CN106085840B - The pipe-line transportation system of KLP-602 sodium alginate micro ball production line and purging system on the spot - Google Patents
The pipe-line transportation system of KLP-602 sodium alginate micro ball production line and purging system on the spot Download PDFInfo
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Abstract
The invention discloses a kind of pipe-line transportation system of KLP-602 sodium alginate micro ball production line and purging system on the spot, mainly by soft water manufacture system, water softening tank, water pump, hot-water cylinder, first sanitary pump, automatic temperature-controlled water heater funnel, six procedure systems, master controller, the whole pipeline work system of a series of stainless steel sanitary pipe and a series of hygiene-type operated pneumatic valves composition KLP-602 sodium alginate micro ball production line, the effective production efficiency improved in production process and product are safe and healthy, improve Workshop Production environment and mitigate the productive labor intensity of operator, it is advantageously implemented KLP-602 sodium alginate micro ball large-scale production, it is advantageously implemented KLP-602 sodium alginate micro ball prepare with scale.The present invention can carry out force feed to leftover materials in pipeline by designated program and rinse, and hygienic requirements of the food to equipment is fully achieved in once purged pipeline, using closed circuit purging system, makes the production environment in whole workshop better.
Description
Technical field
The present invention relates to a kind of pipe-line transportation system and cleaning device, is used for material more particularly to one kind and product conveys
System and cleaning device, applied to protease solidification granulating technique field.
Background technology
KLP-602 sodium alginate micro ball is the upgrading products of antalzyme protein enzyme, is manufactured experimently through laboratory for many years,
It is transformed into production practices on the basis of succeeding and goes to be a kind of urgent need.In the lab, lysozyme dimerization
The manufacturing equipment of body sodium alginate micro ball is microminiature, and working procedure is to rely on laboratory worker, and work is made in upper track
After sequence terminates, continue processing, the obvious nothing of its preparation method in lower road equipment through manually taking out and being placed to from upper track equipment
Method meets the batch production of product.How the manufacture method that from laboratory obtains and technical parameter are utilized, and effective improve is given birth to
The production efficiency of product and safe and healthy during production, improve Workshop Production environment and mitigate operator productive labor it is strong
Degree, turn into technical problem urgently to be resolved hurrily at present.
The content of the invention
In order to solve prior art problem, it is an object of the present invention to overcome the deficiencies of the prior art, and to provide one kind
The pipe-line transportation system of KLP-602 sodium alginate micro ball production line and purging system on the spot, effectively improve production process
In production efficiency and product it is safe and healthy, improve Workshop Production environment simultaneously mitigate the productive labor intensity of operator, favorably
In realizing KLP-602 sodium alginate micro ball large-scale production, present system can be cleaned on the spot, and food is fully achieved
Hygienic requirements of the product to equipment.
Purpose is created to reach foregoing invention, using following technical proposals：
A kind of pipe-line transportation system of KLP-602 sodium alginate micro ball production line and purging system on the spot, whole work
Make system mainly by soft water manufacture system, water softening tank, water pump, hot-water cylinder, the first sanitary pump, automatic temperature-controlled water heater funnel,
First flowmeter, sodium alginate high-shear dissolution tank, second flowmeter, KLP-602 diluent preparing tank, the second health
Pump, mixed liquor flowmeter, KLP-602 sodium alginate soln prepare degassing and pressure transfer pot, water curtain style solidification are granulated
Cylinder, the 3rd sanitary pump, separation of solid and liquid filtering cloth jar, the 4th sanitary pump, calcium chloride solution dissolve storagetank, ultraviolet sterilizer, consolidated
Liquid separating and filtering hanging basket, ebullated dryer, master controller, a series of stainless steel sanitary pipe and a series of hygiene-type operated pneumatic valves
Composition, so as to form the whole pipeline work system of KLP-602 sodium alginate micro ball production line, whole pipeline is defeated
Work system is sent to be controlled by master controller, and using PLC is controlled hot water heating by touch-screen, sodium alginate height is cut
Cut dissolving, KLP-602 diluent preparing, KLP-602 sodium alginate soln preparation degassing and pressure conveying, water curtain
Formula solidification granulation, separation of solid and liquid, separating liquid reuse, solid resultant product collection series of process process, when upper track manufacturing procedure is completed
Afterwards, master controller is controlled by the combination to the exclusive pump of each target subsystem, materail tube, flowmeter and operated pneumatic valve, by mesh
The feed liquid material automatic transport of mark subsystem output is processed or handled to next procedure, until last procedure is completed,
