CN104098241A - Sewage sludge advanced treatment device - Google Patents
Sewage sludge advanced treatment device Download PDFInfo
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- CN104098241A CN104098241A CN201410381230.7A CN201410381230A CN104098241A CN 104098241 A CN104098241 A CN 104098241A CN 201410381230 A CN201410381230 A CN 201410381230A CN 104098241 A CN104098241 A CN 104098241A
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- sewage sludge
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- 239000010801 sewage sludge Substances 0.000 title claims abstract description 24
- 238000007710 freezing Methods 0.000 claims abstract description 69
- 230000008014 freezing Effects 0.000 claims abstract description 69
- 238000001035 drying Methods 0.000 claims abstract description 49
- 239000002918 waste heat Substances 0.000 claims abstract description 25
- 239000010802 sludge Substances 0.000 claims abstract description 23
- 239000007789 gas Substances 0.000 claims abstract description 20
- 238000009434 installation Methods 0.000 claims description 31
- 230000007246 mechanism Effects 0.000 claims description 28
- 239000006200 vaporizer Substances 0.000 claims description 24
- 238000003825 pressing Methods 0.000 claims description 20
- 230000007306 turnover Effects 0.000 claims description 20
- 238000000034 method Methods 0.000 claims description 19
- 239000003546 flue gas Substances 0.000 claims description 16
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 15
- 239000008187 granular material Substances 0.000 claims description 14
- 239000007788 liquid Substances 0.000 claims description 14
- 238000001914 filtration Methods 0.000 claims description 13
- 230000008569 process Effects 0.000 claims description 13
- 238000010438 heat treatment Methods 0.000 claims description 12
- 238000010257 thawing Methods 0.000 claims description 11
- 239000000779 smoke Substances 0.000 claims description 8
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 claims description 5
- 239000012530 fluid Substances 0.000 claims description 5
- 239000013618 particulate matter Substances 0.000 claims description 4
- 238000002485 combustion reaction Methods 0.000 abstract description 3
- 238000004064 recycling Methods 0.000 abstract description 2
- 238000004108 freeze drying Methods 0.000 abstract 2
- 239000013043 chemical agent Substances 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- 239000003795 chemical substances by application Substances 0.000 description 8
- 238000005189 flocculation Methods 0.000 description 8
- 230000016615 flocculation Effects 0.000 description 8
- 230000000694 effects Effects 0.000 description 6
- 239000000084 colloidal system Substances 0.000 description 5
- 230000018044 dehydration Effects 0.000 description 5
- 238000006297 dehydration reaction Methods 0.000 description 5
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- 238000006062 fragmentation reaction Methods 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 4
- 239000010865 sewage Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 3
- 235000011941 Tilia x europaea Nutrition 0.000 description 3
- 230000008030 elimination Effects 0.000 description 3
- 238000003379 elimination reaction Methods 0.000 description 3
- 239000004571 lime Substances 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 239000002912 waste gas Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
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- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
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- 238000007791 dehumidification Methods 0.000 description 1
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Landscapes
- Drying Of Solid Materials (AREA)
- Treatment Of Sludge (AREA)
Abstract
The invention discloses a sewage sludge advanced treatment device which comprises a crushing device, a drying device, a combustion device and a waste heat boiler. The sewage sludge advanced treatment device further comprises a sludge freezing container and a freeze drying energy circulating system. The freeze drying energy circulating system comprises a compressor, an evaporator, a condenser and a first heat exchanger arranged in the sludge freezing container. The air outlet end of the compressor is connected with the condenser, the evaporator is connected with the air inlet end of the compressor through the first heat exchanger, the condenser is communicated with the bottom of the drying device through a gas pipeline, and the evaporator is communicated with the top of the drying device through a gas pipeline. A heat conduction oil pipe is arranged in the waste heat boiler and performs heat transfer with air to heat the air, and the air heated is respectively conveyed to the drying device and the sludge freezing container to be used for sludge drying and unfreezing. According to the sewage sludge advanced treatment device, chemical agents do not need to be added, the sludge treatment amount is not increased, and sludge freezing efficiency and the heat utilization rate are improved through recycling of working medium energy and heat of sludge.
