CN105961607A - Cream production line - Google Patents
Cream production line Download PDFInfo
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- CN105961607A CN105961607A CN201610465790.XA CN201610465790A CN105961607A CN 105961607 A CN105961607 A CN 105961607A CN 201610465790 A CN201610465790 A CN 201610465790A CN 105961607 A CN105961607 A CN 105961607A
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
- A23C13/00—Cream; Cream preparations; Making thereof
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
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- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Confectionery (AREA)
- Dairy Products (AREA)
Abstract
The invention relates to a cream production line which comprises a feeding weighing system, a raw material storage system, a fragrance adding system and a residue cleaning system, wherein a first vacuum system and a second vacuum system are arranged between a blending tank and an aging tank; a third vacuum system is arranged between the aging cylinder and a filling machine; each vacuum system comprises a vacuum pump, an assistant cylinder and a sucking target cylinder; the assistant cylinders are connected with the openings of the sucking target cylinders through assistant pipelines; the openings of the sucking target cylinders are further connected with raw material residue pipelines for sucking; the vacuum pumps are connected with assistant cylinders; the sucking target cylinder in the first vacuum system is a blending cylinder for sucking raw materials in a front half section of a corresponding raw material residue pipeline back to the blending cylinder; the sucking target cylinder in the second vacuum system is an aging cylinder for sucking raw materials in the second half section of a corresponding raw material residue pipeline back to the aging tank; the sucking target cylinder in the third vacuum system is also an aging cylinder for sucking raw materials in a corresponding raw material residue pipeline back to the aging tank.
Description
Technical field
The present invention relates to a kind of butter automatic assembly line, belong to butter production line technology field.
Background technology
The production stage of butter production line include principle storage, dispensing, bus sterilization, homogenizing, aging,
Inner packing (fill), outer package, stacking etc..
Existing butter production line, during the charging of powder, needs to carry out the metering of charging quality,
In prior art, for the charging of powder, general employing weighing device is weighed, when powder is from former
When material storage silo falls in weighing device from top to bottom, can produce impulse force, this impulse force is for quality meter
Amount creates error, and this error is referred to as dynamic error (error of weighing device itself is static error),
In existing butter production line charging weighing system, the dynamic application condition of weighing device is obvious, to charging
The control of precision is unfavorable；Additionally, during existing butter produces, for the liquid material such as oil plant, syrups
Charging typically use mass flowmenter, the precision controlling of quality is the highest, for the control of product quality
It is unfavorable to make；
In the operation of raw material storage, the kind of powder is numerous, and installing additional of powder generally relies on people's work point
The mode joined carries out charging conveying, often occurs adding the situation of wrong material, produces to butter and causes relatively
Big loss, and the control to product quality is unfavorable.Carry out the premix work mixed with liquid material at powder
In sequence, needing to add essence and flavoring agent, essence and flavoring agent has liquid, colloidal state, powder state three kinds, prior art
The feed way used is the most manually to weigh, and is then manually added in premixing tank, and premixing tank mixes
After add material-compound tank carry out dispensing.Owing to being manually to weigh, so spice adds cumbersome,
And precision controlling is poor, and powder uses same weighing device, and weighing device has residual perfume unavoidably
Material, is susceptible to taint of odour, the quality of whipping prods is caused adverse influence；
Existing butter produces, according to the relevant regulations of food safety, it is not possible to be 24 hours uninterrupted
Produce, between each order of classes or grades at school, have longer time interval.Thus, after an order of classes or grades at school terminates, position
Between pill tank and aging tank, and in the pipeline between aging tank and filling machine, can remain
Cream raw material, does not possess temperature controlling function owing to pipeline is usually, and therefore the raw material in pipeline cannot be pacified
Entirely be saved in next order of classes or grades at school, the mode that prior art uses be all after a upper order of classes or grades at school terminates or
Before next order of classes or grades at school starts, the cream raw material in each pipeline is released as waste material, the most also needs
On-line cleaning, sterilization is carried out in the range of specific.Not only cause waste, cause environmental pollution,
The most indirectly add the pressure of production cost and sewage disposal.
