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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

Inactive Publication Date: 2006-06-08
NAT INST OF ADVANCED IND SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0016] That is, it is an object of the first embodiment of the present invention to solve the aforementioned problems of background art and provide a chemical reactor capable of efficiently excluding nitrogen oxides with low power consumption wherein the amount of current required to break down nitrogen oxides is reduced by using pairs of adsorbent substances which are selective for oxygen molecules and nitrogen oxide molecules to facilitate absorption of nitrogen oxides when excess oxygen is present in exhaust gas.
[0054] In the present invention, it is possible to apply current or the like only when the performance of the chemical reaction system has declined in order to ionize and remove by pumping oxygen adsorbed by the oxygen deficient part of the chemical reaction part. Moreover, it is possible to simultaneously reenergize the reduction phase. In this way, the amount of current in the present invention can be much less than the amount of current required for oxygen pumping in conventional electrochemical cell systems.

Problems solved by technology

However, because the exhaust gas from lean burning engines and diesel engines, which allow improved fuel consumption, contains an excess of oxygen, reduction of catalytic activity due to adsorption of oxygen by the surface of the ternary catalyst is a problem, preventing exclusion of nitrogen oxides.
However, the problem is that in the aforementioned method if there is an excess of oxygen in the exhaust gas, because the adsorption and decomposition reaction sites of the coexisting oxygen and nitrogen oxides consist of the same oxygen defects, the adsorption probability of the nitrogen oxides is much lower than that of the oxygen molecules for reasons of both molecular selectivity and coexisting molecular ratios, so that a large flow of current is required to break down the nitrogen oxides, greatly increasing electric power consumption.
However, because in this method residual oxygen molecules in the treated gas which have passed through the upper part of the same layer are still more selectively adsorbed and degraded in the reaction sites than are the nitrogen oxides, the reduction in energy consumption is inadequate.
Moreover, another problem with this method is that the reduction in energy consumption is inadequate because current needs to be supplied continuously in order to remove coexisting oxygen molecules.
Porous membranes which allow selective permeation of molecules include zeolites and other having nanopores, but synthesis of dense zeolite membranes without pinholes has not been established.
However, in a reaction method using a reaction separation membrane in which an ion conductor membrane is provided with electrodes and voltage is applied between the electrodes with the field gradient as the drive force, oxidation and reduction ability is high but selectivity is low.
For example, when removing nitrogen oxides by reduction in a reactor in which the aforementioned ion conductor is provided with electrodes, if oxygen molecules are present they are also broken down into oxygen ions, reducing the efficiency of the reduction removal of nitrogen oxides which is the objective of exhaust gas purification.
Moreover, while a simple oxidation-reduction reaction using a reducing agent or oxidizing agent with suitable selectivity is also possible, in this case the reducing agent or oxidizing agent needs to be supplied or replaced because the reaction cannot continue once this has been exhausted.

Method used

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  • Chemical reaction system of electrochemical cell type, method for activation thereof and method for reaction
  • Chemical reaction system of electrochemical cell type, method for activation thereof and method for reaction
  • Chemical reaction system of electrochemical cell type, method for activation thereof and method for reaction

Examples

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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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Abstract

The present invention relates to a chemical reaction system for efficiently excluding nitrogen oxides with low power consumption when excess oxygen is present in exhaust gas, to a method of use therefor, to an activation method therefor, and to a reaction method for oxidizing or reducing by the use of an oxidation-reduction reactor with high selectivity without the need to supply or exchange a reducing agent or oxidizing agent.

Description

TECHNICAL FIELD [0001] The present invention relates to an electrochemical cell-type chemical reaction system, and more specifically relates to a chemical reaction system which efficiently excludes nitrogen oxides from exhaust gas containing oxygen. The present invention is useful in that it provides a novel chemical reactor which has micro reaction regions for performing oxidation and reduction reactions on a target substance introduced into part of the chemical reaction part of the aforementioned chemical reaction system so that oxygen and nitrogen oxides are separated and adsorbed from exhaust gas by particular structures within the aforementioned micro reaction regions, thus allowing a target substance to be efficiently processed with low electric power consumption. [0002] Moreover, the present invention relates to an energy-saving electrochemical reaction system and an activation method therefor, and relates more particularly to a chemical reaction system which efficiently excl...

Claims

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Application Information

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IPC IPC(8): C25C7/04C25C7/00B01D53/86F01N3/08F01N3/20
CPCB01D53/8631F01N3/0892Y02T10/26F01N2570/14F01N3/2013Y02A50/20Y02T10/12
Inventor AWANO, MASANOBUFUJISHIRO, YOSHINOBUHAE, JIN HWANGKANZAKI, SHUZOBREDIKHIN, SERGEIKATAYAMA, SHINGOHIRAMATSU, TAKUYASHIONO, OSAMU
Owner NAT INST OF ADVANCED IND SCI & TECH