CN203904180U - Sludge drying system - Google Patents
Sludge drying system Download PDFInfo
- Publication number
- CN203904180U CN203904180U CN201420276065.4U CN201420276065U CN203904180U CN 203904180 U CN203904180 U CN 203904180U CN 201420276065 U CN201420276065 U CN 201420276065U CN 203904180 U CN203904180 U CN 203904180U
- Authority
- CN
- China
- Prior art keywords
- oil
- sludge
- screw
- outlet
- blade
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 239000010802 sludge Substances 0.000 title claims abstract description 63
- 238000001035 drying Methods 0.000 title claims abstract description 62
- 239000002912 waste gas Substances 0.000 claims abstract description 12
- 238000004332 deodorization Methods 0.000 claims abstract description 5
- 238000010438 heat treatment Methods 0.000 claims description 17
- 230000001877 deodorizing effect Effects 0.000 claims description 15
- 238000009434 installation Methods 0.000 claims description 14
- 230000005540 biological transmission Effects 0.000 claims description 13
- 238000009413 insulation Methods 0.000 claims description 13
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 10
- 210000005056 cell body Anatomy 0.000 claims description 10
- 230000001105 regulatory effect Effects 0.000 claims description 7
- 229910052742 iron Inorganic materials 0.000 claims description 5
- 239000000567 combustion gas Substances 0.000 claims description 3
- 238000007599 discharging Methods 0.000 abstract description 3
- 125000004122 cyclic group Chemical group 0.000 abstract 1
- 238000000034 method Methods 0.000 description 11
- 230000000694 effects Effects 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 238000010586 diagram Methods 0.000 description 5
- 239000010865 sewage Substances 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- 230000009286 beneficial effect Effects 0.000 description 4
- 238000004064 recycling Methods 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- 230000018044 dehydration Effects 0.000 description 3
- 238000006297 dehydration reaction Methods 0.000 description 3
- 238000013461 design Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 230000001737 promoting effect Effects 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 239000010801 sewage sludge Substances 0.000 description 2
- 238000013022 venting Methods 0.000 description 2
- TVEXGJYMHHTVKP-UHFFFAOYSA-N 6-oxabicyclo[3.2.1]oct-3-en-7-one Chemical compound C1C2C(=O)OC1C=CC2 TVEXGJYMHHTVKP-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 239000010425 asbestos Substances 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 239000013043 chemical agent Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 229910052895 riebeckite Inorganic materials 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
The utility model discloses a sludge drying system, which includes a filter press, a sludge storage bucket, a sludge dryer, a steam condenser, a deodorization tower and a thermal oil furnace, wherein the sludge dryer includes at least two layers of drying boxes stacked from top to bottom, and drying devices positioned inside the drying boxes respectively; each drying box is provided with a feeding end, a discharging end and an exhaust end; each drying device is provided with an oil inlet used for introducing hot oil into the drying device and an oil outlet used for outputting hot oil; all the drying boxes are connected at the feeding ends and the discharging ends, and are communicated and connected in series through taking the joints as serially connected points; each exhaust end connected in series is connected with the air inlet of the steam condenser; the air outlet of the steam condenser is connected with the air inlet of the deodorization tower; the oil inlets are converged and connected to the oil outlet end of the thermal oil furnace, and all the oil outlets are converged and connected to the oil inlet end of the thermal oil furnace. The sludge drying system utilizes hot oil in a cyclic manner, and recycles hot waste gas discharged, improves the thermal energy use ratio and sludge drying efficiency.
Description
Technical field
The utility model relates to dry technology, is specifically related to a kind of sludge drying system.
Background technology
At present, the municipal sludge that industrial wastewater discharge brings becomes a severe environmental problem gradually, and still, the processing speed of domestic sewage work is unable to catch up with the output of sewage far away, causes environmental pollution.
Existing sewage water treatment method is that the mud in sewage is carried out to mummification, generally comprises the mode of direct heat mummification and indirect thermal mummification.Wherein:
Direct heat mummification is the application of thermal convection drying technique.After thermal medium heating, enter in desiccation machine and directly contact mixing with mud, mud heats up, moisture evaporation.In this process, thermal medium directly contacts with mud and is polluted, and the exhaust steam of discharge and waste water need discharge after harmless treatment.There is following problem in this mummification mode: (1) heat energy cannot be recycled, and thermal waste is serious; (2) exhaust emissions amount is large, increases secondary pollution.