Purging system on the spot is also provided with, in each subsystem of the pipe-line transportation system of bacterium enzyme dimer sodium alginate micro ball production line
After corresponding per pass manufacturing procedure terminates, corresponding subsystem is vacuumized, using vacuum, using running water or soft water,
By master controller designated program, to leftover materials carry out force feed simultaneously in the Work container of subsystem and in interconnected materail tube
Rinse, it is molten in sodium alginate high-shear dissolution tank, KLP-602 diluent preparing tank and KLP-602 sodium alginate
Liquid is prepared in degassing and pressure transfer pot, the temperature that required temperature is set by soft water by automatic temperature-controlled water heater funnel
Obtain, and degassing and pressure transfer pot are prepared in sodium alginate high-shear dissolution tank and KLP-602 sodium alginate soln
Constant-temperature hot water is set to circulate heat-insulation system in chuck in Work container wall, it is soft by being flowed in constant-temperature hot water circulation heat-insulation system
Liquid material of the heat that water carries into Work container is transmitted, and the concentration of the feed liquid in each subsystem is by exclusive flow
Meter carries out metering conveying to dispensing liquid, and is put into after being weighed using weight measurer to solid material, make dispensing liquid with
Solid material prepare the preparation of liquid, and in whole pipeline work system, raw water enters soft water through soft water manufacture system
Tank turns into soft water, then soft water is entered hot-water cylinder through water pump, and soft water then is sent into automatic temperature-controlled hot water by the first sanitary pump
Heating system forms hot water, hot water is prepared sodium alginate high-shear dissolution tank and KLP-602 sodium alginate soln de-
Gas and pressure transfer pot carry out heated at constant temperature.
As currently preferred technical scheme, the pipe-line transportation system of KLP-602 sodium alginate micro ball production line
At least six procedure systems are included with purging system on the spot, are specially：
In first of working procedure systems, measured through first flowmeter, the hot water of nominal volume, which is added sodium alginate height, to be cut
Cut in dissolving tank, the hot water of the nominal volume after being computed is matched somebody with somebody through the metered KLP-602 dilution of second flowmeter
In tank processed, and wait the cold water of next procedure to add, the sodium alginate pulvis after weighed metering is added by the entrance that feeds
Sodium alginate high-shear dissolution tank, carry out the quick dissolving of high shear and prepare sodium alginate soln, complete in first of working procedure systems
Middle process；
In second operation work system, the soft water of the nominal volume of the set water temperature after being computed through second flowmeter meter
Amount is added into KLP-602 diluent preparing tank, is reached in KLP-602 diluent preparing tank soft water temperature and is set
Constant temperature degree, and opening electric heater makes in KLP-602 diluent preparing tank water temperature be maintained at design temperature level, matching somebody with somebody
Hinge agent after the completion of system is quantitatively adding hinge agent tank, then is titrated through hinge agent tank to KLP-602 diluent preparing tank
Add and dissolving is stirred by agitating device, prepare KLP-602 dilution, complete in second operation work system
Process；
In three process system, by the KLP-602 dilution after second operation work is processed through lysozyme two
Aggressiveness diluent preparing tank is pumped into sodium alginate high-shear dissolution tank by the second health, prepares mixed liquor, liquid to be diluted
After conveying, hot soft water valve is opened, it is tank connected through the second sanitary pump handle and sodium alginate high-shear dissolution using hot soft water
The surplus dilution whole force feed of product enters sodium alginate high-shear dissolution tank in pipeline, and after force feed, utilizes hot soft water pair
It is rinsed with the tank connected segment pipe of sodium alginate high-shear dissolution, the liquid after flushing is discharged through special waste pipe,
Complete the process in three process system；
In the 4th procedure system, open KLP-602 sodium alginate soln and prepare in degassing and pressure transfer pot
Vacuum valve, after the blended feed liquid flowmeter metering of mixed liquor in sodium alginate high-shear dissolution tank, be inhaled into lysozyme
The preparation of dimer sodium alginate soln deaerates and pressure transfer pot, after the mixed liquor conveying capacity of need to be achieved, closes alginic acid
Outlet valve below sodium high-shear dissolution tank, the air pressure valve of compressed gas source is opened, using feeder is compressed, by outlet valve
Product in the conveyance conduit of lower section remains mixed liquor whole force feed to KLP-602 sodium alginate soln and prepares degassing and pressure
In power transfer pot, and air pressure valve is closed after force feed, open hot water valve, utilize conveying of the hot water below outlet valve
Pipeline is rinsed, and the liquid after flushing is discharged through special waste pipe, completes the process in the 4th procedure system；
In five processes system, running water is added to calcium chloride solution dissolving storage after the metering of originally water ga(u)ge
