WO2016145995A1 - 吸附分离装置 - Google Patents

吸附分离装置 Download PDF

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Publication number
WO2016145995A1
WO2016145995A1 PCT/CN2016/075467 CN2016075467W WO2016145995A1 WO 2016145995 A1 WO2016145995 A1 WO 2016145995A1 CN 2016075467 W CN2016075467 W CN 2016075467W WO 2016145995 A1 WO2016145995 A1 WO 2016145995A1
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refrigerant
adsorption separation
adsorption
heat exchanger
outlet
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PCT/CN2016/075467
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English (en)
French (fr)
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郭应辉
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深圳市贝腾科技有限公司
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Publication of WO2016145995A1 publication Critical patent/WO2016145995A1/zh

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/26—Drying gases or vapours

Definitions

  • the utility model belongs to the technical field of adsorption separation devices, in particular to an adsorption separation device.
  • the adsorption separation device generally only directly passes the adsorption separation agent to dry the gas, and the effect of drying and removing water is not good.
  • the purpose of the utility model is to overcome the above deficiencies of the prior art, and to provide an adsorption separation device, which has good drying and water removal effect and is energy-saving and environmentally friendly.
  • an adsorption separation device comprising an adsorption separation tube set, an air inlet assembly connected to one end of the adsorption separation tube group, and an air outlet assembly connected to the other end of the adsorption separation tube group
  • the air intake assembly has an air inlet for inflow of the intake air flow
  • the air outlet assembly has an air outlet for the outflow of the air flow
  • the adsorption separation device further includes a temperature adjustment device
  • the temperature adjustment device includes a refrigerant compression a machine, a condenser, an evaporator for cooling the intake air flow, and a heat exchanger for heating the regeneration gas stream
  • the refrigerant compressor being connected with a refrigerant pipe passing through the condenser and the heat exchanger
  • a refrigerant is disposed in the refrigerant pipe.
  • the adsorption separation tube group includes a plurality of longitudinally disposed adsorption tubes, wherein the adsorption tube is provided with an adsorption separation material, the air intake assembly is connected to the lower side of the adsorption separation tube group, and the air outlet assembly is connected. Above the adsorption separation tube set.
  • the temperature regulating device is located at one side of the adsorption separation tube group, wherein the condenser is close to the air intake assembly, and the heat exchanger is located above the condenser and close to the Describe the gas component.
  • the intake assembly has a buffered intake manifold, the evaporator is disposed in the buffered intake split chamber, and the evaporator is coupled to the refrigerant compressor through a refrigerant line.
  • the heat exchanger is provided with a temperature probe interface.
  • the adsorption separation tube set includes a first group of adsorption separation tubes and a second group of adsorption separation tubes for alternately performing adsorption separation and regeneration, and the adsorption separation tube group is connected with a first regeneration regulating valve and a second A regeneration regulating valve having a regeneration gas flow inlet and a regeneration gas flow outlet, the regeneration gas flow inlet being connected to the first regeneration regulating valve, the regeneration gas flow outlet being connected to the second regeneration regulating valve.
  • the refrigerant compressor has a refrigerant inlet and a refrigerant outlet
  • the heat exchanger has a connection inlet and a connection outlet
  • the refrigerant inlet is connected with a first pipeline
  • the first pipeline is from the refrigerant inlet Passing through the condenser and the heat exchanger in sequence and connected to the connection outlet
  • the refrigerant outlet is connected with a second pipeline
  • the second pipeline is sequentially passed through the condenser and exchanged from the refrigerant outlet
  • a heat exchanger is coupled to the connection inlet.
  • the first pipeline is connected with a refrigerant filter and an expansion valve.
  • one side of the adsorption separation tube set is connected with a rotatable open hanging box, and the temperature adjustment device is disposed in the hanging box, and the outer side of the hanging box is provided with a manipulation panel.
  • one side of the condenser member is connected with a heat dissipating component, and the heat dissipating component comprises a heat dissipating motor and a fan blade connected to the heat dissipating motor.
  • the adsorption separation device provided by the utility model provides a better drying effect by using a temperature adjustment device to cool the gas through the evaporator before the gas enters the adsorption separation tube group, thereby obtaining a better drying effect and temperature.
  • the heat generated by the adjusting device can heat the regeneration gas stream to increase the temperature of the gas stream, thereby improving the desorption capacity, thereby improving the desorption performance, the drying and dewatering effect is good, and the device energy consumption is low, and the product energy saving and environmental protection effect is good.
  • FIG. 1 is a front view of an adsorption separation device according to an embodiment of the present invention.
  • FIG. 2 is a left side view of the adsorption separation device according to an embodiment of the present invention.
  • FIG. 3 is a schematic view of the adsorption separation device provided by the embodiment of the present invention when the hanging box is turned on;
  • FIG 4 is a right side view of the adsorption separation device provided by the embodiment of the present invention.
  • an adsorption separation device includes an adsorption separation tube group 3, an air intake unit 1 connected to one end of the adsorption separation tube group 3, and a connection to the adsorption unit.
  • the apparatus further includes a temperature regulating device including a refrigerant compressor 41, a condenser 42, an evaporator 43 for cooling the intake airflow, and a heat exchanger 44 for heating the regeneration gas stream,
  • a refrigerant compressor 41 is connected to the condenser 42.
  • the refrigerant compressor 41 is connected to a refrigerant pipe that is bored in the condenser 42 and the heat exchanger 44.
  • the refrigerant pipe is provided with a refrigerant.
  • the gas can be cooled by the evaporator 43 before the gas enters the adsorption separation tube group 3 to precipitate Part of the water, so as to get a better drying effect, and the heat generated by the temperature regulating device can heat the regeneration gas stream to increase the temperature of the gas stream, thereby improving the desorption ability, thereby improving the desorption performance, drying and water removal effect Good, and the device has low energy consumption, and the product has good energy saving and environmental protection effects.
  • the adsorption separation tube group 3 includes a plurality of longitudinally disposed adsorption tubes 31, and the adsorption tube 31 is provided with an adsorption separation material, and the air intake assembly 1 is connected below the adsorption separation tube group 3.
  • the gas outlet component 2 is connected above the adsorption separation tube group 3, and the adsorption separation effect is good.
  • the temperature adjustment device is located at one side of the adsorption separation tube group 3, wherein the condenser 42 is adjacent to the air intake assembly 1, and the heat exchanger 44 is located above the condenser 42 And close to the gas outlet component 2, which utilizes the principle that the hot air is light in weight, improving the performance of the device.
  • the air intake assembly 1 has a buffer air intake manifold 101, the evaporator 43 is disposed in the buffer air intake manifold 101, and the evaporator 43 is connected to the refrigerant compression through a refrigerant pipeline.
  • Machine 41 The evaporator 43 has a plurality of fins having a large surface area and a good cooling effect.
  • the evaporator 43 may have a straight shape or a meandering tubular shape or the like, and may have a suitable shape such as a U-shape or a zigzag shape.
  • the heat exchanger 44 is provided with a temperature probe interface 440, which is advantageous for improving the reliability of the product.
  • the adsorption separation tube group 3 includes a first group of adsorption separation tubes and a second group of adsorption separation tubes for alternately performing adsorption separation and regeneration, and the adsorption separation tube group 3 is connected with a first regeneration regulating valve 301 and The second regeneration regulating valve 302 controls the adsorption separation tube group 3 to adsorb and separate the first group of adsorption separation tubes, and the second group of adsorption separation tubes can perform regeneration and desorption to continuously output the dry gas flow from the source.
  • the refrigerant compressor 41 has a refrigerant inlet 411 and a refrigerant outlet 412
  • the heat exchanger 44 has a connection inlet 441 and a connection outlet 442
  • the refrigerant inlet 411 is connected with a first conduit 451
  • the first The pipeline 451 sequentially passes through the condenser 42 and the heat exchanger 44 from the refrigerant inlet 411 and is connected to the connection outlet 442
  • the refrigerant outlet 412 is connected to a second pipeline 452
  • the second pipeline 452 passes through the condenser 42 and the heat exchanger 44 in sequence from the refrigerant outlet 412 and is connected to the connection inlet 441.
  • the arrows in Fig. 3 indicate the flow sequence of the refrigerant.
  • the heat exchanger 44 has a regeneration gas inlet 444 and a regeneration gas outlet 443, the regeneration gas inlet 444 is connected to the first regeneration regulating valve 301, and the regeneration gas outlet 443 is connected to the second regeneration regulating
  • the first line 451 is connected to a refrigerant filter 46 and an expansion valve 47 (capillary).
  • one side of the adsorption separation tube set 3 is connected with a rotatable open hanging box 48, the temperature adjusting device is disposed in the hanging box 48, and a control panel 49 is disposed outside the hanging box 48. Easy to operate and maintain.
  • the hanging box 48 is provided with a plurality of heat dissipation shutters or heat dissipation holes.
  • one side of the condenser 42 is connected with a heat dissipating component, and the heat dissipating component comprises a heat dissipating motor and a fan blade connected to the heat dissipating motor, and the heat dissipating effect is good.
  • the air outlet assembly 2 has a regulated airflow manifold 201, and one side of the hanging box 48 is provided with a power switch 481 (electrical control system).
  • the bottom of the air intake assembly 1 may be provided with a muffler 12, which is advantageous for reducing noise and good use effect.
  • the adsorption separation device provided by the utility model is provided with a temperature adjustment device, and the gas enters the adsorption separation Before the tube group 3, the gas can be cooled by the evaporator 43 to precipitate part of the water, thereby obtaining a better drying effect, and the heat generated by the temperature regulating device can heat the regeneration gas stream to increase the temperature of the air stream.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Drying Of Gases (AREA)

Abstract

一种吸附分离装置，包括吸附分离管组（3）、进气组件（1）和出气组件（2），进气组件（1）具有进气口，出气组件（2）具有出气口，吸附分离装置还包括温度调节装置，温度调节装置包括冷媒压缩机（41）、冷凝器（42）、蒸发器（43）和换热器（44），冷媒压缩机（41）连接有穿设于冷凝器（42）和换热器（44）的冷媒管路。

Description

吸附分离装置 技术领域
本实用新型属于吸附分离装置技术领域，尤其涉及一种吸附分离装置。
背景技术
目前的吸附分离装置，其一般仅直接通过吸附分离剂干燥气体，干燥除水效果欠佳。
发明内容
本实用新型的目的在于克服上述现有技术的不足，提供了一种吸附分离装置，其干燥除水效果佳且节能环保。
本实用新型是这样实现的：一种吸附分离装置，包括吸附分离管组、连接于所述吸附分离管组一端的进气组件和连接于所述吸附分离管组另一端的出气组件，所述进气组件具有用于供进气气流流入的进气口，所述出气组件具有用于供出气气流流出的出气口，所述吸附分离装置还包括温度调节装置，所述温度调节装置包括冷媒压缩机、冷凝器、用于对进气气流进行降温的蒸发器和用于对再生气流进行加热的换热器，所述冷媒压缩机连接有穿设于所述冷凝器和换热器的冷媒管路，所述冷媒管路内设置有冷媒。
可选地，所述吸附分离管组包括多根纵向设置的吸附管，所述吸附管内设置有吸附分离材料，所述进气组件连接于所述吸附分离管组的下方，所述出气组件连接于所述吸附分离管组的上方。
可选地，所述温度调节装置位于所述吸附分离管组的一侧，其中，所述冷凝器靠近于所述进气组件，所述换热器位于所述冷凝器的上方且靠近于所述出气组件。
可选地，所述进气组件具有缓冲进气分流腔，所述蒸发器设置于所述缓冲进气分流腔内，且所述蒸发器通过冷媒管路连接于所述冷媒压缩机。
可选地，所述换热器设置有温度探头接口。
可选地，所述吸附分离管组包括用于交替进行吸附分离和再生的第一组吸附分离管和第二组吸附分离管，所述吸附分离管组连接有第一再生调节阀和第二再生调节阀，所述换热器具有再生气流入口和再生气流出口，所述再生气流入口连接于所述第一再生调节阀，所述再生气流出口连接于所述第二再生调节阀。
可选地，所述冷媒压缩机具有冷媒入口和冷媒出口，所述换热器具有连接入口和连接出口；所述冷媒入口连接有第一管路，所述第一管路自所述冷媒入口依次穿过所述冷凝器和换热器并连接于所述连接出口，所述冷媒出口连接有第二管路，所述第二管路自所述冷媒出口依次穿过所述冷凝器和换热器并连接于所述连接入口。
可选地，所述第一管路连接有冷媒过滤器和膨胀阀。
可选地，所述吸附分离管组的一侧连接有可转动开启的挂箱，所述温度调节装置设置于所述挂箱内，所述挂箱的外侧设置有操控面板。
可选地，所述冷凝器件的一侧连接有散热组件，所述散热组件包括散热电机和连接于所述散热电机的扇叶。
本实用新型所提供的吸附分离装置，其通过设置温度调节装置，在气体进入吸附分离管组前，能通过蒸发器对气体进行降温，以析出部分水分，从而得到更好的干燥效果，且温度调节装置工作时产生的热量则可以对再生气流进行加热，以提高气流温度，从而提高脱附能力，进而提高提高脱附性能，干燥除水效果佳，且装置能耗低，产品节能环保效果好。
附图说明
为了更清楚地说明本发明实施例中的技术方案，下面将对实施例中所需要使用的附图作简单地介绍，显而易见地，下面描述中的附图仅仅是本发明的一些实施例，对于本领域普通技术人员来讲，在不付出创造性劳动的前提下，还可以根据这些附图获得其他的附图。
图1是本实用新型实施例提供的吸附分离装置的主视图；
图2是本实用新型实施例提供的吸附分离装置的左视图；
图3是本实用新型实施例提供的吸附分离装置中挂箱转动开启时的示意图；
图4是本实用新型实施例提供的吸附分离装置的右视图。
具体实施方式
为了使本实用新型的目的、技术方案及优点更加清楚明白，以下结合附图及实施例，对本实用新型进行进一步详细说明。应当理解，此处所描述的具体实施例仅仅用以解释本实用新型，并不用于限定本实用新型。
需要说明的是，当元件被称为“固定于”或“设置于”另一个元件，它可以直接在另一个元件上或者可能同时存在居中元件。当一个元件被称为是“连接于”另一个元件，它可以是直接连接到另一个元件或者可能同时存在居中元件。
