WO2008092374A1 - A belt-type agitating multilevel sludge drying device with recycled secondary steam - Google Patents
A belt-type agitating multilevel sludge drying device with recycled secondary steam Download PDFInfo
- Publication number
- WO2008092374A1 WO2008092374A1 PCT/CN2008/000161 CN2008000161W WO2008092374A1 WO 2008092374 A1 WO2008092374 A1 WO 2008092374A1 CN 2008000161 W CN2008000161 W CN 2008000161W WO 2008092374 A1 WO2008092374 A1 WO 2008092374A1
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- WIPO (PCT)
- Prior art keywords
- sludge
- belt
- hollow
- secondary steam
- tray
- Prior art date
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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
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
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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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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B17/00—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
- F26B17/02—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by belts carrying the materials; with movement performed by belts or elements attached to endless belts or chains propelling the materials over stationary surfaces
Definitions
- the utility model relates to a sludge drying device, in particular to a multi-stage secondary steam recycling drying device with belt type stirring sludge.
- the sludge heat treatment has a high capacity reduction rate, and the sludge can be disposed in a large amount and quickly, and is harmless and thoroughly developed in recent years.
- the water content is as high as about 80%, and the calorific value is very low.
- 304 ⁇ 565L of heavy oil should be added per ton of dry-based sludge, which consumes a lot of energy.
- the dried sludge has a higher calorific value and can approach the calorific value of the inferior coal. Therefore, heating and dehydrating the sludge after mechanical dewatering and increasing the calorific value of the sludge are the key technologies for sludge fueling.
- the existing belt type sludge single-stage drying device is composed of a sludge agitation conveying machine, a heating chamber and an evaporation chamber.
- the sludge sent to the evaporation chamber is heated by the agitation conveyor to the heat exchange chamber, and the secondary steam is evaporated in the evaporation chamber to be dried.
- the heat source of the heating chamber is provided by a heating system external to the device, and the secondary steam is provided by A separate cooling system outside the unit condenses into water and a small amount of exhaust.
- the thermal energy of lkg water vapor can only evaporate about lkg of sludge water.
- the secondary steam generated by sludge evaporation still has a relatively high calorific value, but it is not conducive to transportation due to its low pressure. And the presence of contaminants in which the applicability is limited, etc., is directly taken out of the drying device for condensation treatment, and its energy is not fully utilized, resulting in a large loss of heat energy in the drying system. Therefore, the development of an energy-saving sludge drying device is an important part of the sludge fueling technology, and it is critical to realize sludge recycling, reduction, and harmlessness.
- the purpose of the utility model is to provide a novel belt-type mixed sludge multi-stage secondary steam reuse drying device with high efficiency, low energy consumption, low investment, and convenient continuous large-scale production in view of the deficiencies of the prior art.
- the utility model comprises a body.
- the top of the body is provided with a feeding mechanism
- the bottom is provided with a discharging mechanism
- the feeding mechanism is provided with a hopper.
- the multi-layer rectangular hollow tray is arranged flat in the body, the three edges of the hollow tray are matched and fixedly connected with the inner wall, and the other edge forms a discharge opening with the inner wall, and the outlet of each hollow tray is arranged at a hollow interval. The two edges of the tray correspond. Empty per floor
- the space above the heart tray is the sludge evaporation chamber.
- the hollow tray as a sludge heating chamber includes a top heating plate and a bottom portion partition plate, and the heating plate and the partition plate are connected by a baffle plate in a vertical direction.
- the baffle is serpentine or labyrinth, and the heating plate, the partition plate and the baffle are enclosed to form a serpentine or labyrinth heat source medium flow channel.
- the starting end of the heat source medium flow channel in the hollow tray of the bottom layer communicates with the heat source through the pipeline, and the sludge evaporation chamber of the top layer communicates with the outside through the pipeline.
- the starting end of the heat source medium flow passage in the remaining hollow trays is connected to the sludge evaporation chamber below it through a pipeline.
- a belt conveyor is disposed on the upper portion of each hollow tube.
- the feeding mechanism is one of a screw conveyor, a scraper conveyor, a chain conveyor, a belt conveyor, and a piston push rod.
- the discharging mechanism is one of a screw conveyor, a scraper conveyor, a chain conveyor, a belt conveyor, and a piston push rod.
- the belt conveying device is one of a chain conveyor, a steel belt conveyor and a mesh belt conveyor, and the feeding direction is a direction toward the discharge opening.
- the terminating end of the heat source medium flow passage in each of the hollow trays is provided with a drain pipe and an exhaust pipe which communicate with the outside.
