CN203776146U - Device for producing reconstituted tobacco in dry paper-making method - Google Patents
Device for producing reconstituted tobacco in dry paper-making method Download PDFInfo
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- CN203776146U CN203776146U CN201420188214.1U CN201420188214U CN203776146U CN 203776146 U CN203776146 U CN 203776146U CN 201420188214 U CN201420188214 U CN 201420188214U CN 203776146 U CN203776146 U CN 203776146U
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Abstract
The utility model relates to a device for producing reconstituted tobacco in a dry paper-making method. The device for producing reconstituted tobacco in the dry paper-making method comprises a fiber decomposing device, a substrate forming device, a pulp spraying device and a drying device which are all connected in sequence. The device for producing reconstituted tobacco in the dry paper-making method is provided with a plurality of material connectors and a built-in pipeline humidifying part, wherein a plurality of pipelines are adopted for feeding, and therefore feeding is even, the controllability is improved, the sprayed pulp contains much tobacco powder, tobacco extract and adhesive, the viscosity is large, the pulp can be fully dispersed through the device for producing reconstituted tobacco in the dry paper-making method, and it can be avoided that because hot air in a drying box flows and is distributed unevenly, part of tobacco is over-dried.
Description
It is on March 7th, 2014 that the utility model requires the applying date, application number is the substrate shaped device that a kind of dry method of paper-making method of the Chinese utility model application of CN2014201047053 is produced reconstituted tobacco, the applying date is on March 7th, 2014, application number is the drying unit that a kind of dry method of paper-making method of the Chinese utility model patent application of CN2014201040533 is produced reconstituted tobacco, the applying date is on March 10th, 2014, application number is the fiber decomposition device that a kind of dry method of paper-making method of the Chinese utility model patent application of CN2014201062509 is produced reconstituted tobacco, the applying date is on March 10th, 2014, application number is the pulp spraying coating device produced of a kind of dry method of paper-making method of Chinese utility model patent application reconstituted tobacco of CN2014201067199 totally four priority.
[technical field]
The utility model relates to the equipment of a tobacco articles, and particularly a kind of dry method of paper-making legal system is made production line and the relevant equipment of reconstituted tobacco.
[background technology]
Reconstituted tobacco is that reconstituted tobacoo claims again recombination tobacco leaf, homogeneous tobacco leaf, mainly by offal fragment, offal or discarded tobacco leaf, and additional part external source fiber, adhesive and other additives form.Reconstituted tobacco has now been widely used in production of cigarettes as tobacco product raw material, has cost low, and fillibility is good, and can reduce the feature such as tar content in flue gas.The manufacture of reconstituted tobacco starts from the 1950's, and manufacture method mainly contains thick slurry method, roll-in method and paper process, and paper process is divided into again wet papermaking method and dry method of paper-making method.But no matter be wet papermaking method or dry method of paper-making method, all must separate string pulpboard fine, in order to moulding, wet papermaking method is by after pulpboard fragmentation with hydrabrusher, in water, with one-level fiberizer, secondary grinding pulp grinder, fiber is carried out to appropriateness and grind, make fiber be single shape, after beating brooming, be dispersed in water form slurry, again through high concentration desanding device and jordan, slurry is placed in to copy front stock tank standby.Dry method of paper-making rule is directly fine without hydrolysis in air, conventionally uses dials, hammer slice type, toothed disc type or second patent flour crushing device, fiber is resolved into single shape in High Rotation Speed.
Through vicennial research and use, this technology has also obtained certain development, is widely used in cigarette products.But also there is certain defect.The one, the operations such as the extraction of tobacco-containing material, concentrated, defibrination, in process, the fragrant loss of smoke and cigarette is obviously.The 2nd, reconstituted tobacco structural slab reality, smooth surface that this method is produced, the spreading rate of tobacco material is low, and general less than 40%, has certain mouthfeel defect.The 3rd, in production process, contain a large amount of sewage discharges.The deficiency existing for conventional wet papermaking-method reconstituted tobaccos, advocates under the overall background that reduces environmental pollution and reducing tar and reducing harm especially at home, and a kind of new technology and device that can improve reconstituted tobacco quality and reduce environmental pollution is all being groped in this area.
A kind of brand-new employing dry method of paper-making legal system is for the equipment of reconstituted tobacco, not only can overcome the environmental pollution that in traditional reconstituted tobacco production process, a large amount of sewage discharges causes, also can effectively avoid the loss of the smoke cigarette taste in reconstituted tobacco production, spreading rate reaches the more than 200 percent of substrate, filling value and wet strength all increase, and reducing tar and reducing harm function is also better than traditional papermaking-method reconstituted tobaccos.
Dry method of paper-making sources of law are the sixties, and the end of the eighties, domestic this technology of having introduced, passed through vicennial development, and Paper DryForming Technology has obtained good development, has been a very ripe technology, is also known technology.The disclosed a kind of air lay dry-papermaking machine of Chinese patent application CN200610117771.4 for example.Domestic also have a patent, and application Paper DryForming Technology is manufactured the self-contained production line of reconstituted tobacco, number of patent application CN201310393610.8.Its equipment is as broad as long with common dry method of paper-making machine equipment and production technology, just many two glue sprayings and drying unit, do not produce the special device of reconstituted tobacco, special do not have for relevant apparatus such as the solution fibre of producing reconstituted tobacco specific (special) requirements, moulding, coating, oven dry.Well-known common wet papermaking machine can not directly be used for producing reconstituted tobacco, need be according to reconstituted tobacco characteristic, and design is installed accordingly to adapt to the production of reconstituted tobacco.Equally, common dry method of paper-making machine is to be directly used for producing reconstituted tobacco, also needs according to the characteristic Design of reconstituted tobacco or increase to install to adapt to the production of reconstituted tobacco accordingly.
[utility model content]
In order to overcome above-mentioned defect, the utility model provides a kind of can overcome the defect that wet papermaking legal system is made reconstituted tobacco, can overcome again production line and relevant equipment that existing dry method of paper-making legal system is made reconstituted tobacco equipment deficiency.
