CN111974176A - Dehumidification module of mixed gas and detection system thereof - Google Patents
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- 238000007791 dehumidification Methods 0.000 title claims abstract description 96
- 238000001514 detection method Methods 0.000 title abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 76
- 239000007789 gas Substances 0.000 claims description 127
- 238000004458 analytical method Methods 0.000 claims description 49
- 239000012528 membrane Substances 0.000 claims description 42
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 5
- 229910021389 graphene Inorganic materials 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 5
- 229910021536 Zeolite Inorganic materials 0.000 claims description 4
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical group O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 4
- 239000010457 zeolite Substances 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims 1
- 239000012855 volatile organic compound Substances 0.000 description 30
- 238000010586 diagram Methods 0.000 description 14
- 238000005516 engineering process Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 238000000926 separation method Methods 0.000 description 5
- 230000005494 condensation Effects 0.000 description 4
- 238000009833 condensation Methods 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 4
- 238000004817 gas chromatography Methods 0.000 description 4
- 230000009471 action Effects 0.000 description 3
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- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- UQSQSQZYBQSBJZ-UHFFFAOYSA-N fluorosulfonic acid Chemical compound OS(F)(=O)=O UQSQSQZYBQSBJZ-UHFFFAOYSA-N 0.000 description 2
- 239000002808 molecular sieve Substances 0.000 description 2
- 239000000741 silica gel Substances 0.000 description 2
- 229910002027 silica gel Inorganic materials 0.000 description 2
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000010409 thin film Substances 0.000 description 2
- 229920000557 Nafion® Polymers 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005264 electron capture Effects 0.000 description 1
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- 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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- B01D53/26—Drying gases or vapours
- B01D53/265—Drying gases or vapours by refrigeration (condensation)
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- G—PHYSICS
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- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N30/00—Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
- G01N30/02—Column chromatography
- G01N30/88—Integrated analysis systems specially adapted therefor, not covered by a single one of the groups G01N30/04 - G01N30/86
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- 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
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- G01N30/88—Integrated analysis systems specially adapted therefor, not covered by a single one of the groups G01N30/04 - G01N30/86
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Abstract
本发明提供一种混合气体的除湿模块及其检测系统,于一第一除湿模块内设置一第一薄膜组件,该第一薄膜组件将该第一除湿模块内分成一第一空间以及一第二空间,一第一泵浦经由一第一管道连通该第一空间并对该第一空间产生一第一吸力,一第二泵浦经由一第二管道并连通该第二空间并对该第二空间产生一第二吸力,且该第二吸力大于该第一吸力,其中当混合气体由一第一进气口进入该第一空间后,因第二空间的真空度大于于第一空间,混合气体中的水分子通过该薄膜组件被分离,并进入该第二空间,被分离水分子的混合气体因为无法通过该薄膜组件,而被该第一泵浦吸出。
The present invention provides a mixed gas dehumidification module and a detection system thereof. A first film component is arranged in a first dehumidification module. The first film component divides the first dehumidification module into a first space and a second space. A first pump is connected to the first space via a first pipe and generates a first suction force to the first space. A second pump is connected to the second space via a second pipe and generates a second suction force to the second space, and the second suction force is greater than the first suction force. When the mixed gas enters the first space from a first air inlet, because the vacuum degree of the second space is greater than that of the first space, the water molecules in the mixed gas are separated through the film component and enter the second space. The mixed gas with the separated water molecules cannot pass through the film component and is sucked out by the first pump.
Description
技术领域technical field
本发明是关于一种对混合气体进行除湿模块及其检测系统的领域。The invention relates to the field of a dehumidification module for mixed gas and a detection system thereof.
背景技术Background technique
现今对于挥发性有机物(Volatile Organic Compounds,简称VOCs)的分析方法还不够完善,于现有技术中,通常用一个简单的冷凝器来除水,但气体中的水分无法彻底清除,且会有部分能溶解于冷凝水的挥发性有机物气体被稀释,同时内部大量累积的水渍没有及时进行清洗,将会堵塞管路,导致分析结果产生偏差,又气体中残余的水分进入检测分析装置后,将会大幅度地降低其使用寿命,严重则导致检测分析装置的毁损,进而无法长时间的进行挥发性有机物气体的检测。Nowadays, the analysis method for volatile organic compounds (VOCs) is not perfect. In the existing technology, a simple condenser is usually used to remove water, but the water in the gas cannot be completely removed, and there will be some The volatile organic compounds that can be dissolved in the condensed water are diluted, and the accumulated water stains inside are not cleaned in time, which will block the pipeline and cause deviations in the analysis results. After the residual moisture in the gas enters the detection and analysis device, it will be The service life will be greatly reduced, and in severe cases, the detection and analysis device will be damaged, and the detection of volatile organic compounds cannot be carried out for a long time.
一般对挥发性有机物气体进行分析前,其常见的除湿方法有1.添加除水剂,如硅胶、无水氯化钙或分子筛等方法进行吸附;2.使用干燥的气体对亲水薄膜,如全氟磺酸(Nafion dryer)进行吹拂,使亲水薄膜内外产生干湿度差,进而将挥发性有机物体内的水气分离;3.冷冻降温,使挥发性有机物气体内的水气凝结成冰或水而被分离。Generally, before analyzing volatile organic compounds, the common dehumidification methods are: 1. Add a water scavenger, such as silica gel, anhydrous calcium chloride or molecular sieve, etc. for adsorption; 2. Use dry gas to dehumidify the hydrophilic film, such as Perfluorosulfonic acid (Nafion dryer) blows to make the difference of dry humidity inside and outside the hydrophilic film, and then separates the water vapor in the volatile organic matter; water is separated.