Description
Technical field
The present invention relates to sewage sludge process field, specifically a kind of sewage sludge advanced treatment apparatus.
Background technology
In sewage treatment process, produce a large amount of mud, its quantity accounts for the 0.3%-0.5% that processes the water yield, processing investment and the running cost of mud are very huge, generally account for the 20%-50% of sewage work's working cost for the expense of sludge treatment, have brought white elephant to sewage disposal.The method of sludge treatment mainly contains conditioning, dehydration, dry, then burns, the Disposal Measures such as landfill, recycling.Sludge dewatering is the very important ring of sludge treatment, and for mud, follow-up processing is disposed and had vital role.The key of sludge dewatering is to improve the dewatering of mud, current traditional treatment process is by adding flocculation agent and lime is first nursed one's health, then enter pressure filter and carry out mechanical dehydration, the mud outward transport that forms water ratio 60% left and right is dried, burning etc.Adding flocculation agent pretreatment process is the throwing out by flocculation agent, reduce the avidity of mud and water, change the existence form of moisture in mud, in and sewage in contrary electric charge, compression double electric layer, plays adsorption bridging to de-steady flocculated particle, makes it form fast large flco, thereby make elimination of colloid stability cohesion, realize solid-liquid separation.Flocculant dosage is to account for the per-cent of sewage sludge solid dry weight, and different flocculant dosages can be distinguished to some extent.Although can significantly improve the dewatering of mud by adding the method for flocculation agent, but due to a large amount of flocculation agent of needs, not only increase the cost of sludge treatment, and a large amount of flocculation agents can be increased in the mud after dehydration, strengthen the treatment capacity of mud, and the lime adding is alkalescence, there is certain corrosive nature for follow-up drying and incinerating equipment, according to practical experience, to burn for the mud that adds flocculation agent and lime, the incinerator life-span can decline.And the amount of heat that other pretreatment processs need to consume as ultrasonic wave, microwave treatment, and need to set up corresponding treatment unit; Adopt biological process and thermodynamic method need to consume a large amount of biotechnological formulations and heat.
Adopt freezing method to carry out pre-treatment in early stage to mud, mud is through destroying the bonding force of mud and water and destroy the structure (be similar to freezing after built-in bean curd) of colloid after repeatedly freezing, make elimination of colloid stability cohesion and membranolysis, make out to form the easily interstitial water to remove of mechanical means with the cell interior water dialysis that mechanical means is difficult to remove, the rapid sedimentation of mud granule, dewatering speed is front higher tens times than freezing, adopt freezing method not add medicament, can save reagent cost, and can additionally not increase the mud handling capacity in later stage, simultaneously, life-span for subsequent processing device does not also affect.In conjunction with mud method for subsequent processing, complete sludge deep minimizing processing again.
But, the freezing main dependence physical environment of prior art to mud, mud being placed in to outdoor dependence physical environment under arctic weather is cooled to-10 DEG C of left and right and carries out freezing and thaw, but low, the consuming time length of efficiency, if and just in southern area or cannot operate in situation non-winter, natural condition require comparatively harsh.In addition, prior art is used external force carry out freezing and thaw and need to freeze and heat dual energy mud mud, and the waste gas of incineration organic efficiency after drying sludge is not high, and cost is very high, therefore be difficult to apply.
Summary of the invention
In view of this, the present invention is directed to the problem that increase flocculation agent can increase mud handling capacity and freezing efficiency is low, the waste gas of incineration rate of recovery is low that above-mentioned prior art exists, provide a kind for the treatment of processes can not increase mud handling capacity, the sewage sludge advanced treatment apparatus that freezing efficiency is high and capacity usage ratio is high.