In groove, the calcium chloride after weighing apparatus Weighing is added to calcium chloride solution dissolving storagetank, and carries out stirring and dissolving, is used
Conductivity gauge detection calcium chloride solution dissolves the calcium chloride solution concentration prepared in storagetank and shown, it is dense to reach production requirement
The calcium chloride solution of degree is sterilized after the conveying of the 5th sanitary pump, then by ultraviolet sterilizer, is made into water curtain style solidification
In grain cylinder, the umbrella shape water curtain of calcium chloride solution is formed, while utilizes blowing plant, KLP-602 sodium alginate is molten
The mixed liquor force feed that liquid is prepared in degassing and pressure transfer pot enters water curtain style solidification and is granulated cylinder, is solidified by water curtain style and is granulated
The fan pressure nozzle assembly of cylinder carries out atomized spray, solidifies in water curtain style and is granulated formation fan-shaped liquid mist in cylinder, penetrates liquid mist
To the umbrella shape water curtain of calcium chloride solution, and KLP-602 sodium alginate micro ball is rapidly condensed into, carries out solidification granulation, condensed
KLP-602 sodium alginate micro ball be pumped into separation of solid and liquid filtering cloth jar through the 3rd health together with calcium chloride solution, solid
In liquid separating and filtering cylinder, the solution after separation of solid and liquid is transmitted back in calcium chloride solution dissolving storagetank through the 4th sanitary pump
Row is reused, until mist projection granulating code terminates, completes the process in five processes system；
In the 6th procedure system, hanging basket is filtered by the separation of solid and liquid in driving hanging out separation of solid and liquid filtering cloth jar, taken
Go out KLP-602 sodium alginate particulate matter in the filter screen of separation of solid and liquid filtering hanging basket, and by KLP-602 sodium alginate
Particulate matter is transferred to ebullated dryer and carries out last drying process processing together, finally gives KLP-602 sodium alginate
Finished microballoon products.
As the further preferred technical scheme of such scheme of the present invention, to sodium alginate high-shear dissolution tank, bacteriolyze
Enzyme dimer diluent preparing tank, KLP-602 sodium alginate soln prepare degassing and pressure transfer pot and water curtain style solidification
It is granulated in cylinder and is respectively equipped with spray cleaning system.
As the further preferred technical scheme of such scheme of the present invention, calcium chloride solution dissolving storagetank is provided with circulation
Cool down water cooling system and auxiliary waste solution channel exhaust system.
The present invention compared with prior art, has following obvious prominent substantive distinguishing features and remarkable advantage：
1. the present invention extends processing in the case where maintaining the basis for testing obtained manufacturing process principle and significant data
The ability of equipment and the automatic conveying system of upper next procedure, the effective production efficiency and health improved in production process
Safety, improve Workshop Production environment and alleviate the productive labor intensity of operator, make experimental result be entirely applied to produce
Field；
2. the present invention can carry out force feed to leftover materials in pipeline by designated program and rinse materail tube, once purged pipe
Hygienic requirements of the food to equipment can be fully achieved in road, using closed circuit purging system, make the production environment in whole workshop better.
Brief description of the drawings
Fig. 1 is the sodium alginate dissolution process pipe-line transportation system when device of the embodiment of the present invention one performs the first procedure
Process chart.
Fig. 2 is the KLP-602 diluent preparing process pipe when device of the embodiment of the present invention one performs second operation work
Pipeline conveying system process chart.
Fig. 3 is KLP-602 dilution when the device of the embodiment of the present invention one performs three process from lysozyme two
Aggressiveness diluent preparing tank is delivered to sodium alginate high-shear dissolution tank pipe-line transportation system process chart.
Fig. 4 is that the lysozyme dimerization sodium alginate when device of the embodiment of the present invention one performs four procedures prepares liquid from sea
Mosanom high-shear dissolution tank is delivered to KLP-602 sodium alginate soln and prepares degassing and pressure transfer pot pipeline
System process.
Fig. 5 is that the KLP-602 sodium alginate when device of the embodiment of the present invention one performs five processes prepares liquid certainly
KLP-602 sodium alginate soln prepares degassing and pressure transfer pot is delivered to water curtain style solidification and is granulated cylinder and calcium chloride
Solution is delivered to water curtain style solidification from calcium chloride solution dissolving storagetank and is granulated earthen pipe pipeline conveying system process chart.
KLP-602 sodium alginate particle when Fig. 6 is the device of the embodiment of the present invention one six procedure of execution is from admittedly
Liquid separating and filtering cylinder is transported to ebullated dryer procedure technology flow chart.
