CN104556618A - FFDS sludge treatment technology - Google Patents
FFDS sludge treatment technology Download PDFInfo
- Publication number
- CN104556618A CN104556618A CN201310474422.8A CN201310474422A CN104556618A CN 104556618 A CN104556618 A CN 104556618A CN 201310474422 A CN201310474422 A CN 201310474422A CN 104556618 A CN104556618 A CN 104556618A
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- CN
- China
- Prior art keywords
- sludge
- fermentation
- treatment
- mud
- drying
- 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.)
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Classifications
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- 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
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- 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
-
- 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
- C02F11/02—Biological treatment
- C02F11/04—Anaerobic treatment; Production of methane by such processes
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F7/00—Fertilisers from waste water, sewage sludge, sea slime, ooze or similar masses
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/20—Sludge processing
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
Abstract
The invention relates to an FFDS sludge treatment technology for sludge treatment, comprising the following specific process: sending sludge with high water content into a sludge thickener to carry out thickening treatment, filtering through a filter material layer, carrying out biochemical fermentation (aerobic fermentation or anaerobic fermentation) by adding a strain into a filtered mixture of a filter material and sludge, deodorizing a gas generated by fermentation through a deodorization device, collecting and utilizing methane generated by anaerobic fermentation, drying a mixture obtained after fermentation by a drying technology mainly by air drying (cold air or hot air), and finally screening the filter material and dried sludge. The filter material is recycled, and the dried sludge is used as a raw material of an organic fertilizer for resource utilization. The invention has beneficial effects as follows: the sludge treatment effect is good, and treatment cost is low; peculiar smell emitted during the treatment process is small; effective utilization of sludge can be realized; secondary pollution to the environment will not be caused; and reduction and resource utilization of sludge treatment are realized.
Description
Technical field
The present invention relates to a kind of disposing technique of mud, belong to environment-friendly treating process.
Especially effectively mud can be carried out processing and utilizing, the FFDS sludge disposal technique that the peculiar smell of process is few and innoxious.
Background technology
Mud refers to a kind of extremely complicated heterogeneous body be made up of organic relic, microorganism, inorganic particle, colloid etc. produced in sewage treatment process.Its main characteristic is that water ratio high (can up to more than 99%) organic content is high, easily smelly, and particle is comparatively thin, and proportion is less, jelly liquid.It is the concentrated thing between liquid and solid, can transport with pump, but is difficult to carry out solid-liquid separation by sedimentation.
The many employings of existing sludge disposal technique dosing after sludge thickener initial concentration is flocculated, and through press filtration removing large quantity of moisture, then filter cake is carried out landfill, burning disposal or landfill or burning disposal again after carrying out fermentation decrement.There is following shortcoming in above treatment process: 1, landfill method process needs to take valuable land resources, pollutes surrounding environment and underground water source, produces secondary pollution; 2, burning disposal cost of investment is large, and processing cost is high, also pollutes the environment after burning; 3, decrement fermentation is final still can remaining mud, need carry out secondary treatment.
Summary of the invention
The object of the invention is to aim to provide that a kind for the treatment of process is effective, processing cost is low, emit bad smell very little, can rational and efficient use mud, the FFDS sludge disposal technique of non-secondary pollution (is filtered, Filter; Fermentation, Fermentation; Mummification, Dry; Screening, Screening), to overcome the deficiency of prior art, realize effective disposing sludge simultaneously, avoid contaminate environment.
The technical solution used in the present invention is: FFDS sludge disposal technique, comprises the following steps:
1, sludge condensation filter: after sewage disposal remaining water ratio be more than 99% mud by sludge pump send into sludge thickener concentrate, after concentrated, water content is generally 96%, supernatant liquor is back in Sewage treatment systems, when mud is after concentration basin concentrating and separating goes out supernatant liquor, the bed of material filters after filtration, filtrate is back to Sewage treatment systems, and mud and filtrate enter next link;
2, sludge fermentation deodorizing: add bacterial classification in the mixture that the filtrate obtained after filtration and mud are formed, carry out aerobic fermentation or anaerobically fermenting, and establish odor removal to carry out deodorizing in zymotechnique part, when adopting anaerobically fermenting, the biogas of generation can carry out Collection utilization;
3, mud filtrate mummification: the rear mixture to obtaining after fermentation that fermented adopts drying process to carry out drying and other treatment, be mainly air-dry---cold wind or hot blast, the biogas combustion heat production that hot blast thermal source can utilize fermentation heat production or use anaerobically fermenting to produce, after drying and other treatment, moisture percentage in sewage sludge is down to less than 60%;
4, screening utilizes: after drying and other treatment, sieved by gains, then recycles, using gained dewatered sludge as organic fertilizer raw material being separated the filtrate drawn.
The filtrate that described FFDS sludge disposal technique adopts is the mixture of a kind of material in chaff shell, vinasse, gravel, pecan shell, gac, quartz sand, ceramic particle, plastic particle material or different materials arbitrarily.
The invention has the beneficial effects as follows: good to the treatment effect of mud, processing cost is low; The peculiar smell distributed in treating processes is very little; Effective utilization of mud can be realized; Secondary pollution can not be caused to environment; Achieve the minimizing of sludge treatment, recycling.
Accompanying drawing explanation
Fig. 1 is anaerobic ferment process schematic flow sheet of the present invention.
Fig. 2 is aerobic fermentation process schematic flow sheet of the present invention.
Embodiment
The present invention is further illustrated by following examples:
Shown in Fig. 1, Fig. 2, FFDS sludge disposal technique adopts following steps successively:
1, sludge condensation filter: after sewage disposal remaining water ratio be more than 99% mud by sludge pump send into sludge thickener concentrate, after concentrated, water content is generally 96%, supernatant liquor is back in Sewage treatment systems, when mud is after concentration basin concentrating and separating supernatant liquor, the bed of material filters after filtration, and the filtrate that filter material layer adopts is the mixture of a kind of material in chaff shell, vinasse, gravel, pecan shell, gac, quartz sand, ceramic particle, plastic particle material or different materials arbitrarily;
2, sludge fermentation deodorizing: add bacterial classification in the mixture that the filtrate obtained after filtration and mud are formed, carry out aerobic fermentation or anaerobically fermenting, after aerobic fermentation, temperature rising generally can reach 50 to 70 degrees Celsius, fermentation can produce foul smell, therefore establish odor removal in zymotechnique part, make foul smell through odor removal deodorizing, adopt during anaerobically fermenting and can produce biogas, collecting methane is utilized;
3, mud filtrate mummification: the rear mixture to obtaining after fermentation that fermented adopts drying process to carry out drying and other treatment, main employing is air-dry---cold wind or hot blast, the biogas combustion heat production that hot blast thermal source can be made good use of aerobe fermentation heat production or use anaerobically fermenting to produce, after drying and other treatment, moisture percentage in sewage sludge can be down to less than 60%;
4, screening utilizes: after drying and other treatment, sieved by gained mummification thing, then carries out reuse being separated the filtrate drawn, using gained dewatered sludge as organic fertilizer raw material, and then is turned waste into wealth by mud.
Claims (2)
1.FFDS sludge disposal technique, is characterized in that: specifically comprise step as follows:
1), sludge condensation filter: after sewage disposal remaining water ratio be more than 99% mud by sludge pump send into sludge thickener concentrate, after concentrated, water content is generally 96%, supernatant liquor is back in Sewage treatment systems, when mud is after concentration basin concentrating and separating goes out supernatant liquor, the bed of material filters after filtration, filtrate is back to Sewage treatment systems, and mud and filtrate enter next link;
2), sludge fermentation deodorizing: add bacterial classification in the mixture that the filtrate obtained after filtration and mud are formed, carry out aerobic fermentation or anaerobically fermenting, and establish odor removal to carry out deodorizing in zymotechnique part, when adopting anaerobically fermenting, the biogas of generation can carry out Collection utilization;
3), mud filtrate mummification: the rear mixture to obtaining after fermentation that fermented adopts drying process to carry out drying and other treatment, be mainly air-dry---cold wind or hot blast, the biogas combustion heat production that hot blast thermal source can utilize fermentation heat production or use anaerobically fermenting to produce, after drying and other treatment, moisture percentage in sewage sludge can be down to less than 60%;
4), screening utilizes: after drying and other treatment, sieved by gains, then recycle, using gained dewatered sludge as organic fertilizer raw material being separated the filtrate drawn.
2. FFDS sludge disposal technique according to claim 1, is characterized in that: the filtrate adopted is the mixture of a kind of material in chaff shell, vinasse, gravel, pecan shell, gac, quartz sand, ceramic particle, plastic particle material or different materials arbitrarily.
Priority Applications (1)
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CN201310474422.8A CN104556618B (en) | 2013-10-12 | 2013-10-12 | FFDS sludge treatment technology |
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CN201310474422.8A CN104556618B (en) | 2013-10-12 | 2013-10-12 | FFDS sludge treatment technology |
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CN104556618A true CN104556618A (en) | 2015-04-29 |
CN104556618B CN104556618B (en) | 2017-01-25 |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108863457A (en) * | 2018-08-09 | 2018-11-23 | 芜湖市三山区绿色食品产业协会 | Natural feather Organic sludge manure and preparation method thereof |
CN109731438A (en) * | 2019-03-22 | 2019-05-10 | 南京凯盛国际工程有限公司 | A kind of CO in white wine sludge recycling cement kiln flue gas2Method and system |
CN110183089A (en) * | 2019-06-24 | 2019-08-30 | 上海华畅环保设备发展有限公司 | Excess sludge dewatering and device |
CN112429933A (en) * | 2020-11-02 | 2021-03-02 | 江苏苏讯新材料科技有限公司 | Low-temperature sludge drying treatment process |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
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JP2006315885A (en) * | 2005-05-11 | 2006-11-24 | Shimizu Corp | Recycled fertilizer and method of producing the same |
CN102329060A (en) * | 2011-06-07 | 2012-01-25 | 甘肃宝地康泰农业科技有限责任公司 | Production process for disposing urban sludge by utilizing attapulgite bio-fermentation technology |
-
2013
- 2013-10-12 CN CN201310474422.8A patent/CN104556618B/en active Active
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006315885A (en) * | 2005-05-11 | 2006-11-24 | Shimizu Corp | Recycled fertilizer and method of producing the same |
CN102329060A (en) * | 2011-06-07 | 2012-01-25 | 甘肃宝地康泰农业科技有限责任公司 | Production process for disposing urban sludge by utilizing attapulgite bio-fermentation technology |
Non-Patent Citations (1)
Title |
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张亚勤等: "上海松江污水处理厂达标改造工程介绍", 《给水排水》 * |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108863457A (en) * | 2018-08-09 | 2018-11-23 | 芜湖市三山区绿色食品产业协会 | Natural feather Organic sludge manure and preparation method thereof |
CN109731438A (en) * | 2019-03-22 | 2019-05-10 | 南京凯盛国际工程有限公司 | A kind of CO in white wine sludge recycling cement kiln flue gas2Method and system |
CN109731438B (en) * | 2019-03-22 | 2024-02-20 | 中材国际智能科技有限公司 | Recovery of CO in cement kiln flue gas by white spirit sludge 2 Method and system of (2) |
CN110183089A (en) * | 2019-06-24 | 2019-08-30 | 上海华畅环保设备发展有限公司 | Excess sludge dewatering and device |
CN112429933A (en) * | 2020-11-02 | 2021-03-02 | 江苏苏讯新材料科技有限公司 | Low-temperature sludge drying treatment process |
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Effective date of registration: 20200201 Address after: 644000 No.3, 21 / F, unit 2, building 3, Yangtze River International Youth City, No.86, Section 2, Bohou Road, Cuiping District, Yibin City, Sichuan Province Patentee after: Yibin Luchuang Technology Co., Ltd. Address before: 644000 Yibin province Sichuan City Cuiping District Jinsha River Road No. 1 Vista 2 unit 2 Building No. 102 Co-patentee before: Luo Chao Patentee before: Xiao Zehua |
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