CN107540123A - Distillery waste solid processing system - Google Patents
Distillery waste solid processing system Download PDFInfo
- Publication number
- CN107540123A CN107540123A CN201710859708.6A CN201710859708A CN107540123A CN 107540123 A CN107540123 A CN 107540123A CN 201710859708 A CN201710859708 A CN 201710859708A CN 107540123 A CN107540123 A CN 107540123A
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- China
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- tank
- filter cylinder
- dense metal
- metal net
- dephosphorization
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- 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.)
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Abstract
Distillery waste solid processing system, including process tank, liquid outlet, second sponge, second Dense metal net, second sponge, pillar, 3rd Dense metal net, first drawing liquid pump, sliding block, slide rail, second drawing liquid pump, water tank, annular silica gel piece, dephosphorization tank, dephosphorization agent nozzle, arc, cylinder, dephosphorization agent liquid case, inflator pump, interior stake, feed tube, first tank, first filter cylinder, first sponge, second tank, first Dense metal net, second filter cylinder, 3rd tank, 3rd filter cylinder and template air bag, the process tank inner top installs feed tube, feed tube lower end is installed by liquid outlet, liquid outlet is located in the first filter cylinder, first filter cylinder is arranged on the first tank, first filter cylinder bottom is installed by the first Dense metal net；It is an advantage of the invention that：Good filtration effect, phosphor-removing effect might as well.
Description
Technical field
The present invention relates to distillery waste solid processing system, belong to waste reduction and disposal equipment technical field.
Background technology
Alcohol waste water is high concentration, high-temperature, the organic wastewater of high suspended matter, and treatment technology starting is more early, and development is very fast.
Waste residue in waste liquid contains the crude fibres such as the cassava skin after crushing, rhizome, and contains substantial amounts of phosphorus in waste water, and phosphorus can result in water
Body eutrophication.It is not good enough that the equipment filter effect of waste residue is removed in distillery waste at present, and the phosphor-removing effect of dephosphorization equipment
Poorly.In order to solve above-mentioned difficulties, it is necessary to the three-dimensional processing of the distillery waste for developing a good filtration effect, phosphor-removing effect
System.
The content of the invention
It is an object of the invention to provide distillery waste solid processing system.
The problem to be solved in the present invention is that the equipment filter effect of removal waste residue in current distillery waste is not good enough, and dephosphorization
The problem of phosphor-removing effect of equipment is also not so good.
To realize the purpose of the present invention, the technical solution adopted by the present invention is：
Distillery waste solid processing system, including process tank, liquid outlet, the second sponge, the second Dense metal net, the 3rd sponge,
Pillar, the 3rd Dense metal net, the first drawing liquid pump, sliding block, slide rail, the second drawing liquid pump, water tank, annular silica gel piece, dephosphorization tank,
Dephosphorization agent nozzle, arc, cylinder, dephosphorization agent liquid case, inflator pump, interior stake, feed tube, the first tank, the first filter cylinder, the first sea
Silk floss, the second tank, the first Dense metal net, the second filter cylinder, the 3rd tank, the 3rd filter cylinder and template air bag, the process tank is interior to be pushed up
Feed tube, feed tube lower end installation liquid outlet are installed by portion, and liquid outlet is located in the first filter cylinder, and the first filter cylinder is arranged on the first tank,
The first Dense metal net is installed in first filter cylinder bottom, and the first sponge of installation, the first Dense metal are off the net on the net for the first Dense metal
Second filter cylinder is installed, the second filter cylinder is arranged in the second tank, and the second tank is arranged under the first tank, the second filter cylinder bottom installation second
Dense metal net, the second Dense metal install the second sponge, the second Dense metal 3rd filter cylinder of installation off the net, the 3rd filter cylinder on the net
In the 3rd tank, the 3rd tank is arranged under the second tank, and the 3rd Dense metal net is installed in the 3rd filter cylinder bottom, and the 3rd is intensive
3rd sponge is installed on wire netting, the 3rd Dense metal sieve bottom installs multiple pillars, and pillar is arranged on process tank inner bottom part, the
The drawing liquid tank of one drawing liquid pump is connected with process tank, and the discharging tube of the first drawing liquid pump is connected with dephosphorization tank, is installed in dephosphorization tank
Interior stake, multiple cylinders are respectively installed in interior four side walls of stake, arc is installed on the piston rod of cylinder, the installation of annular slab bottom is slided
Block, sliding block are arranged on slide rail, and slide rail is arranged on dephosphorization tank inner bottom part, and template air bag is installed between two arcs that are connected,
Template air bag and the outer upper and lower ends of annular slab respectively install annular silica gel piece, and the annular silica gel piece other end is arranged on the inside of dephosphorization tank
Multiple dephosphorization agent nozzles are respectively installed, dephosphorization agent nozzle is connected by pipeline with dephosphorization agent liquid case, dephosphorization agent liquid on wall, on annular slab
Case is arranged in interior stake side wall, and installation inflator pump, inflator pump are connected by pipeline with template air bag on the right side of interior stake, the second drawing liquid
The liquid suction pipe of pump is connected with dephosphorization tank, and the drainpipe of the second drawing liquid pump is connected with water tank.
The first Dense metal sieve bottom, the second Dense metal sieve bottom and the 3rd Dense metal sieve bottom.
First filter cylinder, the second filter cylinder and the 3rd filter cylinder inner and outer wall respectively lay non-woven fabrics.
It is an advantage of the invention that：Waste water is entered in the first filter cylinder from liquid outlet, and the liquid of the first filter cylinder filtering enters downwards
Enter the second filter cylinder, the liquid of the second filter cylinder filtering is downwardly into the 3rd filter cylinder, process tank is flowed to from the 3rd Dense metal sieve bottom
Interior, the liquid in the first tank is back in the first filter cylinder again, and the liquid in the second tank is back in the second filter cylinder, in the 3rd tank
Liquid is back in the 3rd filter cylinder, is flowed to from the 3rd Dense metal sieve bottom in process tank, so liquid the first filter cylinder,
Worn between second filter cylinder and the 3rd cartridge sidewall to wear so that the cleaning waste slag such as cassava skin, rhizome in waste water it is more dry
Only；First sponge, the second sponge and the 3rd sponge have the function that to stop waste residue；First drawing liquid pump draws fluid into dephosphorization tank
Between madial wall, arc outer wall, template air bag outer wall and upper and lower two annular silica gel pieces；Cylinder does stretching motion, makes
Arc is displaced outwardly, and moves sliding block, and the distance between two neighboring arc expands, while inflator pump is to template air bag
Inflation, expands template air bag, and template air bag is connected to two arcs, during this, annular silica gel piece water
Plane is changed into folded bent state from extended configuration, and the sideway stance that annular silica gel piece is connected with template air bag is by folded bent
State is changed into extended configuration, distance between arc and dephosphorization tank madial wall is diminished, and makes dephosphorization tank madial wall, outside arc
The width of liquid between wall, template air bag outer wall and upper and lower two annular silica gel pieces diminishes, and highly uprises, due to liquid
Narrowed thickness, that, which will enable, ejects dephosphorization agent and is more fully mixed with waste liquid, promotes the dephosphorization of waste liquid；This is
System good filtration effect, phosphor-removing effect might as well.
Brief description of the drawings
Fig. 1 is distillery waste solid processing system overall structure figure of the present invention；
Fig. 2 is the top view of annular silica gel piece；
Fig. 3 is the front view of arc；
Fig. 4 is the front view of arc；
In figure：1st, process tank 2, liquid outlet 3, the second sponge 4, the second Dense metal net 5, the 3rd sponge 6, pillar 7,
Three Dense metal nets 8, the first drawing liquid pump 9, sliding block 10, slide rail 11, the second drawing liquid pump 12, water tank 13, annular silica gel
Piece 14, dephosphorization tank 15, dephosphorization agent nozzle 16, arc 17, cylinder 18, dephosphorization agent liquid case 19, inflator pump 20, interior stake
21st, feed tube 22, the first tank 23, the first filter cylinder 24, the first sponge 25, the second tank 26, the first Dense metal net 27,
Two filter cylinders 28, the 3rd tank 29, the 3rd filter cylinder 30, template air bag.
Embodiment
Below in conjunction with the accompanying drawings and embodiment the present invention is further illustrated.
