CN205170639U - Sludge treatment system - Google Patents

Sludge treatment system Download PDF

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Publication number
CN205170639U
CN205170639U CN201520909020.0U CN201520909020U CN205170639U CN 205170639 U CN205170639 U CN 205170639U CN 201520909020 U CN201520909020 U CN 201520909020U CN 205170639 U CN205170639 U CN 205170639U
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gas
pyrolysis
sludge
pyrolysis oven
outlet
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CN201520909020.0U
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巴玉鑫
张安强
吴小飞
贾懿曼
吴道洪
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Beijing Jiejing Environmental Protection Technology Co., Ltd
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Beijing Shenwu Environmental and Energy Technology Co Ltd
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/129Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/40Valorisation of by-products of wastewater, sewage or sludge processing

Abstract

The utility model discloses a sludge treatment's system. Wherein, sludge treatment system includes: sludge drying device, pyrolysis oven, combustion chamber, exhaust -heat boiler and superheated steam passageway. This sludge treatment's system has simple structure, the thermal efficiency is high, the energy consumption is low advantage.

Description

Sludge treating system
Technical field
The utility model relates to the system of sludge treatment.
Background technology
End 2013, wastewater treatment in China factory produces mud per year and reaches 3000-3500 ten thousand tons but about have the mud of 80% without stabilization treatment at present, and a large amount of wet mud, by arbitrarily outward transport, simple landfill or stacking, causes many cities " mud besieged city ".
Existing pyrolyzing sludge technology, obtains oil, gas, charcoal three kinds of products.But in gas-oil separation process, easily cause line clogging.Further, pyrolysis oil quality is low, needs could utilize after hydrogenation, causes utilizing cost to remain high; And a large amount of oily(waste)waters obtained after oily water separation, be difficult to process, add the running cost of sludge treatment.Thus, the system of sludge treatment requires study.
Utility model content
The utility model is intended at least to solve one of technical problem existed in prior art.For this reason, an object of the present utility model be to propose a kind of realize municipal sludge quick minimizing, innoxious, resource utilization sludge treating system.
Thus, according to an aspect of the present utility model, the utility model provides a kind of system of sludge treatment.According to embodiment of the present utility model, this system comprises: mud drying device, described mud drying device has sludge inlet, superheated vapour entrance, dewatered sludge outlet, condensation-water drain, foul smell outlet and mud dries the water vapor relief outlet produced through superheated vapour, described mud drying device is used for carrying out drying and other treatment to mud, to obtain the mud after mummification; Pyrolysis oven, described pyrolysis oven has opening for feed, oil gas vent, discharge port, combustible gas entrance and exhanst gas outlet, described opening for feed exports with the described dewatered sludge of described mud drying device and is connected, for carrying out pyrolysis processing to the mud after described mummification, to obtain pyrolysis oil gas and pyrolytic carbon; Combustion chamber, described combustion chamber has oil gas entrance, combustion air inlet and exhanst gas outlet, described oil gas entrance exports with the described foul smell of described mud drying device with the described oil gas vent of described pyrolysis oven respectively and is connected, foul smell for obtaining described pyrolysis oil gas and described drying and other treatment carries out direct burn processing, to obtain flue gas; Waste heat boiler, described waste heat boiler has smoke inlet, exhanst gas outlet, feedwater entrance and superheated vapour outlet, described waste heat boiler is connected with described combustion chamber, utilizes the water in described flue gas and described waste heat boiler to carry out heat exchange process, to obtain the flue gas after superheated vapour and cooling; And superheated vapour passage, described superheated vapour passage and the described superheated vapour of described waste heat boiler export and are connected with the described superheated vapour entrance of described mud drying device, utilize described superheated vapour to provide heat for described drying and other treatment.
In the utility model, direct burn processing is carried out to described pyrolysis oil gas and refers to pyrolysis oil gas is directly burnt as fuel.
Wherein, combustion chamber is used for carrying out direct burn processing to described pyrolysis oil gas and drying and other treatment gained foul smell, can realize the direct burn processing of pyrolysis oil gas, reaches foul smell simultaneously and directly burns and deodourizing object.
Wherein, described pyrolysis oven has opening for feed, oil gas vent, discharge port, and described pyrolysis oven utilizes pyrolysis oven radiator tube to heat, and described pyrolysis oven radiator tube has combustible gas entrance and exhanst gas outlet.Described opening for feed exports with the described dewatered sludge of described mud drying device and is connected.
