CN106085840A - 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 pipe-line transportation system and the purging system on the spot of a kind of KLP-602 sodium alginate micro ball production line, mainly manufactured system by soft water, water softening tank, water pump, hot-water cylinder, first sanitary pump, automatic temperature-controlled water heater funnel, six procedure systems, master controller, a series of rustless steel sanitary pipe and the whole pipeline transportation work system of a series of hygiene-type operated pneumatic valve composition KLP-602 sodium alginate micro ball production line, the effective production efficiency improved in production process and product safe and sanitary, improve Workshop Production environment and alleviate 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 scale to prepare.The present invention can carry out force feed by designated program to leftover materials in pipeline and rinse, and once purged pipeline is fully achieved the food hygienic requirements to equipment, uses closed circuit purging system, and the production environment making whole workshop is better.
Description
Technical field
The present invention relates to a kind of pipe-line transportation system and clean device, particularly relating to one and carry for material and product
System and clean device, be applied to protease solidification granulating technique field.
Background technology
KLP-602 sodium alginate micro ball is the upgrading products of antalzyme protein enzyme, manufactures experimently through laboratory for many years,
On the basis of succeeding, it is transformed in production practices and goes to be a kind of exigence.In the lab, lysozyme dimerization
The manufacture equipment of body sodium alginate micro ball is hypomegetic, and working procedure is dependent on laboratory worker, makes work at upper track
After sequence terminates, through manually taking out and being placed in lower road equipment continuation processing, the obvious nothing of its manufacture method from upper track equipment
Method meets the batch production of product.How to utilize the manufacture method and technical parameter obtained from laboratory, the most effectively improve life
The production efficiency of product and safe and sanitary during product, improve Workshop Production environment and to alleviate the productive labor of operator strong
Degree, becomes technical problem the most urgently to be resolved hurrily.
Summary of the invention
In order to solve prior art problem, it is an object of the invention to the deficiency overcoming prior art to exist, it is provided that a kind of
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 safe and sanitary, improve Workshop Production environment and alleviate the productive labor intensity of operator, favorably
In realizing KLP-602 sodium alginate micro ball large-scale production, present system can clean on the spot, be fully achieved food
The product hygienic requirements to equipment.
Purpose is created, employing following technical proposals for reaching foregoing invention:
The pipe-line transportation system of a kind of KLP-602 sodium alginate micro ball production line and purging system, whole work on the spot
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-class gauge, sodium alginate high-shear dissolution tank, second gauge, KLP-602 diluent preparing tank, the second health
The preparation degassing of pump, mixed liquor effusion meter, KLP-602 sodium alginate soln and pressure transfer pot, water curtain style solidification pelletize
Cylinder, the 3rd sanitary pump, solid-liquid separation filtering cloth jar, the 4th sanitary pump, calcium chloride solution dissolve storagetank, ultraviolet sterilizer, consolidate
Liquid separating and filtering hanging basket, ebullated dryer, master controller, a series of rustless steel sanitary pipe and a series of hygiene-type operated pneumatic valve
Composition, thus form the whole pipeline transportation work system of KLP-602 sodium alginate micro ball production line, whole pipeline is defeated
Send work system to be controlled by master controller, and use PLC to be controlled hot water heating by touch screen, sodium alginate height is cut
Cut dissolving, KLP-602 diluent preparing, the preparation degassing of KLP-602 sodium alginate soln and pressure conveying, water curtain
Formula solidification pelletize, solid-liquid separation, separation liquid reuse, solid resultant product collection series of process process, when upper track manufacturing procedure completes
After, master controller is controlled by the combination of exclusive pump, materail tube, effusion meter and operated pneumatic valve to each target subsystem, by mesh
The feed liquid material automatic transport of mark subsystem output is processed to next procedure or processes, until completing last procedure,
It is also provided with purging system on the spot, 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 carried out evacuation, utilizes vacuum, use tap water or soft water,
By master controller designated program, leftover materials in the Work container of subsystem and in the materail tube that is interconnected are carried out force feed also
Rinse, molten at sodium alginate high-shear dissolution tank, KLP-602 diluent preparing tank and KLP-602 sodium alginate
In liquid preparation degassing and pressure transfer pot, the temperature that required temperature is set by automatic temperature-controlled water heater funnel by soft water
Obtain, and prepare degassing and pressure transfer pot at sodium alginate high-shear dissolution tank and KLP-602 sodium alginate soln
Chuck in Work container wall arranges constant-temperature hot water circulation heat-insulation system, constant-temperature hot water is circulated in heat-insulation system the soft of flowing
The heat that water carries liquid material in 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 puts into after using weight measurer to weigh solid material, make dispensing liquid with
Solid material carries out preparing the preparation of liquid, and in whole pipeline transportation work system, former water manufactures system through soft water and enters soft water
Tank becomes soft water, then makes soft water enter hot-water cylinder through water pump, is then passed through the first sanitary pump and soft water is sent into automatic temperature-controlled hot water
Heating system forms hot water, makes hot water prepare de-to sodium alginate high-shear dissolution tank and KLP-602 sodium alginate soln
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 comprised with purging system on the spot, particularly as follows:
In first working procedure systems, measure through first-class gauge, the hot water of nominal volume is added sodium alginate height and cuts
Cut in dissolving tank, the hot water of the nominal volume after being computed is added KLP-602 diluent through the metering of second gauge and joins
In tank processed, and wait that the cold water of next procedure adds, the sodium alginate powder after being weighed metering is added by charging entrance
Sodium alginate high-shear dissolution tank, carries out high shear rapid solution and prepares sodium alginate soln, complete at first working procedure systems
The middle course of processing；
In second operation work system, the soft water of the nominal volume of the set water temperature after being computed through second gauge meter
Amount is added in KLP-602 diluent preparing tank, and in making KLP-602 diluent preparing tank, soft water temperature reaches to set
Fixed temperature, and opening electric heater make KLP-602 diluent preparing tank in water temperature be maintained at design temperature level, joining
Hinge agent after having made is quantitatively adding hinge agent tank, then titrates to KLP-602 diluent preparing tank through hinge agent tank
Add and be stirred dissolving by agitating device, preparing KLP-602 diluent, complete in second operation work system
The course of processing；
In three process system, by the KLP-602 diluent after second operation work is processed through lysozyme two
Aggressiveness diluent preparing tank sends into sodium alginate high-shear dissolution tank by the second sanitary pump, prepares mixed liquor, liquid to be diluted
After conveying, open hot soft water valve, utilize hot soft water tank connected with sodium alginate high-shear dissolution through the second sanitary pump handle
In pipeline, the long-pending surplus whole force feed of diluent enters sodium alginate high-shear dissolution tank, and after force feed, utilizes hot soft water pair
Segment pipe tank connected with sodium alginate high-shear dissolution is rinsed, and the liquid after flushing is discharged through special waste pipe,
Complete the course of processing in three process system；
In the 4th procedure system, open in the preparation degassing of KLP-602 sodium alginate soln and pressure transfer pot
Vacuum valve, in sodium alginate high-shear dissolution tank mixed liquor blended feed liquid effusion meter metering after, be inhaled into lysozyme
The preparation degassing of dimer sodium alginate soln and pressure transfer pot, after the mixed liquor conveying capacity of need to be achieved, close alginic acid
Outlet valve below sodium high-shear dissolution tank, opens the air pressure valve of compressed gas source, utilizes compression feeder, by outlet valve
The long-pending surplus whole force feed of mixed liquor in the conveyance conduit of lower section is to the preparation degassing of KLP-602 sodium alginate soln and pressure
In power transfer pot, and after force feed, close air pressure valve, open hot water valve, utilize hot water to the conveying below outlet valve
Pipeline is rinsed, and the liquid after flushing is discharged through special waste pipe, completes the course of processing in the 4th procedure system；
In five processes system, tap water joins calcium chloride solution after tap water effusion meter measures and dissolves storage
In groove, the calcium chloride after weighing apparatus Weighing is joined calcium chloride solution and dissolves storagetank, and carry out stirring and dissolving, use
Conductivity meter detection calcium chloride solution dissolves the calcium chloride solution concentration of preparation in storagetank and shows, reaches production requirement dense
The calcium chloride solution of degree is after the 5th sanitary pump conveying, then sterilizes through ultraviolet sterilizer, enters water curtain style solidification and makes
In grain cylinder, form the umbrella shape water curtain of calcium chloride solution, utilize blowing plant, by molten for KLP-602 sodium alginate simultaneously
Mixed liquor force feed in liquid preparation degassing and pressure transfer pot enters water curtain style solidification pelletize cylinder, solidifies pelletize by water curtain style
The fan pressure nozzle assembly of cylinder carries out atomized spray, forms fan-shaped liquid mist, make liquid mist penetrate in water curtain style solidification pelletize cylinder
To the umbrella shape water curtain of calcium chloride solution, and it is rapidly condensed into KLP-602 sodium alginate micro ball, carries out solidifying pelletize, cohesion
KLP-602 sodium alginate micro ball send into solid-liquid separation filtering cloth jar through the 3rd sanitary pump together with calcium chloride solution, solid
In liquid separating and filtering cylinder, the solution after solid-liquid separation is transmitted back to calcium chloride solution through the 4th sanitary pump and dissolves in storagetank
Row is reused, until mist projection granulating code terminates, completes the course of processing in five processes system；
In the 6th procedure system, filter hanging basket by the solid-liquid separation in driving hanging out solid-liquid separation filtering cloth jar, take
Go out KLP-602 sodium alginate particulate matter in the filter screen of solid-liquid separation filtration 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
The preparation degassing of enzyme dimer diluent preparing tank, KLP-602 sodium alginate soln and pressure transfer pot and water curtain style solidify
It is respectively equipped with spray cleaning system in pelletize cylinder.
As the further preferred technical scheme of such scheme of the present invention, calcium chloride solution dissolves storagetank and is provided with circulation
Cooling water cooling system and auxiliary waste solution channel exhaust system.
The present invention compared with prior art, has and the most obviously highlights substantive distinguishing features and remarkable advantage:
1. the present invention is under maintaining the basis of manufacturing process principle that experiment obtained and significant data, extends processing
The ability of equipment and the automatic conveying system of upper next procedure, the effective production efficiency improved in production process and health
Safety, improves Workshop Production environment and alleviates the productive labor intensity of operator, makes experimental result be entirely applied to produce
Field；
2. the present invention can carry out force feed by designated program and rinse materail tube leftover materials in pipeline, once purged pipe
Road can be fully achieved the food hygienic requirements to equipment, uses closed circuit purging system, and the production environment making whole workshop is better.
Accompanying drawing explanation
Fig. 1 is the sodium alginate dissolution process pipe-line transportation system during embodiment of the present invention one device execution first operation
Process chart.
Fig. 2 is the KLP-602 diluent preparing operation pipe during embodiment of the present invention one device execution second operation work
Pipeline conveying system process chart.
Fig. 3 is that the embodiment of the present invention one device KLP-602 diluent when performing three process is 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 preparation liquid during embodiment of the present invention one device execution four procedure is from sea
Sodium alginate high-shear dissolution tank is delivered to the preparation degassing of KLP-602 sodium alginate soln and the conveying of pressure transfer pot pipeline
System process.
Fig. 5 be the embodiment of the present invention one device KLP-602 sodium alginate preparation liquid when performing five processes from
The preparation degassing of KLP-602 sodium alginate soln and pressure transfer pot are delivered to water curtain style solidification pelletize cylinder and calcium chloride
Solution dissolves storagetank from calcium chloride solution and is delivered to water curtain style solidification pelletize earthen pipe pipeline conveying system process chart.
Fig. 6 is that the KLP-602 sodium alginate granule during embodiment of the present invention one device execution six procedure is from solid
Liquid separating and filtering cylinder is transported to ebullated dryer procedure technology flow chart.
