CN206240094U - Integrate the tobacco extract enrichment facility of antiscale, scale removal - Google Patents
Integrate the tobacco extract enrichment facility of antiscale, scale removal Download PDFInfo
- Publication number
- CN206240094U CN206240094U CN201621300375.0U CN201621300375U CN206240094U CN 206240094 U CN206240094 U CN 206240094U CN 201621300375 U CN201621300375 U CN 201621300375U CN 206240094 U CN206240094 U CN 206240094U
- Authority
- CN
- China
- Prior art keywords
- heating chamber
- magnetic valve
- shower nozzle
- pressure wash
- wash shower
- 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.)
- Active
Links
- 241000208125 Nicotiana Species 0.000 title claims abstract description 16
- 235000002637 Nicotiana tabacum Nutrition 0.000 title claims abstract description 16
- 238000010438 heat treatment Methods 0.000 claims abstract description 46
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 23
- 238000007599 discharging Methods 0.000 claims abstract description 9
- 239000002245 particle Substances 0.000 abstract description 8
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 230000001629 suppression Effects 0.000 abstract description 3
- 239000007921 spray Substances 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 9
- 230000000694 effects Effects 0.000 description 6
- 238000009835 boiling Methods 0.000 description 5
- 238000004140 cleaning Methods 0.000 description 5
- 230000008569 process Effects 0.000 description 4
- 239000012141 concentrate Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 230000008719 thickening Effects 0.000 description 3
- 238000007664 blowing Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 239000002360 explosive Substances 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 235000019504 cigarettes Nutrition 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000004925 denaturation Methods 0.000 description 1
- 230000036425 denaturation Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 235000010987 pectin Nutrition 0.000 description 1
- 229920001277 pectin Polymers 0.000 description 1
- 239000001814 pectin Substances 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Cleaning In General (AREA)
Abstract
The utility model belongs to reconstituted tobacco production technical field, and in particular to a kind of tobacco extract enrichment facility for integrating antiscale, scale removal.It includes disk centrifuge, preheating can, heating chamber and vacuum chamber, described disk centrifuge discharging opening is connected with preheating can, described heating chamber is connected with vacuum chamber, it also includes ultrasonic transmitter, high-pressure wash shower nozzle and controller, ultrasonic transmitter is arranged on heating chamber outer wall, high-pressure wash shower nozzle is arranged at heating chamber upper end center position, high-pressure wash shower nozzle is connected by the water inlet pipe through heating room side wall with water pump, water inlet pipe is provided with the first magnetic valve, heating chamber bottom is connected with drainpipe, drainpipe is provided with the second magnetic valve, the control end of controller is connected with the first magnetic valve and the second magnetic valve.Using the growth of the vibration suppression dirt particle of ultrasonic wave.After the completion of concentration, control high-pressure wash shower nozzle sprays water under high pressure and heating chamber interior walls is cleaned, and further heating chamber is cleaned, and prevents fouling.
Description
Technical field
The utility model belongs to reconstituted tobacco production technical field, and in particular to a kind of cigarette for integrating antiscale, scale removal
Careless extract solution enrichment facility.
Background technology
At present in the production of country's papermaking-method reconstituted tobaccos, pharmacy and food that tobacco extract concentrator is typically with
The multiple-effect vacuum concentration systems that industry is used.The operation of the system is：Under certain vacuum condition, with steam indirectly heat side
Formula, heats to extract solution, makes its explosive evaporation at a lower temperature.It is dense if thickening temperature is too low during concentration
The contracting time can be oversize, influences thickening efficiency；But if temperature is too high, the lower boiling aroma component in part can volatilize, and then influence
Concentrate quality.Due to the complexity of tobacco component, in normal concentration process, concentrate can form product on heating surface
Dirt.The existing method for solving scale problems has using methods such as high flow velocities operation, high-pressure water jet scale removal, mechanical descalings.Adopt
Although gathering for dirty body can be suppressed with the method that high flow velocities are run, because the increase of flow velocity causes energy consumption to sharply increase,
It is disagreed with the original intention of energy-conservation.High-pressure water jet scale removal is that the water under high pressure produced using plunger delivery pump is sprayed by special nozzle
To dirty layer, its installed capacity is big, water consumption is more, there are problems that, while also cannot fast and safely arrange dirt after cleaning.Machinery
Scale removal uses strength wiper (having nail wheel wiper and spiral wiper etc.), these piggings totally to manage interior dirt layer one
As need 5-6 times, up to 10 times sometimes, pigging efficiency is low, of poor quality.Be can be seen that by above-mentioned snaking method domestic dense for vacuum
Fouling countermeasure in compression system steam heat-exchanging is mainly the suppression and removal of passive type, cannot be by fouling institute during system operation
The a series of problems for causing thoroughly is solved.
Utility model content
For the above-mentioned deficiency of prior art, the technical problems to be solved in the utility model is to provide a kind of antiscale of collection, removes
Dirt suppresses the growth of the dirty particle of concentration in the tobacco extract enrichment facility of one, and can implement to get express developed, improves heat transfer effect
Rate, is reduced and shuts down the scale removal time, and the purpose of enriching service efficiency is improved so as to reach.
The technical solution of the utility model is to provide a kind of tobacco extract enrichment facility for integrating antiscale, scale removal,
It includes disk centrifuge, preheating can, heating chamber and vacuum chamber, and described disk centrifuge discharging opening is connected with preheating can, institute
The heating chamber stated is connected with vacuum chamber, and it also includes ultrasonic transmitter, high-pressure wash shower nozzle and controller, the ultrasonic wave
Transmitter is arranged on heating chamber outer wall, and the high-pressure wash shower nozzle is arranged at heating chamber upper end center position, the height
Pressure cleaning sprayer is connected by the water inlet pipe through heating room side wall with water pump, and the water inlet pipe is provided with the first magnetic valve, institute
State heating chamber bottom and be connected with drainpipe, the drainpipe is provided with the second magnetic valve, the control end of the controller and first
Magnetic valve and the second magnetic valve are connected.
Further, the high-pressure wash shower nozzle includes the multiple nozzles towards heating chamber interior walls, multiple nozzle edges
Heating chamber interior walls circumferencial direction is evenly arranged.
Further, also including delivery pump, the charging aperture and discharging opening of described delivery pump connect respectively preheating can and plus
Hot cell.
The beneficial effects of the utility model are：Formed using the vibration of ultrasonic wave microjet effect, cavitation and
Mechanism, it is suppressed that the growth of dirty particle.After the completion of concentration process, one-key start controller, control the first magnetic valve and
Second magnetic valve is opened, and each nozzle of high-pressure wash shower nozzle sprays water under high pressure and heating chamber interior walls are cleaned, and sewage passes through
Bottom discharge pipe is discharged, and further heating chamber is cleaned, and prevents fouling.The present apparatus is reasonable in design, simple structure, and operation is held
Easily, obvious technical effects, can effectively suppress to concentrate the growth of dirty particle, improve heat transfer efficiency, reduce and shut down the scale removal time, improve
Tobacco extract thickening efficiency.
Brief description of the drawings
Fig. 1 is the example structure schematic diagram of the utility model one；
Fig. 2 is the arrangement schematic diagram of high-pressure wash shower nozzle top nozzle；
Accompanying drawing acceptance of the bid note is described below：1-butterfly seperator；2-preheating can；3-delivery pump；4-heating chamber；5-true
Empty room；6-ultrasonic transmitter；7-charging aperture；8-slag notch；9-high-pressure wash shower nozzle；10-water inlet pipe；11-draining
Pipe；12-the first magnetic valve；13-the second magnetic valve；14-controller.
Specific embodiment
Specific embodiment of the present utility model is described in further detail below in conjunction with the accompanying drawings.
As shown in figure 1, the utility model includes disk centrifuge 1, preheating can 2, delivery pump 3, heating chamber 4, the and of vacuum chamber 5
Controller 14, the discharging opening of disk centrifuge 1 is connected with preheating can 2, and heating chamber 4 is connected with vacuum chamber 5.The charging of delivery pump 3
Mouth and discharging opening connect preheating can 2 and heating chamber 4 respectively.Ultrasonic transmitter 6 is provided with the outer wall of heating chamber 4, is heated
Water inlet pipe 10 is equipped with the side wall of room 4, the one end of water inlet pipe 10 is connected with a water pump, and the other end is connected with high-pressure wash shower nozzle
9.High-pressure wash shower nozzle 9 is arranged on the central axis of heating chamber 4, and positioned at the top of heating chamber 4.High-pressure wash shower nozzle 9 is around center
Multiple nozzles are evenly distributed with, the nozzle quantity is no less than 3, as shown in Fig. 2 the present embodiment selects 4 nozzles.Water inlet pipe 10
The first magnetic valve 12 is provided with, a drainpipe 11 is additionally provided with the bottom of heating chamber 4, drainpipe 11 is provided with the second magnetic valve
13.The control end of controller 14 is connected with the first magnetic valve 12 and the second magnetic valve 13 respectively, for two magnetic valves of control
Open and close.After controller 14 receives cleaning enabling signal, sent to the first magnetic valve 12 and the second magnetic valve 13 and opened
Signal, the first magnetic valve 12 and the second magnetic valve 13 are opened.Timer is set in controller 14, when timing reaches the nominal time
Afterwards, controller 14 automatically controls the first magnetic valve 12 and the second magnetic valve 13 is closed.
When the device works, made to flocculant is added in tobacco extract by the charging aperture 7 of butterfly seperator 1 first
The materials such as macro-molecular protein, pectin flocculate into bulky grain colloid by bridging action, are separated from tobacco extract, and
Discharged from slag notch 8, so as to avoid because these material toughness are higher, excessive denaturation, caking, the coking for producing etc. of being heated is existing
As also improving rate of heat transfer.
Feed liquid after separation is directly entered preheating can 2 from the discharging opening of butterfly seperator 1 carries out the pre-heat treatment, on the one hand can prevent
Only feed temperature is too big with heating tube wall temperature difference, causes tube wall easily to tie trowel used for plastering, on the other hand can prevent lower boiling material from acutely boiling
Rise and to form unstable foam and taken away by indirect steam, pollute other firing equipments, increase the loss of product.
Flowed out from preheating can 2 by the extract solution after the pre-heat treatment, by delivery pump 3, and the stabilization under its effect, it is even
Fast enters into the heating chamber 4 being connected with the discharging opening of delivery pump 3.
Under the vacuum condition that vacuum chamber 5 is built, the extract solution in heating chamber 4 is heated indirectly with high-temperature steam, make it
Explosive evaporation at a lower temperature, but because the effect of ultrasonic wave, extract solution accelerates vibration boiling, boiling to produce in heating tubulation
Raw vapor is evaporated from the opening of the top of heating chamber 4, so that extract concentration is stepped up, in the process,
Microjet effect, cavitation and the mechanism formed using the vibration of ultrasonic wave, it is suppressed that the growth of dirty particle.Feed liquid
Continuous shuttling movement, blowing is shut down after feed liquid reaches estimated concentration requirement between heating chamber 4 and vacuum chamber 5.
After blowing is finished, controller 14 is started at once and starts to clean heating chamber 4, controller 14 is to the first magnetic valve
12 and the second magnetic valve 13 send open signal, while open cleaning timing.First magnetic valve 12 and the second magnetic valve 13 are opened,
Water pump pumps into high-pressure wash shower nozzle 9 water, is ejected on the inwall of heating chamber 4 through four nozzles.Due to now heating chamber 4
Temperature does not lower also, and dirty particle is due to the suppression of ultrasonic wave, measures less, and adheres to also insecure, through high pressure water washing energy
Easily dirty particle is washed away, the sewage comprising dirty particle is discharged from the drainpipe of bottom.When the internal timer of controller 14 reaches
Afterwards, controller 14 controls the first magnetic valve 12 and the second magnetic valve 13 to close, and cleaning process is finished.
The above, specific embodiment only of the present utility model, it is noted that any to be familiar with those skilled in the art
In the technical scope disclosed by the utility model, the change or replacement that can be readily occurred in should all be covered in the utility model member
Protection domain within.
Claims (3)
1. a kind of tobacco extract enrichment facility for integrating antiscale, scale removal, it includes disk centrifuge (1), preheating can
(2), heating chamber (4) and vacuum chamber (5), described disk centrifuge (1) discharging opening are connected with preheating can (2), described heating
Room (4) is connected with vacuum chamber (5), it is characterised in that：It also includes ultrasonic transmitter (6), high-pressure wash shower nozzle (9) and control
Device (14) processed, the ultrasonic transmitter (6) is arranged on heating chamber (4) outer wall, and the high-pressure wash shower nozzle (9) is arranged at and adds
Hot cell (4) inner upper end center, the high-pressure wash shower nozzle (9) is by the water inlet pipe (10) through heating chamber (4) side wall
It is connected with water pump, the water inlet pipe (10) is provided with the first magnetic valve (12), heating chamber (4) bottom is connected with drainpipe
(11), the drainpipe (11) is provided with the second magnetic valve (13), the control end of the controller (14) and the first magnetic valve and
Second magnetic valve (12) is connected.
2. a kind of tobacco extract enrichment facility for integrating antiscale, scale removal according to claim 1, its feature exists
In：The high-pressure wash shower nozzle (9) includes the multiple nozzles towards heating chamber (4) inwall, and multiple nozzles are along heating chamber (4)
Inwall circumferencial direction is evenly arranged.
3. a kind of tobacco extract enrichment facility for integrating antiscale, scale removal according to claim 1, its feature exists
In：Also include delivery pump (3), the charging aperture and discharging opening of described delivery pump (3) connect preheating can (2) and heating chamber respectively
(4)。
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621300375.0U CN206240094U (en) | 2016-11-30 | 2016-11-30 | Integrate the tobacco extract enrichment facility of antiscale, scale removal |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621300375.0U CN206240094U (en) | 2016-11-30 | 2016-11-30 | Integrate the tobacco extract enrichment facility of antiscale, scale removal |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206240094U true CN206240094U (en) | 2017-06-13 |
Family
ID=59002748
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621300375.0U Active CN206240094U (en) | 2016-11-30 | 2016-11-30 | Integrate the tobacco extract enrichment facility of antiscale, scale removal |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206240094U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108187360A (en) * | 2018-01-25 | 2018-06-22 | 中山中珠环保科技有限公司 | A kind of vaporising device and its technique of four-effect evaporation reducing energy consumption MCE |
-
2016
- 2016-11-30 CN CN201621300375.0U patent/CN206240094U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108187360A (en) * | 2018-01-25 | 2018-06-22 | 中山中珠环保科技有限公司 | A kind of vaporising device and its technique of four-effect evaporation reducing energy consumption MCE |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204522328U (en) | Three grades with function of mechanical steam recompression continuous falling liquid film circulating and evaporating concentration systems | |
| CN206240094U (en) | Integrate the tobacco extract enrichment facility of antiscale, scale removal | |
| CN207221361U (en) | A kind of medicine extracts processing unit (plant) | |
| CN206103386U (en) | Stills for it is novel | |
| CN206739921U (en) | A kind of titanium white flour flow design air-flow crushing tail gas secondary waste heat recycling system | |
| CN107875796A (en) | It is used for the device and method for removing coke-stove gas impurity on coke oven gas pipe | |
| CN207479071U (en) | A kind of washing device for parts | |
| CN104819446B (en) | Energy-saving steam regeneration system and method | |
| CN203329382U (en) | Anti-scaling tobacco extract concentration device | |
| CN106428849A (en) | Filling pipeline system | |
| CN207429814U (en) | A kind of vacuum oil-filter of good filtration effect | |
| CN203976684U (en) | Modified starch production system | |
| CN207838332U (en) | Evaporator and vaporising device | |
| CN108917320A (en) | Medicinal extract pulsation quick sterilization drying cabinet | |
| CN208952144U (en) | A kind of production of corn starch boiler afterheat recycle device | |
| CN108078761A (en) | Medical treatment device is fumigated by a kind of gynaecology | |
| CN203723380U (en) | Spray dryer for drying alligator snapping turtle powder | |
| CN207734777U (en) | Device on coke oven gas pipe for removing coke-stove gas impurity | |
| CN104964576B (en) | A kind of condenser | |
| CN206198720U (en) | A kind of spray drying device for producing sea cucumber soft capsule | |
| CN208784642U (en) | A kind of water circulation mechanism of cleaning equipment | |
| CN103058307B (en) | Novel tower-free multipipe rotating-film deaerator | |
| CN207893738U (en) | A kind of effluent from boiler residual neat recovering system | |
| CN206965165U (en) | Heating distilling device in distilling machinery | |
| CN105972203A (en) | Lysozyme dimer sodium alginate solution preparation degassing and pressure conveying cylinder device capable of adjusting positive pressure and negative pressure automatically |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |