CN202214277U - Sludge drying system - Google Patents
Sludge drying system Download PDFInfo
- Publication number
- CN202214277U CN202214277U CN2011201584219U CN201120158421U CN202214277U CN 202214277 U CN202214277 U CN 202214277U CN 2011201584219 U CN2011201584219 U CN 2011201584219U CN 201120158421 U CN201120158421 U CN 201120158421U CN 202214277 U CN202214277 U CN 202214277U
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- Prior art keywords
- sludge
- mud
- mummification
- grab bucket
- blower fan
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- 239000010802 sludge Substances 0.000 title claims abstract description 122
- 238000001035 drying Methods 0.000 title claims abstract description 67
- 239000002918 waste heat Substances 0.000 claims abstract description 26
- 239000000463 material Substances 0.000 claims abstract description 20
- 239000007789 gas Substances 0.000 claims abstract description 13
- 238000007789 sealing Methods 0.000 claims description 18
- 238000001816 cooling Methods 0.000 claims description 14
- 239000002912 waste gas Substances 0.000 claims description 13
- 238000007599 discharging Methods 0.000 claims description 11
- 238000002955 isolation Methods 0.000 claims description 9
- 238000011068 load Methods 0.000 claims description 9
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims description 8
- 235000015450 Tilia cordata Nutrition 0.000 claims description 8
- 235000011941 Tilia x europaea Nutrition 0.000 claims description 8
- 239000004571 lime Substances 0.000 claims description 8
- 230000001702 transmitter Effects 0.000 claims description 8
- 239000002351 wastewater Substances 0.000 claims description 8
- 238000009413 insulation Methods 0.000 claims description 6
- 239000002341 toxic gas Substances 0.000 claims description 6
- 206010010742 Conjunctivitis infective Diseases 0.000 claims description 5
- 206010018987 Haemorrhage Diseases 0.000 claims description 5
- 201000001028 acute contagious conjunctivitis Diseases 0.000 claims description 5
- 230000000740 bleeding Effects 0.000 claims description 5
- 231100000319 bleeding Toxicity 0.000 claims description 5
- 238000004332 deodorization Methods 0.000 claims description 2
- 230000000249 desinfective Effects 0.000 claims description 2
- 238000004659 sterilization and disinfection Methods 0.000 claims description 2
- 239000011449 brick Substances 0.000 abstract description 4
- 238000007791 dehumidification Methods 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 238000010438 heat treatment Methods 0.000 description 7
- 238000005516 engineering process Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 239000010865 sewage Substances 0.000 description 6
- 238000003756 stirring Methods 0.000 description 6
- 229910000831 Steel Inorganic materials 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 239000010959 steel Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 239000000796 flavoring agent Substances 0.000 description 3
- 235000019634 flavors Nutrition 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 230000035943 smell Effects 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000010801 sewage sludge Substances 0.000 description 2
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 description 1
- 241000893018 Armeria Species 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 210000004681 Ovum Anatomy 0.000 description 1
- 231100000614 Poison Toxicity 0.000 description 1
- 210000001138 Tears Anatomy 0.000 description 1
- CURLTUGMZLYLDI-UHFFFAOYSA-N carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 230000001877 deodorizing Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000002036 drum drying Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 238000005243 fluidization Methods 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
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- 239000003440 toxic substance Substances 0.000 description 1
- 230000032258 transport Effects 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Images
Classifications
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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
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
Abstract
The utility model discloses a sludge drying system, which comprises a sealed sludge storing cabin and a drying device. Sludge in the sealed sludge storing cabin is added into the drying device for drying the sludge in a feeding mode, wherein the sealed sludge storing cabin comprises a sludge feeding device, a grab bucket hoist, a grab bucket hoist track, a sludge pool edge, a feeding port and a control chamber. The grab bucket hoist grabs and sends the sludge in the sealed sludge storing cabin to a feeding bucket of the sludge feeding device which conveys the sludge to the drying device. The drying device comprises a roof, a wall body, a material platform and a sludge paver, after the sludge paver paves and turns the sludge, waste heat from a flue and solar energy perform temperature increasing, dehumidification and drying on the sludge, and the dried sludge is conveyed outside the drying chamber through a material conveyer. The sludge is stored in a sealed environment, so pollution gas generated by the sludge is prevented from being directly discharged into the air. The waste heat of the kiln and the solar energy are utilized to dry the sludge, and physical heat at the tail portion of burned bricks in a tunnel furnace is further fully made use of, thereby saving large amount of energy.
Description
Technical field
The utility model belongs to harmless processing of municipal sludge and utilization of resources technology, particularly a kind of sludge drying system.
Background technology
Municipal sludge is meant the solid waste that produces in city domestic sewage, the Industrial Wastewater Treatment process, is the regular product of municipal sewage plant.This sludge moisture content is high, perishable, the intensive stink is arranged, and contain toxic substances such as dioxin, bacterium, parasitic ovum and heavy metal.Therefore, need carry out harmless treatment and utilization again to mud, the mummification of mud then is the steps necessary of sludge treatment.The method of mummification at present mainly contains: traditional heat energy sludge drying and sun power sludge drying.
Tradition heat energy sludge drying is meant and utilizes mud heat drying integrated equipment that mud is realized drying and other treatment.According to the way of contact of thermal medium and mud, mummification equipment can be divided into direct mummification, indirectly drying and direct-technology types such as indirect combined formula mummification again.Wherein direct heating sludge drying factory is the most representative be Europe maximum sludge drying factory---(but evaporated water is 7 * 5000kg/h) to the B ransands of Britain; Indirect heating mummification factory is the most representative to be that (but evaporated water is 4 * 5000kg/h) in Hispanic Barcelona.American-European common drying process is main with rotary drum mummification, fluidized-bed mummification, disc type mummification generally.
(1) rotary drum drying process.With Sweet natural gas or biogas is the energy; With the air is heat-transfer medium; Wet mud and part dewatered sludge particle mix in mixing tank, bring it into rotary drum drier by air-flow, and mud advances with stable speed rotation with air-flow in rotary drum drier; Shifted to urceolus by inner core, mud is become particle by mummification gradually.This technology is divided into direct-heating type and indirect heating type.Direct-fired rotary drum dryer will rely on very complicated supervisory system to keep.The indirect heating type rotary drum drier will be operated under the inert environments of strictness because temperature inside and calorie distribution are unbalanced, be prone to cause dust in the subenvironment gather, overheated, can cause very big dangerous hidden danger.
(2) fluidized-bed drying process.Mud does not need pre-treatment, directly sends into fluidized bed dryer.Whole bottom section at fluidized bed dryer blows into fluidizing agent equably, makes its inner fluidized layer that forms.Along with mud mummification gradually, density reduces, and is raised to top, and the gas of taking away with top is again extracted fluidized-bed out.Because of its fluidization characteristic of composition decision of mud, this treatment system changes very sensitivity to the composition of mud, often causes the heat exchange in the fluidized-bed not carry out smoothly, and the wearing and tearing of fluidized-bed and pipeline are very serious, and the energy consumption of system is also higher.
(3) disc type drying process.With oil oven of external heat source heating, through oil body heat energy is passed to drying tray more earlier.Pan dryer is divided into horizontal disc moisture eliminator and vertical polydisc moisture eliminator.The horizontal disc moisture eliminator can only adopt this standard heating medium of steam.Tower crane is configured to a fixed body, forms a horizontal shell, and its inner swivel is by a hollow tubular shaft, and more fixing blank panels are full of steam etc. on the axle in the dish.Also have some agitating vanes to be used for convey materials.Thermal medium gets into disk through hub, is assigned in the rotator simultaneously.The shortcoming of this method is that the dustiness of mummification product is very big, must add independent granulating system in addition, and equipment weares and teares very easily.Vertical polydisc moisture eliminator utilizes the special evaporation curve of mud, is prepared into the hard particles of mud, makes sewage work when realizing the sewage qualified discharge, the safe non-secondary pollution of ability, and save energy.In addition, also have drying process such as disc-type, belt, daylight formula, Flash Type, but heavy construction is used seldom at present.
Domestic also have a lot of sludge drying techniques; Like utility application (200910183107.3) sludge drying system and technology, comprise mixed stirring device, moisture eliminator, multifuctional solar room, solar energy air heat collector, hot dried mud warehouse, odor removal, auxiliary thermal source; Wet mud is put into mixed stirring device and is stirred; The mud that stirs is discharged by the outlet of mixed stirring device; Through the mud travelling belt mud is dropped in the moisture eliminator by the mud of moisture eliminator inlet, the warm air that produces of solar energy air heat collector feeds moisture eliminator through the blower fan in the solar energy air heat collector by the air outlet of solar energy air heat collector wet mud is carried out the first step dehydration and drying simultaneously; Above-mentioned mud is discharged by the moisture eliminator sludge outlet, and sends into through the mud travelling belt and to carry out for second step in the multifuctional solar room and pile up mummification; Last sludge product is deposited in the hot dried mud warehouse; The waste gas that produces in the whole process all can carry out foul smell through the odor removal that links to each other with mixed stirring device, moisture eliminator, multifuctional solar room, hot dried mud warehouse to be handled.Another part utility application (201010280915.4) sludge drying treatment system, this system comprises: solar energy greenhouse, automatic mud cloth, stirring collection device and water storage device; Said solar energy greenhouse one end is provided with can be according to the diffuser of room temperature and moisture control control air input; The other end is provided with the exhaust outlet of deodorizing, air draft and water-freeing arrangement; Said automatic mud cloth, stirring collection device are positioned at solar energy greenhouse; Exhaust outlet in said water storage device and the solar energy greenhouse passes through pipe connection; Water storage device one end is connected with municipal sewage system.The described sludge drying treatment system of the utility model is carried out minimizing and harmlessness disposing under the condition of not using primary energy source when handling domestic sludge, effectively practiced thrift the energy, has reduced energy consumption, has really accomplished energy-saving and emission-reduction.
Owing to will add flocculation agent in the sludge handling process, cause above-mentioned technology in the engineering practice of sludge drying, still to have a lot of problems.As the energy consumption of drying needs is bigger, and the moisture percentage in sewage sludge of mummification is than higher, and off gas treatment is thorough inadequately, also has a large amount of toxic gases, and the mud after the mummification is also further used.
The utility model content
The purpose of the utility model is to provide a kind of waste heat of baking bricks that makes full use of, and can remove waste gas, the sludge drying system that water ratio is low.
The technical solution that realizes the utility model purpose is: a kind of sludge drying system; Comprise sealing mud warehouse, mummification equipment; Mud in the sealing mud warehouse is joined the mummification equipment that is used for dewatered sludge through feeding style; Wherein seal the mud warehouse and comprise that mud feeding device, grab bucket row hang, row hanger rail road, sludge sump stalk, opening for feed, watch-keeping cubicle are grabbed bucket in the first grab bucket row hanger rail road, second; The said first grab bucket row hanger rail road and second grab bucket row hanger rail road is parallel is located on two relative sidewalls of sludge sump stalk, the height of position is identical, and go the hanger rail road with the first grab bucket row hanger rail road and second grab bucket respectively and be slidingly connected in the two ends that the grab bucket row hangs; Opening for feed is located on the sidewall of sludge sump stalk; The outside perpendicular to the sludge sump stalk sidewall of the first grab bucket row hanger rail road and the second grab bucket row hanger rail road direction be provided with one isolate between, this sidewall also as a sidewall between said isolation, is provided with watch-keeping cubicle and mud feeding device between isolation; Wherein the mud feeding device is located at the intersection of sidewall between sludge sump stalk sidewall and isolation; The watch-keeping cubicle connects the grab bucket row through cable hangs and opening for feed, and the grab bucket row hangs the hopper that the mud of picking up in the sealing mud warehouse is delivered to the mud feeding device, and this mud feeding device is delivered to mud the mummification chamber of mummification equipment;
The described mummification equipment that is used for dewatered sludge comprises roof, body of wall, material platform and mud paver; The mummification chamber that this roof, body of wall and ground are formed; And at the indoor transmitter that is provided with of mummification, described material platform is arranged in the mummification chamber, in the set inside of material platform flue is arranged; The pipeline of this flue passes the mummification chamber; Flue communicates with the cooling zone of tunnel, above the material platform, is provided with the mud paver, and the mud feeding device is transported to mud in the mud paver aggregate bin; This mud paver paves mud, turn over and throws the back and by absorbing sun power from the waste heat of flue and roof mud is heated dehumidifying and mummification, and it is outdoor that the mud of mummification is transported to mummification through conveyer.
The utility model compared with prior art; Its remarkable advantage: (1) makes mud in closed environment through the design of sealing mud warehouse, is not directly exposed in the air; Prevent that the dusty gas that mud produces directly is discharged in the air; And prevent that the sewage that mud produces from directly infiltrating the face of land, and pollute the water and soil environment, sealed space can unify to collect body refuse.(2), not only make mud better in closed environment, and protected mud load wagon operator's safety through the design of mud load wagon unloading system in the sealing mud warehouse.(3) in mummification equipment, utilize brick furnace residual heat and solar energy drying, the physics heat of the afterbody of baking bricks in the tunnel is got back and is made full use of, and increases self heat, saves mass energy.(4) mud drying process melts down burning removing exhaust gas, clean environment firendly again.(5) handle waste gas and the waste water that dewatered sludge produces, more further make the expellant gas clean environment firendly.(6) through test, the moisture percentage in sewage sludge of mummification is low, reaches 10-25%.
Below in conjunction with accompanying drawing the utility model is described in further detail.
Description of drawings
Fig. 1 is the composition synoptic diagram of the utility model sludge drying system.
Fig. 2 is the structural representation of sealing mud warehouse: (a) being vertical view, (b) is left view.
Fig. 3 is the opening for feed synoptic diagram of sealing mud warehouse: (a) being structural representation, (b) is the work synoptic diagram.
Fig. 4 (a) is the front view that is used for the mummification equipment of dewatered sludge.
Fig. 4 (b) is the sectional view that is used for the mummification equipment of dewatered sludge.
Fig. 5 is the structural representation of dewatered sludge incinerator.
