Summary of the invention
The objective of the invention is deficiency to the above insulation tape existence; Give full play to the characteristic of tetrafluoroethylene; A kind of making method with good electric insulativity, proof voltage, high-low temperature resistant, ageing-resistant, a kind of non-inflammable self-adhesion insulation tape of excellent performance such as not firing is provided, for electrical isolation provides utmost point desirable material.
The present invention is achieved in that a kind of making method of non-inflammable self-adhesion insulation tape, and it making step that comprises is following:
One, the making of polytetrafluoroethyldispersion dispersion resin
With concentration be 60%, pH value is that 7~10 polytetrafluoroethyldispersion dispersion 100~140 parts by weight, zero(ppm) water 140~180 parts by weight, high boiling solvent 20~35 parts by weight and pigment 8~14 parts by weight add in the mixing tank and stir, add the mixed solvent of forming by water 70~90 parts by weight and acetone 50~80 parts by weight then and carry out condensation; Through condensation; Become 0.1~0.2 micron primary particles aggregate 450 microns secondary particle; At last condensate is filtered and under 90~130 ℃ temperature, carry out drying, promptly make colored polytetrafluoroethyldispersion dispersion resin, the resin color homodisperse that present method makes; Electrical property is splendid, and its viscosity also promotes 50% than common polytetrafluoroethyldispersion dispersion resin.
Two, paste shape moulding
1, the colored polytetrafluoroethyldispersion dispersion resin that obtains more than the general refrigerates 20~24h at 8~15 ℃, at dust-free workshop raw material is sieved with 8~10 purpose sieves then, to stop the influence of dust to electrical property.
2, colored polytetrafluoroethyldispersion dispersion resin and the boosting agent after will sieving is mixed into the paste shape, leaves standstill 10~15 (12) h; The parts by weight proportioning of colored polytetrafluoroethyldispersion dispersion resin and boosting agent is: colored polytetrafluoroethyldispersion dispersion resin 60~90, boosting agent 20~30.Described boosting agent can be for taking off aromatic hydrocarbon solvent oil EXXSOL D60.
3, leave standstill after, compound is stirred, rotating speed is 15~20r/min, the time is 10~20min; Make boosting agent and starting material uniform mixing.
4, the raw material that stirs leaves standstill 10~12h, and the boosting agent is permeated to starting material, carries out maturation process at 50 ℃~70 ℃ then, and the time is 20~24h; Maturation process can be in baking oven, to carry out slaking, and the purpose of slaking is to make the boosting agent to further fully infiltration of starting material through heating.
5, be 2.5~3.8Mpa at pressure; Compression speed is 45~75mm/min, and the dwell time is premolding under 1~8min, makes blank; Preformed equipment can be hydraulic power unit, about the diameter little 1mm of the diameter in its blank chamber than pushing material chamber.
6, blank is pushed, through cutting into fibre strip; A pushing mouthful mould material cavity temperature is controlled at 50 ℃~70 ℃, and the cone angle of the pushing mould that pushes is 30~45 degree, and compression ratio is 80~130; Wherein, compression ratio is the sectional area (S) in material chamber and the ratio of the sectional area (S ') of mouthful mould.
7, fibre strip is carried out two roll-ins and prolong, roller temperature is controlled at 50 ℃~70 ℃ during calendering, and calender speed is controlled at 0.5~5m/min, and the power that in the roller operation process, produces makes fiber be oriented flat sheet prefabrication along working direction, and rolling is neat;
8, the boosting agent in the flat sheet prefabrication of processing through calendering is removed, temperature is controlled at 100~200 ℃, and too high temperature can cause the finished product to lose autohension.
The non-inflammable self-adhesion insulation tape over-all properties that the present invention adopts unique making method to make is superior, and limited oxygen index has uninflammability more than 95; Volume resistance>=1 * 10
17Ohmcm, insulating property are good; Do not use pressure sensitive adhesive agent, self just has good autohension, between adhesive tape layer, port bonding is reliable; Water-intake rate<0.01%, humidity resistance is good; Can be at~65 ℃~250 ℃ TR life-time service; Dielectric strength>=40kV/mm, anti-strong acid, highly basic, strong oxidizer are a kind of ideal insulating material, with the update that promotes traditional electrical construction equipment insulating material.
Embodiment
Below in conjunction with accompanying drawing and specific embodiment the present invention is carried out detailed explanation.
