Chemical reaction system of electrochemical cell type, method for activation thereof and method for reaction
a chemical reaction system and electrochemical cell technology, applied in the field of electrochemical cell type chemical reaction system, can solve the problems of increasing electric power consumption, reducing catalytic activity, and inadequate reduction of energy consumption, and achieves high reactivity, high reactivity, and reduced power consumption
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example 1
[0081] Zirconia stabilized with yttria was used as ion conduction phase 4, in a disk form with a diameter of 20 mm and a thickness of 0.5 mm. Reduction phase 3 was a mixed layer of platinum and zirconia, while working electrode layer 2 was a film consisting of a mixture of nickel oxide and yttria-stabilized zirconia. A platinum film was first screen printed to an area of about 1.8 cm2 on one side of ion conduction phase 4, and formed by heat treatment at 1200° C. A mixed film of nickel oxide and yttria-stabilized zirconia was screen printed on the platinum film with the same area as the platinum film, and formed by heat treatment at 1450° C. The compounding ratio of nickel oxide to yttria-stabilized zirconia was 6:4 mole. Once a platinum film had been screen printed to an area of 1.8 cm2 on the other side of ion conduction phase 4 having a formed reduction phase, it was formed by heat treatment at 1200° C. to make oxidation phase 5. Barrier layer 1 was formed on the upper part of wo...
example 2
[0084] In the energizing and heating process of the final stage of preparing a chemical reaction system as in Example 1, four cycles were performed in which current of 1.2 V to 25 mA was supplied between cathode 3 and anode 5 as the temperature was raised to 650° C. and maintained for 1 hour after which the current was stopped, followed by gradual cooling, and the relationship between number of cycles and ability to process nitrogen oxides was investigated. With 2 cycles a nitrogen oxide removal rate of 50% was achieved at a current density of 25 mA / cm2 and an electric energy consumption of 49 mW / cm2, while with 3 cycles this fell to a current density of 24 mA / cm2 and an electric energy consumption of 47 mW / cm2, but with 4 cycles the results were similar to those achieved with 3 cycles.
example 3
[0085] Changes in reactivity in a chemical reaction system prepared as in Example 1 were investigated relative to amount of coexisting oxygen impeding the reaction and concentration of nitrogen oxides which were the target substance. Under the same experimental conditions as in Example 1, current density and electric energy consumption at 50% degradation were measured (a) with the oxygen amount increased from 2% to 10% and (b) with the nitrogen oxide concentration reduced from 1000 ppm to 500 ppm. The results were (a) current density 55 mA / cm2, electric energy consumption 150 mW / cm2 and (b) current density 20 mA / cm2, electric energy consumption 37 mW / cm2, respectively, showing that in the chemical reaction system of the present invention relative processing ability is improved even with a large amount of coexisting oxygen, while a dramatic improvement in performance is seen with respect to a weak nitrogen oxide concentration.
[0086] Examples of the second embodiment of the present i...
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