CN107159262B - Room temperature removes formaldehyde gas Pd/CuxThe preparation method of O@GO composite catalyst - Google Patents

Room temperature removes formaldehyde gas Pd/CuxThe preparation method of O@GO composite catalyst Download PDF

Info

Publication number
CN107159262B
CN107159262B CN201710486313.6A CN201710486313A CN107159262B CN 107159262 B CN107159262 B CN 107159262B CN 201710486313 A CN201710486313 A CN 201710486313A CN 107159262 B CN107159262 B CN 107159262B
Authority
CN
China
Prior art keywords
solution
composite catalyst
formaldehyde
concentration
preparation
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201710486313.6A
Other languages
Chinese (zh)
Other versions
CN107159262A (en
Inventor
徐志花
严朝雄
刘继延
杨志华
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Jianghan University
Original Assignee
Jianghan University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Jianghan University filed Critical Jianghan University
Priority to CN201710486313.6A priority Critical patent/CN107159262B/en
Publication of CN107159262A publication Critical patent/CN107159262A/en
Application granted granted Critical
Publication of CN107159262B publication Critical patent/CN107159262B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • 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
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/89Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
    • B01J23/8926Copper and noble metals
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86Catalytic processes
    • B01D53/8668Removing organic compounds not provided for in B01D53/8603 - B01D53/8665

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Catalysts (AREA)

Abstract

The invention discloses a kind of room temperatures to remove formaldehyde gas Pd/CuxThe preparation method of O@GO composite catalyst, copper salt solution and GO solution are mixed and to form solution A;Palladium salt solution, solvable alkali and reducing solution are sequentially added in solution A, form B solution;C solution is obtained after B solution is carried out hydro-thermal reaction, the solid in C solution obtains Pd/Cu through centrifuge washing, drying, grindingxO@GO composite catalyst.Using one step hydro thermal method by Pd in-situ deposition in CuxOn O@GO carrier, be conducive to close contact of each component on nanoscale, enhance Pd/CuxThe reactivity of O@GO composite catalyst, without high-temperature calcination or roasting, step is few, it is easy to operate, the upper Surface oxygen-containing groups abundant of GO can improve the absorption property of catalyst PARA FORMALDEHYDE PRILLS(91,95), the further oxidation for being conducive to oxidation of formaldehyde intermediate product converts the formaldehyde of high concentration comparatively fast within a short period of time and decomposes, and concentration quickly reduces.

