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CN104964473B - A kind of energy-saving freezing depth dehumidified air processing method - Google Patents

A kind of energy-saving freezing depth dehumidified air processing method Download PDF

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Publication number
CN104964473B
CN104964473B CN201510275819.3A CN201510275819A CN104964473B CN 104964473 B CN104964473 B CN 104964473B CN 201510275819 A CN201510275819 A CN 201510275819A CN 104964473 B CN104964473 B CN 104964473B
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refrigeration cycle
freeze drying
air
refrigeration
drying kind
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CN104964473A (en
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田小亮
李晓花
孙晖
刘瑞璟
王兆俊
邵杰
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Qingdao University
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Qingdao University
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B1/00Compression machines, plants or systems with non-reversible cycle
    • F25B1/10Compression machines, plants or systems with non-reversible cycle with multi-stage compression
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F12/00Use of energy recovery systems in air conditioning, ventilation or screening
    • F24F12/001Use of energy recovery systems in air conditioning, ventilation or screening with heat-exchange between supplied and exhausted air
    • F24F12/002Use of energy recovery systems in air conditioning, ventilation or screening with heat-exchange between supplied and exhausted air using an intermediate heat-transfer fluid
    • F24F12/003Use of energy recovery systems in air conditioning, ventilation or screening with heat-exchange between supplied and exhausted air using an intermediate heat-transfer fluid using a heat pump
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F3/00Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
    • F24F3/12Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
    • F24F3/14Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F5/00Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B41/00Fluid-circulation arrangements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F3/00Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
    • F24F3/12Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
    • F24F3/14Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification
    • F24F2003/144Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification by dehumidification only
    • F24F2003/1446Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification by dehumidification only by condensing

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Air Conditioning Control Device (AREA)

Abstract

The invention belongs to Refrigeration & Air-Conditioning technical field, it is related to a kind of energy-saving freezing depth dehumidified air processing method, pending air flows out into conditioning section from air pretreatment section, processed air is first cooled by heat pipe cold recovery with evaporator group, then colod-application heat exchanger group is prefabricated again further to cool down, then liquid water droplets are removed through preceding water fender with after evaporator group further cooling by heat pump cycle, again the liquid water droplets carried secretly in air are removed after freeze drying kind of refrigeration cycle carries out depth cooling with evaporator through rear water plate, flow through after freeze drying kind of refrigeration cycle heated with condenser, air sequentially enters air inlet post processing section after two phase flow cold recovery is further heated using condenser group and heat pump cycle condenser group, complete the conditioning processing procedure of air;Its technique is simple, easy to operate, and cost is low, less energy consumption, and energy utilization rate is high, and refrigerated dehumidification efficiency high is environment-friendly.

Description

一种节能型冷冻深度除湿空气处理方法An energy-saving refrigeration deep dehumidification air treatment method

技术领域:Technical field:

本发明属于制冷与空调技术领域,涉及一种将内外复合式气液两相流热管冷量回收节能技术、内外复合式热泵节能技术、多级复合式冷冻深度除湿技术等有机结合而形成的空气处理装置,特别是一种高效节能型冷冻深度除湿空气处理方法。The invention belongs to the technical field of refrigeration and air conditioning, and relates to an air conditioning system formed by organically combining internal and external composite gas-liquid two-phase flow heat pipe cooling energy recovery technology, internal and external composite heat pump energy saving technology, and multi-stage composite refrigeration depth dehumidification technology. A treatment device, in particular a high-efficiency and energy-saving refrigeration deep dehumidification air treatment method.

背景技术:Background technique:

目前,制药、电子、纺织等行业的许多生产过程中一年四季都必须有低湿的工艺性空调环境,而在夏季实现低湿的空气处理过程往往需要消耗大量的能源;对流干燥(也称气流干燥)是工农业生产过程中应用最为广泛的一种干燥方式,要实现对流干燥,必须有低湿度干燥气源,而提供该低湿气源往往也需要消耗大量的能源。现有实现空气除湿的处理方法主要包括冷冻除湿法和转轮除湿法两种方案,通常采用的冷冻除湿法是利用7-12℃的冷冻水作冷媒来冷却被处理的空气,可达到的机器露点温度一般在14℃以上,但是无法满足低温、低湿的空气处理要求;转轮除湿法尽管能达到很低的机器露点温度,能够满足低湿的空气处理要求,但处理过程能耗十分巨大。At present, many production processes in industries such as pharmaceuticals, electronics, and textiles must have a low-humidity technological air-conditioning environment throughout the year, and the air treatment process that achieves low humidity in summer often consumes a lot of energy; convection drying (also known as airflow drying) ) is the most widely used drying method in industrial and agricultural production processes. To achieve convective drying, there must be a low-humidity dry air source, and providing this low-humidity air source often requires a lot of energy consumption. The existing treatment methods for realizing air dehumidification mainly include freezing dehumidification method and rotary dehumidification method. The commonly used freezing dehumidification method uses 7-12°C refrigerated water as a refrigerant to cool the treated air. The dew point temperature is generally above 14°C, but it cannot meet the low temperature and low humidity air treatment requirements; although the rotary dehumidification method can achieve a very low machine dew point temperature and meet the low humidity air treatment requirements, the energy consumption of the treatment process is huge.

为实现对空气较为彻底的除湿,同时降低除湿过程能耗,近几十年来,人们采用了直膨式冷冻除湿方法,如各类小型冷冻除湿机、小型冷冻调温调湿机等,使冷冻除湿法处理空气所能达到的机器露点温度由14℃以上降低为10℃以上,除湿深度有所提高,但仍不能满足许多生产过程的机器露点温度要求。本申请人提出的专利号为ZL201210290885.4的发明专利公开了一种节能式调温调湿空气处理方法,通过将内外复合式两相流热管冷量回收利用技术、并联复合式压缩制冷技术、内外复合式热泵节能技术等有机结合,所构成的空调系统的能耗仅为利用转笼除湿方法空调系统的1/5-1/3,而其使机器露点温度能够长期稳定地控制在4℃,具有显著的节能效果,能够满 足一般工业系统要求的机器露点温度要求,但该技术不能满足许多特殊生产过程要求的机器露点温度低于4℃,有时甚至要求低到-25℃的情形。In order to achieve a more thorough dehumidification of the air and reduce the energy consumption of the dehumidification process, in recent decades, people have adopted direct expansion refrigeration dehumidification methods, such as various small refrigeration dehumidifiers, small refrigeration temperature and humidity control machines, etc. The machine dew point temperature that can be achieved by dehumidification treatment air is reduced from above 14°C to above 10°C, and the depth of dehumidification has increased, but it still cannot meet the machine dew point temperature requirements of many production processes. The invention patent with the patent number ZL201210290885.4 proposed by the applicant discloses an energy-saving air treatment method with temperature and humidity regulation, which uses the internal and external compound two-phase flow heat pipe cooling capacity recycling technology, parallel compound compression refrigeration technology, The energy consumption of the air conditioning system formed by the organic combination of internal and external composite heat pump energy-saving technologies is only 1/5-1/3 of that of the air-conditioning system using the dehumidification method of the tumbler cage, and it enables the dew point temperature of the machine to be stably controlled at 4°C for a long time , has a significant energy-saving effect, and can meet the machine dew point temperature requirements of general industrial systems, but this technology cannot meet the machine dew point temperature required by many special production processes below 4°C, and sometimes even requires as low as -25°C.

发明内容:Invention content:

本发明的目的在于克服现有技术存在的缺点,寻求设计提供一种节能型冷冻深度除湿的空气处理方法,解决现有技术中低湿空气处理过程能耗巨大的问题。The purpose of the present invention is to overcome the shortcomings of the prior art, seek to design and provide an air treatment method for energy-saving refrigeration and deep dehumidification, and solve the problem of huge energy consumption in the low-humidity air treatment process in the prior art.

