A kind of isolation of banbury film and blow-drying system
Technical field
The utility model relates to the banburying operation field of rubber tyre, exactly refers to a kind of isolation and blow-drying system of banbury film.
Background technology
At present, in tire banburying operation, the compressed-air actuated conventional process techniques of freeze drying is generally adopted in the isolation of film.Compressed air stirs the interleaving agent pond after freeze drying, accelerates the speed of stirring by the increase of tolerance, thereby improves the concentration of interleaving agent.Because tradition is isolated and dried up mode energy consumption height, wet weather can't satisfy technological requirement.Interleaving agent concentration is low under the normal temperature, satisfy technological requirement and must continue to increase gas consumption, causes energy consumption higher.Because the compressed air temperature after the freeze drying is low, is unfavorable for the dissolving of interleaving agent, winter and summer temperature differ larger, the bad assurance of the addition of interleaving agent, interleaving agent can not all dissolve sometimes, being deposited in the film surface affects film quality.
Film is coating frame behind the interleaving agent pond, and it is air-dry to utilize natural wind to carry out, but wet season, film often can not blow to be done, and also has the interleaving agent of pasty state to be bonded on the film before lamination.Natural wind dries up limited in one's ability to film, the wet season film often can not blow to be done, and affects film quality, can't reach technological requirement.
The utility model content
For defects, the technical problem that the utility model solves is to provide a kind of isolation and blow-drying system of banbury film, can improve interleaving agent concentration, interleaving agent is evenly distributed on the film, improve film isolation quality, and can dry up the moisture in the interleaving agent on the film, improve film quality; Energy-conserving and environment-protective.
In order to solve above technical problem, isolation and the blow-drying system of the banbury film that the utility model provides comprise film interrupter and film dry body, wherein:
Described film interrupter comprises hot pressing air-source, interleaving agent stirring pool, interleaving agent pond, coil pipe and transmission device, described hot pressing air-source is connected with described coil pipe by the first control valve, offer a plurality of ventholes on the described coil pipe, described coil pipe is placed in the described interleaving agent stirring pool; Described interleaving agent stirring pool is connected with described interleaving agent pond by pipeline, is provided with tubing pump on the described pipeline, and described tubing pump arrives the interleaving agent pump of interleaving agent stirring pool in the described interleaving agent pond; Described transmission device comprises the first roller and cylinder, and described the first roller is by the transmission of bandage realization film, and described cylinder is arranged in the described interleaving agent pond, and described cylinder is compressed on described film below the liquid level in described interleaving agent pond;
Described film dry body comprises film transport machine and blowing shower nozzle, described film transport machine is by the second roller and Belt Conveying film, described blowing shower nozzle is communicated with the hot pressing air-source, the quantity of described blowing shower nozzle has two, the front end that blowing shower nozzle is arranged on described film transport machine dries up the front of film, and the rear end that another blowing shower nozzle is arranged on described film transport machine dries up the back side of film.
Preferably, described film interrupter also comprises temperature probe and controller, described temperature probe is arranged in the described interleaving agent stirring pool, and described temperature probe is connected with described controller, and described controller and described the first control valve are connected and control the aperture of described the first control valve.
Preferably, described controller comprises numerical control table and electropneumatic transducer, connects between described numerical control table and the described electropneumatic transducer, and described numerical control table is connected with described temperature probe, and described electropneumatic transducer is connected with described the first control valve.
Preferably, described hot pressing air-source comprises air compressor and high temperature air accumulator, described coil pipe be connected the blowing shower nozzle and be connected with described high temperature air accumulator by pipeline respectively.
Preferably, be provided with filter on the connecting pipeline between described tubing pump and the described interleaving agent stirring pool.
Preferably, described coil pipe is tortuous the extension in the horizontal direction, and described venthole evenly is arranged on the described coil pipe.
Preferably, described film transport machine is provided with hold-down roller, and described hold-down roller presses the film on the described film transport machine.
Preferably, be provided with the second control valve on described blowing shower nozzle and the pipeline that described hot pressing air-source is connected, be provided with magnetic valve on the connecting line between described the second control valve and the described blowing shower nozzle.
Preferably, described blowing shower nozzle is provided with the blowing opening at length direction, and the width distance of described blowing opening and film is suitable.