Wherein, described combustion chamber has oil gas entrance, combustion air inlet and exhanst gas outlet.The oil gas entrance of described combustion chamber is connected with the oil gas vent of pyrolysis oven.The foul smell that sludge drying produces, through induced draft fan, enters combustion chamber from combustion air inlet.
Wherein, described waste heat boiler has smoke inlet, exhanst gas outlet, feedwater entrance and superheated vapour outlet.The superheated vapour outlet of described waste heat boiler is connected with the superheated vapour entrance of described mud drying device by superheated vapour passage, and the smoke inlet of described waste heat boiler is connected with the exhanst gas outlet of described combustion chamber.
According to the system of the sludge treatment of the utility model embodiment, the high temperature pyrolysis oil gas that pyrolysis oven produces directly enters combustion chambers burn, fully can reclaim sensible heat and latent heat that high-temperature hot vents one's spleen, for the thermal source of sludge drying, it also avoid the pyrolysis oil blocking pipe that pyrolyzing sludge produces, and the treatment process of this system can not produce a large amount of reluctant waste water.The high-temperature flue gas that pyrolysis gas burning simultaneously produces enters waste heat boiler and produces a large amount of superheated vapours, and superheated vapour returns mud drying device by superheated vapour passage, as the thermal source of dewatered sludge.Thus, the system of the sludge treatment of the utility model embodiment has the advantage that structure is simple, thermo-efficiency is high, energy consumption is low.
In addition, following additional technical characteristic can also be had according to the system of the sludge treatment of the utility model above-described embodiment:
Optionally, described pyrolysis oven is rotating bed pyrolysis oven, and described pyrolysis oven comprises: annular body of heater; And gas-fired radiation pipe heater, described gas-fired radiation pipe heater is arranged on the annular inner wall of described annular body of heater.
Optionally, described pyrolysis oven is heat accumulating type rotating bed pyrolysis oven.
Optionally, this system comprises further: sealing duplex discharging machine, described sealing duplex discharging machine is arranged on the described discharge outlet of described pyrolysis oven.
Optionally, this system comprises further: fluidized-bed gasification device, and described fluidized-bed gasification device is connected with the described discharge port of described pyrolysis oven, for carrying out gasification process to described pyrolytic carbon, to obtain combustion gas.Described fluidized-bed gasification device has pyrolytic carbon entrance, gasification agent inlet and mixed gas outlet.The mixed gas outlet of described fluidized-bed gasification device is connected with cooling tower with fly-ash separator.
Optionally, this system comprises further: rotary air preheater, described rotary air preheater is connected with the described combustion air inlet of described combustion chamber with the described exhanst gas outlet of described waste heat boiler, the flue gas after described cooling is utilized to carry out thermal pretreatment to combustion-supporting gas, to obtain the flue gas of the combustion-supporting gas after preheating and cooling, wherein, the combustion-supporting gas after described preheating is used for described burn processing.Described rotary air preheater has smoke inlet and exhanst gas outlet, combustion air inlet and combustion air outlet, condensation water collection mouth.Described combustion air outlet is connected with the combustion air inlet of described combustion chamber, and described smoke inlet is connected with the exhanst gas outlet of described waste heat boiler.The exhanst gas outlet of described rotary air preheater is connected with flue gas purifying equipment.The combustion air air inlet of described rotary air preheater adopts gas blower.The water of condensation of described rotary air preheater is pooled to water collect tank by reclaiming pipe network.
Additional aspect of the present utility model and advantage will part provide in the following description, and part will become obvious from the following description, or be recognized by practice of the present utility model.
Accompanying drawing explanation
Above-mentioned and/or additional aspect of the present utility model and advantage will become obvious and easy understand from accompanying drawing below combining to the description of embodiment, wherein:
Fig. 1 shows the structural representation of the sludge treating system according to the utility model embodiment;
Fig. 2 shows the structural representation of the sludge treating system according to the utility model embodiment;
Fig. 3 shows the structural representation of the sludge treating system according to the utility model embodiment;
Fig. 4 shows the schematic flow sheet of the method for sludge treatment according to the utility model embodiment;
Fig. 5 shows the schematic flow sheet of the method for sludge treatment according to the utility model embodiment;
Fig. 6 shows the schematic flow sheet of the method for sludge treatment according to the utility model embodiment;
Fig. 7 shows the schematic flow sheet of the method for sludge treatment according to the utility model embodiment.
Embodiment
Be described below in detail embodiment of the present utility model, the example of described embodiment is shown in the drawings, and wherein same or similar label represents same or similar element or has element that is identical or similar functions from start to finish.Being exemplary below by the embodiment be described with reference to the drawings, only for explaining the utility model, and can not being interpreted as restriction of the present utility model.
In description of the present utility model, term " longitudinal direction ", " transverse direction ", " on ", D score, "front", "rear", "left", "right", " vertically ", " level ", " top ", the orientation of the instruction such as " end " or position relationship be based on orientation shown in the drawings or position relationship, it is only the utility model instead of require that the utility model with specific azimuth configuration and operation, therefore can not must be interpreted as restriction of the present utility model for convenience of description.
It should be noted that, term " first ", " second " only for describing object, and can not be interpreted as instruction or hint relative importance or imply the quantity indicating indicated technical characteristic.Thus, be limited with " first ", the feature of " second " can express or impliedly comprise one or more these features.Further, in description of the present utility model, except as otherwise noted, the implication of " multiple " is two or more.
According to an aspect of the present utility model, the utility model provides a kind of system of sludge treatment.With reference to figure 1, according to embodiment of the present utility model, explain this system, this system comprises: mud drying device 100, pyrolysis oven 200, combustion chamber 300, waste heat boiler 400 and superheated vapour passage 500.According to embodiment of the present utility model, mud drying device 100 has sludge inlet, superheated vapour entrance, dewatered sludge outlet, condensation-water drain, foul smell outlet and mud dries the water vapor relief outlet produced through superheated vapour, mud drying device 100, for carrying out drying and other treatment to mud, obtains the mud after mummification; Pyrolysis oven 200 has opening for feed, oil gas vent, discharge port, combustible gas entrance and exhanst gas outlet, wherein, opening for feed exports with the dewatered sludge of mud drying device 100 and is connected, and for carrying out pyrolysis processing to the mud after mummification, obtains pyrolysis oil gas and pyrolytic carbon; Combustion chamber 300 has oil gas entrance, combustion air inlet and exhanst gas outlet, wherein, oil gas entrance exports with the described foul smell of described mud drying device 100 with the described oil gas vent of pyrolysis oven 200 respectively and is connected, foul smell for obtaining pyrolysis oil gas and described drying and other treatment carries out burn processing, obtain high-temperature flue gas, wherein, the temperature of high-temperature flue gas is 900-1100 degree Celsius; Waste heat boiler 400 has smoke inlet, exhanst gas outlet, feedwater entrance and superheated vapour outlet, waste heat boiler 400 is connected with the exhanst gas outlet of combustion chamber 300, the water in high-temperature flue gas and waste heat boiler 400 is utilized to carry out heat exchange process, obtain the flue gas after superheated vapour and cooling, wherein, the temperature of the flue gas after cooling is 800-900 degree Celsius; Superheated vapour passage 500 and the described superheated vapour of waste heat boiler 400 export and are connected with the described superheated vapour entrance of mud drying device 100, utilize superheated vapour to provide heat for drying and other treatment.
According to the system of the sludge treatment of the utility model embodiment, the high-temperature hot that pyrolysis oven produces is vented one's spleen and is directly entered combustion chambers burn, not only avoid the pyrolysis oil condensation bonding tube wall in pyrolysis gas and the problems such as the line clogging that causes, and fully can reclaim sensible heat and the latent heat of high temperature pyrolysis oil gas, heat recovery efficiency significantly improves, and can not produce a large amount of reluctant waste water.Meanwhile, the high-temperature flue gas that pyrolysis gas burning produces enters waste heat boiler and produces a large amount of superheated vapours, and superheated vapour returns mud drying device by superheated vapour passage, as the thermal source of dewatered sludge.Thus, the system of the sludge treatment of the utility model embodiment has the advantage that structure is simple, thermo-efficiency is high, energy consumption is low.
According to embodiment of the present utility model, mud containing 80% is directly sent into mud drying device 100, through 140-180 DEG C of superheated vapour mummification to water ratio 40%, the oil gas that sludge drying produces enters combustion chamber 300 and carries out burn processing, mud after mummification enters pyrolysis oven 200, complete pyrolytic reaction, final generation high-temperature oil gas and solid carbon.
