CN205164432U - Adsorption equipment and be used for drying device that car VOC detected - Google Patents
Adsorption equipment and be used for drying device that car VOC detected Download PDFInfo
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- CN205164432U CN205164432U CN201520949411.5U CN201520949411U CN205164432U CN 205164432 U CN205164432 U CN 205164432U CN 201520949411 U CN201520949411 U CN 201520949411U CN 205164432 U CN205164432 U CN 205164432U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Abstract
The utility model relates to an adsorption equipment and be used for drying device that car VOC detected, adsorption equipment includes: at least one first adsorption tube, first adsorption tube is equipped with an airflow channel who is linked together with the external world, at least one second adsorption tube, the second adsorption tube with first adsorption tube swing joint, the second adsorption tube with first adsorption tube matches and forms the 2nd airflow channel, the 2nd airflow channel with an airflow channel is linked together, the second adsorption tube be equipped with respectively with external the 3rd airflow channel that the 2nd airflow channel is linked together, the 3rd airflow channel with an airflow channel staggers mutually. A drying device, including foretell adsorption equipment for car VOC detects. This adsorption equipment and be used for drying device that car VOC detected can improve the gas absorption effect, reduces the dead volume, improves the detection precision of car VOC content.
Description
Technical field
The utility model relates to adsorption technology field, the drying device particularly relating to a kind of adsorbent equipment and detect for automobile VOC.
Background technology
It is the detection technique that development in recent years is got up that automobile VOC detects, and detects at present mainly for automotive material and inside gadget, and conventional method master by distributing VOC after heated sample, will use the absorption of TenaxTA adsorption tube, then detecting with TD-GC-MS.The substantially moist VOC gas come out of traditional testing process, direct adsorption tube adsorbs, and experiment shows, a certain amount of moisture is after TenaxTA adsorption tube, because effect such as cold doubtful grade is attached in pipe and filling surface, affect the adsorption effect of TenaxTA adsorbent equipment, very easily reach adsorption tube and penetrate, directly affect its degree of accuracy detected and stability.
In present technology, generally use " common drying tube+TenaxTA adsorption tube " to gather VOC, avoid the problems referred to above, but it can cause dead volume large, sampling process needs more gas to fill, the automobile VOC content that cannot accurately detect; In addition, easily Airflow obstruction is caused because of the saturated caking of drier.
Summary of the invention
Based on this, be necessary the drying device a kind of adsorbent equipment being provided and detecting for automobile VOC, improve gas absorption effect, reduce dead volume, improve the accuracy of detection of automobile VOC content, and prevent the Airflow obstruction problem in testing process.
Its technical scheme is as follows:
A kind of adsorbent equipment, comprising: at least one first adsorption tube, described first adsorption tube is provided with the first gas channel be connected with the external world; At least one second adsorption tube, described second adsorption tube is flexibly connected with described first adsorption tube, described second adsorption tube matches with described first adsorption tube formation second gas channel, described second gas channel is connected with described first gas channel, described second adsorption tube is provided with the 3rd gas channel be connected with extraneous, described second gas channel respectively, and described 3rd gas channel and described first gas channel are staggered.
Wherein in an embodiment, the mean gap of described first gas channel is less than the mean gap between described first adsorption tube internal adsorbent; The mean gap of described second gas channel is less than the mean gap between described second adsorption tube internal adsorbent.
Wherein in an embodiment, also comprise two gas hoods, two described gas hoods respectively first adsorption tube described with are flexibly connected, and described gas hood is provided with the container cavity be connected with described first gas channel; Described first adsorption tube is at least two, arranges described second adsorption tube between two described first adsorption tubes.
Wherein in an embodiment, described gas hood is also provided with partition, and described partition is arranged in corresponding described container cavity, and is formed with the edge of described gas hood and import and export; Described partition matches with described first adsorption tube formation the 4th gas channel.
Wherein in an embodiment, described first gas channel is arranged in the middle part of described first adsorption tube; Described 3rd gas channel be arranged at the edge of the second adsorption tube.
