会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 4. 发明专利
    • REGENERATING TYPE AIR PREHEATER
    • JPH0947636A
    • 1997-02-18
    • JP20359295
    • 1995-08-09
    • BABCOCK HITACHI KK
    • MUKAI MASATONARITA TSUNEO
    • B01D53/86
    • PROBLEM TO BE SOLVED: To reduce the possibility of blocking of a catalyst by acidic ammonium sulfate by disposing an NH, decomposing catalyst on the gas inlet side of an air preheater element. SOLUTION: An NH3 decomposing catalyst 2 is disposed on the gas inlet side, namely the upstream side of an air preheater element 6 of an air preheater 1. The air preheater 1 is arranged on the downstream of a denitration device and outlet gas of the deaeration gas is passed through the air preheater 1 and flowed into a stack in a system. Gaseous exhaust gas is introduced into the air preheater 1, and denitration and NH3 decomposition are carried out by an NH3 decomposing catalyst 2 disposed on an inlet to the air preheater 1. As a result, NOx is 10ppm at the outlet 2 of the NH3 decomposing catalyst, and NH3 is reduced by the amount more than the amount of consumption in denitration and decreased to 5ppm. As the NH3 concentration is lowered as above-mentioned, the possibility of blocking of the air preheater element 6 generated by acidic ammonium sulfate is reduced, and the stabilized operation of the air preheater 1 can be carried out.
    • 8. 发明专利
    • OPERATION OF DENITRATION DEVICE AND WASTE GAS PURIFYING DEVICE
    • JPH10109017A
    • 1998-04-28
    • JP26288396
    • 1996-10-03
    • BABCOCK HITACHI KK
    • MUKAI MASATONARITA TSUNEO
    • F23J15/00B01D53/56B01D53/86B01D53/94
    • PROBLEM TO BE SOLVED: To prevent the clogging of an air preheater generated by a precipitation of an acidic ammonium sulfate due to an unreacted ammonia or a corrosion of equipment succeeding a low temp. element of the air preheater due to SO3 . SOLUTION: At the time of denitrating a waste gas generated by burning the a fuel containing many sulfur content and vanadium (V) content, for example, fuel oil C, asphalt, natural asphalt, oil coke, etc., a vanadium concn. in a denitration catalyst 7 is increased by sticking of the vanadium incorporated in the waste gas to the denitration catalyst 7, and SO2 oxidation rate is increased with the lapse of an operation time of the denitration device 6. Then a detection of a SO3 concn. is executed at an outlet of the denigration device 6 according to the lapse of the operation time of the denitration device 6, and when an increase in the SO3 concn. at the outlet of the denitration device 6 is recognized, the SO2 oxidation rate is always kept at a low level and a SO3 generating amount is suppressed by controlling a waste gas temp. so that an operation temp. of the denigration device 6 may be decreased gradually from 380 deg.C. Here, the SO2 oxidation rate by the denitration catalyst 7 is affected by the gas temp., for example, when the gas temp. exceeds around 370 deg.C, the oxidation rate has a tendency to rise rapidly.
    • 10. 发明专利
    • COAL-WATER SLURRY COMBUSTION APPARATUS
    • JPS6073204A
    • 1985-04-25
    • JP18251383
    • 1983-09-30
    • BABCOCK HITACHI KK
    • MIURA KAZUONARITA TSUNEOTERADA HIROSHISHIYOUJI KAZUNORI
    • B01D53/50B01D53/77F23B99/00F23J15/04
    • PURPOSE:To decrease the quantity of supplying water to a system, and the power consumption for an induced fan, by decreasing the wet rate and the volume of exhaust gas, as well as to recover circulating liquid by a cooling pipe while it is circulating through the absorption tower of a desulfurizer, in a boiler system for combustion of coal-water slurry, combined with an exhaust gas desulfurizer of wet type. CONSTITUTION:Exhaust gas generated in a boiler 1 is led into the cooling tower 3 of a wet type exhaust gas desulfurizer, after the temperature in the gas is lowered down to about 80 deg.C by a gas . gas heat exchanger 9. The gas is cooled by cooling water which is circulating through the cooling tower 3 by a circulating pump 4, and then the gas is led into an absorption tower 5, where sulfurous acid in the gas is absorbed by lime- water slurry fed into the absorption tower 5. The purified exhaust gas is heated again in the gas . gas heat exchanger 9 in order to prevent white smoke, and is exhausted outside from a stack 10. In this case, the quantity of cooling water circulated by the pump 4 can be saved by the method of cooling slurry by dipping a cooling pipe 7 in the slurry in the absorption tower 5. Besides, the consumption of power for an induced fan can be saved as much as the volume corresponding to the decreased exhaust gas, by installing an induced fan 2 on the downstream side of an exhaust gas desulfurizer.