A kind of fountain staple in bulk processing meanss
Technical field
The present invention relates to a kind of fountain staple in bulk processing meanss, belong to staple in bulk processing technology field.
Background technology
Staple in bulk be typically with dye vat dyeing, by staple in bulk contaminate load dye cage, in hanging in dye vat, control temperature and when
Between carry out dyeing process, after dyeing terminates, carry out multiple tracks cleaning in bathtub, and to soap or alkali cleaning mode is cleaned, clearly
Washed journey needs to consume substantial amounts of moisture, cleaning agent etc., cleans relatively costly;And the rinsing machine of routine mainly by bath and
Some that upper roller setting up and down and lower roll are constituted, lower roll is then located in the washing lotion of bath, based on this structure of rinsing machine,
Only fabric or cloth can be washed, and staple in bulk is non-continuous state, thus cannot be washed using existing rinsing machine, dye
Staple in bulk after color fabric is made into or into after net can only carry out overall washing, need to be washed through multiple tracks, and water washing effect is not
Good, water consumption is huge, and according to the difference of dyestuff, in addition it is also necessary to carry out hot water wash, alkali cleaning, soap or even pickling, wash high cost.
For drawbacks described above, also have using the pouring of horizontal feed roll formula washing and pouring roll formula dyeing, i.e.,:Staple in bulk is placed in
Between lower two layers of mesh, by the extruding of twice net, dyeing or the washing process of staple in bulk are realized, although this mode overcomes
Defect is stated, but in processing procedure, upper off line driven roller roller speed is inconsistent, and fibre web is easily broken;It is upper it is off line between, fiber is received
To larger extruding force, cause fibre net structure fine and close, cleaning or dyeing cannot be properly completed;Meanwhile, because of the dyeing or clear of fiber
Wash it is upper it is off line between complete under squeezing action, web caliper is limited, and accessible fibre weight is also limited.
Based on this, subject application is made.
The content of the invention
Loose stock dyeing or the drawbacks described above existing for washing process in overcome prior art, the application provides a kind of spray
Pouring formula staple in bulk processing meanss.
For achieving the above object, the technical scheme that the present invention takes is as follows:
A kind of fountain staple in bulk processing meanss, including casing, process net, roll and the spraying mechanism in casing,
The described banding of casing four is closed, and only in rear and front end inlet porting and outlet, is processed net and is driven by drive roll, and is entered from import,
Gone out by outlet;Be provided with some groups of roll along net direct of travel is processed, roll includes topping roll and bottom roll, topping roll, under
Roll separation is processed above and below net, and the axis of topping roll misplaces with the axis of bottom roll, and the axis of topping roll
Line passes through bottom roll, and topping roll is contrary with bottom roll rotation direction;Treatment fluid in spraying mechanism from topping roll top spray and
Under, the process such as the staple in bulk online to process is dyeed, fixation, cleaning, softness.
Further, as preferred:
Described spraying mechanism includes treatment trough, and the spray direction opposite rolls axis for the treatment of trough is obliquely installed.Spray
Drench the vertical axis of direction and roll to incline, on the one hand, in topping roll, bottom roll rotation process, can with topping roll, under roll
Roller is flowed into staple in bulk between the two, on the other hand, is also beneficial to strip down the staple in bulk being wrapped on roll, it is to avoid
Collaring.
Described process side off the net arranges and processes liquid bath, is connected by pipeline or pump between the two, for receiving and supplies
Treatment fluid is to treatment trough.
Heating tube is set in described process liquid bath, for stablizing the temperature for the treatment of fluid.
Described process side off the net arranges tank, for supplying the concentration of clear water, adjustment treatment fluid.
Heat exchanger is set in described tank, for stablizing the temperature of clear water and treatment fluid.Set at described tank outlet
Baffle plate is equipped with, baffle plate is located at and processes online side, to avoid fiber from exporting out outflow.It is furthermore preferred that described cabinet wall sets
Fixed seat is put, baffle plate is fixed on the online side of process by fixed seat;Described baffle plate is arranged in pairs on the inwall of casing both sides.
The operation principle of the application and have the beneficial effect that:
(1) be conducive to keeping fibre morphology constant, it is ensured that treatment effect.The application adopts single network mode, entirely processes
Cheng Zhong, pending staple in bulk can be laid immediately on process on the net, under the spray for the treatment of fluid, without the need for into net, dissipating in whole process
Fibre morphology is constant, and during pouring is rolled gradually be in blanket, staple in bulk with soft fluffy state complete dyeing, fixation, cleaning and
The process such as softness, dyeing, cleaning are more abundant.
