CN209143655U - A kind of control system of bottle placer back pressure - Google Patents
A kind of control system of bottle placer back pressure Download PDFInfo
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- CN209143655U CN209143655U CN201821719904.XU CN201821719904U CN209143655U CN 209143655 U CN209143655 U CN 209143655U CN 201821719904 U CN201821719904 U CN 201821719904U CN 209143655 U CN209143655 U CN 209143655U
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Abstract
The utility model relates to aseptic filling technology fields, disclose a kind of control system of bottle placer back pressure, and the control system of bottle placer back pressure includes sterile material tank, and sterile material tank is connected with air inlet pipe and exhaust pipe；It further include constant pressure valve, aeration ratio regulating valve, exhaust ratio regulating valve, pressure-detecting device and controller；Constant pressure valve is set in air inlet pipe；Aeration ratio regulating valve is set in air inlet pipe；Exhaust ratio regulating valve is set on exhaust pipe；Pressure-detecting device is able to detect the pressure of the sterile back pressure gas in sterile material tank；Aeration ratio regulating valve, exhaust ratio regulating valve and pressure-detecting device are electrically connected with the controller.Constant pressure valve carries out preliminarily stabilised to the pressure of air inlet pipe, pressure-detecting device detects the pressure of the sterile back pressure gas in sterile material tank, feed back to controller, controller controls to adjust the aperture of aeration ratio regulating valve or exhaust ratio regulating valve according to detected value, guarantees the stability of the pressure of sterile back pressure gas.
Description
Technical field
The utility model relates to aseptic filling technology field more particularly to a kind of control systems of bottle placer back pressure
Background technique
In beverage aseptic filling process, to ensure sterile material (product) not by outside contamination, it is necessary to sterile material
Tank carries out positive pressure protection, and the sterile gas of certain pressure is usually passed through on sterile material tank, is made by sterile back pressure gas sterile
Material pressure inside the tank is always maintained at greater than sterile material tank external pressure, prevents environmental contaminants from entering in sterile material tank, protection
Gnotobasis is not destroyed in tank.
But the pressure stability of sterile back pressure gas is difficult to control.It will affect filling flow velocity, fluid column stream when pressure is excessive
State, especially some sterile materials easy to foaming, can largely blister, or even emerge from bottleneck in pouring process.One side shadow
Filling accuracy is rung, on the other hand easily causes bottleneck material residual exceeded；Furthermore if sterile material full of nutrition, such as soymilk
Equal neutral beverages, finally fall on board after emerging from bottleneck, easily lead to bacteria breed, the wind for bringing gnotobasis to destroy
Danger.When pressure is too small, then gnotobasis may lose in sterile material tank.
Therefore, a kind of control system of bottle placer back pressure is needed, to solve the above technical problems.
Utility model content
The purpose of this utility model is that proposing a kind of control system of bottle placer back pressure, can adjust in sterile material tank
Sterile back pressure gas pressure, guarantee the stability of the pressure of sterile back pressure gas.
For this purpose, one of the technical solution adopted in the utility model are as follows:
A kind of control system of bottle placer back pressure, including sterile material tank, sterile material tank are connected with air inlet pipe and exhaust
Pipe；
Constant pressure valve is set in the air inlet pipe；
Aeration ratio regulating valve is set in the air inlet pipe；
Exhaust ratio regulating valve is set on the exhaust pipe；
Pressure-detecting device is able to detect the pressure of the sterile back pressure gas in the sterile material tank；
Controller, the aeration ratio regulating valve, the exhaust ratio regulating valve and the pressure-detecting device are and institute
State controller electrical connection.
Constant pressure valve carries out preliminarily stabilised to the pressure of air inlet pipe, and pressure-detecting device detects the sterile back in sterile material tank
The pressure calmed the anger feeds back to controller, and controller controls to adjust aeration ratio regulating valve according to detected value or exhaust ratio is adjusted
The aperture of valve guarantees the stability of the pressure of sterile back pressure gas to adjust the air inflow or capacity in sterile material tank.
Preferably, the sterile material tank is connected with feed pipe, is provided on the feed pipe and is electrically connected with the controller
The charge proportion regulating valve connect is provided with the liquid level detection device being electrically connected with the controller on the sterile material tank.
Preferably, first switch valve is additionally provided in the air inlet pipe, the first switch valve is located at the aeration ratio
Between regulating valve and the constant pressure valve.
