CN107981767B - A kind of terylene wood pulp wet tissue and preparation method thereof - Google Patents
A kind of terylene wood pulp wet tissue and preparation method thereof Download PDFInfo
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- CN107981767B CN107981767B CN201711225455.3A CN201711225455A CN107981767B CN 107981767 B CN107981767 B CN 107981767B CN 201711225455 A CN201711225455 A CN 201711225455A CN 107981767 B CN107981767 B CN 107981767B
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- 229920001131 Pulp (paper) Polymers 0.000 title claims abstract description 92
- 239000005020 polyethylene terephthalate Substances 0.000 title claims abstract description 90
- 229920004933 Terylene® Polymers 0.000 title claims abstract description 75
- 238000002360 preparation method Methods 0.000 title claims abstract description 17
- 239000002994 raw material Substances 0.000 claims abstract description 16
- 150000001875 compounds Chemical class 0.000 claims abstract description 15
- 238000001035 drying Methods 0.000 claims abstract description 15
- 230000006855 networking Effects 0.000 claims abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 13
- 229920004934 Dacron® Polymers 0.000 claims abstract description 12
- 238000009960 carding Methods 0.000 claims abstract description 12
- 238000005360 mashing Methods 0.000 claims abstract description 6
- 238000000034 method Methods 0.000 claims description 15
- 239000000835 fiber Substances 0.000 claims description 10
- 230000018044 dehydration Effects 0.000 claims description 9
- 238000006297 dehydration reaction Methods 0.000 claims description 9
- 239000002131 composite material Substances 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 6
- 229920000742 Cotton Polymers 0.000 claims description 5
- 238000010009 beating Methods 0.000 claims description 5
- 238000010276 construction Methods 0.000 claims description 5
- 230000006798 recombination Effects 0.000 claims description 5
- 238000005215 recombination Methods 0.000 claims description 5
- 235000008331 Pinus X rigitaeda Nutrition 0.000 claims description 3
- 235000011613 Pinus brutia Nutrition 0.000 claims description 3
- 241000018646 Pinus brutia Species 0.000 claims description 3
- 238000000465 moulding Methods 0.000 claims description 3
- JSLMNNPQKHONFW-UHFFFAOYSA-N benzene naphthalene-1-carboxylic acid Chemical compound C1(=CC=CC2=CC=CC=C12)C(=O)O.C1=CC=CC=C1 JSLMNNPQKHONFW-UHFFFAOYSA-N 0.000 claims 1
- 239000004744 fabric Substances 0.000 abstract description 11
- 238000004519 manufacturing process Methods 0.000 abstract description 11
- 229920000297 Rayon Polymers 0.000 abstract description 9
- 239000003292 glue Substances 0.000 abstract description 8
- 238000005516 engineering process Methods 0.000 abstract description 2
- 238000010521 absorption reaction Methods 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 6
- 229920000728 polyester Polymers 0.000 description 6
- 238000005265 energy consumption Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 229920000139 polyethylene terephthalate Polymers 0.000 description 3
- AFCARXCZXQIEQB-UHFFFAOYSA-N N-[3-oxo-3-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(CCNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 AFCARXCZXQIEQB-UHFFFAOYSA-N 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000009472 formulation Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000004745 nonwoven fabric Substances 0.000 description 2
- 238000004806 packaging method and process Methods 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 239000002023 wood Substances 0.000 description 2
- 241001343274 Dichrostachys spicata Species 0.000 description 1
- 244000007853 Sarothamnus scoparius Species 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 210000004919 hair shaft Anatomy 0.000 description 1
- 239000003317 industrial substance Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- -1 polyethylene terephthalate Polymers 0.000 description 1
- 238000004537 pulping Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000000284 resting effect Effects 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
- A47K—SANITARY EQUIPMENT NOT OTHERWISE PROVIDED FOR; TOILET ACCESSORIES
- A47K10/00—Body-drying implements; Toilet paper; Holders therefor
- A47K10/16—Paper towels; Toilet paper; Holders therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/06—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
- B32B27/10—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of paper or cardboard
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/36—Layered products comprising a layer of synthetic resin comprising polyesters
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B29/00—Layered products comprising a layer of paper or cardboard