Detailed description of the invention
Details are as follows for the preferred embodiments of the present invention:
Embodiment one:
In the present embodiment, see Fig. 1～6, the pipeline conveying of a kind of KLP-602 sodium alginate micro ball production line
System and purging system on the spot, whole work system is mainly manufactured system 1, water softening tank 2, water pump 3, hot-water cylinder 4, first by soft water
Sanitary pump 5, automatic temperature-controlled water heater funnel 6, first-class gauge 7, sodium alginate high-shear dissolution tank 8, second gauge 9,
KLP-602 diluent preparing tank the 10, second sanitary pump 13, mixed liquor effusion meter 14, KLP-602 sodium alginate
Solution preparation degassing and pressure transfer pot 15, water curtain style solidification pelletize cylinder the 16, the 3rd sanitary pump 17, solid-liquid separation filtering cloth jar 18,
4th sanitary pump 19, calcium chloride solution dissolve storagetank 20, ultraviolet sterilizer 24, solid-liquid separation filters hanging basket 25, boiling is done
Dry device 26, master controller, a series of rustless steel sanitary pipe and a series of hygiene-type operated pneumatic valve composition, thus form lysozyme
The whole pipeline transportation work system of dimer sodium alginate micro ball production line, whole pipeline transportation work system is by master controller
It is controlled, and uses PLC to be controlled hot water heating, sodium alginate high-shear dissolution, KLP-602 by touch screen
The preparation of diluent preparing, KLP-602 sodium alginate soln deaerates and pressure carries, water curtain style solidifies pelletize, solid-liquid divides
From, separate liquid reuse, solid resultant product collection series of process process, after upper track manufacturing procedure completes, master controller is by right
The combination of exclusive pump, materail tube, effusion meter and the operated pneumatic valve of each target subsystem controls, by the feed liquid of target subsystem output
Material automatic transport is processed to next procedure or processes, until completing last procedure, is also provided with cleaning on the spot system
System, the per pass manufacturing procedure that each subsystem at the pipe-line transportation system of bacterium enzyme dimer sodium alginate micro ball production line is corresponding
After end, corresponding subsystem is carried out evacuation, utilize vacuum, use tap water or soft water, by master controller designated program,
Leftover materials in the Work container of subsystem and in the materail tube that is interconnected are carried out force feed and rinse, cuts at sodium alginate height
Cut dissolving tank 8, KLP-602 diluent preparing tank 10 and the preparation degassing of KLP-602 sodium alginate soln and pressure
In transfer pot 15, the temperature that required temperature is set by automatic temperature-controlled water heater funnel 6 by soft water obtains, and Sargassum
Acid sodium high-shear dissolution tank 8 and the preparation of KLP-602 sodium alginate soln deaerate and the Work container wall of pressure transfer pot 15
Interior chuck arranges constant-temperature hot water circulation heat-insulation system, constant-temperature hot water is circulated the heat that in heat-insulation system, the soft water of flowing carries
Amount liquid material in Work container is transmitted, the concentration of the feed liquid in each subsystem by exclusive effusion meter to proportion liquid
Body carries out metering conveying, and puts into after using weight measurer to weigh solid material, makes dispensing liquid enter with solid material
The preparation of row preparation liquid, in whole pipeline transportation work system, former water enters water softening tank 2 through soft water manufacture system 1 becomes soft
Water, then make soft water enter hot-water cylinder 4 through water pump 3, it is then passed through the first sanitary pump 5 and soft water is sent into automatic temperature-controlled hot water heating system
System 6 formation hot water, soften hot water after reaching 55 DEG C of technological requirement, make hot water to sodium alginate high-shear dissolution tank 8 and molten
Bacterium enzyme dimer sodium alginate soln preparation degassing and pressure transfer pot 15 carry out heated at constant temperature, with above-mentioned Work container perseverance
Temperature characteristics.
In the present embodiment, Fig. 1～6, the pipe-line transportation system of KLP-602 sodium alginate micro ball production line are seen
At least six procedure systems are comprised with purging system on the spot, particularly as follows:
In first working procedure systems, measure through first-class gauge 7, the hot water of nominal volume 1500L is added alginic acid
In sodium high-shear dissolution tank 8, the hot water of the nominal volume after being computed is measured addition KLP-602 through second gauge 9
In diluent preparing tank 10, and wait that the cold water of next procedure adds, the sodium alginate powder after being weighed metering is passed through to add
Material entrance adds sodium alginate high-shear dissolution tank 8, carries out high shear rapid solution and prepares sodium alginate soln, completes first
The course of processing in procedure system, sees Fig. 1；
In second operation work system, by the technique of mixed water method regulation water temperature, after second gauge 9 calculates,
Coolant-temperature gage reaches the hot soft water of the nominal volume 78L of 55 DEG C and is added into KLP-602 diluent through second gauge 9 metering and joins
In tank 10 processed, the most again after second gauge 9 calculates, coolant-temperature gage is reached the cold soft water of nominal volume 372L of 15 DEG C through second
Effusion meter 9 metering is added in KLP-602 diluent preparing tank 10, in making KLP-602 diluent preparing tank 10
Obtain 22 DEG C of soft water 450L, be then turned on water temperature in electric heater 11 makes KLP-602 diluent preparing tank 10 and be maintained at
The design temperature level of 25 DEG C, the hinge agent after preparation is completed is quantitatively adding hinge agent tank 12, then through hinge agent tank 12 to molten
Bacterium enzyme dimer diluent preparing tank 10 is made titration and is added and be stirred dissolving by agitating device, prepares KLP-602
Diluent, completes the course of processing in second operation work system, sees Fig. 2；
In three process system, by the KLP-602 diluent after second operation work is processed through lysozyme two
Aggressiveness diluent preparing tank 10 sends into sodium alginate high-shear dissolution tank 8 by the second sanitary pump 13, prepares mixed liquor, treats dilute
Release liquid conveying after, open hot soft water valve, utilize time controlled system module, utilize hot soft water through the second sanitary pump 13 with
In the pipeline that sodium alginate high-shear dissolution tank 8 connects, the long-pending surplus whole force feed of diluent enters sodium alginate high-shear dissolution tank 8,
Reach set time value and be i.e. automatically stopped force feed, and after force feed, utilize hot soft water pair molten with sodium alginate high shear
The segment pipe solving tank 8 connection is rinsed, and the liquid after flushing is discharged through special waste pipe, completes in three process system
The course of processing in system, sees Fig. 3；
In the 4th procedure system, open the preparation degassing of KLP-602 sodium alginate soln and pressure transfer pot 15
On vacuum valve, make KLP-602 sodium alginate soln preparation degassing and pressure transfer pot 15 in vacuum reach-0.085Mpa,
After mixed liquor blended feed liquid effusion meter 14 metering in sodium alginate high-shear dissolution tank 8,500L mixed liquor is made to be inhaled
Enter the preparation degassing of KLP-602 sodium alginate soln and pressure transfer pot 15, after the mixed liquor conveying capacity of need to be achieved,
Close the outlet valve below sodium alginate high-shear dissolution tank 8, open the air pressure valve of compressed gas source, utilize compression supply dress
Put, the long-pending surplus whole force feed of mixed liquor in the conveyance conduit below outlet valve is joined to KLP-602 sodium alginate soln
In system degassing and pressure transfer pot 15, it is de-gassed froth breaking, and after force feed, closes air pressure valve, open hot water valve,
Utilizing hot water to be rinsed the conveyance conduit below outlet valve, the liquid after flushing is discharged through special waste pipe, completes
The course of processing in the 4th procedure system, sees Fig. 4；
In five processes system, it is molten that the tap water 2000L after tap water effusion meter 21 measures joins calcium chloride
Liquid dissolves in storagetank 20, the calcium chloride after weighing apparatus Weighing is joined calcium chloride solution and dissolves storagetank 20, go forward side by side
Row stirring and dissolving, uses conductivity meter 22 to detect calcium chloride solution and dissolves the calcium chloride solution concentration of preparation in storagetank 20 and carry out
Display, observes for operator and is adjusted production technology and intervenes, when conductivity meter 22 shows that calcium chloride solution dissolves storage
When calcium chloride solution concentration in groove 20 is 10wt.%, stops adding calcium chloride, be then the calcium chloride of 10wt.% by concentration
Solution is after the 5th sanitary pump 23 conveying, then sterilizes through ultraviolet sterilizer 24, enters water curtain style solidification pelletize cylinder 16
In, form the umbrella shape water curtain of calcium chloride solution, utilize blowing plant simultaneously, make KLP-602 sodium alginate soln join
In system degassing and pressure transfer pot 15, pressure rises to 1.1 bars, by the preparation degassing of KLP-602 sodium alginate soln and pressure
Mixed liquor force feed in power transfer pot 15 enters water curtain style solidification pelletize cylinder 16, by 34 groups of water curtain style solidification pelletize cylinder 16
Fan pressure nozzle assembly carries out atomized spray, forms fan-shaped liquid mist, make liquid mist directive in water curtain style solidification pelletize cylinder 16
The umbrella shape water curtain of calcium chloride solution, and it is rapidly condensed into KLP-602 sodium alginate micro ball, carry out solidifying pelletize, cohesion
KLP-602 sodium alginate micro ball sends into solid-liquid separation filtering cloth jar 18 through the 3rd sanitary pump 17 together with calcium chloride solution,
In solid-liquid separation filtering cloth jar 18, the solution after solid-liquid separation is transmitted back to calcium chloride solution through the 4th sanitary pump 19 and is dissolved storage
Groove 20 is reused, until mist projection granulating code terminates, completes the course of processing in five processes system, see figure
5；
In the 6th procedure system, filter hanging basket by the solid-liquid separation in driving hanging out solid-liquid separation filtering cloth jar 18
25, KLP-602 sodium alginate particulate matter in the artificial filter screen taking out solid-liquid separation filtration 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, sees Fig. 6.
In the present embodiment, see Fig. 1～6, sodium alginate high-shear dissolution tank 8, KLP-602 diluent are joined
The preparation degassing of tank 10 processed, KLP-602 sodium alginate soln and pressure transfer pot 15 and water curtain style divide in solidifying pelletize cylinder 16
It is not provided with spray cleaning system.
After the production technology that the present embodiment device is implemented completes, utilize the pressure of soft hot water by the cleaning installed in basin
Spray ball causes jet power, respectively to sodium alginate high-shear dissolution tank 8, KLP-602 diluent preparing tank 10 and lysozyme
The preparation degassing of dimer sodium alginate soln and pressure transfer pot 15 carry out clear Xian on the spot, and the liquid after each tank is cleaned
Delivering to special waste pipe discharge, 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 is prepared the pipe-line transportation system of production line and through design and is installed
After completing, operate in the production process of reality, achieve good Expected Results.The present embodiment apparatus system can pass through pump,
Materail tube, operated pneumatic valve and PLC by programming are controlled a upper track feed liquid automatic transport by touch screen and enter to next procedure
Row feed liquid or materiel machining and process, until completing last procedure, the whole technological process of production increasingly automated, not only
Alleviate the labor intensity of operator, be greatly improved production capacity and economic benefit, avoid because manual operation may simultaneously
The unnecessary loss that the error caused is brought.
Embodiment two:
The present embodiment is essentially identical with embodiment one, is particular in that:
In the present embodiment, in five processes system, calcium chloride solution dissolves storagetank 20 and is provided with recirculated cooling water
Cooling system and auxiliary waste solution channel exhaust system, it is ensured that calcium chloride solution can preserve for a long time, and the present embodiment is also equipped with special
Track Lift-on/Lift-off System, is used for lifting by crane and transport solid-liquid separation and filters hanging basket to appointed place, make the production environment in whole workshop more
Well, the productive labor intensity of operator can be alleviated and make production environment better.
Above in conjunction with accompanying drawing, the embodiment of the present invention is illustrated, but the invention is not restricted to above-described embodiment, it is also possible to
The purpose of the innovation and creation according to the present invention makes multiple change, under all spirit according to technical solution of the present invention and principle
The change made, modify, substitute, combine or simplify, all should be the substitute mode of equivalence, as long as meeting the goal of the invention of the present invention,
Pipe-line transportation system and purging system on the spot without departing from KLP-602 sodium alginate micro ball production line of the present invention
Know-why and inventive concept, broadly fall into protection scope of the present invention.
Claims (4)
1. the pipe-line transportation system of KLP-602 sodium alginate micro ball production line and a purging system on the spot, its feature exists
In: whole work system is mainly manufactured system (1), water softening tank (2), water pump (3), hot-water cylinder (4), the first sanitary pump by soft water
(5), automatic temperature-controlled water heater funnel (6), first-class gauge (7), sodium alginate high-shear dissolution tank (8), second gauge
(9), KLP-602 diluent preparing tank (10), the second sanitary pump (13), mixed liquor effusion meter (14), lysozyme dimerization
Body sodium alginate soln is prepared degassing and pressure transfer pot (15), water curtain style solidification pelletize cylinder (16), the 3rd sanitary pump (17), is consolidated
Liquid separating and filtering cylinder (18), the 4th sanitary pump (19), calcium chloride solution dissolve storagetank (20), ultraviolet sterilizer (24), consolidate
Liquid separating and filtering hanging basket (25), ebullated dryer (26), master controller, a series of rustless steel sanitary pipe and a series of hygiene-type
Operated pneumatic valve forms, thus forms the whole pipeline transportation work system of KLP-602 sodium alginate micro ball production line, whole
Individual pipeline transportation work system is controlled by master controller, and uses PLC to be controlled hot water heating, Sargassum by touch screen
Acid sodium high-shear dissolution, KLP-602 diluent preparing, the preparation degassing of KLP-602 sodium alginate soln and pressure
Conveying, water curtain style solidification pelletize, solid-liquid separation, separation liquid reuse, solid resultant product collection series of process process, when upper track is processed
After operation completes, master controller is by the combination control of exclusive pump, materail tube, effusion meter and operated pneumatic valve to each target subsystem
System, is processed the feed liquid material automatic transport of target subsystem output to next procedure or processes, until completing last
Procedure, is also provided with purging system on the spot, pipe-line transportation system every of bacterium enzyme dimer sodium alginate micro ball production line
After per pass manufacturing procedure corresponding to individual subsystem terminates, corresponding subsystem is carried out evacuation, utilize vacuum, use tap water
Or soft water, by master controller designated program, leftover materials in the Work container of subsystem and in the materail tube that is interconnected are entered
Row force feed also rinses, at sodium alginate high-shear dissolution tank (8), KLP-602 diluent preparing tank (10) and lysozyme two
In the preparation degassing of aggressiveness sodium alginate soln and pressure transfer pot (15), required temperature is passed through automatic temperature-controlled hot water by soft water
The temperature that heating system (6) sets obtains, and molten at sodium alginate high-shear dissolution tank (8) and KLP-602 sodium alginate
Chuck in the Work container wall of liquid preparation degassing and pressure transfer pot (15) arranges constant-temperature hot water circulation heat-insulation system, by perseverance
Warm water is circulated in heat-insulation system heat that the soft water of flowing the carries liquid material in Work container and is transmitted, and at each point is
The concentration of the feed liquid in system is carried out metering by exclusive effusion meter to dispensing liquid and carries, and uses weight measurer to solid material
Put into after weighing, make dispensing liquid and solid material carry out preparing the preparation of liquid, in whole pipeline transportation work system,
Former water manufactures system (1) entrance water softening tank (2) through soft water becomes soft water, then makes soft water enter hot-water cylinder (4) through water pump (3), so
After through the first sanitary pump (5), soft water sent into automatic temperature-controlled water heater funnel (6) and forms hot water, make hot water to sodium alginate
High-shear dissolution tank (8) and the preparation degassing of KLP-602 sodium alginate soln and pressure transfer pot (15) carry out constant temperature and add
Heat.
The most according to claim 1 the pipe-line transportation system of KLP-602 sodium alginate micro ball production line with clean on the spot
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, particularly as follows:
In first working procedure systems, measure through first-class gauge (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 added KLP-602 dilution through second gauge (9) metering
In liquid preparing tank (10), and wait that the cold water of next procedure adds, the sodium alginate powder after being weighed metering is passed through charging
Entrance adds sodium alginate high-shear dissolution tank (8), carries out high shear rapid solution and prepares sodium alginate soln, completes first
The course of processing 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 gauge (9)
Amount is added in KLP-602 diluent preparing tank (10), makes KLP-602 diluent preparing tank (10) interior soft water temperature
Degree reaches design temperature, and opening electric heater (11) makes KLP-602 diluent preparing tank (10) interior water temperature be maintained to set
Fixed temperature level, the hinge agent after preparation is completed is quantitatively adding hinge agent tank (12), then through hinge agent tank (12) to lysozyme
