WO2019219040A1 - Vacuum drying apparatus - Google Patents

Vacuum drying apparatus Download PDF

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Publication number
WO2019219040A1
WO2019219040A1 PCT/CN2019/087120 CN2019087120W WO2019219040A1 WO 2019219040 A1 WO2019219040 A1 WO 2019219040A1 CN 2019087120 W CN2019087120 W CN 2019087120W WO 2019219040 A1 WO2019219040 A1 WO 2019219040A1
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WO
WIPO (PCT)
Prior art keywords
drying
tank
vacuum
drying tank
heat recovery
Prior art date
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PCT/CN2019/087120
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French (fr)
Chinese (zh)
Inventor
周本留
白树生
许德运
Original Assignee
山东名流餐处装备股份有限公司
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Publication of WO2019219040A1 publication Critical patent/WO2019219040A1/en

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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B11/00Machines or apparatus for drying solid materials or objects with movement which is non-progressive
    • F26B11/12Machines or apparatus for drying solid materials or objects with movement which is non-progressive in stationary drums or other mainly-closed receptacles with moving stirring devices
    • F26B11/16Machines or apparatus for drying solid materials or objects with movement which is non-progressive in stationary drums or other mainly-closed receptacles with moving stirring devices the stirring device moving in a vertical or steeply-inclined plane
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B23/00Heating arrangements
    • F26B23/04Heating arrangements using electric heating
    • 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
    • F26B25/04Agitating, stirring, or scraping devices
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B5/00Drying solid materials or objects by processes not involving the application of heat
    • F26B5/04Drying solid materials or objects by processes not involving the application of heat by evaporation or sublimation of moisture under reduced pressure, e.g. in a vacuum
    • 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