但,如果使用添加除水剂,如硅胶、无水氯化钙或分子筛的方法进行水气的吸附时,于此方法中使用的吸附剂需要在停机的情况下定期维护或更换,其衍生出来的耗材费、停机的损失费或运转费,将会对公司产生极大的成本,再者,使用除水剂或亲水薄膜,如全氟磺酸进行水气分离时,容易造成其他极性化合物的吸附与/或穿透,使得分析装置如果对具有极性的化合物分析时,将会造成分析上的错误,而冷冻降温的方法,其需要先运转降温的机台将挥发性有机物气体进行降温,通常温度需要下降至-30度C,才能够确保水分子及水气凝结成冰,进而与挥发性有机物气体分离,但其所需的运转费用以及耗能相当高,相对产生极大的成本。However, if the method of adding water scavengers, such as silica gel, anhydrous calcium chloride or molecular sieve, is used to adsorb water vapor, the adsorbent used in this method needs to be regularly maintained or replaced in the case of shutdown, and its derived The cost of consumables, the loss of downtime or the operation cost will cause a great cost to the company. Furthermore, when using water scavengers or hydrophilic membranes, such as perfluorosulfonic acid for water-gas separation, it is easy to cause other polarities. The adsorption and/or penetration of compounds will cause errors in analysis if the analytical device analyzes compounds with polarity, and the method of freezing and cooling requires first running a cooling machine to remove volatile organic compounds. Cooling, usually the temperature needs to drop to -30 degrees C to ensure that water molecules and water vapor condense into ice, and then separate from volatile organic gas, but the operating cost and energy consumption required are quite high, and relatively large cost.
发明内容SUMMARY OF THE INVENTION
本发明的主要目的,是提供一种混合气体的除湿模块及其检测系统,于一第一除湿模块内设置一第一薄膜组件,该第一薄膜组件将该第一除湿模块内分成一第一空间以及一第二空间,且该第一空间与该第二空间分别通过管路连接一第一泵浦与一第二泵浦,且该第二泵浦产生的吸力大于该第一泵浦,并使第一空间与第二空间产生压力差,当输入至该第一除湿模块内的混合气体中的水分子,将会因为压力差,使得水分子通过薄膜组件分离至第二空间。The main purpose of the present invention is to provide a mixed gas dehumidification module and a detection system thereof. A first membrane assembly is arranged in a first dehumidification module, and the first membrane assembly divides the first dehumidification module into a first dehumidification module. space and a second space, and the first space and the second space are respectively connected with a first pump and a second pump through pipelines, and the suction force generated by the second pump is greater than that of the first pump, A pressure difference is generated between the first space and the second space. When the water molecules in the mixed gas input into the first dehumidification module will be separated into the second space through the membrane module due to the pressure difference.
为了达到上述的目的,本发明公开了一种混合气体的检测系统,其包含一第一除湿模块,其包含一第一中空本体,该第一中空本体内设置一第一薄膜组件,该第一薄膜组件将该第一中空本体分成一第一空间以及一第二空间,该中空本体包含一第一进气口、一第一出气口以及一第二出气口,该第一进气口以及该第一出气口是分别设置于该第一除湿模块的二侧并连通该第一空间,以及该第二出气口是设置于该第一除湿模块上并连通该第二空间,一压力模块,其分别连接该第一出气口以及该第二出气口,且该压力模块包含一第一泵浦,其设置并连接于一第一管道上,且该第一管道的一端是连接该第一出气口,该第一泵浦对该第一空间产生一第一吸力,以及一第二泵浦,其设置并连接该第二管道上,且该第二管道的一端是连接该第二出气口,该第二泵浦对该第二空间产生一第二吸力,一分析装置,其是设置并连接该第一管道上,且该分析装置位于该第一泵浦与该第一除湿模块之间,其中,当一混合气体进入该第一空间,该第一泵浦与该第二泵浦产生压力差,该混合气体中的多个水分子通过该第一薄膜组件分离至该第二空间中,分离该些水分子后的该混合气体再由该第一出气口排出。In order to achieve the above-mentioned purpose, the present invention discloses a mixed gas detection system, which includes a first dehumidification module, which includes a first hollow body, and a first membrane component is arranged in the first hollow body. The thin film assembly divides the first hollow body into a first space and a second space, the hollow body includes a first air inlet, a first air outlet and a second air outlet, the first air inlet and the The first air outlet is respectively arranged on two sides of the first dehumidification module and communicates with the first space, and the second air outlet is arranged on the first dehumidification module and communicates with the second space, a pressure module, which The first air outlet and the second air outlet are respectively connected, and the pressure module includes a first pump, which is arranged and connected to a first pipeline, and one end of the first pipeline is connected to the first air outlet , the first pump generates a first suction force for the first space, and a second pump is arranged and connected to the second pipeline, and one end of the second pipeline is connected to the second air outlet, the The second pump generates a second suction for the second space, an analysis device is disposed and connected to the first pipeline, and the analysis device is located between the first pump and the first dehumidification module, wherein , when a mixed gas enters the first space, the first pump and the second pump generate a pressure difference, and a plurality of water molecules in the mixed gas are separated into the second space through the first membrane element, and the separation The mixed gas after the water molecules is discharged from the first air outlet.
为了达到上述的目的,本发明另外公开了一种混合气体的除湿模块,其包含一第一阀组件,该第一阀组件上分别设置多个前进气口、一第一前出气口以及一第二前出气口,且该第一前出气口连接一第三管道,该第二前出气口连接一第四管道,一第一除湿模块,其包含一第一中空本体,该第一中空本体内设置一第一薄膜组件,该第一薄膜组件将该第一中空本体分成一第一空间以及一第二空间,该第一中空本体包含一第一进气口、一第一出气口以及一第二出气口,该第一进气口以及该第一出气口是分别设置于该第一除湿模块的二侧并连通该第一空间,以及该第二出气口是设置于该第一除湿模块上并连通该第二空间,以及一压力模块,其分别连接该第一出气口以及该第二出气口,且该压力模块包含一第一泵浦,其设置并连接于一第一管道上,且该第一管道的一端是连接该第一出气口,该第一泵浦对该第一空间产生一第一吸力,以及一第二泵浦,其设置并连接该第二管道上,且该第二管道的一端是连接该第二出气口,该第二泵浦对该第二空间产生一第二吸力,一第四泵浦,其设置连接该第四管道上,且该第四管道分别连接该第二前出气口、该第二管道以及该第一管道,其中,该第一阀组件是控制该第一前进气口连通该第一前出气口、该第二前进气口连通该第二前出气口或该第一前进气口连通该第二前出气口、该第二前进气口连通该第一前出气口。In order to achieve the above object, the present invention further discloses a dehumidification module for mixed gas, which includes a first valve assembly, and the first valve assembly is respectively provided with a plurality of front air inlets, a first front air outlet and a second A front air outlet, and the first front air outlet is connected to a third pipe, the second front air outlet is connected to a fourth pipe, a first dehumidification module, which includes a first hollow body, and the first hollow body is arranged inside a first membrane assembly, the first membrane assembly divides the first hollow body into a first space and a second space, the first hollow body includes a first air inlet, a first air outlet and a second Air outlet, the first air inlet and the first air outlet are respectively arranged on two sides of the first dehumidification module and communicate with the first space, and the second air outlet is arranged on the first dehumidification module and The second space is communicated with a pressure module, which is respectively connected to the first air outlet and the second air outlet, and the pressure module includes a first pump, which is arranged and connected to a first pipeline, and the One end of the first pipe is connected to the first air outlet, the first pump generates a first suction force for the first space, and a second pump is arranged and connected to the second pipe, and the second One end of the pipe is connected to the second air outlet, the second pump generates a second suction for the second space, and a fourth pump is arranged and connected to the fourth pipe, and the fourth pipes are respectively connected to the The second front air outlet, the second conduit and the first conduit, wherein the first valve assembly controls the first front air inlet to communicate with the first front air outlet, and the second front air inlet to communicate with the second front air outlet Or the first front air inlet communicates with the second front air outlet, and the second front air inlet communicates with the first front air outlet.
为了达到上述的目的,本发明另外公开了一种混合气体的除湿模块,其包含多个除湿模块,该些除湿模块内分别包含一第一中空本体,该第一中空本体内设置一第一薄膜组件,该第一薄膜组件将该第一中空本体分成一第一空间以及一第二空间,该第一中空本体包含一第一进气口、一第一出气口以及一第二出气口,该第一进气口以及该第一出气口是分别设置于该第一除湿模块的二侧并连通该第一空间,以及该第二出气口是设置于该第一除湿模块上并连通该第二空间,一第二阀组件,该第二阀组件上分别设置多个后进气口、一第一后出气口以及一第二后出气口,该第二阀组件是设置并连接一第一管道,且该第一后出气口是连通该第一管道,该些后进气口是分别连接该些除湿模块的该第一出气口,其中,该第二阀组件是分别控制该些进行气口连通该第一后出气口及该第二后出气口,一压力模块,其分别连接该第一管道以及一第二管道,且该第二管道是分别连接该些除湿模块上的该第二出气口,且该压力模块包含一第一泵浦,其设置并连接于该第一管道上,且该第一管道的一端是连接该第一后出气口,该第一泵浦经由该第二阀组件分别对该些除湿模块的该第一空间产生一第一吸力,以及一第二泵浦,其设置并连接该第二管道上,且该第二管道的一端是连接该第二出气口,该第二泵浦分别对该些除湿模块的该第二空间产生一第二吸力。In order to achieve the above object, the present invention further discloses a mixed gas dehumidification module, which includes a plurality of dehumidification modules, and each of the dehumidification modules includes a first hollow body, and a first film is arranged in the first hollow body. The first membrane assembly divides the first hollow body into a first space and a second space, the first hollow body includes a first air inlet, a first air outlet and a second air outlet, the The first air inlet and the first air outlet are respectively arranged on two sides of the first dehumidification module and communicate with the first space, and the second air outlet is arranged on the first dehumidification module and communicated with the second air outlet. space, a second valve assembly, the second valve assembly is respectively provided with a plurality of rear air inlets, a first rear air outlet and a second rear air outlet, the second valve assembly is installed and connected to a first pipeline , and the first rear air outlet is connected to the first pipeline, and the rear air inlets are respectively connected to the first air outlets of the dehumidification modules, wherein the second valve assembly controls the air ports to communicate with each other. The first rear air outlet and the second rear air outlet, a pressure module, are respectively connected to the first pipeline and a second pipeline, and the second pipeline is respectively connected to the second air outlets on the dehumidification modules , and the pressure module includes a first pump, which is arranged and connected to the first pipeline, and one end of the first pipeline is connected to the first rear air outlet, and the first pump passes through the second valve assembly A first suction force and a second pump are respectively generated for the first spaces of the dehumidification modules, which are arranged and connected to the second pipeline, and one end of the second pipeline is connected to the second air outlet, the The second pump generates a second suction force for the second spaces of the dehumidification modules respectively.
有关本发明的其它功效及实施例的详细内容,配合图式说明如下。The details of other functions and embodiments of the present invention are described below with the help of the drawings.
附图说明Description of drawings
为了更清楚地说明本申请实施例或现有技术中的技术方案,下面将对实施例或现有技术描述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申请中记载的一些实施例,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它的附图。In order to more clearly illustrate the embodiments of the present application or the technical solutions in the prior art, the following briefly introduces the accompanying drawings required for the description of the embodiments or the prior art. Obviously, the drawings in the following description are only These are some embodiments described in this application. For those of ordinary skill in the art, other drawings can also be obtained based on these drawings without creative efforts.
