| Project/Area Number |
06452428
|
|---|
| Research Category |
Grant-in-Aid for General Scientific Research (B)
|
| Allocation Type | Single-year Grants |
|---|
| Research Field |
エネルギー学一般・原子力学
|
|---|
| Research Institution | NAGOYA UNIVERSITY |
|---|
Principal Investigator |
MATSUDA Hitoki NAGOYA UNIV., Energy Engineering and Science, Associate Professor, 工学部, 助教授 (80115633)
|
|---|
| Co-Investigator(Kenkyū-buntansha) |
WATANABE Fujio NAGOYA UNIV., Chemical Engineering, Research Associate, 工学部, 助手 (70109312)
ITAYA Yoshinori NAGOYA UNIV., Energy Engineering and Science, Research Associate, 工学部, 助手 (50176278)
|
|---|
| Project Period (FY) |
1994 – 1995
|
| Project Status |
Completed (Fiscal Year 1995)
|
| Budget Amount *help |
¥3,100,000 (Direct Cost: ¥3,100,000)
Fiscal Year 1995: ¥1,000,000 (Direct Cost: ¥1,000,000)
Fiscal Year 1994: ¥2,100,000 (Direct Cost: ¥2,100,000)
|
|---|
| Keywords | Chemical Heat Pipe / Thermal Energy Transportation / Heat Exchange / Catalytic Reaction / Tube-Wall Reactor / Catalytic Packed-Bed / Equilibrium of Reaction / Chemical Heat Pump |
|---|
| Research Abstract |
The heat excahge characteristics accompanied by an exothermic reaction at heat demand end of a chemical heat pipe system using SO_2/O_2/SO_3 reversible thermochemical reaction was discussed in a lab-scale unit. The effects of the reactant gas composition, the mass flow rate of reactant gas and heat exchange medium on the reaction and the heat exchange characteristics were discussed. Furthermore, a cpmparison between the experimental and calculated results obtained by using a two-dimensional mathematical model, in which the reaction and heat transfer was considered simultaneously, was performed. It was found that the heat exchange characteristics obtained from experiments can be explained tendentiously by the calcutated results. Under the adiabatic conditions, the temperature difference between the outlet and the inlet of the heat exchange medium increased with an increase of the mass flow rate of SO_2 and a decrease of the mass flow rate of the heat exchange medium, while the efficiency on the heat exchange process decreased with an increase of the mass flow rate of SO_2 and a decrease of the mass flow rate of the heat exchange medium.
In order to examine the temperature upgrading effect of the proposed chemical heat pipe, a calculation was made to estimate the effect of reaction pressure on the temperature upgrading. It is shown that the temperature difference, that is, the effect of temperature upgrading increased with an increase in both the molar ratio of SO_2 and the pressure in the reactor of heat demand end. On the other hand, it is shown that the value of COP increased with an increase in the molar ratio of SO_2 but decreased slightly with an increase of pressure in reactor of heat demand end. Consequently, it was clear that SO_2/O_2/SO_3 system can be to apply as a chemical heat pipe with chemical heat-pump function.
|
