CN204897675U - Mud serialization resourceful treatment device - Google Patents
Mud serialization resourceful treatment device Download PDFInfo
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- CN204897675U CN204897675U CN201520542264.XU CN201520542264U CN204897675U CN 204897675 U CN204897675 U CN 204897675U CN 201520542264 U CN201520542264 U CN 201520542264U CN 204897675 U CN204897675 U CN 204897675U
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Abstract
The utility model provides a mud serialization resourceful treatment device, by deodorizing device, the compressed air device, sludge dewatering device, mud conveyor, the mud feed bin, heat reactor in advance, the transducer, the dominant reaction ware, the second order reaction ware, the comdenstion water flash distillation plant, the material flash distillation plant, the material jar of keeping in, charge device, the supernatant enrichment facility, the water storage tank, water conveyor constitutes, can carry out the serialization to mud handles, the final eutrophy soil that produces can regard as afforestation soil or fertilizer to use, raw materialss such as foam concrete and foamite can be regarded as to the concentrate of hydrolysising, the moisturizing of whole system can be regarded as to the comdenstion water of isolating, thereby realize the minimizing of mud, the stabilization, innoxious and resourceful treatment, handle by deodorizing device in unison behind the gas collection that hydrolysis reaction produced, comdenstion water flash distillation plant and material flash distillation plant utilize high temperature comdenstion water and high temperature material vacuum flash evaporation steam raising to preheat mud, effectively improve system efficiency, reduce the energy consumption to realize environmental protection, energy -conservation.
Description
Technical field
The utility model relates to a kind of sludge treatment technique and device, and particularly a kind of mud serialization processing equipment for recycling, belongs to environmental technology field.
Background technology
Along with the development of economic society, the continuous lifting of Urbanization Rate, town domestic sewage discharge increases fast, and sewage treatment industry is also rapidly developed.Often process ten thousand tons of town domestic sewages and can produce 10-15 ton mud (water ratio 80%).Municipal sludge contains a large amount of organic and nutritive element, simultaneously also containing a large amount of heavy metal substances and harmful microorganisms.If specific resistance to filtration is improper, not only take a large amount of limited arable lands, also can cause serious pollution and destruction to ground surface environment and underground water, even cause secondary pollution.
In recent years, the developed country such as European Union and the U.S. continually develops the novel method of sludge disposal and recycling.Sludge treatment, the disposal technology of China are still in initial period, landfill (accounting for 63%), sludge fermentation and compost agricultural (accounting for 14%) after current sludge treating method mainly contains Direct Dehydration, and burning and comprehensive utilization etc.
The recycling treatment of mud, existing a lot of scholar and enterprise are devoted to the research of this aspect, and what even have starts having promoted the use of among a small circle, but all there is certain deficiency, such as can not continuous treatment, equipment volume is large, and invest high, energy consumption is large, energy source optimization structure is reasonable not, overbottom pressure waste heat could not Appropriate application, and external energy waste etc., also have a certain distance with the requirement of energy-conserving and environment-protective.
Summary of the invention
For the above shortcoming of existing method and device, the utility model provides a kind of mud serialization processing equipment for recycling, by the chemical industry catalytic hydrolysis process of uniqueness, make sludge bacteria micelle, organic particle broken, make microorganism cells be hydrolyzed broken wall simultaneously, release protein, finally obtains sludge hydrolytic concentrated solution and eutrophy dregs, realizes sludge reduction, stabilization, innoxious and recycling treatment.System recoveries high-temperature condensation water, flash distillation together with the high temperature sludge solutions after hydrolysis reaction, the mud before the steam preheating hydrolysis reaction of generation, the water of condensation produced after preheating carries out reclaiming and recycles as process water.Whole system serialization runs, and has the advantages such as production efficiency is high, running cost is low, process stabilizing, environmental protection and energy saving.
It is as follows that the utility model solves the technical scheme that its technical problem adopts:
A kind of mud serialization processing equipment for recycling is made up of odor removal, pneumatic plant, sludge dehydration device, sludge conveyer, sludge storage bin, pre-thermal reactor, transverter, main reactor, second reactor, condensed water flash device, material flash distillation plant, material temporary storage tank, chemicals dosing plant, supernatant concentration device, water tank, water conveying device.
