CN105347634A - Designing method of sludge processing apparatus and apparatus thereof - Google Patents
Designing method of sludge processing apparatus and apparatus thereof Download PDFInfo
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- CN105347634A CN105347634A CN201510699376.0A CN201510699376A CN105347634A CN 105347634 A CN105347634 A CN 105347634A CN 201510699376 A CN201510699376 A CN 201510699376A CN 105347634 A CN105347634 A CN 105347634A
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- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
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Abstract
The invention discloses a designing method of a sludge processing apparatus and an apparatus thereof, which belong to the technical field of sludge processing. The designing method of the sludge processing apparatus comprises an integral design of an engine base, a sludge processing roller, a power drive mechanism, an output pipeline and an engine cover as well as a concrete design of each component, the designing method is characterized in that according to the different heavy metal contents in the sludge, the modified sludge with water content being 25-30% is placed in three different sludge processing rollers in order, quantitative glucose powder is added for mechanical stirring at uniform speed for propulsion, and three technical steps of heavy metal and dehydration/denitrification treatment, carbonization treatment and fixed carbon combustion treatment are carried out under normal pressure condition at temperature of 100-450 DEG C. Compared with the prior art, the designing method and the sludge processing apparatus have the advantages of novel and reliable performance, and no secondary pollution; waste can be changed into valuables, and sludge harmlessness treatment is realized, and the designing method and the sludge processing apparatus realize protrude substantiality characteristic and obvious progress for resource processing.
Description
Technical field
The present invention relates to chemical industry and environmental technology field, particularly relate to a kind of for mud, particularly the method for design of urban wastewater treatment firm sludge treatment equipment and device technique field thereof.
Background technology
In recent years, along with the quick raising of wastewater treatment in China ability, sludge quantity also synchronously significantly increases.By in by the end of March, 2013, only with regard to urban wastewater treatment firm mud, whole nation the planned city, county add up to build up urban wastewater treatment firm 3451, sewage treatment capacity about 1.45 billion cubic meters/day, year produces more than 3,500 ten thousand tons, the mud of water content 80%, and increases progressively with the sewage work of about 120 every year.According to statistics, about 80% Sewage Plant has the thickening facility of mud, reaches minimizing to a certain degree.But about there is the mud of 80% without stabilization treatment, land is transferred to containing pollutents such as repugnant substance, pathogenic agent, persistent organisms from sewage in mud, cause pollutent to spread further, the environment building up the sewage treatment facility put into operation is had a greatly reduced quality with reduction of discharging benefit.36 the key cities' specific resistance to filtration rates in the whole nation reach 80%, and other the planned cities reach 70%, and county town and emphasis town reach 30%.And China's urban wastewater treatment firm mud has that floor space is large, water pollution, soil pollution, bacteria breed, topsoil etc. five endanger greatly.And in current disposal options, landfill accounts for 63.0%, sludge aerobic fermentation+agricultural accounts for 13.5%, mud nature mummification comprehensive utilization accounts for 5.4%, sludge incineration accounts for 1.8%, mud air storage and outward transport respectively account for 1.8% and 14.4%.In fact, the mud overwhelming majority of landfill, air storage and outward transport belongs to random disposal, and the ratio really realizing safe disposal is no more than 20%, and sludge treatment situation is very severe.To account for the burning disposal of sludge treatment total amount 1.8%, good treatment process is calculated with regard to sludge incineration in current method for sludge treatment, sludge incineration process is: after being mixed by a certain percentage with appropriate coal-fired coal dust by the mud of water ratio 80%, through granulation, be be delivered in incinerator after preliminary drying in the drying installation of 400 DEG C to burn completely at interior cavity temperature, lime-ash is discharged from bottom.The three wastes that the process of this burning produces still continue to produce secondary pollution again, not only do not handle well, also need supplementary external fuel on the contrary, the source of pollution that the dust, dioxin produced in burning process etc. are new, will cause new pollution to air and environment.And restrict a lot of because have of specific resistance to filtration Facilities Construction at present, but national specific resistance to filtration general technical route is not clearly one of important restriction factor.For improving China's specific resistance to filtration state of the art further, conscientiously the requirement of sewage sludge harmlessness, minimizing, stabilization, resource utilization is reached, avoid the secondary pollution caused thus, alleviate sludge yield and the delayed contradiction of sludge treatment ability, China has put into effect a series of policy, planning in recent years.Its Chinese Home to be combined by house and town and country construction portion, Environmental Protection Department, the Department of Science and Technology in 2009 and has been issued " urban wastewater treatment firm specific resistance to filtration and pollution prevention technique policy (trying) "; Within 2011, house town and country construction portion, National Development and Reform Commission organize in concert and have worked out " urban wastewater treatment firm specific resistance to filtration technical manual (trying) "; Execution plays " urban drainage and sewage disposal regulations " on January 1st, 2014 in country, within 2014, " 65 " China's World Environment Day themes as " declaring a war to pollution ", and to the main direction that pollution is declared a war be: in-depth prevention and control of air pollution, fortified water prevention and cure of pollution, do a good job of it remediation contaminated soil, strengthen heavy metal, chemical and Hazardous Wastes Management and prevent and treat dynamics, in-depth industrial pollution control.As can be seen here, China has a high potential on specific resistance to filtration, and Rapid development stage is stepped in specific resistance to filtration market.Therefore, seek a kind of newly, reliably, the method for design of the sludge treatment equipment of non-secondary pollution, safety and environmental protection and device thereof be for those skilled in the art of the present technique being really a technical task urgent and urgently to be resolved hurrily.
Summary of the invention
Technical problem to be solved by this invention overcomes the deficiencies in the prior art, and provide a kind of newly, technical scheme reliably, non-secondary pollution, turn waste into wealth, efficiency of investment is high, the method for design of the sludge treatment equipment of instant effect.
Another technical problem to be solved by this invention overcomes the deficiencies in the prior art, and provide a kind of newly, reliably, non-secondary pollution, turn waste into wealth, efficiency of investment is high, the sludge treatment equipment of instant effect.
For solving above-mentioned technical problem, the present invention adopts to be implemented as follows technical scheme: a kind of method of design of sludge treatment equipment, comprise support, sludge treatment cylinder, power-driven mechanism, delivery conduit, the global design of hood and the specific design of each component, its special character difference that to be the method for design of described sludge treatment equipment be according to Of Heavy Metal Level In Sludge, by water ratio be 25-30% modified sewage sludge in add quantitative glucose powder after, under normal pressure and different temperature condition successively through 3 sludge treatment cylinders and at the uniform velocity rotate in its mechanical stirring in the process of propelling carry out heavy metal and dehydration denitrogenation processing, carbonizing treatment, fixed carbon burn processing three processing steps, mud after process meets pollutant catabolic gene standard in national agricultural sludge, and three waste products after sludge handling process neutralizing treatment, to environment non-secondary pollution, reach innoxious, the minimizing of mud and the processing requirements of resource utilization.
