power removal
2.DESIGN AND APPLICATION OF CONTROL SYSTEM FOR ASH AND CLINKER REMOVAL IN LARGE-SCALE POWER PLANT
3.Under the optimum condition that the solid/liquid ratio was 1 20(5.0g modified Al2O3 mixed with 100mL phenol 50 % solution) , microwave power was 50W, and the time of the irradiation was 5 min , the phenol removal rate could come up to 92.24% and COD removal rate reached up to 79.13 %. The catalyst could be reused more than 9 times remaining the high rate of the dye removal .
5.The original pneumatic ash removal system in Anshun Power Plant can not meet the normal requirements for ash handing. Clyde Huatong Material Handling Company Limited has adopted the concentrated phase pneumatic ash removal technique and retrofitted the ash handling system from the bottom outlet of the precipitator hopper to the inlet of the ash tank.
6.The effects of grit sizes of wheel, wheel speed, contact force, wheel sharpening and coolant on the removal rate of PCD material are studied In conclusion, it suggested that the removal of PCD material is caused by mechanical force and the removal rate is higher as the effective grinding power is higher during grinding cutting tools
7.The addition agent of sulfur removal can improve the liquid transfer character of absorbent,mitigate the pH value of slurry,enhance the efficiency of sulfur removal and reduce the operational cost. It has the broad applied prospect in flue gas sulfur removal technique of coal-fired power generation plant in China.
9.A pilot test of moisturizing flue gas by spraying in Lan Zhou Second Thermal Power Plant has indicated that the secondary voltage and current running ESP rise 18%～20% and 16%～23%,respectively after the flue gas moisturized. The dust removal efficiency of the ESP is enhanced with different extent on different base efficiency
10.Although the removal efficiency on organics was improved by the increase of ultrasonic power, the capability of oxidation of the dividual sonolysis system was limited, and the time of reaction was so long, which proved the existence of optimal ultrasonic power of the oxidation processes, it was 2.60W/cm2 in this experiment;