(2) staple in bulk treating capacity significantly increases, and is conducive to improving treatment effeciency.The application in processing procedure, with scattered fibre
Only a pair roller and the process net through a pair roller of dimension directly contact, fiber thickness is unrestricted, and feed quantity can be big
Big to improve, treatment effeciency is improved.
(3) treatment fluid absorption efficiency is high.In this application, to sprawl, mode is fluffy to be placed in process on the net to staple in bulk, only exists
Extruded at roll, and (vertical) axis of topping roll misplaces with (vertical) axis of bottom roll, makes topping roll inclined
After bottom roll (i.e. relative to fiber direct of travel, topping roll leans backward, and bottom roll ranks forefront), in this dislocation clamping process,
Be conducive to the extruding of staple in bulk, and treatment fluid is flowed into staple in bulk between the two, improve the absorption for the treatment of fluid.
(4) avoid collaring, processing fluency is good.The emission direction for the treatment of fluid is obliquely installed in the application, its
With the contact area that roll direct of travel increased at an angle, both treatment fluid and staple in bulk, treatment fluid and staple in bulk operation
It is in opposite direction, be conducive to fiber spin-off roll, it is to avoid collaring.
(5) whole processing procedure is closed state, is conducive to improving the utilization rate of the energy, and reduces environmental pollution.At this
In application, treatment fluid, roll and process net processing region be respectively positioned in casing, casing only rear and front end arrange import and
Outlet, processes net and is penetrated by import, is passed by outlet, and staple in bulk is sent, involved process by entering by outlet
Journey almost completes completely in the closing space that casing is formed, it is to avoid the diverging of temperature in processing procedure, corresponding to process
Liquid also can be dissipated in atmosphere with gaseous state or steam condition, and the enclosed construction of casing avoids the operation ring around the process influence
Border, and treatment fluid that these are dissipated and heat be collected, in the environment of insulation and sealing, the box body wall of import and export
Baffle plate is also used as, prevents staple in bulk from dropping, improve injection flow rate, improve spraying effect, while treatment temperature can be appropriate
Higher scope is brought up to, treatment effect is improved, the raising of energy utilization rate, environmental factor interference drop are conducive to again
Low, the controllability of whole processing procedure is improved.
Description of the drawings
Fig. 1 is the structural representation of equipment employed in the application;
Fig. 2 is the partial enlarged drawing at A positions in Fig. 1;
Fig. 3 is the partial enlarged drawing at B positions in Fig. 1;
Fig. 4 is M-M directions enlarged section in Fig. 3.
Wherein label:1. net is processed;2. roll;21. topping rolls;22. bottom rolls;3. treatment trough;4. drive roll;5. process
Liquid bath;6. heating tube;7. tank;8. heat exchanger;9. casing;91. wallboards;92. fixed seats;93. top boards;94. bottom plates;
95. baffle plates.
Specific embodiment
Embodiment 1
A kind of fountain staple in bulk processing meanss of the present embodiment, with reference to Fig. 1, Fig. 2 and Fig. 3, pending staple in bulk is placed in place
On reason net 1, being rotated by drive roll 4 of net 1 is processed, the process direct of travel of net 1 is provided with some groups of roll 2, rolled
Roller 2 includes topping roll 21 and bottom roll 22, and topping roll 21, the separation of bottom roll 22 are processed above and below net 1, topping roll 21
Axis misplaces with the axis of bottom roll 22, and the axis of topping roll 21 passes through bottom roll 22, topping roll 21 and bottom roll
22 rotation directions with net 1 is processed with dragging staple in bulk conversely, advanced;Treatment fluid is sprayed from the treatment trough 3 of the top of topping roll 21
And under, dyeed to processing the staple in bulk on net 1, after fixation, cleaning, softness etc. process, sent.
Wherein, the axis of spray direction opposite rolls 2 for the treatment of fluid is obliquely installed.Spray direction and the vertical axis of roll 2
Line is inclined, on the one hand, in topping roll 21, the rotation process of bottom roll 22, can flow into both it with topping roll 21, bottom roll 22
Between staple in bulk in, on the other hand, be also beneficial to strip down the staple in bulk being wrapped on roll 2, it is to avoid collaring;Place
Reason net 1 on bag be provided with casing 9, roll 2 and treatment fluid are respectively positioned in the casing 9, the two ends of casing 9 be respectively provided with fiber entry and
Fiber outlet, the fibre material after shredding is uniformly laid in process on the net, and enters in casing with net is processed, and treatment fluid is certainly
Spray in treatment trough 3 and under, to through staple in bulk material dyeed, fixation, clean, soap, after softness etc. processes, by going out
Mouth is sent, and when can avoid sending, fiber falls the lower section of process net 1 by band.