The outlet of pneumatic plant and pre-thermal reactor compressed air inlet, main reactor compressed air inlet, second reactor compressed air inlet is connected, odor removal import and sludge storage bin venting port, pre-thermal reactor venting port, main reactor venting port, second reactor venting port is connected, the outlet of sludge conveyer is connected with the import of sludge storage bin mud, chemicals dosing plant outlet is connected with sludge conveyer dosing mouth, the outlet of sludge storage bin connects sludge conveyer, the outlet of sludge conveyer is connected with the import of preheating reactor content, the outlet of preheating reactor content connects sludge conveyer, the outlet of sludge conveyer is connected with transverter entrance, transducer outlet connects sludge conveyer, the outlet of sludge conveyer is connected with the material inlet of main reactor, the material outlet of main reactor connects sludge conveyer, the outlet of sludge conveyer is connected with the material inlet of second reactor, the material outlet of second reactor connects sludge conveyer, the outlet of sludge conveyer is connected with the high temperature inlet of material flash distillation plant, the low-temperature outlet of material flash distillation plant is connected with sludge dehydration device material inlet through sludge conveyer, the vapour outlet of material flash distillation plant is connected with the steam-in of pre-thermal reactor, the water out of sludge dehydration device is connected by the liquor inlet of sludge conveyer with supernatant concentration device, the water out of supernatant concentration device is connected with water tank import.The entrance of condensed water flash device is connected with the condensation-water drain of main reactor, second reactor, the vapour outlet of condensed water flash device is connected with the steam-in of pre-thermal reactor, and the water out of condensed water flash device is connected with water tank import by water conveying device.
Sludge storage bin is provided with material inlet, material outlet, venting port, and bottom is dual hopper structure, and outside is provided with steam preheating coil pipe.
Sludge conveyer is made up of spiral conveyer, pipeline, valve or mud spiral pump, pipeline, valve; Water conveying device is made up of in-line pump, pipeline, valve or vacuum pump, pipeline, valve.
Chemicals dosing plant is add alkali, acid adding, the one added in flocculation agent, adding preservative agent.
Pre-thermal reactor profile is cylindrical, and to be two-layerly made up of inside and outside, internal layer is provided with material inlet, material outlet, compressed air inlet, venting port, agitator, and skin is provided with steam-in, condensation-water drain; Vacuum tank is equipped with at pre-thermal reactor condensation-water drain place, and vacuum tank is furnished with vacuum pump.
Main reactor profile is cylindrical, and to be two-layerly made up of inside and outside, skin is divided into again upper and lower two parts; Main reactor internal layer is provided with material inlet, material outlet, compressed air inlet, venting port, agitator; Skin is provided with steam-in, condensation-water drain.
Second reactor profile is cylindrical, to be two-layerly made up of inside and outside; Second reactor internal layer is provided with material inlet, material outlet, compressed air inlet, venting port, agitator; Skin is provided with steam-in, condensation-water drain.
Transverter is ultrasonic transmission device.
Sludge dehydration device is that mud folds spiral shell machine or plate and frame(type)filter press.
Supernatant concentration device is MVR device or multi-effect evaporating device.
The beneficial effects of the utility model are: adopt the utility model, the objectionable impurities in mud can be removed, mud is converted into hydrolysis concentrated solution and the nutrition dregs being rich in N, P, K and organic matter, the hydrolysis concentrated solution obtained through supernatant concentration device can be used as foamed concrete and fire foam raw material, the eutrophy dregs obtained through sludge dehydration device can afforest soil or fertilizer use the most, really achieves the minimizing of mud, stabilization, innoxious and recycling treatment; Mud is hydrolyzed step by step reaction in pre-thermal reactor, main reactor and second reactor, and reaction more fully, thoroughly; Increasing transverter between pre-thermal reactor and main reactor carries out microwave reinforced to mud, further broken organic particle, ensures reaction effect, Reaction time shorten; Material flash distillation plant and condensed water flash device utilize high-temperature material and high-temperature condensation water vacuum flash to produce mud in steam preheating sludge storage bin and pre-thermal reactor, abundant recovery low grade heat energy, improve efficiency of energy utilization, reduce system energy consumption, realize energy saving of system; Process in odor removal after the unified collection of the gas that hydrolysis reaction produces, whole system serialization runs, and equipment volume is little, energy consumption is low, and improve single device service efficiency, effects of energy saving and emission reduction is remarkable.
Accompanying drawing explanation
Fig. 1 is that the utility model patent applies schematic diagram in sewage work.
Fig. 2 is that the utility model patent applies schematic diagram in sludge treatment factory.
Fig. 3 is sludge storage bin schematic diagram.
Fig. 4 is pre-thermal reactor schematic diagram.
Fig. 5 is main reactor schematic diagram.
Fig. 6 is second reactor schematic diagram.
In Fig. 1,21, odor removal, 2, pneumatic plant, 3, sludge dehydration device, 4, sludge conveyer, 5, sludge storage bin, 6, pre-thermal reactor, 7, transverter, 8, main reactor, 9, second reactor, 10, condensed water flash device, 11, material flash distillation plant, 12, material temporary storage tank, 13, chemicals dosing plant, 14, supernatant concentration device, 15, water tank, 16, water conveying device.
5-01, sludge storage bin material inlet in Fig. 3,5-02, sludge storage bin venting port, 5-03, preheat coil, 5-04, sludge storage bin material outlet.
6-01, the import of preheating reactor content in Fig. 4,6-02, pre-thermal reactor compressed air inlet, 6-03, pre-thermal reactor venting port, 6-04, steam-in, 6-05, preheating reactor content export, 6-06, vacuum pump, 6-07, vacuum tank, 6-08, condensation-water drain, 6-09, agitator.
8-01, main reactor compressed air inlet in Fig. 5,8-02, main reactor material outlet, 8-03, main reactor venting port, 8-04, steam-in, 8-05, condensation-water drain, 8-06, main reactor material inlet, 8-07, agitator.
9-01, second reactor compressed air inlet in Fig. 6,9-02, second reactor material inlet, 9-03, second reactor venting port, 9-04, steam-in, 9-05, second reactor material outlet, 9-06, condensation-water drain, 9-07, agitator.
Embodiment
Below in conjunction with accompanying drawing, the utility model is described in further detail.
Embodiment 1: sludge of sewage treatment plant treatment in situ
A kind of mud serialization processing equipment for recycling is made up of odor removal 1, pneumatic plant 2, sludge dehydration device 3, sludge conveyer 4, sludge storage bin 5, pre-thermal reactor 6, transverter 7, main reactor 8, second reactor 9, condensed water flash device 10, material flash distillation plant 11, material temporary storage tank 12, chemicals dosing plant 13, supernatant concentration device 14, water tank 15, water conveying device 16.
The outlet of pneumatic plant 2 and the compressed air inlet of pre-thermal reactor 6, the compressed air inlet of main reactor 8, the compressed air inlet of second reactor 9 is connected, the venting port of odor removal 1 import and sludge storage bin 5, the venting port of pre-thermal reactor 6, the venting port of main reactor 8, the venting port of second reactor 9 is connected, the outlet of sludge conveyer 4 is connected with the mud import of sludge storage bin 5, the outlet of chemicals dosing plant 13 is connected with the dosing mouth of sludge conveyer 4, the outlet of sludge storage bin 5 connects sludge conveyer 4, the outlet of sludge conveyer 4 is connected with the material inlet of pre-thermal reactor 6, the material outlet of pre-thermal reactor 6 connects sludge conveyer 4, the outlet of sludge conveyer 4 is connected with the entrance of transverter 7, the outlet of transverter 7 connects sludge conveyer 4, the outlet of sludge conveyer 4 is connected with the material inlet of main reactor 8, the material outlet of main reactor 8 connects sludge conveyer 4, the outlet of sludge conveyer 4 is connected with the material inlet of second reactor 9, the material outlet of second reactor 9 connects sludge conveyer 4, the outlet of sludge conveyer 4 is connected with the high temperature inlet of material flash distillation plant 11, the low-temperature outlet of material flash distillation plant 11 is connected through the material inlet of sludge conveyer 4 with sludge dehydration device 3, the vapour outlet of material flash distillation plant 11 is connected with the steam-in of pre-thermal reactor 6, the water out of sludge dehydration device 3 is connected with the liquor inlet of supernatant concentration device 14 by sludge conveyer 4, the water out of supernatant concentration device 14 is connected with the import of water tank 15.The entrance of condensed water flash device 10 is connected with the condensation-water drain of main reactor 8, second reactor 9, the vapour outlet of condensed water flash device 10 is connected with the steam-in of pre-thermal reactor 6, and the water out of condensed water flash device 10 is connected with the import of water tank 15 by water conveying device 16.