For solving above-mentioned technical problem further, the preferred version of technique scheme is:
Heavy metal described above and dehydration denitrogenation processing process are: according to the difference of Of Heavy Metal Level In Sludge, be that the modified sewage sludge of 25-30% is placed in heavy metal and the denitrogenation processing cylinder that dewaters together with the glucose powder of the 0.001-0.005% of its weight by water ratio, in normal pressure and cylinder, temperature is at the uniform velocity rotated in the process of propelling by mechanical stirring under the condition of 100-150 DEG C, water in mud and ammonia form the mixed gas of water and ammonia because making it volatilize by heat effect, and the heavy metal ion in mud is combined the complex compound generating ammonia, after glucose powder generation redox reaction in the complex compound of ammonia and mud, the valency of heavy metal ion reduces or is directly reduced to simple substance, realize the process of heavy metal process and dehydration denitrogenation processing, mud meets pollutant catabolic gene standard in national agricultural sludge after heavy metal process, in treating processes, the mixed gas of remaining water and ammonia enters through pipeline and reclaims cooling stocking system, for the preparation of volatile salt chemical fertilizer, its inflammable gas produced burns to roasting kiln through pipeline communication, for sludge treatment provides thermal source, the discharge port that mud after heavy metal and dehydration denitrogenation processing is arranged by heavy metal and dehydration denitrogenation processing cylinder end enters carbonizing treatment process.
Carbonizing treatment process described above is: the mud after heavy metal and dehydration denitrogenation processing is directly placed in the process that the inherent mechanical stirring of carbonizing treatment cylinder at the uniform velocity rotates propelling, mud temperature be 150-350 DEG C, fiber under condition of normal pressure in its mud is converted into fixed carbon, grease is converted into gas and enters roasting kiln burning, for sludge treatment provides thermal source through pipeline; Residue inflammable gas enters stocking system through pipeline, for combustion power generation; The discharge port that mud after carbonizing treatment is arranged by carbonizing treatment cylinder end enters fixed carbon burning process.
Fixed carbon burning process described above is: the mud after carbonizing treatment is directly placed in the process that the inherent mechanical stirring of fixed carbon burn processing cylinder at the uniform velocity rotates propelling, temperature be 350-450 DEG C, Thorough combustion under the condition of normal pressure, oxygen abundance, its heat produced is as the heat supplement of sludge handling process, and the recrement after fixed carbon burning is for can brickmaking or do building materials and use; Waste gas in burning process carries out passing through discharge of pipes after process reaches emission standard through pipeline communication fume treatment mechanism; The discharge port that mud after fixed carbon burn processing is arranged by fixed carbon burn processing cylinder end enters gas cleaning roller process process.
The method of design of sludge treatment cylinder described above adopts to comprise at least that coaxial package is integrated from the inside to the outside, spiral-line inside cylindrical shell arranges in opposite directions by heavy metal process cylinder, carbonization cylinder and fixed carbon burn that cylinder forms 3, and the sludge treatment cylinder that the spiral-tube that the barrel of spiral-line end is provided with discharge port is formed, its cylinder two ends respectively arrange the structure of a bracing or strutting arrangement.
For overcoming prior art Problems existing further, the technical scheme of sludge treatment equipment of the present invention is: a kind of sludge treatment equipment designed according to above-mentioned method of design, comprise support, sludge treatment cylinder, power-driven mechanism, delivery conduit and hood, its special character is that described sludge treatment equipment comprises at least by heavy metal process cylinder, carbonization cylinder and fixed carbon burning cylinder composition 3 from the inside to the outside coaxial package be integrated, spiral-line inside cylindrical shell is arranged in opposite directions, and the sludge treatment cylinder that the spiral-tube that the barrel of spiral-line end is provided with discharge port is formed, its cylinder two ends respectively arrange a bracing or strutting arrangement, the heavy metal process cylinder of described sludge treatment cylinder and carbonization cylinder are that misconstruction is arranged, barrel outside the bracing or strutting arrangement of heavy metal process cylinder dislocation extension sets gradually a power-driven mechanism and feeding device, its end arranges a gas output tube and cools stocking system with the recovery arranged and is connected, and the output terminal reclaiming cooling stocking system arranges pipeline communication to roasting kiln, the bracing or strutting arrangement outboard end of the carbonization cylinder dislocation extension draw by gas line be arranged in roasting kiln burner hearth that carbonization cylinder misplaces below extension, the upper side tube-wall of fixed carbon burning cylinder is established an exhanst gas outlet and is communicated with flue gas exit pipe after flue gas processing device and is provided with a discharge tube.
For solving above-mentioned technical problem further, the preferred version of technique scheme is:
The spiral-line of sludge treatment cylinder described above is arranged by several spiral-line monomer armors to be welded, and every two spiral-line monomers connected and cylindrical shell inner surface form a triangular-arc through hole; Triangle base slant range is 30-50 ㎜, leg-of-mutton high 50-70 ㎜; Described spiral-line monomer structure be upper and lower limit arc-shaped side with described cylindrical shell inner tube diameter circular arc with spiral-line is installed after the diameter circular arc of spiral-line conform to, the left and right limit of spiral-line monomer is triangular structure.
The outside of the fixed carbon burning cylinder in sludge treatment cylinder described above is provided with a gas cleaning cylinder in cavity structure connected as one with cylinder, the outside of its gas cleaning cylinder is provided with a hood, be provided with thermal insulation layer between hood and gas cleaning cylinder, outer side wall one end of gas cleaning cylinder arranges a recrement discharge port.
Power-driven mechanism described above is motor drive wheel box, and the double chain wheel on wheel box is connected with the double chain wheel on heavy metal process cartridge by pair of chain drive mechanism.
Feeding device described above comprises a material loading hopper, its blanking port is set to uncovered, mouth end is provided with the fixing sleeve being sleeved on heavy metal process cylinder outer surface, the cylindrical shell of heavy metal process cylinder is provided with at least one feeding mouth, forms the structure to heavy metal process drum cavity material loading when feeding mouth overlaps with blanking port.