According to embodiment of the present utility model, described pyrolysis oven is rotating bed pyrolysis oven.Thus, pyrolysis efficiency is high, effective.According to embodiment of the present utility model, described rotating bed pyrolysis oven comprises: annular body of heater and gas-fired radiation pipe heater, wherein, gas-fired radiation pipe heater is arranged on the annular inner wall of annular body of heater, heated by fired-gas radiant tube combustor, namely provide pyrolysis institute heat requirement by burn combustible gas in thermal-radiating mode.Treat that pyrolysis material is arranged on the ring-shaped furnace bottom of ring furnace, this furnace bottom can horizontally rotate, and fired-gas radiant tube combustor is arranged on the ring furnace inwall of ring furnace, and the flue gas in radiator tube and the atmosphere in ring furnace completely cut off.Thus, mud, under anoxic condition, utilizes radiator tube to heat, and pyrolysis gas and high-temperature flue gas completely cut off, and do not produce dioxin and pollute, and the pyrolysis gas quality obtained is high, calorific value is at more than 6000kcal.
According to preferred embodiment of the present utility model, pyrolysis oven is heat accumulating type rotating bed pyrolysis oven.Heat accumulating type rotating bed pyrolysis oven adopts regenerative gas radiant tube heater.Thus, the feature of regenerative gas radiant tube heater to use >700kcal/m 3low-rank fuel gas, pyrolyzing sludge charcoal gasification gained calorific value of fuel gas is greatly about 1200-1500kcal/m 3, therefore, preferentially select heat accumulating type rotating bed pyrolysis oven.
According to embodiment of the present utility model, this system comprises further: sealing duplex discharging machine, described sealing duplex discharging machine is arranged on the described discharge outlet of described pyrolysis oven.By stirring and the squeezing action of sealing duplex discharging machine, break process is carried out to the pyrolytic carbon that pyrolysis processing obtains, obtains pyrolytic carbon particle, the needs making the particle diameter of pyrolytic carbon particle meet the devices such as fluidized-bed to process further.
According to specific embodiment of the utility model, combustion chamber adopts burner to carry out burn processing.Thus, efficiency of combustion is high, pyrolysis oil gas can in combustion chamber Thorough combustion, produce high-temperature flue gas, according to specific embodiment of the utility model, the temperature of high-temperature flue gas reaches 900-1100 DEG C.Then, the combustion product gases of 900-1000 DEG C enters waste heat boiler, and the overheated steam superheated vapour producing 140-180 DEG C with the water heat exchange in boiler enters mud drying device indirectly drying mud.
With reference to figure 2, according to embodiment of the present utility model, this system comprises further: fluidized-bed gasification device 600, and this fluidized-bed gasification device 600 is connected with the discharge port of pyrolysis oven 200, for carrying out gasification process to pyrolytic carbon, obtains combustion gas.Wherein, in gasification process process, air and the water vapour from waste heat boiler 400 mix as vaporized chemical and fluidizing medium, fluidized-bed gasification device 600 is entered from nozzle, making feed stock for blast furnace fluidisation, there is violent mass transfer and heat transfer, and combustion reactions and water-gas reaction occurs in gas, solid two-phase.Gasification temperature is 850 DEG C-1100 DEG C, and after pyrolytic carbon is heated, fast pyrogenation produces tar, phenol and light oil etc., and under bed hot conditions, be cracked into small molecules, thus obtain combustion gas, wherein, according to embodiment of the present utility model, the temperature of combustion gas can be 900-1000 DEG C.According to specific embodiment of the utility model, combustion gas enters the further dedusting cooling of wash cooling tower after tornado dust collector, and outlet gas temperature is down to about 35 DEG C, sends into gas holder, as the fuel of pyrolysis oven pyrolyzing sludge.The lime-ash produced after pyrolytic carbon gasification is arranged in airtight ash bucket through the spiral tapping machine of internal water cooling, is regularly discharged to the furnace bottom slag car, sends out-of-bounds.Thus, pass through gasification installation, the pyrolytic carbon utilizing economic worth low forms the high combustion gas of economic worth, and, only a small amount of residue be can produce after gasification, the minimizing of mud, innoxious and recycling treatment really achieved, and the combustion gas obtained, can be used as fuel is pyrolysis oven heat supply, reduces the sludge treating system of the utility model embodiment to the dependence of extra power.
With reference to figure 3, according to embodiment of the present utility model, this system comprises further: rotary air preheater 700, this rotary air preheater 700 is connected with the exhanst gas outlet of waste heat boiler 400 with the combustion air inlet of combustion chamber 300, the flue gas after cooling is utilized to carry out thermal pretreatment to combustion-supporting gas, obtain the flue gas of the combustion-supporting gas after preheating and cooling, wherein, the combustion-supporting gas after preheating is used for burn processing.Thus, the waste heat of flue gas is utilized to carry out preheating to combustion-supporting gas further, not only be conducive to the burning of combustion-supporting gas, and after thermal pretreatment, the temperature of flue gas reduces further, become liquid water after making a large amount of water vapour in flue gas discharge the latent heat of vaporization in rotary air preheater to recycle, and environmental emission standard can be reached through dust removal process after flue gas cool-down.According to specific embodiment of the utility model, rotate air preheater 700 and adopt ceramic honeycomb body material, there is the features such as corrosion resistance nature is strong, wear-resistant, thermal capacity is large, flue-gas temperature can be down to less than 100 DEG C, in the sensible heat and flue gas of abundant recovered flue gas steam the latent heat of vaporization while, water of condensation that can be a large amount of in recovered flue gas, water of condensation is pooled in water collect tank by reclaiming pipe network.The main component producing flue gas in combustion chamber combustion due to the high-temperature oil gas of complicated component is CO 2and water vapour, after waste heat boiler and the heat exchange of rotary air preheater can after can direct qualified discharge, non-secondary pollution, avoids the defection of traditional oils moisture and produces a large amount of reluctant wastewater problem, have good economic benefit and effects of energy saving and emission reduction.
For the ease of understanding the system of above-mentioned sludge treatment, the system utilizing above-mentioned sludge treatment is provided to carry out the method for sludge treatment at this.With reference to figure 4, according to embodiment of the present utility model, explain the method, the method comprises:
S100 drying and other treatment
According to embodiment of the present utility model, utilize mud drying device that mud is carried out drying and other treatment, obtain the mud after mummification and foul smell.Because the water content of mud is too high, first carry out drying and other treatment, reduce the water content of mud, be convenient to carry out follow-up pyrolysis processing.According to embodiments more of the present utility model, mud containing 80% is directly carried out drying and other treatment, through 140-180 DEG C of water vapor mummification to water ratio 30-50%, the oil gas that sludge drying produces can carry out burn processing, mud after mummification carries out pyrolysis processing, complete pyrolytic reaction, final heat-dissipating is vented one's spleen and pyrolytic carbon.Gained foul smell is through burn processing.
S200 pyrolysis processing
According to embodiment of the present utility model, utilize pyrolysis oven that the mud after mummification is carried out pyrolysis processing, obtain pyrolysis oil gas and pyrolytic carbon.Thus, by pyrolysis processing, the mud after mummification is converted into available, that economic worth is higher pyrolysis gas and pyrolytic carbon.
According to embodiment of the present utility model, provide heat by thermal-radiating mode for pyrolysis processing, this pyrolysis processing is carried out under anoxic condition.Thus, make mud carry out pyrolysis processing under anoxic condition by thermal radiation heating, pyrolysis gas and high-temperature flue gas completely cut off, and do not produce dioxin and pollute, and the pyrolysis gas quality obtained is high, calorific value is at more than 6000kcal.
According to embodiment of the present utility model, the temperature of described pyrolysis processing is 600-800 degree Celsius, and the time is 50-120 minute.Thus, pyrolysis is effective, and the abundant pyrolysis of carbon raw material, the productive rate of pyrolysis oil gas and pyrolytic carbon is high.
The direct burn processing of S300
According to embodiment of the present utility model, utilize combustion chamber that the foul smell that described pyrolysis oil gas and described drying and other treatment obtain is carried out direct burn processing, to obtain flue gas, simultaneously by burning purifying treatment foul smell, reach deodorizing object.Thus, vented one's spleen by the high-temperature hot that pyrolysis processing is produced and carry out direct burn processing, fully can reclaim sensible heat and the latent heat of high temperature pyrolysis oil gas, for the thermal source of sludge drying, it also avoid the pyrolysis oil blocking pipe that pyrolyzing sludge produces, and the method can not produce a large amount of reluctant waste water, do not need gas-purification and post-treatment process.The high-temperature flue gas that pyrolysis gas burning simultaneously produces carries out heat exchange process, and produce a large amount of superheated vapours, overheated steam returns mud drying device by overheated steam passage, as the thermal source of dewatered sludge.
S400 heat exchange process
According to embodiment of the present utility model, utilize waste heat boiler that the water of high-temperature flue gas and waste heat boiler is carried out heat exchange process, obtain the flue gas after superheated vapour and cooling, wherein, superheated vapour provides heat for aforesaid drying and other treatment.Thus, utilize the heat that pyrolyzing sludge and burning produce, by heat exchange process, without the need to external heat source, can obtain in a large number for the superheated vapour of sludge drying.
With reference to figure 5, according to embodiment of the present utility model, the method for this sludge treatment comprises further:
S500 thermal pretreatment
According to embodiment of the present utility model, by described rotary air preheater, utilize the flue gas after cooling to carry out thermal pretreatment to combustion-supporting gas, obtain the flue gas of the combustion-supporting gas after preheating and cooling, wherein, the combustion-supporting gas after described preheating is used for described burn processing.Thus, the waste heat of flue gas is utilized to carry out preheating to combustion-supporting gas, not only be conducive to the burning of combustion-supporting gas, and after thermal pretreatment, the temperature of flue gas reduces further, become liquid water after making a large amount of water vapour release latent heats of vaporization in flue gas to recycle, and environmental emission standard can be reached through dust removal process after flue gas cool-down.According to embodiments more of the present utility model, this thermal pretreatment utilizes rotary air preheater to carry out.Thus, pre-heat effect is good, and in flue gas, the latent heat of water vapour is fully discharged.
With reference to figure 6, according to embodiment of the present utility model, the method for this sludge treatment comprises further:
S600 gasification process
According to embodiment of the present utility model, pyrolytic carbon is carried out gasification process, obtains combustion gas.Wherein, in gasification process process, air and from changing the mixing of heat treated water vapour as vaporized chemical and fluidizing medium, making feed stock for blast furnace fluidisation, there is violent mass transfer and heat transfer, and combustion reactions and water-gas reaction occurs in gas, solid two-phase.Gasification temperature is 850 DEG C-1100 DEG C, and after pyrolytic carbon is heated, fast pyrogenation produces tar, phenol and light oil etc., and under bed hot conditions, be cracked into small molecules, thus obtain combustion gas, wherein, according to embodiment of the present utility model, the temperature of combustion gas can be 900-1000 DEG C.According to specific embodiment of the utility model, combustion gas enters the further dedusting cooling of wash cooling tower after tornado dust collector, and outlet gas temperature is down to about 35 DEG C, sends into gas holder, as the fuel of pyrolysis oven pyrolyzing sludge.The lime-ash produced after pyrolytic carbon gasification is arranged in airtight ash bucket through the spiral tapping machine of internal water cooling, is regularly discharged to the furnace bottom slag car, sends out-of-bounds.Thus, by gasification process, the pyrolytic carbon utilizing economic worth low forms the high combustion gas of economic worth, and, only a small amount of residue be can produce after gasification, the minimizing of mud, innoxious and recycling treatment really achieved.According to embodiment of the present utility model, utilize the combustion gas that obtains to provide fuel for described pyrolysis oven, to provide heat for pyrolysis, reduce the sludge treating system of the utility model embodiment to the dependence of extra power.
According to the method for the sludge treatment of the utility model embodiment, the high-temperature hot that pyrolysis processing produces is vented one's spleen and is carried out direct burn processing, fully can reclaim sensible heat and the latent heat of high temperature pyrolysis oil gas, for the thermal source of sludge drying, it also avoid the pyrolysis oil blocking pipe that pyrolyzing sludge produces, and the method can not produce a large amount of reluctant waste water.The high-temperature flue gas that pyrolysis gas burning simultaneously produces carries out heat exchange process, and produce a large amount of superheated vapours, superheated vapour returns mud drying device by superheated vapour passage, as the thermal source of dewatered sludge.Thus, the system of the sludge treatment of the utility model embodiment has the advantage that structure is simple, thermo-efficiency is high, energy consumption is low.
Below with reference to specific embodiment, be described the utility model, it should be noted that, these embodiments are only illustrative, and can not be interpreted as restriction of the present utility model.
Embodiment 1
In the present embodiment, with the mud of water ratio 80% for raw material, process mud, wherein the one-tenth of mud is grouped into as shown in table 1, and with reference to figure 7, the concrete sludge treatment step of this enforcement is as follows:
Table 1 domestic sludge physical properties (wt%) (empty butt)
(1) mud delivers to feeding device through delivery system, and feeding device enters mud drying device through opening for feed, is 40%, then delivers into pyrolysis oven through the superheated vapor dryings of 180 DEG C to water ratio;
(2) pyrolysis of mud: the main equipment of pyrolysis is without thermal barrier heat storage type pyrolysis stove, and this comprises pyrolysis oven, heat storage type gas radiation pipe burner without thermal barrier heat storage type pyrolysis stove, and the auxiliary mechanism such as cloth, discharging.Its furnace bottom is rotating ring-shaped furnace bottom, heat storage type gas radiation pipe burner is arranged in annular furnace wall, pyrolyzing sludge institute heat requirement is provided in thermal-radiating mode by burn combustible gas, flue gas in radiator tube and the atmosphere in pyrolysis oven completely cut off, wherein, the temperature of pyrolysis zone is 800 DEG C, and reaction generates high-temperature hot and vents one's spleen and pyrolytic carbon, wherein, pyrolysis gas mainly comprises high heating value pyrolysis combustion gas and pyrolysis oil and superheated vapour; At body of heater top, pneumatic outlet being set near pyrolysis zone, venting one's spleen for collecting high-temperature hot.The pyrolytic carbon that pyrolysis obtains is through sealing duplex discharging machine discharging and sending in fluidized-bed, duplex is arranged side by side, and spiral is engaged, through double-helical stirring, squeezing action, shattering process can be completed while discharging, form the raw material meeting fluidized-bed gasification;
(3) high temperature pyrolysis gas firing process: the 750 DEG C of high-temperature hot pyrolysis of pyrolysis oven obtained are vented one's spleen and to be connected with combustion chamber by pipeline, combustion chamber adopts the burner of particular design, pyrolysis combustion gas and pyrolysis oil can in combustion chamber Thorough combustion, produce the high-temperature flue gas of 950 DEG C.
(4) residual heat boiler for exchanging heat: the combustion product gases of 950 DEG C that combustion chambers burn process obtains enters waste heat boiler, produce the superheated vapour of 180 DEG C and middle temperature flue gas with the water heat exchange in boiler, superheated vapour enters mud drying device dewatered sludge.
(5) warm flue gas waste heat recovery in: middle temperature flue gas enters rotary air preheater, combustion chamber combustion air is preheating to 280 DEG C, because rotary air preheater adopts ceramic honeycomb body material, there is the features such as corrosion resistance nature is strong, wear-resistant, thermal capacity is large, flue-gas temperature can be down to 80 DEG C, in the sensible heat and flue gas of abundant recovered flue gas steam the latent heat of vaporization while, water of condensation that can be a large amount of in recovered flue gas, water of condensation is pooled in water collect tank by reclaiming pipe network, the recyclable water of condensation 0.3-0.45t of mud per ton.The main component producing flue gas in combustion chamber combustion due to the high-temperature oil gas of complicated component is CO 2and water vapour, after waste heat boiler and air preheater heat exchange can after can direct qualified discharge, non-secondary pollution, has good economic benefit and effects of energy saving and emission reduction.
(6) fluidized-bed gasification: from the pyrolytic carbon of pyrolysis oven through belt conveyor, crusher, enter in hopper and store, pyrolytic carbon sends into vapourizing furnace bottom cone section by the self-conveyor feed of bin bottom.Air and from the superheated vapour mixing of waste heat boiler as vaporized chemical and fluidizing medium, entering vapourizing furnace from nozzle, make feed stock for blast furnace fluidisation, there is violent mass transfer and heat transfer, and combustion reactions and water-gas reaction occurs in gas, solid two-phase.Gasification temperature is 900 DEG C, and after pyrolytic carbon is heated, fast pyrogenation produces tar, phenol and light oil etc., and is cracked into small molecules under bed hot conditions.Temperature is that the combustion gas of coming out of the stove of 900 DEG C enters the further dedusting cooling of wash cooling tower after tornado dust collector, and outlet gas temperature is down to about 30 DEG C, and send into gas holder, as the fuel of pyrolysis oven pyrolyzing sludge, mud per ton can produce combustible gas 157Nm 3, its composition and calorific value as shown in table 2:
Table 2 combustible gas composition and calorific value
The lime-ash produced after pyrolytic carbon gasification is arranged in airtight ash bucket through the spiral tapping machine of internal water cooling, is regularly discharged to the furnace bottom slag car, sends out-of-bounds, and residual residue is collected and done material of construction or landfill, and level of residue is about 5% of factory's mud.