Definitions

  • the utility model relates to the technical field of environmental protection equipment, in particular to a vacuum drying device.
  • the existing vacuum drying device generally comprises a fermentation tank and a stirring shaft, and the stirring shaft is provided with a stirring blade, and the two ends of the stirring shaft are fixedly connected with the fermentation tank through the bearing and the bearing seat respectively, wherein the fermentation tank is composed of the inner layer, The intermediate layer and the outer layer are formed, and a heat conducting oil is disposed between the intermediate layer and the outer layer, and an electric adding component is arranged on the bottom surface between the intermediate layer and the inner layer, and the intermediate layer is fixedly connected with the inner layer via the strut, the intermediate layer and the outer layer
  • a temperature sensor in the interlayer the top surface of the fermentation tank is provided with a feeding port, a feeding port and an exhaust port, the lower part of the side is provided with a discharging port, an automatic closing device is arranged on the feeding port, and a sealing door is arranged on the inoculating port.
  • the discharge port is provided with a discharge door
  • the automatic door closing device comprises a feeding door, an electric push rod, an electric push rod bracket, a positioning frame, a connecting rod, a guide rod, a right angle bending plate, a sealing pad, a hinge shaft, a positioning sleeve and
  • the hinge shaft and the feeding door are arranged in the fermentation tank, the feeding door corresponds to the feeding port, the upper end of the feeding door is provided with a sealing pad, the lower end is fixedly connected with the right angle bending plate, and the two ends of the feeding door are respectively hinged Hinged to the positioning frame, the positioning frame is fixed in the fermentation
  • an electric push rod bracket is fixed on the top surface of the fermenting tank corresponding to the positioning frame, the upper end of the electric push rod is fixedly connected with the electric push rod bracket, the lower end is fixedly connected with the guide rod, and the guide rod passes through the electric push rod bracket and the fermentation tank.
  • the lower end of the hole provided on the positioning frame is hinged with the connecting rod, and the other end of the connecting rod is hinged with the other end of the right angle curved plate.
  • the disadvantages are as follows: 1. When the equipment needs maintenance, since the drying tank and the sorting cylinder are all integral, the shaft and the drying tank, or the shaft and the sorting cylinder need to be separated by special equipment, which is very troublesome and time consuming.
  • the drying temperature is usually more than 140 degrees due to drying under reduced pressure. Not only does it generate a large amount of high-temperature steam, but also needs to be treated by an ionization deodorizing device.
  • the drying time is long and the energy consumption is high.
  • the steam is emitted to the outside, and because the temperature is too high, all the nutrients such as beneficial bacteria and protein contained in the kitchen waste are destroyed, and the nutrients such as protein contained in the kitchen waste are partially destroyed.
  • the utility model aims to solve the deficiencies of the prior art, and provides a vacuum drying device with novel structure, short processing time, low power consumption, environmental protection and odorless gas discharge, and high operational stability of the device.
  • a vacuum drying device comprising a drying tank, a stirring shaft and a stirring motor, wherein the drying tank is composed of a lower middle slotted body and an upper middle slotted body, and the lower middle slotted body is sealed by a ring and
  • the fixing bolt is fixedly and sealingly connected with the upper middle slotted body, wherein the lower middle slotted body is provided with a hollow inner cavity, wherein the hollow inner cavity is provided with an electric heating device and a heat conducting medium, and the electric heating device is controlled by a control system.
  • the heat transfer medium is in communication with the vacuum waste heat recovery device to facilitate installation and maintenance.
  • the utility model can be provided with a sealing card slot on the circumference of the end face of the lower middle slotted body, and the sealing ring is positioned through the sealing card slot to achieve the quick installation effect.
  • the utility model can also be provided with a vacuum sealing device, which comprises an electric ball valve, a vacuum pump, a waste heat recovery device and a PLC controller.
  • the electric ball valve is connected with the feeding port of the drying tank, and the steam outlet of the drying tank passes through the waste heat recovery device and
  • the vacuum pump is connected, the electric ball valve, the waste heat recovery device and the vacuum pump are respectively connected with the PLC controller, and a vacuum negative pressure is formed in the drying tank by the operation of the vacuum pump, so that the pressure during the drying process is maintained at -0.081 to -0.099 MPa, not only It can kill the harmful bacteria in the kitchen waste which is fermented and dried in the drying tank, and retain the protein, cellulose and other nutrients beneficial to the livestock, so that the granules of the kitchen waste after fermentation drying meet the requirements of the Animal Husbandry Law.
  • the negative pressure reduces the boiling point of the water in the material, and the temperature in the drying tank is about 50-65 ° C, the water in the material can boil, without heating the material to 100 ° C, thereby greatly shortening the drying Time energy consumption; at the same time, through the waste heat recovery device, the odorous steam generated during the drying process is condensed to make the odor molecules Solutions of the condensed water discharged to the sewage treatment system, to avoid odors.
  • the stirring shaft, the stirring rod and the spiral blade in the drying tank of the utility model respectively adopt a structure in which a hollow phase communicates, and one end of the stirring shaft is provided with a rotary joint, and an inlet pipe is arranged in the inner cavity of the stirring shaft, and the inlet
  • the water pipe and the inner wall of the stirring shaft are provided with a return water gap, one end of the water inlet pipe is connected to the water tank via a rotary joint, and the other end is closed, and the side wall of the water inlet pipe is connected to the inner cavity of the spiral blade through the water pipe of the stirring rod through the water pipe
  • the spiral blade is provided with a water return hole, so that the water flows back through the return hole into the return water gap between the inlet pipe and the stirring shaft of the stirring shaft and flows back into the water tank, so as to facilitate absorption by the vacuum waste heat recovery device.
  • the heat energy is transmitted to the stirring shaft and the stirring blade, and then the positive pressure heat in the hollow structure of the stirring shaft, the stirring blade repeatedly stirs and heats the material, and the tank interlayer heats the negative pressure of the material at a low pressure, which not only accelerates the tank body significantly.
  • the drying rate of the material and also significantly saves energy consumption.
  • the utility model has the advantages of novel structure, stable operation, convenient replacement, high work efficiency and long service life due to adopting the above structure.
  • 1 is a schematic exploded view of the utility model.
  • Figure 2 is a schematic view of the structure of the present invention.
  • Figure 3 is a plan view of Figure 2.
  • a vacuum drying device includes a drying tank 11, a stirring shaft 12, and a stirring motor 14.
  • the stirring shaft 12 is provided with a stirring blade 16, and the two ends of the stirring shaft 12 are fixedly connected to the drying tank 11 through a bearing and a bearing housing, respectively.
  • the shaft 12 is connected to the agitating motor 14, a heating element is arranged in the interlayer between the inner layer and the outer layer of the drying tank 11, a temperature sensor is arranged on the outer layer, and a discharging port is arranged in the lower part of the drying tank 11, and the discharging is provided.
  • the outlet is provided with a discharge sealing door, characterized in that: the drying tank is composed of a lower middle slotted body and an upper middle slotted body, and the lower middle slotted body is sealed by a sealing ring and a fixing bolt and an upper middle slotted body a fixed sealing connection, the lower middle slotted body is provided with a hollow inner cavity, wherein the hollow inner cavity is provided with an electric heating device and a heat conducting medium, and the electric heating device is controlled by a control system, and the heat conducting medium and vacuum waste heat are recovered The devices are connected to facilitate installation and maintenance.
  • the utility model can be provided with a sealing card slot on the circumference of the end face of the lower middle slotted body, and the sealing ring is positioned through the sealing card slot to achieve the quick installation effect.
  • the utility model can also be provided with a vacuum sealing device, which comprises an electric ball valve 10, a vacuum pump 9, a waste heat recovery device and a PLC controller, and the electric ball valve 10 is connected with the feeding port of the drying tank 11, and the steam outlet of the drying tank 11
  • the waste heat recovery device is connected to the vacuum pump 9, and the electric ball valve 10, the waste heat recovery device and the vacuum pump 9 are respectively connected to the PLC controller, and a vacuum negative pressure is formed in the drying tank by the operation of the vacuum pump 9, so that the pressure during the drying process is maintained.
  • the PLC controller instructs the heating element to stop heating, without heating the material to 100 ° C, thus greatly reducing the energy consumption of drying time;
  • the waste heat recovery device Through the waste heat recovery device, the odor-laden steam generated in the drying process is condensed, and the odor molecules are dissolved in the condensed water and discharged into the sewage treatment system, thereby avoiding the generation of odor.
  • the stirring shaft 12, the stirring rod 17 and the spiral blade 16 in the drying tank 11 of the present invention respectively adopt a structure in which a hollow phase communicates, and one end of the stirring shaft 12 is provided with a rotary joint, and the center of the inner cavity of the stirring shaft 12 is provided.
  • the inlet pipe, the inlet pipe and the inner wall of the agitating shaft 12 are provided with a return water gap, one end of the inlet pipe is connected to the water tank via a swivel joint, the other end is closed, and the side wall of the inlet pipe passes through the water distribution pipe through the stirring rod
  • the cavity is in communication with the inner cavity of the spiral blade 16, and the spiral blade 16 is provided with a water return hole, so that the water flows back through the return hole into the return water gap between the inlet pipe and the stirring shaft of the stirring shaft and flows back into the water tank.
  • the vacuum waste heat recovery device of the present invention may adopt a heat pump technology, that is, it includes a refrigeration unit 56 and a refrigeration unit II 57.
  • the refrigeration unit includes a compressor 58, a condenser 59, an expansion valve 60, and a surface cooler 61.
  • the steam outlet of the drying tank 11 is sequentially connected to the air cooler 61 of the refrigeration unit 56 and the air cooler 61 of the refrigeration unit 257 and the vacuum pump 9 via the steam filter 30, so that the waste heat recovery process is at -0.081 to 0.099 MPa.
  • the condenser 59 of the refrigeration unit (57) is connected to the flushing water tank 21 through a water pump; the condenser 59 of the refrigeration unit 56 may be disposed in the interlayer, or the condenser 59 may be disposed outside the drying tank through heat exchange.
  • the circulation line communicates with the condenser 59 to facilitate absorption of the heat energy of the steam in the drying tank 11 by the vacuum waste heat recovery device 8, and the heat energy of the steam is transferred to the drying tank interlayer through the condenser 59, and is disposed in the drying tank 11
  • the material is dried, on the other hand, the heat energy is transferred to the flushing water tank, and the kitchen waste is washed by the salt-reducing and fat-reducing device 1, which not only realizes waste heat recovery, but also significantly saves Consumption, reduce the heating time.
  • the PLC controller opens the electric ball valve, the material enters into the drying tank, and then the electric ball valve is closed, and the PLC controller instructs the stirring motor to move, and drives the stirring shaft in the drying tank to stir and dry the material during the drying process.
  • the electric heating element of the drying tank interlayer is firstly electrically heated by the PLC controller. When the temperature in the drying tank rises to 80 degrees Celsius, the electric heating is stopped, and the PLC controller starts the vacuum pump to start vacuuming the drying tank.
  • the compressor heating cable stops, the compressor starts to enter the drying stage, and at the same time, the PLC controller instructs the waste heat recovery device 5 to operate, and the waste heat recovery device 5 dries the material in the drying device 4.
  • the steam generated in the process is heat exchanged, the steam is condensed to form a heat of the liquid waste heat recovery device.
  • the heat of the steam is recovered by the waste heat recovery device to produce hot water of 50-120 ° C, wherein 50-120 ° C of hot water is transferred to the drying tank.
  • the material in the drying tank is added through the drying tank and the stirring shaft and the stirring blade.
  • the hot water of 50-70 °C is washed by the desalting and degreasing device 1; during the heating process, the spiral blade on the stirring shaft is paste-like
  • the kitchen waste is fully stirred to avoid uneven mixing of the kitchen waste in the drying tank and affect the dry quality.
  • the pressure in the drying tank is kept at -0.081 ⁇ -0.099MPa during the drying process, so that the boiling point in the drying tank is It can be boiled at 50-65 °C without heating to 100 °C, which not only accelerates the drying speed of the material in the tank, shortens the drying time, but also saves energy consumption.
  • the temperature is recovered by the vacuum waste heat recovery device. After the temperature is lowered, the condensed water with odor turned into a liquid state is discharged to a vacuum pump circulating water tank through a vacuum pump, and finally discharged into the sewage treatment system.
  • the utility model has the advantages of novel structure, stable operation, convenient replacement, high work efficiency and long service life due to adopting the above structure.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Health & Medical Sciences (AREA)
  • Molecular Biology (AREA)
  • Drying Of Solid Materials (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