Technical solution of the present invention is, a kind of sewage sludge advanced treatment apparatus of following structure is provided, comprise filter-pressing device, shredder assembly, drying installation, incinerator and waste heat boiler, filter-pressing device carries out carrying out break process by shredder assembly after press filtration processing to mud, after sludge crushing, enter drying installation and carry out drying treatment, dried mud granule is sent in incinerator and is burned, and burns the high-temperature flue gas producing and enters waste heat boiler;
Described sewage sludge treatment unit also comprises mud freezing container and lyophilize energy cycle system, described lyophilize energy cycle system comprises compressor, vaporizer, condenser and is arranged at the First Heat Exchanger in mud freezing container, the outlet side of compressor is connected with condenser, condenser is connected with vaporizer through throttling element, and vaporizer is connected with the inlet end of compressor through First Heat Exchanger; Described condenser is connected with drying installation bottom by gas pipeline, and vaporizer is connected with drying installation top by gas pipeline, and described condenser is connected by gas pipeline with vaporizer simultaneously;
In described waste heat boiler, be provided with heat-conducting oil pipes, heat-conducting oil pipes and air carry out heat and transmit air heating, and the air after heating is inputted respectively drying installation and mud freezing container, for drying sludge and thawing.
Adopt above structure, the present invention compared with prior art, have the following advantages: adopt the present invention, utilize lyophilize energy cycle system, realized the freezing of mud in freezing container and being dried mud in drying installation simultaneously, working medium is under compressor effect, output High Temperature High Pressure gaseous working medium, through condenser, heat in working medium is by absorption of air, transfer heat to air, air themperature raises, Temperature of Working reduces, warm air passes in drying installation material is dried, working medium is condensed and becomes high-pressure liquid, high-pressure liquid working medium becomes low-pressure liquid working medium after throttling element step-down, low-pressure liquid working medium enters into vaporizer, absorb the air heat (from material top air out) in vaporizer, to air cooling-down, after saturated air cooling, the moisture that it can hold reduces, unnecessary hydrogenesis becomes liquid water to drain by the water accumulating disc of vaporizer, after working medium heat absorption, become low pressure gaseous state from low-pressure liquid (insufficient if working medium absorbs the heat of air, the working medium that can only ensure operative liquid flashes to gaseous working medium, and the liquid refrigerant of remainder and gaseous working medium form two-phase working substance) enter into First Heat Exchanger, working medium absorbs the heat of mud in First Heat Exchanger, mud is cooled to needed freezing temp-10 DEG C～-15 DEG C (this temperature range is better, but be not limited to this numerical range), now liquid working substance is gasificated into gaseous working medium, gaseous working medium enters in compressor.Mud is through repeatedly freezing and thaw (thaw and can naturally thaw) in mud freezing container, destroy the structure of mud, enter filter-pressing device through the mud thawing, mud is pressed into bulk pie mud by filter-pressing device, send into again shredder assembly and carry out fragmentation formation mud granule, mud granule is dried in drying installation, has realized the stage processing of mud.Due to without adding chemicals in mud, therefore treating processes can not increase mud handling capacity, the recycle of working medium energy has improved the freezing efficiency of mud greatly; Only need the compressor energy a small amount of by cost, working medium can be by the heat " carrying " that is several times as much as energy consumption of compressor in freezing container in loft drier, realize the freezing and drying sludge of mud simultaneously, solved the cold source of freezing needs, solve again the origin of heat of dry needs, make cold and heat reach an extraordinary balance, greatly improved heat service efficiency, energy-saving effect is obvious; Meanwhile, the heat in waste heat boiler is recovered for thawing of mud and being dried of mud granule, has further promoted capacity usage ratio.
As preferably, waste heat boiler is extended at the two ends of heat-conducting oil pipes, and is connected with the second interchanger, and thermal oil enters the second interchanger and transfers heat to air; Air after the device that is condensed heating enters into the second interchanger and continues to absorb heat, forms high temperature air, and high temperature air, after blower fan pressurization, enters drying installation and mud freezing container by hot gas duct respectively.Thereby the heat in waste heat boiler is thawed for mud and mud granule dry.
As preferably, described mud freezing container is multiple, First Heat Exchanger is corresponding one by one with mud freezing container, the two ends of the First Heat Exchanger in multiple mud freezing containers are connected with vaporizer and compressor by working medium reversing valve respectively, the bottom of mud freezing container is provided with filtration, and the bottom of multiple mud freezing containers is passed through liquid reversing valve and is communicated with filter-pressing device through fluid pipeline.Like this, the mud in a mud freezing container carry out freezing in, the mud of part mud freezing container carries out nature and thaws, what thawed is directly delivered in filter-pressing device, thereby improve processing efficiency, can produce continuously.
