CN106542716A - A kind of sludge dewatering abatement system and method - Google Patents
A kind of sludge dewatering abatement system and method Download PDFInfo
- Publication number
- CN106542716A CN106542716A CN201611121827.3A CN201611121827A CN106542716A CN 106542716 A CN106542716 A CN 106542716A CN 201611121827 A CN201611121827 A CN 201611121827A CN 106542716 A CN106542716 A CN 106542716A
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- CN
- China
- Prior art keywords
- sludge
- air pressure
- tank
- pipeline
- 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.)
- Pending
Links
- 239000010802 sludge Substances 0.000 title claims abstract description 92
- 238000000034 method Methods 0.000 title claims abstract description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 18
- 230000000694 effects Effects 0.000 claims abstract description 6
- 239000007788 liquid Substances 0.000 claims description 15
- 230000000740 bleeding effect Effects 0.000 claims description 7
- 238000007664 blowing Methods 0.000 claims description 7
- 239000006228 supernatant Substances 0.000 claims description 3
- 150000001875 compounds Chemical class 0.000 claims 1
- 230000007717 exclusion Effects 0.000 claims 1
- 238000001914 filtration Methods 0.000 claims 1
- 239000002562 thickening agent Substances 0.000 claims 1
- 239000000203 mixture Substances 0.000 abstract description 6
- 238000001802 infusion Methods 0.000 abstract description 2
- 238000002347 injection Methods 0.000 abstract 1
- 239000007924 injection Substances 0.000 abstract 1
- 238000005265 energy consumption Methods 0.000 description 4
- 230000007774 longterm Effects 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 238000004927 wastewater treatment sludge Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
- C02F11/122—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering using filter presses
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Treatment Of Sludge (AREA)
Abstract
The invention discloses a kind of sludge dewatering abatement system and method, including sludge concentration tank, air pressure mud tank and filter press, the sludge concentration tank was connected the first pipeline and was connected with air pressure mud tank, the air pressure mud tank is connected with filter press by second pipe, sump is provided with below filter press, sump is connected with filter press by the 4th water pipe, and sump is connected with sludge concentration tank by the 3rd water pipe.A kind of sludge dewatering abatement system and method that the present invention is obtained, instead of the method that classic screw infusion enters mud mixture, are operated using air pressure mud tank, reduce the expense produced because needing to regularly replace the consumable accessorys such as stator using screw pump；Forced air in injection air pressure mud tank can subsequently play air blow pressure effect, one-object-many-purposes；Overall work cycle phase nearly half for normal treatment process is shortened, dewatering efficiency are high.
Description
Technical field
The present invention relates to sludge treating system, particularly a kind of sludge dewatering abatement system and method.
Background technology
As the environmental protection consciousness of people strengthens, sewage disposal is gradually taken seriously, and various sewage disposals set
Shi Junhui generation wastewater treatment sludge, including materializing strategy sludge, biochemical treatment excess sludge etc..Sludge produce node be
Each sedimentation tank, the sludge that sedimentation tank is excluded are rendered as the muddy water admixture of moisture content 99.5% or so, to the post processing of sludge
Great inconvenience is brought, therefore is required for carrying out the processed of sludge, make sludge curing.
Generally sludge dewatering operation is most commonly used that chamber-type press filter, and Cabin type of Filter press is by muddy water using screw pump
Mixture is injected into filter pressing cabinet bulk, but screw pump needs timing to change the consumable accessory such as stator after long-term use, it is long-term under
Being also a no small expense；And screw pump needs continuous running, power consumption is big, during using Cabin type of Filter press, completes
One spin cycle it is time-consuming also longer, therefore energy consumption is relatively large.So being badly in need of a kind of the good of efficient sludge dewatering
The appearance of method.
The content of the invention
The invention aims to solve above-mentioned the deficiencies in the prior art and provide one kind of a kind of high efficiency, low energy consumption
Sludge dewatering abatement system and method.
To achieve these goals, a kind of sludge dewatering abatement system and method designed by the present invention, including sludge is dense
Contracting pond, air pressure mud tank and filter press, the sludge concentration tank are connected with air pressure mud tank by the first pipeline, in first pipe
Road is provided with sludge pump；The air pressure mud tank is connected with filter press by second pipe, is provided with out on second pipe
Slurry valve, the air pressure mud tank are connected with air compressor machine by dicomponent pipeline, and air pressure is led in one end of the dicomponent pipeline
The top of mud tank and air pressure valve is provided with this pipeline, the other end of dicomponent pipeline leads to second pipe and on this pipeline
Air-blowing valve is provided with, and the 5th pipeline is connected on air pressure mud tank top, is provided with air bleeding valve on the 5th pipeline；Transfer in filter press
Collecting tank is equipped with, sump is provided with below filter press, sump is connected with filter press by the 4th water pipe,
Sump is connected with sludge concentration tank by the 3rd water pipe, wherein the 3rd water pipe is provided with more than one with concentration basin connecting place
Arm, is provided with the pipeline that clear liquid is led to outside on the 3rd water pipe of the junction flowed out in sump and sludge concentration tank clear liquid
Extension.The arm is connected to sludge concentration tank upper orifice seat positioned at the top of sludge concentration tank；The second pipe connects
In the bottom of air pressure mud tank.Matching valve is equipped with arm；The two ends positioned at sludge pump on the first pipeline
Place is respectively provided with a valve；Matching valve is provided with the 4th pipeline.