- the multi-stage secondary steam reuse drying device with belt type agitating sludge of the utility model realizes the directed conveying of sludge by means of mechanical agitation, and can realize the heat exchange stroke of the sludge and the heat exchange of the multi-stage secondary steam heating chamber.
- the utility model only participates in the heat exchange of the final heating chamber with a small amount of external heating source, and indirectly heats the sludge in the final evaporation chamber to evaporate the secondary steam of the sludge, and the secondary steam is reused as the upper heating chamber.
- the heat source participates in the heat exchange of the upper heating chamber; and so on, the secondary steam of the evaporation chamber at each level is utilized step by step until the first stage evaporation chamber.
- the sludge is gradually evaporated in the evaporation chamber of each stage and gradually dried.
- the secondary steam in the evaporation chamber of each level is reused to participate in the heat exchange of the upper heating chamber, and is condensed into water and a small amount of exhaust gas, and the hydrophobic and exhaust gases are discharged from the device.
- the secondary vapor of the first stage evaporation chamber can be directly discharged and cooled by the condenser to water and a small amount of tail gas. Since the exhaust gas has a foul odor, it needs to be sent to the deodorization system for purification. After the secondary steam is concentrated, it is disposed of separately.
- the utility model fully utilizes the secondary steam of the multi-stage evaporation chamber to make the external heating source energy of 1kg of water vapor, and can evaporate about 2 ⁇ 5kg of sludge water, and the energy saving effect is very remarkable.
- FIG. 1 is a schematic structural view of an embodiment of the present invention
- Figure 2 is a cross-sectional view of the A-A of Figure 1.
- the belt-type agitated sludge multi-stage secondary steam reuse drying device of the present invention comprises a sealed body 4 which is externally insulated.
- a screw conveyor 2 and a hopper 1 are disposed at the upper end of the body 4, and a screw conveyor 7 is disposed at the lower end of the body 4.
- Three layers of hollow trays are horizontally disposed in the body 4, and a space above each of the hollow trays is a sludge evaporation chamber 11.
- the hollow tray as a sludge heating chamber includes a top heating plate 10 and a bottom portion partition 8, which is connected to the partition plate 8 by a labyrinth baffle 9 in the vertical direction.
- the heating plate 10, the partitioning plate 8, and the baffle 9 are enclosed to form a labyrinth heat source medium flow path 6.
- the three edges of each hollow tray are matched and fixedly connected with the inner wall of the body 4, and the other edge forms a discharge opening 5 with the inner wall of the body 4, wherein the outlets 5 of the top and bottom layers are in the same position, and the position of the discharge opening 5 of the intermediate layer is The opposite.
- a chain conveyor 3 is disposed on the upper portion of each hollow tube, and the feeding direction is the direction toward the discharge opening 5.
- the starting end of the heat source medium flow path 6 in the hollow tray of the bottom layer communicates with the heat source through the pipeline, and the sludge evaporation chamber 11 of the top layer communicates with the outside through the pipeline.
- the starting end of the heat source medium flow passage 6 in the hollow tray of the top layer and the intermediate layer is connected to the sludge evaporation chamber 11 below it through a pipeline, and the end of the heat source medium flow passage 6 is provided with a discharge pipe and an exhaust pipe which communicate with the outside. .
- Step 1 The sludge is sent to the sludge secondary steam to be reused in the drying device hopper.
- Step 2 The sludge is continuously fed into the primary sludge evaporation chamber by means of a screw conveyor under the hopper.
- Step 3 The sludge in the first-stage sludge evaporation chamber is transported by the chain conveyor, the sludge is laid on the heating plate and continuously turned, and the sludge absorbs the heat energy of the first-stage heating chamber while moving along the heating plate, and evaporates.
- the secondary steam is discharged, and the sludge is turned to the discharge port, and is dropped by gravity into the secondary evaporation chamber.
- the secondary vapor of the primary evaporation chamber can be directly exported from the pipeline.
- the sludge was first dried.
- Step 4 The sludge in the secondary evaporation chamber is transported by the chain conveyor, the sludge is laid on the heating plate and continuously turned, and the sludge absorbs the heat energy of the secondary heating chamber while moving along the heating plate, and evaporates The secondary steam, and the sludge is turned to the discharge port, and is dropped by gravity into the tertiary evaporation chamber.
- the secondary vapor of the stage evaporation chamber is connected to the beginning of the heat source medium flow path of the primary heating chamber through the pipeline.
- the secondary steam of the stage is introduced into the primary heating chamber for use as a heat source to participate in the heat exchange of the heating plate, and the exhaust gas after the heat exchange is led out by the exhaust pipe, and the hydrophobicity is led out by the discharge pipe.
- the sludge was dried in two stages.