Compared with prior art, isolation and the blow-drying system of the banbury film that the utility model provides, the film interrupter is by passing into the hot pressing air to the interleaving agent stirring pool, utilize the heat of hot pressing air self to heat to the interleaving agent stirring pool, improved the temperature of blowing, can improve interleaving agent concentration, interleaving agent is evenly distributed on the film, improve film isolation quality; The film dry body utilizes the heat of hot pressing air self to dry up moisture in the isolation, can reach fast to dry up purpose, reduces gas consumption, improves film quality; Energy-conserving and environment-protective.
Because the solubility of interleaving agent is different during different temperatures, by measuring and calculating, the concentration of interleaving agent is best to the isolation effect of film in the time of 60 ℃, thus with interleaving agent stirring pool temperature stabilization at 60 ℃.Isolation and the blow-drying system of the banbury film that the utility model provides, the film interrupter also comprises temperature probe and controller, temperature probe is arranged in the interleaving agent stirring pool, temperature probe is connected with controller, controller and the first control valve are connected and control to adjust the aperture of valve, and controller comprises numerical control table and electropneumatic transducer, connects between numerical control table and the electropneumatic transducer, the numerical control table is connected with temperature probe, and electropneumatic transducer is connected with control valve; By temperature probe the temperature of interleaving agent stirring pool is measured, the temperature that records is sent to the numerical control table by signal, set the temperature value of interleaving agent stirring pool plan control at the numerical control table, by the temperature of detection and the temperature of setting are compared, control the air capacity that enters the interleaving agent stirring pool by the first control valve that is installed in hot pressing air inlet end again, thereby reach the purpose of control interleaving agent stirring pool water temperature, make water temperature keep constant always, accurately hold the addition of interleaving agent, guarantee the effect of isolation, improve film quality.
Description of drawings
Fig. 1 is the isolation of banbury film among the utility model embodiment and the overall structure schematic diagram of blow-drying system;
Fig. 2 is the structural representation of film interrupter in the isolation of banbury film among the utility model embodiment and the blow-drying system;
Fig. 3 is the structural representation of coil pipe among Fig. 2;
Fig. 4 is the structural representation of film dry body in the isolation of banbury film among the utility model embodiment and the blow-drying system.
The specific embodiment
For those skilled in the art can understand technical scheme provided by the utility model better, set forth below in conjunction with specific embodiment.
See also Fig. 1-Fig. 4, Fig. 1 is the isolation of banbury film among the utility model embodiment and the overall structure schematic diagram of blow-drying system; Fig. 2 is the structural representation of film interrupter in the isolation of banbury film among the utility model embodiment and the blow-drying system; Fig. 3 is the structural representation of coil pipe among Fig. 2; Fig. 4 is the structural representation of film dry body in the isolation of banbury film among the utility model embodiment and the blow-drying system.
Isolation and the blow-drying system of the banbury film that the utility model embodiment provides, comprise film interrupter 1 and film dry body 2, film 17 through after the film interrupter 1 dipping interleaving agent, is drying up the moisture in the interleaving agent by film dry body 2 first.
Film interrupter 1 comprises hot pressing air-source, interleaving agent stirring pool 11, interleaving agent pond 13, coil pipe 12 and transmission device, the hot pressing air-source is connected with coil pipe 12 by the first control valve 19, offer a plurality of ventholes 114 on the coil pipe 12, coil pipe 12 is placed on that interleaving agent stirring pool 11 is interior to be controlled at 60 ℃ with the fluid temperatures in the interleaving agent stirring pool 11; Interleaving agent stirring pool 11 is connected with interleaving agent pond 13 by pipeline, is provided with tubing pump 111 on the pipeline, tubing pump 111 with the interleaving agent pump of interleaving agent stirring pool 11 in interleaving agent pond 13; Transmission device comprises that the first roller 15 and cylinder 14, the first rollers 15 pass through the transmission that bandage 16 is realized films 17, and cylinder 14 is arranged in the interleaving agent pond 13, and cylinder 13 is compressed on film 17 below the liquid level in interleaving agent pond 13.
Film interrupter 1 also comprises temperature probe 18 and controller, and temperature probe 18 is arranged in the interleaving agent stirring pool 11, and temperature probe 18 is connected with controller, and controller and the first control valve 19 are connected and control the aperture of the first control valve 19.Controller comprises numerical control table 112 and electropneumatic transducer 113, connects between numerical control table 112 and the electropneumatic transducer 113, and numerical control table 112 is connected with temperature probe 18, and electropneumatic transducer 113 is connected with the first control valve 19.