Description

Room temperature removes formaldehyde gas Pd/CuxThe preparation method of O@GO composite catalyst
Technical field
The invention belongs to nanocatalyst preparation technical field, specifically a kind of room temperature removes formaldehyde gas Pd/CuxO@ The preparation method of GO composite catalyst.
Background technique
Indoor concentration of formaldehyde is high after house decoration, and harm to the human body is serious.The method of existing removal formaldehyde has physics Absorption method, chemiadsorption, photocatalytic degradation method and plasma method etc., room temperature catalytic oxidation method are not necessarily to extra means and energy Carbon dioxide and water can be oxidized the formaldehyde into, environmental protection and energy saving are high-efficient.Effective catalyst is then in room temperature catalytic oxidation method New and effective carried noble metal catalysis can be made by changing carrier person's character, micro-structure and surface chemical property in key Agent.
In the prior art have room temperature catalytic oxidation method removal formaldehyde catalyst be made, such as application No. is 200710121423.9 Chinese patent provides " a kind of catalyst of complete oxidation of formaldehyde at room temperature ", by porosity without Machine oxide carrier, noble metal component and adjuvant component three parts composition;Porous inorganic oxide carrier is ceria, two Zirconium oxide, titanium dioxide, aluminum oxide, stannic oxide, silica, lanthanum sesquioxide, magnesia, zinc oxide therein one Kind or more than one mixtures or its composite oxides, zeolite, sepiolite, porosity Carbon Materials;Catalyst noble metal group is divided into At least one of platinum, rhodium, palladium, gold, silver, adjuvant component are at least one of alkali metal lithium, sodium, potassium, rubidium, caesium, wherein catalyst Used in noble metal component by metal element wt conversion based on load capacity be 0.1-10%, preferably 0.3-2%, the invention Catalyst roasted in the preparation, maturing temperature be 200~700 DEG C, surface holes abundant can be just obtained after roasting The composite catalyst of structure.
Summary of the invention
The object of the present invention is to provide a kind of room temperatures to remove formaldehyde gas Pd/CuxThe preparation method of O@GO composite catalyst, Preparation method is simple, it is only necessary to the preparation of one step hydro thermal method then achievable composite catalyst;The Pd/Cu of preparationxO@GO is compound to be urged Agent activity is high, can be by the formaldehyde of high concentration fast decoupled in a short time.
To achieve the above object, the technical solution adopted by the present invention is that: a kind of room temperature removes formaldehyde gas Pd/CuxO@GO The preparation method of composite catalyst, comprising the following steps:
1) copper salt solution and GO solution are mixed and forms solution A;Sequentially added in solution A palladium salt solution, solvable alkali and Reducing solution forms B solution;
2) C solution is obtained after B solution being carried out hydro-thermal reaction, the solid in C solution is obtained through centrifuge washing, drying, grinding Obtain Pd/CuxO@GO composite catalyst.
Further, in step 1) copper salt solution and GO solution with mass concentration ratio for 6.67~33.33:2.9, volume ratio It mixes to form solution A for 30:7.
Specifically, mantoquita is one of copper acetate, copper chloride or copper sulphate, and palladium salt is palladium chloride or palladium acetate, solvable Alkali is NaOH or KOH, reducing solution NaBH4Solution or KBH4Solution.
Further, the mass concentration of palladium salt solution is 8~10g/L, the molar concentration of reducing solution is 0.1~ The mass ratio of 0.5mol/L, solvable alkali and mantoquita is 1:1.
Still further, mantoquita and the mass ratio of palladium salt are 0.20~1.0:0.024.
Further, the time of hydro-thermal reaction is 8~12h in step 2), and temperature is 120~200 DEG C.
Further, temperature dry in step 2) is 75~95 DEG C, and the dry time is 8~12h.
1) present invention uses one step hydro thermal method by Pd in-situ deposition in CuxOn O@GO (graphene oxide) carrier, without height Temperature calcining or roasting, step is few, easy to operate;2) Pd in-situ deposition is in CuxOn O@GO carrier, be conducive to each component in nanoscale On close contact, enhance Pd/CuxThe reactivity of O@GO composite catalyst;3) GO Surface oxygen-containing groups rich in, this A little oxygen-containing functional groups can not only improve the absorption property of catalyst PARA FORMALDEHYDE PRILLS(91,95), also help the further of oxidation of formaldehyde intermediate product Oxidation converts the formaldehyde of high concentration comparatively fast within a certain period of time and decomposes, and concentration quickly reduces.
Detailed description of the invention
Fig. 1 is Pd/Cu prepared by the present inventionxThe XRD spectra of O@GO composite catalyst.
Fig. 2 is Pd/Cu prepared by the present inventionxThe SEM figure (Fig. 2 (a)) and EDS spectrogram (Fig. 2 of O@GO composite catalyst (b))。
Fig. 3 is to use Pd/Cu prepared by the present invention at room temperaturexThe Pd/ Cu of O@GO composite catalyst and two-step method preparationxO@ The effect picture of GO composite catalyst PARA FORMALDEHYDE PRILLS(91,95) catalysis.
Fig. 4 is Pd/Cu prepared by the present inventionxO@GO composite catalyst is reused many times pair of room temperature removal formaldehyde efficiency Than figure.
Specific embodiment
Below with reference to preferred embodiment, invention is further described in detail, convenient for more clearly understanding this Invention, but the present invention is not limited to following specific embodiments.