Sludge conveyer 4 is delivered in sludge dehydration device 3 after the mud from secondary sedimentation tank of sewage treatment work is mixed with the flocculation agent in chemicals dosing plant 13, sludge dehydration device 3 herein folds spiral shell machine for mud, delivered to the sludge storage bin material inlet 5-01 of sludge storage bin 5 by sludge conveyer 4 after mud reaches setting concentration, mud is flowed out by material outlet 5-04 after sludge storage bin bottom heating coil pipe 5-03 heats, sludge conveyer 4 has dosing mouth, alkali lye in chemicals dosing plant 13 is entered by dosing mouth and mixes with mud, conditioning of mud pH value is 12-13, then the internal layer of pre-thermal reactor 6 is entered by preheating reactor content import 6-01, under the stirring action of agitator 6-09, stay for some time in pre-thermal reactor 6 and be preheated, the flash-off steam coming from condensed water flash device 10 and material flash distillation plant 11 is entered by the outer field steam-in 6-04 of pre-thermal reactor 6, heat the mud of pre-thermal reactor 6 internal layer, releasing the steam after heat enters in vacuum tank 6-07 from condensation-water drain 6-08 outflow, enter in water tank 15 via water conveying device 16.The mud being preheating to certain temperature is flowed out by the material outlet 6-05 of pre-thermal reactor 6, enter sludge conveyer 4, sludge conveyer 4 is provided with transverter 7, mud organic particle under the intensified by ultrasonic wave effect of transverter 7 is broken, entered the internal layer of main reactor 8 by the material inlet 8-06 of main reactor 8 after further refinement, the outer field steam-in 8-04 of main reactor 8 passes into high-temperature steam, being flowed out by condensation-water drain 8-05 after releasing heat enters in condensed water flash device 10, water of condensation after flash distillation is entered in water tank 15 by water conveying device 16 and reclaims, mud mixes and is pulverized further under the effect of agitator 8-07, be hydrolyzed reaction under high temperature action, then second reactor material inlet 9-02 is delivered to by main reactor material outlet 8-02 through sludge conveyer 4, enter second reactor 9 internal layer, the outer field steam-in 9-04 of second reactor 9 passes into high-temperature steam, being flowed out by condensation-water drain 9-06 after releasing heat enters in condensed water flash device 10, water of condensation after flash distillation is entered in water tank 15 by water conveying device 16 and reclaims, mud proceeds high-temperature hydrolysis under the stirring action of agitator 9-07, material flash distillation plant 11 is delivered to by second reactor material outlet 9-05 through sludge conveyer 4 after sufficient reacting, the steam that vacuum flash produces is for heating the mud in pre-thermal reactor 6, material after flash distillation is after sludge conveyer 4 mixes with the acid solution in chemicals dosing plant 13, conditioning of mud pH value is neutral, then sludge dehydration device 3 is entered, sludge dehydration device 3 is herein plate and frame(type)filter press, dewatered sludge after dehydration directly discharges system, eutrophy dregs is after further process, can be used as greening soil or fertilizer use, the feed liquid of sludge dehydration device 3 output enters supernatant concentration device 14 and continues concentration, the product of output is hydrolysis concentrated solution, the water of condensation produced directly enters in water tank 15, water in water tank 15 can as chemicals dosing plant water, mud diluting water and other process waters, mud is at pre-thermal reactor 6, the gas that the reaction process that is hydrolyzed in main reactor 8 and second reactor 9 produces is respectively by pre-thermal reactor venting port 6-03, main reactor venting port 8-03 and second reactor venting port 9-03 is expelled to odor removal 1 and carries out collection and treatment.
Embodiment 2: outward transport sludge treatment
A kind of mud serialization processing equipment for recycling is made up of odor removal 1, pneumatic plant 2, sludge dehydration device 3, sludge conveyer 4, sludge storage bin 5, pre-thermal reactor 6, transverter 7, main reactor 8, second reactor 9, condensed water flash device 10, material flash distillation plant 11, material temporary storage tank 12, chemicals dosing plant 13, supernatant concentration device 14, water tank 15, water conveying device 16.
The outlet of pneumatic plant 2 and the compressed air inlet of pre-thermal reactor 6, the compressed air inlet of main reactor 8, the compressed air inlet of second reactor 9 is connected, the venting port of odor removal 1 import and sludge storage bin 5, the venting port of pre-thermal reactor 6, the venting port of main reactor 8, the venting port of second reactor 9 is connected, the outlet of sludge conveyer 4 is connected with the mud import of sludge storage bin 5, the outlet of chemicals dosing plant 13 is connected with the dosing mouth of sludge conveyer 4, the outlet of sludge storage bin 5 connects sludge conveyer 4, the outlet of sludge conveyer 4 is connected with the material inlet of pre-thermal reactor 6, the material outlet of pre-thermal reactor 6 connects sludge conveyer 4, the outlet of sludge conveyer 4 is connected with the entrance of transverter 7, the outlet of transverter 7 connects sludge conveyer 4, the outlet of sludge conveyer 4 is connected with the material inlet of main reactor 8, the material outlet of main reactor 8 connects sludge conveyer 4, the outlet of sludge conveyer 4 is connected with the material inlet of second reactor 9, the material outlet of second reactor 9 connects sludge conveyer 4, the outlet of sludge conveyer 4 is connected with the high temperature inlet of material flash distillation plant 11, the low-temperature outlet of material flash distillation plant 11 is connected through the material inlet of sludge conveyer 4 with sludge dehydration device 3, the vapour outlet of material flash distillation plant 11 is connected with the steam-in of pre-thermal reactor 6, the water out of sludge dehydration device 3 is connected with the liquor inlet of supernatant concentration device 14 by sludge conveyer 4, the water out of supernatant concentration device 14 is connected with the import of water tank 15.The entrance of condensed water flash device 10 is connected with the condensation-water drain of main reactor 8, second reactor 9, the vapour outlet of condensed water flash device 10 is connected with the steam-in of pre-thermal reactor 6, and the water out of condensed water flash device 10 is connected with the import of water tank 15 by water conveying device 16.
Sludge conveyer 4 delivers to the sludge storage bin material inlet 5-01 of sludge storage bin 5 outward transport mud, mud is flowed out by material outlet 5-04 after sludge storage bin bottom heating coil pipe 5-03 heats, sludge conveyer 4 has dosing mouth, alkali lye in chemicals dosing plant 13 is entered by dosing mouth and mixes with mud, conditioning of mud pH value is 12-13, then the internal layer of pre-thermal reactor 6 is entered by preheating reactor content import 6-01, under the stirring action of agitator 6-09, stay for some time in pre-thermal reactor 6 and be preheated, the flash-off steam coming from condensed water flash device 10 and material flash distillation plant 11 is entered by the outer field steam-in 6-04 of pre-thermal reactor 6, heat the mud of pre-thermal reactor 6 internal layer, releasing the steam after heat enters in vacuum tank 6-07 from condensation-water drain 6-08 outflow, enter in water tank 15 via water conveying device 16.The mud being preheating to certain temperature is flowed out by the material outlet 6-05 of pre-thermal reactor 6, enter sludge conveyer 4, sludge conveyer 4 is provided with transverter 7, mud organic particle under the intensified by ultrasonic wave effect of transverter 7 is broken, entered the internal layer of main reactor 8 by the material inlet 8-06 of main reactor 8 after further refinement, the outer field steam-in 8-04 of main reactor 8 passes into high-temperature steam, being flowed out by condensation-water drain 8-05 after releasing heat enters in condensed water flash device 10, water of condensation after flash distillation is entered in water tank 15 by water conveying device 16 and reclaims, mud mixes and is pulverized further under the effect of agitator 8-07, be hydrolyzed reaction under high temperature action, then second reactor material inlet 9-02 is delivered to by main reactor material outlet 8-02 through sludge conveyer 4, enter second reactor 9 internal layer, the outer field steam-in 9-04 of second reactor 9 passes into high-temperature steam, being flowed out by condensation-water drain 9-06 after releasing heat enters in condensed water flash device 10, water of condensation after flash distillation is entered in water tank 15 by water conveying device 16 and reclaims, mud proceeds high-temperature hydrolysis under the stirring action of agitator 9-07, material flash distillation plant 11 is delivered to by second reactor material outlet 9-05 through sludge conveyer 4 after sufficient reacting, the steam that vacuum flash produces is for heating the mud in pre-thermal reactor 6, material after flash distillation is after sludge conveyer 4 mixes with the acid solution in chemicals dosing plant 13, conditioning of mud pH value is neutral, then sludge dehydration device 3 is entered, sludge dehydration device 3 is herein plate and frame(type)filter press, dewatered sludge after dehydration directly discharges system, eutrophy dregs is after further process, can be used as greening soil or fertilizer use, the feed liquid of sludge dehydration device 3 output enters supernatant concentration device 14 and continues concentration, the product of output is hydrolysis concentrated solution, the water of condensation produced directly enters in water tank 15, water in water tank 15 can as chemicals dosing plant water, mud diluting water and other process waters, mud is at pre-thermal reactor 6, the gas that the reaction process that is hydrolyzed in main reactor 8 and second reactor 9 produces is respectively by pre-thermal reactor venting port 6-03, main reactor venting port 8-03 and second reactor venting port 9-03 is expelled to odor removal 1 and carries out collection and treatment.
Claims (9)
1. a mud serialization processing equipment for recycling, by odor removal (1), pneumatic plant (2), sludge dehydration device (3), sludge conveyer (4), sludge storage bin (5), pre-thermal reactor (6), transverter (7), main reactor (8), second reactor (9), condensed water flash device (10), material flash distillation plant (11), material temporary storage tank (12), chemicals dosing plant (13), supernatant concentration device (14), water tank (15), water conveying device (16) forms, the outlet of pneumatic plant (2) and pre-thermal reactor compressed air inlet (6-02), main reactor compressed air inlet (8-01), second reactor compressed air inlet (9-01) is connected, the import of odor removal (1) and sludge storage bin venting port (5-02), pre-thermal reactor venting port (6-03), main reactor venting port (8-03), second reactor venting port (9-03) is connected, the outlet of sludge conveyer (4) is connected with sludge storage bin material inlet (5-01), the outlet of chemicals dosing plant (13) is connected with the dosing mouth of sludge conveyer (4), sludge storage bin material outlet (5-04) connects sludge conveyer (4), the outlet of sludge conveyer (4) is connected with preheating reactor content import (6-01), preheating reactor content outlet (6-05) connects sludge conveyer (4), the outlet of sludge conveyer (4) is connected with the entrance of transverter (7), the outlet of transverter (7) connects sludge conveyer (4), the outlet of sludge conveyer (4) is connected with main reactor material inlet (8-06), main reactor material outlet (8-02) connects sludge conveyer (4), the outlet of sludge conveyer (4) is connected with second reactor material inlet (9-02), second reactor material outlet (9-05) connects sludge conveyer (4), the outlet of sludge conveyer (4) is connected with the high temperature inlet of material flash distillation plant (11), the low-temperature outlet of material flash distillation plant (11) is connected through the material inlet of sludge conveyer (4) with sludge dehydration device (3), the vapour outlet of material flash distillation plant (11) is connected with preheating reactor vapor entrance (6-04), the water out of sludge dehydration device (3) is connected with the liquor inlet of supernatant concentration device (14) by sludge conveyer (4), the water out of supernatant concentration device (14) is connected with the import of water tank (15), the entrance of condensed water flash device (10) and main reactor condensation-water drain (8-05), second reactor condensation-water drain (9-06) is connected, the vapour outlet of condensed water flash device (10) is connected with preheating reactor vapor entrance (6-04), the water out of condensed water flash device (10) is connected with the import of water tank (15) by water conveying device (16), it is characterized in that: sludge storage bin (5) is provided with material inlet (5-01), material outlet (5-04), venting port (5-02), outside is provided with steam preheating coil pipe (5-03), wherein bottom is dual hopper structure.