- Step 5 The sludge in the third-stage evaporation chamber is transported by the chain conveyor, the sludge is laid on the heating plate and continuously turned, and the sludge absorbs the heat energy of the three-stage heating chamber along the movement of the heating plate, and evaporates two Secondary steam, and the sludge is turned to the discharge port, which is dropped by gravity into the silo, and the dried product is
- the screw conveyor is sent out to complete the entire sludge drying process.
- the secondary vapor of the stage evaporation chamber is connected to the beginning end of the heat source medium flow path of the secondary heating chamber through a pipeline.
- the secondary steam of the stage is introduced into the secondary heating chamber for use as a heat source to participate in the heat exchange of the heating plate, and the exhaust gas after the heat exchange is led out by the exhaust pipe, and the hydrophobicity is led out by the discharge pipe.
- the sludge was dried in three stages. Since the heating chamber of this stage is the final stage, it is necessary to connect external external heating sources such as steam, heat transfer oil, flue gas and hot air through pipes.
- the multi-stage secondary steam reuse drying device of the belt type agitating sludge of the utility model has the advantages that compared with the existing sludge drying device,
- the belt type agitation conveying structure is adopted, and the secondary steam of the sludge can be reused for multi-stage drying, the system is simple and reliable, the installation power of the device is low, and the power consumption of the plant is saved.
- the oxygen content of the device is very low, which reduces the danger of spontaneous combustion and explosion of dust.
- the external heating source is heated indirectly, and the amount of exhaust gas treatment is small.
- the drying device is in a negative pressure operation state, and no odor is leaked.
- the material has wide adaptability and is suitable for drying (including granulation) of various chemical products and mineral products, especially suitable for slurry materials.
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- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Drying Of Solid Materials (AREA)
- Treatment Of Sludge (AREA)
Abstract
A belt-type agitating multilevel sludge drying device with recycled secondary steam, includes a main body (4), a feeding mechanism provided on the top of the main body (4), and a discharging mechanism provided at the bottom of the main body (4). A hopper (1) is set on the feeding mechanism. Multi-layer rectangle hollow trays are provided inside the main body (4). Three rims of the hollow tray are connected in matching and fixed way with the inner wall of the main body (4). Another rim forms a discharging outlet (5) with the inner wall of the main body (4). The discharging outlet (5) of each layer of hollow tray is alternately provided on the two opposite rims of the hollow tray. A sludge evaporator cell (11) is set in the space over each layer of the hollow tray. The hollow tray comprises a top heating board (10) and a bottom separating board (8). The top heating board (10) and the bottom separating board (8) are connected by vertical baffles (9) to form a heating source media flow passage (6). The start edge of the heating source media flow passage (6) in bottom layer is connected to a heat source by pipeline. The sludge evaporator cell (11) in top layer is connected to outside by pipeline. The start edges of the heating source media flow passages (6) in other layersare connected to the lower sludge evaporator cells (11) by pipeline. A belt-type delivery mechanism (3) is provided on the upper portion of each layer of hollow tray.
Description
带型搅拌污泥多级二次蒸汽回用干燥装置 技术领域 Multi-stage secondary steam reuse drying device with belt type stirring sludge
本实用新型涉及一种污泥干燥装置, 尤其涉及一种带型搅拌污泥多级 二次蒸汽回用干燥装置。 The utility model relates to a sludge drying device, in particular to a multi-stage secondary steam recycling drying device with belt type stirring sludge.
背景技术 Background technique
污泥热处理具有很高的减容率, 且可以大量、 迅速地处置污泥, 无害 化彻底, 近几年得到快速发展。 但由于机械脱水后的湿污泥, 含水率高达 约 80%, 热值很低, 若直接焚烧, 每吨干基污泥需添加 304〜565L重油, 能耗大。 而干燥后的污泥热值较高, 可接近劣质煤的热值水平。 因此, 对 机械脱水后的污泥进行加热脱水干燥, 提升污泥热值, 是污泥燃料化的关 键技术。 The sludge heat treatment has a high capacity reduction rate, and the sludge can be disposed in a large amount and quickly, and is harmless and thoroughly developed in recent years. However, due to the wet sludge after mechanical dewatering, the water content is as high as about 80%, and the calorific value is very low. If it is directly incinerated, 304~565L of heavy oil should be added per ton of dry-based sludge, which consumes a lot of energy. The dried sludge has a higher calorific value and can approach the calorific value of the inferior coal. Therefore, heating and dehydrating the sludge after mechanical dewatering and increasing the calorific value of the sludge are the key technologies for sludge fueling.
现有的带型污泥单级干燥装置由污泥搅拌输送机械、加热室和蒸发室 组成。 送入蒸发室的污泥, 借助搅拌输送机械实现与加热室的换热行程, 在蒸发室蒸发出二次蒸汽而干燥, 加热室的热源由装置外另设的加热系统 提供, 二次蒸汽由装置外另设的冷却系统冷凝成水和少量尾气。 利用单级 干燥装置, 折合 lkg水蒸气的热能, 只能蒸发出约 lkg的污泥水分, 污泥 蒸发产生的二次蒸汽, 仍具有相当高的热值, 却由于其压力低而不利于输 送, 并且其中存在污染物而使其应用性受到局限等原因, 被直接引出干燥 装置外冷凝处理, 其能量未能得到充分利用, 造成了干燥系统热能大量损 耗。 因此, 节能的污泥干燥装置的开发, 是实现污泥燃料化技术的重要内 容, 对实现污泥资源化、 减量化、 无害化极其关键。 The existing belt type sludge single-stage drying device is composed of a sludge agitation conveying machine, a heating chamber and an evaporation chamber. The sludge sent to the evaporation chamber is heated by the agitation conveyor to the heat exchange chamber, and the secondary steam is evaporated in the evaporation chamber to be dried. The heat source of the heating chamber is provided by a heating system external to the device, and the secondary steam is provided by A separate cooling system outside the unit condenses into water and a small amount of exhaust. Using a single-stage drying device, the thermal energy of lkg water vapor can only evaporate about lkg of sludge water. The secondary steam generated by sludge evaporation still has a relatively high calorific value, but it is not conducive to transportation due to its low pressure. And the presence of contaminants in which the applicability is limited, etc., is directly taken out of the drying device for condensation treatment, and its energy is not fully utilized, resulting in a large loss of heat energy in the drying system. Therefore, the development of an energy-saving sludge drying device is an important part of the sludge fueling technology, and it is critical to realize sludge recycling, reduction, and harmlessness.
发明内容 Summary of the invention
本实用新型的目的是针对现有技术的不足,提供一种效率高、能耗少、 投资省和便于实现连续化规模化生产的新型带型搅拌污泥多级二次蒸汽 回用干燥装置。 The purpose of the utility model is to provide a novel belt-type mixed sludge multi-stage secondary steam reuse drying device with high efficiency, low energy consumption, low investment, and convenient continuous large-scale production in view of the deficiencies of the prior art.
本实用新型包括本体。 本体顶部设置有给料机构, 底部设置有出料机 构, 给料机构上设置有料斗。 多层矩形空心塔板平面设置在本体内, 空心 塔板三个边沿与本体内壁配合并固定连接, 另一边沿与本体内壁形成出料 口, 每层空心塔板的出料口间隔设置在空心塔板对应的两个边沿。 每层空
心塔板上方空间为污泥蒸发室。空心塔板作为污泥加热室包括顶部加热板 和底部分隔板, 加热板与分隔板通过竖直方向的折流板连接。 所述的折流 板为蛇形或迷宫形, 加热板、 分隔板和折流板围合形成蛇形或迷宫形热源 介质流道。底层的空心塔板中的热源介质流道的起始端通过管路与热源连 通, 顶层的污泥蒸发室通过管路与外界连通。 其余各层空心塔板中的热源 介质流道的起始端与其下方的污泥蒸发室通过管路连通。每层空心塔板上 部设置有带式输送装置。 The utility model comprises a body. The top of the body is provided with a feeding mechanism, the bottom is provided with a discharging mechanism, and the feeding mechanism is provided with a hopper. The multi-layer rectangular hollow tray is arranged flat in the body, the three edges of the hollow tray are matched and fixedly connected with the inner wall, and the other edge forms a discharge opening with the inner wall, and the outlet of each hollow tray is arranged at a hollow interval. The two edges of the tray correspond. Empty per floor The space above the heart tray is the sludge evaporation chamber. The hollow tray as a sludge heating chamber includes a top heating plate and a bottom portion partition plate, and the heating plate and the partition plate are connected by a baffle plate in a vertical direction. The baffle is serpentine or labyrinth, and the heating plate, the partition plate and the baffle are enclosed to form a serpentine or labyrinth heat source medium flow channel. The starting end of the heat source medium flow channel in the hollow tray of the bottom layer communicates with the heat source through the pipeline, and the sludge evaporation chamber of the top layer communicates with the outside through the pipeline. The starting end of the heat source medium flow passage in the remaining hollow trays is connected to the sludge evaporation chamber below it through a pipeline. A belt conveyor is disposed on the upper portion of each hollow tube.
