CN101602047A - A kind of coating process of solar battery backing plate binder - Google Patents

A kind of coating process of solar battery backing plate binder Download PDF

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Publication number
CN101602047A
CN101602047A CNA2009101812509A CN200910181250A CN101602047A CN 101602047 A CN101602047 A CN 101602047A CN A2009101812509 A CNA2009101812509 A CN A2009101812509A CN 200910181250 A CN200910181250 A CN 200910181250A CN 101602047 A CN101602047 A CN 101602047A
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CN
China
Prior art keywords
adhesive
coating
base material
cavity
coated
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CNA2009101812509A
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Chinese (zh)
Inventor
林健飞
陈天龙
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Jiangsu Huitong Photovoltaic Materials Co Ltd
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Jiangsu Huitong Photovoltaic Materials Co Ltd
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Priority to CNA2009101812509A priority Critical patent/CN101602047A/en
Publication of CN101602047A publication Critical patent/CN101602047A/en
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

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  • Application Of Or Painting With Fluid Materials (AREA)

Abstract

The invention belongs to new energy field, disclose a kind of coating process of solar battery backing plate binder.The present invention adopts the mode of quantitative no feed back, by quantitative feed through metering, be transported to the coating cavity by sealing pipeline, guarantee that material is coated on the base material fully uniformly, there are not the circulation and the material trough that opens wide of material, the material viscosity equilibrium is remained unchanged, make the material of coating even, the whole uniformity in the compound back of film improves.This method is not owing to adopt unlimited hopper simultaneously, and on-the-spot volatilization is lacked in the material, does not cause environmental pollution.

