CN104911848B - Viscose loose fiber continuous dyeing process and adopted viscose loose fiber continuous dyeing machine - Google Patents
Viscose loose fiber continuous dyeing process and adopted viscose loose fiber continuous dyeing machine Download PDFInfo
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- CN104911848B CN104911848B CN201510255834.1A CN201510255834A CN104911848B CN 104911848 B CN104911848 B CN 104911848B CN 201510255834 A CN201510255834 A CN 201510255834A CN 104911848 B CN104911848 B CN 104911848B
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Abstract
The invention discloses a viscose loose fiber continuous dyeing process and a viscose loose fiber continuous dyeing machine, and belongs to the technical field of spinning printing and dyeing. The processes of lapping, dye liquor spraying and dipping, dye liquor padding, hot air drying, color fixing liquor spraying and dipping, hot air drying, steaming, washing, drying, packaging and the like are carried out on viscose loose fibers, and white viscose loose fibers are dyed to colored viscose loose fibers. The viscose loose fiber continuous dyeing process can be achieved through the viscose loose fiber continuous dyeing machine. Compared with a traditional intermittent dyeing tank, dyeing time of the viscose loose fiber continuous dyeing process is greatly shortened, manpower and material resource consumption is reduced, dyeing efficiency is improved, cost is lowered, adopted dye can be recycled again, influence on environment is small, and the viscose loose fiber continuous dyeing process belongs to novel environment-friendly dyeing.
Description
Technical field
The invention belongs to textile printing and dyeing field is and in particular to a kind of viscose glue staple in bulk continuous dyeing process and viscose glue staple in bulk
Continuous dyeing machine.
Background technology
Existing viscose glue loose stock dyeing technique is mainly batch (-type) bobbin dyeing, and viscose glue staple in bulk raw material is compressed into dye fiber
Dyeed after cake, during dyeing, fiber cake is placed in pressure cone yarn dyeing machine and is dyeed.Due to being compressed into fiber cake, dyeing is not
Easily wetting fibre, so dyeing time is typically in 4-8 hour.After the completion of dyeing, repeatedly cleaned, finally drying and beat
Bag.Because this staining method is step colouring method, again through multiple operations such as dyeing, cleanings, consuming man-hour is long, effect
Rate is poorly efficient, and back work amount is big, and the waste water and waste liquid of leakage is many, pollutes environment.
Content of the invention
Goal of the invention: in order to solve the deficiencies in the prior art, the invention provides a kind of viscose glue staple in bulk continuous dyeing work
Skill and viscose glue staple in bulk continuous dyeing machine, enable viscose glue staple in bulk continuous dyeing, shorten dyeing time, reduce manpower, thing
Power consumes, and reduces back work amount, reduces discharge of wastewater, environmental protection.
Technical scheme: a kind of viscose glue staple in bulk continuous dyeing process, through following operations to viscose glue loose stock dyeing:
(1) viscose glue staple in bulk lapping, viscose glue staple in bulk is layered on stainless steel coil net conveyor, and lapping thickness is 2-5cm;
(2) dye liquor spray immersion viscose glue staple in bulk, at least through 2 dipping process, spray immersion dye liquor temperature is 60-90
DEG C, the spray immersion time is 3-15 minute;
(3) pad dyeing viscose glue staple in bulk, at least through 2 pad dyeing operations, pad dyeing operation ensures that the viscose glue that lapping is made dissipates fibre
Dimension blanket is fully contacted with dye liquor, dries viscose glue staple in bulk blanket pick-up 40-80%, for making dye liquor fully react with staple in bulk, dye
Liquid spray immersion step is with pad dyeing viscose glue staple in bulk step alternately;
(4) hot-air seasoning;
(5) fixation liquid spray immersion viscose glue staple in bulk, at least through 2 dipping process, spray immersion fixation liquid temp is
60-90 DEG C, the spray immersion time is 3-15 minute;
(6) dry viscose glue fixation staple in bulk, dry operation at least through 2 times, pad dyeing operation ensures the viscose glue that lapping is made
Staple in bulk blanket is fully contacted with dye liquor, and drying viscose glue staple in bulk blanket liquid carrying rate is 5-40%, for making fixation liquid and staple in bulk abundant
Reaction, dye liquor spray immersion step is with pad dyeing viscose glue staple in bulk step alternately;
(7) hot-air seasoning;
(8) gas of banking up steams viscose glue staple in bulk, and gas steams temperature 102-120 DEG C, and gas steams time 3-30 minute;
(9) washing, viscose glue staple in bulk of soaping, at least through 2 washing soap washings, washing soaps liquid temp for 50-90
DEG C, wash time 0.5-30 minute of soaping;
(10) hot-air seasoning;
(11) pack.