The method of design of sludge treatment equipment of the present invention and device thereof compared with prior art have following outstanding substantive distinguishing features and significant progress:
The method of design of first sludge treatment equipment of the present invention takes to arrange heavy metal process cylinder, carbonization cylinder and fixed carbon burning cylinder, and by these 3 sludge treatment cylinders from the inside to the outside coaxial package be integrated, spiral-line inside cylindrical shell is arranged in opposite directions, its cylinder two ends respectively arrange a bracing or strutting arrangement, the technical scheme of a power-driven mechanism and feeding device is equipped with again in its one end, thus make sludge treatment equipment of the present invention design not only sludge treatment carried out dehydration denitrogenation by the sludge treatment cylinder arranged, heavy metal process, the processing step of carbonizing treatment and fixed carbon burn processing carries out harmless treatment, mud after making it process meets pollutant catabolic gene standard in the agricultural sludge of national requirements (referring to following subordinate list), can brickmaking or do building materials use, conscientiously sewage sludge harmlessness is reached, minimizing, stabilization, the processing requirements of resource utilization, and overcome the dust produced in sludge incineration treating processes in currently available technology, the secondary pollution that the source of pollution that dioxin etc. are new are formed, alleviate sludge yield and the delayed contradiction of sludge treatment ability, the halfway fatal technological deficiency of safe disposal, correct safe disposal is carried out to urban wastewater treatment firm mud, for alleviating sludge yield and the delayed contradiction of sludge treatment ability has played positive effect, thus make the method for design of sludge treatment equipment of the present invention be compared with prior art that one is new, technical scheme reliable, non-secondary pollution, efficiency of investment are high, the method for design of the sludge treatment equipment of instant effect, be that there is outstanding substantive distinguishing features and significant progress.
Two to be method of design of sludge treatment equipment of the present invention be by the mixed gas of heavy metal process and the dehydration remaining water of denitrogenation processing process and ammonia enters through pipeline and reclaim cooling stocking system, for the preparation of volatile salt chemical fertilizer for it; Again its remaining inflammable gas is burnt to roasting kiln through pipeline communication, for sludge treatment provides thermal source; And carbonizing treatment process grease is converted into gas and through pipeline enter roasting kiln burning, for sludge treatment provides thermal source; Residue inflammable gas can enter stocking system through pipeline, for the technical scheme of combustion power generation, the design of this technical scheme is not only sludge handling process solution thermal source and provides a kind of newly, reliable technical scheme, and provide reliable technical guarantee for the resource utilization of sludge treatment, reach and accomplished the important achievement of recycling treatment while realizing sewage sludge harmlessness process.For improving China's specific resistance to filtration state of the art further, the treatment technology of practical solution sewage sludge harmlessness, minimizing, stabilization, resource utilization provides new, a reliable technical scheme, this technical scheme by for the secondary pollution reduced and radical cure brings because of sludge treatment, improve environmental greening level and improve the living environment of our people, the offspring that benefits future generations has positive promoter action, thus makes the method for design of sludge treatment equipment of the present invention and device thereof compared with prior art have outstanding substantive distinguishing features and significant progressive.
Three to be sludge treatment equipments of the present invention be takes 3 sludge treatment cylinders that coaxial package is integrated from the inside to the outside, spiral-line inside cylindrical shell arranges in opposite directions for it, and the pipeline communication that heavy metal process cylinder is arranged is to roasting kiln; The end of the carbonization cylinder dislocation extension draw is by gas line and the technical scheme be arranged in roasting kiln burner hearth that carbonization cylinder misplaces below extension.This technical scheme not only makes the heat energy of sludge handling process obtain mutual supplementing and utilizing, and in mud self with reaction process extract combustiblesubstance carried out sufficient burning, make use of mud own resources to greatest extent, be sludge handling process and provide the energy, this is to those skilled in the art, and this is a breakthrough technical progress.This is not only sludge handling process and saves the energy, reduce the expense in sludge handling process, and be sludge treatment enterprise reduction sludge treatment cost, improve Business Economic Benefit and provide reliable technical guarantee, reach and accomplished the effect of recycling treatment while realizing sewage sludge harmlessness process.Thus make sludge treatment equipment of the present invention compared with prior art have outstanding substantive distinguishing features and significant progress.
Sludge treatment equipment of the present invention in implementation process after testing, after process, heavy metal content substantially all reaches lower than pollutant catabolic gene standard (GB4284-84) standard value in national standard agricultural sludge and city-building industry standard (CJ-T309-2009) to the required value of heavy metal content in the agricultural shale of urban wastewater treatment firm sludge disposal in recrement, and environmental monitoring station of Yantai City gathers as following table to the sludge heavy-metal content detection value after the process of application the technology of the present invention:
Note: A level mud allows to use crop: vegetables, food crop, oil crops, fruit tree, fodder crop, fibre crops; B level mud allows to use crop: oil crops, fruit tree, fodder crop, fibre crops, forbids using vegetables and food crop.
Two samples in table are respectively the modified mud that do not carry out heavy metal process and remaining after carbonization through heavy metal process
Recrement.In general, in mud, organic content can account for about 50% of total amount, and each heavy metal concentration after the process therefore provided in table in residual residue is equivalent to be doubled, and therefore actual numerical value all should reduce by 50% on former basis.From data, after heavy metal treatment systems process, the heavy metal content in mud obviously reduces, and meets the agricultural sludge heavy metal contaminants Con trolling index of national requirements
Accompanying drawing explanation
Included accompanying drawings provides a further understanding of the present invention, and it is incorporated in this specification sheets the part forming this specification sheets, and described accompanying drawing shows embodiments of the invention and is used from specification sheets one explains principle of the present invention.Reference numeral identical in the accompanying drawings represents identical parts.In the accompanying drawings:
Fig. 1 is the structural representation of a kind of sludge treatment equipment of the present invention.
Fig. 2 is the A-A sectional view of the sludge treatment cylinder of Fig. 1.
Fig. 3 is spiral-line monomer structure schematic diagram of the present invention.
Figure tag indicating: number 1 - stand 2-3-3.1 - power drive mechanism supporting device motor 3.2-3.3 double chain wheel transmission 4 - feeding hopper on 4.1-4.1 - blanking mouth tighten set of 5-4.3 - gas delivery pipe 6 - gas storage tank at the beginning of 7-7.1 - pipeline gas recycling cooling storage tanks eight heavy metal treatment 8.1 heavy metal drum drum helical 8.2.1-8.2 - helix monomer arc edge 8.2.2 - next above 8.2.3 - on the left side of the curved side 8.2.4-8.3 triangle curved hole is on the right side roller discharging mouth 8.5 8.4 - heavy metal treatmentInto the mouth of 9-9.1-9.1 carbide carbide roller cylinder helix spiral monomer 9.2.1 - arc edge 9.2.2 - next above 9.2.3 - on the left side of the curved side 9.2.4 - on the right side - triangle curved hole is 9.4-9.3 carbide roller discharging mouth 10 - fixed carbon combustion cylinder fixed carbon combustion cylinder helix 10.2-10.1 - helix monomer 10.2.1 - arc edge 10.2.2 - next above 10.2.3 - on the left side of the curved side 10.2.4-10.3 triangle curved hole is on the right side fixed carbon combustion cylinder discharging mouth 10.5-10.4 - flue gas outlet 11-11.1 residue discharging mouth drum of flue gas purification 12-13 - hood insulation layer 14-15 to 16 flue gas treatment plant flue gas output tube - 17 - carbide flue gas discharge tube roller output shrink tubing 18 to 19 - furnace gas delivery pipe 20 - rotating speed adjustment mechanism.
