CN106669205A - Positive pressure concentration device - Google Patents
Positive pressure concentration device Download PDFInfo
- Publication number
- CN106669205A CN106669205A CN201710054011.1A CN201710054011A CN106669205A CN 106669205 A CN106669205 A CN 106669205A CN 201710054011 A CN201710054011 A CN 201710054011A CN 106669205 A CN106669205 A CN 106669205A
- Authority
- CN
- China
- Prior art keywords
- tank body
- liquid
- breather
- gas
- positive pressure
- 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.)
- Withdrawn
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/0011—Heating features
- B01D1/0041—Use of fluids
Abstract
The invention relates to the technical field of concentration equipment, and in particular relates to a positive pressure concentration device. The positive pressure concentration device of the invention adopts interlayer liquid for heating and drives boiling type mixing of the liquid in a tank by gas, resulting in low energy consumption, rapid evaporation of liquid in the materials, and high concentration ratio. The liquid material is concentrated under gas protection, the concentrated extract has the characteristics of no oxidation loss, no pollution, and the like, and can be conveniently cleaned.
Description
Technical field
The present invention relates to concentrator technical field, more particularly to a kind of malleation enrichment facility.
Background technology
Enrichment facility (concentration tank) is the conventional production equipment of the industries such as medicine, food, is mainly used in liquid material concentration
With solvent recovery, device is made up of heat exchanger, agitator, concentrator, condenser and pipeline valve etc..
Existing concentrator, evaporation rate is slower, and stirring not in time, has oxygen to contact in heating process, cause material
Oxidational losses, affects concentration speed and quality.Accordingly, it is desirable to provide a kind of new technical scheme is solving the above problems.
The content of the invention
The technical problem to be solved in the present invention is：In order to solve existing concentrator, evaporation rate is slower, stirs too late
When, there is oxygen to contact in heating process, cause material oxidational losses, affect the technical problem of concentration speed and quality, the present invention
A kind of malleation enrichment facility is provided.
The technical solution adopted for the present invention to solve the technical problems is：A kind of malleation enrichment facility, including the tank of sealing
Body, breather and gas distributor, gas distributor is arranged on the bottom of tank inner chamber, one end of breather and gas distributor
Gas access be connected, the other end of breather is extend out to outside tank body from tank body upper surface, is set on the other end of breather
Dismountable sealing-plug is equipped with, the upper end of the tank body is additionally provided with gas outlet, and the shell of the tank body is double casing, point
For internal layer and outer layer, the cavity between internal layer and outer layer forms zone of heating, and the lower end of the tank wall is provided with liquid inlet,
The upper end of tank wall is provided with liquid outlet, and liquid inlet is connected with liquid outlet with zone of heating.In tank body of the present invention
The media such as water, oil can be passed through in the interlayer of outer layer and be heated and cooling for liquid material, gases at high pressure enter from the entrance of breather
Enter tank body, liquid material is entered by gas distributor, then flow out from gas outlet, and take away the moisture in material.
Gas-powered pot liquid boiling type mixes, and consumes energy low, and liquid evaporation speed is fast in material, and cocnentration factor is high, liquid material
Concentrated under gas shield, concentrated extract out, with non-oxidation loss, it is pollution-free the features such as, and cleaning side
Just.
For the ease of the pressure in monitor in real time tank body, on the tank body pressure transducer is additionally provided with.
The invention has the beneficial effects as follows, the malleation enrichment facility of the present invention is heated, in gas-powered tank using interlayer liquid
Liquid boiling formula mixes, and consumes energy low, and liquid evaporation speed is fast in material, and cocnentration factor is high, and liquid material is concentrated under gas shield,
Concentration extract out, with non-oxidation loss, it is pollution-free the features such as, it is and easy to clean.
Description of the drawings
With reference to the accompanying drawings and examples the present invention is further described.
Fig. 1 is the structural representation of optimum embodiment of the present invention.
In figure：1st, tank body, 11, internal layer, 12, outer layer, 2, breather, 3, gas distributor, 4, gas outlet, 5, liquid enters
Mouthful, 6, pressure transducer, 7, pressure transducer.
Specific embodiment
In conjunction with the accompanying drawings, the present invention is further detailed explanation.These accompanying drawings are simplified schematic diagram, only with
The basic structure of the illustration explanation present invention, therefore it only shows the composition relevant with the present invention.
As shown in figure 1, be optimum embodiment of the present invention, a kind of malleation enrichment facility, including tank body 1, the breather 2 of sealing
With gas distributor 3, gas distributor 3 is arranged on the bottom of the inner chamber of tank body 1, one end of breather 2 and the gas of gas distributor 3
Body entrance is connected, and the other end of breather 2 is extend out to outside tank body 1 from the upper surface of tank body 1, is set on the other end of breather 2
Dismountable sealing-plug is equipped with, the upper end of tank body 1 is additionally provided with gas outlet 4, is also equipped with gas outlet 4 dismountable close
Blocking, the shell of tank body 1 is double casing, is divided into internal layer 11 and outer layer 12, and the cavity between internal layer 11 and outer layer 12 is formed and added
Thermosphere, the lower end of the outer wall of tank body 1 is provided with liquid inlet 5, and the upper end of the outer wall of tank body 1 is provided with liquid outlet 6, liquid inlet 5
It is connected with zone of heating with liquid outlet 6.Pressure transducer 7 is additionally provided with tank body 1.
