Process for the preparation of bimetallic core/shell nanoparticles and their catalytic applications
11305344 · 2022-04-19
Assignee
Inventors
Cpc classification
B01J37/0234
PERFORMING OPERATIONS; TRANSPORTING
B22F2999/00
PERFORMING OPERATIONS; TRANSPORTING
B01J37/0072
PERFORMING OPERATIONS; TRANSPORTING
B22F1/17
PERFORMING OPERATIONS; TRANSPORTING
B22F1/17
PERFORMING OPERATIONS; TRANSPORTING
B22F9/24
PERFORMING OPERATIONS; TRANSPORTING
B22F2999/00
PERFORMING OPERATIONS; TRANSPORTING
International classification
B22F1/17
PERFORMING OPERATIONS; TRANSPORTING
B01J37/00
PERFORMING OPERATIONS; TRANSPORTING
B01J37/02
PERFORMING OPERATIONS; TRANSPORTING
B01J35/00
PERFORMING OPERATIONS; TRANSPORTING
B22F9/24
PERFORMING OPERATIONS; TRANSPORTING
Abstract
The present invention disclosed an improved process for the preparation of bimetallic core-shell nanoparticles by using facile aqueous phase synthesis strategy and their application in catalysis such as selective hydrogenation of alkynes into alkenes or alkanes and CO hydrogenation to hydrocarbons.
Claims
1. An improved process for the preparation of bimetallic core-shell nanoparticles, the process comprising the steps of: a) adding a solution of reducing agent in water to an aqueous solution of gold precursor with constant stirring to afford gold nanoparticles followed by stirring for 10 to 15 minutes; b) adding a transition metal precursor to the solution of step (a) followed by adding a capping agent, wherein the capping agent is selected from the group consisting of cetyltrimethylammoniumbromide (CTAB), cetyltrimethylammonium chloride (CTAC), Poly(ethylene glycol)-block-poly(propylene glycol)-block-poly(ethylene glycol) (PEG-PPG-PEG), poly vinyl pyrollidone (PVP) and trisodiumcitrate and heating at a temperature in the range of 60 to 70° C.; and c) adding a mixture of hydrazine hydrate and sodium hydroxide to the solution of step (b) to afford the bimetallic core-shell nanoparticles, wherein a core of the core-shell nanoparticles is made up of the gold, a shell of the core-shell nanoparticles is made up of the transition metal, and said process is carried out in an aqueous medium.
2. The process as claimed in claim 1, wherein said reducing agent is selected from the group consisting of sodium borohydride, ascorbic acid, tri sodium citrate and hydrazine.
3. The process as claimed in claim 1, wherein said transition metal precursor is selected from the group consisting of nickel, cobalt, copper and iron.
4. The process as claimed in claim 1, wherein said bimetallic core-shell nanoparticles are used for selective hydrogenation of alkynes into alkenes or alkanes.
5. The process as claimed in claim 1, wherein said bimetallic core-shell nanoparticles are used for various catalytic conversions selected from organic transformations including NO.sub.2 reduction, transfer hydrogenation of various functional groups including carbonyl, nitro, alkenes, steam reforming, CO.sub.2 and CO hydrogenation reactions, methane reforming, and hydrogen production from hydrazine, ammonia borane, and sodium borohydride.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
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DETAILED DESCRIPTION OF THE INVENTION
(16) The invention will now be described in detail in connection with certain preferred and optional embodiments, so that various aspects thereof may be more fully understood and appreciated.
(17) In line with the above objectives, the present invention provides an improved process for the preparation of bimetallic core-shell nanoparticles, wherein core comprises gold and the shell comprises transition metals selected from nickel, cobalt, copper and iron by using aqueous phase synthesis strategy.
(18) In an embodiment, the present invention provides an improved process for the preparation of bimetallic core-shell nanoparticles comprising the steps of: a) Adding solution of reducing agent in water to an aqueous solution of gold precursor with constant stirring to afford gold nanoparticles followed by further stirring for 10 to 15 minutes; b) Adding a transition metal precursor to the solution of step (a) followed by addition of capping agent and heated at temperature in the range of 60 to 70° C.; c) Adding a mixture of hydrazine hydrate and sodium hydroxide to the solution of step (b) to afford bimetallic core-shell nanoparticles;
wherein, the core is made up of gold and shell is made up of transition metal and said process is carried in aqueous medium.