As preferably, described drying installation comprises loft drier and mud panel turnover mechanism, described mud panel turnover mechanism, and level is arranged on the vertical height of difference in loft drier, described mud panel turnover mechanism is staggered, and a mud panel turnover mechanism of bottommost layer stretches out outside loft drier.Like this, mud enters drying installation after fragmentation, first fall into the mud panel turnover mechanism the superiors, along with the transmission of mud panel turnover mechanism, mud drops on the mud panel turnover mechanism of lower one deck, the mud panel turnover mechanism of lower one deck commutates and drives to other one end, and so forth, can realize warm air and contact up and down with mud, omnibearing dry, improve drying effect, in the time dropping down onto a mud panel turnover mechanism of bottommost layer, because it stretches out outside loft drier, mud is sent to outside loft drier by it, enters next step operation processing.
As preferably, described filter-pressing device is plate-and-frame filter press, plate-and-frame filter press comprises multiple sheet frames, below sheet frame, be provided with drawing-plate mechanism, described drawing-plate mechanism comprises polylith guiding piece and slide plate, is provided with articulated linkage, and is equipped with roller between adjacent two guiding pieces under every guiding piece, described polylith guiding piece is placed on slide plate, and can be rolled and be connected with slide plate by roller.Like this, carry out pull by polylith drawing-plate mechanism, can realize the pull of multiple sheet frames, solved the current problem of a sheet frame of pull simultaneously, shorten the arm-tie time, improved the efficiency of press filtering of filter-pressing device.
As preferably, described waste heat boiler is provided with smoke eliminator, and described smoke eliminator removes the sour gas in flue gas and traps the particulate matter in flue gas.
Brief description of the drawings
Fig. 1 is sewage sludge advanced treatment apparatus schematic diagram of the present invention;
Fig. 2 is the structural representation of drawing-plate mechanism;
Fig. 3 adopts the present invention to carry out the FB(flow block) of sewage sludge advanced treatment.
As shown in the figure, 1, filter-pressing device, 1.1, sheet frame, 1.2, guiding piece, 1.3, slide plate, 1.4, articulated linkage, 1.5, roller, 2, shredder assembly, 3, drying installation, 3.1, loft drier, 3.2, mud panel turnover mechanism, 4, mud freezing container, 5, compressor, 6, vaporizer, 7, condenser, 8, First Heat Exchanger, 9, throttling element, 10, gas pipeline, 11, working medium reversing valve, 12, filtration, 13, liquid reversing valve, 14, fluid pipeline, 15, rotor pump, 16, incinerator, 17, waste heat boiler, 18, heat-conducting oil pipes, 19, the second interchanger, 20, hot gas duct, 21, smoke eliminator, 22, flue, 23, transfer mechanism, 24, blower fan.
Embodiment
Below in conjunction with the drawings and specific embodiments, the invention will be further described.
As shown in the figure, a kind of sewage sludge treatment unit of the present invention, comprise filter-pressing device 1, shredder assembly 2, drying installation 3, incinerator 16 and waste heat boiler 17, filter-pressing device 1 carries out carrying out break process by shredder assembly 2 after press filtration processing to mud, after sludge crushing, enter drying installation 3 and carry out drying treatment, dried mud granule is sent into the interior burning of incinerator 16 (entering incinerator by transfer mechanism 23 from the feed opening of drying installation), burns the high-temperature flue gas producing and enters waste heat boiler 17;
Described sewage sludge treatment unit also comprises mud freezing container 4 and lyophilize energy cycle system, described lyophilize energy cycle system comprises compressor 5, vaporizer 6, condenser 7 and is arranged at the First Heat Exchanger 8 in mud freezing container 4, the outlet side of compressor 5 is connected with condenser 6, condenser 7 is connected with vaporizer 6 through throttling element 9, and vaporizer 6 is connected with the inlet end of compressor 5 through First Heat Exchanger 8; Described condenser 7 is connected with drying installation 3 bottoms by gas pipeline 10, and vaporizer 6 is connected with drying installation 3 tops by gas pipeline 10, and described condenser 7 is connected by gas pipeline 10 with vaporizer 6 simultaneously;
In described waste heat boiler 17, be provided with heat-conducting oil pipes 18, heat-conducting oil pipes 8 carries out heat with air and transmits air heating, and the air after heating is inputted respectively drying installation 3 and mud freezing container 4, for mud be dried and thaw.
