 430 is avoided. Of course, the ring and the rib may be provided in a plate with a through hole or in other shapes besides the above-mentioned manner.
As shown in fig. 14, the gas-liquid separator 400 further includes a vortex breaker 440, the vortex breaker 440 is disposed in the gas-liquid separation chamber 411 and connected to the gas-liquid housing 410, the vortex breaker 440 is located at the gas-liquid outlet 4112 and divides a chamber portion of the gas-liquid separation chamber 411 close to the gas-liquid outlet 4112 into a plurality of outlet areas, and each outlet area is communicated with the gas-liquid outlet 4112. Vortex prevention piece 440 can prevent to produce liquid rotation in gas-liquid discharge gate 4112 when discharge liquid material, avoids forming the problem that the efflux of gas-liquid mixture blocks the effect and leads to the liquid flow who has restricted the export for the discharge rate of liquid material, raises the efficiency.
Specifically, the vortex preventing member 440 is radial, the vortex preventing member 440 takes the axis of the gas-liquid separation chamber 411 as a central line and extends along the radial direction of the gas-liquid separation chamber 411 to the periphery, the vortex preventing member 440 is formed by a plurality of rib plates, one end of each rib plate is located at the axis of the gas-liquid separation chamber 411, and the other end extends along the radial direction of the gas-liquid separation chamber 411 to the periphery, so that the vortex preventing member 440 is overall radial, the radial vortex preventing member 440 can separate a chamber part close to the gas-liquid discharge port 4112 to form a plurality of fan-shaped areas, and the fan-shaped areas are shielded by the rib plates in the horizontal direction and cannot be communicated with each other, so that when liquid materials are fed from the gas-liquid discharge port 4112, due to shielding of the rib plates, the liquid materials can be fed independently from each other between the discharge areas, and can not generate vortex, the liquid materials can be prevented from rotating at the gas-liquid discharge port 4112 when the liquid materials are discharged, and the situation that, accelerate the discharge speed of liquid materials and improve the efficiency. The rib plate is preferably arranged as a cross rib in this embodiment, and of course, may be arranged in other shapes as long as the liquid material can be prevented from generating a vortex at the gas-liquid discharge port 4112.
Preferably, the vortex breaker 440 is sized to cover the entire cross-section of the gas-liquid separation chamber 411 to ensure the vortex generation preventing effect. Of course, the size of the vortex breaker 440 may be set according to actual conditions, for example, when another member is provided at the gas-liquid discharge port 4112 to interfere with the vortex breaker 440, the vortex breaker 440 may be provided only on a part of the cross section of the gas-liquid separation chamber 411.
As shown in fig. 9 and 11, an arc-shaped transition section 412 is provided between the side surface and the top surface of the gas-liquid shell 410, that is, the top surface of the gas-liquid shell 410 is an arc-shaped top, so that when the liquid material adheres to the top surface of the gas-liquid shell 410 under the action of negative pressure or evaporates and condenses on the top surface of the gas-liquid shell 410, the liquid film moves downwards along the arc-shaped transition section 412 under the action of gravity and is converged into liquid drops to flow down along the side surface during the movement. If the liquid film is set to be the horizontal flat top surface, the liquid film stays on the flat top surface for a long time, and the liquid film will not drip until the liquid film attached to the flat top surface later and the previous liquid film are converged to form larger liquid drops. Of course, in addition to the transition section 412 being arranged in an arc shape, the transition section 412 may also be arranged in an inclined plane, and the inclined arrangement can also accelerate the speed of the liquid film converging into liquid drops to settle down.
In this embodiment, gas-liquid feed inlet 4111 is located the side that gas-liquid casing 410 is close to the top, and the axis of gas-liquid feed inlet 4111 is parallel with the tangent line of gas-liquid casing 410 in gas-liquid feed inlet 4111 department, when letting in liquid material from gas-liquid feed inlet 4111 to gas-liquid separation chamber 411, liquid material enters into gas-liquid separation chamber 411 along the tangential direction, and can be along the inner wall of gas-liquid casing 410 circumferential motion, can become relative sparsely between this in-process liquid material, input the negative pressure through gas-liquid suction port 4113 and gas-liquid suction pipe 420 to gas-liquid separation chamber 411 this moment and can more effectively take out the gas that is mingled with in the liquid material, thereby realize gas-liquid separation's purpose better, guarantee gas-liquid separation's effect.
