CN110746082A - Integrated sludge drying and carbonizing device - Google Patents
Integrated sludge drying and carbonizing device Download PDFInfo
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- CN110746082A CN110746082A CN201911192793.0A CN201911192793A CN110746082A CN 110746082 A CN110746082 A CN 110746082A CN 201911192793 A CN201911192793 A CN 201911192793A CN 110746082 A CN110746082 A CN 110746082A
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- C—CHEMISTRY; METALLURGY
- 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
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/13—Treatment of sludge; Devices therefor by de-watering, drying or thickening by heating
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- C—CHEMISTRY; METALLURGY
- 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
- C02F11/10—Treatment of sludge; Devices therefor by pyrolysis
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B47/00—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion
- C10B47/02—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion with stationary charge
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
- C10B57/02—Multi-step carbonising or coking processes
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
- C10B57/08—Non-mechanical pretreatment of the charge, e.g. desulfurization
- C10B57/10—Drying
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/06—Sludge reduction, e.g. by lysis
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- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- Treatment Of Sludge (AREA)
Abstract
The invention relates to an integrated sludge drying and carbonizing device, belonging to the technical field of sludge treatment in the aspect of environmental protection; the device comprises a feeding assembly, a furnace body assembly, a transmission assembly, a gas assembly, a feeding assembly, an air distribution assembly and a burner assembly, wherein the feeding assembly is positioned at the upper part of the furnace body assembly and penetrates through a furnace body, and comprises 2-15 rows of feeding mechanisms, each row of feeding mechanism comprises 3-15 layers of conveying pipes, one end of one conveying pipe is an inlet, the other end of the one conveying pipe is an outlet, and the outlet of the upper layer of conveying pipe is connected with the inlet of the lower layer of conveying pipe through a connecting pipe; the inlet of the conveying material pipe positioned at the topmost layer is a feeding hole, the feeding hole is communicated with the feeding assembly, and the outlet of the conveying material pipe positioned at the bottommost layer is a discharging hole; according to the integrated sludge drying and carbonizing device, the sludge is indirectly heated from top to bottom in a layered manner to complete drying and carbonizing, and the device is efficient, energy-saving and low in pollution.
Description
Technical Field
The invention relates to an integrated sludge drying and carbonizing device, and belongs to the technical field of sludge treatment in the aspect of environmental protection.
Background
Sludge is a heterogeneous body composed of organic debris, bacterial bodies, inorganic particles, colloids and the like. It is difficult to perform thorough solid-liquid separation by settling. The sludge produced by sewage treatment is typical organic sludge and has the characteristics of high organic matter content (60-80%), fine particles (0.02-0.2 mm) and small density (1002-1006 Kg/m)3) The sludge is of a colloid structure, is hydrophilic sludge, is easy to convey by a pipeline, and has poor dehydration performance. As the water content of the sludge decreases, the process of the sludge flowing from a pure liquid state to a viscous, plastic, semi-dry solid state to a pure solid state changes. Concentration can reduce the water content to 85% (water-containing state); when the water content is 70-75%, the sludge is in a soft state and is not easy to flow; generally, the water content under dehydration can only be reduced to 60-65%, and the water becomes almost solid at the moment; when the water content is lower than 35-40%, the mixture is in a gathering state (above is in a semi-drying state); further, when the content is as low as 10 to 15%, the powder is formed.
Sludge is an unavoidable byproduct in the sewage treatment process, and generally contains pathogenic microorganisms, parasitic ova, harmful heavy metals and a large amount of difficultly-degradable substances. If the treatment is not thorough, secondary pollution to the environment is easily caused. The proportion of COD (chemical oxygen demand) transferred into the sludge from the sewage is about 30-50%, the proportion of nitrogen transferred into the sludge is about 20-30%, and the proportion of phosphorus transferred into the sludge is about 90%.