为了实现上述目的,本发明在节能型冷冻深度除湿空气处理装置中实现,其具体过程是:在风机的作用下,待处理的空气从空气预处理段中流出并进入调温调湿段,在调温调湿段内,被处理的空气先被内外复合式两相流热管冷量回收利用子系统中的热管冷量回收用蒸发器组冷却降温,然后再被预制冷用换热器子系统的预制冷用换热器组进一步冷却,接着被内外复合式热泵循环子系统的热泵循环用蒸发器组进一步冷却,此时,空气温度不低于4℃,达到第1露点温度;达到第1露点温度的空气经前挡水板去除液态水滴后,再经过多级复合式冷冻除湿制冷循环子系统的2-10个冷冻除湿制冷循环用蒸发器进行深度冷却,被处理的空气最终达到第2露点温度,最低达-25℃,随后,空气经后挡水板去除空气中夹带的液态水滴后依次流经多级复合式冷冻除湿制冷循环子系统的2-10个冷冻除湿制冷循环用冷凝器进行加热,空气温度从第2露点温度加热到4-12℃后,空气进入两相流冷量回收利用冷凝器组被进一步加热到12-20℃,最后进入热泵循环子系统的热泵循环用冷凝器组进一步加热,空气达到设定的供风温度后进入空气后处理段,完成空气的调温调湿处理过程;其中,中央控制子系统通过调节预制冷用换热器子系统与热泵循环子系统的制冷能力控制第1露点温度,达到降温和初步除湿的目标;中央控制子系统通过调节多级复合式冷冻除湿制冷循环子系统的制冷能力控制第2露点温度,达到深度除湿和准确控制相对湿度的目标;再通过调节热泵循环子系统中对外排热量的大小及无排热热泵循环子系统 的工作台数控制出风温度,达到调温的目标。In order to achieve the above object, the present invention is implemented in an energy-saving deep-frozen dehumidification air treatment device. The specific process is: under the action of the fan, the air to be treated flows out from the air pretreatment section and enters the temperature and humidity adjustment section. In the temperature and humidity control section, the treated air is first cooled by the evaporator group for heat pipe cooling recovery in the internal and external composite two-phase flow heat pipe cooling recovery subsystem, and then cooled by the heat exchanger subsystem for pre-cooling The heat exchanger group for pre-cooling is further cooled, and then further cooled by the evaporator group for the heat pump cycle of the internal and external composite heat pump cycle subsystem. The air at the dew point temperature passes through the front water shield to remove liquid water droplets, and then goes through 2-10 refrigerating, dehumidifying and refrigerating cycles of the multi-stage composite refrigerating, dehumidifying and refrigerating cycle subsystem for deep cooling with the evaporator, and the treated air finally reaches the second The dew point temperature is as low as -25°C. Afterwards, the air passes through the rear fender to remove the liquid water droplets entrained in the air, and then flows through 2-10 condensers for refrigeration, dehumidification and refrigeration cycles in the multi-stage composite refrigeration, dehumidification and refrigeration cycle subsystem. After heating, the air temperature is heated from the second dew point temperature to 4-12°C, and then the air enters the two-phase flow cooling recovery and utilization condenser group to be further heated to 12-20°C, and finally enters the heat pump cycle subsystem of the heat pump cycle for condensation After the air reaches the set air supply temperature, it enters the air after-treatment section to complete the air temperature and humidity adjustment process; among them, the central control subsystem adjusts the pre-cooling heat exchanger subsystem and the heat pump circulation sub-system. The cooling capacity of the system controls the first dew point temperature to achieve the goal of cooling and preliminary dehumidification; the central control subsystem controls the second dew point temperature by adjusting the cooling capacity of the multi-stage compound refrigeration dehumidification refrigeration cycle subsystem to achieve deep dehumidification and accurate control of relative humidity. Humidity target; and then by adjusting the amount of heat exhausted in the heat pump circulation subsystem and the number of working units of the heat pump circulation subsystem without heat dissipation, the outlet air temperature is controlled to achieve the goal of temperature regulation.

本发明所述节能型冷冻深度除湿空气处理装置的主体结构包括内外复合式气液两相流热管冷量回收、预制冷用换热器、内外复合式热泵循环、多级复合式冷冻除湿制冷循环和中央控制五个子系统,内外复合式气液两相流热管冷量回收子系统包括热管冷量回收用蒸发器组和热管冷量回收用冷凝器组,热管冷量回收用蒸发器组的两端分别与调温调湿段和预制冷用换热器组连通,调温调湿段的前端与空气预处理段连通;预制冷用换热器子系统包括预制冷用换热器组、预制冷用换热器内外连接管和预制冷用换热器的室外机组;预制冷用换热器组的上端通过预制冷用换热器内外连接管与预制冷用换热器的室外机组连通;内外复合式热泵循环子系统包括热泵循环用蒸发器组和热泵循环用冷凝器组;热泵循环用蒸发器组的前端与预制冷用换热器组连通,后端设有前挡水板,前挡水板后端设有第1露点温度传感器,第1露点温度传感器通过第1露点温度传感器信号线与中央控制器电信息连接;多级复合式冷冻除湿制冷循环子系统由2-10个冷冻除湿制冷循环按照串、并联复合的结构形式布置构成,2-10个冷冻除湿制冷循环的结构与大小完全相同,按气流流动方向,2-10个冷冻除湿制冷循环蒸发器采用并联方式布置,2-10个冷冻除湿制冷循环冷凝器采用串联方式布置,每个冷冻除湿制冷循环均包括冷冻除湿制冷循环蒸发器供液管、冷冻除湿制冷循环化霜电磁阀、冷冻除湿制冷循环节流阀、冷冻除湿制冷循环化霜蒸汽管、冷冻除湿制冷循环干燥过滤器、冷冻除湿制冷循环储液罐、回液管、冷冻除湿制冷循环回气温度传感器、冷冻除湿制冷循环蒸发器用接水盘、冷冻除湿制冷循环回气管、冷冻除湿制冷循环压缩机、冷冻除湿制冷循环排气母管电磁阀、冷冻除湿制冷循环排气母管、冷冻除湿制冷循环用蒸发器和冷冻除湿制冷循环用冷凝器,冷冻除湿制冷循环用蒸发器的后侧设有冷冻除湿制冷循环冷凝器后调节风阀,冷冻除湿制冷循环用蒸发器的下端设有冷冻除湿制冷循环蒸发器用接水盘,冷冻除湿制冷循环用蒸发器分别通过冷冻除湿制冷循环蒸发器供液管、冷冻除湿制冷循环化霜蒸汽 管、回液管、冷冻除湿制冷循环回气管和冷冻除湿制冷循环排气母管与冷冻除湿制冷循环用冷凝器管道联通,冷冻除湿制冷循环压缩机通过冷冻除湿制冷循环回气管从冷冻除湿制冷循环用蒸发器中吸入低压蒸汽,冷冻除湿制冷循环压缩机的排气送入冷冻除湿制冷循环化霜蒸汽管和冷冻除湿制冷循环排气母管,冷冻除湿制冷循环蒸发器供液管和回液管串接联通,冷冻除湿制冷循环蒸发器供液管和回液管之间从前向后依次设有冷冻除湿制冷循环节流阀、冷冻除湿制冷循环干燥过滤器和冷冻除湿制冷循环储液罐,冷冻除湿制冷循环化霜蒸汽管上设有冷冻除湿制冷循环化霜电磁阀,冷冻除湿制冷循环回气管和冷冻除湿制冷循环排气母管之间的管路上依次设有冷冻除湿制冷循环回气温度传感器、冷冻除湿制冷循环压缩机和冷冻除湿制冷循环排气母管电磁阀;第一个冷冻除湿制冷循环用冷凝器的前端设有后挡水板,后挡水板和第一个冷冻除湿制冷循环用冷凝器之间设有第2露点温度传感器;最后一个冷冻除湿制冷循环用冷凝器的后侧依次设有热管冷量回收用冷凝器组、热泵循环用冷凝器组、风机和空气后处理段,空气后处理段内设置有出风口温湿度传感器和出风口风速风量传感器;中央控制子系统包括中央控制器、冷冻除湿制冷循环化霜电磁阀控制线、冷冻除湿制冷循环回气温度传感器信号线、第1露点温度传感器信号线、冷冻除湿制冷循环蒸发器后调节风阀控制线、冷冻除湿制冷循环压缩机控制线、冷冻除湿制冷循环排气母管电磁阀控制线、第2露点温度传感器信号线、风机风量调节控制线、出风口温湿度传感器信号线和出风口风速风量传感器信号线,冻除湿制冷循环化霜电磁阀、冷冻除湿制冷循环回气温度传感器、第1露点温度传感器、冷冻除湿制冷循环蒸发器后调节风阀、冷冻除湿制冷循环压缩机、冷冻除湿制冷循环排气母管电磁阀、第2露点温度传感器、风机、出风口温湿度传感器和出风口风速风量传感器分别通过冷冻除湿制冷循环化霜电磁阀控制线、冷冻除湿制冷循环回气温度传感器信号线、第1露点温度传感器信号线、冷冻除湿制冷循环蒸发器后调节风阀控制线、冷冻除湿制冷循环压缩机控制线、冷冻除湿制冷循环排气母管电 磁阀控制线、第2露点温度传感器信号线、风机风量调节控制线、出风口温湿度传感器信号线和出风口风速风量传感器信号线与中央控制器电信息连接。The main structure of the energy-saving refrigerated deep dehumidification air treatment device of the present invention includes an internal and external composite gas-liquid two-phase flow heat pipe cooling capacity recovery, a heat exchanger for pre-cooling, an internal and external composite heat pump cycle, and a multi-stage composite refrigeration dehumidification refrigeration cycle And the central control five subsystems, the internal and external composite gas-liquid two-phase flow heat pipe cooling capacity recovery subsystem includes the evaporator group for heat pipe cooling capacity recovery and the condenser group for heat pipe cooling capacity recovery, and the two evaporator groups for heat pipe cooling capacity recovery The two ends are respectively connected with the temperature and humidity regulation section and the heat exchanger group for pre-cooling, and the front end of the temperature and humidity regulation section is connected with the air pretreatment section; the heat exchanger subsystem for pre-cooling includes the heat exchanger group for pre-cooling, pre-cooling The inner and outer connecting pipes of the heat exchanger for cooling and the outdoor unit of the heat exchanger for pre-cooling; the upper end of the heat exchanger group for pre-cooling communicates with the outdoor unit of the heat exchanger for pre-cooling through the inner and outer connecting pipes of the heat exchanger for pre-cooling; The internal and external compound heat pump cycle subsystem includes the evaporator group for the heat pump cycle and the condenser group for the heat pump cycle; There is a first dew point temperature sensor at the rear end of the water baffle, and the first dew point temperature sensor is connected with the electrical information of the central controller through the signal line of the first dew point temperature sensor; The dehumidification and refrigeration cycle is arranged in series and parallel composite structure. The structure and size of 2-10 refrigeration, dehumidification and refrigeration cycles are exactly the same. According to the direction of airflow, the evaporators of 2-10 refrigeration, dehumidification and refrigeration cycles are arranged in parallel. 2 -10 refrigerating, dehumidifying and refrigerating cycle condensers are arranged in series, and each refrigerating, dehumidifying and refrigerating cycle includes a liquid supply pipe for the evaporator of the refrigerating, dehumidifying and refrigerating cycle, a defrosting solenoid valve for the refrigerating, dehumidifying and refrigerating cycle, a throttle valve for the refrigerating, dehumidifying and refrigerating cycle, and Dehumidification and refrigeration cycle defrosting steam pipe, freezing and dehumidification and refrigeration cycle drying filter, freezing and dehumidification and refrigeration cycle liquid storage tank, liquid return pipe, freezing and dehumidification and refrigeration cycle return air temperature sensor, freezing and dehumidification and refrigeration cycle evaporator water tray, freezing and dehumidification and refrigeration Circulation return pipe, refrigerating and dehumidifying refrigerating cycle compressor, refrigerating and dehumidifying refrigerating cycle exhaust main solenoid valve, refrigerating and dehumidifying refrigerating cycle exhaust main pipe, evaporator for refrigerating and dehumidifying refrigerating cycle and condenser for refrigerating and dehumidifying refrigerating cycle, refrigerating and dehumidifying and refrigerating The rear side of the evaporator for refrigeration and dehumidification refrigeration cycle is equipped with a rear regulating air valve for the condenser of the refrigeration dehumidification refrigeration cycle. The liquid supply pipe of the evaporator of the refrigerating and dehumidifying refrigeration cycle, the defrosting steam pipe of the refrigerating and dehumidifying and refrigerating cycle, the liquid return pipe, the return pipe of the refrigerating and dehumidifying and refrigerating cycle, and the exhaust main pipe of the refrigerating and dehumidifying and refrigerating cycle are connected with the condenser pipes for the refrigerating, dehumidifying and refrigerating cycle. The dehumidification refrigeration cycle compressor sucks low-pressure steam from the evaporator of the refrigeration dehumidification refrigeration cycle through the return air pipe of the refrigeration dehumidification refrigeration cycle, and the exhaust gas of the refrigeration dehumidification refrigeration cycle compressor is sent to the defrosting steam pipe of the refrigeration dehumidification refrigeration cycle and the exhaust gas of the refrigeration dehumidification refrigeration cycle. The gas main pipe, the liquid supply pipe and the liquid return pipe of the refrigerating and dehumidifying refrigeration cycle evaporator are connected in series, Between the liquid supply pipe and the liquid return pipe of the refrigerating and dehumidifying refrigerating cycle evaporator, a refrigerating and dehumidifying refrigerating cycle throttling valve, a refrigerating and dehumidifying refrigerating cycle drying filter and a refrigerating, dehumidifying and refrigerating cycle liquid storage tank are arranged in sequence from front to back. The frost steam pipe is equipped with a defrosting solenoid valve for the freezing, dehumidification and refrigeration cycle, and the pipeline between the return air pipe of the refrigeration and dehumidification refrigeration cycle and the exhaust main pipe of the refrigeration, dehumidification and refrigeration cycle is provided with a temperature sensor for the return air of the refrigeration, dehumidification and refrigeration cycle, and a temperature sensor for the refrigeration, dehumidification and refrigeration cycle. Circulating compressor and solenoid valve for exhaust main pipe of refrigeration, dehumidification and refrigeration cycle; the front end of the first condenser for refrigeration, dehumidification and refrigeration cycle is provided with a rear water baffle, between the rear water shield and the first condenser for refrigeration, dehumidification and refrigeration cycle There is a second dew point temperature sensor between them; the rear side of the last condenser for refrigeration, dehumidification and refrigeration cycle is equipped with a condenser group for heat pipe cooling recovery, a condenser group for heat pump cycle, a fan and an air post-treatment section, and the air post-treatment There are air outlet temperature and humidity sensors and air outlet wind speed and air volume sensors in the section; the central control subsystem includes the central controller, the control line of the defrosting solenoid valve of the freezing and dehumidification refrigeration cycle, the signal line of the return air temperature sensor of the refrigeration, dehumidification and refrigeration cycle, and the first dew point Temperature sensor signal line, refrigeration dehumidification refrigeration cycle evaporator post-regulation air valve control line, refrigeration dehumidification refrigeration cycle compressor control line, refrigeration dehumidification refrigeration cycle exhaust master solenoid valve control line, second dew point temperature sensor signal line, fan air volume Adjustment control line, air outlet temperature and humidity sensor signal line and air outlet air speed and air volume sensor signal line, freezing and dehumidification refrigeration cycle defrost solenoid valve, refrigeration dehumidification refrigeration cycle return air temperature sensor, first dew point temperature sensor, refrigeration dehumidification refrigeration cycle evaporator Rear adjustment damper, refrigeration dehumidification refrigeration cycle compressor, refrigeration dehumidification refrigeration cycle exhaust main pipe solenoid valve, second dew point temperature sensor, fan, air outlet temperature and humidity sensor and air outlet air speed and air volume sensor respectively defrost through the refrigeration dehumidification refrigeration cycle Solenoid valve control line, refrigerating and dehumidifying refrigeration cycle return air temperature sensor signal line, first dew point temperature sensor signal line, refrigerating, dehumidifying and refrigerating cycle evaporator air valve control line, refrigerating and dehumidifying refrigerating cycle compressor control line, refrigerating and dehumidifying refrigerating cycle The exhaust main pipe electromagnetic valve control line, the second dew point temperature sensor signal line, the fan air volume adjustment control line, the air outlet temperature and humidity sensor signal line, and the air outlet air speed and air volume sensor signal line are connected to the central controller for electrical information.

本发明所述内外复合式两相流热管冷量回收利用子系统与发明专利ZL201210290885.4公开的一种节能式调温调湿空气处理方法中内外复合式两相流热管冷量回收利用子系统相同。The internal and external composite two-phase flow heat pipe cooling capacity recycling subsystem of the present invention and the internal and external composite two-phase flow heat pipe cooling capacity recycling subsystem in an energy-saving temperature and humidity regulation air treatment method disclosed in the invention patent ZL201210290885.4 same.

本发明所述预制冷用换热器子系统为与专利ZL201210290885.4公开的一种节能式调温调湿空气处理方法中相同的并联复合式压缩制冷子系统,或是由通用冷水机组的表冷器构成的换热器子系统,预制冷用换热器子在夏季最炎热的工况下,能高效地排出空调循环系统中多余的热量。The heat exchanger subsystem for pre-refrigeration described in the present invention is the same parallel compound compression refrigeration subsystem as in the energy-saving temperature and humidity regulation air treatment method disclosed in patent ZL201210290885. The heat exchanger subsystem constituted by the cooler, the heat exchanger for pre-refrigeration can efficiently discharge the excess heat in the air conditioning circulation system under the hottest working conditions in summer.

本发明所述热泵循环子系统与发明专利ZL201210290885.4公开的一种节能式调温调湿空气处理方法中热泵循环子系统类同,包括内外复合式带排热热泵循环和内外复合式不带排热热泵循环两类循环,热泵循环子系统的蒸发器的冷量用于进一步冷却预冷后的空气,使其达到第1露点温度,实现高效降温除湿,其冷凝器的排热,一部分用于加热达到第2露点温度后的低温、低湿空气,使调温调湿段出风温度达到设定要求,另一部分多余的热量,通过室外冷凝器排放到外部环境中,实现调温调湿段能量的平衡控制。The heat pump circulation subsystem of the present invention is similar to the heat pump circulation subsystem in an energy-saving temperature and humidity control air treatment method disclosed in the invention patent ZL201210290885.4, including internal and external composite heat pump circulation with heat removal and internal and external composite without There are two types of heat-exhausting heat pump cycle. The cooling capacity of the evaporator of the heat pump cycle subsystem is used to further cool the pre-cooled air to reach the first dew point temperature to achieve efficient cooling and dehumidification. It is used to heat the low-temperature and low-humidity air after reaching the second dew point temperature, so that the temperature of the air outlet in the temperature and humidity adjustment section reaches the set requirements, and the other part of the excess heat is discharged to the external environment through the outdoor condenser to realize the temperature and humidity adjustment section. Energy balance control.

本发明所述多级复合式冷冻除湿制冷循环子系统的工作原理为:冷冻除湿制冷循环用蒸发器对达到第1机器露点温度的空气进一步实现深度冷却除湿,使被处理的空气最终达到很低的第2机器露点温度(最低可达-25℃),而冷冻除湿制冷循环用冷凝器的排热,用于加热达到第2露点温度后的低温、低湿空气,实现冷、热能量的同时高效利用;采用多级复合的目的是通过轮流工作方式,保证在其中一级冷冻除湿制冷循环中进行化霜去冰处理时,其余冷冻除湿制冷循环仍能保证满足深度冷却去湿的要求。The working principle of the multi-stage composite freezing, dehumidification and refrigeration cycle subsystem of the present invention is: the evaporator for the refrigeration, dehumidification and refrigeration cycle further realizes deep cooling and dehumidification of the air reaching the dew point temperature of the first machine, so that the processed air finally reaches a very low temperature. The dew point temperature of the second machine (the lowest can reach -25 ℃), and the heat exhausted by the condenser in the refrigeration dehumidification and refrigeration cycle is used to heat the low-temperature and low-humidity air after reaching the second dew point temperature, so as to realize the high efficiency of cold and heat energy at the same time Utilization; the purpose of adopting multi-stage compounding is to ensure that when defrosting and deicing treatment is performed in one of the first-stage refrigeration and dehumidification refrigeration cycles, the remaining refrigeration, dehumidification and refrigeration cycles can still meet the requirements of deep cooling and dehumidification through the working mode of rotation.

