CN107144113A - A kind of drying system for high temperature production technology - Google Patents
A kind of drying system for high temperature production technology Download PDFInfo
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- CN107144113A CN107144113A CN201710314823.5A CN201710314823A CN107144113A CN 107144113 A CN107144113 A CN 107144113A CN 201710314823 A CN201710314823 A CN 201710314823A CN 107144113 A CN107144113 A CN 107144113A
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- 238000001035 drying Methods 0.000 title claims abstract description 78
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 32
- 238000005516 engineering process Methods 0.000 title claims 4
- 238000000034 method Methods 0.000 claims description 29
- 239000000463 material Substances 0.000 claims description 15
- 239000003507 refrigerant Substances 0.000 claims description 2
- 230000008676 import Effects 0.000 claims 3
- 230000001172 regenerating effect Effects 0.000 claims 3
- 238000010304 firing Methods 0.000 claims 1
- 230000005855 radiation Effects 0.000 claims 1
- 235000013305 food Nutrition 0.000 abstract description 5
- 238000010438 heat treatment Methods 0.000 description 10
- 238000009413 insulation Methods 0.000 description 8
- 238000011084 recovery Methods 0.000 description 8
- 241001092040 Crataegus Species 0.000 description 7
- 235000009917 Crataegus X brevipes Nutrition 0.000 description 7
- 235000013204 Crataegus X haemacarpa Nutrition 0.000 description 7
- 235000009685 Crataegus X maligna Nutrition 0.000 description 7
- 235000009444 Crataegus X rubrocarnea Nutrition 0.000 description 7
- 235000009486 Crataegus bullatus Nutrition 0.000 description 7
- 235000017181 Crataegus chrysocarpa Nutrition 0.000 description 7
- 235000009682 Crataegus limnophila Nutrition 0.000 description 7
- 235000004423 Crataegus monogyna Nutrition 0.000 description 7
- 235000002313 Crataegus paludosa Nutrition 0.000 description 7
- 235000009840 Crataegus x incaedua Nutrition 0.000 description 7
- 235000012055 fruits and vegetables Nutrition 0.000 description 3
- 239000011521 glass Substances 0.000 description 3
- 238000004806 packaging method and process Methods 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 2
- 229930006000 Sucrose Natural products 0.000 description 2
- 238000007605 air drying Methods 0.000 description 2
- 238000010009 beating Methods 0.000 description 2
- 238000007791 dehumidification Methods 0.000 description 2
- 235000011869 dried fruits Nutrition 0.000 description 2
- 238000007602 hot air drying Methods 0.000 description 2
- 238000007689 inspection Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000007790 scraping Methods 0.000 description 2
- 238000007493 shaping process Methods 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000012858 packaging process Methods 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 238000004537 pulping Methods 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
- 238000010257 thawing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B15/00—Machines or apparatus for drying objects with progressive movement; Machines or apparatus with progressive movement for drying batches of material in compact form
- F26B15/10—Machines or apparatus for drying objects with progressive movement; Machines or apparatus with progressive movement for drying batches of material in compact form with movement in a path composed of one or more straight lines, e.g. compound, the movement being in alternate horizontal and vertical directions
- F26B15/12—Machines or apparatus for drying objects with progressive movement; Machines or apparatus with progressive movement for drying batches of material in compact form with movement in a path composed of one or more straight lines, e.g. compound, the movement being in alternate horizontal and vertical directions the lines being all horizontal or slightly inclined
- F26B15/16—Machines or apparatus for drying objects with progressive movement; Machines or apparatus with progressive movement for drying batches of material in compact form with movement in a path composed of one or more straight lines, e.g. compound, the movement being in alternate horizontal and vertical directions the lines being all horizontal or slightly inclined the objects or batches of materials being carried by wheeled trucks