The selection of reactant: the present invention uses CuxO is as Pd/CuxOne of the component of O@GO composite catalyst, CuxIn O Cu element be+1 or+divalent, the Cu of+1 valence2O has oxidation and reduction characteristic simultaneously, which can make CuxO carrier and your gold Belonging between Pd has strong interaction, to be conducive to enhance composite catalyst activity.The surface layered graphite oxide alkene (GO) Containing a large amount of oxygen-containing functional groups, such as hydroxyl, carboxyl, epoxy group, these oxygen-containing groups pass through hydrogen bond action formaldehyde adsorption molecule, To be conducive to the enrichment of formaldehyde molecule on a catalyst.
The invention belongs to one-step method, the one-step method refers to that mixed solution can directly be made by one step hydro thermal method and urges Agent.
A kind of room temperature of the present invention removes formaldehyde gas Pd/CuxThe preparation method of O@GO composite catalyst, including following step It is rapid:
1) by copper salt solution and GO solution with mass concentration ratio for 6.67~33.33:2.9, volume ratio is that 30:7 mixes shape At solution A;The reproducibility that the palladium salt solution of 8~10g/L, solvable alkali and 0.1~0.5 mol/L are sequentially added in solution A is molten Liquid forms B solution;Mantoquita can be one of for copper acetate, copper chloride or copper sulphate, and palladium salt is palladium chloride or palladium acetate, can Molten alkali is NaOH or KOH, reducing solution NaBH4Solution or KBH4Solution;The mass ratio of solvable alkali and mantoquita is 1:1, mantoquita Mass ratio with palladium salt is 0.20~1.0:0.024;
2) B solution is obtained into C solution after temperature is 120~200 DEG C of 8~12h of progress hydro-thermal reaction, consolidating in C solution Body obtains Pd/Cu through 8~12h dry at centrifuge washing, 75~95 DEG C, grindingxO@GO composite catalyst.
In following preferred embodiments, mantoquita selects copper acetate, and copper chloride, copper sulphate have comparable effect to imitate Fruit repeats no more in the description;Palladium salt selects palladium chloride, and palladium acetate has comparable function and effect, no longer superfluous in the description It states;Solvable alkali selects NaOH, KOH to have comparable effect, repeat no more in the description;Reducing solution is NaBH4Solution, KBH4Solution has comparable function and effect, repeats no more in the description.
Embodiment 1
By 0.25g Cu (Ac)2It is dissolved in 30mL water, the GO solution that 7mL concentration is 2.9g/L is then added, fills it It is uniformly dispersed to form solution A;The PdCl that 3mL concentration is 8g/L is added in solution A2Solution adds 0.25g NaOH, so The NaBH that 5mL concentration is 0.1mol/L is added afterwards4Solution continues to stir evenly to form B solution;B solution is transferred to water heating kettle In, 12h, which is reacted, at 180 DEG C obtains C solution;Solid in C solution is through centrifuge washing, and dry 8h is to drying at 80 DEG C, grinding After obtain Pd/CuxO@GO composite catalyst.
The Pd/Cu for taking above-described embodiment 1 to preparexO@GO composite catalyst 0.10g is placed in surface plate, extremely by the surface plate In the organic glass reactor of 5.9L, glass cover is covered.Reactor bottom places the fan of a 5W, will be certain density dense Formalin is injected in reactor, and formaldehyde volatilization is until concentration balance, and the initial concentration after formaldehyde balances is 244.2ppm, by glass Glass lid is removed, at this time Pd/CuxO@GO composite catalyst contacts with each other with formaldehyde gas and is reacted, the concentration variation of formaldehyde It is monitored on-line by Multi-Component Gas Analyzing instrument (INNOVA air Tech Instruments Model 1412), reaction After 111min, concentration of formaldehyde 70.2ppm, formaldehyde removal rate is 71.3%.
Embodiment 2
By 0.20g Cu (Ac)2It is dissolved in 30mL water, the GO solution that 7mL concentration is 2.9g/L is then added, fills it It is uniformly dispersed to form solution A;The PdCl that 2.4mL concentration is 10g/L is added in solution A2Solution adds 0.20g Then the NaBH that 10mL concentration is 0.1mol/L is added in NaOH4Solution continues to stir evenly to form B solution;B solution is shifted Into water heating kettle, 12h is reacted at 120 DEG C and obtains C solution;Dry 9h is extremely through centrifuge washing, at 80 DEG C for solid in C solution Drying, obtains Pd/Cu after grindingxO@GO catalyst.
Pd/Cu prepared by above-described embodiment 2xO@GO composite catalyst 0.10g is placed in surface plate, extremely by the surface plate In the organic glass reactor of 5.9L, glass cover is covered.Reactor bottom places the fan of a 5W, will be certain density dense Formalin is injected in reactor, and formaldehyde volatilization is until concentration balance, and the initial concentration after formaldehyde balances is 243.5ppm, by glass Glass lid is removed, Pd/CuxO@GO composite catalyst contacts with each other with formaldehyde gas and is reacted, and the concentration variation of formaldehyde passes through Multi-Component Gas Analyzing instrument (INNOVA air Tech Instruments Model 1412) on-line monitoring, reacts 111min Afterwards, concentration of formaldehyde 75.6ppm, formaldehyde removal rate are 69.0%.
Embodiment 3
By 0.5g Cu (Ac)2It is dissolved in 30mL water, the GO solution that 7mL concentration is 2.9g/L is then added, make it sufficiently It is uniformly dispersed to form solution A;The PdCl that 3mL concentration is 8g/L is added in solution A2Solution adds 0.5g NaOH, then The NaBH that 1mL concentration is 0.5mol/L is added4Solution continues to stir evenly to form B solution;B solution is transferred in water heating kettle, 12h is reacted at 180 DEG C obtains C solution;Solid in C solution is through centrifuge washing, and dry 10h is to drying at 80 DEG C, after grinding Obtain Pd/CuxO@GO catalyst.
