CN208291520U - Bottle placer discharge automatic control system and bulking system - Google Patents
Bottle placer discharge automatic control system and bulking system Download PDFInfo
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- CN208291520U CN208291520U CN201820700398.3U CN201820700398U CN208291520U CN 208291520 U CN208291520 U CN 208291520U CN 201820700398 U CN201820700398 U CN 201820700398U CN 208291520 U CN208291520 U CN 208291520U
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- open
- close valve
- bottle placer
- instrument
- automatic control
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Abstract
The utility model offer is able to solve product caused by withdrawal rate deviation water inlet and cost increase problem, thus promoted product quality and production capacity and control production cost bottle placer discharge automatic control system and corresponding bulking system.Bulking system (1) has: storage tank (10)；Liftout is with water inlet (11)；Feed pump (20)；Instrument (301) monitors the performance parameter of fluids within pipes；First open and close valve (302), is configured at filling pipeline；Second open and close valve (303), the row's of being configured at ground pipeline；Control module (310) receives the data that the instrument (301) is fed back, issues an instruction to the opening and closing for adjusting first open and close valve (302) and second open and close valve (303)；And bottle placer (40).
Description
Technical field
The utility model relates to bottle placer discharge automatic control system and corresponding bulking systems.
Background technique
Current dairy products processing technology tends to cleaning, and the production of low-temperature yoghurt, filling, storage are due to its special work
Skill process and need stringenter working condition.It is exactly that will flow through to feed liquid that most important preparation is done before feed liquid is filling
Pipeline, the pump housing and bottle placer carry out disinfection.And factory use disinfection way be using 90 DEG C or more hot water circuits flow through it is whole
Set bulking system carries out disinfection, and after disinfection, carries out after needing machine to be filled to be cooled to preference temperature filling.Heat in pipeline
Water can not be expelled directly out, and need product when feeding by the ejection of this part water, row ground.By the mixing of water and feed liquid and water in pipeline
Object all empties, and the process until being completely filled with feed liquid in bottle placer material cylinder is known as the operation of bottle placer discharge.
The operation of bottle placer discharge used in actual production at present is substantially by the empirical value of operative employee and laboratory to finger
Target measured value.Operative employee substantially determines withdrawal rate, row according to the time and visual observation feed liquid color, the mode of state of discharge
Sampling is sent to laboratory Testing index after material, carries out after qualified filling.The mode of this discharge has apparent disadvantage
End, there are error, the interpersonal othernesses of operative employee to cause the difference of withdrawal rate for artificial observation.Withdrawal rate causes to expect more
Liquid is increased by row ground, cost.Withdrawal rate causes the mixture of feed liquid and water to enter product less, influences product quality, or chemical examination
Index is unqualified to lead to secondary sample presentation to influence the filling time.
Need to more precisely control withdrawal rate in production, with this promoted product quality, control cost, promoted production capacity and
Reduce person works' amount.
Utility model content
The utility model is completed in view of above-mentioned actual conditions, and its purpose is to provide be able to solve withdrawal rate deviation
Caused product water inlet and cost increase problem, to promote product quality and production capacity and control the bottle placer discharge of production cost
Automatic control system and corresponding bulking system.
The bottle placer discharge automatic control system of one technical solution of the utility model has: instrument, monitors pipeline
The performance parameter of interior fluid；First open and close valve is configured at filling pipeline；Second open and close valve, the row's of being configured at ground pipeline；And
Control module receives the data that the instrument is fed back, and issues an instruction to adjust first open and close valve and described second and open
The opening and closing of valve closing.
The bulking system of one technical solution of the utility model has: storage tank；Liftout water inlet；Feed pump；Instrument
Table monitors the performance parameter of fluids within pipes；First open and close valve is configured at filling pipeline；Second open and close valve, is configured at
Row ground pipeline；Control module receives the data that the instrument is fed back, and issues an instruction to adjust first open and close valve and institute
State the opening and closing of the second open and close valve；And bottle placer.