Preferably, steam is connected between the first switch valve and the aeration ratio regulating valve in the air inlet pipe
It manages, is provided with second switch valve on the steam pipe.
Preferably, be connected with connecting tube between the air inlet pipe and the feed pipe, the connecting tube be connected to it is described into
The downstream of gas ratio adjusting valve, the connecting tube are connected to the upstream of the charge proportion regulating valve, are arranged in the connecting tube
There is third switch valve.
Preferably, the gas outlet of the exhaust pipe is connected to hundred grades of aseptic areas in bottle placer, connects on the exhaust pipe
There is Clean In Place (abbreviation CIP) return pipe, is provided with the 4th switch valve on the CIP return pipe.
Technical solution two are as follows:
A kind of control method of bottle placer back pressure, which employs the control systems of bottle placer back pressure as described above, comprising:
Constant pressure valve carries out pressure stabilizing to the gas in air inlet pipe；
Pressure-detecting device detects the pressure in sterile material tank, and controller controls to adjust aeration ratio tune according to detected value
The aperture of valve or exhaust ratio regulating valve is saved, to adjust the air inflow or capacity in sterile material tank.
Preferably, the pressure of the sterile back pressure gas in pressure-detecting device detection sterile material tank, and will test value feedback
To controller, controller determines whether detected value is greater than the set value, if detected value is greater than the set value, tunes up exhaust ratio adjusting
The aperture of valve, to increase capacity；If detected value is less than setting value, the aperture of exhaust ratio regulating valve is turned down, to reduce row
Tolerance.
Preferably, the pressure of the sterile back pressure gas in pressure-detecting device detection sterile material tank, and will test value feedback
To controller, controller determines whether detected value is greater than the set value, if detected value is greater than the set value, turns aeration ratio adjusting down
The aperture of valve, to reduce air inflow；If detected value be less than setting value, tune up the aperture of aeration ratio regulating valve, with increase into
Tolerance.
The utility model has the following beneficial effects: constant pressure valve carries out preliminarily stabilised to the pressure of air inlet pipe in the utility model,
Pressure-detecting device detects the pressure of the sterile back pressure gas in sterile material tank, feeds back to controller, controller is according to detected value
The aperture of aeration ratio regulating valve or exhaust ratio regulating valve is controlled to adjust, to adjust the air inflow or exhaust of sterile material tank
Amount, to realize that the stability of the air pressure to the sterile back pressure gas in sterile material tank is adjusted.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of control system provided by the utility model.
In figure: 1, sterile material tank；2, air inlet pipe；3, exhaust pipe；4, aeration ratio regulating valve；5, exhaust ratio is adjusted
Valve；6, pressure-detecting device；7, feed pipe；8, charge proportion regulating valve；9, liquid level detection device；10, constant pressure valve；11, first
Switch valve；12, steam pipe；13, second switch valve；14, connecting tube；15, third switch valve；16, CIP return pipe；17, it the 4th opens
Close valve；18, pneumatic on-off valve；19, flowmeter.
Specific embodiment
The technical solution of the utility model is clearly and completely described below in conjunction with attached drawing, it is clear that described
Embodiment is the utility model a part of the embodiment, instead of all the embodiments.Based on the embodiments of the present invention, originally
Field those of ordinary skill every other embodiment obtained without making creative work belongs to practical
Novel protected range.
As shown in Figure 1, present embodiment discloses a kind of control system of bottle placer back pressure, including sterile material tank 1, air inlet
Pipe 2, exhaust pipe 3, aeration ratio regulating valve 4, exhaust ratio regulating valve 5, pressure-detecting device 6, feed pipe 7, charge proportion tune
Save valve 8, liquid level detection device 9, constant pressure valve 10, first switch valve 11, steam pipe 12, second switch valve 13, connecting tube 14, third
Switch valve 15, CIP return pipe 16, the 4th switch valve 17 and controller.
Air inlet pipe 2 is connected to the air inlet at the top of sterile material tank 1, and exhaust pipe 3 is connected to 1 top of sterile material tank
Exhaust outlet.Aeration ratio regulating valve 4 is set in air inlet pipe 2, and aeration ratio regulating valve 4 is electrically connected with the controller, by controller
Control its aperture.Exhaust ratio regulating valve 5 is set on exhaust pipe 3, and exhaust ratio regulating valve 5 is electrically connected with the controller, by controlling
Device processed controls its aperture.
Preferably, the pressure-detecting device 6 in the present embodiment is pressure sensor, naturally it is also possible to can be examined for other
Survey the device of the pressure of the sterile back pressure gas in sterile material tank 1.Pressure sensor is set in sterile material tank 1.Pressure passes
Sensor is electrically connected with the controller, and the pressure value that pressure sensor can will test feeds back to controller.Controller is according to detected value
The aperture for controlling to adjust exhaust ratio regulating valve 5, guarantees the stability of the pressure of sterile back pressure gas.
Feed pipe 7 is connected to the feed inlet of sterile material tank 1, and charge proportion regulating valve 8 is set on feed pipe 7, charging
Ratio adjusting valve 8 is electrically connected with the controller, and controls to adjust its aperture by controller.Preferably, the liquid level in the present embodiment is examined
Survey device 9 is liquid level sensor, and liquid level sensor is set in sterile material tank 1, the object being able to detect in sterile material tank 1
The liquid level of material, and will test value and feed back to controller, the aperture of charge proportion regulating valve 8 is controlled to adjust by controller, control into
The speed of material.
To avoid charging de-stabilising effect pressure inside the tank from stablizing, if the liquid level of liquid level sensor detection is greater than the set value
When, reduce the aperture of charge proportion regulating valve 8, reduces feed rate.If the liquid level of liquid level sensor detection is less than setting value,
Increase the aperture of charge proportion regulating valve 8, improves feed rate.
Feed pipe 7 serves not only as the pipeline of circulation material, and the circulation duct of cleaning solution is also used as in cleaning.
Constant pressure valve 10 and first switch valve 11 are additionally provided in air inlet pipe 2, first switch valve 11 is located at aeration ratio adjusting
The upstream of valve 4, constant pressure valve 10 are located at the upstream of first switch valve 11.Constant pressure valve 10 in the present embodiment is the perseverance for exporting constant-pressure type
Pressure valve.
Steam pipe 12 is connected in air inlet pipe 2 between first switch valve 11 and aeration ratio regulating valve 4, on steam pipe 12
It is provided with second switch valve 13.
Connecting tube 14 is connected between air inlet pipe 2 and feed pipe 7, connecting tube 14 is connected under aeration ratio regulating valve 4
Trip, connecting tube 14 are connected to the upstream of charge proportion regulating valve 8, third switch valve 15 are provided in connecting tube 14.
The gas outlet of exhaust pipe 3 is connected to hundred grades of aseptic areas in bottle placer, is connected with CIP return pipe 16 on exhaust pipe 3,
The 4th switch valve 17 is provided on CIP return pipe 16.
Preferably, first switch valve 11, second switch valve 13, third switch valve 15 and the 4th switch in the present embodiment
Valve 17 is pneumatic on-off valve.
When bottle placer produces, second switch valve 13 and third switch valve 15 are closed in the air inlet of sterile material tank 1, open the
One switch valve 11, aeration ratio regulating valve 4 are adjusted to setting aperture.Sterile back pressure gas enters from air inlet pipe 2, preliminary through constant pressure valve 10
The outlet pressure of constant pressure valve 10 is adjusted to a lower pressure, then enters nothing through aeration ratio regulating valve 4 again by pressure stabilizing
In fungus batch can 1.The exhaust of sterile material tank 1, closes the 4th switch valve 17, and pressure sensor detects in sterile material tank 1
Pressure, and will test value and feed back to controller, controller determines whether detected value is greater than the set value, if detected value is greater than setting
Value, then controller controls the aperture for increasing exhaust ratio regulating valve 5 according to detected value, and then increases the exhaust of sterile material tank 1
Amount.If detected value is less than setting value, controller controls the aperture for reducing exhaust ratio regulating valve 5 according to detected value, and then subtracts
The capacity of small sterile material tank 1.The capacity of sterile material tank 1 is controlled by adjusting the aperture of exhaust ratio regulating valve 5,
To realize that the stability of the air pressure to the sterile back pressure gas in sterile material tank 1 is adjusted.
Liquid material in sterile material tank 1 flow to filling nozzle through intrusion pipe under the action of sterile back pressure gas and is filled
Dress.It is provided with pneumatic on-off valve 18 on intrusion pipe, controls whether filling, flowmeter 19, flowmeter 19 are additionally provided on intrusion pipe
The flow for detecting material reaches filling completion according to the switch of the total flow control pneumatic on-off valve 18 by flowmeter 19
After one bottle of liquid material, the closing of pneumatic on-off valve 18 is controlled, is stopped filling.