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B1/00—Preliminary treatment of solid materials or objects to facilitate drying, e.g. mixing or backmixing the materials to be dried with predominantly dry solids
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/02—Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure
- F26B21/04—Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure partly outside the drying enclosure
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B23/00—Heating arrangements
- F26B23/001—Heating arrangements using waste heat
- F26B23/002—Heating arrangements using waste heat recovered from dryer exhaust gases
- F26B23/005—Heating arrangements using waste heat recovered from dryer exhaust gases using a closed cycle heat pump system ; using a heat pipe system
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B23/00—Heating arrangements
- F26B23/04—Heating arrangements using electric heating
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/001—Handling, e.g. loading or unloading arrangements
- F26B25/003—Handling, e.g. loading or unloading arrangements for articles
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B3/00—Drying solid materials or objects by processes involving the application of heat
- F26B3/32—Drying solid materials or objects by processes involving the application of heat by development of heat within the materials or objects to be dried, e.g. by fermentation or other microbiological action
- F26B3/34—Drying solid materials or objects by processes involving the application of heat by development of heat within the materials or objects to be dried, e.g. by fermentation or other microbiological action by using electrical effects
- F26B3/347—Electromagnetic heating, e.g. induction heating or heating using microwave energy
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Microbiology (AREA)
- Electromagnetism (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Biotechnology (AREA)
- Physics & Mathematics (AREA)
- Molecular Biology (AREA)
- Drying Of Solid Materials (AREA)
Abstract
本发明一种用于中高温生产工艺的干燥系统,将干燥室与定型室集中到一个生产车间区域,实现产品生产流程在车间内部的无缝链接,该生产工艺与系统车间可适用于中高温等具有相同干燥工艺和干燥车间结构形式的食品生产过程;具有减少一线用工数量与用工劳动强度,节约生产成本,提高成产效率和经济效率的优点,特征是,在货物入口门附近安装微波辅助加热器对货物进行预干燥处理,在货物出口门附近安装红外线辅助加热器对干燥货物进行再干燥处理,实现干燥系统的中高温生产。
The invention is a drying system for medium and high temperature production process, which integrates the drying room and the setting room into one production workshop area, and realizes the seamless link of the product production process in the workshop. The production process and system workshop can be applied to medium and high temperature Food production process with the same drying process and drying workshop structure; it has the advantages of reducing the number of front-line workers and labor intensity, saving production costs, improving production efficiency and economic efficiency, and is characterized in that microwave auxiliary equipment is installed near the cargo entrance door. The heater pre-dries the goods, and an infrared auxiliary heater is installed near the goods exit door to re-dry the dry goods, so as to realize the medium and high temperature production of the drying system.
Description
技术领域technical field
本发明涉及食品、果蔬等干燥生产技术领域,具体涉及的是一种适用于中高温干燥工艺的食品、果蔬、木材等产品的干燥系统和生产工艺。The invention relates to the technical field of drying production of food, fruits and vegetables, in particular to a drying system and production process for food, fruits and vegetables, wood and other products suitable for medium-high temperature drying process.
背景技术Background technique
目前,全国具有一定规模的食品、果蔬等干燥生产企业有成千上万家,多数企业生产规模小,且干燥方式一般采用自然干燥、电烤炉或燃煤热风炉干燥等方法进 行生产,很少采用热泵干燥方法。自然风干是一种落后的风干方式,具有生产效 率低、产品易变质、卫生条件差的缺点,影响其产品的品质和市场价值。因此发 明一种新型的适用于中高温干燥的生产工艺和系统具有重要意义。At present, there are tens of thousands of food, fruit and vegetable drying production enterprises with a certain scale in the country. Less use of heat pump drying method. Natural air-drying is a backward air-drying method, which has the disadvantages of low production efficiency, perishable products, and poor hygienic conditions, which affects the quality and market value of its products. Therefore it is of great significance to invent a novel production process and system suitable for medium and high temperature drying.