Summary of the invention
In order to solve above-mentioned technical problem, the present invention takes techniques below scheme:
A kind of butter production line, including charging weighing system: described charging weighing system includes that powder adds
Material weighing device, liquid material feeding material weighing device；Described powder feed weighing device include powder holding vessel 3,
Screw propulsion mechanism 2, dolly 1 of weighing, frequency conversion motor 4；Described screw propulsion mechanism 2 initiating terminal water
The flat bottom being fixedly installed on powder holding vessel 3, frequency conversion motor 1 coaxially sets with screw propulsion mechanism 2
Put, be used for driving screw propulsion mechanism 2；The bottom of described screw propulsion mechanism 2 end and dolly of weighing
The charging aperture of 1 can coordinate docking；Described dolly 1 of weighing can move, with track in horizontal rail
One row's powder holding vessel 3 corresponding to top matches docking；Described dolly 1 and the frequency conversion motor 4 of weighing
PLC signal connect, frequency conversion motor 4 slows down step by step according to weighing-up wave, until it is little to weigh
Car stops operating after reaching target weight；Described liquid material feeding material weighing device includes interconnective liquid material
Holding vessel, duct type mass flowmenter；With steam spacer type heater in described liquid material holding vessel,
Liquid material viscosity is made to keep constant when discharging；The line end of described duct type mass flowmenter arranges electricity
Magnetic stop valve, the opening and closing of described electromagnet cut off valve control operation and the stopping of liquid material charging respectively；
Also include that raw material stores system, spice add-on system: described raw material storage system includes multiple memory block
Territory, each memory area has 10-20 raw material storage tank；Described each memory area is provided with each
The first barcode scanning device, each storage tank is provided with respective second barcode scanning device, each powder to be fed
Material storage bag is provided with the bar code of record product kind, date of manufacture, weight；Powder storage bag enters
Before entering memory area, can need to be entered after being verified by bar code described in the first barcode scanning device identification
Enter；Powder storage bag, need to be by bar described in the second barcode scanning device identification before raw material storage ladle addition
Shape code, after secondary is verified, can feed；Described spice add-on system multiple spice adding device,
Stepping eccentric driven pump that each spice adding device is each provided with being sequentially connected with, hybrid chamber, conveying pipe, institute
State conveying pipe end be positioned at premix cylinder top, liquid spice, through dissolve powder state spice or warp
The colloidal state spice of dilution is by quantitative being added in described premix cylinder of respective stepping eccentric driven pump；Also wrap
Include surplus material cleaning system: pill tank that described butter production line includes being sequentially connected with, aging tank, fill
Machine；The first vacuum system and the second vacuum system it is provided with, always between described pill tank and aging tank
Change and be provided with the 3rd vacuum system between cylinder and filling machine；Three vacuum systems each include vacuum pump, auxiliary
Help cylinder E2, suction target cylinder E1, pass through between the cylinder mouth of described auxiliary cylinders E2 and suction target cylinder E1
Auxiliary piping connects, and the cylinder mouth of described suction target cylinder E1 is also connected with raw material residual pipeline to be pumped；
Described vacuum pump is connected with auxiliary cylinders E2, produces stable negative pressure in making auxiliary cylinders E2, and this negative pressure makes
Cream raw material in described raw material residual pipeline falls under gravity in suction target cylinder E1, and
Will not enter in auxiliary piping；Suction target cylinder E1 in first vacuum system is pill tank, by correspondence
Raw material residual pipeline first half section in raw material suck back in pill tank；Suction mesh in second vacuum system
Mark cylinder E1 is aging tank, is sucked back in aging tank by the raw material in the corresponding raw material residual pipeline second half section；
Suction target cylinder E1 in 3rd vacuum system is also aging tank, by corresponding raw material residual pipeline kind
Raw material sucks back in aging tank.
Further, described liquid material feeding material weighing device also includes Weighing module, for powder and liquid material
The premix cylinder of mixing, described Weighing module is arranged on the lower section of premix cylinder and enters the material in premix cylinder
Row is weighed；Described Weighing module is connected with duct type mass flowmenter signal, for duct type quality stream
The data that gauge records carry out PID correction, until obtaining the last aimed quality data revised, described
Electromagnet cut off valve is closed.
Further, during discharge of fine material: frequency conversion motor 4 first keeps constant high velocity, when close to stoichiometric point
Before, frequency conversion motor 4 gradually slows down, and transporting velocity slows down gradually until stopping when reaching stoichiometric point；Liquid
During material discharging: duct type effusion meter real time record discharging quality, Weighing module carries out enforcement and weighs, and
The detection data of duct type effusion meter are carried out real-time PID correction, until the revised mass number of PID
According to when reaching stoichiometric point, electromagnet cut off valve receives the shutdown signal of Weighing module feedback and closes.
Further, described liquid material, powder replace discharging successively, and discharging falls in premix cylinder, institute
State Weighing module before the detection data of duct type effusion meter are carried out real-time PID correction, first deducted
Fall into the quality of powder in premix cylinder.
Further, described raw material storage system is according to date of manufacture of described bar code record, weight
The information monitoring powder real-time weight in raw material storage tank 2 and shelf-life.
Further, the multiple of described stepping bias pump delivery is liquid spice addition.
Further, second, third vacuum system described shares a vacuum pump, shares an auxiliary
Cylinder E2, shares an aging tank；And raw material residual pipeline to be pumped is different, and carried out by valve
Switching.
Further, described butter production line surplus material cleaning system also includes cooling water system, described cold
But water system forms circulation, to auxiliary by pipeline and external impetus between vacuum pump and auxiliary cylinders E2
Cylinder E2 and vacuum pump are lowered the temperature.
Further, described cooling water system includes temperature control cistern, the water outlet of described temperature control cistern
Mouth is connected with inlet pipeline；Cooling line, water return pipeline in inlet pipeline, auxiliary cylinders E2 connect successively
Connect；Water return pipeline is connected with the water return outlet of temperature control cistern；It is sequentially provided with first on described inlet pipeline
Valve V8, visor FI40, filter B 2, real-time flow meter V12, the second valve V9, circulating pump
PI1。
The beneficial effects of the present invention is:
For raw material storage system, spice add-on system:
1) by arranging screw propulsion mechanism, frequency conversion motor, and screw propeller is controlled by PLC
The fltting speed of structure successively decreases step by step, and farthest reduction powder falls into from top to bottom and weighs
The dynamic error that device causes, improves the precision of powder metering.
2) dolly of weighing is the form that track moves, it is possible to dock with multiple powder holding vessels,
Designing ingenious, work efficiency is high.
3) use Weighing module that the enforcement data of duct type mass flowmenter are carried out PID correction, obtain
Obtain the qualitative data of more accurate liquid material discharging.The precision of liquid material charging is higher.
4) liquid material, powder replace discharging successively, and discharging falls in premix cylinder, and described Weighing module exists
Before the detection data of duct type effusion meter are carried out real-time PID correction, first deduct and fall into
In premix cylinder, the quality of powder, had both reached the effect of mix homogeneously, had reached again liquid material
The purpose of charging accurate measurement, designs ingenious.
5) raw material after various meterings is automatically sent to premix cylinder mix, premix cylinder itself also with
Metering complex function, makes the metering safety in production process be further strengthened.
6) whole charging weighing system controls to perform and process record according to specific program, also avoids
All drawbacks that in industry, commonly used manual mode of operation is brought. make the peace of product
Quan Xing, retrospective are more added with ensureing.
For raw material storage system, spice add-on system:
1) memory area and single raw material storage tank are equipped with barcode scanning device, are supervised by twice barcode scanning
Control, prevents charging from makeing mistakes, and improves product quality.
2) by the date of manufacture of bar code record, weight information monitoring powder in raw material storage tank
Real-time weight and the shelf-life, automatically-monitored, more reliable.
3) using stepping eccentric driven pump, hybrid chamber, conveying pipe to carry out spice interpolation, spice is by dissolving
Dilution is completely converted into liquid, uses the stepping eccentric driven pump of fixed displacement to feed, more square
Just；Ensure that spice addition is more accurate simultaneously, improve product quality, avoid using simultaneously
Weighing device, it is to avoid spice taint of odour.
For surplus material cleaning system:
1) when butter produces changing shifts, it is not necessary to the original material in pipeline is released, it is to avoid
Waste, protects environment.
2) avoid each order of classes or grades at school to be required in the range of specific to carry out on-line cleaning, sterilization, alleviate
Workload, improves work efficiency.
