CN220968959U - Useless honey dilution system - Google Patents
Useless honey dilution system Download PDFInfo
- Publication number
- CN220968959U CN220968959U CN202322606932.8U CN202322606932U CN220968959U CN 220968959 U CN220968959 U CN 220968959U CN 202322606932 U CN202322606932 U CN 202322606932U CN 220968959 U CN220968959 U CN 220968959U
- Authority
- CN
- China
- Prior art keywords
- pipeline
- waste honey
- waste
- valve
- measurer
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 235000012907 honey Nutrition 0.000 title claims abstract description 92
- 239000012895 dilution Substances 0.000 title claims abstract description 27
- 238000010790 dilution Methods 0.000 title claims abstract description 27
- 239000002699 waste material Substances 0.000 claims abstract description 91
- 239000003085 diluting agent Substances 0.000 claims abstract description 9
- 238000007599 discharging Methods 0.000 claims abstract description 4
- 239000007788 liquid Substances 0.000 claims description 21
- 238000012544 monitoring process Methods 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 14
- 238000007865 diluting Methods 0.000 abstract description 7
- 239000000243 solution Substances 0.000 description 6
- 235000013379 molasses Nutrition 0.000 description 5
- 238000010586 diagram Methods 0.000 description 2
- 238000000855 fermentation Methods 0.000 description 2
- 230000004151 fermentation Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 1
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 1
- 229930006000 Sucrose Natural products 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000008236 heating water Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 125000001436 propyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 239000005720 sucrose Substances 0.000 description 1
Landscapes
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
Abstract
The utility model discloses a waste honey dilution system, and belongs to the technical field of waste honey dilution. The utility model comprises a box body; the discharging end of the hopper scale is connected with the top of the box body; one end of the first pipeline for conveying the waste honey is connected with the hopper scale, and the other end of the first pipeline is connected with the discharge end of the waste honey conveying equipment; one end of the second pipeline for conveying the diluent is connected with the top of the box body, and the other end of the second pipeline is connected with the discharge end of the diluent conveying equipment; a control assembly including a controller, a first flow meter, and a measurer; the first flowmeter is arranged on the second pipeline; the measurer is arranged on the first pipeline; the controller is respectively connected with the hopper scale, the first flowmeter and the measurer through circuits. According to the utility model, the hot water quantity required to be added for diluting the waste honey is calculated through the hopper scale, the measurer, the first flowmeter and the controller, so that the accurate control of waste honey dilution is realized, the waste honey dilution is stable, and the phenomenon that the diluted waste honey is too low or too high in hammer degree due to too much or too little hot water quantity is avoided.
Description
Technical Field
The utility model belongs to the technical field of waste honey dilution, and particularly relates to a waste honey dilution system.
Background
Waste honey (also known as propyl honey) is a byproduct of the sugar industry, is a viscous, semi-fluid liquid containing a large amount of fermentable sugar (mainly sucrose), and is therefore a good fermentation raw material, and can be used as a substrate for yeast, gastroscope, etc. fermentation products or as a raw material for certain foods and animal feeds.
The concentration of the waste honey is often far higher than the requirement of customers before selling, so that the waste honey needs to be diluted to a certain extent to ensure that the concentration requirement of the customers is met. The invention of patent publication No. CN109628650A discloses an automatic control system and method for diluting molasses, which mainly solves the problems of diluting and sand holding of the raw molasses, but is not applicable to waste molasses (the viscosity of the waste molasses is higher than that of the raw molasses).
Therefore, the dilution of the waste honey in the sugar refinery is mostly finished by manually heating water for dilution, and when the manual dilution usually relies on personal experience, water is added into the waste honey, so that the hammer degree of the diluted waste honey is suddenly high and suddenly low, the hammer degree is unstable, and the factory requirement cannot be met.
Disclosure of utility model
The utility model provides a waste honey dilution system, which aims to solve the problems in the background technology.
