WO2019096019A1 - Industrial continuous oily sludge thermal decomposition equipment - Google Patents
Industrial continuous oily sludge thermal decomposition equipment Download PDFInfo
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- WO2019096019A1 WO2019096019A1 PCT/CN2018/113920 CN2018113920W WO2019096019A1 WO 2019096019 A1 WO2019096019 A1 WO 2019096019A1 CN 2018113920 W CN2018113920 W CN 2018113920W WO 2019096019 A1 WO2019096019 A1 WO 2019096019A1
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- WIPO (PCT)
- Prior art keywords
- temperature zone
- high temperature
- thermal decomposition
- conveyor chain
- industrial continuous
- Prior art date
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- 238000005979 thermal decomposition reaction Methods 0.000 title claims abstract description 18
- 239000010802 sludge Substances 0.000 title abstract description 17
- 238000000197 pyrolysis Methods 0.000 claims abstract description 39
- 238000005336 cracking Methods 0.000 claims abstract description 36
- 238000010438 heat treatment Methods 0.000 claims abstract description 24
- 238000007789 sealing Methods 0.000 claims abstract description 23
- 230000001105 regulatory effect Effects 0.000 claims abstract description 7
- 238000001816 cooling Methods 0.000 claims abstract description 6
- 239000012530 fluid Substances 0.000 claims description 31
- 230000005540 biological transmission Effects 0.000 claims description 25
- 239000007787 solid Substances 0.000 claims description 19
- 239000010801 sewage sludge Substances 0.000 claims description 15
- 239000003638 chemical reducing agent Substances 0.000 claims description 10
- 239000000428 dust Substances 0.000 claims description 8
- 239000000446 fuel Substances 0.000 claims description 6
- 238000009413 insulation Methods 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 3
- 239000002245 particle Substances 0.000 abstract description 4
- 239000003921 oil Substances 0.000 description 20
- 239000007789 gas Substances 0.000 description 15
- 239000002994 raw material Substances 0.000 description 9
- 238000000034 method Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 239000000295 fuel oil Substances 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 238000009833 condensation Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 3
- 238000007599 discharging Methods 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 239000003034 coal gas Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000003345 natural gas Substances 0.000 description 2
- 238000007790 scraping Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- KVGZZAHHUNAVKZ-UHFFFAOYSA-N 1,4-Dioxin Chemical compound O1C=COC=C1 KVGZZAHHUNAVKZ-UHFFFAOYSA-N 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 231100000315 carcinogenic Toxicity 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 150000002013 dioxins Chemical class 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000003027 oil sand Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000012958 reprocessing Methods 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Images
Classifications
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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
-
- 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
- C10B47/18—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion with moving charge
-
- 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
- C10B47/28—Other processes
- C10B47/32—Other processes in ovens with mechanical conveying means
- C10B47/40—Other processes in ovens with mechanical conveying means with endless conveying devices
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/40—Valorisation of by-products of wastewater, sewage or sludge processing
Definitions
- the invention relates to the field of thermal decomposition treatment of organic substances such as oil sludge, oil sand, heavy oil pyrolysis and domestic garbage pyrolysis, and particularly relates to a sewage sludge continuous pyrolysis device.
- Oily sludge is a concomitant product of petrochemical production, and its treatment is mainly incineration and landfill.
- these two treatment methods cannot achieve the required harmless treatment.
- Dioxins are easily produced during incineration with sludge, and dioxin is a carcinogenic gas substance that affects the atmosphere and causes secondary pollution.
- these two traditional treatment methods are costly.
- the oily sludge pyrolysis technology is an effective method to solve the oil content in oily sludge.
- the water After the temperature is raised, the water first evaporates, and then the temperature is raised, the light oil is volatilized, and the heavy oil is cracked into small molecules, and the light oil is volatilized and collected, and then the moisture and oil in the sludge are removed, and the obtained dry matter can be obtained.
- the existing equipment for pyrolysis of oily sludge is mainly heated by rotation and has high energy consumption; the equipment covers a large area and the manufacturing cost is high; the particle size of the tailings discharge cannot be well controlled, and sludge coking occurs during the treatment process. To make the pyrolysis insufficient and the equipment cleaned up.
- the present invention proposes a sewage sludge continuous pyrolysis device, which saves the rotary energy consumption of the pyrolysis furnace through multi-layer belt conveyance, reduces the equipment volume, reduces the equipment cost, and precisely controls the tailings particle size and drying. Degree, reduce secondary pollution.
- An industrial continuous sewage sludge thermal decomposition device comprising a pyrolysis furnace and a heating chamber, wherein the heating chamber is disposed on one side or several sides of the outside of the pyrolysis furnace, and a feed inlet is arranged at a front portion of the pyrolysis furnace,
- the pyrolysis furnace includes a full high temperature zone or a low temperature zone-high temperature zone; the pyrolysis furnace is provided with a conveyor chain belt, the end of the conveyor chain belt is a discharge port, and the discharge port is connected with a sealing device;
- a conveyor chain belt is disposed in the full high temperature region, the conveyor chain belt includes at least two layers, and the transmission chain belts between the layers are staggered in a vertical direction;
- the low temperature zone-high temperature zone includes a low temperature zone and a high temperature zone, the low temperature zone is adjacent to the feed port, and a transfer chain belt is disposed between the low temperature zone and the high temperature zone, and the low temperature zone and the high temperature zone are disposed between the low temperature zone and the high temperature zone.
- the conveying chain belt of the low temperature zone comprises a feeding end and a discharging end; the conveying end belt of the feeding end and the discharging end are at least one layer, and the feeding end and the discharging end of each layer
- the end conveyor belts are staggered in a vertical direction; the conveyor belts in the high temperature zone are at least two layers, and the conveyor chains in the high temperature zone are staggered in a vertical direction in a high temperature zone;
- a burner for heating the furnace body of the cracking furnace is provided in the heating chamber, and the burner is connected to the fuel input device.
- the pyrolysis furnace is a cracking furnace
- the sealing device comprises a rotary sealing joint
- the discharge port is connected to one end of the rotary sealing joint
- the other end of the rotary sealing joint is connected with a cooling cylinder.
- the feed port includes a solid feed port, a semi-fluid, and a fluid feed port.
