CN109588757A - A kind of system and method for tobacco structure adjustment and degree of purity optimization - Google Patents

A kind of system and method for tobacco structure adjustment and degree of purity optimization Download PDF

Info

Publication number
CN109588757A
CN109588757A CN201811313310.3A CN201811313310A CN109588757A CN 109588757 A CN109588757 A CN 109588757A CN 201811313310 A CN201811313310 A CN 201811313310A CN 109588757 A CN109588757 A CN 109588757A
Authority
CN
China
Prior art keywords
winnowing
selection
pipe tobacco
jigging conveyer
pneumatic separation
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201811313310.3A
Other languages
Chinese (zh)
Inventor
吴霖
武小松
张辉
郭永
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN201811313310.3A priority Critical patent/CN109588757A/en
Publication of CN109588757A publication Critical patent/CN109588757A/en
Pending legal-status Critical Current

Links

Classifications

    • AHUMAN NECESSITIES
    • A24TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24BMANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B3/00Preparing tobacco in the factory
    • A24B3/18Other treatment of leaves, e.g. puffing, crimpling, cleaning
    • AHUMAN NECESSITIES
    • A24TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24BMANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B3/00Preparing tobacco in the factory
    • A24B3/06Loosening tobacco leaves or cut tobacco
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B07SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07BSEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
    • B07B1/00Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
    • B07B1/12Apparatus having only parallel elements
    • B07B1/16Apparatus having only parallel elements the elements being movable and in other than roller form
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B07SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07BSEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
    • B07B7/00Selective separation of solid materials carried by, or dispersed in, gas currents
    • B07B7/01Selective separation of solid materials carried by, or dispersed in, gas currents using gravity
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B07SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07BSEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
    • B07B9/00Combinations of apparatus for screening or sifting or for separating solids from solids using gas currents; General arrangement of plant, e.g. flow sheets

Landscapes

  • Manufacturing Of Cigar And Cigarette Tobacco (AREA)

Abstract

The invention discloses a kind of system and methods for tobacco structure adjustment and degree of purity optimization, including screening plant, dispersing device I, pneumatic separation device I, dispersing device II, pneumatic separation device II, main air duct and feeder, it first passes through screening plant and filters out pipe tobacco conglomeration, and then dispersing device I carry out loosely solve group and long filament beat it is short, short pipe tobacco enters the progress level-one selection by winnowing of pneumatic separation device I together in filtering out after the completion and before, by level-one selection by winnowing by the long pipe tobaccos of the overwhelming majority and in short pipe tobacco tentatively selected by feeder, remaining mixture enter dispersing device II carry out again the loosely group of solution and long filament beat it is short after into pneumatic separation device II, after second level selection by winnowing by remaining long pipe tobacco and in short pipe tobacco selection by winnowing obtain, stalk label and sundries are discharged by the impurity outlet of pneumatic separation device II;The present invention can effectively adjust tobacco structure, reduce the material loss in volume packet production link, while can improve the rejecting efficiency of stalk label, and then pipe tobacco degree of purity needed for guarantee cigarette.

Description

A kind of system and method for tobacco structure adjustment and degree of purity optimization
Technical field
The present invention relates to a kind of system and methods for tobacco structure adjustment and degree of purity optimization, belong to pipe tobacco processing skill Art field.
Background technique
During current production of cigarettes, cut tobacco occupies very high ratio in finished product cigarette raw material, and pipe tobacco is passing through Cross after being dried the structure for often still containing ingredients such as clusters, wet mass, burnt piece, the stalk label much wound, affecting pipe tobacco and Finished cigarettes quality, specific manifestation are as follows:
The clusters and wet mass wound in cut tobacco, natural cooling cake easy to form influence the subsequent flavoring uniformity and mix With uniformity, and the mildew of cut tobacco is easily caused, while the uniformity of tobacco structure can be adversely affected.
The stalk label contained in cut tobacco affect the consistency of Sensory Quality of Cigarette, the even meeting in burning of part finished product cigarette There is phenomena such as snuff and torticollis, and also can therefore occur finished product cigarette weight mark in cigarette production process partially and run showing for item As, while it has an effect on cigarette appearance, occurs the phenomenon that stalk label puncture cigarette paper when serious.Present part cigar mill is for stalk The rejecting of label is mainly handled using mica wrappingmachine group, there is a problem that accidentally picking that rate is higher, pipe tobacco is lost larger, rejects efficiency It is relatively low.
Cut tobacco adjustment reduces the long filament rate in pipe tobacco, improves middle silk rate, short silk rate in pipe tobacco, filament broken rate is as far as possible It is constant, its advantage is that reducing the long filament rate in pipe tobacco, advantageous to the Key Quality Indicator of cigarette finished product, such as it is conducive to improve cigarette The stability of weight, solve the problems, such as end tobacco-falling, reduce cigarette between resistance to suction variation the problem of etc.;In addition, high speed mica wrappingmachine group It is more sensitive to the situation that long filament is excessive, a phenomenon is run since long filament is excessively easy to appear;Cigarette development becomes after especially Gesture develops toward ramuscule cigarette, and long filament excessively will affect ramuscule tobacco quality (such as resistance to suction, mark are inclined, end end falls silk, pipe tobacco uniformity).Cause This, reduces the long filament rate of pipe tobacco, the developing direction that short silk rate is tobacco business in increase.Currently, tobacco business is to tobacco structure The method of adjustment mainly has fixed length chopping and big and small blade separation, and the latter is to avoid forming length by large stretch of chopping from source Silk.Although both modes can act as reduces the long filament rate of pipe tobacco, short silk rate in increase, but all considerably increases broken silk Rate, to cause that pipe tobacco loss is larger, is all can also have difference using direct fixed length cutting additionally, due to above two mode The disadvantages of controllability of pipe tobacco length is not strong.
Summary of the invention
In view of the above existing problems in the prior art, the present invention provides one kind for tobacco structure adjustment and degree of purity optimization System and method, can effectively adjust tobacco structure, reduce the material loss in volume packet production link, while can improve to obstruct and sign Reject efficiency, and then pipe tobacco degree of purity needed for guarantee cigarette.
To achieve the goals above, the technical solution adopted by the present invention is that: one kind for tobacco structure adjustment and degree of purity The system of optimization, including bracket, screening plant, dispersing device I, pneumatic separation device I, dispersing device II, pneumatic separation device II, feeder And main air duct, screening plant, dispersing device I, pneumatic separation device I, dispersing device II and pneumatic separation device II are each attached on bracket,
The screening plant includes jigging conveyer I, groove body and multiple groups bar screen plate, and groove body is mounted on jigging conveyer I, Multiple groups bar screen plate is in I top of jigging conveyer and is mounted on groove body side wall, and multiple groups bar screen plate is along jigging conveyer I Transporting direction be in cascade arrangement, every group of bar screen plate be mutually equidistantly made of side by side multiple rods;Dispersing device I Feed inlet is in below the bar screen plate nearest apart from I discharge end of jigging conveyer;Jigging conveyer I discharge end and break up Jigging conveyer II is equipped with below the discharge port of device I, the discharge end of jigging conveyer II and the feed inlet of pneumatic separation device I connect It connects,
The pneumatic separation device I includes selection by winnowing cabinet I, blower I and jigging conveyer III, and jigging conveyer III is mounted on selection by winnowing The discharge end of the lower section of feed inlet in cabinet I, jigging conveyer III is connect with the impurity outlet of selection by winnowing cabinet I, jigging conveyer III Conveyor surface be sieve, the air outlet of blower I connect with the selection by winnowing air inlet of selection by winnowing cabinet I, and the air inlet of blower I passes through air duct It is connect with main air duct, the selection by winnowing air outlet of selection by winnowing cabinet I is connect by air duct with main air duct, and the main air duct is equipped with blanking Device;The impurity outlet of selection by winnowing cabinet I is connect with the feed inlet of dispersing device II, discharge port and the pneumatic separation device II of dispersing device II Feed inlet connection;
The pneumatic separation device II includes selection by winnowing cabinet II, blower II and jigging conveyer IV, and jigging conveyer IV is mounted on The discharge end of the lower section of feed inlet in selection by winnowing cabinet II, jigging conveyer IV is connect with the impurity outlet of selection by winnowing cabinet II, is vibrated defeated The conveyor surface for sending machine IV is sieve, and the air outlet of blower II is connect with the selection by winnowing air inlet of selection by winnowing cabinet II, the air inlet of blower II Mouth is connected to the air duct between the air outlet of blower I and the selection by winnowing air inlet of selection by winnowing cabinet I, the wind of selection by winnowing cabinet II by air duct Air port is selected to connect by air duct with main air duct.
Further, the dispersing device I is made of with dispersing device II shell and two opposite rollers of rotation direction, Two rollers are immobilized in the shell and are in the underface of feed inlet, are equipped with harrow nail on two rollers.
Further, the feeder is made of material retaining net, infundibulate blanking cabinet and discharging gas lock, and material retaining net is obliquely installed In main air duct, infundibulate blanking cabinet is fixed on the main air duct below material retaining net, and discharging gas lock is mounted on infundibulate blanking box The discharge port of body.
It is a kind of for tobacco structure adjustment and degree of purity optimization system working method, specific steps are as follows:
A, the pipe tobacco mixture after baking silk being transported in screening plant, pipe tobacco mixture is fallen on multiple groups bar screen plate, Multiple groups bar screen plate is vibrated with jigging conveyer I, and then is driven pipe tobacco mixture to roll to pneumatic separation device I and moved, in pipe tobacco Mixture rolls in moving process, in short pipe tobacco can be fallen on from the gap on bar screen plate on jigging conveyer I it is mobile after fall on On jigging conveyer II, conglomeration pipe tobacco can be with dispersing device I be entered after bar screen plate movement, and dispersing device I is to conglomeration pipe tobacco Beat it is short and loose after fall on jigging conveyer II and enter in pneumatic separation device I together with short pipe tobacco in;
B, pipe blend enters in pneumatic separation device I, makes air-flow bottom-up stream in pneumatic separation device I by the driving of blower I It is dynamic, using long pipe tobacco and in the difference of short pipe tobacco, stalk label, clusters floating velocity in the gas flow carry out level-one selection by winnowing, long pipe tobacco and In short pipe tobacco (i.e. qualified pipe tobacco) with air-flow reach main air duct through the selection by winnowing air outlet of pneumatic separation device I, subsequently into feeder, It does not fall on jigging conveyer III after being conveyed with air-flow mobile stalk label, sundries and clusters and is arranged from the impurity outlet of selection by winnowing cabinet I Out;
C, the stalk label by level-one selection by winnowing and clusters enter in dispersing device II, carry out in dispersing device II to conglomeration pipe tobacco Beat it is short and loose after enter in pneumatic separation device II, air-flow bottom-up flowing in pneumatic separation device II is made by the driving of blower II, Using long pipe tobacco and in short pipe tobacco, stalk label, clusters in the gas flow floating velocity difference carry out second level selection by winnowing, the wind of second level selection by winnowing Speed is greater than the wind speed of level-one selection by winnowing, long pipe tobacco and in short pipe tobacco with air-flow reach main wind through the selection by winnowing air outlet of pneumatic separation device II Road is not fallen on jigging conveyer IV after being conveyed with the mobile stalk label of air-flow and sundries from selection by winnowing subsequently into feeder The impurity outlet of cabinet II is discharged, and completes second level winnowing process;
D, it in entire winnowing process, is controlled by adjusting bar screen plate medium rod stripe pitch and the air quantity of level-one selection by winnowing Into dispersing device I and the mass flow of dispersing device II;Turn by adjusting two rollers in dispersing device I and dispersing device II Clusters are loose and long filament beats short degree for controlling for dynamic speed;Pipe tobacco after selection by winnowing is controlled by adjusting the air quantity of second level selection by winnowing Degree of purity.
Compared with prior art, the present invention uses bracket, screening plant, dispersing device I, pneumatic separation device I, dispersing device II, pneumatic separation device II, feeder and main air duct combine mode, first pass through screening plant and filter out pipe tobacco conglomeration, and then are beating It is in bulk set I progress loosely the group of solution and long filament beat it is short, filter out after the completion and before in short pipe tobacco enter together pneumatic separation device I into Row level-one selection by winnowing is tentatively selected most qualified pipe tobaccos (i.e. long pipe tobacco and in short pipe tobacco) by feeder by level-one selection by winnowing Out, remaining mixture enter dispersing device II carry out again the loosely group of solution and long filament beat it is short after into pneumatic separation device II, by two After grade selection by winnowing by remaining long pipe tobacco and in short pipe tobacco is selected obtains, remaining stalk label and sundries pass through the impurity removal of pneumatic separation device II The process of entire tobacco structure adjustment and degree of purity optimization is completed in mouth discharge;The present invention passes through loose clusters twice and selection by winnowing Primary election and it is selected twice, thus can guarantee short and conglomeration decomposition is beaten to long filament in tobacco raw material, carry out the adjustment of tobacco structure; Then it can reach the optimization to pipe tobacco degree of purity by selection by winnowing twice, can continue to add multistage pneumatic separation device if needed;In addition There is each pneumatic separation device independent blower offer air flow power to be conducive to wind to accomplish to interfere with each other between each other Select the control of precision and system stability.
Detailed description of the invention
Fig. 1 is overall structure diagram of the invention;
Fig. 2 is the partial enlarged view of screening plant and dispersing device I in Fig. 1;
Fig. 3 is the partial enlarged view of pneumatic separation device I in Fig. 1;
Fig. 4 is the partial enlarged view of pneumatic separation device II in Fig. 1;
Fig. 5 is the partial enlarged view of feeder in Fig. 1.
In figure: 1, screening plant, 1-1, jigging conveyer I, 1-2, groove body, 1-3, bar screen plate, 2, jigging conveyer II, 3, blower I, 4, bracket, 5, dispersing device I, 6, pneumatic separation device I, 6-2,6-1, selection by winnowing cabinet I jigging conveyer III, 7, break up Device II, 8, pneumatic separation device II, 8-1, selection by winnowing cabinet II, 8-2, jigging conveyer IV, 9, blower II, 10, main air duct, 11, fall Glassware, 11-1, material retaining net, 11-2, infundibulate blanking cabinet, 11-3, discharging gas lock.
Specific embodiment
The present invention will be further described below.
As shown, the present invention include bracket 4, screening plant 1, dispersing device I 5, pneumatic separation device I 6, dispersing device II 7, Pneumatic separation device II 8, feeder 11 and main air duct 10, screening plant 1, dispersing device I 5, pneumatic separation device I 6, II 7 and of dispersing device Pneumatic separation device II 8 is each attached on bracket 1, can continue that multiple groups dispersing device and pneumatic separation device is arranged if needed, is improved loose And the process of selection by winnowing;
The screening plant 1 includes I 1-1 of jigging conveyer, groove body 1-2 and multiple groups bar screen plate 1-3, and groove body 1-2 is mounted in On I 1-1 of jigging conveyer, multiple groups bar screen plate 1-3 is in above I 1-1 of jigging conveyer and is mounted on groove body 1-2 side wall, And multiple groups bar screen plate 1-3 is in cascade arrangement along the transporting direction of I 1-1 of jigging conveyer, every group of bar screen plate 1-3 is by more A rod mutually equidistantly forms side by side;The feed inlet of dispersing device I 5 is in nearest apart from I 1-1 discharge end of jigging conveyer Below bar screen plate 1-3;Vibrating transportation is equipped with below the discharge end of I 1-1 of jigging conveyer and the discharge port of dispersing device I 5 The discharge end of machine II 2, jigging conveyer II 2 is connect with the feed inlet of pneumatic separation device I 6,
The pneumatic separation device I 6 includes III 6-2 of I 6-1 of selection by winnowing cabinet, blower I 3 and jigging conveyer, III 6- of jigging conveyer 2 are mounted on the lower section of feed inlet in I 6-1 of selection by winnowing cabinet, the discharge end of III 6-2 of jigging conveyer and going out for I 6-1 of selection by winnowing cabinet Miscellaneous mouth connection, the conveyor surface of III 6-2 of jigging conveyer are sieve, and the air outlet of blower I 3 and the selection by winnowing of I 6-1 of selection by winnowing cabinet are entered the wind The air inlet of mouth connection, blower I 3 is connect by air duct with main air duct 10, and the selection by winnowing air outlet of I 6-1 of selection by winnowing cabinet passes through air duct It is connect with main air duct 10, the main air duct 10 is equipped with feeder 11;The impurity outlet of I 6-1 of selection by winnowing cabinet and dispersing device II 7 Feed inlet connection, the discharge port of dispersing device II 7 are connect with the feed inlet of pneumatic separation device II 8;
The pneumatic separation device II 8 includes IV 8-2 of II 8-1 of selection by winnowing cabinet, blower II 9 and jigging conveyer, jigging conveyer IV 8-2 is mounted on the lower section of feed inlet in II 8-1 of selection by winnowing cabinet, the discharge end and II 8- of selection by winnowing cabinet of IV 8-2 of jigging conveyer 1 impurity outlet connection, the conveyor surface of IV 8-2 of jigging conveyer are sieve, and the air outlet of blower II 9 is with II 8-1's of selection by winnowing cabinet The connection of selection by winnowing air inlet, the air inlet of blower II 9 are connected to the air outlet of blower I 3 and the wind of I 6-1 of selection by winnowing cabinet by air duct The air duct between air inlet is selected, the selection by winnowing air outlet of II 8-1 of selection by winnowing cabinet is connect by air duct with main air duct 10.
Further, the dispersing device I 5 and dispersing device II 7 are by the opposite roller group of shell and two rotation directions At two rollers are immobilized in the shell and are in the underface of feed inlet, are equipped with harrow nail on two rollers.By adjusting two Density, shape and the difference of arrangement of harrow nail on speed difference and two rollers between roller, to realize that more conglomerations are different The loose and long filament of degree beats short ability.
Further, the feeder 11 is made of material retaining net 11-1, infundibulate blanking cabinet 11-2 and discharging gas lock 11-3, Material retaining net 11-1 is inclined in main air duct 10, and infundibulate blanking cabinet 11-2 is fixed on the main air duct below material retaining net 11-1 10, discharging gas lock 11-3 is mounted on the discharge port of infundibulate blanking cabinet 11-2.
It is a kind of for tobacco structure adjustment and degree of purity optimization system working method, specific steps are as follows:
A, the pipe tobacco mixture after baking silk is transported in screening plant 1, pipe tobacco mixture falls on multiple groups bar screen plate 1-3 On, multiple groups bar screen plate 1-3 is vibrated with I 1-1 of jigging conveyer, and then is driven pipe tobacco mixture to roll to pneumatic separation device I 6 and moved It is dynamic, in pipe tobacco mixture rolling moving process, the movement of finger can be simulated, clusters are ceaselessly jolted, keep clusters loose It dissipates, and then becomes free silk;In short pipe tobacco can be fallen on from the gap on bar screen plate 1-3 on I 1-1 of jigging conveyer it is mobile after fall Onto jigging conveyer II 2, conglomeration pipe tobacco can with bar screen plate 1-3 it is mobile after enter dispersing device I 5, I 5 pairs of dispersing device Conglomeration pipe tobacco carry out long filament beat short and clusters it is loose after fall on jigging conveyer II 2 and enter pneumatic separation device together with short pipe tobacco in In I 6;
B, pipe blend enters in pneumatic separation device I 6, keeps air-flow bottom-up in pneumatic separation device I 6 by the driving of blower I 3 Flowing, using long pipe tobacco and in short pipe tobacco, stalk label, clusters, sundries in the gas flow floating velocity difference progress level-one selection by winnowing, by Suspension wind speed needed for short pipe tobacco is smaller in, and suspension wind speed needed for obstructing label, clusters is larger, therefore adjusts the wind speed of selection by winnowing After being in the appropriate value needed for short pipe tobacco and stalk label and clusters between floating velocity, long pipe tobacco and in short pipe tobacco passed through with air-flow The selection by winnowing air outlet of pneumatic separation device I 6 reaches main air duct 10, subsequently into feeder 11, not with stalk label, the sundries of upward gas flow (such as burnt piece, crispy rice), the long pipe tobacco of clusters and part are fallen on III 6-2 of jigging conveyer after being conveyed from I 6-1 of selection by winnowing cabinet Impurity outlet discharge (i.e. completion primary election process);
C, the stalk label by level-one selection by winnowing, clusters, the long pipe tobacco in part and sundries enter in dispersing device II 7, are breaing up dress It sets II 7 pairs of conglomeration pipe tobaccos to carry out long filaments and beat short and clusters loosely entering in pneumatic separation device II 8 afterwards, driving by blower II 9 makes gas Flow the bottom-up flowing in pneumatic separation device II 8, using long pipe tobacco and in short pipe tobacco, stalk label, clusters and sundries hang in the gas flow The difference of floating speed carries out second level selection by winnowing, and the wind speed of second level selection by winnowing is greater than the wind speed of level-one selection by winnowing, long pipe tobacco and in short pipe tobacco with Air-flow reaches main air duct 10 through the selection by winnowing air outlet of pneumatic separation device II 8, subsequently into the stalk in feeder 11, not moved with air-flow It signs and sundries falls on IV 8-2 of jigging conveyer after being conveyed and is discharged from the impurity outlet of II 8-1 of selection by winnowing cabinet, complete second level selection by winnowing Process (i.e. refining process);
D, in entire winnowing process, come by adjusting bar screen plate 1-3 medium rod stripe pitch and the air quantity of level-one selection by winnowing Control enters the mass flow of dispersing device I 5 and dispersing device II 7;By adjusting in dispersing device I 5 and dispersing device II 6 two Clusters are loose and long filament beats short degree for controlling for a roller turn speed;Wind is controlled by adjusting the air quantity of second level selection by winnowing The degree of purity of pipe tobacco after choosing.

Claims (4)

1. a kind of system for tobacco structure adjustment and degree of purity optimization, which is characterized in that including bracket, screening plant, beat It is in bulk to set I, pneumatic separation device I, dispersing device II, pneumatic separation device II, feeder and main air duct, screening plant, dispersing device I, wind Screening device I, dispersing device II and pneumatic separation device II are each attached on bracket,
The screening plant includes jigging conveyer I, groove body and multiple groups bar screen plate, and groove body is on jigging conveyer I, multiple groups Bar screen plate is in I top of jigging conveyer and is mounted on groove body side wall, and multiple groups bar screen plate is along the fortune of jigging conveyer I Defeated direction is in cascade arrangement, and every group of bar screen plate is mutually equidistantly made of side by side multiple rods;The charging of dispersing device I Mouth is below the bar screen plate nearest apart from I discharge end of jigging conveyer;In the discharge end and dispersing device of jigging conveyer I Jigging conveyer II is equipped with below I discharge port, the discharge end of jigging conveyer II is connect with the feed inlet of pneumatic separation device I,
The pneumatic separation device I includes selection by winnowing cabinet I, blower I and jigging conveyer III, and jigging conveyer III is mounted on selection by winnowing cabinet The discharge end of the lower section of feed inlet in I, jigging conveyer III is connect with the impurity outlet of selection by winnowing cabinet I, jigging conveyer III it is defeated Sending face is sieve, and the air outlet of blower I is connect with the selection by winnowing air inlet of selection by winnowing cabinet I, and the air inlet of blower I passes through air duct and master The selection by winnowing air outlet of air duct connection, selection by winnowing cabinet I is connect by air duct with main air duct, and the main air duct is equipped with feeder;Wind The impurity outlet of cabinet I and the feed inlet of dispersing device II is selected to connect, the charging of the discharge port and pneumatic separation device II of dispersing device II Mouth connection;
The pneumatic separation device II includes selection by winnowing cabinet II, blower II and jigging conveyer IV, and jigging conveyer IV is mounted on selection by winnowing The discharge end of the lower section of feed inlet in cabinet II, jigging conveyer IV is connect with the impurity outlet of selection by winnowing cabinet II, jigging conveyer IV conveyor surface is sieve, and the air outlet of blower II is connect with the selection by winnowing air inlet of selection by winnowing cabinet II, and the air inlet of blower II is logical The air duct that air duct is connected between the air outlet of blower I and the selection by winnowing air inlet of selection by winnowing cabinet I is crossed, the selection by winnowing of selection by winnowing cabinet II goes out Air port is connect by air duct with main air duct.
2. a kind of system for tobacco structure adjustment and degree of purity optimization according to claim 1, which is characterized in that institute It states dispersing device I and is made of with dispersing device II shell and two opposite rollers of rotation direction, two rollers are fixed on shell In vivo and it is in the underface of feed inlet, is equipped with harrow nail on two rollers.
3. a kind of system for tobacco structure adjustment and degree of purity optimization according to claim 1, which is characterized in that institute It states feeder to be made of material retaining net, infundibulate blanking cabinet and discharging gas lock, material retaining net is inclined in main air duct, infundibulate Blanking cabinet is fixed on the main air duct below material retaining net, and discharging gas lock is mounted on the discharge port of infundibulate blanking cabinet.
4. a kind of according to claim 1 for tobacco structure adjustment and the working method of degree of purity optimization system, feature It is, specific steps are as follows:
A, the pipe tobacco mixture after baking silk is transported in screening plant, pipe tobacco mixture is fallen on multiple groups bar screen plate, multiple groups Bar screen plate is vibrated with jigging conveyer I, and then is driven pipe tobacco mixture to roll to pneumatic separation device I and moved, and is mixed in pipe tobacco In material rolling moving process, long pipe tobacco and in short pipe tobacco can be fallen on from the gap on bar screen plate on jigging conveyer I it is mobile after It falls on jigging conveyer II, conglomeration pipe tobacco can be with dispersing device I be entered after bar screen plate movement, and dispersing device I is to conglomeration Pipe tobacco beat it is short and loose after fall on jigging conveyer II and enter in pneumatic separation device I together with short pipe tobacco in;
B, pipe blend enters in pneumatic separation device I, makes air-flow bottom-up flowing in pneumatic separation device I by the driving of blower I, benefit With long pipe tobacco and in short pipe tobacco, stalk label, clusters floating velocity in the gas flow difference carry out level-one selection by winnowing, long pipe tobacco and in short cigarette Silk reaches main air duct through the selection by winnowing air outlet of pneumatic separation device I with air-flow, subsequently into the stalk in feeder, not moved with air-flow Label, clusters and sundries fall on jigging conveyer III after being conveyed and are discharged from the impurity outlet of selection by winnowing cabinet I;
C, the stalk label by level-one selection by winnowing and clusters enter in dispersing device II, beat to conglomeration pipe tobacco in dispersing device II short And it is loose after enter in pneumatic separation device II, air-flow bottom-up flowing in pneumatic separation device II is made by the driving of blower II, is utilized Middle long pipe tobacco and in short pipe tobacco, stalk label, clusters in the gas flow floating velocity difference carry out second level selection by winnowing, the wind speed of second level selection by winnowing Greater than the wind speed of level-one selection by winnowing, long pipe tobacco and in short pipe tobacco with air-flow through pneumatic separation device II selection by winnowing air outlet reach main air duct, Subsequently into feeder, do not fall on jigging conveyer IV after being conveyed with the mobile stalk label of air-flow and sundries from selection by winnowing cabinet II impurity outlet discharge, completes second level winnowing process;
D, in entire winnowing process, entrance is controlled by adjusting bar screen plate medium rod stripe pitch and the air quantity of level-one selection by winnowing The mass flow of dispersing device I and dispersing device II;By adjusting two roller turn speed in dispersing device I and dispersing device II Clusters are loose and long filament beats short degree for controlling for degree;The pure of pipe tobacco after selection by winnowing is controlled by adjusting the air quantity of second level selection by winnowing Cleanliness.
CN201811313310.3A 2018-11-06 2018-11-06 A kind of system and method for tobacco structure adjustment and degree of purity optimization Pending CN109588757A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201811313310.3A CN109588757A (en) 2018-11-06 2018-11-06 A kind of system and method for tobacco structure adjustment and degree of purity optimization

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811313310.3A CN109588757A (en) 2018-11-06 2018-11-06 A kind of system and method for tobacco structure adjustment and degree of purity optimization

Publications (1)

Publication Number Publication Date
CN109588757A true CN109588757A (en) 2019-04-09

Family

ID=65957799

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201811313310.3A Pending CN109588757A (en) 2018-11-06 2018-11-06 A kind of system and method for tobacco structure adjustment and degree of purity optimization

Country Status (1)

Country Link
CN (1) CN109588757A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111449269A (en) * 2020-04-24 2020-07-28 智思控股集团有限公司 Tobacco multistage winnowing method and system
CN111495749A (en) * 2020-04-30 2020-08-07 合肥开比锐精机科技有限公司 Polycrystalline silicon monocrystalline silicon clean screening device with non-blocking screen plate and method thereof
CN112438422A (en) * 2020-12-09 2021-03-05 河南中烟工业有限责任公司 Method for online regulating and controlling tobacco shred structure
CN113522722A (en) * 2021-07-05 2021-10-22 湖南伍子醉食品有限公司 Betel nut flower base screening device
CN114794516A (en) * 2022-06-06 2022-07-29 河南中烟工业有限责任公司 Dried cut tobacco lumping and cut tobacco structure adjusting device and system
CN114886141A (en) * 2022-05-30 2022-08-12 河北白沙烟草有限责任公司保定卷烟厂 Feeding machine with functions of separating leaves and loosening tobacco blocks independently

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1242055A (en) * 1967-07-12 1971-08-11 Fawkham Dev Ltd Improvements relating to a method of fluidizing aggregate material
DE2108120B2 (en) * 1970-02-19 1979-07-05 Dso Bulgarski Tjutjuni, Sofia Tobacco treatment equipment - has horizontal heat-insulating partitions between conveyors to form separate climatic zones with fans
CN101073438A (en) * 2007-04-24 2007-11-21 李康胜 Tobacco-cut mixing method by wind force and production line thereof
CN201182188Y (en) * 2008-04-03 2009-01-21 湖北中烟工业有限责任公司 Multilevel pneumatic separation device for rejecting silver from tobacco shred
CN205324172U (en) * 2015-11-30 2016-06-22 徐州众凯机电设备制造有限公司 Second grade wind selector that stalk was signed in rejection leaf silk
CN106418654A (en) * 2016-08-31 2017-02-22 江苏恒森烟草机械有限公司 Fine cigarette cut tobacco length controlling and sliver rejecting device and method for processing cut tobaccos

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1242055A (en) * 1967-07-12 1971-08-11 Fawkham Dev Ltd Improvements relating to a method of fluidizing aggregate material
DE2108120B2 (en) * 1970-02-19 1979-07-05 Dso Bulgarski Tjutjuni, Sofia Tobacco treatment equipment - has horizontal heat-insulating partitions between conveyors to form separate climatic zones with fans
CN101073438A (en) * 2007-04-24 2007-11-21 李康胜 Tobacco-cut mixing method by wind force and production line thereof
CN201182188Y (en) * 2008-04-03 2009-01-21 湖北中烟工业有限责任公司 Multilevel pneumatic separation device for rejecting silver from tobacco shred
CN205324172U (en) * 2015-11-30 2016-06-22 徐州众凯机电设备制造有限公司 Second grade wind selector that stalk was signed in rejection leaf silk
CN106418654A (en) * 2016-08-31 2017-02-22 江苏恒森烟草机械有限公司 Fine cigarette cut tobacco length controlling and sliver rejecting device and method for processing cut tobaccos

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111449269A (en) * 2020-04-24 2020-07-28 智思控股集团有限公司 Tobacco multistage winnowing method and system
CN111495749A (en) * 2020-04-30 2020-08-07 合肥开比锐精机科技有限公司 Polycrystalline silicon monocrystalline silicon clean screening device with non-blocking screen plate and method thereof
CN111495749B (en) * 2020-04-30 2021-08-24 合肥开比锐精机科技有限公司 Polycrystalline silicon monocrystalline silicon clean screening device with non-blocking screen plate and method thereof
CN112438422A (en) * 2020-12-09 2021-03-05 河南中烟工业有限责任公司 Method for online regulating and controlling tobacco shred structure
CN112438422B (en) * 2020-12-09 2022-04-19 河南中烟工业有限责任公司 Method for online regulating and controlling tobacco shred structure
CN113522722A (en) * 2021-07-05 2021-10-22 湖南伍子醉食品有限公司 Betel nut flower base screening device
CN114886141A (en) * 2022-05-30 2022-08-12 河北白沙烟草有限责任公司保定卷烟厂 Feeding machine with functions of separating leaves and loosening tobacco blocks independently
CN114794516A (en) * 2022-06-06 2022-07-29 河南中烟工业有限责任公司 Dried cut tobacco lumping and cut tobacco structure adjusting device and system

Similar Documents

Publication Publication Date Title
CN109588757A (en) A kind of system and method for tobacco structure adjustment and degree of purity optimization
CN102771883B (en) Online sliver separating device for high moisture content cut tobaccos and separating method of online sliver separating device
CN201182188Y (en) Multilevel pneumatic separation device for rejecting silver from tobacco shred
CN107647470B (en) Threshing and redrying processing method capable of simultaneously regulating and controlling structure of tobacco strips and stem content in leaves
CN105396782B (en) Efficient pipe tobacco wind selection method and equipment
CN102688857B (en) Cleaning device with double cross-flow fans, three air passages and double-layered vibrating screens
CN101548794A (en) Multistage pneumatic separation device for eliminating stems from tobacco shreds
CN106937756B (en) A kind of high-efficiency vertical wind subset and its technique for applying
CN202566251U (en) Threshed tobacco leaf collecting and processing system with sand sieving function
CN104983060B (en) A kind of tobacco shred sorter and technique
CN204742597U (en) Pipe tobacco sorter
CN104939295A (en) Ultra-large leaf sorting and processing technology adopted after tobacco leaf threshing and pneumatic separating
CN108783573A (en) A method of improving size evenness of bladess of blades after defolate
CN102823930B (en) Tobacco shred screening and shortening equipment
CN101912146B (en) Method for optimizing structure of finished cut tobacco
US3262457A (en) Tobacco feed for automatic cigarette maker
CN114794516B (en) Dried cut tobacco lumping and cut tobacco structure adjusting device and system
CN201008340Y (en) Back-stem leaf beating device
CN206596678U (en) A kind of raising wind component efficiency simultaneously reduces the wind separating device of material broken rate
CN203778343U (en) Stem shred separation chamber capable of winnowing for multiple times
CN103271431B (en) High efficiency energy saving leaf beating wind separating technique
CN108552578A (en) It is a kind of to sign the piece-rate system separated with pipe tobacco and separation method for that obstruct
CN202456367U (en) Novel cut tobacco winnowing equipment
CN202760162U (en) On-line stem sliver separating device for tobacco shreds with high water moisture content
CN208991252U (en) Inclined plate guide wind sorting machine

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20190409