A kind of implementation method of sludge dewatering abatement system is as follows：Pour mud mixture into sludge concentration tank, treat sludge
The bottom of sludge concentration tank is precipitated to, clear liquid is opened sludge pump, by sludge suction air pressure mud tank, waits sludge quantity at top
The valve at sludge pump two ends when reaching air pressure mud tank setting value, is closed, sludge pump is turned off, air compressor machine and air pressure is opened immediately
Valve carries out air pressurized to air pressure mud tank, when waiting pressure in air pressure mud tank to reach setting value, closes air pressure valve and air compressor machine, opens
Air-blowing valve, now the pressure in air pressure mud tank enough sludge therein is pressed in filter press, and subsequent air pressure mud tank
In high pressure exhaust gas the effect for playing air blow pressure is also passed in filter press along second pipe, and will be clear in sludge
Liquid is flowed in sump by the 4th pipeline Jing after blow pressure, and the supernatant in clear liquid and sludge concentration tank in sump is equal
Can be excluded by the 3rd pipeline and be recycled, be gone out substantially most water through the sludge of filter press filter pressing
Point, will drop in collecting tank；The 5th pipeline on air pressure mud tank is used for aerofluxuss, and air bleeding valve is opened when aerofluxuss are needed.
A kind of sludge dewatering abatement system and method that the present invention is obtained, which has the technical effect that：
1st, the method that classic screw infusion enters mud mixture is instead of, is operated using air pressure mud tank, reduced because adopting
The expense that screw pump needs to regularly replace the consumable accessory such as stator and produces；
2nd, the forced air injected in air pressure mud tank can subsequently play air blow pressure effect, one-object-many-purposes；
3rd, from the point of view of apparatus, sludge pump does not need high outlet pressure, therefore preparation power substantially reduce；Air compressor machine is
Intermittent operating, reduces energy consumption, and overall power consumption ratio reduces about 12 kilowatts of installed capacitys using the preparation of screw pump, and sets
The standby time for continuously running can shorten -2 hours 1 hour；
4th, pump into air pressure mud tank from mud mixture to start to the process of the casing for filling filter press generally to only need to 30 points
Clock -40 minutes, whole operation period ratio adopts screw pump or common sludge dewatering system will shorten 3 hours or so, and success is real
The requirement for sloughing moisture in sludge of high efficiency, low energy consumption is showed.
Description of the drawings
Fig. 1 is a kind of simple schematic diagram of sludge dewatering abatement system of embodiment.
In figure：Sludge concentration tank 1, air compressor machine 2, air-blowing valve 3, mud valve 4, sump 5, filter press 6, air bleeding valve 7,
Air pressure mud tank 8, air pressure valve 9, sludge pump 10, the 3rd pipeline 11, the first pipeline 12, second pipe 13, collecting tank 14, arm 15,
4th pipeline 16, dicomponent pipeline 17, the 5th pipeline 18, pipeline extension 19.
Specific embodiment
The present invention is further described with reference to the accompanying drawings and examples.
Embodiment：
As shown in figure 1, a kind of sludge dewatering abatement system that the present embodiment is provided, including sludge concentration tank 1,8 and of air pressure mud tank
Filter press 6, the sludge concentration tank 1 are connected with air pressure mud tank 8 by the first pipeline 12, are provided with the first pipeline 12
Sludge pump 10；The air pressure mud tank 8 is connected with filter press 6 by second pipe 13, is provided with out on second pipe 13
Slurry valve 4, the air pressure mud tank 8 are connected with air compressor machine 2 by dicomponent pipeline 17, and one end of the dicomponent pipeline 17 leads to
To air pressure mud tank 8 top and air pressure valve 9 is provided with this pipeline, the other end of dicomponent pipeline 17 leads to second pipe 13
This pipeline is provided with air-blowing valve 3, is connected to the 5th pipeline 18 on 8 top of air pressure mud tank, is provided with air bleeding valve 7 on the 5th pipeline 18；
Collecting tank 14 being placed with filter press 6, sump 5 being provided with the lower section of filter press 6, sump 5 passes through the 4th
Water pipe 16 is connected with filter press 6, and sump 5 is connected with sludge concentration tank 1 by the 3rd water pipe 11, wherein the 3rd water
Pipe 11 is provided with more than one arm 15 with concentration basin connecting place, in the junction that sump 5 and 1 clear liquid of sludge concentration tank flow out
The 3rd water pipe 11 be provided with by clear liquid lead to outside pipeline extension 19.The arm 15 is connected on sludge concentration tank 1
Mouth of pipe seat is located at the top of sludge concentration tank；The second pipe 13 is connected to the bottom of air pressure mud tank 8.It is all provided with arm 15
There is matching valve；A valve is being respectively provided with first pipeline 12 at the two ends of sludge pump 10；In the 4th pipe
Road 16 is provided with matching valve.
A kind of implementation method of sludge dewatering abatement system is as follows：Pour mud mixture into sludge concentration tank 1, treat sludge
The bottom of sludge concentration tank 1 is precipitated to, clear liquid is opened sludge pump 10, by sludge suction air pressure mud tank 8, waits dirt at top
The valve at 10 two ends of sludge pump when mud amount reaches air pressure mud 8 setting value of tank, is closed, sludge pump 10 is turned off, is opened pneumatics immediately
Machine 2 and air pressure valve 9 carry out air pressurized to air pressure mud tank 8, when waiting pressure in air pressure mud tank 8 to reach setting value, close air pressure
Valve 9 and air compressor machine 2, open air-blowing valve 3, and now sludge therein is pressed into filter press 6 by pressure in air pressure mud tank 8 enough
In, and the high pressure exhaust gas in subsequent air pressure mud tank 8 are also passed into along second pipe 13 and play air in filter press 6 and blow
The effect of pressure, and the clear liquid in sludge is flowed in sump 5 by the 4th pipeline 16 Jing after blow pressure, it is clear in sump 5
The supernatant in liquid and sludge concentration tank 1 can be excluded by the 3rd pipeline 11 and be recycled, through filter press 6
The sludge of filter pressing is gone out most moisture substantially, will be dropped in collecting tank 14；The 5th pipeline 18 on air pressure mud tank 8 is used
In aerofluxuss, air bleeding valve 7 is opened when aerofluxuss are needed.
Claims (4)
1. a kind of sludge dewatering abatement system, it is characterised in that：Including sludge concentration tank（1）, air pressure mud tank（8）And filter press
Machine（6）, the sludge concentration tank（1）By the first pipeline（12）With air pressure mud tank（8）It is connected, in the first pipeline（12）On set
There is sludge pump（10）；The air pressure mud tank（8）By second pipe（13）With filter press（6）It is connected, in second pipe
（13）It is provided with mud valve（4）, the air pressure mud tank（8）By dicomponent pipeline（17）It is connected with air compressor machine（2）, it is described double
To lateral（17）One end lead to air pressure mud tank（8）Top and be provided with air pressure valve on this pipeline（9）, dicomponent pipe
Road（17）The other end lead to second pipe（13）And air-blowing valve is provided with this pipeline（3）, in air pressure mud tank（8）Top is connected to
5th pipeline（18）, in the 5th pipeline（18）It is provided with air bleeding valve（7）；In filter press（6）Under be placed with collecting tank（14）,
In filter press（6）Lower section be provided with sump（5）, sump（5）By the 4th water pipe（16）With filter press（6）Phase
Connection, sump（5）By the 3rd water pipe（11）With sludge concentration tank（1）It is connected, wherein the 3rd water pipe（11）With concentration basin
Connecting place is provided with more than one arm（15）, in sump（5）And sludge concentration tank（1）The 3rd of the junction that clear liquid flows out
Water pipe（11）It is provided with the pipeline extension that clear liquid is led to outside（19）.
2. a kind of sludge dewatering abatement system according to claim 1, it is characterised in that：The arm（15）It is connected to dirt
Mud thickener（1）Upper orifice seat is located at the top of sludge concentration tank；The second pipe（13）It is connected to air pressure mud tank（8）Bottom
Portion.
3. a kind of sludge dewatering abatement system according to claim 1, it is characterised in that：In arm（15）On be equipped with
Matching valve；In the first pipeline（12）On positioned at sludge pump（10）Two ends at be respectively provided with a valve；In the 4th pipe
Road（16）It is provided with matching valve.
4. the implementation method of a kind of sludge dewatering abatement system according to claim 1-3, it is characterised in that：Muddy water is mixed
Compound pours sludge concentration tank into（1）, treat sludge settling to sludge concentration tank（1）Bottom, clear liquid at top, open sludge pump
（10）, by sludge suction air pressure mud tank（8）In, wait sludge quantity to reach air pressure mud tank（8）During setting value, sludge pump is closed（10）Two
The valve at end, turns off sludge pump（10）, air compressor machine is opened immediately（2）And air pressure valve（9）To air pressure mud tank（8）Carry out air
Pressurization, waits air pressure mud tank（8）When middle pressure reaches setting value, air pressure valve is closed（9）And air compressor machine（2）, open air-blowing valve（3）,
Now air pressure mud tank（8）In pressure sludge therein is pressed into into filter press enough（6）In, and subsequent air pressure mud tank
（8）In high pressure exhaust gas also along second pipe（13）It is passed into filter press（6）In play the effect of air blow pressure, and will
Clear liquid in sludge passes through the 4th pipeline Jing after blow pressure（16）It is flowed into sump（5）In, sump（5）In clear liquid and sludge
Concentration basin（1）In the supernatant can pass through the 3rd pipeline（11）Exclusion is recycled, through filter press（6）Pressure
The sludge of filtration is gone out most moisture substantially, will drop into collecting tank（14）In；Air pressure mud tank（8）On the 5th pipeline
（18）For aerofluxuss, air bleeding valve is opened when aerofluxuss are needed（7）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611121827.3A CN106542716A (en) | 2016-12-08 | 2016-12-08 | A kind of sludge dewatering abatement system and method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611121827.3A CN106542716A (en) | 2016-12-08 | 2016-12-08 | A kind of sludge dewatering abatement system and method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106542716A true CN106542716A (en) | 2017-03-29 |
Family
ID=58396686
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611121827.3A Pending CN106542716A (en) | 2016-12-08 | 2016-12-08 | A kind of sludge dewatering abatement system and method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106542716A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109110503A (en) * | 2018-10-13 | 2019-01-01 | 何学文 | A kind of sludge press filtration conveying device and its application method |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201245536Y (en) * | 2008-05-07 | 2009-05-27 | 辽宁省水利水电科学研究院 | Air pressure plate and frame type sludge treater |
| CN201320425Y (en) * | 2008-10-28 | 2009-10-07 | 福建省晋江优兰发纸业有限公司 | Sludge pressure filtering device with pneumatic sludge transport |
| CN202054725U (en) * | 2011-05-27 | 2011-11-30 | 煤炭科学研究总院杭州环保研究院 | Pneumatic pressure stabilizing device for sludge dewatering |
| CN202105482U (en) * | 2011-05-27 | 2012-01-11 | 浙江益万生物科技有限公司 | Plate and frame filter press |
| CN202379863U (en) * | 2011-12-22 | 2012-08-15 | 四川四通欧美环境工程有限公司 | Full-automatic high-pressure membrane filtering-pressing system used for concentrating sludge |
| CN204325101U (en) * | 2014-12-10 | 2015-05-13 | 广东绿美环境科技有限公司 | One is anti-releases the dense dry systems of phosphorus sludge |
| CN206244633U (en) * | 2016-12-08 | 2017-06-13 | 宁波渤川废液处置有限公司 | A kind of sludge dewatering abatement system |
-
2016
- 2016-12-08 CN CN201611121827.3A patent/CN106542716A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201245536Y (en) * | 2008-05-07 | 2009-05-27 | 辽宁省水利水电科学研究院 | Air pressure plate and frame type sludge treater |
| CN201320425Y (en) * | 2008-10-28 | 2009-10-07 | 福建省晋江优兰发纸业有限公司 | Sludge pressure filtering device with pneumatic sludge transport |
| CN202054725U (en) * | 2011-05-27 | 2011-11-30 | 煤炭科学研究总院杭州环保研究院 | Pneumatic pressure stabilizing device for sludge dewatering |
| CN202105482U (en) * | 2011-05-27 | 2012-01-11 | 浙江益万生物科技有限公司 | Plate and frame filter press |
| CN202379863U (en) * | 2011-12-22 | 2012-08-15 | 四川四通欧美环境工程有限公司 | Full-automatic high-pressure membrane filtering-pressing system used for concentrating sludge |
| CN204325101U (en) * | 2014-12-10 | 2015-05-13 | 广东绿美环境科技有限公司 | One is anti-releases the dense dry systems of phosphorus sludge |
| CN206244633U (en) * | 2016-12-08 | 2017-06-13 | 宁波渤川废液处置有限公司 | A kind of sludge dewatering abatement system |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109110503A (en) * | 2018-10-13 | 2019-01-01 | 何学文 | A kind of sludge press filtration conveying device and its application method |
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| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170329 |
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| RJ01 | Rejection of invention patent application after publication |