1116
L.L. Bai et al. / Chinese Chemical Letters 22 (2011) 1115–1118
1
. Experimental
Gas phase photochlorination (GPPC): p-Xylene (0.52 mol) was added to a three neck flask with a jacket reactor,
and the reaction was initiated by fluorescent lamp near the jacket reactor. During the photochlorination, the reaction
medium in the flask was evaporated and reacted with the chlorine gas in the jacket reactor. The chlorinated p-xylene
fell into the flask because of their higher boiling points than that of the reactant. The photochlorination conditions were
as follows: the temperature in the jacket reactor was controlled at 138 8C by transparent heatcycling oil bath; the liquid
temperature in the flask was gradually raised from 138 8C to 205 8C; the flow rate of Cl was 20 mL/min; the reaction
2
time was 11.5 h. After photochlorination, the chlorizates (86.89 g) were obtained.
The synthesis of the hypercrosslinked resins could be mainly classified into three approaches: (1) copolymerization
of chlorizates with benzene; (2) self-polymerization of chlorizates; (3) further postcrosslinking of the resin obtained
from approach 1.
Copolymerization reaction: The GPPC chlorizates (1.6993 g) and benzene (0.2373 g) were added to 1,2-
dichloroethane solution (10 mL) containing anhydrous FeCl (0.1399 g) and dissolved by ultrasonic means. The
3
polymerization was carried through at 60 8C for 5 h and then 80 8C for 6 h, and the resulted brown resin was washed
with HCl (aq.), extracted with acetone in a Soxhlet apparatus and dried at 80 8C under vacuum, respectively. The resin
2
(1.1533 g, BET surface: 810.05 m /g) was obtained.
1
Self-polymerization reaction: The GPPC chlorizates (1.7160 g) were added to a solution of FeCl (0.1437 g) in
3
anhydrous 1,2-dichloroethane (10 mL), and dissolved by ultrasonic means. The polymerization was carried through at
0 8C for 5 h and then 80 8C for 6 h, and the resulted resin was washed with HCl (aq.), extracted with acetone in a
Soxhlet apparatus and dried at 80 8C under vacuum, respectively. The resin 2 was obtained (0.8687 g, BET surface:
6
2
6
28.1 m /g).
Post crosslinking reaction: The resin 1 (0.5620 g) was added to 1,2-dichloroethane solution (10 mL) containing
FeCl (0.0315 g), and swelled at ambient temperature for 5 h. The post crosslinking reaction was carried through at
3
8
0 8C for 17 h, and the resulted resin was filtered and then washed with HCl (aq.), extracted with acetone in a Soxhlet
apparatus and dried at 80 8C under vacuum, respectively. The resulted P-resin 1 was obtained (0.5342 g, BET surface:
2
037.6 m /g).
1
2
. Results and discussion
The photochlorination of alkyl aromatic hydrocarbon is a kind of continuous competitive reaction. Chlorination
degree and isomer species would increase along with the increase of the photochlorination time, the components of the
chlorizates were determined via GC–MS as shown in Fig. 1 and the proportion of each product was monitored by GC.
The final contents of the GPPC chlorizates were as follows: a-chloro-p-xylene: 16.24%; a,a-dichloro-p-xylene: 7.5%;
0
0
0
a,a -dichloro-p-xylene: 47.25%; a,a,a ,a -tetrachloro-p-xylene: 20.59%.
In our investigation, the GPPC chlorizates could be used in the synthesis of hypercrosslinked resin in the
subsequent polymerization, various chloromethyl aromatic compounds could participate in the construction of
hypercrosslinked matrix and the further investigation for the photochlorination is in progress.
Our earlier investigation has demonstrated that the porous adsorptive resin could be obtained via the
0
copolymerization of 1,4-dichlomethyl benzene (XDC) or 4,4 -dichlomethyl diphenyl (CMB) with benzene or
diphenyl [8]. Being different to the pore formation mechanism of traditional hypercrosslinked resin, the novel porous
resins were synthesized in a homogeneous solution system, and went through initial oligomerization and subsequent
phase separation process during the formation of crosslinked network and pore structure. The preliminary results in
this paper further indicated that the mixed chloride species could be used in the preparation of porous resin, and the
[(Fig._1)TD$FIG]
Fig. 1. GC–MS of the main components of GPPC chlorination intermediate.