A vacuum drying apparatus, comprising a drying tank (11), agitation shafts (12), and an agitation motor (14). Agitation blades (16) are provided on the agitation shafts (12). Both ends of the agitation shafts (12) are separately and fixedly connected to the drying tank (11) by means of bearings and bearing seats, and the agitation shafts (12) are connected to the agitation motor (14). A heating element is provided inside an intermediate layer between an inner layer and an outer layer of the drying tank (11). The drying tank (11) consists of a lower centrally-split tank body and an upper centrally-split tank body, said lower and upper tank bodies being sealed and fixedly connected by means of a sealing ring and fixing bolts. A hollow cavity is provided inside the lower centrally-split tank body, the hollow cavity being provided with an electric heating device and a heat-conducting medium. The electric heating device is controlled by a control system, and the heat-conducting medium is in communication with a vacuum waste heat recovery apparatus. The present vacuum drying apparatus features a novel structure, stable operation, convenient replacement, high working efficiency, and a long service life.

Description

真空干燥装置Vacuum drying device 技术领域Technical field
本实用新型涉及环保设备技术领域,具体地说是一种真空干燥装置。The utility model relates to the technical field of environmental protection equipment, in particular to a vacuum drying device.
背景技术Background technique
目前,现有的真空干燥装置通常包括发酵槽和搅拌轴,搅拌轴上设有搅拌叶片,搅拌轴两端分别经轴承、轴承座与发酵槽固定连接,其特征在于发酵槽是由内层、中间层和外层构成,中间层和外层之间设有导热油,中间层和内层之间底面铺设有电加元件,中间层经支杆与内层固定连接,中间层和外层的夹层内设有温度传感器,发酵槽顶面设有进料口、投菌口和排气口,侧面下部设有出料口,进料口上设有自动关门装置,投菌口上设有密封门,出料口上设有出料门,所述自动关门装置包括进料门、电动推杆、电动推杆支架、定位架、连杆、导杆、直角弯板、密封垫、铰轴、定位套和铰轴,进料门设在发酵槽内,进料门与进料口相对应,进料门上端设有密封垫,下端与直角弯板固定连接,进料门一侧两端分别经铰轴与定位架相铰接,定位架固定在发酵槽内顶面,对应定位架的发酵槽顶面上固定有电动推杆支架,电动推杆上端与电动推杆支架固定连接,下端与导杆固定连接,导杆穿过电动推杆支架、发酵槽和定位架上设有的孔下端与连杆相铰接,连杆另一端与直角弯板另一端相铰接。其不足是:1.当设备需要维护时,由于干燥槽、分拣筒都是整体,需要通过专用设备将轴和干燥槽,或者轴和分拣筒分离,拆装非常麻烦,费时费力。At present, the existing vacuum drying device generally comprises a fermentation tank and a stirring shaft, and the stirring shaft is provided with a stirring blade, and the two ends of the stirring shaft are fixedly connected with the fermentation tank through the bearing and the bearing seat respectively, wherein the fermentation tank is composed of the inner layer, The intermediate layer and the outer layer are formed, and a heat conducting oil is disposed between the intermediate layer and the outer layer, and an electric adding component is arranged on the bottom surface between the intermediate layer and the inner layer, and the intermediate layer is fixedly connected with the inner layer via the strut, the intermediate layer and the outer layer There is a temperature sensor in the interlayer, the top surface of the fermentation tank is provided with a feeding port, a feeding port and an exhaust port, the lower part of the side is provided with a discharging port, an automatic closing device is arranged on the feeding port, and a sealing door is arranged on the inoculating port. The discharge port is provided with a discharge door, and the automatic door closing device comprises a feeding door, an electric push rod, an electric push rod bracket, a positioning frame, a connecting rod, a guide rod, a right angle bending plate, a sealing pad, a hinge shaft, a positioning sleeve and The hinge shaft and the feeding door are arranged in the fermentation tank, the feeding door corresponds to the feeding port, the upper end of the feeding door is provided with a sealing pad, the lower end is fixedly connected with the right angle bending plate, and the two ends of the feeding door are respectively hinged Hinged to the positioning frame, the positioning frame is fixed in the fermentation On the inner top surface, an electric push rod bracket is fixed on the top surface of the fermenting tank corresponding to the positioning frame, the upper end of the electric push rod is fixedly connected with the electric push rod bracket, the lower end is fixedly connected with the guide rod, and the guide rod passes through the electric push rod bracket and the fermentation tank. The lower end of the hole provided on the positioning frame is hinged with the connecting rod, and the other end of the connecting rod is hinged with the other end of the right angle curved plate. The disadvantages are as follows: 1. When the equipment needs maintenance, since the drying tank and the sorting cylinder are all integral, the shaft and the drying tank, or the shaft and the sorting cylinder need to be separated by special equipment, which is very troublesome and time consuming.
2.在发酵干燥时,由于采用减压干燥,干燥温度通常在140多度,不但产生大量的高温蒸汽还需要经电离除臭装置进行处理,干燥时间长、耗能高,由于冷凝效果差,导致蒸汽向外散发,而且,由于温度太高,会将餐厨废弃物中含有的有益菌、蛋白质等营养成分全部破坏,是餐厨废弃物中含有的蛋白质等营养成分会被部分破坏。2. During fermentation drying, the drying temperature is usually more than 140 degrees due to drying under reduced pressure. Not only does it generate a large amount of high-temperature steam, but also needs to be treated by an ionization deodorizing device. The drying time is long and the energy consumption is high. The steam is emitted to the outside, and because the temperature is too high, all the nutrients such as beneficial bacteria and protein contained in the kitchen waste are destroyed, and the nutrients such as protein contained in the kitchen waste are partially destroyed.
发明内容Summary of the invention