Fig. 6 is the structural representation of the emission-control equipment in the sludge drying.
Fig. 7 is a structural representation of handling the device of waste gas that dewatered sludge produces and waste water.
Fig. 8 is the structural representation that utilizes residual heat of tunnel kiln dewatered sludge device.
Embodiment
As shown in Figure 1; The utility model sludge drying system; Comprise sealing mud warehouse, mummification equipment; Mud in the sealing mud warehouse is joined the mummification equipment that is used for dewatered sludge through feeding style; Wherein seal the mud warehouse and comprise that mud feeding device 101, grab bucket row hang 102, the first grab bucket row hanger rail road 103, the second grab bucket row hanger rail road 109, sludge sump stalk 105, opening for feed 107, watch-keeping cubicle 106; The said first grab bucket row hanger rail road 103 obstructs on 105 two relative sidewalls with the second grab bucket row hanger rail road, the 109 parallel sludge sumps that are located at, and the height of position is identical, is 60% to 80% of said sidewall height like the first grab bucket row hanger rail road 103 and the second grab bucket row hanger rail road 109 apart from the height that sludge sump obstructs 105 diapires; Promptly wherein two relative sludge sumps obstruct 105 sidewalls and are respectively equipped with a brace table (as shown in Figure 2); On two brace tables, lay a grab bucket row hanger rail road respectively, the grab bucket row hangs 102 and on two grab bucket row hanger rail roads, slides, and the grab bucket row hangs 102 grab bucket and also can on the direction perpendicular to grab bucket row hanger rail road, slide simultaneously.Grab bucket row hangs 102 two ends and goes hanger rail road 109 with the first grab bucket row hanger rail road 103 and second grab bucket respectively and be slidingly connected; Opening for feed 107 is located on the sidewall of sludge sump stalk 105; The outside that the sludge sump perpendicular to the first grab bucket row hanger rail road 103 and the second grab bucket row hanger rail road, 109 directions obstructs 105 sidewalls be provided with one isolate between 110; This sidewall is also as a sidewall of 110 between said isolation; 110 are provided with watch-keeping cubicle 106 and mud feeding device 101 between isolation, wherein mud feeding device 101 be located at sludge sump obstruct 105 sidewalls and isolate between the intersection of sidewall, and the height of mud feeding device 101 obstructs the half the suitable of 105 sidewall height with sludge sump.Watch-keeping cubicle 106 through cable connect the grab bucket row hang 102 with opening for feed 107; The grab bucket row hangs 102 and picks up the hopper that the interior mud of sealing mud warehouse is delivered to mud feeding device 101; This mud feeding device 101 can be the hydraulic pressure feed system of routine; Mud is delivered to the mummification chamber 203 of mummification equipment, shown in Fig. 2 (a), Fig. 2 (b).
The described mummification equipment that is used for dewatered sludge comprises roof 2031, body of wall 2032, material platform 210 and mud paver 207; The mummification chamber 203 that this roof 2031 (being PC sunlight board material), body of wall 2032 and ground are formed; And transmitter 209 is set in mummification chamber 203, and (used transmitter all can be commercial; Like gas sensor, Temperature Humidity Sensor etc., can comprise carbon dioxide sensor, carbon monoxide transducer, methane transducer etc. like gas sensor), described material platform 210 is arranged in mummification chamber 203; Set inside at material platform 210 has flue 205; The pipeline of this flue 205 passes mummification chamber 203, and flue 205 communicates with the cooling zone of tunnel 201, above material platform 210, is provided with mud paver 207; Mud feeding device 101 is transported to mud in mud paver 207 aggregate bins; This mud paver 207 paves mud, turn over and throws the back and by absorbing sun power from the waste heat of flue 205 and roof 2031 mud is heated dehumidifying and mummification, the mud of mummification through siccative collection device 3 (like conveyer 211) be transported to mummification chamber 203 outer siccatives store in a warehouse between 2, shown in Fig. 4 (a), Fig. 4 (b).In addition, in production practice, a master control room 7 will be set also outside mummification chamber 203, power supply and some opertaing devices are in being installed on like the PLC system, so that observe and the process of control mummification.Mud after the mummification detects through commercial AQUA-BOY detector for water content rate, and its water ratio has only 10～25%.
Flue 205 can be S shape flue, waviness etc.The bottom surface of flue 205 also can be provided with thermal insulation layer.Bottom surface at flue 205 is provided with thermal insulation layer, can reduce even avoid heat to distribute to underground, makes that the heat in the flue 205 can conduct heat to the end face of material platform 210.Can utilize more heat like this, improve the efficient of sludge drying.The end face of material platform 210 can be processed by steel plate.Like this, the mud shed of mud paver 207 just drops on the steel plate.The heat-transfer effect of steel plate is good.Heat-carrying air-flow in the flue 205 of material platform 210 can better pass to mud with the heat that discharges through steel plate, helps improving the efficient of sludge drying.