In a preferred technical solution, the instrument is densitometer.
In a preferred technical solution, first open and close valve and second open and close valve are operated pneumatic valves.
In a preferred technical solution, the control module have can according to feed liquid condition real-time adjusting parameter
The configuration part of setting value.
In a preferred technical solution, the storage tank, the feed pump, the instrument, first open and close valve
And the bottle placer is sequentially connected by pipeline, the liftout with water inlet between the storage tank and the instrument,
Second open and close valve with being configured at the row between the instrument and first open and close valve pipeline.
In a preferred technical solution, the bottle placer discharge automatic control system of the utility model and corresponding filling
System is filling for Yoghourt.
Utility model effect
The bottle placer discharge automatic control system of the utility model and corresponding bulking system are able to solve withdrawal rate deviation
Caused product water inlet and cost increase problem, to promote product quality and production capacity, control production cost.
Detailed description of the invention
Fig. 1 is the schematic diagram of the bottle placer discharge automatic control system of the utility model.
Fig. 2 is the schematic diagram of the bulking system of the utility model.
Description of symbols
1 bulking system；10 storage tanks；20 feed pumps；30 bottle placer discharge automatic control systems；310 control modules；301
Instrument；302 first open and close valves；303 second open and close valves；40 bottle placers.
Specific embodiment
Hereinafter, specific embodiment of the present utility model is described in detail referring to attached drawing.It should be noted that with
Under explanation in institute's reference attached drawing summary show embodiment, therefore there are the scale of each component, interval, positions to close
The case where system etc. is exaggerated or the diagram of a part of component is omitted.
As the specific embodiment of bottle placer discharge automatic control system and bulking system, certainly with Yoghourt bottle placer discharge
It is illustrated for autocontrol system 30 and Yoghourt bulking system 1.
Fig. 1 is the schematic diagram of the bottle placer discharge automatic control system of the utility model.As shown in Figure 1, present embodiment
Yoghourt bottle placer discharge automatic control system 30 have: instrument 301, monitor fluids within pipes performance parameter；First opens
Valve closing 302 is configured at filling pipeline；Second open and close valve 303, the row's of being configured at ground pipeline；And control module 310, it connects
The data fed back by instrument 301 issue an instruction to the opening and closing for adjusting the first open and close valve 302 and the second open and close valve 303.In this reality
It applies in mode, instrument 301 is densitometer.In addition, in the present embodiment, the first open and close valve 302 and the second open and close valve 303 are gas
Movable valve.In the Yoghourt bottle placer discharging process of present embodiment, feed liquid top water advances.In the initial state, the first opening and closing
Valve 302 is closed, and the second open and close valve 303 is opened.Densitometer monitors the density of fluids within pipes in real time, then passes through signal wire
Road (dotted portion in figure) is by the data feedback monitored in real time to control module.Control module 310 for example including receiving unit, sentence
Disconnected portion, configuration part and control unit.Control module 310 receives the data that densitometer is fed back by receiving unit, utilizes judging part root
It after being judged according to the density set point set by configuration part, is issued and is instructed to open and close valve by control unit, adjust the first opening and closing
The opening and closing of valve 302 and the second open and close valve 303.
The density of fluid in 301 signal piping of densitometer, and by data Real-time Feedback to control module 310.In control mould
When block 310 is determined as density lower than setting value, the state of the first open and close valve 302 and the second open and close valve 303 is not changed, to maintain
It will expect the state on aqueous mixtures row ground.When control module 310 is determined as that density reaches setting value or is more than setting value, pass through control
Portion processed issues to open and close valve and instructs, and closes the second open and close valve 303 and opens the first open and close valve 302.Row ground terminates as a result, filling
Machine starts charging production.That is, the operated pneumatic valve on row ground is opened when row ground, the operated pneumatic valve for connecting bottle placer is closed；It is arranged when production
The operated pneumatic valve on ground is closed, and the operated pneumatic valve for connecting bottle placer is opened.