本发明所述中央控制子系统的工作原理为:由布置在调温调湿段中的出风温湿度传感器获得送风温度,中央控制器通过对热泵循环子 系统中室外冷凝器风机(详见专利ZL201210290885.4)的转速控制来改变对外排热量,实现对调温调湿段出风温度的调节,若室外冷凝器的风机转速调到极限仍不能满足送风温度的调节要求,则进一步自动调节带排热热泵循环子系统中压缩机的工作频率,完成送风温度的调节,具体过程如ZL201210290885.4公开;中央控制子系统通过布置在调温调湿段中的第1露点温度传感器和第1露点温度传感器信号线获得第1露点温度,中央控制器通过对并联复合式压缩制冷子系统的工作台数及其压缩机的工作频率大小进行自动控制,完成第1露点温度的调节;中央控制子系统通过布置在调温调湿段中的第2露点温度传感器和第2露点温度传感器信号线获得第2露点温度,中央控制器通过对多级复合式冷冻除湿制冷循环压缩机的工作频率大小进行自动控制完成第2露点温度的调节;中央控制子系统由冷冻除湿制冷循环的回气温度传感器获得各冷冻除湿制冷循环压缩机的回气温度,由冷冻除湿制冷循环压缩机的回气温度、工作时间来判断每个冷冻除湿制冷循环用蒸发器的结霜与结冰情况,当其中一个冷冻除湿制冷循环用蒸发器需要进行除霜化冰时,首先启动处于待机工作状态的一个冷冻除湿制冷循环,接着关闭需要进行除霜化冰的冷冻除湿制冷循环用蒸发器后调节风阀,再打开该冷冻除湿制冷循环化霜电磁阀,同时关闭该冷冻除湿制冷循环循环的冷冻除湿制冷循环排气母管电磁阀,使冷冻除湿制冷循环压缩机的排气进入冷冻除湿制冷循环用蒸发器除霜化冰,在除霜化冰过程中,冷冻除湿制冷循环压缩机的回气温度逐步提高,当回气温度升高到4℃时,除霜化冰结束,中央控制子系统关闭该冷冻除湿制冷循环压缩机,让完成除霜化冰的冷冻除湿制冷循环用蒸发器有十分钟以上的壁面干燥过程,随后该冷冻除湿制冷循环便进入待机工作状态;中央控制器按照同一时间最多只能有一个冷冻除湿制冷循环进行除霜过程的原则,科学安排不同冷冻除湿制冷循环的除霜化冰过程;中央控制子系统由布置在调温调湿段中的出风流量传感器获得供风量,中央控制器通过对风机工作频率的调节,保证供风量指标不受结霜过程的影响。The working principle of the central control subsystem of the present invention is as follows: the air supply temperature is obtained by the air outlet temperature and humidity sensor arranged in the temperature and humidity adjustment section, and the central controller controls the outdoor condenser fan in the heat pump circulation subsystem (see The speed control of the patent ZL201210290885.4) is used to change the heat discharged to the outside, and realize the adjustment of the outlet air temperature of the temperature and humidity adjustment section. If the fan speed of the outdoor condenser is adjusted to the limit and still cannot meet the adjustment requirements of the air supply temperature, further automatic adjustment will be made. The operating frequency of the compressor in the heat pump cycle subsystem with heat rejection completes the adjustment of the air supply temperature. The specific process is disclosed in ZL201210290885.4; 1 Dew point temperature sensor signal line obtains the first dew point temperature, and the central controller completes the adjustment of the first dew point temperature by automatically controlling the number of working units of the parallel compound compression refrigeration subsystem and the operating frequency of the compressor; The system obtains the second dew point temperature through the second dew point temperature sensor and the signal line of the second dew point temperature sensor arranged in the temperature and humidity adjustment section. Automatic control completes the adjustment of the second dew point temperature; the central control subsystem obtains the return air temperature of each refrigeration cycle compressor from the return air temperature sensor of the refrigeration, dehumidification and refrigeration cycle, and obtains the return air temperature and working temperature of the refrigeration, dehumidification and refrigeration cycle compressors Time is used to judge the frosting and icing conditions of each evaporator for freezing, dehumidification and refrigeration cycle. When one of the evaporators for freezing, dehumidification and refrigeration cycle needs to defrost and defrost, first start a freezing, dehumidification and refrigeration cycle in standby working state , then close the evaporator for the freezing, dehumidification and refrigeration cycle that needs defrosting and defrosting, and then adjust the air valve, then open the defrosting electromagnetic valve of the refrigeration, dehumidification and refrigeration cycle, and at the same time close the exhaust bus of the refrigeration, dehumidification and refrigeration cycle of the refrigeration, dehumidification and refrigeration cycle Tube electromagnetic valve, so that the exhaust gas of the refrigeration cycle compressor enters the evaporator of the refrigeration cycle for defrosting and deicing. When the air temperature rises to 4°C, the defrosting and icing ends, and the central control subsystem shuts down the compressor of the refrigerating, dehumidifying and refrigerating cycle, so that the evaporator of the refrigerating, dehumidifying and refrigerating cycle that has completed defrosting and thawing has a wall drying process of more than ten minutes. , and then the freezing, dehumidifying and refrigerating cycle enters the standby working state; the central controller scientifically arranges the defrosting and deicing processes of different freezing, dehumidifying and refrigerating cycles according to the principle that only one freezing, dehumidifying and refrigerating cycle can carry out the defrosting process at the same time; The control subsystem obtains the air supply volume from the air flow sensor arranged in the temperature and humidity adjustment section, and the central controller ensures that the air supply volume index is not affected by the frosting process by adjusting the working frequency of the fan.

本发明既能形成高效节能、深度除湿的调温调湿空气调节系统,也能形成高效节能、深度除湿的对流干燥空气动力源系统,两者仅是控制的温湿度(包括供风温湿度、各功能段处理后的温湿度)范围不同,所采用的各类子系统的数量与容量大小不同而已。The present invention can not only form a high-efficiency energy-saving, deep dehumidification temperature-adjusting and humidity-regulating air conditioning system, but also form a high-efficiency energy-saving, deep dehumidification convective dry air power source system, both of which are only controlled temperature and humidity (including supply air temperature and humidity, The range of temperature and humidity after each functional section is different, and the number and capacity of the various subsystems used are different.

本发明中的两相流冷量回收利用子系统用冷凝器组也可安装在多级复合式冷冻除湿制冷循环子系统的冷凝器组前,这样能够让两相流冷量回收利用子系统的工作温差增大,工作能效提高;但此时冷冻除湿制冷循环子系统的工作能效会由于工作温度范围的变大而有所下降。The condenser group for the two-phase flow cooling capacity recovery and utilization subsystem in the present invention can also be installed before the condenser group of the multi-stage compound refrigeration dehumidification refrigeration cycle subsystem, so that the two-phase flow cooling capacity recovery utilization subsystem can The working temperature difference increases, and the working energy efficiency increases; but at this time, the working energy efficiency of the refrigeration, dehumidification and refrigeration cycle subsystem will decrease due to the increase of the working temperature range.

本发明与现有技术相比,具有以下优点:一是冷冻深度除湿空气处理装置及方法的能耗仅为现有转笼除湿方法的25%-40%,而其机器露点温度最低也能够长期稳定地控制在-25℃,大幅度节约了能源,降低了低湿空气处理过程的运行成本;二是被处理空气的机器露点温度由14℃以上降低到最低为-25℃,实现了深度除湿;三是利用热泵节能技术,既实现了高效冷冻除湿过程,又实现了高效加热过程,节省了加热过程能耗;四是采用内外复合式两相流热管冷量回收利用子系统,有效回收利用了达到机器露点的空气中的冷能,大幅度降低了能耗;五是通过内外复合式无排热热泵循环子系统与内外复合式带排热热泵循环子系统的有机组合,能够有效利用冷凝器中排出的热量来加热低温低湿空气,既省去了加热过程能耗,还提高了制冷效率;六是通过特殊布置的多级复合式冷冻除湿制冷循环子系统,实现了更深程度的去湿过程,使机器露点温度由原来的4℃降低到最低为-25℃,能够满足更多生产工艺的要求;其结构简单,操作方便,成本低,能耗少,能源利用率高,制冷除湿效率高,环境友好。Compared with the prior art, the present invention has the following advantages: First, the energy consumption of the freezing depth dehumidification air treatment device and method is only 25%-40% of the existing dehumidification method of the cage, and the dew point temperature of the machine is the lowest and can last for a long time Stable control at -25°C greatly saves energy and reduces the operating cost of the low-humidity air treatment process; second, the machine dew point temperature of the treated air is reduced from above 14°C to a minimum of -25°C, realizing deep dehumidification; The third is to use the heat pump energy-saving technology, which not only realizes the high-efficiency freezing and dehumidification process, but also realizes the high-efficiency heating process, which saves energy consumption in the heating process; the fourth is to adopt the internal and external composite two-phase flow heat pipe cooling capacity recycling subsystem, which effectively recycles and utilizes The cold energy in the air that reaches the dew point of the machine greatly reduces energy consumption; fifthly, through the organic combination of the internal and external composite heat pump circulation subsystem without heat dissipation and the internal and external composite heat pump circulation subsystem with heat dissipation, the condenser can be effectively used The heat discharged from the air is used to heat the low-temperature and low-humidity air, which not only saves the energy consumption of the heating process, but also improves the cooling efficiency; the sixth is to realize a deeper dehumidification process through the specially arranged multi-stage composite refrigeration dehumidification refrigeration cycle subsystem , so that the dew point temperature of the machine is reduced from the original 4°C to the minimum of -25°C, which can meet the requirements of more production processes; it has simple structure, convenient operation, low cost, low energy consumption, high energy utilization rate, and high refrigeration and dehumidification efficiency , Environmentally friendly.

