CN217795643U - Online sugar dissolving device - Google Patents
Online sugar dissolving device Download PDFInfo
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- CN217795643U CN217795643U CN202122375809.0U CN202122375809U CN217795643U CN 217795643 U CN217795643 U CN 217795643U CN 202122375809 U CN202122375809 U CN 202122375809U CN 217795643 U CN217795643 U CN 217795643U
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Abstract
The utility model relates to the technical field of sugar dissolving devices, in particular to an online sugar dissolving device, which comprises a dissolving and stirring tank, a temporary storage tank, a water-powder mixer, a first water inlet branch pipe communicated with the dissolving and stirring tank and a flowmeter connected with the first water inlet branch pipe; a dissolving discharge pipe is arranged at a discharge port at the bottom of the dissolving and stirring tank; the output end of the first centrifugal pump is connected with a front discharge pipe and a front return pipe; a water outlet of the gouache mixer is communicated with a rear material return pipe; the outlet at the bottom of the temporary storage tank is connected with a second centrifugal pump; a feed back stop valve is arranged on the front feed back pipe; the front discharging pipe is provided with a discharging stop valve. Use the utility model discloses the time, this structure realizes the automation of syrup through forming the circulating line and dissolves for the syrup is more even, passes through the accurate water injection of flowmeter moreover, makes syrup sugariness obtain guaranteeing.
Description
Technical Field
The utility model relates to a dissolve sugared technical field, in particular to online dissolve sugared device.
Background
The sugar is dissolved by putting weighed sugar and a certain amount of water into a stirring container according to a certain proportion until the sugar is completely dissolved in the water. Because the stirring rake can't reach in the agitator tank, so the sugar of agitator tank bottom is difficult to dissolve, and some impurity that goes into along with the sugar can remain in the bottom of agitator tank in addition, is discharged at first when the syrup is used, influences the quality of product.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide an online dissolve sugar device that can obtain more even syrup to prior art's defect and not enough.
In order to achieve the above object, the utility model adopts the following technical scheme:
the utility model relates to an online sugar dissolving device, which comprises a dissolving and stirring tank, a temporary storage tank, a water-powder mixer, a first water inlet branch pipe communicated with the dissolving and stirring tank and a flowmeter connected with the first water inlet branch pipe; a dissolving discharge pipe is arranged at a discharge port at the bottom of the dissolving and stirring tank; the dissolving discharge pipe is connected with a first centrifugal pump; the output end of the first centrifugal pump is connected with a front discharging pipe and a front returning pipe;
a water inlet of the water-powder mixer is communicated with the front material return pipe; a water outlet of the gouache mixer is communicated with a rear material return pipe; the rear material return pipe is communicated with the dissolving and stirring tank; a powder inlet of the water-powder mixing machine is connected with a feed hopper;
the front discharging pipe is connected to the temporary storage tank; the outlet at the bottom of the temporary storage tank is connected with a second centrifugal pump; a feed back stop valve is arranged on the front feed back pipe; the front discharging pipe is provided with a discharging stop valve.
Further, a discharge filter is arranged on the front discharge pipe; the discharge filter is arranged in the discharge direction of the discharge stop valve; and a feed back filter is arranged on the rear feed back pipe.
Furthermore, the outer surface of the dissolving and stirring tank is wrapped with an insulating layer.
Further, a first drain pipe is connected to the dissolving discharge pipe; the outlet at the bottom of the temporary storage tank is connected with a second sewage discharge pipe; the first sewage discharge pipe and the second sewage discharge pipe are both provided with stop valves; the top of the dissolving and stirring tank is communicated with a second water inlet branch pipe; the top of the temporary storage tank is communicated with a third water inlet branch pipe.
