CN108837644A - A kind of oil fog purification plant of glycerol and water - Google Patents
A kind of oil fog purification plant of glycerol and water Download PDFInfo
- Publication number
- CN108837644A CN108837644A CN201810949794.4A CN201810949794A CN108837644A CN 108837644 A CN108837644 A CN 108837644A CN 201810949794 A CN201810949794 A CN 201810949794A CN 108837644 A CN108837644 A CN 108837644A
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- China
- Prior art keywords
- glycerol
- cold water
- slot
- atomization
- storage cistern
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
- B01D47/06—Spray cleaning
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
Abstract
The invention discloses a kind of oil fog purification plants of glycerol and water, including atomization cold water storage cistern and glycerol slot, the atomization cold water storage cistern lower end is equipped with suction opening by air draft pipe, it is atomized cold water storage cistern upper end and exhaust apparatus is connected with by connecting tube, the glycerol slot is mounted on suction opening lower end, and glycerol slot upper end is by being connected on atomization cold water storage cistern communicating pipe.The oil fog purification plant of glycerol and water of the present invention, high-temperature heating glycerol slot greater than 100 degrees Celsius generates hot oil mist, hot oil mist is generated to enter in air draft pipe by suction opening, it is thoroughly mixed into the atomization cold water inside atomization cooling water case, under the hot oil mist for the glycerol being less than after mutually melting under the characteristic that the hot oil mist of glycerol mutually melts with atomization cold water with the strength of exhausting and the gravity of atomization cold water mixture, and then mixture is back to down in glycerol slot, since the boiling point of water is lower than the boiling point of glycerol, water can boil volatilization in the heating tank of high temperature, and then play the effect of recycling glycerol, persistent loop uses.
Description
Technical field
The present invention relates to a kind of purification device, the oil fog purification plant of specifically a kind of glycerol and water.
Background technique
Glycerine, national standard is known as glycerol, colourless, odorless, sweet, and appearance is in clear and bright viscous liquid state, is a kind of organic
Object is commonly called as glycerol.Glycerine can absorb moisture from air, can also absorb hydrogen sulfide, hydrogen cyanide and sulfur dioxide.It is insoluble in
Benzene, chloroform, carbon tetrachloride, carbon disulfide, petroleum ether and oils.
Currently, well known glycerol oil mist filter is directly to take high-temperature oil mist away by exhausting system to coagulate to the cold later
Knot, fraction recycling.The process of the mixture heating evaporation of glycerol and water, due to not handling in time, mist of oil meeting surrounding diffusion,
Then it condenses, causes the pollution of large area that can't recycle.
Summary of the invention
The purpose of the present invention is to provide a kind of oil fog purification plants of glycerol and water, to solve to mention in above-mentioned background technique
Out the problem of.
To achieve the above object, the present invention provides the following technical solutions：
A kind of oil fog purification plant of glycerol and water, including atomization cold water storage cistern and glycerol slot, the atomization cold water storage cistern lower end pass through
Air draft pipe is equipped with suction opening, is atomized cold water storage cistern upper end by connecting tube and is connected with exhaust apparatus, the glycerol slot is mounted on
Suction opening lower end, glycerol slot upper end is by being connected on atomization cold water storage cistern communicating pipe.
As a further solution of the present invention：Industrial refrigerator and atomizer are installed inside the atomization cold water storage cistern.
As further scheme of the invention：The model AC-5B of the industry refrigerator.
As further scheme of the invention：The suction opening setting rotary table big in the small lower end diameter of upper end diameter
Shape.
As further scheme of the invention：Propeller fan, propeller fan are installed inside the exhaust apparatus
It is equipped with exhaust pipe.
As further scheme of the invention：The model SF-5G of the propeller fan.
Compared with prior art, the beneficial effects of the invention are as follows：
The oil fog purification plant of glycerol and water of the present invention, the high-temperature heating glycerol slot greater than 100 degrees Celsius generate hot oil mist, generate
Hot oil mist is entered in air draft pipe by suction opening, is thoroughly mixed into the atomization cold water inside atomization cooling water case, in glycerol
Hot oil mist be less than the hot oil mist of the glycerol after mutually melting with the strength of exhausting under the characteristic mutually melted of atomization cold water and be atomized cold water
Under the gravity of mixture, and then mixture is back to down in glycerol slot, since the boiling point of water is lower than the boiling point of glycerol, in high temperature
Heating tank in water can boil volatilization, and then play the effect of recycling glycerol, persistent loop uses.
Detailed description of the invention
Fig. 1 is a kind of structural schematic diagram of the oil fog purification plant of glycerol and water.
Wherein：Glycerol slot 1, atomization cold water storage cistern 2, suction opening 3, exhaust apparatus 4.
Specific embodiment
Technical solution of the present invention is described in more detail With reference to embodiment.
