CN210787259U - Full-automatic syrup mixing system - Google Patents
Full-automatic syrup mixing system Download PDFInfo
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- CN210787259U CN210787259U CN201921316120.7U CN201921316120U CN210787259U CN 210787259 U CN210787259 U CN 210787259U CN 201921316120 U CN201921316120 U CN 201921316120U CN 210787259 U CN210787259 U CN 210787259U
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- 239000006188 syrup Substances 0.000 title claims abstract description 232
- 235000020357 syrup Nutrition 0.000 title claims abstract description 227
- 238000002156 mixing Methods 0.000 title claims abstract description 79
- 239000007788 liquid Substances 0.000 claims abstract description 113
- 238000011084 recovery Methods 0.000 claims abstract description 41
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 40
- 238000002360 preparation method Methods 0.000 claims abstract description 38
- 238000003860 storage Methods 0.000 claims abstract description 35
- 238000004140 cleaning Methods 0.000 claims description 4
- 238000004891 communication Methods 0.000 claims description 4
- 239000002002 slurry Substances 0.000 claims 1
- 239000000243 solution Substances 0.000 description 9
- 238000002347 injection Methods 0.000 description 7
- 239000007924 injection Substances 0.000 description 7
- 238000004519 manufacturing process Methods 0.000 description 5
- 238000003756 stirring Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 238000009429 electrical wiring Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000000523 sample Substances 0.000 description 1
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- Jellies, Jams, And Syrups (AREA)
Abstract
The utility model relates to a full-automatic syrup mixing system, include: the syrup mixing device comprises a dilute syrup recovery tank for recovering used syrup, a syrup mixing tank for mixing syrup concentration, a syrup storage tank for storing mixed syrup, and a dilute syrup output pipeline connected with a liquid outlet of the dilute syrup recovery tank; the syrup mixing tank is connected with the high-concentration syrup tank through a high-concentration syrup conveying pipeline, and the bottom of the syrup mixing tank is provided with a water inlet and a liquid outlet of the mixing tank; the liquid inlet of the syrup storage tank is connected with a syrup input pipeline, and the liquid outlet of the syrup storage tank is connected with a syrup output pipeline; the liquid outlet pipeline and the dilute syrup outlet pipeline of the blending tank are connected to one side of the circulating pump in parallel, and the blending pipeline and the syrup inlet pipeline are connected to the other side of the circulating pump in parallel. The utility model can automatically prepare the syrup with set percentage concentration in a short time, thereby improving the controllability and accuracy of syrup preparation concentration; does not need manual operation, has high automation degree, can continuously carry out the blending work of syrup and has high working efficiency.
Description
Technical Field
The utility model relates to a syrup allotment equipment especially relates to a full-automatic syrup allotment system.
Background
At present, the blending of syrup concentration is basically realized in two blending modes in the production process, one mode is to pour sugar solution with high concentration into a groove or a tank containing water or low-concentration sugar solution for manual stirring; the other is to stir in a stirring tank by using the power of a motor reducer. The two stirring modes need to manually pour sugar liquid, the concentration of the sugar liquid is lower than that of the sugar liquid, and the concentration of the sugar liquid is higher than that of the sugar liquid added with water or the sugar liquid with low concentration. Therefore, the concentration controllability of the sugar liquid is poor, the percentage concentration of the prepared sugar liquid is not accurate, and the labor intensity is high.
In order to accurately control the concentration of sugar solution blending and reduce the labor intensity of workers, the utility model designs a full-automatic syrup blending device.
SUMMERY OF THE UTILITY MODEL
The utility model aims to solve the technical problem that a do not need manual operation and accurate full-automatic syrup mixing system of syrup concentration regulation is provided.
