磷肥与复肥
燐肥與複肥
린비여복비
PHOSPHATE & COMPOUND FERTILIZER
2012年
3期
20-22
,共3页
钙镁磷肥%大型化装置设计%节能降耗%环保
鈣鎂燐肥%大型化裝置設計%節能降耗%環保
개미린비%대형화장치설계%절능강모%배보
fused calcium magnesium phosphate (FCMP)%design of larger-scale unit%energy saving and consumption reduction%environmental protection
为达到大型钙镁磷肥装置节能降耗、环保的要求，介绍其设计的工艺流程及高炉、热风炉、煤气净化设备等主要设备的选择要求，该设计在云南大通磷化工公司的装置上实施，每吨钙镁磷肥折标焦耗不到200kg，送入高炉热风温度大于650℃，并有进一步节能降耗的空间。
為達到大型鈣鎂燐肥裝置節能降耗、環保的要求，介紹其設計的工藝流程及高爐、熱風爐、煤氣淨化設備等主要設備的選擇要求，該設計在雲南大通燐化工公司的裝置上實施，每噸鈣鎂燐肥摺標焦耗不到200kg，送入高爐熱風溫度大于650℃，併有進一步節能降耗的空間。
위체도대형개미린비장치절능강모、배보적요구，개소기설계적공예류정급고로、열풍로、매기정화설비등주요설비적선택요구，해설계재운남대통린화공공사적장치상실시，매둔개미린비절표초모불도200kg，송입고로열풍온도대우650℃，병유진일보절능강모적공간。
To satisfy the requirements of energy saving and emission reduction and environmental protection for larger-scale FCMP plant, the design process, the selection requirements of blast furnace, hot blast heater, the equipments for gas purification are introduced. With the application of this design on the plant of Yunnan Datong Phosphate Chemical Company, the coke consumption of one ton FCMP is less than 200 kg, the temperature of hot air to blast furnace is more than 650 ℃, there is some space of energy saving and consumption reduction.
