CN102978963A - Camouflage tent cloth coating technology - Google Patents
Camouflage tent cloth coating technology Download PDFInfo
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- CN102978963A CN102978963A CN2012104350397A CN201210435039A CN102978963A CN 102978963 A CN102978963 A CN 102978963A CN 2012104350397 A CN2012104350397 A CN 2012104350397A CN 201210435039 A CN201210435039 A CN 201210435039A CN 102978963 A CN102978963 A CN 102978963A
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Abstract
The invention provides a camouflage tent cloth coating technology. The technology comprises the following steps: 1, priming a fabric base cloth by PA glue; 2, carrying out PVC whitening of the primed fabric base cloth by a PVC coat; and 3, carrying out PU silver surface coating of the PVC-whitened fabric base cloth by a PU silver paste. The technology enables the fabric base cloth fabric to have a high light color fastness function, a high hydrostatic pressure resistance function and a high water repellency, and has the advantages of reasonableness and low economic cost.
Description
Technical field
The present invention relates to field of textiles, be specifically related to a kind of coating process of camouflage color tent cloth.
Background technology
In existing outdoor coatings textiles and the military outdoor textiles, especially pretend tent and camouflage clothes as combatant's clothes, not only need to have preferably camouflage painting function, also should possess resistance to light and the high hydraulic pressure function of wearing comfort, excellence.But the coloured material of present camouflage painting mainly is coating, and pigment dyeing generally is used for the camouflage of fixed target, but there is the not good problem of feel, crock fastness in it, and comfortableness is poor; In addition, in the process that existing camouflage fabric is parked in the open, direct irradiation of sunlight is to fabric, because humidity can change between 0 ~ 100%, and light (especially ultraviolet light), heat, the comprehensive function of wetting, the dyestuff on the fabric can be destroyed faster, cause fabric fading fast, simultaneously also can destroy fabric itself, cause powerful decline, thereby have influence on Practical Performance and the hydraulic pressure performance of fabric.And the textiles that generally is used for direct coating all forms by warp and weft interweaving, the out-of-flatness of the fabric face utmost point, and directly coating certainly will cause coated film that light is formed diffuse reflection.Existing technique is that fabric is carried out first satinage, warp and weft interweaving point is offseted as far as possible, and then coating, and the method can not fundamentally solve the not high problem of coat side brightness, and fabric rolls more flatly, and the peel strength of its coated film and fabric is poorer.
Summary of the invention
Technical problem to be solved by this invention is to provide a kind of coating process of camouflage color tent cloth, make fabric base cloth fabric not only have high color fastness to light function, high hydrostatic pressure resistance function, but also have the effect of higher water-sprinkling degree, and technique is reasonable, and financial cost is low.
For solving above-mentioned existing technical problem, the present invention adopts following scheme: a kind of coating process of camouflage color tent cloth may further comprise the steps: the first step, employing PA glue carry out bottoming to the fabric base cloth; Second step, the PVC that carries out that starches fabric base cloth after the bottoming with the PVC coating whitewash; The 3rd step, the fabric base cloth after with PU silver slurry PVC being whitewashed carry out the silver-colored finishing coat of PU.
As preferably, described PA glue comprises PA coating adhesive, crosslinking agent, solvent, and the weight ratio of PA coating adhesive, crosslinking agent, solvent is 80 ~ 100:1 ~ 2:4 ~ 8.
As preferably, the weight ratio of described PA coating adhesive, crosslinking agent, solvent is 80:2:5.
As preferably, described crosslinking agent is polyisocyanates, and described solvent is ethyl acetate.
As preferably, the preparation process of described PA glue is: solvent is joined in the crosslinking agent mix well, then join in the coating adhesive and stir, add toluene adjusting viscosity to 8000 ~ 10000mPaS in the time of stirring, leave standstill 30min after stirring evenly.
As preferably, viscosity is adjusted to 9000mPaS.
As preferably, the technological parameter in the described first step during with the bottoming of PA glue is: select the acute angle scraper, adjusting scraper angle is 115 ~ 125 degree, the magnetic force of regulating magnetic roller is 90 ~ 100%, control baking oven proparea temperature is 70 ~ 80 ℃, 110 ~ 120 ℃ of back zone temperature, criteria thus the drying time 30 ~ 35s.
As preferably, the technological parameter in the described first step during with the bottoming of PA glue is: select the acute angle scraper, adjusting scraper angle is 120 degree, and the magnetic force of regulating magnetic roller is 95%, and control baking oven proparea temperature is 75 ℃, 115 ℃ of back zone temperature, criteria thus the drying time 30s.
As preferably, described PVC coating slurry comprises polyvinyl chloride resin, plasticizer, heat stabilizer, and the weight ratio of polyvinyl chloride resin, plasticizer, heat stabilizer is 100:100:0.5 ~ 4, and described PVC coating slurry also comprises whiting.
As preferably, described plasticizer comprises DOP, DBP, and the weight ratio of DOP, DBP is 1:1, and described heat stabilizer is stearate, and described stearate comprises that the weight ratio of zinc stearate, barium stearate, calcium stearate and zinc stearate, barium stearate, calcium stearate is 0.5:1:1.2.
As preferably, the weight ratio of described polyvinyl chloride resin, DOP, DBP, stearate is 100:50:50:0.5.
As preferably, the preparation process of described PVC coating slurry is: add first a part of plasticizer in stearate and whiting, stir evenly, then pour in the mixer with polyvinyl chloride resin, add again remaining plasticizer, stir evenly and grind 1 ~ 2 time with three-roll grinder afterwards, the batching with milled stirs 5 ~ 10min more at last, leaves standstill 30min or vacuumize to carry out deaeration and process.
As preferably, the preparation process of described PVC coating slurry is: the plasticizer that adds first 1/5 part in stearate and whiting, stir evenly, then pour in the mixer with polyvinyl chloride resin, add again remaining plasticizer, stir evenly and grind 2 times with three-roll grinder afterwards, the batching with milled stirs 10min more at last, leaves standstill 30min or vacuumize to carry out deaeration and process.
As preferably, the technological parameter that PVC whitewashes in the described second step is: select the acute angle scraper, adjust scraper angle 115 ~ 125 degree, regulate magnetic roller magnetic force 90 ~ 100%, 170 ~ 190 ℃ of control oven temperatures, fusion time 2 ~ 3min, the clot after the cold water roller cooling of the fabric base cloth after PVC whitewashes.
As preferably, the technological parameter that PVC whitewashes in the described second step is: select the acute angle scraper, adjust scraper angle 120 degree, regulate magnetic roller magnetic force 95%, 180 ℃ of control oven temperatures, fusion time 0.5min, the clot after the cold water roller cooling of the fabric base cloth after PVC whitewashes.
As preferably, described PU silver slurry comprises mono-component polyurethane, aluminum paste, MEK, dimethyl formamide, and the weight ratio of described mono-component polyurethane, aluminum paste, MEK, dimethyl formamide is 50:10:25 ~ 30:5 ~ 10.
As preferably, the weight ratio of described mono-component polyurethane, aluminum paste, MEK, dimethyl formamide is 50:10:25:10.
As preferably, described aluminum paste is 320 order aluminum pastes.
As preferably, the preparation process of described PU silver slurry is: first a part of solvent is joined in the aluminum paste, add polyurethane adhesive after stirring evenly again, add while stirring remaining solvent, adjust viscosity 5000 ~ 6000mPaS, leave standstill 30min or vacuumizing and defoaming.
As preferably, adjustment viscosity is 6000mPaS.
As preferably, the technological parameter that carries out PU silver finishing coat in described the 3rd step is: select the acute angle scraper, adjust scraper angle 110 ~ 125 degree, regulate magnetic roller magnetic force 75 ~ 85%, 125 ~ 135 ℃ of control proparea oven temperatures, 145 ~ 155 ℃ of back zone temperature, drying time 30 ~ 40s.
As preferably, the technological parameter that carries out PU silver finishing coat in described the 3rd step is: select the acute angle scraper, adjust scraper angle 110 degree, regulate magnetic roller magnetic force 80%, 135 ℃ of control proparea oven temperatures, 150 ℃ of back zone temperature, drying time 35s.
As preferably, described fabric base cloth is the terylene OXFORD, and terylene OXFORD specification is 600 * 600D.
Beneficial effect:
The present invention adopts the coating process of a kind of camouflage color tent cloth that technique scheme provides, and makes fabric panel not only have high color fastness to light function, high hydrostatic pressure resistance function, but also has the effect of higher water-sprinkling degree, and technique is reasonable, and financial cost is low.
The specific embodiment
Embodiment one:
A kind of coating process of camouflage color tent cloth may further comprise the steps: the first step, employing PA glue carry out bottoming to the fabric base cloth; Second step, the PVC that carries out that starches fabric base cloth after the bottoming with the PVC coating whitewash; The 3rd step, the fabric base cloth after with PU silver slurry PVC being whitewashed carry out the silver-colored finishing coat of PU.Described PA glue comprises PA coating adhesive, crosslinking agent, solvent, and the weight ratio of PA coating adhesive, crosslinking agent, solvent is 80 ~ 100:1 ~ 2:4 ~ 8.The weight ratio of described PA coating adhesive, crosslinking agent, solvent is 80:2:5.Described crosslinking agent is polyisocyanates, and described solvent is ethyl acetate.The preparation process of described PA glue is: solvent is joined in the crosslinking agent mix well, then join in the coating adhesive and stir, add toluene adjusting viscosity to 8000 ~ 10000mPaS in the time of stirring, leave standstill 30min after stirring evenly.Viscosity is adjusted to 9000mPaS.Technological parameter in the described first step during with the bottoming of PA glue is: select the acute angle scraper, adjusting scraper angle is 115 ~ 125 degree, and the magnetic force of regulating magnetic roller is 90 ~ 100%, and control baking oven proparea temperature is 70 ~ 80 ℃, 110 ~ 120 ℃ of back zone temperature, criteria thus the drying time 30 ~ 35s.Technological parameter in the described first step during with the bottoming of PA glue is: select the acute angle scraper, adjusting scraper angle is 120 degree, and the magnetic force of regulating magnetic roller is 95%, and control baking oven proparea temperature is 75 ℃, 115 ℃ of back zone temperature, criteria thus the drying time 30s.Described PVC coating slurry comprises polyvinyl chloride resin, plasticizer, heat stabilizer, and the weight ratio of polyvinyl chloride resin, plasticizer, heat stabilizer is 100:100:0.5 ~ 4, and described PVC coating slurry also comprises whiting.The weight ratio of described polyvinyl chloride resin, DOP, DBP, stearate is 100:50:50:0.5.Described plasticizer comprises DOP, DBP, and the weight ratio of DOP, DBP is 1:1, described heat stabilizer is stearate, and described stearate comprises that the weight ratio of zinc stearate, barium stearate, calcium stearate and zinc stearate, barium stearate, calcium stearate is 0.5:1:1.2.The preparation process of described PVC coating slurry is: add first a part of plasticizer in stearate and whiting, stir evenly, then pour in the mixer with polyvinyl chloride resin, add again remaining plasticizer, stir evenly rear with three-roll grinder grinding 1 ~ 2 time, batching with milled stirs 5 ~ 10min more at last, leaves standstill 30min or vacuumize to carry out the deaeration processing.The preparation process of described PVC coating slurry is: the plasticizer that adds first 1/5 part in stearate and whiting, stir evenly, then pour in the mixer with polyvinyl chloride resin, add again remaining plasticizer, stir evenly rear with three-roll grinder grinding 2 times, batching with milled stirs 10min more at last, leaves standstill 30min or vacuumize to carry out the deaeration processing.The technological parameter that PVC whitewashes in the described second step is: select the acute angle scraper, adjust scraper angle 115 ~ 125 degree, regulate magnetic roller magnetic force 90 ~ 100%, 170 ~ 190 ℃ of control oven temperatures, fusion time 2 ~ 3min, the clot after the cold water roller cooling of the fabric base cloth after PVC whitewashes.The technological parameter that PVC whitewashes in the described second step is: select the acute angle scraper, adjust scraper angle 120 degree, regulate magnetic roller magnetic force 95%, 180 ℃ of control oven temperatures, fusion time 0.5min, the clot after the cold water roller cooling of the fabric base cloth after PVC whitewashes.Described PU silver slurry comprises mono-component polyurethane, aluminum paste, MEK, dimethyl formamide, and the weight ratio of described mono-component polyurethane, aluminum paste, MEK, dimethyl formamide is 50:10:25 ~ 30:5 ~ 10.The weight ratio of described mono-component polyurethane, aluminum paste, MEK, dimethyl formamide is 50:10:25:10.Described aluminum paste is 320 order aluminum pastes.The preparation process of described PU silver slurry is: first a part of solvent is joined in the aluminum paste, add polyurethane adhesive after stirring evenly again, add while stirring remaining solvent, adjust viscosity 5000 ~ 6000mPaS, leave standstill 30min or vacuumizing and defoaming.Adjustment viscosity is 6000mPaS.The technological parameter that carries out PU silver finishing coat in described the 3rd step is: select the acute angle scraper, adjust scraper angle 110 ~ 125 degree, regulate magnetic roller magnetic force 75 ~ 85%, 125 ~ 135 ℃ of control proparea oven temperatures, 145 ~ 155 ℃ of back zone temperature, drying time 30 ~ 40s.The technological parameter that carries out PU silver finishing coat in described the 3rd step is: select the acute angle scraper, adjust scraper angle 110 degree, regulate magnetic roller magnetic force 80%, 135 ℃ of control proparea oven temperatures, 150 ℃ of back zone temperature, drying time 35s.Described fabric base cloth is the terylene OXFORD, and terylene OXFORD specification is 600 * 600D.
The terylene OXFORD that makes by the present invention has preferably high hydrostatic pressure resistance function, quality is strong, wear-resisting, closely abundant, has good waterproofing function, marching tent, rainwater-proof tarpaulin, top fabric, train tarpaulin etc. can be used to do, the industries such as electric power, oil field, railway, reinforcing bar, harbour, papermaking can be widely used in.Among the present invention, PA glue is polyamide-based resin glue, adds polyisocyanate crosslinker in the PA glue, to increase its reactivity worth.Aluminum paste can be divided into the different cultivars such as 250 orders, 320 orders by granularity, and the present invention selects 320 orders, is the aluminum paste of flat, and the reflective that its outward appearance is flat is strong, and it is good to be granular coating uniformity; The covering power that the order number is low is good, and gloss is strong.Plasticizer can be dibutyl phthalate (DOP), dioctyl phthalate (DBP) etc.PA glue and PU silver slurry add solvent, such as toluene, ethyl acetate, butanone and dimethyl formamide etc., the viscosity that can regulate coating agent.The general textiles that is used for direct coating is all formed by warp and weft interweaving, the out-of-flatness of the fabric face utmost point, and directly coating certainly will cause coated film that light is formed diffuse reflection.The present invention carries out silver slurry coating after with polyvinyl chloride resin fabric being carried out " filling and leading up " processing again, can effectively address the above problem, and with the bottoming of PA coating, can prevent PVC coating slurry seepage before the PVC coating, affects fabric appearance.In addition, to light fabric, for preventing silver color to the impact of cloth cover color, can in PVC coating slurry, add the special-purpose whiting of an amount of plastics.The performance indications of the 600D OXFORD fabric of the employing present embodiment preparation that records through experiment are as follows: 4.5 grades of 6 grades of color fastness to light ﹥, water-fastness COLOR FASTNESS ﹥, resistance to hydrostatic pressure ﹥ 2000mmH2O, refused water grade ﹥ 90 minutes.Wherein water-fastness COLOR FASTNESS is tested according to the standard testing of GB/T4744-1997 hydrostatic pressing according to GB/T8427 COLOR FASTNESS testing standard, resistance to hydrostatic pressure according to GB/T3921.3-1997 standard testing, color fastness to light; Spray rating is according to the GB/T4745-1997 standard testing.
Embodiment two:
Be with the difference of embodiment one: described PA glue comprises PA coating adhesive, crosslinking agent, solvent, and the weight ratio of PA coating adhesive, crosslinking agent, solvent is 100:2:8.Technological parameter in the described first step during with the bottoming of PA glue is: select the acute angle scraper, adjusting scraper angle is 125 degree, and the magnetic force of regulating magnetic roller is 100%, and control baking oven proparea temperature is 80 ℃, 120 ℃ of back zone temperature, criteria thus the drying time 35s.Described PVC coating slurry comprises polyvinyl chloride resin, plasticizer, heat stabilizer, and the weight ratio of polyvinyl chloride resin, plasticizer, heat stabilizer is 100:100:4.The preparation process of described PVC coating slurry is: add first a part of plasticizer in stearate and whiting, stir evenly, then pour in the mixer with polyvinyl chloride resin, add again remaining plasticizer, stir evenly rear with three-roll grinder grinding 1 time, batching with milled stirs 10min more at last, leaves standstill 30min or vacuumize to carry out the deaeration processing.The technological parameter that PVC whitewashes in the described second step is: select the acute angle scraper, adjust scraper angle 125 degree, regulate magnetic roller magnetic force 100%, 190 ℃ of control oven temperatures, fusion time 3min, the clot after the cold water roller cooling of the fabric base cloth after PVC whitewashes.Described PU silver slurry comprises mono-component polyurethane, aluminum paste, MEK, dimethyl formamide, and the weight ratio of described mono-component polyurethane, aluminum paste, MEK, dimethyl formamide is 50:10:30:10.The technological parameter that carries out PU silver finishing coat in described the 3rd step is: select the acute angle scraper, adjust scraper angle 125 degree, regulate magnetic roller magnetic force 85%, 135 ℃ of control proparea oven temperatures, 155 ℃ of back zone temperature, drying time 40s.
Embodiment three:
Be with the difference of embodiment one: described PA glue comprises PA coating adhesive, crosslinking agent, solvent, and the weight ratio of PA coating adhesive, crosslinking agent, solvent is 80:1:4.Technological parameter in the described first step during with the bottoming of PA glue is: select the acute angle scraper, adjusting scraper angle is 115 degree, and the magnetic force of regulating magnetic roller is 90%, and control baking oven proparea temperature is 70 ℃, 110 ℃ of back zone temperature, criteria thus the drying time 30s.Described PVC coating slurry comprises polyvinyl chloride resin, plasticizer, heat stabilizer, and the weight ratio of polyvinyl chloride resin, plasticizer, heat stabilizer is 100:100:0.5.The preparation process of described PVC coating slurry is: add first a part of plasticizer in stearate and whiting, stir evenly, then pour in the mixer with polyvinyl chloride resin, add again remaining plasticizer, stir evenly rear with three-roll grinder grinding 1 time, batching with milled stirs 5min more at last, leaves standstill 30min or vacuumize to carry out the deaeration processing.The technological parameter that PVC whitewashes in the described second step is: select the acute angle scraper, adjust scraper angle 115 degree, regulate magnetic roller magnetic force 90%, 170 ℃ of control oven temperatures, fusion time 2min, the clot after the cold water roller cooling of the fabric base cloth after PVC whitewashes.Described PU silver slurry comprises mono-component polyurethane, aluminum paste, MEK, dimethyl formamide, and the weight ratio of described mono-component polyurethane, aluminum paste, MEK, dimethyl formamide is 50:10:25:5.The technological parameter that carries out PU silver finishing coat in described the 3rd step is: select the acute angle scraper, adjust scraper angle 110 degree, regulate magnetic roller magnetic force 75%, 125 ℃ of control proparea oven temperatures, 145 ℃ of back zone temperature, drying time 30s.
The present invention illustrates its preparation technology as an example of the novel terylene camouflage OXFORD of 600D example, if prepare this type of coated fabric base cloth of other function, then according to selecting corresponding auxiliary agent to get final product to the requirement of fabric base cloth function.Adopt the product structure of technology of preparing of the present invention preparation reasonable, novel in design, multi-functional combination has the functions such as high hydrostatic pressure resistance, high fracture strength, and product is applicable to base camp tent etc.It is multi-functional in one that logical hyperchromatic method makes fabric have a high weathering color fastness and high friction and color fastness to water, high fabric ultimate strength etc., and technological process is simple, feasible, has significantly energy-conservation, conservation.
Claims (10)
1. the coating process of a camouflage color tent cloth is characterized in that: may further comprise the steps: the first step, adopt PA glue that the fabric base cloth is carried out bottoming; Second step, the PVC that carries out that starches fabric base cloth after the bottoming with the PVC coating whitewash; The 3rd step, the fabric base cloth after with PU silver slurry PVC being whitewashed carry out the silver-colored finishing coat of PU.
2. the coating process of a kind of camouflage color tent cloth according to claim 1, it is characterized in that: described PA glue comprises PA coating adhesive, crosslinking agent, solvent, and the weight ratio of PA coating adhesive, crosslinking agent, solvent is 80 ~ 100:1 ~ 2:4 ~ 8.
3. the coating process of a kind of camouflage color tent cloth according to claim 2, it is characterized in that: the preparation process of described PA glue is: solvent is joined in the crosslinking agent mix well, then join in the coating adhesive and stir, add toluene adjusting viscosity to 8000 ~ 10000mPaS when stirring, leave standstill 30min after stirring evenly.
4. the coating process of a kind of camouflage color tent cloth according to claim 3, it is characterized in that: the technological parameter in the described first step during with the bottoming of PA glue is: select the acute angle scraper, adjusting scraper angle is 115 ~ 125 degree, the magnetic force of regulating magnetic roller is 90 ~ 100%, control baking oven proparea temperature is 70 ~ 80 ℃, 110 ~ 120 ℃ of back zone temperature, criteria thus the drying time 30 ~ 35s.
5. the coating process of a kind of camouflage color tent cloth according to claim 4, it is characterized in that: described PVC coating slurry comprises polyvinyl chloride resin, plasticizer, heat stabilizer, and the weight ratio of polyvinyl chloride resin, plasticizer, heat stabilizer is 100:100:0.5 ~ 4, and described PVC coating slurry also comprises whiting.
6. the coating process of a kind of camouflage color tent cloth according to claim 5, it is characterized in that: the preparation process of described PVC coating slurry is: add first a part of plasticizer in stearate and whiting, stir evenly, then pour in the mixer with polyvinyl chloride resin, add again remaining plasticizer, stir evenly and grind 1 ~ 2 time with three-roll grinder afterwards, the batching with milled stirs 5 ~ 10min more at last, leaves standstill 30min or vacuumize to carry out deaeration and process.
7. the coating process of a kind of camouflage color tent cloth according to claim 6, it is characterized in that: the technological parameter that PVC whitewashes in the described second step is: select the acute angle scraper, adjust scraper angle 115 ~ 125 degree, regulate magnetic roller magnetic force 90 ~ 100%, 170 ~ 190 ℃ of control oven temperatures, fusion time 2 ~ 3min, the clot after the cold water roller cooling of the fabric base cloth after PVC whitewashes.
8. the coating process of a kind of camouflage color tent cloth according to claim 1, it is characterized in that: described PU silver slurry comprises mono-component polyurethane, aluminum paste, MEK, dimethyl formamide, and the weight ratio of described mono-component polyurethane, aluminum paste, MEK, dimethyl formamide is 50:10:25 ~ 30:5 ~ 10.
9. the coating process of a kind of camouflage color tent cloth according to claim 8, it is characterized in that: the preparation process of described PU silver slurry is: first a part of solvent is joined in the aluminum paste, add again polyurethane adhesive after stirring evenly, add while stirring remaining solvent, adjust viscosity 5000 ~ 6000mPaS, leave standstill 30min or vacuumizing and defoaming.
10. the coating process of a kind of camouflage color tent cloth according to claim 9, it is characterized in that: the technological parameter that carries out PU silver finishing coat in described the 3rd step is: select the acute angle scraper, adjust scraper angle 110 ~ 125 degree, regulate magnetic roller magnetic force 75 ~ 85%, 125 ~ 135 ℃ of control proparea oven temperatures, 145 ~ 155 ℃ of back zone temperature, drying time 30 ~ 40s.
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| CN2012104350397A CN102978963A (en) | 2012-11-02 | 2012-11-02 | Camouflage tent cloth coating technology |
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| CN2012104350397A CN102978963A (en) | 2012-11-02 | 2012-11-02 | Camouflage tent cloth coating technology |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103757925A (en) * | 2014-01-07 | 2014-04-30 | 平湖市新保复合制品有限公司 | Novel warm keeping and ventilating film used for fabrics |
| CN105127072A (en) * | 2015-07-31 | 2015-12-09 | 浙江宇立新材料有限公司 | Manufacturing technique for high-definition high-light-reflection projection curtain |
| CN108505355A (en) * | 2018-06-01 | 2018-09-07 | 郑佳 | The preparation method and application of novel camouflage cover cloth |
-
2012
- 2012-11-02 CN CN2012104350397A patent/CN102978963A/en active Pending
Non-Patent Citations (1)
| Title |
|---|
| 黄玉媛等: "《轻化工助剂配方》", 31 August 2008, 中国纺织出版社 * |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103757925A (en) * | 2014-01-07 | 2014-04-30 | 平湖市新保复合制品有限公司 | Novel warm keeping and ventilating film used for fabrics |
| CN103757925B (en) * | 2014-01-07 | 2015-12-30 | 平湖市新保复合制品有限公司 | A kind of heat-insulation breathable film for fabric |
| CN105127072A (en) * | 2015-07-31 | 2015-12-09 | 浙江宇立新材料有限公司 | Manufacturing technique for high-definition high-light-reflection projection curtain |
| CN108505355A (en) * | 2018-06-01 | 2018-09-07 | 郑佳 | The preparation method and application of novel camouflage cover cloth |
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Application publication date: 20130320 |