3) auxiliary cylinders matches with vacuum pump and provides stable negative pressure, and utilizes the effect of gravity,
Making raw material also will not will not suck in auxiliary cylinders and auxiliary piping in suction pump, design is skilful
Wonderful.
4) auxiliary cylinders top is connected with the entrance of suction target cylinder by auxiliary piping, reasonable in design.
5) arranging three vacuum systems, the first vacuum system is for the pipe between pill tank and homogen jar
The first half section on road；After second vacuum system is for the pipeline between pill tank and homogen jar
Half section；3rd vacuum system for the pipeline between aging tank and filling machine, configuration optimization,
Carefully think out.
6) second, third vacuum system is shared identical aging tank, auxiliary cylinders is abundant to resource
Integrating, intensivism is high, cost-effective, improves efficiency.
7) use circulating water cooling system, auxiliary cylinders and vacuum pump are implemented cooling, it is ensured that true simultaneously
Empty pump and the reasonable temperature of auxiliary cylinders, the work efficiency of cooling system is high.
8) the first valve V8, visor FI40, filter B 2, reality are set in circulating water cooling system
Time effusion meter V12, the second valve V9, circulating pump PI1, water loop control is more convenient,
Monitoring property is good, and reliability is high.
Accompanying drawing explanation
Fig. 1 is the technical process schematic diagram of butter production line.
Fig. 2 is that in butter production line charging weighing system, powder body stores, metering process elevation.
Fig. 3 with Fig. 2 is corresponding, in powder body storage, metering process elevation, and dolly of weighing, spiral shell
The attachment structure figure of the rotation parts such as propulsive mechanism, powder storing tank.
Fig. 4 is the process chart of spice add-on system.
Fig. 5 is the partial enlarged drawing of Fig. 4.
Fig. 6 is the partial enlarged drawing of Fig. 4.
Fig. 7 is the partial enlarged drawing of Fig. 4.
Fig. 8 is the partial enlarged drawing of Fig. 4.
Fig. 9 is in butter production line surplus material cleaning system, the structural representation of one of them vacuum system.
The partial enlarged drawing on Figure 10 figure 9 above top.
Figure 11 is the partial enlarged drawing of Fig. 9 bottom.
In figure, 1. weigh dolly, 2. screw propulsion mechanism, 3. powder storing tank, 4. frequency conversion motor.
Detailed description of the invention
The present invention is further described with specific embodiment below in conjunction with the accompanying drawings.
First against charging weighing system:
Seeing Fig. 1-Fig. 3, feed weighing system, claims including powder feed weighing device, liquid material charging
Refitting is put；Described powder feed weighing device includes powder holding vessel 3, screw propulsion mechanism 2, weighs
Dolly 1, frequency conversion motor 4；Described screw propulsion mechanism 2 initiating terminal level is fixedly installed on powder and stores
The bottom of tank 3, frequency conversion motor 1 is coaxially disposed with screw propulsion mechanism 2, is used for driving screw propulsion
Mechanism 2；It is right that the bottom of described screw propulsion mechanism 2 end can coordinate with the charging aperture of dolly 1 of weighing
Connect；Described dolly 1 of weighing can move in horizontal rail, a row powder corresponding with above track
Holding vessel 3 matches docking；The PLC signal of described weigh dolly 1 and frequency conversion motor 4 is even
Connecing, frequency conversion motor 4 slows down step by step according to weighing-up wave, until dolly of weighing stops after reaching target weight
Spline is moved；Described liquid material feeding material weighing device includes interconnective liquid material holding vessel, duct type quality
Effusion meter；With steam spacer type heater in described liquid material holding vessel, make liquid material viscosity in discharging
Time keep constant；The line end of described duct type mass flowmenter arranges electromagnet cut off valve, described electricity
The opening and closing of magnetic stop valve control operation and the stopping of liquid material charging respectively.
Described liquid material feeding material weighing device also includes Weighing module, the premix mixed for powder and liquid material
Cylinder, described Weighing module is arranged on the lower section of premix cylinder and weighs the material in premix cylinder；Institute
State Weighing module to be connected with duct type mass flowmenter signal, duct type mass flowmenter is recorded
Data carry out PID correction, until obtaining the last aimed quality data revised, described electromagnet cut off valve
Close.