The sealing mud warehouse of the utility model sludge drying system also comprises first blower fan 104 and louver(-vre) 108; Said first blower fan 104 is located at sludge sump stalk 105 and is parallel on the first grab bucket row hanger rail road 103 and the sidewall near mud feeding device 101, and the height that this first blower fan 104 obstructs 105 diapires apart from sludge sump is approximately the 80%-90% of said sidewall height.The height of this first blower fan 104 is higher than the first grab bucket row hanger rail road 103, and louver(-vre) 108 is located on another relative sidewall of sludge sump stalk 105 and first blower fan 104, and highly the height with first blower fan 104 is roughly suitable for it.First blower fan 104 also is connected watch-keeping cubicle 106 through cable with louver(-vre) 108.First blower fan 104 is used for the foul smell suction mummification chamber in the mud warehouse 203 is handled, and therefore in the mud warehouse, forms negative pressure, and louver(-vre) 108 makes outside fresh air get into the mud warehouse.The diapire of sludge sump stalk 105 is downward-sloping by opening for feed 107 beginnings.The angle that tilts is 3 ° to 15 °, and it is inner to make that like this mud of sending into can be advanced into the mud warehouse certainly.Watch-keeping cubicle 106 is provided with the PLC system; Through cable connect that the grab bucket row hangs 102, the blower fan 104 of bleeding, opening for feed 107 and louver(-vre) 108; The switching of may command opening for feed;, and open and close louver(-vre) 108 synchronously and give the ventilation of mud warehouse through opening and closing the speed of first blower fan, 104 control dusty gass to 203 dischargings of mummification chamber according to the concentration of mud warehouse internal contamination gas, also operation grab bucket row hangs 102 and grasps mud and be transported to mud feeding device 101.Double-deck transparent material is adopted in watch-keeping cubicle 106, and the height in watch-keeping cubicle 106 is not less than the height of mud feeding device 101, for observation.
Shown in Fig. 3 (a), Fig. 3 (b); The opening for feed 107 of the sealing mud warehouse of the utility model sludge drying system (also is meant between the dump among Fig. 11; In order to make the sealing of mud warehouse; With between dump 1, the opening for feed 107 that promptly seals the mud warehouse has carried out particular design) comprise first sect 801, be provided with second sect 802, discharging hopper 804 and the Hydraulic for lifting load bar 805 of blower fan 803, this second sect 802 is located at a side edge of sludge sump stalk 105; First sect 801 is located at apart from second sect 802 away from 6 to 12 meters of mud warehouse direction; One end of said discharging hopper 804 is near second sect 802, and the other end is near ground, the outside, and Hydraulic for lifting load bar 805 links to each other with the bottom of discharging hopper 804.The mud loading-unloading vehicle that loads mud is when approaching mud warehouse; Open earlier at first sect 801, this moment second sect 802 state that keeps shut, the mud loading-unloading vehicle is near discharging hopper 804; The vehicle driver handles the mud loading-unloading vehicle, and the mud of vehicle loading is discharged on the discharging hopper; After treating the whole completions of discharge of mud, the mud loading-unloading vehicle rolls 801, the first sects 801, first sect away from and closes again, and open subsequently at second sect 802; Hydraulic for lifting load bar 805 begins action, makes discharging hopper 804 be upturned near an end at first sect 801, and is downward-sloping near an end at second sect 802, makes that the mud in the discharging hopper 804 is discharged in the mud warehouse through second sect 802 of opening; After mud was unsnatched, Hydraulic for lifting load bar 805 recovered former state, and discharging hopper 804 is set level again, and second sect 802 is closed again.Also be provided with the blower fan 803 of bleeding on second sect 802, open at first sect 801, the blower fan 803 of bleeding when the mud loading-unloading vehicle drives into is started working; Foul smell is drawn into the mud warehouse; Close at first sect 801, when opened at second sect 802, the blower fan 803 of bleeding quit work.
As shown in Figure 5; On the utility model sludge drying system, also increase dewatered sludge incinerator 4; Be located at the intensification band of tunnel; Be between preheating zone and the roasting band, form negative pressuren zone in the kiln here, make the effectively mud (arrow is the direction of hot gas among Fig. 5) behind the burning and drying of heat in the kiln.This dewatered sludge incinerator 4 comprises the helical feed formula feeding machine 402 of being located at tunnel 201 tops; The feed end of this helical feed formula feeding machine 402 is provided with funnel 403; This funnel links to each other with the mummification chamber 203 of mummification equipment through conveying belt; Mud gets in the funnel 403 through conveying belt after through the mummification of mummification chamber 203, the discharge end of helical feed formula feeding machine 402 and tunnel 201 intensifications with on pinkeye 408 link to each other, the output terminal of said helical feed formula feeding machine 402 links to each other through valve 407 with the pinkeye of tunnel 201; The control pinkeye is closed; Prevent calorific loss, can effectively control dewatered sludge and get into the speed that tunnel 201 burns, reach better effect.