本实用新型的目的在于解决现有技术的不足,提供一种结构新颖、处理时间短、功耗低、环保无臭气排放、设备运行稳定性高的真空干燥装置。The utility model aims to solve the deficiencies of the prior art, and provides a vacuum drying device with novel structure, short processing time, low power consumption, environmental protection and odorless gas discharge, and high operational stability of the device.
本实用新型解决其技术问题所采用的技术方案是:The technical solution adopted by the utility model to solve the technical problems thereof is:
一种真空干燥装置,包括干燥槽、搅拌轴和搅拌电机,其特征在于:所述干燥槽是由下中开槽体和上中开槽体组成,所述下中开槽体经密封圈和固定螺栓与上中开槽体固定密封连接,所述下中开槽体设有中空内腔,所述中空内腔中设有电加热装置和导热介质,所述电加热装置经控制系统控制,所述导热介质与真空余热回收装置相连通,以达到方便安装和维修的作 用。A vacuum drying device comprising a drying tank, a stirring shaft and a stirring motor, wherein the drying tank is composed of a lower middle slotted body and an upper middle slotted body, and the lower middle slotted body is sealed by a ring and The fixing bolt is fixedly and sealingly connected with the upper middle slotted body, wherein the lower middle slotted body is provided with a hollow inner cavity, wherein the hollow inner cavity is provided with an electric heating device and a heat conducting medium, and the electric heating device is controlled by a control system. The heat transfer medium is in communication with the vacuum waste heat recovery device to facilitate installation and maintenance.
本实用新型可在所述下中开槽体端面圆周设有密封卡槽,所述密封圈经密封卡槽定位,以达到安装快捷的作用。The utility model can be provided with a sealing card slot on the circumference of the end face of the lower middle slotted body, and the sealing ring is positioned through the sealing card slot to achieve the quick installation effect.
本实用新型还可设有真空密封装置,其包括电动球阀、真空泵、余热回收装置和PLC控制器,所属电动球阀与干燥槽的进料口相连接,干燥槽的出汽口通过余热回收装置与真空泵相连接,所述电动球阀、余热回收装置和真空泵分别与PLC控制器相连接,通过真空泵的工作使干燥槽内形成真空负压,使干燥过程中压力维持在-0.081至-0.099MPa,不但能将干燥槽内发酵干燥的餐厨废弃物中的有害细菌杀死,保留了有益于牲畜的蛋白质、纤维素和其它营养成分,使发酵干燥后的餐厨废弃物颗粒符合畜牧法的规定而形成牲畜饲料;而且,负压降低了物料中水的沸点,干燥槽内的温度在50-65℃左右时,物料中的水即可沸腾,无需将物料加热到100℃,从而大大缩短了干燥时间的能耗;同时,通过余热回收装置,将干燥过程中产生的带有臭味的蒸汽进行冷凝,使臭气分子溶解到冷凝水中排放到污水处理系统中,避免了异味产生。The utility model can also be provided with a vacuum sealing device, which comprises an electric ball valve, a vacuum pump, a waste heat recovery device and a PLC controller. The electric ball valve is connected with the feeding port of the drying tank, and the steam outlet of the drying tank passes through the waste heat recovery device and The vacuum pump is connected, the electric ball valve, the waste heat recovery device and the vacuum pump are respectively connected with the PLC controller, and a vacuum negative pressure is formed in the drying tank by the operation of the vacuum pump, so that the pressure during the drying process is maintained at -0.081 to -0.099 MPa, not only It can kill the harmful bacteria in the kitchen waste which is fermented and dried in the drying tank, and retain the protein, cellulose and other nutrients beneficial to the livestock, so that the granules of the kitchen waste after fermentation drying meet the requirements of the Animal Husbandry Law. Forming livestock feed; moreover, the negative pressure reduces the boiling point of the water in the material, and the temperature in the drying tank is about 50-65 ° C, the water in the material can boil, without heating the material to 100 ° C, thereby greatly shortening the drying Time energy consumption; at the same time, through the waste heat recovery device, the odorous steam generated during the drying process is condensed to make the odor molecules Solutions of the condensed water discharged to the sewage treatment system, to avoid odors.
本实用新型所述干燥槽内的搅拌轴、搅拌杆和螺旋叶片分别采用中空相连通的结构,所述搅拌轴一端设有回转接头,所述搅拌轴内腔中设有进水管,所述进水管和搅拌轴内壁设有回水间隙,所述进水管一端经回转接头与水箱相连接,另一端封闭,且所述进水管侧壁经分水管穿过搅拌杆空腔与螺旋叶片内腔相连通,所述螺旋叶片上设有回水孔,以使水经回水孔返流进入搅拌轴的进水管与搅拌轴间的回水间隙并回流进入水箱,以利于通过真空余热回收装置将吸收的热能传递给搅拌轴和搅拌叶片,再通过搅拌轴的中空结构内的正压热量、搅拌叶片对物料反复搅拌加热,以及槽体夹层对物料的负压低沸点加热,不但显著加快了槽体内的物料的干燥速度,而且,还显著节省了能量的消耗。The stirring shaft, the stirring rod and the spiral blade in the drying tank of the utility model respectively adopt a structure in which a hollow phase communicates, and one end of the stirring shaft is provided with a rotary joint, and an inlet pipe is arranged in the inner cavity of the stirring shaft, and the inlet The water pipe and the inner wall of the stirring shaft are provided with a return water gap, one end of the water inlet pipe is connected to the water tank via a rotary joint, and the other end is closed, and the side wall of the water inlet pipe is connected to the inner cavity of the spiral blade through the water pipe of the stirring rod through the water pipe The spiral blade is provided with a water return hole, so that the water flows back through the return hole into the return water gap between the inlet pipe and the stirring shaft of the stirring shaft and flows back into the water tank, so as to facilitate absorption by the vacuum waste heat recovery device. The heat energy is transmitted to the stirring shaft and the stirring blade, and then the positive pressure heat in the hollow structure of the stirring shaft, the stirring blade repeatedly stirs and heats the material, and the tank interlayer heats the negative pressure of the material at a low pressure, which not only accelerates the tank body significantly. The drying rate of the material, and also significantly saves energy consumption.
本实用新型由于采用上述结构,具有结构新颖、运行稳定、更换方便、工作效率高、使用寿命长等优点。The utility model has the advantages of novel structure, stable operation, convenient replacement, high work efficiency and long service life due to adopting the above structure.
附图说明DRAWINGS
图1是本实用新型的分解结构示意图。1 is a schematic exploded view of the utility model.
图2是本实用新型的结构示意图。Figure 2 is a schematic view of the structure of the present invention.
图3是图2的俯视图。Figure 3 is a plan view of Figure 2.