Distillery waste solid processing system of the present invention, including process tank 1, liquid outlet 2, the second sponge 3, the second Dense metal
Net 4, the 3rd sponge 5, pillar 6, the 3rd Dense metal net 7, the first drawing liquid pump 8, sliding block 9, slide rail 10, the second drawing liquid pump 11, storage
Water pot 12, annular silica gel piece 13, dephosphorization tank 1414, dephosphorization agent nozzle 15, arc 16, cylinder 17, dephosphorization agent liquid case 18, inflation
Pump 19, interior stake 20, feed tube 21, the first tank 22, the first filter cylinder 23, the first sponge 24, the second tank 25, the first Dense metal net
26th, the second filter cylinder 27, the 3rd tank 28, the 3rd filter cylinder 29 and template air bag 30, the inner top of process tank 1 install feed tube,
Liquid outlet 2 is installed in feed tube lower end, and liquid outlet 2 is located in the first filter cylinder, and the first filter cylinder is arranged on the first tank, the first filter cylinder bottom
First Dense metal net is installed, the first Dense metal installs the first sponge on the net, and the first Dense metal is off the net to install the second filter cylinder,
Second filter cylinder is arranged in the second tank, and the second tank is arranged under the first tank, and the second Dense metal net 4 is installed in the second filter cylinder bottom,
Second sponge 3 is installed, the first sponge, the second sponge 3 and the 3rd sponge 5 have the work for stopping waste residue on second Dense metal net 4
With；Second Dense metal net 4 times installs the 3rd filter cylinder, and the 3rd filter cylinder is arranged in the 3rd tank, and the 3rd tank is arranged under the second tank,
The 3rd Dense metal net is installed in 3rd filter cylinder bottom, and the 3rd Dense metal installs the 3rd sponge 5, the 3rd Dense metal net on the net
Multiple pillars are installed in bottom, and pillar is arranged on the inner bottom part of process tank 1, and waste water is entered in the first filter cylinder from liquid outlet 2, the first filter
The liquid of cylinder filtering is downwardly into the second filter cylinder, and the liquid of the second filter cylinder filtering is downwardly into the 3rd filter cylinder, from the 3rd intensive gold
Category sieve bottom is flowed in process tank 1, and the liquid in the first tank is back in the first filter cylinder again, and the liquid in the second tank is back to the
In two filter cylinders, the liquid in the 3rd tank is back in the 3rd filter cylinder, is flowed to from the 3rd Dense metal sieve bottom in process tank 1, this
Sample one carrys out liquid and worn between the first filter cylinder, the second filter cylinder and the 3rd cartridge sidewall to wear so that cassava skin, root in waste water
The cleaning waste slags such as stem it is cleaner；The drawing liquid tank of first drawing liquid pump is connected with process tank 1, the discharging tube of the first drawing liquid pump with
Dephosphorization tank 14 is connected, and the first drawing liquid pump draws fluid into the madial wall of dephosphorization tank 14, arc outer wall, template air bag outer wall
And between upper and lower two annular silica gel pieces；Stake in installation in dephosphorization tank 14, multiple cylinders, gas are respectively installed in interior four side walls of stake
Arc, annular slab bottom installation sliding block are installed, sliding block is arranged on slide rail, and slide rail is arranged on dephosphorization tank 14 on the piston rod of cylinder
Inner bottom part, template air bag, each mounting ring of the outer upper and lower ends of template air bag and annular slab are installed between two arcs that are connected
Shape silica gel piece, the annular silica gel piece other end are arranged on the madial wall of dephosphorization tank 14, and multiple dephosphorization agent nozzles are respectively installed on annular slab,
Dephosphorization agent nozzle is connected by pipeline with dephosphorization agent liquid case, and dephosphorization agent liquid case is arranged in interior stake side wall, is installed and is filled on the right side of interior stake
Air pump, inflator pump are connected by pipeline with template air bag, and the liquid suction pipe of the second drawing liquid pump is connected with dephosphorization tank 14, and second takes out
The drainpipe of liquid pump is connected with water tank, and cylinder does stretching motion, is displaced outwardly arc, moves sliding block, and adjacent two
The distance between individual arc expands, while inflator pump expands template air bag, template fills template inflatable bag inflating
Airbag is connected to two arcs, and during this, annular silica gel piece horizontal plane is changed into folded bent state, ring from extended configuration
Shape silica gel piece is changed into extended configuration with the sideway stance that template air bag is connected from folded bent state, makes arc and dephosphorization tank
Distance diminishes between 14 madial walls, makes the madial wall of dephosphorization tank 14, arc outer wall, template air bag outer wall and upper and lower two rings
The width of liquid between shape silica gel piece diminishes, and highly uprises, and due to the narrowed thickness of liquid, that will to eject to remove
Phosphorus agent can be mixed more fully with waste liquid, promote the dephosphorization of waste liquid；The system good filtration effect, phosphor-removing effect, first
Dense metal sieve bottom, the bottom of the second Dense metal net 4 and the 3rd Dense metal sieve bottom, the first filter cylinder, the second filter cylinder and
Three filter cylinder inner and outer walls respectively lay non-woven fabrics.
Application method of the present invention：Waste water is entered in the first filter cylinder from liquid outlet 2, and the liquid of the first filter cylinder filtering enters downwards
Enter the second filter cylinder, the liquid of the second filter cylinder filtering is downwardly into the 3rd filter cylinder, process tank 1 is flowed to from the 3rd Dense metal sieve bottom
Interior, the liquid in the first tank is back in the first filter cylinder again, and the liquid in the second tank is back in the second filter cylinder, in the 3rd tank
Liquid is back in the 3rd filter cylinder, is flowed to from the 3rd Dense metal sieve bottom in process tank 1, and so liquid is in the first filter
Worn between cylinder, the second filter cylinder and the 3rd cartridge sidewall to wear so that the cleaning waste slag such as cassava skin, rhizome in waste water is more
Totally；First sponge, the second sponge 3 and the 3rd sponge 5 have the function that to stop waste residue；First drawing liquid pump is drawn fluid into going
Between the madial wall of phosphorus tank 14, arc outer wall, template air bag outer wall and upper and lower two annular silica gel pieces；Cylinder does flexible fortune
It is dynamic, arc is displaced outwardly, moves sliding block, the distance between two neighboring arc expands, while inflator pump is to template
Inflatable bag inflating, expand template air bag, template air bag is connected to two arcs, during this, annular silicon
Film horizontal plane is changed into folded bent state from extended configuration, and the sideway stance that annular silica gel piece is connected with template air bag is by rolling over
Folded case of bending is changed into extended configuration, distance between arc and the madial wall of dephosphorization tank 14 is diminished, make the madial wall of dephosphorization tank 14,
The width of liquid between arc outer wall, template air bag outer wall and upper and lower two annular silica gel pieces diminishes, and highly uprises,
Due to the narrowed thickness of liquid, that, which will enable, ejects dephosphorization agent and is more fully mixed with waste liquid, promotes waste liquid
Dephosphorization；The system good filtration effect, phosphor-removing effect might as well.
Claims (3)
1. distillery waste solid processing system, including process tank（1）, liquid outlet（2）, the second sponge（3）, the second Dense metal net
（4）, the 3rd sponge（5）, pillar（6）, the 3rd Dense metal net（7）, the first drawing liquid pump（8）, sliding block（9）, slide rail（10）, second
Drawing liquid pump（11）, water tank（12）, annular silica gel piece（13）, dephosphorization tank（14）（14）, dephosphorization agent nozzle（15）, arc
（16）, cylinder（17）, dephosphorization agent liquid case（18）, inflator pump（19）, interior stake（20）, feed tube（21）, the first tank（22）, first filter
Cylinder（23）, the first sponge（24）, the second tank（25）, the first Dense metal net（26）, the second filter cylinder（27）, the 3rd tank（28）,
Three filter cylinders（29）With template air bag（30）, it is characterized in that：The process tank（1）Inner top installs feed tube（21）, feed tube
（21）Lower end is installed by liquid outlet（2）, liquid outlet（2）Positioned at the first filter cylinder（23）It is interior, the first filter cylinder（23）Installed in the first tank
（22）, the first filter cylinder（23）Bottom is installed by the first Dense metal net（26）, the first Dense metal net（26）The first sponge of upper installation
（24）, the first Dense metal net（26）The second filter cylinder of lower installation（27）, the second filter cylinder（27）Installed in the second tank（25）It is interior, second
Tank（25）Installed in the first tank（22）Under, the second filter cylinder（27）Bottom is installed by the second Dense metal net（4）, the second Dense metal net
（4）The second sponge of upper installation（3）, the second Dense metal net（4）The 3rd filter cylinder of lower installation（29）, the 3rd filter cylinder（29）Installed in
Three tanks（28）It is interior, the 3rd tank（28）Installed in the second tank（25）Under, the 3rd filter cylinder（29）Bottom is installed by the 3rd Dense metal net（7）
, the 3rd Dense metal net（7）The 3rd sponge of upper installation（5）, the 3rd Dense metal net（7）Bottom is installed by multiple pillars（6）, pillar
（6）Installed in process tank（1）Inner bottom part, the first drawing liquid pump（8）Drawing liquid tank and process tank（1）It is connected, the first drawing liquid pump（8）
Discharging tube and dephosphorization tank（14）（14）It is connected, dephosphorization tank（14）（14）Stake in interior installation（20）, interior stake（20）Four side walls
Upper each multiple cylinders of installation（17）, cylinder（17）Piston rod on arc is installed（16）, annular slab bottom installation sliding block（9）,
Sliding block（9）Installed in slide rail（10）On, slide rail（10）Installed in dephosphorization tank（14）（14）Inner bottom part, be connected two arcs（16）
Between install template air bag（30）, template air bag（30）Annular silica gel piece is respectively installed with upper and lower ends outside annular slab（13）,
Annular silica gel piece（13）The other end is arranged on dephosphorization tank（14）（14）Multiple dephosphorization agent nozzles are respectively installed on madial wall, on annular slab
（15）, dephosphorization agent nozzle（15）Pass through pipeline and dephosphorization agent liquid case（18）It is connected, dephosphorization agent liquid case（18）Installed in interior stake（20）
In side wall, interior stake（20）Right side is installed by inflator pump（19）, inflator pump（19）Pass through pipeline and template air bag（30）It is connected, second
Drawing liquid pump（11）Liquid suction pipe and dephosphorization tank（14）（14）It is connected, the second drawing liquid pump（11）Drainpipe and water tank（12）Phase
Connection.
2. distillery waste solid processing system according to claim 1, it is characterized in that：The first Dense metal net（26）
Bottom, the second Dense metal net（4）Bottom and the 3rd Dense metal net（7）Bottom.
3. distillery waste solid processing system according to claim 1, it is characterized in that：First filter cylinder（23）, second
Filter cylinder（27）With the 3rd filter cylinder（29）Inner and outer wall respectively lays non-woven fabrics.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710859708.6A CN107540123B (en) | 2017-09-21 | 2017-09-21 | Three-dimensional processing system of winery wastes material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710859708.6A CN107540123B (en) | 2017-09-21 | 2017-09-21 | Three-dimensional processing system of winery wastes material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN107540123A true CN107540123A (en) | 2018-01-05 |
| CN107540123B CN107540123B (en) | 2022-08-23 |
Family
ID=60963692
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710859708.6A Active CN107540123B (en) | 2017-09-21 | 2017-09-21 | Three-dimensional processing system of winery wastes material |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107540123B (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201125201Y (en) * | 2007-04-02 | 2008-10-01 | 珠海兰利环保技术有限公司 | Combined type intermediate water treating eqiupment |
| CN103126530A (en) * | 2012-11-20 | 2013-06-05 | 金星环保科技（香港）公司 | Multi-functional circulation filter water dispenser |
| CN104478121A (en) * | 2014-11-13 | 2015-04-01 | 东华大学 | Helical flow dephosphorization reactor |
| CN106430809A (en) * | 2016-08-08 | 2017-02-22 | 武汉泰康翔科技股份有限公司 | Sewage and sludge treatment system and environmental-friendly recycling method thereof |
| CN106977000A (en) * | 2017-05-05 | 2017-07-25 | 广汉海天洁诚水务有限公司 | A kind of reusing sewage pre-processing device |
-
2017
- 2017-09-21 CN CN201710859708.6A patent/CN107540123B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201125201Y (en) * | 2007-04-02 | 2008-10-01 | 珠海兰利环保技术有限公司 | Combined type intermediate water treating eqiupment |
| CN103126530A (en) * | 2012-11-20 | 2013-06-05 | 金星环保科技（香港）公司 | Multi-functional circulation filter water dispenser |
| CN104478121A (en) * | 2014-11-13 | 2015-04-01 | 东华大学 | Helical flow dephosphorization reactor |
| CN106430809A (en) * | 2016-08-08 | 2017-02-22 | 武汉泰康翔科技股份有限公司 | Sewage and sludge treatment system and environmental-friendly recycling method thereof |
| CN106977000A (en) * | 2017-05-05 | 2017-07-25 | 广汉海天洁诚水务有限公司 | A kind of reusing sewage pre-processing device |
Non-Patent Citations (1)
| Title |
|---|
| 高大文 等主编: "《环境工程学》", 31 July 2017 * |
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| Publication number | Publication date |
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| CN107540123B (en) | 2022-08-23 |
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Effective date of registration: 20220727 Address after: 316000 room 206, 2nd floor, No.10, west section of Xingzhou Avenue, Yancang street, Dinghai District, Zhoushan City, Zhejiang Province Applicant after: ZHOUSHAN JUYANG TECHNOLOGY DEVELOPMENT Co.,Ltd. Address before: 316000 rooms 1106 and 1107, building 2, Haijing Times Square, No. 765, Haiyin Road, Donggang street, Putuo District, Zhoushan City, Zhejiang Province Applicant before: ZHEJIANG TIANMEI ENVIRONMENT TECHNOLOGY CO.,LTD. |
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