附图说明:Description of drawings:

图1为本发明所述节能型冷冻深度除湿空气处理装置的主体结构原理示意图。Fig. 1 is a schematic diagram of the main structure of the energy-saving refrigerated deep dehumidification air treatment device of the present invention.

具体实施方式:detailed description:

下面通过实施例并结合附图作进一步说明。Further description will be given below through the embodiments and in conjunction with the accompanying drawings.

实施例:Example:

本实施例所述节能型冷冻深度除湿空气处理装置的主体结构包括内外复合式气液两相流热管冷量回收、预制冷用换热器、内外复合式热泵循环、多级复合式冷冻除湿制冷循环和中央控制五个子系统,内外复合式气液两相流热管冷量回收子系统包括热管冷量回收用蒸发器组16和热管冷量回收用冷凝器组24,热管冷量回收用蒸发器组16的两端分别与调温调湿段15和预制冷用换热器组17连通,调温调湿段15的前端与空气预处理段14连通;预制冷用换热器子系统包括预制冷用换热器组17、预制冷用换热器内外连接管32和预制冷用换热器的室外机组33;预制冷用换热器组17的上端通过预制冷用换热器内外连接管32与预制冷用换热器的室外机组33的连通;内外复合式热泵循环子系统包括热泵循环用蒸发器组18和热泵循环用冷凝器组25;热泵循环用蒸发器组18的前端与预制冷用换热器组17连通,后端设有前挡水板19,前挡水板后端设有第1露点温度传感器28,第1露点温度传感器28通过第1露点温度传感器信号线36与中央控制器44电信息连接;多级复合式冷冻除湿制冷循环子系统由2-10个冷冻除湿制冷循环按照串、并联复合的结构形式布置构成,2-10个冷冻除湿制冷循环的结构与大小完全相同,按气流流动方向,2-10个冷冻除湿制冷循环蒸发器20采用并联方式布置,2-10个冷冻除湿制冷循环冷凝器23采用串联方式布置,每个冷冻除湿制冷循环均包括冷冻除湿制冷循环蒸发器供液管1、冷冻除湿制冷循环化霜电磁阀2、冷冻除湿制冷循环节流阀3、冷冻除湿制冷循环化霜蒸汽管4、冷冻除湿制冷循环干燥过滤器5、冷冻除湿制冷循环储液罐6、回液管7、冷冻除湿制冷循环回气温度传感器8、冷冻除湿制冷循环蒸发器用接水盘9、冷冻除湿制冷循环回气管10、冷冻除湿制冷循环压缩机11、冷冻除湿制冷循环排气母管电磁阀12、冷冻除湿制冷循环排气母管13、冷冻除湿制冷循环用蒸发器20和冷冻除湿制冷循环用冷凝器23,冷冻除湿制冷循环用蒸发器20的后侧设有冷冻除湿制冷循环冷凝器后调节风阀21,冷冻除湿制冷循环用蒸发器20的下端设 有冷冻除湿制冷循环蒸发器用接水盘9,冷冻除湿制冷循环用蒸发器20分别通过冷冻除湿制冷循环蒸发器供液管1、冷冻除湿制冷循环化霜蒸汽管4、回液管7、冷冻除湿制冷循环回气管10和冷冻除湿制冷循环排气母管13与冷冻除湿制冷循环用冷凝器23管道联通,冷冻除湿制冷循环压缩机11通过冷冻除湿制冷循环回气管10从冷冻除湿制冷循环用蒸发器20中吸入低压蒸汽,冷冻除湿制冷循环压缩机11的排气送入冷冻除湿制冷循环化霜蒸汽管4和冷冻除湿制冷循环排气母管13,冷冻除湿制冷循环蒸发器供液管1和回液管7串接联通,冷冻除湿制冷循环蒸发器供液管1和回液管7之间从前向后依次设有冷冻除湿制冷循环节流阀3、冷冻除湿制冷循环干燥过滤器5和冷冻除湿制冷循环储液罐6,冷冻除湿制冷循环化霜蒸汽管4上设有冷冻除湿制冷循环化霜电磁阀2,冷冻除湿制冷循环回气管10和冷冻除湿制冷循环排气母管13之间的管路上依次设有冷冻除湿制冷循环回气温度传感器8、冷冻除湿制冷循环压缩机11和冷冻除湿制冷循环排气母管电磁阀12;第一个冷冻除湿制冷循环用冷凝器23的前端设有后挡水板22,后挡水板22和第一个冷冻除湿制冷循环用冷凝器23之间设有第2露点温度传感器29;最后一个冷冻除湿制冷循环用冷凝器23的后侧依次设有热管冷量回收用冷凝器组24、热泵循环用冷凝器组25、风机26和空气后处理段27,空气后处理段27内设置有出风口温湿度传感器30和出风口风速风量传感器31;中央控制子系统包括中央控制器44、冷冻除湿制冷循环化霜电磁阀控制线34、冷冻除湿制冷循环回气温度传感器信号线35、第1露点温度传感器信号线36、冷冻除湿制冷循环蒸发器后调节风阀控制线37、冷冻除湿制冷循环压缩机控制线38、冷冻除湿制冷循环排气母管电磁阀控制线39、第2露点温度传感器信号线40、风机风量调节控制线41、出风口温湿度传感器信号线42和出风口风速风量传感器信号线43,冻除湿制冷循环化霜电磁阀2、冷冻除湿制冷循环回气温度传感器8、第1露点温度传感器28、冷冻除湿制冷循环蒸发器后调节风阀21、冷冻除湿制冷循环压缩机11、冷冻除湿制冷循环排气母管电磁阀12、 第2露点温度传感器29、风机26、出风口温湿度传感器30和出风口风速风量传感器31分别通过冷冻除湿制冷循环化霜电磁阀控制线34、冷冻除湿制冷循环回气温度传感器信号线35、第1露点温度传感器信号线36、冷冻除湿制冷循环蒸发器后调节风阀控制线37、冷冻除湿制冷循环压缩机控制线38、冷冻除湿制冷循环排气母管电磁阀控制线39、第2露点温度传感器信号线40、风机风量调节控制线41、出风口温湿度传感器信号线42和出风口风速风量传感器信号线43与中央控制器44电信息连接。The main structure of the energy-saving refrigerated deep dehumidification air treatment device described in this embodiment includes internal and external composite gas-liquid two-phase flow heat pipe cooling capacity recovery, pre-refrigeration heat exchanger, internal and external composite heat pump cycle, multi-stage composite refrigeration dehumidification refrigeration Circulation and central control five subsystems, internal and external composite gas-liquid two-phase flow heat pipe cooling capacity recovery subsystem includes heat pipe cooling capacity recovery evaporator group 16, heat pipe cooling capacity recovery condenser group 24, heat pipe cooling capacity recovery evaporator The two ends of the group 16 are connected with the temperature and humidity regulation section 15 and the heat exchanger group 17 for pre-cooling respectively, and the front end of the temperature and humidity regulation section 15 is connected with the air pretreatment section 14; the heat exchanger subsystem for pre-cooling includes pre-cooling Cooling heat exchanger group 17, pre-cooling heat exchanger internal and external connecting pipe 32 and pre-cooling heat exchanger outdoor unit 33; the upper end of pre-cooling heat exchanger group 17 passes through the pre-cooling heat exchanger internal and external connecting pipe 32 is connected with the outdoor unit 33 of the heat exchanger for pre-cooling; the internal and external composite heat pump cycle subsystem includes the evaporator group 18 for the heat pump cycle and the condenser group 25 for the heat pump cycle; the front end of the evaporator group 18 for the heat pump cycle is connected to the pre- The cooling heat exchanger group 17 is connected, the rear end is provided with a front water baffle 19, and the rear end of the front water baffle is provided with a first dew point temperature sensor 28, and the first dew point temperature sensor 28 communicates with the first dew point temperature sensor signal line 36. The central controller 44 is connected to the electrical information; the multi-stage composite refrigeration, dehumidification and refrigeration cycle subsystem is composed of 2-10 refrigeration, dehumidification and refrigeration cycles arranged in series and parallel composite structures, and the structure and size of the 2-10 refrigeration, dehumidification and refrigeration cycles It is exactly the same, according to the air flow direction, 2-10 refrigerating and dehumidifying refrigerating cycle evaporators 20 are arranged in parallel, and 2-10 refrigerating and dehumidifying refrigerating cycle condensers 23 are arranged in series, and each refrigerating, dehumidifying and refrigerating cycle includes refrigerating and dehumidifying Refrigeration cycle evaporator liquid supply pipe 1, refrigeration dehumidification refrigeration cycle defrost solenoid valve 2, refrigeration dehumidification refrigeration cycle throttle valve 3, refrigeration dehumidification refrigeration cycle defrost steam pipe 4, refrigeration dehumidification refrigeration cycle drying filter 5, refrigeration dehumidification refrigeration Circulating liquid storage tank 6, liquid return pipe 7, refrigerating and dehumidifying refrigerating cycle return air temperature sensor 8, refrigerating and dehumidifying refrigerating cycle evaporator water tray 9, refrigerating and dehumidifying refrigerating cycle return air pipe 10, refrigerating and dehumidifying refrigerating cycle compressor 11, refrigerating and dehumidifying Refrigeration cycle exhaust main pipe electromagnetic valve 12, refrigeration dehumidification refrigeration cycle exhaust main pipe 13, refrigeration dehumidification refrigeration cycle evaporator 20 and refrigeration dehumidification refrigeration cycle condenser 23, the rear side of refrigeration dehumidification refrigeration cycle evaporator 20 is provided The air valve 21 is adjusted behind the condenser of the freezing, dehumidifying and refrigerating cycle, the lower end of the evaporator 20 for the refrigerating, dehumidifying and refrigerating cycle is provided with a water receiving tray 9 for the evaporator of the refrigerating, dehumidifying and refrigerating cycle, and the evaporator 20 for the refrigerating, dehumidifying and refrigerating cycle passes through Evaporator liquid supply pipe 1, freezing, dehumidification and refrigeration cycle defrost steam pipe 4, liquid return pipe 7, refrigeration, dehumidification and refrigeration cycle return pipe 10, refrigeration, dehumidification and refrigeration cycle exhaust main pipe 13, and condenser 23 for freezing, dehumidification and refrigeration cycle. , the refrigerating and dehumidifying refrigerating cycle compressor 11 passes through the refrigerating and dehumidifying refrigerating cycle The loop-back air pipe 10 draws low-pressure steam from the evaporator 20 for the refrigeration, dehumidification and refrigeration cycle, and the exhaust gas from the compressor 11 of the refrigeration, dehumidification and refrigeration cycle is sent to the defrosting steam pipe 4 and the exhaust main pipe 13 of the refrigeration, dehumidification and refrigeration cycle. The liquid supply pipe 1 and the liquid return pipe 7 of the refrigerating and dehumidifying refrigerating cycle evaporator are connected in series, and the refrigerating, dehumidifying and refrigerating cycle evaporator is provided with a throttle valve 3 for the refrigerating, dehumidifying and refrigerating cycle from front to back between the liquid supply pipe 1 and the liquid returning pipe 7 , freeze dehumidification refrigeration cycle drying filter 5 and refrigeration dehumidification refrigeration cycle liquid storage tank 6, freeze dehumidification refrigeration cycle defrost steam pipe 4 is provided with refrigeration dehumidification refrigeration cycle defrost solenoid valve 2, freeze dehumidification refrigeration cycle return air pipe 10 and freezer The pipeline between the dehumidification and refrigeration cycle exhaust main pipes 13 is successively provided with a refrigeration dehumidification refrigeration cycle return air temperature sensor 8, a refrigeration dehumidification refrigeration cycle compressor 11 and a refrigeration dehumidification refrigeration cycle exhaust main pipe solenoid valve 12; The front end of the condenser 23 for the dehumidification and refrigeration cycle is provided with a rear fender 22, and a second dew point temperature sensor 29 is arranged between the rear fender 22 and the first condenser 23 for the refrigeration, dehumidification and refrigeration cycle; The rear side of the condenser 23 for circulation is provided with a condenser group 24 for heat pipe cooling recovery, a condenser group 25 for heat pump circulation, a blower fan 26 and an air post-processing section 27 in sequence, and the air post-processing section 27 is provided with an air outlet temperature and humidity Sensor 30 and wind speed and air volume sensor 31 at the air outlet; the central control subsystem includes a central controller 44, a control line 34 for the defrosting solenoid valve of the refrigeration, dehumidification and refrigeration cycle, a signal line 35 for the return air temperature sensor of the refrigeration, dehumidification and refrigeration cycle, and a signal from the first dew point temperature sensor. Line 36, refrigerating, dehumidifying and refrigerating cycle evaporator rear regulating air valve control line 37, refrigerating, dehumidifying and refrigerating cycle compressor control line 38, refrigerating, dehumidifying and refrigerating cycle exhaust master solenoid valve control line 39, second dew point temperature sensor signal line 40, Fan air volume adjustment control line 41, air outlet temperature and humidity sensor signal line 42 and air outlet air volume sensor signal line 43, freezing and dehumidification refrigeration cycle defrost solenoid valve 2, refrigeration dehumidification refrigeration cycle return air temperature sensor 8, first dew point temperature sensor 28. Regulating air valve 21 after evaporator of refrigeration, dehumidification and refrigeration cycle, compressor of refrigeration, dehumidification and refrigeration cycle 11, solenoid valve of exhaust main pipe of refrigeration, dehumidification and refrigeration cycle 12, second dew point temperature sensor 29, fan 26, air outlet temperature and humidity sensor 30 and the wind speed and air volume sensor 31 at the air outlet respectively through the control line 34 of the defrosting solenoid valve of the freezing and dehumidification refrigeration cycle, the signal line 35 of the return air temperature sensor of the refrigeration and dehumidification refrigeration cycle, the signal line 36 of the first dew point temperature sensor, and the post-adjustment of the evaporator of the refrigeration, dehumidification and refrigeration cycle. Air valve control line 37, refrigeration dehumidification refrigeration cycle compressor control line 38, refrigeration dehumidification refrigeration cycle exhaust main solenoid valve control line 39, second dew point temperature sensor signal line 40, fan air volume adjustment control line 41, air outlet temperature and humidity The sensor signal line 42 and the air outlet wind speed and air volume sensor signal line 43 are electrically connected to the central controller 44 .