所述的给料机构为螺旋输送机、 刮板输送机、 链板输送机、 皮带输送 机、 活塞推杆中的一种。 The feeding mechanism is one of a screw conveyor, a scraper conveyor, a chain conveyor, a belt conveyor, and a piston push rod.
所述的出料机构为螺旋输送机、 刮板输送机、 链板输送机、 皮带输送 机、 活塞推杆中的一种。 The discharging mechanism is one of a screw conveyor, a scraper conveyor, a chain conveyor, a belt conveyor, and a piston push rod.
所述的带式输送装置为链板输送机、 钢带输送机、 网带输送机中的一 种, 其送料方向为向出料口方向。 The belt conveying device is one of a chain conveyor, a steel belt conveyor and a mesh belt conveyor, and the feeding direction is a direction toward the discharge opening.
所述的各层空心塔板中的热源介质流道的终止端设置有与外界连通 的放水管和排气管。 The terminating end of the heat source medium flow passage in each of the hollow trays is provided with a drain pipe and an exhaust pipe which communicate with the outside.
本实用新型的带型搅拌污泥多级二次蒸汽回用干燥装置, 以机械搅拌 为手段实现污泥定向输送, 能实现污泥换热行程与多级二次蒸汽加热室换 热。 本实用新型仅以少量的外加热源参与末级加热室换热, 将末级蒸发室 中的污泥进行间接加热蒸发出污泥二次蒸汽, 该二次蒸汽被回用作为上一 级加热室的热源参与上级加热室换热; 依次类推, 实现各级蒸发室二次蒸 汽的逐级利用, 直至第一级蒸发室。 污泥在各级蒸发室中被不断蒸发出二 次蒸汽而逐渐干燥。各级蒸发室的二次蒸汽被回用参与上一级加热室换热 后, 冷凝为水和少量尾气, 疏水和尾气均排出装置。 第一级蒸发室的二次 蒸汽可直接排出, 经冷凝器冷却为水和少量尾气。 由于尾气具有恶臭, 需 送往脱臭系统净化处理。 二次蒸汽疏水集中后另作处置。 本实用新型由于 充分回用了多级蒸发室的污泥二次蒸汽, 使折合 1kg水蒸气的外加热源能 量, 可蒸发出约 2〜5kg的污泥水分, 节能效果非常显著。 The multi-stage secondary steam reuse drying device with belt type agitating sludge of the utility model realizes the directed conveying of sludge by means of mechanical agitation, and can realize the heat exchange stroke of the sludge and the heat exchange of the multi-stage secondary steam heating chamber. The utility model only participates in the heat exchange of the final heating chamber with a small amount of external heating source, and indirectly heats the sludge in the final evaporation chamber to evaporate the secondary steam of the sludge, and the secondary steam is reused as the upper heating chamber. The heat source participates in the heat exchange of the upper heating chamber; and so on, the secondary steam of the evaporation chamber at each level is utilized step by step until the first stage evaporation chamber. The sludge is gradually evaporated in the evaporation chamber of each stage and gradually dried. The secondary steam in the evaporation chamber of each level is reused to participate in the heat exchange of the upper heating chamber, and is condensed into water and a small amount of exhaust gas, and the hydrophobic and exhaust gases are discharged from the device. The secondary vapor of the first stage evaporation chamber can be directly discharged and cooled by the condenser to water and a small amount of tail gas. Since the exhaust gas has a foul odor, it needs to be sent to the deodorization system for purification. After the secondary steam is concentrated, it is disposed of separately. The utility model fully utilizes the secondary steam of the multi-stage evaporation chamber to make the external heating source energy of 1kg of water vapor, and can evaporate about 2~5kg of sludge water, and the energy saving effect is very remarkable.
附图说明 DRAWINGS
图 1为本实用新型一实施例的结构示意图; 1 is a schematic structural view of an embodiment of the present invention;
图 2为图 1的 A- A剖面示意图。 Figure 2 is a cross-sectional view of the A-A of Figure 1.