传统的干燥方式是采用鼓风热风开放式干燥,空气由燃烧化石燃料的热风炉进行加热,形成温度高,相对湿度较小、干燥能力较强的热风,热空气在鼓风机的驱动下吹扫物料,达到热风干燥的目的。采用的干燥车间是主要针对燃煤热风干燥方式所设计的,物料的解冻,前期处理工艺均采用人工处理的方式,存在明显的能源浪费,占地空间大,生产效率低等缺点。并且旧车间采用开放式空气循环对产品进行干燥,干燥后产品的质量有明显的下滑。针对这些缺点本发明提出了定型干燥自动化车间。新车间是针对应用热泵干燥机干燥山楂饼等中高温干燥产品的新型车间。车间由并行的热泵控制室和干燥室两部分组成。新风从新风入口进入之后,经过热泵机组进行除湿加热。然后通过鼓风机的驱动将高温低湿的空气送入到干燥室内进行直接定型和干燥过程。新型车间在占地面积相同情况下,生产效率提高。并且采用闭式空气循环回路对产品进行干燥,干燥产物于外界空气没有直接接触,生产产品更加卫生安全。The traditional drying method is open drying with blast hot air. The air is heated by a hot air stove burning fossil fuels to form hot air with high temperature, low relative humidity and strong drying capacity. The hot air blows the material under the drive of the blower. , to achieve the purpose of hot air drying. The drying workshop adopted is mainly designed for the coal-fired hot air drying method. The thawing of materials and the pre-treatment process are all manually processed, which has the disadvantages of obvious energy waste, large space occupation, and low production efficiency. In addition, the old workshop uses open air circulation to dry the products, and the quality of the products after drying has declined significantly. For these shortcomings, the present invention proposes a sizing and drying automatic workshop. The new workshop is a new workshop for medium and high temperature drying products such as hawthorn cakes using heat pump dryers. The workshop consists of two parts, the parallel heat pump control room and the drying room. After the fresh air enters from the fresh air inlet, it goes through the heat pump unit for dehumidification and heating. Then, driven by the blower, the high-temperature and low-humidity air is sent into the drying room for direct shaping and drying. The production efficiency of the new workshop is improved under the same floor space. And the closed air circulation loop is used to dry the product, the dried product has no direct contact with the outside air, and the produced product is more hygienic and safe.
经检索,申请号CN201610519856申请的果脯烘干方法的发明专利提供一种果脯烘干装置,能够使热能在烘房内的烘干室内部均匀循环,减少烘干时温差。但是后一种专利只是适用于小批量的果脯烘干,对于大产量的产品干燥并不适用。After searching, the invention patent of the dried fruit drying method applied for by the application number CN201610519856 provides a dried fruit drying device, which can make the heat energy circulate evenly inside the drying chamber in the drying room and reduce the temperature difference during drying. But the latter patent is only applicable to the drying of preserved fruit in small batches, and is not suitable for the drying of large-scale products.
发明内容Contents of the invention
本发明的任务在于克服现有技术中存在的缺点,在现有生产工艺和干燥车间结构形式的基础上,构造一种新型的一体化车间,将干燥室与定型室集中到一个生产车间区域,实现产品生产流程在车间内部的无缝链接。该生产工艺与系统车间可适用于中高温等具有相同干燥工艺和干燥车间结构形式的食品生产过程。具有减少一线用工数量与用工劳动强度,节约生产成本,提高生产效率和经济效率的优点。The task of the present invention is to overcome the shortcomings in the prior art, and to construct a new type of integrated workshop on the basis of the existing production process and the structure of the drying workshop. The drying room and the setting room are concentrated in one production workshop area. Realize the seamless link of the product production process in the workshop. The production process and system workshop are suitable for medium and high temperature food production processes with the same drying process and drying workshop structure. It has the advantages of reducing the number and labor intensity of front-line workers, saving production costs, and improving production efficiency and economic efficiency.
本发明的目的是通过以下技术方案实现的:The purpose of the present invention is achieved through the following technical solutions:
一种用于中高温生产工艺的干燥系统,包括热泵机组和干燥室隧道系统。其中干燥室隧道系统包括送风风道,干燥室,回风风道,新风入口门,货物进口门,货物出口门,货物搁架,货架调整门,中间工艺门,送风口导流板,回风口导流板,保温墙体,红外线辅助加热器,微波辅助加热器和排风通道口。所述的送风风道是风机将达到指定温湿度空气送入到干燥室的通道,送风风道内设置干燥用货物搁架,被干燥货物放置于干燥货架上。所述的回风风道是将流过物料之后的空气送回热泵机组的通道,回风风道内也设置货物搁架。所述的新风入口门是新风进入系统的通道,与部分回风混合达到合适的温湿度。所述的货物进口门,货物出口门与货物搁架导轨相连,方便完成相关工艺后物料的输运。所述的货物搁架用于放置所需要干燥的物料及物料在各工艺步骤中的运输。货架调整门用来对干燥搁架的位置进行调节,可作为检修排风风机通道的检修门。中间工艺门可以作为检修门,也可作为干燥过程中间工艺货物搁架进出通道。所述的送风口导流板和回风口导流板是对空气进行导流,减小风阻,进风口导流板将经过热泵机组后的空气变向,导流到干燥室内,通过干燥室之后再经过回风口导流板,回到热泵机组完成下一次循环。所述的保温墙体采用具有防火功能的保温板,减少与外界进行热交换。为提高干燥效率,所述的红外线辅助加热器和微波辅助加热器为干燥物料温度要求较高或者水分扩散较慢时对空气辅助加热的热源,红外线辅助加热器安装在货物出口门附近的隧道内,微波辅助加热器安装在货物进口门附近的隧道内。所述的排风通道口是将一部分回风排出干燥室的通道,安装在干燥室回风口的顶部,利用风机完成排气工作。A drying system for a medium-high temperature production process, including a heat pump unit and a drying chamber tunnel system. The drying room tunnel system includes the air supply duct, the drying room, the return air duct, the fresh air inlet door, the cargo inlet door, the cargo outlet door, the cargo shelf, the shelf adjustment door, the intermediate process door, the air supply outlet deflector, the return Air outlet deflector, thermal insulation wall, infrared auxiliary heater, microwave auxiliary heater and exhaust channel opening. The air-supply duct is a channel through which the fan sends air reaching a specified temperature and humidity into the drying chamber. Shelves for drying goods are arranged in the air-supply duct, and the dried goods are placed on the drying shelves. The return air duct is a channel for sending the air flowing through the material back to the heat pump unit, and cargo shelves are also arranged in the return air duct. The fresh air inlet door is a channel through which fresh air enters the system, and is mixed with part of the return air to achieve a suitable temperature and humidity. The goods inlet door and the goods outlet door are connected with the goods shelf guide rails to facilitate the transportation of materials after the relevant processes are completed. The cargo shelf is used for placing the materials to be dried and for transporting the materials in each process step. The shelf adjustment door is used to adjust the position of the drying shelf, and can be used as an inspection door for inspecting the passage of the exhaust fan. The intermediate process door can be used as an inspection door, and can also be used as an access channel for intermediate process goods shelves in the drying process. The deflector at the air supply port and the deflector at the return air port guide the air to reduce wind resistance, and the deflector at the air inlet redirects the air passing through the heat pump unit and guides it into the drying room. After passing through the deflector of the return air outlet, it returns to the heat pump unit to complete the next cycle. The thermal insulation wall adopts the thermal insulation board with fireproof function to reduce heat exchange with the outside world. In order to improve the drying efficiency, the infrared auxiliary heater and the microwave auxiliary heater are heat sources for auxiliary heating of the air when the temperature of the dried material is high or the moisture diffusion is slow. The infrared auxiliary heater is installed in the tunnel near the cargo exit door , The microwave auxiliary heater is installed in the tunnel near the cargo entrance door. The air exhaust passage is a passage for discharging a part of the return air out of the drying chamber, and is installed on the top of the return air outlet of the drying chamber, and the fan is used to complete the exhaust work.
