CN210846259U - Online blending device - Google Patents
Online blending device Download PDFInfo
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- CN210846259U CN210846259U CN201921294944.9U CN201921294944U CN210846259U CN 210846259 U CN210846259 U CN 210846259U CN 201921294944 U CN201921294944 U CN 201921294944U CN 210846259 U CN210846259 U CN 210846259U
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Abstract
The utility model discloses an online blending device, include: the device comprises a balance tank, wherein a mother liquor storage tank, a metering tank and a proportional tank are sequentially arranged above the balance tank from top to bottom, the mother liquor storage tank is connected with a mother liquor input pipe and a mother liquor output pipe, the mother liquor output pipe is communicated to the metering tank, the metering tank output pipe at the bottom of the metering tank is connected to the proportional tank, the proportional tank output pipe at the bottom of the proportional tank is communicated to the balance tank, a first water inlet pipe at the output end of a process water pipe is communicated to the proportional tank output pipe, a liquid outlet at the bottom of the balance tank is provided with a liquid outlet pipe, a backflow port at the upper end part of a tank body of the balance tank is connected with the liquid outlet pipe, the output end; the liquid outlet pipe is provided with a delivery pump and a check valve. The utility model has the advantages that: the structure is simple and reliable, the production cost is low, the uniformity of the prepared solution is good, and the on-line preparation can be realized.
Description
Technical Field
The utility model relates to a beverage filling equipment technical field, concretely relates to allotment device of liquid seal medium in beverage filling equipment.
Background
The rotary sterile filling machine is provided with a liquid seal groove, and a liquid seal medium is arranged in the liquid seal groove. The arrangement of the liquid seal groove separates the sterile environment and the non-sterile environment of the rotary sterile filling machine, thereby ensuring the reliability of the sterile environment. The allocation of the liquid seal medium in the liquid seal water tank needs to be measured by means of a flow meter, so that real-time online allocation can be realized, but the setting of the flow meter is high in cost, the quality of the allocated liquid seal medium is not good, and the allocation efficiency is low.
SUMMERY OF THE UTILITY MODEL
The utility model discloses the technical problem that needs to solve is: the on-line blending device is simple in structure and low in cost, and the blended solution is good in quality and high in blending efficiency.
In order to solve the above problem, the utility model adopts the following technical scheme: an online blending device, comprising: the device comprises a balance tank, wherein a mother liquor storage tank, a metering tank and a proportional tank are sequentially arranged above the balance tank from top to bottom, the mother liquor storage tank is connected with a mother liquor input pipe and a mother liquor output pipe, the mother liquor output pipe is communicated to the metering tank, the metering tank output pipe at the bottom of the metering tank is connected to the proportional tank, the proportional tank output pipe at the bottom of the proportional tank is communicated to the balance tank, the output end of a process water pipe communicated with a process water source is connected with a first water inlet pipe, the first water inlet pipe is communicated to the proportional tank output pipe, the bottom of the balance tank is provided with a liquid outlet, the upper end of the tank body of the balance tank is provided with a backflow port, the liquid outlet of the balance tank is provided with a liquid outlet pipe, the output end of the; the mother liquor input pipe, the mother liquor output pipe, the metering tank output pipe, the constant ratio tank output pipe, the first water inlet pipe, the return pipe and the output pipe are all provided with control valves, the liquid outlet pipe is provided with a delivery pump and a check valve, and the first water inlet pipe is communicated with the constant ratio tank output pipe between the control valve on the constant ratio tank output pipe and the bottom of the constant ratio tank.
Further, in the online blending device, a mother liquid tank level meter is arranged on the mother liquid tank.
Further, in the online blending device, a metering tank liquid level meter is arranged on the metering tank.
Further, aforementioned online blending device, wherein, be provided with the balance tank level gauge on the balance tank, be connected with the balance tank delivery pipe on the drain pipe between the liquid outlet of balance tank and the delivery pump, be provided with the bleeder valve on the balance tank delivery pipe.
Further, in the online blending device, the return pipe is provided with a first sampling valve.