图1是本发明的第一实施例的系统结构示意图;Fig. 1 is the system structure schematic diagram of the first embodiment of the present invention;
图2是本发明的第二实施例的系统做动示意图;FIG. 2 is a schematic diagram of the system operation of the second embodiment of the present invention;
图3A是本发明的第三实施例的系统做动示意图;3A is a schematic diagram of the system operation of the third embodiment of the present invention;
图3B是本发明的第三实施例的系统做动示意图;3B is a schematic diagram of the system operation of the third embodiment of the present invention;
图3C是本发明的第三实施例的系统做动示意图;以及3C is a schematic diagram of the system operation of the third embodiment of the present invention; and
图4是本发明的第四实施例的系统做动示意图。FIG. 4 is a schematic diagram of system operation according to the fourth embodiment of the present invention.
符号说明Symbol Description
1混合气体的除湿模块及其检测系统1 Dehumidification module of mixed gas and its detection system
20除湿模块 22第一中空本体20
222第一空间 224第二空间222
226第一进气口 227第一出气口226
228第二出气口 24第一薄膜组件228 The
26第二除湿模块 262第二中空本体26 The
264第二薄膜组件 265第三空间264
266第四空间 267第二进气口266
268第三出气口 269第四出气口268 The
3第一泵浦 4分析装置3First pump 4Analysis device
5第二泵浦 6冷凝装置5
62储水装置 64第三泵浦62
66第四泵浦 68第五泵浦66
7第一阀组件 70前进气口7 The first valve assembly 70 Front air intake
71第一前进气口 72第二前进气口71 First
73第一前出气口 74第二前出气口73 First
8第二阀组件 80后进气口8 Second valve assembly 80 Rear air inlet
81第一后进气口 82第二后进气口8281 1st
83第一后出气口 84第二后出气口83 The first
A混合气体 D压力模块A Mixed gas D Pressure module
W水分子 VOCs挥发性有机物气体W water molecule VOCs volatile organic compound gas
H1第一温湿度计 H2第二温湿度计H1 first temperature and humidity meter H2 second temperature and humidity meter
L1第一输气管 L2第二输气管L1 first gas pipe L2 second gas pipe
T1第一管道 T2第二管道T1 first pipe T2 second pipe
T3第三管道 T4第四管道T3 third pipe T4 fourth pipe
T5第五管道 T6第六管道T5 fifth pipe T6 sixth pipe
P1第一吸力 P2第二吸力P1 first suction P2 second suction
P3第三吸力 P4第四吸力P3 third suction P4 fourth suction
P5第五吸力 V1第一真空计 V2第二真空计P5 fifth suction V1 first vacuum gauge V2 second vacuum gauge
具体实施方式Detailed ways
在下文的实施方式中所述的位置关系,包括:上,下,左和右,若无特别指明,皆是以图式中组件绘示的方向为基准。The positional relationships described in the following embodiments, including: up, down, left and right, are based on the directions shown by the components in the drawings unless otherwise specified.
首先,请参阅图1,其是本发明的第一实施例的系统结构示意图,如图所示,本发明是为一种混合气体的除湿模块及其检测系统1,其包含一第一除湿模块2以及一压力模块D。First, please refer to FIG. 1 , which is a schematic diagram of the system structure of the first embodiment of the present invention. As shown in the figure, the present invention is a dehumidification module for mixed gas and a
该第一除湿模块2内包含一第一中空本体22以及一第一薄膜组件24,该第一薄膜组件24是设置于该第一中空本体22内,该第一薄膜组件24将该第一中空本体22分成一第一空间222以及一第二空间224,且该第一中空本体22上包含一第一进气口226、一第一出气口227以及一第二出气口228,该第一进气口226以及该第一出气口227分别设置于该第一除湿模块2的二侧并连通该第一空间222,该第二出气口228设置于该第一除湿模块2上并连通该第二空间224,该压力模块D是分别连接该第一出气口227以及该第二出气口228,该压力模块D包含一第一泵浦3以及一第二泵浦5,该第一泵浦3是设置并连接一第一管道T1上,且该第一管道T1的一端是连接该第一出气口227,使该第一管道T1连通该第一空间222,该第一泵浦3设置并连接于该第一管道T1上,且该第一泵浦3对第一空间222产生一第一吸力P1,该第二泵浦5是设置并连接于一第二管道T2上,且该第二管道T2的一端是连接该第一除湿模块2的该第二出气口228,且该第二泵浦5对该第二空间224产生一第二吸力P2,其中该第二泵浦5产生的该第二吸力P2通过该第二管道T2,将该第二吸力P2传递至该第二空间224,且该第二吸力P2是大于该第一吸力P1,当该第一除湿模块2外部的混合气体由该第一进气口226进入该第一空间222,因该第一泵浦3对该第一空间222产生一第一吸力P1,该第二泵浦5对该第二空间224产生一第二吸力P2,使得该第一空间222与该第二空间224因为该第一泵浦3与该第二泵浦5的作用产生压力差,而混合气体进入该第一空间222后,混合气体内的水分子将会通过该第一薄膜组件24将水分子分离,混合气体内的水分子会被分离至该第二空间224,脱离水分子的混合气体将会经由该第一出气口227进入该第一管道T1。The