Embodiment
Describe the method for design of a kind of sludge treatment equipment of the present invention and the specific structural details of device thereof in detail below in conjunction with accompanying drawing and install and use process, the limiting to the claimed invention gone up in all senses must not be interpreted as.
Embodiment 1:
The method of design of a kind of sludge treatment equipment of the embodiment of the present invention 1, comprise support, sludge treatment cylinder, power-driven mechanism, delivery conduit, the global design of hood and the specific design of each component, its special character difference that to be the method for design of described sludge treatment equipment be according to Of Heavy Metal Level In Sludge, by water ratio be 25-30% modified sewage sludge in add quantitative glucose powder after, under normal pressure and different temperature condition successively through 3 sludge treatment cylinders and at the uniform velocity rotate in its mechanical stirring in the process of propelling carry out heavy metal and dehydration denitrogenation processing, carbonizing treatment, fixed carbon burn processing three processing steps, mud after process meets pollutant catabolic gene standard in national agricultural sludge, and three waste products after sludge handling process neutralizing treatment, to environment non-secondary pollution, reach innoxious, the minimizing of mud and the processing requirements of resource utilization.
Heavy metal described above and dehydration denitrogenation processing process are: according to the difference of Of Heavy Metal Level In Sludge, be that the modified sewage sludge of 25-30% is placed in heavy metal and the denitrogenation processing cylinder that dewaters together with the glucose powder of the 0.001-0.005% of its weight by water ratio, in normal pressure and cylinder, temperature is at the uniform velocity rotated in the process of propelling by mechanical stirring under the condition of 100-150 DEG C, water in mud and ammonia form the mixed gas of water and ammonia because making it volatilize by heat effect, and the heavy metal ion in mud is combined the complex compound generating ammonia, after glucose powder generation redox reaction in the complex compound of ammonia and mud, the valency of heavy metal ion reduces or is directly reduced to simple substance, realize the process of heavy metal process and dehydration denitrogenation processing, the agricultural sludge that mud meets national Specification after heavy metal process returns field standard, in treating processes, the mixed gas of remaining water and ammonia enters through pipeline and reclaims cooling stocking system, for the preparation of volatile salt chemical fertilizer, its inflammable gas produced burns to roasting kiln through pipeline communication, for sludge treatment provides thermal source, the discharge port that mud after heavy metal and dehydration denitrogenation processing is arranged by heavy metal and dehydration denitrogenation processing cylinder end enters carbonizing treatment process.
Carbonizing treatment process described above is: the mud after heavy metal and dehydration denitrogenation processing is directly placed in the process that the inherent mechanical stirring of carbonizing treatment cylinder at the uniform velocity rotates propelling, mud temperature be 150-350 DEG C, fiber under condition of normal pressure in its mud is converted into fixed carbon, grease is converted into gas and enters roasting kiln burning, for sludge treatment provides thermal source through pipeline; Residue inflammable gas enters stocking system through pipeline, for combustion power generation; The discharge port that mud after carbonizing treatment is arranged by carbonizing treatment cylinder end enters fixed carbon burning process.
Fixed carbon burning process described above is: the mud after carbonizing treatment is directly placed in the process that the inherent mechanical stirring of fixed carbon burn processing cylinder at the uniform velocity rotates propelling, temperature be 350-450 DEG C, Thorough combustion under the condition of normal pressure, oxygen abundance, its heat produced is as the heat supplement of sludge handling process, and the recrement after fixed carbon burning is for can brickmaking or do building materials and use; Waste gas in burning process carries out passing through discharge of pipes after process reaches emission standard through pipeline communication fume treatment mechanism; The discharge port that mud after fixed carbon burn processing is arranged by fixed carbon burn processing cylinder end enters gas cleaning roller process process.
The method of design of sludge treatment cylinder described above adopts to comprise at least that coaxial package is integrated from the inside to the outside, spiral-line inside cylindrical shell arranges in opposite directions by heavy metal process cylinder, carbonization cylinder and fixed carbon burn that cylinder forms 3, and the sludge treatment cylinder that the spiral-tube that the barrel of spiral-line end is provided with discharge port is formed, its cylinder two ends respectively arrange the structure of a bracing or strutting arrangement.
The sludge treatment equipment designed according to above-mentioned method of design is (see Fig. 1, Fig. 2, Fig. 3), comprise support 1, sludge treatment cylinder 8, 9, 10, 11, power-driven mechanism 3, delivery conduit 5, 14, 18 and hood 12, sludge treatment equipment described in it comprises by heavy metal process cylinder 8, carbonization cylinder 9 and fixed carbon burning cylinder 10 form 3 from the inside to the outside coaxial package be integrated, a spiral-line 8.1 inside cylindrical shell, 9.1, 10.1 arrange in opposite directions, and spiral-line 8.1, 9.1, the barrel of 10.1 ends is provided with discharge port 8.4, 9.4, the sludge treatment cylinder that the spiral-tube of 10.4 is formed, its cylinder two ends respectively arrange a bracing or strutting arrangement 2, the heavy metal process cylinder 8 of described sludge treatment cylinder is arranged in misconstruction with carbonization cylinder 9, heavy metal process cylinder 8 misplace extension bracing or strutting arrangement 2 outside barrel on set gradually a power-driven mechanism 3 and feeding device 4, its end one gas output tube 5 is set and with deposit tank 6 at the beginning of the gas arranged and cool hold-up vessel 7 with gas recovery and be connected, the output terminal that gas recovery cools hold-up vessel 7 arranges pipeline 7.1 and is communicated to roasting kiln 19, carbonization cylinder 9 misplace the extension draw 17 bracing or strutting arrangement 2 outboard end by combustion gas output tube 18 be arranged in roasting kiln 19 burner hearth that carbonization cylinder 9 misplaces below extension, the upper side tube-wall of fixed carbon burning cylinder 10 establishes an exhanst gas outlet 10.5 and communicates with the flue gas exit pipe 14 that gas cleaning cylinder 11 is arranged, flue gas exit pipe 14 connects with flue gas processing device 15, is provided with a discharge tube 16 after flue gas processing device 15.
