CN1546229A - Catalyst for porous support carried NiB amorphous alloy and preparation method thereof - Google Patents
Catalyst for porous support carried NiB amorphous alloy and preparation method thereof Download PDFInfo
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- CN1546229A CN1546229A CNA2003101075172A CN200310107517A CN1546229A CN 1546229 A CN1546229 A CN 1546229A CN A2003101075172 A CNA2003101075172 A CN A2003101075172A CN 200310107517 A CN200310107517 A CN 200310107517A CN 1546229 A CN1546229 A CN 1546229A
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Abstract
The invention refers to a manufacturing method for a kind of load noncrystal alloy catalyst, which uses inorganic oxide and molecular sift as carrier, made up of load transition metal inducer and noncrystal alloy loaded with efficient amount of NiB; the multiaperture carrier load efficient active component NiB accounts for 5%-50% of catalyst weight, Ni:B=70:30; the weight percentage content of inducer on multiaperture carrier is 0.1%-10%. The multiaperture carrier which contains transition metal inducer M into the stable chemical plating liquid, the noncrystal NiB is plated chemically on the multiaperture carrier surface by inducer M. the operation is simple, the cost is low, the dispersant of the alloy is good, the catalyst activity is high, and it is safe.
Description
Technical field
The present invention relates to a kind of preparation method of carried non-crystal alloy catalyst, say so more specifically and adopt the Catalysts and its preparation method of transition metal as derivant loading NiB amorphous alloy on porous carrier.
Background technology
From Smith in 1980 was proposing the paper of first piece of use amorphous alloy as catalyst in the 7th the international catalysis meeting after, the research of amorphous alloy catalyst had caused people's very big interest.And the preparation carried non-crystal alloy catalyst is again a focus of present stage amorphous alloy catalyst research.
CN1196975A has announced a kind of loaded catalyst of being made up of 0.1～30.0 heavy %NiB amorphous alloy and metallic addition M and 70.0～99.9 heavy % porous carrier materials, the atomic ratio of its Ni and M is 0.1～1000, (Ni+M) atomic ratio with B is 0.5～10.0,10～1000 meters of specific surfaces
2/ gram.This Preparation of catalysts method is included in that to be higher than the solution solidifies o'clock atomic ratio that a kind of Ni and M fed intake to 100 ℃ the scope be the NH that contains of the porous carrier materials of 0.1～80 nickeliferous and M and molar concentration 0.5～10.0
4 +Solution contact by 0.1～10.0 B and (Ni+M) atomic ratio that feeds intake.
CN1286140A discloses the preparation method of the amorphous alloy catalyst of a kind of support type boracic, nickel and metallic addition M, be with salt solution impregnation, oven dry, the roasting of porous carrier materials through containing metallic additive M, after solution containing nickel dipping, the oven dry, in 0 to 100 ℃ scope be 0.5～15.0% the BH that contains with molar concentration
4 -Solution contact.
CN1262147A has invented and has belonged to TiO
2The catalyst of carrier of non-crystal NiB metal alloy, it is with TiO
2Be carrier, the NiB amorphous alloy of load effective dose and rare earth element active component constitute; Described TiO
2Carrier loaded effective active composition NiB accounts for 5.26% of catalyst weight, and described rare earth element accounts for 1% of catalyst weight.Catalyst has the selectivity of very high low temperature active and nearly 100% to aromatic hydrogenation, and has hydrodesulfurization (HDS) activity, can be applicable to oil hydrogenation and makes with extra care.
The preparation of above-mentioned support type NiB amorphous alloy catalyst is to adopt the immersion reduction method preparation basically.Earlier Ni salt and other metallic addition M are loaded on the porous carrier, filter then, dry, with BH
4 -Ion reducing metal ion, the preparation carried non-crystal alloy catalyst.
Summary of the invention
The catalyst that the purpose of this invention is to provide a kind of porous carrier loading NiB amorphous alloy, it is improvements over the prior art.Adopt the technology of industrial chemistry plating NiB coating, as derivant, on the voluminous powder carrier surface, carry out Electroless Plating Ni B amorphous alloy with transition metal.By the distribution of control transition metal, thereby reach control NiB amorphous alloy in the lip-deep distribution of porous carrier.That the prepared carried non-crystal alloy catalyst of this method has is simple to operate, prepared in batches good reproducibility, Preparation of Catalyst cost are low, the good dispersion degree of NiB amorphous alloy, and the catalyst activity height, and safe in utilization.
The present invention is to be carrier with inorganic oxide and molecular sieve, and the NiB amorphous alloy of carrying transition metal derivant and load effective dose constitutes, particle diameter: 10～100nm; Described porous carrier load effective active composition NiB accounts for 5%～50% of catalyst quality, wherein Ni: B=70: 30; The quality percentage composition of described derivant on porous carrier is 0.1%～10%.
Described porous carrier comprises: Al
2O
3, TiO
2, SiO
2, ZrO
2, MgO, molecular sieve or active carbon.Preferred TiO
2, MgO or beta-molecular sieve.
Described transition metal derivant is: Pd, Pt, Ag, Fe, Cu or Ni.Preferred transition metal derivant is Pd, Ag or Cu.
The hydrogenization catalyst preparation method of porous carrier loading NiB amorphous alloy comprises the steps:
(1) with soluble metal Ni salting liquid, complexing agent, contain BH
4 -Solution mix, with the pH value to 14 of aqueous slkali NaOH or KOH regulator solution, form stable chemical plating fluid.The atomic ratio of Ni and B is 0.1～10 in the plating bath, Ni
2+With the mol ratio of complexing agent be 1: 2～6.
(2) the transition metal derivant is loaded on 20～200 purpose porous carrier surfaces, the required presoma of preparation chemical plating, the weight percentage of derivant on porous carrier is 0.1%～10%.
(3) after 10～150 minutes, use distilled water and ethanol washed product 0～90 ℃ of haptoreaction above-mentioned presoma and above-mentioned chemical plating fluid to neutral.Preferred 25～60 ℃ of contacts.
Described soluble nickel salt is one or more in nickel chloride, nickelous sulfate, nickel nitrate and the nickel acetate.
Described complexing agent is glacial acetic acid, citric acid, ammoniacal liquor, ethylenediamine or sodium tartrate.Preferred complexing agent is ammoniacal liquor or ethylenediamine.
Described presoma is method with the salting liquid and the described carrier impregnation of solubility derivant or adopts the method preparation of known chemical deposition, after oven dry, the roasting, again with containing BH
4 -Solution reduction.
Adopting the catalyst of the present invention's preparation is amorphous state through the NiB of characterization methods such as XRD, SEM, TEM and SAED proof institute load, and is evenly distributed, and particle size can be controlled in the scope of 10～100nm.Accompanying drawing 1 is an X-ray diffractogram, generates the NiB product and equal 45 ° of diffuse peaks of locating a broadening at 2 θ after Ag induces, and has proved NiB amorphous state characteristic peak.Adopting MgO is that carrier is the support type NiB catalyst of derivant preparation with Ag, does not produce corresponding disperse diffraction maximum owing to the high degree of dispersion of NiB, but after online XRD crystallization, has the characteristic peak of corresponding crystallization Ni to occur.NiB alloy that can the load of indirect proof institute by above-mentioned experiment is an amorphous state.Accompanying drawing 2 is for being the HRSEM picture of the support type NiB amorphous alloy catalyst of derivant preparation with MgO for carrier A g, and as can be seen from the figure the NiB amorphous alloy of institute's load is evenly distributed, and particle diameter is at 30～50nm.
The carried non-crystal alloy catalyst of the present invention's preparation has the selectivity of very high low temperature active and nearly 100% to aromatic hydrogenation, can be applicable to catalytic hydrogenation reaction.That the present invention has is simple to operate, prepared in batches good reproducibility, Preparation of Catalyst cost are low, the good dispersion degree of NiB amorphous alloy, and the catalyst activity height, and safe in utilization.
Description of drawings
The X-ray diffractogram of the catalyst of Fig. 1 the present invention preparation.
Fig. 2 is for being the HRSEM picture of the support type NiB amorphous alloy catalyst of derivant preparation with MgO for carrier A g.
The specific embodiment
The present invention can describe in detail by embodiment, but they are not that the present invention is done any restriction.
Embodiment 1～18:
With concentration is the AgNO of 0.003M
3The PdCl of solution or 0.003M
2Cu (the NO of solution or 0.005M
3)
2Solution 11.4ml and 2g carrier at room temperature flooded 4 hours, and the transition washing is to neutral, and in 120 ℃ of oven dry 4 hours, 400 ℃ of following roastings were the KBH of 0.16M with excessive concentration after 2 hours
4The above-mentioned product of solution reduction obtains containing the presoma of derivant M and carrier.
Obtain solution concentration is the KBH of 0.16M
4The NiSO of solution, 0.31M
4Each 100ml of the ethylenediamine solution of solution and 0.62M gets KBH respectively
4Solution 86ml, NiSO
4Solution 22ml, ethylenediamine solution 44ml mix, and regulate the pH value to 14 of above-mentioned solution with the NaOH solution of 6M, and it is stand-by to make stable chemical plating fluid.
Above-mentioned chemical plating fluid is heated to fixed temperature, the precursor powder that makes is under agitation poured in the chemical plating fluid, react after 45 minutes, no longer including bubble produces, the filtration washing product is used absolute ethanol washing again to neutrality, promptly obtain support type NiB amorphous alloy catalyst.
Selected various raw materials and reaction temperature are listed in the table 1 in the preparation process.The X-ray diffractogram of the catalyst of Fig. 1 the present invention preparation.(a: pure state NiB (Ag) amorphous alloy; The b:MgO carrier; C:NiB (Ag)/MgO; D: NiB after the crystallization (Ag)/MgO); (mark place is the characteristic peak of MgO; Mark ◇ just is Mg (OH)
2Characteristic peak).The various catalyst that prepare are amorphous state through the NiB that instrument characterizes the load of proof institute, and its granular size is in 20～60nm scope.Detect through ICP, the weight percentage of inducing metal is 0.12%, and the weight percentage of Ni is 13.7%, and the atom of NiB consists of Ni
70B
30
Table 1:
| Embodiment | Carrier | Complexing agent | Derivant | Reaction temperature |
| ????1 | ????TiO 2 | Ammoniacal liquor | ????Pd | ????25℃ |
| ????2 | ????TiO 2 | Ammoniacal liquor | ????Ag | ????45℃ |
| ????3 | ????TiO 2 | Ammoniacal liquor | ????Cu | ????60℃ |
| ????4 | ????TiO 2 | Ethylenediamine | ????Pd | ????25℃ |
| ????5 | ????TiO 2 | Ethylenediamine | ????Ag | ????45℃ |
| ????6 | ????TiO 2 | Ethylenediamine | ????Cu | ????60℃ |
| ????7 | ????MgO | Ammoniacal liquor | ????Pd | ????25℃ |
| ????8 | ????MgO | Ammoniacal liquor | ????Ag | ????45℃ |
| ????9 | ????MgO | Ammoniacal liquor | ????Cu | ????60℃ |
| ????10 | ????MgO | Ethylenediamine | ????Pd | ????25℃ |
| ????11 | ????MgO | Ethylenediamine | ????Ag | ????45℃ |
| ????12 | ????MgO | Ethylenediamine | ????Cu | ????60℃ |
| ????13 | Beta-molecular sieve | Ammoniacal liquor | ????Pd | ????25℃ |
| ????14 | Beta-molecular sieve | Ammoniacal liquor | ????Ag | ????45℃ |
| ????15 | Beta-molecular sieve | Ammoniacal liquor | ????Cu | ????60℃ |
| ????16 | Beta-molecular sieve | Ethylenediamine | ????Pd | ????25℃ |
| ????17 | Beta-molecular sieve | Ethylenediamine | ????Ag | ????45℃ |
| ????18 | Beta-molecular sieve | Ethylenediamine | ????Cu | ????60℃ |
Claims (10)
1, a kind of catalyst of porous carrier loading NiB amorphous alloy is characterized in that it is is carrier with inorganic oxide and molecular sieve, and the NiB amorphous alloy of carrying transition metal derivant and load effective dose constitutes, particle diameter: 10～100nm; Described porous carrier load effective active composition NiB accounts for 5%～50% of catalyst quality, wherein Ni: B=70: 30; The quality percentage composition of described derivant on porous carrier is 0.1%～10%.
2,, it is characterized in that described porous carrier comprises: Al according to the catalyst of the described porous carrier loading NiB amorphous alloy of claim 1
2O
3, TiO
2, SiO
2, ZrO
2, MgO, molecular sieve or active carbon.
3,, it is characterized in that described porous carrier is: TiO according to the catalyst of the described porous carrier loading NiB amorphous alloy of claim 2
2, MgO or beta-molecular sieve.
4,, it is characterized in that described transition metal derivant is: Pd, Pt, Ag, Fe, Cu or Ni according to the catalyst of the described porous carrier loading NiB amorphous alloy of claim 1.
5,, it is characterized in that described transition metal derivant is Pd, Ag or Cu according to the catalyst of the described porous carrier loading NiB amorphous alloy of claim 4.
6, the hydrogenization catalyst preparation method of the described porous carrier loading NiB amorphous alloy of claim 1 is characterized in that it comprises the steps:
(1) with soluble metal Ni salting liquid, complexing agent, contain BH
4 -Solution mix, to 14, form stable chemical plating fluid with the pH value of aqueous slkali NaOH or KOH regulator solution.The atomic ratio of Ni and B is 0.1～10 in the plating bath, Ni
2+With the mol ratio of complexing agent be 1: 2～6.
(2) the transition metal derivant is loaded on the porous carrier surface below 20 orders, the required presoma of preparation chemical plating, the weight percentage of derivant M on porous carrier is 0.1%～10%.
(3) with above-mentioned presoma and above-mentioned chemical plating fluid 0～90 ℃ of haptoreaction after 10～150 minutes, product water and ethanol washing.
7,, it is characterized in that described soluble nickel salt is one or more in nickel chloride, nickelous sulfate, nickel nitrate and the nickel acetate according to the hydrogenization catalyst preparation method of the described porous carrier loading NiB amorphous alloy of claim 6.
8,, it is characterized in that described complexing agent is glacial acetic acid, citric acid, ammoniacal liquor, ethylenediamine or sodium tartrate according to the hydrogenization catalyst preparation method of the described porous carrier loading NiB amorphous alloy of claim 6.
9,, it is characterized in that chemical plating fluid is contacted 45 minutes with presoma at 25～60 ℃ according to the Preparation of catalysts method of the described porous carrier loading NiB amorphous alloy of claim 6.
10, according to the Preparation of catalysts method of the described porous carrier loading NiB amorphous alloy of claim 6, it is characterized in that described presoma is that salting liquid and described carrier with the described derivant of solubility at room temperature flooded 4 hours, washing is to neutral, in 120 ℃ of oven dry 4 hours, 400 ℃ of following roastings are after 2 hours or adopt the method preparation of chemical deposition, after oven dry, the roasting, adopt KBH
4The reducing solution reduction.
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|---|---|---|---|
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|---|---|---|---|
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| Publication Number | Publication Date |
|---|---|
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| CN1286557C CN1286557C (en) | 2006-11-29 |
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|---|---|---|---|---|
| CN100357286C (en) * | 2005-12-13 | 2007-12-26 | 天津市瑞凯科技发展有限公司 | Process for preparing tetrahydrofurfuryl alcohol by catalytic hydrogenation of furfuralcohol |
| CN101484610A (en) * | 2005-10-13 | 2009-07-15 | 维罗西股份有限公司 | Electroless plating in microchannels |
| CN100594059C (en) * | 2006-01-12 | 2010-03-17 | 南开大学 | Method for preparing NiB non-crystalline alloy catalyst with the aid of microwave |
| CN101829575A (en) * | 2010-05-17 | 2010-09-15 | 天津市安凯特催化剂有限公司 | Preparation method and application of composite nano nickel catalyst |
| CN102011004A (en) * | 2010-12-28 | 2011-04-13 | 江苏美特林科特殊合金有限公司 | Nickel-based nickel-boron intermediate alloy and preparation method thereof |
| CN102500399A (en) * | 2011-10-18 | 2012-06-20 | 桂林理工大学 | Preparation method of catalyst for producing perillaldehyde by isomerizing myrtenal |
| CN101229515B (en) * | 2008-01-17 | 2012-08-29 | 南开大学 | Method of preparing highly effective hydrogenation amorphous alloy catalyst |
| CN102795954A (en) * | 2011-05-24 | 2012-11-28 | 中国石油化工股份有限公司 | Selective hydrogenation method for long-chain diene |
| CN103638947A (en) * | 2013-12-09 | 2014-03-19 | 江苏大学 | Preparation and application of Ni/Ag/Cu/TiO2 composite catalyst |
| CN104001552A (en) * | 2014-05-30 | 2014-08-27 | 绍兴文理学院 | Terpolymer nanosphere-loaded Ni-B catalyst as well as preparation method and application of terpolymer nanosphere-loaded Ni-B catalyst |
| CN105817268A (en) * | 2014-05-30 | 2016-08-03 | 绍兴文理学院 | Terpolymer nanosphere loaded Ni-B catalyst |
| CN106632169A (en) * | 2016-12-30 | 2017-05-10 | 常茂生物化学工程股份有限公司 | Method for preparing butanedioic anhydride based on amorphous alloy catalytic maleic anhydride through hydrogenation |
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| CN111482177A (en) * | 2020-05-07 | 2020-08-04 | 江苏新河农用化工有限公司 | Catalyst for preparing hydrogenated terphenyl and preparation method and application thereof |
| CN112221502A (en) * | 2020-09-29 | 2021-01-15 | 清华大学 | Hollow spherical shell carrier loaded nickel-based alloy catalyst and preparation method thereof |
| CN107983357B (en) * | 2017-12-08 | 2021-05-18 | 西安近代化学研究所 | Catalyst for synthesizing propane diamine and preparation method thereof |
| CN113198497A (en) * | 2021-04-29 | 2021-08-03 | 清创人和生态工程技术有限公司 | Preparation method and application of nickel-phosphorus amorphous alloy catalyst |
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2003
- 2003-12-15 CN CN 200310107517 patent/CN1286557C/en not_active Expired - Fee Related
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| CN101484610A (en) * | 2005-10-13 | 2009-07-15 | 维罗西股份有限公司 | Electroless plating in microchannels |
| CN101484610B (en) * | 2005-10-13 | 2015-05-13 | 维罗西股份有限公司 | Electroless plating in microchannels |
| CN100357286C (en) * | 2005-12-13 | 2007-12-26 | 天津市瑞凯科技发展有限公司 | Process for preparing tetrahydrofurfuryl alcohol by catalytic hydrogenation of furfuralcohol |
| CN100594059C (en) * | 2006-01-12 | 2010-03-17 | 南开大学 | Method for preparing NiB non-crystalline alloy catalyst with the aid of microwave |
| CN101229515B (en) * | 2008-01-17 | 2012-08-29 | 南开大学 | Method of preparing highly effective hydrogenation amorphous alloy catalyst |
| CN101829575A (en) * | 2010-05-17 | 2010-09-15 | 天津市安凯特催化剂有限公司 | Preparation method and application of composite nano nickel catalyst |
| CN102011004B (en) * | 2010-12-28 | 2012-07-04 | 江苏美特林科特殊合金有限公司 | Nickel-based nickel-boron intermediate alloy and preparation method thereof |
| CN102011004A (en) * | 2010-12-28 | 2011-04-13 | 江苏美特林科特殊合金有限公司 | Nickel-based nickel-boron intermediate alloy and preparation method thereof |
| CN102795954A (en) * | 2011-05-24 | 2012-11-28 | 中国石油化工股份有限公司 | Selective hydrogenation method for long-chain diene |
| CN102795954B (en) * | 2011-05-24 | 2015-04-15 | 中国石油化工股份有限公司 | Selective hydrogenation method for long-chain diene |
| CN102500399A (en) * | 2011-10-18 | 2012-06-20 | 桂林理工大学 | Preparation method of catalyst for producing perillaldehyde by isomerizing myrtenal |
| CN103638947A (en) * | 2013-12-09 | 2014-03-19 | 江苏大学 | Preparation and application of Ni/Ag/Cu/TiO2 composite catalyst |
| CN103638947B (en) * | 2013-12-09 | 2015-08-26 | 江苏大学 | A kind of Ni/Ag/Cu/TiO 2the preparation of composite catalyst and application thereof |
| CN105817268B (en) * | 2014-05-30 | 2018-06-12 | 绍兴文理学院 | The Ni-B catalyst of terpolymer nanosphere load |
| CN104001552A (en) * | 2014-05-30 | 2014-08-27 | 绍兴文理学院 | Terpolymer nanosphere-loaded Ni-B catalyst as well as preparation method and application of terpolymer nanosphere-loaded Ni-B catalyst |
| CN105817268A (en) * | 2014-05-30 | 2016-08-03 | 绍兴文理学院 | Terpolymer nanosphere loaded Ni-B catalyst |
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| CN109433209A (en) * | 2018-09-26 | 2019-03-08 | 昆明理工大学 | Nickel-boron amorphous alloy catalyst and its preparation method and application |
| CN109608304A (en) * | 2019-01-24 | 2019-04-12 | 嘉兴学院 | A kind of method that furfural hydrogenation directly produces 1,2- pentanediol |
| CN109608304B (en) * | 2019-01-24 | 2021-08-06 | 嘉兴学院 | Method for directly producing 1, 2-pentanediol by furfural hydrogenation |
| CN111482177A (en) * | 2020-05-07 | 2020-08-04 | 江苏新河农用化工有限公司 | Catalyst for preparing hydrogenated terphenyl and preparation method and application thereof |
| CN112221502A (en) * | 2020-09-29 | 2021-01-15 | 清华大学 | Hollow spherical shell carrier loaded nickel-based alloy catalyst and preparation method thereof |
| CN113198497A (en) * | 2021-04-29 | 2021-08-03 | 清创人和生态工程技术有限公司 | Preparation method and application of nickel-phosphorus amorphous alloy catalyst |
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|---|---|
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