- the top of the cracking furnace is provided with an oil and gas outlet and a dust removing device.
- the oil and gas are mainly light oil and water vapor. After the oil and gas are discharged, the water and oil are separated by condensation, and the obtained oil can be reused.
- the dust removal device is mainly a wet dust removal device, which reduces the dust in the cracking furnace.
- the furnace body of the cracking furnace is any one of a rectangular shape, a circular shape and a tubular shape. However, it is not limited to these types, and the shape of the furnace body can be selected and designed according to specific conditions.
- a scraper is disposed at the bottom of the cracking furnace.
- the scraper is mainly used to scrape the residual material on the conveyor chain to strengthen the operation of the equipment.
- the low temperature zone-high temperature zone includes a low temperature zone and a high temperature zone; and the burner is disposed in the heating chamber of the full high temperature zone or the high temperature zone.
- control device and the transmission power device are electrically connected, and the control device is electrically connected to the transmission power device; the transmission power device is connected to the transmission chain.
- a solid conveyor belt for conveying solids is connected to the front end of the solid feed port.
- a fluid and a semi-fluid transfer pump for transporting a semi-fluid or a fluid is connected to the front end of the semi-fluid and fluid feed port.
- the transmission power device comprises a motor, a speed reducer, a driving wheel and a tensioning wheel, wherein the speed reducer is respectively connected with the driving wheel and the motor; the motor is an AC variable frequency stepless speed regulating motor; the tensioning wheel is set On the drive wheel, the conveyor chain is disposed between the drive wheel and the tensioning wheel.
- the AC variable frequency stepless speed regulating motor is used to adjust the speed of the conveyor chain, effectively control the pyrolysis rate and residence time, and accurately control the particle size and dryness of the tailings.
- the high temperature zone is provided with a burner, while in the low temperature zone, the burner is not provided, and the material in the high temperature zone directly enters the low temperature zone, because the low temperature zone and the feed port phase Adjacent, the waste heat from the high temperature zone can heat the raw materials in the low temperature zone after the feed port, making full use of heat energy. It can reduce the setting of the burner while saving energy.
- the pyrolysis contains sludge, and the hydrocarbons in the sludge are collected in the meteorological environment without causing air pollution, recycling, and environmental protection.
- FIG. 1 is a schematic view showing the structure of a pyrolysis furnace in a high temperature zone in the present invention
- FIG. 2 is a schematic view showing the structure of the pyrolysis furnace in the low temperature zone-high temperature zone and the low temperature zone in the present invention
- FIG. 3 is a schematic view showing the structure of the pyrolysis furnace in the low temperature zone-high temperature zone and the low temperature zone in the present invention
- 1-cracking furnace 2-heating bin, 3-transport chain, 4-full high temperature zone, 5-low temperature zone, 6-high temperature zone, 7-discharge port, 8-rotation sealing joint, 9-cooling cylinder, 10 - burner, 11-solid feed port, 12-semifluid and fluid feed port, 13-oil and gas outlet, 14-solid conveyor, 15-fluid and semi-fluid transfer pump, 16-scraper, 17-dust removal device, 18-insulation board.
- FIG. 1 An industrial continuous sewage sludge thermal decomposition device is shown in Fig. 1, comprising a pyrolysis furnace 1 and a heating chamber 2, and the heating chamber can be disposed on either side of the pyrolysis furnace, or on both sides, or three according to requirements.
- the pyrolysis furnace may preferably be the cracking furnace 1.
- the heating chamber 2 in this embodiment is disposed on the lower side of the cracking furnace 1, and the front end of the cracking furnace 1 is provided with a feeding port, and the feeding port includes a solid feeding port 11, a semi-fluid and a fluid inlet port 12, when the raw material is In the case of a solid, it can be directly transported by a solid conveying device.
- the solid conveying belt 14 is preferably used for direct conveying; when the raw material is semi-fluid or fluid, the fluid and semi-fluid conveying pump 15 can be used for the raw material.
- the inside of the cracking furnace 1 includes a full-temperature zone 4; the cracking furnace 1 is provided with a conveyor chain 3, the end of the conveyor chain 3 is a discharge port 7, and the discharge port 7 is connected with a sealing device.
- the sealing device preferably comprises a rotary sealing joint 8, ie the discharge opening 7 can preferably be connected to one end of the rotary sealing joint 8, the other end of the rotary sealing joint 8 is connected to the cooling cylinder 9; in the full high temperature zone 4 there is a conveyor chain 3, which is conveyed
- the chain belt 3 comprises at least two layers, and the conveyor chain belts 3 between each layer are staggered in a vertical direction;
- the heating chamber 2 is provided with a burner 10 for heating the furnace body of the cracking furnace 1, the burner 10 and the gas Input device connection.
- the fuel may include gas, coal gas, natural gas, fuel oil, etc., and the burners 10 are adapted to each other depending on the fuel.
- the furnace body of the cracking furnace 1 is any one of a rectangular shape, a circular shape and a tubular shape, but is not limited to these types, and the shape of the furnace body can be selected and designed according to specific actual conditions.
- the top of the cracking furnace 1 is provided with an oil and gas outlet 13 and a dust removing device 17.
- the oil and gas contain water vapor, and the oil and gas after the separation is separated and collected by condensation, and the obtained oil can be reused.
- the bottom of the cracking furnace 1 is provided with a scraper 16 which is mainly disposed near the discharge port 7 to facilitate scraping of the tailings on the drive chain belt at the discharge port 7, thereby ensuring smooth operation of the equipment.
- the control of the transmission chain belt mainly adopts a control device and a transmission power device, and the control device is electrically connected with the transmission power device;
- the transmission power device comprises an AC variable frequency stepless speed regulation motor, a speed reducer, a driving wheel and a tensioning wheel, and a speed reducer.
- the driving wheel and the motor are respectively connected;
- the tensioning wheel is disposed on the driving wheel,
- the transmission chain belt 3 is disposed between the driving wheel and the tensioning wheel, the driving wheel rotates, and the transmission chain belt is driven to move by friction.
- the control device can directly control the frequency of the AC variable frequency stepless speed regulating motor, and then control the speed of the speed reducer and the driving wheel to control the running speed of the raw material in the cracking furnace 1 and ensure the granularity and dryness of the tailings.