本实施例实现节能型冷冻深度除湿空气处理的具体过程是:在风机26的作用下,待处理的空气从空气预处理段14中流出并进入调温调湿段15,在调温调湿段15内,被处理的空气先被内外复合式两相流热管冷量回收利用子系统中的热管冷量回收用蒸发器组16冷却降温,然后再被预制冷用换热器子系统的预制冷用换热器组17进一步冷却,接着被内外复合式热泵循环子系统的热泵循环用蒸发器组18进一步冷却,此时,空气温度不低于4℃,达到第1露点温度;达到第1露点温度的空气经前挡水板19去除液态水滴后,再经过多级复合式冷冻除湿制冷循环子系统的2-10个冷冻除湿制冷循环用蒸发器20进行深度冷却,被处理的空气最终达到第2露点温度,最低可达-25℃,随后,空气经后挡水板22去除空气中夹带的液态水滴后依次流经多级复合式冷冻除湿制冷循环子系统的2-10个冷冻除湿制冷循环用冷凝器23进行加热,空气温度从第2露点温度加热到4-12℃后,空气进入两相流冷量回收利用冷凝器组24被进一步加热到12-20℃,最后进入热泵循环子系统的热泵循环用冷凝器组25进一步加热,空气达到设定的供风温度后进入空气后处理段27,完成空气的调温调湿处理过程;其中,中央控制子系统通过调节预制冷用换热器子系统与热泵循环子系统的制冷能力控制第1露点温度,达到降温和初步除湿的目标;中央控制子系统通过调节多级复合式冷冻除湿制冷循环子系统的制冷能力控制第2露点温度,达到深度除湿和准确控制相对湿度的目标;再通过调节热泵循环子系统中对外排热量的大小及无排热 热泵循环子系统的工作台数控制出风温度,达到调温的目标。The specific process of this embodiment to realize the energy-saving deep-frozen dehumidification air treatment is: under the action of the fan 26, the air to be treated flows out from the air pretreatment section 14 and enters the temperature and humidity adjustment section 15, and in the temperature and humidity adjustment section In 15, the treated air is first cooled and lowered by the evaporator group 16 for heat pipe cooling recovery in the internal and external composite two-phase flow heat pipe cooling capacity recovery subsystem, and then by the pre-cooling unit of the pre-cooling heat exchanger subsystem. Use the heat exchanger group 17 for further cooling, and then be further cooled by the heat pump cycle evaporator group 18 of the internal and external composite heat pump cycle subsystem. At this time, the air temperature is not lower than 4°C, reaching the first dew point temperature; The air at high temperature passes through the front water baffle 19 to remove liquid water droplets, and then goes through 2-10 refrigerating, dehumidifying and refrigerating cycles of the multi-stage composite refrigerating, dehumidifying and refrigerating cycle subsystem for deep cooling with the evaporator 20, and the treated air finally reaches the first 2 Dew point temperature, the lowest can reach -25°C, and then the air passes through the rear fender 22 to remove the liquid water droplets entrained in the air, and then flows through 2-10 refrigeration, dehumidification and refrigeration cycles of the multi-stage composite refrigeration, dehumidification and refrigeration cycle subsystem The condenser 23 is used for heating. After the air temperature is heated from the second dew point temperature to 4-12°C, the air enters the two-phase flow cooling capacity recycling condenser group 24 and is further heated to 12-20°C, and finally enters the heat pump circulation subsystem The heat pump cycle is further heated by the condenser group 25. After the air reaches the set air supply temperature, it enters the air post-treatment section 27 to complete the air temperature and humidity adjustment process; wherein, the central control subsystem adjusts the pre-cooling heat exchange The refrigeration capacity of the heat pump subsystem and the heat pump circulation subsystem controls the first dew point temperature to achieve the goal of cooling and preliminary dehumidification; the central control subsystem controls the second dew point temperature by adjusting the refrigeration capacity of the multi-stage composite refrigeration dehumidification refrigeration circulation subsystem, Achieve the goal of deep dehumidification and accurate control of relative humidity; and then control the outlet air temperature by adjusting the amount of heat exhausted in the heat pump circulation subsystem and the number of working units of the heat pump circulation subsystem without heat dissipation, so as to achieve the goal of temperature adjustment.

