CN112237787B - Production equipment and method of filter particles - Google Patents
Production equipment and method of filter particles Download PDFInfo
- Publication number
- CN112237787B CN112237787B CN202011147582.8A CN202011147582A CN112237787B CN 112237787 B CN112237787 B CN 112237787B CN 202011147582 A CN202011147582 A CN 202011147582A CN 112237787 B CN112237787 B CN 112237787B
- Authority
- CN
- China
- Prior art keywords
- pipeline
- particles
- filtrate
- storage tank
- box body
- 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.)
- Expired - Fee Related
Links
- 239000002245 particle Substances 0.000 title claims abstract description 121
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 17
- 238000000034 method Methods 0.000 title claims abstract description 17
- 238000003860 storage Methods 0.000 claims abstract description 50
- 239000007788 liquid Substances 0.000 claims abstract description 34
- 238000000926 separation method Methods 0.000 claims abstract description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 17
- 238000002791 soaking Methods 0.000 claims abstract description 5
- 239000000706 filtrate Substances 0.000 claims description 77
- 239000006188 syrup Substances 0.000 claims description 22
- 235000020357 syrup Nutrition 0.000 claims description 22
- 229920002261 Corn starch Polymers 0.000 claims description 11
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 claims description 11
- 239000008120 corn starch Substances 0.000 claims description 11
- 239000008103 glucose Substances 0.000 claims description 11
- 239000013618 particulate matter Substances 0.000 claims description 8
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 6
- 239000003546 flue gas Substances 0.000 claims description 6
- 229920006221 acetate fiber Polymers 0.000 claims description 5
- 230000018044 dehydration Effects 0.000 claims description 5
- 238000006297 dehydration reaction Methods 0.000 claims description 5
- 230000000391 smoking effect Effects 0.000 claims description 5
- 238000002156 mixing Methods 0.000 claims description 4
- 210000003296 saliva Anatomy 0.000 claims description 4
- 239000007787 solid Substances 0.000 claims description 4
- 239000013078 crystal Substances 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims description 3
- 238000012856 packing Methods 0.000 claims description 3
- 230000000717 retained effect Effects 0.000 claims description 3
- 229920006395 saturated elastomer Polymers 0.000 claims description 3
- 238000009489 vacuum treatment Methods 0.000 claims description 3
- 235000019504 cigarettes Nutrition 0.000 abstract description 12
- 239000000463 material Substances 0.000 abstract description 4
- 239000000779 smoke Substances 0.000 description 9
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 6
- 239000011324 bead Substances 0.000 description 4
- 238000005422 blasting Methods 0.000 description 4
- 238000001125 extrusion Methods 0.000 description 4
- 238000004108 freeze drying Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- BJEPYKJPYRNKOW-REOHCLBHSA-N (S)-malic acid Chemical compound OC(=O)[C@@H](O)CC(O)=O BJEPYKJPYRNKOW-REOHCLBHSA-N 0.000 description 2
- CHHHXKFHOYLYRE-UHFFFAOYSA-M 2,4-Hexadienoic acid, potassium salt (1:1), (2E,4E)- Chemical compound [K+].CC=CC=CC([O-])=O CHHHXKFHOYLYRE-UHFFFAOYSA-M 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- YASYEJJMZJALEJ-UHFFFAOYSA-N Citric acid monohydrate Chemical compound O.OC(=O)CC(O)(C(O)=O)CC(O)=O YASYEJJMZJALEJ-UHFFFAOYSA-N 0.000 description 2
- BJEPYKJPYRNKOW-UHFFFAOYSA-N alpha-hydroxysuccinic acid Natural products OC(=O)C(O)CC(O)=O BJEPYKJPYRNKOW-UHFFFAOYSA-N 0.000 description 2
- 229960004106 citric acid Drugs 0.000 description 2
- 229960002303 citric acid monohydrate Drugs 0.000 description 2
- 239000003086 colorant Substances 0.000 description 2
- 210000000887 face Anatomy 0.000 description 2
- 235000013373 food additive Nutrition 0.000 description 2
- 239000002778 food additive Substances 0.000 description 2
- 239000001630 malic acid Substances 0.000 description 2
- 235000011090 malic acid Nutrition 0.000 description 2
- 239000004302 potassium sorbate Substances 0.000 description 2
- 235000010241 potassium sorbate Nutrition 0.000 description 2
- 229940069338 potassium sorbate Drugs 0.000 description 2
- WXMKPNITSTVMEF-UHFFFAOYSA-M sodium benzoate Chemical compound [Na+].[O-]C(=O)C1=CC=CC=C1 WXMKPNITSTVMEF-UHFFFAOYSA-M 0.000 description 2
- 239000004299 sodium benzoate Substances 0.000 description 2
- 235000010234 sodium benzoate Nutrition 0.000 description 2
- 229960003885 sodium benzoate Drugs 0.000 description 2
- SNICXCGAKADSCV-JTQLQIEISA-N (-)-Nicotine Chemical compound CN1CCC[C@H]1C1=CC=CN=C1 SNICXCGAKADSCV-JTQLQIEISA-N 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 210000000214 mouth Anatomy 0.000 description 1
- 229960002715 nicotine Drugs 0.000 description 1
- SNICXCGAKADSCV-UHFFFAOYSA-N nicotine Natural products CN1CCCC1C1=CC=CN=C1 SNICXCGAKADSCV-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/02—Loose filtering material, e.g. loose fibres
-
- A—HUMAN NECESSITIES
- A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
- A24D—CIGARS; CIGARETTES; TOBACCO SMOKE FILTERS; MOUTHPIECES FOR CIGARS OR CIGARETTES; MANUFACTURE OF TOBACCO SMOKE FILTERS OR MOUTHPIECES
- A24D3/00—Tobacco smoke filters, e.g. filter-tips, filtering inserts; Filters specially adapted for simulated smoking devices; Mouthpieces for cigars or cigarettes
- A24D3/06—Use of materials for tobacco smoke filters
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
The invention relates to the technical field of cigarette filter material production, in particular to a production device and a method of filter particles, which comprises the following steps: liquid storage pot, output pipeline, water pump, bin, return line, separator, dewatering box, output pipeline comprises many sections pipelines, includes: the filter liquid of the invention drives the particles to move in the process of moving along the output pipeline, the soaking of the particles and the separation of the particles are completed in the process of moving the filter liquid, and the particles push the particles to move out of the pipeline IV.
Description
Technical Field
The invention relates to the technical field of cigarette filter material production, in particular to production equipment and a method of filter particles.
Background
The cigarette filter tip can filter partial harmful components in smoke when smoking, and can effectively intercept total particulate matters in main stream smoke of the cigarette, reduce tar content, reduce the harm of the smoke to the health and the environment of smokers, in order to further improve the filtering effect of the smoke, the blasting beads are added into the existing cigarette filter tip, the filtering effect of the smoke is enhanced through liquid in the blasting beads, but the smokers need to apply certain extrusion force externally, the blasting beads in the cigarette filter tip are broken, then gel or liquid is released into acetate fibers, the effect of filtering the smoke is achieved, but the mode operation is unchanged, and the cigarette filter tip can also deform due to extrusion when the blasting beads are pinched, the appearance of the cigarette filter tip is influenced, and the smoking experience of the cigarette is also influenced.
In view of the above problems, there is a need for a filter material for cigarette filters and an apparatus for producing the filter material.
Disclosure of Invention
Therefore, the present invention has been made in view of the above problems, and an object of the present invention is to provide a production apparatus and a method for filter particles, which can achieve the above object by the following technical solutions:
a filter particle production apparatus comprising: the device comprises a liquid storage tank, an output pipeline, a water pump, a storage tank, a return pipeline, a separation device and a dewatering tank;
the liquid storage tank is internally stored with filtrate, the filtrate is formed by mixing corn starch syrup or glucose syrup, water, food additives (citric acid monohydrate, potassium sorbate, sodium benzoate and colorant) and citric acid or malic acid, wherein the corn starch syrup or glucose syrup accounts for the largest proportion;
the output pipeline is composed of a plurality of sections of pipelines and comprises: the device comprises a first pipeline, a second pipeline, a third pipeline and a fourth pipeline, wherein one end of the first pipeline is connected with a liquid storage tank, the other end of the first pipeline extends upwards to be connected with the second pipeline, a water pump is mounted on the first pipeline, the second pipeline is horizontal, the second pipeline is connected with the third pipeline, the third pipeline is vertical, the third pipeline extends downwards to be connected with the fourth pipeline, the joint of the third pipeline and the fourth pipeline is arc-shaped, one end of the fourth pipeline is communicated with a dewatering box, and a separating device is connected to the fourth pipeline;
the lower end of the storage tank is horn-shaped, the storage tank is arranged above the second pipeline through a support, the lower end of the storage tank is communicated with the second pipeline, the diameter of the position where the second pipeline is communicated with the storage tank is larger than that of the other parts, and the purpose of the storage tank is to enable filtrate to be far away from the lower end of the storage tank and prevent the filtrate from being filled into the storage tank;
the separation device is a strip-shaped shell, the lower end of the separation device is horn-shaped, the separation device is horizontally communicated below the four pipelines, the bottom surfaces of the four pipelines are grid surfaces, and the diameters of the grid surfaces are smaller than those of the particles;
the dewatering box includes: the device comprises a box body, a cold air pipeline, a tray, a condenser, a vacuum pipeline, a discharge pipeline and a valve;
the box body consists of an outer layer and an inner layer, the lower end of the outer layer is horn-shaped, the horn-shaped lower end of the outer layer is communicated with a discharge pipeline, a first electromagnetic valve is mounted on the discharge pipeline, the inner layer is arranged at the upper end of the outer layer, the lower end face of the inner layer is close to the middle of the outer layer, a plurality of air outlets are formed in the wall surface of the inner layer at equal intervals, and an exhaust pipeline is communicated between the inner layer and the outer layer;
the tray is horn-shaped, the side with the smaller diameter faces downwards, a plurality of holes are formed in the side with the smaller diameter of the tray, the diameter of each hole is slightly larger than the particle, the tray is connected to the upper end of the inner layer through a spring, a pneumatic vibrator is mounted on the tray, and the tray vibrates up and down through the pneumatic vibrator;
the valve is arranged in the box body, is positioned in the middle of the box body, and is divided into an upper cavity and a lower cavity through the valve;
the condenser is arranged in a cavity below the box body, a vacuum pipeline is communicated with the cavity below the box body, and the vacuum pipeline is communicated with the vacuum pump;
in one embodiment, the third tube is helical;
in one embodiment, the four pipes are connected with one end of the dewatering box and arranged obliquely upwards.
The invention also provides a method for producing the filter particles by adopting the filter particle production equipment, which comprises the following steps:
s1: firstly, introducing the particles into a storage tank, and allowing part of the particles to enter a second pipeline along the lower end of the storage tank;
s2: the water pump is started, filtrate in the liquid storage tank rises along the first pipeline and enters the second pipeline, the filtrate is mixed with the particulate matters and carries the particulate matters to move towards the third pipeline, the particulate matters and the filtrate are fully soaked in the third pipeline, the filtrate enters the third pipeline along micropores of the particulate matters, and then the particulate matters and the filtrate enter the fourth pipeline;
s3: the filter liquid enters the separation device through the grid surface of the pipeline IV, the particles are kept in the pipeline IV, the filter liquid flows circularly, so that the particles are carried into the pipeline IV continuously, the particles are gathered in the pipeline IV, the particles push the particles to enter the dewatering box along the pipeline IV, in the moving process of the particles, excessive filter liquid on the surfaces of the particles falls into the separation device, the filter liquid in the separation device enters the liquid storage tank again through the backflow pipeline, and the circulation is carried out;
s4: the particles and the attached filtrate drop on the tray, and the tray vibrates up and down to separate the particles into particles and drop along a plurality of holes on the bottom surface of the tray;
s5: cold air enters along the cold air pipeline and then uniformly flows out along the plurality of air outlets, filtrate on the surface of particles falling along the tray is condensed, the condensed particles fall to the top surface of the valve, when more and more condensed particles are stacked, the stress of the torsion spring at the joint of the semicircular plate and the box body shaft reaches the upper limit, the two semicircular plates are opened, the stacked condensed particles fall to the lower end of the outer layer, and the two semicircular plates are closed again through the torsion spring;
s6: starting a vacuum pump, performing vacuum treatment on the lower end part of the box body through a vacuum pipeline, starting a condenser, heating the lower end part of the box body, sublimating ice crystals condensed by filtrate into vapor to escape (the principle is a freeze-drying principle), dehydrating filtrate attached to particles, and because most of the filtrate is corn starch syrup or glucose syrup, the filtrate can become a solid state after the corn starch syrup or glucose syrup is dehydrated, so that a layer of film is constructed on the particles, micropores of the particles are blocked, the filtrate in the particles can dissolve the film on the particles, the thickness of the film is thinned, and then the film is saturated, so that the filtrate in the particles is sealed, at the moment, a first electromagnetic valve is opened, a discharge pipeline is opened, and the completed particles are moved out of a dehydration box;
s7: thereby during the particulate matter packing to the filter tip after the completion, when smoking, the film on the particulate matter can be dissolved to the heat of flue gas or people's saliva, and the micropore is opened, and during the interior filtrate release looks for the acetate fiber, the completion was filtered the flue gas.
Has the advantages that:
the filter liquid is used for soaking the particles, the filter liquid enters the filter liquid along micropores of the particles and is attached to the surfaces of the particles, the filter liquid attached to the particles is changed into a solid state through a freeze-drying technology, so that a layer of film is constructed on the particles, the micropores of the particles are blocked by the film, the filter liquid inside the particles is stored, the processed particles are mixed into the filter tip, when a user smokes the cigarette, the heat of smoke or saliva in an oral cavity can dissolve the film, the micropores are opened, the filter liquid inside the filter tip is released into acetate fibers, the smoke and the filter liquid react, the content of nicotine in the smoke is reduced, and the inconvenience in operation and the deformation of the cigarette filter tip due to extrusion caused by the fact that the user needs to apply a certain extrusion force to the outside are avoided.
The filter liquor drives the particles to move in the process of moving along the output pipeline, the soaking and the separation of the particles are finished in the process of moving the filter liquor, and the particles push the particles to move out of the pipeline IV, so that the whole structure is simple, and the efficiency is high.
Drawings
FIG. 1 is a schematic view of the overall structure of the present invention;
FIG. 2 is a schematic side view of the present invention;
FIG. 3 is a partial schematic view of the present invention;
FIG. 4 is a schematic structural view of a fourth pipeline and a separating device according to the present invention;
FIG. 5 is a schematic view of the dewatering box of the present invention;
FIG. 6 is a schematic view showing the internal structure of the dewatering box according to the present invention;
FIG. 7 is a schematic view of the mixing process of filtrate and particles according to the present invention;
FIG. 8 is a schematic diagram of the process for separating the filtrate and particles according to the present invention.
Description of reference numerals:
1. a liquid storage tank; 2. an output pipe; 3. a water pump; 4. a storage tank; 5. a return line; 6. a separation device; 7. a dewatering box; 21. a first pipeline; 22. a second pipeline; 23. a third pipeline; 24. a fourth pipeline; 41. a support; 71. a box body; 72. a cold air duct; 73. a tray; 74. a condenser; 75. a vacuum line; 76. a discharge pipeline; 77. a valve; 241. a grid surface; 711. an outer layer; 712. an inner layer; 713. an air outlet; 731. a pneumatic vibrator; 761. an electromagnetic valve; 771. a semicircular plate.
Detailed Description
The present invention is further illustrated in the following description with reference to specific embodiments and the accompanying drawings, wherein the details are set forth in order to provide a thorough understanding of the present invention, but it is apparent that the present invention can be embodied in many other forms different from the description herein, and it will be readily appreciated by those skilled in the art that the present invention can be embodied in many different forms without departing from the spirit and scope of the invention.
As shown in fig. 1-2, a production apparatus for filter particles, comprising: a liquid storage tank 1, an output pipeline 2, a water pump 3, a storage tank 4, a return pipeline 5, a separation device 6 and a dewatering tank 7.
The liquid storage tank 1 is internally stored with filtrate, the filtrate is formed by mixing corn starch syrup or glucose syrup, water, food additives (citric acid monohydrate, potassium sorbate, sodium benzoate and colorant) and citric acid or malic acid, wherein the corn starch syrup or glucose syrup accounts for the largest proportion;
as shown in fig. 3, the output duct 2 is composed of a plurality of sections including: a first pipeline 21, a second pipeline 22, a third pipeline 23 and a fourth pipeline 24;
one end of the first pipeline 21 is connected with the liquid storage tank 1, and the other end of the first pipeline extends upwards to be connected with a second pipeline 22, wherein the first pipeline 21 is provided with a water pump 3;
the second pipeline 22 is horizontal, the second pipeline 22 is connected with the third pipeline 23, and the second pipeline 22 is connected with the storage box 4;
the third pipeline 23 is vertical, the third pipeline 23 extends downwards to be connected with the fourth pipeline 24, the joint of the third pipeline 23 and the fourth pipeline 24 is arc-shaped, one end of the fourth pipeline 24 is communicated with the dewatering box 7, and the fourth pipeline 24 is connected with the separating device 6;
the filtrate moves upwards along the first pipeline 21, horizontally moves through the second pipeline 22, vertically moves downwards through the third pipeline 23 and finally enters the fourth pipeline 24;
the lower end of the storage tank 4 is horn-shaped and is used for storing particles, the storage tank 4 is arranged above the second pipeline 22 through a support 41, the lower end of the storage tank 4 is communicated with the second pipeline 22, the diameter of the position where the second pipeline 22 is communicated with the storage tank 4 is larger than that of the rest part of the storage tank, and the purpose of the storage tank is to enable filtrate to be far away from the lower end of the storage tank 4 and prevent the filtrate from being filled into the storage tank 4;
the particles can be activated carbon particles or ceramic particles and the like with microporous structures;
the particles enter the second pipeline 22 along the lower end of the storage tank 4, and the filtrate in the second pipeline 22 drives the particles to flow to the third pipeline 23;
as shown in fig. 4, the separation device 6 is a strip-shaped shell, the lower end of the separation device is in a horn shape, the separation device 6 is horizontally communicated below the pipeline four 24, the bottom surface of the pipeline four 24 is a grid surface 241, and the diameter of the grid surface 241 is smaller than that of the particles;
one end of the return pipeline 5 is communicated with the lower end of the separation device 6, the other end of the return pipeline is communicated with the liquid storage tank 1, and filtrate circularly flows in the liquid storage tank 1, the output pipeline 2, the separation device 6 and the return pipeline 5 under the action of the water pump 3;
the filtrate carries the particles into the fourth pipe 24, the filtrate enters the separation device 6 through the grid surface 241 of the fourth pipe 24, the particles are retained in the fourth pipe 24, the filtrate continuously carries the particles into the fourth pipe 24 due to the circulation flow of the filtrate, the particles are gathered in the fourth pipe 24, the particles push the particles to enter the dewatering box 7 along the fourth pipe 24,
because the most specific components of the filtrate are corn starch syrup or glucose syrup, the viscosity is high, the filtrate can be rapidly separated from the particles through the third vertical pipeline 23 and the grid surface 241, after the particles enter the fourth pipeline 24, part of the filtrate attached to the particles drops downwards along the grid surface 241, and the particles cannot be contacted with the filtrate again in the process, so that the particles are effectively separated from the filtrate;
the dehydration box 7 is used for condensing and dehydrating filtrate on the surface of the particulate matter, and the principle of the dehydration box is the same as that of freeze-drying;
as shown in fig. 5 to 6, the dewatering box 7 includes: box 71, cold air pipeline 72, tray 73, condenser 74, vacuum pipeline 75, discharge pipeline 76, valve 77;
the box body 71 consists of an outer layer 711 and an inner layer 712;
the lower end of the outer layer 711 is horn-shaped, the horn-shaped lower end of the outer layer 711 is communicated with a discharge pipeline 76, and a first electromagnetic valve 761 is mounted on the discharge pipeline 76;
the inner layer 712 is arranged at the upper end of the outer layer 711, the lower end surface of the inner layer 712 is close to the middle of the outer layer 711, a plurality of air outlets 713 are arranged on the wall surface of the inner layer 712 at equal intervals, and an exhaust pipeline (not shown in the figure) is communicated between the inner layer 712 and the outer layer 711;
the tray 73 is in a horn shape, the side with the smaller diameter faces downwards, wherein a plurality of holes are formed in the side with the smaller diameter of the tray 73, and the diameter of each hole is slightly larger than that of the particles (only one particle is allowed to pass through);
the tray 73 is connected to the upper end of the inner layer 712 through a spring, a pneumatic vibrator 731 is mounted on the tray 73, and the tray 73 is vibrated up and down through the pneumatic vibrator 731;
the valve 77 is arranged in the box body 71 and positioned in the middle of the box body 71, and the box body 71 is divided into an upper cavity and a lower cavity through the valve 77;
the valve 77 is formed by two half semicircular plates 771 which are opposite, the semicircular plates 771 are connected with the box body 71 through shafts, and torsion springs are arranged at the shaft connection positions;
the condenser 74 is arranged in a cavity below the box body 71, a vacuum pipeline 75 is communicated with the cavity below the box body 71, and the vacuum pipeline 75 is communicated with a vacuum pump.
Preferably, as an implementation mode, the third pipe 23 is spiral, and the purpose of the increased fourth pipe 24 is to increase the length of the pipe, so as to increase the soaking time of the particulate matters in the filtrate, and the particulate matters are displaced in multiple directions in the spiral third pipe 23, thereby facilitating the filtrate to enter the particulate matters.
Preferably, as an implementation mode, the end of the pipeline four 24 connected with the dewatering box 7 is arranged obliquely upwards, and the purpose of the pipeline four 24 is to increase the length of the pipeline and better separate filtrate and particulate matters.
The invention also provides a method for producing the filter particles by adopting the filter particle production equipment, which comprises the following steps:
s1: firstly, introducing the particles into a storage tank 4, and allowing part of the particles to enter a second pipeline 22 along the lower end of the storage tank 4;
s2: the water pump 3 is started, as shown in fig. 7, the filtrate in the liquid storage tank 1 rises along the first pipeline 21 to enter the second pipeline 22, the filtrate is mixed with the particulate matters and carries the particulate matters to move to the third pipeline 23, the particulate matters and the filtrate are fully soaked in the third pipeline 23, the filtrate enters the interior of the third pipeline along micropores of the particulate matters, and then the particulate matters and the filtrate enter the fourth pipeline 24;
s3: as shown in fig. 8, the filtrate enters the separation device 6 through the mesh surface 241 of the fourth pipe 24, while the particulate matters are retained in the fourth pipe 24, as the filtrate flows circularly, the particulate matters are continuously carried into the fourth pipe 24, the particulate matters are gathered in the fourth pipe 24, the particulate matters push the particulate matters to enter the dewatering box 7 along the fourth pipe 24, in the process of moving the particulate matters, excessive filtrate on the surface of the particulate matters falls into the separation device 6, and the filtrate in the separation device 6 enters the liquid storage tank 1 again through the backflow pipe 5, so that the circulation is performed;
s4: the particles and the attached filtrate drop on the tray 73, and the tray 73 vibrates up and down to separate the particles into clusters and drop along a plurality of holes on the bottom surface of the tray 73;
s5: cold air enters along the cold air pipeline 72 and then uniformly flows out along the plurality of air outlets 713, filtrate on the surfaces of particles falling along the tray 73 is also condensed, the condensed particles fall to the top surface of the valve 77, when more and more condensed particles are stacked, the stress of the torsion spring at the axial connection part of the semicircular plate 771 and the box body 71 reaches the upper limit, the two semicircular plates 771 are opened, the stacked condensed particles fall to the lower end of the outer layer 711, and the two semicircular plates 771 are closed again through the torsion spring;
s6: starting a vacuum pump, performing vacuum treatment on the lower end part of the box body 71 through a vacuum pipeline 75, then starting a condenser 74, heating the lower end part of the box body 71, sublimating ice crystals condensed in filtrate into water vapor to escape (the principle is a freeze-drying principle), dehydrating filtrate attached to particles, and because most of the filtrate is corn starch syrup or glucose syrup, the filtrate can become solid after the corn starch syrup or glucose syrup is dehydrated, so that a layer of film is constructed on the particles, micropores of the particles are blocked, the filtrate in the particles can dissolve the film on the particles, the film is thinned, the film is saturated, the filtrate in the particles is sealed, at the moment, a first electromagnetic valve 761 is opened, a discharge pipeline 76 is opened, and the completed particles are moved out of the dehydration box 7;
s7: thereby during the particulate matter packing to the filter tip after the completion, when smoking, the film on the particulate matter can be dissolved to the heat of flue gas or people's saliva, and the micropore is opened, and during the interior filtrate release looks for the acetate fiber, the completion was filtered the flue gas.
Claims (4)
1. A filter particle production apparatus comprising: the device comprises a liquid storage tank (1), an output pipeline (2), a water pump (3), a storage tank (4), a return pipeline (5), a separation device (6) and a dewatering tank (7); the method is characterized in that: the output duct (2) is composed of a plurality of sections of duct, including: the device comprises a first pipeline (21), a second pipeline (22), a third pipeline (23) and a fourth pipeline (24), wherein one end of the first pipeline (21) is connected with the second pipeline (22) which extends upwards and is connected with the liquid storage tank (1), the first pipeline (21) is provided with a water pump (3), the second pipeline (22) is connected with one end of the third pipeline (23), the other end of the second pipeline (22) is connected with a storage tank (4), one end of the third pipeline (23) which extends downwards is connected with one end of the fourth pipeline (24), the other end of the fourth pipeline (24) is communicated with a dewatering tank (7), the fourth pipeline (24) is connected with a separating device (6), the lower end of the storage tank (4) is horn-shaped, the storage tank (4) is arranged above the second pipeline (22) through a support (41), the lower end of the storage tank is communicated with the second pipeline (22), the separating device (6) is a bar-shaped shell, the lower end of the separating device (6) is horizontally communicated below the fourth pipeline (24), wherein four (24) bottom surfaces of pipeline are net face (241), and the diameter of net face (241) is less than the particulate matter, backflow pipeline (5) one end intercommunication separator (6) lower extreme, other end intercommunication liquid storage pot (1), and dewatering box (7) include: the refrigerator comprises a box body (71), a cold air pipeline (72), a tray (73), a condenser (74), a vacuum pipeline (75), a discharge pipeline (76) and a valve (77), wherein the box body (71) consists of an outer layer (711) and an inner layer (712), the lower end of the outer layer (711) is horn-shaped, the horn-shaped lower end of the outer layer (711) is communicated with the discharge pipeline (76), a first electromagnetic valve (761) is installed on the discharge pipeline (76), the inner layer (712) is arranged at the upper end part of the outer layer (711), the lower end face of the inner layer (712) is close to the middle part of the outer layer (711), a plurality of air outlets (713) are equidistantly formed in the wall face of the inner layer (712), an exhaust pipeline is communicated between the inner layer (712) and the outer layer (711), the tray (73) is horn-shaped, the face with the smaller diameter faces downwards, a plurality of holes are formed in the face with the smaller diameter of the tray (73), the valve (77) is arranged in the box body (71), the condenser is positioned in the middle of the box body (71), the condenser (74) is arranged in a cavity below the box body (71), a vacuum pipeline (75) is communicated in the cavity below the box body (71), the vacuum pipeline (75) is communicated with a vacuum pump, the tray (73) is connected to the upper end of the inner layer (712) through a spring, and a pneumatic vibrator (731) is installed on the tray (73).
2. The production facility of filter particles according to claim 1, characterized in that: the second pipeline (22) is horizontal, the third pipeline (23) is vertical, and the joint of the third pipeline (23) and the fourth pipeline (24) is arc-shaped.
3. The production facility of filter particles according to claim 1, characterized in that: the valve (77) is formed by two half semicircular plates (771) which are opposite, the semicircular plates (771) are connected with the box body (71) through shafts, and torsion springs are arranged at the connection positions of the shafts.
4. The method of using the filter particle production facility of claim 3, comprising the steps of:
s1, firstly, introducing the particles into a storage box (4), and enabling part of the particles to enter a second pipeline (22) along the lower end of the storage box (4);
s2, starting a water pump (3), enabling filtrate in a liquid storage tank (1) to rise along a first pipeline (21) and enter a second pipeline (22), mixing the filtrate with particles and carrying the particles to move towards a third pipeline (23), fully soaking the particles and the filtrate in the third pipeline (23), enabling the filtrate to enter the interior of the third pipeline along micropores of the particles, and then enabling the particles and the filtrate to enter a fourth pipeline (24);
s3, enabling filtrate to enter a separation device (6) through a grid surface (241) of a pipeline IV (24), and enabling particles to be retained in the pipeline IV (24), wherein the filtrate continuously carries the particles to enter the pipeline IV (24) due to circulation flow of the filtrate, the particles are gathered in the pipeline IV (24), the particles are pushed to enter a dewatering box (7) along the pipeline IV (24), excessive filtrate on the surfaces of the particles falls into the separation device (6) in the movement process of the particles, and the filtrate in the separation device (6) enters a liquid storage tank (1) again through a return pipeline (5) and circulates in the way;
s4: the particles and the attached filtrate drop on the tray (73), and the tray (73) vibrates up and down to separate the particles into particles and drop along a plurality of holes on the bottom surface of the tray (73);
s5: cold air enters along a cold air pipeline (72) and uniformly flows out along a plurality of air outlets (713), filtrate on the surface of particles falling along the tray (73) is condensed, the condensed particles fall to the top surface of the valve (77), when the condensed particles are more and more stacked, the stress of a torsion spring at the axial connection part of the semicircular plate (771) and the box body (71) reaches the upper limit, the two semicircular plates (771) are opened, the stacked condensed particles fall to the lower end of the outer layer (711), and the two semicircular plates (771) are closed again through the torsion spring;
s6: starting a vacuum pump, performing vacuum treatment on the lower end part of a box body (71) through a vacuum pipeline (75), then starting a condenser (74), heating the lower end part of the box body (71), sublimating ice crystals condensed in filtrate into steam to escape, and dehydrating filtrate attached to particles, wherein most of the filtrate is corn starch syrup or glucose syrup, and when the corn starch syrup or glucose syrup is dehydrated, the filtrate becomes solid, so that a layer of film is constructed on the particles, micropores of the particles are blocked, the filtrate in the particles can dissolve the film on the particles, the thickness of the film is thinned, and then the film is saturated, so that the filtrate in the particles is sealed, at the moment, a first electromagnetic valve (761) is opened, a discharge pipeline (76) is opened, and the completed particles are moved out of a dehydration tank (7);
s7: thereby during the particulate matter packing to the filter tip after the completion, when smoking, the film on the particulate matter can be dissolved to the heat of flue gas or people's saliva, and the micropore is opened, and during the interior filtrate release looks for the acetate fiber, the completion was filtered the flue gas.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011147582.8A CN112237787B (en) | 2020-10-23 | 2020-10-23 | Production equipment and method of filter particles |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011147582.8A CN112237787B (en) | 2020-10-23 | 2020-10-23 | Production equipment and method of filter particles |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN112237787A CN112237787A (en) | 2021-01-19 |
| CN112237787B true CN112237787B (en) | 2022-04-01 |
Family
ID=74169513
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202011147582.8A Expired - Fee Related CN112237787B (en) | 2020-10-23 | 2020-10-23 | Production equipment and method of filter particles |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN112237787B (en) |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003062407A (en) * | 2001-08-24 | 2003-03-04 | Ebara Corp | Treating method and treating device for contaminated water |
| DE102010023290A1 (en) * | 2010-06-10 | 2011-12-15 | Charalampos Avgoustinos | Method for sealing and closing leakage of e.g. liquid medium in e.g. pipeline, involves mixing ferromagnetic materials in form of particles or powders or flowing medium to seal leakage or blockage and/or damming of pipe, valve or equipment |
| CN103660066A (en) * | 2013-12-27 | 2014-03-26 | 马鞍山市秋枫工程塑料异型材料制造有限责任公司 | Granulating method of air plastic granulating device |
| CN105745283A (en) * | 2013-12-17 | 2016-07-06 | 克罗内斯国际公司 | Method for producing composite particles |
| CN108744908A (en) * | 2018-07-02 | 2018-11-06 | 芜湖万向新元环保科技有限公司 | A kind of flue dust removes nitre sulphur removal environmental protection equipment |
| CN108913337A (en) * | 2018-07-19 | 2018-11-30 | 安徽华禹食品有限公司 | A kind of rapeseed Processing device and its application method |
| CN109198720A (en) * | 2018-10-22 | 2019-01-15 | 四川三联新材料有限公司 | A kind of extraordinary filter stick with blending cooling |
Family Cites Families (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3470883A (en) * | 1968-08-29 | 1969-10-07 | Nat Patent Dev Corp | Tobacco smoke filters |
| EP1537846A1 (en) * | 2002-09-11 | 2005-06-08 | Tanabe Seiyaku Co., Ltd. | Process for the production of microspheres and unit therefor |
| GB0915814D0 (en) * | 2009-09-10 | 2009-10-07 | British American Tobacco Co | Smoke filtration |
| CN101828769B (en) * | 2010-04-16 | 2011-08-31 | 云南正邦生物技术有限公司 | Preparation method of cigarette flavor compensating particles |
| CN105001988B (en) * | 2015-07-17 | 2018-07-24 | 云南中烟工业有限责任公司 | A kind of preparation facilities and its application process of three-layer sandwich structure spice slow-releasing additives of filter tip |
| CN107772530B (en) * | 2016-08-24 | 2022-06-21 | 贵州中烟工业有限责任公司 | Composite cigarette filter tip for improving cigarette taste and application |
| CN207456027U (en) * | 2017-10-27 | 2018-06-05 | 上海悦联生物科技有限公司 | A kind of freeze drying equipment for Pesticidal products |
| CN107677059A (en) * | 2017-11-15 | 2018-02-09 | 吴兴润茂纺织品织造厂 | Particulate material drying device is used in one kind weaving |
| CN109123775B (en) * | 2018-08-06 | 2021-03-16 | 江西中烟工业有限责任公司 | Heating non-combustion cigarette containing herbal fragrance type solid aromatic beads and preparation method thereof |
| CN110982625A (en) * | 2019-12-29 | 2020-04-10 | 亿利耐雀生物科技有限公司 | Licorice-flavored dried beads for cigarette filter tips and preparation method thereof |
-
2020
- 2020-10-23 CN CN202011147582.8A patent/CN112237787B/en not_active Expired - Fee Related
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003062407A (en) * | 2001-08-24 | 2003-03-04 | Ebara Corp | Treating method and treating device for contaminated water |
| DE102010023290A1 (en) * | 2010-06-10 | 2011-12-15 | Charalampos Avgoustinos | Method for sealing and closing leakage of e.g. liquid medium in e.g. pipeline, involves mixing ferromagnetic materials in form of particles or powders or flowing medium to seal leakage or blockage and/or damming of pipe, valve or equipment |
| CN105745283A (en) * | 2013-12-17 | 2016-07-06 | 克罗内斯国际公司 | Method for producing composite particles |
| CN103660066A (en) * | 2013-12-27 | 2014-03-26 | 马鞍山市秋枫工程塑料异型材料制造有限责任公司 | Granulating method of air plastic granulating device |
| CN108744908A (en) * | 2018-07-02 | 2018-11-06 | 芜湖万向新元环保科技有限公司 | A kind of flue dust removes nitre sulphur removal environmental protection equipment |
| CN108913337A (en) * | 2018-07-19 | 2018-11-30 | 安徽华禹食品有限公司 | A kind of rapeseed Processing device and its application method |
| CN109198720A (en) * | 2018-10-22 | 2019-01-15 | 四川三联新材料有限公司 | A kind of extraordinary filter stick with blending cooling |
Also Published As
| Publication number | Publication date |
|---|---|
| CN112237787A (en) | 2021-01-19 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN112237787B (en) | Production equipment and method of filter particles | |
| CN105999918B (en) | Minute dust particle filtering adsorption system | |
| CN105921489B (en) | Animal innocent treatment equipment and method | |
| CN206823448U (en) | A kind of machining center oil mist removing removes water smoke purifier | |
| CN101107053A (en) | Method and apparatus for treatment of exhaust gas | |
| CN205323327U (en) | Filter | |
| CN211851788U (en) | Ground coal bed gas well discharging and mining device | |
| CN117382032A (en) | Automatic pressing and screening device for cable insulation particle production | |
| CN208145721U (en) | A kind of smoke exhaust pipe for gas cleaning | |
| CN207628153U (en) | A kind of improved demister | |
| CN105013278B (en) | Purifying equipment with demountable filtering structure | |
| CN209423253U (en) | A kind of Combined industry oil smoke filtrating equipment of flue gas | |
| CN207256939U (en) | A kind of cow dung separating dry space from moist space machine | |
| CN215233046U (en) | Air bleeder for crystal growth | |
| CN206424737U (en) | A kind of centrifugal filtration type fume purifier of fume | |
| CN112316562B (en) | Production equipment and method of cigarette filter tip filtering material | |
| CN209049178U (en) | Moxibustion smoke-purifying machine | |
| CN102250680B (en) | Fat processing method | |
| CN206823430U (en) | Micro-heat regeneration absorbent drying machine and its air cleaner | |
| CN101643685A (en) | Filtering and impurity removing technology for oil with high colloid content | |
| CN217449487U (en) | Improved filter assembly for purifying flue gas | |
| CN105498257B (en) | A kind of deslagging device and deslagging method of papermaking-method reconstituted tobaccos production line inspissator | |
| CN216035233U (en) | Be applicable to carbon adsorbent granule partial shipment device | |
| CN110314469A (en) | A kind of household air filter | |
| CN220968679U (en) | Carbonization coke-discharging flue gas treatment device |
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 | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20220401 |