还需要说明的是，本实用新型实施例中的左、右、上、下等方位用语，仅是互为相对概念或是以产品的正常使用状态为参考的，而不应该认为是具有限制性的。
如图1～图4所示，本实用新型实施例提供的一种吸附分离装置，包括吸附分离管组3、连接于所述吸附分离管组3一端的进气组件1和连接于所述吸附分离管组3另一端的出气组件2，所述进气组件1具有用于供进气气流流入的进气口，所述出气组件2具有用于供出气气流流出的出气口，所述吸附分离装置还包括温度调节装置，所述温度调节装置包括冷媒压缩机41、冷凝器42、用于对进气气流进行降温的蒸发器43和用于对再生气流进行加热的换热器44，所述冷凝器42连接有冷媒压缩机41，所述冷媒压缩机41连接有穿设于所述冷凝器42和换热器44的冷媒管路，所述冷媒管路内设置有冷媒。通过设置温度调节装置，在气体进入吸附分离管组3前，能通过蒸发器43对气体进行降温，以析出 部分水分，从而得到更好的干燥效果，且温度调节装置工作时产生的热量则可以对再生气流进行加热，以提高气流温度，从而提高脱附能力，进而提高提高脱附性能，干燥除水效果佳，且装置能耗低，产品节能环保效果好。
具体地，所述吸附分离管组3包括多根纵向设置的吸附管31，所述吸附管31内设置有吸附分离材料，所述进气组件1连接于所述吸附分离管组3的下方，所述出气组件2连接于所述吸附分离管组3的上方，吸附分离效果好。
具体地，所述温度调节装置位于所述吸附分离管组3的一侧，其中，所述冷凝器42靠近于所述进气组件1，所述换热器44位于所述冷凝器42的上方且靠近于所述出气组件2，其利用了热空气比重轻的原理，提高了设备的性能。
具体地，所述进气组件1具有缓冲进气分流腔101，所述蒸发器43设置于所述缓冲进气分流腔101内，且所述蒸发器43通过冷媒管路连接于所述冷媒压缩机41。蒸发器43具有多个翅片，其表面积大，冷却效果好。蒸发器43可呈直线形或呈迂回管状等，例如U字形或Z字形等合适形状。
具体地，所述换热器44设置有温度探头接口440，有利于提高产品的可靠性。
具体地，所述吸附分离管组3包括用于交替进行吸附分离和再生的第一组吸附分离管和第二组吸附分离管，所述吸附分离管组3连接有第一再生调节阀301和第二再生调节阀302，通过控制吸附分离管组3，使第一组吸附分离管进行吸附分离的同时，第二组吸附分离管可进行再生脱附，以源源不断输出干燥气流。
具体地，所述冷媒压缩机41具有冷媒入口411和冷媒出口412，所述换热器44具有连接入口441和连接出口442；所述冷媒入口411连接有第一管路451，所述第一管路451自所述冷媒入口411依次穿过所述冷凝器42和换热器44并连接于所述连接出口442，所述冷媒出口412连接有第二管路452，所述第二管路452自所述冷媒出口412依次穿过所述冷凝器42和换热器44并连接于所述连接入口441，图3中箭头所示即为冷媒的流动顺序。换热器44具有再生气流入口444和再生气流出口443，再生气流入口444连接于第一再生调节阀301，再生气流出口443连接于第二再生调节阀302。
具体地，所述第一管路451连接有冷媒过滤器46和膨胀阀47(毛细管)。
具体地，所述吸附分离管组3的一侧连接有可转动开启的挂箱48，所述温度调节装置设置于所述挂箱48内，所述挂箱48的外侧设置有操控面板49，以便于操作和维护。挂箱48设置多个散热百叶窗或散热孔位。
具体地，所述冷凝器42件的一侧连接有散热组件，所述散热组件包括散热电机和连接于所述散热电机的扇叶，其散热效果好。
具体地，出气组件2具有稳压气流汇流腔201，挂箱48的一侧设置有电源开关481(电气控制系统)。
具体地，进气组件1的底部可以设置有消音器12，其有利于降低噪音，使用效果好。
本实用新型所提供的吸附分离装置，其通过设置温度调节装置，在气体进入吸附分离 管组3前，能通过蒸发器43对气体进行降温，以析出部分水分，从而得到更好的干燥效果，且温度调节装置工作时产生的热量则可以对再生气流进行加热，以提高气流温度，从而提高脱附能力，进而提高提高脱附性能，干燥除水效果佳，且装置能耗低，产品节能环保效果好。
以上所述仅为本实用新型的较佳实施例而已，并不用以限制本实用新型，凡在本实用新型的精神和原则之内所作的任何修改、等同替换或改进等，均应包含在本实用新型的保护范围之内。