Chinese patent CN201810912325.5 discloses an indirect heat transfer type sludge pyrolysis carbonization device, including pyrolysis carbonization stove and the first combustor of supply high temperature flue gas in the pyrolysis carbonization stove, be equipped with the pyrolysis conveyer that is used for carrying mud in the pyrolysis carbonization stove motion in the pyrolysis carbonization stove, the pyrolysis conveyer includes the auger delivery ware of multistage horizontal arrangement, multistage auger delivery ware is arranged from top to bottom, auger delivery ware carries mud from its first end to second end at the horizontal direction, the direction of delivery of upper and lower adjacent auger delivery ware is opposite, the first end of the auger delivery ware of below receives the mud that falls from the auger delivery ware's of adjacent top second end, every section auger delivery ware includes the casing and is located the auger delivery ware that promotes the mud motion in the casing, the first end of every section auger delivery ware's casing has the receiving opening that receives mud, the second end of every section auger delivery ware's casing has the discharge opening of discharge mud. The indirect sludge pyrolysis carbonization device for the bio-oil does not produce bio-oil which is difficult to separate. However, this device has low efficiency and low heat utilization.
Disclosure of Invention
The technical problem to be solved by the invention is as follows: overcomes the defects of the prior art, provides an integrated sludge drying and carbonizing device, indirectly heats sludge from top to bottom in a layered manner to complete drying and carbonizing, and has high efficiency, energy conservation and low pollution.
The invention relates to an integrated sludge drying and carbonizing device, which comprises a feeding component, a furnace body component, a transmission component, a gas component, a feeding component, an air distribution component and a burner component,
the feeding assembly is positioned at the upper part of the furnace body assembly, penetrates through the furnace body and comprises 2-15 rows of feeding mechanisms, each row of feeding mechanisms comprises 3-15 layers of conveying pipes, one end of one conveying pipe is an inlet, the other end of the one conveying pipe is an outlet, and the outlet of the upper layer of conveying pipe is connected with the inlet of the lower layer of conveying pipe through a connecting pipe; the inlet of the conveying material pipe positioned at the topmost layer is a feeding hole, the feeding hole is communicated with the feeding assembly, and the outlet of the conveying material pipe positioned at the bottommost layer is a discharging hole;
the feeding assembly is connected with the feeding assembly and is used for conveying sludge to the feeding assembly;
the transmission assembly provides power to convey sludge from the feed inlet to the discharge outlet;
the furnace body component comprises a furnace body, a smoke outlet and a combustion chamber, wherein the smoke outlet is communicated with the top of the furnace body, and the combustion chamber is positioned in the lower space of the furnace body component;
the gas component) comprises gas pipes and gas outlets, the number of layers of the gas pipes is one layer more than that of the feeding mechanisms, one end of each two adjacent layers of the gas pipes is connected together through a regulating valve, the other end of each two adjacent layers of the gas pipes is closed, the gas pipe positioned at the bottommost layer is communicated with the combustion chamber, the rest gas pipes are transversely communicated with 2-15 rows of feeding mechanisms, and the other side of the end, connected with the lower layer of gas pipe, of the gas pipe positioned at the topmost layer is connected with the;
the air distribution component is communicated with the combustion chamber and is used for providing combustion improver;
the combustor assembly is in communication with the combustion chamber for providing fuel.
The feeding assembly can comprise 2 rows of feeding mechanisms, and each row of feeding mechanisms comprises 15 layers of feeding pipes; the device also can comprise 15 rows of feeding mechanisms, wherein each row of feeding mechanism comprises 3 layers of feeding pipes; and 7 rows of feeding mechanisms can also be included, and each row of feeding mechanisms comprises 8 layers of feeding pipes.