Also generally there is following problem in other indirect thermal mummification modes: (1) existing indirectly drying equipment adopts single passage design, and bulky, floor space is large; (2) wet mud minimizing degree in drying process is larger, and the situation that sludge volume sharply reduces often appears in single-channel drying machine rear, and rear warm air ratio increases.Because being required to be micro-subnormal ambient in cylinder, the water vapor in cylinder is extracted out and processed, the unnecessary warm air that rear is taken away has caused the waste of heat energy, and heat utilization rate is low; (3) mud is in drying process, and single passage design makes the interior each several part water vapor concentration variation of cylinder in mummification process not cause the mummification efficiency of mud not high very much; (4) adopt single oil circuit (thermal barrier thermal oil) design, in drying process, oil temperature can not be adjusted, and affects the optimum utilization effect of heat energy; (5) most of moisture eliminator cannot carry out recycle by thermal medium.
Utility model content
In order to overcome the deficiencies in the prior art, the purpose of this utility model is to provide a kind of sludge drying system, and energy recycle deep fat, can also recycle the hot waste gas of discharge, promotes heat utilization rate and sludge drying efficiency.
The purpose of this utility model adopts following technical scheme to realize:
A kind of sludge drying system, comprise the pressure filter for sludge dewatering, for the storage bucket of mud storage, for heating the sludge drier of dewatered sludge, be used for the steam condenser of the heat energy that reclaims waste gas, for the deodorizing tower to exhaust air deodorization with for heating the heat-conducting oil furnace of deep fat, the outlet of described pressure filter is connected with the entrance of storage bucket, the storage outlet of bucket and the feeding end of sludge drier are connected, described sludge drier comprises at least two-layer stacked loft drier from top to bottom and lays respectively at the drying installation in loft drier, each loft drier all has the described feeding end for passing into mud, for exporting the discharge end of mud, for the exhaust side of combustion gas, each drying installation has past drying installation and passes into the oil-in of deep fat and the oil outlet of output deep fat, each loft drier is connected with discharge end with feeding end, and some serial connection is communicated with using this tie point as serial connection, after each exhaust side series connection, be connected with the inlet mouth of steam condenser, the air outlet of steam condenser is connected with the inlet mouth of deodorizing tower, and each oil-in confluxes and is connected to the oil outlet end of heat-conducting oil furnace, and each oil outlet confluxes and is connected to the oil inlet end of heat-conducting oil furnace.
Preferably, described drying installation is spiral propeller, loft drier is wrapped with the groove cylinder for being incubated, described feeding end and discharge end run through the correspondence position of loft drier and groove cylinder, described spiral propeller comprises the rotating driving device of adjustable rotating speed and is driven at least one screw rod of rotation by rotating driving device, in the body of rod of each screw rod, be provided with pipeline road, this pipeline road has described oil-in and described oil outlet, each oil-in confluxes and is connected to the oil outlet end of heat-conducting oil furnace respectively after a regulated valve separately, oil-in and oil outlet are positioned at same one end of the body of rod, antetheca, rear wall and the diapire of described groove cylinder are hollow structure, form oil pocket, and the antetheca of groove cylinder and rear wall have oiler and oil discharge outlet, and oiler one side is communicated with oil discharge outlet through oil pocket, and oiler opposite side is communicated with oil outlet through a conduit.
Preferably, the body of rod outer side of described screw rod is provided with screw-blade, in screw-blade, hollow forms spiral oil duct, and described oil-in connects oil duct through one first and is communicated with one end of spiral oil duct, and the other end of spiral oil duct connects oil duct through one second and is communicated with oil outlet; Described the first connection oil duct, spiral oil duct are connected oil duct with second and form described pipeline road.
Preferably, described oil-in is multiple, and bobbin is symmetrical centered by the rotary middle spindle of screw rod; First to connect oil duct be corresponding with oil-in quantity multiple, and extend internally along the length direction of screw rod.
Preferably, in the body of rod of described screw rod, be made as hollow heat insulation chamber, described second connect oil duct by one end of the body of rod of screw rod to unsettled stretching out in hollow heat insulation chamber, this second external part that connects oil duct is communicated with oil outlet.
Preferably, described spiral propeller also comprises transmission rig, and described rotating driving device is in transmission connection through transmission rig and screw rod.
Preferably, the body of rod of each described screw rod comprises active rotation bar and driven dwang, described screw-blade comprises the active screw-blade of being located at active rotation bar outer side and the driven screw-blade of being located at driven dwang outer side, initiatively the rotation direction of screw-blade is contrary with the rotation direction of driven screw-blade, and initiatively screw-blade engages with driven screw-blade; Described transmission rig comprises driving toothed gear, follower gear, the rotation output terminal of rotating driving device is fixedly inserted to the center of driving toothed gear, follower gear engages with driving toothed gear, active rotation bar is all connected with loft drier along the length direction of loft drier rotationally with driven dwang, active rotation bar is fixed in the center of driving toothed gear, and driven dwang is fixed in the center of follower gear.
Preferably, the two ends of described active rotation bar and driven dwang are stretched out by the two ends of groove cylinder respectively, and the two ends of described groove cylinder have the perforate that supplies active rotation bar and driven dwang to pass.
Preferably, the two ends of described groove cylinder are respectively equipped with right baffle-plate and right baffle plate, and described perforate lays respectively in right baffle-plate and right baffle plate; Described groove cylinder is enclosed with for heat insulation iron sheet cover.
Preferably, described loft drier comprises cell body and is sealed on the upper cover plate on the notch of cell body, and described feeding end is by protruding upward in upper cover plate, and runs through groove cylinder; Described discharge end is stretched out downwards by the bottom land of cell body, and runs through groove cylinder; Described exhaust side is by stretching out on upper cover plate.
Compared to existing technology, the beneficial effects of the utility model are:
(1) the dehydration pre-treatment that pressure filter of the present utility model provides for mud, also outwards be delivered to sludge drier in the storage through storage bucket dry, the hot waste gas of discharging through venting hole after this sludge drier heat drying will pass into steam condenser, in this steam condenser, heat cold water and form hot water for recycling, waste gas finally enters deodorizing tower deodorizing to rear discharge up to standard simultaneously, pollution-free, this process implementation the recycling of heat energy, be beneficial to environmental protection, and, pass into deep fat in drying installation through heat-conducting oil furnace circulating-heating, realize recycling of thermal medium, prevent thermal waste.
(2) loft drier of the present utility model is long strip shape, and stacked from top to bottom, has greatly reduced volume, and floor space is little;
(3) the utility model, by the adjustable temperature passing in drying installation of heat-conducting oil furnace, is convenient to flexible mummification speed;
(4) the utility model adopts the screw rod with pipeline road, when making screw rod to sludge agitation, can contact mud by the high-temperature hot oil of the pipeline road of flowing through, the heat of deep fat is transferred to mud, provide sludge drying required main heat, meanwhile, the rotation process of screw rod increases screw rod and mud contact area greatly, the mummification speed of mud that added piece, improve mummification efficiency, be applicable to a large amount of continuous sludge treatment; Meanwhile, flow out the deep fat of screw rod also can be in the oil pocket of groove cylinder to loft drier insulation, the deep fat that prevents from passing into screw rod is too fast toward extraneous heat radiation, and has promoted heat utilization rate;
(5) screw rod of the present utility model is two, and active rotation and the incorgruous rotation of driven dwang can realize the effect that stirs mud, mud are heated more even, further improve mummification efficiency;
(6) the first connection oil duct of the present utility model, spiral oil duct, second connect the setting of oil duct, can make deep fat flow at the body of rod internal recycle of screw rod, realize the repeatedly utilization of the remaining temperature of deep fat, again further improve the mummification efficiency of mud;
(7) of the present utility modelly pass into mud by feeding end, utilize deep fat as heat-conducting medium, mud is provided after heat, deep fat self can facilitate recycle, and the waste gas of sludge creation will be discharged by exhaust side, and the mud after mummification is discharged by discharge end.
(8), in the stepped construction of the utility model sludge drier, by the speed adjustment to each rotating driving device, regulate the rotating speed of the screw rod of each layer, and then control the mud handling capacity of each layer; And, by regulating each regulated valve to enter the deep fat flow of each layer of pipeline road by adjusting, and then control the heat supplied of each layer; Through adjusting this mud handling capacity and deep fat flow, drying time section that can be different according to mud, manufactures pointed mummification condition, reaches optimum mummification and energy-saving effect.
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail.
Brief description of the drawings
Fig. 1 is the utility model sludge drying system connection diagram;
Fig. 2 is the mummification of the propelling layer by layer schematic diagram of the utility model sludge dry system;
Fig. 3 is one of loft drier internal structure schematic diagram of the utility model sludge drying system;
Fig. 4 be the utility model sludge drying system loft drier internal structure schematic diagram two;
Fig. 5 is the structural representation of the upper cover plate of the utility model sludge drying system;
Fig. 6 is the STRUCTURE DECOMPOSITION figure of the groove cylinder of the utility model sludge drying system;
Fig. 7 is the sectional view of the utility model groove cylinder;
Fig. 8 is one of structural representation of the utility model pipeline road;
Fig. 9 be the utility model pipeline road structural representation two;
Figure 10 is the schematic diagram of the end of the utility model active rotation bar.
In figure: 100, pressure filter; 200, storage bucket; 300, sludge drier; 400, steam condenser; 500, deodorizing tower; 600, heat-conducting oil furnace; 1, variable-frequency motor; 2, transmission rig; 3, spiral propeller; 4, loft drier; 41, cell body; 42, upper cover plate; 5, oil discharge outlet; 6, right baffle-plate; 7, oiler; 8, right baffle plate; 9, iron sheet cover; 10, groove cylinder; 11, oil pocket; 12, driving toothed gear; 13, follower gear; 14, driven screw-blade; 15, active screw-blade; 16, first connects oil duct; 17, second connects oil duct; 18, oil-in; 19, spiral oil duct; 20, oil outlet; 21, hollow heat insulation chamber; 22, feeding end; 23, exhaust side; 24, discharge end; 25, pipeline road; 26, active rotation bar; 27, driven dwang; 28, perforate.
Embodiment
A kind of sludge drying system as shown in Figure 1 and 2, comprise the pressure filter 100 for sludge dewatering, for the storage bucket 200 of mud storage, for heating the sludge drier 300 of dewatered sludge, be used for the steam condenser 400 of the heat energy that reclaims waste gas, for the deodorizing tower 500 to exhaust air deodorization with for heating the heat-conducting oil furnace 600 of deep fat, the outlet of pressure filter 100 is connected with the entrance of storage bucket 200, the outlet of storage bucket 200 is connected with the feeding end of sludge drier 300, sludge drier 300 comprises at least two-layer stacked loft drier 4 from top to bottom and lays respectively at the drying installation in loft drier 4, each loft drier 4 all has the feeding end 22 for passing into mud, for exporting the discharge end 24 of mud, for the exhaust side 23 of combustion gas, each drying installation has toward self passing into the oil-in 18 of deep fat and the oil outlet 20 of output deep fat, each loft drier 4 is connected with discharge end 24 with feeding end 22, and some serial connection is communicated with using this tie point as serial connection, after each exhaust side 22 series connection, be connected with the inlet mouth of steam condenser 400, the air outlet of steam condenser 400 is connected with the inlet mouth of deodorizing tower 500, each oil-in 18 confluxes and is connected to the oil outlet end of heat-conducting oil furnace 600, and each oil outlet 20 confluxes and is connected to the oil inlet end of heat-conducting oil furnace 600.
The mud that is accompanied with sewage first dewaters by pressure filter 100, and this example adopts conventional sludge plate-frame filter press, with the mechanical dehydration pattern of centrifuge dehydration, filter press, belt type dewaterer, moisture percentage in sewage sludge is down to " 80%～60% ".In storage bucket 200, be provided with the e Foerderanlage for delivery of mud, mud inputted from pressure filter 100 to storage, and exported the mud of storage to sludge drier 300.In the drying installation of mud in each loft drier 4, advanced layer by layer dry.The thermal medium using in drying process---deep fat, will be with the persistently overheating heating of heat-conducting oil furnace 600, and regulate and control the temperature of deep fat by heat-conducting oil furnace 600, and then speed and the mummification effect of regulation and control sludge drying, mud is after mummification, water ratio obviously reduces, and moisture percentage in sewage sludge can be down to below 30%, and the dewatered sludge that the discharge end 24 of orlop loft drier 4 is exported can be transported through tipper.The hot waste gas producing in drying process is discharged via venting port 23, and the cold water that passes into of this hot waste gas in can heating steam condenser 400, becomes hot water for recycling cool water heating, and spent air temperture can be down to 40 DEG C of left and right.Reclaim waste gas after heat energy by steam condenser 400 and enter emission compliance tail gas after deodorizing tower 500 deodorizing, deodorizing tower 500 can select to comprise activated carbon adsorber, the equipment such as biological deodorizing filtration, chemical agent deodorizing, ionization deodorizing.
For promoting the mummification effect of mud and promoting sludge drying speed, as shown in Fig. 3 ~ 6, this routine drying installation is spiral propeller 3, and loft drier 4 is wrapped with the groove cylinder 10 for being incubated, and feeding end 22 and discharge end 24 run through loft drier 4 and groove cylinder 10.Spiral propeller 3 comprises the rotating driving device of adjustable rotating speed and is driven at least one screw rod of rotation by rotating driving device, this routine rotating driving device comprises variable-frequency motor 1, its rotating speed is adjustable, also can increase the reduction box being used in conjunction with this variable-frequency motor 1, also can adopt the rotary power units such as rotating liquid cylinder pressure; Screw rod is only one in this example, also can be set to more than one any amount according to mummification demand.As shown in Fig. 8 ~ 9, in the body of rod of each screw rod, be provided with pipeline road 25, this pipeline road 25 has oil outlet 20 and for passing into the oil-in 18 of deep fat, each oil-in 18 confluxes and is connected to the oil outlet end of heat-conducting oil furnace 600 respectively after a regulated valve (not shown) separately, makes the deep fat fuel delivery of each layer of pipeline road 25 independent adjustable.Oil-in 18 and oil outlet 20 are positioned at same one end of the body of rod, can coordinate dynamic-sealing rotary joint to realize same one end with heat-conducting oil furnace 600 and pass in and out oily being connected; As shown in Figure 7, antetheca, rear wall and the diapire of groove cylinder 10 are hollow structure, form oil pocket 11, the antetheca of groove cylinder 10 and rear wall have oiler 7 and oil discharge outlet 5, oiler 7 one sides are communicated with oil discharge outlet 5 through oil pocket 11, and oiler 7 opposite sides are communicated with oil outlet 20 through a conduit (not shown).