Description

A kind of coating process of solar battery backing plate binder
Technical field
The invention belongs to new energy field, relate to a kind of coating process of solar battery backing plate binder.
Background technology
Solar cell module back veneer is a kind of important auxilliary material in the industry, and its high-end market is blank always by external monopolization at home.08 year backboard global market share is about 5,000,000,000 yuans according to statistics, in the application of China nearly 1,500,000,000 yuans, and along with the development of photovoltaic industry, authoritative institution predicts about the year two thousand twenty, it is present more than ten times that the application of photovoltaic industry will reach, calculate that in view of the above the market of global back veneer material can reach about nearly 50,000,000,000 RMB.Even China still keeps the present market share, still having nearly about 15,000,000,000 yuans market uses, China has become the photovoltaic industry processing base of output first in the world at present still more, rapid more than other national development, be trend of the times in the domestic backboard manufacturing enterprise that sets up of China for this reason.
The combined solar energy cell module back veneer is normally formed by the adhesive adhering and solidifying that base material or film surface were coated with by retes such as PET base material and fluoro-containing copolymer films.And the coating process that contains adhesive in the combined solar energy cell module back veneer of fluorine film now is generally modes such as roller coat, intaglio plate, scraper, these modes coating thickness in process of production are to determine by the depth of groove of gap between the roller or roller, all there is the circulation (as shown in Figure 1) of the material that opens wide, to such an extent as to changing, material viscosity cause coating layer thickness to change, cause the compound uniformity of film that fluctuation is arranged, material trough is open simultaneously, at dispensing area more solvent evaporates is arranged, form environmental pollution.
Summary of the invention
The adhesive coating evenly reaches the shortcoming of dispensing area solvent evaporates to the operating area ambient influnence inadequately when the objective of the invention is to overcome prior art production solar cell module back veneer, and a kind of coating process of solar battery backing plate binder is provided.
Technical scheme of the present invention is:
A kind of coating process of solar battery backing plate binder is characterized in that this method is made up of following steps:
1) adhesive is placed the liquid storage equipment that links to each other with the measuring pump of controllable flow amount;
2) calculate the adhesive output flow that is coated with cavity outlet according to the base material speed of service, adhesive coating thickness and base material width;
3) by the definite adhesive output flow that is coated with cavity outlet of the measuring pump of adjustable throttle amount;
4) measuring pump of adjustable throttle amount with adhesive by the closed conduit pump to being coated with cavity, the adhesive that the outlet of coating cavity adhesive is flowed out contacts directly with base material adhesive is coated on substrate surface.
Wherein, described method preferably is made up of following steps:
1) adhesive is placed the liquid storage equipment that links to each other with the measuring pump of controllable flow amount;
2) Programmable Logic Controller calculates the adhesive output flow that is coated with cavity outlet according to the signal combination adhesive coating thickness and the base material width of the base material speed of service that receives;
3) the adhesive output flow signal of the Programmable Logic Controller coating cavity outlet that will calculate is delivered to the measuring pump of adjustable throttle amount, determines the adhesive output flow of coating cavity outlet by the measuring pump of adjustable throttle amount;
4) measuring pump of adjustable throttle amount with adhesive by the closed conduit pump to being coated with cavity, the adhesive that the outlet of coating cavity adhesive is flowed out contacts directly with base material adhesive is coated on substrate surface.
The base material drying of adhesive is removed solvent in the described coating.
Liquid storage equipment described in this method is non-uncovered type liquid storage equipment, to prevent adhesive volatilization in the coating process.
Related coating system comprises measuring pump, coating back flow roll and the coating cavity of non-uncovered type liquid storage equipment, controllable flow amount in the described coating process.Wherein the adhesive suction inlet of the measuring pump of controllable flow amount places non-uncovered type liquid storage device interior, preferably places the bottom, and its adhesive outlet links to each other by closed conduit with the adhesive inlet of coating cavity; Leaving the slit of passing through for base material and the width of the adhesive delivery outlet that is coated with cavity and the width of base material between the adhesive outlet of coating cavity and the coating back flow roll is consistent.
Coating system related in the described coating process also can comprise Programmable Logic Controller (PLC) and/or drying unit simultaneously.
The signal input part of described Programmable Logic Controller (PLC) links to each other with the speed probe that coating is carried on the back among the Kun, gather the linear velocity of coating back of the body Kun, its signal output part links to each other with the measuring pump of controllable flow amount, the adhesive output quantity instruction that calculates is delivered to the measuring pump of adjustable throttle amount.
Described drying unit is generally tunnel drier, protective cover is located preferably to be provided with directly over being positioned at base material in the outside of drying unit, on the one hand can reduce the solvent that evaporates from substrate surface and enter the environment, also play the effect on the base material that the dust that prevents in the environment or other solid impurities fall coated adhesive on the other hand with coated adhesive.
Related various device is the conventional equipment of this area among the present invention.
Utilize method coating solar cell module back veneer of the present invention, the range of flow of charging pump generally is controlled at 500-1200ml/min, and the error of control accuracy is less than 0.5%.Tu Bu adhesive phase thickness and precision error is less than 0.5 micron in this way.
Beneficial effect of the present invention:
The present invention adopts the mode of quantitative no feed back, and the quantitative feed by through metering is transported to the coating cavity by sealing pipeline, guarantees that adhesive is coated on the base material fully uniformly.Native system does not have the circulation and the material trough that opens wide of material, and the material viscosity equilibrium is remained unchanged, and makes the material of coating even, and the whole uniformity in the compound back of film improves, and has improved product quality.Owing to do not adopt unlimited hopper, reduce the solvent evaporates amount in the applying material significantly simultaneously, do not caused environmental pollution, more helped environmental protection.By adopting the PLC control system can adjust the material output quantity automatically, play the real-time monitoring of system and the effect of adjustment, production operation is more simplified, can carry out industrial continuous production easily.
Description of drawings
The present invention is further illustrated below in conjunction with drawings and Examples.
Fig. 1 open type material coating system
Fig. 2 does not quantitatively have feed back coating system production control figure
Wherein 1 is non-uncovered type liquid storage equipment, the measuring pump of 2 controllable flow amounts, and 3 is Programmable Logic Controller (PLC), and 4 are the coating back flow roll, and 5 are the coating cavity, and 6 is drying baker, and 7 is protective cover, and 8 is base material.Dotted line is a control circuit, feeds back signal to PLC from the roller velocity of rotation, sends to measuring pump through after calculating, and measuring pump is regulated outputting material.
The specific embodiment
Embodiment 1 coating thickness (wet stock) is 30 microns a dual-component polyurethane class adhesive (production control figure is referring to accompanying drawing 2)
Adhesive is placed the fluid reservoir of adding a cover that links to each other with the measuring pump of controllable flow amount, the base material width is 1.6m, setting the base material speed of service is 30m/min, the adhesive output flow that Programmable Logic Controller is calculated the coating cavity outlet according to the base material running speed signal that receives in conjunction with adhesive coating thickness and base material width gauge is 1440ml/min, Programmable Logic Controller is delivered to this flow signal the measuring pump of adjustable throttle amount, measuring pump by the adjustable throttle amount by the closed conduit pump to being coated with cavity, and the adhesive output flow of control coating cavity outlet is 1440ml/min, and the adhesive that the coating cavity flows out contacts directly with base material adhesive is coated on substrate surface.The base material of adhesive is sent to dryer by the coating back flow roll in the coating, and solvent is removed in 110 ℃ of oven dry, enters next step compound working procedure.Effect: the adhesive coating is even, and thickness deviation is less than 2%.
Embodiment 2 coating thickness (wet stock) are 30 microns one-component hot setting adhesive (production control figure is referring to accompanying drawing 2)
Adhesive is placed the fluid reservoir of adding a cover that links to each other with the measuring pump of controllable flow amount, the base material width is 1m, setting the base material speed of service is 20m/min, the adhesive output flow that Programmable Logic Controller is calculated the coating cavity outlet according to the base material running speed signal that receives in conjunction with adhesive coating thickness and base material width gauge is 600ml/min, Programmable Logic Controller is delivered to this flow signal the measuring pump of adjustable throttle amount, measuring pump by the adjustable throttle amount by the closed conduit pump to being coated with cavity, and the adhesive output flow of control coating cavity outlet is 600ml/min, and the adhesive that the coating cavity flows out contacts directly with base material adhesive is coated on substrate surface.The base material of adhesive is sent to dryer by the coating back flow roll in the coating, and solvent is removed in 100 ℃ of oven dry, enters next step compound working procedure.Effect: the adhesive coating is even, and thickness deviation is less than 2%.
Embodiment 3 coating thickness (wet stock) are 25 microns one-component hot setting adhesive (production control figure is referring to accompanying drawing 2)
Adhesive is placed the fluid reservoir of adding a cover that links to each other with the measuring pump of controllable flow amount, the base material width is 1m, setting the base material speed of service is 30m/min, the adhesive output flow that Programmable Logic Controller is calculated the coating cavity outlet according to the base material running speed signal that receives in conjunction with adhesive coating thickness and base material width gauge is 750ml/min, Programmable Logic Controller is delivered to this flow signal the measuring pump of adjustable throttle amount, measuring pump by the adjustable throttle amount by the closed conduit pump to being coated with cavity, and the adhesive output flow of control coating cavity outlet is 600ml/min, and the adhesive that the coating cavity flows out contacts directly with base material adhesive is coated on substrate surface.The base material of adhesive is sent to dryer by the coating back flow roll in the coating, and solvent is removed in 105 ℃ of oven dry, enters next step compound working procedure.Effect: the adhesive coating is even, and thickness deviation is less than 2%.
The part that the present invention does not relate to prior art that maybe can adopt all same as the prior art is realized.