Pass through the control of admission pressure and air inflow, the control of capacity and the control of inlet amount to sterile material tank 1
System, can accurately guarantee the stability of the pressure of the sterile back pressure gas in sterile material tank 1, will not be a large amount of in pouring process
Blistering, guarantees filling precision, significantly reduces bottleneck material and remain exceeded risk.
When bottle placer cleans, first switch valve 11 is closed, opens second switch valve 13, closes aeration ratio regulating valve 4；To
It is passed through aseptic steam in steam pipe 12, the downstream of first switch valve 11 and the upstream of aeration ratio regulating valve 4 is isolated, realizes
Vapor barrier guarantees that the Upstream section of the aeration ratio regulating valve of air inlet pipe 2 is not contaminated.
When cleaning aeration ratio 4 tract of regulating valve of air inlet pipe 2, third switch valve 15,17 and of the 4th switch valve are opened
Exhaust ratio regulating valve 5 closes charge proportion regulating valve 8.Cleaning solution from feed pipe 7 enter, through third switch valve 15 flow into
4 tract of aeration ratio regulating valve of tracheae 2, flow to sterile material tank 1, flow to exhaust pipe 3, then by 16 row of CIP return pipe
Out.Can 4 tract of aeration ratio regulating valve to air inlet pipe 2 and sterile material tank 1 clean.
When cleaning exhaust pipe 3, third switch valve 15 is closed, opens the 4th switch valve 17, charge proportion regulating valve 8 and exhaust
Ratio adjusting valve 5, cleaning solution enter from CIP return pipe 16, flow to exhaust pipe 3, flow to sterile material tank 1, flow to feed pipe 7,
Then it is discharged by feed pipe 7.Feed pipe 7 and exhaust pipe 3 can be cleaned.
Setting connecting tube 14, steam pipe 12, CIP return pipe 16, second switch valve 13, third switch valve 15 and the 4th are opened
Close valve 17, opening or closing by controlling each valve, and the inlet of transformation cleaning solution, may be implemented to air inlet pipe 2 into
The cleaning of gas ratio adjusting valve 4 tract, sterile material tank 1, feed pipe 7 and exhaust pipe 3.
The present embodiment also discloses a kind of control method of bottle placer back pressure, which employs control system as described above,
Include:
Constant pressure valve carries out pressure stabilizing to the gas in air inlet pipe；
Pressure-detecting device detects the pressure in sterile material tank, and controller controls to adjust aeration ratio tune according to detected value
The aperture of valve or exhaust ratio regulating valve is saved, to adjust the air inflow or capacity in sterile material tank.
Specifically, preferably, in the present embodiment, constant pressure valve carries out preliminary pressure stabilizing to the gas in air inlet pipe, makes air inlet
Pressure is held essentially constant.By the pressure in pressure sensor detection sterile material tank 1, and it will test value and feed back to controller,
Controller determines whether detected value is greater than the set value, if detected value is greater than the set value, controller is controlled according to detected value to be increased
The aperture of exhaust ratio regulating valve 5, and then increase the capacity of sterile material tank 1.If detected value is less than setting value, controller
The aperture for reducing exhaust ratio regulating valve 5 is controlled according to detected value, and then reduces the capacity of sterile material tank 1.Pass through adjusting
The aperture of exhaust ratio regulating valve 5 controls the capacity of sterile material tank 1, to realize to the sterile back in sterile material tank 1
The stability for the air pressure calmed the anger is adjusted.
In other examples it is also possible that by the pressure in pressure sensor detection sterile material tank 1, and it will test value
Controller is fed back to, controller determines whether detected value is greater than the set value, if detected value is greater than the set value, controller is according to inspection
Measured value control reduces the aperture of aeration ratio regulating valve 4, and then reduces the air inflow of sterile material tank 1.It is set if detected value is less than
Definite value, then controller according to detected value control increase aeration ratio regulating valve 4 aperture, and then increase sterile material tank 1 into
Tolerance.The aperture of aeration ratio valve 4 is adjusted to control the air inflow of sterile material tank 1, to realize to the nothing in sterile material tank 1
The stability of the air pressure of bacterium back pressure gas is adjusted.