Wherein in an embodiment, described 3rd gas channel is many articles, and arranges along the circumferential edge interval of described second adsorption tube; Or described 3rd gas channel is annulus, and be arranged at the edge of described second adsorption tube.
Wherein in an embodiment, described first adsorption tube is provided with two first ends be oppositely arranged, and described first gas channel is arranged between two described first ends, and described first end is outwardly.
Wherein in an embodiment, described second adsorption tube is provided with two the second ends be oppositely arranged, and described 3rd gas channel is arranged between two described the second ends, and described the second end sets to the concave; Described the second end matches with described first end and forms described second gas channel.
Wherein in an embodiment, also comprise at least two sand core tubes, wherein described sand core tube to be arranged in described first adsorption tube and to form described first gas channel, and wherein one article of described sand core tube to be arranged in described second adsorption tube and to form described 3rd gas channel.
For the drying device that automobile VOC detects, comprise above-mentioned adsorbent equipment.
" first " described in above-mentioned the utility model, " second ", " the 3rd ", " the 4th " do not represent concrete quantity and order, are only used for the differentiation of title; Described VOC: VOC, comprises the compounds such as benzene,toluene,xylene, ethylbenzene, styrene, is that a class has the pernicious gas material of directly harm to human body; Described TenaxTA adsorbent equipment: a kind of adsorbent equipment using TenaxTA porous adsorption stuffing, has good adsorption capacity to VOC, and VOC can be discharged again by mode of heating, detects VOC in instrument; TenaxTA: poly-(two) phenylate (polyphenylene oxides); Described TD-GC-MS: Thermal desorption-gas chromatograph-mass spectrometer (GC-MS), a kind of instrument for detecting VOC; Described adsorbent equipment penetrates: refer to that adsorption device adsorbs is saturated, and VOC content exceedes the adsorption capacity of absorption, and unnecessary VOC is not directly adsorbed by adsorbent equipment, cannot detect; Dead volume: refer to adsorbent equipment filled after space, i.e. the volume of gas in adsorbent equipment.
Above-mentioned the beneficial effects of the utility model:
When above-mentioned adsorbent equipment uses, detect gas to enter from the first adsorption tube, the second adsorption tube is entered again through the first adsorption tube, after the first adsorption tube is because of absorption water-vapo(u)r saturation, detect gas and can pass through the first gas channel, enter the second adsorption tube through the second gas channel, after the second adsorption tube is again because of absorption water-vapo(u)r saturation, this detection gas can be flowed out by the 3rd gas channel or be entered another first adsorption tube again and adsorb.This adsorbent equipment can ensure that detecting gas all absorbs, and makes full use of the adsorbent stored in adsorption tube simultaneously, does not need extra drying to detect gas, reduces experimentation cost, reduce dead volume simultaneously, prevent Airflow obstruction, improve accuracy of detection.
When the above-mentioned drying device for automobile VOC detection uses, VOC gas enters from from the first adsorption tube, the second adsorption tube is entered again through the first adsorption tube, after the first adsorption tube is because of absorption water-vapo(u)r saturation, VOC gas can pass through the first gas channel, the second adsorption tube is entered through the second gas channel, after the second adsorption tube is again because of absorption water-vapo(u)r saturation, VOC gas can be flowed out (whether detect it by dry indicating device absorbs complete) by the 3rd gas channel or be entered another first adsorption tube again and adsorb.This is used for the drying device that automobile VOC detects, and ensures drying effect, prevents Airflow obstruction, improves the adsorption effect of VOC gas on TenaxTA, reduces dead volume simultaneously, improves the accuracy of detection of automobile VOC content, reduces the drying device that experimentation cost detects.