A kind of viscose glue staple in bulk continuous dyeing machine realizing viscose glue staple in bulk continuous dyeing process, including staple in bulk lapping
Machine, at least 2 dye liquor spray immersion grooves, at least 2 dyeing rolling rolls, air flow dryer one, at least 2 fixation liquid spray immersion
Groove, at least 2 fixation liquid rolling rolls, air flow dryer two, gas steams stacking box, at least 2 rinsing bowls, air flow dryer three, and dissipates
Fiber baling press, they are connected in turn.
As optimization: for promoting viscose glue staple in bulk to be fully contacted with dye liquor, dye liquor spray immersion trench bottom is equipped with suction dye
Liquid device makes dye liquor circulate, and dye liquor spray immersion groove top, equipped with dye liquor injection apparatus, is sprayed liquid and originated and roll for rolling roll
Remaining dye liquor, maceration tank suction dye liquor and fresh configuration dyeing replenisher, maceration tank conveyer belt is stainless steel coil net conveyor, for adding
Strong transmission viscose rayon blanket efficiency, stainless steel coil net conveyor one side carries perpendicular hook.
As optimization: described three air flow dryers are infrared-hot blast composite drier, conveyer belt direction of transfer and level
Face is in 30 ° of -60 ° of angles, and an opposite direction motion rustless steel cotton carding spiked roller is put by side on a moving belt, rustless steel cotton carding spiked roller with
Conveyer belt compartment distance ensures that fiber part is passed through, and partly returns continuation hot-air seasoning, and air flow dryer conveyer belt is not
Rust steel.
As optimization: for promoting viscose glue staple in bulk to be fully contacted with fixation liquid, fixation liquid spray immersion trench bottom is equipped with taking out
Inhaling fixation liquid device makes fixation liquid recycle stream move, and liquid, equipped with fixation liquid jetting device, is sprayed in fixation liquid spray immersion groove top
Originate and roll remaining fixation liquid, maceration tank suction fixation liquid and fresh configuration fixation replenisher for rolling roll, maceration tank conveyer belt is stainless
Steel ring net conveyor, for strengthening transmission viscose rayon blanket efficiency, stainless steel coil net conveyor one side carries perpendicular hook.
As optimization: described gas steam box has steam jet, an opposite direction motion cotton carding spiked roller, gas are put by side on a moving belt
Steam box conveyer belt is bamboo.
Beneficial effect: the viscose glue staple in bulk continuous dyeing process designed by the present invention and viscose glue staple in bulk continuous dyeing machine have
Following advantage:
1. shorten the viscose glue loose stock dyeing time, improve staining efficiency, reduce production cost, the viscose glue designed by the present invention
Loose stock dyeing technique is to put into viscose glue staple in bulk raw material in viscose glue staple in bulk continuous dyeing machine, and viscose glue staple in bulk sequentially passes through
Lapping, spray immersion dye liquor, dry, drying, spray immersion fixation liquid, dry, drying, gas steam, washing, dry, packing etc. work
Sequence continuous treatment, directly dyes colored viscose glue staple in bulk from raw material white viscose glue staple in bulk.In dyeing, staple in bulk is paved into 2-
5cm thick fiber blanket passes through chroma tank, and viscose glue staple in bulk sprays through dye liquor, contaminates, and rolling roll roll compacting colouring absorption, due to dye liquor
Concentration is higher, and above-mentioned three kinds of modes are processed, and viscose glue staple in bulk is easy to and dye contacts, thus contaminates fiber relatively on dyestuff
Short.Gas steam and in, viscose glue dye fiber be easier to contact intensification with vapourss, thus the fixation time shorten dramatically it is thus only necessary to
A few minutes to more than ten minutes, compared with conventional cartridge yarn-dyed staple in bulk cake, save substantial amounts of dyeing time.Due to the method for the present invention
Be seriality dyeing it is not necessary to the substantial amounts of back work of inter process, thus save artificial, reduce the consumption of water power equal energy source,
Reduce production cost.
2. viscose glue staple in bulk continuous dyeing machine maceration tank, the dye liquor in pad dyeing groove, fixation liquid all with suction circulating device,
In each groove, liquid all does to viscose rayon blanket after supplementing new liq and sprays, after the washings in rinsing bowl are used for multiple times, through dye
Discharge after the whole process with sewage apparatus, thus the discharge of waste liquid, waste water is all up to standard, environmental protection.
3. low cost, yield is high.Compared with viscose glue staple in bulk continuous dyeing process soaks cylinder dye with tradition, dyeing time is to pass
The 1/15 of system, and between each operation, do not need auxiliary operation, cost substantially reduces.
Brief description
Fig. 1 is a kind of structural representation of viscose glue staple in bulk continuous dyeing machine transmission system;
Fig. 2 is spray immersion slot structure schematic diagram;
Fig. 3 is air flow dryer structural representation.
Specific embodiment
With reference to specific embodiment, the invention will be further described.
A kind of viscose glue staple in bulk continuous dyeing machine realizing viscose glue staple in bulk continuous dyeing process, including staple in bulk lapping
Machine, at least 2 dye liquor spray immersion grooves, at least 2 dyeing rolling rolls, air flow dryer, at least 2 fixation liquid spray immersion grooves,
At least 2 fixation liquid rolling rolls, air flow dryer, gas steaming stacking box, at least 2 rinsing bowls, dehydrator, and staple in bulk baling press,
They are connected in turn.
For promoting viscose glue staple in bulk to be fully contacted with dye liquor, dye liquor spray immersion trench bottom makes equipped with suction dye liquor device
Dye liquor circulates, and dye liquor spray immersion groove top, equipped with dye liquor injection apparatus, is sprayed liquid and originated and roll remaining dye liquor, dipping for rolling roll
Groove suction dye liquor and fresh configuration dyeing replenisher.Maceration tank conveyer belt is stainless steel coil net conveyor, for strengthening transmission viscose glue
Tapetum fibrosum efficiency, stainless steel coil net conveyor one side carries perpendicular hook.
Described air flow dryer is infrared-hot blast composite drier, and conveyer belt direction of transfer presss from both sides horizontal by 30 ° -60 °
Angle, just puts an opposite direction motion rustless steel cotton carding spiked roller, rustless steel cotton carding spiked roller and conveyer belt spacer portion on a moving belt
Divide distance to ensure that fiber part is passed through, partly return continuation hot-air seasoning, air flow dryer conveyer belt is bamboo.
For promoting viscose glue staple in bulk to be fully contacted with fixation liquid, fixation liquid spray immersion trench bottom is equipped with suction fixation liquid dress
Put so that fixation liquid recycle stream moves, fixation liquid spray immersion groove top, equipped with fixation liquid jetting device, is sprayed liquid and originated as rolling roll
Roll remaining fixation liquid, maceration tank suction fixation liquid and fresh configuration fixation replenisher.Maceration tank conveyer belt transmits for rustless steel hoop net
Band, for strengthening transmission viscose rayon blanket efficiency, stainless steel coil net conveyor one side carries perpendicular hook.
Described gas steam box has steam jet, and an opposite direction motion cotton carding spiked roller is put by side on a moving belt, and gas steam box transmits
Carry as bamboo.
Embodiment 1
It is as follows that a kind of viscose glue staple in bulk carries out reactive dyeing process:
(1) viscose glue staple in bulk lapping, viscose glue staple in bulk is layered on stainless steel coil net conveyor, and lapping thickness is 2cm.
(2) dye liquor spray immersion viscose glue staple in bulk, injection, impregnation liquid are reactive dye 40g/l, penetrating agent 4g/l, Sal
200g/l, pads dye liquor (pick-up 80%), and through 2 dipping process, spray immersion dye liquor temperature is 60 DEG C, during spray immersion
Between be 3 minutes.
(3) 110 DEG C of hot-air seasonings, hot-air seasoning conveyer belt keeps 60 ° with level angle, in top setting one opposite direction fortune
Short for portion adhesive fibre is back and forth returned baking oven bottom it is ensured that fiber part is passed through by dynamic rustless steel cotton carding spiked roller, partly returns and continues
Continuous hot-air seasoning, improves baking oven dry efficiency.
(4) fixation liquid spray immersion viscose glue staple in bulk, injection, impregnation liquid are soda 20g/l, and Caustic soda 6g/l pads dye liquor
(pick-up 80%), through 2 dipping process, spray immersion fixation liquid temp is 60 DEG C, and the spray immersion time is 3 minutes.
(5) (3) 110 DEG C of hot-air seasonings, hot-air seasoning conveyer belt keeps 60 ° with level angle, arranges a negative side on top
To motion rustless steel cotton carding spiked roller, short for portion adhesive fibre is back and forth returned baking oven bottom, improve baking oven dry efficiency.
(6) gas of banking up steams viscose glue staple in bulk, and saturated air steams 120 DEG C, and gas steams 10 minutes time, and it is bamboo that gas steams conveyer belt.
(7) fiber enter water become tapetum fibrosum washed (room temperature, 30s) → neutralization (acetic acid 1m l/l, 30s) → hot water wash
(80 DEG C × 30s) → soap boiling (detergent 1g/l, 90 DEG C × 60s) → hot water wash (80 DEG C × 60s) → washing (room temperature × 30s)
(8) 110 DEG C of hot-air seasonings, hot-air seasoning conveyer belt keeps 60 ° with level angle, in top setting one opposite direction fortune
Short for portion adhesive fibre is back and forth returned baking oven bottom by dynamic rustless steel cotton carding spiked roller, improves baking oven dry efficiency.
(9) pack.
Embodiment 2
Reactive dyeing process is carried out to a kind of viscose glue staple in bulk as follows:
(1) viscose glue staple in bulk lapping, viscose glue staple in bulk is layered on stainless steel coil net conveyor, and lapping thickness is 5cm.
(2) dye liquor spray immersion viscose glue staple in bulk, injection, impregnation liquid are reactive dye 40g/l, penetrating agent 4g/l, Sal
200g/l, pads dye liquor (pick-up 80%), and through 1 dipping process, spray immersion dye liquor temperature is 90 DEG C, during spray immersion
Between be 15 minutes.
(3) 110 DEG C of hot-air seasonings, hot-air seasoning conveyer belt keeps 60 ° with level angle, in top setting one opposite direction fortune
Short for portion adhesive fibre is back and forth returned baking oven bottom by dynamic rustless steel cotton carding spiked roller, improves baking oven dry efficiency.
(4) fixation liquid spray immersion viscose glue staple in bulk, injection, impregnation liquid are soda 20g/l, and Caustic soda 6g/l pads dye liquor
(pick-up 80%), through 1 dipping process, spray immersion fixation liquid temp is 90 DEG C, and the spray immersion time is 15 minutes.
(5) 110 DEG C of hot-air seasonings, hot-air seasoning conveyer belt keeps 60 ° with level angle, in top setting one opposite direction fortune
Short for portion adhesive fibre is back and forth returned baking oven bottom by dynamic rustless steel cotton carding spiked roller, improves baking oven dry efficiency.
(6) gas of banking up steams viscose glue staple in bulk, and saturated air steams 120 DEG C, and gas steams 10 minutes time, and it is bamboo that gas steams conveyer belt.
(7) fiber enter water become tapetum fibrosum washed (room temperature, 30s) → neutralization (acetic acid 1ml/l, 30s) → hot water wash (80
DEG C × 30s) → soap boiling (detergent 1g/l, 90 DEG C × 60s) → hot water wash (80 DEG C × 60s) → washing (room temperature × 30s)
(8) 110 DEG C of hot-air seasonings, hot-air seasoning conveyer belt keeps 60 ° with level angle, in top setting one opposite direction fortune
Short for portion adhesive fibre is back and forth returned baking oven bottom by dynamic rustless steel cotton carding spiked roller, improves baking oven dry efficiency.
(9) pack.
Embodiment 3
Described in the present embodiment, viscose glue continuous dyeing machine removes spray immersion groove and supporting drying plant on the basis of Fig. 1,
Direct dyeing technique is carried out to a kind of viscose glue staple in bulk as follows:
(1) viscose glue staple in bulk lapping, viscose glue staple in bulk is layered on stainless steel coil net conveyor, and lapping thickness is 3cm.
(2) dye liquor spray immersion viscose glue staple in bulk, injection, impregnation liquid are direct dyess 40g/l, penetrating agent 4g/l, Sal
200g/l, pads dye liquor (pick-up 80%), and through 1 dipping process, spray immersion dye liquor temperature is 80 DEG C, during spray immersion
Between be 10 minutes.
(3) 110 DEG C of hot-air seasonings, hot-air seasoning conveyer belt keeps 60 ° with level angle, in top setting one opposite direction fortune
Short for portion adhesive fibre is back and forth returned baking oven bottom by dynamic rustless steel cotton carding spiked roller, improves baking oven dry efficiency.
(4) gas of banking up steams viscose glue staple in bulk, and saturated air steams 120 DEG C, and gas steams 10 minutes time, and it is bamboo that gas steams conveyer belt.
(5) hot water wash (80 DEG C × 30s) → soap boiling (detergent 1g/l, 90 DEG C × 60s) → hot water wash (80 DEG C × 60s) →
Washing (room temperature × 30s)
(6) 110 DEG C of hot-air seasonings, hot-air seasoning conveyer belt keeps 60 ° with level angle, in top setting one opposite direction fortune
Short for portion adhesive fibre is back and forth returned baking oven bottom by dynamic rustless steel cotton carding spiked roller, improves baking oven dry efficiency.
(7) pack.
Embodiment 4
Described in the present embodiment, viscose glue continuous dyeing machine removes spray immersion groove and supporting drying plant on the basis of Fig. 1,
Direct dyeing technique is carried out to a kind of viscose glue staple in bulk as follows:
(1) viscose glue staple in bulk lapping, viscose glue staple in bulk is layered on stainless steel coil net conveyor, and lapping thickness is 4cm.
(2) dye liquor spray immersion viscose glue staple in bulk, injection, impregnation liquid are direct dyess 40g/l, penetrating agent 4g/l, Sal
200g/l, pads dye liquor (pick-up 80%), and through 1 dipping process, spray immersion dye liquor temperature is 75 DEG C, during spray immersion
Between be 12 minutes.
(3) 110 DEG C of hot-air seasonings, hot-air seasoning conveyer belt keeps 60 ° with level angle, in top setting one opposite direction fortune
Short for portion adhesive fibre is back and forth returned baking oven bottom by dynamic rustless steel cotton carding spiked roller, improves baking oven dry efficiency.
(4) gas of banking up steams viscose glue staple in bulk, and saturated air steams 120 DEG C, and gas steams 10 minutes time, and it is bamboo that gas steams conveyer belt.
(5) hot water wash (80 DEG C × 30s) → soap boiling (detergent 1g/l, 90 DEG C × 60s) → hot water wash (80 DEG C × 60s) →
Washing (room temperature × 30s)
(6) 110 DEG C of hot-air seasonings, hot-air seasoning conveyer belt keeps 60 ° with level angle, in top setting one opposite direction fortune
Short for portion adhesive fibre is back and forth returned baking oven bottom by dynamic rustless steel cotton carding spiked roller, improves baking oven dry efficiency.
(7) pack.
The present invention is not limited to above-mentioned preferred forms, and anyone can show that under the enlightenment of the present invention other are various
The product of form, however, making any change in its shape or structure, every have skill identical or similar to the present application
Art scheme, is within the scope of the present invention.
Claims (3)
1. a kind of viscose glue staple in bulk continuous dyeing machine realizing viscose glue staple in bulk continuous dyeing process it is characterised in that: include dissipate
Fiber lapping machine, at least 2 dye liquor spray immersion grooves, at least 2 dyeing rolls, air flow dryer one, at least 2 fixation liquid sprays
Penetrate maceration tank, at least 2 fixation liquid rolls, air flow dryer two, decatize stacking box, at least 2 rinsing bowls, air flow dryer
Three, staple in bulk baling press, they are connected in turn;
Described three air flow dryers are infrared-hot blast composite drier, and conveyer belt direction of transfer presss from both sides horizontal by 30 ° -60 °
Angle, just puts an opposite direction motion rustless steel cotton carding spiked roller, rustless steel cotton carding spiked roller and conveyer belt spacer portion on a moving belt
Divide distance to ensure that fiber part is passed through, partly return continuation hot-air seasoning, air flow dryer conveyer belt is stainless steel;
For promoting viscose glue staple in bulk to be fully contacted with fixation liquid, fixation liquid spray immersion trench bottom makes equipped with suction fixation liquid device
Fixation liquid recycle stream moves, fixation liquid spray immersion groove top equipped with fixation liquid jetting device, spray liquid originate roll for roll remaining
Fixation liquid, maceration tank suction fixation liquid and fresh configuration fixation replenisher, maceration tank conveyer belt is stainless steel coil net conveyor, is
Strengthen transmission viscose rayon blanket efficiency, stainless steel coil net conveyor one side carries perpendicular hook;
Described steaming box has steam jet, and an opposite direction motion cotton carding spiked roller is put by side on a moving belt, and steaming box conveyer belt is
Bamboo.
2. the viscose glue staple in bulk continuous dyeing machine realizing viscose glue staple in bulk continuous dyeing process according to claim 1, its
It is characterised by: for promoting viscose glue staple in bulk to be fully contacted with dye liquor, dye liquor spray immersion trench bottom makes equipped with suction dye liquor device
Obtain dye liquor to circulate, dye liquor spray immersion groove top, equipped with dye liquor injection apparatus, is sprayed liquid and originated and roll remaining dye liquor, leaching for roll
Stain groove suction dye liquor and fresh configuration dyeing replenisher, maceration tank conveyer belt is stainless steel coil net conveyor, viscous for strengthening transmission
Glue fiber blanket efficiency, stainless steel coil net conveyor one side carries perpendicular hook.
3. the viscose glue staple in bulk continuous dyeing machine realizing viscose glue staple in bulk continuous dyeing process according to claim 1, its
It is characterised by: through following operations to viscose glue loose stock dyeing:
(1) viscose glue staple in bulk lapping, viscose glue staple in bulk is layered on stainless steel coil net conveyor, and lapping thickness is 2-5cm;
(2) dye liquor spray immersion viscose glue staple in bulk, at least through 2 dipping process, spray immersion dye liquor temperature is 60-90 DEG C,
The spray immersion time is 3-15 minute;
(3) pad dyeing viscose glue staple in bulk, at least through 2 pad dyeing operations, pad dyeing operation ensures the viscose glue staple in bulk blanket that lapping is made
It is fully contacted with dye liquor, dries viscose glue staple in bulk blanket pick-up 40-80%, for making dye liquor fully react with staple in bulk, dye liquor sprays
Penetrate impregnation steps with pad dyeing viscose glue staple in bulk step alternately;
(4) hot-air seasoning;
(5) fixation liquid spray immersion viscose glue staple in bulk, at least through 2 dipping process, spray immersion fixation liquid temp is 60-90
DEG C, the spray immersion time is 3-15 minute;
(6) dry viscose glue fixation staple in bulk, dry operation at least through 2 times, pad dyeing operation ensures that the viscose glue that lapping is made dissipates fibre
Dimension blanket is fully contacted with dye liquor, and drying viscose glue staple in bulk blanket liquid carrying rate is 5-40%, for making fixation liquid and staple in bulk fully react,
Dye liquor spray immersion step is with pad dyeing viscose glue staple in bulk step alternately;
(7) hot-air seasoning;
(8) decatize of banking up viscose glue staple in bulk, 102-120 DEG C of steam temperature, steaming time 3-30 minute;
(9) washing, viscose glue staple in bulk of soaping, at least through 2 washing soap washings, washing soaps liquid temp for 50-90 DEG C, water
Wash time 0.5-30 minute of soaping;
(10) hot-air seasoning;
(11) pack.
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Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108547096A (en) * | 2018-06-20 | 2018-09-18 | 绍兴国周针织科技有限公司 | A kind of cold batching process |
CN109162120A (en) * | 2018-07-24 | 2019-01-08 | 恒天海龙(潍坊)新材料有限责任公司 | A kind of high-quality colored regenerated cellulose fiber and preparation method thereof |
CN109736034B (en) * | 2018-12-30 | 2021-09-10 | 山东黄河三角洲纺织科技研究院有限公司 | Dyeing device and dyeing method for cotton fibers |
CN110565386A (en) * | 2019-10-09 | 2019-12-13 | 福建七匹狼实业股份有限公司 | Preparation method of ultraviolet-resistant fabric and ultraviolet-resistant fabric |
CN111575940A (en) * | 2020-05-27 | 2020-08-25 | 山东黄河三角洲纺织科技研究院有限公司 | Continuous dyeing method for fiber web |
CN111575950A (en) * | 2020-06-12 | 2020-08-25 | 苏州中纺学面料产业研究院 | Dyeing equipment for loose fiber open-width continuous dyeing process |
CN112267318B (en) * | 2020-10-31 | 2022-12-16 | 山东高棉智能纤染科技有限公司 | Loose fiber dyeing process and matched dyeing treatment system |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101446048A (en) * | 2008-12-30 | 2009-06-03 | 上虞新晟化工工业有限公司 | Continuous pad dyeing method of polyamide fibers and blended fabrics thereof |
CN102191642A (en) * | 2010-03-01 | 2011-09-21 | 温国俊 | Reactive dye pad dyeing and steaming process |
CN103774368A (en) * | 2014-01-09 | 2014-05-07 | 绍兴国周针织科技有限公司 | Continuous type colored loose fiber machining device |
CN103774361A (en) * | 2014-01-09 | 2014-05-07 | 绍兴金渔纺织新技术有限公司 | Spray-rolling type loose fiber cold-batch dyeing process |
CN103882637A (en) * | 2014-03-19 | 2014-06-25 | 绍兴国周纺织新材料有限公司 | Loose stock dyeing device |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007009353A (en) * | 2005-06-29 | 2007-01-18 | Horie Senko Kk | Method and apparatus for continuous dyeing and finishing |
-
2015
- 2015-05-19 CN CN201510255834.1A patent/CN104911848B/en active Active
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101446048A (en) * | 2008-12-30 | 2009-06-03 | 上虞新晟化工工业有限公司 | Continuous pad dyeing method of polyamide fibers and blended fabrics thereof |
CN102191642A (en) * | 2010-03-01 | 2011-09-21 | 温国俊 | Reactive dye pad dyeing and steaming process |
CN103774368A (en) * | 2014-01-09 | 2014-05-07 | 绍兴国周针织科技有限公司 | Continuous type colored loose fiber machining device |
CN103774361A (en) * | 2014-01-09 | 2014-05-07 | 绍兴金渔纺织新技术有限公司 | Spray-rolling type loose fiber cold-batch dyeing process |
CN103882637A (en) * | 2014-03-19 | 2014-06-25 | 绍兴国周纺织新材料有限公司 | Loose stock dyeing device |
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