CN105169732B - A kind of destilling tower - Google Patents
A kind of destilling tower Download PDFInfo
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- CN105169732B CN105169732B CN201510576329.7A CN201510576329A CN105169732B CN 105169732 B CN105169732 B CN 105169732B CN 201510576329 A CN201510576329 A CN 201510576329A CN 105169732 B CN105169732 B CN 105169732B
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Abstract
The invention discloses a kind of destilling tower, including steam inlet, pure steam import, gas-liquid separation chamber, funnel, demarcation strip, air storage chamber, steam boiling water outlet, raw material water inlet, catalyst inlet, vaporization chamber, heat-insulation layer and distilled water outlet, the steam inlet is located at the upper end of vaporization chamber, one end of the vaporization chamber is provided with steam inlet, the other end of the vaporization chamber is provided with catalyst inlet, the heat-insulation layer is wrapped in the outer end of vaporization chamber, the distilled water outlet is located at the bottom side of vaporization chamber, the gas-liquid separation chamber is located at the lower end of vaporization chamber, the pure steam import is located at one end of gas-liquid separation chamber, the funnel is located at the lower end of gas-liquid separation chamber, the air storage chamber is located at the lower section of gas-liquid separation chamber, demarcation strip is provided between the air storage chamber and gas-liquid separation chamber.The destilling tower can accelerate the progress of distillation using catalyst inlet, and distilling effect is good, utilizes multistage evaporation so that evaporation efficiency more preferably, is not easily blocked, simple in construction, cost is low.
Description
Technical field
The invention belongs to destilling tower technical field, and in particular to a kind of destilling tower.
Background technology
Cellulose ethanol is one of direction that new energy is given priority to, and large-scale industrial production is there is no so far.Due to production
Raw material used in cellulose ethanol is biomass cellulose, with the starchy material of existing ripe production alcohol fuel completely not
Together, production technologies and equipment therefore used in both are entirely different.Due to the reason of raw material, contain in fermenting cellulosic ethanol liquid big
The solid fiber particles of amount, in still-process, are particularly easy to block distillation equipment.Traditional packed tower pressure drop is small, operates bullet
Property it is big, be particularly suitable for use in large-scale tower；But easily blocked in use, and clean difficult after blocking, seriously hinder it containing solid
Body granule materials separate the application of occasion, the particularly application in cellulose ethanol production.
The content of the invention
It is an object of the invention to provide a kind of destilling tower, to solve the problems mentioned in the above background technology.
To achieve the above object, the present invention provides following technical scheme：A kind of destilling tower, including steam inlet, pure steam
Import, gas-liquid separation chamber, funnel, demarcation strip, air storage chamber, the outlet of steaming boiling water, raw material water inlet, catalyst inlet, vaporization chamber, guarantor
Warm layer and distilled water outlet, the steam inlet are located at the upper end of vaporization chamber, and the upper end side of the vaporization chamber is entered provided with steam
Mouthful, the vaporization chamber upper end is provided with catalyst inlet relative to the opposite side of steam inlet, and the heat-insulation layer is wrapped in vaporization chamber
Outer end, the distilled water outlet is located at the bottom side of vaporization chamber, and the gas-liquid separation chamber is located at the lower end of vaporization chamber, described
Pure steam import is located at one end of gas-liquid separation chamber, and the funnel is located at the lower end of gas-liquid separation chamber, and the air storage chamber is located at gas
The lower section of liquid separation chamber, is provided with demarcation strip between the air storage chamber and gas-liquid separation chamber.
It is preferred that, the funnel is V-structure.
It is preferred that, the bottom of the funnel is run through demarcation strip and is connected in air storage chamber.
The technique effect and advantage of the present invention：The destilling tower can accelerate the progress of distillation, distillation using catalyst inlet
Effect is good, utilizes multistage evaporation so that evaporation efficiency more preferably, is not easily blocked, simple in construction, cost is low.
Brief description of the drawings
Fig. 1 is structural representation of the invention.
In figure：1st, steam inlet；2nd, pure steam import；3rd, gas-liquid separation chamber；4th, funnel；5th, demarcation strip；6th, air storage chamber；7、
Steam boiling water outlet；8th, raw material water inlet；9th, catalyst inlet；10th, vaporization chamber；11st, heat-insulation layer and 12, distilled water outlet.
Embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Site preparation is described, it is clear that described embodiment is only a part of embodiment of the invention, rather than whole embodiments.It is based on
Embodiment in the present invention, it is every other that those of ordinary skill in the art are obtained under the premise of creative work is not made
Embodiment, belongs to the scope of protection of the invention.
The invention provides a kind of destilling tower as shown in Figure 1, including steam inlet 1, pure steam import 2, gas-liquid separation
Room 3, funnel 4, demarcation strip 5, air storage chamber 6, steaming boiling water outlet 7, raw material water inlet 8, catalyst inlet 9, vaporization chamber 10, heat-insulation layer
11 and distilled water outlet 12, steam inlet 1 is located at the upper end of vaporization chamber 10, and the upper end side of the vaporization chamber 10 is entered provided with steam
Mouth 1, the upper end of vaporization chamber 10 is provided with catalyst inlet 9 relative to the opposite side of steam inlet 1, and heat-insulation layer 11 is wrapped in evaporation
The outer end of room 10, distilled water outlet 12 is located at the bottom side of vaporization chamber 10, and gas-liquid separation chamber 3 is located at the lower end of vaporization chamber 10,
Pure steam import 2 is located at one end of gas-liquid separation chamber 3, and funnel 4 is located at the lower end of gas-liquid separation chamber 3, and funnel 4 is V-structure, storage
Air chamber 6 is located at the lower section of gas-liquid separation chamber 3, demarcation strip 5 is provided between air storage chamber 6 and gas-liquid separation chamber 3, the bottom of funnel 4 is passed through
Wear demarcation strip 5 and be connected in air storage chamber 6.
Operation principle：The progress of distillation can be accelerated using catalyst inlet 9, distilling effect is good, using multistage evaporation, makes
Obtain evaporation efficiency more preferably, be not easily blocked, simple in construction, cost is low.
Finally it should be noted that：The preferred embodiments of the present invention are the foregoing is only, are not intended to limit the invention,
Although the present invention is described in detail with reference to the foregoing embodiments, for those skilled in the art, it still may be used
To be modified to the technical scheme described in foregoing embodiments, or equivalent substitution is carried out to which part technical characteristic,
Within the spirit and principles of the invention, any modification, equivalent substitution and improvements made etc., should be included in the present invention's
Within protection domain.
Claims (3)
1. a kind of destilling tower, including steam inlet（1）, pure steam import（2）, gas-liquid separation chamber（3）, funnel（4）, demarcation strip
（5）, air storage chamber（6）, steam boiling water outlet（7）, raw material water inlet（8）, catalyst inlet（9）, vaporization chamber（10）, heat-insulation layer（11）
And distilled water outlet（12）, it is characterised in that：The steam inlet（1）It is located at vaporization chamber（10）Upper end, the vaporization chamber
（10）Upper end side be provided with steam inlet（1）, the vaporization chamber（10）Upper end is relative to steam inlet（1）Opposite side be provided with
Catalyst inlet（9）, the heat-insulation layer（11）It is wrapped in vaporization chamber（10）Outer end, the distilled water outlet（12）It is located at evaporation
Room（10）Bottom side, the gas-liquid separation chamber（3）It is located at vaporization chamber（10）Lower end, the pure steam import（2）It is located at
Gas-liquid separation chamber（3）One end, the funnel（4）It is located at gas-liquid separation chamber（3）Lower end, the air storage chamber（6）It is located at gas-liquid
Separation chamber（3）Lower section, the air storage chamber（6）And gas-liquid separation chamber（3）Between be provided with demarcation strip（5）.
2. a kind of destilling tower according to claim 1, it is characterised in that：The funnel（4）For V-structure.
3. a kind of destilling tower according to claim 1, it is characterised in that：The funnel（4）Bottom run through demarcation strip（5）
And it is connected to air storage chamber（6）It is interior.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510576329.7A CN105169732B (en) | 2015-09-11 | 2015-09-11 | A kind of destilling tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510576329.7A CN105169732B (en) | 2015-09-11 | 2015-09-11 | A kind of destilling tower |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105169732A CN105169732A (en) | 2015-12-23 |
| CN105169732B true CN105169732B (en) | 2017-09-26 |
Family
ID=54892451
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510576329.7A Active CN105169732B (en) | 2015-09-11 | 2015-09-11 | A kind of destilling tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105169732B (en) |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| NL8005927A (en) * | 1979-11-22 | 1981-06-16 | Kotobuki Seihan Printing Co | METHOD AND APPARATUS FOR RE-SHARPENING CUTTING TOOLS BY AN ELECTROPOLISHING PROCESS. |
| CN102080040A (en) * | 2009-11-26 | 2011-06-01 | 河南农业大学 | Complete plant for producing straw cellulosic ethanol |
| CN202289510U (en) * | 2011-10-26 | 2012-07-04 | 上海煦旻化工科技发展有限公司 | Anti-blocking distillation tower distributor |
| CN203829677U (en) * | 2014-05-21 | 2014-09-17 | 郑州凯山生化工程有限公司 | Cellulosic ethanol four-tower distillation apparatus |
| CN205031914U (en) * | 2015-09-11 | 2016-02-17 | 湖州周吴鼎盛化工有限公司 | Distillation tower |
-
2015
- 2015-09-11 CN CN201510576329.7A patent/CN105169732B/en active Active
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| Publication number | Publication date |
|---|---|
| CN105169732A (en) | 2015-12-23 |
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| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CB03 | Change of inventor or designer information |
Inventor after: Tian Xufeng Inventor before: Pan Lianjiang |
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| CB03 | Change of inventor or designer information | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20171205 Address after: 101200, No. 28, West Street, Pinggu Town, Pinggu District, Beijing (Pinggu town government hospital) Patentee after: TIAN XUFENG Address before: 313000, No. 118, cool mountain road, Huzhou Industrial Zone, Nanxun Town, Zhejiang, China Patentee before: HUZHOU ZHOUWU DINGSHENG CHEMICAL CO., LTD. |
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| TR01 | Transfer of patent right | ||
| CP03 | Change of name, title or address |
Address after: 101299 No. 28, Fu Qian West Street, Pinggu Town, Pinggu District, Beijing (Pinggu town government hospital) Patentee after: Union think (Beijing) Environmental Engineering Co., Ltd. Address before: 101200 No. 28, Fu Qian West Street, Pinggu Town, Pinggu District, Beijing (Pinggu town government hospital) Patentee before: TIAN XUFENG |
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| CP03 | Change of name, title or address |