Chem. J. Chinese Universities ›› 2014, Vol. 35 ›› Issue (4): 755.doi: 10.7503/cjcu20130749
• Organic Chemistry • Previous Articles Next Articles
DU Yongmei, LI Chunying, ZHANG Jianwei, WANG Wei, KANG Jianping, LÜ Jian*()
Received:
2013-08-03
Online:
2014-04-10
Published:
2014-03-14
Contact:
LÜ Jian
E-mail:lujian204@sina.net
Supported by:
CLC Number:
TrendMD:
DU Yongmei, LI Chunying, ZHANG Jianwei, WANG Wei, KANG Jianping, LÜ Jian. Synthesis and Thermal Decomposition of Tetrahydrotricyclopentadiene as a High Density Hydrocarbon Fuel†[J]. Chem. J. Chinese Universities, 2014, 35(4): 755.
Test item | Test result | Test method |
---|---|---|
Density/(g·cm-3)(20 ℃) | 1.082 | GJB770B-2005 |
Combustionheat/(MJ·L-1) | 47.5 | GJB770B-2005 701.2 |
Flash point/℃ | 120 | GB/T261 |
Freezing point/℃ | 48—49 | GB/T2430-81 |
Table 1 Properties of tetrahydrotricyclopentadiene
Test item | Test result | Test method |
---|---|---|
Density/(g·cm-3)(20 ℃) | 1.082 | GJB770B-2005 |
Combustionheat/(MJ·L-1) | 47.5 | GJB770B-2005 701.2 |
Flash point/℃ | 120 | GB/T261 |
Freezing point/℃ | 48—49 | GB/T2430-81 |
Temperature/K | 973 | 973 | 1073 | 1073 | 1123 | 1123 |
---|---|---|---|---|---|---|
Pyrolysis time/s | 4 | 8 | 4 | 7 | 4 | 8 |
Product of methane(%) | 0.13 | 0.17 | 0.07 | 0.13 | 0.02 | 0.02 |
Product of ethylene(%) | 1.21 | 2.34 | 2.15 | 9.42 | 5.93 | 18.32 |
Product of ethane(%) | 0.28 | 0.42 | 0.42 | 1.32 | 0.78 | 2.74 |
Product of propylene(%) | 0.30 | 0.36 | 0.73 | 1.41 | 0.26 | 1.56 |
Product of propane(%) | 0.05 | 0.07 | 0.23 | 0.32 | 0.40 | 0.13 |
Product of butane(%) | 0.52 | 0.59 | 0.86 | 1.62 | 0.93 | 1.73 |
Product of penditene(%) | 0.03 | 0.23 | 0.13 | 0.14 | 0.02 | 0.02 |
Product of cyclopentene+cyclopenditene(%) | 2.44 | 4.12 | 3.81 | 8.46 | 3.47 | 7.08 |
Product of benzene(%) | 1.35 | 3.56 | 3.73 | 10.98 | 8.03 | 20.53 |
Product of toluene(%) | 0.53 | 1.75 | 1.52 | 2.59 | 1.82 | 6.97 |
Product of 5-penditenylcyclopenditene(%) | 1.85 | 2.04 | 0.62 | 2.48 | 0.85 | 3.83 |
Product of other(%) | 1.06 | 3.32 | 1.75 | 1.89 | 1.10 | 1.24 |
Product of conversion(%) | 9.32 | 18.97 | 16.02 | 40.76 | 23.61 | 64.17 |
Table 2 Reaction products during pyrolysis of tetrahydrotricyclopentadiene
Temperature/K | 973 | 973 | 1073 | 1073 | 1123 | 1123 |
---|---|---|---|---|---|---|
Pyrolysis time/s | 4 | 8 | 4 | 7 | 4 | 8 |
Product of methane(%) | 0.13 | 0.17 | 0.07 | 0.13 | 0.02 | 0.02 |
Product of ethylene(%) | 1.21 | 2.34 | 2.15 | 9.42 | 5.93 | 18.32 |
Product of ethane(%) | 0.28 | 0.42 | 0.42 | 1.32 | 0.78 | 2.74 |
Product of propylene(%) | 0.30 | 0.36 | 0.73 | 1.41 | 0.26 | 1.56 |
Product of propane(%) | 0.05 | 0.07 | 0.23 | 0.32 | 0.40 | 0.13 |
Product of butane(%) | 0.52 | 0.59 | 0.86 | 1.62 | 0.93 | 1.73 |
Product of penditene(%) | 0.03 | 0.23 | 0.13 | 0.14 | 0.02 | 0.02 |
Product of cyclopentene+cyclopenditene(%) | 2.44 | 4.12 | 3.81 | 8.46 | 3.47 | 7.08 |
Product of benzene(%) | 1.35 | 3.56 | 3.73 | 10.98 | 8.03 | 20.53 |
Product of toluene(%) | 0.53 | 1.75 | 1.52 | 2.59 | 1.82 | 6.97 |
Product of 5-penditenylcyclopenditene(%) | 1.85 | 2.04 | 0.62 | 2.48 | 0.85 | 3.83 |
Product of other(%) | 1.06 | 3.32 | 1.75 | 1.89 | 1.10 | 1.24 |
Product of conversion(%) | 9.32 | 18.97 | 16.02 | 40.76 | 23.61 | 64.17 |
Reation | R1 | R2 | R3 | R4 | R5 | R6 | R7 | R8 | R9 |
---|---|---|---|---|---|---|---|---|---|
Ratio | 0.120 | 0.105 | 0.107 | 0.110 | 0.107 | 0.111 | 0.111 | 0.110 | 0.121 |
Table 3 Ratio of reation routes
Reation | R1 | R2 | R3 | R4 | R5 | R6 | R7 | R8 | R9 |
---|---|---|---|---|---|---|---|---|---|
Ratio | 0.120 | 0.105 | 0.107 | 0.110 | 0.107 | 0.111 | 0.111 | 0.110 | 0.121 |
T/K | t/s | ln[1/(1-x)] | k | T/K | t/s | ln[1/(1-x)] | k |
---|---|---|---|---|---|---|---|
973 | 5 | 0.1823 | 0.03646 | 1123 | 5 | 0.5376 | 0.10755 |
1023 | 6 | 0.3098 | 0.05163 | 1153 | 8 | 1.0381 | 0.12976 |
1073 | 7 | 0.5036 | 0.07194 |
Table 4 Rate of constants of different temperature
T/K | t/s | ln[1/(1-x)] | k | T/K | t/s | ln[1/(1-x)] | k |
---|---|---|---|---|---|---|---|
973 | 5 | 0.1823 | 0.03646 | 1123 | 5 | 0.5376 | 0.10755 |
1023 | 6 | 0.3098 | 0.05163 | 1153 | 8 | 1.0381 | 0.12976 |
1073 | 7 | 0.5036 | 0.07194 |
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