CN209034534U - A kind of mill base processing unit (plant) - Google Patents

Abstract

This application involves a kind of mill base processing unit (plant)s, belong to the dyeing or stamp processing technology field of fabric etc..Including mixed zone, corase grinding area, fine grinding area, storing area, inspection area and the bagging area being sequentially arranged, the stain, dispersing agent are added by mixed zone and are mixed in mixed zone, setting pump one between mixed zone and corase grinding area, realize that material is sent from mixed zone to corase grinding area；Rotor, separator, grinding pearl are set in corase grinding area, separator gap is 0.5-1.5mm, grinds bead diameter 0.8-2mm；Rotor, separator and grinding pearl are set in fine grinding area, separator gap L T.LT.LT 0.8mm, grinding pearl is PU pearl or 95 and the above zirconium oxide bead, grinds bead diameter 0.4mm or less.The application is applied to the industries such as printing and dyeing, dyeing and finishing, printing, has many advantages, such as Non-water washing, short route, pollution-free.

Description

A kind of mill base processing unit (plant)

Technical field

This application involves a kind of mill base processing unit (plant)s, belong to the dyeing such as fabric or stamp processing technology field.

Background technique

The dyeing of fabric, fiber etc. is mainly made of processes such as pre-treatment, dyeing/stamp, post-processings, wherein post-processing In included at least four cleaning: why alkali cleaning, washing, pickling, washing need to carry out multiple cleaning, and main cause exists In: conventional use of dyestuff is as composite finished product, and decontaminant itself is outer, itself also contains a large amount of impurity, filler, dispersion On the one hand the ingredients such as agent and auxiliary agent, these ingredients are to maintain the performance of dyestuff is stable to stablize with specification, another further aspect is then base In considering for color fastness, dye-uptake etc., must largely be added for commercial object.Therefore, during upper dye, dye Agent is the main function ingredient of upper dye, and impurity, filler, dispersing agent and other auxiliary agents then mainly play bridge and catalysis Effect, continue to remain in process object after upper dye, can exist take it is bad, using unsafe defect, therefore, after Multiple tracks cleaning main purpose in processing is just being that the ingredient to above-mentioned catalysis, function served as bridge is cleared up and removed, therefore passes Not only process is more, the period is long in technique of uniting, and can also generate a large amount of cleaning waste water；Meanwhile the presence of above-mentioned catalyst component, it is knitting Certain barrier action can be also played between object structure and stain, and is embodied in loose colour, therefore, one can be contained in ejected wash water The stain of certainty ratio, these stains not only result in ejected wash water muddiness, continue also with the ingredient for playing catalysis, function served as bridge Cause the COD value of ejected wash water higher.

The above problem be exactly traditional dyeing and finishing industry all the time environmental protection, in terms of by institute the main reason for denouncing ?.The low pollution even no pollution, energy conservation and environmental protection for how realizing printing and dyeing, are this field urgent problems to be solved.

Based on this, the application is made.

Utility model content

For the drawbacks described above in the presence of existing dyestuff use, the application provides a kind of Non-water washing, upper dye efficiency first It is high, can effectively shorten the print paste processing unit (plant) of dyeing cycle.

To achieve the above object, the technical solution that the application takes is as follows:

A kind of mill base processing unit (plant), including mixed zone, corase grinding area, fine grinding area, storing area, inspection area and the packet being sequentially arranged Area is filled, the stain, dispersing agent are added by mixed zone and are mixed in mixed zone, and setting pump one, real between mixed zone and corase grinding area Existing material is sent from mixed zone to corase grinding area；Rotor, separator, grinding pearl are set in corase grinding area, separator gap is 0.5- 1.5mm grinds bead diameter 0.8-2mm；Rotor, separator and grinding pearl, separator gap L T.LT.LT 0.8mm are set in fine grinding area (it is furthermore preferred that the separator gap be 0.05-0.6mm), grinding pearl are PU pearl or 95 and the above zirconium oxide bead, grinding bead Sub- diameter 0.4mm or less.