本实施例所述内外复合式两相流热管冷量回收利用子系统与发明专利ZL201210290885.4公开的一种节能式调温调湿空气处理方法相同。The internal and external composite two-phase flow heat pipe cooling capacity recycling subsystem described in this embodiment is the same as the energy-saving air treatment method for temperature and humidity regulation disclosed in the invention patent ZL201210290885.4.

本实施例所述预制冷用换热器子系统为与发明专利ZL201210290885.4公开的一种节能式调温调湿空气处理方法中相同的并联复合式压缩制冷子系统,或是由通用冷水机组的表冷器构成的换热器子系统,预制冷用换热器子在夏季最炎热的工况下,能高效地排出空调循环系统中多余的热量。The heat exchanger subsystem for pre-refrigeration described in this embodiment is the same parallel compound compression refrigeration subsystem as that disclosed in the invention patent ZL201210290885. The heat exchanger subsystem composed of the surface cooler, the pre-cooling heat exchanger can efficiently discharge the excess heat in the air conditioning circulation system under the hottest working conditions in summer.

本实施例所述热泵循环子系统与发明专利ZL201210290885.4公开的一种节能式调温调湿空气处理方法中热泵循环子系统类同,包括内外复合式带排热热泵循环和内外复合式不带排热热泵循环两类循环,热泵循环子系统的蒸发器的冷量用于进一步冷却预冷后的空气,使其达到第1露点温度,实现高效降温除湿,其冷凝器的排热,一部分用于加热达到第2露点温度后的低温、低湿空气,使调温调湿段出风温度达到设定要求,另一部分多余的热量,通过室外冷凝器排放到外部环境中,实现调温调湿段能量的平衡控制。The heat pump circulation subsystem described in this embodiment is similar to the heat pump circulation subsystem in an energy-saving temperature and humidity regulation air treatment method disclosed in the invention patent ZL201210290885. There are two types of heat pump cycle with heat removal. The cooling capacity of the evaporator of the heat pump cycle subsystem is used to further cool the pre-cooled air to reach the first dew point temperature to achieve efficient cooling and dehumidification. The heat removal of the condenser is partly It is used to heat the low-temperature and low-humidity air after reaching the second dew point temperature, so that the temperature of the air outlet in the temperature and humidity control section reaches the set requirements, and the other part of the excess heat is discharged to the external environment through the outdoor condenser to realize temperature and humidity control Segment energy balance control.

本实施例所述多级复合式冷冻除湿制冷循环子系统的工作原理为:冷冻除湿制冷循环用蒸发器对达到第1机器露点温度的空气进一步实现深度冷却除湿,使被处理的空气最终达到很低的第2机器露点温度(最低可达-25℃),而冷冻除湿制冷循环用冷凝器23的排热,用于加热达到第2露点温度后的低温、低湿空气,实现冷、热能量的同时高效利用;采用多级复合的目的是通过轮流工作方式,保证在其中一级冷冻除湿制冷循环中进行化霜去冰处理时,其余冷冻除湿制冷循环仍能保证满足深度冷却去湿的要求。The working principle of the multi-stage composite freezing, dehumidification and refrigeration cycle subsystem described in this embodiment is: the evaporator in the refrigeration, dehumidification and refrigeration cycle further realizes deep cooling and dehumidification of the air reaching the dew point temperature of the first machine, so that the processed air finally reaches a very high temperature. Low second machine dew point temperature (the lowest can reach -25°C), and the heat exhausted by the condenser 23 used in the freezing and dehumidification refrigeration cycle is used to heat the low-temperature and low-humidity air after reaching the second dew point temperature, so as to realize the exchange of cold and heat energy At the same time, it is used efficiently; the purpose of adopting multi-stage compounding is to ensure that when the defrosting and deicing treatment is performed in one of the first-stage refrigeration and dehumidification refrigeration cycles, the remaining refrigeration, dehumidification and refrigeration cycles can still meet the requirements of deep cooling and dehumidification.

本实施例所述中央控制子系统的工作原理为:由布置在调温调湿段15中的出风温湿度传感器30获得送风温度,中央控制器44通过对热泵循环子系统中室外冷凝器风机(详见专利ZL201210290885.4)的转速控制来改变对外排热量,实现对调温调湿段16出风温度的调 节,若室外冷凝器的风机转速调到极限仍不能满足送风温度的调节要求,则进一步自动调节带排热热泵循环子系统中压缩机的工作频率,完成送风温度的调节,具体过程如ZL201210290885.4公开;中央控制子系统通过布置在调温调湿段15中的第1露点温度传感器28和第1露点温度传感器信号线36获得第1露点温度,中央控制器44通过对并联复合式压缩制冷子系统的工作台数及其压缩机的工作频率大小进行自动控制,完成第1露点温度的调节;中央控制子系统通过布置在调温调湿段15中的第2露点温度传感器29和第2露点温度传感器信号线40获得第2露点温度,中央控制器44通过对多级复合式冷冻除湿制冷循环压缩机11的工作频率大小进行自动控制完成第2露点温度的调节;中央控制子系统由冷冻除湿制冷循环的回气温度传感器8获得各冷冻除湿制冷循环压缩机11的回气温度,由冷冻除湿制冷循环压缩机11的回气温度、工作时间等指标来判断每个冷冻除湿制冷循环用蒸发器20的结霜与结冰情况,当某个冷冻除湿制冷循环用蒸发器20需要进行除霜化冰时,首先启动处于待机工作状态的一个冷冻除湿制冷循环,接着关闭需要进行除霜化冰的冷冻除湿制冷循环用蒸发器后调节风阀21,再打开该冷冻除湿制冷循环化霜电磁阀2,同时关闭该冷冻除湿制冷循环循环的冷冻除湿制冷循环排气母管电磁阀12,使冷冻除湿制冷循环压缩机11的排气进入冷冻除湿制冷循环用蒸发器20除霜化冰,在除霜化冰过程中,冷冻除湿制冷循环压缩机11的回气温度逐步提高,当回气温度升高到4℃时,除霜化冰结束,中央控制子系统关闭该冷冻除湿制冷循环压缩机11,让完成除霜化冰的冷冻除湿制冷循环用蒸发器20有十分钟以上的壁面干燥过程,随后该冷冻除湿制冷循环便进入待机工作状态;中央控制器44按照同一时间最多只能有一个冷冻除湿制冷循环进行除霜过程的原则,科学安排不同冷冻除湿制冷循环的除霜化冰过程;中央控制子系统由布置在调温调湿段中的出风流量传感器31获得供风量,中央控制器44通过对风机26工作频率的调节,保证供风量指标不受结霜过程的影响。The working principle of the central control subsystem described in this embodiment is as follows: the air supply temperature is obtained by the air outlet temperature and humidity sensor 30 arranged in the temperature and humidity adjustment section 15, and the central controller 44 controls the temperature of the outdoor condenser in the heat pump circulation subsystem. The speed control of the fan (see patent ZL201210290885.4 for details) is used to change the heat discharged to the outside to realize the adjustment of the outlet air temperature of the temperature and humidity adjustment section 16. If the fan speed of the outdoor condenser is adjusted to the limit, it still cannot meet the adjustment requirements of the air supply temperature , then further automatically adjust the operating frequency of the compressor in the heat pump cycle subsystem with heat removal to complete the adjustment of the air supply temperature. The specific process is disclosed in ZL201210290885.4; 1 Dew point temperature sensor 28 and the first dew point temperature sensor signal line 36 obtain the first dew point temperature, and the central controller 44 automatically controls the number of working units of the parallel compound compression refrigeration subsystem and the operating frequency of the compressor to complete the first dew point temperature. 1. Adjustment of dew point temperature; the central control subsystem obtains the second dew point temperature through the second dew point temperature sensor 29 and the second dew point temperature sensor signal line 40 arranged in the temperature and humidity adjustment section 15, and the central controller 44 controls the multi-level The operating frequency of the compound refrigeration dehumidification refrigeration cycle compressor 11 is automatically controlled to complete the adjustment of the second dew point temperature; the central control subsystem obtains the return air temperature sensor 8 of each refrigeration dehumidification refrigeration cycle compressor 11. Air temperature, the frosting and freezing conditions of each evaporator 20 for freezing, dehumidification and refrigeration cycle are judged by indicators such as the return air temperature and working time of the compressor 11 of the refrigeration, dehumidification and refrigeration cycle. 20. When it is necessary to defrost and defrost, first start a freezing, dehumidifying and refrigerating cycle in the standby working state, then close the evaporator for the freezing, dehumidifying and refrigerating cycle that needs to be defrosted and defrosted, and then adjust the air valve 21, and then open the refrigerating, dehumidifying and refrigerating cycle. Cycle defrost solenoid valve 2, and close the refrigeration, dehumidification and refrigeration cycle exhaust main pipe solenoid valve 12 of the refrigeration, dehumidification and refrigeration cycle at the same time, so that the exhaust gas of the refrigeration, dehumidification and refrigeration cycle compressor 11 enters the evaporator 20 for freezing, dehumidification and refrigeration cycle for defrosting Deicing, in the process of defrosting and deicing, the return air temperature of the refrigeration cycle compressor 11 for freezing and dehumidification is gradually increased. The refrigerating cycle compressor 11 allows the evaporator 20 of the refrigerating, dehumidifying and refrigerating cycle having completed defrosting and deicing to have a wall surface drying process of more than ten minutes, and then the refrigerating, dehumidifying and refrigerating cycle enters a standby working state; The principle that there can only be one freezing, dehumidifying and refrigerating cycle for the defrosting process scientifically arranges the defrosting and deicing processes of different refrigerating, dehumidifying and refrigerating cycles; Air volume, the central controller 44 ensures that the air supply volume index is not affected by the frosting process by adjusting the operating frequency of the fan 26 .