The hot pressing air-source comprises air compressor 3 and high temperature air accumulator 4, and coil pipe 12 is connected with high temperature air accumulator 4 by pipeline respectively with the shower nozzle 22 of being connected.Be provided with filter 110 on the connecting pipeline between tubing pump 111 and the interleaving agent stirring pool 11.Coil pipe 12 is tortuous the extension in the horizontal direction, and venthole 114 evenly is arranged on the coil pipe 12, can more equably the liquid in the interleaving agent stirring pool 11 be heated and stir.
Film dry body 2 comprises film transport machine 21 and blowing shower nozzle 22, film transport machine 21 is carried film by the second roller 23 and belt 24, blowing shower nozzle 22 is communicated with the hot pressing air-source, the quantity of blowing shower nozzle 22 has two, the front end that blowing shower nozzle is arranged on film transport machine 21 dries up the front of film 17, and the rear end that another blowing shower nozzle is arranged on film transport machine 21 dries up the back side of film 17.
Film transport machine 21 is provided with hold-down roller 27, and hold-down roller 27 presses the film 17 on the film transport machine 21, can make film 17 more smooth, and interleaving agent distributes more even.
Be provided with the second control valve 25 on blowing shower nozzle 22 and the pipeline that the hot pressing air-source is connected, control the flow of hot pressing air by the second control valve 25 adjusting apertures; Be provided with magnetic valve 26 on the connecting line between the second control valve 25 and the blowing shower nozzle 22, by the switch of control valve 26 control blowing shower nozzles 22 blowings.
Blowing shower nozzle 22 is provided with the blowing opening at length direction, and the width distance of blowing opening and film 17 is suitable, film integral body on width can be dried up.
Particularly, the hot pressing air that the isolation of the banbury film that the utility model provides and blow-drying system use is out without the compressed air that cools off (about 180 ° of C) from air compressor, through over-heat-exchanger climate comfort to 100 ° C, deliver to the high temperature air accumulator, from high temperature air accumulator compressed air out through overregulating decompression, pressure drops to 0.4MPa by 0.7~0.8MPa, arrives about 80 ° of C of workshop board temperature again.Out lay one tunnel snorkel that insulation Φ 100mm is arranged to the workshop from the high temperature air accumulator, reducing Φ 50mm is to each board again, the coil pipe that divides again two-way to divide behind the board to be clipped in the interleaving agent stirring pool and the blowing shower nozzle in the film dry body.The interleaving agent stirring pool is installed temperature control system, and interleaving agent pond water temperature is constant in 60 ° of C, and interleaving agent concentration obtains raising, interleaving agent is evenly distributed on the film, in addition, because higher without the compressed air temperature of cooling, film water mark is dried up rapidly, and gas consumption greatly reduces.
Compared with prior art, isolation and the blow-drying system of the banbury film that the utility model provides, the film interrupter is by passing into the hot pressing air to the interleaving agent stirring pool, utilize the heat of hot pressing air self to heat to the interleaving agent stirring pool, improved the temperature of blowing, can improve interleaving agent concentration, interleaving agent is evenly distributed on the film, improve film isolation quality; The film dry body utilizes the heat of hot pressing air self to dry up moisture in the isolation, can reach fast to dry up purpose, reduces gas consumption, improves film quality; Energy-conserving and environment-protective.
Because the solubility of interleaving agent is different during different temperatures, by measuring and calculating, the concentration of interleaving agent is best to the isolation effect of film in the time of 60 ℃, thus with interleaving agent stirring pool temperature stabilization at 60 ℃.Isolation and the blow-drying system of the banbury film that the utility model provides, by temperature probe the temperature of interleaving agent stirring pool is measured, the temperature that records is sent to the numerical control table by signal, set the temperature value of interleaving agent stirring pool plan control at the numerical control table, by the temperature of detection and the temperature of setting are compared, control the air capacity that enters the interleaving agent stirring pool by the first control valve that is installed in hot pressing air inlet end again, thereby reach the purpose of control interleaving agent stirring pool water temperature, make water temperature keep constant always, accurately hold the addition of interleaving agent, guarantee the effect of isolation, improve film quality.
To the above-mentioned explanation of the disclosed embodiments, make this area professional and technical personnel can realize or use the utility model.Multiple modification to these embodiment will be apparent concerning those skilled in the art, and General Principle as defined herein can in the situation that does not break away from spirit or scope of the present utility model, realize in other embodiments.Therefore, the utility model will can not be restricted to these embodiment shown in this article, but will meet the widest scope consistent with principle disclosed herein and features of novelty.