In sum, in the present embodiment, the flue gas in pyrolysis oven radiator tube and burner hearth pyrolysis atmosphere completely cut off, mud pyrolysis under complete anoxic condition, and can not produce dioxin and pollute, the environmental pollution of sludge treatment is little.And the high-temperature oil gas that pyrolysis pyrolysis produces directly enters combustion chambers burn, can fully reclaim high-temperature hot vent one's spleen in sensible heat and latent heat, and a large amount of reluctant waste water can not be produced, effectively prevent the problem of pyrolysis oil blocking pipe.Wherein, high-temperature flue gas and water vapour enter mud drying device dewatered sludge after entering a large amount of superheated vapours that residual heat boiler for exchanging heat obtains, and decrease the demand to the external energy, serve the effect of energy-saving and emission-reduction.In obtaining after residual heat boiler for exchanging heat, warm flue gas enters rotary air preheater, flue-gas temperature can be down to less than 100 DEG C, can the abundant latent heat of vaporization of steam in the sensible heat of recovered flue gas and flue gas, water of condensation that can also be a large amount of in recovered flue gas, greatly reduces pyrolysis energy consumption.The pyrolytic carbon that pyrolysis obtains enters fluidized-bed gasification and produces clean gas, can be used as the combustion gas of pyrolysis oven pyrolyzing sludge, only can produce a small amount of residue, really achieve the resource utilization of mud, minimizing and harmless treatment after solid carbon gasification.Thus, the sludge treating system of this enforcement achieves the resource utilization of mud, minimizing and harmless treatment efficiently.
In the description of this specification sheets, specific features, structure, material or feature that the description of reference term " embodiment ", " some embodiments ", " example ", " concrete example " or " some examples " etc. means to describe in conjunction with this embodiment or example are contained at least one embodiment of the present utility model or example.In this manual, identical embodiment or example are not necessarily referred to the schematic representation of above-mentioned term.And the specific features of description, structure, material or feature can combine in an appropriate manner in any one or more embodiment or example.
Although illustrate and described embodiment of the present utility model, those having ordinary skill in the art will appreciate that: can carry out multiple change, amendment, replacement and modification to these embodiments when not departing from principle of the present utility model and aim, scope of the present utility model is by claim and equivalents thereof.

Claims (5)

1. a sludge treating system, is characterized in that, comprising:
Mud drying device, described mud drying device has sludge inlet, superheated vapour entrance, dewatered sludge outlet, condensation-water drain, foul smell outlet and mud dries the water vapor relief outlet produced through superheated vapour;
Pyrolysis oven, described pyrolysis oven has opening for feed, oil gas vent, discharge port, combustible gas entrance and exhanst gas outlet, and described opening for feed exports with the described dewatered sludge of described mud drying device and is connected;
Combustion chamber, described combustion chamber has oil gas entrance, combustion air inlet and exhanst gas outlet, and described oil gas entrance exports with the described foul smell of described mud drying device with the described oil gas vent of described pyrolysis oven respectively and is connected;
Waste heat boiler, described waste heat boiler has smoke inlet, exhanst gas outlet, feedwater entrance and superheated vapour outlet, and described waste heat boiler is connected with the described exhanst gas outlet of described combustion chamber;
Superheated vapour passage, described superheated vapour passage and the described superheated vapour of described waste heat boiler export and are connected with the described superheated vapour entrance of described mud drying device.
2. sludge treating system according to claim 1, is characterized in that, comprises further:
Fluidized-bed gasification device, described fluidized-bed gasification device is connected with the described discharge port of described pyrolysis oven.
3. sludge treating system according to claim 1, is characterized in that, comprises further:
Rotary air preheater, described rotary air preheater is connected with the described exhanst gas outlet of described waste heat boiler with the described combustion air inlet of described combustion chamber.
4. sludge treating system according to claim 1, is characterized in that, described pyrolysis oven is rotating bed pyrolysis oven, and described pyrolysis oven comprises:
Annular body of heater; And
Gas-fired radiation pipe heater, described gas-fired radiation pipe heater is arranged on the annular inner wall of described annular body of heater.
5. sludge treating system according to claim 1, is characterized in that, comprises further:
Sealing duplex discharging machine, described sealing duplex discharging machine is arranged on the described discharge outlet of described pyrolysis oven.
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106556016A (en) * 2016-11-30 2017-04-05 中冶华天南京工程技术有限公司 Sludge carbonization plus incinerating method and system
CN108954364A (en) * 2018-05-19 2018-12-07 潘礼斌 A kind of excrement gasification cleaning heating system
CN109563991A (en) * 2016-07-28 2019-04-02 弗罗拉德瑞有限公司 Fractional combustion

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109563991A (en) * 2016-07-28 2019-04-02 弗罗拉德瑞有限公司 Fractional combustion
CN106556016A (en) * 2016-11-30 2017-04-05 中冶华天南京工程技术有限公司 Sludge carbonization plus incinerating method and system
CN108954364A (en) * 2018-05-19 2018-12-07 潘礼斌 A kind of excrement gasification cleaning heating system

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