The application adopts single network mode, and in whole processing procedure, pending staple in bulk can be laid immediately on process net 1,
Without the need for into net, staple in bulk form is constant in whole process, and it is in gradually blanket during pouring is rolled under the spray for the treatment of fluid
Shape, staple in bulk completes dyeing, fixation, cleaning and softness etc. and processes with soft fluffy state, and dyeing, cleaning are more abundant.
Only a pair roller 2 and the process net through a pair roller 2 in processing procedure, with staple in bulk directly contact
1, fiber thickness is unrestricted, and feed quantity is greatly improved, and treatment effeciency is improved.
In this application, to sprawl, mode is fluffy to be placed on process net 1 staple in bulk, is only extruded at roll 2, and
(vertical) axis of topping roll 21 misplaces with (vertical) axis of bottom roll 22, makes topping roll 21 to the rear in bottom roll 22
(i.e. relative to fiber direct of travel, topping roll leans backward, and bottom roll ranks forefront), in this dislocation clamping process, is conducive to dissipating fibre
The extruding of dimension, and treatment fluid is flowed into staple in bulk between the two, improve the absorption for the treatment of fluid.
The emission direction for the treatment of fluid is obliquely installed, its increased at an angle, both with the direct of travel of roll 2 treatment fluid with
The contact area of staple in bulk, treatment fluid and staple in bulk traffic direction are conversely, be conducive to fiber spin-off roll, it is to avoid curling round the roll shows
As.
The processing region for the treatment of fluid, roll 2 and process net 1 is respectively positioned in casing 9, and casing 9 is only arranged in rear and front end
Inlet and outlet, processes net 1 and is penetrated by import, is passed by outlet, and staple in bulk is sent by entering by outlet, involved
Processing procedure almost complete in the closing space that casing 9 is formed completely, it is to avoid the diverging of temperature, phase in processing procedure
The treatment fluid answered also can be dissipated in atmosphere with gaseous state or steam condition, and the enclosed construction of casing 9 is avoided around the process influence
Operating environment, and treatment fluid that these are dissipated and heat be collected, in the environment of insulation and sealing, import and export
Box body wall be also used as baffle plate, prevent staple in bulk from dropping, improve injection flow rate, improve spraying effect, while treatment temperature can
Higher scope is brought up to appropriate, it is to avoid treatment fluid is because the too high caused a large amount of discharge of steam of temperature are to operating environment
In, and it is easy to insulation, and treatment effect is improved, the raising of energy utilization rate is conducive to again, environmental factor interference is reduced, whole
The controllability of individual processing procedure is improved.
Embodiment 2
The present embodiment is identical with the setting of embodiment 1 and operation principle, and difference is:Process the lower section of net 1 and treatment fluid is set
Groove 5, for storage and providing chemical liquid to treatment trough 3;Process and arrange in liquid bath 5 heating tube 6, process the lower section of net 1 and tank is set
7, for supplying the concentration of clear water, adjustment treatment fluid;Heat exchanger 8 is set in tank 7, for stablizing the temperature of clear water and treatment fluid
For stablizing the temperature for the treatment of fluid.
Treatment fluid is entered by the process liquid bath in last area 51 (i.e. along net direct of travel is processed, near tank outlet), Jing
Pump is driven into treatment trough 3, and fibre material is processed after overflow, and treatment fluid returns to the next process liquid bath 52 of the treatment trough
In, the rest may be inferred, and first is processed after liquid bath at material inlet, and the heat exchanger 8 in overflow and Jing tanks 7 is by unnecessary heat
In the moisturizing returned in feed trough 7, energy saving.
Embodiment 3
The present embodiment is identical with the setting of embodiment 1 and operation principle, and difference is:With reference to Fig. 4, export near casing 9
Position at, be respectively fixed with fixed seat 92 in the relative two side wall panels 91 of casing 9, top board 93 is installed in fixed seat 92
With bottom plate 94, process between two fixed seats 92 of the fixing phase pair of net 1, diagonally downward, it is towards process net 1 for top board 93
One end arranges baffle plate 95, and baffle plate 95 may be configured as having resilient rubber slab, and bottom plate 94 is located at the lower section for processing net 1, both may be used
Together with top board 93 fix fixed seat, again can together with top board 93 fixing process net 1.The fiber Jing baffle plates being disposed
95 scrape, it is to avoid it is taken out of together with process net by the outlet of casing 9.
