CN221174521U - Device for comparing adsorption and catalytic degradation performances of smoke pollutants - Google Patents
Device for comparing adsorption and catalytic degradation performances of smoke pollutants Download PDFInfo
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- CN221174521U CN221174521U CN202323085259.4U CN202323085259U CN221174521U CN 221174521 U CN221174521 U CN 221174521U CN 202323085259 U CN202323085259 U CN 202323085259U CN 221174521 U CN221174521 U CN 221174521U
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- pipeline
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- actual reaction
- catalytic degradation
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- 230000015556 catabolic process Effects 0.000 title claims abstract description 20
- 230000003197 catalytic effect Effects 0.000 title claims abstract description 20
- 238000006731 degradation reaction Methods 0.000 title claims abstract description 20
- 238000001179 sorption measurement Methods 0.000 title claims abstract description 19
- 239000003344 environmental pollutant Substances 0.000 title claims abstract description 16
- 231100000719 pollutant Toxicity 0.000 title claims abstract description 16
- 239000000779 smoke Substances 0.000 title claims abstract description 14
- 238000010438 heat treatment Methods 0.000 claims abstract description 69
- 238000006243 chemical reaction Methods 0.000 claims abstract description 34
- 239000000376 reactant Substances 0.000 claims abstract description 25
- 239000007789 gas Substances 0.000 claims description 59
- 238000004321 preservation Methods 0.000 claims description 16
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 13
- 239000003546 flue gas Substances 0.000 claims description 12
- 230000000694 effects Effects 0.000 abstract description 4
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 6
- 238000013461 design Methods 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 238000009413 insulation Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- SNICXCGAKADSCV-JTQLQIEISA-N (-)-Nicotine Chemical compound CN1CCC[C@H]1C1=CC=CN=C1 SNICXCGAKADSCV-JTQLQIEISA-N 0.000 description 1
- DPZYLEIWHTWHCU-UHFFFAOYSA-N 3-ethenylpyridine Chemical compound C=CC1=CC=CN=C1 DPZYLEIWHTWHCU-UHFFFAOYSA-N 0.000 description 1
- 241000208125 Nicotiana Species 0.000 description 1
- 235000002637 Nicotiana tabacum Nutrition 0.000 description 1
- 238000004887 air purification Methods 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 235000019506 cigar Nutrition 0.000 description 1
- 235000019504 cigarettes Nutrition 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005485 electric heating Methods 0.000 description 1
- 239000003571 electronic cigarette Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229960002715 nicotine Drugs 0.000 description 1
- SNICXCGAKADSCV-UHFFFAOYSA-N nicotine Natural products CN1CCCC1C1=CC=CN=C1 SNICXCGAKADSCV-UHFFFAOYSA-N 0.000 description 1
- 230000002028 premature Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000000391 smoking effect Effects 0.000 description 1
- 235000019505 tobacco product Nutrition 0.000 description 1
- 239000012855 volatile organic compound Substances 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
- 150000003738 xylenes Chemical class 0.000 description 1
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- Investigating Or Analyzing Non-Biological Materials By The Use Of Chemical Means (AREA)
- Sampling And Sample Adjustment (AREA)
Abstract
The utility model provides a device for comparing the adsorption or catalytic degradation performance of smoke pollutants, which comprises a gas input pipeline, a comparison gas circuit pipeline, an actual reaction pipeline, a heating component and a detector, wherein the gas input pipeline is connected with the comparison gas circuit pipeline; the gas input pipeline is respectively communicated with the inlet of the comparison gas circuit pipeline and the inlet of the actual reaction pipeline through the switching valve, and the outlet of the comparison gas circuit pipeline and the outlet of the actual reaction pipeline are respectively communicated with the gas inlet of the detector; heating components are arranged outside the gas input pipeline, the comparison gas circuit pipeline and the actual reaction pipeline; the actual reaction pipeline is internally provided with reactants, so that the gas can adsorb or catalytically degrade the set target components through the reactants. The device is used for the contrast effect that a single component or a certain component in the gas component is adsorbed or catalytically degraded.