In order to solve the technical problem, the technical scheme of the utility model is that: a fully automatic syrup blending system comprising:
the thin syrup recovery tank is used for recovering the used syrup, a recovery tank liquid inlet connected with a recovery pipeline is formed in the top of the thin syrup recovery tank, a recovery tank liquid outlet used for outputting the thin syrup is formed in the bottom of the thin syrup recovery tank, a thin syrup output pipeline is connected to the recovery tank liquid outlet, and a recovery tank liquid outlet valve is mounted on the thin syrup output pipeline;
the syrup mixing tank is used for mixing syrup concentration, a high-concentration syrup inlet and a mixing port are formed in the top of the syrup mixing tank, the high-concentration syrup inlet is connected with the high-concentration syrup tank through a high-concentration syrup conveying pipeline, a syrup pump and a syrup outlet big valve are mounted on the high-concentration syrup conveying pipeline, the mixing port is connected with a mixing pipeline, and a syrup inlet mixing tank valve is mounted on the mixing pipeline; the bottom of the syrup blending tank is provided with a water inlet and a blending tank liquid outlet, the water inlet is connected with a water inlet pipeline, the water inlet pipeline is provided with a water inlet valve, the blending tank liquid outlet is connected with a blending tank liquid outlet pipeline, the blending tank liquid outlet pipeline is provided with a blending tank valve, and the syrup blending tank is also provided with a sugar degree sensor and a liquid level sensor;
the syrup storage tank is used for storing the prepared syrup, a storage tank liquid inlet is formed in the top of the syrup storage tank, a storage tank liquid outlet for outputting the prepared syrup is formed in the bottom of the syrup storage tank, a syrup input pipeline is connected to the storage tank liquid inlet, a storage tank inlet valve is installed on the syrup input pipeline, a syrup output pipeline is connected to the storage tank liquid outlet, and a storage tank outlet valve is installed on the syrup output pipeline;
one end of the circulating pump is connected with a circulating inlet pipeline, the other end of the circulating pump is connected with a circulating outlet pipeline, a circulating control valve is further mounted on the circulating outlet pipeline, a liquid outlet pipeline of the blending tank and a dilute syrup output pipeline are connected to the circulating inlet pipeline in parallel, and a blending pipeline and a syrup input pipeline are connected to the circulating outlet pipeline in parallel;
the PLC controller, brix sensor and level sensor electricity are connected to the input port of PLC controller, the recovery tank goes out the liquid valve, advances blending tank valve, water intaking valve, goes out blending tank valve, advances holding vessel valve, circulating pump and syrup pump and all connects electrically to the output port of PLC controller.
Preferably, the syrup pump is a twin turbine syrup pump.
As the preferred technical scheme, the dilute syrup recovery tank, the syrup blending tank and the syrup storage tank are all provided with windows.
As the preferred technical scheme, the number of the windows on the dilute syrup recovery tank, the syrup blending tank and the syrup storage tank is two, and the two windows are arranged up and down.
As the preferred technical scheme, the top of the syrup preparation tank is provided with an atmosphere communication hole and a manhole.
As the preferred technical scheme, the top of the syrup preparation tank is also provided with an automatic cleaning head extending into the syrup preparation tank.
As a preferred technical solution, the water inlet pipe is connected to the water outlet circulation pipe through a first branch pipe.
As a preferred technical solution, the water inlet is connected to the water outlet circulation pipeline through a second branch pipeline.
As an optimized technical scheme, two ends of the sugar liquid outlet big valve are connected in parallel with a high-concentration syrup conveying branch pipe, the pipe diameter of the high-concentration syrup conveying branch pipe is smaller than that of the high-concentration syrup conveying pipeline, and a sugar liquid outlet small valve is installed on the high-concentration syrup conveying branch pipe.
By adopting the technical scheme, the utility model can automatically prepare the syrup with set percentage concentration in a short time, thereby improving the controllability and accuracy of the syrup preparation concentration; the utility model discloses do not need manual operation, degree of automation is high, has alleviateed workman's intensity of labour, has reduced the cost of labor.
The utility model discloses can carry out the allotment work of syrup in succession, the allotment time is short, and work efficiency is high, and the rare syrup after can effectual recycle uses has realized the recycle of resource, has saved the cost.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings needed to be used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to these drawings without inventive exercise.
Fig. 1 is a schematic structural diagram of an embodiment of the present invention;
FIG. 2 is a top view of the syrup blending tank of FIG. 1;
fig. 3 is an electrical wiring diagram of a PLC controller in an embodiment of the present invention;
in the figure: 1-dilute syrup recovery tank; 101-liquid inlet of recovery tank; 102-a recovery tank liquid outlet; 11-a recovery pipeline; 12-dilute syrup outlet pipe; 13-a liquid outlet valve of the recovery tank; 14-a window; 2-syrup preparation tank; 201-high concentration syrup inlet; 202-preparing a port; 203-a brix sensor interface; 204-preparing a tank liquid outlet; 21-high concentration syrup conveying pipe; 211-syrup pump; 212-a sugar liquid outlet big valve; 22-preparing a pipeline; 221-enter blending tank valve; 23-a water inlet pipe; 231-a water inlet valve; 232-a first subduct; 233-a second branch pipe; 24-dispensing tank liquid outlet pipeline; 241-out of a blending tank valve; 25-high concentration syrup conveying branch pipes; 251-a sugar liquid outlet small valve; 26-a window; 27-atmosphere communication hole; 28-manhole; 29-self-cleaning head; 3-syrup storage tank; 301-liquid inlet of storage tank; 302-a holding tank liquid outlet; 31-syrup inlet line; 32-inlet storage tank valve; 33-syrup outlet conduit; 34-outlet storage tank valve; 35-a window; 4-sugar degree sensor; 5-a liquid level sensor; 6-circulating pump; 61-a circulation pipeline; 62-a circulation pipeline; 63-circulation flow control valve.
Detailed Description
As shown in fig. 1 to 3, a fully automatic syrup preparation system comprises:
a thin syrup recovery tank 1 for retrieving after syrup uses, the top of thin syrup recovery tank 1 is equipped with the recovery tank inlet 101 of being connected with recovery pipeline 11, and the bottom of thin syrup recovery tank 1 is equipped with the recovery tank liquid outlet 102 that is used for exporting thin syrup, and recovery tank liquid outlet 102 is connected with thin syrup output pipeline 12, installs recovery tank liquid outlet valve 13 on the thin syrup output pipeline 12.
A syrup allotment jar 2 for syrup concentration allotment, the top of syrup allotment jar 2 is equipped with high concentration syrup inlet 201 and allotment mouth 202, and high concentration syrup inlet 201 passes through high concentration syrup pipeline 21 and is connected with high concentration syrup jar, installs syrup pump 211 on the high concentration syrup pipeline 21 and goes out sugar liquid big valve 212, and allotment mouth 202 is connected with allotment pipeline 22, installs on the allotment pipeline 22 and advances allotment jar valve 221. Two ends of the sugar liquid outlet big valve 212 are connected in parallel with high-concentration syrup conveying branch pipes 25, the pipe diameter of each high-concentration syrup conveying branch pipe 25 is smaller than that of the high-concentration syrup conveying pipeline 21, and a sugar liquid outlet small valve 251 is installed on each high-concentration syrup conveying branch pipe 25.
In this embodiment, the syrup pump 211 is a twin turbo syrup pump.
A syrup preparation tank liquid outlet 204 is arranged at the bottom of the syrup preparation tank 2, a sugar sensor 4 is arranged on a sugar sensor interface 203, a detection probe of the sugar sensor is communicated with a water inlet pipe 23, a water inlet valve 231 is arranged on the water inlet pipe 23, the syrup preparation tank liquid outlet 204 is connected with a preparation tank liquid outlet pipe 24, a preparation tank valve 241 is arranged on the preparation tank liquid outlet pipe 24, and a liquid level sensor 5 is also arranged on the syrup preparation tank 2, wherein in the embodiment, the liquid level sensor 5 is a differential pressure liquid level sensor.
A syrup holding vessel 3 for carrying out the syrup of storing with the ready syrup of allotment, the top of syrup holding vessel 3 is equipped with holding vessel inlet 301, the bottom of syrup holding vessel 3 is equipped with the holding vessel outlet 302 that is used for exporting the ready syrup of allotment, holding vessel inlet 301 is connected with syrup input pipeline 31, install into holding vessel valve 32 on the syrup input pipeline 31, holding vessel outlet 302 is connected with syrup output pipeline 33, install out holding vessel valve 34 on the syrup output pipeline 33.
