A kind of manufacturing approach of aqueous polyurethane synthetic leather bass
Technical field
The present invention relates to a kind of manufacturing approach of aqueous polyurethane synthetic leather bass.
Background technology
Contain a large amount of volatile organic solvent (VOC) in the solvent type resin, in use enter atmosphere, not only destroy environment, be detrimental to health, also cause the waste of the resource and the energy simultaneously.Present whole synthetic leather industry production processing all is that to be based upon with the solvent borne polyurethane be in the basic unit of main body; In the production process in a large number with an organic solvent; Like dimethyl formamide, MEK, acetone, toluene, ethyl acetate etc., these solvents are very harmful to human body.General use for synthetic leather polyurethane resin solid content is about 30%, and the organic solvent amount reaches 70%, and in the process of synthetic leather, also can add certain amount of organic solvent again, so the use amount of organic solvent is bigger during actual production.Although in recent years because the rise of the prices of raw and semifnished materials; The restriction of aspects such as environment protection emission; Make enterprise have to consider the recycling of solvent, the solvent recovery ability reaches about 90%, but still has the solvent about 10% to reclaim; Mode with gas and waste water has been discharged in the environment, and environment and human body have been caused very big harm.
Waterborne polyurethane resin is to be decentralized medium with water, has nontoxic, environmental protection, safety, advantage such as do not fire, and be the best substitute products of solvent type resin.But the application of waterborne polyurethane resin on synthetic leather relatively lags behind comparatively speaking; Mainly concentrate on the surface finish of synthetic leather; Have only the water-based dry method to move technology such as membrane technology and printing and be applied in the actual production, aqueous polyurethane synthetic leather bass also only is in the development in laboratory stage.
Summary of the invention
The manufacturing approach that the purpose of this invention is to provide a kind of aqueous polyurethane synthetic leather bass; Through adopting waterborne polyurethane resin can make the aqueous polyurethane use for synthetic leather semi-finished product of nonwoven fabric base with similar solvent-borne type wet-process coating; The structure of itself and solvent-borne type wet method bass is similar, but production process uses the waterborne polyurethane resin of more environmental protection to make the synthetic leather bass.
The technical scheme that the present invention adopted is: a kind of manufacturing approach of aqueous polyurethane synthetic leather bass is characterized in that: comprise the steps that successively (a) prepares base fabric: base fabric is selected a kind of in nonwoven fabric, woven cloth or the knitted cloth for use; (b) preliminary treatment: finishing agent solution formula ratio is: water soluble polymer: 0-3 part; Organosilicon drilling additives: 1-3 part; Water: 100 parts; Preliminary treatment base fabric liquid carrying rate is 30~100%; (e) apply the aqueous polyurethane intumescent coating: aqueous polyurethane foaming layer formula of size ratio is: waterborne polyurethane resin: 100 parts; Foaming agent: 1.5-2 part; Foam stabilizer: 2-3 part; Thickener: 1-4 part; Colouring agent: 1 part; Crosslinking agent: 0-3 part; Physique filler: 1 part; The foaming slurry density is 300~700g/L; The every square meter coating weight of coating liquid is 100~800g/m
2(f) Infrared Heating or microwave dryer are adopted in oven dry, oven dry usually.
Water soluble polymer content is 2-3 part in the above-mentioned steps (b), and preliminary treatment base fabric liquid carrying rate is 50~80; (e) the foaming slurry density is 400~600g/L in the step; The every square meter coating weight of coating liquid is 200~500g/m
2
Water soluble polymer is polyvinyl alcohol, cellulose derivative, gelatin or modified starch in the above-mentioned steps (b); Organosilicon drilling additives is amido silicon oil or amino-modified silicone oil softener; Waterborne polyurethane resin is anion fat adoption ester type, anion fat adoption ether type, anion fat adoption ester-polyether-type, anion aromatic polyester type, anion aromatic polyether type or anion aromatic polyester-polyether-type in the step (e); Thickener is acrylic thickener, polyurethanes thickener or cellulose thickener; Crosslinking agent is isocyanate-based crosslinking agent or melamine-type crosslinking agent; Colouring agent is aqueous pigment cream or dyestuff; Foaming agent is fatty acid salt surfactant, fatty alcohol sulphuric acid salt surfactant, alkyl benzene sulphonate surfactant; Foam stabilizer is fatty acid amide surfactants, amine-oxides surfactant or cationic surfactant; The physique filler is superfine silicon dioxide, Paris white, ultra-fine natural skin powder, natural feather powder, natural wool powder, natural silk powder or lignocellulose.
Water soluble polymer is a polyvinyl alcohol in the above-mentioned steps (b); Organosilicon drilling additives is the amino-modified silicone oil softener; Waterborne polyurethane resin is anion fat adoption ester-polyether-type and anion aromatic polyester-polyether-type in the step (e); Thickener is acrylic thickener, polyurethanes thickener or cellulose thickener, preferably uses acrylic compounds and polyurethanes thickener; Crosslinking agent is isocyanate-based crosslinking agent; Colouring agent is aqueous pigment cream or dyestuff, preferably uses aqueous pigment cream; Foaming agent is fatty acid salt surfactant and alkyl benzene sulphonate surfactant; Foam stabilizer is a fatty acid amide surfactants; The physique filler is superfine silicon dioxide, lignocellulose, Paris white or ultra-fine natural skin powder.
Above-mentioned (b) step and (e) between also comprise following two steps: (c) oven dry: bake out temperature is 80~160 ℃ ℃; (d) steep water based polyurethane slurry: the aqueous polyurethane slurry is to be got by one or more mixing in waterborne polyurethane resin, thickener, crosslinking agent and the colouring agent, and its pulp solution formula rate is: waterborne polyurethane resin: 100 parts; Water: 0-30 part; Thickener: 1-4 part; Colouring agent: 1-3 part; Crosslinking agent: 0-1 part; Dipping back nonwoven fabric liquid carrying rate 50~60%.
Bake out temperature is 130~150 ℃ in above-mentioned (c) step; Waterborne polyurethane resin is anion fat adoption ester type, anion fat adoption ether type, anion fat adoption ester-polyether-type, anion aromatic polyester type, anion aromatic polyether type or anion aromatic polyester-polyether-type in the step (d); Thickener is acrylic thickener, polyurethanes thickener or cellulose thickener; Crosslinking agent is isocyanate-based crosslinking agent or melamine-type crosslinking agent; Colouring agent is aqueous pigment cream or dyestuff.
Waterborne polyurethane resin is anion fat adoption ester-polyether-type and anion aromatic polyester-polyether-type in the above-mentioned steps (d); Thickener is acrylic compounds or polyurethanes thickener; Crosslinking agent is isocyanate-based crosslinking agent; Colouring agent is an aqueous pigment cream.
The present invention has the following advantages: the aqueous polyurethane synthetic leather bass through the present invention's preparation, have the basic structure of solvent-borne type wet-method synthetic leather bass, and its feel and rerum natura are near solvent-borne type synthetic leather bass; Do not use any solvent to process in the whole process of production; Can be used to the back processing and manufacturing of any synthetic leather product, move film, printing spraying, embossing embossing, flour milling etc., particularly select for use the back processing of waterborne polyurethane resin material to have more the feature of environmental protection like dry method; Adopt water-base polyurethane material to carry out back processing, can be used as footwear leather, sofa artificial leather, luggage leather, clothing leather etc., compare no solvent residue in finished product, health is not had harm with the solvent-borne type product; Process route of the present invention is simple, and to compare Costco Wholesale suitable with solvent-borne type, do not use solvent in the whole process of production, and basic VOC free discharging had both reduced solvent reclaimer input, use cost, had reduced energy waste and environmental pollution again.
The specific embodiment
Below in conjunction with specific embodiment the present invention is at length explained.
Capital equipment involved in the specific embodiment of the invention comprises: put cloth holder, Chu Buji, band knobbling rolls dipping tank, be coated with conventional equipments such as head, infrared or microwave drying typing line, winder.
Employed portioned product title, purposes and behavioral illustrations in the specific embodiment of the invention:
Embodiment 1: (a) base fabric is the employing W-1023S120 of Fujian Nanfang Co., Ltd. nonwoven fabric, 1.0mm, 230g/m in the step
2, PA30/PET70; (b) the finishing agent solution formula is in the step:
Polyvinyl alcohol | 2 parts |
Softening agent for fibres | 1 part |
Water | 100 parts |
Preliminarytreatment base fabric liquid carrying rate is 60%.
(c) bake out temperature is 130 ℃ in the step.
(d) the aqueous polyurethane formula of size is in the step:
Anion fat family aqueous polyurethane | 100 parts |
Water | 30 parts |
Acrylic thickener | 4 parts |
Aqueous pigment cream | 3 parts |
The isocyanates crosslinking agent | 1 part |
Dippingback nonwoven fabric liquid carrying rate 60%.
(e) the aqueous polyurethane formula of size is in the step:
Anion fat family aqueous polyurethane | 100 parts |
The fatty acid salt surfactant | 2 parts |
The succinyl amine salt | 3 parts |
Acrylic thickener | 4 parts |
Aqueous pigment cream | 1 part |
The isocyanates crosslinking agent | 3 parts |
Superfine silicon dioxide | 1 part |
Adoptthe blade coating mode to apply behind the mechanical foaming.
(f) microwave drying, microwave 10KV are adopted in oven dry in the step.
Embodiment 2: (a) base fabric is the employing HS-1028 of Fujian Nanfang Co., Ltd., 1.0mm, 280g/m in the step
2High-density non-woven fabrics.
(b) the finishing agent solution formula is in the step:
Polyvinyl alcohol | 3 parts |
Softening agent for fibres | 1.5 part |
Water | 100 parts |
Preliminarytreatment base fabric liquid carrying rate is 50%.
(c) bake out temperature is 150 ℃ in the step.
(d) the aqueous polyurethane formula of size is in the step:
The anion aromatic waterborne polyurethane | 100 parts |
The polyurethanes thickener | 1 part |
Aqueous pigment cream | 1 part |
Dippingback nonwoven fabric liquid carrying rate 50%.
(e) the aqueous polyurethane formula of size is in the step:
The anion aromatic waterborne polyurethane | 100 parts |
The fatty acid salt surfactant | 1.5 part |
The succinyl amine salt | 2 parts |
The polyurethanes thickener | 1 part |
Aqueous pigment cream | 1 part |
Lignocellulose | 1 part |
Adoptroll coating model to apply behind the mechanical foaming.
(f) microwave drying, microwave 10KV are adopted in oven dry in the step.
Embodiment 3: (a) base fabric is single for adopting Fu Jiannan to spin 0.55mm PU leather base cloth (grey black, wet) in the step.
(b) the finishing agent solution formula is in the step:
Softening agent for fibres | 1 part |
Water | 100 parts |
(c),(d) two steps need not carry out, and directly carry out (e) step.
(e) the aqueous polyurethane formula of size is in the step:
Anion fat family aqueous polyurethane | 100 parts |
The fatty acid salt surfactant | 2 parts |
The succinyl amine salt | 3 parts |
Acrylic thickener | 4 parts |
Aqueous pigment cream | 1 part |
The isocyanates crosslinking agent | 3 parts |
Superfine silicon dioxide | 1 part |
Adoptthe blade coating mode to apply behind the mechanical foaming.
(f) the Infrared Heating mode is adopted in oven dry in the step, and the oven temperature gradient is at 50-70-90-110-130 ℃.
Embodiment 4: (a) base fabric is given birth to through compiling the imitative cashmere of 0.7mm black for adopting Haining person of outstanding talent in the step.
(b) the finishing agent solution formula is in the step:
Softening agent for fibres | 3 parts |
Water | 100 parts |
Preliminary treatment base fabric liquid carrying rate is 50%.[0032] (c) in the step bake out temperature be 150 ℃.[0033] (c), (d) two steps need not carry out, and directly carry out (e) step; (e) the aqueous polyurethane formula of size is in the step:
The anion aromatic waterborne polyurethane | 100 parts |
The fatty acid salt surfactant | 1.5 part |
The succinyl amine salt | 2 parts |
The polyurethanes thickener | 1 part |
Aqueous pigment cream | 1 part |
Lignocellulose | 1 part |
Adoptthe blade coating mode to apply behind the mechanical foaming.
(f) the Infrared Heating mode is adopted in oven dry in the step, and the oven temperature gradient is at 50-70-90-110-130 ℃.
Embodiment 5: (a) base fabric is to adopt Bandung, Wujiang 50Dx75D 140g of Fabritex S.r.l. through compiling suede nap in the step.
(b) the finishing agent solution formula is in the step:
Softening agent for fibres | 1 part |
Water | 100 parts |
Preliminary treatment base fabric liquid carrying rate is 40%; (c), (d) two steps need not carry out, and directly carry out (e) step; (e) the aqueous polyurethane formula of size is in the step:
The anion aromatic waterborne polyurethane | 100 parts |
The fatty acid salt surfactant | 1.5 part |
The succinyl amine salt | 2 parts |
The polyurethanes thickener | 1 part |
Aqueous pigment cream | 1 part |
Lignocellulose | 1 part |
Adoptthe blade coating mode to apply behind the mechanical foaming.
(f) the Infrared Heating mode is adopted in oven dry in the step, and the oven temperature gradient is at 50-70-90-110-130 ℃.