During discharge of fine material: frequency conversion motor 4 first keeps constant high velocity, when before stoichiometric point, variable-frequency electric
Machine 4 gradually slows down, and transporting velocity slows down gradually until stopping when reaching stoichiometric point；During liquid material discharging:
Duct type effusion meter real time record discharging quality, Weighing module carries out enforcement and weighs, and to duct type stream
The detection data of gauge carry out real-time PID correction, until the revised qualitative data of PID reaches metering
During point, electromagnet cut off valve receives the shutdown signal of Weighing module feedback and closes.
Described liquid material, powder replace discharging successively, and discharging falls in premix cylinder, and described Weighing module exists
Before the detection data of duct type effusion meter are carried out real-time PID correction, first deduct and fall in premix cylinder
The quality of powder.
Powder uses the weighing system of electronics+machinery, electronic scale is integrated in PLC, as PLC's
Functional module, can be completed the process of weighing, it is also possible to according to one by the program deposited in systems
Under conditions of fixed license, the program of scale is made suitable amendment.By PLC program, electronic scale is seamless
It is integrated in PLC automatic control system, various different Weighing control can be completed, solve routine
Electronic scale instrument controls to control compatible shortcoming with PLC.Add VFC feed screw
Mechanism, by the charging curve set, the pulse expected during further reducing discharge of fine material is to metering
The impact of precision, say, that powder body discharging speed first keeps high speed constant, when will be close to before stoichiometric point
Transporting velocity is the most slack-off, reduces the impact to measuring element, improves measuring accuracy.
Metering to oil plant, syrups raw material is to use duct type mass flowmenter+Weighing module to combine
Composite mode, material is measured by mass flowmenter, and the material that effusion meter is measured by Weighing module enters
Row metering is compound to be checked so that double insurance is accomplished in the metering of material in system.In holding vessel also with
Steam spacer type heater, makes storage material viscosity keep constant when discharging, makes measuring accuracy energy
Fit like a glove and produce the requirement of high-quality product.
Raw material after various meterings being automatically sent to premix cylinder mix, premix cylinder itself is also with metering
Complex function, makes the metering safety in production process be further strengthened.
Whole system controls to perform and process record according to specific program, universal in it also avoid industry
Use all drawbacks that manual mode of operation is brought. make the safety of product, retrospective more added with protecting
Card.
Second for raw material storage system, spice add-on system:
See Fig. 4-Fig. 8, the storage of butter production line raw material, spice add-on system, store including raw material
System, spice add-on system；Described raw material storage system includes multiple memory area, each memory block
Territory has 10-20 raw material storage tank 2；Described each memory area is provided with respective first barcode scanning device,
Each storage tank is provided with respective second barcode scanning device, and each powder storage bag to be fed is provided with note
Record product category, date of manufacture, the bar code of weight；Before powder storage bag enters memory area, need
By bar code described in the first barcode scanning device identification, it is allowed for access after being verified；Powder storage bag to
In raw material storage tank 2 before charging, need to be by bar code described in the second barcode scanning device identification, secondary is verified
By rear, can feed；Described spice add-on system multiple spice adding device, each spice adds
Stepping eccentric driven pump that unit is each provided with being sequentially connected with, hybrid chamber, conveying pipe, the end of described conveying pipe
End is positioned at the top of premix cylinder, and liquid spice, powder state spice through dissolving or diluted colloidal state are fragrant
Material is by quantitative being added in described premix cylinder of respective stepping eccentric driven pump.
Described raw material storage system monitors powder according to date of manufacture, the weight information of described bar code record
Expect the real-time weight in raw material storage tank 2 and shelf-life.
The multiple of described stepping bias pump delivery is liquid spice addition.
Described hybrid chamber is used for the dissolving of powder state spice, the dilution of liquid/colloidal state spice.
Heating apparatus and the stirring vane of step-less adjustment it is provided with in described premix cylinder.
Last for surplus material cleaning system:
See Fig. 9-Figure 11, pill tank that butter production line includes being sequentially connected with, aging tank, filling machine；
The first vacuum system and the second vacuum system it is provided with, at aging tank between described pill tank and aging tank
And it is provided with the 3rd vacuum system between filling machine；Three vacuum systems each include vacuum pump, auxiliary cylinders
E2, suction target cylinder E1, by auxiliary between the cylinder mouth of described auxiliary cylinders E2 and suction target cylinder E1
Pipeline connects, and the cylinder mouth of described suction target cylinder E1 is also connected with raw material residual pipeline to be pumped；Institute
Stating vacuum pump to be connected with auxiliary cylinders E2, produce stable negative pressure in making auxiliary cylinders E2, this negative pressure makes institute
The cream raw material stated in raw material residual pipeline falls under gravity in suction target cylinder E1, and not
Can enter in auxiliary piping；Suction target cylinder E1 in first vacuum system is pill tank, by correspondence
Raw material in raw material residual pipeline first half section sucks back in pill tank；Suction target in second vacuum system
Cylinder E1 is aging tank, is sucked back in aging tank by the raw material in the corresponding raw material residual pipeline second half section；The
Suction target cylinder E1 in three vacuum systems is also aging tank, and corresponding raw material is remained the former of pipeline kind
Material sucks back in aging tank.
Second, third vacuum system described shares a vacuum pump, shares auxiliary cylinders E2, shares
One aging tank；And raw material residual pipeline to be pumped is different, and switched over by valve.
Seeing Figure 11, described butter production line surplus material cleaning system also includes cooling water system, described cold
But water system forms circulation, to auxiliary by pipeline and external impetus between vacuum pump and auxiliary cylinders E2
Cylinder E2 and vacuum pump are lowered the temperature.
Seeing Figure 11, described cooling water system includes temperature control cistern, the water outlet of described temperature control cistern
Mouth is connected with inlet pipeline；Cooling line, water return pipeline in inlet pipeline, auxiliary cylinders E2 connect successively
Connect；Water return pipeline is connected with the water return outlet of temperature control cistern；It is sequentially provided with first on described inlet pipeline
Valve V8, visor FI40, filter B 2, real-time flow meter V12, the second valve V9, circulating pump
PI1。
Seeing Figure 10, described auxiliary piping is connected with the sidewall on auxiliary cylinders E2 top, and horizontal.
When butter production line is changed shifts when, three vacuum system unlatching work, each raw material is remained
In pipeline, the cream raw material of residual is drawn in corresponding suction target cylinder E1, thus avoids raw material
The waste released, protects environment；Also avoid each order of classes or grades at school to be required in the range of specific to enter simultaneously
Row on-line cleaning, sterilization, alleviate workload, improves work efficiency.The effect of auxiliary cylinders be with
Vacuum pump matches and provides stable negative pressure, will not make in raw material suction pump, also will not suck auxiliary
In cylinder and auxiliary piping.
Being above the preferred embodiment of the present invention, those of ordinary skill in the art can be carried out rationally
Conversion, this conversion should also be as being equal to the protection domain required by claims of the present invention defining.
Claims (9)
1. a butter production line, it is characterised in that:
Including charging weighing system: described charging weighing system include powder feed weighing device,
Liquid material feeding material weighing device；Described powder feed weighing device includes powder holding vessel (3), spiral shell
Rotation propulsive mechanism (2), dolly of weighing (1), frequency conversion motor (4)；Described screw propulsion mechanism
(2) initiating terminal level is fixedly installed on the bottom of powder holding vessel (3), frequency conversion motor (1)
It is coaxially disposed with screw propulsion mechanism (2), is used for driving screw propulsion mechanism (2)；Described
It is right that the bottom of screw propulsion mechanism (2) end can coordinate with the charging aperture of dolly of weighing (1)
Connect；Described dolly of weighing (1) can be moved in horizontal rail, corresponding with above track
One row's powder holding vessel (3) matches docking；Described dolly of weighing (1) and frequency conversion motor (4)
PLC signal connect, frequency conversion motor (4) slows down step by step according to weighing-up wave, directly
Stop operating after reaching target weight to dolly of weighing；Described liquid material feeding material weighing device includes phase
The liquid material holding vessel that connects, duct type mass flowmenter；With steaming in described liquid material holding vessel
Vapour spacer type heater, makes liquid material viscosity keep constant when discharging；Described duct type quality
The line end of effusion meter arranges electromagnet cut off valve, and the opening and closing of described electromagnet cut off valve divide
Not Kong Zhi liquid material charging operation and stopping；
Also include that raw material stores system, spice add-on system: described raw material storage system includes many
Individual memory area, each memory area has 10-20 raw material storage tank；Described each storage
Region is provided with respective first barcode scanning device, and each storage tank is provided with respective second barcode scanning dress
Putting, each powder storage bag to be fed is provided with record product kind, date of manufacture, weight
Bar code；Powder storage bag enters before memory area, need to be by the first barcode scanning device identification institute
State bar code, be allowed for access after being verified；Powder storage bag stores before ladle addition to raw material,
, can need to be fed after secondary is verified by bar code described in the second barcode scanning device identification；
Described spice add-on system multiple spice adding device, each spice adding device is each provided with depending on
The stepping eccentric driven pump of secondary connection, hybrid chamber, conveying pipe, the end of described conveying pipe is positioned at premix
The top of cylinder, liquid spice, through dissolve powder state spice or diluted colloidal state spice pass through
What respective stepping eccentric driven pump was quantitative is added in described premix cylinder；
Also include surplus material cleaning system: pill tank that described butter production line includes being sequentially connected with,
Aging tank, filling machine；The first vacuum system and it is provided with between described pill tank and aging tank
Two vacuum systems, are provided with the 3rd vacuum system between aging tank and filling machine；Three vacuum systems
System each includes vacuum pump, auxiliary cylinders (E2), suction target cylinder (E1), described auxiliary cylinders (E2)
And it is connected by auxiliary piping between the cylinder mouth of suction target cylinder (E1), described suction target cylinder
(E1) cylinder mouth is also connected with raw material residual pipeline to be pumped；Described vacuum pump and auxiliary cylinders
(E2) connecting, produce stable negative pressure in making auxiliary cylinders (E2), this negative pressure makes described raw material
Cream raw material in residual pipeline falls under gravity in suction target cylinder (E1), and
Will not enter in auxiliary piping；Suction target cylinder (E1) in first vacuum system is pill tank,
Raw material in corresponding raw material residual pipeline first half section is sucked back in pill tank；Second vacuum system
In suction target cylinder (E1) be aging tank, by the corresponding raw material residual pipeline second half section
Raw material sucks back in aging tank；Suction target cylinder (E1) in 3rd vacuum system is also aging tank,
The raw material of corresponding raw material residual pipeline kind is sucked back in aging tank.
2. butter production line as claimed in claim 1, it is characterised in that: the charging of described liquid material is weighed dress
Putting the premix cylinder also including Weighing module, mixing for powder and liquid material, described Weighing module sets
Put in the lower section of premix cylinder and the material in premix cylinder is weighed；Described Weighing module and pipe
Road formula mass flowmenter signal connects, and the data recorded for duct type mass flowmenter are carried out
PID revises, until obtaining the last aimed quality data revised, described electromagnet cut off valve is closed.
3. the butter production line described in a claim 1, it is characterised in that:
During discharge of fine material: frequency conversion motor (4) first keeps constant high velocity, when before stoichiometric point,
Frequency conversion motor (4) gradually slows down, and transporting velocity slows down gradually until stopping when reaching stoichiometric point；
During liquid material discharging: duct type effusion meter real time record discharging quality, Weighing module carries out reality
Execute and weigh, and the detection data of duct type effusion meter are carried out real-time PID correction, until PID
When revised qualitative data reaches stoichiometric point, electromagnet cut off valve receives the pass of Weighing module feedback
Close signal and close.
4. butter production line as claimed in claim 3, it is characterised in that: described liquid material, powder are successively
Alternately discharging, discharging falls in premix cylinder, and described Weighing module is in the inspection to duct type effusion meter
Survey before data carry out real-time PID correction, first deduct and fall into the quality of powder in premix cylinder.
5. butter production line as claimed in claim 1, it is characterised in that: described raw material storage system root
Powder is monitored in raw material storage tank (2) according to date of manufacture, the weight information of described bar code record
In real-time weight and the shelf-life.
6. butter production line as claimed in claim 1, it is characterised in that: the row of described stepping eccentric driven pump
The multiple of amount is liquid spice addition.
7. butter production line as claimed in claim 1, it is characterised in that: second, third vacuum described
System shares a vacuum pump, shares an auxiliary cylinders (E2), shares an aging tank；And
Raw material residual pipeline to be pumped is different, and is switched over by valve.
8. butter production line as claimed in claim 1, it is characterised in that: the surplus material of described butter production line
Cleaning system also includes cooling water system, and described cooling water system is existed by pipeline and external impetus
Form circulation between vacuum pump and auxiliary cylinders (E2), auxiliary cylinders (E2) and vacuum pump are carried out
Cooling.
9. butter production line as claimed in claim 1, it is characterised in that:
Described cooling water system includes temperature control cistern, the outlet of described temperature control cistern with enter
Water lines connects；Cooling line in inlet pipeline, auxiliary cylinders (E2), water return pipeline are successively
Connect；Water return pipeline is connected with the water return outlet of temperature control cistern；
The first valve (V8), visor (FI40), filter it is sequentially provided with on described inlet pipeline
(B2), real-time flow meter (V12), the second valve (V9), circulating pump (PI1).
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| CN201610465790.XA CN105961607B (en) | 2016-06-24 | 2016-06-24 | Cream production line |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610465790.XA CN105961607B (en) | 2016-06-24 | 2016-06-24 | Cream production line |
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| CN105961607A true CN105961607A (en) | 2016-09-28 |
| CN105961607B CN105961607B (en) | 2023-02-24 |
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| CN201610465790.XA Active CN105961607B (en) | 2016-06-24 | 2016-06-24 | Cream production line |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108308508A (en) * | 2018-03-26 | 2018-07-24 | 上海冠生园蜂制品有限公司 | A kind of high viscosity liquid food semi-finished product traceability system |
| CN109132980A (en) * | 2018-09-28 | 2019-01-04 | 广东浪淘砂新型材料有限公司 | A kind of method of ingredient automatic identification charging |
| CN112021411A (en) * | 2020-07-30 | 2020-12-04 | 上海海融食品科技股份有限公司 | Online bubble removing device and method for cream production line |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102657259A (en) * | 2012-06-05 | 2012-09-12 | 光明乳业股份有限公司 | Device and method for producing additive-free yogurt |
| CN202680372U (en) * | 2012-06-05 | 2013-01-23 | 光明乳业股份有限公司 | Device for producing yogurt without additives |
| CN203563635U (en) * | 2013-07-10 | 2014-04-30 | 上海海融食品工业有限公司 | Mixing and circulating system for cream ingredients |
| CN206213154U (en) * | 2016-06-24 | 2017-06-06 | 上海海融食品科技股份有限公司 | A kind of cream production line |
-
2016
- 2016-06-24 CN CN201610465790.XA patent/CN105961607B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102657259A (en) * | 2012-06-05 | 2012-09-12 | 光明乳业股份有限公司 | Device and method for producing additive-free yogurt |
| CN202680372U (en) * | 2012-06-05 | 2013-01-23 | 光明乳业股份有限公司 | Device for producing yogurt without additives |
| CN203563635U (en) * | 2013-07-10 | 2014-04-30 | 上海海融食品工业有限公司 | Mixing and circulating system for cream ingredients |
| CN206213154U (en) * | 2016-06-24 | 2017-06-06 | 上海海融食品科技股份有限公司 | A kind of cream production line |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108308508A (en) * | 2018-03-26 | 2018-07-24 | 上海冠生园蜂制品有限公司 | A kind of high viscosity liquid food semi-finished product traceability system |
| CN109132980A (en) * | 2018-09-28 | 2019-01-04 | 广东浪淘砂新型材料有限公司 | A kind of method of ingredient automatic identification charging |
| CN109132980B (en) * | 2018-09-28 | 2021-06-22 | 广东浪淘砂新型材料有限公司 | Method for automatically identifying components for charging |
| CN112021411A (en) * | 2020-07-30 | 2020-12-04 | 上海海融食品科技股份有限公司 | Online bubble removing device and method for cream production line |
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| Publication number | Publication date |
|---|---|
| CN105961607B (en) | 2023-02-24 |
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