CN201962220U - Solid continuous distillation device - Google Patents
Solid continuous distillation device Download PDFInfo
- Publication number
- CN201962220U CN201962220U CN2011200269876U CN201120026987U CN201962220U CN 201962220 U CN201962220 U CN 201962220U CN 2011200269876 U CN2011200269876 U CN 2011200269876U CN 201120026987 U CN201120026987 U CN 201120026987U CN 201962220 U CN201962220 U CN 201962220U
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- distillation
- retort
- steam
- distillation device
- solid
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model relates to a solid continuous distillation device which belongs to the technical field of solid distillation and comprises a distillation retort, wherein the top of the distillation retort is provided with a feeding hole and a secondary steam outlet, a material distributor is arranged below the feeding hole, a steam distributor connected with a steam inlet is arranged in the middle of the distillation retort, a discharge hole is arranged at the bottom of the distillation retort, and a continuous discharging device is arranged at the inner side of the discharge hole. During distillation, the steam distributor is used for guiding steam into the distillation retort, material after fermentation enters from the feeding hole and falls onto the material distributor, and the material distributor is used for uniformly scattering the material downwards continuously. The material encounters with ascending steam in a countercurrent way during falling to conduct heat exchange, alcohol contained in the material is changed into alcohol steam which is brought away by the generated secondary steam, and the material after distillation is constantly accumulated in a discharging bin and is discharged steadily under the propulsion of the continuous discharging device, thus realizing the continuous and direct distillation of solid material. Compared with a traditional distillation device, the solid continuous distillation device has the advantages of high automation degree, large capacity, difficult blockage and the like.
Description
Technical field
The utility model belongs to the solid state distillation technical field, particularly a kind of continous way solid state distillation device.
Background technology
Along with the lasting discharging of the worsening shortages and the greenhouse gases of international crude resources, energy problem has become the great difficult problem of pendulum in face of in various countries, the whole world.The simple coordinated development that relies on fossil energy to be difficult to realize economy, society and environment, Renewable Energy Development, particularly bioenergy are the important outlets that solves energy dilemma.
Alcohol fuel has been realized commercially producing in many countries because its sophisticated production technology and abundant raw material sources have become the bioenergy of countries in the world first-selection.Yet present alcohol fuel is mainly formed by feedstock conversion such as grain and sugarcanes, strives grain with the people, causes global higher food prices.Thereby under this background, be that the cellulose ethanol of raw material becomes the research focus gradually with the agriculture and forestry organic waste material.
At present, more about cellulosic material being converted into alcoholic acid research both at home and abroad, wherein solid state fermentation is one of focus, contains the glycogen material as sweet sorghum or other.Solid state distillation is not only the process of concentrating and separating alcohol, and is the process that fragrance extracts and reconfigures, but generally be intermittently to distill with the rice steamer bucket in China's tradition liquor industry.CN86108012A provides a kind of more rational solid state distillation method and apparatus at bent wine production, and promptly being increases fractionation process on the basis of original rice steamer bucket distillation-water cooler condensation flow process, to improve the output capacity of the bent wine of high-quality, removes the different assorted flavor in the bent wine.Right this device still belongs to batch distillation.
CN1912129A then provides a kind of method of producing ethanol by straw solid fermentation, this method is raw material with the stalk, in fermentor tank, finish the discharge of fermentation back and contain cellulase and zymic mixed bacteria liquid, directly feed steam then and distill, carry out the fermentation of a new round after distillation finishes again from the fermentor tank bottom.Fermentation, distillation hocket in same container, have determined this patented method still to belong to intermittent type, and its equipment therefor also belongs to the intermittent type device naturally.
And for alcohol fuel, output or production efficiency are the important factors of its market position of decision.Along with the continuous increase of market demand, rely on traditional batch distillation device be able to not satisfy the demands.Therefore, it is extremely urgent to develop a kind of continuous still battery equipment of suitable solid state fermentation at cellulose ethanol.
The utility model content
The purpose of this utility model is for a kind of suitable fiber biomass being provided, can realizing the water distilling apparatus that serialization is produced.
For achieving the above object, of the present utility modelly taked following technical scheme:
A kind of solid continuous distillation device, comprise retort, the retort top is provided with opening for feed and secondary steam outlet, the opening for feed below is provided with the material uniform device, the retort middle part is provided with the steam distributor that is connected with steam inlet, retort bottom is provided with discharge port, and the discharge port inboard is provided with continuous discharger, with guarantee after the distillation solid substances continuously, discharge reposefully.
The retort bottom is funnel-form, is for going out feed bin; Continuously discharger is located at out in the feed bin, by forming with the co-axial rotating shaft of retort, axis drive motor and the scraper plate and/or the screw-blade that are located in the rotating shaft.
For further promoting discharging efficient, prevent to stop up, described discharge port is arranged at out the feed bin bottom sides, is circumscribed with discharge nozzle, and discharge nozzle is built-in with pushing screw rod.
Open Side Down for the vapour outlet of steam distributor, can prevent that so not only material from stopping up pore, can also promote the homogeneity of steam simultaneously.
Described secondary steam exit is equipped with scum dredger, is used for the drop of separated secondary entrainment with steam.
Described scum dredger is the board-like scum dredger of screen type, folded plate type, spherical cap type or eddy flow.
During distillation, utilize steam inlet and steam distributor to the inner logical steam of retort earlier, the material after the fermentation enters from opening for feed, falls on the material uniform device, and is continuously evenly dispensed downwards by the material uniform device.Material meets with the steam counter-flow that rises in dropping process, carries out heat exchange, and institute's spirituosity becomes alcohol steam in the material, is taken away by the secondary steam that produces, thereby realizes alcohol distillation.Material after the distillation is constantly going out the feed bin accumulation, and production is so continuously distilled in steadily discharging under the propelling of continuous discharger.Compare with traditional water distilling apparatus, the utility model has been realized the serialization straight run distillation of solid substances, has advantages such as level of automation height, big, the difficult obstruction of production capacity.
Description of drawings
Fig. 1 is the structural representation of solid continuous distillation device among the embodiment 1;
Fig. 2 is the structural representation of solid continuous distillation device among the embodiment 2;
Fig. 3 is the structural representation of solid continuous distillation device among the embodiment 3.
Embodiment
As Figure 1-3, solid continuous distillation device of the present utility model totally can be divided into feed zone 1, distilling period 2 and discharging section 3 three parts, and its middle and upper part feed zone 1 comprises opening for feed 1-1, material uniform device 1-2, secondary steam outlet 1-3 and scum dredger 1-4; Middle part distilling period 2 comprises steam inlet 2-1 and steam distributor 2-2; Bottom discharging section 3 comprises feed bin 3-1, discharge port 3-2 and continuous discharger.
Below in conjunction with concrete drawings and Examples present embodiment is described further.
Embodiment 1:
A kind of solid continuous distillation device, as described in Figure 1, comprise retort 4, retort 4 tops are provided with opening for feed 1-1 and secondary steam outlet 1-3, secondary steam outlet 1-3 below is equipped with spherical cap type scum dredger 1-4, and fixed material uniform device 1-2 then is arranged on opening for feed 1-1 below.
Embodiment 2:
A kind of solid continuous distillation device as described in Figure 2, comprises retort 4, and retort 4 upper portion side wall are provided with opening for feed 1-1, and rotating material uniform device 1-2 is arranged on opening for feed 1-1 below, by external motor by shaft drive.Retort 4 tops are provided with secondary steam outlet 1-3, and secondary steam outlet 1-3 below is equipped with screen type scum dredger 1-4.
Retort 4 middle parts are provided with steam distributor 2-2, and 2-1 is connected with steam inlet, and steam distributor 2-2 is provided with the vapour outlet that Open Side Down.
Embodiment 3:
A kind of solid continuous distillation device, as described in Figure 1, comprise retort 4, retort 4 tops are provided with opening for feed 1-1 and secondary steam outlet 1-3, under the secondary steam outlet 1-3 screen type scum dredger 1-4 is installed, fixed material uniform device 1-2 then is arranged on opening for feed 1-1 below.
Retort 4 middle parts are provided with steam distributor 2-2, and 2-1 is connected with steam inlet, and steam distributor 2-2 is provided with the vapour outlet that Open Side Down.
Claims (6)
1. solid continuous distillation device, comprise retort, the retort top is provided with opening for feed and secondary steam outlet, the opening for feed below is provided with the material uniform device, the retort middle part is provided with the steam distributor that is connected with steam inlet, the retort bottom is provided with discharge port, it is characterized in that the discharge port inboard is provided with continuous discharger.
2. solid continuous distillation device as claimed in claim 1 is characterized in that, the retort bottom is funnel-form, is for going out feed bin; Continuously discharger is located at out in the feed bin, by forming with the co-axial rotating shaft of retort, axis drive motor and the scraper plate and/or the screw-blade that are located in the rotating shaft.
3. solid continuous distillation device as claimed in claim 2 is characterized in that described discharge port is arranged at out the feed bin bottom sides, is circumscribed with discharge nozzle, and discharge nozzle is built-in with pushing screw rod.
4. as the arbitrary described solid continuous distillation device of claim 1-3, it is characterized in that Open Side Down for the vapour outlet of steam distributor.
5. solid continuous distillation device as claimed in claim 4 is characterized in that, described secondary steam exit is equipped with scum dredger.
6. solid continuous distillation device as claimed in claim 5 is characterized in that, described scum dredger is the board-like scum dredger of screen type, folded plate type, spherical cap type or eddy flow.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200269876U CN201962220U (en) | 2011-01-27 | 2011-01-27 | Solid continuous distillation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200269876U CN201962220U (en) | 2011-01-27 | 2011-01-27 | Solid continuous distillation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201962220U true CN201962220U (en) | 2011-09-07 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011200269876U Expired - Lifetime CN201962220U (en) | 2011-01-27 | 2011-01-27 | Solid continuous distillation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201962220U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103131616A (en) * | 2013-02-19 | 2013-06-05 | 河北科技大学 | Device of producing wine by continuously distilling solid fermented grains |
| CN104195023A (en) * | 2014-09-09 | 2014-12-10 | 孙祯芳 | Combined type solid-state distillation device |
| CN105624022A (en) * | 2016-03-16 | 2016-06-01 | 江南大学 | Dry-method ozone pretreatment pretreater capable of increasing straw enzymolysis saccharification ratio and method |
| CN108522937A (en) * | 2017-03-05 | 2018-09-14 | 熊杰 | A kind of superhigh temperature transient surface continuous sterilization process of unsetting solid material |
| CN110373305A (en) * | 2018-04-11 | 2019-10-25 | 北京百漾酒业科技股份有限公司 | The continuous distillation plant and method of white wine |
-
2011
- 2011-01-27 CN CN2011200269876U patent/CN201962220U/en not_active Expired - Lifetime
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103131616A (en) * | 2013-02-19 | 2013-06-05 | 河北科技大学 | Device of producing wine by continuously distilling solid fermented grains |
| CN104195023A (en) * | 2014-09-09 | 2014-12-10 | 孙祯芳 | Combined type solid-state distillation device |
| CN104195023B (en) * | 2014-09-09 | 2015-12-16 | 孙祯芳 | Combined type solid-state water distilling apparatus |
| CN105624022A (en) * | 2016-03-16 | 2016-06-01 | 江南大学 | Dry-method ozone pretreatment pretreater capable of increasing straw enzymolysis saccharification ratio and method |
| CN105624022B (en) * | 2016-03-16 | 2018-06-19 | 江南大学 | A kind of dry method ozone pretreatment pretreater and method for improving stalk enzymatic saccharification rate |
| CN108522937A (en) * | 2017-03-05 | 2018-09-14 | 熊杰 | A kind of superhigh temperature transient surface continuous sterilization process of unsetting solid material |
| CN110373305A (en) * | 2018-04-11 | 2019-10-25 | 北京百漾酒业科技股份有限公司 | The continuous distillation plant and method of white wine |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20110907 |
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| CX01 | Expiry of patent term |