Embodiment
Details are as follows for the preferred embodiments of the present invention：
Embodiment one：
In the present embodiment, referring to Fig. 1~6, a kind of pipeline of KLP-602 sodium alginate micro ball production line
System and purging system on the spot, whole work system is mainly by soft water manufacture system 1, water softening tank 2, water pump 3, hot-water cylinder 4, first
Sanitary pump 5, automatic temperature-controlled water heater funnel 6, first flowmeter 7, sodium alginate high-shear dissolution tank 8, second flowmeter 9,
KLP-602 diluent preparing tank 10, the second sanitary pump 13, mixed liquor flowmeter 14, KLP-602 sodium alginate
Solution prepare degassing and pressure transfer pot 15, water curtain style solidification be granulated cylinder 16, the 3rd sanitary pump 17, separation of solid and liquid filtering cloth jar 18,
4th sanitary pump 19, calcium chloride solution dissolving storagetank 20, ultraviolet sterilizer 24, separation of solid and liquid filtering hanging basket 25, boiling are dry
Dry device 26, master controller, a series of stainless steel sanitary pipe and a series of hygiene-type operated pneumatic valves composition, so as to form lysozyme
The whole pipeline work system of dimer sodium alginate micro ball production line, whole pipeline work system is by master controller
It is controlled, and hot water heating, sodium alginate high-shear dissolution, KLP-602 is controlled by touch-screen using PLC
Diluent preparing, KLP-602 sodium alginate soln prepare degassing and pressure conveying, water curtain style solidification granulation, solid-liquid point
From, separating liquid reuse, solid resultant product collection series of process process, after the completion of upper track manufacturing procedure, it is right that master controller passes through
The combination of the exclusive pump, materail tube, flowmeter and operated pneumatic valve of each target subsystem controls, by the feed liquid of target subsystem output
Material automatic transport is processed or handled to next procedure, until completing last procedure, is also provided with cleaning on the spot and is
System, per pass manufacturing procedure corresponding to each subsystem in the pipe-line transportation system of bacterium enzyme dimer sodium alginate micro ball production line
After end, corresponding subsystem is vacuumized, using vacuum, using running water or soft water, by master controller designated program,
Force feed is carried out to leftover materials in the Work container of subsystem and in interconnected materail tube and rinsed, is cut in sodium alginate height
Cut dissolving tank 8, KLP-602 diluent preparing tank 10 and KLP-602 sodium alginate soln and prepare degassing and pressure
In transfer pot 15, the temperature that required temperature is set by soft water by automatic temperature-controlled water heater funnel 6 obtains, and in marine alga
Sour sodium high-shear dissolution tank 8 and KLP-602 sodium alginate soln prepare the Work container wall of degassing and pressure transfer pot 15
Set constant-temperature hot water to circulate heat-insulation system in interior chuck, constant-temperature hot water is circulated to the heat that the soft water flowed in heat-insulation system carries
The liquid material measured into Work container is transmitted, and the concentration of the feed liquid in each subsystem is by exclusive flowmeter to proportion liquid
Body carries out metering conveying, and is put into after being weighed using weight measurer to solid material, dispensing liquid is entered with solid material
Row prepares the preparation of liquid, and in whole pipeline work system, raw water enters water softening tank 2 through soft water manufacture system 1 turns into soft
Water, then soft water is entered hot-water cylinder 4 through water pump 3, soft water is then sent into automatic temperature-controlled hot water heating system by the first sanitary pump 5
System 6 forms hot water, and softening hot water makes hot water to sodium alginate high-shear dissolution tank 8 and molten after reaching 55 DEG C of technological requirement
Bacterium enzyme dimer sodium alginate soln prepares degassing and pressure transfer pot 15 carries out heated at constant temperature, with the perseverance of above-mentioned Work container
Temperature characteristics.