- An industrial continuous sewage sludge thermal decomposition device is shown in Fig. 2 and Fig. 3, and comprises a pyrolysis furnace 1 and a heating chamber 2, and the heating chamber can be disposed on either side or both sides of the outside of the pyrolysis furnace according to requirements. Or, on the three sides, or on the four sides, in the second embodiment of the present invention, the pyrolysis furnace may preferably be the cracking furnace 1.
- the heating chamber 2 in this embodiment is disposed on the lower side of the cracking furnace 1, and the front end of the cracking furnace 1 is provided with a feeding port, and the feeding port includes a solid feeding port 11, a semi-fluid and a fluid inlet port 12, when the raw material is When solid, it can be directly transported through the solid conveyor belt 14; when the raw material is semi-fluid or fluid, the raw material can be fed and fed by the fluid and semi-fluid transfer pump 15 at this time.
- the inside of the cracking furnace 1 includes a low temperature zone-high temperature zone; the cracking furnace 1 is provided with a conveyor chain belt 3, the end of the conveyor chain belt 3 is a discharge port 7, and the discharge port 7 is connected with a sealing device, in the second embodiment of the present invention
- the sealing device preferably comprises a rotary sealing joint 8, that is, the discharge opening 7 can preferably be connected to one end of the rotary sealing joint 8, and the other end of the rotary sealing joint 8 is connected with the cooling cylinder 9;
- the low temperature zone-high temperature zone includes the low temperature zone 5 and the high temperature zone 6, wherein the low temperature zone 5 is adjacent to the feed port, the transfer chain zone 3 is provided between the low temperature zone and the high temperature zone, the heat insulation board 18 is arranged between the low temperature zone 5 and the high temperature zone 6, and the conveyor chain zone of the low temperature zone 5 is provided.
- the conveyor belt 3 of the high temperature zone 6 is at least two layers, and the conveyor chain belts 3 of the high temperature zone 6 are staggered in the vertical direction in the high temperature zone 6;
- the heating compartment 2 is provided with a heating for heating the furnace body of the cracking furnace 1.
- the nozzle 10 is mainly disposed below the high temperature zone 6, and the burner 10 is connected to the gas input device.
- the fuel may include gas, coal gas, natural gas, fuel oil, etc., and the burners 10 are adapted to each other depending on the fuel.
- the furnace body of the cracking furnace 1 is any one of a rectangular shape, a circular shape and a tubular shape, but is not limited to these types, and the shape of the furnace body can be selected and designed according to specific actual conditions.
- the top of the cracking furnace 1 is provided with an oil and gas outlet 13 and a dust removing device 17.
- the oil and gas contain water vapor, and the oil and gas after the separation is separated and collected by condensation, and the obtained oil can be reused.
- the bottom of the cracking furnace 1 is provided with a scraper 16 which is mainly disposed near the discharge port 7 to facilitate scraping of the tailings on the drive chain belt at the discharge port 7, thereby ensuring smooth operation of the equipment.
- the control of the transmission chain belt mainly adopts a control device and a transmission power device, and the control device is electrically connected with the transmission power device;
- the transmission power device comprises an AC variable frequency stepless speed regulating motor, a speed reducer, a driving wheel and a tensioning wheel, The reducer is respectively connected with the driving wheel and the motor;
- the tensioning wheel is disposed on the driving wheel,
- the transmission chain belt 3 is disposed between the driving wheel and the tensioning wheel, the driving wheel rotates, and the transmission chain belt is driven by friction .
- the control device can directly control the frequency of the AC variable frequency stepless speed regulating motor, and then control the speed of the speed reducer and the driving wheel to control the running speed of the raw material in the cracking furnace 1 and ensure the granularity and dryness of the tailings.
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Abstract
Provided is an industrial continuous oily sludge thermal decomposition equipment, belonging to the field of oily sludge treatment. The industrial continuous oily sludge thermal decomposition equipment comprises a cracking furnace and a heating chamber, wherein the heating chamber is arranged outside the cracking furnace, and the cracking furnace interior comprises a full high temperature region or a low temperature region-high temperature region. The cracking furnace is provided with a conveyor chain belt, and the conveyor chain belt can be multi-layered and staggered. The end of the conveyor chain belt is a discharge port, the discharge port is connected to one end of a rotary sealing joint, and the other end of the rotary sealing joint is connected with a cooling cylinder. In the equipment, the conveyor chain belt is staggered in the vertical direction, which increases the residence time of the oily sludge in the cracking furnace, so that the pyrolysis is more sufficient. Meanwhile the length and size of the equipment is shortened, which saves equipment investment. An AC variable frequency stepless speed regulating motor is used to adjust the speed of the conveyor chain belt, so that the pyrolysis rate and residence time can be effectively controlled, and the particle size and dryness of tailings can be precisely controlled.
Description
本发明涉及油泥、油砂、稠油热解、生活垃圾热解等有机类物质热分解处理领域,具体涉及一种污油泥连续热解装置。The invention relates to the field of thermal decomposition treatment of organic substances such as oil sludge, oil sand, heavy oil pyrolysis and domestic garbage pyrolysis, and particularly relates to a sewage sludge continuous pyrolysis device.
含油污泥的是石化生产的伴随品,而其处理方式主要为焚烧及填埋,然而这两种处理方式并不能做到要求的无害化处理。含有污泥的焚烧过程中容易产生二恶英,而二恶英为致癌气体物质,影响大气,造成二次污染,同时这两种传统处理方式成本高。而含油污泥热解技术是解决含油污泥中油分的有效方法。将温度升温后,水分先蒸发,继而再将温度升高,轻质油挥发,重质油则裂解成小分子轻质油挥发收集,继而去除油泥中的水分和油分,得到的干物质则可直接排放或再处理,避免了二次污染。现有的用于含油污泥热解的设备主要是通过旋转受热,能耗大;设备占地面积大,制造成本高;不能良好的控制尾渣出料的粒度,且处理过程中产生油泥结焦,使热解不充分,设备清理困难。Oily sludge is a concomitant product of petrochemical production, and its treatment is mainly incineration and landfill. However, these two treatment methods cannot achieve the required harmless treatment. Dioxins are easily produced during incineration with sludge, and dioxin is a carcinogenic gas substance that affects the atmosphere and causes secondary pollution. At the same time, these two traditional treatment methods are costly. The oily sludge pyrolysis technology is an effective method to solve the oil content in oily sludge. After the temperature is raised, the water first evaporates, and then the temperature is raised, the light oil is volatilized, and the heavy oil is cracked into small molecules, and the light oil is volatilized and collected, and then the moisture and oil in the sludge are removed, and the obtained dry matter can be obtained. Direct discharge or reprocessing to avoid secondary pollution. The existing equipment for pyrolysis of oily sludge is mainly heated by rotation and has high energy consumption; the equipment covers a large area and the manufacturing cost is high; the particle size of the tailings discharge cannot be well controlled, and sludge coking occurs during the treatment process. To make the pyrolysis insufficient and the equipment cleaned up.
