CN207678831U - A kind of extraction system of reconstituted tobacco raw material offal - Google Patents
A kind of extraction system of reconstituted tobacco raw material offal Download PDFInfo
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- CN207678831U CN207678831U CN201721774753.3U CN201721774753U CN207678831U CN 207678831 U CN207678831 U CN 207678831U CN 201721774753 U CN201721774753 U CN 201721774753U CN 207678831 U CN207678831 U CN 207678831U
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Abstract
The utility model discloses a kind of extraction systems of reconstituted tobacco raw material offal, it is desirable to provide a kind of extraction system of efficient reconstituted tobacco raw material offal.It includes that pre-processing device, fiber slightly solve equipment, extraction and solid-liquid separating equipment and extracting solution cleaning equipment；The pre-processing device includes for receiving offal and wash the rotary drum terrier wash machine of stalk, be used for the offal moisture regaining machine and drainage screw conveyor of regaining moisture of cabo；It includes the double helix thread rolling machine that material inlet is connect with offal moisture regaining machine material outlet that the fiber, which slightly solves equipment,；The extraction and solid-liquid separating equipment include the conveyer that input terminal is connect with double helix thread rolling machine material outlet; the extractor that material inlet is connect with conveyer input terminal; the refining storehouse that material inlet is connect with extractor material outlet; the fiber uncoiling machine that material inlet is connect with refining storehouse material outlet; the offal surge tank and three-level double helix solid-liquid separating equipment that material inlet is connect with fiber uncoiling machine material outlet.
Description
Technical field
The utility model is related to tobacco leaf processing technique fields, more particularly, to a kind of extraction system of reconstituted tobacco raw material offal
System.
Background technology
Offal extraction process is as one of the critical process in papermaking-method reconstituted tobaccos production process, it is to promoting paper process
Reconstituted tobacco production Technology level and product quality play the role of vital." 12th Five-Year Plan " period tobacco business
Development enters the new historical stage, and the deep propulsion of the proposition and work of " horizontal on cigarette " goal task, especially brand is sent out
Implementation horizontal in horizontal and technological innovation in exhibition, to promoting the propositions such as cigarette brand value, lowering harm and decreasing coking, Product quality and safety
Requirements at the higher level.Papermaking-method reconstituted tobaccos as one of the important means of solving these problems, have been assigned higher responsibility and
Mission.
In face of this new situations, new task and new demand, current domestic papermaking-method reconstituted tobaccos technology level and production
Quality level still has apparent deficiency.Mainstream extraction process is single tank, interval extraction process at present, its advantage is that scheduling of production
Flexibly, it is suitble to the offal extraction of small lot multi items, small investment etc. when small-scale production.The disadvantage is that overall efficiency is low, it is produced into
This height, large-scale production investment is high, extraction process cannot achieve and automatically control, and causes the unstable quality of reconstituted tobacco.One
There are technical barriers in amplification for a little extraction processes newly developed.Meanwhile not enough for the extraction of tobacco business offal research
Maturation, in manufacturing ability, clean manufacturing ability, physics and chemistry when cannot be satisfied papermaking-method reconstituted tobaccos large-scale industrial production
Ability of regulation and control, the requirement of the technologies and process aspect such as quality stability, formula applicability.
Utility model content
The purpose of this utility model is intended to overcome the shortcomings of the prior art, provides a kind of extraction efficiency height, production
It is at low cost, reconstituted tobacco stable quality, the extraction system for the reconstituted tobacco raw material offal that energy conservation and environmental protection and satisfaction mass produce.