热泵机组包括加热段、动力室、预热段和能量回收段。所述的加热段主要包括热泵机组的冷凝器,负责对除湿后的空气进行加热,使空气达到干燥要求的温度条件。所述的动力室包括压缩机和送风机。压缩机负责提供制冷剂循环所需要的动力。送风机用来提供整个干燥室内的空气循环动力。所述的预热段是将部分加热段安装在动力室与能量回收段之间,用来预热进入动力室的空气,提高空气干度,防止损坏电气设备。所述能量回收段主要由热泵机组的蒸发器组成,回收回风的空气余能,达到能量回收的作用、提高机组效率。干燥室内的循环空气是新风从新风入口进入回风风道与部分回风混合之后,经过热泵机组的能量回收段进行除湿后,通过动力室,流经热泵机组的加热段进行加热,达到设定温度送入干燥室,实现空气在干燥室和热泵机组之间的循环流动。The heat pump unit includes a heating section, a power room, a preheating section and an energy recovery section. The heating section mainly includes the condenser of the heat pump unit, which is responsible for heating the dehumidified air to make the air reach the temperature required for drying. The power chamber includes a compressor and a blower. The compressor is responsible for providing the power required for the refrigerant cycle. The blower is used to provide air circulation power throughout the drying room. In the preheating section, part of the heating section is installed between the power chamber and the energy recovery section to preheat the air entering the power chamber, improve the dryness of the air, and prevent damage to electrical equipment. The energy recovery section is mainly composed of the evaporator of the heat pump unit, which recovers the residual air energy of the return air, so as to achieve the function of energy recovery and improve the efficiency of the unit. The circulating air in the drying room is fresh air which enters the return air duct from the fresh air inlet and mixes with part of the return air. After passing through the energy recovery section of the heat pump unit for dehumidification, it passes through the power room and flows through the heating section of the heat pump unit for heating to reach the set value. The temperature is sent into the drying room to realize the circulation of air between the drying room and the heat pump unit.
以山楂饼制造干燥工艺为例,介绍本发明的内容。山楂饼的制造工艺主要包括打浆、刮片、干燥、揭片、焖片、成品加工及包装这六部分。所述的打浆是将山楂煮烂之后与白糖等配料混合,并加入适当的水倒入打料机中打成浆泥。所述的刮片是将调好的果浆平摊到玻璃上,并用刮刀等工具刮成厚度1.5mm左右的湿片。所述的干燥是刮好浆液的玻璃板放在运载车架上,由货物入口门推入干燥室,等基本固定成型,且表面不会沾手,把运载货架由中间工艺门推出。所述揭片工艺是把半湿状态的饼片从玻璃板上揭下来,放入筛网上,再次用货物搁架推入干燥室内进行进一步干燥,当饼片含水量满足要求时,把货物搁架由出口门推出。所述焖片工艺是把干燥好的饼片用包装纸层层隔开,堆放到焖片室中,使饼片的白糖充分融化,并均匀扩散到饼片中。成品加工即包装是指把焖好的饼片切割,包装成成品。这其中以干燥,揭片,焖片为主要的加工工艺。干燥是将货物搁架上的山楂饼浆送入到干燥车间进行除去水分的过程。干燥车间的进风温度为65~70℃。通过导流板将处理过后的空气导流到干燥室内,对山楂饼进行干燥。干燥后的空气部分通过排风口排到大气中,另一部分与新风混合继续进行下一个循环。生产流程中,将热泵机组开启之后,经过制浆,刮片工艺之后。将干燥物料放置在货物搁架上,从货物入口进入。经过干燥过程之后,通过中间工艺门取出,进行揭片工艺。之后再由工艺门送入干燥室继续进行揭片工艺。经过揭片之后的半成品山楂饼由货物出口取出,进行焖片工艺,再进行成品加工以及包装工艺,完成整个生产过程。Taking the manufacturing and drying process of hawthorn cake as an example, the content of the present invention is introduced. The manufacturing process of hawthorn cake mainly includes six parts: beating, scraping, drying, peeling, stewing, finished product processing and packaging. The beating is to mix the hawthorn with white sugar and other ingredients after being boiled, and add appropriate water and pour it into a beater to make a slurry. The scraper is to spread the adjusted pulp on the glass, and scrape it into a wet sheet with a thickness of about 1.5mm with a scraper or other tools. The drying is to put the scraped glass plate on the carrier frame, push it into the drying room through the cargo entrance door, wait for the basic fixed shape, and the surface will not stick to hands, and push the carrier frame out through the intermediate process door. The peeling process is to peel off the semi-wet cake from the glass plate, put it on the screen, and push it into the drying room with the goods rack for further drying. When the water content of the cake meets the requirements, put the