Note that above are only the preferred embodiment and institute's application technology principle of the utility model.Those skilled in the art's meeting
Understand, the utility model is not limited to specific embodiment described here, is able to carry out for a person skilled in the art various bright
Aobvious variation, readjustment and substitution is without departing from the protection scope of the utility model.Therefore, although passing through above embodiments
The utility model is described in further detail, but the utility model is not limited only to above embodiments, is not departing from
It can also include more other equivalent embodiments in the case that the utility model is conceived, and the scope of the utility model is by appended
Scope of the claims determine.
Claims (6)
1. a kind of control system of bottle placer back pressure, including sterile material tank (1), the sterile material tank (1) is connected with air inlet
Manage (2) and exhaust pipe (3), which is characterized in that further include:
Constant pressure valve (10) is set on the air inlet pipe (2)；
Aeration ratio regulating valve (4) is set on the air inlet pipe (2) and is located at the downstream of the constant pressure valve；
Exhaust ratio regulating valve (5) is set on the exhaust pipe (3)；
Pressure-detecting device (6) is able to detect the pressure of the sterile back pressure gas in the sterile material tank (1)；
Controller, the aeration ratio regulating valve (4), the exhaust ratio regulating valve (5) and the pressure-detecting device (6) are equal
It is electrically connected with the controller.
2. control system according to claim 1, which is characterized in that the sterile material tank (1) is connected with feed pipe
(7), the charge proportion regulating valve (8) being electrically connected with the controller, the sterile material tank are provided on the feed pipe (7)
(1) liquid level detection device (9) being electrically connected with the controller is provided on.
3. control system according to claim 1, which is characterized in that be additionally provided with first switch on the air inlet pipe (2)
Valve (11), the first switch valve (11) is between the aeration ratio regulating valve (4) and the constant pressure valve (10).
4. control system according to claim 3, which is characterized in that in the first switch valve on the air inlet pipe (2)
(11) it is connected between the aeration ratio regulating valve (4) steam pipe (12), is provided with second on the steam pipe (12) and opens
It closes valve (13).
5. control system according to claim 2, which is characterized in that between the air inlet pipe (2) and the feed pipe (7)
It is connected with connecting tube (14), the connecting tube (14) is connected to the downstream of the aeration ratio regulating valve (4), the connecting tube
(14) it is connected to the upstream of the charge proportion regulating valve (8), is provided with third switch valve (15) on the connecting tube (14).
6. control system according to claim 1, which is characterized in that the gas outlet of the exhaust pipe (3) is connected to filling
Hundred grades of aseptic areas in machine are connected with CIP return pipe (16) on the exhaust pipe (3), are provided on the CIP return pipe (16)
4th switch valve (17).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821719904.XU CN209143655U (en) | 2018-10-23 | 2018-10-23 | A kind of control system of bottle placer back pressure |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821719904.XU CN209143655U (en) | 2018-10-23 | 2018-10-23 | A kind of control system of bottle placer back pressure |
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| Publication Number | Publication Date |
|---|---|
| CN209143655U true CN209143655U (en) | 2019-07-23 |
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ID=67269321
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821719904.XU Active CN209143655U (en) | 2018-10-23 | 2018-10-23 | A kind of control system of bottle placer back pressure |
Country Status (1)
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| CN (1) | CN209143655U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109095418A (en) * | 2018-10-23 | 2018-12-28 | 广州达意隆包装机械股份有限公司 | A kind of control system and control method of bottle placer back pressure |
-
2018
- 2018-10-23 CN CN201821719904.XU patent/CN209143655U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109095418A (en) * | 2018-10-23 | 2018-12-28 | 广州达意隆包装机械股份有限公司 | A kind of control system and control method of bottle placer back pressure |
| CN109095418B (en) * | 2018-10-23 | 2023-12-15 | 广州达意隆包装机械股份有限公司 | Control system and control method for back pressure of filling machine |
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Legal Events
| Date | Code | Title | Description |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP02 | Change in the address of a patent holder | ||
| CP02 | Change in the address of a patent holder |
Address after: 510530 No. 23 Yunpu Road, Huangpu District, Guangzhou City, Guangdong Province Patentee after: Guangzhou Tech-Long Packing Machinery Co., Ltd. Address before: 510530 Guangdong city of Guangzhou province Luogang District YUNPU Road No. 23 Patentee before: Guangzhou Tech-Long Packing Machinery Co., Ltd. |