- B32B29/02—Layered products comprising a layer of paper or cardboard next to a fibrous or filamentary layer
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B38/00—Ancillary operations in connection with laminating processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B38/00—Ancillary operations in connection with laminating processes
- B32B38/16—Drying; Softening; Cleaning
- B32B38/164—Drying
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B5/00—Layered products characterised by the non- homogeneity or physical structure, i.e. comprising a fibrous, filamentary, particulate or foam layer; Layered products characterised by having a layer differing constitutionally or physically in different parts
- B32B5/02—Layered products characterised by the non- homogeneity or physical structure, i.e. comprising a fibrous, filamentary, particulate or foam layer; Layered products characterised by having a layer differing constitutionally or physically in different parts characterised by structural features of a fibrous or filamentary layer
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2262/00—Composition or structural features of fibres which form a fibrous or filamentary layer or are present as additives
- B32B2262/02—Synthetic macromolecular fibres
- B32B2262/0276—Polyester fibres
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2307/00—Properties of the layers or laminate
- B32B2307/50—Properties of the layers or laminate having particular mechanical properties
- B32B2307/54—Yield strength; Tensile strength
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2307/00—Properties of the layers or laminate
- B32B2307/70—Other properties
- B32B2307/728—Hydrophilic
Landscapes
- Health & Medical Sciences (AREA)
- Public Health (AREA)
- Nonwoven Fabrics (AREA)
- Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
- Paper (AREA)
Abstract
The present invention relates to a kind of terylene wood pulp wet tissue and preparation method thereof, which includes the raw material of following mass percent: wood pulp 30-40%, terylene 60-70%.Wood pulp is adjusted into moisture content after mashing, mill, then papermaking forms, and obtains wood pulp paper;Will be compound with wood pulp paper after dacron carding networking, successively water content is adjusted to get terylene wooden oar wet tissue through spun lacing, plain net suction, drying cylinder.The present invention is by adjusting production technology, adjustment wood pulp cloth terylene and wood pulp proportion find the optimum formula that can replace terylene viscose glue flexibility, by adjusting the compound rear drying mode of wood pulp cloth, wood pulp cloth wet tissue thickness during post-production is enabled to meet or exceed common wet tissue thickness on the market.
Description
Technical field
The present invention relates to a kind of terylene wood pulp wet tissues and preparation method thereof, belong to wet tissue technical field.
Background technique
The wet tissue market of sustainable growth and people constantly stimulate wet tissue product to health, health, the demand of environment-friendly products
Weed out the old and bring forth the new.At the same time, higher requirements are also raised for performance of the people to wet tissue spunlace non-woven material.Existing city
Wet tissue on face, which is generally formulated, to be produced for terylene viscose glue or full terylene as raw material, the rigid big, moisture absorption of polyester fiber
It is small, water conservation is poor, content excessively easily leads to product flexibility is poor, formulation absorption ability is poor, the resting period is short etc., therefore pure polyester production
Product are not typically used as wet tissue.
Become viscose glue terylene wet tissue by the way that a certain amount of viscose rayon is added, the hydrophilicity of terylene hydro-entangled non-woven fabric is big
It is big to improve, but when viscose glue content is greater than 10%, with the increase of viscose glue content, the mechanical property of terylene hydro-entangled non-woven fabric is bright
Aobvious decline;Strong stretching property, hard and soft and moisture absorbability and moisture retentivity are the important indicators for measuring wet tissue physical property.
Viscose glue and terylene do cost of material generally will be high, and manufacturing cost is high.In comparison wood pulp cellulose and polyester fiber
Compound wood pulp cloth formulation absorption ability is strong, and water retention property, mechanical property and moisture absorbability and moisture retentivity all improve a lot, while because of wood
Pulp fibres price is lower, and manufacturing cost is greatly reduced.
Chinese patent document CN106283839A (application number: 201610660119.0) is disclosed a kind of ultrashort using polyester
Fiber, wood pulp are by raw-material weight percentage by the spun lacing material of wet process water jet process machine-shaping for primary raw material
The wood by defibrination wire-dividing broom purification that the polyester superbhort fiber of 10-80%, the reinforced superbhort fiber of 0-5%, 15-90% are matched
Slurry mixes.Its forming method: wood pulp pulping rear sub-wire brooming, polyester superbhort fiber and reinforced superbhort fiber open liquid after packet
Mutually disperse, is then pierced in advance after the mixing of three's liquid phase, hygrometric state forming in titled net formation net, spun lacing, suction, drying, stain are examined
It surveys, coiled, cutting packaging after grammes per square metre detection.However, wood pulp cloth substitutes common wet tissue, there is also some problems, such as: wood pulp is fine
Dimension hplc excessively easily leads to that product flexibility is poor, and wet tissue thickness does not reach requirement, and later period packaging molding has been not easy to wrap.General wood
It starches in cloth production process in line with save the cost, reduces the principle of energy consumption, wringer is needed to carry out physics after platform spun lacing is compound
Dry, heated drying carries out dehydration and drying processing.But in order to make wood pulp cloth reach thickness requirement, reaches post-production packet as far as possible and want
It asks, squeezes the physics dehydration of mode, while dehydration, greatly reduce the thickness of product.It is applied alone steam-heated mode to carry out
Dry mode improves production cost firstly, steam consumption increases considerably, and produces speed critical constraints;Secondly heated drying
Temperature is excessively high, and drying too long in flow can make product hair shaft harden, and is not suitable for enhancing product performance.
Therefore, exploitation softness is high, and it is urgently to be resolved to become this field for the wood pulp cloth wet tissue of the performances composite demand such as thickness
The technical issues of.
Summary of the invention
In view of the deficiencies of the prior art, the present invention provides a kind of terylene wood pulp wet tissue and preparation method thereof.
The present invention adjusts wood pulp cloth terylene and finds with wood pulp proportion and terylene viscose glue can be replaced soft by adjusting production technology
Soft optimum formula, by adjusting the compound rear drying mode of wood pulp cloth, so that wood pulp cloth wet tissue thickness during post-production
Common wet tissue thickness on the market can be met or exceeded.
Technical scheme is as follows:
A kind of terylene wood pulp wet tissue, the raw material including following mass percent:
Wood pulp 30-40%, terylene 60-70%.
, according to the invention it is preferred to, the mass concentration of the wood pulp is 0.5-5wt%, further preferred 0.8-
1.5wt%, most preferably 1.2wt%;
Preferably, the raw material of wood pulp is needlebush, further preferred pine.
, according to the invention it is preferred to, the terylene is polyethylene terephthalate (PET);
Preferably, the fiber number of the terylene is 1.56dtex, and the length of the terylene is 38mm.
, according to the invention it is preferred to, the terylene wooden oar wet tissue with a thickness of 0.25-0.35mm, further preferably
0.28-0.30mm;
Preferably, the water content of the terylene wooden oar wet tissue is 3-5wt%.
, according to the invention it is preferred to, terylene wood pulp wet tissue, the raw material including following mass percent:
Wood pulp 30%, terylene 70%.
, according to the invention it is preferred to, terylene wood pulp wet tissue, the raw material including following mass percent:
Wood pulp 40%, terylene 60%.
According to the present invention, the preparation method of above-mentioned terylene wood pulp wet tissue, comprises the following steps that
Wood pulp is adjusted into moisture content after mashing, mill, then papermaking forms, and obtains wood pulp paper;
Will be compound with wood pulp paper after dacron carding networking, successively through spun lacing, plain net suction, drying cylinder adjust water content to get
Terylene wooden oar wet tissue.
Preparation method according to the present invention, it is preferred that it is 17-18 ° of SR that beating degree is controlled after wood pulp mill;
Preferably, wood pulp adjust moisture content after mass concentration be 0.5-5wt%, further preferred 0.8-1.5wt%, it is optimal
Select 1.2wt%.
Preparation method according to the present invention, it is preferred that through fine opener, the processing of air pressure cotton machine before dacron carding molding.More
Be conducive to subsequent combing networking.
Preparation method according to the present invention, it is preferred that after dacron carding networking and in wood pulp paper recombination process, wood pulp paper two
Face is compound respectively at terylene networking, forms wood pulp paper in centre, upper and lower surface is the composite construction of dacron carding net.
Preparation method according to the present invention, it is preferred that plain net aspiration procedure is to pass through vacuum between upper layer and lower layer plain net
Pump suction dehydration.It is aspirated by plain net, avoids causing the thickness of wet tissue not reach requirement using the dewatering type of physical squeezing;Greatly
The usage amount of heat drying steam has been saved greatly, and has saved energy consumption.
The present invention prepares wet tissue collectively as raw material using wood pulp and terylene, because wood pulp water absorbing properties itself are good, so that raw
It does not need to add during the industrial chemicals such as any hydrophilic agent are just well positioned to meet the processing of later period wet tissue during producing and match
Square absorbent properties.
Beneficial effects of the present invention are as follows:
1, terylene wooden oar wet tissue of the invention is much lower compared to full terylene or viscose glue terylene wet tissue manufacturing cost, by adjusting
The proportion of wooden oar and terylene, so that terylene wooden oar wet tissue pulling force, thickness, moisture content, the uniformity and flexibility are superior.
2, terylene wooden oar wet tissue of the invention, the wood pulp of use account for optimal ratio, so that wet tissue is healthier, hygienic, ring
It protects, is conducive to degrade.
3, terylene wooden oar wet tissue of the invention, wood pulp good water absorption itself can be locked very well without adding any hydrophilic agent
Firmly moisture.
4, it is avoided by vacuum suction dehydration using the de- of physical squeezing in terylene wooden oar wet tissue preparation process of the invention
Water mode causes the thickness of wet tissue not reach requirement;The usage amount of heat drying steam is greatly saved, and has saved energy consumption.
Specific embodiment
Below by specific embodiment, the present invention will be further described, but not limited to this.
Raw materials used in embodiment is conventional raw material, and device therefor is conventional equipment, commercial products.
Wherein: wood pulp used is pine slurry, and terylene used is PET, and the fiber number of terylene is 1.56dtex, and described washs
The length of synthetic fibre is 38mm.
Embodiment 1
A kind of terylene wood pulp wet tissue, the raw material including following mass percent:
Wood pulp 30%, terylene 70%.
Preparation method comprises the following steps that
Wood pulp is adjusted into moisture content after mashing, mill, then papermaking forms, and obtains wood pulp paper;
It is 17-18 ° of SR that beating degree is controlled after mill, and mass concentration is 1.5wt% after wood pulp adjusts moisture content;
Terylene is combed into networking after fine opener, air pressure cotton machine (600Pa pressure) processing respectively, it is compound with wood pulp paper,
Wood pulp paper two sides is compound respectively at terylene networking in recombination process, forms wood pulp paper in centre, upper and lower surface is dacron carding net
Composite construction;
Water content successively is adjusted through spun lacing, plain net suction, drying cylinder again, curling is cut to get terylene wooden oar wet tissue product.
Plain net aspiration procedure is to pass through vacuum pump suction dehydration between upper layer and lower layer plain net.
Embodiment 2
A kind of terylene wood pulp wet tissue, the raw material including following mass percent:
Wood pulp 40%, terylene 60%.
Preparation method comprises the following steps that
Wood pulp is adjusted into moisture content after mashing, mill, then papermaking forms, and obtains wood pulp paper;
It is 17-18 ° of SR that beating degree is controlled after mill, and mass concentration is 1.2wt% after wood pulp adjusts moisture content;
Terylene is combed into networking after fine opener, air pressure cotton machine (600Pa pressure) processing respectively, it is compound with wood pulp paper,
Wood pulp paper two sides is compound respectively at terylene networking in recombination process, forms wood pulp paper in centre, upper and lower surface is dacron carding net
Composite construction;
Water content successively is adjusted through spun lacing, plain net suction, drying cylinder again, curling is cut to get terylene wooden oar wet tissue product.
Plain net aspiration procedure is to pass through vacuum pump suction dehydration between upper layer and lower layer plain net.
Embodiment 3
A kind of terylene wood pulp wet tissue, the raw material including following mass percent:
Wood pulp 35%, terylene 65%.
Preparation method comprises the following steps that
Wood pulp is adjusted into moisture content after mashing, mill, then papermaking forms, and obtains wood pulp paper;
It is 17-18 ° of SR that beating degree is controlled after mill, and mass concentration is 0.8wt% after wood pulp adjusts moisture content;
Terylene is combed into networking after fine opener, air pressure cotton machine (600Pa pressure) processing respectively, it is compound with wood pulp paper,
Wood pulp paper two sides is compound respectively at terylene networking in recombination process, forms wood pulp paper in centre, upper and lower surface is dacron carding net
Composite construction;
Water content successively is adjusted through spun lacing, plain net suction, drying cylinder again, curling is cut to get terylene wooden oar wet tissue product.
Plain net aspiration procedure is to pass through vacuum pump suction dehydration between upper layer and lower layer plain net.
Comparative example 1
As described in Example 1, unlike:
Material quality percentage are as follows: wood pulp 20%, terylene 80%.
Comparative example 2
As described in Example 1, unlike:
Material quality percentage are as follows: wood pulp 50%, terylene 50%.
Test example 1
Using 50g wet tissue as final products, in the case that other process conditions are constant, only change terylene and wood pulp matches, it will
Terylene wooden oar wet tissue test performance index made from embodiment 1-3 and comparative example 1-2, the results are shown in Table 1.
Table 1
Project/number | Embodiment 1 | Embodiment 2 | Embodiment 3 | Comparative example 1 | Comparative example 2 |
Horizontal pulling force/N | 36N | 32N | 34N | 30N | 27N |
Wet thickness/mm | 0.32mm | 0.30mm | 0.31mm | 0.28mm | 0.25mm |
Liquid absorption amount/times | 920 | 960 | 930 | 810 | 830 |
Grammes per square metre/g | 49-51g | 49-51g | 48-51g | 48-53g | 48-51g |
The uniformity | Uniformly | Uniformly | Uniformly | Unevenly | Unevenly |
Stain | Nothing | Nothing | Nothing | Nothing | Nothing |
Flexibility | It is excellent | It is excellent | It is excellent | Difference | Difference |
From table 1 it follows that several important physical indexs of terylene wood pulp wet tissue, embodiment 1-3 are better than comparative example 1-2
Very much, especially on liquid absorption amount and wet thickness, common wet tissue performance on the market can be met or exceeded.
Claims (5)
1. a kind of terylene wood pulp wet tissue, which is characterized in that the wet tissue includes the raw material of following mass percent:
Wood pulp 30-40%, terylene 60-70%;
The mass concentration of the wood pulp is 0.8-1.5wt%, and the raw material of wood pulp is pine, and the terylene is poly- to benzene
Naphthalate (PET), the fiber number of the terylene are 1.56dtex, and the length of the terylene is 38mm;
The terylene wooden oar wet tissue with a thickness of 0.25-0.35mm, the water content of the terylene wooden oar wet tissue is 3-5wt%.
2. terylene wood pulp wet tissue according to claim 1, which is characterized in that the wet tissue includes the original of following mass percent
Material:
Wood pulp 30%, terylene 70%;
Alternatively, wood pulp 40%, terylene 60%.
3. the preparation method of the described in any item terylene wood pulp wet tissues of claim 1-2, comprises the following steps that
Wood pulp is adjusted into moisture content after mashing, mill, then papermaking forms, and obtains wood pulp paper;
Will be compound with wood pulp paper after dacron carding networking, successively water content is adjusted to get terylene through spun lacing, plain net suction, drying cylinder
Wooden oar wet tissue.
4. preparation method according to claim 3, which is characterized in that controlling beating degree after wood pulp mill is 17-18 ° of SR;
Mass concentration is 0.5-5wt% after wood pulp adjusts moisture content.
5. preparation method according to claim 3, which is characterized in that through fine opener, air pressure cotton before dacron carding molding
Machine processing;
After dacron carding networking and in wood pulp paper recombination process, wood pulp paper two sides is compound respectively at terylene networking, forms wood pulp paper
In centre, upper and lower surface is the composite construction of dacron carding net;
Plain net aspiration procedure is to pass through vacuum pump suction dehydration between upper layer and lower layer plain net.
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CN111035296A (en) * | 2020-01-07 | 2020-04-21 | 山东昌诺新材料科技有限公司 | Terylene foot bath cloth and preparation method thereof |
CN111214157B (en) * | 2020-01-10 | 2022-04-22 | 竹海堂(湖南)医疗连锁管理有限公司 | Wormwood sterilizing wet tissue and preparation method thereof |
CN115089041B (en) * | 2022-04-13 | 2025-04-25 | 中国制浆造纸研究院有限公司 | Wet toilet wipe substrate and preparation method thereof |
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CN102605557A (en) * | 2011-12-09 | 2012-07-25 | 常熟市飞龙无纺机械有限公司 | Three-in-one spunlaced composite non-woven fabric |
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CN106283839B (en) * | 2016-08-12 | 2019-06-07 | 杭州诺邦无纺股份有限公司 | Polyester wood pulp wet process spun lacing material |
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