Accompanying drawing explanation
Fig. 1 is the structural representation of adsorbent equipment described in the utility model;
Fig. 2 is the use schematic diagram of adsorbent equipment described in the utility model;
Fig. 3 is the use schematic diagram of another kind of adsorbent equipment described in the utility model;
Fig. 4 is the structural representation of the adsorbent equipment of band gas hood described in the utility model;
Fig. 5 is the use schematic diagram a of the adsorbent equipment of band gas hood described in the utility model;
Fig. 6 is the use schematic diagram b of the adsorbent equipment of band gas hood described in the utility model;
Fig. 7 is the use schematic diagram c of the adsorbent equipment of band gas hood described in the utility model;
Fig. 8 is the first adsorption tube schematic cross-section described in the utility model;
Fig. 9 is the second adsorption tube schematic cross-section described in the utility model.
Description of reference numerals:
100, the first adsorption tube, the 110, first gas channel, 120, first end, 200, the second adsorption tube, 210, the 3rd gas channel, 220, the second end, 300, gas hood, 310, container cavity, 320, partition, 302, import and export, the 402, second gas channel, 404, the 4th gas channel, 500, dry indicating device.
Detailed description of the invention
For making the purpose of this utility model, technical scheme and advantage clearly understand, below in conjunction with the drawings and the specific embodiments, the utility model is described in further detail.Should be understood that, detailed description of the invention described herein, only in order to explain the utility model, does not limit protection domain of the present utility model.
Shown in Fig. 1,2 and 3, a kind of adsorbent equipment described in the utility model, comprising: at least one first adsorption tube 100, first adsorption tube 100 is provided with the first gas channel 110 be connected with the external world; At least one second adsorption tube 200, second adsorption tube 200 is flexibly connected with the first adsorption tube 100, second adsorption tube 200 matches with the first adsorption tube 100 formation second gas channel 402, second gas channel 402 is connected with the first gas channel 110, second adsorption tube 200 is provided with the 3rd gas channel the 210, three gas channel 210 that is connected with extraneous, the second gas channel 402 respectively and the first gas channel 110 is staggered.
Shown in Fig. 1,2 and 3, when adsorbent equipment uses, detect gas to enter from the first adsorption tube 100, the second adsorption tube 200 is entered again through the first adsorption tube 100, after the first adsorption tube 100 is because of absorption water-vapo(u)r saturation, detect gas and can pass through the first gas channel 110, the second adsorption tube 200 is entered through the second gas channel 402, after the second adsorption tube 200 is again because of absorption water-vapo(u)r saturation, this detection gas can be flowed out by the 3rd gas channel 210 or enter another first adsorption tube 100 again and adsorb; Or detection gas enters from the second adsorption tube 200, the first adsorption tube 100 is entered again through the second adsorption tube 200, after the second adsorption tube 200 is because of absorption water-vapo(u)r saturation, detect gas and can pass through the 3rd gas channel 210, the first adsorption tube 100 is entered through the second gas channel 402, after the first adsorption tube 100 is again because of absorption water-vapo(u)r saturation, this detection gas can be flowed out by the first gas channel 110 or enter another second adsorption tube 200 again and adsorb.This adsorbent equipment adopts multi-stage absorption design, the quantity of the first adsorption tube 100 or the second adsorption tube 200 can be increased as required, ensure that detecting gas all absorbs, make full use of the adsorbent stored in adsorption tube simultaneously, do not need extra dry detection gas, reduce experimentation cost, reduce dead volume simultaneously, improve accuracy of detection.
First adsorption tube 100 adopts different connected modes from the second adsorption tube 200, as movable connection methods such as screw thread, nested type bayonet socket, flange-interfaces.
It should be noted that, this combination of the first adsorption tube 100 and the second adsorption tube 200 has various ways, as the first adsorption tube 100+ second adsorption tube 200, first adsorption tube 100+ second adsorption tube 200+ first adsorption tube 100, second adsorption tube 200+ first adsorption tube 100+ second adsorption tube 200, first adsorption tube 100+ second adsorption tube 200+ first adsorption tube 100+ second adsorption tube 200, second combination such as adsorption tube 200+ first adsorption tube 100+ second adsorption tube 200+ first adsorption tube 100+ second adsorption tube 200 grade, as long as it makes use of the adsorption design of more than this two-stage of the utility model first adsorption tube 100+ second adsorption tube 200, all belong to the scope of the utility model protection.