再者,该混合气体的除湿模块及其检测系统1更进一步包含一分析装置4,该分析装置4设置并连接于该第一管道T1上,且该分析装置4位于该第一除湿模块2与该第一泵浦3之间,其中该第一泵浦3产生的该第一吸力P1通过该第一管道T1并经过该分析装置4,将该第一吸力P1传递至该第一空间222中,使得混合气体内的水分子被分离后,干燥的混合气体将由该第一出气口227进入该第一管道T1至该分析装置4进行分析。Furthermore, the mixed gas dehumidification module and its
其中该分析装置4是为气象色谱法分析装置、气相色谱法串连质谱法分析装置、气相层析电子捕捉侦测器或气相层析火焰离子化侦检器。The
此外,该第一薄膜组件24的材料是为沸石或石墨烯,当该第一薄膜组件24的材料为沸石时,则该第一薄膜组件24上具有多个孔洞,且该些孔洞大小是大于水分子,使得水分子能够通过材料为沸石的该第一薄膜组件24由第一空间222进入第二空间224,而分子大小小于水分子的混合气体将无法通过该第一薄膜组件24。In addition, the material of the
又,该第一薄膜组件24的材料是为石墨烯时,其是利用石墨烯整齐堆栈的方式产生水分子能通过的信道大小或利用石墨烯的亲水性,使水分子通过真空/压力牵引或毛细现象,使水分子经由该第一薄膜组件24到达真空度较大侧。In addition, when the material of the first
接着,请继续参阅图2,其是为本发明的第二实施例的系统做动示意图,如图所示,本实施例与第一实施例的差异在于本实施例更进一步包含一冷凝装置6以及一储水装置62,其他组件与第一实施例相同,此不再赘述。Next, please continue to refer to FIG. 2 , which is a schematic diagram of the system operation of the second embodiment of the present invention. As shown in the figure, the difference between this embodiment and the first embodiment is that this embodiment further includes a
该冷凝装置6是设置并连接该第二管道T2,且该冷凝装置6位于该第一除湿模块2与该第二泵浦5之间,该储水装置62是设置并连接该第二管道T2,且该储水装置62位于该冷凝装置6与该第二泵浦5之间,该冷凝装置6与该储水装置62相互连通,使得该第二泵浦5产生的该第二吸力P2能够经由该第二管道T2通过该储水装置62与该冷凝装置6对该第二空间224产生该第二吸力P2。The condensing
此外,为了增加该第二空间224内的该第二吸力P2,更进一步设置并连接一第三泵浦64于该第二管道上T2,且该第三泵浦64位于该第一除湿模块2与该第二泵浦5之间,而本实施方式是将该第三泵浦64设置于该第一除湿模块2与该冷凝装置6之间进行说明,当该第二吸力P2由该第二泵浦5传递至该第二空间222时,如果该第二吸力P2不足,将无法有效地将水分子分离至该第二空间224,但能够开启该第三泵浦64,使第三泵浦64产生一第三吸力P3,该第三吸力P3将结合该第二吸力P2于该第二空间224,进而增加该第一空间222与该第二空间224之间的压力差。In addition, in order to increase the second suction force P2 in the
再者,为了更精准取得混合气体的湿度以及温度,其能够于该第一进气口226的一侧设置一第一温湿度计H1,以及该第一除湿模块2与该分析装置4间的该第一管道T1上设置一第二温湿度计H2,其能够通过该第一温湿度计H1量测由该第一进气口226通入的混合气体的温度及湿度,以及该第二温湿度计H2量测通过该第一除湿模块2后的混合气体的温度及湿度,通过上述的该第一温湿度计H1以及该第二温湿度计H2的量测,能够监测通过该第一除湿模块2的混合气体内的水分子的浓度及温度。Furthermore, in order to obtain the humidity and temperature of the mixed gas more accurately, a first temperature and humidity meter H1 can be installed on one side of the
以及,该第一管道T1上更能够设置一第一真空计V1,该第二管道T2上设置一第二真空计V2,当该第一泵浦3产生该第一吸力P1于该第一管道T1时,该第一真空计V1能够量测该第一吸力P1相对于该第一管道T1内的真空度,以及当该第二泵浦5产生的该第二吸力P2于该第二管道T2时,该第二真空计V2能够量测该第二吸力P2相对于该第二管道T2内的真空度,该第二真空计V2更能够设置于该第二管道T2上,并位于该第三泵浦64与该第一除湿模块2之间,则该第二真空计V2是量测该第二吸力P2加该第三吸力P3相对于该第二管道T2内的真空度。And, a first vacuum gauge V1 can be set on the first pipeline T1, and a second vacuum gauge V2 can be set on the second pipeline T2. When the first pump 3 generates the first suction force P1 on the first pipeline At T1, the first vacuum gauge V1 can measure the first suction force P1 relative to the degree of vacuum in the first pipe T1, and the second suction force P2 generated by the
请再继续参阅图2,其为本发明的第二实施例的系统做动示意图,如图所示,当该混合气体的除湿模块及其检测系统1的外部输入或通以一混合气体A至该第一除湿模块2内,其中该混合气体A是包含一挥发性有机物气体VOCs以及多个水分子W,该混合气体A内更能够包含空气或其他气体,此外,本发明所提及的实施例内的该混合气体A皆包含上述的该挥发性有机物气体VOCs以及该些水分子W,之后不再赘述,该第一泵浦3产生该第一吸力P1,经由该第一管道T1传递至该第一空间222,该第二泵浦5产生该第二吸力P2,经由该第二管道T2传递至该第二空间224,使该第一除湿模块2内的该第一空间222与该第二空间224之间产生压力差,其中该第二吸力P2是大于该第一吸力P1,该混合气体A经由该第一进气口226进入至该第一空间222后,因为该第一空间222与该第二空间224具有压力差的关系,该混合气体A会先向该第一薄膜组件24靠近,而该第一薄膜组件24会因为其材质的关系,使该混合气体A内的该些水分子W通过该第一薄膜组件24上的孔径大小或真空/压力牵引和毛细现象的关系,使该混合气体A内的该些水分子W被该第一薄膜组件24分离至该第二空间224,该混合气体A内的该挥发性有机物气体VOCs将被该第一吸力P1经由该第一管道T1吸入至该分析装置4内进行该挥发性有机物气体VOCs的分析,且分析完或是过多的该挥发性有机物气体VOCs可通过该第一吸力P1排出。Please continue to refer to FIG. 2 , which is a schematic diagram of the operation of the system according to the second embodiment of the present invention. As shown in the figure, when the external input of the mixed gas dehumidification module and its
再者,为了使进入该第二空间224的该些水分子W能够更有效率地排出,其能够于该第二管道T2上设置并连接该冷凝装置6以及该储水装置62,该些水分子W进入该第二空间224后,会再经由该第二出气口228由该第二管道T2输入至该冷凝装置6进行该些水分子W的凝结,接着再被该第二吸力P2吸至该储水装置62储存,当储水装置62的水量达一定值时,将会一并排出。Furthermore, in order to allow the water molecules W entering the
此外,为了增强该第二泵浦5所产生的该第二吸力P2,能够更进一步设置该第三泵浦64于该第一除湿模块2与该第二泵浦5之间,更详细说明,该第三泵浦64能够设置于该冷凝装置6与该第二空间224之间,并产生一第三吸力P3与该第二泵浦5所产生的该第二吸力P2结合,进而造成该第一空间222与该第二空间224更大的压力差。In addition, in order to enhance the second suction force P2 generated by the
接着,请继续参阅图3A,其是为本发明的第三实施例的系统做动示意图,如图所示,该混合气体的除湿模块及其检测系统1包含一第一除湿模块2、一第一泵浦3、一分析装置4以及一第二泵浦5,其中,上述的组件的连接关系与第一实施方式相同,在此不再赘述。Next, please continue to refer to FIG. 3A , which is a schematic diagram of the operation of the system according to the third embodiment of the present invention. As shown in the figure, the mixed gas dehumidification module and its
本实施方式的该混合气体的除湿模块及其检测系统1更进一步包含一第一阀组件7以及一第四泵浦66,该第一阀组件7上分别设置多个前进气口70、一第一前出气口73以及一第二前出气口74,本实施例的该些前进气口70是以一第一前进气口71以及一第二前进气口72进行说明,之后不再赘述,该第一前出气口73是连接一第三管道T3,且该第三管道T3连接该第一进气口226,使该第一前出气口73能够经由该第三管道T3由该第一进气口226连通至该第一空间222,该第四泵浦66是设置并连接一第四管道T4上,且该第四管道T4分别连接该第二前出气口74、该第二管道T2以及该第一管道T1,该第四泵浦66产生一第四吸力P4通过该第四管道T4传递至该第一阀组件7、该第二管道T2以及该第一管道T1。The mixed gas dehumidification module and its
该第一前进气口71是连通该第一前出气口73或该第二前出气口74、该第二前进气口72是连通该第一前出气口73或该第二前出气口74,而该第一阀组件7是控制该第一前进气口71连通该第一前出气口73、该第二前进气口72连通该第二前出气口74或该第一前进气口71连通该第二前出气口74、该第二前进气口72连通该第一前出气口73。The first front air inlet 71 is connected to the first
接着,请继续参阅图3A,其为本发明的第三实施例的系统做动示意图,如图所示,当该第一阀组件7的该第一前进气口71及该第二前进气口72分别由外部输入或通以一混合气体A至该第一阀组件7内,且分别输入至该第一前进气口71与该第二前进气口72的该混合气体A内的该挥发性有机物气体VOCs的种类及浓度是为相同或不相同,以及该些水分子W的浓度是为相同或不相同,当该混合气体A分别输入至该第一前进气口71以及该第二进气口72时,该第一阀组件7能够选择该第一前进气口71连通该第一前出气口73、该第二前进气口72连通该第二前出气口74或该第一前进气口71连通该第二前出气口74、该第二进气口72连通该第一前出气口73,如果该第一阀组件7选择前者的连接方式,则该第一前进气口71的该混合气体A将由该第一阀组件7的该第一前出气口73经由该第三管道T3输入至该第一除湿模块2的该第一空间222,该第一除湿模块2内产生压力差的方式与前述第一实施方式以及第二实施方式相同,在此不再赘述,进入该第一空间222的该混合气体A,因该第二空间224的真空度大于该第一空间222,使得该些水分子W通过该第一薄膜组件24进入至该第二空间224,而去除该些水分子W后该第一空间222内的该挥发性有机物气体VOCs将由该第一管道T1输入至该分析装置4进行气体的分析。Next, please continue to refer to FIG. 3A , which is a schematic diagram of the operation of the system according to the third embodiment of the present invention. As shown in the figure, when the first front air inlet 71 and the second
该第四泵浦66是产生一第四吸力P4于该第四管道T4中,使分别连通该第四管道T4的该第二前出气口74、该第二管道T2以及该第一管道T1皆产生该第四吸力P4,而该第二前进气口72输入的该混合气体A将经由该第一阀组件7的该第二前出气口74连通至该第四管道T4,并随着该第四吸力P4经由该第四泵浦66进行排出。The fourth pump 66 generates a fourth suction force P4 in the fourth pipe T4, so that the second
又,该第四泵浦66是经由该第四管道T4分别连接该第二前出气口74、该第二泵浦5上的该第二管道T2以及该第一管道T1,当进入该第二空间224的该些水分子W能够经由该第二管道T2连通至该第四管道T4,并通过该第四泵浦66产生的该第四吸力P4排出,以及该第一管道T1上的去除水分子的该混合气体A进入分析装置分析结束后,剩下去除水分子的该混合气体A也是由该第一管道T1连接至该第四泵浦66,并经由第四泵浦66排出。In addition, the fourth pump 66 is respectively connected to the second
请继续参阅图3B,其为本发明的第三实施例的系统做动示意图,如图所示,当由该第一前出气口73输入至该第三管道T3上的进气量过大时,其能够更进一步设置一第一输气管L1,该第一输气管L1是分别连接该第三管道T3以及该第四管道T4,其能够直接将该第三管道T3上的气体进行分流,经由该第一输气管L1直接连通至该第四管道T4进行排出。Please continue to refer to FIG. 3B , which is a schematic diagram of the operation of the system according to the third embodiment of the present invention. As shown in the figure, when the amount of air input from the first
请继续参阅图3C,其为本发明的第三实施例的系统做动示意图,如图所示,本实施例的该第一输气管L1的一端更能够连接该分析装置4与该第一除湿模块2间的该第一管道T1,该第一输气管L1的另一端是连接该第一泵浦3后端的该第一管道T1上,其能够将该第一除湿模块2与该分析装置4间无法实时排出的气体,通过该第一输气管L1进行分流,使多余的气体能够不须通过该分析装置4以及该第一泵浦3直接连接至该第一泵浦3后端的该第一管道T1。Please continue to refer to FIG. 3C , which is a schematic diagram of the operation of the system according to the third embodiment of the present invention. As shown in the figure, one end of the first air pipe L1 in this embodiment can be further connected to the
经由上述第三实施方式的叙述,该混合气体的除湿模块及其检测系统1其能够于通过该第一阀组件先对输入的混合气体进行选择/控制,本实施方式是以该第一阀组件控制该第一前进气口连通该第一前出气口至该第三管道,该第二前进气口连通该第四管道进行说明,接着进入该第三管道的该混合气体则进入该第一空间内进行该些水分子的分离,分离该些水分子后的该混合气体再由该第一管道输入至该分析装置进行分析,分析结束或是过多的该混合物气体则由该第一管道输入至该第四管道进行排出;接着该第二空间的该些水分子是由该第二管道输入至该第四管道进行排出;以及该第二前进气口则连接该第二前出气口输入至该第四管道直接将该混合气体A进行排出,通过上述的说明,其是于该第一阀组件控制连通该第一除湿模块的气体后,将气体输入至该第一除湿模块,并于二空间之间设置一薄膜并利用压力差的方式将混合气体中的水分子进行分离,其相较于先前将水分子分离的技术比较,本发明运转费用以及耗材耗能均相对低廉,且可长时间维持运转,并可依照需求条件调节除湿效能及流量的控制。Through the description of the above-mentioned third embodiment, the mixed gas dehumidification module and its
接着,请继续参阅图4,其为本发明的第四实施例的系统做动示意图,如图所示,该混合气体的除湿模块及其检测系统1包含多个除湿模块20、一第一泵浦3、一分析装置4以及一第二泵浦5,其中,上述的组件的连接关系与第一实施方式相同,在此不再赘述。Next, please continue to refer to FIG. 4 , which is a schematic diagram of the operation of the system according to the fourth embodiment of the present invention. As shown in the figure, the mixed gas dehumidification module and its
本实施例的该些除湿模块20是以一第一除湿模块2以及一第二除湿模块26进行说明,,该第二除湿模块26内包含一第二中空本体262以及一第二薄膜组件264,该第二薄膜组件264是设置于该第二中空本体262内,该第二薄膜组件264将该第二中空本体262分成一第三空间265以及一第四空间266,一第二进气口267以及一第三出气口268分别设置于该第二除湿模块26的二侧并连通该第三空间264,一第四出气口269设置于该第二除湿模块26上并连通该第四空间266。The
该混合气体的除湿模块及其检测系统1更进一步包含一第二阀组件8,该第二阀组件8上分别设置多个后进气口80、一第一后出气口83以及一第二后出气口84,本实施例的该些后进气口80是以该第一后进气口81以及一第二后进气口82进行说明,之后不再赘述,该第二阀组件8是设置并连接该第一管道T1,并位于该第一除湿模块2与该分析装置4之间,一第五管道T5分别连接该第三出气口268以及该第二后进气口82,且该第二后进气口82是连通该第一后出气口83,该第二阀组件8是控制该第一后进气口81连通该第一后出气口83、该第二后进气口82连通该第二后出气口84,或该第一后进气口81连通该第二后出气口84、该第二后进气口82连通该第一后出气口83。The mixed gas dehumidification module and its
再者,更进一步设置一第五泵浦68,该第五泵浦68是设置并连接一第六管道T6上,且该第六管道T6分别连接该第一泵浦3上的该第一管道T1、该第二后出气口84以及该第二泵浦5,且第五泵浦68产生一第五吸力P5分别对该第一泵浦3上的该第一管道T1、该第二后出气口84以及该第二泵浦5上的该第二管道T2产生该第五吸力P5。Furthermore, a
请继续参阅图4,如图所示,该混合气体的除湿模块及其检测系统1的外部分别输入不同种类或相同种类的一混合气体A至该第一进气口226以及该第二进气口267,当该混合气体A分别由该第一进气口226以及该第二进气口267进入至该第一空间222与该第三空间265后,因为该第一空间222与该第二空间224以及该第三空间265与该第四空间266之间具有压力差,使得该混合气体A中的该些水分子W将通过该第一薄膜组件24以及该第二薄膜组件264分离至该第二空间224以及该第四空间266,上述该第一除湿模块2与该第二除湿模块26分离水分子是为相同的结构,在此不再赘述,分离该些水分子W后的该挥发性有机物气体VOCs将经由该第一管道T1以及该第五管道T5分别连接至该第一后进气口81以及该第二后进气口82,接着再由该第二阀组件8控制该第一后进气口81连通该第一后出气口83或该第二后进气口82连通该第一后出气口83,未连接该第一后出气口83的进气口将连接该第二后出气口84,假设该第一后进气口81是连接该第二后出气口83,则该第二后进气口82是连接该第二后出气口84。Please continue to refer to FIG. 4 , as shown in the figure, the outside of the mixed gas dehumidification module and its
接着,该第一管道T1上的该挥发性有机物气体VOCs该第一后进气口81连通至该第一后出气口83,并经由该第二阀组件8与该分析装置4之间的该第一管道T1流入至该分析装置4内进行分析,且分析结束后的该挥发性有机物气体VOCs会因为该第五泵浦68产生的该第五吸力P5的作用,经由该第一管道T1输送至该第六管道T6,再通过该第五泵浦68向外排出。Next, the first
又,该第二后进气口82是连接该第二后出气口84,当该挥发性有机物气体VOCs由该第三空间265经由该第五管道T5通过该第二后进气口82,并由该第二后出气口84被该第五吸力P5吸至该第六管道T6,接着再通过该第五泵浦68向外排出。In addition, the second
再者,该第一除湿模块2与该第二除湿模块26内的该第二空间224以及该第四空间266上是分别设置该第二出气口228以及该第四出气口269,且该第二出气口228以及该第四出气口269是分别连接/连通该第二管道T2,该第二泵浦5分别由该第二管道T2上的该第二出气口228以及该第四出气口269对该第二空间224以及该第四空间266产生该第二吸力P2,且该第五泵浦68连接该第二管道T2,使得该第二空间224以及该第四空间266内所受到的吸力是为第二吸力P2加第五吸力P5,当该些水分子W通过该第一薄膜组件24以及该第二薄膜组件264进入至该第二空间224以及该第四空间266,该些水分子W能够由该第二出气口228以及该第四出气口269吸入至该第二管道T2上,接着由该第二管道T2吸入至该第六管道T6,之后再通过该第五泵浦68向外排出。Furthermore, the
此外,当第二阀组件8的该第一后出气口83输入气体至该第一管道T1进入该第一该分析装置4,经由该第一后出气口83输入至该第一管道T1的进气量过大,导致气体无法实时排出时,其能够更进一步设置一第二输气管L2,该第二输气管L2是连接该第一后出气口83与该分析装置4之间的该第一管道T1以及该第六管道T6,其中该第二输气管L2连接的该第六管道T6是位于该第一管道T1与该第五泵浦68之间的该第六管道T6,该第二输气管L2能够将该第一管道T1上的气流或该挥发性有机物气体VOCs分流至该第六管道T6上,接着再通过该第六管道T6上该第五泵浦68向外排出。In addition, when the first
经由上述第四实施方式的叙述,该混合气体的除湿模块及其检测系统1其能够于通过该第一除湿模块以及该第二除湿模块先将输入的该混合气体内的该些水分子进行分离,接着分离该些水分子后的该混合气体(挥发性有机物气体)再分别输入至该第二阀组件,该第二阀组件对输入的混合气体进行选择/控制,该第二阀组件控制该第一后进气口连通该第一后出气口至该第一管道或该第二后进气口连通该第一后出气口至该第一管道,而未连接该第一管道的该第一后进气口或该第二后进气口,则将连接该第二后出气口至第六管道,接着进入该第一管道的挥发性有机物气体则传递至该分析装置进行分析,分析结束或是过多的挥发性有机物气体则由第一管道输入至第六管道进行排出,而未连接该第一后出气口的该第一后进气口或该第二后进气口则连接该第二后出气口输入至该第六管道进行排出,通过上述的说明,其是先利用该第一除湿模块以及该第二除湿模块将混合气体进行水分子的分离后,再连接至该第二阀组件,该第二阀组件再控制管道的连通,进而将要分析的混合气体输送至分析装置,不需分析的气体则由另一条管路直接排出,其相较于先前将水分子分离的技术比较,本发明运转费用以及耗材耗能均相对低廉,且可长时间维持运转,并可依照需求条件调节除湿效能及流量的控制。Through the description of the above-mentioned fourth embodiment, the mixed gas dehumidification module and its
综上所述,本发明是通过该第一泵浦与该第二泵浦于该第一空间与该第二空间产生压力差,使得输入至该第一空间内的混合气体能够通过该第一薄膜组件来分离水分子,进而干燥该混合气体,分离水分子后的该混合气体再经由该第一吸力的作用,由该第一管道传递至该分析装置进行分析,而第二空间内的水分子则经由该第二吸力的作用,由该第二管道进行排出,于此,本发明具操作方便、无耗材、不需停机维护且低耗能,且可长时间维持运转,并可依照需求条件调节除湿效能及流量的控制。In summary, the present invention generates a pressure difference between the first space and the second space through the first pump and the second pump, so that the mixed gas input into the first space can pass through the first space. Membrane component to separate water molecules, and then dry the mixed gas, the mixed gas after separation of water molecules is then transferred to the analysis device through the first pipeline through the action of the first suction for analysis, and the water in the second space Molecules are then discharged from the second pipeline through the action of the second suction. Therefore, the present invention has the advantages of convenient operation, no consumables, no downtime for maintenance and low energy consumption, and can maintain operation for a long time, and can be operated according to requirements. Condition adjustment dehumidification efficiency and flow control.
以上所述的实施例及/或实施方式,仅是用以说明实现本发明技术的较佳实施例及/或实施方式,并非对本发明技术的实施方式作任何形式上的限制,任何本领域技术人员,在不脱离本发明内容所公开的技术手段的范围,当可作些许的更动或修饰为其它等效的实施例,但仍应视为与本发明实质相同的技术或实施例。The above-mentioned embodiments and/or implementations are only used to illustrate the preferred embodiments and/or implementations for realizing the technology of the present invention, and are not intended to limit the implementation of the technology of the present invention in any form. Personnel, without departing from the scope of the technical means disclosed in the content of the present invention, may make some changes or modifications to other equivalent embodiments, but they should still be regarded as substantially the same technology or embodiment of the present invention.
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