In this embodiment, the gas-liquid separation chamber 411 further has a gas-liquid exhaust port 4114 for exhausting gas, and when positive pressure is input to the gas-liquid feed port 4111, the gas-liquid exhaust port 4114 is opened, and the positive pressure gas is exhausted through the gas-liquid exhaust port 4114. After the gas in the gas-liquid suction port 4113 inputs negative pressure to extract liquid materials is completed, the gas-liquid exhaust port 4114 is opened again, positive pressure is input into the gas-liquid separation cavity 411 through the gas-liquid feed inlet 4111, the liquid materials remained in the pipeline are blown into the gas-liquid separation cavity 411 by the gas of the positive pressure, the liquid materials are merged with the separated liquid, the liquid materials are prevented from remaining, the positive pressure gas can be smoothly discharged through the gas-liquid exhaust port 4114, the gas pressure inside and outside the gas-liquid separation cavity 411 can be balanced by the gas-liquid exhaust port 4114, and the potential safety hazard caused by overlarge internal pressure in the gas.
In the present embodiment, the gas-liquid separator 400 further includes a gas-liquid relief valve 450, and the gas-liquid relief valve 450 communicates with the gas-liquid separation chamber 411 and opens when the pressure in the gas-liquid separation chamber 411 reaches a preset value. When positive pressure is introduced into the gas-liquid separation cavity 411 through the gas-liquid inlet 4111 until the pressure reaches a preset value, the gas-liquid pressure release valve 450 is automatically pushed open by the pressure, gas in the gas-liquid separation cavity 411 is directly discharged, danger caused by overlarge pressure in the gas-liquid separation cavity 411 is avoided, and the safety of the gas-liquid separator 400 is improved. The specific numerical value is set correspondingly according to the actual situation.
In this embodiment, the gas-liquid separator 400 further includes a blocking valve for controlling the on-off state, and the gas-liquid outlet 4112, the gas-liquid inlet 4111, the gas-liquid outlet 4114, and the gas-liquid inlet 4113 are all provided with a blocking valve for controlling the gas or liquid to flow in and out. One or more of the above positions may be provided with a blocking valve, and the other positions where no blocking valve is provided may be controlled to be opened or closed by opening or closing a power source that supplies gas to the gas-liquid separator 400.
Optionally, the inner wall of the gas-liquid casing 410 may be further coated with a non-stick coating, silicone, or other anti-stick material, so as to further reduce the residue of the liquid material on the inner wall of the gas-liquid casing 410 and accelerate the speed of the liquid drops on the inner wall settling.
In this embodiment, the gas-liquid casing 410 is provided in a split manner, the gas-liquid casing 410 includes an upper casing and a lower casing, the upper casing and the lower casing are butted to form a gas-liquid separation chamber 411, the vortex-eliminating member 430 is detachably mounted between the upper casing and the lower casing, and a seal ring can be additionally arranged between the vortex-eliminating member 430 and the upper casing and the lower casing to ensure the gas tightness of the gas-liquid separation chamber 411.
The operation method of the gas-liquid separator 400 of the present embodiment is roughly divided into the following three processes:
negative pressure material suction: opening a gas-liquid feeding hole 4111 of the gas-liquid separator 400 and a gas-liquid suction hole 4113 of the gas-liquid separator 400, introducing negative pressure gas into the gas-liquid separation cavity 411 through the gas-liquid suction hole 4113, extracting liquid materials into the gas-liquid separation cavity 411 from the gas-liquid feeding hole 4111 by the negative pressure gas, and separating and extracting gas in the liquid materials by the negative pressure gas in the process to realize gas-liquid separation;
positive pressure blowing: after the material suction is completed, the gas-liquid suction port 4113 is closed, the gas-liquid exhaust port 4114 of the gas-liquid separator 400 is opened, positive pressure gas is introduced into the gas-liquid separation cavity 411 through the gas-liquid feed port 4111, the liquid material remained in the pipeline is blown into the gas-liquid separation cavity 411 by the positive pressure gas, the positive pressure gas entering the gas-liquid separation cavity 411 is discharged from the gas-liquid exhaust port 4114, the gas-liquid exhaust port 4114 is opened only in the positive pressure material blowing stage, and the gas-liquid exhaust port 4114 is closed in other stages;
positive pressure feeding: after the gas separation is completed, the gas-liquid exhaust port 4114 is closed, the gas-liquid discharge port 4112 of the gas-liquid separator 400 is opened, positive pressure gas is introduced into the gas-liquid separation cavity 411 through the gas-liquid feed port 4111, and the liquid material in the gas-liquid separation cavity 411 is blown out by the positive pressure gas, so that the feeding is realized.
As shown in fig. 15 and 16, the storage container 200 of the present embodiment is used for storing liquid materials such as edible oil and sesame oil which do not need to be subjected to gas-liquid separation, and the liquid materials and solid materials which need to be subjected to gas-liquid separation are subjected to gas separation and storage by the gas-liquid separator 400 and the gas-solid separator 300. The material storage member 200 comprises a material storage shell 210 and a diffusion structure 220 for detecting the material quantity, wherein the material storage shell 210 is provided with a material storage cavity 211 for containing materials; the diffusion structure 220 is connected with the storage housing 210, at least one part of the diffusion structure 220 extends into the storage cavity 211, and the diffusion structure 220 detects the material amount in the storage cavity 211, sends a feeding signal when the material amount is lower than a low preset value, and sends an overflow signal when the material amount is higher than a high preset value.
This embodiment is through being provided with diffusion structure 220, diffusion structure 220 is the amplifier promptly, diffusion structure 220 can detect the material volume of the storage in the storage spare 200, and convert the material volume into corresponding signal value, based on the structure of diffusion structure 220 self, diffusion structure 220 can amplify the detected signal, even the material volume takes place small change, diffusion structure 220 also can sharp sensing, thereby guarantee the detection precision, when diffusion structure 220 detects that the material volume in the storage cavity 211 is less than the default, diffusion structure 220 sends the feed supplement signal, realize automatic feed supplement or remind operating personnel in time to add the material, and send the overflow signal when the material volume is higher than the default, automatic stop feed supplement or remind operating personnel to stop the feed supplement. Above-mentioned mode of setting up has improved storage member 200 to the detection precision of material volume, can in time automatic feed supplement remind operating personnel to add the material, guarantees the continuous stable work of proportioning machine.
In this embodiment, the diffuser structure 220 covers as much of the entire height of the reservoir 211 as possible. Like this, no matter how much of material volume in the storage cavity 211, diffusion structure 220 homoenergetic detects to guarantee the comprehensiveness and the stability of detecting.
In this embodiment, the via hole has been seted up to the top surface of storage shell 210, and diffusion structure 220 passes the via hole and stretches into in the storage cavity 211, and diffusion structure 220 stretches into in the storage cavity 211 from the top of storage cavity 211 like this to can detect high liquid level department in the storage cavity 211. Certainly, also can set up the via hole in the top side of storage shell 210, diffusion structure 220 is the form of buckling, and diffusion structure 220 stretches into storage cavity 211 from the via hole of side, bends downwardly extending to the bottom of storage cavity 211 after stretching into storage cavity 211, and this mode of setting can reduce the occupation of storage 200 top space, and when storage 200 top space was not enough, the outside extension and the connection of diffusion structure 220 can be realized to the space that can utilize storage 200 both sides.
Further, the bottom end of the diffuser structure 220 is close to the bottom surface of the reservoir 211, or the bottom end of the diffuser structure 220 is in contact with the bottom surface of the reservoir 211. Like this, diffusion structure 220 can be close to the bottom surface of storage cavity 211 as far as possible to can detect low liquid level department in the storage cavity 211, cooperate the aforesaid to the detection of high liquid level department, realize guaranteeing the comprehensive nature that detects to the detection of whole storage cavity 211 height.
In this embodiment, the storage member 200 further includes a liquid level meter 230, the liquid level meter 230 is connected with the diffusion structure 220, the liquid level meter 230 is disposed outside the storage cavity 211, the liquid level meter 230 can receive the material supplement signal sent by the diffusion structure 220, and the material supplement signal is transmitted to the controller, and the controller receives the material supplement signal to control automatic material supplement or send an alarm to remind an operator to supplement the material.
Preferably, the liquid level gauge 230 is a gas film liquid level gauge 230. Of course, other types of liquid level meters 230 may be used, as long as the precise detection of the material amount can be realized by matching with the diffuser structure 220.
The diffusion structure 220 and the level gauge 230 of this embodiment are the one-to-one setting, and every diffusion structure 220 is connected with a level gauge 230 that corresponds respectively promptly, and when diffusion structure 220 was one, the level gauge 230 only need set up one, and when diffusion structure 220 was a plurality of, the level gauge 230 also was provided with a plurality ofly, every diffusion structure 220 respectively with a level gauge 230 be connected can. Of course, a plurality of diffusion structures 220 may be provided, correspondingly, only one liquid level meter 230 may be provided, the plurality of diffusion structures 220 are simultaneously connected with one liquid level meter 230, detection of the amount of the materials at multiple positions is realized through cooperation of one liquid level meter 230 and the diffusion structures 220, or a plurality of liquid level meters 230 may be provided, wherein a part of the diffusion structures 220 is connected with the same liquid level meter 230, and another part of the diffusion structures 220 is respectively connected with one liquid level meter 230. Can set up the length between diffuser structure 220 different as required and diffuser structure 220 stretches into the distance difference in the storage cavity 211 promptly, just also correspond and set up different warning positions, it is different to the urgent demand of feed supplement, go on when the culinary art, just also can judge when to carry out the feed supplement action according to the urgent degree of feed supplement.
In the present embodiment, the storage chamber 211 has a storage inlet 2111, a storage outlet 2112 and an overflow 2113, the storage inlet 2111 and the overflow 2113 are located at the top of the storage chamber 211, and the storage outlet 2112 is located at the bottom of the storage chamber 211. Storage spare 200 adds supplementary material through storage feed inlet 2111 in to storage cavity 211, throw the material through storage discharge gate 2112 realization, overflow mouth 2113's setting makes when parts such as diffusion structure 220 break down or manual operation mistake mistaking, if the too much condition of supplementary material appears, unnecessary material can in time be followed overflow mouth 2113 and discharged, avoid the too much condition that causes storage spare 200 can not bear and damage or even explode of material to take place, guarantee storage spare 200's security.
Preferably, the overflow 2113 is located on the top surface of the accumulator chamber 211. Therefore, when the material storage cavity 211 is completely full of materials, the materials are continuously added, and the materials are discharged from the overflow port 2113, so that the loss of the materials is reduced, and the loss cost is reduced. It should be noted that the height of the overflow 2113 should not be too low, but should be as high as possible to avoid accidental discharge of material from the overflow 2113 without overflow. Of course, the overflow 2113 may also be provided on the top side of the accumulator chamber 211. Therefore, when the material added into the material storage cavity 211 exceeds a certain height, the material can be discharged from the overflow port 2113, and the situation that the material completely occupies the material storage cavity 211 to damage the shell is avoided.
In this embodiment, every storage member 200 only is provided with a storage cavity 211, correspondingly, diffusion structure 220 only need set up one and can realize the detection to the material volume in this storage cavity 211, perhaps can be provided with a plurality of diffusion structures 220 in this storage cavity 211, and each diffusion structure 220 detects jointly, can improve detection accuracy on the one hand, and on the other hand still can have diffusion structure 220 to normally work when partial diffusion structure 220 breaks down, realizes detecting the reliability. Of course, the storage member 200 may also be provided with a plurality of storage cavities 211, and each storage cavity 211 may contain different materials, specifically, the space area in the storage housing 210 may be divided into a plurality of storage cavities 211 independent of each other, or a plurality of storage housings 210 may also be directly provided, and each storage housing 210 has one storage cavity 211 therein, or the above two manners are combined, that is, a plurality of storage housings 210 are provided, wherein the containing area in a part of the storage housings 210 is divided into a plurality of storage cavities 211, and one storage cavity 211 is provided in another part of the storage housings 210, when a plurality of storage cavities 211 are provided, the diffuser structure 220 is also provided in a plurality, and preferably, one diffuser structure 220 is provided in each storage cavity 211, so that the amount of materials in each storage cavity 211 can be detected. Of course, the diffuser structure 220 may be disposed in only a portion of the reservoir chamber 211 where the material quantity is to be measured.
And the batch feeder also comprises a controller, one or more storage pieces 200 can be arranged, the liquid level meter 230 of each storage piece 200 is electrically connected with the controller, and the controller receives a batch feeding signal transmitted by the liquid level meter 230, so that a corresponding mechanism is controlled to automatically feed or give an alarm to remind an operator to feed in time. The controller may be a computer and may communicate signals with the level gauge 230 in a wired or wireless manner.
Optionally, the magazine housing 210 is provided with an enlargement component, such as a magnifying glass or the like, in communication with the diffuser structure 220.
As shown in fig. 1 to 4, the housing 100 of the feeder is used as the outermost external component of the feeder, and the storage member 200, the separating device and the like are disposed in the housing 100, wherein the power source can be disposed in the housing 100 or disposed outside the housing 100. The housing 100 has a discharge outlet and the overflow 2113 of the magazine 200 communicates with the discharge outlet via the flow guide 240, such that material flowing from the overflow 2113 is conveyed through the flow guide 240 to the discharge outlet and out of the feeder via the discharge outlet.
In this embodiment, the batch charger further comprises a flow meter 500, the flow meter 500 is disposed between the liquid storage member and the gas-liquid separator 400, and the flow meter 500 can detect and count the flow rate of the liquid material, so as to detect the batch amount of the liquid material.
Optionally, the feeder further comprises at least one control valve disposed between the magazine 200 and the separating device, and/or between the separating device and the power source. The control valves of this embodiment are provided with a plurality of control valves, wherein the negative pressure control switch 610 and the negative pressure regulator 620 are provided with a plurality of groups in a matching manner, and the negative pressure control switch 610 and the negative pressure regulator 620 are connected with the gas-solid suction port 3113 of the gas-solid separator 300 or the gas-liquid suction port 4113 of the gas-liquid separator 400, so as to control and regulate the negative pressure parameter of the suction gas of the gas-solid separator 300 or the gas-liquid separator 400, thereby better achieving the effect of gas separation; the positive pressure control switch 630 and the positive pressure regulator 640 are provided with a plurality of groups in a mutually matched manner, and the positive pressure control switch 630 and the positive pressure regulator 640 are connected with the gas-solid gas inlet 3116 of the gas-solid separator 300 or the gas-liquid feed inlet 4111 of the gas-liquid separator 400, so that the positive pressure parameters of the gas introduced into the gas-solid separator 300 or the gas-liquid separator 400 are controlled and regulated, and the discharging effect is better realized; in addition, valves such as an electromagnetic valve 650, a straight-through ball valve 660 and the like are arranged to control the feeding of solid materials or liquid materials. The control valve can be used for replacing the valve types or additionally arranging the valves according to the requirements.
The power source of this embodiment has a variety, including the air supply that provides power for gas-solid separator 300 and vapour-liquid separator 400 and gear pump 710 that provides power for the material is thrown to the material in the storage spare 200, the air supply is provided with two kinds positive pressure air supply and negative pressure air supply, positive pressure air supply and gas-solid air inlet 3116 and gas-liquid feed inlet 4111 intercommunication, provide positive pressure power for gas-solid separator 300 and vapour-liquid separator 400, negative pressure air supply and gas-solid induction port 3113 and gas-liquid induction port 4113 intercommunication, provide negative pressure power for gas-solid separator 300 and vapour-liquid separator 400, gear pump 710 sets up in storage discharge gate 2112 of storage spare 200, thereby provide power for the material of throwing of storage spare 200. Of course, other power sources may be added or other types of power devices may be used in place of the air source and gear pump 710 described above, as desired.
It should be noted that, a plurality in the above embodiments means at least two.
From the above description, it can be seen that the above-mentioned embodiments of the present invention achieve the following technical effects:
1. the problem of poor feeding precision of a feeding device in the prior art is solved;
2. the solid material and the liquid material are respectively and independently stored, separated by gas, fed and the like, so that the feeder can be applied to the solid and the liquid, the mutual interference between the solid and the liquid is avoided, and the feeding precision is ensured;
3. the first filtering structure of the gas-solid separator filters materials with larger particles, and the second filtering structure filters solid materials with smaller particles, so that the filtering effect is ensured by classified filtering, and the filtering efficiency is improved;
4. the filtering holes of the first filtering structure and the second filtering structure of the gas-solid separator are arranged on the side surfaces, so that the end surfaces can play a certain role in blocking solid materials, and the filtering capacity of the filtering mechanism is reduced;
5. the end surfaces of the first filtering structure and the second filtering structure of the gas-solid separator are sealed ends, so that most solid materials are filtered while exhaust is not blocked;
6. the extending end and the extending part of the gas-solid separator can block solid materials in ascending gas flow to a great extent, and gas included in the solid materials can be separated more effectively;
7. the whole structure of the gas-solid separator is mainly in threaded connection, and the gas-solid separator is convenient and reliable to assemble and disassemble;
8. the cleaning mechanism of the gas-solid separator is beneficial to cleaning the pipeline, can increase the feeding precision of solid materials and reduce the static electricity generated by collision friction of the solid materials
9. The stop surface of the gas-liquid separator stops the sucked liquid, so that the possibility of sucking the liquid material away is reduced;
10. the eddy eliminating piece of the gas-liquid separator reduces the influence of the tail part of the central gas flow eddy on the separated liquid in the gas-liquid separation cavity;
11. the vortex-proof piece of the gas-liquid separator prevents liquid materials from rotating during discharging, and avoids the problem that the liquid flow at the outlet is limited due to the jet flow blocking effect of gas-liquid mixing;
12. the flow guide structure of the gas-liquid separator is beneficial to converging the liquid film at the jagged sharp corner to form larger liquid drops to drop, and the process of converging the liquid film into the liquid drops is accelerated;
13. the overflow port can discharge redundant materials in time, so that the safety of the material storage piece is ensured;
14. the diffusion structure amplifies the detection signal, and even if the material quantity changes slightly, the diffusion structure can also sense acutely, so that the detection precision is ensured.
It is obvious that the above described embodiments are only some of the embodiments of the present invention, and not all of them. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative efforts shall belong to the protection scope of the present invention.
It is noted that the terminology used herein is for the purpose of describing particular embodiments only and is not intended to be limiting of example embodiments according to the present application. As used herein, the singular is intended to include the plural unless the context clearly dictates otherwise, and it should be further understood that the terms "comprises" and/or "comprising," when used in this specification, specify the presence of features, steps, operations, devices, components, and/or combinations thereof.
It should be noted that the terms "first," "second," and the like in the description and claims of this application and in the drawings described above are used for distinguishing between similar elements and not necessarily for describing a particular sequential or chronological order. It is to be understood that the data so used is interchangeable under appropriate circumstances such that the embodiments of the application described herein are capable of operation in sequences other than those illustrated or described herein.
The above description is only a preferred embodiment of the present invention and is not intended to limit the present invention, and various modifications and changes may be made by those skilled in the art. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.

Claims (15)

1. An applicator for kitchen equipment, comprising:
a housing (100);
at least one magazine (200), the magazine (200) having a magazine chamber (211) for storing material;
the separation device can store materials and separate gas in the materials introduced into the separation device;
a power source connected to the separator and/or the storage member (200) and providing power for movement of the material.
2. A feeder according to claim 1, characterised in that the separation device comprises:
a gas-solid separator (300) for storing solid material, the gas-solid separator (300) separating gas from the introduced solid material;
a gas-liquid separator (400) for storing the liquid material, the gas-liquid separator (400) separating gas from the introduced liquid material.
3. A feeder according to claim 2, characterised in that the gas-solid separator (300) comprises:
the gas-solid separation device comprises a gas-solid shell (310), wherein the gas-solid shell (310) is provided with a gas-solid separation cavity (311), and the gas-solid separation cavity (311) is provided with a gas-solid feeding hole (3111), a gas-solid discharging hole (3112) and a gas-solid suction hole (3113);
filtering mechanism (320), filtering mechanism (320) sets up in gas-solid separation chamber (311), and will gas-solid separation chamber (311) fall into first cavity (3114) and the gaseous second cavity (3115) of extraction that hold the material, gas-solid feed inlet (3111) with gas-solid discharge gate (3112) is located first cavity (3114) department, gas-solid induction port (3113) are located second cavity (3115) department, filtering mechanism (320) obstruct the solid material and get into second cavity (3115).
4. A feeder according to claim 3, characterised in that the filtering means (320) comprise:
the mechanism shell (321), the mechanism shell (321) is connected with the gas-solid shell (310);
a first filter structure (322);
the first filtering structure (322) and the second filtering structure (323) are arranged in the mechanism shell (321), the first filtering structure (322) is close to the first cavity (3114) compared with the second filtering structure (323), the side surfaces of the first filtering structure (322) and the second filtering structure (323) are provided with filtering holes, and the size of the materials filtered by the first filtering structure (322) is larger than that of the materials filtered by the second filtering structure (323).
5. The batch feeder according to claim 4,
the end surface of the first filter structure (322) and/or the second filter structure (323) is a sealed end; or
The end face of the first filter structure (322) and/or the second filter structure (323) is a non-sealing end, and the size of the material filtered by the end face is smaller than that of the material filtered by the side face.