After the structure is adopted, the utility model discloses beneficial effect does: the utility model relates to an online sugar dissolving device, which comprises a dissolving and stirring tank, a temporary storage tank, a water-powder mixer, a first water inlet branch pipe communicated with the dissolving and stirring tank and a flowmeter connected with the first water inlet branch pipe; a dissolving discharge pipe is arranged at a discharge port at the bottom of the dissolving and stirring tank; the dissolving discharge pipe is connected with a first centrifugal pump; the output end of the first centrifugal pump is connected with a front discharge pipe and a front return pipe; the water inlet of the water-powder mixer is communicated with the front feed back pipe; a water outlet of the gouache mixer is communicated with a rear material return pipe; the rear material return pipe is communicated with the dissolving and stirring tank; a powder inlet of the water-powder mixer is connected with a feed hopper; the front discharging pipe is communicated with the temporary storage tank; the outlet at the bottom of the temporary storage tank is connected with a second centrifugal pump; a feed back stop valve is arranged on the front feed back pipe; the front discharging pipe is provided with a discharging stop valve. When the utility model is used, sugar materials are manually put into the feed hopper, the main water inlet pipe injects water with the temperature of the temperature into the dissolving and stirring tank through the first water inlet branch pipe, the water inlet quantity is set by the flow meter after the water consumption matched with the corresponding sugar materials is calculated, and the water injection quantity entering the dissolving and stirring tank is accurately controlled by the flow meter; closing the discharge stop valve, and opening the feed back stop valve; water enters the inside of the water-powder mixing machine through the dissolving discharge pipe, the first centrifugal pump and the front feed back pipe and is mixed with sugar falling into the water-powder mixing machine under the action of gravity through the feed hopper to form syrup solution. The syrup solution flows back to the dissolving and stirring tank through a back material return pipe to form circulation until the sugar is completely dissolved; the discharge stop valve is opened, the feed back stop valve is closed, and the first centrifugal pump pumps the syrup from the dissolving and stirring tank into the temporary storage tank for later use through the front discharge pipe; in the temporary storage tank, the syrup can be continuously stirred; when syrup needs to be used, the valve body at the bottom of the temporary storage tank is opened, and the second centrifugal pump discharges the syrup from the discharge pipe; pumping residual syrup in the discharge pipe into a temporary storage tank again through a slurry supply return pipe; this structure realizes the automation of syrup through forming circulating line and dissolves for the syrup is more even, passes through the accurate water injection of flowmeter moreover, makes syrup sweetness obtain guaranteeing.
Drawings
Fig. 1 is a schematic structural diagram of the present invention;
FIG. 2 is a schematic view showing a structure of a circulating line for dissolving sugar;
description of the reference numerals:
1. a main water inlet pipe; 2. a flow meter; 3. a first water inlet branch pipe; 4. a dissolving and stirring tank;
5. dissolving a discharge pipe; 6. a first centrifugal pump; 7. a feed back stop valve; 8. a discharge stop valve;
9. a discharge filter; 10. a front discharging pipe; 11. a second centrifugal pump; 12. a temporary storage tank;
13. a slurry supply and return pipe; 14. a third water inlet branch pipe; 15. a second water inlet branch pipe;
16. a front feed back pipe; 17. a water-powder mixer; 18. a feed hopper; 19. a feed back filter;
20. a rear material return pipe; 21. a first drain pipe; 22. a second sewage draining pipe.
Detailed Description
The present invention will be further described with reference to the accompanying drawings.
As shown in fig. 1 to 2, the on-line sugar dissolving device of the present invention comprises a dissolving and stirring tank 4, a temporary storage tank 12, a water-powder mixer 17, a first water inlet branch pipe 3 connected to the dissolving and stirring tank 4, and a flow meter 2 connected to the first water inlet branch pipe 3; a dissolving discharge pipe 5 is arranged at a discharge port at the bottom of the dissolving and stirring tank 4; the dissolving discharge pipe 5 is connected with a first centrifugal pump 6; the output end of the first centrifugal pump 6 is connected with a front discharge pipe 10 and a front return pipe 16;
the water inlet of the water-powder mixer 17 is communicated with the front feed back pipe 16; the water outlet of the gouache mixer 17 is communicated with a rear material return pipe 20; the rear material return pipe 20 is communicated with the dissolving and stirring tank 4; a powder inlet of the water-powder mixer 17 is connected with a feed hopper 18;
the front discharging pipe 10 is connected on the temporary storage tank 12; the outlet at the bottom of the temporary storage tank 12 is connected with a second centrifugal pump 11; a feed back stop valve 7 is arranged on the front feed back pipe 16; a discharge stop valve 8 is arranged on the front discharge pipe 10; the water-powder mixer 17 is not essentially different from the prior art, and thus is not described in detail;
the sugar is manually put into the feed hopper 18, the main water inlet pipe 1 injects 93 ℃ water into the dissolving and stirring tank 4 through the first water inlet branch pipe 3, the water inflow is set through the flow meter 2 after the water consumption matched with the corresponding sugar is calculated, and the water injection amount entering the dissolving and stirring tank 4 is accurately controlled through the flow meter 2; the discharge stop valve 8 is closed, and the feed back stop valve 7 is opened; water enters the inside of the water-powder mixer 17 through the dissolving discharge pipe 5, the first centrifugal pump 6 and the front feed back pipe 16 and is mixed with sugar falling into the water-powder mixer 17 by the feed hopper 18 under the action of gravity to form syrup solution. The syrup solution flows back to the dissolving and stirring tank 4 through a back material return pipe 20 to form circulation until the sugar is completely dissolved;
the discharge stop valve 8 is opened, the feed back stop valve 7 is closed, and the first centrifugal pump 6 pumps the syrup from the dissolving and stirring tank 4 into the temporary storage tank 12 through the front discharge pipe 10 for standby; in the temporary storage tank 12, the syrup is continuously stirred; when syrup needs to be used, the valve body at the bottom of the temporary storage tank 12 is opened, and the second centrifugal pump 11 discharges the syrup from the discharge pipe; pumping residual syrup in the discharge pipe into the temporary storage tank 12 through a syrup supply return pipe 13; this structure realizes the automation of syrup through forming circulation pipeline and dissolves for the syrup is more even, through the accurate water injection of flowmeter 2 moreover, makes syrup sweetness obtain guaranteeing.