Pd/Cu prepared by above-described embodiment 3xO@GO composite catalyst 0.10g is placed in surface plate, extremely by the surface plate In the organic glass reactor of 5.9L, glass cover is covered.Reactor bottom places the fan of a 5W, will be certain density dense Formalin is injected in reactor, and formaldehyde volatilization is until concentration balance, and the initial concentration after formaldehyde balances is 247ppm, by glass Lid is removed, Pd/CuxO@GO composite catalyst contacts with each other with formaldehyde gas and is reacted, and the concentration variation of formaldehyde passes through more Component gas analyzer (INNOVA air Tech Instruments Model 1412) on-line monitoring, after reacting 111min, Concentration of formaldehyde is 165.7ppm, and formaldehyde removal rate is 32.9%.
Embodiment 4
By 0.75g Cu (Ac)2It is dissolved in 30mL water, the GO solution that 7mL concentration is 2.9g/L is then added, fills it It is uniformly dispersed to form solution A;The PdCl that 3mL concentration is 8g/L is added in solution A2Solution adds 0.75g NaOH, so The NaBH that 5mL concentration is 0.1mol/L is added afterwards4Solution continues to stir evenly to form B solution;B solution is transferred to water heating kettle In, 12h, which is reacted, at 200 DEG C obtains C solution;Solid in C solution is through centrifuge washing, and dry 8h is to drying at 95 DEG C, grinding After obtain Pd/CuxO@GO catalyst.
Pd/Cu prepared by above-described embodiment 4xO@GO composite catalyst 0.10g is placed in surface plate, extremely by the surface plate In the organic glass reactor of 5.9L, glass cover is covered.Reactor bottom places the fan of a 5W, will be certain density dense Formalin is injected in reactor, and formaldehyde volatilization is until concentration balance, and the initial concentration after formaldehyde balances is 234.5ppm, by glass Glass lid is removed, Pd/CuxO@GO composite catalyst contacts with each other with formaldehyde gas and is reacted, and the concentration variation of formaldehyde passes through Multi-Component Gas Analyzing instrument (INNOVA air Tech Instruments Model 1412) on-line monitoring, reacts 111min Afterwards, concentration of formaldehyde 148.2ppm, formaldehyde removal rate are 36.8%.
Embodiment 5
By 1.0g Cu (Ac)2It is dissolved in 30mL water, the GO solution that 7mL concentration is 2.9g/L is then added, make it sufficiently It is uniformly dispersed to form solution A;The PdCl that 3mL concentration is 8g/L is added in solution A2Solution adds 1.0g NaOH, then The NaBH that 5mL concentration is 0.1mol/L is added4Solution continues to stir evenly to form B solution;B solution is transferred in water heating kettle, 12h is reacted at 180 DEG C obtains C solution;Through centrifuge washing, dry 8h at 80 DEG C obtains Pd/ after grinding for solid in C solution CuxO@GO catalyst.
Pd/Cu prepared by above-described embodiment 5xO@GO composite catalyst 0.10g is placed in surface plate, extremely by the surface plate In the organic glass reactor of 5.9L, glass cover is covered.Reactor bottom places the fan of a 5W, will be certain density dense Formalin is injected in reactor, and formaldehyde volatilization is until concentration balance, and the initial concentration after formaldehyde balances is 230ppm, by glass Lid is removed, Pd/CuxO@GO composite catalyst contacts with each other with formaldehyde gas and is reacted, and the concentration variation of formaldehyde passes through more Component gas analyzer (INNOVA air Tech Instruments Model 1412) on-line monitoring, after reacting 111min, Concentration of formaldehyde is 150ppm, and formaldehyde removal rate is 34.8%.
Embodiment 6
By 0.25g Cu (Ac)2It is dissolved in 30mL water, the GO solution that 7mL concentration is 2.9g/L is then added, fills it It is uniformly dispersed to form solution A;The PdCl that 3mL concentration is 8g/L is added in solution A2Solution adds 0.25g NaOH, so The NaBH that 3mL concentration is 0.5mol/L is added afterwards4Solution continues to stir evenly to form B solution;B solution is transferred to water heating kettle In, 8h, which is reacted, at 200 DEG C obtains C solution;Through centrifuge washing, dry 12h at 75 DEG C is obtained after grinding for solid in C solution Pd/CuxO@GO catalyst.
Pd/Cu prepared by above-described embodiment 6xO@GO composite catalyst 0.10g is placed in surface plate, extremely by the surface plate In the organic glass reactor of 5.9L, glass cover is covered.Reactor bottom places the fan of a 5W, will be certain density dense Formalin is injected in reactor, and formaldehyde volatilization is until concentration balance, and the initial concentration after formaldehyde balances is 241ppm, by glass Lid is removed, Pd/CuxO@GO composite catalyst contacts with each other with formaldehyde gas and is reacted, and the concentration variation of formaldehyde passes through more Component gas analyzer (INNOVA air Tech Instruments Model 1412) on-line monitoring, after reacting 111min, Concentration of formaldehyde is 86.5ppm, and formaldehyde removal rate is 64.1%.
Comparative example 1
0.25g copper acetate and 0.78g CTAB is taken to be dissolved in 40mL water, after completely dissolution, 4mL concentration, which is added, is The NaOH solution of 0.5mol/L, the hydro-thermal process 12h at 120 DEG C are centrifuged, washing, after alcohol is washed, 80 DEG C of drying at least 8h, and grinding And obtain CuO solid;It takes 0.3g CuO solid to be dispersed in 30mL water, the GO solution that 7mL concentration is 2.9g/L is then added, 3mL concentration is the PdCl of 8g/L2Solution continues to stir evenly;It is 0.1mol/L NaBH that 5mL concentration is added in the solution later4+ 0.1mol/L NaOH mixed solution is evaporated in 80 DEG C of stirrings, obtains Pd/CuxO@GO composite catalyst.This method is two-step method, is Hydro-thermal method+chemical reduction method.
Pd/Cu prepared by above-mentioned comparison 1xO@GO composite catalyst 0.10g is placed in surface plate, by the surface plate as In the organic glass reactor of 5.9L, glass cover is covered.Reactor bottom places the fan of a 5W, by certain density dense first Aldehyde solution injects in reactor, and formaldehyde volatilization is until concentration balance, and the initial concentration after formaldehyde balances is 227.8ppm, by glass Lid is removed, Pd/CuxO@GO composite catalyst contacts with each other with formaldehyde gas and is reacted, and the concentration variation of formaldehyde passes through more Component gas analyzer (INNOVA air Tech Instruments Model 1412) on-line monitoring, after reacting 111min, Concentration of formaldehyde is 168.9ppm, and formaldehyde removal rate is 25.9%.
Comparative example 2
By 0.25g Cu (Ac)2It is dissolved in 30mL water, the PdCl that 3mL concentration is 8g/L is then added2Solution fills it It is uniformly dispersed;0.25g NaOH is added later, adds the NaBH that 5mL concentration is 0.1mol/L4It is equal to continue stirring for solution It is even;The solution of mixing is transferred in water heating kettle, reacts 12h at 180 DEG C, centrifuge washing, dry 8h at 80 DEG C, after grinding Obtain Pd/CuxO composite catalyst.
Pd/Cu prepared by above-mentioned comparison 2xO@GO composite catalyst 0.10g is placed in surface plate, by the surface plate as In the organic glass reactor of 5.9L, glass cover is covered.Reactor bottom places the fan of a 5W, by certain density dense first Aldehyde solution injects in reactor, and formaldehyde volatilization is until concentration balance, and the initial concentration after formaldehyde balances is 228.2ppm, by glass Lid is removed, Pd/CuxO@GO composite catalyst contacts with each other with formaldehyde gas and is reacted, and the concentration variation of formaldehyde passes through more Component gas analyzer (INNOVA air Tech Instruments Model 1412) on-line monitoring, after reacting 111min, Concentration of formaldehyde is 174.6ppm, and formaldehyde removal rate is 23.5%.
It can be obtained by Examples 1 to 6 and comparative example 1~2, using Pd/Cu prepared by the present inventionxO@GO composite catalyst is short In the case where time 111min and high concentration of formaldehyde, formaldehyde removal efficiency is above the Pd/Cu of 1 two-step method of comparative example preparationxO@ The Pd/Cu of GO composite catalyst and one step hydro thermal method preparationxO composite catalyst.Simultaneously in the preparation when the amount of the mantoquita used It is less when being 0.2~0.25g, under equal conditions test, 0.10g Pd/CuxO@GO composite catalyst is in 111min to height The removal efficiency of concentration formaldehyde (230~245ppm) is high.Specific preparation method is copper salt solution and GO solution with mass concentration ratio For 6.67~8.33:2.9, volume ratio is that 30:7 mixes to form solution A;The palladium salt that 8~10g/L is sequentially added in solution A is molten The reducing solution of liquid, solvable alkali and 0.1~0.5mol/L forms B solution;Mantoquita can be copper acetate, copper chloride or sulfuric acid One of copper, palladium salt are palladium chloride or palladium acetate, and solvable alkali is NaOH or KOH, reducing solution NaBH4Solution or KBH4 Solution;The mass ratio of solvable alkali and mantoquita is 1:1, and the mass ratio of mantoquita and palladium salt is 0.20~0.25:0.024;By B solution Temperature be 120~200 DEG C of 8~12h of progress hydro-thermal reaction after obtain C solution, the solid in C solution through centrifuge washing, 75~ Dry 8~12h, grinding obtain Pd/Cu at 95 DEG CxO@GO composite catalyst, under equal conditions test, 0.10g Pd/CuxO@ GO composite catalyst is 64% or more to the removal efficiency of high-concentration formaldehyde (230~245ppm) in 111min, increases reaction Time is completely removed to 160min formaldehyde.
The Pd/Cu prepared with embodiment 1xO@GO composite catalyst is tested and is characterized, as follows:
Pd/Cu as shown in Figure 1xThe XRD diagram of O@GO composite catalyst is it is found that Pd/CuxO@GO composite catalyst mainly by Cu2O and CuO phase composition, does not observe the XRD diffraction maximum of GO and Pd, mainly they content is less or high degree of dispersion.
The Pd/Cu as shown in Fig. 2 (a)xThe SEM of O@GO composite catalyst schemes it is found that the Cu to reunitexO is supported on the GO of fold Surface, CuxThe size of O particle is nanoscale;The Pd/Cu shown in Fig. 2 (b)xIt, can be in the EDS figure of O GO composite catalyst The presence for observing Pd, shows Pd/CuxO@GO composite catalyst is successfully prepared.
Pd/Cu prepared by embodiment 1 as shown in Figure 3xThe Pd/ of O@GO composite catalyst and the preparation of 1 two-step method of comparative example CuxO@GO composite catalyst room temperature be catalyzed formaldehyde performance map it is found that by 160min formaldehyde catalysis reaction after, Pd/CuxO@GO Catalyst can be at room temperature by the HCHO exhaustive oxidation of high concentration at CO2And water, compared with comparative example 1, prepared by embodiment 1 Pd/CuxThe catalytic performance of O@GO composite catalyst PARA FORMALDEHYDE PRILLS(91,95) is much better than Pd/Cu prepared by comparative example 1xO@GO composite catalyst.
Pd/Cu prepared by embodiment 1 as shown in Figure 4xThe multiple room temperature of O@GO composite catalyst removes high-concentration formaldehyde Effect picture, as can be seen from Figure 4 prepared Pd/CuxO@GO composite catalyst be reused many times after at 111min pairs The removal efficiency of high-concentration formaldehyde remains unchanged.
Unspecified content is the prior art known to a person of ordinary skill in the art in this specification.
Above-described specific embodiment is only schematical, and used technical term is limited in the present invention For qualifier only for convenience of description of the invention, those skilled in the art remove formaldehyde gas Pd/ in room temperature of the present invention CuxUnder the enlightenment of the preparation method of O@GO composite catalyst, present inventive concept and scope of the claimed protection are not being departed from In the case of, many forms can be also derived, these are within the scope of the present invention.

Claims (4)

1. a kind of room temperature removes formaldehyde gas Pd/CuxThe preparation method of O@GO composite catalyst, which is characterized in that including following step It is rapid:
1) by copper salt solution and GO solution with mass concentration ratio for 6.67~33.33:2.9, volume ratio is that 30:7 mixes that form A molten Liquid;Palladium salt solution, solvable alkali and reducing solution are sequentially added in solution A, form B solution;Wherein, the solvable alkali is NaOH or KOH, reducing solution NaBH4Solution or KBH4Solution;The mass ratio of the solvable alkali and mantoquita be 1:1, mantoquita with The mass ratio of palladium salt is 0.20~0.25:0.024;
2) C solution is obtained after B solution being carried out hydro-thermal reaction, the solid in C solution obtains Pd/ through centrifuge washing, drying, grinding CuxO@GO composite catalyst;The time of hydro-thermal reaction is 8~12h, and temperature is 120~200 DEG C.
2. room temperature according to claim 1 removes formaldehyde gas Pd/CuxThe preparation method of O@GO composite catalyst, feature Be: mantoquita is one of copper acetate, copper chloride or copper sulphate, and palladium salt is palladium chloride or palladium acetate.
3. room temperature according to claim 1 removes formaldehyde gas Pd/CuxThe preparation method of O@GO composite catalyst, feature Be: the mass concentration of palladium salt solution is 8~10g/L, and the molar concentration of reducing solution is 0.1~0.5mol/L.
4. room temperature according to claim 1 removes formaldehyde gas Pd/CuxThe preparation method of O@GO composite catalyst, feature Be: dry temperature is 75~95 DEG C in step 2), and the dry time is 8~12h.
CN201710486313.6A 2017-06-23 2017-06-23 Room temperature removes formaldehyde gas Pd/CuxThe preparation method of O@GO composite catalyst Active CN107159262B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710486313.6A CN107159262B (en) 2017-06-23 2017-06-23 Room temperature removes formaldehyde gas Pd/CuxThe preparation method of O@GO composite catalyst

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710486313.6A CN107159262B (en) 2017-06-23 2017-06-23 Room temperature removes formaldehyde gas Pd/CuxThe preparation method of O@GO composite catalyst

Publications (2)

Publication Number Publication Date
CN107159262A CN107159262A (en) 2017-09-15
CN107159262B true CN107159262B (en) 2019-10-08

Family

ID=59819194

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710486313.6A Active CN107159262B (en) 2017-06-23 2017-06-23 Room temperature removes formaldehyde gas Pd/CuxThe preparation method of O@GO composite catalyst

Country Status (1)

Country Link
CN (1) CN107159262B (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107876044A (en) * 2017-10-26 2018-04-06 上海交通大学 Nano composite material catalyst and its production and use
CN108847490B (en) * 2018-06-08 2021-07-09 西北工业大学 Ag-CuO-NrGO air electrode with super-capacitive performance and preparation method thereof
CN109682865B (en) * 2019-01-07 2022-01-18 北京工业大学 Self-reduction preparation method of gold nanoparticle-loaded tin dioxide nanoflower gas-sensitive material
CN112023937B (en) * 2019-11-26 2022-10-21 天津大学 Nano copper oxide coated palladium nanowire heterogeneous catalyst, preparation method thereof and application thereof in methanol electrocatalytic oxidation
CN112588299A (en) * 2020-12-29 2021-04-02 苏州美吉科环保科技有限公司 Method for treating polluted air based on composite catalyst
CN112588298A (en) * 2020-12-29 2021-04-02 苏州美吉科环保科技有限公司 Composite catalyst for air purification and preparation method and application thereof
CN112774691B (en) * 2021-01-27 2022-04-19 宁波方太厨具有限公司 Preparation method of aldehyde-removing catalyst