The utility model provides a kind of dry method of paper-making method to produce the equipment of reconstituted tobacco, comprise the fiber decomposition device connecting successively, substrate shaped device, pulp spraying coating device and drying unit, wherein, described fiber decomposition device comprises connected successively primary mill 101, primary mill 102, fiber storage tank 103 and the fine machine 104 of meter, the front end of described primary mill 101 is material inlets, the material outlet of the fine machine 104 of described meter is connected to the shaped device that dry method of paper-making method is produced reconstituted tobacco, it is characterized in that described fiber decomposition device also comprises antistatic damping device, described antistatic damping device comprises highly humid air generator 105 and highly humid air pipeline, the output of described highly humid air generator 105 is connected to the material inlet of primary mill 101 and the material outlet of the fine machine 104 of meter by highly humid air pipeline respectively,
Described substrate shaped device comprises moulding guipure, net belt conveying apparatus, be arranged on the substrate shaped device frame 218 on moulding guipure top, in substrate shaped device frame 218, be provided with one or more groups moulded head, in described moulded head, there is air-supply arrangement, be arranged on the negative pressure device of guipure bottom, every composing type head has symmetrically arranged the first screen drum 213 and the second screen drum 214, in the first screen drum 213, prolong axial length direction and be provided with the first fibre conveying channel 201 and the second fibre conveying channel 202, in the second screen drum 214, prolong axial length direction and be provided with the 3rd fibre conveying channel 203 and the 4th fibre conveying channel 204, the first fibre conveying channel 201 and the second fibre conveying channel 202 are arranged on the first half in the first screen drum 213 symmetrically, the 3rd fibre conveying channel 203 and the 4th fibre conveying channel 204 are arranged on the first half in the second screen drum 214 symmetrically, Lower Half in the first screen drum 213 and the second screen drum 214 is provided with respectively first and breaks up roller 212 and second and break up roller 211, first breaks up roller 212 and second breaks up roller 211 and lays respectively under the first screen drum 213 and second screen drum 214 centers of circle, front and rear at the first screen drum 213 and the second screen drum 214 is respectively equipped with the 215He Hou circular passage, front circular passage 216 that is communicated with screen drum inner space,
Described pulp spraying coating device comprises the constant slurry dispenser 322 to pressing storage tank 305, being connected with the constant material outlet to pressing storage tank 305, described slurry dispenser 322 has a plurality of slurry outlets 324, each slurry outlet 324 is connected to slurry buffer 314 by measuring pump 325 respectively, described slurry buffer 314 is connected to the slurry import 329 of binary nozzle 328 by stop valve 319, described binary nozzle 328 also has compressed air inlet 330, and compressed air pressure regulating valve 331 is connected to compressed air inlet 330 by pipeline; Described pulp spraying coating device also comprises the spray equipment frame 304 being erected on guipure, spray equipment frame 304 both sides are provided with install bin 301, slurry dispenser 322 and measuring pump 325 are arranged in install bin 301, slurry buffer 314 is arranged on the slurry buffer fixed mount 334 at spray equipment frame 304 middle parts, described spray equipment frame 304 middle parts are also provided with nozzle fixed mount 332, nozzle fixed mount 332 is provided with the many nozzle fixed mounts 333 that length angle is adjustable, and binary nozzle 328 is arranged on nozzle fixed mount 333.
Drying unit, comprise baking oven casing, the hot-air air inlet 411 being connected with described baking oven casing, it is characterized in that being provided with in described baking oven casing three fixing the first even windshield plate 402 of even windshield plate 401, second and the 3rd even windshield plates 403, described three even windshield plates are arranged in parallel, spacing is identical between adjacent two even windshield plates, described three even windshield plates are arranged in described baking oven casing, join with hot-air air inlet 411, every even windshield plate tail end is respectively equipped with adjustable baffle plate, and the rear portion of described baking oven casing is also provided with forces humidity-discharging device 407.
In the utility model, primary mill 101 front portions of described fiber decomposition device also have independently material interface, described material interface comprises fiberous material interface 112 and granular material interface 113, and described fiberous material interface 112 and granular material interface 113 are respectively equipped with independently switching device.
Preferably, the material inlet of the primary mill 101 of described fiber decomposition device is provided with flexible connection, the movable barrier of detachable multichannel.
More preferably, the first screen drum 213 of described substrate shaped device is contrary with the direction of rotation of the second screen drum 214.
According to another kind of preferred embodiment, every group of screen drum of described substrate shaped device is contrary with the direction of rotation of breaing up roller in being arranged on this screen drum.
In the utility model, the length of the first fibre conveying channel 201 of described substrate shaped device is identical with the length of the 4th fibre conveying channel 204, the length of the second fibre conveying channel 202 is identical with the length of the 3rd fibre conveying channel 203, and the length of the first fibre conveying channel 201 is greater than the length of the second fibre conveying channel 202; The first fibre conveying channel 201 and the second fibre conveying channel 202 are from the first screen drum 213 front portions to the interior extension of the first screen drum 213, and the 3rd fibre conveying channel 203 and the 4th fibre conveying channel 204 are from the first screen drum 213 rear portions to the interior extension of the first screen drum 213
Preferably, the slurry buffer fixed mount 334 of described pulp spraying coating device is " ︺ " type.
More preferably, described pulp spraying coating device constant give to press storage tank 305 comprise tank body, be located at described tank base slurry outlet 313, be located at described tank body upper side slurry import 312, be located at the agitator 306 of tank interior, describedly constantly give to press storage tank 305 also to there is pressure display unit 307, be arranged on overpressure safety valve 308, constant-voltage controller 309 and the compressed air pressure regulating valve 310 on described tank body top, on tank body top, also there is the stirring motor 311 being connected with agitator 306.
In the utility model, the slurry buffer 314 of described pulp spraying coating device has buffer slurry import 317 and buffer slurry outlet 318, buffer slurry import 317 is located at slurry buffer 314 sides, middle and lower part, buffer slurry outlet 318 is located at slurry buffer 314 bottoms, and described slurry buffer 314 tops are also provided with purge valve 315 and pressure display unit 316.
In the utility model, between the adjustable baffle plate of described drying unit and described even windshield plate, by removable pin, be connected, between described adjustable baffle plate and described even windshield plate, there is angle adjustable.
Preferably, the pressure humidity-discharging device 407 of described drying unit comprises negative pressure box 409, is arranged on the moisture deflector 408 in negative pressure box 409, described negative pressure box 409 communicates with described baking oven casing, and is connected to negative-pressure air fan 410 by pipeline, and negative-pressure air fan is connected with frequency converter controller.
More preferably, the first even windshield plate 402 of even windshield plate 401, second of described drying unit and the baffle length of the 3rd even windshield plate 403 have equal difference relation, and described oven dry bellows are divided into four parts.
Below explain in more detail the technical solution of the utility model.
Dry method of paper-making method is produced the equipment of reconstituted tobacco, comprises the fiber decomposition device, substrate shaped device, pulp spraying coating device and the drying unit that connect successively.Wherein, the solution fibre of string pulpboard is the first working procedure that dry method of paper-making method reconstituted tobacco is produced, but there is defect in the production line of the existing dry method of paper-making, for mouthfeel, need on the one hand, in separating fine step, often to through metering, carry the moulding that feeds intake with two or more strings simultaneously, make the substrate that contains multiple fiber; According to dry method of paper-making method, produce the special type of reconstituted tobacco simultaneously, be necessary to reduce the external source fiber content in substrate through amount, need to when separating fibre, add fibrous or granular tobacco, separate fibre with string simultaneously, make the substrate containing the less dry process reproduction tobacco leaf of external source fiber, and the fiber decomposition device of existing dry method of paper-making method can only be separated to single fiber of planting fine; Electrostatic problem on the other hand, because dry method solution fibre is to carry out in air, fiber can produce static in the rotation of air high speed and friction, the accumulation of static electricity of fiber surface is too much, can form reunion shape, affect dispersion, conveying and the moulding of fiber, conventionally more outstanding at ambient humidity electrostatic phenomenon lower than 50% time, until cause normally producing.