Fig. 2 is the schematic diagram of the bulking system of the utility model.As shown in Fig. 2, the Yoghourt bulking system 1 of present embodiment
Have: storage tank (being in the present embodiment container for storing milk) 10；Liftout water inlet 11；Feed pump 20；Instrument 301, monitoring
The performance parameter of fluids within pipes；First open and close valve 302, is configured at filling pipeline；Second open and close valve 303, the row of being configured at
Ground pipeline；Control module 310 receives the data that instrument 301 is fed back, and issues an instruction to adjust the first open and close valve 302 and the
The opening and closing of two open and close valves 303；And bottle placer 40.The Yoghourt bulking system 1 of present embodiment applies above-mentioned Yoghourt bottle placer
Discharge automatic control system 30.
More specifically, container for storing milk 10, feed pump 20, instrument 301, the first open and close valve 302 and bottle placer 40 pass through pipe
Road is sequentially connected, and for liftout with water inlet 11 between container for storing milk 10 and instrument 301, the second open and close valve 303 is configured at instrument 301
Row between the first open and close valve 302 ground pipeline.
In disinfection, hot water is poured into pipeline and bottle placer from liftout with water inlet 11.And filling after disinfection
When installation discharge, liftout water inlet 11 is closed, feed liquid is made to enter production pipeline from container for storing milk 10, feed liquid top water advances.As before
Described, in the initial state, the first open and close valve 302 is closed, and the second open and close valve 303 is opened.Densitometer is to the close of fluids within pipes
Degree is monitored in real time, then passes through signal line (dotted portion in figure) for the data feedback monitored in real time to control module.
Control module 310 is for example including receiving unit, judging part, configuration part and control unit.Control module 310 receives density by receiving unit
Count fed back data, after being judged using judging part according to the density set point set by configuration part, by control unit to
Open and close valve issues instruction, adjusts the opening and closing of the first open and close valve 302 and the second open and close valve 303.
The density of fluid in 301 signal piping of densitometer, and by data Real-time Feedback to control module 310.In control mould
When block 310 is determined as density lower than setting value, the state of the first open and close valve 302 and the second open and close valve 303 is not changed, to maintain
It will expect the state on aqueous mixtures row ground.When control module 310 is determined as that density reaches setting value or is more than setting value, pass through control
Portion processed issues to open and close valve and instructs, and closes the second open and close valve 303 and opens the first open and close valve 302, starts filling.
In the above-described embodiment, the configuration part of control module 310 real-time adjusting parameter can be set according to Yoghourt condition
Definite value, so as to be suitable for the production of different types of Yoghourt.
Certainly, the control mode of control module 310 is different according to the setting position of densitometer 301, if density
The setting position of meter 301 and the distance between filling exit can be ignored, then control module 310 after density reaches setting value immediately
Close the second open and close valve 303 and open the first open and close valve 302, if between the setting position and filling exit of densitometer 301 away from
From that can not ignore farther out, then control module 310 turns off the second open and close valve by the stipulated time after density reaches setting value
303 and the first open and close valve 302 is opened, which presets according to flow velocity of liquid etc..
For the ease of illustration, in fig. 1 and 2 by instrument 301, the first open and close valve 302, the second open and close valve 303 and filling
Installation 40 is drawn in such a way that interval is farther away, but actually also includes instrument 301, the first open and close valve 302 and the second open and close valve
303 setting is apart from close, and the case where be all arranged close to bottle placer 40.
According to the utility model, efficiently separating for feed liquid and water in pipeline can be conveniently and efficiently realized.According to fluid
Performance parameter determines the state of fluids within pipes, for example, being joined in the specific embodiment enumerated according to product density
The state of several pairs of fluids within pipes determines, has effectively achieved the normalizing operation of bottle placer withdrawal rate.