The sludge enters the feeding assembly through the feeding assembly, and is dried and carbonized at low temperature in multiple rows and multiple columns, and the multiple rows work simultaneously, so that the yield is high and the efficiency is high. The flue gas that the combustion of combustion chamber produced carries out indirect heating to the mud in the pay-off subassembly, and mud from top to bottom heats by layers, and the flue gas temperature reduces from bottom to top constantly, and mud from top to bottom utilizes the flue gas of temperature from low to high to heat up in proper order and accomplishes mummification, carbonization, make full use of flue gas heat, energy-conservation. The regulating valve is used for controlling, distilled water vapor generated in the upper layer drying process of the sludge is collected by the gas pipe and is discharged through the exhaust port, distilled oil gas generated in the lower layer carbonization process of the sludge is collected by the gas pipe and is combusted in the combustion chamber, heat for heating the sludge is provided, energy is fully utilized, and energy conservation and low pollution are achieved.
Preferably, the transmission assembly comprises a motor, a chain wheel and a conveyor shaft, and the motor is connected with the chain wheel through a transmission chain; the conveyer shaft crosses the material conveying pipe, one end is connected with the chain wheel, and the other end is connected with the feeding component through a bearing.
The conveyor shaft pushes the sludge in the conveying material pipe and moves from the inlet of the conveying material pipe to the outlet.
Preferably, the feeding assembly comprises a hopper, a kick-out device and a feed opening, the feed opening is located below the hopper, the feed opening is communicated with the bottom of the hopper, the other end of the feed opening is communicated with the feed opening of the feeding assembly, the kick-out device is arranged between the hopper and the feed opening, and the number of the feed openings is the same as that of the feed openings of the feeding assembly.
The sludge is stirred in the hopper through the stirring device and enters the feeding hole of the feeding assembly.
Preferably, the air distribution assembly comprises a fan, an air distribution pipe and an air regulation port which are sequentially communicated, and the air regulation port is arranged on the air distribution pipe and communicated with the combustion chamber.
The fan makes the combustion-supporting air enter the combustion chamber through the air distribution pipe and the air adjusting port in sequence to support combustion.
Preferably, the regulating valves between the third and fourth tier gas pipes are closed and the remaining regulating valves are opened.
When oil gas begins to be produced at the fourth layer of the conveying pipe, the regulating valves between the third layer of the gas pipe and the fourth layer of the gas pipe are closed, other regulating valves are opened, the oil gas at the lower layer is isolated from the gas at the upper layer, the oil gas is controlled to enter the combustion chamber, and the gas at the upper layer is discharged through the exhaust port. The open-close state of the regulating valve is not limited, and can be adjusted according to actual conditions.
Preferably, the other side of the gas pipe positioned at the topmost layer is connected with an exhaust port through a regulating valve.
The regulating valve is used for controlling the flowing direction of gas in the gas pipe.
Preferably, a first combustion nozzle and a second combustion nozzle are arranged in the combustion chamber, the number of the first combustion nozzles is the same as the number of the rows of the gas mechanisms, the first combustion nozzles are communicated with the gas pipe at the bottommost layer, and the second combustion nozzles are communicated with the combustor assembly.
The first burner is used for burning distilled oil gas generated in the sludge carbonization process, and the second burner is used for burning gas provided by the burner component.
Preferably, the burner assembly provides gas or natural gas or biogas.
For combustion by the second fuel burner.
Preferably, the smoke outlet is communicated with a smoke treatment system.
The device is used for treating flue gas and discharging the flue gas after reaching the standard.
Compared with the prior art, the invention has the following beneficial effects:
according to the integrated sludge drying and carbonizing device, the sludge is indirectly heated from top to bottom in a layered manner to complete drying and carbonizing, and the device is efficient, energy-saving and low in pollution.
Drawings
FIG. 1 is a schematic structural view of the front side of the integrated sludge drying and carbonizing apparatus of the present invention;
FIG. 2 is a schematic structural view of the left side of the integrated sludge drying and carbonizing apparatus of the present invention;
FIG. 3 is a schematic front view of the conveying structure according to the present invention;
FIG. 4 is a schematic diagram of the right side structure of the conveying structure according to the present invention;
FIG. 5 is a schematic front view of the feeding assembly of the present invention;
FIG. 6 is a schematic cross-sectional view taken along line A-A in FIG. 5;
FIG. 7 is a schematic front view of the gas module of the present invention;
FIG. 8 is a schematic view of the left side of the gas module of the present invention;
FIG. 9 is a schematic front view of the furnace assembly of the present invention;
FIG. 10 is a schematic view of the left side structure of the furnace body assembly according to the present invention.