2. a kind of mud serialization processing equipment for recycling according to claim 1, is characterized in that: sludge conveyer (4) is made up of spiral conveyer, pipeline, valve or mud spiral pump, pipeline, valve; Water conveying device (16) is made up of in-line pump, pipeline, valve or vacuum pump, pipeline, valve.
3. a kind of mud serialization processing equipment for recycling according to claim 1, is characterized in that: chemicals dosing plant (13) is for adding alkali, acid adding, the one added in flocculation agent, adding preservative agent.
4. a kind of mud serialization processing equipment for recycling according to claim 1, it is characterized in that: pre-thermal reactor (6) profile is cylindrical, two-layerly to be made up of inside and outside, internal layer is provided with material inlet (6-01), material outlet (6-05), compressed air inlet (6-02), venting port (6-03), agitator (6-09), skin is provided with steam-in (6-04), condensation-water drain (6-08), vacuum tank (6-07) is equipped with at pre-thermal reactor condensation-water drain (6-08) place, and vacuum tank (6-07) is furnished with vacuum pump (6-06).
5. a kind of mud serialization processing equipment for recycling according to claim 1, it is characterized in that: main reactor (8) profile is cylindrical, two-layerly to be made up of inside and outside, skin is divided into again upper and lower two parts, and internal layer is provided with material inlet (8-06), material outlet (8-02), compressed air inlet (8-01), venting port (8-03), agitator (8-07); Skin is provided with steam-in (8-04), condensation-water drain (8-05).
6. a kind of mud serialization processing equipment for recycling according to claim 1, it is characterized in that: second reactor (9) profile is cylindrical, two-layerly to be made up of inside and outside, internal layer is provided with material inlet (9-02), material outlet (9-05), compressed air inlet (9-01), venting port (9-03), agitator (9-07), and skin is provided with steam-in (9-04), condensation-water drain (9-06).
7. a kind of mud serialization processing equipment for recycling according to claim 1, is characterized in that: transverter (7) is ultrasonic transmission device.
8. a kind of mud serialization processing equipment for recycling according to claim 1, is characterized in that: sludge dehydration device (3) folds spiral shell machine or plate and frame(type)filter press for mud.
9. a kind of mud serialization processing equipment for recycling according to claim 1, is characterized in that: supernatant concentration device (14) is MVR device or multi-effect evaporating device.
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| CN201520542264.XU CN204897675U (en) | 2015-07-24 | 2015-07-24 | Mud serialization resourceful treatment device |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107445424A (en) * | 2017-08-07 | 2017-12-08 | 东华大学 | It is a kind of to realize the debirs thermocatalytic efficiently device of decrement and recycling |
| CN108285253A (en) * | 2018-04-13 | 2018-07-17 | 科尼兹环保科技（大连）有限公司 | A kind of integrated technology for enterprise's sludge deep processing |
-
2015
- 2015-07-24 CN CN201520542264.XU patent/CN204897675U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107445424A (en) * | 2017-08-07 | 2017-12-08 | 东华大学 | It is a kind of to realize the debirs thermocatalytic efficiently device of decrement and recycling |
| CN108285253A (en) * | 2018-04-13 | 2018-07-17 | 科尼兹环保科技（大连）有限公司 | A kind of integrated technology for enterprise's sludge deep processing |
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