CN105758152B - Temperature air-source heat pump tower drier - Google Patents

Temperature air-source heat pump tower drier Download PDF

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CN105758152B
CN105758152B CN201610266909.0A CN201610266909A CN105758152B CN 105758152 B CN105758152 B CN 105758152B CN 201610266909 A CN201610266909 A CN 201610266909A CN 105758152 B CN105758152 B CN 105758152B
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heat pump
source heat
temperature air
outer cylinder
outlet
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CN105758152A (en
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程烨
朱景申
庞俊峰
李兴书
冯云鹏
闫小广
李长彬
李霖
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HENAN BAIHENG ENERGY SAVING TECHNOLOGY Co Ltd
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HENAN BAIHENG ENERGY SAVING TECHNOLOGY Co Ltd
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B17/00Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
    • F26B17/12Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed solely by gravity, i.e. the material moving through a substantially vertical drying enclosure, e.g. shaft
    • F26B21/25
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B25/00Details of general application not covered by group F26B21/00 or F26B23/00
    • F26B25/005Treatment of dryer exhaust gases
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/10Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Drying Of Solid Materials (AREA)

Abstract

本发明公开了高温空气源热泵立式烘干机,它包括炉体,进料口和出料口,炉体上设置有上部进风热口和下部进热风口,炉体的中部设置有废气出气口,废气出气口上对接有管道,炉体为双圆筒结构,双圆筒结构由外圆筒、内环筒构成,外圆筒沿上部进风口和下部进风口的中间区域设有内外通透的气孔,气孔的外部焊接有一个集气罩,外圆筒的内壁上分层排列有翅圈,外圆筒里套装有内环筒两者间隙配合构成料层,炉体的底部用隔板均匀隔出出料单元,每个出料单元上对应安装有卸料装置,内环筒为网状结构,立式烘干机的中部安装有检测物料温度的热电偶。烘热温度在90°左右,更加适合低燃点物料的烘干,并且余热可重复循环利用,是一种节能环保的清洁能源烘干机。

The invention discloses a high-temperature air source heat pump vertical dryer, which comprises a furnace body, a material inlet and a material outlet. The gas outlet and the exhaust gas outlet are connected with pipes. The furnace body is a double-cylinder structure. The double-cylinder structure is composed of an outer cylinder and an inner ring cylinder. Permeable air hole, the outside of the air hole is welded with a gas collecting cover, the inner wall of the outer cylinder is layered with fin rings, the outer cylinder is set with an inner ring tube, and the gap between the two forms a material layer. The bottom of the furnace body is used The partitions evenly separate the discharge units, each discharge unit is equipped with a discharge device, the inner ring is a mesh structure, and the middle of the vertical dryer is installed with a thermocouple to detect the temperature of the material. The drying temperature is about 90°, which is more suitable for drying materials with low ignition point, and the waste heat can be recycled repeatedly. It is an energy-saving and environmentally friendly clean energy dryer.

Description

高温空气源热泵立式烘干机High temperature air source heat pump vertical dryer

技术领域:Technical field:

本发明涉及烘干机领域,特别适用于低温烘干、余热回收利用一种高温空气源热泵立式烘干机。The invention relates to the field of dryers, in particular a high-temperature air source heat pump vertical dryer suitable for low-temperature drying and waste heat recovery and utilization.

背景技术:Background technique:

立式烘干机又称立式干燥机,其被广泛应用至型煤、水泥、化肥、煤化工等生产过程中对物料的烘干,具有占地小、投资少和运行稳定的特点。Vertical dryer, also known as vertical dryer, is widely used to dry materials in the production process of briquette, cement, fertilizer, coal chemical industry, etc. It has the characteristics of small footprint, low investment and stable operation.

近年来,经过不断的发展和改进,市场上可见的立式烘干机已经多种多样,其中公开号为CN167361A的中国专利申请公开的立式烘干机就是诸多立式烘干机中的一种。该立式烘干机包括筒体以及设于筒体中的挡料圈和扬料圈,挡料圈为从上向下逐渐变大的锥套,其位于筒体的中心处并且与筒体同轴线设置,挡料圈的外壁面与筒体的内壁面之间形成物料通道;扬料圈为从上向下逐渐缩小的锥套形,固定在筒体的内壁面上并且与筒体同轴线设置。在使用该立式烘干机时,物料从筒体的顶部落入筒体中并沿挡料圈与筒体内壁面之间形成的物料通道落下,热风通过筒体上所设的进风口通入挡料圈中,相邻两挡料圈之间的间隙形成热风的出口,物料在下落的过程中被通过热风出口吹出的热风烘干。但不适合低温烘干的要求。In recent years, through continuous development and improvement, there are many kinds of vertical dryers available on the market. Among them, the vertical dryer disclosed in the Chinese patent application with publication number CN167361A is one of many vertical dryers. kind. The vertical dryer includes a cylinder and a retaining ring and a lifting ring arranged in the cylinder. The retaining ring is a tapered sleeve that gradually becomes larger from top to bottom, which is located at the center of the cylinder and connected to the cylinder. The coaxial line is set, and the material channel is formed between the outer wall surface of the retaining ring and the inner wall surface of the cylinder; Coaxial setup. When using the vertical dryer, the material falls into the cylinder from the top of the cylinder and falls along the material channel formed between the material retaining ring and the inner wall of the cylinder, and the hot air enters through the air inlet on the cylinder. In the material retaining ring, the gap between two adjacent material retaining rings forms a hot air outlet, and the material is dried by the hot air blown through the hot air outlet during the falling process. But it is not suitable for low temperature drying requirements.

其次目前大多数立式烘干机的供热热源都是采用燃煤或燃气,这种供热方式最大的危害就是高污染,排放大量的二氧化碳,对空气造成严重的污染,其次经过收尘器从烘干机排放到大气的废气温度在100℃左右,余热废气直接排空不能得到回收利用,耗费了大量的可利用能源,这显然限制了立式烘干机的长远可持续发展前景。燃煤和燃气的热值较高,不适合低燃点物料的烘干,容易造成着火事故,不利于安全生产。Secondly, at present, the heating source of most vertical dryers is coal or gas. The biggest hazard of this heating method is high pollution, which emits a large amount of carbon dioxide and causes serious pollution to the air. Secondly, it passes through the dust collector. The temperature of the exhaust gas discharged from the dryer to the atmosphere is about 100°C, and the waste heat exhaust gas cannot be recycled directly, which consumes a lot of available energy, which obviously limits the long-term sustainable development prospects of the vertical dryer. The calorific value of coal and gas is high, which is not suitable for drying materials with low ignition point, which may easily cause fire accidents and is not conducive to safe production.

通过以上对上述立式烘干机的工作原理的描述可知,影响其烘干物料品种、效率和发展前景的主要因素有两个,即其物料的受热面积、受热均匀性与采用热源的形式。From the above description of the working principle of the above-mentioned vertical dryer, it can be seen that there are two main factors affecting the variety, efficiency and development prospects of its drying materials, namely, the heating area of the material, the uniformity of heating and the form of the heat source used.

针对前者来说,为了提高烘干效率,只能将筒体的直径加大,这种方式虽然能够在一定程度上提高产量,但是不利于物料的顺畅流动,同时进风受热面积受到限制。For the former, in order to improve the drying efficiency, the diameter of the cylinder can only be increased. Although this method can increase the output to a certain extent, it is not conducive to the smooth flow of materials, and the heating area of the air inlet is limited.

针对后者,如果想要适应低燃点物料的烘干、回收排放的废气余热和使用清洁能源,目前,现有技术中还没有关于使用低温热源和清洁能源来烘干易燃物料的信息。For the latter, if you want to adapt to the drying of materials with low ignition point, recover the waste heat of exhaust gas and use clean energy, at present, there is no information about the use of low-temperature heat source and clean energy to dry flammable materials in the prior art.