Wherein, 1, a feeding component; 101. a hopper; 102. a kick-out device; 103. a feeding port; 104. a rotating shaft; 105. a belt pulley; 106. a material stirring head; 106-1, a fixed seat; 106-2, a material shifting sheet; 106-3, a through hole; 2. a furnace body assembly; 201. a furnace body; 202. a smoke outlet; 203. a combustion chamber; 204. a first burner tip; 205. a second fuel burner; 206. a feed hole; 207. a combustion nozzle; 208. an air inlet; 209. a burner port; 210. a bevel; 3. a transmission assembly; 301. a motor; 302. a sprocket; 303. a conveyor shaft; 4. a gas component; 401. a gas pipe; 402. an exhaust port; 403. adjusting a valve; 404. a burner tip tube; 405. a gas port; 5. a feeding assembly; 501. a material conveying pipe; 502. a connecting pipe; 503. a discharge port; 504. a feed pipe; 505. a discharge pipe; 6. a wind distribution assembly; 601. a fan; 602. an air distribution pipe; 603. adjusting the air outlet; 7. a burner assembly.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention more apparent, embodiments of the present invention will be described in detail with reference to the accompanying drawings.
As shown in fig. 1-10, the integrated sludge drying and carbonizing apparatus of the present invention includes a feeding assembly 1, a furnace body assembly 2, a transmission assembly 3, a gas assembly 4, a feeding assembly 5, an air distribution assembly 6, and a burner assembly 7, wherein the feeding assembly 5 is located at the upper portion of the furnace body assembly 2, penetrates through a furnace body 201, and includes 10 rows of feeding mechanisms, each row of feeding mechanisms includes 9 layers of conveying pipes 501, one end of one conveying pipe 501 is an inlet, the other end is an outlet, the outlet of the upper layer conveying pipe 501 is connected with the inlet of the lower layer conveying pipe 501 through a connecting pipe 502; the inlet of the conveying material pipe 501 positioned at the topmost layer is a feeding hole, the feeding hole is communicated with the feeding assembly 1, and the outlet of the conveying material pipe 501 positioned at the bottommost layer is a discharging hole 503;
the feeding component 1 is connected with the feeding component 5 and is used for conveying sludge to the feeding component 5;
the transmission component 3 provides power to convey sludge from the feed inlet to the discharge outlet 503;
the furnace body component 2 comprises a furnace body 201, a smoke outlet 202 and a combustion chamber 203, wherein the smoke outlet 202 is communicated with the top of the furnace body 201, and the combustion chamber 203 is positioned in the lower space of the furnace body component 2;
the gas component 4 comprises gas pipes 401 and an exhaust port 402, the number of layers of the gas pipes 401 is one layer more than that of the feeding mechanism, one end of each two adjacent layers of the gas pipes 401 is connected together through a regulating valve 403, the other end of each two adjacent layers of the gas pipes is closed, the gas pipes 401 positioned at the bottommost layer are communicated with the combustion chamber 203, the rest gas pipes 401 are transversely communicated with 10 rows of feeding mechanisms, and the other side of the end, connected with the gas pipe 401 positioned at the topmost layer, of the gas pipe 401 at the lower layer is connected with;
the air distribution component 6 is communicated with the combustion chamber 203 and is used for providing combustion improver; the air distribution assembly 6 comprises a fan 601, an air distribution pipe 602 and an air regulation port 603 which are sequentially communicated, wherein the air regulation port 603 is arranged on the air distribution pipe 602 and is communicated with the combustion chamber 203.
The burner assembly 7 communicates with the combustion chamber 203 for providing fuel.