Further, in the online blending device, a proportional tank sampling valve is further arranged on the proportional tank output pipe between the control valve on the proportional tank output pipe and the bottom of the proportional tank.
Further, aforementioned online blending device, wherein, the output of technology water pipe still is connected with the second inlet tube, and the second inlet tube communicates with the ball cleaner, the ball cleaner setting in the upper end of balance jar, be provided with second inlet tube control valve on the second inlet tube, second inlet tube control valve adopts the pneumatic valve.
Further, in the above online blending device, the control valves on the mother liquor input pipe, the mother liquor output pipe, the metering tank output pipe, the constant proportion tank output pipe, the first water inlet pipe, the return pipe and the output pipe are all pneumatic valves.
Further, aforementioned online blending device, wherein, be connected with the recovery pipeline on the jar body of compensating tank, be provided with control valve and second sample valve on the recovery pipeline, the last control valve of recovery pipeline adopts LL type pneumatic switching-over valve, is connected with the waste liquid outlet pipe on the LL type pneumatic switching-over valve.
Further, in the above on-line blending device, a gas discharge pipe with a valve is arranged at the top of the mother liquor storage tank.
The utility model has the advantages that: the structure is simple and reliable, the production cost is low, the uniformity of the prepared solution is good, and the on-line preparation can be realized, thereby providing reliable guarantee for the aseptic filling production.
Drawings
Fig. 1 is a schematic structural diagram of an online blending device according to the present invention.
Detailed Description
The invention will be described in further detail with reference to the drawings and preferred embodiments.
As shown in fig. 1, an on-line blending apparatus includes: the balance tank 1, in order to facilitate the monitoring of the liquid level in the balance tank 1, the bottom of the balance tank 1 is provided with a balance tank liquid level meter 101. The mother liquor storage tank 2, the metering tank 3 and the proportional tank 4 are sequentially arranged above the balance tank 1 from top to bottom.
The mother liquor storage tank 2 is connected with a mother liquor input pipe 21 and a mother liquor output pipe 22, and the top of the mother liquor storage tank 2 is provided with a gas discharge pipe 23. The gas discharge valve is provided for the purpose of: discharge the waste gas in the mother liquor storage tank 2, avoid 2 internal pressure of mother liquor storage tanks too high. In order to facilitate monitoring of the liquid level in the mother liquid storage tank 2, a mother liquid storage tank level gauge 201 is arranged in the mother liquid storage tank 2. Mother liquor output tube 22 communicates to metering tank 3, for the convenience of monitoring the liquid level in metering tank 3, is provided with metering tank level gauge 301 in metering tank 3. A metering tank output pipe 31 at the bottom of the metering tank 3 is connected to the constant ratio tank 4, and a constant ratio tank output pipe 41 at the bottom of the constant ratio tank 4 is connected to the equalizing tank 1. The output end of the process water pipe 5 communicated with the process water source is connected with a first water inlet pipe 6, and the first water inlet pipe 6 is communicated to an output pipe 41 of the constant-ratio tank.
The bottom of compensating tank 1 is provided with liquid outlet 11, and the upper end of the 1 jar of body of compensating tank is provided with backward flow mouth 12, and the liquid outlet 11 of compensating tank 1 is connected with drain pipe 111, and the output of drain pipe 111 is connected with back flow 7 and output tube 8, and the liquid in compensating tank 1 is outwards exported to output tube 8, and back flow 7 is connected to the backward flow mouth 12 of compensating tank 1, is provided with first sample valve 71 on the back flow 7. The liquid outlet pipe 111 is provided with a delivery pump 112 and a check valve 113. In this embodiment, a balance tank discharge pipe 115 is connected to the liquid outlet pipe 111 between the liquid outlet 11 of the balance tank 1 and the delivery pump 112, and a discharge valve 114 is disposed on the balance tank discharge pipe 115. In addition, be connected with recovery pipeline 13 on the jar body of compensating tank 1, be provided with control valve and second sample valve 132 on recovery pipeline 13, for the convenience of connecting, be provided with the control valve on recovery pipeline 13 and adopt LL type pneumatic switching-over valve 131, be connected with waste liquid outlet pipe 133 on LL type pneumatic switching-over valve 131.
Control valves are arranged on the mother liquor input pipe 21, the mother liquor output pipe 22, the metering tank output pipe 31, the constant ratio tank output pipe 41, the first water inlet pipe 6, the return pipe 7 and the output pipe 8, and the control valves are pneumatic valves. Specifically, in the present embodiment, the first pneumatic valve 211 is disposed on the mother liquor input pipe 21, the second pneumatic valve 221 is disposed on the mother liquor output pipe 22, the third pneumatic valve 311 is disposed on the metering tank output pipe 31, the fourth pneumatic valve 411 is disposed on the comparing tank output pipe 41, the fifth pneumatic valve 61 is disposed on the first water inlet pipe 6, the sixth pneumatic valve 711 is disposed on the return pipe 7, and the seventh pneumatic valve 81 is disposed on the output pipe 8. For the convenience of control, the first inlet pipe 6 in this embodiment is connected to the fixed ratio tank outlet pipe 41 between the fourth pneumatic valve 411 on the fixed ratio tank outlet pipe 41 and the bottom of the fixed ratio tank 4. A fixed ratio tank sampling valve 401 is also arranged on the fixed ratio tank output pipe 41 between the fourth pneumatic valve 411 on the fixed ratio tank output pipe 41 and the bottom of the fixed ratio tank 4.
In this embodiment, the output end of the process water pipe 5 is further connected with a second water inlet pipe 9, the second water inlet pipe 9 is communicated with a cleaning ball 92 with a plurality of nozzles, the cleaning ball 92 is arranged at the upper end part in the balancing tank 1, a second water inlet pipe control valve 91 is arranged on the second water inlet pipe 9, and the second water inlet pipe control valve 91 also adopts a pneumatic valve.
The working principle is as follows: deposit the required mother liquor that is used for allotment liquid seal medium solution in the mother liquor storage tank 2, set up high, well, low three liquid level in the mother liquor storage tank 2 usually, the liquid level in the mother liquor storage tank 2 of mother liquor storage tank level gauge 201 real-time supervision, in case when finding the liquid level in the mother liquor storage tank 2 and being less than high liquid level, first pneumatic valve 211 on the mother liquor input tube 21 will open and supply the mother liquor, ensure that the liquid level in the mother liquor storage tank 2 keeps at high liquid level, thereby make full preparation for the allotment of liquid seal medium solution.
The liquid level in the compensating tank 1 of compensating tank 1 bottom real-time supervision compensating tank level gauge 101, compensating tank 1 also is provided with high, well, low three liquid level, in the allotment course of operation of liquid seal medium solution, when compensating tank level gauge 101 detects the liquid level in compensating tank 1 and is low liquid level, the allotment work of liquid seal medium solution is started, when compensating tank level gauge 101 detects the liquid level in compensating tank 1 and is high liquid level, the allotment work stops.
The blending steps are as follows: first, the second air-operated valve 221 is opened, the mother liquid in the mother liquid tank 2 enters the metering tank 3, and when the metering tank level meter 301 detects that the liquid level in the metering tank 3 reaches a set value, the second air-operated valve 221 is closed.
Then, the third pneumatic valve 311 on the output pipe 31 of the metering tank is opened, the mother liquor in the metering tank 3 enters the constant ratio tank 4, when the metering tank liquid level meter 301 detects that no liquid level display exists in the metering tank 3, it indicates that all the mother liquor in the metering tank 3 enters the constant ratio tank 4, at this time, the fifth pneumatic valve 61 is opened, so that the process water is added into the constant ratio tank 4 through the first water inlet pipe 6, when the constant ratio tank liquid level meter 42 detects that the liquid level reaches a set value, the process water in the constant ratio tank 4 is added to the amount required by blending, at this time, the fifth pneumatic valve 61 is closed, and the constant ratio tank 4 completes the work of once blending. In order to ensure that the concentration of the solution in the constant ratio tank 1 satisfies the requirement, the constant ratio tank sampling valve 401 is opened and the judgment is made by sampling detection.
Then, the fourth pneumatic valve 411 of the constant ratio tank outlet pipe 41 is opened, and the liquid in the constant ratio tank 4 enters the equilibrium tank 1. The above-mentioned step is repeated constantly, and when the liquid level in the balance tank 1 reached well liquid level when balance tank level gauge 101 detected, delivery pump 112 started, and sixth pneumatic valve 711 opened simultaneously, the liquid in the balance tank 1 will be under delivery pump 112's pumping, constantly through drain pipe 111 outflow, in the reflux pipe 7 backward flow arrives balance tank 1 again to constantly carry out the self-loopa, the purpose of self-loopa lies in: the uniformity of the solution is improved. When the balance tank liquid level meter 101 detects that the liquid level in the balance tank 1 reaches a high liquid level, the blending work is ended. The sixth pneumatic valve 711 is closed and the seventh pneumatic valve 81 is opened so that the solution in the equalization tank 1 can be transported out through the outlet conduit 8 to the rotary aseptic filling machine for use as a liquid seal medium.
Because the recovery pipeline 13 is connected to the tank body of the balance tank 1, the recovery pipeline 13 is connected with the rotary type aseptic filling machine, after the rotary type aseptic filling machine 10 finishes filling work, the liquid seal medium solution in the rotary type aseptic filling machine 10 can be discharged out of the rotary type aseptic filling machine through the recovery pipeline 13, sampling detection is carried out at the second sampling valve 132, each component of the liquid seal medium solution in the recovery pipeline 13 meets the requirement of recoverability, the liquid seal medium solution in the rotary type aseptic filling machine 10 returns to the balance tank 1 through the recovery pipeline 13, the purpose of recovery and reutilization is achieved, and cost is effectively saved. When the liquid seal medium solution in the recovery pipeline 13 is detected, the indexes of all the components do not reach the recoverable requirement, and the liquid seal medium solution in the rotary sterile filling machine is discharged outwards through the recovery pipeline 13, the LL-type pneumatic reversing valve 131 and the waste liquid outlet pipe 133 in sequence.
When the balance tank 1 needs to be cleaned, liquid in the balance tank 1 is firstly drained through the drain valve 114, when the balance tank liquid level meter 101 detects that the liquid level in the balance tank 1 reaches a low liquid level, the drain valve 114 is closed, at the moment, the second water inlet pipe control valve 91 is opened, so that process water enters the cleaning ball 92 through the second water inlet pipe 9, the process water in the cleaning ball 92 sprays and washes the balance tank 1, when the balance tank liquid level meter 101 detects that the liquid level in the balance tank 1 reaches a medium liquid level, the conveying pump 112 and the sixth pneumatic valve 711 are opened, so that self-circulation cleaning can be carried out, after cleaning for a period of time, the liquid in the balance tank 1 is discharged through the drain valve 114, and after the balance tank liquid level meter 101 detects that the liquid level in the balance tank 1 is a low liquid level, the drain valve 114 is closed in a delayed manner, so as to ensure that the liquid in the balance tank.
The utility model has the advantages that: the structure is simple and reliable, the production cost is low, the uniformity of the prepared solution is good, and the on-line preparation can be realized, thereby providing reliable guarantee for the aseptic filling production. The blending device has wide application range and can be applied to solution blending in the fields of beverages, chemical industry, pharmacy and the like.
Claims (10)
1. An online blending device, comprising: the surge tank, its characterized in that: a mother liquor storage tank, a metering tank and a proportional tank are sequentially arranged above the balancing tank from top to bottom, a mother liquor input pipe and a mother liquor output pipe are connected onto the mother liquor storage tank, the mother liquor output pipe is communicated to the metering tank, a metering tank output pipe at the bottom of the metering tank is connected to the proportional tank, a proportional tank output pipe at the bottom of the proportional tank is communicated to the balancing tank, the output end of a process water pipe communicated with a process water source is connected with a first water inlet pipe, the first water inlet pipe is communicated to a proportional tank output pipe, a liquid outlet is arranged at the bottom of the balancing tank, a backflow port is arranged at the upper end of the tank body of the balancing tank, a liquid outlet pipe is arranged at the liquid outlet of the balancing tank, the output end of the liquid outlet pipe is connected; the mother liquor input pipe, the mother liquor output pipe, the metering tank output pipe, the constant ratio tank output pipe, the first water inlet pipe, the return pipe and the output pipe are all provided with control valves, the liquid outlet pipe is provided with a delivery pump and a check valve, and the first water inlet pipe is communicated with the constant ratio tank output pipe between the control valve on the constant ratio tank output pipe and the bottom of the constant ratio tank.
2. The on-line blending device of claim 1, wherein: a mother liquid storage tank liquid level meter is arranged on the mother liquid storage tank.
3. The on-line blending device of claim 1, wherein: the metering tank is provided with a metering tank liquid level meter.
4. The on-line blending device of claim 1, wherein: the balance tank is provided with a balance tank liquid level meter, a balance tank discharge pipe is connected to a liquid outlet pipe between the liquid outlet of the balance tank and the delivery pump, and a discharge valve is arranged on the balance tank discharge pipe.
5. The on-line blending device of claim 1, wherein: the return pipe is provided with a first sampling valve.
6. The on-line blending device of claim 1, wherein: and a constant-ratio tank sampling valve is also arranged on the constant-ratio tank output pipe between the control valve on the constant-ratio tank output pipe and the bottom of the constant-ratio tank.
7. The on-line blending device of claim 1, wherein: the output end of the process water pipe is also connected with a second water inlet pipe, the second water inlet pipe is communicated with a cleaning ball, the cleaning ball is arranged at the upper end part in the balancing tank, a second water inlet pipe control valve is arranged on the second water inlet pipe, and the second water inlet pipe control valve adopts a pneumatic valve.
8. The on-line blending device of claim 1, wherein: the mother liquor input pipe, the mother liquor output pipe, the metering tank output pipe, the constant proportion tank output pipe, the first water inlet pipe, the backflow pipe and the control valves on the output pipe are all pneumatic valves.
9. The on-line blending device of claim 1, wherein: the tank body of the balance tank is connected with a recovery pipeline, a control valve and a second sampling valve are arranged on the recovery pipeline, the control valve on the recovery pipeline adopts an LL-type pneumatic reversing valve, and a waste liquid outlet pipe is connected on the LL-type pneumatic reversing valve.
10. The on-line blending device of claim 1, wherein: the top of the mother liquid storage tank is provided with a gas discharge pipe with a valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921294944.9U CN210846259U (en) | 2019-08-12 | 2019-08-12 | Online blending device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921294944.9U CN210846259U (en) | 2019-08-12 | 2019-08-12 | Online blending device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210846259U true CN210846259U (en) | 2020-06-26 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921294944.9U Active CN210846259U (en) | 2019-08-12 | 2019-08-12 | Online blending device |
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| Country | Link |
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| CN (1) | CN210846259U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110479181A (en) * | 2019-08-12 | 2019-11-22 | 江苏新美星包装机械股份有限公司 | A kind of online deployment device |
-
2019
- 2019-08-12 CN CN201921294944.9U patent/CN210846259U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110479181A (en) * | 2019-08-12 | 2019-11-22 | 江苏新美星包装机械股份有限公司 | A kind of online deployment device |
| CN110479181B (en) * | 2019-08-12 | 2024-04-09 | 江苏新美星包装机械股份有限公司 | Online allocation device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20220402 Address after: 215600 South District of Zhangjiagang Economic Development Zone, Suzhou City, Jiangsu Province (Xinjing East Road) Patentee after: Jiangsu xinmeixing Industrial Research Institute Co.,Ltd. Address before: 215600 Jiangsu xinmeixing Packaging Machinery Co., Ltd., Xinjing East Road, South District, Zhangjiagang Economic Development Zone, Suzhou City, Jiangsu Province Patentee before: JIANGSU NEWAMSTAR PACKAGING MACHINERY Co.,Ltd. |
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| TR01 | Transfer of patent right |