CN207822641U - A kind for the treatment of tank reducing the loss of papermaking-method reconstituted tobaccos extracting solution - Google Patents
A kind for the treatment of tank reducing the loss of papermaking-method reconstituted tobaccos extracting solution Download PDFInfo
- Publication number
- CN207822641U CN207822641U CN201820038760.5U CN201820038760U CN207822641U CN 207822641 U CN207822641 U CN 207822641U CN 201820038760 U CN201820038760 U CN 201820038760U CN 207822641 U CN207822641 U CN 207822641U
- Authority
- CN
- China
- Prior art keywords
- tank
- extracting solution
- filter screen
- tank body
- loss
- 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.)
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Links
- 241000208125 Nicotiana Species 0.000 title claims abstract description 16
- 235000002637 Nicotiana tabacum Nutrition 0.000 title claims abstract description 16
- 238000000034 method Methods 0.000 title claims abstract description 11
- 239000007788 liquid Substances 0.000 claims abstract description 18
- 239000000654 additive Substances 0.000 claims abstract description 9
- 230000000996 additive effect Effects 0.000 claims abstract description 9
- 239000010865 sewage Substances 0.000 claims abstract description 6
- 229910001220 stainless steel Inorganic materials 0.000 claims description 2
- 239000010935 stainless steel Substances 0.000 claims description 2
- 239000006228 supernatant Substances 0.000 abstract description 9
- 238000005189 flocculation Methods 0.000 abstract description 6
- 230000016615 flocculation Effects 0.000 abstract description 6
- 238000009434 installation Methods 0.000 abstract description 5
- 239000013049 sediment Substances 0.000 abstract description 5
- 239000012530 fluid Substances 0.000 abstract description 2
- 238000012544 monitoring process Methods 0.000 abstract description 2
- 239000002245 particle Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 230000002776 aggregation Effects 0.000 description 2
- 238000004220 aggregation Methods 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000000758 substrate Substances 0.000 description 2
- 229920002472 Starch Polymers 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 230000003311 flocculating effect Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 229920001277 pectin Polymers 0.000 description 1
- 235000010987 pectin Nutrition 0.000 description 1
- 239000001814 pectin Substances 0.000 description 1
- 235000018102 proteins Nutrition 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 230000001953 sensory effect Effects 0.000 description 1
- 230000000391 smoking effect Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
A kind for the treatment of tank reducing the loss of papermaking-method reconstituted tobaccos extracting solution, rotation seat including tank body, set on top of the tank, the rotation seat center is equipped with shaft, it is linked motor by gearing the shaft upper end, the shaft lower end is equipped with agitating device, and the agitating device closes on side wall and is equipped with density sensor and density display；The top of the tank is equipped with additive charge door by motor side, and tank wall is equipped with visor below the additive charge door, and the visor lower end is equipped with filter screen, and the corresponding position of the filter screen is equipped with liquid outlet；The top of the tank other side is equipped with inlet tube；The tank body lower end is equipped with supporting rack；Affiliated tank body centre bottom is equipped with blowdown valve and sewage draining exit.The utility model accurately observes liquid situation, avoids the loss of extracting solution by the change of the installation monitoring fluid density of on-line densimeter；By the installation of tank wall lower end filter screen, the sediment after pre- preventing flocculation is mixed into supernatant, ensures the degree of purity of extracting solution, improves the quality of extracting solution.
Description
Technical field
The utility model is related to papermaking-method reconstituted tobaccos field, specifically a kind of reduction papermaking-method reconstituted tobaccos extracting solution damage
The treatment tank of mistake.
Background technology
Papermaking-method reconstituted tobaccos production technology is that the raw materials such as the offal that will be discarded, offal are separated by solid-liquid separation after extraction, Gu
Body portion mixes with other non-tobacco raw-materials and manufactures paper with pulp into substrate, returns and is coated onto on substrate after the extracting solution containing soluble matter is concentrated.
Tobacco extract contains tobacco flavor material most in raw material, its quality directly determines the physics and chemistry of final products
Matter and aesthetic quality.Contain a large amount of protein, starch, pectin etc. in extracting solution when reconstituted tobacco produces after separation of solid and liquid
Macromolecular substances and fiber fines suspended matter, it will usually which flocculant is added, and so that these is unfavorable for the flocculation of the substance of sensory evaluating smoking heavy
It forms sediment, supernatant further cleans through disk centrifuge, so that extracting solution quality-improving.
After sedimentation time reaches technological requirement regulation, operating personnel, which open Pump for giving-out, makes supernatant enter disk centrifuge,
Whether supernatant has gone out from the outside of visor；And the sediment after flocculating then is discharged by settling tank bottom blow-down mouth.But it is real
Since extracting solution coloration is deeper when border is run, operating personnel often can not accurately observe liquid situation, can only by virtue of experience estimate
The liquid level of supernatant, and need the discharge of reserved liquid level to ensure to extract to avoid the sediment after flocculation from being mixed into supernatant
The degree of purity of liquid.This not only causes the loss of reconstituted tobacco extracting solution, also affects the stability of product quality.
Utility model content
For deficiencies of the prior art, the utility model provides a kind of reduction papermaking-method reconstituted tobaccos extracting solution
The treatment tank of loss effectively improves the quality of extracting solution, surely by the installation of on-line densimeter and tank wall lower end filter screen
Fixed output quota quality.
A kind for the treatment of tank reducing the loss of papermaking-method reconstituted tobaccos extracting solution, including tank body, the rotation set on top of the tank
Seat, the rotation seat center are equipped with shaft, and by gearing linkage motor, the shaft lower end is equipped with and stirs for the shaft upper end
Device is mixed, the agitating device closes on side wall and is equipped with density sensor and density display；The top of the tank leans on motor side
Equipped with additive charge door, tank wall is equipped with visor below the additive charge door, and the visor lower end is equipped with filter screen,
The corresponding position of the filter screen is equipped with liquid outlet；The top of the tank other side is equipped with inlet tube；The tank body lower end is set
There is supporting rack；Affiliated tank body centre bottom is equipped with blowdown valve and sewage draining exit.
Preferably, the filter screen be stainless steel filter screen, the filter screen at least provided with two layers, the filter screen with
The joint of tank body is provided with gasket.
The utility model is accurately observed liquid situation, is kept away by the change of the installation monitoring fluid density of on-line densimeter
Exempt from the loss of extracting solution；By the installation of tank wall lower end filter screen, the sediment after pre- preventing flocculation is mixed into supernatant, ensures
The degree of purity of extracting solution improves the quality of extracting solution.
Description of the drawings
Fig. 1 is the structural schematic diagram of the utility model.
In figure：1-tank body, 2-rotation seats, 3-shafts, 4-gearings, 5-motors, 6-agitating devices, 7-add
Add agent charge door, 8-inlet tubes, 9-visors, 10-density sensors, 11-density displays, 12-filter screens, 13-go out
Liquid mouth, 14-supporting racks, 15-blowdown valves, 16-sewage draining exits.
Specific implementation mode
The principles of the present invention and feature are described below in conjunction with attached drawing, example is served only for explaining this practicality
It is novel, it is not intended to limit the scope of the utility model.
As shown in Figure 1, it is a kind of reduce papermaking-method reconstituted tobaccos extracting solution loss treatment tank, including tank body 1, be set to tank body
1 top rotation seat 2,2 center of the rotation seat be equipped with shaft 3,3 upper end of the shaft by gearing 4 link motor 5,
3 lower end of the shaft is equipped with agitating device 6, and the agitating device 6 closes on side wall and is equipped with density sensor 10 and density display
11；1 top of the tank body is equipped with additive charge door 7 by 5 side of motor, and 7 lower section tank body of additive charge door, 1 side wall is set
There are visor 9,9 lower end of the visor to be equipped with filter screen 12,12 corresponding position of the filter screen is equipped with liquid outlet 13；The tank body
1 top other side is equipped with inlet tube 8；The tank body lower end is equipped with supporting rack 14；Affiliated tank body centre bottom is equipped with blowdown
Valve 15 and sewage draining exit 16.
Originally the operation principle for being utility model is：Extracting solution is put into refined tank body 1 by inlet tube 8, opens motor 5,
Rotation seat 2, gearing 4, shaft 3 and agitating device 6 start.Flocculant is added by additive charge door 7, stirring reaches work
After skill requires, motor 5 is closed, is stood, flocculant is sufficiently mixed with extracting solution, different segment absorption in the macromolecular chain of flocculant
On variable grain, promote particle and particle aggregation that many independent particles in suspension is made to form aggregation (floc sedimentation).When standing
Between reach technological requirement after, open liquid outlet 13, pass through visor 9, density sensor 10 and density display 11 observe supernatant
Impurity can further be removed by filter screen 12 when supernatant goes out liquid by going out liquid situation；Lower part contain flocculation group mixed liquor relatively on
Clear liquid density is big, and liquid outlet 13 is closed when density significant changes.Blowdown valve 15 and sewage draining exit 16 are opened, discharge contains flocculation group
Mixed liquor, flow terminate.
The above is only the preferred embodiment of the present invention, is not intended to limit the utility model, all in this practicality
Within novel spirit and principle, made by any modification, equivalent replacement etc., should be included in the scope of protection of the utility model
Within.
Claims (2)
1. a kind for the treatment of tank reducing the loss of papermaking-method reconstituted tobaccos extracting solution, it is characterised in that：Including tank body (1), it is set to tank
Rotation seat (2) at the top of body, rotation seat (2) center are equipped with shaft (3), and shaft (3) upper end passes through gearing (4)
Link motor (5), and shaft (3) lower end is equipped with agitating device (6), and the agitating device (6) is closed on side wall and passed equipped with density
Sensor (10) and density display (11)；The top of the tank is equipped with additive charge door (7), the additive by motor side
Tank wall is equipped with visor (9) below charge door (7), and visor (9) lower end is equipped with filter screen (12), the filter screen (12)
Corresponding position is equipped with liquid outlet (13)；The top of the tank other side is equipped with inlet tube (8)；The tank body lower end is equipped with branch
Support (14)；Affiliated tank body centre bottom is equipped with blowdown valve (15) and sewage draining exit (16).
2. reducing the treatment tank of papermaking-method reconstituted tobaccos extracting solution loss as described in claim 1, it is characterised in that：The mistake
Strainer (12) is stainless steel filter screen, and the filter screen (12) is at least provided with two layers, the filter screen (12) and tank body (1)
Joint is provided with gasket.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820038760.5U CN207822641U (en) | 2018-01-10 | 2018-01-10 | A kind for the treatment of tank reducing the loss of papermaking-method reconstituted tobaccos extracting solution |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820038760.5U CN207822641U (en) | 2018-01-10 | 2018-01-10 | A kind for the treatment of tank reducing the loss of papermaking-method reconstituted tobaccos extracting solution |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207822641U true CN207822641U (en) | 2018-09-07 |
Family
ID=63392408
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820038760.5U Active CN207822641U (en) | 2018-01-10 | 2018-01-10 | A kind for the treatment of tank reducing the loss of papermaking-method reconstituted tobaccos extracting solution |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207822641U (en) |
-
2018
- 2018-01-10 CN CN201820038760.5U patent/CN207822641U/en active Active
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