发明内容Summary of the invention
为了解决上述问题,本发明提出了一种污油泥连续热解装置,通过多层带式传送,节省热解炉旋转能耗,同时减小设备体积,降低设备成本,精确控制尾渣粒度和干燥度,降低二次污染。In order to solve the above problems, the present invention proposes a sewage sludge continuous pyrolysis device, which saves the rotary energy consumption of the pyrolysis furnace through multi-layer belt conveyance, reduces the equipment volume, reduces the equipment cost, and precisely controls the tailings particle size and drying. Degree, reduce secondary pollution.
为了实现上述目的,本发明是通过以下技术方案来实现的:In order to achieve the above object, the present invention is achieved by the following technical solutions:
一种工业连续化污油泥热分解设备,包括热解炉和加热仓,所述加热仓设置在热解炉外侧的任意一侧或几侧,所述热解炉前部设有进料口,所述热解炉内部包括全高温区或低温区-高温区;所述热解炉内设有传送链带,所述传送链带的末端为出料口,所述出料口连接密封装置;An industrial continuous sewage sludge thermal decomposition device, comprising a pyrolysis furnace and a heating chamber, wherein the heating chamber is disposed on one side or several sides of the outside of the pyrolysis furnace, and a feed inlet is arranged at a front portion of the pyrolysis furnace, The pyrolysis furnace includes a full high temperature zone or a low temperature zone-high temperature zone; the pyrolysis furnace is provided with a conveyor chain belt, the end of the conveyor chain belt is a discharge port, and the discharge port is connected with a sealing device;
所述全高温区内设有传送链带,所述传送链带包括至少两层,所述每层之间的传送链带沿竖直方向相互交错分布;a conveyor chain belt is disposed in the full high temperature region, the conveyor chain belt includes at least two layers, and the transmission chain belts between the layers are staggered in a vertical direction;
所述低温区-高温区包括低温区及高温区,所述低温区与进料口相邻,所述低温区与高温区之间设有传送链带,所述低温区与高温区之间设有隔热板,所 述低温区的传送链带包括进料端和出料端;所述进料端和出料端的传送链带均为至少一层,所述每层进料端和出料端的传送链带之间沿竖直方向相互交错分布;所述高温区内的传送链带为至少两层,所述高温区内的传送链带在高温区沿竖直方向相互交错分布;The low temperature zone-high temperature zone includes a low temperature zone and a high temperature zone, the low temperature zone is adjacent to the feed port, and a transfer chain belt is disposed between the low temperature zone and the high temperature zone, and the low temperature zone and the high temperature zone are disposed between the low temperature zone and the high temperature zone. There is a heat insulation board, the conveying chain belt of the low temperature zone comprises a feeding end and a discharging end; the conveying end belt of the feeding end and the discharging end are at least one layer, and the feeding end and the discharging end of each layer The end conveyor belts are staggered in a vertical direction; the conveyor belts in the high temperature zone are at least two layers, and the conveyor chains in the high temperature zone are staggered in a vertical direction in a high temperature zone;
所述加热仓内设有用于对裂解炉的炉体加热的烧嘴,所述烧嘴与燃料输入装置连接。A burner for heating the furnace body of the cracking furnace is provided in the heating chamber, and the burner is connected to the fuel input device.
进一步,所述热解炉为裂解炉,所述密封装置包括旋转密封接头,所述出料口连接所述旋转密封接头的一端;所述旋转密封接头的另一端连接有冷却筒。Further, the pyrolysis furnace is a cracking furnace, the sealing device comprises a rotary sealing joint, the discharge port is connected to one end of the rotary sealing joint, and the other end of the rotary sealing joint is connected with a cooling cylinder.
进一步的,所述进料口包括固体进料口、半流体及流体进料口。Further, the feed port includes a solid feed port, a semi-fluid, and a fluid feed port.
进一步的,所述裂解炉顶部设有油气出口和除尘装置。油气主要为轻质油和水蒸气,出来后的油气通过冷凝将水油分离,得到的油品可再次利用。除尘装置主要为湿式除尘装置,降低裂解炉中的粉尘。Further, the top of the cracking furnace is provided with an oil and gas outlet and a dust removing device. The oil and gas are mainly light oil and water vapor. After the oil and gas are discharged, the water and oil are separated by condensation, and the obtained oil can be reused. The dust removal device is mainly a wet dust removal device, which reduces the dust in the cracking furnace.
进一步的,所述裂解炉的炉体为矩形、圆形和管形中的任意一种。但不仅限于这几种,炉体的形状可根据具体的实际情况进行选择和设计。Further, the furnace body of the cracking furnace is any one of a rectangular shape, a circular shape and a tubular shape. However, it is not limited to these types, and the shape of the furnace body can be selected and designed according to specific conditions.
进一步的,所述裂解炉底部设有刮板。刮板主要用于对传送链带上的余料进行刮出,强化设备运行。Further, a scraper is disposed at the bottom of the cracking furnace. The scraper is mainly used to scrape the residual material on the conveyor chain to strengthen the operation of the equipment.
进一步的,所述低温区-高温区中包括低温区和高温区;所述烧嘴设置在所述全高温区或高温区的加热仓中。Further, the low temperature zone-high temperature zone includes a low temperature zone and a high temperature zone; and the burner is disposed in the heating chamber of the full high temperature zone or the high temperature zone.
