CN203729085U - Wringer suitable for dehydrating loose fiber or loose fiber cakes - Google Patents
Wringer suitable for dehydrating loose fiber or loose fiber cakes Download PDFInfo
- Publication number
- CN203729085U CN203729085U CN201420012285.6U CN201420012285U CN203729085U CN 203729085 U CN203729085 U CN 203729085U CN 201420012285 U CN201420012285 U CN 201420012285U CN 203729085 U CN203729085 U CN 203729085U
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- Prior art keywords
- bulk fibre
- cylinder body
- tubular cylinder
- wringer
- cake
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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- 239000000835 fiber Substances 0.000 title claims abstract description 160
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 24
- 230000018044 dehydration Effects 0.000 claims description 24
- 238000006297 dehydration reaction Methods 0.000 claims description 24
- 239000012530 fluid Substances 0.000 claims description 15
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 claims description 8
- 230000000903 blocking effect Effects 0.000 claims description 4
- 239000011148 porous material Substances 0.000 claims description 3
- 238000004043 dyeing Methods 0.000 abstract description 19
- 238000000034 method Methods 0.000 abstract description 17
- 239000000975 dye Substances 0.000 description 54
- 238000005406 washing Methods 0.000 description 11
- 239000007788 liquid Substances 0.000 description 9
- 238000012805 post-processing Methods 0.000 description 9
- 238000009736 wetting Methods 0.000 description 6
- 238000005097 cold rolling Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 238000010276 construction Methods 0.000 description 4
- 238000010186 staining Methods 0.000 description 4
- 229920000742 Cotton Polymers 0.000 description 3
- 239000012752 auxiliary agent Substances 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000004744 fabric Substances 0.000 description 3
- 238000002203 pretreatment Methods 0.000 description 3
- 230000007115 recruitment Effects 0.000 description 3
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000004061 bleaching Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000003086 colorant Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 238000011156 evaluation Methods 0.000 description 2
- 238000005457 optimization Methods 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 238000002791 soaking Methods 0.000 description 2
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 239000007844 bleaching agent Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000005282 brightening Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005213 imbibition Methods 0.000 description 1
- 239000010446 mirabilite Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 238000005554 pickling Methods 0.000 description 1
- 239000000344 soap Substances 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 238000009968 stock dyeing Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- 238000004048 vat dyeing Methods 0.000 description 1
- 238000003809 water extraction Methods 0.000 description 1
Landscapes
- Treatment Of Fiber Materials (AREA)
Abstract
The utility model relates to a wringer suitable for dehydrating loose fiber or loose fiber cakes and belongs to the technical field of loose fiber dyeing. The wringer comprises a base, a tubular cylinder body and a top plate. The tubular cylinder body is installed on the base, leak holes are formed in the tubular cylinder body, the top plate is movably connected with the tubular cylinder body, the upper side of the top plate is connected with a pressure assembly, and a power assembly drives the top plate to make piston motion in the tubular cylinder body so that water in the loose fiber in the tubular cylinder body can be squeezed out. The wringer suitable for dehydrating loose fiber or loose fiber cakes is applied to dyeing cold rolled piles of the loose fiber and has the advantages of being even in dyeing, little in water using amount, simple in procedure and the like.
Description
Technical field
The utility model relates to a kind of wringer that is applicable to bulk fibre or the dehydration of bulk fibre cake, belongs to bulk fibre dehydration technique field.
Background technology
Bulk fibre cake after dyeing contains a large amount of moisture, directly dries and can consume a large amount of energy, and existing dehydration procedure generally carries out on centrifugal dehydrator, conventional centrifugal dehydrator is tubular structure, when dehydration, first bulk fibre cake is put into the cylinder of Water Extraction Machinery, then closed upper cover, starter motor, under motor drives, carry out the centrifugal dehydration of bulk fibre cake, after dehydration, take out after also shredding, send in drying unit and dry.But due to the structural limitation of centrifugal drier, the restriction of bulk fibre dehydration technique and state of art, adopt existing centrifugal dewatering technology cannot carry out the dehydration of large cotton piece, also just further have influence on the lifting of bulk fibre dye vat volume, dyeing, dehydration, oven dry are service intermittent, and each workpiece place will be equipped with corresponding personnel, recruitment is more, in dehydration, labor intensity of operating staff is large, and electric energy consumption is high, and production efficiency is very low.
Utility model content
For overcoming the existing above-mentioned defect of loose stock dyeing in prior art, the utility model provides a kind of wringer that is applicable to bulk fibre or the dehydration of bulk fibre cake.
For achieving the above object, the technical scheme that the utility model is taked is as follows:
A kind of wringer that is applicable to bulk fibre or the dehydration of bulk fibre cake, comprise pedestal, tubular cylinder body and top board, tubular cylinder body is arranged on pedestal, on tubular cylinder body, be provided with small opening, top board is flexibly connected with tubular cylinder body, top board top is connected with pressure assembly, and Power Component drives top board to do piston movement in tubular cylinder body, to realize, the squeezing of moisture in bulk fibre in tubular cylinder body is extruded.
Further, as preferably:
On the bottom of described tubular cylinder body and/or sidewall, be provided with small opening, the aperture of small opening is 2-3mm, the every cm of percent opening 50-70%(
2on the body wall of tubular cylinder body, the area of small opening accounts for 50-70%).
Described Power Component comprises briquetting, crossbeam, power source and column, and briquetting is between top board and crossbeam, and crossbeam movable set is on column, and power source drives crossbeam move up and down or rotatablely move along column, to realize the movement of briquetting or briquetting and top board.As preferably, described power source is cylinder, oil cylinder or electronic.
Described tubular cylinder body below is provided with collecting tank, for collecting the moisture flowing out with emptying small opening.
Described collecting tank is provided with leakage fluid dram, and leakage fluid dram place is provided with filter screen, prevents that fiber from blocking leakage fluid dram.
On described tubular inboard wall of cylinder block, be provided with water distributing pore, water distributing pore is connected with clear water pipe, after squeezing water, cleans tubular cylinder body.
Bulk fibre or bulk fibre cake are positioned in tubular cylinder body, under the effect of Power Component, top board moves down, and push bulk fibre or the bulk fibre cake between top board and tubular cylinder body, under external force, moisture in bulk fibre or bulk fibre cake is extruded, and the small opening arranging on tubular cylinder body flows out, after the moisture in bulk fibre or bulk fibre cake drains, Power Component drives top board to move up, and top board is shifted out from tubular cylinder body, the bulk fibre or the bulk fibre cake that remove moisture are completely sent in postprocessing working procedures, because most moisture and dyestuff are squeezed out from bulk fibre or bulk fibre cake, what bring post processing into is only moisture and the dyestuff of minute quantity, thereby alleviate and in last handling process, washed difficulty, water consumption and washing time greatly reduce.
Adopt above-mentioned wringer to carry out the dehydration procedure of the cold-rolling heap staining of bulk fibre, bulk fibre successively contaminating device one, drain device, contaminate and soak squeezings (contaminate for the first time → drain → dip-dye for the second time) in device two, in rotary type cold dome machine, be rotated after formula cold dome, after pushing in the utility model wringer and draining, send into again after-treatment device, adopt the beneficial effect of this device dehydration as follows:
1. the utility model is applied in whole cold-rolling heap staining flow process, wherein, soak the dip-dye device one that squeezes in device, drain device and contaminate device two and carry out successively two and soak a squeezing (contaminate for the first time → drain → contaminate for the second time) mode and carry out, the utility model, as the device that drains wherein, has guaranteed that dyestuff is evenly distributed in bulk fibre or bulk fibre cake.Bulk fibre is contaminated for the first time successively → is drained → dip-dye for the second time, first by wetting to outer field bulk fibre or bulk fibre cake, after outer bulk fibre or bulk fibre cake are wetting, drain, drain in process, pass through External Force Acting, by dyestuff from outer bulk fibre or bulk fibre cake are extruded when, also the dye liquor on outer bulk fibre or bulk fibre cake is clamp-oned in internal layer, internal layer bulk fibre is tentatively soaked, while once dip-dye again after draining, because bulk fibre or the bulk fibre cake of outer and internal layer are all wetting states, can well absorb dye liquor, soak squeezing effect better evenly, for follow-up cold dome fixation provides guarantee.
2. wringer is for the dehydration of bulk fibre after follow-up dyeing, like this setting can be fully, fast moisture and dye liquor are extruded from bulk fibre or bulk fibre cake.Bulk fibre or bulk fibre cake are positioned in tubular cylinder body, under the effect of Power Component, top board moves down, and push bulk fibre or the bulk fibre cake between top board and tubular cylinder body, under external force, moisture in bulk fibre or bulk fibre cake is extruded, and the small opening arranging on tubular cylinder body flows out, after the moisture in bulk fibre or bulk fibre cake drains, Power Component drives top board to move up, and top board is shifted out from tubular cylinder body, because most moisture and dyestuff are squeezed out from bulk fibre or bulk fibre cake, avoid dye liquor and moisture to be brought in postprocessing working procedures, thereby alleviate the working strength of last handling process, washing difficulty has reduced, water consumption is reduced to 1/8 of conventional dye vat dyeing, washing time is also shortened.
Bulk fibre soaks squeezing and adds squeeze water in wringer provided by the utility model, overcome the difficult problem that discontinuous state bulk fibre cannot adopt cold rolling heap technology dyeing, directly raw material bulk fibre or bulk fibre cake are dyeed, bulk fibre after dyeing is weaved again, compared with dying mode on conventional dye vat, on dye more even, and on dye in process without adding dyeing auxiliaries, also need not provide extra thermal source to heat, manufacturing procedure is simplified, washing, baked strength in post processing reduce, and water consumption, energy consumption and production cost reduce greatly.
Brief description of the drawings
Fig. 1 is the structural representation of the utility model while being applied to bulk fibre cold-rolling heap staining;
Fig. 2 is the structural representation of rotary type cold dome machine in Fig. 1;
Fig. 3 is the structural representation of the utility model wringer.
Number in the figure: 1. soak squeezing device; 11. contaminate device one; 12. drain device; 13. contaminate device two; 2. rotary type cold dome machine; 21. frames; 22. chassis; 23. transverse axis; 24. side shafts; 25. handles one; 26. handles two; 3. wringer; 30. pedestals; 31. tubular cylinder bodies; 32. small openings; 33. top boards; 34. collecting tanks; 35. briquettings; 36. crossbeams; 37. columns; 38. leakage fluid drams; 39. filter screens; 4. after-treatment device; 5. dye cage; 6. hermetically-sealed construction.
Detailed description of the invention
Embodiment 1
In conjunction with Fig. 1, the present embodiment is the wringer that is applicable to bulk fibre or the dehydration of bulk fibre cake, the utility model wringer is applied in bulk fibre cold-rolling heap staining streamline, this wringer front is for soaking device 1 and the rotary type cold dome machine 2 of squeezing, adopt this wringer to carry out the dyeing of bulk fibre, squeeze device 1(and contaminate device 1 → drain device 12 → dip-dye device 2 13 through soaking successively), rotary type cold dome machine 2 and wringer 3, wherein:
(1) soak squeezing device: soak squeezing device 1 and comprise dip-dye device 1, drain device 12 and contaminate device 2 13, bulk fibre is successively through contaminating device 1, draining device 12 and contaminate device 2 13 and carry out two and soak a squeezing, bulk fibre or bulk fibre cake are first contaminated for the first time in dip-dye device 1, contaminate and play pretreated object for the first time, first by wetting to outer field bulk fibre or bulk fibre cake; Bulk fibre after wetting or bulk fibre cake are placed in and drain device 12 and drain, pass through External Force Acting, by dyestuff when outer bulk fibre or bulk fibre cake are extruded, also the dye liquor on outer bulk fibre or bulk fibre cake is clamp-oned in internal layer, internal layer bulk fibre is soaked; Bulk fibre after draining or bulk fibre cake are put into dip-dye device 2 13 again and are contaminated for the second time, while dip-dye for the second time, because bulk fibre or the bulk fibre cake of outer and internal layer are all wetting states, can well absorb dye liquor, it is better evenly that entirety is soaked squeezing effect, for follow-up cold dome fixation provides guarantee.