As shown in Figure 6; On the utility model sludge drying system, also increase the emission-control equipment 5 in a kind of sludge drying; This emission-control equipment 5 comprises inlet pipe 301, second blower fan 303, escape pipe 302, and the inlet mouth of described inlet pipe 301 is communicated with mummification chamber 203, and the air outlet of inlet pipe 301 is communicated with the inlet mouth of escape pipes 302 through second blower fan 303; The air outlet of this escape pipe 302 is communicated with the air inlet port 208 on tunnel 201 insulation belts; Transmitter 209 perception indoor exhaust airs when mummification chamber 203 still contain toxic gas, then through the pipeline flow-direction air lock of adjustment second blower fan 303, waste gas is fed air inlet port 208 in tunnel 201, carry out burning disposal.
Mud drying process carries out in mummification chamber 203.The obnoxious flavour that mud produces in drying process is released in the mummification chamber 203.Utilize second blower fan 303, the obnoxious flavour in the mummification chamber 203 is pumped in the inlet pipe 301.The obnoxious flavour escape pipe 302 of flowing through finally gets in the tunnel 201.In tunnel 201, toxic gas is by high-temp combustion, thereby eliminated toxic gas, avoids directly the toxic gas that produces in the mud drying process being discharged contaminate environment to the external world.Emission-control equipment in sludge drying can also be provided with valve 304, and valve 304 is arranged in inlet pipe 301.According to the situation of sludge drying, can utilize valve 304 to regulate the flow of effusive waste gas from mummification chamber 203 at any time.
As shown in Figure 7; On the utility model sludge drying system, also increase the another kind of waste gas of dewatered sludge generation and the device of waste water handled; The waste gas that this processing dewatered sludge produces and the device of waste water comprise transfer lime 507, the 3rd blower fan 202, treating pond 504, an end of the outlet connection transfer lime 507 of mummification chamber 203, and the other end of this transfer lime 507 connects the import of the 3rd blower fan 202; The outlet of the 3rd blower fan 202 feeds in the treating pond 504 through main ventpipe 508; On main ventpipe 508, connect a plurality of ventpipes 509, number is confirmed as required, as 4-10.On each ventpipe 509, ventilating pit 510 is set; When the transmitter 209 perception indoor gas allow compliance with emission standards of mummification chamber 203; The indoor gas of mummification chamber 203 is dispersed in the purifying waste water in the treating pond 504 (like liming, be used for absorbing waste gas) through ventilating pit 510 carries out deodorization and disinfection.In addition, an end of the outlet of mummification chamber 203 and transfer lime 507 links to each other through gate 505; Chimney 503 also is set, and this chimney 503 communicates with treating pond 504 through vapor pipe 511, and this vapor pipe is provided with lock 506.
As shown in Figure 8; Between the flue 205 of the utility model sludge drying system and the cooling zone of tunnel 201 residual heat using device 6 is set; This residual heat using device 6 comprises to be utilized waste heat inlet pipe 601, four fan device 602, utilizes waste heat escape pipe 603; Utilize the cooling zone of the inlet mouth connection tunnel 201 of waste heat inlet pipe 601; Utilize the air outlet of waste heat inlet pipe 601 to be communicated with the inlet mouth that utilizes waste heat escape pipe 603 through four fan device 602, this utilizes the air outlet of waste heat escape pipe 603 to be communicated with flue 205.Residual heat using device 6 also comprises frequency transformer 604, and described frequency transformer 604 is connected with blower fan 602.According to the situation of sludge drying, can utilize frequency transformer 604 to regulate the running speed of four fan device 602 at any time, and then regulate the waste heat amount of input mummification chamber 203.
Because being the cooling zone from tunnel 201, the adobe of processing transports, so, utilize the inlet mouth of waste heat inlet pipe 601 to be communicated with the cooling zone of tunnel 201.Owing to need utilize the waste heat of tunnel 201, so need not add the device of cooling residual heat such as blower fan at the cooling zone of tunnel 201.Like this, the cooling zone of tunnel 201 has just omitted refrigerating unit, has simplified the structure of tunnel 201.Utilize four fan device 602, the waste heat of tunnel 201 is got into from the cooling zone of tunnel 201 utilize waste heat inlet pipe 601, through utilizing waste heat escape pipe 603, finally get into mummification chamber 203 again.In mummification chamber 203, waste heat discharges its heat dewatered sludge.Adopt this device, the waste heat of tunnel 201 is delivered directly to dewatered sludge in the mummification chamber 203.This had both reached the purpose of dewatered sludge, made full use of existing thermal source again, helped economizing on resources.
Above-mentioned tunnel 201 is common practise of those skilled in the art, begins from opening for feed, gets into heat up band, roasting band, insulation belt, cooling zone successively, arrives discharge port at last and finishes.Waste gas is sent into burning from the insulation belt of tunnel 201.
Claims (9)
1. sludge drying system; It is characterized in that comprising sealing mud warehouse, mummification equipment; Mud in the sealing mud warehouse is joined the mummification equipment that is used for dewatered sludge through feeding style; Wherein seal the mud warehouse and comprise that mud feeding device (101), grab bucket row hang (102), the first grab bucket row hanger rail road (103), the second grab bucket row hanger rail road (109), sludge sump stalk (105), opening for feed (107), watch-keeping cubicle (106); The said first grab bucket row hanger rail road (103) is parallel with the second grab bucket row hanger rail road (109) to be located on (105) two relative sidewalls of sludge sump stalk; The height of position is identical; The two ends that grab bucket row hangs (102) are slidingly connected with the first grab bucket row hanger rail road (103) and the second grab bucket row hanger rail road (109) respectively, and opening for feed (107) is located on the sidewall of sludge sump stalk (105), are being provided with between an isolation (110) perpendicular to the outside of the first grab bucket row hanger rail road (103) with sludge sump stalk (105) sidewall of second grab bucket row hanger rail road (109) direction; This sidewall is also as the sidewall of (110) between said isolation; (110) are provided with watch-keeping cubicle (106) and mud feeding device (101) between isolation, and wherein mud feeding device (101) is located at the intersection of sidewall between sludge sump stalk (105) sidewall and isolation, and watch-keeping cubicle (106) connect the grab bucket row through cable and hang (102) and opening for feed (107); The grab bucket row hangs (102) and picks up the hopper that the interior mud of sealing mud warehouse is delivered to mud feeding device (101), and this mud feeding device (101) is delivered to mud the mummification chamber (203) of mummification equipment;
The described mummification equipment that is used for dewatered sludge comprises roof (2031), body of wall (2032), material platform (210) and mud paver (207); The mummification chamber (203) that this roof (2031), body of wall (2032) and ground are formed; And transmitter (209) is set in mummification chamber (203); Described material platform (210) is arranged in mummification chamber (203); Set inside at material platform (210) has flue (205), and the pipeline of this flue (205) passes mummification chamber (203), and flue (205) communicates with the cooling zone of tunnel (201); Be provided with mud paver (207) in the top of material platform (210); Mud feeding device (101) is transported to mud in mud paver (207) aggregate bin, and this mud paver (207) paves mud, turn over and throws the back and absorb sun power by the waste heat from flue (205) with roof (2031) mud is heated dehumidifying and mummification, the mud of mummification through siccative collection device (3) be transported to siccative outside the mummification chamber (203) store in a warehouse between (2).
2. sludge drying system according to claim 1; It is characterized in that said sealing mud warehouse also comprises first blower fan (104) and louver(-vre) (108); Said first blower fan (104) is located at sludge sump stalk (105) and is parallel on the first grab bucket row hanger rail road (103) and the sidewall near mud feeding device (101); The height of this first blower fan (104) is higher than the first grab bucket row hanger rail road (103); Louver(-vre) (108) is located on sludge sump stalk (105) another sidewall relative with first blower fan (104), and first blower fan (104) also is connected watch-keeping cubicle (106) through cable with louver(-vre) (108).
3. sludge drying system according to claim 1; The opening for feed (107) that it is characterized in that said sealing mud warehouse comprises first sect (801), is provided with second sect (802) of the blower fan of bleeding (803), discharging hopper (804) and Hydraulic for lifting load bar (805); This second sect (802) is located at a side edge of sludge sump stalk (105); First sect (801) is located at apart from second sect (802) 6 to 12 meters away from mud warehouse direction; One end of said discharging hopper (804) is near second sect (802), and the other end is near ground, the outside, and Hydraulic for lifting load bar (805) links to each other with the bottom of discharging hopper (804).
4. sludge drying system according to claim 1; It is characterized in that on sludge drying system, also increasing dewatered sludge incinerator (4); This dewatered sludge incinerator (4) comprises the helical feed formula feeding machine (402) of being located at tunnel (201) top; The feed end of this helical feed formula feeding machine (402) is provided with funnel (403); This funnel links to each other with the mummification chamber (203) of mummification equipment through conveying belt, the discharge end of helical feed formula feeding machine (402) and tunnel (201) intensification with on pinkeye (408) link to each other, the pinkeye of the output terminal of said helical feed formula feeding machine (402) and tunnel (201) links to each other through valve (407).