发明内容:Invention content:

本发明的任务是提出一种既有效利用余热又节省了大量的能源消耗,同时又降低环境污染的高温空气源热泵立式烘干机。The task of the present invention is to propose a high-temperature air source heat pump vertical dryer which not only effectively utilizes waste heat but also saves a lot of energy consumption and reduces environmental pollution.

本发明的任务是这样完成的,它包括炉体,进料口和出料口,其特征在于:所述炉体上设置有上部进热风口和下部进热风口,炉体的中部设置有废气出气口,废气出气口上对接有管道,炉体为双圆筒结构,双圆筒结构由外圆筒、内环筒构成,所述外圆筒沿上部进热风口和下部进热风口的中间区域设有内外通透的气孔,所述气孔的外部焊接有一个集气罩,外圆筒的内壁上分层排列有翅圈,所述外圆筒里套装有内环筒两者间隙配合构成料层,炉体的底部用隔板均匀隔出出料单元,每个所述出料单元上对应安装有卸料装置,所述内环筒为网状结构,所述立式烘干机的中部安装有检测物料温度的热电偶。废气出气口上对应的管道的另一端连有除尘器,所述除尘器的出口通过管道与高温空气源热泵系统的进口相连构成废气回收管路,所述高温空气源热泵系统的出口通过管路分别与炉体上设置的上、下部进热风口相连构成送风管路,除尘器的出口处和高温空气源热泵系统的出口之间连有旁路管道。气孔的布置是均匀分布形成多个废气出口,所述集气罩的安装位置与外圆筒上开的气孔上下对应构成密闭的废气通道。所述内环筒的头部呈锥形,底部为平面,外炉体的头部为平面,其底部为锥形料斗。所述高温空气源热泵系统由压缩机、冷凝器、膨胀阀、蒸发器、循环风机、干燥过滤器、分液分离器、储液罐、保温箱体、送风管道和废气回收管道构成。所述高温空气源热泵位于炉体的外部安装。The task of the present invention is accomplished in this way, which includes a furnace body, a feed port and a discharge port, and is characterized in that: the furnace body is provided with an upper hot air inlet and a lower hot air inlet, and the middle part of the furnace body is provided with a waste gas The gas outlet and the waste gas outlet are connected with pipes, and the furnace body is a double-cylinder structure. The double-cylinder structure is composed of an outer cylinder and an inner ring cylinder. There are internal and external air holes in the area, and a gas collecting cover is welded on the outside of the air holes, and fin rings are arranged in layers on the inner wall of the outer cylinder, and the inner ring tube is set in the outer cylinder. The material layer, the bottom of the furnace body is evenly separated from the discharge unit by a partition, each of the discharge units is correspondingly equipped with a discharge device, the inner ring cylinder is a mesh structure, and the vertical dryer A thermocouple for detecting the temperature of the material is installed in the middle. The other end of the corresponding pipeline on the exhaust gas outlet is connected with a dust collector, and the outlet of the dust collector is connected to the inlet of the high-temperature air source heat pump system through a pipeline to form an exhaust gas recovery pipeline, and the outlet of the high-temperature air source heat pump system passes through the pipeline They are respectively connected with the upper and lower hot air inlets provided on the furnace body to form an air supply pipeline, and a bypass pipeline is connected between the outlet of the dust collector and the outlet of the high-temperature air source heat pump system. The arrangement of air holes is evenly distributed to form a plurality of exhaust gas outlets, and the installation position of the gas collecting hood corresponds to the upper and lower sides of the air holes opened on the outer cylinder to form a closed exhaust gas channel. The head of the inner ring tube is conical and the bottom is flat, and the head of the outer furnace body is flat and the bottom is a conical hopper. The high-temperature air source heat pump system is composed of a compressor, a condenser, an expansion valve, an evaporator, a circulating fan, a dry filter, a liquid separator, a liquid storage tank, an insulation box, an air supply pipe and an exhaust gas recovery pipe. The high temperature air source heat pump is installed outside the furnace body.

本发明具有以下效果:烘热温度在90°左右,更加适合低燃点物料的烘干,并且余热可重复循环利用,是一种节能环保的清洁能源烘干机。The invention has the following effects: the drying temperature is about 90°, which is more suitable for drying materials with low ignition point, and the waste heat can be recycled repeatedly. It is an energy-saving and environment-friendly clean energy dryer.

附图说明:Description of drawings:

图1是本高温空气源热泵立式烘干机结构示意图;图2是高温空气源立式烘干机系统结构示意图;图3是图2的俯视图。Fig. 1 is a schematic structural diagram of the high-temperature air source heat pump vertical dryer; Fig. 2 is a schematic structural diagram of the high-temperature air source vertical dryer system; Fig. 3 is a top view of Fig. 2 .

图面说明:1、外圆筒,2、上部进热风口,3、集气罩,4、翅圈,5、热电偶,6、下部进热风口,7、出气口,8、内环筒,9、卸料装置,10、下料斗,11、隔板,12、立式烘干机,13、除尘器,14、高温空气源热泵系统,15、管道,16、旁路管道。Drawing description: 1. Outer cylinder, 2. Upper hot air inlet, 3. Air collecting hood, 4. Fin ring, 5. Thermocouple, 6. Lower hot air inlet, 7. Air outlet, 8. Inner ring cylinder , 9, unloading device, 10, lower hopper, 11, clapboard, 12, vertical dryer, 13, dust collector, 14, high temperature air source heat pump system, 15, pipeline, 16, bypass pipeline.

具体实施方式:detailed description:

本技术方案涉及的立式烘干机12结构更加合理,物料进风受热面积大大提高,更加符合烘干低燃点物料,同时采用高温空气源热泵做热源,烘干机的废气又会收到热泵系统,余热得到充分利用,形成一个闭路循环的热风系统;热风温度在90°左右,特别适合低燃点物料的烘干,具体实施例如图1所示,高温空气源热泵立式烘干机12包括由炉体,所述炉体上设置有上部进热风口2和下部进热风口6,炉体的中部设置有废气出气口7,废气出气口上对接有管道15,管道15的另一端连有除尘器13,所述除尘器的出口通过管道与高温空气源热泵系统14的进口相连构成废气回收管路,所述高温空气源热泵系统的出口通过管路分别与炉体上设置的上、下部进热风口相连构成送风管路,除尘器的出口处和高温空气源热泵系统的出口之间连有旁路管道16。The structure of the vertical dryer 12 involved in this technical solution is more reasonable, and the material intake air heating area is greatly increased, which is more suitable for drying low-ignition materials. system, the waste heat is fully utilized to form a closed-circuit circulation hot air system; the hot air temperature is about 90°, which is especially suitable for drying materials with low ignition points. The specific implementation is shown in Figure 1. The high-temperature air source heat pump vertical dryer 12 includes From the furnace body, the upper hot air inlet 2 and the lower hot air inlet 6 are arranged on the furnace body, the middle part of the furnace body is provided with a waste gas outlet 7, and a pipe 15 is connected to the waste gas outlet, and the other end of the pipe 15 is connected with a Dust collector 13, the outlet of the dust collector is connected to the inlet of the high-temperature air source heat pump system 14 through pipelines to form a waste gas recovery pipeline, and the outlet of the high-temperature air source heat pump system is respectively connected to the upper and lower parts of the furnace body through pipelines. The hot air inlets are connected to form an air supply pipeline, and a bypass pipeline 16 is connected between the outlet of the dust collector and the outlet of the high-temperature air source heat pump system.

所述高温空气源热泵系统由压缩机、冷凝器、膨胀阀、蒸发器、循环风机、干燥过滤器、分液分离器、储液罐、保温箱体、送风管道和废气回收管道构成,以上所述的是现有技术在这里不再详述。The high-temperature air source heat pump system is composed of a compressor, a condenser, an expansion valve, an evaporator, a circulating fan, a dry filter, a liquid separator, a liquid storage tank, an insulated box, an air supply pipeline and an exhaust gas recovery pipeline, the above What is described is the prior art and will not be described in detail here.

所述高温空气源热泵位于炉体的外部安装。The high temperature air source heat pump is installed outside the furnace body.

所述炉体的顶部是入料口,其底部是出料口,炉体为双圆筒结构,双圆筒结构由外圆筒1、内环筒8构成,所述外圆筒沿上部进热风口2和下部进热风口6的中间区域设有内外通透的气孔,气孔的布置是均匀分布形成多个废气出气口,所述气孔的外部焊接有一个集气罩3,进一步说,集气罩的安装位置与外圆筒上开的气孔上下对应构成密闭的废气通道,废气集于废气通道里由炉体上设置的出气风口排出炉体外,外圆筒的内壁上分层排列有翅圈4,目的是物料进入外筒后用于挡料和有顺序的交替错落出料,不堵塞,再者有利于排气,所述外圆筒里套装有内环筒两者间隙配合构成料层,内环筒的头部呈锥形,底部为平面,外炉体的头部为平面,其底部为锥形下料斗10,炉体 的底部用隔板11均匀隔出出料单元,方便物料有顺序的下料,所述每个出料单元上对应安装有卸料装置9。The top of the furnace body is a material inlet, and the bottom is a material outlet. The furnace body is a double-cylinder structure. The double-cylinder structure is composed of an outer cylinder 1 and an inner ring cylinder 8. The outer cylinder enters along the top The middle area between the hot air outlet 2 and the lower hot air inlet 6 is provided with internal and external air holes, and the air holes are evenly distributed to form a plurality of exhaust gas outlets. An air collecting cover 3 is welded outside the air holes. Further, the air collecting The installation position of the gas hood corresponds to the upper and lower sides of the air holes opened on the outer cylinder to form a closed exhaust gas channel. The exhaust gas is collected in the exhaust gas channel and discharged out of the furnace through the outlet air outlet set on the furnace body. The inner wall of the outer cylinder is arranged in layers. Ring 4, the purpose is that after the material enters the outer cylinder, it is used to block the material and alternately stagger the material in an orderly manner, without clogging, and it is also conducive to exhaust. The outer cylinder is fitted with an inner ring cylinder to form a material Layer, the head of the inner ring cylinder is conical, the bottom is flat, the head of the outer furnace body is flat, the bottom is a conical lower hopper 10, and the bottom of the furnace body is evenly separated by a partition 11 to separate the discharge unit, which is convenient The materials are unloaded sequentially, and each unloading unit is correspondingly equipped with an unloading device 9 .

所述内环筒8为网状结构,网孔可以是圆孔、长孔等,根据物料最小粒度确定和选择,目的是保证物料进入外圆筒内热风透风面积更加均匀,所述炉体上、下部设置的进热风口延伸至内环筒内,从上、下部进热风口进入的热风在内环筒聚集均匀从网孔向外圆筒扩散,从而保证物料上下受热温度均匀。The inner ring cylinder 8 has a mesh structure, and the mesh holes can be round holes, long holes, etc., which are determined and selected according to the minimum particle size of the material. The purpose is to ensure that the hot air ventilation area of the material entering the outer cylinder is more uniform. , The hot air inlet set at the lower part extends into the inner ring cylinder, and the hot air entering the inner ring cylinder from the upper and lower hot air inlets gathers evenly and diffuses from the mesh to the outer cylinder, thus ensuring that the material is heated evenly at the upper and lower sides.

本发明所述立式烘干机的中部安装有检测物料温度的热电偶5,热电偶的安装数量至少两个以上。The middle part of the vertical dryer of the present invention is installed with a thermocouple 5 for detecting the temperature of the material, and the number of thermocouples installed is at least two or more.

本发明特别是涉及利用低温烘干、余热回收的一种高温空气源热泵立式烘干机及使用该烘干机的烘干系统。高温空气源热泵立式烘干机包括竖式炉体和设于炉体中的导料通风部件,炉体的下部和上部具有热风进口,所述炉体外部还设有高温空气源热泵为烘干机供热除湿,所述高温空气源热泵系统由压缩机、冷凝器、膨胀阀、蒸发器、循环风机、干燥过滤器、气液分离器、储液罐、保温箱体、送风管道和废气回收管道组成。其特征在于:所述高温空气源热泵位于炉体的外部。由于该空气源热泵立式烘干机的炉体具有上下两个热风进口,并且热源是采用高温空气源热泵,因此,在使用的时候,大量的热空气从上部进入炉体中首先与物料进行热交换并被自外而内的干燥,少量的热空气从底部进入与即将干燥的物料进行热交换,使物料在排出炉体前彻底干燥。中部设有出风口,经热交换后排出的废气由回风道进入收尘器除尘后分成两路,一路由旁路管道直接回到烘干机内进行循环利用,一路进入热泵系统,余热由热泵系统进行回收提升,回风内的水蒸气由蒸发器冷凝排出。这样既有效利用了余热节省了大量的能源消耗,同时又降低了环境污染,是一种清洁能源的立式烘干系统。In particular, the invention relates to a high-temperature air source heat pump vertical dryer utilizing low-temperature drying and waste heat recovery and a drying system using the dryer. The high temperature air source heat pump vertical dryer includes a vertical furnace body and a material guide and ventilation part arranged in the furnace body. The lower and upper parts of the furnace body have hot air inlets. Dryer heat supply and dehumidification, the high temperature air source heat pump system consists of a compressor, a condenser, an expansion valve, an evaporator, a circulating fan, a dry filter, a gas-liquid separator, a liquid storage tank, an insulation box, an air supply pipe and Exhaust gas recovery pipeline composition. It is characterized in that the high temperature air source heat pump is located outside the furnace body. Since the furnace body of the air source heat pump vertical dryer has upper and lower hot air inlets, and the heat source is a high-temperature air source heat pump, when in use, a large amount of hot air enters the furnace body from the upper part and firstly interacts with the materials. The heat is exchanged and dried from the outside to the inside. A small amount of hot air enters from the bottom to exchange heat with the material to be dried, so that the material is completely dried before being discharged from the furnace. There is an air outlet in the middle. The exhaust gas discharged after heat exchange enters the dust collector through the return air duct and is divided into two paths. One path is directly returned to the dryer for recycling through the bypass pipe, and the other path enters the heat pump system. The heat pump system performs recovery and upgrading, and the water vapor in the return air is condensed and discharged by the evaporator. This not only effectively utilizes the waste heat, saves a lot of energy consumption, but also reduces environmental pollution. It is a clean energy vertical drying system.

Claims (6)

1. temperature air-source heat pump tower drier, it includes body of heater, charging aperture and discharging opening, it is characterised in that:The body of heater On be provided with top hot air inlet and bottom hot air inlet, be provided with waste gas gas outlet in the middle part of body of heater, it is right on waste gas gas outlet Pipeline is connected to, body of heater is double cylindrical structures, and double cylindrical structures are made up of outer cylinder, endocyclic tube, and the outer cylinder enters heat along top Air port and the intermediate region of bottom hot air inlet are provided with inside and outside penetrating stomata, and the outside weldings of the stomata have a gas collection Cover, the inwall higher slice of outer cylinder are arranged with wing circle, and both endocyclic tubes gap is set with the outer cylinder and coordinates the composition bed of material, The bottom of body of heater is uniformly separated out discharging unit with dividing plate, and device for discharging is correspondingly provided with each discharging unit, described interior Ring cylinder is network structure, and the thermocouple of detection temperature of charge is provided with the middle part of the tower drier.
2. temperature air-source heat pump tower drier according to claim 1, it is characterised in that:It is corresponding on waste gas gas outlet The other end of pipeline be connected with deduster, the outlet of the deduster passes through pipeline and the import phase of temperature air-source heat pump system Even form waste gas recovery pipeline, the temperature air-source heat pump system outlet by pipeline respectively with set on body of heater it is upper, Bottom hot air inlet, which is connected, forms air supply pipeline, is connected between the exit of deduster and the outlet of temperature air-source heat pump system Bypass duct.
3. temperature air-source heat pump tower drier according to claim 1, it is characterised in that:The arrangement of stomata is uniform Distribution forms multiple waste gas outlets, and corresponding composition is closed up and down with the stomata opened in outer cylinder for the installation site of the gas skirt Exhaust steam passage.
4. temperature air-source heat pump tower drier according to claim 1, it is characterised in that:The head of the endocyclic tube Tapered, bottom is plane, and the head of external furnace body is plane, and its bottom is broach hopper.
5. temperature air-source heat pump tower drier according to claim 2, it is characterised in that:The temperature air-source heat Pumping system is by compressor, condenser, expansion valve, evaporator, circulating fan, device for drying and filtering, liquid separation separator, fluid reservoir, guarantor Incubator body, air supply duct and exhaust gas recovery conduit are formed.
6. temperature air-source heat pump tower drier according to claim 2, it is characterised in that:The temperature air-source heat Pump is located at the outside installation of body of heater.
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Families Citing this family (5)