By the speed adjustment to each rotating driving device, regulate the rotating speed of the screw rod of each layer, and then control the mud handling capacity of each layer; And, by regulating each regulated valve to enter the deep fat flow of each layer of pipeline road 25 by adjusting, and then control the heat supplied of each layer; Through adjusting this mud handling capacity and deep fat flow, drying time section that can be different according to mud, manufactures pointed mummification condition, reaches optimum mummification and energy-saving effect.
Mud enters loft drier 4 through feeding end 22, under the rotation of screw rod by fully, uniform stirring, simultaneously, deep fat enters the pipeline road 25 of screw rod through oil-in 18, through screw rod heating mud, make mud in whipping process, obtain being subject to heat drying, deep fat enters oil pocket 11 through oiler 7 after oil outlet 20, heating tank cylinder 10 comes the heat-preservation sludge in loft drier 4, the remaining temperature of performance deep fat, and deep fat is exported finally by oil discharge outlet 5.Due to the continuous rotation of screw rod, make mud enter loft drier 4 from feeding end 22 incessantly, the mud after mummification is discharged from discharge end 24, realizes continuous, the efficient mummification of mud.Deep fat can return again and enter oil-in 18 recycles after heat-conducting oil furnace 600 heats up.This example is furnished with conventional dynamic sealing swivel coupling at catheter interface place, so that deep fat still input and output hermetically smoothly in the rotation process of screw rod.
As shown in Figure 6, be the heat insulation effect of upgrading slot cylinder 10, can, in groove cylinder 10 external parcel for heat insulation iron sheet cover 9, further can in overlapping 9, iron sheet add resistant to elevated temperatures asbestos.
For strengthening the heat conduction efficiency of deep fat to mud, the body of rod outer side of screw rod is provided with screw-blade, as shown in Fig. 8 ~ 9, in screw-blade, hollow forms spiral oil duct 19, oil-in 18 connects oil duct 16 through one first and is communicated with one end of spiral oil duct 19, and the other end of spiral oil duct 19 connects oil duct 17 through one second and is communicated with oil outlet 20; The first connection oil duct 16, spiral oil duct 19 are connected oil duct 17 and form above-mentioned pipeline road 25 with second.Be connected under the effect of oil duct 17 with second at the first connection oil duct 16, pipeline road 25 obtains bending roundabout, and under the effect of spiral oil duct 19, pipeline road 25 obtains spiral and goes for a stroll, make screw rod obtain fully, be heated uniformly, and then strengthened the heating surface area of mud.
As shown in figure 10, this example is made as oil-in 18 multiple, and bobbin is symmetrical centered by the rotary middle spindle of screw rod; First to connect oil duct 16 be corresponding with oil-in 18 quantity multiple, and extend internally along the length direction of screw rod.
As shown in Figure 9, for preventing that deep fat from having reduced the temperature of screw-blade at spiral oil duct 19 with interacting during second is connected oil duct 17, in the body of rod of screw rod, be made as hollow heat insulation chamber 21, second connect oil duct 17 by one end of the body of rod of screw rod to hollow heat insulation chamber 21 interior unsettled stretching out, this second external part that connects oil duct 17 is communicated with oil outlet 20.In the second connection oil duct 17, deep fat that reflux, lesser temps is isolated by hollow heat insulation chamber 21, ensures that screw-blade obtains the temperature that deep fat is higher.
As shown in Fig. 3 ~ 4, this routine spiral propeller 3 also comprises transmission rig 2, and rotating driving device is in transmission connection through transmission rig 2 and screw rod.The body of rod of each screw rod comprises active rotation bar 26 and driven dwang 27, screw-blade comprises the driven screw-blade 14 of being located at the active screw-blade 15 of active rotation bar 26 outer sides and being located at driven dwang 27 outer sides, initiatively the rotation direction of screw-blade 15 is contrary with the rotation direction of driven screw-blade 14, and initiatively screw-blade 15 engages with driven screw-blade 14; Transmission rig 2 comprises driving toothed gear 12, follower gear 13, the rotation output terminal of rotating driving device is fixedly inserted to driving toothed gear 12 center, follower gear 13 engages with driving toothed gear 12, active rotation bar 26 is all connected with loft drier 4 along the length direction of loft drier 4 rotationally with driven dwang 27, active rotation bar 26 is fixed in driving toothed gear 12 center, and driven dwang 27 is fixed in follower gear 13 center.This routine rotating driving device is variable-frequency motor 1, and rotation output terminal is the output shaft of this variable-frequency motor 1.
Variable-frequency motor 1 drives driving toothed gear 12 to rotate, drive follower gear 13 to rotate, and then make active rotation bar 26 and the incorgruous rotation of driven dwang 27, initiatively screw-blade 15 and also incorgruous rotation of driven screw-blade 14, further be beneficial to uniform stirring mud, promote stirring efficiency.Due to active rotation bar 26, driven dwang 27, initiatively screw-blade 15, driven screw-blade 14 is interior all has deep fat to pass through, therefore mud has obtained more heating surface area, further promotes mummification efficiency.Driving toothed gear 12 and follower gear 13 also can be made as elliptic gear, and active rotation bar 26 and the driven dwang 27 transmitting ratio moment in rotation process is changed, and are beneficial to initiatively screw-blade 15 extruding relative to driven screw-blade 14 and pulverize mud.
The two ends of active rotation bar 26 and driven dwang 27 are stretched out by the two ends of groove cylinder 10 respectively, and the two ends of groove cylinder 10 have the perforate 28 that supplies active rotation bar 26 and driven dwang 27 to pass.The two ends of groove cylinder 10 are respectively equipped with right baffle-plate 6 and right baffle plate 8, and perforate 28 lays respectively in right baffle-plate 6 and right baffle plate 8.
This routine loft drier 4 comprises cell body 41 and is sealed on the upper cover plate 42 on the notch of cell body 41, and feeding end 22 is by protruding upward in upper cover plate 42, and runs through groove cylinder 10; Discharge end 24 is stretched out downwards by the bottom land of cell body 41, and runs through groove cylinder 10; As shown in Figure 5, exhaust side 23 is by stretching out on upper cover plate 42.
When work, as shown in Figure 2, the drying process of propelling layer by layer of sludge drier 300 is as follows: mud is advanced into the discharge end 24 of right-hand member in the loft drier 4 of top layer by spiral propeller 3 by the feeding end 22 in left side, after dry, sludge volume reduces, but degree is not obvious, loft drier 4 internal volumes still major part take mud, and the heat of being taken away by pump drainage effect is few.In the time that mud enters lower one deck loft drier 4, can reduce variable-frequency motor 1 rotating speed (rotating speed compared with top layer) of the spiral propeller in this layer of loft drier 4, make this place's mud present " accumulation " phenomenon, the in the situation that of low-rotate speed, this layer of loft drier 4 internal volume still can major part take mud, thereby the relative volume of minimizing air reduces the heat of taking away because of pump drainage.Follow-up each layer of running condition by that analogy, system can remain that the each layer of most of volume of loft drier 4 all has mud to occupy, and reduces the calorific loss of taking away because of steam condenser 400 pump drainage hot waste gass, ensures that the temperature in loft drier 4 reaches the requirement of dewatered sludge.As shown in Figure 1 and 2, loft drier 4 is made as four layers by this example, also can be made as two-layer above any amount according to the condition of the humidity of mud, hot oil temperature.
In each spiral propeller 3, mud enters in loft drier 4 through groove cylinder 10 from feeding end 22, follow the rotation of the screw rod under variable-frequency motor 1 driving, mud is advanced to discharge end 24 places by screw rod from feeding end 22 places, in this process, owing to being subject to the interior deep fat heating of pipeline road 25, moisture evaporation obtains mummification to mud, and the mud that arrives discharge end 24 places has obtained mummification, and mud heating makes the waste gas producing discharge through exhaust side 23.Mud is subject to the stirring of screw rod in the process advancing simultaneously, mud is heated evenly and is unlikely to caking.
Hot oiling oil circuit: active rotation bar 26 is identical with the deep fat principle of work on driven dwang 27 and driven screw-blade 14 with the deep fat principle of work on active screw-blade 15, the oil circuit in this selects active rotation bar 26 and active screw-blade 15 describes.
Deep fat enters the first connection oil duct 16 by oil-in 18, wherein, this routine oil-in 18 is evenly distributed with six on the rod end of active rotation bar 26, deep fat enters spiral oil duct 19 after entering the first connection oil duct 16, deep fat flows and realizes heat exchange with the mud of active screw-blade 15 outsides in spiral oil duct 19, then deep fat enters the rear backflow of the second connection oil duct 17, leaves active rotation bar 26 through oil outlet 20.Then deep fat again via conduit by the oiler of lead-in groove cylinder 10 7, thereby deep fat enters in oil pocket 11, realizes the second stage employ of the remaining temperature of deep fat, flows out finally by the oil discharge outlet 5 of groove cylinder 10.Again deep fat is inducted into heat-conducting oil furnace 600 and heats up, again lead back to oil-in 18, realize hot oiling utilization.
Above-mentioned embodiment is only preferred implementation of the present utility model; the scope that can not limit with this utility model protection, the variation of any unsubstantiality that those skilled in the art does on basis of the present utility model and replacement all belong to the utility model scope required for protection.
Claims (10)
1. a sludge drying system, it is characterized in that: comprise the pressure filter for sludge dewatering, for the storage bucket of mud storage, for heating the sludge drier of dewatered sludge, be used for the steam condenser of the heat energy that reclaims waste gas, for the deodorizing tower to exhaust air deodorization with for heating the heat-conducting oil furnace of deep fat, the outlet of described pressure filter is connected with the entrance of storage bucket, the storage outlet of bucket and the feeding end of sludge drier are connected, described sludge drier comprises at least two-layer stacked loft drier from top to bottom and lays respectively at the drying installation in loft drier, each loft drier all has the described feeding end for passing into mud, for exporting the discharge end of mud, for the exhaust side of combustion gas, each drying installation has past drying installation and passes into the oil-in of deep fat and the oil outlet of output deep fat, each loft drier is connected with discharge end with feeding end, and some serial connection is communicated with using this tie point as serial connection, after each exhaust side series connection, be connected with the inlet mouth of steam condenser, the air outlet of steam condenser is connected with the inlet mouth of deodorizing tower, and each oil-in confluxes and is connected to the oil outlet end of heat-conducting oil furnace, and each oil outlet confluxes and is connected to the oil inlet end of heat-conducting oil furnace.
2. sludge drying system according to claim 1, it is characterized in that: described drying installation is spiral propeller, loft drier is wrapped with the groove cylinder for being incubated, described feeding end and discharge end run through the correspondence position of loft drier and groove cylinder, described spiral propeller comprises the rotating driving device of adjustable rotating speed and is driven at least one screw rod of rotation by rotating driving device, in the body of rod of each screw rod, be provided with pipeline road, this pipeline road has described oil-in and described oil outlet, each oil-in confluxes and is connected to the oil outlet end of heat-conducting oil furnace respectively after a regulated valve separately, oil-in and oil outlet are positioned at same one end of the body of rod, antetheca, rear wall and the diapire of described groove cylinder are hollow structure, form oil pocket, and the antetheca of groove cylinder and rear wall have oiler and oil discharge outlet, and oiler one side is communicated with oil discharge outlet through oil pocket, and oiler opposite side is communicated with oil outlet through a conduit.
3. sludge drying system according to claim 2, it is characterized in that: the body of rod outer side of described screw rod is provided with screw-blade, in screw-blade, hollow forms spiral oil duct, described oil-in connects oil duct through one first and is communicated with one end of spiral oil duct, and the other end of spiral oil duct connects oil duct through one second and is communicated with oil outlet; Described the first connection oil duct, spiral oil duct are connected oil duct with second and form described pipeline road.
4. sludge drying system according to claim 3, is characterized in that: described oil-in is multiple, and bobbin is symmetrical centered by the rotary middle spindle of screw rod; First to connect oil duct be corresponding with oil-in quantity multiple, and extend internally along the length direction of screw rod.
5. sludge drying system according to claim 3, it is characterized in that: in the body of rod of described screw rod, be made as hollow heat insulation chamber, described second connect oil duct by one end of the body of rod of screw rod to unsettled stretching out in hollow heat insulation chamber, this second external part that connects oil duct is communicated with oil outlet.
6. according to the sludge drying system described in claim 3 ~ 5 any one, it is characterized in that: described spiral propeller also comprises transmission rig, described rotating driving device is in transmission connection through transmission rig and screw rod.
7. sludge drying system according to claim 6, it is characterized in that: the body of rod of each described screw rod comprises active rotation bar and driven dwang, described screw-blade comprises the active screw-blade of being located at active rotation bar outer side and the driven screw-blade of being located at driven dwang outer side, initiatively the rotation direction of screw-blade is contrary with the rotation direction of driven screw-blade, and initiatively screw-blade engages with driven screw-blade; Described transmission rig comprises driving toothed gear, follower gear, the rotation output terminal of rotating driving device is fixedly inserted to the center of driving toothed gear, follower gear engages with driving toothed gear, active rotation bar is all connected with loft drier along the length direction of loft drier rotationally with driven dwang, active rotation bar is fixed in the center of driving toothed gear, and driven dwang is fixed in the center of follower gear.