goods on the shelf The rack is pushed out by the exit door. The process of stewing slices is to separate the dried cake slices layer by layer with wrapping paper, and stack them in the slice stewing chamber, so that the white sugar of the cake slices is fully melted and evenly diffused into the cake slices. Finished product processing or packaging refers to cutting and packaging the stewed pie slices into finished products. Among them, drying, peeling and stewing are the main processing techniques. Drying is the process of sending the hawthorn cake slurry on the cargo shelf to the drying workshop to remove moisture. The air inlet temperature of the drying workshop is 65~70℃. The treated air is guided into the drying chamber through the deflector to dry the hawthorn cake. Part of the dried air is discharged into the atmosphere through the air outlet, and the other part is mixed with fresh air to continue the next cycle. In the production process, after the heat pump unit is turned on, it goes through the pulping and scraping process. Place dry materials on the cargo rack, which is accessed through the cargo inlet. After the drying process, it is taken out through the middle process door to perform the peeling process. Then it is sent to the drying room by the process door to continue the peeling process. After peeling, the semi-finished hawthorn cakes are taken out from the export of goods, subjected to the stewing process, and then to the finished product processing and packaging process to complete the entire production process.
附图说明Description of drawings
图1为本发明实施例的中高温生产工艺的干燥系统示意图。Fig. 1 is a schematic diagram of a drying system of a medium-high temperature production process according to an embodiment of the present invention.
具体实施方式detailed description
下面结合附图,通过具体实施例,对本发明的技术方案进行说明。The technical solutions of the present invention will be described below through specific embodiments in conjunction with the accompanying drawings.
本发明实施例提供了一种用于中高温生产工艺的干燥系统,请参考图1,包括:干燥室隧道系统和热泵机组。其中干燥室隧道系统包括送风风道,回风风道,送风口导流板1,新风入口门5,货物进口门7,货架调整门8,排风通道口9,回风口导流板10,保温墙体11,中间工艺门12,货物搁架13,红外线辅助加热器14,货物出口门15和微波辅助加热器17。热泵机组送风口经过送风口导流板1,将空气导流到送风风道内,空气在送风风道内对货物进行干燥之后再经过回风口导流板10流入回风风道。干燥室,回风风道,送风风道均通过保温墙体11与外界环境隔绝。货物进口门7,货物出口门15,货架调整门8和中间工艺门12与外界隔热隔气,密封良好。货物进口门7,货物出口门15与货物搁架13的导轨相连,方便完成相关工艺后物料的输运。货物搁架13分为干燥用平板隔板和揭片用铁架搁架,用于搁置所需要干燥的物料及物料在各工艺步骤中的运输。货架调整门8可以用来调节货物搁架的位置。中间工艺门12负责将完成定型工艺后的产品取出,进行揭片工艺之后,再送入回风通道进行焖片工艺。中间隔热墙2与保温墙体11采用一定厚度保温板,减少与外界进行热交换。红外线辅助加热器14安装在送风风道入口靠近货物出口门15处,用于干燥所需温度较高物料的辅助加热,提高干燥效率;微波辅助加热器17安装于货物进口门7附近的干燥隧道内。An embodiment of the present invention provides a drying system for a medium-high temperature production process, please refer to FIG. 1 , including: a drying chamber tunnel system and a heat pump unit. The drying room tunnel system includes air supply duct, return air duct, air supply outlet deflector 1, fresh air inlet door 5, cargo inlet door 7, shelf adjustment door 8, exhaust air passage opening 9, return air outlet deflector 10 , Insulation wall 11, intermediate process door 12, goods shelf 13, infrared auxiliary heater 14, goods export door 15 and microwave auxiliary heater 17. The air supply port of the heat pump unit passes the air supply port deflector 1 to guide air into the air supply duct, and the air flows into the return air duct through the return air deflector 10 after drying the goods in the air supply duct. The drying room, return air duct, and air supply duct are all isolated from the external environment by the thermal insulation wall 11 . The goods inlet door 7, the goods outlet door 15, the shelf adjustment door 8 and