The transmission assembly 3 comprises a motor 301, a chain wheel 302 and a conveyor shaft 303, wherein the motor 301 and the chain wheel 302 are connected through a transmission chain 304; the conveyor shaft 303 crosses the conveying pipe 501, one end of the conveyor shaft is connected with the chain wheel 302 on one side of the conveying pipe 501, and the other end of the conveyor shaft is connected with the other side of the conveying pipe 501 through a bearing.
The working process of the integrated sludge drying and carbonizing device is as follows:
sludge enters the feeding component 5 through the feeding component 1, and is dried and carbonized at low temperature in multiple rows and multiple columns, and the simultaneous working of multiple rows is high in yield and high in efficiency. The flue gas that combustion chamber 203 burning produced carries out indirect heating to the mud in the feeding subassembly 5, and mud from top to bottom heats by layers, and the flue gas temperature from bottom to top constantly reduces, and mud from top to bottom utilizes the flue gas of temperature from low to high to heat up in proper order and accomplishes mummification, carbonization, make full use of flue gas heat, and is energy-conserving. The distilled water vapor generated in the drying process of the upper layer of the sludge is collected by the gas pipe 401 and discharged through the exhaust port 402 under the control of the regulating valve 403, and the distilled oil gas generated in the carbonization process of the lower layer of the sludge is collected by the gas pipe 401 and combusted in the combustion chamber 203, so that the heat for heating the sludge is provided, the energy is fully utilized, the energy is saved, and the pollution is low. The integrated sludge drying and carbonizing device is isolated from the outside air through the feeding assembly 5, and the sludge is dried and carbonized in an anaerobic environment.
The conveying structure comprises a transmission assembly 3 and a feeding assembly 5.
Specifically, the conveying pipe 501 is cylindrical with two closed ends, and the connecting pipe 502 is cylindrical with two open ends, so that the cylindrical friction force is small, and the sludge movement is facilitated. The feeding port of the feeding component 5 is connected with the feeding component 1 through a feeding pipe 504 for feeding; the discharge port 503 is connected with a discharge pipe 505 for discharging. Each row of feeding mechanisms is provided with a motor 301, and one motor 301 is connected with a plurality of chain wheels 302 through chains 304 to drive a plurality of conveying material pipes 501; the number of layers of the sprocket 302 and the conveying pipe 501 is the same. The two adjacent layers of conveyor shafts 303 are respectively provided with a positive helical blade and a negative helical blade.
Here, a motor 301 is connected to a plurality of sprockets 302 via a chain 304 to drive a plurality of conveyor shafts 303. One layer of the conveyor shaft 303 of the two adjacent layers is provided with a positive helical blade, the other layer is provided with a negative helical blade, and the conveying directions of the two layers are opposite; if the upper layer conveying pipe 501 pushes the sludge from the inlet to the outlet through the positive helical blade, the lower layer conveying pipe 501 pushes the sludge from the inlet to the outlet through the negative helical blade. The moving directions of the sludge in the two adjacent conveying material pipes 501 are opposite, one layer is from left to right, and the other layer is from right to left.
The working process of the conveying structure is as follows:
10 motors 301 drive 10 rows of feeding mechanisms to feed materials, and one motor 301 is connected with a plurality of chain wheels 302 through chains 304 to drive a plurality of conveyor shafts 303 to work. The single-layer conveyor shaft 303 is provided with positive helical blades, the double-layer conveyor shaft 303 is provided with negative helical blades, and the conveying directions of the two layers are opposite; the single-layer conveying pipe 501 pushes the sludge to move from left to right through the positive helical blades, and the double-layer conveying pipe 501 pushes the sludge to move from right to left through the negative helical blades.
The feeding assembly 1 comprises a hopper 101, a kick-out device 102 and a feed opening 103, the feed opening 103 is located below the hopper 101, the feed opening 103 is communicated with the bottom of the hopper 101, the other end of the feed opening is communicated with a feed opening of the feeding assembly 5, the kick-out device 102 is arranged between the hopper 101 and the feed opening 103, and the number of the feed openings 103 is 10. The kick-out device 102 comprises a kick-out head 106 and a rotating shaft 104, wherein the center of the kick-out head 106 is positioned at the center of the upper edge of the feed opening 103 and is the same as the feed opening 103 in number; the rotating shaft 104 penetrates through the material stirring head 106, and the material stirring head 106 is driven to rotate by the belt pulley 105 and the motor.