具体实施方式Detailed ways
下面结合附图和实施例对本实用新型进行说明。The present invention will be described below in conjunction with the accompanying drawings and embodiments.
如附图所示,As shown in the figure,
一种真空干燥装置,包括干燥槽11、搅拌轴12、搅拌电机14,搅拌轴12上设有搅拌叶片16,搅拌轴12两端分别经轴承、轴承座与干燥槽11固定连接,所述搅拌轴12与搅拌电机14相连接,所述干燥槽11的内层和外层之间的夹层内设有加热元件,外层上设有温度传感器,干燥槽11下部设有出料口,出料口上设有出料密封门,其特征在于:所述干燥槽是由下中开槽体和上中开槽体组成,所述下中开槽体经密封圈和固定螺栓与上中开槽体固定密封连接,所述下中开槽体设有中空内腔,所述中空内腔中设有电加热装置和导热介质,所述电加热装置经控制系统控制,所述导热介质与真空余热回收装置相连通,以达到方便安装和维修的作用。A vacuum drying device includes a drying tank 11, a stirring shaft 12, and a stirring motor 14. The stirring shaft 12 is provided with a stirring blade 16, and the two ends of the stirring shaft 12 are fixedly connected to the drying tank 11 through a bearing and a bearing housing, respectively. The shaft 12 is connected to the agitating motor 14, a heating element is arranged in the interlayer between the inner layer and the outer layer of the drying tank 11, a temperature sensor is arranged on the outer layer, and a discharging port is arranged in the lower part of the drying tank 11, and the discharging is provided. The outlet is provided with a discharge sealing door, characterized in that: the drying tank is composed of a lower middle slotted body and an upper middle slotted body, and the lower middle slotted body is sealed by a sealing ring and a fixing bolt and an upper middle slotted body a fixed sealing connection, the lower middle slotted body is provided with a hollow inner cavity, wherein the hollow inner cavity is provided with an electric heating device and a heat conducting medium, and the electric heating device is controlled by a control system, and the heat conducting medium and vacuum waste heat are recovered The devices are connected to facilitate installation and maintenance.
本实用新型可在所述下中开槽体端面圆周设有密封卡槽,所述密封圈经密封卡槽定位,以达到安装快捷的作用。The utility model can be provided with a sealing card slot on the circumference of the end face of the lower middle slotted body, and the sealing ring is positioned through the sealing card slot to achieve the quick installation effect.
本实用新型还可设有真空密封装置,其包括电动球阀10、真空泵9、余热回收装置和PLC控制器,所属电动球阀10与干燥槽11的进料口相连接,干燥槽11的出汽口通过余热回收装置与真空泵9相连接,所述电动球阀10、余热回收装置和真空泵9分别与PLC控制器相连接,通过真空泵9的工作使干燥槽内形成真空负压,使干燥过程中压力维持在-0.081至-0.099MPa,不但能将干燥槽内发酵干燥的餐厨废弃物中的有害细菌杀死,保留了有益于牲畜的蛋白质、纤维素和其它营养成分,使发酵干燥后的餐厨废弃物颗粒符合畜牧法的规定而形成牲畜饲料;而且,负压降低了物料中水的沸点,干燥槽内的温度在50-65℃左右时,物料中的水即可沸腾,温度传感器将信息上传至PLC控制器,PLC控制器即指令加热元件停止加热,无需将物料加热到100℃,从而大大缩短了干燥时间的能耗;同时,通过余热回收装置,将干燥过程中产生的带有臭味的蒸汽进行冷凝,使臭气分子溶解到冷凝水中排放到污水处理系统中,避免了异味产生。The utility model can also be provided with a vacuum sealing device, which comprises an electric ball valve 10, a vacuum pump 9, a waste heat recovery device and a PLC controller, and the electric ball valve 10 is connected with the feeding port of the drying tank 11, and the steam outlet of the drying tank 11 The waste heat recovery device is connected to the vacuum pump 9, and the electric ball valve 10, the waste heat recovery device and the vacuum pump 9 are respectively connected to the PLC controller, and a vacuum negative pressure is formed in the drying tank by the operation of the vacuum pump 9, so that the pressure during the drying process is maintained. From -0.081 to -0.099 MPa, it not only kills the harmful bacteria in the fermented and dried kitchen waste in the drying tank, but also preserves the protein, cellulose and other nutrients that are beneficial to the livestock, so that the dried and dried kitchen utensils The waste particles meet the requirements of the Animal Husbandry Law to form livestock feed; moreover, the negative pressure reduces the boiling point of the water in the material. When the temperature in the drying tank is around 50-65 °C, the water in the material can boil, and the temperature sensor will information. Uploaded to the PLC controller, the PLC controller instructs the heating element to stop heating, without heating the material to 100 ° C, thus greatly reducing the energy consumption of drying time; Through the waste heat recovery device, the odor-laden steam generated in the drying process is condensed, and the odor molecules are dissolved in the condensed water and discharged into the sewage treatment system, thereby avoiding the generation of odor.
本实用新型所述干燥槽11内的搅拌轴12、搅拌杆17和螺旋叶片16分别采用中空相连通的结构,所述搅拌轴12一端设有回转接头,所述搅拌轴12内腔中心设有进水管,所述进水管和搅拌轴12内壁设有回水间隙,所述进水管一端经回转接头与水箱相连接,另一端封闭,且所述进水管侧壁经分水管穿过搅拌杆空腔与螺旋叶片16内腔相连通,所述螺旋叶片16上设有回水孔,以使水经回水孔返流进入搅拌轴的进水管与搅拌轴间的回水间隙并回流进入水箱,以利于通过真空余热回收装置7将吸收的热能传递给搅拌轴12和搅拌桨叶,增大传热面积通过搅拌桨叶对物料反复搅拌加热,以及槽体夹层对物料的加热,不但显著加快了槽体内的物料的干燥速度,而且还显著节省了能量的消耗。The stirring shaft 12, the stirring rod 17 and the spiral blade 16 in the drying tank 11 of the present invention respectively adopt a structure in which a hollow phase communicates, and one end of the stirring shaft 12 is provided with a rotary joint, and the center of the inner cavity of the stirring shaft 12 is provided. The inlet pipe, the inlet pipe and the inner wall of the agitating shaft 12 are provided with a return water gap, one end of the inlet pipe is connected to the water tank via a swivel joint, the other end is closed, and the side wall of the inlet pipe passes through the water distribution pipe through the stirring rod The cavity is in communication with the inner cavity of the spiral blade 16, and the spiral blade 16 is provided with a water return hole, so that the water flows back through the return hole into the return water gap between the inlet pipe and the stirring shaft of the stirring shaft and flows back into the water tank. In order to facilitate the transfer of the absorbed heat energy to the stirring shaft 12 and the stirring blade through the vacuum waste heat recovery device 7, increasing the heat transfer area by repeatedly stirring and heating the material by the stirring blade, and heating the material by the tank interlayer, not only significantly speeds up The drying rate of the material in the tank, and also significantly saves energy consumption.
本实用新型所述真空余热回收装置可以采用热泵技术,即其包括制冷机组一56、制 冷机组二57,所述制冷机组包括压缩机58、冷凝器59、膨胀阀60、表冷器61,所述干燥槽11的出汽口经蒸汽过滤器30依次与制冷机组一56的表冷器61和制冷机组二57的表冷器61与真空泵9相连,以使余热回收过程在-0.081~0.099MPa压力下进行,制冷机组二57的冷凝器59通过水泵与冲洗水箱21相连;可以将制冷机组一56的冷凝器59设置在夹层内,也可以将冷凝器59设置在干燥槽外部,通过换热循环管路与冷凝器59相连通,以利于通过真空余热回收装置8吸收干燥槽11内的蒸汽的热能,通过冷凝器59一方面将蒸汽的热能传递到干燥槽夹层内,对干燥槽11内的物料进行干燥,另一方面将热能传递到冲洗水箱中,通过降盐降脂装置1对餐厨废弃物进行冲洗,不但实现了余热回收,而且还显著节约了能耗,缩短了加热时间。The vacuum waste heat recovery device of the present invention may adopt a heat pump technology, that is, it includes a refrigeration unit 56 and a refrigeration unit II 57. The refrigeration unit includes a compressor 58, a condenser 59, an expansion valve 60, and a surface cooler 61. The steam outlet of the drying tank 11 is sequentially connected to the air cooler 61 of the refrigeration unit 56 and the air cooler 61 of the refrigeration unit 257 and the vacuum pump 9 via the steam filter 30, so that the waste heat recovery process is at -0.081 to 0.099 MPa. Under pressure, the condenser 59 of the refrigeration unit (57) is connected to the flushing water tank 21 through a water pump; the condenser 59 of the refrigeration unit 56 may be disposed in the interlayer, or the condenser 59 may be disposed outside the drying tank through heat exchange. The circulation line communicates with the condenser 59 to facilitate absorption of the heat energy of the steam in the drying tank 11 by the vacuum waste heat recovery device 8, and the heat energy of the steam is transferred to the drying tank interlayer through the condenser 59, and is disposed in the drying tank 11 The material is dried, on the other hand, the heat energy is transferred to the flushing water tank, and the kitchen waste is washed by the salt-reducing and fat-reducing device 1, which not only realizes waste heat recovery, but also significantly saves Consumption, reduce the heating time.
本实用新型在工作时,PLC控制器打开电动球阀,物料进入到干燥槽内,然后关闭电动球阀,PLC控制器指令搅拌电机动作,带动干燥槽内的搅拌轴对物料进行搅拌干燥,在干燥过程中,先通过PLC控制器指令干燥槽夹层的电加热元件电加热,当干燥槽内的温度上升到80摄氏度时,即停止电加热,PLC控制器启动真空泵,开始对干燥槽内抽真空,当干燥槽内的真空度达到-0.06MPa时,压缩机伴热带停止,压缩机启动进入干燥阶段,同时,PLC控制器指令余热热回收装置5工作,余热回收装置5对干燥装置4中的物料干燥过程中产生的蒸汽进行热交换后,将蒸汽冷凝形成液体余热回收装置蒸汽的热量被余热热回收装置再回收产生50-120℃的热水,其中50-120℃的热水传递至干燥槽内的夹层和搅拌轴的中空结构中,通过干燥槽内和搅拌轴和搅拌叶片对干燥槽内的物料进行再加热,另一部分至将热能传递到冲洗水箱32中,50-70℃的热水通过除盐除脂装置1对餐厨废弃物进行冲洗;在加热过程中,搅拌轴上的螺旋叶片对膏状的餐厨废弃物进行充分搅拌,避免干燥槽内的餐厨废弃物搅拌不均匀而影响干燥质量,干燥过程中始终保持干燥槽体内压力在-0.081~-0.099MPa,使干燥槽内的沸点在50-65℃时即可沸腾,无需加热到100℃,不但显著加快了槽体内的物料的干燥速度,缩短了干燥时间,而且还显著节省了能量的消耗;同时,通过真空余热回收装置将温度降低,降温后变成液态的带有异味的冷凝水再通过真空泵,将其排放到真空泵循环水箱中,最终排放到污水处理系统中。When the utility model is in operation, the PLC controller opens the electric ball valve, the material enters into the drying tank, and then the electric ball valve is closed, and the PLC controller instructs the stirring motor to move, and drives the stirring shaft in the drying tank to stir and dry the material during the drying process. First, the electric heating element of the drying tank interlayer is firstly electrically heated by the PLC controller. When the temperature in the drying tank rises to 80 degrees Celsius, the electric heating is stopped, and the PLC controller starts the vacuum pump to start vacuuming the drying tank. When the vacuum degree in the drying tank reaches -0.06 MPa, the compressor heating cable stops, the compressor starts to enter the drying stage, and at the same time, the PLC controller instructs the waste heat recovery device 5 to operate, and the waste heat recovery device 5 dries the material in the drying device 4. After the steam generated in the process is heat exchanged, the steam is condensed to form a heat of the liquid waste heat recovery device. The heat of the steam is recovered by the waste heat recovery device to produce hot water of 50-120 ° C, wherein 50-120 ° C of hot water is transferred to the drying tank. In the hollow structure of the interlayer and the stirring shaft, the material in the drying tank is added through the drying tank and the stirring shaft and the stirring blade. Heat, another part to transfer heat energy to the flushing water tank 32, the hot water of 50-70 °C is washed by the desalting and degreasing device 1; during the heating process, the spiral blade on the stirring shaft is paste-like The kitchen waste is fully stirred to avoid uneven mixing of the kitchen waste in the drying tank and affect the dry quality. The pressure in the drying tank is kept at -0.081~-0.099MPa during the drying process, so that the boiling point in the drying tank is It can be boiled at 50-65 °C without heating to 100 °C, which not only accelerates the drying speed of the material in the tank, shortens the drying time, but also saves energy consumption. At the same time, the temperature is recovered by the vacuum waste heat recovery device. After the temperature is lowered, the condensed water with odor turned into a liquid state is discharged to a vacuum pump circulating water tank through a vacuum pump, and finally discharged into the sewage treatment system.
本实用新型由于采用上述结构,具有结构新颖、运行稳定、更换方便、工作效率高、使用寿命长等优点。The utility model has the advantages of novel structure, stable operation, convenient replacement, high work efficiency and long service life due to adopting the above structure.

Claims (4)

  1. 一种真空干燥装置,包括干燥槽、搅拌轴和搅拌电机,其特征在于:所述干燥槽是由下中开槽体和上中开槽体组成,所述下中开槽体经密封圈和固定螺栓与上中开槽体固定密封连接,所述下中开槽体设有中空内腔,所述中空内腔中设有电加热装置和导热介质,所述电加热装置经控制系统控制,所述导热介质与真空余热回收装置相连通。A vacuum drying device comprising a drying tank, a stirring shaft and a stirring motor, wherein the drying tank is composed of a lower middle slotted body and an upper middle slotted body, and the lower middle slotted body is sealed by a ring and The fixing bolt is fixedly and sealingly connected with the upper middle slotted body, wherein the lower middle slotted body is provided with a hollow inner cavity, wherein the hollow inner cavity is provided with an electric heating device and a heat conducting medium, and the electric heating device is controlled by a control system. The heat transfer medium is in communication with a vacuum waste heat recovery device.
  2. 根据权利要求1所述的一种真空干燥装置,其特征在于所述下中开槽体端面圆周设有密封卡槽,所述密封圈经密封卡槽定位。A vacuum drying apparatus according to claim 1, wherein a sealing card groove is disposed on an end surface of the lower middle slotted body, and the sealing ring is positioned through the sealing card slot.
  3. 根据权利要求1所述的一种真空干燥装置,其特征在于设有真空密封装置,其包括电动球阀、真空泵、余热回收装置和PLC控制器,所属电动球阀与干燥槽的进料口相连接,干燥槽的出汽口通过余热回收装置与真空泵相连接,所述电动球阀、余热回收装置和真空泵分别与PLC控制器相连接。A vacuum drying device according to claim 1, characterized in that a vacuum sealing device is provided, which comprises an electric ball valve, a vacuum pump, a waste heat recovery device and a PLC controller, and the electric ball valve is connected to the feed port of the drying tank. The steam outlet of the drying tank is connected to the vacuum pump through a waste heat recovery device, and the electric ball valve, the waste heat recovery device and the vacuum pump are respectively connected to the PLC controller.
  4. 根据权利要求1所述的一种真空干燥装置,其特征在于所述干燥槽内的搅拌轴、搅拌杆和螺旋叶片分别采用中空相连通的结构,所述搅拌轴一端设有回转接头,所述搅拌轴内腔中设有进水管,所述进水管和搅拌轴内壁设有回水间隙,所述进水管一端经回转接头与水箱相连接,另一端封闭,且所述进水管侧壁经分水管穿过搅拌杆空腔与螺旋叶片内腔相连通,所述螺旋叶片上设有回水孔。A vacuum drying apparatus according to claim 1, wherein the agitating shaft, the stirring rod and the spiral vane in the drying tank are respectively connected by a hollow phase, and one end of the stirring shaft is provided with a swivel joint, An inlet pipe is disposed in the inner cavity of the agitating shaft, and the inner wall of the inlet pipe and the agitating shaft is provided with a return water gap, and one end of the inlet pipe is connected to the water tank via a rotary joint, and the other end is closed, and the side wall of the inlet pipe is divided The water pipe communicates with the inner cavity of the spiral blade through the cavity of the stirring rod, and the spiral blade is provided with a water return hole.
PCT/CN2019/087120 2018-05-15 2019-05-15 Vacuum drying apparatus WO2019219040A1 (en)

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CN201820721885.8U CN208186984U (en) 2018-05-15 2018-05-15 Minton dryer

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WO2019219040A1 true WO2019219040A1 (en) 2019-11-21

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN208186984U (en) * 2018-05-15 2018-12-04 山东名流餐处装备股份有限公司 Minton dryer

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CN2039402U (en) * 1988-11-04 1989-06-14 上海华元干燥技术工程公司 Plate-type dryer with heating arrangement and stirring device
JP2001153556A (en) * 1999-11-30 2001-06-08 Agurikkusu:Kk Vacuum drying device
CN2871544Y (en) * 2006-01-17 2007-02-21 微聚科技股份有限公司 Powder vaccinal dry concentrator
CN202195666U (en) * 2011-08-18 2012-04-18 王贵孝 Horizontal cylinder double-helix rake vacuum drier
CN204268814U (en) * 2014-09-16 2015-04-15 湖南启天环保科技有限公司 A kind of Novel vacuum drying device
CN205014756U (en) * 2015-09-07 2016-02-03 安徽纽曼精细化工有限公司 Rake type vacuum dryer
CN205425698U (en) * 2016-02-29 2016-08-03 浙江诚信医化设备有限公司 Vacuum drier
CN206751757U (en) * 2017-03-21 2017-12-15 郑州恒博科技股份有限公司 A kind of diatomaceous batch (-type) of oil-containing puies forward oily equipment
CN208186984U (en) * 2018-05-15 2018-12-04 山东名流餐处装备股份有限公司 Minton dryer
CN208466828U (en) * 2018-05-15 2019-02-05 山东名流餐处装备股份有限公司 Kitchen castoff processing unit
CN109485466A (en) * 2018-05-15 2019-03-19 山东名流餐处装备股份有限公司 Kitchen castoff processing method and processing unit

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2039402U (en) * 1988-11-04 1989-06-14 上海华元干燥技术工程公司 Plate-type dryer with heating arrangement and stirring device
JP2001153556A (en) * 1999-11-30 2001-06-08 Agurikkusu:Kk Vacuum drying device
CN2871544Y (en) * 2006-01-17 2007-02-21 微聚科技股份有限公司 Powder vaccinal dry concentrator
CN202195666U (en) * 2011-08-18 2012-04-18 王贵孝 Horizontal cylinder double-helix rake vacuum drier
CN204268814U (en) * 2014-09-16 2015-04-15 湖南启天环保科技有限公司 A kind of Novel vacuum drying device
CN205014756U (en) * 2015-09-07 2016-02-03 安徽纽曼精细化工有限公司 Rake type vacuum dryer
CN205425698U (en) * 2016-02-29 2016-08-03 浙江诚信医化设备有限公司 Vacuum drier
CN206751757U (en) * 2017-03-21 2017-12-15 郑州恒博科技股份有限公司 A kind of diatomaceous batch (-type) of oil-containing puies forward oily equipment
CN208186984U (en) * 2018-05-15 2018-12-04 山东名流餐处装备股份有限公司 Minton dryer
CN208466828U (en) * 2018-05-15 2019-02-05 山东名流餐处装备股份有限公司 Kitchen castoff processing unit
CN109485466A (en) * 2018-05-15 2019-03-19 山东名流餐处装备股份有限公司 Kitchen castoff processing method and processing unit

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