CN203672850U - Adsorption/thermal desorption sample feeding device - Google Patents
Adsorption/thermal desorption sample feeding device Download PDFInfo
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- CN203672850U CN203672850U CN201320896707.6U CN201320896707U CN203672850U CN 203672850 U CN203672850 U CN 203672850U CN 201320896707 U CN201320896707 U CN 201320896707U CN 203672850 U CN203672850 U CN 203672850U
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Abstract
The utility model relates to an adsorption/thermal desorption sample feeding device. The adsorption/thermal desorption sample feeding device comprises a multi-position valve, an enrichment tube, a chromatographic column, a flow regulating unit and a control unit, wherein a first port of the enrichment tube is connected with the multi-position valve. The adsorption/thermal desorption sample feeding device is characterized by further comprising a pressure regulating unit and a switching unit, wherein a first port and a second port of the pressure regulating unit are connected with the multi-position valve and the chromatographic column respectively; the switching unit is arranged on a flow path between a second port of the enrichment tube and the multi-position valve and connected with a third port of the pressure regulating unit; the switching unit is controlled by the control unit to enable the multi-position valve to be selectively communicated with a flow path between the second port of the enrichment tube and the third port of the pressure regulating unit; and the flow regulating unit is arranged on a flow path between a gas carrying inlet and the switching unit. The problem of pressure fluctuations produced by valve switching in a pre-desorption process is solved through the device.
Description
Technical field
The utility model relates to a kind of sampling device, especially a kind of absorption thermal desorption sampling device.
Background technology
Heat of adsorption desorb is the preconditioning technique of volatility and half volatile component in a kind of enrichment analytic sample, and the method does not need to use any organic solvent, and easy to operate, highly sensitive, detectability reaches 10
-9level.The method has been applied to the multiple fields such as environmental sample, food and drink, medicine, plant, mineralogical analysis at present, and almost any sample that contains volatile organic matter can use this technology to analyze, and has greatly expanded the analyst coverage of gas chromatography.
Heat of adsorption desorb generally comprises two processes: adsorption process and thermal desorption process.Refer to Fig. 1, adsorption process is to make it by filling the sampling pipe 20 of particular adsorbent by the volatile constituent that sampling pump 100 sucks above gas or inert carrier gas purging sample, some determined volatile matter will be adsorbed agent and optionally adsorb, thereby can reach the object of the target detection material in enriched sample.Refer to Fig. 2, thermal desorption process is exactly that heating arrangement 50 is heated the sampling pipe 20 that has adsorbed material to be detected, the material being adsorbed is desorbed, entered in gas chromatograph, separated by chromatographic column 30 and detected by detecting device 40 by inert carrier gas high pure nitrogen or the high-pure helium band of gas.Sampling pipe 20 is commonly referred to as adsorption tube or enrichment pipe.
Current common thermal desorption input mode has two kinds:
One is direct injected, refers to Fig. 2, and when sample heating, the object that carrier gas directly desorbs enrichment pipe is directly brought chromatographic column into.Because heating to desired value, enrichment pipe needs the regular hour, sample is slowly brought into chromatographic column and carrier gas meeting continues in heating process, can to cause solution to be drawn onto object peak broadening in chromatographic column comparatively serious for this input mode, causes the detection limit of method poor.
Another kind of mode comprises pre-desorption procedure, refer to Fig. 3 and Fig. 4, by a multi-position valve 60, gas circuit is switched, first to the enrichment pipe 20 pre-desorb that heats up, after balance a period of time (enrichment pipe is not flow through in now carrier gas), at high temperature first desorb of sample is cut valve after in enrichment pipe again and is carried out gas circuit switching, and moment is brought the good object of the desorb in enrichment pipe into chromatographic column 30.
This mode can improve the detection limit of whole method greatly, but pre-desorb is completely different from desorption process enrichment pipe stream of living in, can make the stream pressure jump of enrichment pipe place in the time that multi-position valve is cut valve, cause pressing fluctuation obviously before post, can affect the repeatability of sample introduction.And if in sample, contained large quantity of moisture, in pre-desorption process, because heating steam expands, in the time carrying out desorb, the temperature when pipeline temperature that sample passes through can be lower than the pre-desorb of enrichment pipe, could cause sample loss.