Sludge treatment cylinder described above is made up of heavy metal process cylinder 8, carbonization cylinder 9 and fixed carbon burning cylinder 10, their spiral-line 8.1,9.1,10.1 is that in armor, arrangement is welded by several spiral-line monomers 8.2,9.2,10.2, and every two spiral-line monomers connected 8.2,9.2,10.2 and cylindrical shell inner surface form a triangular-arc through hole 8.3,9.3,10.3; Triangle base slant range is 30-35 ㎜, leg-of-mutton high 50-55 ㎜; Described spiral-line monomer 8.2,9.2,10.2 structure is top arc-shaped side 8.2.1,9.2.1,10.2.1, below arc-shaped side 8.2.2,9.2.2,10.2.2 and described cylindrical shell inner tube diameter circular arc with spiral-line is installed after the diameter circular arc of spiral-line conform to, limit, the left side 8.2.3 of spiral-line monomer 8.2,9.2,10.2,9.2.3,10.2.3, right edge 8.2.4,9.2.4,10.2.4 are triangular structure.
The outside of the fixed carbon burning cylinder 10 in sludge treatment cylinder described above is provided with a gas cleaning cylinder 11 in cavity structure connected as one with cylinder, the outside of its gas cleaning cylinder 11 is provided with a hood 12, be provided with thermal insulation layer 13 between hood 12 and gas cleaning cylinder 11, outer side wall one end of gas cleaning cylinder 11 arranges a recrement discharge port 11.1.
Power-driven mechanism 2 described above drives wheel box 3.2 for electric motor 3.1, and the double chain wheel 3.3 on wheel box 3.2 is connected with the double chain wheel on heavy metal process cylinder 8 by pair of chain drive mechanism; Described power-driven mechanism is provided with a housing and velocity of rotation adjustment mechanism 20.
Feeding device 4 described above comprises a material loading hopper 4.1, its blanking port 4.2 is set to uncovered, mouth end is provided with the fixing sleeve 4.3 being sleeved on heavy metal process cylinder 8 outer surface, the cylindrical shell of heavy metal process cylinder 8 is provided with at least one feeding mouth 8.5, forms to heavy metal process cylinder 8 inner chamber material loading when feeding mouth 8.5 overlaps with blanking port 4.2.
Be more than the method for design of a kind of sludge treatment equipment of the embodiment of the present invention 1 and a static structure of device thereof.
Embodiment 2:
The method of design of a kind of sludge treatment equipment of the embodiment of the present invention 2, comprise support, sludge treatment cylinder, power-driven mechanism, delivery conduit, the global design of hood and the specific design of each component, its special character difference that to be the method for design of described sludge treatment equipment be according to Of Heavy Metal Level In Sludge, by water ratio be 25-30% modified sewage sludge in add quantitative glucose powder after, under normal pressure and different temperature condition successively through 3 sludge treatment cylinders and at the uniform velocity rotate in its mechanical stirring in the process of propelling carry out heavy metal and dehydration denitrogenation processing, carbonizing treatment, fixed carbon burn processing three processing steps, mud after process meets pollutant catabolic gene standard in national agricultural sludge, and three waste products after sludge handling process neutralizing treatment, to environment non-secondary pollution, reach innoxious, the minimizing of mud and the processing requirements of resource utilization.
Heavy metal described above and dehydration denitrogenation processing process are: according to the difference of Of Heavy Metal Level In Sludge, be that the modified sewage sludge of 25-30% is placed in heavy metal and the denitrogenation processing cylinder that dewaters together with the glucose powder of the 0.001-0.005% of its weight by water ratio, in normal pressure and cylinder, temperature is at the uniform velocity rotated in the process of propelling by mechanical stirring under the condition of 100-150 DEG C, water in mud and ammonia form the mixed gas of water and ammonia because making it volatilize by heat effect, and the heavy metal ion in mud is combined the complex compound generating ammonia, after glucose powder generation redox reaction in the complex compound of ammonia and mud, the valency of heavy metal ion reduces or is directly reduced to simple substance, realize the process of heavy metal process and dehydration denitrogenation processing, the agricultural sludge that mud meets national Specification after heavy metal process returns field standard, in treating processes, the mixed gas of remaining water and ammonia enters through pipeline and reclaims cooling stocking system, for the preparation of volatile salt chemical fertilizer, its inflammable gas produced burns to roasting kiln through pipeline communication, for sludge treatment provides thermal source, the discharge port that mud after heavy metal and dehydration denitrogenation processing is arranged by heavy metal and dehydration denitrogenation processing cylinder end enters carbonizing treatment process.
Carbonizing treatment process described above is: the mud after heavy metal and dehydration denitrogenation processing is directly placed in the process that the inherent mechanical stirring of carbonizing treatment cylinder at the uniform velocity rotates propelling, mud temperature be 150-350 DEG C, fiber under condition of normal pressure in its mud is converted into fixed carbon, grease is converted into gas and enters roasting kiln burning, for sludge treatment provides thermal source through pipeline; Residue inflammable gas enters stocking system through pipeline, for combustion power generation; The discharge port that mud after carbonizing treatment is arranged by carbonizing treatment cylinder end enters fixed carbon burning process.
Fixed carbon burning process described above is: the mud after carbonizing treatment is directly placed in the process that the inherent mechanical stirring of fixed carbon burn processing cylinder at the uniform velocity rotates propelling, temperature be 350-450 DEG C, Thorough combustion under the condition of normal pressure, oxygen abundance, its heat produced is as the heat supplement of sludge handling process, and the recrement after fixed carbon burning is for can brickmaking or do building materials and use; Waste gas in burning process carries out passing through discharge of pipes after process reaches emission standard through pipeline communication fume treatment mechanism; The discharge port that mud after fixed carbon burn processing is arranged by fixed carbon burn processing cylinder end enters gas cleaning roller process process.
The method of design of sludge treatment cylinder described above adopts to comprise at least that coaxial package is integrated from the inside to the outside, spiral-line inside cylindrical shell arranges in opposite directions by heavy metal process cylinder, carbonization cylinder and fixed carbon burn that cylinder forms 3, and the sludge treatment cylinder that the spiral-tube that the barrel of spiral-line end is provided with discharge port is formed, its cylinder two ends respectively arrange the structure of a bracing or strutting arrangement.
The sludge treatment equipment designed according to above-mentioned method of design is (see Fig. 1, Fig. 2, Fig. 3), comprise support 1, sludge treatment cylinder 8, 9, 10, 11, power-driven mechanism 3, delivery conduit 5, 14, 18 and hood 12, sludge treatment equipment described in it comprises by heavy metal process cylinder 8, carbonization cylinder 9 and fixed carbon burning cylinder 10 form 3 from the inside to the outside coaxial package be integrated, spiral-line 8.1 inside cylindrical shell, 9.1, 10.1 arrange in opposite directions, and spiral-line 8.1, 9.1, the barrel of 10.1 ends is provided with discharge port 8.4, 9.4, the sludge treatment cylinder that the spiral-tube of 10.4 is formed, its cylinder two ends respectively arrange a bracing or strutting arrangement 2, the heavy metal process cylinder 8 of described sludge treatment cylinder is arranged in misconstruction with carbonization cylinder 9, heavy metal process cylinder 8 misplace extension bracing or strutting arrangement 2 outside barrel on set gradually a power-driven mechanism 3 and feeding device 4, its end one gas output tube 5 is set and with deposit tank 6 at the beginning of the gas arranged and cool hold-up vessel 7 with gas recovery and be connected, the output terminal that gas recovery cools hold-up vessel 7 arranges pipeline 7.1 and is communicated to roasting kiln 19, carbonization cylinder 9 misplace the extension draw 17 bracing or strutting arrangement 2 outboard end by combustion gas output tube 18 be arranged in roasting kiln 19 burner hearth that carbonization cylinder 9 misplaces below extension, the upper side tube-wall of fixed carbon burning cylinder 10 establishes an exhanst gas outlet 10.5 and communicates with the flue gas exit pipe 14 that gas cleaning cylinder 11 is arranged, flue gas exit pipe 14 connects with flue gas processing device 15, is provided with a discharge tube 16 after flue gas processing device 15.
Sludge treatment cylinder described above is made up of heavy metal process cylinder 8, carbonization cylinder 9 and fixed carbon burning cylinder 10, their spiral-line 8.1,9.1,10.1 is that in armor, arrangement is welded by several spiral-line monomers 8.2,9.2,10.2, and every two spiral-line monomers connected 8.2,9.2,10.2 and cylindrical shell inner surface form a triangular-arc through hole 8.3,9.3,10.3; Triangle base slant range is 35-40 ㎜, leg-of-mutton high 55-60 ㎜; Described spiral-line monomer 8.2,9.2,10.2 structure is top arc-shaped side 8.2.1,9.2.1,10.2.1, below arc-shaped side 8.2.2,9.2.2,10.2.2 and described cylindrical shell inner tube diameter circular arc with spiral-line is installed after the diameter circular arc of spiral-line conform to, limit, the left side 8.2.3 of spiral-line monomer 8.2,9.2,10.2,9.2.3,10.2.3, right edge 8.2.4,9.2.4,10.2.4 are triangular structure.
The outside of the fixed carbon burning cylinder 10 in sludge treatment cylinder described above is provided with a gas cleaning cylinder 11 in cavity structure connected as one with cylinder, the outside of its gas cleaning cylinder 11 is provided with a hood 12, be provided with thermal insulation layer 13 between hood 12 and gas cleaning cylinder 11, outer side wall one end of gas cleaning cylinder 11 arranges a recrement discharge port 11.1.
Power-driven mechanism 2 described above drives wheel box 3.2 for electric motor 3.1, and the double chain wheel 3.3 on wheel box 3.2 is connected with the double chain wheel on heavy metal process cartridge 8 by pair of chain drive mechanism; Described power-driven mechanism is provided with a housing and velocity of rotation adjustment mechanism 20.
Feeding device 4 described above comprises a material loading hopper 4.1, its blanking port 4.2 is set to uncovered, mouth end is provided with the fixing sleeve 4.3 being sleeved on heavy metal process cylinder 8 outer surface, the cylindrical shell of heavy metal process cylinder 8 is provided with at least one feeding mouth 8.5, forms to heavy metal process cylinder 8 inner chamber material loading when feeding mouth 8.5 overlaps with blanking port 4.2.
Be more than the method for design of a kind of sludge treatment equipment of the embodiment of the present invention 2 and a static structure of device thereof.
Embodiment 3:
The method of design of a kind of sludge treatment equipment of the embodiment of the present invention 3, comprise support, sludge treatment cylinder, power-driven mechanism, delivery conduit, the global design of hood and the specific design of each component, its special character difference that to be the method for design of described sludge treatment equipment be according to Of Heavy Metal Level In Sludge, by water ratio be 25-30% modified sewage sludge in add quantitative glucose powder after, under normal pressure and different temperature condition successively through 3 sludge treatment cylinders and at the uniform velocity rotate in its mechanical stirring in the process of propelling carry out heavy metal and dehydration denitrogenation processing, carbonizing treatment, fixed carbon burn processing three processing steps, the agricultural sludge that mud after process meets national Specification returns field standard, and three waste products after sludge handling process neutralizing treatment, to environment non-secondary pollution, reach innoxious, the minimizing of mud and the processing requirements of resource utilization.
Heavy metal described above and dehydration denitrogenation processing process are: according to the difference of Of Heavy Metal Level In Sludge, be that the modified sewage sludge of 25-30% is placed in heavy metal and the denitrogenation processing cylinder that dewaters together with the glucose powder of the 0.001-0.005% of its weight by water ratio, in normal pressure and cylinder, temperature is at the uniform velocity rotated in the process of propelling by mechanical stirring under the condition of 100-150 DEG C, water in mud and ammonia form the mixed gas of water and ammonia because making it volatilize by heat effect, and the heavy metal ion in mud is combined the complex compound generating ammonia, after glucose powder generation redox reaction in the complex compound of ammonia and mud, the valency of heavy metal ion reduces or is directly reduced to simple substance, realize the process of heavy metal process and dehydration denitrogenation processing, mud meets pollutant catabolic gene standard in national agricultural sludge after heavy metal process, in treating processes, the mixed gas of remaining water and ammonia enters through pipeline and reclaims cooling stocking system, for the preparation of volatile salt chemical fertilizer, its inflammable gas produced burns to roasting kiln through pipeline communication, for sludge treatment provides thermal source, the discharge port that mud after heavy metal and dehydration denitrogenation processing is arranged by heavy metal and dehydration denitrogenation processing cylinder end enters carbonizing treatment process.
Carbonizing treatment process described above is: the mud after heavy metal and dehydration denitrogenation processing is directly placed in the process that the inherent mechanical stirring of carbonizing treatment cylinder at the uniform velocity rotates propelling, mud temperature be 150-350 DEG C, fiber under condition of normal pressure in its mud is converted into fixed carbon, grease is converted into gas and enters roasting kiln burning, for sludge treatment provides thermal source through pipeline; Residue inflammable gas enters stocking system through pipeline, for combustion power generation; The discharge port that mud after carbonizing treatment is arranged by carbonizing treatment cylinder end enters fixed carbon burning process.