Specifically, the stirring head 106 comprises a fixed seat 106-1 and a plurality of stirring sheets 106-2, the plurality of stirring sheets 106-2 are uniformly distributed on the outer circumference of the fixed seat 106-1, and one end of each stirring sheet 106-2 is obliquely inserted into the fixed seat 106-1. The center of the fixing seat 106-1 is provided with a through hole 106-3, and the rotating shaft 104 penetrates through the fixing seat 106-1 through the through hole 106-3. The through hole 106-3 is circular, and the fixing seat 106-1 and the rotating shaft 104 are integrally formed or welded and fixed. The number of the material stirring pieces 106-2 is 6, and the material discharging opening 103 is in a cylindrical shape with two open ends.
The working process of the feeding assembly 1 of the invention is as follows:
the number of the feed openings 103 is the same as the number of the rows of the feeding mechanisms, 10 feed openings 103 are respectively communicated with the feed openings of the 10 rows of the feeding mechanisms, and the feed openings 103 can be combined with the communicated feed openings in the installation process. The belt pulley 105 and the motor drive the material stirring head 106 to rotate, and the sludge is stirred by the material stirring head 106 in the hopper 101 to enter the communicated feeding holes through the 10 material discharging holes 103 and further enter the corresponding feeding mechanisms.
The gas subassembly 4 includes gas pipe 401, gas vent 402, and the number of piles of gas pipe 401 is the one deck more than feeding mechanism's the number of piles, and the one end of gas pipe 401 connects gradually, the other end seals, and the gas pipe 401 that is located the bottommost layer communicates combustion chamber 203, and remaining gas pipe 401 transversely communicates 10 feeding mechanism through gas port 405, and the gas pipe 401 that is located the topmost layer is connected the opposite side of one end with lower floor's gas pipe 401 and is connected with gas vent 402.
Specifically, the gas pipe 401 located at the bottommost layer is communicated with the combustion chamber 203 through a burner tip pipe 404, 1-3 burner tip pipes 404 are arranged, and the burner tip pipe 404 is in a circular pipe shape with two open ends. One ends of the gas pipes 401 in two adjacent layers are connected together through a regulating valve 403, and the other side of the gas pipe 401 at the topmost layer is connected with an exhaust port 402 through the regulating valve 403. The regulating valve 403 is a manual valve or an electric valve, and the regulating valve 403 is used for controlling the direction of gas flow in the gas pipe 401. When the adjusting valve 403 is an electric valve, the opening and closing of the adjusting valve 403 can be controlled by the temperature in the conveying pipe 501; when the temperature of oil gas generation begins to be reached at a certain layer of the conveying pipe 501, the regulating valve 403 between the layer and the gas pipe 401 adjacent to the layer is closed, and the rest regulating valves 403 are opened. Distilled water vapor generated in the drying process of the upper layer of the sludge is collected by the gas pipe 401 and discharged through the exhaust port 402, and distilled oil gas generated in the carbonization process of the lower layer of the sludge is collected by the gas pipe 401 to the combustion chamber 203 for combustion. The open/close state of the regulating valve 403 is not limited, and may be adjusted according to actual conditions.
The working process of the gas component 4 of the invention is as follows:
when oil and gas are generated in the fourth to ninth floors of the feed pipe 501, the regulating valves 403 between the third and fourth floors of the gas pipe 401 are closed, and the remaining regulating valves 403 are opened. The lower layer of oil gas is isolated from the upper layer of gas, the oil gas is collected by a gas port 405 and enters the combustion chamber 203 along a gas pipe 401 through a combustion nozzle pipe 404, and the upper layer of gas is discharged along the gas pipe 401 through a gas outlet 402.