进一步的,包括控制装置和传动动力装置,所述控制装置与所述传动动力装置电连;所述传动动力装置与传送链带连接。Further, the control device and the transmission power device are electrically connected, and the control device is electrically connected to the transmission power device; the transmission power device is connected to the transmission chain.
进一步的,所述固体进料口的前端连接有用于输送固体的固体传送带。Further, a solid conveyor belt for conveying solids is connected to the front end of the solid feed port.
进一步的,所述半流体及流体进料口的前端连接有用于输送半流体或流体的流体及半流体输送泵。Further, a fluid and a semi-fluid transfer pump for transporting a semi-fluid or a fluid is connected to the front end of the semi-fluid and fluid feed port.
进一步的,所述传动动力装置包括电机、减速器、主动轮和张紧轮,所述减速器分别与主动轮和电机连接;所述电机为交流变频无极调速电机;所述张紧轮设置在主动轮上,所述传送链带设置在所述主动轮和张紧轮之间。Further, the transmission power device comprises a motor, a speed reducer, a driving wheel and a tensioning wheel, wherein the speed reducer is respectively connected with the driving wheel and the motor; the motor is an AC variable frequency stepless speed regulating motor; the tensioning wheel is set On the drive wheel, the conveyor chain is disposed between the drive wheel and the tensioning wheel.
本发明工业连续化污油泥热分解设备,其有益效果在于:The industrial continuous chemical sludge thermal decomposition equipment of the invention has the beneficial effects of:
(1)在热解炉内部通过传送链带进行固体或半干固体的传送并裂解,避免了因炉体旋转而增加的能耗。采用传送链带传送裂解,更加节能。(1) The solid or semi-dry solids are transported and cracked by a conveyor chain inside the pyrolysis furnace, thereby avoiding an increase in energy consumption due to the rotation of the furnace body. Conveying the chain with a conveyor belt is more energy efficient.
(2)在热解炉中的传送链带沿竖直方向相互交错分布,增大了含油污泥在裂解炉中的停留时间,使热解更加充分;(2) The conveyor chains in the pyrolysis furnace are staggered in the vertical direction, which increases the residence time of the oily sludge in the cracking furnace, so that the pyrolysis is more sufficient;
(3)在热解炉中的传送链带沿竖直方向相互交错分布,缩短了设备长度,减小设备体积,节省设备投资。(3) The conveyor chains in the pyrolysis furnace are staggered in the vertical direction, which shortens the length of the equipment, reduces the size of the equipment, and saves equipment investment.
(4)采用交流变频无极调速电机调节传送链带的速率,有效控制热解速率和停留时间,精确控制尾渣的粒度和干燥度。(4) The AC variable frequency stepless speed regulating motor is used to adjust the speed of the conveyor chain, effectively control the pyrolysis rate and residence time, and accurately control the particle size and dryness of the tailings.
(5)在具有低温区-高温区的热解炉中,高温区设有烧嘴,而低温区未设置烧嘴,高温区的物料出来后直接进入低温区,由于低温区与进料口相邻,高温区出来的物料余热可对进料口后的低温区的原料进行加热,充分利用热能。可减少烧嘴的设置,同时节省能耗。采用热解含有污泥,将将油泥中的烃类物质进行气象进行收集,不产生大气污染,回收利用,绿色环保。(5) In the pyrolysis furnace with low temperature zone-high temperature zone, the high temperature zone is provided with a burner, while in the low temperature zone, the burner is not provided, and the material in the high temperature zone directly enters the low temperature zone, because the low temperature zone and the feed port phase Adjacent, the waste heat from the high temperature zone can heat the raw materials in the low temperature zone after the feed port, making full use of heat energy. It can reduce the setting of the burner while saving energy. The pyrolysis contains sludge, and the hydrocarbons in the sludge are collected in the meteorological environment without causing air pollution, recycling, and environmental protection.
为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动性的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the embodiments or the description of the prior art will be briefly described below. Obviously, the drawings in the following description are only It is a certain embodiment of the present invention, and other drawings can be obtained from those skilled in the art without any inventive labor.
图1是本发明中热解炉为全高温区的结构示意图;1 is a schematic view showing the structure of a pyrolysis furnace in a high temperature zone in the present invention;
图2是本发明中热解炉为低温区-高温区且低温区为两层的结构示意图;2 is a schematic view showing the structure of the pyrolysis furnace in the low temperature zone-high temperature zone and the low temperature zone in the present invention;
图3是本发明中热解炉为低温区-高温区且低温区为多层的结构示意图;3 is a schematic view showing the structure of the pyrolysis furnace in the low temperature zone-high temperature zone and the low temperature zone in the present invention;
1-裂解炉,2-加热仓,3-传送链带,4-全高温区,5-低温区,6-高温区,7-出料口,8-旋转密封接头,9-冷却筒,10-烧嘴,11-固体进料口、12-半流体及流体进料口,13-油气出口,14-固体传送带,15-流体及半流体输送泵,16-刮板,17-除尘装置,18-隔热板。1-cracking furnace, 2-heating bin, 3-transport chain, 4-full high temperature zone, 5-low temperature zone, 6-high temperature zone, 7-discharge port, 8-rotation sealing joint, 9-cooling cylinder, 10 - burner, 11-solid feed port, 12-semifluid and fluid feed port, 13-oil and gas outlet, 14-solid conveyor, 15-fluid and semi-fluid transfer pump, 16-scraper, 17-dust removal device, 18-insulation board.
下面结合具体实施例及附图来进一步详细说明本发明。The present invention will be further described in detail below in conjunction with the specific embodiments and the accompanying drawings.
