CN114870838A - Hydrogen sensor catalyst, preparation method thereof and hydrogen sensor - Google Patents

Hydrogen sensor catalyst, preparation method thereof and hydrogen sensor Download PDF

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Publication number
CN114870838A
CN114870838A CN202210653263.7A CN202210653263A CN114870838A CN 114870838 A CN114870838 A CN 114870838A CN 202210653263 A CN202210653263 A CN 202210653263A CN 114870838 A CN114870838 A CN 114870838A
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Prior art keywords
hydrogen sensor
carrier
sensor catalyst
nitrate
hydrogen
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Chinese (zh)
Inventor
靳亚龙
穆庆辉
吴勐
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Shanghai Songbai Sensor Technology Co ltd
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Shanghai Songbai Sensor Technology Co ltd
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/54Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/56Platinum group metals
    • B01J23/63Platinum group metals with rare earths or actinides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/10Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of rare earths
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00Catalysts comprising molecular sieves
    • B01J29/04Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/40Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively
    • B01J29/48Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively containing arsenic, antimony, bismuth, vanadium, niobium tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N27/00Investigating or analysing materials by the use of electric, electrochemical, or magnetic means
    • G01N27/02Investigating or analysing materials by the use of electric, electrochemical, or magnetic means by investigating impedance
    • G01N27/04Investigating or analysing materials by the use of electric, electrochemical, or magnetic means by investigating impedance by investigating resistance
    • G01N27/14Investigating or analysing materials by the use of electric, electrochemical, or magnetic means by investigating impedance by investigating resistance of an electrically-heated body in dependence upon change of temperature
    • G01N27/16Investigating or analysing materials by the use of electric, electrochemical, or magnetic means by investigating impedance by investigating resistance of an electrically-heated body in dependence upon change of temperature caused by burning or catalytic oxidation of surrounding material to be tested, e.g. of gas
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2229/00Aspects of molecular sieve catalysts not covered by B01J29/00
    • B01J2229/10After treatment, characterised by the effect to be obtained
    • B01J2229/18After treatment, characterised by the effect to be obtained to introduce other elements into or onto the molecular sieve itself
    • B01J2229/186After treatment, characterised by the effect to be obtained to introduce other elements into or onto the molecular sieve itself not in framework positions

Abstract

The invention relates to a hydrogen sensor catalyst, a preparation method thereof and a hydrogen sensor 2 O 3 One of ZSM-5 or nano silicon oxide, and the carrier is modified by using the nitrate of lanthanide and actinide; the active component is one or more of salts or acids of ruthenium, rhodium, palladium, osmium, iridium or platinum, and the catalyst enables the hydrogen sensor to have almost no response to methane, has obvious response to hydrogen and has high selectivity to hydrogen.

Description

Hydrogen sensor catalyst, preparation method thereof and hydrogen sensor
Technical Field
The invention belongs to the technical field of gas measurement sensors, and particularly relates to a hydrogen sensor catalyst, a preparation method thereof and a hydrogen sensor.
Background
A catalytic combustion type gas sensor is a sensor for detecting combustible gas. The catalytic combustion gas sensor consists of a small sphere of about 1mm in size, made up of a platinum wire coil wrapped with a catalyst. During normal work, the platinum silk circular telegram heats the bobble to certain operating temperature, and when combustible gas exists, the oxidation reaction can take place on the catalyst for the combustible gas body, and the heat that the oxidation reaction produced can heat the platinum silk to change the resistance value of platinum silk, and then realize surveying combustible gas's function. The main component of the catalyst is alumina supported noble metal material.
Hydrogen is a combustible gas and therefore can be detected using this type of gas sensor, but current catalytic combustion gas sensors cannot distinguish whether the gas being measured is methane or hydrogen, i.e., current catalytic combustion gas sensors cannot achieve high selectivity for hydrogen.
Disclosure of Invention
The invention aims to provide a hydrogen sensor catalyst to improve the sensitivity of hydrogen detection.
Another object of the present invention is to provide a method for preparing a hydrogen sensor catalyst.
It is a third object of the present invention to provide a hydrogen sensor
In order to achieve the above purpose, the invention adopts the technical scheme that:
a hydrogen sensor catalyst comprises a carrier and an active component, wherein the carrier is one of gamma-Al 2O3, ZSM-5 or nano silicon oxide, and the carrier is modified by using nitrate of actinide elements; the active component is palladium, platinum and one of ruthenium, rhodium, osmium and iridium.
Preferably, the active ingredient accounts for 4-5.5% of the mass of the carrier.
Preferably, the nitrate of the actinide accounts for 1.8-2.5% of the mass of the carrier.
The preparation method of the hydrogen sensor catalyst comprises the following steps:
1) dissolving nitrate of actinide elements in water to prepare a nitrate solution, then mixing the nitrate solution and the carrier uniformly, standing for 24-72 h, drying, then baking, and obtaining a modified carrier after baking is finished;
2) preparing active solution from salt or acid of the active component and solution water, mixing the active solution and the modified carrier, uniformly stirring, standing for 24-72 h, drying, baking, and finishing baking.
Preferably, the mass concentration of the nitrate aqueous solution is 6-8.3 g.L -1
Preferably, the active solution is a mixture of aqueous solutions of ammonium chloropalladate, chloroplatinic acid and iridium chloride, and the mass concentrations of the ammonium chloropalladate, the chloroplatinic acid and the iridium chloride are respectively 5-13.3 g.L -1 、100~130g.L -1 、5~26.7g.L -1
Preferably, the drying in the step 1) is carried out for 24-72 hours at the temperature of 100-200 ℃, and the baking is carried out for 2-6 hours at the temperature of 400-800 ℃.
Preferably, the drying in the step 2) is carried out for 24-72 hours at the temperature of 100-200 ℃, and the baking is carried out for 2-6 hours at the temperature of 400-800 ℃.
A hydrogen sensor comprising the hydrogen sensor catalyst.
The invention has the beneficial effects that:
according to the hydrogen sensor, the active component and the carrier are mixed to prepare the catalyst, so that the catalyst has almost no response to methane, has obvious response to hydrogen, and is high in selectivity of the hydrogen sensor to hydrogen.
Drawings
FIG. 1 shows the response of a commercially available catalytic combustion gas sensor and a hydrogen sensor of example 1 to hydrogen;
FIG. 2 shows the results of the response of a commercially available catalytic combustion gas sensor and the hydrogen sensor of example 1 to methane.
Detailed Description
The present invention will be further described with reference to the following examples and accompanying drawings.
Example 1
The hydrogen sensor catalyst comprises a carrier and an active component, wherein the carrier is gamma-Al 2 O 3 The support was modified with thorium nitrate. The active component is a mixture of ammonium chloropalladate, chloroplatinic acid and iridium chlorideThe atomic ratio of palladium, platinum and iridium was 1:7:2, and the total supporting amount was 20%.
The preparation method of the hydrogen sensor catalyst of the embodiment includes the following steps:
1) weighing 0.25g of thorium nitrate and dissolving in 30mL of water to obtain a thorium nitrate solution.
2) 10g of commercially available gamma-Al was weighed 2 O 3 And put into a beaker.
3) Pouring the thorium nitrate solution obtained in the step 1) into the gamma-Al weighed in the step 2) 2 O 3 Uniformly stirring, standing for 24h at 25 ℃, drying in a 100 ℃ oven for 24h, roasting in a muffle furnace at the temperature rise rate of 5 ℃/min from room temperature to 500 ℃, and continuously roasting at 500 ℃ for 4h to obtain thorium-modified gamma-Al 2 O 3
4) 0.4g of ammonium chloropalladate, 3.9g of chloroplatinic acid and 0.8g of iridium chloride are weighed and dissolved in 30mL of water to obtain an active component solution.
5) Weighing 10g of thorium modified gamma-Al obtained in the step 3) 2 O 3 And put into a beaker.
6) Pouring the active component solution obtained in the step 4) into the thorium modified gamma-Al weighed in the step 5) 2 O 3 And uniformly stirring, standing for 24h at 25 ℃, drying in a 100 ℃ oven for 24h, roasting in a muffle furnace at the temperature rise rate of 5 ℃/min, raising the temperature from room temperature to 500 ℃, and continuously roasting at 500 ℃ for 4h to obtain the hydrogen sensor catalyst.
The hydrogen sensor catalyst of the present example, that is, the hydrogen sensor catalyst prepared by the method of preparing the hydrogen sensor catalyst of the present example.
The hydrogen sensor of this example was obtained by mixing the hydrogen sensor catalyst of this example with deionized water to form a slurry and coating the slurry on the surface of a platinum wire.
Example 2
The hydrogen sensor catalyst comprises a carrier and an active component, wherein the carrier is gamma-Al 2 O 3 The carrier is modified by praseodymium nitrate. The active component is a mixture of ammonium chloropalladate, chloroplatinic acid and iridium chlorideThe atomic ratio of palladium, platinum and ruthenium was 0.5:8:1.5, and the total supporting amount was 15%.
The preparation method of the hydrogen sensor catalyst of the embodiment includes the following steps:
1) 0.2g of praseodymium nitrate is weighed and dissolved in 30mL of water to obtain a praseodymium nitrate solution.
2) 10g of commercially available gamma-Al was weighed 2 O 3 And put into a beaker.
3) Pouring the praseodymium nitrate solution obtained in the step 1) into the gamma-Al weighed in the step 2) 2 O 3 Uniformly stirring, standing for 24h at 25 ℃, drying in an oven at 150 ℃ for 24h, roasting in a muffle furnace at a heating rate of 5 ℃/min from room temperature to 600 ℃, and continuously roasting at 600 ℃ for 4h to obtain thorium-modified gamma-Al 2 O 3
4) 0.12g of ammonium chloropalladate, 2.79g of chloroplatinic acid and 0.03g of ruthenium chloride are weighed and dissolved in 30mL of water to obtain an active component solution.
5) Weighing 10g of thorium modified gamma-Al obtained in the step 3) 2 O 3 And put into a beaker.
6) Pouring the active component solution obtained in the step 4) into the thorium modified gamma-Al weighed in the step 5) 2 O 3 And uniformly stirring, standing for 24h at 25 ℃, drying in a 100 ℃ oven for 24h, roasting in a muffle furnace at the temperature rise rate of 5 ℃/min from room temperature to 600 ℃, and continuously roasting at 600 ℃ for 4h to obtain the hydrogen sensor catalyst.
The hydrogen sensor catalyst of the present example, that is, the hydrogen sensor catalyst prepared by the method of preparing the hydrogen sensor catalyst of the present example.
The hydrogen sensor of this example was obtained by mixing the hydrogen sensor catalyst of this example with deionized water to form a slurry and coating the slurry on the surface of a platinum wire.
Example 3
The hydrogen sensor catalyst comprises a carrier and an active component, wherein the carrier is gamma-Al 2 O 3 The support was modified with thorium nitrate. The active components are mixture of ammonium chloropalladate, chloroplatinic acid and iridium chlorideThe atomic ratio of palladium, platinum and iridium was 1:7:0.5, and the total supporting amount was 16%.
The preparation method of the hydrogen sensor catalyst of the embodiment includes the following steps:
1) weighing 0.18g of thorium nitrate and dissolving in 30mL of water to obtain a thorium nitrate solution.
2) 10g of commercially available gamma-Al was weighed 2 O 3 And put into a beaker.
3) Pouring the thorium nitrate solution obtained in the step 1) into the gamma-Al weighed in the step 2) 2 O 3 Uniformly stirring, standing for 24h at 25 ℃, drying in a 100 ℃ oven for 48h, roasting in a muffle furnace at the temperature rise rate of 5 ℃/min from room temperature to 400 ℃, and continuously roasting at 400 ℃ for 2h to obtain thorium-modified gamma-Al 2 O 3
4) 0.3g of ammonium chloropalladate, 3.6g of chloroplatinic acid and 0.15g of iridium chloride are weighed and dissolved in 30mL of water to obtain an active component solution.
5) Weighing 10g of thorium modified gamma-Al obtained in the step 3) 2 O 3 And put into a beaker.
6) Pouring the active component solution obtained in the step 4) into the thorium modified gamma-Al weighed in the step 5) 2 O 3 And (3) uniformly stirring, standing for 24h at 25 ℃, then placing into a 100 ℃ oven for drying for 48h, then roasting in a muffle furnace at the heating rate of 5 ℃/min, heating from room temperature to 400 ℃, and then continuously roasting for 2h at 400 ℃ to obtain the hydrogen sensor catalyst.
The hydrogen sensor catalyst of the present example, that is, the hydrogen sensor catalyst prepared by the method of preparing the hydrogen sensor catalyst of the present example.
The hydrogen sensor of this example was obtained by mixing the hydrogen sensor catalyst of this example with deionized water to form a slurry and coating the slurry on the surface of a platinum wire.
Example 4
The hydrogen sensor catalyst comprises a carrier and an active component, wherein the carrier is gamma-Al 2 O 3 The carrier is modified by praseodymium nitrate. The active components are ammonium chloropalladate, chloroplatinic acid and iridium chlorideThe atomic ratio of palladium, platinum and ruthenium in the mixture was 1:7:3, and the total supporting amount was 18%.
The preparation method of the hydrogen sensor catalyst of the embodiment includes the following steps:
1) 0.2g of praseodymium nitrate is weighed and dissolved in 30mL of water to obtain a praseodymium nitrate solution.
2) 10g of commercially available gamma-Al was weighed 2 O 3 And put into a beaker.
3) Pouring the praseodymium nitrate solution obtained in the step 1) into the gamma-Al weighed in the step 2) 2 O 3 Uniformly stirring, standing for 24h at 25 ℃, drying for 72h in a 100 ℃ oven, roasting in a muffle furnace at the temperature rise rate of 5 ℃/min from room temperature to 800 ℃, and continuously roasting for 6h at 800 ℃ to obtain thorium-modified gamma-Al 2 O 3
4) 0.4g of ammonium chloropalladate, 3.6g of chloroplatinic acid and 0.6g of ruthenium chloride are weighed and dissolved in 30mL of water to obtain an active component solution.
5) Weighing 10g of thorium modified gamma-Al obtained in the step 3) 2 O 3 And put into a beaker.
6) Pouring the active component solution obtained in the step 4) into the thorium modified gamma-Al weighed in the step 5) 2 O 3 And uniformly stirring, standing for 24h at 25 ℃, drying in a 100 ℃ oven for 24h, roasting in a muffle furnace at the temperature rise rate of 5 ℃/min, raising the temperature from room temperature to 800 ℃, and continuously roasting at 800 ℃ for 6h to obtain the hydrogen sensor catalyst.
The hydrogen sensor catalyst of the present example, that is, the hydrogen sensor catalyst prepared by the method of preparing the hydrogen sensor catalyst of the present example.
The hydrogen sensor of this example was obtained by mixing the hydrogen sensor catalyst of this example with deionized water to form a slurry and coating the slurry on the surface of a platinum wire.
Examples of the experiments
The results of identifying hydrogen and methane using the hydrogen sensor of example 1 and a commercially available hydrogen sensor are shown in fig. 1 and 2, respectively.

Claims (9)

1. A kind ofThe hydrogen sensor catalyst comprises a carrier and an active component, and is characterized in that the carrier is gamma-Al 2 O 3 The carrier is modified by using nitrate of actinide elements; the active component is a mixture of palladium, platinum and an element A, wherein the element A is one of ruthenium, rhodium, osmium or iridium.
2. The hydrogen sensor catalyst according to claim 1, wherein the active component accounts for 4 to 5.5% by mass of the carrier.
3. The hydrogen sensor catalyst according to claim 1, wherein the actinide nitrate accounts for 1.8 to 2.5% by mass of the carrier.
4. The method for preparing a hydrogen sensor catalyst according to claim 1, comprising the steps of:
1) dissolving nitrate of actinide elements in water to prepare a nitrate solution, then mixing the nitrate solution and the carrier uniformly, standing for 24-72 h, drying, then baking, and obtaining a modified carrier after baking is finished;
2) preparing active solution from salt or acid of the active component and solution water, mixing the active solution and the modified carrier, uniformly stirring, standing for 24-72 h, drying, baking, and finishing baking.
5. The method for preparing the hydrogen sensor catalyst according to claim 4, wherein the mass concentration of the nitrate aqueous solution is 6 to 8.3g.L -1
6. The method for preparing the hydrogen sensor catalyst according to claim 4, wherein the active solution is a mixture of ammonium chloropalladate, chloroplatinic acid, a salt of the element A or an aqueous solution of acid, and the mass concentration of the ammonium chloropalladate, the chloroplatinic acid, the salt of the element A or the acid is 5-13.3 g.L -1 、100~130g.L -1 、5~26.7g.L -1
7. The preparation method of the hydrogen sensor catalyst according to claim 4, wherein the drying in the step 1) is performed at 100-200 ℃ for 24-72 h, and the baking is performed at 400-800 ℃ for 2-6 h.
8. The method for preparing the hydrogen sensor catalyst according to claim 4, wherein the drying in the step 2) is performed at 100-200 ℃ for 24-72 hours, and the baking is performed at 400-800 ℃ for 2-6 hours.
9. A hydrogen sensor comprising the hydrogen sensor catalyst according to claim 1.
CN202210653263.7A 2022-06-09 2022-06-09 Hydrogen sensor catalyst, preparation method thereof and hydrogen sensor Pending CN114870838A (en)

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005321215A (en) * 2004-05-06 2005-11-17 Tokyo Gas Co Ltd Catalytic combustion type gas sensor
JP2006112894A (en) * 2004-10-14 2006-04-27 Matsushita Electric Ind Co Ltd Hydrogen gas sensor
JP2007327806A (en) * 2006-06-07 2007-12-20 Ngk Spark Plug Co Ltd Catalytic combustion type gas sensor, and gas detector
DE102007033113A1 (en) * 2007-07-13 2009-01-15 Bayer Technology Services Gmbh Stable, high activity hydrogen chloride oxidation catalyst, for producing chlorine, comprises active component supported on carrier based on uranium compound
US20140072493A1 (en) * 2011-03-04 2014-03-13 Umicore Shokubai Usa Inc. Catalyst for exhaust gas purification, method for producing the same, and exhaust gas purification method using the same

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005321215A (en) * 2004-05-06 2005-11-17 Tokyo Gas Co Ltd Catalytic combustion type gas sensor
JP2006112894A (en) * 2004-10-14 2006-04-27 Matsushita Electric Ind Co Ltd Hydrogen gas sensor
JP2007327806A (en) * 2006-06-07 2007-12-20 Ngk Spark Plug Co Ltd Catalytic combustion type gas sensor, and gas detector
DE102007033113A1 (en) * 2007-07-13 2009-01-15 Bayer Technology Services Gmbh Stable, high activity hydrogen chloride oxidation catalyst, for producing chlorine, comprises active component supported on carrier based on uranium compound
US20140072493A1 (en) * 2011-03-04 2014-03-13 Umicore Shokubai Usa Inc. Catalyst for exhaust gas purification, method for producing the same, and exhaust gas purification method using the same
CN107413336A (en) * 2011-03-04 2017-12-01 优美科触媒日本有限公司 Exhaust gas purification catalyst, its preparation method and the exhaust gas purifying method using the catalyst

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