In the present embodiment, referring to Fig. 1~6, the pipe-line transportation system of KLP-602 sodium alginate micro ball production line
At least six procedure systems are included with purging system on the spot, are specially：
In first of working procedure systems, measured through first flowmeter 7, nominal volume 1500L hot water is added alginic acid
In sodium high-shear dissolution tank 8, the hot water of the nominal volume after being computed through 9 metered KLP-602 of second flowmeter
In diluent preparing tank 10, and the cold water of next procedure is waited to add, the sodium alginate pulvis after weighed metering by adding
Expect that entrance adds sodium alginate high-shear dissolution tank 8, carry out the quick dissolving of high shear and prepare sodium alginate soln, complete first
Process in procedure system, referring to Fig. 1；
In second operation work system, by mixing the technique of water method regulation water temperature, after the calculating of second flowmeter 9,
Coolant-temperature gage up to 55 DEG C of nominal volume 78L hot soft water are added into KLP-602 dilution through the metering of second flowmeter 9 and matched somebody with somebody
In tank 10 processed, then again through second flowmeter 9 calculating after, coolant-temperature gage up to 15 DEG C of nominal volume 372L cold soft water through second
The metering of flowmeter 9 is added into KLP-602 diluent preparing tank 10, is made in KLP-602 diluent preparing tank 10
22 DEG C of soft water 450L are obtained, being then turned on electric heater 11 is maintained at water temperature in KLP-602 diluent preparing tank 10
25 DEG C of design temperature is horizontal, and the hinge agent after the completion of preparation is quantitatively adding hinge agent tank 12, then through hinge agent tank 12 to molten
Bacterium enzyme dimer diluent preparing tank 10 makees titration and adds and be stirred dissolving by agitating device, prepares KLP-602
Dilution, the process in second operation work system is completed, referring to Fig. 2；
In three process system, by the KLP-602 dilution after second operation work is processed through lysozyme two
Aggressiveness diluent preparing tank 10 is sent into sodium alginate high-shear dissolution tank 8 by the second sanitary pump 13, prepares mixed liquor, treats dilute
After releasing liquid conveying, open hot soft water valve, using time controlled system module, using hot soft water through the second sanitary pump 13 with
The surplus dilution whole force feed of product enters sodium alginate high-shear dissolution tank 8 in the pipeline that sodium alginate high-shear dissolution tank 8 connects,
Reach set time value and be automatically stopped force feed, and after force feed, it is molten using hot soft water pair and sodium alginate high shear
The segment pipe that solution tank 8 connects is rinsed, and the liquid after flushing is discharged through special waste pipe, is completed in three process system
Process in system, referring to Fig. 3；
In the 4th procedure system, open KLP-602 sodium alginate soln and prepare degassing and pressure transfer pot 15
On vacuum valve, make KLP-602 sodium alginate soln prepare degassing and pressure transfer pot 15 in vacuum reach -0.085Mpa,
After the blended feed liquid flowmeter 14 of mixed liquor in sodium alginate high-shear dissolution tank 8 measures, inhaled 500L mixed liquors
Enter KLP-602 sodium alginate soln prepare degassing and pressure transfer pot 15, it is to be achieved need to mixed liquor conveying capacity after,
The outlet valve of the lower section of sodium alginate high-shear dissolution tank 8 is closed, opens the air pressure valve of compressed gas source, utilizes compression supply dress
Put, the product in the conveyance conduit below outlet valve is remained into mixed liquor whole force feed to KLP-602 sodium alginate soln matches somebody with somebody
In system degassing and pressure transfer pot 15, defoaming is de-gassed, and air pressure valve is closed after force feed, opens hot water valve,
It is rinsed using conveyance conduit of the hot water below outlet valve, the liquid after flushing is discharged through special waste pipe, is completed
The process in the 4th procedure system, referring to Fig. 4；
In five processes system, it is molten that the running water 2000L after the metering of originally water ga(u)ge 21 is added to calcium chloride
In liquid dissolving storagetank 20, the calcium chloride after weighing apparatus Weighing is added to calcium chloride solution dissolving storagetank 20, gone forward side by side
Row stirring and dissolving, the calcium chloride solution concentration prepared in calcium chloride solution dissolving storagetank 20 and progress are detected using conductivity gauge 22
It has been shown that, observed for operator and production technology is adjusted and intervened, when conductivity gauge 22 shows calcium chloride solution dissolving storage
When calcium chloride solution concentration in groove 20 is 10wt.%, stop addition calcium chloride, then the calcium chloride by concentration for 10wt.%
Solution is sterilized after the conveying of the 5th sanitary pump 23, then by ultraviolet sterilizer 24, is solidified into water curtain style and is granulated cylinder 16
In, the umbrella shape water curtain of calcium chloride solution is formed, while blowing plant is utilized, match somebody with somebody KLP-602 sodium alginate soln
Pressure rises to 1.1 bars in system degassing and pressure transfer pot 15, and KLP-602 sodium alginate soln is prepared into degassing and pressure
Mixed liquor force feed in power transfer pot 15 enters water curtain style solidification and is granulated cylinder 16, solidifies be granulated cylinder 16 34 groups by water curtain style
Fan pressure nozzle assembly carries out atomized spray, solidifies in water curtain style and is granulated formation fan-shaped liquid mist in cylinder 16, makes liquid mist directive
The umbrella shape water curtain of calcium chloride solution, and KLP-602 sodium alginate micro ball is rapidly condensed into, solidification granulation is carried out, cohesion
KLP-602 sodium alginate micro ball is sent into separation of solid and liquid filtering cloth jar 18 together with calcium chloride solution through the 3rd sanitary pump 17,
In separation of solid and liquid filtering cloth jar 18, the solution after separation of solid and liquid is transmitted back to calcium chloride solution dissolving storage through the 4th sanitary pump 19
Reused in groove 20, until mist projection granulating code terminates, the process in five processes system is completed, referring to figure
5；
In the 6th procedure system, hanging basket is filtered by the separation of solid and liquid in driving hanging out separation of solid and liquid filtering cloth jar 18
25, KLP-602 sodium alginate particulate matter in the artificial filter screen for taking out separation of solid and liquid filtering hanging basket 25, and by lysozyme two
Aggressiveness sodium alginate particulate matter is transferred to ebullated dryer 26 and carries out last drying process processing together, finally gives lysozyme
Dimer sodium alginate micro ball finished product, referring to Fig. 6.