(19) In preferred embodiment, said reducing agent is selected from sodium borohydride, ascorbic acid, tri sodium citrate or hydrazine.
(20) In another preferred embodiment, said transition metal precursor is selected from nickel, cobalt, copper or iron.
(21) In yet another preferred embodiment, said capping agent is selected from cetyltrimethylammoniumbromide (CTAB), cetyltrimethylammonium chloride (CTAC) Pluronic P123, poly vinyl pyrollidone (PVP) or trisodiumcitrate.
(22) The wine red colour of the solution after reduction of gold ions with NaBH.sub.4 indicates the formation of small gold nanoparticles with size around 10-15 nm, and it is confirmed by the UV-Vis spectroscopy.
(23) The powder XRD patterns obtained from the as synthesized core shell nanoparticles with different shell thickness are given in
(24) The large area and HR-TEM images of the as synthesized core shell particles is shown in
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(27) In situ surface characterization by using AP-XPS for the Au.sub.80@Ni.sub.20 core shell nanoparticles is carried out. The experimental results obtained for the in situ analysis is shown in the
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(33) The synthesis of Au@Co core shell bimetallic catalyst monitored by UV-VIS spectroscopy (
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(35) In another embodiment, the present invention provides use of said bimetallic core-shell nanoparticles for selective hydrogenation of alkynes into alkenes or alkanes.
(36) In yet another embodiment, the present invention provides use of said bimetallic core-shell nanoparticles for various catalytic conversions such as organic transformations like NO.sub.2 reduction, transfer hydrogenation of various functional groups (carbonyl, nitro, alkenes, etc.), steam reforming, CO.sub.2 and CO hydrogenation reactions, methane reforming and other areas like hydrogen production from hydrazine, ammonia borane or sodiumborohydride.
(37) The highly oxidation resistant Au.sub.80@Ni.sub.20 core-shell nanoparticles are tested for their catalytic activity analysis. It is observed that the catalyst can efficiently hydrogenate alkynes by using hydrogen gas at mild temperatures. Further, enhanced activity of the catalysts for the selective hydrogenation of alkynes into alkenes or alkanes by minor change in the reaction parameters is observed.
(38) The complete utilization of oxidation resistant material property by tuning the selectivity for the desired products styrene and ethylbenzene. The activity results obtained for phenylacetylene hydrogenation (alkyne) are shown in the Table 1 and 2.
(39) The table 1 shows the comparison of catalytic activity of Au.sub.80@Ni.sub.20 with monometallic counterparts Au and Ni. The coreshell Au.sub.80@Ni.sub.20 nanoparticles showed excellent activity and selectivity for ethylbenzene production and outweigh the monometallic counterparts.
(40) TABLE-US-00001 TABLE 1 P.A hydrogenation by using Au.sub.80@Ni.sub.20, Au and Ni nanoparticles in MeOH Pressure Selectivity (%) Sr. no. Catalyst Amount Temp. (° C.) (psi) Conversion E.B/Styrene 1 Au.sub.80@Ni.sub.20 5 50 50 100 100/0 2 Ni alone 5 50 50 60 60/40 3 Au alone 5 50 50 ≤5 —/— Solvent = Methanol, Time = 3 hrs
(41) In table 2 shows that by changing the solvent from methanol (MeOH) to dichloromethane (DCM) there is a selectivity change from ethylbenzene (E.B) to an industrially important styrene production. It is observed that catalyst can achieve almost 80% selectivity for styrene with 100% conversion of phenylacetylene under mild conditions in DCM solvent even at room temperature with lesser conversion.
(42) TABLE-US-00002 TABLE 2 Catalytic activity results obtained for P.A hydrogenation by using Au.sub.80@Ni.sub.20 nanoparticles in MeOH and DCM (50 ml) by using a Parr reactor at different temperatures & pressures [in MeOH and DCM, the substrate (P.A) is 5 & 1 mmol, respectively. Selectivity Temp. Conversion (%) Sr. no. Catalyst Amount Time Solvent (° C.) (%) E.B/Styrene 1 Au.sub.80@Ni.sub.20 5 3 MeOH 50 100 100/0 2 Au.sub.80@Ni.sub.20 5 3 MeOH 30 45 40/60 3 Au.sub.80@Ni.sub.20 10 10 DCM 40 100 20/80 4 Au.sub.80@Ni.sub.20 10 10 DCM 30 55 15/85 Pressure = 50 psi.
(43) The following examples, which include preferred embodiments, will serve to illustrate the practice of this invention, it being understood that the particulars shown are by way of example and for purpose of illustrative discussion of preferred embodiments of the invention.
EXAMPLES
Example 1: Synthesis of Noble Metal Based Core Shell Nanoparticles
(44) An aqueous solution of 2.5×10.sup.−4 M HAuCl.sub.4.3H.sub.2O is made in 50 ml of millipore water. While stirring the solution gently, 650 microliter (μL) of 0.1M ice cold NaBH.sub.4 solution in millipore water is added and stirring continued for another 15 minutes. Complete reduction of gold ions to colloidal gold nanoparticles is observed with an immediate colour change from pale yellow gold precursor solution to wine red colour with the addition of NaBH.sub.4. In the second phase, the colloidal gold solution is heated to 70° C. with a ramping rate of 3° C./min., simultaneously nickel acetyl acetonate (Nickel precursor) is added to the solution with desired ratio to the gold metal (for obtaining various shell thickness) and stirred well. After the nickel precursor addition, 500 mg of cetyltrimethylammoniumbromide (CTAB) which acts as the capping agent for the nanoparticles is added to the solution and dispersed thoroughly. When the temperature reaches 70° C., a mixture of 750 microliter (μL) hydrazine hydrate and NaOH (prepared by dissolving 80 mg NaOH dissolved in 2 ml 80% hydrazine hydrate) is added to the solution drop wise for reducing nickel ions. The solution turns to a black colloidal suspension after a while indicating the formation of Au@Ni core shell nanoparticles. The mole ratio of gold to nickel is adjusted by changing the nickel precursor amount to tune the shell thickness. To get a 2 nm shell thickness 0.01 mmol nickclacetylacetonate is added and the obtained core shell nanoparticles are denoted as Au.sub.80@Ni.sub.20 (to increase the shell thickness to 4 nm (Au.sub.65@Ni.sub.35) and 8 nm (Au.sub.50@Ni.sub.50) the nickel precursor ratio to 0.02 mmol and 0.04 mmol is added respectively, keeping the ratio of reducing agent to the nickel precursor same).
Example 2: Synthesis of Au@Co Core Shell Nanoparticle
(45) Au@Co nanoparticles were synthesized by chemical approach using above mentioned chemicals. Aqueous HAuCl.sub.4.3H.sub.2O solution of 2×10.sup.−4M concentration was made in 50 ml. Au precursor has been reduced by using appropriate amount of 0.1 M NaBH.sub.4. The reduction of Au precursor can be easily identified by instant change in color from pale yellow to red wine. The solution was heated to 70° C. with simultaneous addition of Cobalt acetate and the resultant solution capped with CTAB surfactant and dispersed it fully while stirring. When temperature reached to 70° C. then alkaline solution of hydrazine hydrate (80%) added slowly into the above solution to reduce the Cobalt ions on gold nanoparticle surface. The solution turns to black suspension indicating the formation of Au@Co core shell nanoparticle. The nano particles were collected by using external magnet and observed the whole transparent solution after putting the magnet which is clear evidence for formation of complete Au@Co core shell system, them is no separate Au nanoparticle left over.
Example 3: Catalytic Activity Measurements
(46) Highly oxidation resistant Au.sub.80@Ni.sub.20 core-shell nanoparticles are tested for their catalytic activity analysis. The catalyst can efficiently hydrogenate alkynes by using hydrogen gas at mild temperatures. The enhanced activity of the catalysts for the selective hydrogenation of alkynes into alkenes or alkanes by minor change in the reaction parameters is also demonstrated. Finally, the complete utilization of oxidation resistant material property by tuning the selectivity for the desired products styrene and ethylbenzene is explored. The catalytic tests were carried out in a conventional stirred tank Parr reactor having a volume of 100 ml capacity. The pressure and temperature can be adjusted over a wide range according to the reaction parameters. In a typical P.A. hydrogenation reaction the stirred tank is charged with required amounts of Au@Ni core shell catalysts dispersed in 50 ml solvent (MeOH/DCM) followed by the addition of substrate to the reaction vessel. The reaction vessel was closed and flushed with hydrogen 3 times to remove the air and other impurities from the vessel then it is pressurized to the desired condition. The samples were collected at specific time intervals and analyzed with the help of a Gas chromatograph equipped with a flame ionization detector. The activity results obtained for phenylacetylene hydrogenation (alkyne) are shown in the Table 1 and 2. Table 1 shows the comparison of catalytic activity of Au.sub.80@Ni.sub.20 with monometallic counterparts Au and Ni. Our coreshell Au.sub.80@Ni.sub.20 nanoparticles showed excellent activity and selectivity for ethylbenzene production and outweigh the monometallic counterparts. In table 2 it is observed that by changing the solvent from methanol (MeOH) to dichloromethane (DCM) there is a selectivity change from ethylbenzene (E.B) to an industrially important styrene production. It is observed that the catalyst can achieve almost 80% selectivity for styrene with 100% conversion of phenylacetylene under mild conditions in DCM solvent. In addition it is also observed that our catalyst can be used even at room temperature with lesser conversion.
(47) TABLE-US-00003 TABLE 1 P.A hydrogenation by using Au.sub.80@Ni.sub.20, Au and Ni nanoparticles in MeOH Pressure Selectivity (%) Sr. no. Catalyst Amount Temp. (° C.) (psi) Conversion E.B/Styrene 1 Au.sub.80@Ni.sub.20 5 50 50 100 100/0 2 Ni alone 5 50 50 60 60/40 3 Au alone 5 50 50 ≤5 —/— *Solvent = Methanol, Time = 3 hrs.
(48) TABLE-US-00004 TABLE 2 Catalytic activity results obtained for P.A hydrogenation by using Au.sub.80@Ni.sub.20 nanoparticles in MeOH and DCM (50 ml) by using a Parr reactor at different temperatures & pressures [in MeOH and DCM, the substrate (P.A) is 5 & 1 mmol, respectively. Selectivity Temp. Conversion (%) Sr. no. Catalyst Amount Time Solvent (° C.) (%) E.B/Styrene 1 Au.sub.80@Ni.sub.20 5 3 MeOH 50 100 100/0 2 Au.sub.80@Ni.sub.20 5 3 MeOH 30 45 40/60 3 Au.sub.80@Ni.sub.20 10 10 DCM 40 100 20/80 4 Au.sub.80@Ni.sub.20 10 10 DCM 30 55 15/85 Pressure = 50 psi.
Example 4: CO Hydrogenation Using Au@Co Nanostructures
(49) CO hydrogenation (Fischer Tropsch) reaction done at atmospheric pressure on Au@Co nanostructures show that Au@Co 1:0.5 shows very good and stable conversion at temperature range 220° C. to 240° C. (
Advantages of Invention
(50) 1. Bimetallic core shell nanostructures are synthesized in aqueous medium (Green solvent) under mild conditions. 2. Avoid expensive organic solvents like oleyl amine, octadecene, oleic acid, dodecyl amine previously reported for synthesizing similar bimetallic compositions. 3. Aqueous medium synthesis prevents the difficulties of removing the organic solvents and capping agents while using for various applications including catalysis. 4. Good control of Ni shell thickness can be achieved from 2 nm to 8 nm and above. 5. The nanomaterials synthesized in water medium has the advantage of easy washing of the excess reagents used in the synthesis which will provide a much cleaner surface for catalysis. 6. Due to the electronic and geometric modifications at the interface, the nickel surface is found to resist ambient oxidation and even at high temperatures up to 200° C. 7. Improved catalytic activity and selectivity is due to the large presence of exposed metallic (Ni, Co, Fe, Cu etc.) surface of bimetallic core-shell nanoparticles for selective hydrogenation of alkynes into alkenes or alkanes. 8. The application of these core-shell materials can be extended to various catalytic conversions such as organic transformations like NO.sub.2 reduction, transfer hydrogenation of various functional groups (carbonyl, nitro, alkenes, etc.), steam reforming, CO.sub.2 and CO hydrogenation reactions, methane reforming and other areas like hydrogen production from hydrazine, ammonia borane, sodium borohydride etc.