And one end of the circulating pump 6 is connected with a circulating pipeline 61, the other end of the circulating pump 6 is connected with a circulating pipeline 62, a circulating flow control valve 63 is further installed on the circulating pipeline 62, the blending tank liquid outlet pipeline 24 and the dilute syrup output pipeline 12 are connected in parallel to the circulating pipeline 61, and the blending tank liquid outlet pipeline 24 and the syrup input pipeline 31 are connected in series with the circulating pipeline 62.
The water inlet pipe 23 is connected to the outlet circulation pipe 62 through a first branch pipe 232, the water inlet valve 231 and the sugar degree sensor interface 203 are connected to the outlet circulation pipe 62 through a second branch pipe 233, the first branch pipe 232 and the second branch pipe 233 are both provided with flow control valves, and when the water inlet valve 231 and the blending tank valve 241 are opened and the first branch pipe 232 and the second branch pipe 233 are communicated with the inlet circulation pipe 61, water enters the syrup blending tank 2 through the outlet circulation pipe 62.
The PLC controller, the sugar degree sensor 4 and the liquid level sensor 5 are electrically connected to the input port of the PLC controller, and the liquid outlet valve 13 of the recovery tank, the inlet blending tank valve 221, the water inlet valve 231, the outlet blending tank valve 241, the inlet storage tank valve 32, the circulating pump 6 and the syrup pump 211 are electrically connected to the output port of the PLC controller.
The sugar liquid outlet small valve 251 and the sugar liquid outlet large valve 212 are also electrically connected with the PLC and controlled by the PLC.
For the convenience of observation, all be equipped with the window on syrup blending tank 2 and the syrup holding vessel 3, set up window 14 on weak syrup recovery tank 1 respectively, set up window 26 on syrup blending tank 2, set up window 35 on syrup holding vessel 3.
In order to observe the position of the syrup, the number of the windows 14, 26 and 35 is two, and the windows are arranged up and down to observe the high and low liquid levels.
Wherein, the top of the syrup preparation tank 2 is provided with an atmosphere communication hole 27 and a manhole 28, and the top of the syrup preparation tank 2 is also provided with an automatic cleaning head 29 extending into the interior.
The working principle of the utility model is as follows:
when the production is started, the water inlet valve 231 is opened firstly to inject a certain amount of water for diluting the high-concentration sugar solution into the syrup preparation tank 2, the injection amount is detected by the liquid level sensor 5, when the injection amount reaches the set liquid level, the PLC outputs a control signal to close the water inlet valve 231, and the water injection is finished.
The PLC automatically opens a dispensing tank valve 241, a circulating pump 6 and a dispensing tank valve 221 of the syrup dispensing tank 2 to circulate the dilution water in the syrup dispensing tank 2, and simultaneously opens a twin-turbine sugar liquid pump 211 and a sugar liquid outlet big valve 212 to inject the high-concentration sugar liquid into the syrup dispensing tank 2. The sugar liquid concentration is detected by the sugar sensor 4 and sent to the PLC controller, when the sugar liquid concentration in the syrup preparation tank 2 is close to the set percentage concentration, the sugar liquid outlet big valve 212 is closed, meanwhile, the sugar liquid outlet small valve 251 is opened, and the high-concentration sugar liquid continuously enters the syrup preparation tank 2 through the sugar liquid outlet small valve 251. When the concentration of the syrup in the syrup preparation tank 2 reaches the set percentage concentration for use, the twin-turbine sugar liquid pump 211 and the sugar liquid outlet small valve 251 are closed, the sugar liquid inlet preparation tank valve 221 is closed, the sugar liquid inlet storage tank valve 32 is opened, and the prepared syrup is injected into the syrup storage tank 3 for production and use. The automatic blending of the next water and the high-concentration sugar solution is as above.
The concentration of the prepared syrup is reduced after the prepared syrup is used, and the prepared syrup can be recycled to the dilute syrup recycling tank 1. When a certain amount of dilute syrup is recovered, the dilute syrup is conveyed to the syrup blending tank 2 for blending by observing through the window 14, and the process is automatically controlled by a PLC (programmable logic controller). The method comprises the following steps: firstly, the liquid outlet valve 13 of the recovery tank and the valve 221 of the inlet blending tank are opened, the circulating pump 6 is opened, and the dilute syrup is injected into the syrup blending tank 2 through the dilute syrup outlet pipe 12, the inlet circulating pipe 61, the outlet circulating pipe 62 and the blending pipe 22.