Embodiment 4
The present embodiment is identical with the setting of embodiment 1 and operation principle, and difference is:Process the lower section of net 1 and treatment fluid is set
Groove 5, for storage and providing chemical liquid to treatment trough 3;Process and arrange in liquid bath 5 heating tube 6, process the lower section of net 1 and tank is set
7, for supplying the concentration of clear water, adjustment treatment fluid;Heat exchanger 8 is set in tank 7, for stablizing the temperature of clear water and treatment fluid
For stablizing the temperature for the treatment of fluid.
Treatment fluid is entered by the process liquid bath in last area 51 (i.e. along net direct of travel is processed, near tank outlet), Jing
Pump is driven into treatment trough 3, and fibre material is processed after overflow, and treatment fluid returns to the next process liquid bath 52 of the treatment trough
In, the rest may be inferred, and first is processed after liquid bath at material inlet, and the heat exchanger 8 in overflow and Jing tanks 7 is by unnecessary heat
In the moisturizing returned in feed trough 7, energy saving.
With reference to Fig. 4, at the position of the outlet of casing 9, in the relative two side wall panels 91 of casing 9 fixation is respectively fixed with
Seat 92, is provided with top board 93 and bottom plate 94 in fixed seat 92, process between two fixed seats 92 of the fixing phase pair of net 1, on
Diagonally downward, it arranges baffle plate 95 to pressing plate 93 towards the one end for processing net 1, and baffle plate 95 may be configured as having resilient rubber slab,
Bottom plate 94 is located at the lower section for processing net 1, and fixed seat both can have been fixed together with top board 93, can consolidate together with top board 93 again
Surely net 1 is processed.The fiber Jing baffle plates 95 being disposed are scraped, it is to avoid it is taken out of together with process net by the outlet of casing 9.
Comparative example 1
With the embodiment as a comparison of patent 20141000095711, its cleaning performance is contrasted, ginseng is shown in Table 1.
Comparative example 2
With the embodiment as a comparison of patent 20141000095656, its Color is contrasted, ginseng is shown in Table 2.
Washing process effect comparison table under the different implementation conditions of table 1
|
Comparative example 1 |
Present invention washing |
Treating capacity (kg/24h) |
10000 |
20000 |
Water consumption (T/ ton staple in bulks) |
40 |
15 |
Energy consumption (yuan/ton) |
145-150 |
70-80 |
The treatment effect table of comparisons is dyeed under the different implementation conditions of table 2
|
Comparative example 1 |
Present invention dyeing |
Treating capacity (kg/24h) |
10000 |
20000 |
Consumption amount of dye (T/ ton staple in bulks) |
45-50 |
18-23 |
Energy consumption (yuan/ton) |
165-180 |
80-110 |
The application adopts single network mode, and in whole processing procedure, pending staple in bulk can be laid immediately on process on the net,
Without the need for into net, staple in bulk form is constant in whole process, and it is in gradually blanket during pouring is rolled under the spray for the treatment of fluid,
Staple in bulk completes dyeing, fixation, cleaning and softness etc. and processes with soft fluffy state, and dyeing, cleaning are more abundant;In processing procedure
In, only a pair roller and the process net through a pair roller with staple in bulk directly contact, fiber thickness is unrestricted, feeds
Enter amount to be multiplied, and the speed for processing net 1 can slow down, treatment effeciency is improved;Meanwhile, water drenching amount can also be simultaneously into extraordinarily
Greatly, exchange capacity is increased, fluffy staple in bulk is more beneficial for the infiltration of shower water, can improve cleaning performance;Staple in bulk is sprawling
Mode is fluffy to be placed in process on the net, is only extruded at roll, and (vertical) axis of topping roll is (perpendicular with bottom roll
Directly) axis dislocation, (i.e. relative to fiber direct of travel, topping roll leans backward, and bottom roll is occupied in bottom roll to make topping roll to the rear
Before), in this dislocation clamping process, be conducive to the extruding of staple in bulk, and treatment fluid is flowed into staple in bulk between the two,
Improve the absorption for the treatment of fluid;The closed structure of casing 9, decreases the loss of heat;Spray is divided into two kinds of forms, rolls upper
At roller, bottom roll, spray is carried out in an inclined manner, can avoid the winding of fiber, and other positions are then using normal spray.
Above content is combine that the preferred embodiment of the invention made to provided technical scheme further detailed
Describe in detail bright, it is impossible to assert that the invention is embodied as being confined to above-mentioned these explanations, for the affiliated technology of the invention
For the those of ordinary skill in field, without departing from the concept of the premise of the invention, some simple deductions can also be made
Or replace, should all be considered as belonging to the protection domain of the invention.