In order to achieve the above purpose, the utility model adopts the following technical scheme:
A waste honey dilution system comprises a box body; the discharging end of the hopper scale is connected with the top of the box body; one end of the first pipeline for conveying the waste honey is connected with the hopper scale, and the other end of the first pipeline is connected with the discharge end of the waste honey conveying equipment; one end of the second pipeline for conveying the diluent is connected with the top of the box body, and the other end of the second pipeline is connected with the discharge end of the diluent conveying equipment; a control assembly including a controller, a first flow meter, and a measurer; the first flowmeter is arranged on the second pipeline; the measurer is arranged on the first pipeline; the controller is respectively connected with the hopper scale, the first flowmeter and the measurer in a circuit mode.
As a further improvement of the technical scheme, the measurer is a flowmeter.
As a further improvement of the technical scheme, the measurer is a brix gauge.
As a further improvement of the technical scheme, the hopper scale is positioned above the box body.
As a further improvement of the technical solution, the control assembly further comprises a level gauge for monitoring the tank liquid volume; the liquid level meter is arranged on the box body; the liquid level meter is in circuit connection with the controller.
As a further improvement of the technical proposal, the control component also comprises a third pipeline and a waste honey pump; one end of the third pipeline is connected with the bottom of the box body; the waste honey pump is arranged on the third pipeline; and the waste honey pump is in circuit connection with the controller.
As a further improvement of the technical solution, the control assembly further comprises a first valve; the first valve is arranged on the first pipeline; the measurer is located between the first valve and the hopper scale.
As a further improvement of the technical solution, the control assembly further comprises a second valve; the second valve is arranged on the second pipeline; the first flow meter is located between the second valve and the tank.
As a further improvement of the technical scheme, the first valve and the second valve are both control valves; the controller is in circuit connection with the first valve and the second valve.
Compared with the prior art, the utility model has the following beneficial effects:
According to the utility model, the hot water quantity required to be added for diluting the waste honey is calculated through the hopper scale, the measurer, the first flowmeter and the controller, so that the accurate control of waste honey dilution is realized, the waste honey dilution is stable, the phenomenon that the diluted waste honey is too low or too high in weight and cannot meet the factory requirement due to too much or too little hot water quantity is avoided, meanwhile, the manual operation can be reduced through the control of the controller, and the manual working strength is reduced.
Drawings
In order to more clearly illustrate the technical solutions of the embodiments of the present utility model, the drawings that are needed in the embodiments will be briefly described below, it being understood that the following drawings only illustrate some embodiments of the present utility model and therefore should not be considered as limiting the scope, and other related drawings may be obtained according to these drawings without inventive effort for a person skilled in the art.
FIG. 1 is a schematic diagram of a waste honey dilution system according to the present utility model;
Fig. 2 is a front view of fig. 1
FIG. 3 is a schematic diagram of the structure provided by the present utility model;
reference numerals: 1-box, 2-hopper scale, 3-first pipeline, 4-second pipeline, 5-control assembly, 51-controller, 52-first flowmeter, 53-caliber, 54-liquid level meter, 55-third pipeline, 56-waste honey pump, 57-first valve, 58-second valve.
Detailed Description
In order to make the objects, technical solutions and advantages of the embodiments of the present utility model more clear, the technical solutions of the embodiments of the present utility model will be clearly and completely described below with reference to the accompanying drawings of the embodiments of the present utility model. It will be apparent that the described embodiments are some, but not all, embodiments of the utility model. All other embodiments, which can be made by a person skilled in the art without creative efforts, based on the described embodiments of the present utility model fall within the protection scope of the present utility model. Unless defined otherwise, technical or scientific terms used herein should be given the ordinary meaning as understood by one of ordinary skill in the art to which this utility model belongs.
The terms "first," "second," and the like in the description and in the claims, are not used for any order, quantity, or importance, but are used for distinguishing between different elements. Also, unless the context clearly indicates otherwise, singular forms "a," "an," or "the" and similar terms do not denote a limitation of quantity, but rather denote the presence of at least one. The terms "comprises," "comprising," or the like are intended to cover a feature, integer, step, operation, element, and/or component recited as being present in the element or article that "comprises" or "comprising" does not exclude the presence or addition of one or more other features, integers, steps, operations, elements, components, and/or groups thereof. "up", "down", "left", "right" and the like are used only to indicate a relative positional relationship, and when the absolute position of the object to be described is changed, the relative positional relationship may be changed accordingly.