Summary of the invention
In order to solve above-mentioned deficiency of the prior art, the utility model provides a kind of can effectively solve the peak broadening problem occurring in thermal desorption process, avoid cutting in pre-desorption process the pressure surge problem of valve generation, and can prevent from occurring in pre-desorption process the heat of adsorption desorption apparatus of sample loss.
For realizing above-mentioned utility model object, the utility model adopts following technical scheme:
A kind of absorption thermal desorption sampling device, comprise multi-position valve, enrichment pipe, chromatographic column, flow regulating unit and control module, described enrichment pipe the first port is connected with described multi-position valve, is characterized in: described absorption thermal desorption sampling device also comprises pressure regulating unit and switch unit;
The first port of described pressure regulating unit is connected with described chromatographic column with described multi-position valve respectively with the second port;
Described switch unit is arranged on the stream between enrichment pipe the second port and multi-position valve and with the 3rd port of described pressure regulating unit and is connected;
Described switch unit under the control of control module, make multi-position valve optionally and described enrichment pipe the second port or pressure regulating unit the 3rd port between stream be connected;
Described flow regulating unit is arranged on the stream between carrier gas inlet and switch unit.
As preferably, described switch unit is connected with enrichment pipe the second port.
As preferably, described switch unit with after described multi-position valve is once connected with described enrichment pipe the second end
mouthfulbe connected.
Further, described pressure regulating unit comprises pressure transducer and proportioning valve.
Further, described flow regulating unit is mass flowmeter.
As preferably, described switch unit is T-valve.
Further, described multi-position valve is six-way valve or ten-way valve.
Further, on the stream being connected with multi-position valve in carrier gas, pressure transducer is set.
The utility model compared with prior art has following beneficial effect:
1, the flow path designs of innovation, can eliminate multi-position valve in thermal desorption sample introduction process and cut pressure surge problem in valve process, solves the sample introduction instability problem producing in current thermal desorption sample introduction process;
Can carry out stable pre-desorb sample introduction, prevent from occurring sample loss in pre-desorption process, efficiently solve the peak broadening problem occurring in thermal desorption process, can greatly improve repeatability and the detection limit of thermal desorption method;
In conjunction with multi-position valve and solenoid valve, and electronic flow and pressure control, can realize the operator scheme of multiple heat of adsorption desorb, comprise that enrichment pipe sampling, pre-desorb conciliate the various modes such as inspiration sample, meet the application under different condition.
Accompanying drawing explanation
Fig. 1 is direct injected mode sampling process schematic diagram in background technology;
Fig. 2 is direct injected mode desorption process schematic diagram in background technology;
Fig. 3 is by adopting the pre-desorb sample introduction stream schematic diagram of multi-position valve sample introduction in background technology;
Fig. 4 is by adopting the desorb sample introduction stream schematic diagram of multi-position valve sample introduction in background technology;
Fig. 5 is the sampling stream schematic diagram in embodiment 1;
Fig. 6 is the pre-desorb stream schematic diagram in embodiment 1;
Fig. 7 is the desorb stream schematic diagram in embodiment 1;
Fig. 8 is the sampling stream schematic diagram in embodiment 2;
Fig. 9 is the pre-desorb stream schematic diagram in embodiment 2;
Figure 10 is the desorb stream schematic diagram in embodiment 2;
Figure 11 is the sampling stream schematic diagram in embodiment 3;
Figure 12 is the pre-desorb stream schematic diagram in embodiment 3;
Figure 13 is the desorb stream schematic diagram in embodiment 3.
Embodiment
Embodiment 1
Refer to Fig. 5～Fig. 7, a kind of absorption thermal desorption sampling device, comprises multi-position valve 11, enrichment pipe 21, chromatographic column 31, pressure regulating unit 41, switch unit 51, flow regulating unit 61 and control module (not marking in figure).
Described in the present embodiment, multi-position valve 11 is ten-way valve;
Described enrichment pipe the first port 211 is connected with the 9th interface of described multi-position valve 11.
The first port 411 of described pressure regulating unit 41 is connected with described chromatographic column 31 with the 10th interface of described multi-position valve 11 respectively with the second port 412;
Described switch unit 51 is arranged on the stream between enrichment pipe the second port 212 and multi-position valve 11 and with the 3rd port 413 of described pressure regulating unit 41 and is connected;
Described switch unit 51 and enrichment pipe the second port 212 is directly connected or described switch unit 51 is connected with described enrichment pipe 21 second ports 212 after being connected with described multi-position valve 11 one or many again;
Described flow regulating unit 61 is arranged on the stream between carrier gas inlet 71 and switch unit 51; Described flow regulating unit 61 is mass flowmeter EFC.
Described in the present embodiment, pressure regulating unit 41 comprises pressure transducer 414 and proportioning valve 415.Described switch unit 51 is T-valve.Described switch unit 51 is directly connected with enrichment pipe the second port 212, and the R mouth of described switch unit 51 is directly connected with enrichment pipe 21 second ports 212, and A mouth is connected with the 2nd interface of multi-position valve 11, and P mouth is connected with the 3rd port 413 of pressure regulating unit 41; Flow switch unit 61 is connected with the 5th interface of carrier gas inlet 71 and multi-position valve 11.
Described switch unit 51 under the control of control module, make multi-position valve 11 optionally and described enrichment pipe 21 second ports 212 or pressure regulating unit 41 the 3rd port 413 between stream be connected.
The present embodiment also provides a kind of heat of adsorption desorb sample injection method, comprises the following steps:
A, provide the absorption thermal desorption sampling device of the present embodiment, enrichment pipe sampling
Switch unit is connected the stream between enrichment pipe the second port and multi-position valve, makes sample pass into enrichment pipe and samples, specific as follows:
Refer to Fig. 5, control module control multi-position valve 11 and switch unit 51, make that the 8th interface of multi-position valve 11 and the 9th interface are connected, the 2nd interface and interface 3 be connected, and R mouth and the A mouth of switch unit 51 are connected; The 8th interface of sample and multi-position valve 11 is connected; Meanwhile, control module control enrichment pipe sampling condition, realizes enrichment pipe sampling; State of the art when control module control enrichment pipe sampling condition carries out enrichment pipe sampling, does not repeat them here;
B, pre-desorb
Switch unit disconnect the stream between enrichment pipe the second port and multi-position valve and connect multi-position valve and pressure regulating unit the 3rd port between stream, described enrichment pipe the first port is connected with chromatographic column, carrier gas enters chromatographic column without enrichment pipe; Regulate carrier gas flux and stream pressure, make the front pressure balanced of post to consistent with the pressure under desorb sample introduction state; To enrichment pipe, heating realizes sample desorb in control module control; Specific as follows:
Refer to Fig. 6, control module control multi-position valve 11 and switch unit 51, make that the 9th interface of multi-position valve 11 and the 10th interface are connected, the 1st interface and the 2nd interface is connected, the 5th interface and the 6th interface are connected, and P mouth and the A mouth of switch unit 51 are connected;
Now, carrier gas passes into from carrier gas inlet 71, passes through successively the 5th interface, the 6th interface, the 1st interface and the 2nd interface of multi-position valve 11, the A mouth of switch unit 51 and P mouth, and the 3rd port 413 of pressure regulating unit 41, the second port 412 finally enter chromatographic column 31;
Meanwhile, control module control flow regulating unit 61 regulates carrier gas flux, pressure regulating unit 41 to regulate pressure, makes the front pressure balanced of post to consistent with the pressure under desorb sample introduction state;
Control module control realizes sample desorb to enrichment pipe heating: control module control is heated enrichment pipe 21, and now carrier gas is without enrichment pipe 21, stable being retained in enrichment pipe 21 of object that enrichment pipe 21 is desorbed under pre-desorption state;
Carrier gas is entered pressure regulating unit and is finally entered chromatographic column by A mouth and the P mouth of switch unit, although enrichment pipe is not passed through in carrier gas, but owing to being communicated with between the first port of enrichment pipe and pressure regulating unit, to make pressure in enrichment pipe and the gaseous tension of switch unit A mouth be balance to gas diffusional effect.
C, desorb sample introduction
Switch unit disconnects the stream between multi-position valve and pressure regulating unit the 3rd port and connects the stream between enrichment pipe the second port and multi-position valve, makes carrier gas pass into enrichment pipe and brings the sample in enrichment pipe into chromatographic column, specific as follows:
Refer to Fig. 7, control module control multi-position valve 11 is consistent the state in its state and step B, and the R mouth of switch unit 51 and A mouth are connected;
Now, carrier gas passes into from carrier gas inlet 71, pass through successively the 5th interface, the 6th interface, the 1st interface and the 2nd interface of multi-position valve 11, the A mouth of switch unit 51 and R mouth, the second port 212 of enrichment pipe 21, the first port 211, the 9th interface of multi-position valve 11 and the 10th interface, the first port 411 of pressure regulating unit 41, the second port 412 finally enter chromatographic column 31.
In sample introduction process, because pressing before post, balance is good, and what carrier gas can fast and stable brings sample into chromatographic column, effectively solves the peak broadening problem occurring in thermal desorption process.
In the moment of the A of switch unit mouth and enrichment pipe the second port connection, the gaseous tension fluctuation in enrichment pipe can be very little.This has just guaranteed in switch unit handoff procedure, to keep the stable of enrichment pipe internal pressure, and can prevent from occurring sample loss in pre-desorption process.
Under pre-desorb and two kinds of different conditions of sample introduction desorb, stream is pipeline of difference (the R mouth of switch unit 11 is to the pipeline between the 9th interface of multi-position valve) only, and pressure transducer and control ratio valve are placed in after enrichment pipe, can guarantee in switch unit handoff procedure, pressure surge minimum, and can reply fast, thereby guarantee good sample introduction repeatability, and improve the detection limit of method.
Refer to Fig. 8～Figure 10, a kind of absorption thermal desorption sampling device, different from the absorption thermal desorption sampling device described in embodiment 1:
1, described switch unit 52 is connected with described enrichment pipe 21 second ports 212 after being once connected with described multi-position valve 11 again, the R mouth that is described switch unit 51 is connected with multi-position valve the 1st interface, A mouth is connected with the 6th interface of multi-position valve 11, and P mouth is connected with pressure regulating unit 41; The 2nd interface of multi-position valve 11 is connected with enrichment pipe 21 second ports 212.
2, described flow regulating unit 61 is arranged between the 6th interface and the A mouth of switch unit 52 of multi-position valve 11;
The present embodiment also provides a kind of heat of adsorption desorb sample injection method, different from the heat of adsorption desorb sample injection method described in embodiment:
1,, in steps A, provide the absorption thermal desorption sampling device of the present embodiment;
Refer to Fig. 8, control module control multi-position valve 11 and switch unit 52, make that the 8th interface of multi-position valve 11 and the 9th interface are connected, the 2nd interface and interface 3 be connected, and R mouth and the A mouth of switch unit 52 are connected; The 8th interface of sample and multi-position valve 11 is connected;
2, in step B, refer to Fig. 9, carrier gas passes into from carrier gas inlet 71, passes through successively the 5th interface and the 6th interface of multi-position valve 11, the A mouth of switch unit 52 and P mouth, and the 3rd port 413 of pressure regulating unit 41, the second port 412 finally enter chromatographic column 31;
3, in step C, refer to Figure 10, carrier gas passes into from carrier gas inlet 71, pass through successively the 5th interface and the 6th interface of multi-position valve 11, the A mouth of switch unit 52 and R mouth, the 1st interface of multi-position valve 11 and the 2nd interface, enrichment pipe 21, the 9th interface of multi-position valve 11 and the 10th interface, the first port 411 of pressure regulating unit 41, the second port 412 finally enter chromatographic column 31.
Refer to Figure 11～Figure 12, a kind of absorption thermal desorption sampling device, different from the absorption thermal desorption sampling device described in embodiment 1:
1, multi-position valve 13 is six-way valves, and pressure regulating unit 43 comprises pressure transducer 434 and proportioning valve 435;
2, enrichment pipe 23 first ports 231 are connected with the 6th interface of multi-position valve 13.
The first port 431 of pressure regulating unit 43 is connected with the 1st interface, the chromatographic column 33 of described multi-position valve 13 respectively with the second port 432;
Described switch unit 53 under the control of control module, make multi-position valve 13 optionally and described enrichment pipe 23 second ports or pressure regulating unit 43 the 3rd port between stream be connected.
The present embodiment also provides a kind of heat of adsorption desorb sample injection method, different from the heat of adsorption desorb sample injection method described in embodiment:
1,, in steps A, provide the absorption thermal desorption sampling device of the present embodiment;
2, in steps A, refer to Figure 10, control module control multi-position valve 13 and switch unit 53, make that the 5th interface of multi-position valve 13 and the 6th interface are connected, interface 3 and the 4th interface is connected, and R mouth and the A mouth of switch unit 53 are connected; The 5th interface of sample and multi-position valve 13 is connected;
3, in step B, refer to Figure 11, carrier gas passes into from carrier gas inlet 73, passes through successively the 2nd interface and interface 3 of multi-position valve 13, the A mouth of switch unit 53 and P mouth, and pressure regulating unit 43 the 3rd port 433, the second port 432 finally enter chromatographic column 33;
4, in step C, refer to Figure 12, carrier gas passes into from carrier gas inlet 73, pass through successively the 2nd interface and interface 3 of multi-position valve 13, the A mouth of switch unit 53 and R mouth, enrichment pipe 23, the 6th interface of multi-position valve 13 and the 1st interface, the first port 431 of pressure regulating unit 43, the second port 432 finally enter chromatographic column 33.
The utility model is not only confined to adopt the embodiment of multi-position valve and switch unit,
Above-mentioned embodiment should not be construed as the restriction to the utility model protection domain.Key of the present utility model is: when pre-desorb by multi-position valve Pre-handoff under sample introduction state, and sample introduction pressure equilibrium is good, effectively solve the peak broadening problem occurring in thermal desorption process, avoid cutting in pre-desorption process the pressure surge problem of valve generation, and can prevent from occurring sample loss in pre-desorption process.In the situation that not departing from the utility model spirit, within any type of change that the utility model is made all should fall into protection domain of the present utility model.
Claims (8)
1. an absorption thermal desorption sampling device, comprise multi-position valve, enrichment pipe, chromatographic column, flow regulating unit and control module, described enrichment pipe the first port is connected with described multi-position valve, it is characterized in that: described absorption thermal desorption sampling device also comprises pressure regulating unit and switch unit;
The first port of described pressure regulating unit is connected with described chromatographic column with described multi-position valve respectively with the second port;
Described switch unit is arranged on the stream between enrichment pipe the second port and multi-position valve and with the 3rd port of described pressure regulating unit and is connected;
Described switch unit under the control of control module, make multi-position valve optionally and described enrichment pipe the second port or pressure regulating unit the 3rd port between stream be connected;
Described flow regulating unit is arranged on the stream between carrier gas inlet and switch unit.
2. absorption thermal desorption sampling device according to claim 1, is characterized in that: described switch unit is connected with enrichment pipe the second port.
3. absorption thermal desorption sampling device according to claim 1, is characterized in that: after described switch unit is once connected with described multi-position valve, be connected with described enrichment pipe the second port.
4. absorption thermal desorption sampling device according to claim 1, is characterized in that: described pressure regulating unit comprises pressure transducer and proportioning valve.
5. absorption thermal desorption sampling device according to claim 1, is characterized in that: described flow regulating unit is mass flowmeter.
6. absorption thermal desorption sampling device according to claim 1, is characterized in that: described switch unit is T-valve.
7. absorption thermal desorption sampling device according to claim 1, is characterized in that: described multi-position valve is six-way valve or ten-way valve.
8. absorption thermal desorption sampling device according to claim 1, is characterized in that: on the stream being connected with multi-position valve in carrier gas, pressure transducer is set.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201320896707.6U CN203672850U (en) | 2013-12-31 | 2013-12-31 | Adsorption/thermal desorption sample feeding device |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201320896707.6U CN203672850U (en) | 2013-12-31 | 2013-12-31 | Adsorption/thermal desorption sample feeding device |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103760283A (en) * | 2013-12-31 | 2014-04-30 | 聚光科技(杭州)股份有限公司 | Adsorption and thermal desorption feeding device and method |
| CN109507276A (en) * | 2018-12-20 | 2019-03-22 | 汉威科技集团股份有限公司 | A kind of novel environmental air TVOC on-line monitoring system |
-
2013
- 2013-12-31 CN CN201320896707.6U patent/CN203672850U/en not_active Withdrawn - After Issue
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103760283A (en) * | 2013-12-31 | 2014-04-30 | 聚光科技(杭州)股份有限公司 | Adsorption and thermal desorption feeding device and method |
| CN103760283B (en) * | 2013-12-31 | 2015-11-25 | 聚光科技(杭州)股份有限公司 | A kind of absorption thermal desorption sampling device and method |
| CN109507276A (en) * | 2018-12-20 | 2019-03-22 | 汉威科技集团股份有限公司 | A kind of novel environmental air TVOC on-line monitoring system |
| CN109507276B (en) * | 2018-12-20 | 2024-05-31 | 汉威科技集团股份有限公司 | Novel ambient air TVOC on-line monitoring system |
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Granted publication date: 20140625 Effective date of abandoning: 20151125 |
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