具体实施方式
如图 1和图 2所示, 本实用新型的带型搅拌污泥多级二次蒸汽回用干 燥装置包括外保温的密闭本体 4。 在本体 4上端设有螺旋输送机 2和料斗 1, 本体 4下端设置有螺旋输送机 7。 本体 4内水平设置有三层空心塔板, 每层空心塔板的上方空间为污泥蒸发室 11。空心塔板作为污泥加热室包括 顶部加热板 10和底部分隔板 8, 加热板 10与分隔板 8通过竖直方向的迷 宫形折流板 9连接。加热板 10、分隔板 8和折流板 9围合形成迷宫形热源 介质流道 6。 每层空心塔板三个边沿与本体 4内壁配合并固定连接, 另一 边沿与本体 4内壁形成出料口 5, 其中顶层和底层的出料口 5位置相同, 中间层出料口 5的位置与其相反。每层空心塔板上部设置有链板输送机 3, 其送料方向为向出料口 5方向。底层的空心塔板中的热源介质流道 6的起 始端通过管路与热源连通, 顶层的污泥蒸发室 11 通过管路与外界连通。 顶层和中间层的空心塔板中热源介质流道 6的起始端与其下方的污泥蒸发 室 11通过管路连通, 热源介质流道 6的终止端设置有与外界连通的放水 管和排气管。 detailed description As shown in FIG. 1 and FIG. 2, the belt-type agitated sludge multi-stage secondary steam reuse drying device of the present invention comprises a sealed body 4 which is externally insulated. A screw conveyor 2 and a hopper 1 are disposed at the upper end of the body 4, and a screw conveyor 7 is disposed at the lower end of the body 4. Three layers of hollow trays are horizontally disposed in the body 4, and a space above each of the hollow trays is a sludge evaporation chamber 11. The hollow tray as a sludge heating chamber includes a top heating plate 10 and a bottom portion partition 8, which is connected to the partition plate 8 by a labyrinth baffle 9 in the vertical direction. The heating plate 10, the partitioning plate 8, and the baffle 9 are enclosed to form a labyrinth heat source medium flow path 6. The three edges of each hollow tray are matched and fixedly connected with the inner wall of the body 4, and the other edge forms a discharge opening 5 with the inner wall of the body 4, wherein the outlets 5 of the top and bottom layers are in the same position, and the position of the discharge opening 5 of the intermediate layer is The opposite. A chain conveyor 3 is disposed on the upper portion of each hollow tube, and the feeding direction is the direction toward the discharge opening 5. The starting end of the heat source medium flow path 6 in the hollow tray of the bottom layer communicates with the heat source through the pipeline, and the sludge evaporation chamber 11 of the top layer communicates with the outside through the pipeline. The starting end of the heat source medium flow passage 6 in the hollow tray of the top layer and the intermediate layer is connected to the sludge evaporation chamber 11 below it through a pipeline, and the end of the heat source medium flow passage 6 is provided with a discharge pipe and an exhaust pipe which communicate with the outside. .
具体工作流程如下: The specific workflow is as follows:
步骤一: 将污泥送入污泥二次蒸汽回用干燥装置料斗。 Step 1: The sludge is sent to the sludge secondary steam to be reused in the drying device hopper.
步骤二: 利用料斗下方的螺旋输送机将污泥定量连续送入一级污泥蒸 发室。 Step 2: The sludge is continuously fed into the primary sludge evaporation chamber by means of a screw conveyor under the hopper.
步骤三: 一级污泥蒸发室中的污泥借助链板输送机的输送, 将污泥平 铺在加热板上并不断翻动, 污泥沿加热板边运动边吸收一级加热室热能, 蒸发出二次蒸汽, 并将污泥翻动到出料口, 由重力作用掉到二级蒸发室。 一级蒸发室的二次蒸汽可直接由管路导出。 污泥得到了一级干燥。 Step 3: The sludge in the first-stage sludge evaporation chamber is transported by the chain conveyor, the sludge is laid on the heating plate and continuously turned, and the sludge absorbs the heat energy of the first-stage heating chamber while moving along the heating plate, and evaporates. The secondary steam is discharged, and the sludge is turned to the discharge port, and is dropped by gravity into the secondary evaporation chamber. The secondary vapor of the primary evaporation chamber can be directly exported from the pipeline. The sludge was first dried.
步骤四: 二级蒸发室中的污泥借助链板输送机的输送, 将污泥平铺在 加热板上并不断翻动, 污泥沿加热板边运动边吸收二级加热室热能, 蒸发 出二次蒸汽, 并将污泥翻动到出料口, 由重力作用掉到三级蒸发室。 该级 蒸发室二次蒸汽通过管路连通一级加热室的热源介质流道的起始端。 由 此, 该级二次蒸汽被导入一级加热室回用作为热源参与加热板换热, 换热 后的尾气由排气管导出, 疏水由放水管导出。 污泥得到了二级干燥。 Step 4: The sludge in the secondary evaporation chamber is transported by the chain conveyor, the sludge is laid on the heating plate and continuously turned, and the sludge absorbs the heat energy of the secondary heating chamber while moving along the heating plate, and evaporates The secondary steam, and the sludge is turned to the discharge port, and is dropped by gravity into the tertiary evaporation chamber. The secondary vapor of the stage evaporation chamber is connected to the beginning of the heat source medium flow path of the primary heating chamber through the pipeline. Therefore, the secondary steam of the stage is introduced into the primary heating chamber for use as a heat source to participate in the heat exchange of the heating plate, and the exhaust gas after the heat exchange is led out by the exhaust pipe, and the hydrophobicity is led out by the discharge pipe. The sludge was dried in two stages.