5. sludge drying system according to claim 1; It is characterized in that on sludge drying system, also increasing the emission-control equipment (5) in the sludge drying; This emission-control equipment (5) comprises inlet pipe (301), second blower fan (303), escape pipe (302); The inlet mouth of described inlet pipe (301) is communicated with mummification chamber (203); The air outlet of inlet pipe (301) is through the inlet mouth of second blower fan (303) connection escape pipe (302), and the air outlet of this escape pipe (302) is communicated with the air inlet port (208) on tunnel (201) insulation belt, and transmitter (209) the perception indoor exhaust air when mummification chamber (203) still contains toxic gas; Then, waste gas is fed air inlet port (208) in tunnel (201), carry out burning disposal through the pipeline flow-direction air lock of adjustment second blower fan (303).
6. sludge drying system according to claim 1; It is characterized in that on sludge drying system, also increasing the waste gas of processing dewatered sludge generation and the device of waste water; The waste gas that this processing dewatered sludge produces and the device of waste water comprise transfer lime (507), the 3rd blower fan (202), treating pond (504); The outlet of mummification chamber (203) connects an end of transfer lime (507); The other end of this transfer lime (507) connects the import of the 3rd blower fan (202); The outlet of the 3rd blower fan (202) feeds in the treating pond (504) through main ventpipe (508), goes up at main ventpipe (508) to connect a plurality of ventpipes (509), on a ventpipe (509), ventilating pit (510) is set; When transmitter (209) the perception indoor gas allow compliance with emission standards of mummification chamber (203), the indoor gas of mummification chamber (203) is dispersed in the purifying waste water in the treating pond (504) through ventilating pit (510) carries out deodorization and disinfection.
7. sludge drying system according to claim 6 is characterized in that the outlet of mummification chamber (203) and an end of transfer lime (507) link to each other through gate (505); Chimney (503) also is set, and this chimney (503) communicates with treating pond (504) through vapor pipe (511), and this vapor pipe is provided with lock (506).
8. sludge drying system according to claim 1; It is characterized in that between the cooling zone of flue (205) and tunnel (201) residual heat using device (6) being set; This residual heat using device (6) comprises to be utilized waste heat inlet pipe (601), four fan device (602), utilizes waste heat escape pipe (603); Utilize the cooling zone of the inlet mouth connection tunnel (201) of waste heat inlet pipe (601); Utilize the air outlet of waste heat inlet pipe (601) to be communicated with the inlet mouth that utilizes waste heat escape pipe (603) through four fan device (602), this utilizes the air outlet of waste heat escape pipe (603) to be communicated with flue (205).
9. sludge drying system according to claim 8 is characterized in that described residual heat using device (6) also comprises frequency transformer (604), and described frequency transformer (604) is connected with four fan device (602).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201584219U CN202214277U (en) | 2011-05-16 | 2011-05-16 | Sludge drying system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201584219U CN202214277U (en) | 2011-05-16 | 2011-05-16 | Sludge drying system |
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| Publication Number | Publication Date |
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| CN202214277U true CN202214277U (en) | 2012-05-09 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011201584219U Expired - Lifetime CN202214277U (en) | 2011-05-16 | 2011-05-16 | Sludge drying system |
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| CN (1) | CN202214277U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102531317A (en) * | 2011-05-16 | 2012-07-04 | 南京鑫翔新型建筑材料有限责任公司 | Sludge drying system |
| CN103508647A (en) * | 2012-06-28 | 2014-01-15 | 中国科学院理化技术研究所 | Solar sludge drying system/device |
| CN105645730A (en) * | 2016-01-14 | 2016-06-08 | 上海交通大学 | Energy-saving quick dewatering method of argillaceous biomass refuse |
| CN109231759A (en) * | 2018-11-28 | 2019-01-18 | 南通曙光机电工程有限公司 | A kind of sludge drying processing method and processing unit |
-
2011
- 2011-05-16 CN CN2011201584219U patent/CN202214277U/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102531317A (en) * | 2011-05-16 | 2012-07-04 | 南京鑫翔新型建筑材料有限责任公司 | Sludge drying system |
| CN102531317B (en) * | 2011-05-16 | 2013-06-19 | 南京鑫翔新型建筑材料有限责任公司 | Sludge drying system |
| CN103508647A (en) * | 2012-06-28 | 2014-01-15 | 中国科学院理化技术研究所 | Solar sludge drying system/device |
| CN105645730A (en) * | 2016-01-14 | 2016-06-08 | 上海交通大学 | Energy-saving quick dewatering method of argillaceous biomass refuse |
| CN105645730B (en) * | 2016-01-14 | 2018-10-19 | 上海交通大学 | A kind of the energy saving of shale biomass garbage quickly goes water method |
| CN109231759A (en) * | 2018-11-28 | 2019-01-18 | 南通曙光机电工程有限公司 | A kind of sludge drying processing method and processing unit |
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