CN204563889U - Adsorption separation device - Google Patents
Adsorption separation device Download PDFInfo
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- CN204563889U CN204563889U CN201520145249.1U CN201520145249U CN204563889U CN 204563889 U CN204563889 U CN 204563889U CN 201520145249 U CN201520145249 U CN 201520145249U CN 204563889 U CN204563889 U CN 204563889U
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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
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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
- B01D53/26—Drying gases or vapours
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Abstract
本实用新型适用于吸附分离装置技术领域,提供了一种吸附分离装置,包括吸附分离管组、进气组件和出气组件,进气组件具有进气口,出气组件具有出气口,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、冷凝器、蒸发器和换热器,冷媒压缩机连接有穿设于冷凝器和换热器的冷媒管路。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。
The utility model is suitable for the technical field of adsorption and separation devices, and provides an adsorption and separation device, which includes an adsorption and separation tube group, an air intake assembly and an air outlet assembly. It includes a temperature regulating device. The temperature regulating device includes a refrigerant compressor, a condenser, an evaporator and a heat exchanger. The refrigerant compressor is connected with a refrigerant pipeline passing through the condenser and the heat exchanger. The adsorption separation device provided by the utility model, by setting a temperature adjustment device, can cool down the gas through the evaporator before the gas enters the adsorption separation tube group, so as to separate out part of the water, so as to obtain a better drying effect, and the temperature The heat generated during the operation of the regulating device can heat the regeneration airflow to increase the temperature of the airflow, thereby improving the desorption capacity and further improving the desorption performance. The effect of drying and water removal is good, and the energy consumption of the device is low, and the product is energy-saving and environmentally friendly.
Description
技术领域technical field
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。The utility model belongs to the technical field of adsorption separation devices, in particular to an adsorption separation device.
背景技术Background technique
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。The current adsorption separation devices generally only dry the gas directly through the adsorption separation agent, and the effect of drying and removing water is not good.
实用新型内容Utility model content
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。The purpose of the utility model is to overcome the shortcomings of the above-mentioned prior art, and provide an adsorption separation device, which has good drying and water removal effect and is energy-saving and environment-friendly.
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。The utility model is realized as follows: an adsorption separation device, comprising an adsorption separation tube group, an air intake 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 The air intake assembly has an air inlet for the intake airflow to flow in, and the air outlet assembly has an air outlet for the outlet airflow to flow out. The adsorption separation device also includes a temperature adjustment device, and the temperature adjustment device includes a refrigerant compressor. machine, a condenser, an evaporator for cooling the intake airflow, and a heat exchanger for heating the regeneration airflow, and the refrigerant compressor is connected with a refrigerant pipe passing through the condenser and the heat exchanger The refrigerant pipeline is provided with a refrigerant.
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。Optionally, the adsorption-separation tube set includes a plurality of adsorption tubes arranged longitudinally, and adsorption and separation materials are arranged in the adsorption tubes, the inlet assembly is connected below the adsorption-separation tube set, and the gas outlet assembly is connected to above the adsorption separation tube set.
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。Optionally, the temperature adjustment device is located on one side of the adsorption separation tube group, wherein the condenser is close to the intake assembly, and the heat exchanger is located above the condenser and close to the Outlet components.
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。Optionally, the air intake component has a buffer intake air distribution chamber, the evaporator is arranged in the buffer intake air distribution chamber, and the evaporator is connected to the refrigerant compressor through a refrigerant pipeline.
可选地,所述换热器设置有温度探头接口。Optionally, the heat exchanger is provided with a temperature probe interface.
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。Optionally, the adsorption-separation tube group 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, the heat exchanger has a regeneration gas inlet and a regeneration gas outlet, the regeneration gas inlet is connected to the first regeneration regulating valve, and the regeneration gas outlet is connected to the second regeneration regulating valve.
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。Optionally, the refrigerant compressor has a refrigerant inlet and a refrigerant outlet, and the heat exchanger has a connection inlet and a connection outlet; the refrigerant inlet is connected with a first pipeline, and the first pipeline connects with the refrigerant inlet Pass through the condenser and heat exchanger in turn and connect to the connection outlet, the refrigerant outlet is connected with a second pipeline, and the second pipeline passes through the condenser and the heat exchanger sequentially from the refrigerant outlet The heater is connected to the connection inlet.
可选地,所述第一管路连接有冷媒过滤器和膨胀阀。Optionally, the first pipeline is connected with a refrigerant filter and an expansion valve.
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。Optionally, a rotatable and open hanging box is connected to one side of the adsorption-separation tube group, the temperature adjustment device is arranged in the hanging box, and a control panel is arranged on the outside of the hanging box.
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。Optionally, a heat dissipation assembly is connected to one side of the condensation device, and the heat dissipation assembly includes a heat dissipation motor and a fan blade connected to the heat dissipation motor.
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。The adsorption separation device provided by the utility model, by setting a temperature adjustment device, can cool down the gas through the evaporator before the gas enters the adsorption separation tube group, so as to separate out part of the water, so as to obtain a better drying effect, and the temperature The heat generated during the operation of the regulating device can heat the regeneration airflow to increase the temperature of the airflow, thereby improving the desorption capacity, thereby improving the desorption performance, the effect of drying and water removal is good, and the energy consumption of the device is low, and the product is energy-saving and environmentally friendly. .
附图说明Description of drawings
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。In order to more clearly illustrate the technical solutions in the embodiments of the present invention, the following will briefly introduce the accompanying drawings that need to be used in the embodiments. Obviously, the accompanying drawings in the following description are only some embodiments of the present invention. For Those of ordinary skill in the art can also obtain other drawings based on these drawings without making creative efforts.
图1是本实用新型实施例提供的吸附分离装置的主视图;Fig. 1 is the front view of the adsorption separation device provided by the embodiment of the utility model;
图2是本实用新型实施例提供的吸附分离装置的左视图;Fig. 2 is a left view of the adsorption separation device provided by the embodiment of the utility model;
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;Fig. 3 is a schematic diagram when the hanging box is rotated and opened in the adsorption separation device provided by the embodiment of the present invention;
图4是本实用新型实施例提供的吸附分离装置的右视图。Fig. 4 is a right side view of the adsorption separation device provided by the embodiment of the utility model.
具体实施方式Detailed ways
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。In order to make the purpose, technical solution and advantages of the utility model clearer, the utility model will be further described in detail below in conjunction with the accompanying drawings and embodiments. It should be understood that the specific embodiments described here are only used to explain the utility model, and are not intended to limit the utility model.
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。It should be noted that when an element is referred to as being “fixed on” or “disposed on” another element, it may be directly on the other element or there may be an intervening element at the same time. When an element is referred to as being "connected to" another element, it can be directly connected to the other element or intervening elements may also be present.
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。It should also be noted that the orientation terms such as left, right, up, and down in the embodiments of the present utility model are only relative concepts or refer to the normal use state of the product, and should not be regarded as restrictive of.
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。As shown in Figures 1 to 4, an adsorption separation device provided by an embodiment of the present invention includes an adsorption separation tube group 3, an air intake assembly 1 connected to one end of the adsorption separation tube group 3, and an air intake assembly connected to the adsorption separation tube group 3. The air outlet assembly 2 at the other end of the separation tube group 3, the air intake assembly 1 has an air inlet for the intake airflow to flow in, and the air outlet assembly 2 has an air outlet for the outlet airflow to flow out. The adsorption separation The device also includes a temperature regulating device, which includes a refrigerant compressor 41, a condenser 42, an evaporator 43 for cooling the intake airflow, and a heat exchanger 44 for heating the regeneration airflow. The condenser 42 is connected with a refrigerant compressor 41, and the refrigerant compressor 41 is connected with a refrigerant pipeline passing through the condenser 42 and the heat exchanger 44, and the refrigerant pipeline is provided with a refrigerant. By setting the temperature adjustment device, before the gas enters the adsorption separation tube group 3, the gas can be cooled by the evaporator 43 to precipitate part of the water, so as to obtain a better drying effect, and the heat generated by the temperature adjustment device can be reduced. The regenerated airflow is heated to increase the temperature of the airflow, thereby improving the desorption capacity, thereby improving the desorption performance, the effect of drying and water removal is good, and the energy consumption of the device is low, and the product has a good energy-saving and environmental protection effect.
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。Specifically, the adsorption-separation tube group 3 includes a plurality of adsorption tubes 31 arranged longitudinally, and adsorption and separation materials are arranged in the adsorption tubes 31, and the air intake assembly 1 is connected below the adsorption-separation tube group 3 , The air outlet assembly 2 is connected above the adsorption separation tube group 3, and the adsorption separation effect is good.
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。Specifically, the temperature adjustment device is located on one side of the adsorption separation tube group 3, wherein the condenser 42 is close to the intake assembly 1, and the heat exchanger 44 is located above the condenser 42 And it is close to the air outlet assembly 2, which utilizes the principle of light specific gravity of hot air to improve the performance of the equipment.
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。Specifically, the air intake assembly 1 has a buffer intake air distribution chamber 101, the evaporator 43 is arranged in the buffer intake air distribution chamber 101, and the evaporator 43 is connected to the refrigerant compressor through a refrigerant pipeline. Machine 41. The evaporator 43 has a plurality of fins, its surface area is large, and its cooling effect is good. The evaporator 43 may be in a straight line or a circuitous tubular shape, such as a U-shape or a Z-shape.
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。Specifically, the heat exchanger 44 is provided with a temperature probe interface 440, which is beneficial to improve product reliability.
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。Specifically, 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 a The second regeneration control valve 302 controls the adsorption separation tube group 3 so that while the first group of adsorption separation tubes is performing adsorption separation, the second group of adsorption separation tubes can perform regeneration and desorption to continuously output dry airflow.
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。Specifically, the refrigerant compressor 41 has a refrigerant inlet 411 and a refrigerant outlet 412, and the heat exchanger 44 has a connection inlet 441 and a connection outlet 442; the refrigerant inlet 411 is connected to a first pipeline 451, and the first The pipeline 451 passes through the condenser 42 and the heat exchanger 44 sequentially from the refrigerant inlet 411 and is connected to the connection outlet 442. The refrigerant outlet 412 is connected to a second pipeline 452, and the second pipeline 452 passes through the condenser 42 and the heat exchanger 44 sequentially from the refrigerant outlet 412 and is connected to the connection inlet 441 , and the flow sequence of the refrigerant is shown by arrows in FIG. 3 . 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 valve 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)。Specifically, the first pipeline 451 is connected with a refrigerant filter 46 and an expansion valve 47 (capillary).
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。Specifically, one side of the adsorption separation tube group 3 is connected with a rotatable and openable hanging box 48, the temperature adjustment device is arranged in the hanging box 48, and the outer side of the hanging box 48 is provided with a control panel 49, For easy operation and maintenance. Hanging box 48 is provided with a plurality of louvers or radiating holes.
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。Specifically, one side of the condenser 42 is connected with a heat dissipation assembly, and the heat dissipation assembly includes a heat dissipation motor and a fan blade connected to the heat dissipation motor, which has a good heat dissipation effect.
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(电气控制装置、电气控制系统)。Specifically, the air outlet assembly 2 has a stabilized air flow confluence cavity 201 , and a power switch 481 (electrical control device, electrical control system) is provided on one side of the hanging box 48 .
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。Specifically, the bottom of the air intake assembly 1 can be provided with a muffler 12, which is beneficial to reduce noise and has a good use effect.
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。The adsorption separation device provided by the utility model can cool down the gas through the evaporator 43 before the gas enters the adsorption separation tube group 3 by setting a temperature adjustment device, so as to separate out part of the water, thereby obtaining a better drying effect. And the heat generated when the temperature adjustment device is working can heat the regeneration airflow to increase the temperature of the airflow, thereby improving the desorption capacity, thereby improving the desorption performance, the effect of drying and water removal is good, and the energy consumption of the device is low, and the product is energy-saving and environmentally friendly The effect is good.
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。The above descriptions are only preferred embodiments of the present utility model, and are not intended to limit the present utility model. Any modification, equivalent replacement or improvement made within the spirit and principles of the present utility model shall be included in this utility model. within the scope of protection of utility models.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520145249.1U CN204563889U (en) | 2015-03-13 | 2015-03-13 | Adsorption separation device |
| PCT/CN2016/075467 WO2016145995A1 (en) | 2015-03-13 | 2016-03-03 | Adsorption-separation-apparatus |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520145249.1U CN204563889U (en) | 2015-03-13 | 2015-03-13 | Adsorption separation device |
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| CN204563889U true CN204563889U (en) | 2015-08-19 |
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|---|---|---|---|
| CN201520145249.1U Expired - Lifetime CN204563889U (en) | 2015-03-13 | 2015-03-13 | Adsorption separation device |
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| CN (1) | CN204563889U (en) |
| WO (1) | WO2016145995A1 (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2016145995A1 (en) * | 2015-03-13 | 2016-09-22 | 深圳市贝腾科技有限公司 | Adsorption-separation-apparatus |
| CN109613146A (en) * | 2018-12-08 | 2019-04-12 | 苏州贞成分析仪器有限公司 | A kind of adsorption/desorption pipe |
| CN112337272A (en) * | 2020-12-11 | 2021-02-09 | 深圳市贝腾科技有限公司 | Adsorption separation device |
| WO2022121209A1 (en) * | 2020-12-11 | 2022-06-16 | 深圳市贝腾科技有限公司 | Adsorptive separation apparatus |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1202896C (en) * | 2002-02-07 | 2005-05-25 | 北京燕化高新技术股份有限公司 | Air-purifying method during separating air |
| US9038409B2 (en) * | 2009-09-21 | 2015-05-26 | Korea Research Institute Of Chemical Technology | Apparatus for treating air by using porous organic-inorganic hybrid materials as an absorbent |
| CN102553403A (en) * | 2012-01-06 | 2012-07-11 | 郭应辉 | Adsorption drying machine |
| CN202460431U (en) * | 2012-01-06 | 2012-10-03 | 郭应辉 | Adsorption drying machine |
| CN102553402A (en) * | 2012-01-06 | 2012-07-11 | 郭应辉 | Adsorption drying machine |
| CN202427328U (en) * | 2012-01-06 | 2012-09-12 | 郭应辉 | Absorption dryer |
| CN204563889U (en) * | 2015-03-13 | 2015-08-19 | 郭应辉 | Adsorption separation device |
-
2015
- 2015-03-13 CN CN201520145249.1U patent/CN204563889U/en not_active Expired - Lifetime
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2016
- 2016-03-03 WO PCT/CN2016/075467 patent/WO2016145995A1/en not_active Ceased
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2016145995A1 (en) * | 2015-03-13 | 2016-09-22 | 深圳市贝腾科技有限公司 | Adsorption-separation-apparatus |
| CN109613146A (en) * | 2018-12-08 | 2019-04-12 | 苏州贞成分析仪器有限公司 | A kind of adsorption/desorption pipe |
| CN112337272A (en) * | 2020-12-11 | 2021-02-09 | 深圳市贝腾科技有限公司 | Adsorption separation device |
| WO2022121209A1 (en) * | 2020-12-11 | 2022-06-16 | 深圳市贝腾科技有限公司 | Adsorptive separation apparatus |
| US12350620B2 (en) | 2020-12-11 | 2025-07-08 | Shenzhen Biteman Technology Co., Ltd | Adsorptive separation apparatus |
| CN112337272B (en) * | 2020-12-11 | 2025-09-02 | 深圳市贝腾科技有限公司 | Adsorption separation device |
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| Publication number | Publication date |
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| WO2016145995A1 (en) | 2016-09-22 |
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Effective date of registration: 20161025 Address after: 518333, Guangdong, Shenzhen Xixiang street Baoan District iron road oyster industry park 1 and 2 buildings (first branch garden 1, workshop 4, C) Patentee after: BITEMAN TECHNOLOGY Co.,Ltd. Address before: Shenzhen City, Guangdong province Baoan 518000 West Coast Garden District 48 Haifeng Ge 1-4C Patentee before: Guo Yinghui |
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Granted publication date: 20150819 |