Dimer diluent preparing tank (10) is made titration and is added and be stirred dissolving by agitating device, and preparation KLP-602 is dilute
Release liquid, complete the course of processing in second operation work system；
In three process system, by the KLP-602 diluent after second operation work is processed through KLP-602
Diluent preparing tank (10) sends into sodium alginate high-shear dissolution tank (8) by the second sanitary pump (13), prepares mixed liquor, treats
After diluent conveying, open hot soft water valve, utilize hot soft water through the second sanitary pump (13) molten with sodium alginate high shear
Solve the long-pending surplus whole force feed of diluent in the pipeline that tank (8) connects and enter sodium alginate high-shear dissolution tank (8), and complete at force feed
After, the segment pipe utilizing hot soft water pair to be connected with sodium alginate high-shear dissolution tank (8) is rinsed, and the liquid after flushing is through specially
It is discharged with waste pipe, completes the course of processing in three process system；
In the 4th procedure system, open in the preparation degassing of KLP-602 sodium alginate soln and pressure transfer pot (15)
Vacuum valve, in sodium alginate high-shear dissolution tank (8) mixed liquor blended feed liquid effusion meter (14) metering after, be inhaled into
The preparation degassing of KLP-602 sodium alginate soln and pressure transfer pot (15), after the mixed liquor conveying capacity of need to be achieved,
Close the outlet valve of sodium alginate high-shear dissolution tank (8) lower section, open the air pressure valve of compressed gas source, utilize compression supply
Device, by the long-pending surplus whole force feed of mixed liquor in the conveyance conduit below outlet valve to KLP-602 sodium alginate soln
In preparation degassing and pressure transfer pot (15), and after force feed, close air pressure valve, 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, completes in the 4th road work
The course of processing in sequence system；
In five processes system, tap water joins calcium chloride solution after tap water effusion meter (21) measures and dissolves storage
In groove (20), the calcium chloride after weighing apparatus Weighing is joined calcium chloride solution and dissolves storagetank (20), and be stirred
Dissolve, use conductivity meter (22) detection calcium chloride solution dissolve the calcium chloride solution concentration of preparation in storagetank (20) and show
Show, reach the calcium chloride solution of production requirement concentration after the 5th sanitary pump (23) conveying, then through ultraviolet sterilizer (24)
Sterilize, enter in water curtain style solidification pelletize cylinder (16), form the umbrella shape water curtain of calcium chloride solution, utilize compressed air simultaneously
Device, enters water by the mixed liquor force feed in the preparation degassing of KLP-602 sodium alginate soln and pressure transfer pot (15)
Curtain formula solidification pelletize cylinder (16), carries out atomized spray by the fan pressure nozzle assembly of water curtain style solidification pelletize cylinder (16),
In water curtain style solidification pelletize cylinder (16), 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 solidifying pelletize, the KLP-602 sodium alginate micro ball of cohesion and chlorine
Change calcium solution and send into solid-liquid separation filtering cloth jar (18), in solid-liquid separation filtering cloth jar (18), warp through the 3rd sanitary pump (17) together
Solution after solid-liquid separation carries out repeating to make in the 4th sanitary pump (19) is transmitted back to calcium chloride solution dissolving storagetank (20)
With, until mist projection granulating code terminates, complete the course of processing in five processes system；
In the 6th procedure system, filter hanging basket by the solid-liquid separation in driving hanging out solid-liquid separation filtering cloth jar (18)
(25), KLP-602 sodium alginate particulate matter in the filter screen of solid-liquid separation filtration 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.
The pipe-line transportation system of KLP-602 sodium alginate micro ball production line the most according to claim 1 or claim 2 with on the spot
Purging system, it is characterised in that: to sodium alginate high-shear dissolution tank (8), KLP-602 diluent preparing tank (10), molten
The preparation degassing of bacterium enzyme dimer sodium alginate soln and pressure transfer pot (15) and water curtain style set in solidifying pelletize cylinder (16) respectively
There is spray cleaning system.
The pipe-line transportation system of KLP-602 sodium alginate micro ball production line the most according to claim 1 or claim 2 with on the spot
Purging system, it is characterised in that: in five processes system, calcium chloride solution dissolves storagetank (20) and is provided with recirculated cooling water
Cooling system and auxiliary waste solution channel exhaust system.
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| CN201610452686.7A CN106085840B (en) | 2016-06-21 | 2016-06-21 | The pipe-line transportation system of KLP-602 sodium alginate micro ball production line and purging system on the spot |
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| CN106085840B (en) | 2018-04-10 |
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