实施例1Example 1
一种工业连续化污油泥热分解设备如图1所示,包括热解炉1和加热仓2,可根据需求将加热仓设置在热解炉的外侧的任何一侧、或两侧、或三侧、或四侧,本发明具体实施例1中,热解炉可优选为裂解炉1。而本实施例中的加热仓 2设置在裂解炉1下侧,裂解炉1前部设有进料口,进料口包括固体进料口11、半流体及流体进料口12,当原料为固体时,可通过固体输送设备直接输送,本发明具体实施例1中,优选使用固体传送带14进行直接输送;当原料为半流体或流体的时候,此时可用流体及半流体输送泵15对原料进行输送进料。裂解炉1内部包括全高温区4;裂解炉1内设有传送链带3,传送链带3的末端为出料口7,出料口7连接有密封装置,本发明具体实施例1中,密封装置优选包括旋转密封接头8,即出料口7可优选连接旋转密封接头8的一端,旋转密封接头8的另一端连接有冷却筒9;全高温区4内设有传送链带3,传送链带3包括至少两层,每层之间的传送链带3沿竖直方向相互交错分布;加热仓2内设有用于对裂解炉1的炉体加热的烧嘴10,烧嘴10与燃气输入装置连接。燃料可包括煤气、煤制气、天然气和燃料油等,且根据不同的燃料,烧嘴10进行相配合的更改。裂解炉1的炉体为矩形、圆形和管形中的任意一种,但不仅限于这几种,炉体的形状可根据具体的实际情况进行选择和设计。裂解炉1顶部设有油气出口13和除尘装置17。油气中包含水蒸气,出来后的油气通过冷凝将油水分离收集,得到的油品可再次利用。裂解炉1的底部设有刮板16,刮板16主要设置在靠近出料口7的地方,便于对出料口7处的传动链带上的尾料进行刮除,保障设备顺利运行。An industrial continuous sewage sludge thermal decomposition device is shown in Fig. 1, comprising a pyrolysis furnace 1 and a heating chamber 2, and the heating chamber can be disposed on either side of the pyrolysis furnace, or on both sides, or three according to requirements. On the side or the four sides, in the embodiment 1 of the present invention, the pyrolysis furnace may preferably be the cracking furnace 1. The heating chamber 2 in this embodiment is disposed on the lower side of the cracking furnace 1, and the front end of the cracking furnace 1 is provided with a feeding port, and the feeding port includes a solid feeding port 11, a semi-fluid and a fluid inlet port 12, when the raw material is In the case of a solid, it can be directly transported by a solid conveying device. In the specific embodiment 1, the solid conveying belt 14 is preferably used for direct conveying; when the raw material is semi-fluid or fluid, the fluid and semi-fluid conveying pump 15 can be used for the raw material. Carrying in the feed. The inside of the cracking furnace 1 includes a full-temperature zone 4; the cracking furnace 1 is provided with a conveyor chain 3, the end of the conveyor chain 3 is a discharge port 7, and the discharge port 7 is connected with a sealing device. In the specific embodiment 1, The sealing device preferably comprises a rotary sealing joint 8, ie the discharge opening 7 can preferably be connected to one end of the rotary sealing joint 8, the other end of the rotary sealing joint 8 is connected to the cooling cylinder 9; in the full high temperature zone 4 there is a conveyor chain 3, which is conveyed The chain belt 3 comprises at least two layers, and the conveyor chain belts 3 between each layer are staggered in a vertical direction; the heating chamber 2 is provided with a burner 10 for heating the furnace body of the cracking furnace 1, the burner 10 and the gas Input device connection. The fuel may include gas, coal gas, natural gas, fuel oil, etc., and the burners 10 are adapted to each other depending on the fuel. The furnace body of the cracking furnace 1 is any one of a rectangular shape, a circular shape and a tubular shape, but is not limited to these types, and the shape of the furnace body can be selected and designed according to specific actual conditions. The top of the cracking furnace 1 is provided with an oil and gas outlet 13 and a dust removing device 17. The oil and gas contain water vapor, and the oil and gas after the separation is separated and collected by condensation, and the obtained oil can be reused. The bottom of the cracking furnace 1 is provided with a scraper 16 which is mainly disposed near the discharge port 7 to facilitate scraping of the tailings on the drive chain belt at the discharge port 7, thereby ensuring smooth operation of the equipment.
而本发明对于传动链带的控制主要采用控制装置和传动动力装置,控制装置与传动动力装置电连;传动动力装置包括交流变频无极调速电机、减速器、主动轮和张紧轮,减速器分别与主动轮和电机连接;张紧轮设置在主动轮上,传送链带3设置在所述主动轮和张紧轮之间,主动轮转动,并通过摩擦力带动传动链带进行运动。而控制装置可直接控制交流变频无极调速电机的频率,继而控制减速器和主动轮的转速,达到控制原料在裂解炉1内的运行速率,保障尾渣的粒度和干燥度。The control of the transmission chain belt mainly adopts a control device and a transmission power device, and the control device is electrically connected with the transmission power device; the transmission power device comprises an AC variable frequency stepless speed regulation motor, a speed reducer, a driving wheel and a tensioning wheel, and a speed reducer. The driving wheel and the motor are respectively connected; the tensioning wheel is disposed on the driving wheel, the transmission chain belt 3 is disposed between the driving wheel and the tensioning wheel, the driving wheel rotates, and the transmission chain belt is driven to move by friction. The control device can directly control the frequency of the AC variable frequency stepless speed regulating motor, and then control the speed of the speed reducer and the driving wheel to control the running speed of the raw material in the cracking furnace 1 and ensure the granularity and dryness of the tailings.