Fixed carbon burning process described above is: the mud after carbonizing treatment is directly placed in the process that the inherent mechanical stirring of fixed carbon burn processing cylinder at the uniform velocity rotates propelling, temperature be 350-450 DEG C, Thorough combustion under the condition of normal pressure, oxygen abundance, its heat produced is as the heat supplement of sludge handling process, and the recrement after fixed carbon burning is for can brickmaking or do building materials and use; Waste gas in burning process carries out passing through discharge of pipes after process reaches emission standard through pipeline communication fume treatment mechanism; The discharge port that mud after fixed carbon burn processing is arranged by fixed carbon burn processing cylinder end enters gas cleaning roller process process.
The method of design of sludge treatment cylinder described above adopts to comprise at least that coaxial package is integrated from the inside to the outside, spiral-line inside cylindrical shell arranges in opposite directions by heavy metal process cylinder, carbonization cylinder and fixed carbon burn that cylinder forms 3, and the sludge treatment cylinder that the spiral-tube that the barrel of spiral-line end is provided with discharge port is formed, its cylinder two ends respectively arrange the structure of a bracing or strutting arrangement.
The sludge treatment equipment designed according to above-mentioned method of design is (see Fig. 1, Fig. 2, Fig. 3), comprise support 1, sludge treatment cylinder 8, 9, 10, 11, power-driven mechanism 3, delivery conduit 5, 14, 18 and hood 12, sludge treatment equipment described in it comprises by heavy metal process cylinder 8, carbonization cylinder 9 and fixed carbon burning cylinder 10 form 3 from the inside to the outside coaxial package be integrated, spiral-line 8.1 inside cylindrical shell, 9.1, 10.1 arrange in opposite directions, and spiral-line 8.1, 9.1, the barrel of 10.1 ends is provided with discharge port 8.4, 9.4, the sludge treatment cylinder that the spiral-tube of 10.4 is formed, its cylinder two ends respectively arrange a bracing or strutting arrangement 2, the heavy metal process cylinder 8 of described sludge treatment cylinder is arranged in misconstruction with carbonization cylinder 9, heavy metal process cylinder 8 misplace extension bracing or strutting arrangement 2 outside barrel on set gradually a power-driven mechanism 3 and feeding device 4, its end one gas output tube 5 is set and with deposit tank 6 at the beginning of the gas arranged and cool hold-up vessel 7 with gas recovery and be connected, the output terminal that gas recovery cools hold-up vessel 7 arranges pipeline 7.1 and is communicated to roasting kiln 19, carbonization cylinder 9 misplace the extension draw 17 bracing or strutting arrangement 2 outboard end by combustion gas output tube 18 be arranged in roasting kiln 19 burner hearth that carbonization cylinder 9 misplaces below extension, the upper side tube-wall of fixed carbon burning cylinder 10 establishes an exhanst gas outlet 10.5 and communicates with the flue gas exit pipe 14 that gas cleaning cylinder 11 is arranged, flue gas exit pipe 14 connects with flue gas processing device 15, is provided with a discharge tube 16 after flue gas processing device 15.
Sludge treatment cylinder described above is made up of heavy metal process cylinder 8, carbonization cylinder 9 and fixed carbon burning cylinder 10, their spiral-line 8.1,9.1,10.1 is that in armor, arrangement is welded by several spiral-line monomers 8.2,9.2,10.2, and every two spiral-line monomers connected 8.2,9.2,10.2 and cylindrical shell inner surface form a triangular-arc through hole 8.3,9.3,10.3; Triangle base slant range is 45-50 ㎜, leg-of-mutton high 65-70 ㎜; Described spiral-line monomer 8.2,9.2,10.2 structure is top arc-shaped side 8.2.1,9.2.1,10.2.1, below arc-shaped side 8.2.2,9.2.2,10.2.2 and described cylindrical shell inner tube diameter circular arc with spiral-line is installed after the diameter circular arc of spiral-line conform to, limit, the left side 8.2.3 of spiral-line monomer 8.2,9.2,10.2,9.2.3,10.2.3, right edge 8.2.4,9.2.4,10.2.4 are triangular structure.
The outside of the fixed carbon burning cylinder 10 in sludge treatment cylinder described above is provided with a gas cleaning cylinder 11 in cavity structure connected as one with cylinder, the outside of its gas cleaning cylinder 11 is provided with a hood 12, be provided with thermal insulation layer 13 between hood 12 and gas cleaning cylinder 11, outer side wall one end of gas cleaning cylinder 11 arranges a recrement discharge port 11.1.
Power-driven mechanism 2 described above drives wheel box 3.2 for electric motor 3.1, and the double chain wheel 3.3 on wheel box 3.2 is connected with the double chain wheel on heavy metal process cartridge 8 by pair of chain drive mechanism; Described power-driven mechanism is provided with a housing and velocity of rotation adjustment mechanism 20.
Feeding device 4 described above comprises a material loading hopper 4.1, its blanking port 4.2 is set to uncovered, mouth end is provided with the fixing sleeve 4.3 being sleeved on heavy metal process cylinder 8 outer surface, the cylindrical shell of heavy metal process cylinder 8 is provided with at least one feeding mouth 8.5, forms to heavy metal process cylinder 8 inner chamber material loading when feeding mouth 8.5 overlaps with blanking port 4.2.
Be more than the method for design of a kind of sludge treatment equipment of the embodiment of the present invention 3 and a static structure of device thereof.
Claims (10)
1. the method for design of a sludge treatment equipment, comprise support, sludge treatment cylinder, power-driven mechanism, delivery conduit, the global design of hood and the specific design of each component, it is characterized in that the method for design of described sludge treatment equipment is the difference according to Of Heavy Metal Level In Sludge, by water ratio be 25-30% modified sewage sludge in add quantitative glucose powder after, under normal pressure and different temperature condition successively through 3 sludge treatment cylinders and at the uniform velocity rotate in its mechanical stirring in the process of propelling carry out heavy metal and dehydration denitrogenation processing, carbonizing treatment, fixed carbon burn processing three processing steps, mud after process meets pollutant catabolic gene standard in national agricultural sludge, and three waste products after sludge handling process neutralizing treatment, to environment non-secondary pollution, reach innoxious, the minimizing of mud and the processing requirements of resource utilization.