步骤五: 三级蒸发室中的污泥借助链板输送机的输送, 将污泥平铺在 加热板上并不断翻动, 污泥沿加热板边运动边吸收三级加热室热能, 蒸发 出二次蒸汽, 并将污泥翻动到出料口, 由重力作用掉到料仓, 干燥产品经
螺旋输送机送出, 最终完成整个污泥干燥过程。 该级蒸发室二次蒸汽通过 管路连通二级加热室的热源介质流道的起始端。 由此, 该级二次蒸汽被导 入二级加热室回用作为热源参与加热板换热, 换热后的尾气由排气管导 出, 疏水由放水管导出。 污泥得到了三级干燥。 由于该级加热室为末级, 需要通过管路连接外界的外加热源如蒸汽、 导热油、 烟气和热风等。 Step 5: The sludge in the third-stage evaporation chamber is transported by the chain conveyor, the sludge is laid on the heating plate and continuously turned, and the sludge absorbs the heat energy of the three-stage heating chamber along the movement of the heating plate, and evaporates two Secondary steam, and the sludge is turned to the discharge port, which is dropped by gravity into the silo, and the dried product is The screw conveyor is sent out to complete the entire sludge drying process. The secondary vapor of the stage evaporation chamber is connected to the beginning end of the heat source medium flow path of the secondary heating chamber through a pipeline. Therefore, the secondary steam of the stage is introduced into the secondary heating chamber for use as a heat source to participate in the heat exchange of the heating plate, and the exhaust gas after the heat exchange is led out by the exhaust pipe, and the hydrophobicity is led out by the discharge pipe. The sludge was dried in three stages. Since the heating chamber of this stage is the final stage, it is necessary to connect external external heating sources such as steam, heat transfer oil, flue gas and hot air through pipes.
本实用新型的带型搅拌污泥多级二次蒸汽回用千燥装置与现有污泥 干燥装置相比, 其优点在于- The multi-stage secondary steam reuse drying device of the belt type agitating sludge of the utility model has the advantages that compared with the existing sludge drying device,
( 1 ) 采用带型搅拌输送结构,并能实现污泥二次蒸汽回用于多级干燥, 系统简单可靠, 装置装机功率低, 节省厂用电。 (1) The belt type agitation conveying structure is adopted, and the secondary steam of the sludge can be reused for multi-stage drying, the system is simple and reliable, the installation power of the device is low, and the power consumption of the plant is saved.
(2 ) 污泥二次蒸汽导出流程短, 阻力小, 不易在蒸发室中重新冷凝液 化而使污泥返潮。 (2) The secondary steam exporting process of sludge is short, the resistance is small, and it is not easy to recondense and liquefy in the evaporation chamber to make the sludge return to moisture.
( 3 ) 搅拌面覆盖各级加热板, 板面不易粘结。 (3) The stirring surface covers the heating plates at all levels, and the surface of the plate is not easy to bond.
(4) 装置含氧量非常低, 降低了粉尘自燃和爆炸等危险, 外加热源间 接加热, 尾气处理量很少。 (4) The oxygen content of the device is very low, which reduces the danger of spontaneous combustion and explosion of dust. The external heating source is heated indirectly, and the amount of exhaust gas treatment is small.
( 5 ) 多级蒸发室的污泥二次蒸汽能量得到充分利用, 使得污泥干燥利 用外加热源耗量极少, 节能效果非常显著。 (5) The secondary steam energy of the sludge in the multi-stage evaporation chamber is fully utilized, so that the sludge drying is limited by the external heating source, and the energy saving effect is very remarkable.
( 6 ) 污泥进入干燥装置前无需造粒, 使得干燥系统大大简化。 (6) The granulation is not required before the sludge enters the drying unit, which greatly simplifies the drying system.
( 7) 干燥装置处于负压运行状态, 无臭气外泄。 (7) The drying device is in a negative pressure operation state, and no odor is leaked.
( 8 ) 物料适应性广, 对多种化工产品和矿产品的干燥 (含造粒) 同样 适用, 尤其适合于浆状物料。 (8) The material has wide adaptability and is suitable for drying (including granulation) of various chemical products and mineral products, especially suitable for slurry materials.
( 9) 调节方便。 通过改变级数、 搅拌输送机构型式、 搅拌速度等, 调 节污泥物料的停留时间, 达到干燥产品的要求。
(9) Easy to adjust. By changing the number of stages, the type of mixing mechanism, the stirring speed, etc., the residence time of the sludge material is adjusted to meet the requirements of the dry product.
