CN105058580B - High-speed air-exhausting and defoaming stirring machine - Google Patents
High-speed air-exhausting and defoaming stirring machine Download PDFInfo
- Publication number
- CN105058580B CN105058580B CN201510529399.7A CN201510529399A CN105058580B CN 105058580 B CN105058580 B CN 105058580B CN 201510529399 A CN201510529399 A CN 201510529399A CN 105058580 B CN105058580 B CN 105058580B
- Authority
- CN
- China
- Prior art keywords
- mixer housing
- blast pipe
- puddler
- stirring machine
- air
- 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.)
- Expired - Fee Related
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B28—WORKING CEMENT, CLAY, OR STONE
- B28C—PREPARING CLAY; PRODUCING MIXTURES CONTAINING CLAY OR CEMENTITIOUS MATERIAL, e.g. PLASTER
- B28C5/00—Apparatus or methods for producing mixtures of cement with other substances, e.g. slurries, mortars, porous or fibrous compositions
- B28C5/08—Apparatus or methods for producing mixtures of cement with other substances, e.g. slurries, mortars, porous or fibrous compositions using driven mechanical means affecting the mixing
- B28C5/10—Mixing in containers not actuated to effect the mixing
- B28C5/12—Mixing in containers not actuated to effect the mixing with stirrers sweeping through the materials, e.g. with incorporated feeding or discharging means or with oscillating stirrers
- B28C5/14—Mixing in containers not actuated to effect the mixing with stirrers sweeping through the materials, e.g. with incorporated feeding or discharging means or with oscillating stirrers the stirrers having motion about a horizontal or substantially horizontal axis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B28—WORKING CEMENT, CLAY, OR STONE
- B28C—PREPARING CLAY; PRODUCING MIXTURES CONTAINING CLAY OR CEMENTITIOUS MATERIAL, e.g. PLASTER
- B28C5/00—Apparatus or methods for producing mixtures of cement with other substances, e.g. slurries, mortars, porous or fibrous compositions
- B28C5/08—Apparatus or methods for producing mixtures of cement with other substances, e.g. slurries, mortars, porous or fibrous compositions using driven mechanical means affecting the mixing
- B28C5/0806—Details; Accessories
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Structural Engineering (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Accessories For Mixers (AREA)
Abstract
A high-speed air-exhausting and defoaming stirring machine comprises a stirring machine shell and a transmission component, wherein a feeding inlet is formed in the top of the stirring machine shell; a discharging outlet is formed in the bottom of the stirring machine shell; a stirring rod is arranged in the stirring machine shell and connected with the stirring machine shell through a fixing frame; the transmission component is connected with the stirring rod. The high-speed air-exhausting and defoaming stirring machine is further provided with an exhaust fan which is connected with the stirring machine shell through an exhaust pipe and the exhaust pipe is communicated with the inside of the stirring machine shell. When the high-speed air-exhausting and defoaming stirring machine is used for stirring filling slurry, air in the filling slurry can be exhausted through the exhaust pipe. Therefore, the full package degree of the filling slurry is increased, an air blockage phenomenon is avoided, and conveying efficiency is improved.
Description
Technical field
The present invention relates to one kind exhaust de-bubble homogenizer.
Background technology
In the whipping process for carrying out last mortar, in order to filling slurry be stirred, it is necessary to be reached using some devices
To preferable mixing effect.
Generally, in order to ensure the mixing effect of filling slurry, the puddler for generally using works as tailings for cylindric
When thicker, puddler can wear and tear quickly；Simultaneously as a upper link of high-speed stirred can bring some air entrainments into casting resin
Among slurry, when these air accumulations are larger air bubble, the full packages degree of filling slurry conveying is often influenced whether, when serious
Air lock can be formed, conveying effect is exerted an adverse impact, or even cause plugging booster.
At present, also without a kind of agitating device of effective exhaust de-bubble.
The content of the invention
The technical problems to be solved by the invention are to overcome the shortcomings of above-mentioned background technology, there is provided one kind can increase filling
The full packages degree of slurry, it is to avoid form air lock, extends the use time of puddler, improves the exhaust de-bubble high-speed stirring of transfer efficiency
Mix machine.
The technical scheme that the present invention solves the use of its technical problem is that one kind is vented de-bubble homogenizer, including stirring
Casing body, drive disk assembly, the mixer case top are provided with charging aperture, and mixer housing bottom is provided with discharging opening, mixer
Puddler is provided with housing, the puddler is connected by fixed mount with mixer housing, the drive disk assembly and puddler phase
Even, air exhauster is additionally provided with, the air exhauster is connected by blast pipe with mixer housing, in the blast pipe and mixer housing
Portion connects.
Further, the blast pipe includes VERTICAL TUBE, and VERTICAL TUBE is directly connected with mixer housing, the upper surface of VERTICAL TUBE
Higher than the upper surface of mixer housing.
Further, the height of the VERTICAL TUBE is 200~1000mm.
Further, the puddler is curved-surface structure by charge level.
Further, the puddler is corrugated inclined-plane by charge level, and inclined plane is in 5~15 ° of angles with horizontal direction.
Further, the inclined plane and horizontal direction are in 12 ° of angles.
Further, the mixer case top is additionally provided with gas skirt, and the blast pipe is connected with gas skirt, gas skirt with
Mixer housing is connected；The gas skirt is provided with water spout.
Further, the blast pipe is provided with check valve.
Compared with prior art, advantages of the present invention is as follows：
（1）Air exhauster, blast pipe are provided with, when more bubble is contained in filling slurry, air exhauster are opened, in filling slurry
Air through blast pipe discharge, so as to increase the full packages degree of filling slurry, it is to avoid formed air lock, eliminate cutout plugging wind
Danger, improves transfer efficiency, improves the accuracy of slurry flow measurement.
（2）Blast pipe includes VERTICAL TUBE, and using the deadweight of filling slurry, the extender paste for making to be bonded in blast pipe is less,
Avoid blast pipe from being filled with slurry to paste and influence exhaust effect.
（3）Puddler is used curved-surface structure by charge level, it is to avoid the granule materials in mixed slurry attack puddler directly, reduce
The abrasion of puddler.
（4）Gas skirt and water spout are provided with, the separated water spout opened on gas skirt of timing can be dry by gas skirt cleaning
Only, the cleaning and exhaust de-bubble effect of gas skirt are kept；Water consumption is few, does not interfere with the concentration of slurry, will not also bring into
Air.
（5）Blast pipe is provided with check valve, and the open/close states of check valve are by the air in air exhauster and mixer housing
Pressure differential is controlled, while realization automatically adjusts exhaust, it is also possible to avoid the air of outside from being again introduced into mixer housing.
Brief description of the drawings
Fig. 1 is the front view of the embodiment of the present invention.
Fig. 2 is the side sectional view of embodiment illustrated in fig. 1.
Fig. 3 is the gas skirt of embodiment illustrated in fig. 1 and the partial enlarged drawing of water spout.
In figure：1-discharging opening, 2-mixer housing, 3-drive disk assembly, 4-fixed mount, 5-puddler, 6-charging
Mouthful, 7-blast pipe, 8-check valve, 9-air exhauster, 10 --- gas skirt, 11-water spout.
Specific embodiment
Below in conjunction with the accompanying drawings and specific embodiment is described in further detail to the present invention.
Reference picture 1, Fig. 2, Fig. 3, the present embodiment includes mixer housing 2, drive disk assembly 3, and the top of mixer housing 2 is provided with
Charging aperture 6, the bottom of mixer housing 2 is provided with and puddler 5 is provided with discharging opening 1, mixer housing 2, and puddler 5 passes through fixed mount
4 are connected with mixer housing 2, and drive disk assembly 3 is connected with puddler 5, drive puddler 5 to rotate；It is additionally provided with air exhauster 9, exhausting
Machine 9 is connected by blast pipe 7 with mixer housing 2, and blast pipe 7 is connected with the inside of mixer housing 2；The top of mixer housing 2
Gas skirt 10 is additionally provided with, blast pipe 7 is connected with gas skirt 10, and gas skirt 10 is connected with mixer housing 2；Gas skirt 10 is provided with
The water spout 11 that two height stagger；Blast pipe 7 includes VERTICAL TUBE, and VERTICAL TUBE is directly connected with mixer housing 2, VERTICAL TUBE
Higher than the upper surface of mixer housing 2, the height of VERTICAL TUBE is 500mm for upper surface；Puddler 5 is corrugated oblique by charge level
Face, inclined plane is in 12 ° of angles with horizontal direction；Blast pipe 7 is provided with check valve 8.
Operation principle of the invention is as follows：
In the mixer course of work, the drive fixed mount 4 of drive disk assembly 3 and the puddler 5 being installed on fixed mount 4 are rotated,
Attal is entered into mixer housing 2 from charging aperture 6, and agitated bar 5 quickly stirs, and is then discharged from discharging opening 1.
When more bubble is contained in filling slurry, air exhauster 9 is opened, the air in filling slurry is discharged through blast pipe 7, so as to increase
The full packages degree of filling slurry, improves transfer efficiency；After certain interval of time, when being attached to gas skirt 10 if any slurry, can be interrupted
Open the stagger water spout 11 of installation of two height and wash away gas skirt 10, so as to keep the cleaning of gas skirt 10 and exhaust de-bubble to imitate
Really；Water consumption is few, does not interfere with the concentration of slurry, will not also bring air into.
In order to further improve the full packages degree of filling slurry, blast pipe 7 is provided with check valve 8, the open/close states of check valve 8
Controlled by the air pressure difference in air exhauster 9 and mixer housing 2, when the air pressure in mixer housing 2 is more than taking out
During pressure in blower fan 9, check valve 8 is opened, and air exhauster 9 discharges the air in mixer housing 2, realizes the row of automatically adjusting
Gas；When the air pressure in mixer housing 2 is less than or equal to the pressure in air exhauster 9, check valve 8 is closed all the time, it is to avoid
The air of outside is again introduced into mixer housing 2.
To avoid the granule materials in mixed slurry from attacking puddler 5 directly, the abrasion of puddler 5, the material feeding of puddler 5 are reduced
Face uses curved-surface structure.Experiment proves, when puddler 5 is corrugated inclined-plane by charge level, inclined plane and horizontal direction in 5~
During 15 ° of angles, the abrasion of puddler 5 is less, and compared with conventional puddler, wear rate can reduce 25~50%, in the present embodiment
Puddler 5 is corrugated inclined-plane by charge level, and inclined plane is in 12 ° of angles with horizontal direction, now weares and teares minimum, with routine
Puddler is compared, and wear rate can reduce about 50%.
Paste and influence exhaust effect to avoid blast pipe 7 from being filled with slurry, blast pipe 7 can be arranged to vertical direction
Pipeline, i.e. VERTICAL TUBE, the upper surface of the upper surface higher than mixer housing 2 of VERTICAL TUBE, VERTICAL TUBE need to have certain height, profit
With the deadweight of filling slurry, make the extender paste being bonded in blast pipe 7 less；One for upper one preparation link being also mixed into simultaneously
Partial air is pumped out, and further functions as the effect for increasing filling slurry full packages degree, improves conveying effect, improves pipeline effect
Rate, so as to play preferably effect to improving filling quality.
The present apparatus is applied to the non-open transporting pattern of filling slurry, and simple structure, easy to process, low cost.
Those skilled in the art can carry out various modifications and variations to the embodiment of the present invention, if these modifications and change
Within the scope of the claims in the present invention and its equivalent technologies, then these modifications and modification are also in protection scope of the present invention for type
Within.
In the prior art that the content not described in detail in specification is known to the skilled person.
Claims (9)
1. a kind of exhaust de-bubble homogenizer, including mixer housing（2）, drive disk assembly（3）, the mixer housing（2）
Top is provided with charging aperture（6）, mixer housing（2）Bottom is provided with discharging opening（1）, mixer housing（2）Inside it is provided with puddler
（5）, the puddler（5）By fixed mount（4）With mixer housing（2）Connection, the drive disk assembly（3）With puddler（5）
It is connected, it is characterised in that：It is additionally provided with air exhauster（9）, the air exhauster（9）By blast pipe（7）With mixer housing（2）Phase
Even, the blast pipe（7）With mixer housing（2）Inside connection；The mixer housing（2）Top is additionally provided with gas skirt
（10）, the blast pipe（7）With gas skirt（10）Connection, gas skirt（10）With mixer housing（2）It is connected；The gas skirt
（10）It is provided with water spout（11）.
It is 2. as claimed in claim 1 to be vented de-bubble homogenizer, it is characterised in that：The blast pipe（7）Including VERTICAL TUBE,
VERTICAL TUBE directly with mixer housing（2）Connection, the upper surface of VERTICAL TUBE is higher than mixer housing（2）Upper surface.
It is 3. as claimed in claim 2 to be vented de-bubble homogenizer, it is characterised in that：The height of the VERTICAL TUBE be 200~
1000mm。
4. the exhaust de-bubble homogenizer as described in claim 1 or 2 or 3, it is characterised in that：The puddler（5）Receive
Charge level is curved-surface structure.
It is 5. as claimed in claim 4 to be vented de-bubble homogenizer, it is characterised in that：The puddler（5）Be by charge level
Corrugated inclined-plane, inclined plane is in 5~15 ° of angles with horizontal direction.
It is 6. as claimed in claim 5 to be vented de-bubble homogenizer, it is characterised in that：The inclined plane is in horizontal direction
12 ° of angles.
7. the exhaust de-bubble homogenizer as described in claim 1 or 2 or 3, it is characterised in that：The blast pipe（7）On set
There is check valve（8）.
It is 8. as claimed in claim 4 to be vented de-bubble homogenizer, it is characterised in that：The blast pipe（7）It is provided with unidirectional
Valve（8）.
It is 9. as claimed in claim 5 to be vented de-bubble homogenizer, it is characterised in that：The blast pipe（7）It is provided with unidirectional
Valve（8）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510529399.7A CN105058580B (en) | 2015-08-26 | 2015-08-26 | High-speed air-exhausting and defoaming stirring machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510529399.7A CN105058580B (en) | 2015-08-26 | 2015-08-26 | High-speed air-exhausting and defoaming stirring machine |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105058580A CN105058580A (en) | 2015-11-18 |
| CN105058580B true CN105058580B (en) | 2017-05-24 |
Family
ID=54488203
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510529399.7A Expired - Fee Related CN105058580B (en) | 2015-08-26 | 2015-08-26 | High-speed air-exhausting and defoaming stirring machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105058580B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108437220B (en) * | 2018-04-28 | 2019-11-26 | 重庆市长寿区分素装饰工程有限责任公司 | Foamed concrete agitating device |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN204894220U (en) * | 2015-08-26 | 2015-12-23 | 长沙矿山研究院有限责任公司 | Exhaust removes bubble high speed mixer |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6021211Y2 (en) * | 1980-05-28 | 1985-06-25 | 技術資源開発株式会社 | Continuous concrete mixer |
| CN202685093U (en) * | 2012-02-10 | 2013-01-23 | 安徽省安工机械制造有限公司 | Mixing rod of concrete mixer |
| CN202606066U (en) * | 2012-04-25 | 2012-12-19 | 林美复合材料(苏州)有限公司 | Stirring machine |
| CN203198059U (en) * | 2013-03-21 | 2013-09-18 | 四川卓安消防材料有限公司 | Horizontal single-shaft double-helical-ribbon blender |
-
2015
- 2015-08-26 CN CN201510529399.7A patent/CN105058580B/en not_active Expired - Fee Related
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN204894220U (en) * | 2015-08-26 | 2015-12-23 | 长沙矿山研究院有限责任公司 | Exhaust removes bubble high speed mixer |
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| Publication number | Publication date |
|---|---|
| CN105058580A (en) | 2015-11-18 |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170524 Termination date: 20180826 |