The furnace body component 2 comprises a furnace body 201, a smoke vent 202 and a combustion chamber 203, wherein the smoke vent 202 is communicated with the top of the furnace body 201, 10 rows of feeder holes 206 penetrating through the furnace body 201 are formed in the upper part of the furnace body 201, and 9 layers of feeder holes 206 are arranged in each row; the combustion chamber 203 is positioned in the lower space of the furnace body 201, the combustion chamber 203 is provided with a combustion nozzle 207, an air inlet 208 and a burner port 209, the number of the combustion nozzle 207 is the same as that of the air inlet 208, the combustion nozzle 207 is positioned above the air inlet 208, and the air inlet 208 is positioned at the lower side of the furnace body 201. The combustion chamber 203 is provided with first burners 204 and second burners 205, the first burners 204 are provided inside the burner ports 207 in the same number as the burner ports 207, and the second burners are provided inside the burner ports 209. The feeding assembly 5 penetrates through the furnace body 201 through the feeder hole 206.
Specifically, the furnace body 201 is formed by welding a steel shell, and inner village insulating bricks and insulating cotton; the furnace body 201 is a cuboid, and a group of opposite sides at the top are inclined planes 210. The feeder holes 206 are circular, the number of the combustion nozzles 207 is 3, the combustion nozzles 207 are circular, and the air inlets 208 are circular. The exhaust port 202 communicates with the flue gas treatment system.
The working process of the furnace body component 2 of the invention is as follows:
the 10 rows of feeding mechanisms are fixed through the 10 rows of feeder holes 206, and the 9 layers of feeding pipes 501 of each row of feeding mechanisms are fixed through the 9 layers of feeder holes 206 of each row. The air adjusting opening 603 penetrates through the air inlet 208 to be communicated with the combustion chamber 203, and combustion air enters the combustion chamber 203 through the air adjusting opening 603. The burner assembly 7 penetrates through the burner port 209 and is communicated with the second burner 205, and the sludge in the feeding assembly 5 is indirectly heated by flue gas generated by burning coal gas or natural gas or methane in the second burner 205. The burner tip pipe 404 passes through the burner tip opening 207 and is communicated with the first burner tip 204, and distilled oil gas generated in the lower-layer high-temperature carbonization process of sludge is combusted.
The above description is only for the purpose of illustrating the preferred embodiments of the present invention and is not to be construed as limiting the invention, but rather the intention is to cover all modifications, equivalents, and alternatives falling within the spirit and scope of the invention as defined by the appended claims.
Claims (9)
1. The utility model provides an integration sludge drying, carbonization device which characterized in that: comprises a feeding component (1), a furnace body component (2), a transmission component (3), a gas component (4), a feeding component (5), an air distribution component (6) and a burner component (7),
the feeding assembly (5) is positioned at the upper part of the furnace body assembly (2), penetrates through the furnace body (201), and comprises 2-15 rows of feeding mechanisms, each row of feeding mechanisms comprises 3-15 layers of conveying pipes (501), one end of one conveying pipe (501) is an inlet, the other end of the one conveying pipe is an outlet, and the outlet of the upper layer of conveying pipes (501) is connected with the inlet of the lower layer of conveying pipes (501) through a connecting pipe (502); the inlet of the conveying material pipe (501) positioned at the topmost layer is a feeding hole, the feeding hole is communicated with the feeding assembly (1), and the outlet of the conveying material pipe (501) positioned at the bottommost layer is a discharging hole (503);
the feeding component (1) is connected with the feeding component (5) and is used for conveying sludge to the feeding component (5);
the transmission assembly (3) provides power to convey sludge from the feed inlet to the discharge outlet (503);
the furnace body component (2) comprises a furnace body (201), a smoke outlet (202) and a combustion chamber (203), wherein the smoke outlet (202) is communicated with the top of the furnace body (201), and the combustion chamber (203) is positioned in the lower space of the furnace body component (2);
the gas component (4) comprises gas pipes (401) and an exhaust port (402), the number of layers of the gas pipes (401) is one layer more than that of the feeding mechanism, one end of each two adjacent layers of the gas pipes (401) is connected together through an adjusting valve (403), the other end of each two adjacent layers of the gas pipes is sealed, the gas pipes (401) positioned at the bottommost layer are communicated with the combustion chamber (203), the rest gas pipes (401) are transversely communicated with 2-15 rows of feeding mechanisms, and the exhaust port (402) is connected to the other side of the end, connected with the lower layer of gas pipes (401), of the gas pipes (401) positioned at;
the air distribution component (6) is communicated with the combustion chamber (203) and is used for providing combustion improver;
the combustor assembly (7) is in communication with the combustion chamber (203) for providing fuel.