The mean gap of the first gas channel 110 is less than the mean gap between the first adsorption tube 100 internal adsorbent, prevent most of gas from passing through from the first gas channel 110, and do not reach the object of absorption, only has adsorbent because of imbibition, after gap shrinks, detect gas can not by during sorbent just from the first gas channel 110 by entering next stage adsorption tube; The mean gap of the second gas channel 210 is less than the mean gap between the second adsorption tube 200 internal adsorbent, prevent most of gas from passing through from the 3rd gas channel 210, and do not reach the object of absorption, only has adsorbent because of imbibition, after gap shrinks, detect gas can not by during sorbent just from the 3rd gas channel 210 by entering next stage adsorption tube.
Shown in Fig. 4,5,6 and 7, also comprise two gas hoods, 300, two gas hoods 300 and be flexibly connected with first adsorption tube 100 respectively, gas hood 300 is provided with the container cavity 310 be connected with the first gas channel 110; First adsorption tube 100 is at least two, arranges second adsorption tube 200 between two the first adsorption tubes 100.Wherein, first gas channel 110 is communicated with container cavity 210 and the second gas channel 210 respectively, or first gas channel 110 is communicated with two the second gas channels 210 respectively.By the mode of angle docking, staggered air-flow, improve drying efficiency, and ensure to continue in use procedure to keep air-flow unobstructed, do not block air-flow because drier water adsorption is saturated.Gas hood 300 works the air-flow that leads, and is convenient to adsorbent equipment simultaneously and is connected with other airflow apparatus; Container cavity 310 has buffer gas flow, makes gas more easily enter the first adsorption tube 100.Gas hood 300 is also provided with partition 320, and partition 320 is arranged in container cavity 310, and forms import and export 302 with gas hood 300 edge; Partition 320 matches with the first adsorption tube 100 formation the 4th gas channel 404.The internal gas flow of container cavity 310 is planned in the effect of partition 320 further, makes gas enter from import and export 302 or go out; Gas plays the effect of guiding air-flow when import and export 302 enter, is convenient to the first adsorption tube 100 and absorbs; Gas is cushioning effect from import and export 302 are gone out, delay air-flow flow out, time detect gas fully absorbed by adsorbent equipment.
Gas hood 300 adopts different connected modes from the first adsorption tube 100, as movable connection methods such as screw thread, nested type bayonet socket, flange-interfaces.
Shown in Fig. 8,9, the first gas channel 110 to be arranged in the middle part of the first adsorption tube 100; 3rd gas channel 210 is arranged at the edge of the second adsorption tube 200.3rd gas channel 210 is many articles, and arranges along the circumferential edge interval of the second adsorption tube 300; Or the 3rd gas channel 210 be annulus, and be arranged at the edge of the second adsorption tube 200.By the mode of angle docking, staggered air-flow, improve drying efficiency, and ensure to continue in use procedure to keep air-flow unobstructed, do not block air-flow because drier water adsorption is saturated; While maintenance air-flow, reduce dead volume.
Shown in Fig. 4, the first adsorption tube 100 is provided with two first ends be oppositely arranged 120, first gas channel 110 and is arranged between two first ends 120, and first end 120 is outwardly.Second adsorption tube 200 is provided with two the second ends be oppositely arranged the 220, three gas channel 210 and is arranged between two the second ends 220, and the second end 220 sets to the concave; The second end 220 matches with first end 210 formation second gas channel 402.By the mode of angle docking, staggered air-flow, improve drying efficiency.
Shown in Fig. 8,9, also comprise at least two sand core tubes 500, wherein sand core tube 500 to be arranged in the first adsorption tube 100 and to form the first gas channel 110, and wherein one article of sand core tube 500 to be arranged in the second adsorption tube 200 and to form the 3rd gas channel 210.Sand core tube 500 is used to form the first gas channel 110 and the second gas channel 210, the mean gap being convenient to guarantee first gas channel 110 is less than the mean gap between the first adsorption tube 100 internal adsorbent, prevent most of gas from passing through from the first gas channel 110, and do not reach the order of absorption; The mean gap of the second gas channel 210 is less than the mean gap between the second adsorption tube 200 internal adsorbent, prevents most of gas from passing through from the 3rd gas channel 210, and does not reach the object of absorption.
In the utility model, the adsorption process of adsorbent equipment is:
(1) as shown in Figure 4, when the equal unsaturation of adsorbent equipment, gas enters from the air inlet pipe (mark) of gas hood 300, after dispersion, enter the first adsorption tube 100 adsorb, gas after absorption is directly by the second follow-up adsorption tube 200, first adsorption tube 100 and gas hood 300, give vent to anger after drying indicating device 500, now dry indicating device 500 shows gas is dry gas.
(2) as shown in Figure 5, when the first absorption 100 is saturated above, gas cannot pass through adsorbent smoothly, the first gas channel from the first absorption 100 passes through by air-flow, direct arrival second adsorption tube 200, adsorbent in the second adsorption tube 200, the gas after absorption is directly by the first follow-up adsorption tube 100 and gas hood 300, and now dry indicating device 500 shows gas is dry gas.
(3) as shown in Figure 6, when the first adsorption tube 100 and the second adsorption tube 200 all reach capacity, gas cannot pass through adsorbent smoothly, the 3rd gas channel 210 from the second adsorption tube 200 passes through by air-flow, direct arrival second the first adsorption tube 100 adsorbs, gas after absorption is directly by the first follow-up adsorption tube 100 and gas hood 300, and now dry indicating device 500 shows gas is dry gas.
(4) as shown in Figure 7, when second the first adsorption tube 100 also reaches capacity, the first gas channel that air-flow flows to the first absorption 100 gradually flows out through gas hood 300, and now dry indicating device 500 shows gas is moisture, adsorption tube lost efficacy, and need access another adsorption tube again.
This adsorbent equipment adopts multi-stage absorption design, the quantity of the first adsorption tube 100 or the second adsorption tube 200 can be increased as required, ensure that detecting gas all absorbs, make full use of the adsorbent stored in adsorption tube simultaneously, do not need extra dry detection gas, reduce experimentation cost, reduce dead volume simultaneously, improve accuracy of detection.
For the drying device that automobile VOC detects, comprise above-mentioned adsorbent equipment.
When drying device for automobile VOC detection uses, VOC gas enters from from the first adsorption tube 100, the second adsorption tube 200 is entered again through the first adsorption tube 100, after the first adsorption tube 100 is because of absorption water-vapo(u)r saturation, VOC gas can pass through the first gas channel 110, the second adsorption tube 200 is entered through the second gas channel 402, after the second adsorption tube 200 is again because of absorption water-vapo(u)r saturation, VOC gas can be flowed out by the 3rd gas channel 210 (whether detect moisture by dry indicating device absorbs complete) or enter another first adsorption tube 110 again adsorbs again.This is used for the drying device that automobile VOC detects, and ensures drying effect, prevents Airflow obstruction, improves the adsorption effect of VOC gas on TenaxTA, reduces dead volume simultaneously, improves the accuracy of detection of automobile VOC content, reduces the drying device that experimentation cost detects.
Each technical characteristic of the above embodiment can combine arbitrarily, for making description succinct, the all possible combination of each technical characteristic in above-described embodiment is not all described, but, as long as the combination of these technical characteristics does not exist contradiction, be all considered to be the scope that this description is recorded.
The above embodiment only have expressed several embodiment of the present utility model, and it describes comparatively concrete and detailed, but therefore can not be interpreted as the restriction to utility model patent scope.It should be pointed out that for the person of ordinary skill of the art, without departing from the concept of the premise utility, can also make some distortion and improvement, these all belong to protection domain of the present utility model.Therefore, the protection domain of the utility model patent should be as the criterion with claims.
Claims (10)
1. an adsorbent equipment, is characterized in that, comprising:
At least one first adsorption tube, described first adsorption tube is provided with the first gas channel be connected with the external world;
At least one second adsorption tube, described second adsorption tube is flexibly connected with described first adsorption tube, described second adsorption tube matches with described first adsorption tube formation second gas channel, described second gas channel is connected with described first gas channel, described second adsorption tube is provided with the 3rd gas channel be connected with extraneous, described second gas channel respectively, and described 3rd gas channel and described first gas channel are staggered.
2. adsorbent equipment according to claim 1, is characterized in that, the mean gap of described first gas channel is less than the mean gap between described first adsorption tube internal adsorbent; The mean gap of described second gas channel is less than the mean gap between described second adsorption tube internal adsorbent.
3. adsorbent equipment according to claim 1, is characterized in that, also comprises two gas hoods, and two described gas hoods respectively first adsorption tube described with are flexibly connected, and described gas hood is provided with the container cavity be connected with described first gas channel; Described first adsorption tube is at least two, arranges described second adsorption tube between two described first adsorption tubes.
4. adsorbent equipment according to claim 3, is characterized in that, described gas hood is also provided with partition, and described partition is arranged in described container cavity, and is formed with the edge of described gas hood and import and export; Described partition matches with described first adsorption tube formation the 4th gas channel.
5. adsorbent equipment according to claim 1, is characterized in that, described first gas channel is arranged in the middle part of described first adsorption tube; Described 3rd gas channel be arranged at the edge of the second adsorption tube.
6. adsorbent equipment according to claim 5, is characterized in that, described 3rd gas channel is many articles, and arranges along the circumferential edge interval of described second adsorption tube; Or described 3rd gas channel is annulus, and be arranged at the edge of described second adsorption tube.
7. adsorbent equipment according to claim 1, is characterized in that, described first adsorption tube is provided with two first ends be oppositely arranged, and described first gas channel is arranged between two described first ends, and described first end is outwardly.
8. adsorbent equipment according to claim 7, is characterized in that, described second adsorption tube is provided with two the second ends be oppositely arranged, and described 3rd gas channel is arranged between two described the second ends, and described the second end sets to the concave; Described the second end matches with described first end and forms described second gas channel.
9. the adsorbent equipment according to any one of claim 1-8, it is characterized in that, also comprise at least two sand core tubes, wherein described sand core tube to be arranged in described first adsorption tube and to form described first gas channel, and wherein one article of described sand core tube to be arranged in described second adsorption tube and to form described 3rd gas channel.
10., for the drying device that automobile VOC detects, it is characterized in that, comprise the adsorbent equipment described in claim 1-9.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520949411.5U CN205164432U (en) | 2015-11-24 | 2015-11-24 | Adsorption equipment and be used for drying device that car VOC detected |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520949411.5U CN205164432U (en) | 2015-11-24 | 2015-11-24 | Adsorption equipment and be used for drying device that car VOC detected |
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| Publication Number | Publication Date |
|---|---|
| CN205164432U true CN205164432U (en) | 2016-04-20 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520949411.5U Withdrawn - After Issue CN205164432U (en) | 2015-11-24 | 2015-11-24 | Adsorption equipment and be used for drying device that car VOC detected |
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| CN (1) | CN205164432U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105363316A (en) * | 2015-11-24 | 2016-03-02 | 工业和信息化部电子第五研究所 | Adsorption device and drying device for automobile VOC detection |
-
2015
- 2015-11-24 CN CN201520949411.5U patent/CN205164432U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105363316A (en) * | 2015-11-24 | 2016-03-02 | 工业和信息化部电子第五研究所 | Adsorption device and drying device for automobile VOC detection |
| CN105363316B (en) * | 2015-11-24 | 2018-01-02 | 工业和信息化部电子第五研究所 | Adsorbent equipment and the drying device for automobile VOC detections |
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|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20160420 Effective date of abandoning: 20180102 |
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| AV01 | Patent right actively abandoned |