In the description of the present utility model, it should be noted that unless explicitly stated and limited otherwise, the terms "mounted," "connected," and "disposed" should be construed broadly, and may be, for example, fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; can be directly connected or indirectly connected through an intermediate medium, and can be communication between two elements. The specific meaning of the above terms in the present utility model will be understood in specific cases by those of ordinary skill in the art.
Embodiment one:
As shown in fig. 1 to 3, a waste honey diluting system includes a tank 1; the discharging end of the hopper scale 2 is connected with the top of the box body 1, the hopper scale 2 is communicated with the inside of the box body 1, and optionally, the hopper scale 2 can convey waste honey into the box body 1 through a pump body and can be fixedly arranged above the box body 1, and the waste honey in the hopper scale 2 is injected into the box body 1 through gravity, preferably, the hopper scale 2 is fixedly arranged above the box body 1 and is injected into the box body 1 through gravity, so that the manufacturing cost is reduced; a piston is arranged in the hopper scale 2 and controls the outflow of waste honey in the hopper scale 2; a first pipe 3 for conveying the waste honey, one end of which is connected with the hopper scale 2, and the other end of which is connected with the discharge end of the waste honey conveying device so as to inject the waste honey into the hopper scale 2; one end of a second pipeline 4 for conveying the diluent is connected with the top of the box body 1, the other end of the second pipeline is connected with the discharge end of the diluent conveying equipment, and the diluent is hot water; a control assembly 5 comprising a controller 51, a first flow meter 52 and a measurer 53; the first flowmeter 52 is arranged on the second pipeline 4 to monitor the amount of dilution material injected into the box body 1; the measurer 53 is disposed on the first pipe 3, and the measurer 53 may be a flowmeter or a brix meter, in this embodiment, the measurer 53 is a flowmeter, and measures the volume of the waste honey flow entering the hopper scale 2; the controller 51 is respectively connected with the hopper scale 2, the first flowmeter 52 and the measurer 53 in a circuit manner, the controller 51 can be installed in a control room or on the box body 1, and the controller 51 is a PLC controller. In addition, it should be noted that the hopper scale belongs to the prior art, and can be purchased in the market, and the connection mode of the controller and the first flowmeter, the measurer and the hopper scale is conventional connection, wherein the specific model related to the controller, the first flowmeter, the measurer and the hopper scale is not the improvement point of the present application, and will not be described in detail herein.
The working mode is as follows:
During operation, the waste honey is conveyed to the hopper scale 2 through the first pipeline 3, the hopper scale 2 collects the weight of the waste honey and conveys the weight M1 of the waste honey to the controller 51, when the weight of the waste honey reaches a preset value, the piston in the hopper scale 2 is stopped to convey the waste honey to the hopper scale 2, the controller 51 controls the piston in the hopper scale 2 to be opened, the waste honey in the hopper scale 2 is injected into the box body 1, the measurer 53 measures the flow volume of the waste honey entering the hopper scale 2 and conveys the volume V of the waste honey to the controller 51, the controller 51 calculates the density of the waste honey according to the weight M1 of the waste honey and the volume V of the waste honey, the weights of the waste honey are different, the densities of the waste honey are also different, when the densities of the waste honey are calculated, the waste honey weight B1 can be calculated, for example, the waste honey weight B2 is diluted by a comparison table of the sugar weight and the density is determined on the controller 51, and the controller 51 calculates the waste honey weight B2 according to the formula: M=M11.B1/B2-M1 (the formula is a conventional formula for diluting the waste honey), the weight of M is calculated, wherein M is the weight of added hot water, the first flowmeter 52 monitors the added hot water in real time, when the added hot water reaches the weight value of the added hot water (the density of water is 1 KG/L), the hot water is stopped to be added into the box body 1, the accurate control of diluting the waste honey is realized, the dilution of the waste honey is stable, the excessive or insufficient amount of the added hot water is avoided, the excessive or insufficient amount of the diluted waste honey is caused, the excessive or insufficient amount of the diluted waste honey cannot meet the factory requirement, and meanwhile, the manual operation can be reduced and the manual working strength is reduced through the control of the controller 51.
As shown in fig. 1 and 3, the control assembly 5 preferably further comprises a level gauge 54 for monitoring the liquid level of the tank 1, a third pipe 55 and a waste honey pump 56; the liquid level meter 54 is fixedly arranged on the box body 1 to monitor the liquid level in the box body 1, and the liquid level meter 54 can be an acoustic wave liquid level meter, a floating ball liquid level meter or a radar liquid level meter; the liquid level meter 54 is in circuit connection with the controller 51 and transmits the liquid level in the box body 1 to the controller 51 in real time; one end of the third pipeline 55 is connected with the bottom of the box body 1, and the other end of the third pipeline is connected with the waste honey tower; the waste honey pump 56 is arranged on the third pipeline 55, the waste honey pump 56 is a common pump body and mainly conveys diluted waste honey to the waste honey tower; the waste honey pump 56 is in circuit connection with the controller 51; when the liquid level in the box body 1 exceeds a set value, the controller 51 controls the starting of the waste honey pump 56, the waste honey pump 56 conveys waste honey in the box body 1 into the waste honey tower through the third pipeline 55 for storage, and when the liquid level in the box body 1 is lower than the set value, conveying is stopped, so that unattended operation is realized. In addition, it should be noted that the connection mode of the controller, the liquid level meter and the waste honey pump is conventional connection, and the specific model of the waste honey pump and the liquid level pump is not an improvement point of the application, and will not be described herein.
As shown in fig. 1 to 3, the control assembly 5 also preferably comprises a first valve 57; the first valve 57 is arranged on the first pipeline 3; the measurer 53 is located between the first valve 57 and the hopper scale 2, the first valve 57 can be an electric valve or a pneumatic valve, the first valve 57 is in circuit connection with the controller 51, and when the weight in the hopper scale 2 reaches a preset value, the controller 51 controls the first valve 57 to be closed, and the waste honey is stopped being conveyed into the hopper scale 2. In addition, it should be noted that the connection manner of the first valve and the controller is conventional connection, and the specific model of the first valve is not an improvement point of the present application, and will not be described herein.
As shown in fig. 1-2, the control assembly 5 also preferably includes a second valve 58; the second valve 58 is arranged on the second pipeline 4; the first flowmeter 52 is located between the second valve 58 and the tank 1; the second valve 58 can be an electric valve or a pneumatic valve, the second valve 58 is connected with the controller 51 in a circuit, and when the weight in the tank 1 reaches a preset value, the controller 51 controls the second valve 58 to be closed, and the hot water is stopped being fed into the tank 1. In addition, it should be noted that the connection manner of the second valve and the controller is conventional connection, and the specific model of the second valve is not an improvement point of the present application, and will not be described herein.
Embodiment two:
As shown in fig. 3, the difference from the first embodiment is that: the measurer 53 is a brix gauge; the measurer 53 is a brix gauge; when the measurer 53 is the brix timer, the waste honey brix B1 can be directly detected by the measurer 53, and the measurer 53 transmits the data of the waste honey brix B1 to the controller 51, so that the controller 51 can omit the calculation and estimation process compared with the first embodiment in which the measurer 53 is the brix timer. In addition, it should be noted that the connection mode of the measurer and the controller is conventional connection, and the specific model of the measurer is not an improvement point of the present application, and will not be described herein.
The foregoing description of the preferred embodiments of the utility model is not intended to be limiting, but rather is intended to cover all modifications, equivalents, and alternatives falling within the spirit and principles of the utility model.
Claims (9)
1. A waste honey dilution system, comprising:
A case (1);
The discharging end of the hopper scale (2) is connected with the top of the box body (1);
One end of the first pipeline (3) for conveying the waste honey is connected with the hopper scale (2), and the other end of the first pipeline is connected with the discharge end of the waste honey conveying equipment;
One end of a second pipeline (4) for conveying the diluent is connected with the top of the box body (1), and the other end of the second pipeline is connected with the discharge end of the diluent conveying equipment;
a control assembly (5) comprising a controller (51), a first flowmeter (52) and a measurer (53); the first flowmeter (52) is arranged on the second pipeline (4); the measurer (53) is arranged on the first pipeline (3); the controller (51) is respectively connected with the hopper scale (2), the first flowmeter (52) and the measurer (53) in a circuit mode.
2. The waste honey dilution system according to claim 1, wherein the measurer (53) is a flow meter.
3. The waste honey dilution system according to claim 1, wherein the measurer (53) is a brix meter.
4. The waste honey dilution system according to claim 1, wherein the hopper scale (2) is located above the tank (1).
5. The waste honey dilution system according to claim 1, wherein the control assembly (5) further comprises a level gauge (54) for monitoring the liquid amount of the tank (1); the liquid level meter (54) is arranged on the box body (1); the liquid level meter (54) is in circuit connection with the controller (51).
6. The waste honey dilution system according to claim 5, wherein the control assembly (5) further comprises a third conduit (55) and a waste honey pump (56); one end of the third pipeline (55) is connected with the bottom of the box body (1); the waste honey pump (56) is arranged on the third pipeline (55); the waste honey pump (56) is in circuit connection with the controller (51).
7. The waste honey dilution system according to any one of claims 1-6, wherein the control assembly (5) further comprises a first valve (57); the first valve (57) is arranged on the first pipeline (3); the measurer (53) is located between the first valve (57) and the hopper scale (2).
8. The waste honey dilution system according to claim 7, wherein the control assembly (5) further comprises a second valve (58); the second valve (58) is arranged on the second pipeline (4); the first flowmeter (52) is located between the second valve (58) and the tank (1).
9. The waste honey dilution system according to claim 8, wherein the first valve (57) and the second valve (58) are both control valves; the controller (51) is electrically connected to the first valve (57) and the second valve (58).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202322606932.8U CN220968959U (en) | 2023-09-25 | 2023-09-25 | Useless honey dilution system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202322606932.8U CN220968959U (en) | 2023-09-25 | 2023-09-25 | Useless honey dilution system |
Publications (1)
Publication Number | Publication Date |
---|---|
CN220968959U true CN220968959U (en) | 2024-05-17 |
Family
ID=91042626
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202322606932.8U Active CN220968959U (en) | 2023-09-25 | 2023-09-25 | Useless honey dilution system |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN220968959U (en) |
-
2023
- 2023-09-25 CN CN202322606932.8U patent/CN220968959U/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN201705330U (en) | Mobile Oil Well Multiphase Flow Metering Device | |
CN220968959U (en) | Useless honey dilution system | |
CN206557619U (en) | Fluid reservoir dynamic Liquid Surface height controller | |
CN207552450U (en) | A kind of continuous electroplating tin unit is passivated section chemicals dosing plant | |
CN207197646U (en) | The device of charging control in titanium sponge reduction production process | |
CN207204044U (en) | It is a kind of to be automatically introduced into set amount hydrogen peroxide plant to being vacuumized in reactor | |
CN112823873A (en) | Method and device for accurately controlling feeding of reaction kettle | |
CN206713988U (en) | A kind of online enzyme preparation add-on system of rice protein feed liquid multistage timesharing | |
CN217093368U (en) | Intelligent blending device for digital hot pot oil dishes | |
CN212374420U (en) | Centralized feeding system of beverage automatic production line | |
CN201808148U (en) | Air-blowing admixture metering system | |
CN205426283U (en) | Anticorrosion liquid level detection device | |
CN209232873U (en) | A kind of dynamic lithium battery electrolysis liquid transportation system | |
CN204509129U (en) | For the feeder system of sticky material spraying | |
CN206270106U (en) | One kind is to measuring tank feeding control system and water paint blanking system | |
CN204714511U (en) | A kind of weighing type fluid dispensing system and weighing container system | |
CN206337315U (en) | A kind of automatic filling antirust liquid device | |
CN212732121U (en) | PH adjusting device of polyether product | |
CN219926509U (en) | Intelligent slurry preparation equipment | |
CN220579311U (en) | Negative pressure discharging device of continuous sugar boiling tank | |
CN216275952U (en) | Water supply system for paving brick mixing | |
CN217628406U (en) | Continuous automatic starch milk mixing system in starch sugar production | |
CN213050324U (en) | Slurry concentration detection feedback control device | |
CN211147799U (en) | Water metering device for preparing foam extinguishing agent | |
CN221234110U (en) | Quantitative canning equipment for water-based edging liquid |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |