CN107970676A - Tobacco extract double-cylinder type micro-filtration - Google Patents
Tobacco extract double-cylinder type micro-filtration Download PDFInfo
- Publication number
- CN107970676A CN107970676A CN201711304509.5A CN201711304509A CN107970676A CN 107970676 A CN107970676 A CN 107970676A CN 201711304509 A CN201711304509 A CN 201711304509A CN 107970676 A CN107970676 A CN 107970676A
- Authority
- CN
- China
- Prior art keywords
- shell
- outlet pipe
- lower shell
- upper shell
- pipe
- 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
Links
- 235000002637 Nicotiana tabacum Nutrition 0.000 title claims abstract description 30
- 238000001471 micro-filtration Methods 0.000 title claims abstract description 9
- 244000061176 Nicotiana tabacum Species 0.000 title 1
- 241000208125 Nicotiana Species 0.000 claims abstract description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 20
- 238000004519 manufacturing process Methods 0.000 abstract description 7
- 238000005265 energy consumption Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 7
- 239000012141 concentrate Substances 0.000 description 6
- 238000007654 immersion Methods 0.000 description 4
- 230000009467 reduction Effects 0.000 description 4
- 235000019504 cigarettes Nutrition 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 239000007788 liquid Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000010009 beating Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 230000000391 smoking effect Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D36/00—Filter circuits or combinations of filters with other separating devices
- B01D36/02—Combinations of filters of different kinds
-
- A—HUMAN NECESSITIES
- A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
- A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
- A24B15/00—Chemical features or treatment of tobacco; Tobacco substitutes, e.g. in liquid form
- A24B15/18—Treatment of tobacco products or tobacco substitutes
- A24B15/24—Treatment of tobacco products or tobacco substitutes by extraction; Tobacco extracts
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Manufacture Of Tobacco Products (AREA)
Abstract
The invention discloses a kind of tobacco extract double-cylinder type micro-filtration, belong to tobacco leaf production technical field.Including upper shell and lower shell, the top of lower shell is connected with the lower end of upper shell, and junction is equipped with valve, upper shell is internally provided with some filter sticks and concentration outlet system, filter stick is with concentrating outlet system to be connected, outlet system is concentrated to be connected with outlet pipe first, outlet pipe first is located at the outside of upper shell, the lower end of upper shell is also associated with water inlet pipe, lower shell includes stack shell, and the lower part of lower shell is equipped with slagging valve, and lower shell is internally provided with outlet pipe second, the side of lower shell is also associated with air inlet pipe, and air inlet pipe is located at the top of outlet pipe second.The configuration of the present invention is simple, few easy workout part, energy consumption are low, and insolubles content thoroughly solves the problems, such as that offal extracting solution influences reconstituted tobacoo product because insoluble matter is exceeded below one thousandth in the tobacco extract after the present apparatus filters.
Description
Technical field
The present invention relates to tobacco leaf production technical field, and specifically, more particularly to a kind of tobacco extract is declined with the bitubular
Filter device.
Background technology
In recent years, the tobacco leaf production enterprise in China is good for human body with reducing smoking to further carry out tar reduction to cigarette
Health produces harm, for this reason, seeking the method for tar reduction by every possible means, the method for tar reduction at present mainly has filter tip laser to beat online
Hole, pipe tobacco formula improve and mix thin slice etc., while on the basis of learning overseas advanced technology, constantly bring forth new ideas and utilize paper process
Pipe tobacco is reproduced to carry out tar reduction.