In the present embodiment, referring to Fig. 1~6, sodium alginate high-shear dissolution tank 8, KLP-602 dilution are matched somebody with somebody
Tank 10, KLP-602 sodium alginate soln preparation degassing and pressure transfer pot 15 processed and water curtain style solidification are granulated in cylinder 16 and divided
She You not spray cleaning system.
After the completion of the production technology that the present embodiment device is implemented, pass through the cleaning installed in basin using the pressure of soft hot water
Spray ball causes jet power, respectively to sodium alginate high-shear dissolution tank 8, KLP-602 diluent preparing tank 10 and lysozyme
Dimer sodium alginate soln prepares degassing and pressure transfer pot 15 carries out clear Xian on the spot, and the liquid after being cleaned to each tank
Deliver to special waste pipe to be discharged, once purged pipeline and Work container can be fully achieved food and want the health of equipment
Ask.
The present embodiment KLP-602 sodium alginate micro ball prepares the pipe-line transportation system of production line through designing and installing
After the completion of, operate in actual production process, achieve good Expected Results.The present embodiment apparatus system can by pump,
Materail tube, operated pneumatic valve and PLC by programming are controlled a upper track feed liquid automatic transport by touch-screen and entered to next procedure
Row feed liquid or materiel machining and processing, until complete last procedure, the whole technological process of production it is increasingly automated, not only
The labor intensity of operator is alleviated, greatly improves production capacity and economic benefit, while is avoided because of manually operated possibility
Caused by error caused by unnecessary loss.
Embodiment two：
The present embodiment and embodiment one are essentially identical, are particular in that：
In the present embodiment, in five processes system, calcium chloride solution dissolving storagetank 20 is provided with recirculated cooling water
Cooling system and auxiliary waste solution channel exhaust system, ensure that calcium chloride solution can preserve for a long time, the present embodiment is also equipped with special
Track Lift-on/Lift-off System, hanging basket is filtered to appointed place for lifting by crane and transporting separation of solid and liquid, makes the production environment in whole workshop more
Well, the productive labor intensity of operator can be mitigated and make production environment better.
The embodiment of the present invention is illustrated above in conjunction with accompanying drawing, but the invention is not restricted to above-described embodiment, can be with
A variety of changes are made according to the purpose of the innovation and creation of the present invention, under all Spirit Essence and principle according to technical solution of the present invention
Change, modification, replacement, combination or the simplification made, should be equivalent substitute mode, as long as meeting the goal of the invention of the present invention,
Without departing from the pipe-line transportation system and purging system on the spot of KLP-602 sodium alginate micro ball production line of the present invention
Technical principle and inventive concept, belong to protection scope of the present invention.