Claims
1、 带型搅拌污泥多级二次蒸汽回用干燥装置, 包括本体, 其特征在 于本体顶部设置有给料机构, 底部设置有出料机构, 给料机构上设置有料 斗; 多层矩形空心塔板平面设置在本体内, 空心塔板三个边沿与本体内壁 配合并固定连接, 另一边沿与本体内壁形成出料口, 每层空心塔板的出料 口间隔设置在空心塔板对应的两个边沿; 每层空心塔板上方空间为污泥蒸 发室; 空心塔板作为污泥加热室包括顶部加热板和底部分隔板, 加热板与 分隔板通过竖直方向的折流板连接; 所述的折流板为蛇形或迷宫形, 加热 板、 分隔板和折流板围合形成蛇形或迷宫形热源介质流道; 底层的空心塔 板中的热源介质流道的起始端通过管路与热源连通, 顶层的污泥蒸发室通 过管路与外界连通; 其余各层空心塔板中的热源介质流道的起始端与其下 方的污泥蒸发室通过管路连通; 每层空心塔板上部设置有带式输送装置。 1. A multi-stage secondary steam reuse drying device with a belt type agitating sludge, comprising a body, characterized in that a feeding mechanism is arranged at the top of the body, a discharging mechanism is arranged at the bottom, and a hopper is arranged on the feeding mechanism; The tray plane is disposed in the body, the three edges of the hollow tray are matched and fixedly connected with the inner wall of the body, and the other edge forms a discharge port with the inner wall of the inner wall, and the outlet of each hollow tray is arranged at intervals corresponding to the hollow tray. Two edges; the space above each hollow tray is a sludge evaporation chamber; the hollow tray serves as a sludge heating chamber including a top heating plate and a bottom partition, and the heating plate and the partition plate are connected by a vertical baffle The baffle plate is serpentine or labyrinth, and the heating plate, the partition plate and the baffle plate are enclosed to form a serpentine or labyrinth heat source medium flow channel; the heat source medium flow channel in the bottom hollow plate The beginning end communicates with the heat source through the pipeline, and the sludge evaporation chamber of the top layer communicates with the outside through the pipeline; the starting end of the heat source medium flow passage in the remaining hollow trays and the sludge evaporation below it It communicates through a line; hollow upper portion of each tray is provided with a belt conveyor apparatus.
2、 如权利要求 1所述的带型搅拌污泥多级二次蒸汽回用干燥装置, 其特征在于所述的给料机构为螺旋输送机、 刮板输送机、 链板输送机、 皮 带输送机、 活塞推杆中的一种。 2. The belt-type agitated sludge multi-stage secondary steam reuse drying device according to claim 1, wherein the feeding mechanism is a screw conveyor, a scraper conveyor, a chain conveyor, and a belt conveyor. One of the machine and piston push rods.
3、 如权利要求 1所述的带型搅拌污泥多级二次蒸汽回用干燥装置, 其特征在于所述的出料机构为螺旋输送机、 刮板输送机、 链板输送机、 皮 带输送机、 活塞推杆中的一种。 3. The belt-type agitated sludge multi-stage secondary steam reuse drying device according to claim 1, wherein the discharging mechanism is a screw conveyor, a scraper conveyor, a chain conveyor, and a belt conveyor. One of the machine and piston push rods.
4、 如权利要求 1所述的带型搅拌污泥多级二次蒸汽回用干燥装置, 其特征在于所述的带式输送装置为链板输送机、 钢带输送机、 网带输送机 中的一种, 其送料方向为向出料口方向。 4. The belt type agitating sludge multi-stage secondary steam recycling drying device according to claim 1, wherein the belt conveying device is a chain conveyor, a steel belt conveyor, and a mesh belt conveyor. One type, the feeding direction is the direction of the discharge port.
5、 如权利要求 1所述的带型搅拌污泥多级二次蒸汽回用干燥装置, 其特征在于所述的各层空心塔板中的热源介质流道的终止端设置有与外 界连通的放水管和排气管。
5. The belt-type agitated sludge multi-stage secondary steam reuse drying apparatus according to claim 1, wherein the end of the heat source medium flow passage in each of the hollow trays is provided with a connection with the outside. Drain pipe and exhaust pipe.
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EP2301896A1 (en) * | 2009-09-09 | 2011-03-30 | Dormeyer, Roland | Drying device for sewage sludge |
RU2459164C1 (en) * | 2011-03-29 | 2012-08-20 | Государственное образовательное учреждение высшего профессионального образования "Белгородский государственный технологический университет им. В.Г. Шухова" | Drier |
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