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Publication number Priority date Publication date Assignee Title
CN106524691A (en) * 2016-12-29 2017-03-22 成都智胜达节能环保科技有限公司 Mixed-flow mosquito-repellent incense drying device and mosquito-repellent incense drying system
CN111678298A (en) * 2020-07-08 2020-09-18 开原市天诚干燥设备有限公司 Heat Pump Drying System
CN113983766A (en) * 2021-09-26 2022-01-28 山东汇凯莱机械设备有限公司 High-efficiency pipeline type suspension flash drying technology and equipment
CN115540520A (en) * 2022-05-18 2022-12-30 郭赛娇 Drying equipment is used in preparation of high-efficient industrial enzyme
CN118705827A (en) * 2024-07-03 2024-09-27 邵武鼎盛机械制造有限公司 Circulating air drying method

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4004351A (en) * 1975-07-28 1977-01-25 Gilmore-Tatge Manufacturing Co., Inc. Grain drying apparatus
CN203100394U (en) * 2013-03-04 2013-07-31 河南省德耀节能科技有限公司 Vertical-type drying machine achieving bidirectional air inflow
CN103759516A (en) * 2014-01-06 2014-04-30 新乡仲德能源科技有限公司 Vertical drying machine uniform in air distribution
CN103759517A (en) * 2014-01-06 2014-04-30 新乡仲德能源科技有限公司 Multichannel vertical dryer
CN203657397U (en) * 2014-01-06 2014-06-18 新乡仲德能源科技有限公司 Drainable vertical dryer
CN205747852U (en) * 2016-04-27 2016-11-30 河南佰衡节能科技股份有限公司 Temperature air-source heat pump tower drier

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8356420B2 (en) * 2009-03-09 2013-01-22 The Gsi Group, Llc Adjustable divider/hopper for a grain tower dryer
US8601714B2 (en) * 2010-07-14 2013-12-10 The Gsi Group, Llc Grain turner for tower grain dryer and method of drying

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4004351A (en) * 1975-07-28 1977-01-25 Gilmore-Tatge Manufacturing Co., Inc. Grain drying apparatus
CN203100394U (en) * 2013-03-04 2013-07-31 河南省德耀节能科技有限公司 Vertical-type drying machine achieving bidirectional air inflow
CN103759516A (en) * 2014-01-06 2014-04-30 新乡仲德能源科技有限公司 Vertical drying machine uniform in air distribution
CN103759517A (en) * 2014-01-06 2014-04-30 新乡仲德能源科技有限公司 Multichannel vertical dryer
CN203657397U (en) * 2014-01-06 2014-06-18 新乡仲德能源科技有限公司 Drainable vertical dryer
CN205747852U (en) * 2016-04-27 2016-11-30 河南佰衡节能科技股份有限公司 Temperature air-source heat pump tower drier

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