For this reason, in production equipment of the present utility model, fiber decomposition device comprises connected successively primary mill 101, advanced mill 102, fiber storage tank 103 and the fine machine 104 of meter, the front end of described primary mill 101 is material inlets, the material outlet of the fine machine 104 of described meter is connected to the shaped device that dry method of paper-making method is produced reconstituted tobacco, wherein, described fiber decomposition device also comprises antistatic damping device, described antistatic damping device comprises highly humid air generator 105 and highly humid air pipeline, the output of described humid air generator 105 is connected to the material inlet of primary mill 101 and the material outlet of the fine machine 104 of meter by highly humid air pipeline respectively.
The front portion of described primary mill 101 also has independently material interface, and described material interface comprises fiberous material interface 112 and granular material interface 113, and described fiberous material interface 112 and granular material interface 113 are respectively equipped with independently switching device.
Preferably, the material interface of primary mill 101 can have more than two.
Two groups (or more than) independently charging interface is set in the side of primary mill, extra fiberous material or the granular material adding of need can be added in primary mill by these interfaces, rotor through primary mill together with the string pulpboard feeding from material inlet is broken into the approximately sheet of 1～2cm2 of area, in tablet, can be mixed with fibrous and granular material, by advanced mill fluted disc solution is fine, disperse again, enter storage tank, by agitator in tank, evenly mix, through counting fine machine metering, be delivered to fiberizing portion.The inlet amount of above-mentioned each interface, by VFC, is set up the correlation module of charging rate and inlet amount, makes the proportioning of several different fibers meet the technique initialization requirement of dry process reproduction tobacco leaf substrate.
Particularly preferably, the material inlet of primary mill 101 is provided with flexible connection, the movable barrier of detachable multichannel.
By the material inlet place at primary mill, the movable barrier of multichannel is set, different string pulpboards can be sent into respectively to primary mill by each individual passage and separate fibre simultaneously, operation is convenient.When only needing single Plants fiber board solution fine, dismountable movable barrier.
In the utility model, highly humid air generator can adopt high pressure nozzle or ultrasonic atomizer.Preferably, at the fore side of separating fine system, highly humid air generator is set, its volume is 1m
3, the humid air of abundant atomization is provided with high pressure nozzle or ultrasonic atomizer, its humidity remains on more than 80%.The outlet of highly humid air generator is connected to form closed loop with the conveying fan of primary mill material inlet and the metering conveying fan mouth of the fine machine of meter (104) respectively with the PE pipe of Φ 160mm, separating under the effect of fine system negative pressure, by the continual suction of humidifying air, reach the inside humidification effect to the fine induction system of string pulpboard solution.
Papermaking-method reconstituted tobaccos is wet papermaking method reconstituted tobacco, be the first water extraction of low-quality tobacco raw material, the natural fiber of insoluble thing and interpolation enters paper machine after making slurry, manufactures paper with pulp into gauze, after drying, extract and the additive of gauze dipping after concentrated, is finished product after being dried.Papermaking-method reconstituted tobaccos has certain intensity, and filling capacity is also better, adds the tar producing after cigarette also lower, but also has certain disappearance, and its production process has a large amount of sewage discharges, and equipment investment is large, and operating cost is high.
Substrate moulding is the second step that Paper DryForming Technology is produced reconstituted tobacco, its principle is that natural fiber is dispersed in air after separating fibre, by wind, deliver to forming part, in each moulded head, there are two screen drums, screen drum is the cylinder that the whole body is covered with hole, cylinder accumbency is on forming net, the switched in opposite of two screen drums, the pipeline and the nail roller of breaing up fiber that in screen drum, have conveying fiber, the switched in opposite of nail roller and screen drum, the fabric thrashing of being convenient to keep watch and bringing, after fabric thrashing, from the hole of screen drum, fall, descend slowly and lightly on forming net, it below forming net, is a vacuum tank, form negative pressure.Under the protection of negative pressure, form a fibrage, forming net moves forward, and forms the fibrage of continuous uniform, is the substrate of dry method of paper-making method reconstituted tobacco, enters rear road manufacturing procedure.
Substrate shaped device of the present utility model comprises moulding guipure, net belt conveying apparatus, be arranged on the substrate shaped device frame 218 on moulding guipure top, in substrate shaped device frame 218, be provided with one or more groups moulded head, in described moulded head, there is air-supply arrangement, be arranged on the negative pressure device of guipure bottom, every composing type head has symmetrically arranged the first screen drum 213 and the second screen drum 214, wherein, in the first screen drum 213, prolong axial length direction and be provided with the first fibre conveying channel 201 and the second fibre conveying channel 202, in the second screen drum 214, prolong axial length direction and be provided with the 3rd fibre conveying channel 203 and the 4th fibre conveying channel 204, the first fibre conveying channel 201 and the second fibre conveying channel 202 are arranged on the first half in the first screen drum 213 symmetrically, the 3rd fibre conveying channel 203 and the 4th fibre conveying channel 204 are arranged on the first half in the second screen drum 214 symmetrically, Lower Half in the first screen drum 213 and the second screen drum 214 is provided with respectively first and breaks up roller 212 and second and break up roller 211, first breaks up roller 212 and second breaks up roller 211 and lays respectively under the first screen drum 213 and second screen drum 214 centers of circle, front and rear at the first screen drum 213 and the second screen drum 214 is respectively equipped with the 215He Hou circular passage, front circular passage 216 that is communicated with screen drum inner space.
Preferably, the direction of rotation of the first screen drum 213 and the second screen drum 214 is contrary; Every group of screen drum is contrary with the direction of rotation of breaing up roller in being arranged on this screen drum.
More preferably, the length of the first fibre conveying channel 201 is identical with the length of the 4th fibre conveying channel 204, the length of the second fibre conveying channel 202 is identical with the length of the 3rd fibre conveying channel 203, and the length of the first fibre conveying channel 201 is greater than the length of the second fibre conveying channel 202.
Particularly preferably, the first fibre conveying channel 201 and the long 50-60cm of the 4th fibre conveying channel 204, the second fibre conveying channel 202 and the long 30-40cm of the 3rd fibre conveying channel 203.
More preferably, the first fibre conveying channel 201 and the second fibre conveying channel 202 are from the first screen drum 213 front portions to the interior extension of the first screen drum 213, and the 3rd fibre conveying channel 203 and the 4th fibre conveying channel 204 are from the first screen drum 213 rear portions to the interior extension of the first screen drum 213.
In the utility model, in the screen drum of substrate shaped device, can be provided with two above dimension conveyance conduits.
In order further to improve the uniformity coefficient that fiber distributes, can on fibre conveying channel, have a plurality of distribution holes.
In the utility model, by each screen drum inside, two fibre conveying channels being set, and the length of fibre conveying channel is different, has increased fiber outlet, thereby effectively improves the accuracy that fiber is carried;
Circular passage before and after arranging between two screen drums in same moulded head, is communicated with the space in two screen drums, reduces fiber in the accumulation of screen drum two box house.
After substrate shaped device, fibrage forms paper web through precompressed, namely the substrate of reconstituted tobacco.Substrate is on guipure, and by spray equipment, to substrate spraying slurry, during spraying, the reverse side of substrate has negative pressure protection to prevent that substrate from being started with slurry and splashing when spraying, is conducive to the infiltration of slurry in substrate, and quantity for spray is determined as required.Substrate after spraying slurry enters drying baker and dries; bake out temperature is between 105 ℃-110 ℃; substrate after oven dry simultaneously existing slurry applies; substrate is transferred to through guipure the below that net is dried in spraying; by spray equipment, the another side of substrate is sprayed, the reverse side of same spray-coating surface has negative pressure protection again, while preventing substrate spraying, is started and the splashing of slurry; also contribute to the infiltration of slurry in substrate, quantity for spray is determined as required.After spraying, entering drying baker dries; bake out temperature is between 105 ℃-110 ℃; substrate after oven dry is transferred to by guipure the top that net is dried in spraying; again by spray equipment to spraying slurry on substrate; during spraying, the reverse side of spray-coating surface has negative pressure protection, starting and the splashing of slurry while preventing the spraying of substrate.Substrate through four sprayings and oven dry has become reconstituted tobacco, through transmitting net, reconstituted tobacco is introduced to tablet machine, breaks into a certain size tablet through tablet machine, is the final finished of reconstituted tobacco.
Pulp spraying coating device in production equipment of the present utility model comprises constant in pressing storage tank 305, the slurry dispenser 322 being connected with the constant material outlet to pressing storage tank 305, wherein, described slurry dispenser 322 has a plurality of slurry outlets 324, each slurry outlet 324 is connected to slurry buffer 314 by measuring pump 325 respectively, described slurry buffer 314 is connected to the slurry import 329 of binary nozzle 328 by stop valve 319, described binary nozzle 328 also has compressed air inlet 330, compressed air pressure regulating valve 331 is connected to compressed air inlet 330 by pipeline,
Described pulp spraying coating device also comprises the spray equipment frame 304 being erected on guipure, spray equipment frame 304 both sides are provided with install bin 301, slurry dispenser 322 and measuring pump 325 are arranged in install bin 301, slurry buffer 314 is arranged on the slurry buffer fixed mount 334 at spray equipment frame 304 middle parts, described spray equipment frame 304 middle parts are also provided with nozzle fixed mount 332, nozzle fixed mount 332 is provided with the many nozzle fixed mounts 333 that length angle is adjustable, and binary nozzle 328 is arranged on nozzle fixed mount 333
Preferably, slurry buffer fixed mount 334 is " ︺ " types.
Constant give to press storage tank 305 comprise tank body, be located at described tank base slurry outlet 313, be located at described tank body upper side slurry import 312, be located at the agitator 306 of tank interior, describedly constantly give to press storage tank 305 also to there is pressure display unit 307, be arranged on overpressure safety valve 308, constant-voltage controller 309 and the compressed air pressure regulating valve 310 on described tank body top, on tank body top, also there is the stirring motor 311 being connected with agitator 306.
More preferably, slurry buffer 314 has buffer slurry import 316 and buffer slurry outlet 318, buffer slurry import 316 is located at slurry buffer 314 sides, middle and lower part, buffer slurry outlet 318 is located at slurry buffer 314 bottoms, and described slurry buffer 314 tops are also provided with purge valve 315 and pressure display unit 316.
In the utility model, measuring pump 325 can be screw metering pump, peristaltic meatering pump or diaphragm metering pump, can use the measuring pump of single a type, also can mix use.
In the utility model, the slurry outlet 324 of slurry dispenser 322 has 4-8.By slurry dispenser, can constant giving press storage tank can be connected to many group spray bodies, realize stable, synchronously spraying.
Preferably, at the interior two groups of nozzle fixed mounts 332 that symmetry is set of install bin 301, every group of nozzle fixed mount 332 is at its arranged outside 4-10 group nozzle fixed mount 333.
In the utility model, stop valve 319 can be angle pedestal valve, electric check valve or pneumatic stopping valve, can use the valve of single a type, also can mix use.
Preferably, install bin 301 bottoms are provided with and connect glue device 303, described connect glue device 303 comprise connect glue groove and be arranged on described in connect and connect glue baffle plate on glue groove, described connecing on glue baffle plate, be provided with Frictioning device, described Frictioning device comprises drive motors, the spreading roller being connected with described drive motors, is located at the rubber plate of described spreading roller end.
Drying unit of the present utility model comprises baking oven casing, the hot-air air inlet 411 being connected with described baking oven casing, wherein, in described baking oven casing, be provided with three the first fixing even windshield plates 401, the second even windshield plate 402 and the 3rd even windshield plate 403, described three even windshield plates are arranged in parallel, between adjacent two even windshield plates, spacing is identical, described three even windshield plates are arranged in described baking oven casing, join with hot-air air inlet 411, every even windshield plate tail end is respectively equipped with adjustable baffle plate, the rear portion of described baking oven casing is also provided with forces humidity-discharging device 407.
Between wherein said adjustable baffle plate and described even windshield plate, by removable pin, be connected, between described adjustable baffle plate and described even windshield plate, there is angle adjustable.Preferably there are angle 60 degree-150 degree.
In the utility model, described even windshield plate can have three or more than.
Preferably, in the utility model, to force humidity-discharging device 407 to connect two groups of identical drying units.
Force humidity-discharging device 407 to comprise negative pressure box 409, be arranged on the moisture deflector 408 in negative pressure box 409, described negative pressure box 409 communicates with described baking oven casing, and is connected to negative-pressure air fan 410 by pipeline, and negative-pressure air fan is connected with frequency converter controller.
Preferably, in the utility model, the baffle length of the first even windshield plate 402 of even windshield plate 401, second and the 3rd even windshield plate 403 has equal difference relation; The length of three adjustable baffle plate is different, and the baffle length of adjacent adjustable baffle plate has equal difference relation, and described oven dry bellows are divided into four parts.
More preferably, the spacing between three even windshield plates is 8-15cm.
The utility model by arranging three (or more than three) fixing even windshield plate of length equal difference in baking oven, three even windshield plates are connected with removable pin with adjustable baffle plate respectively, regulate according to actual needs in process of production the angle between fixing even windshield plate and adjustable baffle plate.
Pressure humidity-discharging device is arranged between every two groups of baking ovens, by be provided with deflector, negative pressure box in forcing humidity-discharging device, negative pressure box is connected with negative-pressure air fan by pipeline, the air quantity of negative-pressure air fan is by Frequency Converter Control, forms oven dry, hydrofuge, dries, low temperature, the flash baking system of hydrofuge again.
Compared with prior art, the utlity model has following beneficial effect:
1, fiber decomposition device has various materials interface and built-in pipe humidification: A, has overcome the defect that prior art is used Single Fiber raw material, uses multiple fiber and add partial material to make the mouthfeel of reconstituted tobacco get a promotion.The generation of static in fine process is understood in B, reduction, has overcome in the fine process of prior art solution and has added antistatic additive disappearance, has avoided the mouthfeel impact of antistatic additive on reconstituted tobacco.
2, the shaped device of low grammes per square metre is compared with prior art: A, overcome prior art feed pipe unicity, adopt multi-pipeline feeding to make charging uniformity, controllability is improved, B, circular passage prevents that fiber is in the accumulation of casing compared to existing technology, make the reconstituted tobacco substrate good uniformity of moulding, C, the grammes per square metre of the paper that existing Paper DryForming Technology is produced is in 40g/ ㎡ left and right, be difficult to reach below 40g/ ㎡, the utility model device is because fibre metering conveying capacity has accurately improved controlled, in fiber course of conveying, at conveyance conduit, be evenly distributed, the even wind of upper air-supply is good, negative pressure box body is handling good, negative pressure is evenly adjustable, directly make the substrate grammes per square metre of moulding be less than 20g/ ㎡.
3, the spray equipment of high viscosity, high solids content compared with prior art: the solid content of the glue of A, the spraying of prior art glue liquid spray coating device is in 6% left and right, the slurry solid content of this device spraying is more than 15%, poor fluidity, use device of the present utility model to make the slurry that solid content is higher reach sufficient dispersion, and can reach the effect of accurate measurement.B, overcome the defect that existing Paper DryForming Technology spray equipment can only spray the sizing material that viscosity is lower, the slurry of the utility model device spraying contains more tobacco powder, tobacco extract and adhesive, viscosity is large, uses this device can make slurry fully be disperseed.C, use spray equipment of the present utility model also to overcome prior art spreading rate to only have 40% defect (in the utility model, spreading rate should be understood to the weightening finish of substrate after coating, oven dry, and the weight of increase is spreading rate with respect to the ratio of original substrate.This index belongs to the computational methods of tobacco material content in reconstituted tobacco, is also an important index of reconstituted tobacco), spray equipment spreading rate of the present utility model can arrive more than 80%, and coating weight can reach the more than 200 percent of substrate.
4, the drying unit that low temperature forced-ventilated is wet is compared with prior art: in the paper web that A, existing Paper DryForming Technology are dried, moisture is lower, and the drying baker that drying efficiency is low also can make material reach drying effect.The moisture that the utility model is dried for reconstituted tobacco reaches the more than seven times of substrate, in order to prevent that tobacco material from losing in drying course, and temperature that again can not unconfined raising drying baker.The utility model adopts the device of forcing hydrofuge, installs strong humidity-discharging device between two baking ovens additional, makes the high speed circulation of air, takes away the moisture in reconstituted tobacco.In B, drying unit, installed guiding device additional, avoided in prior art drying baker without guiding device, hot blast is skewness when internal flow, in the time of can causing whole oven dry, and the phenomenon that part is excessively dried.In drying unit of the present utility model, installed deflector additional, can adjust as required, guaranteed that reconstituted tobacco full width synchronously dries, avoided local high temperature and cause the loss of tobacco flavor and produce burnt roasting peculiar smell.
[accompanying drawing explanation]
Fig. 1 is for separating the front view of fibre and transmission measurement system;
Fig. 2 is the top view of primary mill;
Fig. 3 is substrate shaped device schematic diagram of the present utility model;
Fig. 4 is two schematic diagrames of arranging that send fiber conduit in moulded head;
Fig. 5 is three schematic diagrames of arranging that send fiber conduit in moulded head;
Fig. 6 breaks up roller schematic diagram in moulded head;
Fig. 7 is screen drum and circular passage schematic diagram in moulded head;
Fig. 8 is pulp spraying coating device scheme of installation of the present utility model;
Fig. 9 is frame, install bin part plan structure figure;
Figure 10 is single cover pulp spraying coating device schematic diagram;
Figure 11 is constant in pressing storage tank schematic diagram;
Figure 12 is slurry dispenser schematic diagram;
Figure 13 is measuring pump schematic diagram;
Figure 14 is slurry buffer schematic diagram;
Figure 15 is stop valve schematic diagram;
Figure 16 is binary nozzle schematic diagram;
Figure 17 is compressed air pressure regulating valve schematic diagram;
Figure 18 is binary nozzle scheme of installation;
Figure 19 is for connecing offset plate front view;
Figure 20 is for connecing offset plate top view;
Figure 21 is oven interior structure chart;
Figure 22 is baking oven schematic diagram;
Figure 23 is baking oven top view;
In figure, 101, primary mill; 102, advanced mill; 103, fiber storage tank; 104, count fine machine; 105, highly humid air generator; 106, coarse crushing conveying fan mouth; 107, count fine machine metering conveying fan air inlet; 108, movable barrier; 109, the feeding-passage that movable barrier is divided into; 112, fiberous material interface; 113, granular material interface; 114, primary mill material inlet;
201, the first fibre conveying channel; 202, the second fibre conveying channel; 203, the 3rd fibre conveying channel; 204, the 4th fibre conveying channel; 205, the 5th fibre conveying channel; 206, the 6th fibre conveying channel; 207, the 7th fibre conveying channel; 208, the 8th fibre conveying channel; 209, the 9th fibre conveying channel; 210, the tenth fibre conveying channel; 211, first break up roller; 212, second break up roller; 213, the first screen drum; 214, the second screen drum; 215, front circular passage; 216, rear circular passage; 217, negative pressure box; 218, substrate shaped device frame; 219, guipure;
301, install bin; 302, spray equipment negative pressure box; 303, connect glue device; 304, spray equipment frame; 305, constant giving pressed storage tank; 306, agitator; 307, pressure display unit; 308, overpressure safety valve; 309, constant-voltage controller; 310, compressed air pressure regulating valve; 311, stirring motor; 312, slurry import; 313, slurry outlet; 314, slurry buffer; 315, purge valve; 316, pressure display unit; 317, slurry import; 318; Slurry outlet; 319, stop valve; 320, slurry import; 321, slurry outlet; 322, slurry dispenser; 323, slurry import; 324, slurry outlet; 325, measuring pump; 326, slurry import; 327, slurry outlet; 328, binary nozzle; 329, slurry import; 330, compressed air inlet; 331, compressed air pressure regulating valve; 332, the fixing body frame of nozzle; 333, movable nozzle fixed mount; 334, slurry buffer fixed mount; 335, connect offset plate; 336 rotating shafts; 337, doctor kiss coater; 338, electric rotating machine.
401, the first even wind plate washer; 402, the second even wind plate washer; 403, the 3rd even wind plate washer; 404, the first adjustable baffle plate; 405, the second adjustable baffle plate; 406, the 3rd controllable register; 407, force humidity-discharging device; 408, deflector; 409, negative pressure box; 410, negative-pressure air fan; 411, hot-air air inlet.
[specific embodiment]
Below in conjunction with embodiment, the utility model is further explained.Following examples are for explaining without limitation the technical solution of the utility model.Protection domain of the present utility model should be determined by claims.
Fiber decomposition device as shown in Figure 1-2, comprise connected successively primary mill 101, advanced mill 102, fiber storage tank 103 and count fine machine 104, the front end of described primary mill 101 is material inlets, the material outlet of the fine machine 104 of described meter is connected to the shaped device that dry method of paper-making method is produced reconstituted tobacco, wherein, described fiber decomposition device also comprises highly humid air generator 105 and highly humid air pipeline, and the output of described humid air generator 105 is connected to the material inlet of primary mill 101 and the material outlet of the fine machine 104 of meter by highly humid air pipeline respectively.
The front portion of primary mill 101 has independently material interface, and material interface comprises fiberous material interface 112 and granular material interface 113, and fiberous material interface 112 and granular material interface 113 are respectively equipped with independently switching device.Material inlet is provided with flexible connection, the movable barrier of detachable multichannel.
Two groups of independently charging interfaces are set in the side of primary mill, extra fiberous material or the granular material adding of need can be added in primary mill by these interfaces, rotor through primary mill together with the string pulpboard feeding from material inlet is broken into the approximately sheet of 1～2cm2 of area, in tablet, can be mixed with fibrous and granular material, by advanced mill fluted disc solution is fine, disperse again, enter storage tank, by agitator in tank, evenly mix, through counting fine machine metering, be delivered to fiberizing portion.The inlet amount of above-mentioned each interface, by VFC, is set up the correlation module of charging rate and inlet amount, makes the proportioning of several different fibers meet the technique initialization requirement of dry process reproduction tobacco leaf substrate.
Highly humid air generator, its volume is 1m
3, the humid air of abundant atomization is provided with high pressure nozzle or ultrasonic atomizer, its humidity remains on more than 80%.The outlet of highly humid air generator is connected to form closed loop with the conveying fan of primary mill material inlet and the metering conveying fan mouth of the fine machine 104 of meter respectively with the PE pipe of Φ 160mm, separating under the effect of fine system negative pressure, by the continual suction of humidifying air, reach the inside humidification effect to the fine induction system of string pulpboard solution.
Through separating fine fiber, be admitted to substrate shaped device.As shown in Fig. 3-7, substrate shaped device comprises moulding guipure, net belt conveying apparatus, be arranged on the substrate shaped device frame 218 on moulding guipure top, in substrate shaped device frame 218, be provided with one or more groups moulded head, in described moulded head, there is air-supply arrangement, be arranged on the negative pressure device of guipure bottom, every composing type head has symmetrically arranged the first screen drum 213 and the second screen drum 214, wherein, in the first screen drum 213, prolong axial length direction and be provided with the first fibre conveying channel 201 and the second fibre conveying channel 202, in the second screen drum 214, prolong axial length direction and be provided with the 3rd fibre conveying channel 203 and the 4th fibre conveying channel 204, the first fibre conveying channel 201 and the second fibre conveying channel 202 are arranged on the first half in the first screen drum 213 symmetrically, the 3rd fibre conveying channel 203 and the 4th fibre conveying channel 204 are arranged on the first half in the second screen drum 214 symmetrically, Lower Half in the first screen drum 213 and the second screen drum 214 is provided with respectively first and breaks up roller 212 and second and break up roller 211, first breaks up roller 212 and second breaks up roller 211 and lays respectively under the first screen drum 213 and second screen drum 214 centers of circle, front and rear at the first screen drum 213 and the second screen drum 214 is respectively equipped with the 215He Hou circular passage, front circular passage 216 that is communicated with screen drum inner space.
The direction of rotation of the first screen drum 213 and the second screen drum 214 is contrary; Screen drum is contrary with the direction of rotation of breaing up roller in being arranged on this screen drum.
The length of the first fibre conveying channel 201 is identical with the length of the 4th fibre conveying channel 204, the length of the second fibre conveying channel 202 is identical with the length of the 3rd fibre conveying channel 203, and the length of the first fibre conveying channel 201 is greater than the length of the second fibre conveying channel 202.
The first fibre conveying channel 201 and the second fibre conveying channel 202 are from the first screen drum 213 front portions to the interior extension of the first screen drum 213, and the 3rd fibre conveying channel 203 and the 4th fibre conveying channel 204 are from the first screen drum 213 rear portions to the interior extension of the first screen drum 213.
After substrate shaped device, by spray equipment, to substrate spraying slurry, and dried by drying unit, as shown in Fig. 8-23.Pulp spraying coating device comprises the constant slurry dispenser 322 to pressing storage tank 305, being connected with the constant material outlet to pressing storage tank 305, wherein, described slurry dispenser 322 has a plurality of slurry outlets 324, each slurry outlet 324 is connected to slurry buffer 314 by measuring pump 325 respectively, described slurry buffer 314 is connected to the slurry import 329 of binary nozzle 328 by stop valve 319, described binary nozzle 328 also has compressed air inlet 330, and compressed air pressure regulating valve 331 is connected to compressed air inlet 330 by pipeline.This pulp spraying coating device also comprises the spray equipment frame 304 being erected on guipure, spray equipment frame 304 both sides are provided with install bin 301, constant giving presses storage tank 305, slurry dispenser 322 and measuring pump 325 to be arranged in install bin 301, slurry buffer 314 is arranged on " ︺ " type slurry buffer fixed mount 334 at spray equipment frame 304 middle parts, described spray equipment frame 304 middle parts are also provided with nozzle fixed mount 332, nozzle fixed mount 332 is provided with the many nozzle fixed mounts 333 that length angle is adjustable, and binary nozzle 328 is arranged on nozzle fixed mount 333
Constant give to press storage tank 305 comprise tank body, be located at described tank base slurry outlet 313, be located at described tank body upper side slurry import 312, be located at the agitator 306 of tank interior, describedly constantly give to press storage tank 305 also to there is pressure display unit 307, be arranged on overpressure safety valve 308, constant-voltage controller 309 and the compressed air pressure regulating valve 310 on described tank body top, on tank body top, also there is the stirring motor 311 being connected with agitator 306.
Slurry buffer 314 has buffer slurry import 316 and buffer slurry outlet 318, buffer slurry import 316 is located at slurry buffer 314 sides, middle and lower part, buffer slurry outlet 318 is located at slurry buffer 314 bottoms, and described slurry buffer 314 tops are also provided with purge valve 315 and pressure display unit 316.
The slurry outlet 324 of slurry dispenser 322 has 4.By slurry dispenser, can constant giving press storage tank can be connected to many group spray bodies, realize stable, synchronously spraying.
At the interior two groups of nozzle fixed mounts 332 that symmetry is set of install bin 301, every group of nozzle fixed mount 332 is at 8 groups of nozzle fixed mounts 333 of its arranged outside.
In install bin 301 bottoms, be provided with and connect glue device 303, described connect glue device 303 comprise connect glue groove and be arranged on described in connect and connect glue baffle plate on glue groove, described connecing on glue baffle plate, be provided with Frictioning device, described Frictioning device comprises drive motors, the spreading roller being connected with described drive motors, is located at the rubber plate of described spreading roller end.
And drying unit comprises baking oven casing, the hot-air air inlet 411 being connected with baking oven casing, wherein, in described baking oven casing, be provided with three fixing the first even windshield plate 402 of even windshield plate 401, second and the 3rd even windshield plates 403, described three even windshield plates are arranged in parallel, spacing is identical between adjacent two even windshield plates, described three even windshield plates are arranged in described baking oven casing, join with hot-air air inlet 411, every even windshield plate tail end is respectively equipped with adjustable baffle plate, and the rear portion of described baking oven casing is also provided with forces humidity-discharging device 407.
Between wherein said adjustable baffle plate and described even windshield plate, by removable pin, be connected, between described adjustable baffle plate and described even windshield plate, there is angle adjustable.
To force humidity-discharging device 407 to connect two groups of identical drying units.Force humidity-discharging device 407 to comprise negative pressure box 409, be arranged on the moisture deflector 408 in negative pressure box 409, described negative pressure box 409 communicates with described baking oven casing, and is connected to negative-pressure air fan 410 by pipeline, and negative-pressure air fan is connected with frequency converter controller.
Pressure humidity-discharging device is arranged between every two groups of baking ovens, by be provided with deflector, negative pressure box in forcing humidity-discharging device, negative pressure box is connected with negative-pressure air fan by pipeline, the air quantity of negative-pressure air fan is by Frequency Converter Control, forms oven dry, hydrofuge, dries, low temperature, the flash baking system of hydrofuge again.
By above setting, fiber decomposition device has various materials interface and built-in pipe humidification on the one hand, therefore can use multiple fiber simultaneously and add partial material, to promote the mouthfeel of reconstituted tobacco; Damping device reduces understands the static producing in fine process, effectively avoids the mouthfeel impact of antistatic additive on reconstituted tobacco.
Owing to adopting multi-pipeline feeding, by breaing up the unique design of roller, screen drum and ring device, charging uniformity, controllability are improved, fiber can not piled up in casing, makes the reconstituted tobacco substrate good uniformity of moulding.Owing to being evenly distributed at conveyance conduit in fiber course of conveying, handling good, therefore directly make the substrate grammes per square metre of moulding be less than 20g/ ㎡.
Therefore spray equipment of the present utility model can guarantee that the slurry that solid content is higher fully disperses, and carries out accurate-metering, can spray and contain more tobacco powder, tobacco extract and adhesive, slurry that viscosity is large, and applicability is strong.
In addition, adopt the wet drying unit of low temperature forced-ventilated can prevent that tobacco material from losing in drying course, can significantly not improve again the temperature of drying baker.Between two baking ovens, install strong humidity-discharging device additional, make air high speed circulation and take away the moisture in reconstituted tobacco.Deflector in drying unit guarantees that reconstituted tobacco full width synchronously dries, and has avoided local high temperature and causes the loss of tobacco flavor and produce burnt roasting peculiar smell.
Therefore, device of the present utility model can the whole productivity that improves reconstituted tobacco, has obvious excellent effect.
Claims (12)
1. a dry method of paper-making method is produced the equipment of reconstituted tobacco, comprise the fiber decomposition device connecting successively, substrate shaped device, pulp spraying coating device and drying unit, it is characterized in that described fiber decomposition device comprises connected successively primary mill (101), advanced mill (102), fiber storage tank (103) and meter fine machine (104), the front end of described primary mill (101) is material inlet, the material outlet of the fine machine of described meter (104) is connected to the shaped device that dry method of paper-making method is produced reconstituted tobacco, it is characterized in that described fiber decomposition device also comprises antistatic damping device, described antistatic damping device comprises highly humid air generator (105) and highly humid air pipeline, the output of described highly humid air generator (105) is connected to the material inlet of primary mill (101) and the material outlet of the fine machine of meter (104) by highly humid air pipeline respectively,
Described substrate shaped device comprises moulding guipure, net belt conveying apparatus, be arranged on the substrate shaped device frame (218) on moulding guipure top, in substrate shaped device frame (218), be provided with one or more groups moulded head, in described moulded head, there is air-supply arrangement, be arranged on the negative pressure device of guipure bottom, every composing type head has symmetrically arranged the first screen drum (213) and the second screen drum (214), in the first screen drum (213), prolong axial length direction and be provided with the first fibre conveying channel (201) and the second fibre conveying channel (202), in the second screen drum (214), prolong axial length direction and be provided with the 3rd fibre conveying channel (203) and the 4th fibre conveying channel (204), the first fibre conveying channel (201) and the second fibre conveying channel (202) are arranged on the first half in the first screen drum (213) symmetrically, the 3rd fibre conveying channel (203) and the 4th fibre conveying channel (204) are arranged on the first half in the second screen drum (214) symmetrically, Lower Half in the first screen drum (213) and the second screen drum (214) is provided with respectively first and breaks up roller (212) and second and break up roller (211), first breaks up roller (212) and second breaks up roller (211) and lays respectively under the first screen drum (213) and the second screen drum (214) center of circle, front and rear at the first screen drum (213) and the second screen drum (214) is respectively equipped with front circular passage (215) and rear circular passage (216) that are communicated with screen drum inner space,
Described pulp spraying coating device comprises constant in pressing storage tank (305), the slurry dispenser (322) being connected with the constant material outlet to pressing storage tank (305), described slurry dispenser (322) has a plurality of slurry outlets (324), each slurry outlet (324) is connected to slurry buffer (314) by measuring pump (325) respectively, described slurry buffer (314) is connected to the slurry import (329) of binary nozzle (328) by stop valve (319), described binary nozzle (328) also has compressed air inlet (330), compressed air pressure regulating valve (331) is connected to compressed air inlet (330) by pipeline, described pulp spraying coating device also comprises the spray equipment frame (304) being erected on guipure, spray equipment frame (304) both sides are provided with install bin (301), slurry dispenser (322) and measuring pump (325) are arranged in install bin (301), slurry buffer (314) is arranged on the slurry buffer fixed mount (334) at spray equipment frame (304) middle part, described spray equipment frame (304) middle part is also provided with nozzle fixed mount (332), nozzle fixed mount (332) is provided with the many nozzle fixed mounts (333) that length angle is adjustable, binary nozzle (328) is arranged on nozzle fixed mount (333)
Drying unit, comprise baking oven casing, the hot-air air inlet (411) being connected with described baking oven casing, it is characterized in that being provided with in described baking oven casing three the first fixing even windshield plates (401), the second even windshield plate (402) and the 3rd even windshield plate (403), described three even windshield plates are arranged in parallel, between adjacent two even windshield plates, spacing is identical, described three even windshield plates are arranged in described baking oven casing, join with hot-air air inlet (411), every even windshield plate tail end is respectively equipped with adjustable baffle plate, the rear portion of described baking oven casing is also provided with forces humidity-discharging device (407).
2. the equipment of production reconstituted tobacco according to claim 1, primary mill (101) front portion that it is characterized in that described fiber decomposition device also has independently material interface, described material interface comprises fiberous material interface (112) and granular material interface (113), and described fiberous material interface (112) and granular material interface (113) are respectively equipped with independently switching device.
3. the equipment of production reconstituted tobacco according to claim 1, is characterized in that the material inlet of the primary mill (101) of described fiber decomposition device is provided with flexible connection, the movable barrier of detachable multichannel.
4. the equipment of production reconstituted tobacco according to claim 1, is characterized in that first screen drum (213) of described substrate shaped device is contrary with the direction of rotation of the second screen drum (214).
5. the equipment of production reconstituted tobacco according to claim 1, is characterized in that every group of screen drum of described substrate shaped device is contrary with the direction of rotation of breaing up roller in being arranged on this screen drum.
6. the equipment of production reconstituted tobacco according to claim 1, the length of the first fibre conveying channel (201) that it is characterized in that described substrate shaped device is identical with the length of the 4th fibre conveying channel (204), the length of the second fibre conveying channel (202) is identical with the length of the 3rd fibre conveying channel (203), and the length of the first fibre conveying channel (201) is greater than the length of the second fibre conveying channel (202); The first fibre conveying channel (201) and the second fibre conveying channel (202) extend in the first screen drum (213) from the first screen drum (213) is anterior, and the 3rd fibre conveying channel (203) and the 4th fibre conveying channel (204) be interior extension from the first screen drum (213) rear portion to the first screen drum (213).
7. the equipment of production reconstituted tobacco according to claim 1, the slurry buffer fixed mount (334) that it is characterized in that described pulp spraying coating device is " ︺ " type.
8. the equipment of production reconstituted tobacco according to claim 1, it is characterized in that the constant in pressing storage tank (305) to comprise tank body of described pulp spraying coating device, be located at the slurry outlet (313) of described tank base, be located at the slurry import (312) of described tank body upper side, be located at the agitator (306) of tank interior, described constant giving presses storage tank (305) also to have pressure display unit (307), be arranged on the overpressure safety valve (308) on described tank body top, constant-voltage controller (309) and compressed air pressure regulating valve (310), on tank body top, also there is the stirring motor (311) being connected with agitator (306).
9. the equipment of production reconstituted tobacco according to claim 1, the slurry buffer (314) that it is characterized in that described pulp spraying coating device has buffer slurry import (317) and buffer slurry outlet (318), buffer slurry import (317) is located at slurry buffer (314) side, middle and lower part, buffer slurry outlet (318) is located at slurry buffer (314) bottom, and described slurry buffer (314) top is also provided with purge valve (315) and pressure display unit (316).
10. the equipment of production reconstituted tobacco according to claim 1, is connected by removable pin between the adjustable baffle plate that it is characterized in that described drying unit and described even windshield plate, between described adjustable baffle plate and described even windshield plate, has angle adjustable.
The equipment of 11. production reconstituted tobaccos according to claim 1, the pressure humidity-discharging device (407) that it is characterized in that described drying unit comprises negative pressure box (409), is arranged on the moisture deflector (408) in negative pressure box (409), described negative pressure box (409) communicates with described baking oven casing, and being connected to negative-pressure air fan (410) by pipeline, negative-pressure air fan is connected with frequency converter controller.
The equipment of 12. production reconstituted tobaccos according to claim 1, the baffle length that it is characterized in that the first even windshield plate (401), the second even windshield plate (402) and the 3rd even windshield plate (403) of described drying unit has equal difference relation, and described oven dry bellows are divided into four parts.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420188214.1U CN203776146U (en) | 2014-03-07 | 2014-04-17 | Device for producing reconstituted tobacco in dry paper-making method |
Applications Claiming Priority (9)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420104705 | 2014-03-07 | ||
| CN201420104705.3 | 2014-03-07 | ||
| CN201420104053.3 | 2014-03-07 | ||
| CN201420104053 | 2014-03-07 | ||
| CN201420106250.9 | 2014-03-10 | ||
| CN201420106719 | 2014-03-10 | ||
| CN201420106250 | 2014-03-10 | ||
| CN201420106719.9 | 2014-03-10 | ||
| CN201420188214.1U CN203776146U (en) | 2014-03-07 | 2014-04-17 | Device for producing reconstituted tobacco in dry paper-making method |
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| Publication Number | Publication Date |
|---|---|
| CN203776146U true CN203776146U (en) | 2014-08-20 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420188214.1U Withdrawn - After Issue CN203776146U (en) | 2014-03-07 | 2014-04-17 | Device for producing reconstituted tobacco in dry paper-making method |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103892440A (en) * | 2014-03-07 | 2014-07-02 | 广东省金叶科技开发有限公司 | Equipment for producing reconstituted tobacco through dry-method paper making method |
| WO2015158175A1 (en) * | 2014-04-17 | 2015-10-22 | 广东省金叶科技开发有限公司 | Apparatus for producing reconstituted tobacco sheet via dry paper-making method |
| CN113349410A (en) * | 2021-07-04 | 2021-09-07 | 乐元芬 | Method and device for reproducing tobacco leaves |
| CN113349398A (en) * | 2021-06-17 | 2021-09-07 | 厦门烟草工业有限责任公司 | Device and method for adjusting moisture content of tobacco material on line and tobacco processing production line |
-
2014
- 2014-04-17 CN CN201420188214.1U patent/CN203776146U/en not_active Withdrawn - After Issue
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103892440A (en) * | 2014-03-07 | 2014-07-02 | 广东省金叶科技开发有限公司 | Equipment for producing reconstituted tobacco through dry-method paper making method |
| WO2015158175A1 (en) * | 2014-04-17 | 2015-10-22 | 广东省金叶科技开发有限公司 | Apparatus for producing reconstituted tobacco sheet via dry paper-making method |
| US9901112B2 (en) | 2014-04-17 | 2018-02-27 | Guangdong Golden Leaf Technology Development Co., Ltd. | Apparatus for producing reconstituted tobacco sheet via dry paper-making method |
| CN113349398A (en) * | 2021-06-17 | 2021-09-07 | 厦门烟草工业有限责任公司 | Device and method for adjusting moisture content of tobacco material on line and tobacco processing production line |
| CN113349410A (en) * | 2021-07-04 | 2021-09-07 | 乐元芬 | Method and device for reproducing tobacco leaves |
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