CN203878049U - Sludge deep-dehydrating treatment system - Google Patents
Sludge deep-dehydrating treatment system Download PDFInfo
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- CN203878049U CN203878049U CN201420227386.5U CN201420227386U CN203878049U CN 203878049 U CN203878049 U CN 203878049U CN 201420227386 U CN201420227386 U CN 201420227386U CN 203878049 U CN203878049 U CN 203878049U
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Abstract
The utility model relates to a sludge deep-dehydrating treatment system, and belongs to the technical field of environmental and geotechnical engineering. The dehydrating treatment system consists of a magnetizing pretreatment system, an automatic powder dosing device, an automatic water dosing device, a pipeline, a valve, a sensor, a sludge metering pump, a reagent metering pump, a sludge pump, a vacuum pressure meter, a plate-and-frame filter press and a filtrate collector, wherein the magnetizing pretreatment system can save adding amount of the reagent, and can lower reagent cost; the sensor, the automatic powder dosing device and the automatic water dosing device are connected with a control system, so that data can be monitored online in real time, dosing can be automatically regulated, and working efficiency is greatly improved; by virtue of cycle treatment of the sludge, the optimal pretreatment effect of the sludge can be reached, so that deep dehydrating of the sludge is achieved. The sludge deep-dehydrating treatment system disclosed by the utility model is reasonable in design, simple in structure, convenient to operate, capable of deeply dehydrating sludge under magnetizing and reagent multi-factor synergetic pre-treating conditions, and low in energy consumption and low in cost in a sludge modulating and dehydrating process.
Description
Technical field
The utility model relates to a kind of deeply dehydrating sludge treatment system, belongs to environmental geotechnical technical field.
Background technology
Mud is the by product forming in sewage purification process, mud because water ratio is high, organic content is high, heavy metal content is high, germ content is high is regarded as " hazardous substance " by many countries in the world.
Along with the lifting of wastewater treatment in China ability, sludge yield increases substantially.By 2015, the whole nation approximately produced 3,359 ten thousand tons every year, produced 9.2 ten thousand tons, mud daily, and China will become the country of global sludge creation amount maximum.
The situation is tense for China's sludge treatment disposal, research and analyse according to the Chinese network of rivers, nationwide enters in the mud of processing links, after only having at present 10% left and right to process by aerobic fermentation, be back to use soil, there is in addition 20% employing sanitary landfill, also have a small amount of modes such as burning, building materials utilization that adopt to dispose, remaining 70% just arbitrarily outward transport, simple landfill or stacking.If a large amount of mud can not get effectively processing and disposing, will pollute thing and invade the serious secondary pollution accident such as underground water and soil, foul gas erosion atmosphere, water body, soil and atmosphere are caused to great harm and burden.
Sludge treatment is disposed taking " minimizing, stabilization, innoxious and resource utilization " as fundamental principle, and in four principles, minimizing is basis, and stabilization treatment is core, the harmless aim that turns to, and recycling is target.Minimizing is the prerequisite that sludge treatment is disposed, and the water ratio of reduction mud is the important channel of realizing sludge reduction.
Although it is very fast that domestic sludge treatment is disposed industry development, but still have following problem: the one, dewatering efficiency is low, technique imperfection; The 2nd, technology is single, equipment is perfect not, and operation cost is relatively high; The 3rd, the mud secondary pollution after disposing has a big risk, and recycling rate is low.Therefore, novel method, new installation and the novel process of innovation sludge disposal, the disposal efficiency that improves mud is extremely urgent.
Magnetic technology has a extensive future in sludge treatment disposal field, magnetic field energy can make mud disrupted cell, change the surperficial physico-chemical property of liquid phase in mud, in mud, in microorganism inside or flco structure, a large amount of interstitial waters become free water, and mud can significantly improve the dewatering of mud after magnetization is processed.Though the equipment of chemicals treatment mud has report at home, the domestic equipment about magnetic field treatment mud rarely has report, and the equipment of the collaborative medicament pretreating sludge of magnetization is reported still less.
Therefore, be based on existing Research foundation, integrated existing technology and equipment, the deeply dehydrating sludge treatment system of the multifactor collaborative pretreating sludges such as degree research and development magnetic field and medicament, many indexs Simultaneous Monitoring is very necessary, and it is efficiently fast-developing that the research and development of deep dehydration treatment system will promote China's sludge treatment to dispose industry.
Summary of the invention
For the problem of above-mentioned existence, the purpose of this utility model is to provide a kind of deeply dehydrating sludge treatment system from the multifactor collaborative pretreating sludge of profound level, multi-angle, research and development magnetic field and medicament, many indexs Simultaneous Monitoring and modified dehydration is easy to operate, less energy consumption, cost are low.
To achieve these goals, the technical solution that the utility model adopts is:
A kind of deeply dehydrating sludge treatment system, described treatment system is made up of mud transfer roller, the first sludge pump, the second sludge pump, magnetizing assembly, the first online pH meter, the first online moisture transducer, pipeline, valve, the first mud volume pump, the second mud volume pump, the second online pH meter, the second online moisture transducer, pulvis automatic medicine adding apparatus, aqua automatic medicine adding apparatus, retort, the 3rd online pH meter, the 3rd online moisture transducer, spiral pump, vacuum pressure gauge, plate-and-frame filter press, filtrate collection.
Wherein, it is cylindric that magnetizing assembly is, on the inwall of magnetizing assembly, be provided with screen layer, screen layer is made up of magnetic shielding material, magnetizing assembly center is provided with magnetic conduction pipeline, between magnetic conduction pipeline and screen layer, be provided with strip-shaped permanent-magnet iron and strip excitation pure iron sheet, the cross section of strip-shaped permanent-magnet iron and strip excitation pure iron sheet is all fan shape, between strip excitation pure iron sheet and strip-shaped permanent-magnet iron, be evenly spaced, the two ends of strip-shaped permanent-magnet iron and strip excitation pure iron sheet are separately fixed on magnetic conduction pipeline and screen layer, and the two ends of magnetizing assembly are provided with baffle plate.
Mud transfer roller is connected with the import of the magnetic conduction pipeline in magnetizing assembly by pipeline, on connecting tube, is disposed with the first sludge pump, the first online pH meter, the first online moisture transducer, the first valve by mud transfer roller to the direction of magnetizing assembly.
The outlet of the magnetic conduction pipeline in magnetizing assembly is connected with the import of retort by pipeline, on connecting tube, be disposed with the first mud volume pump by magnetizing assembly to the direction of retort, the second online pH meter, the second online moisture transducer, in retort, be provided with retort agitator, pulvis automatic medicine adding apparatus and aqua automatic medicine adding apparatus are separately positioned on the top of retort, the outlet of retort is connected by pipeline with the import of plate-and-frame filter press, on connecting tube, be disposed with the second mud volume pump by retort to the direction of plate-and-frame filter press, the 3rd online pH meter, the 3rd online moisture transducer, the second valve, spiral pump, vacuum pressure gauge, the outlet of plate-and-frame filter press is connected with filtrate collection.
On the pipeline between the first valve and the second valve, be provided with circulating line, the Link Port of circulating line one end is between the first valve and magnetizing assembly, be provided with the 3rd valve at Link Port place, the Link Port of the circulating line the other end is between the 3rd online moisture transducer and the second valve, be provided with the 4th valve at Link Port place, in the middle of circulating line, be provided with the second sludge pump.
Described the first online pH meter, the first online moisture transducer, the second online pH meter, the second online moisture transducer, the 3rd online pH meter, the 3rd online moisture transducer, pulvis automatic medicine adding apparatus are connected with Controlling System by wire respectively with aqua automatic medicine adding apparatus.
Described strip excitation pure iron sheet and strip-shaped permanent-magnet iron cross-sectional area are than being 1:2.
Owing to adopting above technical scheme, a kind of deeply dehydrating sludge treatment system that the utility model relates to, the magnetization pretreatment unit adopting can make mud disrupted cell, improve the dewatering of mud, saving dosage and the medicament expense of medicament uses, circulating line makes repeatedly circular treatment of mud, sludge treatment is even, in working cycle, the moisture of moisture transducer and the rear mud of pH meter Real-Time Monitoring processing and pH value can obtain the best pretreatment parameter of mud, pulvis is connected the automatic feeding of having realized medicament with Controlling System by wire with aqua automatic medicine adding apparatus, can increase work efficiency, the utility model is reasonable in design, simple in structure, easy to operate, can be issued to deep dehydration and the modified dehydration less energy consumption of mud of mud in magnetization and the multifactor collaborative pretreatment condition of medicament, cost is low.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model
Fig. 2 is the A-A diagrammatic cross-section of Fig. 1
specific implementation method
Below in conjunction with accompanying drawing, the utility model is explained in further detail.
See accompanying drawing, a kind of deeply dehydrating sludge treatment system, described treatment system is by mud transfer roller 1, the first sludge pump 2, the second sludge pump 20, magnetizing assembly 6, the first online pH meter 3, the first online moisture transducer 4, pipeline, valve, the first mud volume pump 7, the second mud volume pump 23, the second online pH meter 8, the second online moisture transducer 9, pulvis automatic medicine adding apparatus, aqua automatic medicine adding apparatus, retort 22, the 3rd online pH meter 16, the 3rd online moisture transducer 17, spiral pump 25, vacuum pressure gauge 26, plate-and-frame filter press 27, filtrate collection 28 forms.
Wherein, magnetizing assembly 6 is cylindric, is provided with screen layer 29 on the inwall of magnetizing assembly 6, and screen layer is made up of magnetic shielding material, and screen layer 29 can be by magnetic field shielding, reduces magnetic field impact to external world.The center of magnetizing assembly 6 is provided with magnetic conduction pipeline, between magnetic conduction pipeline and screen layer 29, be provided with strip-shaped permanent-magnet iron 31 and strip excitation pure iron sheet 30 around even circumferential, the two ends of strip-shaped permanent-magnet iron 31 and strip excitation pure iron sheet 30 are separately fixed on magnetic conduction pipeline and screen layer 29.The cross section of strip-shaped permanent-magnet iron 31 and strip excitation pure iron sheet 30 is all fan shape, and strip excitation pure iron sheet 30 and strip-shaped permanent-magnet iron 31 cross-sectional areas are than being 1:2.Between strip excitation pure iron sheet 30 and strip-shaped permanent-magnet iron 31, be evenly spaced, strip-shaped permanent-magnet iron 31 and strip excitation pure iron sheet 30 provide magnetic field for magnetizing assembly.Strip excitation pure iron sheet 30 can improve the magneticstrength of strip-shaped permanent-magnet iron 31, plays the effect of excitation.The two ends of magnetizing assembly 6 are provided with baffle plate.
Mud transfer roller 1 is connected with the import of the magnetic conduction pipeline in magnetizing assembly 6 by pipeline, on connecting tube, is disposed with the first sludge pump 2, the first online pH meter 3, the first online moisture transducer 4, the first valve 5 by mud transfer roller 1 to the direction of magnetizing assembly 6;
The outlet of the magnetic conduction pipeline in magnetizing assembly 6 is connected with the import of retort 22 by pipeline, on connecting tube, be disposed with the first mud volume pump 7 by magnetizing assembly 6 to the direction of retort 22, the second online pH meter 8, the second online moisture transducer 9, in retort 22, be provided with retort agitator 21, pulvis automatic medicine adding apparatus and aqua automatic medicine adding apparatus are separately positioned on the top of retort 22, pulvis automatic medicine adding apparatus is by pulvis volume pump 12, powder dispenser 10 and powder dispenser agitator 11 form, the entrance end of pulvis volume pump 12 connects powder dispenser 10 by pipeline, the exit end of pulvis volume pump 12 is by pipeline ligation tank 22, in powder dispenser 10, be provided with powder dispenser agitator 11, aqua automatic medicine adding apparatus is by aqua volume pump 13, aqua tank 15 and aqua jar agitator 14 form, the entrance end of aqua volume pump 13 connects aqua tank 15 by pipeline, the exit end of aqua volume pump 13 is by pipeline ligation tank 22, in aqua tank 15, be provided with aqua jar agitator 14,
The outlet of retort 22 is connected by pipeline with the import of plate-and-frame filter press 27, on connecting tube, be disposed with the second mud volume pump 23, the 3rd online pH meter 16, the 3rd online moisture transducer 17 by retort 22 to the direction of plate-and-frame filter press 27, the second valve 18, spiral pump 25, vacuum pressure gauge 26, the outlet of plate-and-frame filter press 27 is connected with filtrate collection 28;
On the pipeline between the first valve 5 and the second valve 18, be provided with circulating line, the Link Port of circulating line one end is between the first valve 5 and magnetizing assembly 6, be provided with the 3rd valve 19 at Link Port place, the Link Port of the circulating line the other end is between the 3rd online moisture transducer 17 and the second valve 18, be provided with the 4th valve 24 at Link Port place, in the middle of circulating line, be provided with the second sludge pump 20.
Described the first online pH meter 3, the first online moisture transducer 4, the second online pH meter 8, the second online moisture transducer 9, the 3rd online pH meter 16, the 3rd online moisture transducer 17, pulvis automatic medicine adding apparatus are connected with Controlling System by wire respectively with aqua automatic medicine adding apparatus, and Controlling System can adopt PLC automatic programme control system.
The principle of work of the utility model testing apparatus:
When the operation of this deeply dehydrating sludge treatment system, connect the power supply of PLC automatic programme control system, open computer control system, each online pH meter, online moisture transducer, pulvis automatic medicine adding apparatus and aqua automatic medicine adding apparatus are normally worked.Open the first valve, carry mud to extract out through the first sludge pump by mud transfer roller, after the first online pH meter and the first online moisture transducer, can demonstrate pH value and the moisture content of pending mud.Pending mud magnetizes processing after entering magnetizing assembly, determine the volume that enters mud in retort by the first mud volume pump, when reach retort volume 3/4ths time close the first valve, gone out pH value and the moisture content of mud after magnetization is processed by the second online pH meter and the second online moisture transducer Real-Time Monitoring.Select medicament kind by the pH value of monitoring and moisture content, volume pump by pulvis automatic medicine adding apparatus and aqua automatic medicine adding apparatus is injected into the medicament stirring in retort, and after magnetization pre-treatment, mud evenly mixes under the effect of retort agitator with medicament after entering retort.Extract out by the second mud volume pump through the mud magnetizing after pre-treatment and chemicals treatment mix, demonstrate in real time pH value and the moisture content of mud after magnetization and the collaborative pre-treatment of medicament by the 3rd online pH meter and the 3rd online moisture transducer.If pH value and the moisture content of mud reach dehydration requirement after the collaborative pre-treatment of magnetization and medicament, opening the second valve is injected in plate-and-frame filter press by spiral pump, in the time that mud volume reaches the volume that plate-and-frame filter press can work, start plate-and-frame filter press and carry out sludge dewatering treatment, filtrate collection after filter press is in filtrate collection, and the filter cake after filter press carries out disposal of resources.If pH value and the moisture content of mud do not reach dehydration requirement after the collaborative pre-treatment of magnetization and medicament, open the 3rd valve and the 4th valve, the complete mud of first pre-treatment is re-injected in magnetization pretreatment unit by the second sludge pump being arranged in circulating line, by the rotating speed control magnetizing time of volume pump, gone out pH value and the moisture content of mud after magnetization is processed by the second online pH meter and the second online moisture transducer Real-Time Monitoring.Select medicament kind and added amount of chemical by the pH value of monitoring and moisture content, volume pump by pulvis and aqua automatic medicine adding apparatus is injected into the medicament stirring in retort, and after magnetization pre-treatment, mud evenly mixes under the effect of retort agitator with medicament after entering retort.Extract out by the second mud volume pump through the mud magnetizing after pre-treatment and chemicals treatment mix, demonstrate in real time pH value and the moisture content of mud after magnetization and the collaborative pre-treatment of medicament by the 3rd online pH meter and the 3rd online moisture transducer, circulation reaches dehydration requirement until magnetization and medicament are worked in coordination with pH value and the moisture content of mud after pre-treatment successively, closes the 3rd valve and the 4th valve.Opening the second valve is injected in plate-and-frame filter press by spiral pump, in the time that mud volume reaches the volume that plate-and-frame filter press can work, start plate-and-frame filter press and carry out sludge dewatering treatment, the filtrate collection after filter press is in filtrate collection, and the filter cake after filter press carries out disposal of resources.After system is out of service, will cleans in time and maintain, the each device for the treatment of system should be made regular check on, and changes in time the device that does not meet treatment system requirement and have potential safety hazard, guarantees the work-ing life for the treatment of system and safe trouble-free operation next time.
Claims (3)
1. a deeply dehydrating sludge treatment system, it is characterized in that: described treatment system is by mud transfer roller (1), the first sludge pump (2), the second sludge pump (20), magnetizing assembly (6), the first online pH meter (3), the first online moisture transducer (4), pipeline, valve, the first mud volume pump (7), the second mud volume pump (23), the second online pH meter (8), the second online moisture transducer (9), pulvis automatic medicine adding apparatus, aqua automatic medicine adding apparatus, retort (22), the 3rd online pH meter (16), the 3rd online moisture transducer (17), spiral pump (25), vacuum pressure gauge (26), plate-and-frame filter press (27), filtrate collection (28) composition,
Wherein, magnetizing assembly (6) is cylindric, on the inwall of magnetizing assembly (6), be provided with screen layer (29), screen layer is made up of magnetic shielding material, magnetizing assembly (6) center is provided with magnetic conduction pipeline, between magnetic conduction pipeline and screen layer (29), be provided with strip-shaped permanent-magnet iron (31) and strip excitation pure iron sheet (30), the cross section of strip-shaped permanent-magnet iron (31) and strip excitation pure iron sheet (30) is all fan shape, between strip excitation pure iron sheet (30) and strip-shaped permanent-magnet iron (31), be evenly spaced, the two ends of strip-shaped permanent-magnet iron (31) and strip excitation pure iron sheet (30) are separately fixed on magnetic conduction pipeline and screen layer (29), the two ends of magnetizing assembly (6) are provided with baffle plate,
Mud transfer roller (1) is connected with the import of the magnetic conduction pipeline in magnetizing assembly (6) by pipeline, on connecting tube, is disposed with the first sludge pump (2), the first online pH meter (3), the first online moisture transducer (4), the first valve (5) by mud transfer roller (1) to the direction of magnetizing assembly (6);
The outlet of the magnetic conduction pipeline in magnetizing assembly (6) is connected with the import of retort (22) by pipeline, on connecting tube, be disposed with the first mud volume pump (7), the second online pH meter (8), the second online moisture transducer (9) by magnetizing assembly (6) to the direction of retort (22), in retort (22), be provided with retort agitator (21), pulvis automatic medicine adding apparatus and aqua automatic medicine adding apparatus are separately positioned on the top of retort (22);
The outlet of retort (22) is connected by pipeline with the import of plate-and-frame filter press (27), on connecting tube, be disposed with the second mud volume pump (23), the 3rd online pH meter (16), the 3rd online moisture transducer (17) by retort (22) to the direction of plate-and-frame filter press (27), the second valve (18), spiral pump (25), vacuum pressure gauge (26), the outlet of plate-and-frame filter press (27) is connected with filtrate collection (28);
On the pipeline between the first valve (5) and the second valve (18), be provided with circulating line, the Link Port of circulating line one end is positioned between the first valve (5) and magnetizing assembly (6), be provided with the 3rd valve (19) at Link Port place, the Link Port of the circulating line the other end is positioned between the 3rd online moisture transducer (17) and the second valve (18), be provided with the 4th valve (24) at Link Port place, in the middle of circulating line, be provided with the second sludge pump (20).
2. a kind of deeply dehydrating sludge treatment system as claimed in claim 1, is characterized in that: described the first online pH meter (3), the first online moisture transducer (4), the second online pH meter (8), the second online moisture transducer (9), the 3rd online pH meter (16), the 3rd online moisture transducer (17), pulvis automatic medicine adding apparatus are connected with Controlling System by wire respectively with aqua automatic medicine adding apparatus.
3. a kind of deeply dehydrating sludge treatment system as claimed in claim 1, is characterized in that: described strip excitation pure iron sheet (30) and strip-shaped permanent-magnet iron (31) cross-sectional area are than being 1:2.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420227386.5U CN203878049U (en) | 2014-05-06 | 2014-05-06 | Sludge deep-dehydrating treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420227386.5U CN203878049U (en) | 2014-05-06 | 2014-05-06 | Sludge deep-dehydrating treatment system |
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| Publication Number | Publication Date |
|---|---|
| CN203878049U true CN203878049U (en) | 2014-10-15 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420227386.5U Withdrawn - After Issue CN203878049U (en) | 2014-05-06 | 2014-05-06 | Sludge deep-dehydrating treatment system |
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| Country | Link |
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| CN (1) | CN203878049U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103979764A (en) * | 2014-05-06 | 2014-08-13 | 中国科学院武汉岩土力学研究所 | Deep dewatering treatment system for sludge |
| CN108548910A (en) * | 2018-04-16 | 2018-09-18 | 中国计量大学 | A kind of deep dehydration sludge moisture content detection method |
-
2014
- 2014-05-06 CN CN201420227386.5U patent/CN203878049U/en not_active Withdrawn - After Issue
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103979764A (en) * | 2014-05-06 | 2014-08-13 | 中国科学院武汉岩土力学研究所 | Deep dewatering treatment system for sludge |
| CN108548910A (en) * | 2018-04-16 | 2018-09-18 | 中国计量大学 | A kind of deep dehydration sludge moisture content detection method |
| CN108548910B (en) * | 2018-04-16 | 2020-06-23 | 中国计量大学 | Method for detecting water content of deep dewatered sludge |
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Legal Events
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20141015 Effective date of abandoning: 20150805 |
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| AV01 | Patent right actively abandoned |
Granted publication date: 20141015 Effective date of abandoning: 20150805 |
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| RGAV | Abandon patent right to avoid regrant |