Waste heat boiler 17 is extended at the two ends of heat-conducting oil pipes 18, and is connected with the second interchanger 19, and thermal oil enters the second interchanger 19 and transfers heat to air; The air being condensed after device 7 heating enters into the second interchanger 19 and continues to absorb heat, forms high temperature air, and high temperature air, after blower fan 24 pressurizations, enters drying installation 3 and mud freezing container 4 by hot gas duct 20 respectively.
Described mud freezing container 4 is multiple, First Heat Exchanger 8 is corresponding one by one with mud freezing container 4, the two ends of the First Heat Exchanger 8 in multiple mud freezing containers 4 are connected with vaporizer 6 and compressor 5 by working medium reversing valve 11 respectively, the bottom of mud freezing container 4 is provided with filtration 12, and the bottom of multiple mud freezing containers 4 is communicated with filter-pressing device 1 by liquid reversing valve 13 and through fluid pipeline 14; Mud after thawing pumps into filter-pressing device 1 by rotor pump 15 from mud freezing container 4.
Described drying installation 3 comprises loft drier 3.1 and mud panel turnover mechanism 3.2, described mud panel turnover mechanism, level is arranged on the vertical height of difference in loft drier 3.1, and described mud panel turnover mechanism 3.2 is staggered, and a mud panel turnover mechanism 3.2 of bottommost layer stretches out outside loft drier 3.1.
Described filter-pressing device 1 is plate-and-frame filter press, plate-and-frame filter press comprises multiple sheet frames 1.1, below sheet frame 1.1, be provided with drawing-plate mechanism, described drawing-plate mechanism comprises polylith guiding piece 1.2 and slide plate 1.3, between adjacent two guiding pieces 1.2, be provided with articulated linkage 1.4, and being equipped with roller 1.5 1.2 times at every guiding piece, described polylith guiding piece 1.2 is placed on slide plate 1.3, and can be rolled and be connected with slide plate 1.3 by roller 1.5.
High-temperature gas enters waste heat boiler 17 by flue 22, and described waste heat boiler 17 is provided with smoke eliminator 21, and described smoke eliminator 21 removes the sour gas in flue gas and traps the particulate matter in flue gas.
Sludge deep process flow is:
1) carry out repeatedly under 72 hours in freezing temp-10 DEG C～-15 DEG C, freezing time freezing;
2) between 20-50 DEG C, thaw (can adopt normal temperature unfreezing), thawing time is about 6 hours;
3) in plate-and-frame filter press, carry out mechanical dehydration, first it is the press filtration stage, press filtration pressure is 1.0-1.2Mpa, time of filter pressing is 1.5-2 hour, now moisture percentage in sewage sludge 65%-70%, then enter into the press dewatering stage, squeeze pressure is 1.5Mpa, the squeezing time is 1 hour, now the about 60%-65% of moisture percentage in sewage sludge;
4) plate-and-frame filter press bulk mud cake shape mud is out carried out to fragmentation in mud mixing shredder assembly, form little mud granule, mud granule size is generally in 20mm left and right;
5) mud after fragmentation is delivered in drying installation and is dried, drying installation is Multi-layer panel-turnover, and be 1 hour time of drying, drying temperature 60-100 DEG C, after super-dry, the water ratio of mud is 10%-15%, and now vaporizer provides cold to mud freezing container;
6) burn being sent to incinerator through the mud of super-dry, 850 DEG C of flue gases of generation are discharged and are entered into waste heat boiler by flue;
7) in waste heat boiler, high-temperature flue gas transfers heat to thermal oil, and thermal oil is heated to 250 DEG C of left and right, and thermal oil enters into the second interchanger and transfers heat to air, air is heated, and the air after heating enters in drying installation mud is dried;
8) smoke eliminator of Heat Treatment device gas outlet setting removes and the trapping of particulate matter sour gas, makes the flue gas of discharging atmosphere meet environmental requirement.
Specific works principle is as follows:
Mud enters into mud freezing container, first under First Heat Exchanger effect, refrigeration working medium enter into First Heat Exchanger in, working medium is absorbed heat to mud, make the freezing temp of mud reach specified temperature, mud under-10 DEG C～-15 DEG C, freezing time 72 hours through repeatedly freezing, destroy the bonding force of mud and water and the structure of destruction colloid, make elimination of colloid stability cohesion and membranolysis, the rapid sedimentation of mud granule, dewatering significantly improves, and dewatering speed is front higher tens times than freezing, freezing end.Now, working medium reversing valve flows to and commutates working medium, and working medium flow-reversal, in another mud freezing container, has now been passed into the air with certain temperature in freezing mud freezing container and thawed, air themperature is between 20-50 DEG C, and thawing time is 6 hours.
After thawing, mud passes through fluid pipeline, enter rotor pump, adding of rotor pump depress enter board and frame machine (plate-and-frame filter press) start press filtration carry out mechanical dehydration, after press filtration after a while, pull open sheet frame, the mud of mud cake shape drops in device for transporting objects, be transported to crusher through device for transporting objects, crusher carries out fragmentation to mud cake, form little mud granule, mud granule size remains on 20mm left and right, become short grained mud to improve the specific surface area of mud, be beneficial to the contact area that increases mud and high temperature air in dry, improve drying rate and effect.
Little mud granule enters into the upper strata turnover panel in drying machine, drops from level to level from top to down, and in the process dropping, constantly upset of mud, all fully contacts each surface with air.Dry air contacts with mud from bottom to top, absorption of air the moisture of mud become the wet air that humidity is very high and after vaporizer, drop to below dew point, separate out moisture, the moisture of separating out is discharged through water accumulating disc, air continues after condenser heated, enters in loft drier mud is dried.Mud leaves loft drier after being heated and being dried after basecoat turnover panel.
Mud is transported to incinerator by device for transporting objects after leaving loft drier, adjusting enters a wind of combustion chamber, under refiner effect, make it in fluidized bed combustion state, because the medium in fluidized-bed is in suspended state, gas-solid can fully mix contact, in whole stove, the temperature of burning zone is comparatively even, and the approximately 850 DEG C of discharges of waste gas that produce after burning enter into waste heat boiler.Meanwhile, the thermal oil in waste heat boiler is heated to 250 DEG C by 220 DEG C, and the thermal oil after heated heats air by the second interchanger, and the air after heating enters into dehumidification system and thawing apparatus to drying sludge and the heat supply of thawing.Gas-cleaning installation is made up of removing with particle collection two parts of sour gas, gas sweetening can adopt semidrying, in flue gas, spray into certain calcium oxide, make it to react with the acidic substance in flue gas, and reach spray-dired reaction process by spraying plant control moisture.Depickling reactant is essentially solid state, there will not be discharge of wastewater.In flue gas, particle collection can be realized in conjunction with cyclonic separator or cloth bag by filtering net, sprays into a certain amount of activated carbon grain powder, the objectionable impuritiess such as absorption heavy metal in flue gas and Dioxins before.Can discharge atmosphere through purified gas, environmental pollution is few.
Below only just preferred embodiment of the present invention is described, but can not be interpreted as it is limitations on claims.The present invention is not only confined to above embodiment, and its concrete structure allows to change.In a word, all various variations of doing in the protection domain of independent claim of the present invention are all in protection scope of the present invention.
Claims (6)
1. a sewage sludge advanced treatment apparatus, comprise filter-pressing device (1), shredder assembly (2), drying installation (3), incinerator (16) and waste heat boiler (17), filter-pressing device (1) carries out carrying out break process by shredder assembly (2) after press filtration processing to mud, after sludge crushing, enter drying installation (3) and carry out drying treatment, dried mud granule is sent in incinerator (16) and is burned, and burns the high-temperature flue gas producing and enters waste heat boiler (17); It is characterized in that:
Described sewage sludge advanced treatment apparatus also comprises mud freezing container (4) and lyophilize energy cycle system, described lyophilize energy cycle system comprises compressor (5), vaporizer (6), condenser (7) and be arranged at the First Heat Exchanger (8) in mud freezing container (4), the outlet side of compressor (5) is connected with condenser (7), condenser (7) is connected with vaporizer (6) through throttling element (9), vaporizer (6) is connected with the inlet end of compressor (5) through First Heat Exchanger (8), described condenser (7) is connected with drying installation (3) bottom by gas pipeline (10), vaporizer (6) is connected with drying installation (3) top by gas pipeline (10), and described condenser (7) is connected by gas pipeline (10) with vaporizer (6) simultaneously,
In described waste heat boiler (17), be provided with heat-conducting oil pipes (18), heat-conducting oil pipes (8) carries out heat with air and transmits air heating, air after heating is inputted respectively drying installation (3) and mud freezing container (4), for drying sludge and thawing.
2. sewage sludge advanced treatment apparatus according to claim 1, it is characterized in that: waste heat boiler (17) is extended at the two ends of heat-conducting oil pipes (18), and be connected with the second interchanger (19), thermal oil enters the second interchanger (19) and transfers heat to air; Air after the device (7) that is condensed heating enters into the second interchanger (19) and continues to absorb heat, form high temperature air, high temperature air, after blower fan (24) pressurization, enters drying installation (3) and mud freezing container (4) by hot gas duct (20) respectively.
3. sewage sludge advanced treatment apparatus according to claim 1, it is characterized in that: described mud freezing container (4) is for multiple, First Heat Exchanger (8) is corresponding one by one with mud freezing container (4), the two ends of the First Heat Exchanger (8) in multiple mud freezing containers (4) are connected with vaporizer (6) and compressor (5) by working medium reversing valve (11) respectively, the bottom of mud freezing container (4) is provided with filtration (12), the bottom of multiple mud freezing containers (4) is passed through liquid reversing valve (13) and is communicated with filter-pressing device (1) through fluid pipeline (14), mud after thawing pumps into filter-pressing device (1) by rotor pump (15) from mud freezing container (4).
4. sewage sludge advanced treatment apparatus according to claim 1 and 2, it is characterized in that: described drying installation (3) comprises loft drier (3.1) and mud panel turnover mechanism (3.2), described mud panel turnover mechanism, level is arranged on the vertical height of difference in loft drier (3.1), described mud panel turnover mechanism (3.2) is staggered, and a mud panel turnover mechanism (3.2) of bottommost layer stretches out outside loft drier (3.1).
5. sewage sludge advanced treatment apparatus according to claim 1 and 2, it is characterized in that: described filter-pressing device (1) is plate-and-frame filter press, plate-and-frame filter press comprises multiple sheet frames (1.1), be provided with drawing-plate mechanism in sheet frame (1.1) below, described drawing-plate mechanism comprises polylith guiding piece (1.2) and slide plate (1.3), between adjacent two guiding pieces (1.2), be provided with articulated linkage (1.4), and under every guiding piece (1.2), be equipped with roller (1.5), described polylith guiding piece (1.2) is placed on slide plate (1.3), and can roll and be connected with slide plate (1.3) by roller (1.5).
6. sewage sludge advanced treatment apparatus according to claim 2, it is characterized in that: described waste heat boiler (17) is provided with smoke eliminator (21), described smoke eliminator (21) removes the sour gas in flue gas and traps the particulate matter in flue gas.
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104556619A (en) * | 2014-12-03 | 2015-04-29 | 嵊州领航信息科技有限公司 | Energy-saving environment-friendly manure drying system |
| CN105546548A (en) * | 2016-02-03 | 2016-05-04 | 湖南鹞翔环保能源科技有限公司 | Multifunctional solid waste treatment device and solid waste treatment method thereof |
| CN105565621A (en) * | 2016-01-27 | 2016-05-11 | 中国海洋石油总公司 | Oil washing method for viscous-elastic oily sludge |
| CN107120654A (en) * | 2017-05-27 | 2017-09-01 | 福建长生环保有限公司 | A kind of waste disposal method of sanitation and hygiene |
| CN107382016A (en) * | 2017-09-01 | 2017-11-24 | 浙江海河环境科技有限公司 | Low temperature closed loop sludge drying system |
| CN108443889A (en) * | 2018-02-28 | 2018-08-24 | 上海锅炉厂有限公司 | A kind of discarded metal catalyst and organic sludge coprocessing device and method |
| CN114177693A (en) * | 2021-10-20 | 2022-03-15 | 华能济宁运河发电有限公司 | Device for cleaning sludge sundries online |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102758090A (en) * | 2012-06-29 | 2012-10-31 | 中国瑞林工程技术有限公司 | Treatment method for electroplating sludge |
| CN102815848A (en) * | 2012-09-13 | 2012-12-12 | 江苏江达生态科技有限公司 | Surplus sludge high-efficiency drying technique |
| CN103030259A (en) * | 2013-01-07 | 2013-04-10 | 北京科技大学 | Method for conditioning and dehydrating residual sludge |
| CN203999290U (en) * | 2014-08-04 | 2014-12-10 | 饶宾期 | Sewage sludge advanced treatment apparatus |
-
2014
- 2014-08-04 CN CN201410381230.7A patent/CN104098241B/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102758090A (en) * | 2012-06-29 | 2012-10-31 | 中国瑞林工程技术有限公司 | Treatment method for electroplating sludge |
| CN102815848A (en) * | 2012-09-13 | 2012-12-12 | 江苏江达生态科技有限公司 | Surplus sludge high-efficiency drying technique |
| CN103030259A (en) * | 2013-01-07 | 2013-04-10 | 北京科技大学 | Method for conditioning and dehydrating residual sludge |
| CN203999290U (en) * | 2014-08-04 | 2014-12-10 | 饶宾期 | Sewage sludge advanced treatment apparatus |
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104556619A (en) * | 2014-12-03 | 2015-04-29 | 嵊州领航信息科技有限公司 | Energy-saving environment-friendly manure drying system |
| CN104556619B (en) * | 2014-12-03 | 2016-04-06 | 嵊州领航信息科技有限公司 | A kind of ight soil dehumidification system of energy-conserving and environment-protective |
| CN105565621B (en) * | 2016-01-27 | 2017-11-21 | 中国海洋石油总公司 | A kind of washing oil method of viscoplasticity oily sludge |
| CN105565621A (en) * | 2016-01-27 | 2016-05-11 | 中国海洋石油总公司 | Oil washing method for viscous-elastic oily sludge |
| CN105546548B (en) * | 2016-02-03 | 2017-08-04 | 湖南鹞翔环保能源科技有限公司 | A kind of device and its solid waste substance treating method of multi-functional processing solid waste |
| CN105546548A (en) * | 2016-02-03 | 2016-05-04 | 湖南鹞翔环保能源科技有限公司 | Multifunctional solid waste treatment device and solid waste treatment method thereof |
| CN107120654A (en) * | 2017-05-27 | 2017-09-01 | 福建长生环保有限公司 | A kind of waste disposal method of sanitation and hygiene |
| CN107120654B (en) * | 2017-05-27 | 2023-08-01 | 厦门市高科禹翔科技有限公司 | Sanitary garbage disposal method |
| CN107382016A (en) * | 2017-09-01 | 2017-11-24 | 浙江海河环境科技有限公司 | Low temperature closed loop sludge drying system |
| CN107382016B (en) * | 2017-09-01 | 2023-08-18 | 浙江海河环境科技有限公司 | Low-temperature closed-loop sludge drying system |
| CN108443889A (en) * | 2018-02-28 | 2018-08-24 | 上海锅炉厂有限公司 | A kind of discarded metal catalyst and organic sludge coprocessing device and method |
| CN108443889B (en) * | 2018-02-28 | 2023-08-08 | 上海锅炉厂有限公司 | Waste metal catalyst and organic sludge co-treatment device and method |
| CN114177693A (en) * | 2021-10-20 | 2022-03-15 | 华能济宁运河发电有限公司 | Device for cleaning sludge sundries online |
| CN114177693B (en) * | 2021-10-20 | 2023-09-26 | 华能济宁运河发电有限公司 | Device for cleaning sludge sundries on line |
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