Claims (1)

1. a kind of energy-saving freezing depth dehumidified air processing method, it is characterised in that at energy-saving freezing depth dehumidified air Realized in reason device, its detailed process is:In the presence of blower fan, pending air flows out from air pretreatment section goes forward side by side Enter conditioning section, in conditioning section, processed air is first recycled by inside and outside combined type two phase flow heat pipe cold Heat pipe cold recovery in subsystem is cooled with evaporator group, is then prefabricated the pre- refrigeration of colod-application heat exchanger subsystem again Further cooled down with heat exchanger group, it is then further with evaporator group by the heat pump cycle of inside and outside combined heat pump cycle subsystem Cooling, now, air themperature are not less than 4 DEG C, reach the 1st dew-point temperature;The premenstrual water fender of air for reaching the 1st dew-point temperature is gone Used after liquid water droplets, then by 2-10 freeze drying kind of refrigeration cycle of multistage combined freeze drying kind of refrigeration cycle subsystem Evaporator carries out depth cooling, and processed air is finally reached the 2nd dew-point temperature, and minimum to reach -25 DEG C, then, air is after The 2- of multistage combined freeze drying kind of refrigeration cycle subsystem is flowed through after the liquid water droplets carried secretly in water fender removal air successively 10 freeze drying kind of refrigeration cycle are heated with condenser, and air themperature is after the 2nd dew-point temperature is heated to 4-12 DEG C, air 12-20 DEG C is further heated to using condenser group into two phase flow cold recovery, finally enters heat pump cycle subsystem Heat pump cycle is further heated with condenser group, and air reaches air inlet post processing section after the ventilation temperature of setting, completes empty The conditioning processing procedure of gas;Wherein, central control subsystem is followed by adjusting pre- heat exchanger for refrigerating subsystem with heat pump The refrigerating capacity of loop subsystems controls the 1st dew-point temperature, reaches cooling and the target tentatively to dehumidify;Central control subsystem passes through Adjust multistage combined freeze drying kind of refrigeration cycle subsystem refrigerating capacity control the 2nd dew-point temperature, reach depth dehumidifying and The target of accurate control relative humidity;Again by the size of external heat exhaust in adjusting heat pump cycle subsystem and without heat extraction heat pump Air temperature is made in the workbench numerical control of cycle subsystem, reaches the target of temperature adjustment;At the energy-saving freezing depth dehumidified air Managing the agent structure of device includes inside and outside combined type biphase gas and liquid flow heat pipe cold recovery, pre- heat exchanger for refrigerating, inside and outside compound Five formula heat pump cycle, multistage combined freeze drying kind of refrigeration cycle and center control subsystems, inside and outside combined type gas-liquid two-phase Stream heat pipe cold recovery subsystem includes heat pipe cold recovery evaporator group and heat pipe cold recovery condenser group, heat pipe cold Amount recovery is connected with conditioning section and pre- heat exchanger for refrigerating group respectively with the both ends of evaporator group, the front end of conditioning section Connected with air pretreatment section;Pre- heat exchanger for refrigerating subsystem is including in pre- heat exchanger for refrigerating group, pre- heat exchanger for refrigerating The outdoor unit of outer connecting pipe and pre- heat exchanger for refrigerating;The upper end of pre- heat exchanger for refrigerating group passes through in pre- heat exchanger for refrigerating Outer connecting pipe connects with the outdoor unit of pre- heat exchanger for refrigerating;Inside and outside combined heat pump cycle subsystem is used including heat pump cycle Evaporator group and heat pump cycle condenser group;Heat pump cycle is connected with the front end of evaporator group with pre- heat exchanger for refrigerating group, Rear end is provided with preceding water fender, and preceding water fender rear end is provided with the 1st dew point temperature sensor, and the 1st dew point temperature sensor passes through the 1st dew Point temperature sensor signal line is connected with central controller power information;Multistage combined freeze drying kind of refrigeration cycle subsystem is by 2- 10 freeze drying kind of refrigeration cycle arrange composition, 2-10 freeze drying kind of refrigeration cycle according to the compound structure type of series and parallel Structure it is identical with size, by air current flow direction, 2-10 freeze drying kind of refrigeration cycle evaporator uses parallel way Arrangement, 2-10 freeze drying kind of refrigeration cycle condenser use arranged in series, and each freeze drying kind of refrigeration cycle includes Freeze drying kind of refrigeration cycle evaporator feed pipe, freeze drying kind of refrigeration cycle defrost magnetic valve, the throttling of freeze drying kind of refrigeration cycle Valve, freeze drying kind of refrigeration cycle defrost steam pipe, freeze drying kind of refrigeration cycle device for drying and filtering, freeze drying kind of refrigeration cycle liquid storage Tank, liquid back pipe, freeze drying kind of refrigeration cycle suction temperature sensor, freeze drying kind of refrigeration cycle evaporator drip tray, freezing Desiccant cooling circulation muffler, freeze drying kind of refrigeration cycle compressor, freeze drying kind of refrigeration cycle exhaust main pipe magnetic valve, freezing Desiccant cooling circulating exhaust main pipe, freeze drying kind of refrigeration cycle evaporator and freeze drying kind of refrigeration cycle condenser, freezing The rear side of desiccant cooling circulation evaporator is provided with regulating valve after freeze drying kind of refrigeration cycle condenser, freeze drying kind of refrigeration cycle Freeze drying kind of refrigeration cycle evaporator drip tray is provided with the lower end of evaporator, freeze drying kind of refrigeration cycle is distinguished with evaporator Pass through freeze drying kind of refrigeration cycle evaporator feed pipe, freeze drying kind of refrigeration cycle defrost steam pipe, liquid back pipe, freeze drying system SAPMAC method muffler and freeze drying kind of refrigeration cycle exhaust main pipe and freeze drying kind of refrigeration cycle condenser tubes UNICOM, freezing Desiccant cooling recycle compressor is sucked by freeze drying kind of refrigeration cycle muffler from freeze drying kind of refrigeration cycle with evaporator Freeze drying kind of refrigeration cycle defrost steam pipe and freeze drying are sent into low-pressure steam, the exhaust of freeze drying kind of refrigeration cycle compressor Kind of refrigeration cycle exhaust main pipe, freeze drying kind of refrigeration cycle evaporator feed pipe and liquid back pipe concatenation UNICOM, freeze drying refrigeration are followed Freeze drying kind of refrigeration cycle choke valve, freeze drying refrigeration are sequentially provided between ring evaporator feed pipe and liquid back pipe from front to back Cyclic drying filter and freeze drying kind of refrigeration cycle fluid reservoir, freeze drying kind of refrigeration cycle defrost steam pipe remove provided with freezing Wet kind of refrigeration cycle defrost magnetic valve, the pipe between freeze drying kind of refrigeration cycle muffler and freeze drying kind of refrigeration cycle exhaust main pipe Freeze drying kind of refrigeration cycle suction temperature sensor, freeze drying kind of refrigeration cycle compressor and freeze drying system are sequentially provided with road SAPMAC method exhaust main pipe magnetic valve;The front end of first freeze drying kind of refrigeration cycle condenser is provided with rear water plate, rear water The 2nd dew point temperature sensor is provided between plate and first freeze drying kind of refrigeration cycle condenser;Last freeze drying Kind of refrigeration cycle is with being sequentially provided with heat pipe cold recovery condenser group, heat pump cycle condenser group, blower fan on rear side of condenser Section is post-processed with air, air outlet Temperature Humidity Sensor and air outlet wind speed air flow sensor are provided with air post processing section; Central control subsystem includes central controller, freeze drying kind of refrigeration cycle defrost control line of electromagnetic valve, freeze drying refrigeration and followed Wind is adjusted after ring suction temperature sensor signal lines, the 1st dew point temperature sensor signal wire, freeze drying kind of refrigeration cycle evaporator Valve control line, freeze drying kind of refrigeration cycle compressor control line, freeze drying kind of refrigeration cycle exhaust main pipe control line of electromagnetic valve, 2 dew point temperature sensor signal wires, fan delivery adjustment control line, air outlet Temperature Humidity Sensor signal wire and air outlet wind speed Air flow sensor signal wire, freeze desiccant cooling circulation defrost magnetic valve, freeze drying kind of refrigeration cycle suction temperature sensor, the 1st Adjusting air valve, freeze drying kind of refrigeration cycle compressor, freezing remove after dew point temperature sensor, freeze drying kind of refrigeration cycle evaporator Wet kind of refrigeration cycle exhaust main pipe magnetic valve, the 2nd dew point temperature sensor, blower fan, air outlet Temperature Humidity Sensor and air-out one's intention as revealed in what one says Fast air flow sensor passes through freeze drying kind of refrigeration cycle defrost control line of electromagnetic valve, freeze drying kind of refrigeration cycle suction temperature respectively Adjusting air valve control line after sensor signal lines, the 1st dew point temperature sensor signal wire, freeze drying kind of refrigeration cycle evaporator, Freeze drying kind of refrigeration cycle compressor control line, freeze drying kind of refrigeration cycle exhaust main pipe control line of electromagnetic valve, the 2nd dew-point temperature Sensor signal lines, fan delivery adjustment control line, air outlet Temperature Humidity Sensor signal wire and air outlet wind speed air quantity sensing Device signal wire is connected with central controller power information.
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