The raw material of producing tobacco flake in method similar to papermaking is defeated for tobacco leaf production enterprise automation equipment during cigarette is produced
Conveying cut tobacco shakes thin offal and tobacco leaf planting base tobacco Redrying Factory that the offal sieved, deduster dedusting are got off in beating and double roasting
During the tobacco leaf fragment that drops, paper-making method reconstructed pipe tobacco manufacturing enterprise will be reproduced after these raw materials recoveries using paper process
Pipe tobacco, the production technology for reproducing pipe tobacco are that offal is obstructed lower water immersion, and the offal offal after immersion is caused through crushing slurrying and cigarette
The similar thin slice paper of leaf thickness, separated extracting solution removes wherein harmful material and then through dense through handling after immersion
Certain additive such as essence, wine, sugar etc. are added after contracting, concentrate is sprayed on the surface of thin slice paper and dries chopping and formed again
Reproduce pipe tobacco.
In the prior art, the liquid that offal obtains after immersion is carried on serial automatic production line after sedimentation separation
Liquid is taken, the part insoluble matter light compared with water is still remained in extracting solution to separate, and the extracting solution containing insoluble matter is after concentration
Viscosity number is exceeded, and concentrate can not be absorbed moment on thin slice paper is sprayed to, and the thin slice paper surface after drying can form demoulding
Phenomenon, has seriously affected the product quality of thin slice paper.
The content of the invention
To solve the above-mentioned problems, the invention discloses a kind of tobacco extract double-cylinder type micro-filtration, by the dress
Insolubles content is put in the extracting solution after filtering below one thousandth, thoroughly solve offal extracting solution because insoluble matter is exceeded and
The problem of influencing reconstituted tobacoo product.
The present invention is achieved by the following technical solutions:
A kind of tobacco extract double-cylinder type micro-filtration, including upper shell and lower shell, the top of the lower shell with
The lower end connection of the upper shell, and junction is equipped with valve, the upper shell includes stack shell and the work for being connected to stack shell one end
Dynamic end socket, the upper shell are internally provided with some filter sticks and concentration outlet system, and the filter stick is with concentrating out water system
System connection, the concentration outlet system are connected with outlet pipe first, and the outlet pipe first is located at the outside of the upper shell, it is described go out
The side of water pipe first is also associated with two branch pipes, and blowback air valve and anti-wash-out valve of intaking are respectively fixed with branch pipe, described
The lower end of upper shell is also associated with water inlet pipe, and the lower shell includes stack shell, and the lower part of the lower shell is equipped with slagging valve, institute
That states lower shell is internally provided with outlet pipe second, and one end of the outlet pipe second passes through the first half of stack shell and extends in outside stack shell
Side, the other end of the outlet pipe second are connected with strainer and the middle and lower part inside the lower shell, the side of the lower shell
Face is also associated with air inlet pipe, and the air inlet pipe is located at the top of the outlet pipe second.
The stack shell lower part of the lower shell is tapered.
Compared with prior art, the beneficial effects of the invention are as follows:
The configuration of the present invention is simple, few easy workout part, consume energy low, alternative settling screw centrifugal separator, and tobacco industry is looked forward to
Industry is cost-effective, increasing economic efficiency plays a role;Insoluble matter contains in tobacco extract after the present apparatus filters
Amount thoroughly solves the problems, such as that offal extracting solution influences reconstituted tobacoo product because insoluble matter is exceeded below one thousandth.
Brief description of the drawings
Fig. 1 is the structure diagram of the present invention.
In figure:1st, upper shell;2nd, movable end socket;3rd, lower shell;4th, filter stick;5th, outlet system is concentrated;6th, water inlet pipe;7、
Outlet pipe first;8th, blowback air valve;9th, anti-wash-out valve of intaking;10th, air inlet pipe;11st, outlet pipe second;12nd, strainer;13rd, valve;
14th, slagging valve.
Embodiment
The present invention is further described below in conjunction with the accompanying drawings:
A kind of tobacco extract double-cylinder type micro-filtration, including upper shell 1 and lower shell 3, the top of the lower shell 3
Connected with the lower end of the upper shell 1, and junction is equipped with valve 13, the upper shell 1 includes stack shell and is connected to stack shell one
The movable end socket 2 at end, the upper shell 1 be internally provided with some filter sticks 4 and concentrate outlet system 5, the filter stick 4 with
Outlet system 5 is concentrated to connect, the concentration outlet system 5 is connected with outlet pipe first 7, and the outlet pipe first 7 is located at the upper cylinder
The outside of body 1, the side of the outlet pipe first 7 are also associated with two branch pipes, and blowback air valve 8 and anti-is respectively fixed with branch pipe
Water inlet wash-out valve 9, the lower end of the upper shell 1 are also associated with water inlet pipe 6, and the lower shell 3 includes stack shell, the lower shell
3 lower part is equipped with slagging valve 14, and the lower shell 3 is internally provided with outlet pipe second 11, and one end of the outlet pipe second 11 is worn
Cross the first half of stack shell and extend on the outside of stack shell, the other end of the outlet pipe second 11 is connected with strainer 12 and under described
Middle and lower part inside cylinder 3, the side of the lower shell 3 are also associated with air inlet pipe 10, and the air inlet pipe 10 is located at the water outlet
The top of pipe second 11.
The stack shell lower part of the lower shell 3 is tapered.
As shown in Figure of description Fig. 1, a kind of tobacco extract double-cylinder type micro-filtration, including upper shell 1 and lower cylinder
Body 3, the top of lower shell 3 are connected with the lower end of upper shell 1, and junction is equipped with valve 13, and upper shell 1 includes stack shell and connection
Movable end socket 2 in stack shell one end, upper shell 1 are internally provided with some filter sticks 4 and concentrate outlet system 5, and filter stick 4 is
1000 mesh, shape is similar with bottle shape, and filter stick 4 with concentrating outlet system 5 to be connected, concentrates outlet system 5 and outlet pipe first 7
Connection, outlet pipe first 7 are located at the outside of upper shell 1, and the side of outlet pipe first 7 is also associated with two branch pipes, consolidates respectively on branch pipe
Surely blowback air valve 8 and anti-water inlet wash-out valve 9, the lower end of upper shell 1 are also associated with water inlet pipe 6, lower shell 3 includes cylinder
Body, the stack shell lower part of lower shell 3 is tapered, and the lower part of lower shell 3 is equipped with slagging valve 14, and lower shell 3 is internally provided with water outlet
Pipe second 11, one end of outlet pipe second 11 pass through the first half of stack shell and extend on the outside of stack shell, and the other end of outlet pipe second 11 connects
Strainer 12 and the middle and lower part inside lower shell 3 are connected to, the side of lower shell 3 is also associated with air inlet pipe 10, air inlet pipe 10
In the top of outlet pipe second 11;The volume of upper shell is 1m3, the volume of lower shell is 0.3m3。
The present embodiment course of work is as follows:Tobacco extract enters in upper shell 1 under the action of screw pump from water inlet pipe 6
Portion, the interior formation pressure of bucket, which squeezes into extracting solution in filter stick 4, to be filtered, and the extracting solution after being filtered is collected to out of filter stick
Concentrate outlet system 5 and discharged from outlet pipe first 7, the insoluble matter in extracting solution is intercepted in upper shell, and upper lower shell is connected
It is logical, therefore extracting solution is also filled with lower shell, calculated with theory, the concentration of insoluble matter is about 4/1000ths in extracting solution, per ton
Contain insoluble matter 4Kg in extracting solution, flow is calculated with 10 tons per hour then the insoluble matter of 40Kg, when operation 12 is small after, up and down
For having added up 480Kg insoluble matters in cylinder, at this moment the content of insoluble matter is about 37% in cylinder up and down, few due to containing in insoluble matter
Amount sedimentation, it is believed that the insolubles content in lower shell is 40% or so, when needing to carry out deslagging to device at this time, by valve 13
Close, in order not to waste in lower shell extracting solution about 60% effective component, open compressed gas source and enter from air inlet pipe 10
In lower shell 3, about 60% effective extracting solution is extruded part from outlet pipe second 11 by strainer 12 and returns to filtering by compressed gas
In preceding container, slagging valve 14 is opened, remaining insoluble matter slag charge carries out deslagging, opens valve 13 after the completion of deslagging, use
When slagging frequency can be determined according to the insolubles content of charging, in order to reduce the filtration resistance of filter stick in upper shell, deslagging
Time may be set to carry out once when 6-8 is small, and when lower shell deslagging does not influence the filter process of upper shell, can realize continuously mistake
Filter;When equipment needs to be cleaned comprehensively, compressed air can be used to enter from blowback air valve 8 in upper lower shell it is carried out
Purging, can also use clear water to enter from anti-water inlet wash-out valve 9 in upper lower shell and it is cleaned, whole device can be with control
Device control connection processed, the valvular startup of institute and closing can be realized automatically.
The present apparatus can filter the tobacco extract of different insolubles contents, and slagging frequency can be improved when insolubles content is high
Rate, can reduce slagging frequency when insolubles content is low.
In conclusion only presently preferred embodiments of the present invention, be not used for limiting the scope that the present invention is implemented, it is all according to
The equivalent changes and modifications carried out by shape, construction, feature and spirit described in scope of the invention as claimed, should all be included in this
In the right of invention.
Claims (2)
- A kind of 1. tobacco extract double-cylinder type micro-filtration, it is characterised in that:It is described including upper shell (1) and lower shell (3) The top of lower shell (3) is connected with the lower end of the upper shell (1), and junction is equipped with valve (13), upper shell (1) bag Include stack shell and be connected to the movable end socket (2) of stack shell one end, the upper shell (1) is internally provided with some filter sticks (4) and collection Middle outlet system (5), the filter stick (4) is with concentrating outlet system (5) to be connected, the concentration outlet system (5) and water outlet Pipe first (7) connects, and the outlet pipe first (7) is located at the outside of the upper shell (1), and the side of the outlet pipe first (7) also connects Two branch pipes are connected to, blowback air valve (8) and anti-water inlet wash-out valve (9) are respectively fixed with branch pipe, the upper shell (1) Lower end is also associated with water inlet pipe (6), and the lower shell (3) includes stack shell, and the lower part of the lower shell (3) is equipped with slagging valve (14), the lower shell (3) is internally provided with outlet pipe second (11), and one end of the outlet pipe second (11) passes through the upper half of stack shell Portion is simultaneously extended on the outside of stack shell, and the other end of the outlet pipe second (11) is connected with strainer (12) and is located at the lower shell (3) Internal middle and lower part, the side of the lower shell (3) are also associated with air inlet pipe (10), and the air inlet pipe (10) is located at the water outlet The top of Guan Yi (11).
- 2. tobacco extract according to claim 1 double-cylinder type micro-filtration, it is characterised in that:The lower shell (3) Stack shell lower part it is tapered.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711304509.5A CN107970676A (en) | 2017-12-11 | 2017-12-11 | Tobacco extract double-cylinder type micro-filtration |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711304509.5A CN107970676A (en) | 2017-12-11 | 2017-12-11 | Tobacco extract double-cylinder type micro-filtration |
Publications (1)
Publication Number | Publication Date |
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CN107970676A true CN107970676A (en) | 2018-05-01 |
Family
ID=62009838
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201711304509.5A Pending CN107970676A (en) | 2017-12-11 | 2017-12-11 | Tobacco extract double-cylinder type micro-filtration |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110975411A (en) * | 2019-12-20 | 2020-04-10 | 中核二七二铀业有限责任公司 | Pretreatment filtering equipment for extraction stock solution |
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Publication number | Priority date | Publication date | Assignee | Title |
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GB834991A (en) * | 1958-09-26 | 1960-05-18 | Yarrow & Co Ltd | Improvements in and relating to the filtration of liquids |
GB1093016A (en) * | 1963-11-11 | 1967-11-29 | Georges Zwicky | Improvements in or relating to filtering apparatus |
CN2468560Y (en) * | 2001-03-28 | 2002-01-02 | 承德金龙环保设备厂 | Precision filtering device for water treatment |
CN2885838Y (en) * | 2006-04-18 | 2007-04-04 | 范又方 | magnetized water purifier using active carbon |
CN202343006U (en) * | 2011-11-21 | 2012-07-25 | 桑德集团有限公司 | Two-stage filtration system suitable to remove suspended matters in biomembrane treatment process |
CN102728141A (en) * | 2012-07-19 | 2012-10-17 | 江苏凯力克钴业股份有限公司 | Precise filter device for solution |
CN102989230A (en) * | 2012-06-23 | 2013-03-27 | 唐伟钊 | Water purifier or water purifying plant with circulating filtration function of filter elements and manufacturing method |
CN202893202U (en) * | 2012-11-25 | 2013-04-24 | 成都源创环保工程有限公司 | Water treatment microfiltration device |
CN105056596A (en) * | 2015-09-07 | 2015-11-18 | 大连碧蓝节能环保科技有限公司 | Cross-flow type candle filter |
CN106422486A (en) * | 2016-11-09 | 2017-02-22 | 扬州市康嵩达机电设备有限公司 | Microfiltration apparatus for tobacco extract |
CN206508628U (en) * | 2017-01-13 | 2017-09-22 | 云南鼎和环保科技有限公司 | It is a kind of to drain slag filter with function of on-line cleaning |
CN207628078U (en) * | 2017-12-11 | 2018-07-20 | 扬州市康嵩达机电设备有限公司 | Tobacco extract double-cylinder type micro-filtration |
-
2017
- 2017-12-11 CN CN201711304509.5A patent/CN107970676A/en active Pending
Patent Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB834991A (en) * | 1958-09-26 | 1960-05-18 | Yarrow & Co Ltd | Improvements in and relating to the filtration of liquids |
GB1093016A (en) * | 1963-11-11 | 1967-11-29 | Georges Zwicky | Improvements in or relating to filtering apparatus |
CN2468560Y (en) * | 2001-03-28 | 2002-01-02 | 承德金龙环保设备厂 | Precision filtering device for water treatment |
CN2885838Y (en) * | 2006-04-18 | 2007-04-04 | 范又方 | magnetized water purifier using active carbon |
CN202343006U (en) * | 2011-11-21 | 2012-07-25 | 桑德集团有限公司 | Two-stage filtration system suitable to remove suspended matters in biomembrane treatment process |
CN102989230A (en) * | 2012-06-23 | 2013-03-27 | 唐伟钊 | Water purifier or water purifying plant with circulating filtration function of filter elements and manufacturing method |
CN102728141A (en) * | 2012-07-19 | 2012-10-17 | 江苏凯力克钴业股份有限公司 | Precise filter device for solution |
CN202893202U (en) * | 2012-11-25 | 2013-04-24 | 成都源创环保工程有限公司 | Water treatment microfiltration device |
CN105056596A (en) * | 2015-09-07 | 2015-11-18 | 大连碧蓝节能环保科技有限公司 | Cross-flow type candle filter |
CN106422486A (en) * | 2016-11-09 | 2017-02-22 | 扬州市康嵩达机电设备有限公司 | Microfiltration apparatus for tobacco extract |
CN206508628U (en) * | 2017-01-13 | 2017-09-22 | 云南鼎和环保科技有限公司 | It is a kind of to drain slag filter with function of on-line cleaning |
CN207628078U (en) * | 2017-12-11 | 2018-07-20 | 扬州市康嵩达机电设备有限公司 | Tobacco extract double-cylinder type micro-filtration |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110975411A (en) * | 2019-12-20 | 2020-04-10 | 中核二七二铀业有限责任公司 | Pretreatment filtering equipment for extraction stock solution |
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