4 research outputs found
Heat of Fusion of Na3AlF6 Eutectic Mixtures with CaF2 and Al2O3
The heat of fusion of eutectic mixtures of sodium cryolite with alumina and calcium fluoride was measured using differential scanning calorimetry. Melting temperatures were found to be in good agreement with literature data. The molar heat of fusion of cryolite salts and eutectic mixtures was found to be directly dependent on melting temperature. The temperature dependence coefficient is the same as that of alkali halides
ΠΠ½Π°Π»ΡΠ· ΠΏΠΎΠΊΠ°Π·Π½ΠΈΠΊΡΠ² Π½Π°Π΄ΡΠΉΠ½ΠΎΡΡΡ ΠΏΡΠΈ ΠΊΠ°ΡΠΊΠ°Π΄Π½ΠΈΡ ΡΠ΅ΡΠΌΠΎΠ΅Π»Π΅ΠΊΡΡΠΈΡΠ½ΠΈΡ ΠΎΡ ΠΎΠ»ΠΎΠ΄ΠΆΡΠ²Π°ΡΠΈΠ² Ρ ΡΡΠ·Π½ΠΈΡ ΡΡΡΡΠΌΠΎΠ²ΠΈΡ ΡΠ΅ΠΆΠΈΠΌΠ°Ρ
Strict requirements for the operating conditions for thermally loaded elements of radio-electronic systems contribute to essential relevance of the problem of increasing the indices of reliability of thermoelectric coolers in the implementation of their thermal modes. This leads to the need for increasing the indices of reliability not only through the use of new materials, design and technological solutions, but also optimization of the current modes of thermoelectric modules.The aim of this work is the search for the possibility of increasing the indices of reliability of cascade thermoelectric coolers, without changing their design parameters and material of thermoelements, by the selection of current modes at varied operating conditions.In the work we proposed a mathematical model of interrelation of the relative magnitude of the failure rate of two-stage thermoelectric device with the number of thermoelements, relative operating current, thermal load, and temperature difference in the