Claims (4)
1. a kind of pipe-line transportation system of KLP-602 sodium alginate micro ball production line with purging system, its feature exist on the spot
In：Whole work system is mainly by soft water manufacture system (1), water softening tank (2), water pump (3), hot-water cylinder (4), the first sanitary pump
(5), automatic temperature-controlled water heater funnel (6), first flowmeter (7), sodium alginate high-shear dissolution tank (8), second flowmeter
(9), KLP-602 diluent preparing tank (10), the second sanitary pump (13), mixed liquor flowmeter (14), lysozyme dimerization
Body sodium alginate soln prepares degassing and pressure transfer pot (15), water curtain style solidification are granulated cylinder (16), the 3rd sanitary pump (17), solid
Liquid separating and filtering cylinder (18), the 4th sanitary pump (19), calcium chloride solution dissolve storagetank (20), ultraviolet sterilizer (24), consolidated
Liquid separating and filtering hanging basket (25), ebullated dryer (26), master controller, a series of stainless steel sanitary pipe and a series of hygiene-types
Operated pneumatic valve forms, whole so as to form the whole pipeline work system of KLP-602 sodium alginate micro ball production line
Individual pipeline work system is controlled by master controller, and is controlled hot water heating, marine alga by touch-screen using PLC
Sour sodium high-shear dissolution, KLP-602 diluent preparing, KLP-602 sodium alginate soln prepare degassing and pressure
Conveying, water curtain style solidification granulation, separation of solid and liquid, separating liquid reuse, solid resultant product collection series of process process, when upper track is processed
After the completion of process, master controller passes through the combination control to the exclusive pump of each target subsystem, materail tube, flowmeter and operated pneumatic valve
System, the feed liquid material automatic transport of target subsystem output is processed or handled to next procedure, until completing last
Procedure, be also provided with purging system on the spot, bacterium enzyme dimer sodium alginate micro ball production line pipe-line transportation system it is every
After per pass manufacturing procedure terminates corresponding to individual subsystem, corresponding subsystem is vacuumized, using vacuum, using running water
Or soft water, by master controller designated program, to leftover materials enter in the Work container of subsystem and in interconnected materail tube
Row force feed simultaneously rinses, in sodium alginate high-shear dissolution tank (8), KLP-602 diluent preparing tank (10) and lysozyme two
Aggressiveness sodium alginate soln is prepared in degassing and pressure transfer pot (15), and required temperature passes through automatic temperature-controlled hot water by soft water
The temperature of heating system (6) setting obtains, and molten in sodium alginate high-shear dissolution tank (8) and KLP-602 sodium alginate
Liquid, which is prepared in the chuck in the Work container wall of degassing and pressure transfer pot (15), sets constant-temperature hot water to circulate heat-insulation system, by perseverance
Liquid material of the heat that the soft water flowed in warm water circulation heat-insulation system carries into Work container is transmitted, and is at each point
The concentration of feed liquid in system carries out metering conveying to dispensing liquid by exclusive flowmeter, and using weight measurer to solid material
Put into after being weighed, dispensing liquid with solid material prepare the preparation of liquid, in whole pipeline work system,
Raw water enters water softening tank (2) through soft water manufacture system (1) turns into soft water, then soft water is entered hot-water cylinder (4) through water pump (3), so
Soft water is sent into automatic temperature-controlled water heater funnel (6) by the first sanitary pump (5) afterwards and forms hot water, makes hot water to sodium alginate
High-shear dissolution tank (8) and KLP-602 sodium alginate soln prepare degassing and pressure transfer pot (15) carries out constant temperature and added
Heat.
2. the pipe-line transportation system of KLP-602 sodium alginate micro ball production line with cleaning on the spot according to claim 1
System, it is characterised in that the pipe-line transportation system of KLP-602 sodium alginate micro ball production line and purging system bag on the spot
Containing at least six procedure systems, it is specially：
In first of working procedure systems, measured through first flowmeter (7), the hot water of nominal volume is added sodium alginate high shear
In dissolving tank (8), the hot water of the nominal volume after being computed is diluted through the metered KLP-602 of second flowmeter (9)
In liquid preparing tank (10), and wait the cold water of next procedure to add, the sodium alginate pulvis after weighed metering is passed through charging
Entrance adds sodium alginate high-shear dissolution tank (8), carries out the quick dissolving of high shear and prepares sodium alginate soln, completes first
Process in procedure system；
In second operation work system, the soft water of the nominal volume of the set water temperature after being computed is counted through second flowmeter (9)
Amount is added into KLP-602 diluent preparing tank (10), makes the interior soft water temperature of KLP-602 diluent preparing tank (10)
Degree reaches design temperature, and opening electric heater (11) is maintained at KLP-602 diluent preparing tank (10) interior water temperature to set
Determine temperature levels, the hinge agent after the completion of preparation is quantitatively adding hinge agent tank (12), then through hinge agent tank (12) to lysozyme
Dimer diluent preparing tank (10) makees titration and adds and be stirred dissolving by agitating device, and it is dilute to prepare KLP-602
Liquid is released, completes the process in second operation work system；
In three process system, by the KLP-602 dilution after second operation work is processed through KLP-602
Diluent preparing tank (10) is sent into sodium alginate high-shear dissolution tank (8) by the second sanitary pump (13), prepares mixed liquor, treats
After dilution conveys, hot soft water valve is opened, using hot soft water through the second sanitary pump (13) molten with sodium alginate high shear
The surplus dilution whole force feed of product enters sodium alginate high-shear dissolution tank (8) in the pipeline of solution tank (8) connection, and is finished in force feed
Afterwards, it is rinsed using hot soft water pair with the segment pipe that sodium alginate high-shear dissolution tank (8) is connected, the liquid after flushing is through special
It is discharged with waste pipe, completes the process in three process system；
In the 4th procedure system, open KLP-602 sodium alginate soln and prepare in degassing and pressure transfer pot (15)
Vacuum valve, after blended feed liquid flowmeter (14) metering of mixed liquor in sodium alginate high-shear dissolution tank (8), be inhaled into
The preparation of KLP-602 sodium alginate soln deaerates and pressure transfer pot (15), after the mixed liquor conveying capacity of need to be achieved,
The outlet valve closed below sodium alginate high-shear dissolution tank (8), the air pressure valve of compressed gas source is opened, supplied using compression
Device, the product in the conveyance conduit below outlet valve is remained into mixed liquor whole force feed to KLP-602 sodium alginate soln
Prepare in degassing and pressure transfer pot (15), and air pressure valve is closed after force feed, open hot water valve, utilize hot water pair
Conveyance conduit below outlet valve is rinsed, and the liquid after flushing is discharged through special waste pipe, is completed in the 4th work
Process in sequence system；
In five processes system, running water is added to calcium chloride solution dissolving storage after originally water ga(u)ge (21) metering
In groove (20), the calcium chloride after weighing apparatus Weighing is added to calcium chloride solution dissolving storagetank (20), and be stirred
Dissolving, using the calcium chloride solution concentration prepared in conductivity gauge (22) detection calcium chloride solution dissolving storagetank (20) and shown
Show, reach the calcium chloride solution of production requirement concentration after the conveying of the 5th sanitary pump (23), then by ultraviolet sterilizer (24)
Sterilized, solidify into water curtain style and be granulated in cylinder (16), form the umbrella shape water curtain of calcium chloride solution, while utilize compressed air
Device, KLP-602 sodium alginate soln is prepared into the mixed liquor force feed in degassing and pressure transfer pot (15) and enters water
Curtain formula solidification is granulated cylinder (16), and the fan pressure nozzle assembly for solidifying granulation cylinder (16) by water curtain style carries out atomized spray,
Solidify to be granulated in cylinder (16) in water curtain style and form fan-shaped liquid mist, make the umbrella shape water curtain of liquid mist directive calcium chloride solution, and coagulate rapidly
Form KLP-602 sodium alginate micro ball, carry out solidification granulation, the KLP-602 sodium alginate micro ball and chlorine of cohesion
Change calcium solution and be sent into separation of solid and liquid filtering cloth jar (18) through the 3rd sanitary pump (17) together, in separation of solid and liquid filtering cloth jar (18), warp
Solution after separation of solid and liquid is transmitted back in calcium chloride solution dissolving storagetank (20) through the 4th sanitary pump (19) to carry out repeating to make
With until mist projection granulating code terminates, completing the process in five processes system；
In the 6th procedure system, hanging basket is filtered by the separation of solid and liquid in driving hanging out separation of solid and liquid filtering cloth jar (18)
(25) KLP-602 sodium alginate particulate matter in the filter screen of separation of solid and liquid filtering hanging basket (25), is taken out, and by lysozyme two
Aggressiveness sodium alginate particulate matter is transferred to ebullated dryer (26) and carries out last drying process processing together, finally gives bacteriolyze
Enzyme dimer sodium alginate micro ball finished product.
3. the pipe-line transportation system of KLP-602 sodium alginate micro ball production line according to claim 1 or claim 2 with the spot
Purging system, it is characterised in that：To sodium alginate high-shear dissolution tank (8), KLP-602 diluent preparing tank (10), molten
Bacterium enzyme dimer sodium alginate soln prepares degassing and pressure transfer pot (15) and water curtain style solidification is granulated in cylinder (16) and set respectively
There is spray cleaning system.
4. the pipe-line transportation system of KLP-602 sodium alginate micro ball production line according to claim 1 or claim 2 with the spot
Purging system, it is characterised in that：In five processes system, calcium chloride solution dissolving storagetank (20) is provided with recirculated cooling water
Cooling system and auxiliary waste solution channel exhaust system.
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| CN107187879A (en) * | 2017-07-07 | 2017-09-22 | 合肥佳粮机械科技有限公司 | A kind of defeated lid equipment of wind-driven type for conveying a variety of cap-type |
| CN108607492A (en) * | 2018-07-18 | 2018-10-02 | 上海艾魁英生物科技有限公司 | A kind of full-automatic preparation tank of cationic cure liquid for lysozyme dimer granulation |
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