实施例2Example 2
一种工业连续化污油泥热分解设备如图2和图3所示,包括热解炉1和加热仓2,可根据需求将加热仓设置在热解炉的外侧的任何一侧、或两侧、或三侧、或四侧,本发明具体实施例2中,热解炉可优选为裂解炉1。而本实施例中的加热仓2设置在裂解炉1下侧,裂解炉1前部设有进料口,进料口包括固体进料 口11、半流体及流体进料口12,当原料为固体时,可通过固体传送带14直接输送;当原料为半流体或流体的时候,此时可用流体及半流体输送泵15对原料进行输送进料。裂解炉1内部包括低温区-高温区;裂解炉1内设有传送链带3,传送链带3的末端为出料口7,出料口7连接有密封装置,本发明具体实施例2中,密封装置优选包括旋转密封接头8,即出料口7可优选连接旋转密封接头8的一端,旋转密封接头8的另一端连接有冷却筒9;低温区-高温区包括低温区5及高温区6,其中低温区5与进料口相邻,低温区与高温区之间设有传送链带3,低温区5与高温区6之间设有隔热板18,低温区5的传送链带3包括进料端和出料端;进料端和出料端的传送链带3均为至少一层,每层进料端和出料端的传送链带3之间沿竖直方向相互交错分布;高温区6的传送链带3为至少两层,高温区6的传送链带3在高温区6沿竖直方向相互交错分布;加热仓2内设有用于对裂解炉1的炉体加热的烧嘴10,烧嘴10主要设定在高温区6的下方,烧嘴10与燃气输入装置连接。燃料可包括煤气、煤制气、天然气和燃料油等,且根据不同的燃料,烧嘴10进行相配合的更改。裂解炉1的炉体为矩形、圆形和管形中的任意一种,但不仅限于这几种,炉体的形状可根据具体的实际情况进行选择和设计。裂解炉1顶部设有油气出口13和除尘装置17。油气中包含水蒸气,出来后的油气通过冷凝将油水分离收集,得到的油品可再次利用。裂解炉1的底部设有刮板16,刮板16主要设置在靠近出料口7的地方,便于对出料口7处的传动链带上的尾料进行刮除,保障设备顺利运行。An industrial continuous sewage sludge thermal decomposition device is shown in Fig. 2 and Fig. 3, and comprises a pyrolysis furnace 1 and a heating chamber 2, and the heating chamber can be disposed on either side or both sides of the outside of the pyrolysis furnace according to requirements. Or, on the three sides, or on the four sides, in the second embodiment of the present invention, the pyrolysis furnace may preferably be the cracking furnace 1. The heating chamber 2 in this embodiment is disposed on the lower side of the cracking furnace 1, and the front end of the cracking furnace 1 is provided with a feeding port, and the feeding port includes a solid feeding port 11, a semi-fluid and a fluid inlet port 12, when the raw material is When solid, it can be directly transported through the solid conveyor belt 14; when the raw material is semi-fluid or fluid, the raw material can be fed and fed by the fluid and semi-fluid transfer pump 15 at this time. The inside of the cracking furnace 1 includes a low temperature zone-high temperature zone; the cracking furnace 1 is provided with a conveyor chain belt 3, the end of the conveyor chain belt 3 is a discharge port 7, and the discharge port 7 is connected with a sealing device, in the second embodiment of the present invention The sealing device preferably comprises a rotary sealing joint 8, that is, the discharge opening 7 can preferably be connected to one end of the rotary sealing joint 8, and the other end of the rotary sealing joint 8 is connected with the cooling cylinder 9; the low temperature zone-high temperature zone includes the low temperature zone 5 and the high temperature zone 6, wherein the low temperature zone 5 is adjacent to the feed port, the transfer chain zone 3 is provided between the low temperature zone and the high temperature zone, the heat insulation board 18 is arranged between the low temperature zone 5 and the high temperature zone 6, and the conveyor chain zone of the low temperature zone 5 is provided. 3 comprising a feed end and a discharge end; the transfer chain 3 of the feed end and the discharge end are each at least one layer, and the transfer chain strips 3 at the feed end and the discharge end of each layer are staggered in a vertical direction; The conveyor belt 3 of the high temperature zone 6 is at least two layers, and the conveyor chain belts 3 of the high temperature zone 6 are staggered in the vertical direction in the high temperature zone 6; the heating compartment 2 is provided with a heating for heating the furnace body of the cracking furnace 1. The nozzle 10 is mainly disposed below the high temperature zone 6, and the burner 10 is connected to the gas input device. The fuel may include gas, coal gas, natural gas, fuel oil, etc., and the burners 10 are adapted to each other depending on the fuel. The furnace body of the cracking furnace 1 is any one of a rectangular shape, a circular shape and a tubular shape, but is not limited to these types, and the shape of the furnace body can be selected and designed according to specific actual conditions. The top of the cracking furnace 1 is provided with an oil and gas outlet 13 and a dust removing device 17. The oil and gas contain water vapor, and the oil and gas after the separation is separated and collected by condensation, and the obtained oil can be reused. The bottom of the cracking furnace 1 is provided with a scraper 16 which is mainly disposed near the discharge port 7 to facilitate scraping of the tailings on the drive chain belt at the discharge port 7, thereby ensuring smooth operation of the equipment.
而本发明对于传动链带的控制主要采用控制装置和传动动力装置,控制装置与所述传动动力装置电连;传动动力装置包括交流变频无极调速电机、减速器、主动轮和张紧轮,减速器分别与主动轮和电机连接;张紧轮设置在主动轮上,传送链带3设置在所述主动轮和张紧轮之间,主动轮转动,并通过摩擦力带动传动链带进行运动。而控制装置可直接控制交流变频无极调速电机的频率,继而控制减速器和主动轮的转速,达到控制原料在裂解炉1内的运行速率,保障尾渣的粒度和干燥度。The control of the transmission chain belt mainly adopts a control device and a transmission power device, and the control device is electrically connected with the transmission power device; the transmission power device comprises an AC variable frequency stepless speed regulating motor, a speed reducer, a driving wheel and a tensioning wheel, The reducer is respectively connected with the driving wheel and the motor; the tensioning wheel is disposed on the driving wheel, the transmission chain belt 3 is disposed between the driving wheel and the tensioning wheel, the driving wheel rotates, and the transmission chain belt is driven by friction . The control device can directly control the frequency of the AC variable frequency stepless speed regulating motor, and then control the speed of the speed reducer and the driving wheel to control the running speed of the raw material in the cracking furnace 1 and ensure the granularity and dryness of the tailings.
以上对本发明实施例所提供的技术方案进行了详细介绍,本文中应用了具体个例对本发明实施例的原理以及实施方式进行了阐述,以上实施例的说明只适用于帮助理解本发明实施例的原理;同时,对于本领域的一般技术人员,依 据本发明实施例,在具体实施方式以及应用范围上均会有改变之处,综上所述,本说明书内容不应理解为对本发明的限制。The technical solutions provided by the embodiments of the present invention are described in detail above. The principles and implementation manners of the embodiments of the present invention are described in the following. The description of the foregoing embodiments is only applicable to help understand the embodiments of the present invention. The present invention is not limited by the scope of the present invention, and the description of the present invention is not limited to the details of the present invention.