Claims (5)

1, a kind of coating process of solar battery backing plate binder is characterized in that this method is made up of following steps:
(1) adhesive is placed the liquid storage equipment that links to each other with the measuring pump of controllable flow amount;
(2) calculate the adhesive output flow that is coated with cavity outlet according to the base material speed of service, adhesive coating thickness and base material width;
(3) by the definite adhesive output flow that is coated with cavity outlet of the measuring pump of adjustable throttle amount;
(4) measuring pump of adjustable throttle amount with adhesive by the closed conduit pump to being coated with cavity, the adhesive that the outlet of coating cavity adhesive is flowed out contacts directly with base material adhesive is coated on substrate surface.
2, the coating process of a kind of solar battery backing plate binder according to claim 1 is characterized in that described method is made up of following steps:
1) adhesive is placed the liquid storage equipment that links to each other with the measuring pump of controllable flow amount;
2) Programmable Logic Controller calculates the adhesive output flow that is coated with cavity outlet according to the signal combination adhesive coating thickness and the base material width of the base material speed of service that receives;
3) the adhesive output flow signal of the Programmable Logic Controller coating cavity outlet that will calculate is delivered to the measuring pump of adjustable throttle amount, determines the adhesive output flow of coating cavity outlet by the measuring pump of adjustable throttle amount;
4) measuring pump of adjustable throttle amount with adhesive by the closed conduit pump to being coated with cavity, the adhesive that the outlet of coating cavity adhesive is flowed out contacts directly with base material adhesive is coated on substrate surface.
3, the coating process of a kind of solar battery backing plate binder according to claim 1 is characterized in that the base material drying of adhesive in the described coating is removed solvent.
4, the coating process of a kind of solar battery backing plate binder according to claim 1 is characterized in that described liquid storage equipment is non-uncovered type liquid storage equipment.
5, the coating process of a kind of solar battery backing plate binder according to claim 1 is characterized in that the width of adhesive delivery outlet of described coating cavity and the width of base material are consistent.
CNA2009101812509A 2009-07-21 2009-07-21 A kind of coating process of solar battery backing plate binder Pending CN101602047A (en)

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Application Number Priority Date Filing Date Title
CNA2009101812509A CN101602047A (en) 2009-07-21 2009-07-21 A kind of coating process of solar battery backing plate binder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNA2009101812509A CN101602047A (en) 2009-07-21 2009-07-21 A kind of coating process of solar battery backing plate binder

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CN101602047A true CN101602047A (en) 2009-12-16

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102553791A (en) * 2010-12-24 2012-07-11 无锡尚德太阳能电力有限公司 Surface treatment method and device for solar cell assembly back plate
CN102937476A (en) * 2012-11-17 2013-02-20 汕头市鑫瑞纸品有限公司 Online coating weight monitoring method
CN103846189A (en) * 2012-12-04 2014-06-11 明冠能源(江西)有限公司 Environment-friendly precise coating method
CN114950871A (en) * 2022-06-17 2022-08-30 中山市松鸿机械设备有限公司 Non-contact hot melt adhesive film laminating system and film laminating method thereof

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102553791A (en) * 2010-12-24 2012-07-11 无锡尚德太阳能电力有限公司 Surface treatment method and device for solar cell assembly back plate
CN102937476A (en) * 2012-11-17 2013-02-20 汕头市鑫瑞纸品有限公司 Online coating weight monitoring method
CN102937476B (en) * 2012-11-17 2015-04-15 广东鑫瑞新材料科技有限公司 Online coating weight monitoring method
CN103846189A (en) * 2012-12-04 2014-06-11 明冠能源(江西)有限公司 Environment-friendly precise coating method
CN114950871A (en) * 2022-06-17 2022-08-30 中山市松鸿机械设备有限公司 Non-contact hot melt adhesive film laminating system and film laminating method thereof

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Open date: 20091216