In the description of the present invention, it is to be understood that, term " center ", " longitudinal direction ", " transverse direction ", "upper", "lower",
The orientation or positional relationship of the instructions such as "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outside" is
It is based on the orientation or positional relationship shown in the drawings, is merely for convenience of description of the present invention and simplification of the description, rather than instruction or dark
Show that signified device or element must have a particular orientation, be constructed and operated in a specific orientation, therefore should not be understood as pair
Limitation of the invention.
In the description of the present invention, it should be noted that unless otherwise clearly defined and limited, term " installation ", " phase
Even ", " connection " shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or be integrally connected；It can
To be mechanical connection, it is also possible to be electrically connected；It can be directly connected, can also can be indirectly connected through an intermediary
Connection inside two elements.For the ordinary skill in the art, above-mentioned term can be understood by concrete condition
Concrete meaning in the present invention.
Embodiment 1
Referring to Fig. 1, a kind of oil fog purification plant of glycerol and water, including atomization cold water storage cistern 2 and glycerol slot 1, the atomization are cold
2 lower end of water tank is equipped with suction opening 3 by air draft pipe, the setting of suction opening 3 in big round table-like of the small lower end diameter of upper end diameter,
It is atomized 2 upper end of cold water storage cistern and exhaust apparatus 4 is connected with by connecting tube, propeller fan, axis circulation are installed inside exhaust apparatus 4
The model SF-5G of blower, propeller fan are equipped with exhaust pipe, and exhaust pipe is communicated to outdoor, and the glycerol slot 1 is mounted on
3 lower end of suction opening, for 1 upper end of glycerol slot by being connected to communicating pipe on atomization cold water storage cistern 2, glycerol slot 1 is being greater than 100 degrees Celsius
Glycerol can generate hot oil mist under the condition of high temperature, hot oil mist can under the guidance of suction opening 3 with the atomization inside atomization cooling water case 2
Cold water is thoroughly mixed, and hot oil mist is dissolved in the mixture liquid that glycerol and water are formed in atomization cold water, and mixture liquid can pass through company
Siphunculus flows back in glycerol slot 1, because glycerol tank liquor temperature is greater than 100 degrees Celsius, a small amount of moisture can be evaporated immediately, from
And the air for keeping the purity of glycerol, and being atomized in cold water storage cistern 2 can be discharged to outdoor with exhaust apparatus 4.
Embodiment 2
Referring to Fig. 1, a kind of oil fog purification plant of glycerol and water, including atomization cold water storage cistern 2 and glycerol slot 1, the atomization are cold
Industrial refrigerator and atomizer, the model AC-5B of industrial refrigerator are installed, atomization 2 lower end of cold water storage cistern leads to inside water tank 2
It crosses air draft pipe and suction opening 3, the setting of suction opening 3 round table-like, the atomization cold water storage cistern 2 big in the small lower end diameter of upper end diameter is installed
Upper end is connected with exhaust apparatus 4 by connecting tube, and propeller fan, the model of propeller fan are equipped with inside exhaust apparatus 4
For SF-5G, propeller fan is equipped with exhaust pipe, and exhaust pipe is communicated to outdoor, and the glycerol slot 1 is mounted under suction opening 3
End, for 1 upper end of glycerol slot by being connected to communicating pipe on atomization cold water storage cistern 2, glycerol slot 1 is being greater than 100 degrees Celsius of the condition of high temperature
Lower glycerol can generate hot oil mist, and hot oil mist can be complete with the atomization cold water inside atomization cooling water case 2 under the guidance of suction opening 3
Mixing, hot oil mist are dissolved in the mixture liquid that glycerol and water are formed in atomization cold water, and mixture liquid can be flowed back to by communicating pipe
In glycerol slot 1, because glycerol tank liquor temperature is greater than 100 degrees Celsius, a small amount of moisture can be evaporated immediately, to keep sweet
The purity of oil, and the air being atomized in cold water storage cistern 2 can be discharged to outdoor with exhaust apparatus 4.
The working principle of the invention is：The oil fog purification plant of glycerol and water of the present invention, the high temperature greater than 100 degrees Celsius add
Hot glycerine slot 1 generates hot oil mist, generates hot oil mist and is entered in air draft pipe by suction opening 3, into inside atomization cooling water case 2
Atomization cold water be thoroughly mixed, glycerol hot oil mist under the characteristic mutually melted of atomization cold water and the strength of exhausting is less than after mutually melting
The hot oil mist of glycerol and the gravity of atomization cold water mixture under, and then mixture is back to down in glycerol slot 1, due to water
Boiling point is lower than the boiling point of glycerol, and water can boil volatilization in the heating tank of high temperature, and then plays the effect for recycling glycerol, persistently follows
Ring uses.
Better embodiment of the invention is explained in detail above, but the present invention is not limited to above-mentioned embodiment party
Formula within the knowledge of one of ordinary skill in the art can also be without departing from the purpose of the present invention
Various changes can be made.