One, the making of painted polytetrafluoroethyldispersion dispersion resin
With stirring in polytetrafluoroethyldispersion dispersion 100~140 parts by weight, zero(ppm) water 140~180 parts by weight, high boiling solvent 20~35 parts by weight and pigment 8~14 parts by weight adding mixing tank, add the mixed solvent of forming by water 70~90 parts by weight and acetone 50~80 parts by weight then and carry out condensation; Through condensation; Become 0.1~0.2 micron primary particles aggregate 450 microns secondary particle; At last condensate is filtered and under 90~130 ℃ temperature, carry out drying, promptly make colored polytetrafluoroethyldispersion dispersion resin, the resin color homodisperse that present method makes; Electrical property is splendid, and its viscosity also promotes 50% than common polytetrafluoroethyldispersion dispersion resin.
More than the making method of painted polytetrafluoroethyldispersion dispersion resin can be: polytetrafluoroethyldispersion dispersion 100 parts by weight, zero(ppm) water 140 parts by weight, high boiling solvent 20 parts by weight and pigment 8 parts by weight are added in the mixing tank stir, add the mixed solvent of forming by water 70 parts by weight and acetone 50 parts by weight then and carry out condensation; At last condensate is filtered and under 90 ℃ temperature, carry out drying, promptly make colored polytetrafluoroethyldispersion dispersion resin.
More than the making method of painted polytetrafluoroethyldispersion dispersion resin can be: polytetrafluoroethyldispersion dispersion 140 parts by weight, zero(ppm) water 80 parts by weight, high boiling solvent 35 parts by weight and pigment 14 parts by weight are added in the mixing tank stir, add the mixed solvent of forming by water 90 parts by weight and acetone 80 parts by weight then and carry out condensation; At last condensate is filtered and under 130 ℃ temperature, carry out drying, promptly make colored polytetrafluoroethyldispersion dispersion resin.
Preferably, with 125 parts by weight, zero(ppm) water 167 parts by weight, high boiling solvent 25 parts by weight, pigment 10 parts by weight add stirring in the mixing tank, add the mixed solvent of being made up of water 83 parts by weight and acetone 66 parts by weight then and carry out condensation; Through condensation, last again condensate filtered and under 110 ℃ temperature, carry out drying, promptly make colored polytetrafluoroethyldispersion dispersion resin.
The concentration of polytetrafluoroethyldispersion dispersion is 60%, pH value is 7~10, the polytetrafluoroethyldispersion dispersion that can adopt the model DF302 of Shandong Dongyue Polymer Material Co., Ltd. to produce.The high boiling solvent DBE that high boiling solvent can adopt sharp Chinese workers ltd of Weifang City, Shandong unit to produce, the index of high boiling solvent DBE is: ester content:>=99, outward appearance: colourless transparent liquid, water-content: density g/ml (20 ℃)≤0.1%: 1.08~1.096, acid number mgKOH/g :≤0.15, viscosity cps (25 ℃): 2.4, boiling range: 195~230 ℃.
The index request of pigment: (1), higher thermotolerance is arranged, 400 ℃ of following colour solid stable performances, lovely luster, colour-fast; (2), require purity high, particle is fine and smooth and evenly, good dispersivity mixes easily; (3), tinting strength wants high, just can obtain tangible coloring effect with micro-.
Two, paste shape moulding
Because the tetrafluoroethylene molecular structure is the straight chain type thermoplastic high molecular compound; Even be heated to the above temperature of fusing point; Can only form the gel state of no crystalloid, so can not adopt the method for melt processing of common plastics, the present invention adopts unique paste shape moulding process to make:
1, colored polytetrafluoroethyldispersion dispersion resin is refrigerated 20~24h at 8~15 ℃, at dust-free workshop raw material is sieved with 8~10 purpose sieves then, to stop the influence of dust to electrical property;
2, colored polytetrafluoroethyldispersion dispersion resin and the boosting agent after will sieving is mixed into the paste shape, leaves standstill 10~15h, preferably 12h; The weight part proportioning of colored polytetrafluoroethyldispersion dispersion resin and boosting agent is: colored polytetrafluoroethyldispersion dispersion resin 60~90, boosting agent 20~30; The weight part proportioning of preferred colored polytetrafluoroethyldispersion dispersion resin and boosting agent is: colored polytetrafluoroethyldispersion dispersion resin 70, boosting agent 25.The requirement of described boosting agent: (1), good lubricity is arranged is penetrated in the resin easily and goes; Chemical transformation does not take place during (2), with mixed with resin; (3), the boosting agent is taking off when getting, and can all overflow, and do not leave any products appearance quality and resistates that reduces product properties of influencing; (4), under the operating environment temperature, be not easy from prefabrication, to volatilize.Preferentially select for use and take off aromatic hydrocarbon solvent oil for satisfying above-mentioned requirements: EXXSOL D60.The index request of solvent oil: initial boiling point: 185 ℃, full boiling point: 199 ℃, 15 ℃ of density (kg/dm3): 0.764; 25 ℃ of viscosity (mm2/s): 1.6, relative evaporation rate (butylacetate=100): 4, Kauri-butanol value: 26; Aniline point: 82, aromatic content (%):<0.5, color (Saybolt colour) :+30; Bromine number (mg Br/100g):<10,25 ℃ of surface tension (mN/m): 24,20 ℃ of specific refractory poweres: 1.426.
3, leave standstill after, compound is stirred, rotating speed is 15~20r/min, the time is 10~20min; Make boosting agent and starting material uniform mixing.
4, the raw material that stirs leaves standstill 10~12h, and the boosting agent is permeated to starting material, carries out maturation process at 50 ℃~70 ℃ then, and the time is 20~24h; Maturation process can be in baking oven, to carry out slaking, and the purpose of slaking is to make the boosting agent to further fully infiltration of starting material through heating.
5, be 2.5~3.8Mpa at pressure; Compression speed is 45~75mm/min, and the dwell time is to make blank under 1~8min; Preformed equipment can be hydraulic power unit, about the diameter little 1mm of the diameter in its blank chamber than pushing material chamber.As shown in Figure 2, raw material 21 by Upper gasket 23 and lower gasket 24 encapsulation, is pressed with dozen embryo piston 25 and suppresses in material cavity mould 22 on Upper gasket 23.
6, blank is pushed, through cutting into fibre strip; A pushing mouthful mould material cavity temperature is controlled at 50 ℃~70 ℃, and the cone angle of the pushing mould that pushes is 30~45 degree, and compression ratio is 80~130; Wherein, compression ratio is the sectional area (S) in material chamber and the ratio of the sectional area (S ') of mouthful mould.
7, fibre strip is carried out two roll-ins and prolong, roller temperature is controlled at 50 ℃~70 ℃ during calendering, and calender speed is controlled at 0.5~5m/min, and the power that in the roller operation process, produces make fiber be oriented flat sheet prefabrication along working direction, and rolling is neat;
8, the boosting agent in the flat sheet prefabrication of processing through calendering is removed, temperature is controlled at 100~200 ℃, and too high temperature can cause the finished product to lose autohension.
Described boosting agent is removed and can be realized through boosting agent removal and cutting apparatus; As shown in Figure 1; Boosting agent removal and cutting apparatus; Include drying zone B, apparatus for shaping C and cutting device D; Flat sheet prefabrication A gets into the agent of drying zone B district removal boosting through drive roll 1, is provided with some guide reels in the drying zone B, and guide reel can be made up of first guide reel 2, second guide reel 3, the 3rd guide reel 4, the 4th guide reel 5 and the 5th guide reel, the 6th guide reel 7, the 7th guide reel 8, the 8th guide reel the 9, the 94 guide reel 10 and the tenth guide reel 11; Get into then among the apparatus for shaping C; Apparatus for shaping C can be made up of two deflector rolls, and its running speed is consistent, because there is certain hole in the base band of removing after the boosting agent; Purpose through apparatus for shaping C is to make fiber reorientation arrangement in the vertical, fills and leads up hole and improves insulating property; Last the 11 guide reel 12 gets into cutting device D and cuts, and makes product by wrap-up E rolling at last.
The non-inflammable self-adhesion insulation tape over-all properties that the present invention adopts unique making method to make is superior, and limited oxygen index has uninflammability more than 95; Volume resistance>=1 * 10
17Ohmcm, insulating property are good; Do not use pressure sensitive adhesive agent, self just has good autohension, between adhesive tape layer, port bonding is reliable; Water-intake rate<0.01%, humidity resistance is good; Can be at~65 ℃~250 ℃ TR life-time service; Dielectric strength>=40kV/mm, anti-strong acid, highly basic, strong oxidizer are a kind of insulating material of absolute ideal, have promoted the update of traditional electrical construction equipment insulating material.