2. the method for design of sludge treatment equipment according to claim 1, it is characterized in that described heavy metal and dehydration denitrogenation processing process are: according to the difference of Of Heavy Metal Level In Sludge, be that the modified sewage sludge of 25-30% is placed in heavy metal and the denitrogenation processing cylinder that dewaters together with the glucose powder of the 0.001-0.005% of its weight by water ratio, in normal pressure and cylinder, temperature is at the uniform velocity rotated in the process of propelling by mechanical stirring under the condition of 100-150 DEG C, water in mud and ammonia form the mixed gas of water and ammonia because making it volatilize by heat effect, and the heavy metal ion in mud is combined the complex compound generating ammonia, after glucose powder generation redox reaction in the complex compound of ammonia and mud, the valency of heavy metal ion reduces or is directly reduced to simple substance, realize the process of heavy metal process and dehydration denitrogenation processing, mud meets pollutant catabolic gene standard in national agricultural sludge after heavy metal process, in treating processes, the mixed gas of remaining water and ammonia enters through pipeline and reclaims cooling stocking system, for the preparation of volatile salt chemical fertilizer, its inflammable gas produced burns to roasting kiln through pipeline communication, for sludge treatment provides thermal source, the discharge port that mud after heavy metal and dehydration denitrogenation processing is arranged by heavy metal and dehydration denitrogenation processing cylinder end enters carbonizing treatment process.
3. the method for design of sludge treatment equipment according to claim 1 or 2, it is characterized in that described carbonizing treatment process is: the mud after heavy metal and dehydration denitrogenation processing is directly placed in the process that the inherent mechanical stirring of carbonizing treatment cylinder at the uniform velocity rotates propelling, mud temperature be 150-350 DEG C, fiber under condition of normal pressure in its mud is converted into fixed carbon, grease is converted into gas and enters roasting kiln burning, for sludge treatment provides thermal source through pipeline; Residue inflammable gas enters stocking system through pipeline, for combustion power generation; The discharge port that mud after carbonizing treatment is arranged by carbonizing treatment cylinder end enters fixed carbon burning process.
4. the method for design of sludge treatment equipment according to claim 1 or 2, it is characterized in that described fixed carbon burning process is: the mud after carbonizing treatment is directly placed in the process that the inherent mechanical stirring of fixed carbon burn processing cylinder at the uniform velocity rotates propelling, temperature be 350-450 DEG C, Thorough combustion under the condition of normal pressure, oxygen abundance, its heat produced is as the heat supplement of sludge handling process, and the recrement after fixed carbon burning is for can brickmaking or do building materials and use; Waste gas in burning process carries out passing through discharge of pipes after process reaches emission standard through pipeline communication fume treatment mechanism; The discharge port that mud after fixed carbon burn processing is arranged by fixed carbon burn processing cylinder end enters gas cleaning roller process process.
5. the method for design of sludge treatment equipment according to claim 1 or 2, it is characterized in that the method for design of described sludge treatment cylinder adopts to comprise at least to be burnt by heavy metal process cylinder, carbonization cylinder and fixed carbon that coaxial package is integrated cylinder form 3 from the inside to the outside, spiral-line inside cylindrical shell arranges in opposite directions, and the sludge treatment cylinder that the spiral-tube that the barrel of spiral-line end is provided with discharge port is formed, its cylinder two ends respectively arrange the structure of a bracing or strutting arrangement.
6. the sludge treatment equipment of the design of the method for design according to sludge treatment equipment according to claim 1, comprise support, sludge treatment cylinder, power-driven mechanism, delivery conduit and hood, it is characterized in that described sludge treatment equipment comprises and at least burnt by heavy metal process cylinder, carbonization cylinder and fixed carbon that coaxial package is integrated cylinder form 3 from the inside to the outside, spiral-line inside cylindrical shell arranges in opposite directions, and the sludge treatment cylinder that the spiral-tube that the barrel of spiral-line end is provided with discharge port is formed, its cylinder two ends respectively arrange a bracing or strutting arrangement; The heavy metal process cylinder of described sludge treatment cylinder and carbonization cylinder are that misconstruction is arranged, barrel outside the bracing or strutting arrangement of heavy metal process cylinder dislocation extension sets gradually a power-driven mechanism and feeding device, its end arranges a gas output tube and cools stocking system with the recovery arranged and is connected, and the output terminal reclaiming cooling stocking system arranges pipeline communication to roasting kiln; The bracing or strutting arrangement outboard end of the carbonization cylinder dislocation extension draw by gas line be arranged in roasting kiln burner hearth that carbonization cylinder misplaces below extension; The upper side tube-wall of fixed carbon burning cylinder is established an exhanst gas outlet and is communicated with flue gas exit pipe after flue gas processing device and is provided with a discharge tube.
7. sludge treatment equipment according to claim 6, it is characterized in that the spiral-line of described sludge treatment cylinder is arranged by several spiral-line monomer armors to be welded, and every two spiral-line monomers connected and cylindrical shell inner surface form a triangular-arc through hole; Triangle base slant range is 30-50 ㎜, leg-of-mutton high 50-70 ㎜; Described spiral-line monomer structure be upper and lower limit arc-shaped side with described cylindrical shell inner tube diameter circular arc with spiral-line is installed after the diameter circular arc of spiral-line conform to, the left and right limit of spiral-line monomer is triangular structure.
8. the sludge treatment equipment according to claim 6 or 7, it is characterized in that outside that described sludge treatment cylinder is also included in fixed carbon burning cylinder be provided with one with cylinder connect as one in the gas cleaning cylinder of cavity structure, the outside of its gas cleaning cylinder is provided with a hood, be provided with thermal insulation layer between hood and gas cleaning cylinder, outer side wall one end of gas cleaning cylinder arranges a recrement discharge port.
9. the sludge treatment equipment according to claim 6 or 7, it is characterized in that described power-driven mechanism is motor drive wheel box, the double chain wheel on wheel box is connected with the double chain wheel on heavy metal process cartridge by pair of chain drive mechanism.
10. the sludge treatment equipment according to claim 6 or 7, it is characterized in that described feeding device comprises a material loading hopper, its blanking port is set to uncovered, mouth end is provided with the fixing sleeve being sleeved on heavy metal process cylinder outer surface, the cylindrical shell of heavy metal process cylinder is provided with at least one feeding mouth, forms the structure to heavy metal process drum cavity material loading when feeding mouth overlaps with blanking port.
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JP2003010877A (en) * | 2001-06-29 | 2003-01-14 | Kurita Water Ind Ltd | Activated sludge treatment method for sewage and its apparatus |
JP2009125636A (en) * | 2007-11-21 | 2009-06-11 | Torasuto Kikaku Kk | Sludge treatment method |
CN103087779A (en) * | 2011-11-04 | 2013-05-08 | 考克利尔维修工程 | Method for recycling valuable by-product by pyrolysis treatment of organic residue and inorganic residue in multihearth |
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