Description
Technical Field
The utility model relates to the technical field of adsorption or catalytic degradation analysis of gas components, in particular to a device for comparing adsorption or catalytic degradation performances of smoke pollutants.
Background
In the technical field of tobacco, various tobacco products, such as cigarettes, cigars, electronic cigarettes and the like, are various in gas components generated after smoking, relatively complex, and at present, corresponding analysis instruments are provided, so that the components of smoke can be analyzed in full components, the specific distribution of the smoke components can be obtained, and further a theoretical basis for processing is provided for purifying the smoke in an indoor environment.
However, the analysis scheme for the treatment effect is deficient, the currently produced indoor air purifying equipment is similar to the general air purifier principle, only the purifying filter element structure is replaced by a specific component, and the flue gas can be fully trapped under the theoretical state to purify the air, but the quantitative reference is not available, and the development of special equipment in the field is disadvantageous.
Therefore, it is necessary to design a device capable of comparing and analyzing the adsorption or catalytic degradation degree of various components in the flue gas, and also consider the influence of environmental parameters, so as to provide meaningful references for the design and modification of the air purifier, which is a practical problem to be solved by those skilled in the art, and in order to solve the above problems, an ideal technical solution is always sought.
Disclosure of utility model
The utility model aims at overcoming the defects of the prior art, and provides a device for comparing the adsorption or catalytic degradation performances of smoke pollutants, which realizes the comparison effect of adsorbing or catalytic degradation of a single component or a certain class of components in a gas component.
In order to achieve the above purpose, the technical scheme adopted by the utility model is as follows: the device for comparing the adsorption performance or the catalytic degradation performance of the smoke pollutants comprises a gas input pipeline, a comparison gas circuit pipeline, an actual reaction pipeline, a heating component and a detector;
the gas input pipeline is respectively communicated with the inlet of the comparison gas circuit pipeline and the inlet of the actual reaction pipeline through the switching valve, and the outlet of the comparison gas circuit pipeline and the outlet of the actual reaction pipeline are respectively communicated with the gas inlet of the detector;
heating components are arranged outside the gas input pipeline, the comparison gas circuit pipeline and the actual reaction pipeline;
The actual reaction pipeline is internally provided with reactants, so that the gas can adsorb or catalytically degrade the set target components through the reactants.
The switching valve is a three-way switching valve.
Based on the above, the heating component outside the gas input pipeline is a first heating component, and the first heating component is a heating belt and a heat preservation layer which are wrapped outside the pipeline.
The heating assembly outside the comparison gas circuit pipeline is a second heating assembly, and the second heating assembly is a heating belt and a heat preservation layer which are wrapped outside the pipeline.
The heating assembly outside the actual reaction pipeline is a third heating assembly, the third heating assembly comprises a heating belt and a heat preservation layer which are arranged around the pipeline part and a heating heat preservation chamber which is arranged around the reaction area of the reactant, and the heating temperature in the heating heat preservation chamber is adjustable.
The second half section of the comparison gas circuit pipeline and the second half section of the actual reaction pipeline are combined into a single output pipeline through the three-way valve, and the heating belt and the heat preservation layer are wrapped outside the output pipeline.
Based on the above, the gas outlet of the detector is connected with the tail gas treatment unit.
As described above, the region for placing the reactants is provided as a reactor, which is a pipe of unequal diameter.
Compared with the prior art, the utility model has substantial characteristics and progress, and in particular has the following advantages:
1. According to the utility model, two branch pipelines are arranged, one branch pipeline is used for comparison, the other branch pipeline is used for reaction, and the other branch pipeline is communicated with the detector, so that the gas components are fully analyzed, and the actual condition that a single component or a certain class of components in the gas components are adsorbed or catalytically degraded can be known through the comparison of the components analyzed before and after, so that a technician is helped to select specific reactants or determine the quantity of the reactants.
2. The heating component is added to control the temperature of the transmission gas and the temperature of the reaction process, so that the comparison analysis at different temperatures is realized, the actual performance of different reactants at different temperatures can be known, and a reference is provided for the parameter design of the air purification equipment containing the flue gas.
Drawings
FIG. 1 is a schematic structural diagram of the device for comparing the adsorption or catalytic degradation performance of the flue gas pollutants in example 1 of the present utility model.
In the figure: 1. a gas input conduit; 2. comparing the gas path pipelines; 3. an actual reaction pipeline; 4. a detector; 5. a tail gas treatment unit; 6. a three-way switching valve; 7. a reactor; 8. a three-way valve; 11. a first heat recovery assembly; 12. a second heating assembly; 13. a third heating assembly; 14. and heating the heat-preserving chamber.
Detailed Description
The technical scheme of the utility model is further described in detail through the following specific embodiments.
As shown in fig. 1, a device for comparing the adsorption or catalytic degradation performance of smoke pollutants comprises a gas input pipeline 1, a comparison gas circuit pipeline 2, an actual reaction pipeline 3, a heating component, a detector 4 and an exhaust gas treatment unit 5.
The gas input pipeline 1 is respectively communicated with the inlet of the comparison gas circuit pipeline 2 and the inlet of the actual reaction pipeline 3 through the three-way switching valve 6, and the outlet of the comparison gas circuit pipeline 2 and the outlet of the actual reaction pipeline 3 are respectively communicated with the gas inlet of the detector 4.
And heating components are arranged outside the gas input pipeline 1, the comparison gas circuit pipeline 2 and the actual reaction pipeline 3.
Specifically, the heating component outside the gas input pipeline 1 is a first heating component 11, the first heating component 11 is a heating belt and a heat insulation layer which are wrapped outside the pipeline, wherein the heating belt is clung to the outer wall of the gas input pipeline 1, and the heat insulation layer wraps the heating belt and the gas input pipeline 1, so that the main purpose is to ensure that the gas components are transmitted at a certain set temperature, and avoid the premature condensation or other unknown changes of certain gas components. The actual reaction pipeline is internally provided with reactants, so that the gas can adsorb or catalytically degrade the set target components through the reactants.
The heating component outside the comparison gas circuit pipeline 2 is a second heating component 12, the second heating component 12 is a heating belt and a heat preservation layer which are wrapped outside the pipeline, and the structural principle is the same as that of the first heating component 11.
The heating element outside the actual reaction pipeline 3 is the third heating element 13, because the reactant is provided in the actual reaction pipeline 3, the area for placing the reactant is set as the reactor 7, the reactor 7 is a pipeline with unequal diameters, the reactor 7 is used for storing the reactant, and because the variety of the reactant is various, the required amount is also different, so the pipeline with unequal diameters is adopted, the determination can be made according to the usage amount of the reactant, and the design purpose is that: at the small pipe diameter, a small amount of reactants can have a preset gas circulation length, so that the requirement of reaction time is met; at large pipe diameters, a large amount of reactants can be compressed into a shorter gas flow length, preventing the length from being too long and excessively large in resistance.
Therefore, the third heating assembly 13 includes a heating belt and a heat-insulating layer disposed around the pipe portion, and a heating and heat-insulating chamber 14 disposed around the reaction area of the reactant, where the heating temperature in the heating and heat-insulating chamber 14 is adjustable, and specifically, an electric heating wire may be used to heat the environment by using radiation heating, and the diameter of the heating and heat-insulating chamber 14 is larger than that of the reactor 7.
The second half section of the comparison gas circuit pipeline 2 and the second half section of the actual reaction pipeline 3 are combined into a single output pipeline through a three-way valve 8, and the output pipeline is wrapped with a heating belt and a heat preservation layer, so that the temperature of gas entering the detector is kept constant.
The detector is a conventional instrument for analyzing the components of the smoke, can acquire the specific components of the smoke, and is characterized in that the residual substances after the analysis reaction are compared with all the components which are not reacted, so that the quantity of the missing components is acquired, and the adsorption or catalytic degradation effect of certain substances and reactants in the smoke can be known under the current condition.
In particular use, to achieve quantitative contrast, the flow rate of the gas input needs to be kept stable, and then quantified according to the time of gas flow, i.e., the time of test run.
The purpose of not using the flow control component is to avoid the change of the air pressure caused by the flow control component to the flue gas, wherein the temperature is increased and lowered, so that certain interference exists.
In determining the composition of the reactants, one may choose from the more common gas constituents such as carbon monoxide, nitrogen oxides (NO, NO2, total nitrogen oxides), formaldehyde, nicotine, 3-vinylpyridine, VOCs (benzene, toluene, xylenes, TVOCs) and the like.
The heating zones used in this example were all temperature controllable, and the heating could be turned off under certain conditions, depending on the conditions required for the test.
Finally, it should be noted that the above-mentioned embodiments are only for illustrating the technical scheme of the present utility model and are not limiting; while the utility model has been described in detail with reference to the preferred embodiments, those skilled in the art will appreciate that: modifications may be made to the specific embodiments of the present utility model or equivalents may be substituted for part of the technical features thereof; without departing from the spirit of the utility model, it is intended to cover the scope of the utility model as claimed.
Claims (8)
1. A device for flue gas pollutant adsorption or catalytic degradation performance contrast, its characterized in that: the device comprises a gas input pipeline, a comparison gas circuit pipeline, an actual reaction pipeline, a heating component and a detector;
the gas input pipeline is respectively communicated with the inlet of the comparison gas circuit pipeline and the inlet of the actual reaction pipeline through the switching valve, and the outlet of the comparison gas circuit pipeline and the outlet of the actual reaction pipeline are respectively communicated with the gas inlet of the detector;
heating components are arranged outside the gas input pipeline, the comparison gas circuit pipeline and the actual reaction pipeline;
The actual reaction pipeline is internally provided with reactants, so that the gas can adsorb or catalytically degrade the set target components through the reactants.
2. The device for flue gas pollutant adsorption or catalytic degradation performance comparison according to claim 1, wherein: the switching valve is a three-way switching valve.
3. The device for flue gas pollutant adsorption or catalytic degradation performance comparison according to claim 2, wherein: the heating component outside the gas input pipeline is a first heating component, and the first heating component is a heating belt and a heat preservation layer which are wrapped outside the pipeline.
4. A device for smoke pollutant adsorption or catalytic degradation performance comparison according to claim 2 or 3, characterized in that: the heating component outside the comparison gas circuit pipeline is a second heating component, and the second heating component is a heating belt and a heat preservation layer which are wrapped outside the pipeline.
5. The device for flue gas pollutant adsorption or catalytic degradation performance comparison according to claim 4, wherein: the heating component outside the actual reaction pipeline is a third heating component, the third heating component comprises a heating belt, a heat preservation layer and a heating heat preservation chamber, the heating belt and the heat preservation layer are arranged around the pipeline part, the heating heat preservation chamber is arranged around the reaction area of the reactant, and the heating temperature in the heating heat preservation chamber is adjustable.
6. The device for flue gas pollutant adsorption or catalytic degradation performance comparison according to claim 5, wherein: the second half section of the comparison gas circuit pipeline and the second half section of the actual reaction pipeline are combined into a single output pipeline through a three-way valve, and the output pipeline is wrapped with a heating belt and a heat preservation layer.
7. The device for flue gas pollutant adsorption or catalytic degradation performance comparison according to claim 6, wherein: and an air outlet of the detector is connected with the tail gas treatment unit.
8. The device for flue gas pollutant adsorption or catalytic degradation performance comparison according to claim 1, wherein: the zone for placing the reactants is provided as a reactor, which is a pipe of unequal diameter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202323085259.4U CN221174521U (en) | 2023-11-15 | 2023-11-15 | Device for comparing adsorption and catalytic degradation performances of smoke pollutants |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202323085259.4U CN221174521U (en) | 2023-11-15 | 2023-11-15 | Device for comparing adsorption and catalytic degradation performances of smoke pollutants |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN221174521U true CN221174521U (en) | 2024-06-18 |
Family
ID=91459910
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202323085259.4U Active CN221174521U (en) | 2023-11-15 | 2023-11-15 | Device for comparing adsorption and catalytic degradation performances of smoke pollutants |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN221174521U (en) |
-
2023
- 2023-11-15 CN CN202323085259.4U patent/CN221174521U/en active Active
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| GR01 | Patent grant |