2. The integrated sludge drying and carbonizing apparatus of claim 1, wherein: the transmission assembly (3) comprises a motor (301), a chain wheel (302) and a conveyor shaft (303), and the motor (301) is connected with the chain wheel (302) through a transmission chain (304); the conveyor shaft (303) traverses the conveying material pipe (501), one end of the conveyor shaft is connected with the chain wheel (302), and the other end of the conveyor shaft is connected with the feeding assembly (5) through a bearing.
3. The integrated sludge drying and carbonizing apparatus according to claim 1 or 2, wherein: the feeding assembly (1) comprises a hopper (101), a kick-out device (102) and a feed opening (103), wherein the feed opening (103) is located below the hopper (101), the feed opening (103) is communicated with the bottom of the hopper (101), the other end of the feed opening is communicated with a feed opening of the feeding assembly (5), the kick-out device (102) is arranged between the hopper (101) and the feed opening (103), and the number of the feed openings (103) is the same as that of the feed openings of the feeding assembly (5).
4. The integrated sludge drying and carbonizing apparatus of claim 3, wherein: the air distribution assembly (6) comprises a fan (601), an air distribution pipe (602) and an air regulation port (603) which are sequentially communicated, wherein the air regulation port (603) is arranged on the air distribution pipe (602) and communicated with the combustion chamber (203).
5. The integrated sludge drying and carbonizing apparatus of claim 4, wherein: the regulating valve (403) between the third layer and the fourth layer gas pipe (401) is closed, and the rest regulating valves (403) are opened.
6. The integrated sludge drying and carbonizing apparatus according to claim 1 or 5, wherein: the other side of the gas pipe (401) positioned at the topmost layer is connected with an exhaust port (402) through a regulating valve (403).
7. The integrated sludge drying and carbonizing apparatus according to claim 1 or 2, wherein: first combustion nozzles (204) and second combustion nozzles (205) are arranged in the combustion chamber (203), the number of the first combustion nozzles (204) is the same as the number of rows of the gas mechanism, the first combustion nozzles (204) are communicated with the gas pipe (401) at the bottommost layer, and the second combustion nozzles (205) are communicated with the combustor assembly (7).
8. The integrated sludge drying and carbonizing apparatus of claim 7, wherein: the burner assembly (7) provides gas or natural gas or biogas.
9. The integrated sludge drying and carbonizing apparatus according to claim 6 or 8, wherein: the smoke outlet (202) is communicated with a smoke treatment system.
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CN201911192793.0A CN110746082A (en) | 2019-11-28 | 2019-11-28 | Integrated sludge drying and carbonizing device |
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CN201911192793.0A CN110746082A (en) | 2019-11-28 | 2019-11-28 | Integrated sludge drying and carbonizing device |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110436742A (en) * | 2019-09-12 | 2019-11-12 | 秦皇岛开发区春光铸造机械有限公司 | The continuous indirect heating apparatus and method of scraper plate conveying are buried in a kind of utilization |
-
2019
- 2019-11-28 CN CN201911192793.0A patent/CN110746082A/en not_active Withdrawn
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110436742A (en) * | 2019-09-12 | 2019-11-12 | 秦皇岛开发区春光铸造机械有限公司 | The continuous indirect heating apparatus and method of scraper plate conveying are buried in a kind of utilization |
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