Also, according to the utility model, the withdrawal rate of bottle placer discharge has more reliability, eliminates and operates band by personnel
The maloperation hidden danger and cost come increase, and play a significant role to the stabilization of product quality.The technical side of the utility model simultaneously
Case is easily achieved, and is not needed the newly-increased of large scale equipment or is improved, increasing a small amount of instrument, valve etc. newly on existing equipment can be real
It applies.In addition, can set different parameters according to the difference of condition, flexibility is high, can meet the bottle placer discharge of conventional feed liquid
Process requirement.
Embodiment is illustrated above, but above embodiment is only to illustrate, and the utility model is not by upper
State embodiment restriction.Above embodiment can be implemented in the form of other are various, can not depart from utility model
Carry out various combinations in the range of purport, omit, replace, change etc..
Industrial availability
The bottle placer discharge automatic control system of the utility model and corresponding bulking system are for the clear of sour milk production line
It is clean, it is able to solve the water inlet of product caused by withdrawal rate deviation and cost increases problem, to promote product quality and production capacity, control
Production cost.
Claims (11)
1. a kind of bottle placer discharge automatic control system, which is characterized in that have:
Instrument monitors the performance parameter of fluids within pipes；
First open and close valve is configured at filling pipeline；
Second open and close valve, the row's of being configured at ground pipeline；And
Control module receives the data that the instrument is fed back, and issues an instruction to adjust first open and close valve and described
The opening and closing of two open and close valves.
2. bottle placer discharge automatic control system according to claim 1, which is characterized in that
The instrument is densitometer.
3. bottle placer discharge automatic control system according to claim 1, which is characterized in that
First open and close valve and second open and close valve are operated pneumatic valves.
4. bottle placer discharge automatic control system according to claim 1, which is characterized in that
The control module has being capable of according to the feed liquid condition and real-time configuration part of adjusting parameter setting value.
5. bottle placer discharge automatic control system according to claim 1, which is characterized in that
The bottle placer discharge automatic control system is filling for Yoghourt.
6. a kind of bulking system, which is characterized in that have:
Storage tank；
Liftout water inlet；
Feed pump；
Instrument monitors the performance parameter of fluids within pipes；
First open and close valve is configured at filling pipeline；
Second open and close valve, the row's of being configured at ground pipeline；
Control module receives the data that the instrument is fed back, and issues an instruction to adjust first open and close valve and described
The opening and closing of two open and close valves；And
Bottle placer.
7. bulking system according to claim 6, which is characterized in that
The instrument is densitometer.
8. bulking system according to claim 6, which is characterized in that
First open and close valve and second open and close valve are operated pneumatic valves.
9. bulking system according to claim 6, which is characterized in that
The control module has being capable of according to the feed liquid condition and real-time configuration part of adjusting parameter setting value.
10. bulking system according to claim 6, which is characterized in that
The storage tank, the feed pump, the instrument, first open and close valve and the bottle placer pass through pipeline successively phase
Even,
The liftout with water inlet between the storage tank and the instrument,
Second open and close valve with being configured at the row between the instrument and first open and close valve pipeline.
11. bulking system according to claim 6, which is characterized in that
The bulking system is filling for Yoghourt.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820700398.3U CN208291520U (en) | 2018-05-10 | 2018-05-10 | Bottle placer discharge automatic control system and bulking system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820700398.3U CN208291520U (en) | 2018-05-10 | 2018-05-10 | Bottle placer discharge automatic control system and bulking system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208291520U true CN208291520U (en) | 2018-12-28 |
Family
ID=64702724
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820700398.3U Active CN208291520U (en) | 2018-05-10 | 2018-05-10 | Bottle placer discharge automatic control system and bulking system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208291520U (en) |
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2018
- 2018-05-10 CN CN201820700398.3U patent/CN208291520U/en active Active
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