temperature range of workability of a cooler.We carried out comparative analysis of the main significant parameters and indices of reliability of two-stage thermoelectric coolers for different current modes of operation in a wide range of temperature differences from =60Β K to =90Β K, taking into account the thermal load. It was demonstrated that with an increase in the general temperature difference, the ratio of the number of thermoelements in the adjacent cascades increases, the total number of thermoelements increases, the refrigeratory coefficient decreases, the relative magnitude of the failure rate grows and the probability of failure-free operation decreases. We obtained expression for determining the optimum relative operating current, at which the minimum value of relative number of thermoelements in the cascades is observed.Comparative analysis of the main parameters and indices of reliability demonstrated the possibility of selection and implementation of different current modes of operation of a cascade thermoelectric cooler for the varied operation conditions. Two extremeΒ (characteristic) modes were proposed: the mode providing a minimum number of thermoelements, that is, minimum mass and overall dimensions of device; and the mode, providing the minimum failure rate and the maximum probability of failure-free operation. The proposed modes may be applied in the process of designing thermoelectric devices of minimum mass and increased reliability.Π Π°ΡΡΠΌΠΎΡΡΠ΅Π½Π° ΠΌΠΎΠ΄Π΅Π»Ρ Π²Π·Π°ΠΈΠΌΠΎΡΠ²ΡΠ·ΠΈ ΠΏΠΎΠΊΠ°Π·Π°ΡΠ΅Π»Π΅ΠΉ Π½Π°Π΄Π΅ΠΆΠ½ΠΎΡΡΠΈ ΠΈ ΠΎΡΠ½ΠΎΠ²Π½ΡΡ
Π·Π½Π°ΡΠΈΠΌΡΡ
ΠΏΠ°ΡΠ°ΠΌΠ΅ΡΡΠΎΠ² Π΄Π²ΡΡ
ΠΊΠ°ΡΠΊΠ°Π΄Π½ΠΎΠ³ΠΎ ΡΠ΅ΡΠΌΠΎΡΠ»Π΅ΠΊΡΡΠΈΡΠ΅ΡΠΊΠΎΠ³ΠΎ ΠΎΡ
Π»Π°Π΄ΠΈΡΠ΅Π»Ρ, ΡΠ°Π±ΠΎΡΠ°ΡΡΠ΅Π³ΠΎ Π² ΡΠ°Π·Π»ΠΈΡΠ½ΡΡ
ΡΠΎΠΊΠΎΠ²ΡΡ
ΡΠ΅ΠΆΠΈΠΌΠ°Ρ
ΠΏΡΠΈ ΠΏΠΎΡΠ»Π΅Π΄ΠΎΠ²Π°ΡΠ΅Π»ΡΠ½ΠΎΠΌ ΡΠ»Π΅ΠΊΡΡΠΈΡΠ΅ΡΠΊΠΎΠΌ ΡΠΎΠ΅Π΄ΠΈΠ½Π΅Π½ΠΈΠΈ ΠΊΠ°ΡΠΊΠ°Π΄ΠΎΠ². ΠΡΠΎΠ²Π΅Π΄Π΅Π½ ΡΡΠ°Π²Π½ΠΈΡΠ΅Π»ΡΠ½ΡΠΉ Π°Π½Π°Π»ΠΈΠ· ΠΎΡΠ½ΠΎΠ²Π½ΡΡ
Π·Π½Π°ΡΠΈΠΌΡΡ
ΠΏΠ°ΡΠ°ΠΌΠ΅ΡΡΠΎΠ² ΠΈ ΠΏΠΎΠΊΠ°Π·Π°ΡΠ΅Π»Π΅ΠΉ Π½Π°Π΄Π΅ΠΆΠ½ΠΎΡΡΠΈ ΠΎΡ
Π»Π°Π΄ΠΈΡΠ΅Π»Π΅ΠΉ Π΄Π»Ρ ΡΠ°Π·Π»ΠΈΡΠ½ΡΡ
ΡΠΎΠΊΠΎΠ²ΡΡ
ΡΠ΅ΠΆΠΈΠΌΠΎΠ² ΡΠ°Π±ΠΎΡΡ Π² ΡΠΈΡΠΎΠΊΠΎΠΌ Π΄ΠΈΠ°ΠΏΠ°Π·ΠΎΠ½Π΅ ΠΏΠ΅ΡΠ΅ΠΏΠ°Π΄ΠΎΠ² ΡΠ΅ΠΌΠΏΠ΅ΡΠ°ΡΡΡΡ ΠΎΡ ΞΠ’=60 K Π΄ΠΎ ΞΠ’=90 K Ρ ΡΡΠ΅ΡΠΎΠΌ ΡΠ΅ΠΏΠ»ΠΎΠ²ΠΎΠΉ Π½Π°Π³ΡΡΠ·ΠΊΠΈΠ ΠΎΠ·ΡΠΎΠ±Π»Π΅Π½Π° ΠΌΠΎΠ΄Π΅Π»Ρ Π²Π·Π°ΡΠΌΠΎΠ·Π²βΡΠ·ΠΊΡ ΠΏΠΎΠΊΠ°Π·Π½ΠΈΠΊΡΠ² Π½Π°Π΄ΡΠΉΠ½ΠΎΡΡΡ Ρ ΠΎΡΠ½ΠΎΠ²Π½ΠΈΡ
Π·Π½Π°ΡΡΡΠΈΡ
ΠΏΠ°ΡΠ°ΠΌΠ΅ΡΡΡΠ² Π΄Π²ΠΎΠΊΠ°ΡΠΊΠ°Π΄Π½ΠΎΠ³ΠΎ ΡΠ΅ΡΠΌΠΎΠ΅Π»Π΅ΠΊΡΡΠΈΡΠ½ΠΎΠ³ΠΎ ΠΎΡ
ΠΎΠ»ΠΎΠ΄ΠΆΡΠ²Π°ΡΠ°, ΡΠΎ ΠΏΡΠ°ΡΡΡ Ρ ΡΡΠ·Π½ΠΈΡ
ΡΡΡΡΠΌΠΎΠ²ΠΈΡ
ΡΠ΅ΠΆΠΈΠΌΠ°Ρ
ΠΏΡΠΈ ΠΏΠΎΡΠ»ΡΠ΄ΠΎΠ²Π½ΠΎΠΌΡ Π΅Π»Π΅ΠΊΡΡΠΈΡΠ½ΠΎΠΌΡ Π·βΡΠ΄Π½Π°Π½Π½Ρ ΠΊΠ°ΡΠΊΠ°Π΄ΡΠ². ΠΠ°Π²Π΅Π΄Π΅Π½ΠΎ ΠΏΠΎΡΡΠ²Π½ΡΠ»ΡΠ½ΠΈΠΉ Π°Π½Π°Π»ΡΠ· ΠΎΡΠ½ΠΎΠ²Π½ΠΈΡ
Π·Π½Π°ΡΡΡΠΈΡ
ΠΏΠ°ΡΠ°ΠΌΠ΅ΡΡΡΠ² Ρ ΠΏΠΎΠΊΠ°Π·Π½ΠΈΠΊΡΠ² Π½Π°Π΄ΡΠΉΠ½ΠΎΡΡΡ ΠΎΡ
ΠΎΠ»ΠΎΠ΄ΠΆΡΠ²Π°ΡΠ° Π΄Π»Ρ ΡΡΠ·Π½ΠΈΡ
ΡΡΡΡΠΌΠΎΠ²ΠΈΡ
ΡΠ΅ΠΆΠΈΠΌΡΠ² Ρ ΡΠΈΡΠΎΠΊΠΎΠΌΡ Π΄ΡΠ°ΠΏΠ°Π·ΠΎΠ½Ρ ΠΏΠ΅ΡΠ΅ΠΏΠ°Π΄ΡΠ² ΡΠ΅ΠΌΠΏΠ΅ΡΠ°ΡΡΡΠΈ Π²ΡΠ΄ ΞΠ’=60 K Π΄ΠΎ ΞΠ’=90 K Π· ΡΡΠ°Ρ
ΡΠ²Π°Π½Π½ΡΠΌ ΡΠ΅ΠΏΠ»ΠΎΠ²ΠΎΠ³ΠΎ Π½Π°Π²Π°Π½ΡΠ°ΠΆΠ΅Π½Π½
Phase transitions and thermal expansion of cryolite based eutectic mixture in solid state
ΠΡΠ»ΠΈ ΠΈΡΡΠ»Π΅Π΄ΠΎΠ²Π°Π½Ρ Π½Π΅ΠΊΠΎΡΠΎΡΡΠ΅ ΡΠ²ΡΠ΅ΠΊΡΠΈΡΠ΅ΡΠΊΠΈΠ΅ ΡΠΌΠ΅ΡΠΈ ΠΊΡΠΈΠΎΠ»ΠΈΡΠ° Π½Π°ΡΡΠΈΡ Ρ Al[2]O[3] ΠΈ CaF[2], Π° ΡΠ°ΠΊΠΆΠ΅ Π½Π΅ΠΊΠΎΡΠΎΡΡΠ΅ Π»Π΅Π³ΠΊΠΎΠΏΠ»Π°Π²ΠΊΠΈΠ΅ ΡΠ²ΡΠ΅ΠΊΡΠΈΡΠ΅ΡΠΊΠΈΠ΅ ΡΠΌΠ΅ΡΠΈ. ΠΠΎΠ»ΡΡΠ΅Π½Π½ΡΠ΅ ΡΠ΅Π·ΡΠ»ΡΡΠ°ΡΡ ΠΏΠΎΠΊΠ°Π·ΡΠ²Π°ΡΡ Π½Π΅ΡΠΊΠΎΠ»ΡΠΊΠΎ ΡΠΎΡΠ΅ΠΊ ΠΏΠ΅ΡΠ΅Ρ
ΠΎΠ΄Π° Π΄Π»Ρ ΡΠΌΠ΅ΡΠ΅ΠΉ Π½Π° ΠΎΡΠ½ΠΎΠ²Π΅ ΠΊΡΠΈΠΎΠ»ΠΈΡΠ° Π½Π°ΡΡΠΈΡ