It is use herein to supplementary material mainly include three samples: the synthesis of stain, dispersing agent and subsequent possible addition helps Agent, the stain and dispersing agent of powder form are roughly ground, are refined, and reduce partial size step by step, it is ensured that molding mill base partial size 200nm with Under, it can be in dyeing course directly in conjunction with fiber, the addition of dye auxiliary agent etc., avoids the occurrence of loose colour in reduction, effectively reduces clear The residual quantity of dyestuff in process and ejected wash water is washed, and can realize the self-loopa process of water, water-saving saves time；To in dispersing agent S content is controlled, and the COD for the treatment of fluid is effectively reduced, and comprehensive auxiliary agent is added on demand before fine grinding discharging, is made with meeting difference With the particular/special requirement of environment.

It is not same as above dye demand to meet, the fine grinding area is also correspondingly arranged on comprehensive auxiliary agent area, comprehensive auxiliary agent area and fine grinding Material transferring is realized with pump two between area.

Applicant has done further research to fine grinding on the basis of above scheme, to improve mill base in grinding fineness side The quality in face, the fine grinding area include refiner, A cylinder and B cylinder, and separator and grinding pearl are arranged in refiner, and A cylinder is set Two entrances one opening is set, one entrance and corase grinding area connect, and another entrance and comprehensive auxiliary agent area connect；Opening and refiner It connects, B cylinder sets two openings, and an opening is connected to refiner, and another opening is connected to storing area；It roughly grinds area's discharging and enters A cylinder, warp A cylinder is sent into refiner, after completing grinding in refiner, is sent into B cylinder and returns back to refiner, then be transferred to B after standing in B cylinder Cylinder is transferred to A cylinder through refiner, opens comprehensive auxiliary agent area, synthesis is added on demand and helps and so on to when road second from the bottom grinding Agent, then be transferred to refiner and carry out last grinding together, storing area is sent into through B cylinder.Stain and dispersing agent are the main works in upper dye With ingredient, the two is first mixed and is refined through corase grinding and the road (N-1) by the application, is then turned on the entrance of A cylinder and comprehensive auxiliary agent area, The synthesis auxiliary agent that must be measured is added in the stain and dispersing agent for having been subjected to (N-1) secondary fine grinding, is then transferred in refiner, it is complete After last fine grinding (i.e. n-th fine grinding) together, storing area is sent by B cylinder, above-mentioned material is at A cylinder, refiner and B cylinder three It is reciprocal to transfer, interior circulation fine grinding is constituted, different circulations is realized respectively for different materials, has both taken full advantage of grinding work Sequence, and the excessive grinding that other are not necessarily to excessive grinding material is avoided, improve grinding fineness.

The corase grinding area mainly includes main engine bed, rack, and main engine bed is located in rack, and operation panel is arranged on main engine bed； Grinding chamber is set in main engine bed, and rotor, separator and grinding pearl are located in main engine bed, and feed pipe one end connects pneumatic diaphragm Pump, and by pneumatic diaphragm pump access pump one, in the grinding chamber in other end access host seat；Cut-in temperature table and pressure on grinding chamber Power table, thermometer and pressure gauge are connect with operation panel respectively, monitor the temperature and pressure in grinding chamber by operation panel；It is main Baiting valve and discharge nozzle is arranged in base bottom, and baiting valve is selected one with discharge nozzle and is connected to fine grinding area.

The application has also done further work with regard to the cooling in above scheme, to avoid because caused by grinding high temperature it is poly- Close: cooling water pipe is arranged in the refiner outer wall, and cooling water pipe is with the coolant liquid of 0-30 DEG C of cooling water or (- 25-15 DEG C) As cooling medium, for carrying out cooling and isothermal holding to refiner.With the progress of grinding, high speed grinding friction can be generated Certain heat, these heats are built up in fixed space, will cause material temperature in entire grinding chamber and grinding chamber The promotion of degree, and stain, dispersing agent can generate high temperature polymerization under the high temperature conditions, not only influence raw material (refer to stain, dispersing agent and The synthesis auxiliary agent of necessary amount, similarly hereinafter) utilization rate, it also will form raw material impurity, influence the molding effect of mill base, the application is to fine grinding Area's temperature is controlled, and preferably built-in temperature is especially refined in fine grinding area and is controlled at 0-40 DEG C with cooling water or coolant liquid, Both the normal effect that will not influence raw material plays, and also avoids the excessive consumption of energy.