Claims (10)
- 一种工业连续化污油泥热分解设备,其特征在于:包括热解炉和加热仓,所述加热仓设置在热解炉外侧的任意一侧或几侧,所述热解炉前部设有进料口,所述热解炉内部包括全高温区或低温区-高温区;所述热解炉内设有传送链带,所述传送链带的末端为出料口,所述出料口连接密封装置;An industrial continuous sewage sludge thermal decomposition device, comprising: a pyrolysis furnace and a heating chamber, wherein the heating chamber is disposed on either side or sides of the pyrolysis furnace, and the front portion of the pyrolysis furnace is provided a feed port, the pyrolysis furnace includes a full high temperature zone or a low temperature zone-high temperature zone; the pyrolysis furnace is provided with a conveyor chain belt, and the end of the conveyor chain belt is a discharge port, and the discharge port Connecting the sealing device;所述全高温区内设有传送链带,所述传送链带包括至少两层,所述每层之间的传送链带沿竖直方向相互交错分布;a conveyor chain belt is disposed in the full high temperature region, the conveyor chain belt includes at least two layers, and the transmission chain belts between the layers are staggered in a vertical direction;所述低温区-高温区包括低温区及高温区,所述低温区与进料口相邻,所述低温区与高温区之间均设有传送链带,所述低温区与高温区之间设有隔热板,所述低温区的传送链带包括进料端和出料端;所述进料端和出料端的传送链带均为至少一层,所述每层进料端和出料端的传送链带之间沿竖直方向相互交错分布;所述高温区内的传送链带为至少两层,所述高温区内的传送链带在高温区沿竖直方向相互交错分布;The low temperature zone-high temperature zone includes a low temperature zone and a high temperature zone, the low temperature zone is adjacent to the feed port, and a transfer chain belt is disposed between the low temperature zone and the high temperature zone, and between the low temperature zone and the high temperature zone Provided with a heat insulation panel, the conveyor belt of the low temperature zone comprises a feed end and a discharge end; the conveyor chain of the feed end and the discharge end are at least one layer, and the feed end and the outlet of each layer The conveyor chain belts of the material end are staggered in a vertical direction; the conveyor chain belts in the high temperature zone are at least two layers, and the conveyor chain belts in the high temperature zone are staggered in a vertical direction in a high temperature zone;所述加热仓内设有用于对热解炉的炉体加热的烧嘴,所述烧嘴与燃料输入装置连接。A burner for heating the furnace body of the pyrolysis furnace is provided in the heating chamber, and the burner is connected to the fuel input device.
- 根据权利要求1所述的工业连续化污油泥热分解设备,其特征在于:所述热解炉为裂解炉,所述密封装置包括旋转密封接头,所述出料口连接所述旋转密封接头的一端;所述旋转密封接头的另一端连接有冷却筒。The industrial continuous sewage sludge thermal decomposition apparatus according to claim 1, wherein the pyrolysis furnace is a cracking furnace, the sealing device comprises a rotary sealing joint, and the discharge port is connected to the rotary sealing joint. One end; the other end of the rotary sealing joint is connected with a cooling cylinder.
- 根据权利要求2所述的工业连续化污油泥热分解设备,其特征在于:所述进料口包括固体进料口、半流体及流体进料口。The industrial continuous sewage sludge thermal decomposition apparatus according to claim 2, wherein the feed port comprises a solid feed port, a semi-fluid, and a fluid feed port.
- 根据权利要求2所述的工业连续化污油泥热分解设备,其特征在于:所述裂解炉顶部设有油气出口和除尘装置。The industrial continuous sewage sludge thermal decomposition apparatus according to claim 2, characterized in that the top of the cracking furnace is provided with an oil and gas outlet and a dust removing device.
- 根据权利要求2所述的工业连续化污油泥热分解设备,其特征在于:所述裂解炉的炉体为矩形、圆形和管形中的任意一种。The industrial continuous sewage sludge thermal decomposition apparatus according to claim 2, wherein the furnace body of the cracking furnace is any one of a rectangular shape, a circular shape and a tubular shape.
- 根据权利要求2所述工业连续化污油泥热分解设备,其特征在于:所述烧嘴设置在所述全高温区或高温区的加热仓中。The industrial continuous sewage sludge thermal decomposition apparatus according to claim 2, wherein the burner is disposed in the heating chamber of the high temperature zone or the high temperature zone.
- 根据权利要求2所述工业连续化污油泥热分解设备,其特征在于:包括控制装置和传动动力装置,所述控制装置与所述传动动力装置电连;所述传动动力装置与传送链带连接。The industrial continuous sewage sludge thermal decomposition apparatus according to claim 2, comprising: a control device and a transmission power device, wherein said control device is electrically connected to said transmission power device; said transmission power device is connected to a transmission chain .
- 根据权利要求3所述工业连续化污油泥热分解设备,其特征在于:所述 固体进料口的前端连接有用于输送固体的固体输送设备。The industrial continuous sewage sludge thermal decomposition apparatus according to claim 3, wherein a solid conveying means for conveying solids is connected to the front end of said solid feed port.
- 根据权利要求3所述工业连续化污油泥热分解设备,其特征在于:所述半流体及流体进料口的前端连接有用于输送半流体或流体的流体及半流体输送泵。The industrial continuous sewage sludge thermal decomposition apparatus according to claim 3, characterized in that the front end of the semi-fluid and fluid feed port is connected with a fluid for transporting a semi-fluid or a fluid and a semi-fluid transfer pump.
- 根据权利要求7所述工业连续化污油泥热分解设备,其特征在于:所述传动动力装置包括电机、减速器、主动轮和张紧轮,所述减速器分别与主动轮和电机连接;所述电机为交流变频无极调速电机;所述张紧轮设置在主动轮上,所述传送链带设置在所述主动轮和张紧轮之间。The industrial continuous sewage sludge thermal decomposition apparatus according to claim 7, wherein the transmission power unit comprises a motor, a speed reducer, a driving wheel and a tensioning wheel, and the speed reducer is respectively connected to the driving wheel and the motor; The motor is an AC variable frequency stepless speed regulating motor; the tensioning wheel is disposed on the driving wheel, and the transmission chain belt is disposed between the driving wheel and the tensioning wheel.
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