The liquid level sensor 5 acquires the injection amount of the dilute syrup by detecting the liquid level of the syrup preparation tank 2, and when the injection of the dilute syrup reaches the set liquid level, the injection is finished, the liquid outlet valve 13 of the dilute syrup recovery tank is closed, and the preparation tank valve 241 is opened simultaneously, so that the dilute syrup circulates in the syrup preparation tank 2. And then the double-turbine sugar liquid pump 211 and the sugar liquid outlet small valve 251 are opened, the high-concentration sugar liquid is injected into the syrup preparation tank 2, and the injection amount and the syrup concentration are respectively detected by the liquid level sensor 5 and the sugar degree sensor 4. When the concentration of the syrup in the syrup preparation tank 2 reaches the set percentage concentration, the twin-turbine sugar liquid pump 211 and the sugar liquid outlet small valve 251 are closed, the sugar liquid inlet preparation tank valve 221 is closed, the sugar liquid inlet storage tank valve 32 is opened, and the prepared syrup is injected into the syrup storage tank 3 for production and use. During continuous production, the steps of automatically blending the next dilute syrup and the high-concentration sugar solution are the same as the above steps.
The utility model discloses in, the PLC controller is the controller commonly used in the industrial control, belong to prior art, therefore, technical personnel in the field can select the brand and the model of PLC controller according to the production needs, retrieve jar liquid valve 13, advance allotment jar valve 221, water intaking valve 231, go out allotment jar valve 241, advance holding vessel valve 32, circulating pump 6, syrup pump 211, go out the big valve of sugar liquid 212, go out the little valve 251 of sugar liquid and also be the electronic control component commonly used among the prior art, can realize the solenoid valve of above-mentioned its function among the prior art, the motorised valve all can regard as the utility model provides a retrieve jar liquid valve 13, advance allotment jar valve 221, water intaking valve 231, go out allotment jar valve 241, advance holding vessel valve 32, go out holding vessel valve 34, go out the big valve of sugar liquid 212, go out the control valve on the little valve 251 of sugar liquid and use.
Sugar degree sensor, level sensor and pump among the prior art all are applicable to the utility model discloses in.
In this embodiment, the PLC controller adopts OMRON C40P, and the PLC controller is electrically connected with the solenoid valve or the electrically operated valve to reach the electrical connection with the sugar degree sensor, the level sensor and the pump, according to the PLC controllers of different brands and models, technical personnel in the art can carry out the change of adjustability, and no longer repeated here.
The basic principles, main features and advantages of the present invention have been shown and described above. It will be understood by those skilled in the art that the present invention is not limited to the above embodiments, and that the foregoing embodiments and descriptions are provided only to illustrate the principles of the present invention without departing from the spirit and scope of the present invention. The scope of the invention is defined by the appended claims and equivalents thereof.
Claims (9)
1. A fully automatic syrup blending system, comprising:
the thin syrup recovery tank is used for recovering the used syrup, a recovery tank liquid inlet connected with a recovery pipeline is formed in the top of the thin syrup recovery tank, a recovery tank liquid outlet used for outputting the thin syrup is formed in the bottom of the thin syrup recovery tank, a thin syrup output pipeline is connected to the recovery tank liquid outlet, and a recovery tank liquid outlet valve is mounted on the thin syrup output pipeline;
the syrup mixing tank is used for mixing syrup concentration, a high-concentration syrup inlet and a mixing port are formed in the top of the syrup mixing tank, the high-concentration syrup inlet is connected with the high-concentration syrup tank through a high-concentration syrup conveying pipeline, a syrup pump and a syrup outlet big valve are mounted on the high-concentration syrup conveying pipeline, the mixing port is connected with a mixing pipeline, and a syrup inlet mixing tank valve is mounted on the mixing pipeline; the bottom of the syrup blending tank is provided with a water inlet and a blending tank liquid outlet, the water inlet is connected with a water inlet pipeline, the water inlet pipeline is provided with a water inlet valve, the blending tank liquid outlet is connected with a blending tank liquid outlet pipeline, the blending tank liquid outlet pipeline is provided with a blending tank valve, and the syrup blending tank is also provided with a sugar degree sensor and a liquid level sensor;