As a preferred mode of the present invention, a discharging filter 9 is disposed on the front discharging pipe 10; the discharge filter 9 is arranged in the discharge direction of the discharge stop valve 8; a feed back filter 19 is arranged on the rear feed back pipe 20; the liquid passing through the circulating pipeline can be filtered and separated from slag through the feed back filter 19; the discharging filter 9 further filters the syrup entering the temporary storage tank 12, thereby improving the purity of the syrup.
As a preferred mode of the utility model, the outer surface of the dissolving and stirring tank 4 is wrapped with a heat-insulating layer; because the temperature of water for dissolving sugar material is higher, set up the heat preservation and can effectively reduce energy loss, guarantee the dissolution efficiency of sugar material.
As a preferred mode of the utility model, the dissolving and discharging pipe 5 is connected with a first discharging pipe 21; the outlet at the bottom of the temporary storage tank 12 is connected with a second sewage discharge pipe 22; the first sewage discharge pipe 21 and the second sewage discharge pipe 22 are both provided with stop valves; the top of the dissolving and stirring tank 4 is communicated with a second water inlet branch pipe 15; the top of the temporary storage tank 12 is communicated with a third water inlet branch pipe 14;
when the dissolving and stirring tank 4, the temporary storage tank 12 and pipelines thereof do not need to be cleaned, the stop valves on the second water inlet branch pipe 15 and the third water inlet branch pipe 14 are closed; when the dissolving and stirring tank 4 needs to be cleaned, water entering the second water inlet branch pipe 15 from the main water inlet pipe 1 enters the dissolving and stirring tank 4, the dissolving and discharging pipe 5, the first centrifugal pump 6, the front material return pipe 16, the water-powder mixer 17 and the rear material return pipe 20, and then the pipe is connected with the pipe Lu Qingli; then the material return stop valve 7 and the material discharge stop valve 8 are closed, the stop valve on the first sewage discharge pipe 21 is opened, and the wastewater is discharged from the first sewage discharge pipe 21; water entering the third water inlet branch pipe 14 from the main water inlet pipe 1 enters the temporary storage tank 12, and then the stop valve on the two sewage discharge pipes 22 is opened to discharge sewage to the temporary storage tank 12.
When the utility model is used, sugar materials are manually put into the feed hopper, the main water inlet pipe injects water with the temperature of the temperature into the dissolving and stirring tank through the first water inlet branch pipe, the water inlet quantity is set by the flow meter after the water consumption matched with the corresponding sugar materials is calculated, and the water injection quantity entering the dissolving and stirring tank is accurately controlled by the flow meter; closing the discharge stop valve, and opening the feed back stop valve; water enters the inside of the water-powder mixing machine through the dissolving discharge pipe, the first centrifugal pump and the front feed back pipe and is mixed with sugar falling into the water-powder mixing machine under the action of gravity through the feed hopper to form syrup solution. The syrup solution flows back to the dissolving and stirring tank through a back material return pipe to form circulation until the sugar is completely dissolved; the discharge stop valve is opened, the feed back stop valve is closed, and the first centrifugal pump pumps the syrup from the dissolving and stirring tank into the temporary storage tank for later use through the front discharge pipe; in the temporary storage tank, the syrup can be continuously stirred; when syrup needs to be used, the valve body at the bottom of the temporary storage tank is opened, and the second centrifugal pump discharges the syrup from the discharge pipe; pumping residual syrup in the discharge pipe into a temporary storage tank again through a slurry supply return pipe; according to the structure, the syrup is automatically dissolved by forming the circulating pipeline, so that the syrup is more uniform, and the syrup sweetness is ensured by accurately injecting water through the flow meter; the liquid passing through the circulating pipeline can be filtered and separated from slag through the feed back filter 19; the discharging filter 9 further filters the syrup entering the temporary storage tank 12, thereby improving the purity of the syrup. When the dissolving and stirring tank, the temporary storage tank and pipelines thereof do not need to be cleaned, the stop valves on the second water inlet branch pipe and the third water inlet branch pipe are closed; when the dissolving and stirring tank needs to be cleaned, water entering the second water inlet branch pipe from the main water inlet pipe enters the dissolving and stirring tank, the dissolving and discharging pipe, the first centrifugal pump, the front feed back pipe, the water powder mixer and the rear feed back pipe Lu Qingli; then the feed back stop valve and the discharge stop valve are closed, the stop valve on the first sewage discharge pipe is opened, and the wastewater is discharged from the first sewage discharge pipe; the water entering the third water inlet pipe from the main water inlet pipe enters the temporary storage tank, and then the stop valves on the two drain pipes are opened to drain the temporary storage tank.
The above is only the preferred embodiment of the present invention, so all the equivalent changes or modifications made by the structure, features and principles in accordance with the claims of the present invention are included in the claims of the present invention.
Claims (4)
1. An online dissolve sugared device which characterized in that: the device comprises a dissolving and stirring tank (4), a temporary storage tank (12), a water-powder mixer (17), a first water inlet branch pipe (3) communicated with the dissolving and stirring tank (4) and a flowmeter (2) connected to the first water inlet branch pipe (3); a dissolving discharge pipe (5) is arranged at a discharge port at the bottom of the dissolving and stirring tank (4); the dissolving discharge pipe (5) is connected with a first centrifugal pump (6); the output end of the first centrifugal pump (6) is connected with a front discharge pipe (10) and a front return pipe (16);
a water inlet of the water-powder mixer (17) is communicated with the front material return pipe (16); a water outlet of the gouache mixer (17) is communicated with a rear material return pipe (20); the rear material return pipe (20) is communicated with the dissolving and stirring tank (4); a powder inlet of the water-powder mixer (17) is connected with a feed hopper (18);
the front discharging pipe (10) is communicated with the temporary storage tank (12); the bottom outlet of the temporary storage tank (12) is connected with a second centrifugal pump (11); a feed back stop valve (7) is arranged on the front feed back pipe (16); a material discharge stop valve (8) is arranged on the front material discharge pipe (10).
2. An on-line sugar dissolving device as claimed in claim 1, wherein: a discharge filter (9) is arranged on the front discharge pipe (10); the discharge filter (9) is arranged in the discharge direction of the discharge stop valve (8); and a feed back filter (19) is arranged on the rear feed back pipe (20).
3. An on-line sugar dissolving device as claimed in claim 1, wherein: the outer surface of the dissolving and stirring tank (4) is wrapped with a heat-insulating layer.
4. An on-line sugar dissolving device as claimed in claim 1, wherein: the dissolving and discharging pipe (5) is connected with a first sewage discharging pipe (21); the outlet at the bottom of the temporary storage tank (12) is connected with a second sewage discharge pipe (22); the first sewage discharge pipe (21) and the second sewage discharge pipe (22) are both provided with stop valves; the top of the dissolving and stirring tank (4) is communicated with a second water inlet branch pipe (15); the top of the temporary storage tank (12) is communicated with a third water inlet pipe (14).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122375809.0U CN217795643U (en) | 2021-09-29 | 2021-09-29 | Online sugar dissolving device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122375809.0U CN217795643U (en) | 2021-09-29 | 2021-09-29 | Online sugar dissolving device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN217795643U true CN217795643U (en) | 2022-11-15 |
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ID=83959235
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202122375809.0U Active CN217795643U (en) | 2021-09-29 | 2021-09-29 | Online sugar dissolving device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN217795643U (en) |
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2021
- 2021-09-29 CN CN202122375809.0U patent/CN217795643U/en active Active
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