CN110092552A - A method of processing sludge conditioning excessive concentration - Google Patents
A method of processing sludge conditioning excessive concentration Download PDFInfo
- Publication number
- CN110092552A CN110092552A CN201810089059.0A CN201810089059A CN110092552A CN 110092552 A CN110092552 A CN 110092552A CN 201810089059 A CN201810089059 A CN 201810089059A CN 110092552 A CN110092552 A CN 110092552A
- Authority
- CN
- China
- Prior art keywords
- sludge
- concentration
- blowback
- filter cloth
- mud
- 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- Withdrawn
Links
- 239000010802 sludge Substances 0.000 title claims abstract description 39
- 238000000034 method Methods 0.000 title claims abstract description 13
- 230000003750 conditioning effect Effects 0.000 title claims abstract description 8
- 239000004744 fabric Substances 0.000 claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 4
- 238000011084 recovery Methods 0.000 claims description 3
- 239000002699 waste material Substances 0.000 abstract description 8
- 239000003814 drug Substances 0.000 abstract description 4
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 238000012423 maintenance Methods 0.000 abstract description 2
- 230000008676 import Effects 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- GOLXNESZZPUPJE-UHFFFAOYSA-N spiromesifen Chemical compound CC1=CC(C)=CC(C)=C1C(C(O1)=O)=C(OC(=O)CC(C)(C)C)C11CCCC1 GOLXNESZZPUPJE-UHFFFAOYSA-N 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
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Treatment Of Sludge (AREA)
Abstract
A method of processing sludge conditioning excessive concentration, when being utilized in conditioner excessive concentration, parking plus water, reduction concentration is on the lower side to normal value, while manual blowback, manual blowback is more than three times, each blowback time is not less than 30 seconds, and mud channel blockage sludge is walked in removal, then starts first to filter press into the lower sludge of concentration, it further washes away on filter cloth into sludge, improves the permeable gap of filter cloth by the obstruction of sludge.The beneficial effects of the present invention are: first is that the waste for avoiding having added medicament can be realized, second is that workshop and plant area's road is avoided to cause secondary pollution, third is that avoiding the waste of production time, the reduction of processing capacity on duty is caused, fourth is that maintenance time and cost are reduced, fifth is that saving operation cost.
Description
Technical field
The present invention relates to a kind of processing method of solid waste, especially a kind of side for handling sludge conditioning excessive concentration
Method.
Background technique
Filter press handles sludge processes route, and in specific production, conditioner sludge concentration technique requires to be moisture content
95%, examined equipment limit (most smart devices error is ± 5%), therefore each unit of operation is all by operator's micro-judgment.
Such as conditioner excessive concentration, will cause the too fast, inputiing mud volume to filter press into mud pressure buildup drop suddenly, filter chamber it is empty
Chamber, the serious problems that can not be squeezed, operation require to meet such situation, need to bleed off filter press into former mud and (import raw material again
Storehouse), forbid to squeeze, avoid spoiled filter plate, especially wash cloth again the time need 4 hours, in this way, first is that causing added medicament
Waste, second is that sposh is scattered, workshop and plant area's road cause secondary pollution, third is that causing the waste of production time, cause on duty
The reduction of processing capacity.The main reason is that conditioner excessive concentration, when to filter press low pressure into mud, walks mud channel and block up in advance
It fills in, into the filter chamber sludge obstruction permeable gap of filter cloth.To solve this problem, using manual blowback, it is logical that mud is walked in removal to the present invention
Road blocks sludge, then starts first further to wash away to filter press into the lower sludge of concentration on filter cloth into sludge, reduces sludge
Block the influence in the permeable gap of filter cloth.
Summary of the invention
It is an object of the present invention to provide a kind of methods for handling sludge conditioning excessive concentration, it can be achieved that avoiding having added medicament
Waste, workshop and plant area's road cause secondary pollution, avoid the waste of production time, cause the reduction of processing capacity on duty.
The present invention is realized using such method in order to solve the above problem: a kind of processing sludge conditioning excessive concentration
Method, when being utilized in conditioner excessive concentration, parking plus water, reduction concentration is on the lower side to normal value, while manual blowback, manually
Blowback more than three times, each blowback time be not less than 30 seconds, removal walk mud channel blockage sludge, then start first to filter press into
The lower sludge of concentration further washes away on filter cloth into sludge, improves the permeable gap of filter cloth by the obstruction of sludge, not into the mud time
Greater than 8 minutes, then manual blowback 30 seconds again, then start first further to wash away on filter cloth to filter press into the lower sludge of concentration
Into sludge, the influence in the sludge obstruction permeable gap of filter cloth is reduced, until normal into mud speed and pressure recovery.
The beneficial effects of the present invention are: first is that the waste for avoiding having added medicament can be realized, second is that avoiding workshop and plant area
Road causes secondary pollution, third is that avoiding the waste of production time, causes the reduction of processing capacity on duty, fourth is that when reducing maintenance
Between and cost, fifth is that save operation cost.
A specific embodiment of the invention is further described below.
Specific embodiment
The present invention is realized using such method: a method of processing sludge conditioning excessive concentration is utilized in
When conditioner excessive concentration, parking plus water, it is on the lower side to normal value to reduce concentration, while manual blowback, manual blowback more than three times,
Each blowback time is not less than 30 seconds, and mud channel blockage sludge is walked in removal, then starts first to filter press into the lower sludge of concentration,
It further washes away on filter cloth into sludge, improves the permeable gap of filter cloth by the obstruction of sludge, into the mud time no more than 8 minutes, so
Manual blowback 30 seconds again afterwards, then start first further to wash away to filter press into the lower sludge of concentration on filter cloth into sludge, it reduces
Sludge blocks the influence in the permeable gap of filter cloth, until into mud speed and pressure recovery production work condition.
Claims (1)
1. a kind of method for handling sludge conditioning excessive concentration, it is characterised in that: in conditioner excessive concentration, parking plus water,
Concentration is reduced to normal value 95% hereinafter, manual blowback simultaneously, more than three times, each blowback time is not less than 30 seconds for manual blowback,
Mud channel blockage sludge is walked in removal, then starts first further to wash away on filter cloth to filter press into the lower sludge of concentration into dirt
Mud, improves the permeable gap of filter cloth by the obstruction of sludge, is not more than 8 minutes into the mud time, then manual blowback 30 seconds again, then starts
First to filter press into the lower sludge of concentration, further washes away on filter cloth into sludge, reduce the sludge obstruction permeable gap of filter cloth
It influences, until into mud speed and pressure recovery production work condition.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810089059.0A CN110092552A (en) | 2018-01-30 | 2018-01-30 | A method of processing sludge conditioning excessive concentration |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810089059.0A CN110092552A (en) | 2018-01-30 | 2018-01-30 | A method of processing sludge conditioning excessive concentration |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN110092552A true CN110092552A (en) | 2019-08-06 |
Family
ID=67441949
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810089059.0A Withdrawn CN110092552A (en) | 2018-01-30 | 2018-01-30 | A method of processing sludge conditioning excessive concentration |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110092552A (en) |
Citations (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3138800A1 (en) * | 1981-09-30 | 1983-04-14 | Eckard Ing.(grad.) 7700 Singen Walter | Backwashable water filter |
| CN2080417U (en) * | 1990-12-06 | 1991-07-10 | 杭州塑料防腐设备厂 | Antiplugging plate and frame press filter |
| CN1244439A (en) * | 1998-08-06 | 2000-02-16 | 宋家骏 | Filter cake unloading and filter cloth washing mechanism and method for press filter and press filter with said mechanism |
| EP1485181A2 (en) * | 2002-02-21 | 2004-12-15 | Gordon Construction, Inc. | Self-cleaning fluid filter system |
| CN101224355A (en) * | 2007-10-15 | 2008-07-23 | 核工业烟台同兴实业有限公司 | Filter cloth cleaning device |
| WO2012149582A2 (en) * | 2011-04-26 | 2012-11-01 | Niazi Sarfaraz K | Concentrator filter |
| CN202620819U (en) * | 2012-05-16 | 2012-12-26 | 浙江方远建材科技有限公司 | Reverse blowing device for pressure filter sludge |
| CN202876572U (en) * | 2012-09-24 | 2013-04-17 | 徐作仁 | Bag cage blockage remover |
| CN103550966A (en) * | 2013-10-30 | 2014-02-05 | 广州市新之地环保产业有限公司 | Operation method of diaphragm pressure filter |
| CN203494239U (en) * | 2013-08-15 | 2014-03-26 | 江苏安士德环境科技有限公司 | Plate-and-frame filter press with back flushing system |
| CN204073563U (en) * | 2014-05-26 | 2015-01-07 | 北京海斯顿水处理设备有限公司 | A kind of can the filter washed of back suction |
| CN106943779A (en) * | 2017-04-08 | 2017-07-14 | 饶宾期 | High throughput sewage sludge depth minus quantization device |
| CN107261581A (en) * | 2017-08-18 | 2017-10-20 | 郭俊海 | A kind of plate and frame type filter-press of new discharge way |
-
2018
- 2018-01-30 CN CN201810089059.0A patent/CN110092552A/en not_active Withdrawn
Patent Citations (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3138800A1 (en) * | 1981-09-30 | 1983-04-14 | Eckard Ing.(grad.) 7700 Singen Walter | Backwashable water filter |
| CN2080417U (en) * | 1990-12-06 | 1991-07-10 | 杭州塑料防腐设备厂 | Antiplugging plate and frame press filter |
| CN1244439A (en) * | 1998-08-06 | 2000-02-16 | 宋家骏 | Filter cake unloading and filter cloth washing mechanism and method for press filter and press filter with said mechanism |
| EP1485181A2 (en) * | 2002-02-21 | 2004-12-15 | Gordon Construction, Inc. | Self-cleaning fluid filter system |
| CN101224355A (en) * | 2007-10-15 | 2008-07-23 | 核工业烟台同兴实业有限公司 | Filter cloth cleaning device |
| WO2012149582A2 (en) * | 2011-04-26 | 2012-11-01 | Niazi Sarfaraz K | Concentrator filter |
| CN202620819U (en) * | 2012-05-16 | 2012-12-26 | 浙江方远建材科技有限公司 | Reverse blowing device for pressure filter sludge |
| CN202876572U (en) * | 2012-09-24 | 2013-04-17 | 徐作仁 | Bag cage blockage remover |
| CN203494239U (en) * | 2013-08-15 | 2014-03-26 | 江苏安士德环境科技有限公司 | Plate-and-frame filter press with back flushing system |
| CN103550966A (en) * | 2013-10-30 | 2014-02-05 | 广州市新之地环保产业有限公司 | Operation method of diaphragm pressure filter |
| CN204073563U (en) * | 2014-05-26 | 2015-01-07 | 北京海斯顿水处理设备有限公司 | A kind of can the filter washed of back suction |
| CN106943779A (en) * | 2017-04-08 | 2017-07-14 | 饶宾期 | High throughput sewage sludge depth minus quantization device |
| CN107261581A (en) * | 2017-08-18 | 2017-10-20 | 郭俊海 | A kind of plate and frame type filter-press of new discharge way |
Non-Patent Citations (3)
| Title |
|---|
| 林海等: "《市政污水处理技术的理论与实践》", 31 December 2017 * |
| 赵修坦等: "Larox PF型压滤机常见故障分析及预防处理措施", 《山东冶金》 * |
| 钟妙坤等: "防堵塞板框压滤机 ", 《化工装备技术》 * |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN109483316A (en) | A kind of numerically-controlled machine tool cooling liquid filtering apparatus | |
| CN204428942U (en) | A kind of sludge dewatering belt filter press | |
| CN115671818A (en) | Intelligent control method and system for plate-and-frame filter press | |
| CN103432813A (en) | Reverse cleaning system and reverse cleaning method of ceramic filter in iron ore dehydration | |
| CN110092552A (en) | A method of processing sludge conditioning excessive concentration | |
| CN102618720B (en) | Method for backwash leaching and washing mineral leached materials | |
| CN205024063U (en) | Sludge dewatering handles car | |
| CN102432119B (en) | Sewage and waste acid treatment device and treatment process | |
| CN105000780A (en) | Sludge dewatering treatment vehicle and sludge dewatering treatment method | |
| CN110404665A (en) | A kind of processing method of ultra-fine coal slurry dehydration | |
| CN210915802U (en) | Device for recycling municipal sludge | |
| CN105090175A (en) | Filtering system | |
| CN205549728U (en) | Pressure filter dewatering system | |
| CN102626571A (en) | Slime water treatment process for separately clarifying filtrate | |
| CN205084868U (en) | Dry -discharge system for tailings | |
| CN205055526U (en) | Pressure filter | |
| CN207520741U (en) | A kind of closed circuit water supply system for slag processing | |
| CN112209593A (en) | Squeezing method of continuous deep dehydration equipment | |
| CN205616726U (en) | Integrated machine for sewage treatment | |
| CN203602429U (en) | System for separating solid from liquid of electroplating wastewater | |
| CN221601325U (en) | Filter liquor monitoring device of filter press | |
| CN209602096U (en) | A kind of wash mill of Wet-process Phosphoric Acid Production system | |
| CN209538022U (en) | A kind of highway bridge bridge deck drainage drainage trough | |
| CN220684896U (en) | Magnetic filter for recycling circulating water in steelmaking production | |
| CN217710531U (en) | Waterproof drainage device is used in hydraulic engineering construction |
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 | ||
| WW01 | Invention patent application withdrawn after publication |
Application publication date: 20190806 |
|
| WW01 | Invention patent application withdrawn after publication |