(2) rotary type cold dome machine: in conjunction with Fig. 2, rotary type cold dome machine 2 comprises frame 21 and chassis 22, and chassis 22 is movably installed in frame 21 by transverse axis 23, transverse axis 23 is by handle one 25 regulation and control; Chassis 22 peripheries are symmetrically arranged with six for fixedly dying the side shaft 24 of cage 5, and side shaft 24 is by handle 2 26 regulation and control; Soak and squeeze complete bulk fibre or fabric taking-up, be vertically placed on rotary type cold dome machine 2 together with dying cage 5, and at bulk fibre or bulk fibre cake, hermetically-sealed construction 6 is set outward, as a kind of economic, mode easily, sealing structure can be passed through at bulk fibre or bulk fibre outer wrapping thin film, bulk fibre or bulk fibre cake and dye liquor sealing are contained in hermetically-sealed construction 6, and hermetically-sealed construction 6 provides a sealed environment for the rotary cold dome of bulk fibre or bulk fibre cake; Rotary handle 1, rotating shaft 23 drives chassis 22 and dyes cage 5 and rotate to the right inclination (directions of arrow in rotary type cold dome machine 2 left sides that in Fig. 1, rotary cold dome is corresponding), bulk fibre or bulk fibre cake in yarn cylinder and yarn cylinder are transferred to after level by vertical state, handle 1 stops operating, and start rotary handle 2 26, dye cage 5 and rotate (directions of arrow on rotary type cold dome machine 2 right sides that in Fig. 1, rotary cold dome is corresponding) with chassis 22, after cold dome completes, rotating shaft 23 drives chassis 22 direction rotation to the left, and yarn cylinder 5 is transferred to vertically by level.
(3) wringer: bulk fibre or bulk fibre cake are sent in wringer 3 and added squeeze water after rotary type cold dome machine 2 is processed, in conjunction with Fig. 3, wringer 3 comprises pedestal 30, tubular cylinder body 31 and top board 33, tubular cylinder body 31 is arranged on pedestal 30, on tubular cylinder body 31, be provided with small opening 32, top board 33 is flexibly connected with tubular cylinder body 31, top board 31 tops are connected with pressure assembly, Power Component drives top board 33 to do piston movement in tubular cylinder body 31, to realize, the squeezing of moisture in the interior bulk fibre of tubular cylinder body 31 is extruded.Wherein, small opening 32 is uniformly distributed on the bottom and sidewall of tubular cylinder body 31, and the aperture of small opening 32 is 2.5mm, and percent opening is 60%/cm
2(on every square centimeter of cylinder body body wall 31, the area of small opening 32 accounts for 60%); Power Component comprises briquetting 35, crossbeam 36, power source and column 37, briquetting 36 is between top board 33 and crossbeam 35, crossbeam 35 movable sets are on column 37, power source is cylinder, power source drives crossbeam 35 move up and down or rotatablely move along column 37, to realize the movement of briquetting 36 and top board 33.Bulk fibre or bulk fibre cake are positioned in tubular cylinder body 31, under the effect of Power Component, top board 33 moves down, and push bulk fibre or the bulk fibre cake between top board 33 and tubular cylinder body 31, under external force, moisture in bulk fibre or bulk fibre cake is extruded, and the small opening 32 arranging on tubular cylinder body 31 flows out, after the moisture in bulk fibre or bulk fibre cake drains, Power Component drives top board 33 to move up, and top board 33 is shifted out from tubular cylinder body 31, the bulk fibre or the bulk fibre cake that remove moisture are completely sent in postprocessing working procedures, because most moisture and dyestuff are squeezed out from bulk fibre or bulk fibre cake, what bring post processing into is only moisture and the dyestuff of minute quantity, thereby alleviate and in last handling process, washed difficulty, water consumption and washing time subtract greatly.
By adding after squeeze water of wringer 3, in bulk fibre or bulk fibre cake, no liquid flows out, and proceeds in after-treatment device 4, washes the post processings such as finish, antistatic, oven dry.
Adopt the above-mentioned dyeing apparatus of the present embodiment, can directly dye to raw material bulk fibre or bulk fibre cake, bulk fibre after dyeing is weaved again, compared with dying mode on conventional dye vat, above dye more even, and on dye in process without adding dyeing auxiliaries, also need not provide extra thermal source to heat, manufacturing procedure is simplified, and washing, baked strength in post processing reduce, and water consumption, energy consumption and production cost reduce greatly.
Embodiment 2
The present embodiment is identical with setting and the operation principle of embodiment 1, difference is: tubular cylinder body 31 belows of wringer 3, be provided with collecting tank 34 in pedestal 30 peripheries, collecting tank 34 is provided with leakage fluid dram 38, leakage fluid dram 38 places are provided with filter screen 39, collecting tank 34 is positioned at tubular cylinder body 31 belows, in bulk fibre or fabric, contain dyestuff, the liquid of auxiliary agent is after small opening 32 flows out, concentrate in collecting tank 34, again by leakage fluid dram 38, the liquid of collection is carried out emptying, and filter screen 39 can prevent that fiber from blocking leakage fluid dram 38, avoid carrying it in follow-up washing, these liquid are focused on, when alleviating follow-up washing work difficulty, the recyclable recycling of liquid of collecting, can realize the optimization utilization of resource, small opening 32 aperture 3mm, percent opening 70%.
Embodiment 3
The present embodiment is identical with setting and the operation principle of embodiment 1, difference is: below tubular cylinder body 31, be provided with collecting tank 34 in pedestal 30 peripheries, collecting tank 34 is provided with leakage fluid dram 38, leakage fluid dram 38 places are provided with filter screen 39, collecting tank 34 is positioned at tubular cylinder body 31 belows, in bulk fibre or fabric, contain dyestuff, the liquid of auxiliary agent is after small opening 32 flows out, concentrate in collecting tank 34, again by leakage fluid dram 38, the liquid of collection is carried out emptying, and filter screen 39 can prevent that fiber from blocking leakage fluid dram 38, avoid carrying it in follow-up washing, these liquid are focused on, when alleviating follow-up washing work difficulty, the recyclable recycling of liquid of collecting, can realize the optimization utilization of resource, the water distributor arranging on tubular cylinder body 31 inwalls, after the stock-dye of different batches, different colours, cleans tubular inboard wall of cylinder block, the impact of the fiber that can avoid last cylinder product residue on next cylinder product quality, small opening aperture 2mm, percent opening 50%.
Embodiment 4: comparative example
Adopt conventional dyeing apparatus (dye vat) to dye to bulk fibre, dyeing flow process and process conditions are as follows:
(1) pre-treatment: bulk fibre is carried out carrying out pre-treatment under high-temperature alkaline condition, make cotton there is good water imbibition, be beneficial to absorption, the diffusion of dyestuff in dyeing.
(2) bleach and brighten: the bulk fibre after pre-treatment is carried out to oxygen and float bleaching, wherein oxygen floats middle need interpolation alkaline agent and hydrogen peroxide stabilizer, and carries out pickling.
(3) dyeing: add dyestuff and auxiliary agent in bathtub; bath raio is 1:(10-20); be placed in this dye vat through the bulk fibre through bleaching and after brightening; dye liquor relies on the conveying of main pump; between fiber, penetrate circulation from dye vat internal layer to skin; dyestuff is dyed on evenly, after circulation a period of time, in nearly neutral dye liquor, gradation is added the accelerant such as glauber salt dyestuff is attached on bulk fibre as far as possible equably; In the time that dyestuff attachment fiber approaches balance, gradation adds alkaline agent to improve gradually dye liquor pH value, accelerates the fixation reaction of dyestuff and fiber, thereby dyestuff bonding is anchored on fiber, reaches painted object.
(4) post processing: after dyeing, a large amount of loose colours are built-up in cotton fiber surface, need be through soap boiling, washing to remove loose colour, and water consumption is 700-750 ton/ton fiber, then dewaters, dries.
The result table of comparisons
Embodiment 1-4 gained bulk fibre is carried out to recruitment evaluation, and test result refers to table 1.
The recruitment evaluation parameter table of comparisons of the each embodiment of table 1
Compared with comparative example's gained bulk fibre of above-described embodiment 1-3 gained bulk fibre and embodiment 4, on the bulk fibre of embodiment 1-3, dye uniformity better, the physical indexs such as work flow is short, the intensity on bulk fibre after dyeing impact is little, and water consumption is only 1/8 left and right of embodiment 4.
Claims (7)
1. one kind is applicable to the wringer of bulk fibre or the dehydration of bulk fibre cake, it is characterized in that: comprise pedestal, tubular cylinder body and top board, tubular cylinder body is arranged on pedestal, on tubular cylinder body, be provided with small opening, top board is flexibly connected with tubular cylinder body, top board top is connected with pressure assembly, and Power Component drives top board to do piston movement in tubular cylinder body, to realize, the squeezing of moisture in bulk fibre in tubular cylinder body is extruded.
2. a kind of wringer that is applicable to bulk fibre or the dehydration of bulk fibre cake as claimed in claim 1, is characterized in that: on the bottom of described tubular cylinder body and/or sidewall, be provided with small opening, the aperture of small opening is 2-3mm, percent opening 50-70%.
3. a kind of wringer that is applicable to bulk fibre or the dehydration of bulk fibre cake as claimed in claim 1, it is characterized in that: described Power Component comprises briquetting, crossbeam, power source and column, briquetting is between top board and crossbeam, crossbeam movable set is on column, power source drives crossbeam move up and down or rotatablely move along column, remove from tubular cylinder body to realize briquetting and top board, be convenient to hanging in or hanging out of bulk fibre.
4. a kind of wringer that is applicable to bulk fibre or the dehydration of bulk fibre cake as claimed in claim 3, is characterized in that: described power source is cylinder or oil cylinder.
5. a kind of wringer that is applicable to bulk fibre or the dehydration of bulk fibre cake as claimed in claim 1, is characterized in that: described tubular cylinder body below is provided with collecting tank, for collecting the moisture flowing out with emptying small opening.
6. a kind of wringer that is applicable to bulk fibre or the dehydration of bulk fibre cake as claimed in claim 5, is characterized in that: described collecting tank is provided with leakage fluid dram, and leakage fluid dram place is provided with filter screen, prevents that fiber from blocking leakage fluid dram.
7. a kind of wringer that is applicable to bulk fibre or the dehydration of bulk fibre cake as claimed in claim 1, it is characterized in that: on described tubular inboard wall of cylinder block, be provided with annular water distributor, on annular water distributor, be provided with water distributing pore, annular water distributor is connected with clear water pipe, after squeezing water, cleans tubular cylinder body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420012285.6U CN203729085U (en) | 2014-01-09 | 2014-01-09 | Wringer suitable for dehydrating loose fiber or loose fiber cakes |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420012285.6U CN203729085U (en) | 2014-01-09 | 2014-01-09 | Wringer suitable for dehydrating loose fiber or loose fiber cakes |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203729085U true CN203729085U (en) | 2014-07-23 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420012285.6U Expired - Lifetime CN203729085U (en) | 2014-01-09 | 2014-01-09 | Wringer suitable for dehydrating loose fiber or loose fiber cakes |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203729085U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105040309A (en) * | 2015-08-25 | 2015-11-11 | 绍兴国周控股集团有限公司 | Continuous loose fiber treatment device |
| CN105671833A (en) * | 2015-10-30 | 2016-06-15 | 朱忠良 | Cold-pad batch dyeing process of loose fibers |
-
2014
- 2014-01-09 CN CN201420012285.6U patent/CN203729085U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105040309A (en) * | 2015-08-25 | 2015-11-11 | 绍兴国周控股集团有限公司 | Continuous loose fiber treatment device |
| CN105671833A (en) * | 2015-10-30 | 2016-06-15 | 朱忠良 | Cold-pad batch dyeing process of loose fibers |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140723 |