The application has done further work with regard to the rotor in above scheme, it is ensured that material circulation is quick: the rotor packet It includes ontology, shaft, turn tooth and turn trough, shaft is fixedly connected by its rotation of power source drive, shaft with ontology, body outer wall setting Turn tooth, turning the section of tooth is trapezoidal, the adjacent groove turned between tooth and body outer wall composition turn trough；Grinding pearl is located at turn trough In, and cooperate with turn trough and realize grinding；End turns suit separator on tooth, and (separator is preferably arranged to mesh structure, sieve screen apertures Gap between diameter or adjacent screen mesh is separator gap).When shaft drives ontology rotation, turns tooth and occur to turn therewith It is dynamic, turn the small trapezoidal sectional shape of the outer imperial palace of tooth and effectively material is driven to rotate with it, and material is made to form vortex between turn trough Form, to effectively increase grinding efficiency.

To ensure to install leakproofness, funnel is set, and funnel will seal sample and be sent into rotor tip, and turn above the rotor Sub- end solidifies profile sealing element.

To ensure to grind sufficiently, the application also improves mixed zone, equal with the mixing for improving stain and dispersing agent Even property: the mixed zone includes agitator, agitating shaft and agitator disk, and the agitating shaft is driven by motor, and agitating shaft lower end is protruded into In agitator, and agitator disk is set on the agitating shaft being located in agitator.After material enters agitator, agitating shaft is in motor It is started turning under drive, this rotation inherently will drive material and rotate with it and mix, and agitator disk is arranged then effectively will be with The material of rotation axis rotation is stirred, and aggravates the mixing of stain and dispersing agent, uniformly provides premise for subsequent grinding.It is more excellent Choosing, the agitator disk is provided with multilayer.

The application is applied to the processing of mill base, filter cake is uniformly mixed in advance with dispersing agent, these mixtures are another It rises and completes the entire fine grinding roughly ground with the overwhelming majority, in the material formed at this time, stain is wrapped up by dispersing agent；It is helped when synthesis is added After agent carries out the fine grinding of remainder, stain is wrapped up by dispersing agent and comprehensive auxiliary agent, and the mill base of final molding is except partial size is lower, can Synthesis auxiliary agent that is outer in conjunction with fiber directly in dyeing course, only containing dispersing agent and must measure, impurity is few, without carrying out Washing, compared to traditional handicraft, has at least saved twice cleaning, and water-saving saves time, and water consumption reduces by 75% or so, dyes duration Then reduced by 3h to half the time；Since stain and fiber binding strength are higher when using cleaning after dyeing, thus ejected wash water can It realizes that self-loopa uses, the dyeing waste water of high COD, high chroma will not be generated, decrease and help in ejected wash water cycling and reutilization The repetition of agent is added, and auxiliary agent is reduced, and cost can be controlled effectively.

Detailed description of the invention

Fig. 1 is the structural schematic diagram of the application；

Fig. 2 is the structural schematic diagram of mixed zone in Fig. 1；

Fig. 3 is the structural schematic diagram that area is roughly ground in Fig. 1；

Fig. 4 is the sectional view of the application；

Fig. 5 is the schematic diagram of the section structure of rotor in the application；

Fig. 6 is the principle explanatory diagram of the application.

Figure label: 1. mixed zones；11. motor；12. driving belt；13. belt pulley；14. agitating shaft；15. agitator； 16. dispersion impeller；17. ball valve；18. column；2. roughly grinding area；21. feed pipe；211. pressure gauge；22. water inlet pipe；23. outlet pipe； 24. funnel；241. sealing element；25. pneumatic diaphragm pump；251. oil water separator；26. baiting valve；27. discharge nozzle；271. discharging Pedestal；272. thermometer；28. main engine bed；281. operation panel；29. rack；3. refining area；31.A cylinder；32. refiner；33.B Cylinder；3a. ontology；3b. turns tooth；3c. turn trough；3d. shaft；3e. connects pearl bucket；3f. separator；4. storing area；5. inspection area；6. packet Fill area；7. pump one；8. comprehensive auxiliary agent area；9. pump two.