6. The dispenser according to claim 4, characterized in that the end of the first filter structure (322) remote from the second filter structure (323) is a protruding end, at least a portion of which protrudes into the first cavity (3114), the mechanism housing (321) having a protruding portion (3211), at least a portion of the protruding portion (3211) protruding into the first cavity (3114), and the protruding portion (3211) protruding into the first cavity (3114) over a greater length than the protruding portion (3114) received in the protruding portion (3211).
7. A feeder according to claim 3, characterised in that the gas-solid separator (300) further comprises a cleaning mechanism comprising:
the cleaning pipeline is used for conveying cleaning liquid and is detachably arranged at the gas-solid feed port (3111);
the heating element is arranged on the outer side of the gas-solid shell (310).
8. The batch feeder according to claim 2, characterized in that the gas-liquid separator (400) comprises:
the gas-liquid shell (410) is provided with a gas-liquid separation cavity (411) for containing materials, and the gas-liquid separation cavity (411) is provided with a gas-liquid feeding hole (4111), a gas-liquid discharging hole (4112) and a gas-liquid suction hole (4113);
the gas-liquid suction pipe (420), the gas-liquid suction pipe (420) is communicated with the gas-liquid suction port (4113), at least one part of the gas-liquid suction pipe (420) extends into the gas-liquid separation cavity (411), and the gas-liquid suction pipe (420) extends into the opening end of the gas-liquid separation cavity (411) and is provided with a stop surface (421) for stopping liquid materials;
a vortex breaker (430), the vortex breaker (430) being disposed within the gas-liquid separation chamber (411) with a surface of the vortex breaker (430) facing the open end.
9. The feeder according to claim 8, wherein the inner wall surface of the open end is the stop surface (421), the stop surface (421) is inclined, and the stop surface (421) is inclined towards the center of the gas-liquid suction pipe (420) along the direction of sucking gas by the gas-liquid suction pipe (420).
10. The batch feeder according to claim 8, characterized in that the end of the open end has a flow guiding structure (422), and the liquid on the stop surface (421) is concentrated into a stream via the flow guiding structure (422).
11. The batch feeder according to claim 8, wherein the vortex breaker (430) comprises a vortex breaker (431), the vortex breaker (431) is opposite to the gas-liquid suction pipe (420), and at least a portion of the vortex breaker (431) protrudes in a direction close to the gas-liquid suction pipe (420).
12. The batch feeder according to claim 8, characterized in that the gas-liquid separator (400) further comprises a vortex breaker (440), the vortex breaker (440) being disposed within the gas-liquid separation chamber (411) and dividing a chamber portion of the gas-liquid separation chamber (411) adjacent to the gas-liquid outlet (4112) into a plurality of discharge areas, each of the discharge areas being in communication with the gas-liquid outlet (4112).
13. The feeder according to any one of claims 1 to 12, characterised in that the magazine (200) comprises:
a magazine housing (210), the magazine housing (210) having the magazine chamber (211);
the diffusion structure (220) is used for detecting the material quantity, the diffusion structure (220) is connected with the material storage shell (210), at least one part of the diffusion structure (220) extends into the material storage cavity (211), the diffusion structure (220) detects the material quantity in the material storage cavity (211), and sends a material supplementing signal when the material quantity is lower than a low preset value and sends an overflow signal when the material quantity is higher than a high preset value.
14. The feeder according to claim 13, characterized in that the bottom end of the diffuser structure (220) is close to the bottom surface of the magazine chamber (211) or the bottom end of the diffuser structure (220) is in contact with the bottom surface of the magazine chamber (211).
15. The feeder according to any one of claims 1 to 12, characterised in that the storage chamber (211) has an overflow (2113) for the outflow of material.
CN201921063108.XU 2019-07-08 2019-07-08 Material feeder for kitchen equipment Active CN210697393U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201921063108.XU CN210697393U (en) 2019-07-08 2019-07-08 Material feeder for kitchen equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201921063108.XU CN210697393U (en) 2019-07-08 2019-07-08 Material feeder for kitchen equipment

Publications (1)

Publication Number Publication Date
CN210697393U true CN210697393U (en) 2020-06-09

Family

ID=70940331

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201921063108.XU Active CN210697393U (en) 2019-07-08 2019-07-08 Material feeder for kitchen equipment

Country Status (1)

Country Link
CN (1) CN210697393U (en)

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