8. sludge drying system according to claim 7, is characterized in that: the two ends of described active rotation bar and driven dwang are stretched out by the two ends of groove cylinder respectively, and the two ends of described groove cylinder have the perforate that supplies active rotation bar and driven dwang to pass.
9. sludge drying system according to claim 8, is characterized in that: the two ends of described groove cylinder are respectively equipped with right baffle-plate and right baffle plate, and described perforate lays respectively in right baffle-plate and right baffle plate; Described groove cylinder is enclosed with for heat insulation iron sheet cover.
10. sludge drying system according to claim 7, is characterized in that: described loft drier comprises cell body and be sealed on the upper cover plate on the notch of cell body, and described feeding end is by protruding upward in upper cover plate, and runs through groove cylinder; Described discharge end is stretched out downwards by the bottom land of cell body, and runs through groove cylinder; Described exhaust side is by stretching out on upper cover plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420276065.4U CN203904180U (en) | 2014-05-27 | 2014-05-27 | Sludge drying system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420276065.4U CN203904180U (en) | 2014-05-27 | 2014-05-27 | Sludge drying system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203904180U true CN203904180U (en) | 2014-10-29 |
Family
ID=51778469
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420276065.4U Expired - Lifetime CN203904180U (en) | 2014-05-27 | 2014-05-27 | Sludge drying system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203904180U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103992018A (en) * | 2014-05-27 | 2014-08-20 | 广州市海森环境节能科技工程有限公司 | Sludge drying system |
-
2014
- 2014-05-27 CN CN201420276065.4U patent/CN203904180U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103992018A (en) * | 2014-05-27 | 2014-08-20 | 广州市海森环境节能科技工程有限公司 | Sludge drying system |
| CN103992018B (en) * | 2014-05-27 | 2016-02-10 | 广州市海森环保科技股份有限公司 | A kind of sludge drying system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103992018B (en) | A kind of sludge drying system | |
| CN203904181U (en) | Spiral propulsion continuous drying device | |
| CN107555759A (en) | Microwave nurses one's health dehydration and drying sludge treating system | |
| KR100724686B1 (en) | Closed Circulation Type Drying Apparatus | |
| CN103575077A (en) | Multi-layer belt type drying system | |
| JP6639330B2 (en) | Dehydration system and dehydration method | |
| CN105417923B (en) | A kind of sludge drying system | |
| CN101549945A (en) | Set treatment device of sludge drying | |
| CN106045274A (en) | MVR belt sludge drying machine | |
| CN109368981A (en) | A kind of sludge semi-dry processing system and processing method | |
| CN102557383A (en) | Inclined disk blade dryer for drying sludge and treatment method thereof | |
| CN203048755U (en) | Steam heat-cycling sludge drying system | |
| CN203904180U (en) | Sludge drying system | |
| CN201096447Y (en) | Highly effective energy-saving drying-machine | |
| CN108627000A (en) | A kind of drying unit of source heat pump heat | |
| CN110395873B (en) | Van-type vacuum drying device for urban sludge | |
| CN204891253U (en) | Evaporative concentration system of emulsion | |
| CN214571600U (en) | Drying and fermenting device for organic fertilizer | |
| CN206089407U (en) | MVR drying system | |
| CN107014160A (en) | Solar energy, air energy Dual-energy source drying integral machine | |
| CN105716408A (en) | Low-temperature fodder drier | |
| CN208872037U (en) | A kind of drying unit of source heat pump heat | |
| CN202390303U (en) | Swash plate type paddle drier for drying sludge | |
| CN208087445U (en) | Sludge dry system | |
| CN205974233U (en) | MVR mud belt mummification machine |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee |
Owner name: GUANGZHOU HAISEN ENVIRONMENTAL PROTECTION TECHNOLO Free format text: FORMER NAME: GUANGZHOU HAISEN ENVIRONMENT ENERGY SAVING TECHNOLOGY ENGINEERING CO., LTD. |
|
| CP01 | Change in the name or title of a patent holder |
Address after: 510000, 314, 5, two street, Keshan Road, Ring West Road, Liwan District, Guangdong, Guangzhou Patentee after: GUANGZHOU HAISEN ENVIRONMENT ENERGY SAVING TECHNOLOGY ENGINEERING CO., LTD. Address before: 510000, 314, 5, two street, Keshan Road, Ring West Road, Liwan District, Guangdong, Guangzhou Patentee before: Guangzhou Haisen Environment Energy-saving Technology Engineering Co.,Ltd. |