PHOSPHORUS, SULFUR, AND SILICON
5
Table . The TG-MS results for PR, Mo- and CoMo-containing resin precursors.
Weight loss (%)
Assignment
Sample
>°C
Resin dehydration
Resin dehydration and MoO formation
Resin dehydration and CoMoOx formation
>°C
PR
.
.
.
.
.
.
Resin carburization
Resin carburization and MoC formation
Resin carburization and CoMoCx formation
Mo precursor
CoMo precursor
which was probably due to the carburization of resin to produce raw resin was dried at 110°C for 12 h, and then ground to a
carbon.[27] A large quantity of multi-component gases were fine powder. After that, the resin powder was incipient-wetness
detected by MS and the simultaneous signals of m/z = 2, 16, 18 impregnated by an aqueous solution of (NH4)6Mo7O24·4H2O,
and 28 corresponded to H2, CH4, H2O and C2H4, respectively. or an aqueous solution of (NH4)6Mo7O24·4H2O and
In comparison to the PR, the TG-MS profiles of Mo- and CoMo- Co(NO3)2·6H2O mixture (1:1 Mo:Co ratio) with a 30 wt%
containing resin precursors showed several different features in Mo loading. The slurries were evaporated at 110°C for 12 h
both the low- and the high-temperature stages. On the one hand, to obtain Mo- and CoMo-containing resin precursors. Finally,
we observed that in the low-temperature regions (see Figs. 6b about 1.0 g of the dried resin precursor was packed in the mid-
and c), the difficulty in the dehydration of resin ranked in the dle of a 4.2 cm ID, quartz tubular reactor. The quartz reactor
order of CoMo-containing resin (215°C) < Mo-containing was heated with a tubular electric resistance furnace equipped
resin (360°C) < PR (400°C). The results indicated that Mo and with a temperature controller (purchased from Xiamen Yudian
Co metal species (especially for Co) can facilitate the dehydra- Automation Technology Co. Ltd.) and the temperature was mea-
tion of resin. And the weight losses of Mo and CoMo precursors sured with a thermocouple placed adjacent to the sample inside
(25.89 and 22.58%) were less than that of PR (see Table 1), the reactor. The carrier gas (Ar or H2) was controlled using mass
which suggested the formation of MoOx and CoMoOx.[27] On flow controllers (purchased from Beijing Sevenstar Electronics
the other hand, in the high-temperature ranges (Figs. 6b and c), Co. Ltd.) and was introduced at a flow rate of 50 mL min−1. The
the TG curves showed another strong weight losses around 830 precursor was heated from room temperature (RT) to a given
and 790°C for Mo and CoMo precursors, respectively, but the value at a rate of 10°C min−1 and maintained at this temperature
weight losses (26.87 and 26.36%) were more than that of PR (see for different times from 1 to 48 h, followed by cooling to RT
Table 1). In addition, MS curves showed that a large amount under Ar or H2 flow, and then passivated in a 1% O2/Ar flow
of CO was evolved, accompanied with a small amount of CO2. for 2 h. A series of products were obtained from heating at 500,
The facts indicated that the high-temperature carburization 600, 630, 650, 700, 800 and 900°C, designated as Mo-Ar/H2-T-t
stages of Mo- and CoMo-containing resin precursors involved and CoMo-Ar/H2-T-t for Mo and CoMo samples, respectively
strong redox reactions, leading to the formation of carbides. (T = 500, 600, 630, 650, 700, 800 and 900, t = 1, 6, 12, 24
It was therefore reasonable to conclude that the solid product or 48).
(i.e. carbon) from thermal carburization of resin should serve
as a reducing agent in these redox reactions. In addition, there
was a consumption of the H2 generated at about 600°C during
Sample characterizations
carburization processes, which contributed more or less to the
reduction of oxide precursors. It was obvious from Figs. 6b and
c that the final carbide products were formed at 830 and 790°C
for Mo- and CoMo-containing resin precursors, respectively.
The results also indicated that the addition of Co to resin
precursor facilitated the formation of carbide, which was in
accord with the XRD analyses (Figs. 2 and 3).
The formation processes of carbides under H2 atmo-
sphere via carbothermal reduction method were proposed as
following.[20] Reduction of metal oxides by hydrogen; reaction
between partially reduced oxides and surface carbon atoms
of carbon materials under the hydrogen atmosphere. The
processes were similar to those under Ar mentioned above.
However, it can be seen from Figs. 2 and 3 that H2 atmosphere
facilitated the formation of carbides at lower temperatures than
Ar atmosphere.
X-ray diffraction (XRD) measurements were carried out using
Cu Kα source with a X’Pert Pro MPD diffractometer. BET
surface area and pore structure of the sample were measured
through nitrogen adsorption at liquid-nitrogen tempera-
ture (77 K) by a surface area analyzer (NOVA4200). The
morphologies and microstructure of the products were char-
acterized by transmission electron microscopy (TEM, Philips
Tecnal 10) equipped with an EDX system. Thermogravimetry-
mass spectrometry (TG-MS) experiments were performed
using thermoanalyzer STA 449 F5 Jupiter coupled with
quadrupolar mass-spectrometer QMS 403 D Aeolos. The
samples were heated in a stream of pure Ar gas at a rate of 10°C
Table . The major indexes and properties of the phenolic resin.
Index/Property
Value
-
.
.
.
Experimental
BET surface areab (m g−
)
Sample preparation
Average pore diameterb (nm)
Total pore volumeb (cm− g−
)
The raw resin used was a phenolic resin (PR, [C6H6O·CH2O]x,
purchased from Wuxi Xinyehao Chemical Co. Ltd.) and the
major indexes and properties were listed in Table 2. Firstly, the
aProvided by the company.
bObtained by BET surface area measurement.