Method for preparing surface-active onion-like carbon nanospheres based on vapor deposition
11326251 · 2022-05-10
Assignee
Inventors
- Lei Qin (Shanxi, CN)
- Weifeng Liu (Shanxi, CN)
- Yan Cui (Shanxi, CN)
- Xuguang Liu (Shanxi, CN)
- Yongzhen Yang (Shanxi, CN)
Cpc classification
Y10T428/30
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
C01B32/18
CHEMISTRY; METALLURGY
C23C16/4481
CHEMISTRY; METALLURGY
B01J31/1616
PERFORMING OPERATIONS; TRANSPORTING
B82Y30/00
PERFORMING OPERATIONS; TRANSPORTING
C23C16/4417
CHEMISTRY; METALLURGY
B82Y40/00
PERFORMING OPERATIONS; TRANSPORTING
C23C16/45534
CHEMISTRY; METALLURGY
International classification
B32B9/00
PERFORMING OPERATIONS; TRANSPORTING
C01B32/18
CHEMISTRY; METALLURGY
B01J31/16
PERFORMING OPERATIONS; TRANSPORTING
Abstract
The present invention discloses a method for preparing surface-active onion-like carbon nanospheres based on vapor deposition, comprising: directly preparing high-surface-activity onion-like carbon nanospheres formed by coating ferroferric oxide nano-particles on an onion-like graphitized shell by taking liquid small organic molecule alkane n-dodecane as a carbon source to perform chemical vapor deposition at high temperature of 650˜700° C. in an inert carrier gas environment with existence of a ferrocene catalyst. An onion-like carbon nanosphere product prepared according to the present invention has good surface activity and thermal stability, is wide in practicability, and can be widely applied to the fields of adsorbing materials, energy storage materials, catalytic materials, medical materials and the like.
Claims
1. A method for preparing surface-active onion-like carbon nanospheres based on vapor deposition, comprising: directly preparing high-surface-activity onion-like carbon nanospheres formed by coating ferroferric oxide nano-particles on an onion-like graphitized shell by taking liquid small organic molecule alkane n-dodecane as a carbon source to perform chemical vapor deposition at high temperature of 650˜700° C. in an inert carrier gas environment with existence of a ferrocene catalyst.
2. The method according to claim 1, wherein the use amount of the catalyst ferrocene is 0.050˜0.055 time of the mass of the carbon source n-dodecane.
3. The method according to claim 1, wherein the carbon source and the catalyst are added into water to prepare an aqueous dispersion.
4. The method according to claim 3, wherein the use amount of the water is 2˜3 times of the volume of the carbon source.
5. The method according to claim 1, wherein the chemical vapor deposition reaction time is 15˜20 min.
6. The method according to claim 1, wherein the inert carrier gas flow in the chemical vapor deposition reaction process is 5+/−1 mL/min.
7. The method according to claim 6, wherein the inert carrier gas flow is controlled to be not greater than 3 mL/min in a temperature rise period, and after temperature rises to a reaction temperature, adjusting the inert carrier gas flow to 5+/−1 mL/min.
8. Surface-active onion-like carbon nanospheres prepared by the method according to claim 1, wherein an Fe.sub.3O.sub.4 nanocrystalline metal kernel is coated inside the carbon nanosphere, and an outer layer being of an onion-like graphitized shell structure, with average particle size of 30 nm.
9. Surface-active onion-like carbon nanospheres prepared by the method according to claim 2, wherein an Fe.sub.3O.sub.4 nanocrystalline metal kernel is coated inside the carbon nanosphere, and an outer layer being of an onion-like graphitized shell structure, with average particle size of 30 nm.
10. Surface-active onion-like carbon nanospheres prepared by the method according to claim 3, wherein an Fe.sub.3O.sub.4 nanocrystalline metal kernel is coated inside the carbon nanosphere, and an outer layer being of an onion-like graphitized shell structure, with average particle size of 30 nm.
11. Surface-active onion-like carbon nanospheres prepared by the method according to claim 4, wherein an Fe.sub.3O.sub.4 nanocrystalline metal kernel is coated inside the carbon nanosphere, and an outer layer being of an onion-like graphitized shell structure, with average particle size of 30 nm.
12. Surface-active onion-like carbon nanospheres prepared by the method according to claim 5, wherein an Fe.sub.3O.sub.4 nanocrystalline metal kernel is coated inside the carbon nanosphere, and an outer layer being of an onion-like graphitized shell structure, with average particle size of 30 nm.
13. Surface-active onion-like carbon nanospheres prepared by the method according to claim 6, wherein an Fe.sub.3O.sub.4 nanocrystalline metal kernel is coated inside the carbon nanosphere, and an outer layer being of an onion-like graphitized shell structure, with average particle size of 30 nm.
14. Surface-active onion-like carbon nanospheres prepared by the method according to claim 7, wherein an Fe.sub.3O.sub.4 nanocrystalline metal kernel is coated inside the carbon nanosphere, and an outer layer being of an onion-like graphitized shell structure, with average particle size of 30 nm.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1)
(2)
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DESCRIPTION OF THE EMBODIMENTS
(8) The following embodiments are merely preferred technical schemes of the present invention, and are not used for limiting the present invention in any form. A person skilled in the art may make various changes and variations. Any modification, equivalent replacement or improvements made within the spirit and principle of the present invention should fall within the protection scope of the present invention.
Embodiment 1
(9) Taking 2.5 mL (1.9 g) of n-dodecane and weighing 0.1 g of ferrocene, putting into 5 mL of deionized water together to perform ultrasonic mixing uniformly, and then putting the mixture into a quartz boat. Putting the quartz boat in the middle of a horizontal resistance furnace tube, and placing a glass slide at the tail portion in the furnace tube for products collection.
(10) Adjusting carrier gas flow to 30 mL/min by taking argon as a carrier gas to exhaust air in the furnace tube and start to heat; when temperature is risen to 100° C. at a temperature rise rate of 10° C./min, adjusting carrier gas flow down to 3 mL/min; continuing to rise temperature to 700° C. at a same temperature rise rate, adjusting carrier gas flow to 5 mL/min, and reacting for 20 min, so that vaporized n-dodecane performs sufficient carbonation reaction in a high temperature reaction zone to deposit on the glass slide prearranged in the furnace tube.
(11) After reaction is ended, adjusting carrier gas flow to 10 mL/min, naturally cooling to room temperature and then taking out the glass slide, and scraping to collect a black sediment on the glass slide, to obtain the pure surface-active onion-like carbon nanospheres.
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Embodiment 2
(17) Taking 1.5 mL (1.1 g) of n-dodecane and weighing 0.1 g of ferrocene, putting into 5 mL of deionized water together to perform ultrasonic mixing uniformly, and then putting the mixture into a quartz boat. Putting the quartz boat in the middle of a horizontal resistance furnace tube, and placing a glass slide at the tail portion in the furnace tube for products collection.
(18) Performing carbonation reaction according to conditions of embodiment 1, to prepare surface-active onion-like carbon nanospheres with particle size of about 30 nm.
Embodiment 3
(19) Taking 2.5 mL (1.9 g) of n-dodecane and weighing 0.1 g of ferrocene, putting into 10 mL of deionized water together to perform ultrasonic mixing uniformly, and then putting the mixture into a quartz boat. Putting the quartz boat in the middle of a horizontal resistance furnace tube, and placing a glass slide at the tail portion in the furnace tube for products collection.
(20) Performing carbonation reaction according to conditions of embodiment 1, to prepare surface-active onion-like carbon nanospheres with particle size of about 30 nm.
Comparative Example 1
(21) Taking 3.5 mL (2.6 g) of n-dodecane and weighing 0.1 g of ferrocene, putting into 5 mL of deionized water together to perform ultrasonic mixing uniformly, and then putting the mixture into a quartz boat. Putting the quartz boat in the middle of a horizontal resistance furnace tube, and placing a glass slide at the tail portion in the furnace tube for products collection, and performing carbonation reaction according to conditions of embodiment 1.
(22)
Comparative Example 2
(23) Taking 2.5 mL (1.9 g) of n-dodecane and weighing 0.1 g of ferrocene, putting into 5 mL of deionized water together to perform ultrasonic mixing uniformly, and then putting the mixture into a quartz boat. Putting the quartz boat in the middle of a horizontal resistance furnace tube, and placing a glass slide at the tail portion in the furnace tube for products collection.
(24) Adjusting carrier gas flow to 30 mL/min by taking argon as a carrier gas to exhaust air in the furnace tube and start to heat; when temperature is risen to 100° C. at a temperature rise rate of 10° C./min, adjusting carrier gas flow down to 3 mL/min; continuing to rise temperature to 600° C. at a same temperature rise rate, adjusting carrier gas flow to 5 mL/min, and reacting for 20 min, so that vaporized n-dodecane performs sufficient carbonation reaction in a high temperature reaction zone to deposit on the glass slide prearranged in the furnace tube.
(25) After reaction is ended, adjusting carrier gas flow to 10 mL/min, naturally cooling to room temperature and then taking out the glass slide, and scraping to collect a black sediment on the glass slide.
(26) It may be seen from a transmission electron microscope morphological image of a prepared product shown in
Comparative Example 3
(27) Other conditions are all the same as those in embodiment 1, and the difference only lies in that reaction is only performed for 10 min after temperature rises to 700° C., and then an obtained produced is collected.
(28) Because reaction time is too short, the carbon source fails to be effectively carbonized and adhered to the catalyst Fe.sub.3O.sub.4 metal particles, the transmission electron microscope image of the corresponding product is similar to that in
Comparative Example 4
(29) Other conditions are all the same as those in embodiment 1, and the difference only lies in that reaction is extended to 30 min after temperature rises to 700° C., and then an obtained product is collected.
(30) Due to reaction time extension and carrier gas purging, under the action of surface tension and diffusion force, catalyst particles are held up, to push a thermal carbon layer to grow along a length direction, meanwhile, pyrolytic carbon settles continuously, so as to finally obtain multi-walled carbon nanotubes.