Claims (10)

  1. 一种吸附分离装置，包括吸附分离管组、连接于所述吸附分离管组一端的进气组件和连接于所述吸附分离管组另一端的出气组件，所述进气组件具有用于供进气气流流入的进气口，所述出气组件具有用于供出气气流流出的出气口，其特征在于，所述吸附分离装置还包括温度调节装置，所述温度调节装置包括冷媒压缩机、冷凝器、用于对进气气流进行降温的蒸发器和用于对再生气流进行加热的换热器，所述冷媒压缩机连接有穿设于所述冷凝器和换热器的冷媒管路，所述冷媒管路内设置有冷媒。
  2. 如权利要求1所述的吸附分离装置，其特征在于，所述吸附分离管组包括多根纵向设置的吸附管，所述吸附管内设置有吸附分离材料，所述进气组件连接于所述吸附分离管组的下方，所述出气组件连接于所述吸附分离管组的上方。
  3. 如权利要求2所述的吸附分离装置，其特征在于，所述温度调节装置位于所述吸附分离管组的一侧，其中，所述冷凝器靠近于所述进气组件，所述换热器位于所述冷凝器的上方且靠近于所述出气组件。
  4. 如权利要求1所述的吸附分离装置，其特征在于，所述进气组件具有缓冲进气分流腔，所述蒸发器设置于所述缓冲进气分流腔内，且所述蒸发器通过冷媒管路连接于所述冷媒压缩机。
  5. 如权利要求1所述的吸附分离装置，其特征在于，所述换热器设置有温度探头接口。
  6. 如权利要求1所述的吸附分离装置，其特征在于，所述吸附分离管组包括用于交替进行吸附分离和再生的第一组吸附分离管和第二组吸附分离管，所述吸附分离管组连接有第一再生调节阀和第二再生调节阀，所述换热器具有再生气流入口和再生气流出口，所述再生气流入口连接于所述第一再生调节阀，所述再生气流出口连接于所述第二再生调节阀。
  7. 如权利要求1至6中任一项所述的吸附分离装置，其特征在于，所述冷媒压缩机具有冷媒入口和冷媒出口，所述换热器具有连接入口和连接出口；所述冷媒入口连接有第一管路，所述第一管路自所述冷媒入口依次穿过所述冷凝器和换热器并连接于所述连接出口，所述冷媒出口连接有第二管路，所述第二管路自所述冷媒出口依次穿过所述冷凝器和换热器并连接于所述连接入口。
  8. 如权利要求7所述的吸附分离装置，其特征在于，所述第一管路连接有冷媒过滤器和膨胀阀。
  9. 如权利要求7所述的吸附分离装置，其特征在于，所述吸附分离管组的一侧连接有可转动开启的挂箱，所述温度调节装置设置于所述挂箱内，所述挂箱的外侧设置有操控面板。
  10. 如权利要求1至6中任一项所述的吸附分离装置，其特征在于，所述冷凝器件的一侧连接有散热组件，所述散热组件包括散热电机和连接于所述散热电机的扇叶。
PCT/CN2016/075467 2015-03-13 2016-03-03 吸附分离装置 WO2016145995A1 (zh)

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CN204563889U (zh) * 2015-03-13 2015-08-19 郭应辉 吸附分离装置
CN109613146A (zh) * 2018-12-08 2019-04-12 苏州贞成分析仪器有限公司 一种吸附脱附管
WO2022121209A1 (zh) * 2020-12-11 2022-06-16 深圳市贝腾科技有限公司 吸附分离装置

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