the middle process door 12 are heat and air insulated from the outside world, and are well sealed. The goods inlet door 7 and the goods outlet door 15 are connected with the guide rails of the goods shelf 13, so as to facilitate the transportation of materials after completing related processes. The cargo shelf 13 is divided into a flat partition for drying and an iron frame shelf for peeling off, and is used for shelving the materials that need to be dried and the transportation of the materials in each process step. The shelf adjustment door 8 can be used to adjust the position of the cargo shelf. The middle process door 12 is responsible for taking out the products after the shaping process is completed, and after performing the peeling process, it is sent into the return air channel for the stewing process. The middle insulation wall 2 and the insulation wall body 11 adopt a certain thickness of insulation board to reduce heat exchange with the outside. The infrared auxiliary heater 14 is installed at the entrance of the air supply duct close to the cargo outlet door 15, and is used for auxiliary heating of materials with higher temperature required for drying to improve drying efficiency; the microwave auxiliary heater 17 is installed in the drying area near the cargo inlet door 7. inside the tunnel.
热泵机组由压缩机、安装于风道内的蒸发器、冷凝器、预热段16、储液器、干燥过滤器、节流阀组成。压缩机和风机组成的动力室4内还包括了储液器、干燥过滤器、节流阀等装置。送风机位于动力室4内,为空气循环提供动力。加热段3安装在空气出口端,由热泵机组的冷凝器组成,用于加热除湿后的空气,使得温度达到干燥室要求的温度。能量回收段6安装在回风入口端,由热泵机组的蒸发器组成,用于能量回收,提高热泵机组的效率。中央控制室来控制整套系统的动力室4的启停。预热段16安装在动力室4和能量回收段6中间的位置,用来预热进入动力室的空气,提高空气干度,防止损坏电气设备。The heat pump unit is composed of a compressor, an evaporator installed in the air duct, a condenser, a preheating section 16, a liquid receiver, a dry filter, and a throttle valve. The power chamber 4 composed of the compressor and the fan also includes devices such as a liquid reservoir, a dry filter, a throttle valve, and the like. The blower is located in the power chamber 4 and provides power for air circulation. The heating section 3 is installed at the air outlet end and is composed of the condenser of the heat pump unit, which is used to heat the dehumidified air so that the temperature reaches the temperature required by the drying room. The energy recovery section 6 is installed at the inlet of the return air and is composed of the evaporator of the heat pump unit, used for energy recovery and improving the efficiency of the heat pump unit. The central control room is used to control the start and stop of the power room 4 of the whole system. The preheating section 16 is installed in the middle of the power chamber 4 and the energy recovery section 6, and is used to preheat the air entering the power chamber, improve the dryness of the air, and prevent damage to electrical equipment.
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CN105716410A (en) * | 2016-03-23 | 2016-06-29 | 青岛大学 | Haw flake and caked sugar heat pump dryer and drying system |
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CN207247812U (en) * | 2017-05-07 | 2018-04-17 | 青岛大学 | A kind of drying system for high temperature production technology |
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CN101936644A (en) * | 2009-09-30 | 2011-01-05 | 湖南省浏阳市择明热工器材有限公司 | Hot air drying system heated by double energy sources |
CN104279853A (en) * | 2014-09-28 | 2015-01-14 | 东莞市蓝冠环保节能科技有限公司 | Air source fluoride pump type drying and dehumidifying integrated machine and drying system thereof |
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Application publication date: 20170908 |