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1795970B (en) * 2004-12-28 2011-04-13 中国科学院生态环境研究中心 High performance catalyst for catalyzing formaldehyde to complete oxidation under room temperature temperature
FI20106086A0 (en) * 2010-10-21 2010-10-21 Oulun Yliopisto PHOTO - CATALYTIC MATERIAL
CN103071489A (en) * 2011-10-25 2013-05-01 上海纳米技术及应用国家工程研究中心有限公司 Supported active carbon catalytic material capable of eliminating formaldehyde at room temperature and preparation method thereof
CN102814178B (en) * 2012-08-23 2015-03-25 南京理工大学 Palladium-transition metal oxide-graphene ternary composite catalyst and preparation method thereof
CN102895969A (en) * 2012-10-15 2013-01-30 武汉理工大学 Method for preparing formaldehyde room temperature oxidation catalyst
CN104138756A (en) * 2014-08-02 2014-11-12 孙超 Supported catalyzer for low-temperature catalytic combustion of VOCs and method for preparing supported catalyzer for low-temperature catalytic combustion of VOCs
CN104368335B (en) * 2014-10-15 2016-08-17 深圳市艾迪盈创科技有限公司 A kind of preparation method and applications of purifying formaldehyde noble metal monolithic catalyst

Also Published As

Publication number Publication date
CN107159262A (en) 2017-09-15

Similar Documents

Publication Publication Date Title
CN107159262B (en) Room temperature removes formaldehyde gas Pd/CuxThe preparation method of O@GO composite catalyst
CN105884576B (en) A kind of CuZn bimetallic organic framework material is the copper-based catalysts and its preparation method and application of presoma
JP6651362B2 (en) Zeolite containing metal particles
CN108855069A (en) A kind of nano bar-shape Pt/CeO2The preparation method of loaded catalyst and the application in CO catalysis reaction
CN105772027B (en) A kind of support type cobaltosic oxide catalyst and its preparation method and application
CN101362080B (en) Active carbon loading ruthenium ammonia synthesis catalyst and preparation method thereof
CN109939689A (en) A kind of Rare Earth Mine monolithic catalyst, preparation method and applications
CN108479855A (en) A kind of nucleocapsid metal organic framework base composite photocatalyst and preparation method thereof
CN109999902A (en) The supported porous grade titanium-silicon molecular sieve catalyst of encapsulation type platinum family sub-nanometer metal and its preparation and application
CN111139108B (en) Carbon monoxide steam conversion reaction method using Pt-based catalyst
CN109718775A (en) A kind of CuCo2O4The preparation method of nano spinel catalyst
CN108993485A (en) The preparation method and application of a kind of mesoporous carbon microspherical catalyst of original position carried metal
CN109731579A (en) A kind of mesoporous lanthanum oxide catalyst of nickel load and preparation method thereof
CN113477252B (en) Preparation method and application of composite porous catalyst containing titanium and other transition metals simultaneously
CN106378141A (en) ZnO/Cu nanometer crystal composite material, and preparation method and application thereof
Yousaf et al. Synergistic effect of interfacial phenomenon on enhancing catalytic performance of Pd loaded MnO x–CeO 2–C hetero-nanostructure for hydrogenation and electrochemical reactions
CN101022887A (en) Compound having a pyrochlore-structure and its use as a catalyst carrier in water gas shift reaction
WO2024078051A1 (en) Biomass skeleton carbon-metal composite micro-nano structure catalytic material, and preparation method and use
CN109453762A (en) A kind of preparation method and application of modified clay mine loaded palladium catalyst
CN108043462A (en) A kind of Ag/UiO-66-NH2Composite material and its preparation method and application
CN103721754B (en) For the preparation method of the alpha-alumina molding carrier of silver catalyst
CN101773854B (en) Nano-spherical mesoporous organic metal catalyst, preparation method and application thereof
CN110508312A (en) With the method for Ni-Pt nanometer sheet catalyst visible light catalytic ammonia borine dehydrogenation
CN106955701A (en) One kind SiO containing aluminium2Load high dispersive Pt catalyst and its preparation method and application
CN106378142A (en) Catalyst for removing alkene material flow impurity through deep purification at room temperature, preparation method and application thereof

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant