CN110639510A - Method for preparing monatomic catalyst through re-dispersion of Pt nanoparticles - Google Patents
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- 239000003054 catalyst Substances 0.000 title claims abstract description 70
- 238000000034 method Methods 0.000 title claims abstract description 29
- 239000002105 nanoparticle Substances 0.000 title claims abstract description 25
- 239000006185 dispersion Substances 0.000 title description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Substances [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims abstract description 71
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 10
- 239000000203 mixture Substances 0.000 claims abstract description 3
- 230000032683 aging Effects 0.000 claims description 17
- 239000003795 chemical substances by application Substances 0.000 claims description 11
- 239000000243 solution Substances 0.000 claims description 10
- 229920006395 saturated elastomer Polymers 0.000 claims description 6
- 239000007864 aqueous solution Substances 0.000 claims description 4
- 238000002360 preparation method Methods 0.000 claims description 4
- 239000011865 Pt-based catalyst Substances 0.000 claims description 2
- 229910052697 platinum Inorganic materials 0.000 abstract description 12
- 230000000694 effects Effects 0.000 abstract description 6
- 230000008929 regeneration Effects 0.000 abstract description 3
- 238000011069 regeneration method Methods 0.000 abstract description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 23
- 239000010453 quartz Substances 0.000 description 9
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 9
- 239000007789 gas Substances 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 4
- 238000000731 high angular annular dark-field scanning transmission electron microscopy Methods 0.000 description 4
- 238000001833 catalytic reforming Methods 0.000 description 3
- 239000001307 helium Substances 0.000 description 3
- 229910052734 helium Inorganic materials 0.000 description 3
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 238000002407 reforming Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 230000005865 ionizing radiation Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 229910002835 Pt–Ir Inorganic materials 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 230000009849 deactivation Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000003209 petroleum derivative Substances 0.000 description 1
- 238000005504 petroleum refining Methods 0.000 description 1
- 230000036316 preload Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
- B01J23/42—Platinum
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
- B01J35/391—Physical properties of the active metal ingredient
- B01J35/394—Metal dispersion value, e.g. percentage or fraction
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
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Abstract
本发明公开了一种Pt纳米颗粒再分散制备单原子催化剂的方法,属于Pt催化剂技术领域。包括如下步骤:(1)制备含有Pt纳米颗粒的催化剂;(2)将含有Pt纳米颗粒的催化剂使用空气、水、HCl的混合物高温下进行再分散处理,得到Pt单原子催化剂。本发明提供的一种Pt纳米颗粒再分散制备单原子催化剂的方法,具有操作简单、效果显著的优点,能有效地将Pt纳米颗粒分散成Pt单原子,既适用于新制备单原子Pt催化剂,也适用于将使用后失活的铂基催化剂再生。
The invention discloses a method for preparing a single-atom catalyst by redispersion of Pt nano-particles, and belongs to the technical field of Pt catalysts. The method includes the following steps: (1) preparing a catalyst containing Pt nanoparticles; (2) redispersing the catalyst containing Pt nanoparticles at a high temperature with a mixture of air, water and HCl to obtain a Pt single-atom catalyst. The method for preparing single-atom catalyst by redispersion of Pt nanoparticles provided by the present invention has the advantages of simple operation and remarkable effect, can effectively disperse Pt nanoparticles into Pt single atoms, and is suitable for newly preparing single-atom Pt catalysts. Also suitable for regeneration of platinum-based catalysts that have been deactivated after use.
Description
技术领域technical field
本发明属于Pt催化剂技术领域,涉及一种Pt纳米颗粒再分散制备单原子催化剂的方法。The invention belongs to the technical field of Pt catalysts, and relates to a method for preparing a single-atom catalyst by redispersing Pt nanoparticles.
背景技术Background technique
铂催化剂是化学、石油和化工反应过程经常采用的一种催化剂,具有较高的催化活性,良好的选择性,且催化剂制作简单方便,催化剂使用量少,可以通过制造方法的变化和改进改善其性能。因此被广泛用于氨氧化、石油烃重整、不饱和化合物氧化及加氢、气体中一氧化碳、氮氧化物的脱除等反应过程。Platinum catalyst is a kind of catalyst often used in chemical, petroleum and chemical reaction processes. It has high catalytic activity, good selectivity, and the catalyst is simple and convenient to make, and the amount of catalyst used is small. It can be improved by changing and improving the manufacturing method. performance. Therefore, it is widely used in reaction processes such as ammonia oxidation, petroleum hydrocarbon reforming, oxidation and hydrogenation of unsaturated compounds, and removal of carbon monoxide and nitrogen oxides in gases.
催化重整是石油炼制过程之一,即在有催化剂作用的条件下,对汽油馏分中的烃类分子结构进行重新排列成新的分子,使原油蒸馏所得的轻汽油馏分转变成富含芳烃的高辛烷值汽油。铂催化剂是催化重整反应中优异的催化剂,但随着反应的进行,高温以及含水氛围下Pt会发生严重的积聚,马爱增等人研究发现石脑油催化重整反应中运转1 967天的催化剂中Pt严重集聚,Pt最大晶粒直径达到90nm,催化剂活性大幅下降,要想恢复催化剂的活性,需将聚集的Pt颗粒再分散。Catalytic reforming is one of the petroleum refining processes, that is, under the condition of catalyst, the molecular structure of hydrocarbons in gasoline fraction is rearranged into new molecules, so that the light gasoline fraction obtained by crude oil distillation is converted into rich aromatic hydrocarbons. of high-octane gasoline. The platinum catalyst is an excellent catalyst in the catalytic reforming reaction, but with the progress of the reaction, Pt will accumulate seriously at high temperature and in a water-containing atmosphere. The Pt is seriously aggregated in the medium, and the maximum grain size of Pt reaches 90 nm, and the catalyst activity is greatly reduced. In order to restore the activity of the catalyst, the aggregated Pt particles need to be redispersed.
USP4444897公开了一种Pt-Ir基催化剂再分散方法,该方法将催化剂还原后,再用无氧气氛下含HCl和水的氦气处理,最后用含HCl和氧的气体处理,使得活性组分再分散。USP4444897 discloses a Pt-Ir-based catalyst redispersion method. After the catalyst is reduced, it is treated with helium gas containing HCl and water in an oxygen-free atmosphere, and finally treated with a gas containing HCl and oxygen to make the active components Redispersed.
CN 106268883 B公开了一种高Pt分散的方法,该方法将负载活性组分的氧化铝载体进行电离辐射处理,再进行水氯活化、还原制得较高铂分散度的铂基化剂。CN 106268883 B discloses a high-Pt dispersion method, which comprises subjecting an alumina carrier loaded with active components to ionizing radiation treatment, and then performing water chlorine activation and reduction to obtain a platinum-based agent with higher platinum dispersion.
CN107362834A公布了一种恢复在用连续重整催化剂活性的方法,该方法将使用过的催化剂烧焦后,置于盐酸中30℃浸泡2h,除去废液、干燥,最后在510℃水氯活化4h,得到活化后的催化剂。经实验测试该方法可有效恢复连续重整催化剂的活性。CN107362834A discloses a method for recovering the activity of continuous reforming catalysts in use. In this method, the used catalysts are scorched, soaked in hydrochloric acid at 30°C for 2 hours, the waste liquid is removed, dried, and finally activated with water chlorine at 510°C for 4 hours , to obtain the activated catalyst. Experiments show that this method can effectively restore the activity of continuous reforming catalysts.
现有催化剂再分散方法存在各种缺陷与不足,专利USP4444897使用无氧气氛下含HCl和水的氦气处理,工业上使用氦气成本较高;专利CN 106268883 B需预先将负载活性组分的氧化铝载体进行电离辐射处理,步骤繁琐;专利CN107362834 A置于盐酸中30℃浸泡2h,除去废液、干燥,步骤繁琐且难以在线处理。Existing catalyst redispersion methods have various defects and deficiencies. Patent USP4444897 uses helium gas containing HCl and water in an oxygen-free atmosphere, and the cost of industrially using helium gas is relatively high; patent CN 106268883 B needs to pre-load the active component The alumina carrier is treated with ionizing radiation, and the steps are cumbersome; the patent CN107362834 A is soaked in hydrochloric acid at 30 ° C for 2 hours, and the waste liquid is removed and dried. The steps are cumbersome and difficult to handle online.
发明内容SUMMARY OF THE INVENTION
本发明的目的是提供一种使Pt团簇再分散成单原子或制备单原子Pt催化剂的方法,该方法操作简单,无需对载体及催化剂进行特殊处理,使用空气当处理介质成本低,可在线操作且能有效使Pt团簇再分散成单原子。该发明可为工业上催化重整中铂基催化剂失活再生(再分散)提供技术支持。本发明的目的通过以下技术方案实现。The purpose of the present invention is to provide a method for redispersing Pt clusters into single atoms or preparing single-atom Pt catalyst. operation and can effectively redisperse Pt clusters into single atoms. The invention can provide technical support for the deactivation regeneration (redispersion) of platinum-based catalysts in industrial catalytic reforming. The object of the present invention is achieved through the following technical solutions.
一种Pt纳米颗粒再分散制备单原子催化剂的方法,其特征在于,包括如下步骤:(1)制备含有Pt纳米颗粒的催化剂;(2)将含有Pt纳米颗粒的催化剂使用空气、水、HCl的混合物高温下进行再分散处理,得到Pt单原子催化剂。A method for preparing a single-atom catalyst by redispersion of Pt nanoparticles is characterized in that, comprising the following steps: (1) preparing a catalyst containing Pt nanoparticles; (2) using the catalyst containing Pt nanoparticles using air, water, HCl The mixture is redispersed at high temperature to obtain a Pt single-atom catalyst.
进一步地,Pt基催化剂中的Pt含量为0.01~3wt.%。Further, the Pt content in the Pt-based catalyst is 0.01-3 wt.%.
进一步地,再分散处理所使用的温度为400~600℃,优选450~550℃。Further, the temperature used for the redispersion treatment is 400 to 600°C, preferably 450 to 550°C.
进一步地,再分散处理所使用介质制备方法为:空气通过HCl水溶液,得到含有HCl的饱和空气。Further, the preparation method of the medium used in the redispersion treatment is as follows: air passes through the HCl aqueous solution to obtain saturated air containing HCl.
进一步地,再分散制备处理使用介质的HCl水溶液浓度为:0.01~0.5mol/L,优选0.01~0.2mol/L。Further, the concentration of the HCl aqueous solution used in the redispersion preparation treatment medium is: 0.01-0.5 mol/L, preferably 0.01-0.2 mol/L.
进一步地,再分散处理所使用介质气剂比为1000:0.5~1000:10。气剂比:每小时通过催化剂床层的气体量与催化剂体积之比。Further, the medium gas-agent ratio used in the redispersion treatment is 1000:0.5-1000:10. Gas-to-agent ratio: The ratio of the amount of gas passing through the catalyst bed per hour to the volume of the catalyst.
进一步地,再分散处理时间为2~15h。Further, the redispersion treatment time is 2-15h.
为模拟反应中因Pt严重积聚造成失活的催化剂,本发明对新制备的催化剂进行水热老化以获得含有Pt纳米颗粒的催化剂。步骤(1)得到的含有Pt纳米颗粒的催化剂,经过水热老化处理以后,采用步骤(2)再分散处理;水热老化条件为:水热老化温度为400~700℃,水热老化介质含水量为5~40v%,老化时间为10~72h,气剂比为1000:0.5~1000:10。In order to simulate the catalyst deactivated due to the severe accumulation of Pt in the reaction, the present invention performs hydrothermal aging on the newly prepared catalyst to obtain a catalyst containing Pt nanoparticles. The catalyst containing Pt nanoparticles obtained in step (1) is subjected to redispersion treatment in step (2) after hydrothermal aging treatment; the hydrothermal aging conditions are: the hydrothermal aging temperature is 400-700° C., and the hydrothermal aging medium contains The amount of water is 5-40v%, the aging time is 10-72h, and the air-agent ratio is 1000:0.5-1000:10.
本发明提供的一种Pt纳米颗粒再分散制备单原子催化剂的方法,具有操作简单、效果显著的优点,能有效地将Pt纳米颗粒分散成Pt单原子,既适用于新制备单原子Pt催化剂,也适用于将使用后失活的铂基催化剂再生。The method for preparing single-atom catalyst by redispersion of Pt nano-particles provided by the invention has the advantages of simple operation and remarkable effect, can effectively disperse Pt nanoparticles into Pt single-atom, and is suitable for newly preparing single-atom Pt catalysts. Also suitable for regeneration of platinum-based catalysts that have been deactivated after use.
附图说明Description of drawings
图1为水热老化24h后的铂催化剂的HAADF STEM图。Figure 1 is the HAADF STEM image of the platinum catalyst after hydrothermal aging for 24 h.
图2为经过8h再分散处理的铂催化剂的HAADF STEM图。Figure 2 is the HAADF STEM image of the platinum catalyst after 8h redispersion treatment.
具体实施方式Detailed ways
以下结合附图对本发明做进一步说明。The present invention will be further described below with reference to the accompanying drawings.
实施例1Example 1
催化剂的老化Aging of the catalyst
通过浸渍法制备好的催化剂于石英管反应器中,催化剂装填量为100ml,水热老化温度500℃,老化介质含水量20v%,气剂比为1000:1,水热老化时间为24h。The catalyst prepared by the impregnation method was placed in a quartz tube reactor. The catalyst loading was 100ml, the hydrothermal aging temperature was 500°C, the moisture content of the aging medium was 20v%, the gas-agent ratio was 1000:1, and the hydrothermal aging time was 24h.
老化后的铂催化剂的HAADF STEM图如图1所示,从图中可以看出经过水热老化24h后铂催化剂上Pt严重积聚,呈大颗粒状。The HAADF STEM image of the aged platinum catalyst is shown in Figure 1. It can be seen from the figure that after hydrothermal aging for 24 h, Pt is seriously accumulated on the platinum catalyst, which is in the form of large particles.
实施例2Example 2
Pt纳米颗粒的再分散处理Redispersion of Pt Nanoparticles
将老化后的催化剂,即含Pt纳米颗粒的催化剂置于石英管中,催化剂装填量为100ml,加热温度设定为400℃,气剂比为1000:0.5,使用HCl溶液浓度为0.02mol/L,空气预先通过HCl溶液制得含HCl的饱和空气,然后进入石英管与催化剂接触,再分散处理时间为2h。The aged catalyst, that is, the catalyst containing Pt nanoparticles, was placed in a quartz tube, the catalyst loading was 100ml, the heating temperature was set to 400°C, the gas-to-agent ratio was 1000:0.5, and the concentration of the HCl solution was 0.02mol/L. , the air is passed through the HCl solution to obtain saturated air containing HCl, and then enters the quartz tube to contact with the catalyst, and the redispersion treatment time is 2h.
实施例3Example 3
Pt纳米颗粒的再分散处理Redispersion of Pt Nanoparticles
将老化后的催化剂,即含Pt纳米颗粒的催化剂置于石英管中,催化剂装填量为100ml,加热温度设定为500℃,气剂比为1000:1,使用HCl溶液浓度为0.05mol/L,空气预先通过HCl溶液制得含HCl的饱和空气,然后进入石英管与催化剂接触,再分散处理时间为5h。The aged catalyst, that is, the catalyst containing Pt nanoparticles, was placed in a quartz tube, the catalyst loading was 100ml, the heating temperature was set to 500°C, the gas-to-agent ratio was 1000:1, and the concentration of the HCl solution was 0.05mol/L. , the air is passed through the HCl solution to obtain saturated air containing HCl, and then enters the quartz tube to contact with the catalyst, and the redispersion treatment time is 5h.
实施例4Example 4
Pt纳米颗粒的再分散处理Redispersion of Pt Nanoparticles
将老化后的催化剂,即含Pt纳米颗粒的催化剂置于石英管中,催化剂装填量为100ml,加热温度设定为500℃,气剂比为1000:1,使用HCl溶液浓度为0.2mol/L,空气预先通过HCl溶液制得含HCl的饱和空气,然后进入石英管与催化剂接触,再分散处理时间为8h。The aged catalyst, that is, the catalyst containing Pt nanoparticles, was placed in a quartz tube, the catalyst loading was 100ml, the heating temperature was set to 500°C, the gas-to-agent ratio was 1000:1, and the concentration of HCl solution was 0.2mol/L. , the air is passed through the HCl solution to obtain saturated air containing HCl, and then enters the quartz tube to contact with the catalyst, and the redispersion treatment time is 8h.
再分散处理的铂催化剂的HAADF STEM图如图2所示,从图中可看中Pt颗粒被有效地分散开来,呈单原子状态。综合图1和图2,充分说明对于积聚较严重的Pt颗粒,本发明的再分散处理方法能够有效地将Pt颗粒分散成单原子。The HAADF STEM image of the redispersed platinum catalyst is shown in Figure 2, from which it can be seen that the Pt particles are effectively dispersed and are in a single atomic state. Combining Fig. 1 and Fig. 2, it is fully demonstrated that for Pt particles with serious accumulation, the redispersion treatment method of the present invention can effectively disperse the Pt particles into single atoms.
实施例5Example 5
Pt纳米颗粒的再分散处理Redispersion of Pt Nanoparticles
将老化后的催化剂,即含Pt纳米颗粒的催化剂置于石英管中,催化剂装填量为100ml,加热温度设定为550℃,气剂比为1000:2,使用HCl溶液浓度为0.01mol/L,空气预先通过HCl溶液制得含HCl的饱和空气,然后进入石英管与催化剂接触,再分散处理时间为10h。The aged catalyst, that is, the catalyst containing Pt nanoparticles, was placed in a quartz tube, the catalyst loading was 100ml, the heating temperature was set to 550°C, the gas-to-agent ratio was 1000:2, and the concentration of HCl solution was 0.01mol/L. , the air is passed through the HCl solution to obtain saturated air containing HCl, and then enters the quartz tube to contact with the catalyst, and the redispersion treatment time is 10h.
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CN114618476A (en) * | 2022-02-16 | 2022-06-14 | 中国科学院大连化学物理研究所 | Monoatomic platinum-based catalyst, and preparation method and application thereof |
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CN114618476A (en) * | 2022-02-16 | 2022-06-14 | 中国科学院大连化学物理研究所 | Monoatomic platinum-based catalyst, and preparation method and application thereof |
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