Claims (6)
1. a kind of oil fog purification plant of glycerol and water, including atomization cold water storage cistern（2）With glycerol slot（1）, which is characterized in that it is described
It is atomized cold water storage cistern（2）Lower end is equipped with suction opening by air draft pipe（3）, it is atomized cold water storage cistern（2）Upper end is connected by connecting tube
There is exhaust apparatus（4）, the glycerol slot（1）It is mounted on suction opening（3）Lower end, glycerol slot（1）Upper end is connected to by communicating pipe
It is atomized cold water storage cistern（2）On.
2. a kind of oil fog purification plant of glycerol and water according to claim 1, which is characterized in that the atomization cold water storage cistern
（2）Inside is equipped with industrial refrigerator and atomizer.
3. a kind of oil fog purification plant of glycerol and water according to claim 2, which is characterized in that the industry refrigerator
Model AC-5B.
4. a kind of oil fog purification plant of glycerol and water according to claim 1, which is characterized in that the suction opening（3）
It is arranged in big round table-like of the small lower end diameter of upper end diameter.
5. a kind of oil fog purification plant of glycerol and water according to claim 1, which is characterized in that the exhaust apparatus
（4）Inside is equipped with propeller fan, and propeller fan is equipped with exhaust pipe.
6. a kind of oil fog purification plant of glycerol and water according to claim 6, which is characterized in that the propeller fan
Model SF-5G.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810949794.4A CN108837644A (en) | 2018-08-20 | 2018-08-20 | A kind of oil fog purification plant of glycerol and water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810949794.4A CN108837644A (en) | 2018-08-20 | 2018-08-20 | A kind of oil fog purification plant of glycerol and water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108837644A true CN108837644A (en) | 2018-11-20 |
Family
ID=64188194
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810949794.4A Pending CN108837644A (en) | 2018-08-20 | 2018-08-20 | A kind of oil fog purification plant of glycerol and water |
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| Country | Link |
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| CN (1) | CN108837644A (en) |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB191015829A (en) * | 1910-07-01 | 1911-05-25 | Alfred Julius Boult | Improvements in or relating to the Production of Polyglycerins. |
| JP2005307086A (en) * | 2004-04-23 | 2005-11-04 | Toshiba Corp | Thermal decomposition treatment system |
| US20080305445A1 (en) * | 2007-06-06 | 2008-12-11 | North Carolina State University | Process for combustion of high viscosity low heating value liquid fuels |
| JP2010285320A (en) * | 2009-06-12 | 2010-12-24 | Ihi Corp | Glycerol reformer and reforming method |
| CN102794134A (en) * | 2012-09-04 | 2012-11-28 | 如皋市双马化工有限公司 | Discharge structure of glycerol granulation tower |
| CN203620281U (en) * | 2013-12-26 | 2014-06-04 | 无锡联威科技有限公司 | Glycerol recovery device |
| CN204830107U (en) * | 2015-07-29 | 2015-12-02 | 焦作大学 | Dirty environmental protection equipment of high -efficient oil extraction |
| US20160347697A1 (en) * | 2015-05-26 | 2016-12-01 | Council Of Scientific & Industrial Research | Process for recovery of pure components from product mixture of one step dimethyl ether synthesis reactor |
-
2018
- 2018-08-20 CN CN201810949794.4A patent/CN108837644A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB191015829A (en) * | 1910-07-01 | 1911-05-25 | Alfred Julius Boult | Improvements in or relating to the Production of Polyglycerins. |
| JP2005307086A (en) * | 2004-04-23 | 2005-11-04 | Toshiba Corp | Thermal decomposition treatment system |
| US20080305445A1 (en) * | 2007-06-06 | 2008-12-11 | North Carolina State University | Process for combustion of high viscosity low heating value liquid fuels |
| JP2010285320A (en) * | 2009-06-12 | 2010-12-24 | Ihi Corp | Glycerol reformer and reforming method |
| CN102794134A (en) * | 2012-09-04 | 2012-11-28 | 如皋市双马化工有限公司 | Discharge structure of glycerol granulation tower |
| CN203620281U (en) * | 2013-12-26 | 2014-06-04 | 无锡联威科技有限公司 | Glycerol recovery device |
| US20160347697A1 (en) * | 2015-05-26 | 2016-12-01 | Council Of Scientific & Industrial Research | Process for recovery of pure components from product mixture of one step dimethyl ether synthesis reactor |
| CN204830107U (en) * | 2015-07-29 | 2015-12-02 | 焦作大学 | Dirty environmental protection equipment of high -efficient oil extraction |
Non-Patent Citations (1)
| Title |
|---|
| 赵晓;陈冠益;颜蓓蓓;刘宗攀;赵丽霞;张枭雄;: "生物质与甘油共气化正交法实验研究", 太阳能学报, no. 11 * |
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