Using front, first the sealing-plug on the other end of the sealing-plug in gas outlet 4 and breather 2 is opened, tank body 1
Built with liquid material to be concentrated, hot water is passed through in the zone of heating of tank body 1 from liquid inlet 5, flows out from liquid outlet 6,
High pressure nitrogen is entered in tank body 1 by gas actuating device from the other end of breather 2, then distributes nitrogen by gas distributor 3,
So that nitrogen distributes in the bottom of tank body 1 to surrounding, into liquid material, then nitrogen flows out from gas outlet 4, liquid material
The moisture of middle evaporation is also taken out of by gas outlet 4 in the lump, and into subsequent condensation retracting device, final liquid material is concentrated.
With the above-mentioned desirable embodiment according to the present invention as enlightenment, by above-mentioned description, relevant staff is complete
Entirely various change and modification can be carried out in the range of without departing from this invention technological thought.The technology of this invention
Property scope is not limited to the content in description, it is necessary to its technical scope is determined according to right.
Claims (2)
1. a kind of malleation enrichment facility, it is characterised in that：Tank body (1), breather (2) and gas distributor (3) including sealing,
Gas distributor (3) is arranged on the bottom of tank body (1) inner chamber, one end of breather (2) and the gas access of gas distributor (3)
It is connected, the other end of breather (2) extend out to tank body (1) outside from tank body (1) upper surface, on the other end of breather (2)
Dismountable sealing-plug is provided with, the upper end of the tank body (1) is additionally provided with gas outlet (4), and the shell of the tank body (1) is
Double casing, is divided into internal layer (11) and outer layer (12), and the cavity between internal layer (11) and outer layer (12) forms zone of heating, the tank
The lower end of body (1) outer wall is provided with liquid inlet (5), and the upper end of tank body (1) outer wall is provided with liquid outlet (6), liquid inlet
(5) it is connected with zone of heating with liquid outlet (6).
2. malleation enrichment facility as claimed in claim 1, it is characterised in that：Pressure transducer is additionally provided with the tank body (1)
(7)。
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710054011.1A CN106669205A (en) | 2017-01-24 | 2017-01-24 | Positive pressure concentration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710054011.1A CN106669205A (en) | 2017-01-24 | 2017-01-24 | Positive pressure concentration device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106669205A true CN106669205A (en) | 2017-05-17 |
Family
ID=58859095
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710054011.1A Withdrawn CN106669205A (en) | 2017-01-24 | 2017-01-24 | Positive pressure concentration device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106669205A (en) |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000225301A (en) * | 1999-02-05 | 2000-08-15 | Ricoh Co Ltd | Organic solvent recovery apparatus and recovery method |
| US20090159421A1 (en) * | 2007-12-21 | 2009-06-25 | Chip Aadland | Portable closed circuit, sealed, pressurized distillation system |
| CN201286988Y (en) * | 2008-08-06 | 2009-08-12 | 杨昌燕 | Dish type single-pore linear falling-film evaporator |
| CN102470336A (en) * | 2010-05-17 | 2012-05-23 | R3融合公司 | Continuous processing reactors and methods of using same |
| CN203030037U (en) * | 2013-01-18 | 2013-07-03 | 湖北中烟工业有限责任公司 | Energy-saving glass extraction tank |
| CN105126363A (en) * | 2015-09-02 | 2015-12-09 | 中国农业科学院蜜蜂研究所 | Concentration device special for propolis extracting solution |
| CN205598674U (en) * | 2016-05-06 | 2016-09-28 | 湖州柳荫生物科技有限公司 | Concentrating tank |
| CN106215441A (en) * | 2016-08-29 | 2016-12-14 | 四川弘毅智慧知识产权运营有限公司 | A kind of anti-riot spherical enrichment facility of thermally equivalent |
| US20170008776A1 (en) * | 2014-01-24 | 2017-01-12 | Starklab | Facility and method for treating water pumped in a natural environment by evaporation/condensation |
-
2017
- 2017-01-24 CN CN201710054011.1A patent/CN106669205A/en not_active Withdrawn
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000225301A (en) * | 1999-02-05 | 2000-08-15 | Ricoh Co Ltd | Organic solvent recovery apparatus and recovery method |
| US20090159421A1 (en) * | 2007-12-21 | 2009-06-25 | Chip Aadland | Portable closed circuit, sealed, pressurized distillation system |
| CN201286988Y (en) * | 2008-08-06 | 2009-08-12 | 杨昌燕 | Dish type single-pore linear falling-film evaporator |
| CN102470336A (en) * | 2010-05-17 | 2012-05-23 | R3融合公司 | Continuous processing reactors and methods of using same |
| CN203030037U (en) * | 2013-01-18 | 2013-07-03 | 湖北中烟工业有限责任公司 | Energy-saving glass extraction tank |
| US20170008776A1 (en) * | 2014-01-24 | 2017-01-12 | Starklab | Facility and method for treating water pumped in a natural environment by evaporation/condensation |
| CN105126363A (en) * | 2015-09-02 | 2015-12-09 | 中国农业科学院蜜蜂研究所 | Concentration device special for propolis extracting solution |
| CN205598674U (en) * | 2016-05-06 | 2016-09-28 | 湖州柳荫生物科技有限公司 | Concentrating tank |
| CN106215441A (en) * | 2016-08-29 | 2016-12-14 | 四川弘毅智慧知识产权运营有限公司 | A kind of anti-riot spherical enrichment facility of thermally equivalent |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| CB02 | Change of applicant information |
Address after: 213000 Changzhou Xinbei District, Jiangsu Province Applicant after: Changzhou Oufu agricultural science and Technology Development Co. Ltd. Address before: 213000 Changzhou City, Jiangsu Province, science and Education City, knowledge and practice building 300 Applicant before: Changzhou Oufu agricultural science and Technology Development Co. Ltd. |
|
| CB02 | Change of applicant information | ||
| WW01 | Invention patent application withdrawn after publication |
Application publication date: 20170517 |
|
| WW01 | Invention patent application withdrawn after publication |