the syrup storage tank is used for storing the prepared syrup, a storage tank liquid inlet is formed in the top of the syrup storage tank, a storage tank liquid outlet for outputting the prepared syrup is formed in the bottom of the syrup storage tank, a syrup input pipeline is connected to the storage tank liquid inlet, a storage tank inlet valve is installed on the syrup input pipeline, a syrup output pipeline is connected to the storage tank liquid outlet, and a storage tank outlet valve is installed on the syrup output pipeline;
one end of the circulating pump is connected with a circulating inlet pipeline, the other end of the circulating pump is connected with a circulating outlet pipeline, a circulating control valve is further mounted on the circulating outlet pipeline, a liquid outlet pipeline of the blending tank and a dilute syrup output pipeline are connected to the circulating inlet pipeline in parallel, and a blending pipeline and a syrup input pipeline are connected to the circulating outlet pipeline in parallel;
the system comprises a PLC (programmable logic controller), wherein the sugar degree sensor and the liquid level sensor are electrically connected to an input port of the PLC, a liquid outlet valve of the recovery tank, a large sugar liquid outlet valve, a blending tank inlet valve, a water inlet valve, a blending tank outlet valve, a storage tank inlet valve, a storage tank outlet valve, a circulating pump and a sugar slurry pump are electrically connected to an output port of the PLC.
2. The fully automatic syrup preparation system according to claim 1, wherein: the syrup pump is a twin turbine syrup pump.
3. The fully automatic syrup preparation system according to claim 2, wherein: and windows are arranged on the dilute syrup recovery tank, the syrup blending tank and the syrup storage tank.
4. The fully automatic syrup preparation system according to claim 3, wherein: the window quantity on thin syrup recovery tank, syrup blending tank and the syrup holding vessel all is two, two windows set up from top to bottom.
5. The fully automatic syrup preparation system according to claim 1, wherein: the top of the syrup preparation tank is provided with an atmosphere communication hole and a manhole.
6. The fully automatic syrup preparation system according to claim 1, wherein: the top of the syrup preparation tank is also provided with an automatic cleaning head extending into the syrup preparation tank.
7. The fully automatic syrup preparation system according to claim 1, wherein: the water inlet pipeline is connected to the water outlet circulation pipeline through a first branch pipeline.
8. The fully automatic syrup preparation system according to claim 1, wherein: the water inlet is connected to the circulating outlet pipeline through a second branch pipeline.
9. The fully automatic syrup preparation system according to claim 1, wherein: and two ends of the sugar liquid outlet big valve are connected in parallel with high-concentration syrup conveying branch pipes, the pipe diameters of the high-concentration syrup conveying branch pipes are smaller than those of the high-concentration syrup conveying pipeline, and the sugar liquid outlet small valve is installed on the high-concentration syrup conveying branch pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921316120.7U CN210787259U (en) | 2019-08-14 | 2019-08-14 | Full-automatic syrup mixing system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921316120.7U CN210787259U (en) | 2019-08-14 | 2019-08-14 | Full-automatic syrup mixing system |
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| Publication Number | Publication Date |
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| CN210787259U true CN210787259U (en) | 2020-06-19 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201921316120.7U Active CN210787259U (en) | 2019-08-14 | 2019-08-14 | Full-automatic syrup mixing system |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110639424A (en) * | 2019-08-14 | 2020-01-03 | 诸城市中远机械有限公司 | A fully automatic syrup preparation system |
| CN118846947A (en) * | 2024-06-29 | 2024-10-29 | 中国船舶集团有限公司第七〇三研究所 | A fully automatic ethanol blending system and method |
-
2019
- 2019-08-14 CN CN201921316120.7U patent/CN210787259U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110639424A (en) * | 2019-08-14 | 2020-01-03 | 诸城市中远机械有限公司 | A fully automatic syrup preparation system |
| CN110639424B (en) * | 2019-08-14 | 2025-02-21 | 诸城市中远机械有限公司 | A fully automatic syrup mixing system |
| CN118846947A (en) * | 2024-06-29 | 2024-10-29 | 中国船舶集团有限公司第七〇三研究所 | A fully automatic ethanol blending system and method |
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