In order to solve the above-mentioned technical problem, the utility model is achieved through the following technical solutions：
A kind of extraction system of reconstituted tobacco raw material offal, including pre-processing device, fiber slightly solve equipment, extraction and solid-liquid
Separation equipment and extracting solution cleaning equipment；
The pre-processing device includes for receiving offal and wash the rotary drum terrier wash machine of stalk, for regaining moisture of cabo
Offal moisture regaining machine and input terminal connect with rotary drum terrier wash machine material outlet, output end and offal moisture regaining machine material inlet
The drainage screw conveyor of connection；
It includes the double helix thread rolling machine that material inlet is connect with offal moisture regaining machine material outlet that the fiber, which slightly solves equipment,；
The extraction and solid-liquid separating equipment include the conveyer that input terminal is connect with double helix thread rolling machine material outlet, object
The extractor that material entrance is connect with conveyer input terminal, the refining storehouse that material inlet is connect with extractor material outlet, material enter
The fiber uncoiling machine that mouth is connect with refining storehouse material outlet, the offal surge tank that material inlet is connect with fiber uncoiling machine material outlet, and
Three-level double helix solid-liquid separating equipment；The three-level double helix solid-liquid separating equipment includes that sequentially connected first order double helix is solid
Liquid separation equipment, second level double helix solid-liquid separating equipment and third level double helix solid-liquid separating equipment；The offal surge tank
It is connect with the material inlet of first order double helix solid-liquid separating equipment by screw pump；
The extracting solution cleaning equipment includes that material inlet is connect with first order double helix solid-liquid separating equipment liquid outlet
Slag draining and separating machine, the centrifuge that material inlet is connect with slag draining and separating machine liquid outlet, material inlet and centrifuge liquid discharge
Mouthful connection disk filter, and respectively with slag draining and separating machine stalk slag outlet, centrifuge stalk slag outlet and disk filter obstruct
The stalk slag collecting tank of slag outlet connection.
Preferably, the first order double helix solid-liquid separating equipment material outlet is set with second level double helix separation of solid and liquid
Standby material inlet is connected by the first screw conveyor, second level double helix solid-liquid separating equipment material outlet and the double spiral shells of the third level
Rotation solid-liquid separating equipment material inlet is connected by the second screw conveyor.
Preferably, the first spiral of stalk the slag collecting tank and second level double helix solid-liquid separating equipment material inlet end
Conveyer connects.
Preferably, the material inlet of the liquid outlet of the second level double helix solid-liquid separating equipment and extractor connects
It connects.
Preferably, the liquid outlet of the third level double helix solid-liquid separating equipment is separated by solid-liquid separation with second level double helix
First screw conveyor at equipment material inlet end connects.
Preferably, the material inlet of the liquid outlet and slag draining and separating machine of the first order double helix solid-liquid separating equipment
Connection.
Compared with prior art, the utility model has the following advantages that：
It, can be maximum by wash stalk to offal, steaming stalk and fiber slightly solves in the entire production process of the utility model
Degree promotes the recovery rate of offal, reduces post processing extraction solvent consumption, and extraction time is shorter, and is extracted by Horizontal extraction pot,
Extraction process is simple and easy to control, and energy consumption significantly reduces, and the material discharging after being extracted is continuous, and technique is more simplified；Entire extraction process
It is more easy to realize automation, intelligence, reduces human interference, the quality and homogeneity of steadily control extraction product improve life
Produce efficiency and product yield, reduce raw material and energy consumption, when meeting papermaking-method reconstituted tobaccos large-scale industrial production
Manufacturing ability, clean manufacturing ability, physics and chemistry ability of regulation and control, technologies and the process aspects such as quality stability, formula applicability
Requirement.For develop with lowering harm and decreasing coking, increase the functions such as humectation papermaking-method reconstituted tobaccos product provide it is efficient, stable, can
The novel extractive technique of control promotes the applicability of papermaking-method reconstituted tobaccos product, and special to cigarette brand quality and style
The contribution degree of color.
Description of the drawings
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, the accompanying drawings in the following description is only
It is some embodiments of the utility model, for those of ordinary skill in the art, in the premise not made the creative labor
Under, it can also be obtained according to these attached drawings other attached drawings.
Fig. 1 is the schematic diagram of the utility model.
Specific implementation mode
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are not under the premise of making the creative labor
The every other embodiment obtained, shall fall within the protection scope of the present invention.
The extraction system of the offal of reconstituted tobacco raw material shown in Fig. 1, including pre-processing device A, fiber slightly solve equipment B, extraction
And solid-liquid separating equipment C and extracting solution cleaning equipment D；
The pre-processing device A includes for receiving offal and wash the rotary drum terrier wash machine a1 of stalk, returned for offal
The offal moisture regaining machine a3 and input terminal of tide connect with rotary drum terrier wash machine a1 material outlets, output end and offal moisture regaining machine
The drainage screw conveyor a2 of a3 material inlets connection；
It includes the double helix thread rolling machine that material inlet is connect with offal moisture regaining machine a3 material outlets that the fiber, which slightly solves equipment B,
b1；
The extraction and solid-liquid separating equipment C include the conveyer that input terminal is connect with double helix thread rolling machine b1 material outlets
C1, the extractor c2 that material inlet is connect with conveyer c1 input terminals, material inlet connect even with extractor c2 material outlets
Feed bin c3, the fiber uncoiling machine c4 that material inlet is connect with refining storehouse c3 material outlets, material inlet connect with fiber uncoiling machine c4 material outlets
The offal surge tank c5 and three-level double helix solid-liquid separating equipment connect；The three-level double helix solid-liquid separating equipment include according to
First order double helix solid-liquid separating equipment c7, the second level double helix solid-liquid separating equipment c9 and third level double helix of secondary connection are solid
Liquid separation equipment c8；The offal surge tank c5 is entered by screw pump c6 and the material of first order double helix solid-liquid separating equipment c7
Mouth connection；
The extracting solution cleaning equipment D includes that material inlet connects with first order double helix solid-liquid separating equipment c7 liquid outlets
The slag draining and separating machine d1 connect, the centrifuge d3 that material inlet is connect with slag draining and separating machine d1 liquid outlets, material inlet and centrifugation
The disk filter d4 of machine d3 liquid outlets connection, and go out respectively with the outlet of slag draining and separating machine d1 stalk slags, centrifuge d3 stalk slags
Mouth and the stalk slag collecting tank d5 of disk filter d4 stalk slag outlet connections.
The first order double helix solid-liquid separating equipment material outlet enters with second level double helix solid-liquid separating equipment material
Mouth passes through the first screw conveyor and connects, second level double helix solid-liquid separating equipment material outlet and third level double helix solid-liquid point
It is connected by the second screw conveyor from equipment material inlet.
First spiral transferring at the material inlet end of the stalk slag collecting tank d5 and second level double helix solid-liquid separating equipment c9
Machine is sent to connect.
The liquid outlet of the second level double helix solid-liquid separating equipment c9 is connect with the material inlet of extractor c2.
The liquid outlet of the third level double helix solid-liquid separating equipment c8 and second level double helix solid-liquid separating equipment c9
Material inlet end the first screw conveyor connection.
The liquid outlet of the first order double helix solid-liquid separating equipment c7 is connect with the material inlet of slag draining and separating machine d1.
It, can be utmostly by wash stalk to offal, steaming stalk and fiber slightly solves in the entire production process of the present invention
The recovery rate of offal is promoted, post processing extraction solvent consumption is reduced, extraction time is shorter, and is extracted by Horizontal extraction pot, extraction
Process is simple and easy to control, and energy consumption significantly reduces, and the material discharging after being extracted is continuous, and technique is more simplified, and entire extraction process is more easy to
It realizes automation, intelligence, reduces human interference, the quality and homogeneity of steadily control extraction product improve production and imitate
Rate and product yield reduce raw material and energy consumption, are being produced when meeting papermaking-method reconstituted tobaccos large-scale industrial production
Manufacturing capacity, clean manufacturing ability, physics and chemistry ability of regulation and control, the technologies such as quality stability, formula applicability and process aspect are wanted
It asks.
The above is only the preferred embodiment of the utility model only, is not intended to limit the utility model, all at this
Within the spirit and principle of utility model, any modification, equivalent replacement, improvement and so on should be included in the utility model
Protection domain within.
Claims (6)
1. a kind of extraction system of reconstituted tobacco raw material offal, including pre-processing device, fiber slightly solve equipment, extraction and solid-liquid point
From equipment and extracting solution cleaning equipment；It is characterized in that：
The pre-processing device includes for receiving offal and wash the rotary drum terrier wash machine of stalk, be used for the offal of regaining moisture of cabo
Damping machine and input terminal are connect with rotary drum terrier wash machine material outlet, output end and offal moisture regaining machine material inlet connect
Drainage screw conveyor；
It includes the double helix thread rolling machine that material inlet is connect with offal moisture regaining machine material outlet that the fiber, which slightly solves equipment,；
The extraction and solid-liquid separating equipment include the conveyer that input terminal is connect with double helix thread rolling machine material outlet, and material enters
The extractor that is connect with conveyer input terminal of mouth, the refining storehouse that material inlet is connect with extractor material outlet, material inlet and
The fiber uncoiling machine of refining storehouse material outlet connection, the offal surge tank and three-level that material inlet is connect with fiber uncoiling machine material outlet
Double helix solid-liquid separating equipment；The three-level double helix solid-liquid separating equipment includes sequentially connected first order double helix solid-liquid point
From equipment, second level double helix solid-liquid separating equipment and third level double helix solid-liquid separating equipment；The offal surge tank passes through
Screw pump is connect with the material inlet of first order double helix solid-liquid separating equipment；
The extracting solution cleaning equipment includes the row that material inlet is connect with first order double helix solid-liquid separating equipment liquid outlet
Slag seperator, the centrifuge that material inlet is connect with slag draining and separating machine liquid outlet, material inlet connect with centrifuge liquid outlet
The disk filter connect, and go out respectively with the outlet of slag draining and separating machine stalk slag, centrifuge stalk slag outlet and disk filter stalk slag
The stalk slag collecting tank of mouth connection.
2. the extraction system of reconstituted tobacco raw material offal according to claim 1, it is characterised in that：The first order double helix
Solid-liquid separating equipment material outlet is connect with second level double helix solid-liquid separating equipment material inlet by the first screw conveyor,
Second level double helix solid-liquid separating equipment material outlet passes through the second spiral shell with third level double helix solid-liquid separating equipment material inlet
Revolve conveyer connection.
3. the extraction system of reconstituted tobacco raw material offal according to claim 1 or claim 2, it is characterised in that：The stalk slag is collected
Tank is connect with first screw conveyor at second level double helix solid-liquid separating equipment material inlet end.
4. the extraction system of reconstituted tobacco raw material offal according to claim 1 or claim 2, it is characterised in that：The second level is double
The liquid outlet of spiral solid-liquid separating equipment and the material inlet of extractor connect.
5. the extraction system of reconstituted tobacco raw material offal according to claim 1 or claim 2, it is characterised in that：The third level is double
First helical feed of the liquid outlet and second level double helix solid-liquid separating equipment material inlet end of spiral solid-liquid separating equipment
Machine connects.
6. the extraction system of reconstituted tobacco raw material offal according to claim 1 or claim 2, it is characterised in that：The first order is double
The liquid outlet of spiral solid-liquid separating equipment and the material inlet of slag draining and separating machine connect.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721774753.3U CN207678831U (en) | 2017-12-18 | 2017-12-18 | A kind of extraction system of reconstituted tobacco raw material offal |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721774753.3U CN207678831U (en) | 2017-12-18 | 2017-12-18 | A kind of extraction system of reconstituted tobacco raw material offal |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207678831U true CN207678831U (en) | 2018-08-03 |
Family
ID=62998183
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721774753.3U Active CN207678831U (en) | 2017-12-18 | 2017-12-18 | A kind of extraction system of reconstituted tobacco raw material offal |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207678831U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107927896A (en) * | 2017-12-18 | 2018-04-20 | 云南昆船环保技术有限公司 | A kind of continuous countercurrent extraction process and its extraction system of reconstituted tobacco raw material offal |
| CN109832655A (en) * | 2019-04-01 | 2019-06-04 | 博颉(上海)管理咨询有限公司 | Heat reconstituted tobacco extract equipment of not burning |
-
2017
- 2017-12-18 CN CN201721774753.3U patent/CN207678831U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107927896A (en) * | 2017-12-18 | 2018-04-20 | 云南昆船环保技术有限公司 | A kind of continuous countercurrent extraction process and its extraction system of reconstituted tobacco raw material offal |
| CN109832655A (en) * | 2019-04-01 | 2019-06-04 | 博颉(上海)管理咨询有限公司 | Heat reconstituted tobacco extract equipment of not burning |
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