Specific embodiment

Embodiment 1

A kind of mill base processing unit (plant) of the present embodiment, in conjunction with Fig. 1, including the mixed zone 1, corase grinding area 2, fine grinding area being sequentially arranged 3, storing area 4, inspection area 5 and bagging area 6, stain, dispersing agent are added by mixed zone 1 and are mixed in mixed zone 1, mixed zone 1 with Setting pump 1 between area 2 is roughly ground, realizes that material is sent from mixed zone 1 to corase grinding area 2；Corase grinding sets rotor in area 2, separator 3f, grinds Pearl is ground, the gap separator 3f is 0.5-1.5mm, grinds bead diameter 0.8-2mm；Rotor, separator are set in fine grinding area and are ground Grind pearl, separator gap L T.LT.LT 0.8mm, grinding pearl is PU pearl or 95 and the above zirconium oxide bead, grind bead diameter 0.4mm with Under.

Specifically, it after stain, dispersing agent being mixed in mixed zone 1, is sent into corase grinding area 2 and is roughly ground by pump 1, tied Fig. 2, Fig. 3, Fig. 4, Fig. 5 are closed, roughly grinds and sets rotor, separator 3f, grinding pearl (falling in the turn trough 3c of rotor), separation in area 2 (mesh structure can be used in separator 3f, at this point, between gap refers between the aperture or adjacent screen mesh of sieve in the gap device 3f Gap) be 0.6-1.0mm, revolving speed 1500r/min, linear velocity 11.5m/s, grind bead diameter 1.5mm, be ground to 10 μm of partial size with Under, it is transferred to fine grinding area 3 and is refined；Fine grinding sets rotor in area 3, (mesh structure can be used in separator to separator, at this point, gap Refer to the gap between the aperture or adjacent screen mesh of sieve) and grinding pearl, separator gap L T.LT.LT 0.59mm is (as preferred case Example, separator gap are 0.05-0.15mm), grinding pearl is PU pearl or 95 and the above zirconium oxide bead, grinds bead diameter 0.4mm is hereinafter, complete in lapping process, it is ensured that the temperature in fine grinding area 3 is 0-40 DEG C, handling duration 6-20h, linear velocity 5- 18m/s；Fine grinding discharging is transferred to storing area 4, is finished product mill base through inspection area 5, bagging area 6.

Above equipment carry out mill base preparation when, by stain, dispersing agent mix after, roughly grind and be ground to 10 μm of partial size hereinafter, It is transferred to fine grinding, fine grinding temperature is 0-40 DEG C (preferably 11-17 DEG C；For convenience of control, it is subject to drop temperature), handling duration is 5-20h, linear velocity 5-20m/s；Comprehensive auxiliary agent is added on demand before fine grinding discharging, then is transferred to storing, inspection, packaging, as at Product mill base.

It is use herein to supplementary material mainly include three samples: the synthesis of stain, dispersing agent and subsequent possible addition helps Agent (nonessential ingredient can add on demand), the stain and dispersing agent of powder form are roughly ground, are refined, and reduce partial size step by step, really Molding mill base partial size is protected in 200nm hereinafter, and comprehensive auxiliary agent is added on demand before fine grinding discharging, to meet different use environments Particular/special requirement.

The forming process of mill base can be described as Fig. 6 form: filter cake is uniformly mixed in advance with dispersing agent, these mixtures Another completion is entirely roughly ground and most fine grindings, and in the material formed at this time, stain is wrapped up by dispersing agent；It is comprehensive when being added After closing the fine grinding that auxiliary agent carries out remainder, stain is wrapped up by dispersing agent and comprehensive auxiliary agent, the mill base of final molding except partial size compared with It is low, can be outer in conjunction with fiber directly in dyeing course, the synthesis auxiliary agent that only contains dispersing agent and must measure, impurity is few, nothing It need to be washed, compared to traditional handicraft, at least save twice cleaning, water-saving saves time, and water consumption reduces by 75% or so, dye Color duration is then reduced by 3h to half the time；Since stain and fiber binding strength are higher when using cleaning after dyeing, thus it is clear Wash water can realize that self-loopa uses, and will not generate the dyeing waste water of high COD, high chroma, also subtract in ejected wash water cycling and reutilization The repetition addition of auxiliary agent is lacked, auxiliary agent is reduced, and cost can be controlled effectively.

Applicant has done further research to fine grinding on the basis of above scheme, to improve mill base in grinding fineness side The quality in face, in conjunction with Fig. 1, refining area 3 includes refiner 32, A cylinder 31 and B cylinder 33, and separator and grinding pearl are arranged at essence In grinding machine 32, two entrances one opening is arranged in A cylinder 31, and one entrance and corase grinding area 2 connect, and another entrance is matched by pump 29 It closes and comprehensive auxiliary agent area 8 is set, and connected with comprehensive auxiliary agent area 8；Opening is connected with refiner 32, and B cylinder 33 sets two openings, an opening It is connected to refiner 32, another opening is connected to storing area 4；It roughly grinds the discharging of area 2 and enters A cylinder 31, sent in the direction of the arrow through A cylinder 31 Enter refiner 32, after completing grinding in refiner 32, is sent into B cylinder 33 and returns back to refiner 32, then turn after standing in B cylinder 33 Enter B cylinder 33, and so on to when road second from the bottom grinding, is transferred to A cylinder 31 through refiner 32, opens pump 29 and comprehensive auxiliary agent area 8, comprehensive auxiliary agent is added on demand, then be transferred to refiner 32 and finally grind together, is sent into storing area 4 through B cylinder 33.Stain with point Powder is the main function ingredient in upper dye, and the two is first mixed and refined through corase grinding and the road (N-1) by the application, is then turned on A The synthesis auxiliary agent that must be measured, is added to stain and the dispersion for having been subjected to (N-1) secondary fine grinding by the entrance of cylinder 31 and comprehensive auxiliary agent area 8 It in agent, is then transferred in refiner 32, after completing last fine grinding (i.e. n-th fine grinding) together, storing area 4 is sent by B cylinder 33, on It states material back and forth to transfer at A cylinder 31, refiner 32 and B cylinder 33 3, constitutes interior circulation fine grinding, distinguish for different materials It realizes different circulations, not only takes full advantage of grinding process, but also avoid the excessive grinding that other are not necessarily to excessive grinding material, mention High grinding fineness.

For convenience of use, refiner 32 and corase grinding area 2 can be set as to construct identical structure, consider the function of the two not Together, the specification of specific rotor, grinding pearl, separator is specifically arranged；For roughly grinding area 2, in conjunction with Fig. 3, area 2 is roughly ground It mainly include main engine bed 28, rack 29, main engine bed 28 is located in rack 29, and operation panel 281 is arranged on main engine bed 28；Grinding chamber Be set in main engine bed 28, rotor, separator 3f and grinding pearl be located in main engine bed 28,21 one end of feed pipe connect pneumatically every Membrane pump 25, and by the access of pneumatic diaphragm pump 25 pump 1 (for example refiner is then connected by pneumatic diaphragm pump and A cylinder), the other end In grinding chamber in access host seat 28；Funnel 24 is set at the top of main engine bed 28, funnel 24 provides lubricating oils to rotor, and Sealing element 241, cut-in temperature table 272 and pressure gauge 211 on grinding chamber, thermometer 272 and pressure gauge are formed in rotor tip 211 connect with operation panel 281 respectively, monitor the temperature and pressure in grinding chamber by operation panel 281, it is ensured that grinding is suitable It is carried out under the conditions of preferably；Baiting valve 26 and discharge nozzle 27 is arranged in 28 bottom of main engine bed, as corase grinding area 2 in use, baiting valve 26 with Discharge nozzle 27 is selected one (preferably discharge nozzle 27) and is connected to area 3 (in A cylinder 31) is refined；As refiner in use, baiting valve 26 It is connected to A cylinder 31, discharge nozzle 27 is connected to B cylinder.

The application has also done further work with regard to the cooling in above scheme, to avoid because caused by grinding high temperature it is poly- Close: cooling water pipe is arranged in 32 outer wall of refiner, and cooling water pipe is with the coolant liquid of 0-30 DEG C of cooling water or (- 25-15 DEG C) work For cooling medium, for carrying out cooling and isothermal holding to refiner；By taking Fig. 3 as an example, 28 outer wall of main engine bed is equipped with water inlet pipe 22 and outlet pipe 23 be used as cooling water pipe, be connected with cooling water or coolant liquid in water inlet pipe 22, outlet pipe 23, grinding chamber dropped Temperature.With the progress of grinding, high speed grinding friction can generate certain heat, these heats are built up in fixed space, It will cause the promotion of temperature of charge in entire grinding chamber and grinding chamber, and stain, dispersing agent can generate under the high temperature conditions High temperature polymerization not only influences raw material (referring to the synthesis auxiliary agent of stain, dispersing agent and necessary amount, similarly hereinafter) utilization rate, also will form original Expecting impurity, influences the molding effect of mill base, the application controls fine grinding area's temperature, and preferably with cooling water or coolant liquid, Built-in temperature control is especially refined at 0-40 DEG C in fine grinding area, the normal effect that both will not influence raw material plays, and also avoids The excessive consumption of energy.

The application has done further work with regard to the rotor in above scheme, it is ensured that material circulation is quick: in conjunction with Fig. 5, turning Attached bag includes ontology 3a, shaft 3d, turns tooth 3b and turn trough 3c, and shaft 3d (is not shown in figure by power source, the conducts such as motor can be used Power source) its rotation is driven, shaft 3d is fixedly connected with ontology 3a, and the setting of ontology 3a outer wall turns tooth 3b, and the section for turning tooth 3b is Trapezoidal, the adjacent groove turned between tooth 3b and ontology 3a outer wall constitute turn trough 3c, and grinding pearl is fallen in turn trough 3c, and is matched therewith It closes and completes grinding.When shaft 3d drives ontology 3a rotation, turn tooth 3b and rotate therewith, turns outside tooth 3b (to refer to far from ontology 3a Side) small trapezoidal sectional shape effectively drives material to rotate with it to the imperial palace side of ontology 3a (refer to close to), and makes material Vortex form is formed between turn trough 3c, to effectively increase grinding efficiency.

To ensure to grind sufficiently, the application also improves mixed zone, equal with the mixing for improving stain and dispersing agent Even property: in conjunction with Fig. 2, mixed zone 1 includes agitator 15, agitating shaft 14 and agitator disk 16, and motor 11 is located on column 18, motor 11 Output end and shaft 14 belt pulley 13 between with the connection of driving belt 12, motor 11 rotates, through driving belt 12 by power It is transferred to agitating shaft 14, and agitating shaft 14 is driven to rotate, 14 lower end of agitating shaft is protruded into agitator 15, and is being located at agitator 15 In agitating shaft 14 on be arranged agitator disk 16 (16 settable one layers of agitator disk, may also set up multilayer).When material enters agitator After 15, agitating shaft 14 is started turning in the case where motor 11 (non-same with corase grinding area, fine grinding area) drives, and this rotation inherently can It drives material to rotate with it and mix, and agitator disk 16 is set and is then effectively stirred the material rotated with rotation axis, aggravate The mixing of stain and dispersing agent uniformly provides premise for subsequent grinding.After to be ground, ball valve 17 is opened, can will be mixed Even material is transferred to corase grinding area 2.

The mill base of above-mentioned apparatus preparation is detected, mill base solid content is 13.25% (disposable sample, 180kg).Mill base Grain fineness reached nanoscale, and without adding the dispersion hydrotropy analog assistant such as excessive diffusion machine, grinding agent, so thereon Dye rate is higher very than Conventional dye (such as commercially available disperse orange S-4RL, disperse scarlet GS, disperse dark blue H-GL, dispersion are ECT black) It is more；" foot water " is limpider after dye, and no excessive defective material exists, and in addition to special dark color, reduction cleaning that it goes without doing substantially can be saved also Original cleaning and afterwash procedure, to reduce dyeing water consumption act on highly significant, water-saving 3, save with sodium hydrosulfite, alkali or 80 DEG C × 30 minutes reduction cleanings of reduction cleaner and the neutralization of rear road acid, water-washing process.

During carrying out placement detection stability, suspended substance stable system, long-term storage is not in conjunctiva, agglomerates now As, can prevent powder dyestuff because worker's sawing sheet it is bad caused by color dot, color spot and other issues；Yarn dyeing can directly be poured into Cylinder adds water to dye, and reduces or remits the sawing sheet time, effectively improves production efficiency.

(examination criteria: GB/T 21295-2014 " clothes is detected to the fabric dyed using present case mill base The technical requirements of physicochemical property ", GB 18401-2010 " national general safety technical code for textile products " B class directly contacts skin The textile product of skin), color fastness to washing, colour fastness to rubbing, colour fastness to perspiration, color fastness to light meet that (report number is GZHT02021837) respective standard requirement.See Table 1 for details for specific testing result-table 4.

1 product color fastness to washing testing result summary sheet of table

2 product fastness to rubbing testing result summary sheet of table

3 product fastness to perspiration testing result summary sheet of table

4 product color fastness to light testing result summary sheet of table

Claims (10)

1. a kind of mill base processing unit (plant), it is characterised in that: including be sequentially arranged mixed zone, corase grinding area, fine grinding area, storing area, Inspection area and bagging area, the stain, dispersing agent are added by mixed zone and are mixed in mixed zone, set between mixed zone and corase grinding area Pump one is set, realizes that material is sent from mixed zone to corase grinding area；Rotor, separator, grinding pearl are set in corase grinding area, separator gap is 0.5-1.5mm grinds bead diameter 0.8-2mm；Rotor, separator and grinding pearl, separator gap L T.LT.LT are set in fine grinding area 0.8mm, grinding pearl are PU pearl or 95 and the above zirconium oxide bead, grind bead diameter 0.4mm or less.

2. a kind of mill base processing unit (plant) as described in claim 1, it is characterised in that: the fine grinding area is also correspondingly arranged on synthesis Auxiliary agent area realizes material transferring between comprehensive auxiliary agent area and fine grinding area with pump two.

3. a kind of mill base processing unit (plant) as described in claim 1, it is characterised in that: in the fine grinding area, separator gap is 0.05-0.6mm。

4. a kind of mill base processing unit (plant) as described in any one of claims 1-3, it is characterised in that: the fine grinding area includes fine grinding Machine, A cylinder and B cylinder, separator and grinding pearl are arranged in refiner, and two entrances one opening, one entrance is arranged in A cylinder It is connected with corase grinding area, another entrance and comprehensive auxiliary agent area connect；Opening is connected with refiner, and B cylinder sets two openings, an opening and essence Grinding machine connection, another opening are connected to storing area；It roughly grinds area's discharging and enters A cylinder, be sent into refiner through A cylinder, it is complete in refiner After grinding, it is sent into B cylinder and returns back to refiner, then be transferred to B cylinder after standing in B cylinder, and so on ground to road second from the bottom When, it is transferred to A cylinder through refiner, opens comprehensive auxiliary agent area, comprehensive auxiliary agent is added on demand, then is transferred to refiner progress and finally grinds together Mill is sent into storing area through B cylinder.

5. a kind of mill base processing unit (plant) as described in claim 1, it is characterised in that: the corase grinding area mainly include main engine bed, Rack, main engine bed are located in rack, and operation panel is arranged on main engine bed；Grinding chamber is set in main engine bed, rotor, separator and Grinding pearl is located in main engine bed, and feed pipe one end connects pneumatic diaphragm pump, and by pneumatic diaphragm pump access pump one, another termination Enter in the grinding chamber in main engine bed；Cut-in temperature table and pressure gauge on grinding chamber, thermometer and pressure gauge respectively with operation panel Connection monitors the temperature and pressure in grinding chamber by operation panel；Baiting valve and discharge nozzle, baiting valve is arranged in main engine bed bottom One is selected with discharge nozzle to be connected to fine grinding area.

6. a kind of mill base processing unit (plant) as claimed in claim 5, it is characterised in that: the refiner constitutes phase with corase grinding area Together, specification is different, and the pneumatic diaphragm pump and A cylinder of feed pipe connection are connected；Baiting valve is connected to A cylinder, and discharge nozzle is connected to B cylinder.

7. a kind of mill base processing unit (plant) as claimed in claim 4, it is characterised in that: the rotor includes ontology, shaft, turns tooth And turn trough, shaft are fixedly connected by its rotation of power source drive, shaft with ontology, body outer wall setting turns tooth, turns the section of tooth To be trapezoidal, the adjacent groove turned between tooth and body outer wall constitute turn trough；Grinding pearl is located in turn trough, and cooperates in fact with turn trough Now grind；End turns to be set with separator on tooth.

8. a kind of mill base processing unit (plant) as claimed in claim 7, it is characterised in that: the separator is mesh structure.

9. a kind of mill base processing unit (plant) as described in claim 1, it is characterised in that: the mixed zone includes agitator, stirring Axis and agitator disk, the agitating shaft are driven by motor, and agitating shaft lower end is protruded into agitator, and in the stirring being located in agitator Agitator disk is set on axis.

10. a kind of mill base processing unit (plant) as described in claim 1, it is characterised in that: cooling water is arranged in the refiner outer wall Pipe.