化肥设计
化肥設計
화비설계
CHEMICAL FERTILIZER DESIGN
2013年
4期
56-58
,共3页
陈世通%苏庆贺%林广顺%刘强%孙善楠
陳世通%囌慶賀%林廣順%劉彊%孫善楠
진세통%소경하%림엄순%류강%손선남
氨循环压缩机%冰机%氨回收系统%压力过高%填料泄漏%处理措施
氨循環壓縮機%冰機%氨迴收繫統%壓力過高%填料洩漏%處理措施
안순배압축궤%빙궤%안회수계통%압력과고%전료설루%처리조시
ammonia recycling compressor%refrigeration compressor%ammonia recovery system%pressure being too high%packing leakage%treatment measure
分析了氨回收系统压力过高的原因，提出了相应的处理措施。结果表明：通过技术改造，在负荷不变的情况下，冰机出口压力由1．48 MPa下降到1．05 MPa，风机由8台全开减少到只开5台，每年可节省电费450430．8元。
分析瞭氨迴收繫統壓力過高的原因，提齣瞭相應的處理措施。結果錶明：通過技術改造，在負荷不變的情況下，冰機齣口壓力由1．48 MPa下降到1．05 MPa，風機由8檯全開減少到隻開5檯，每年可節省電費450430．8元。
분석료안회수계통압력과고적원인，제출료상응적처리조시。결과표명：통과기술개조，재부하불변적정황하，빙궤출구압력유1．48 MPa하강도1．05 MPa，풍궤유8태전개감소도지개5태，매년가절성전비450430．8원。
Author has analyzed the cause being too high in ammonia recovery system, has supposed the appropriate treatment measure.Result indi-cates that outlet pressure of refrigeration compressor is reduced from 1.48MPa to 1.05MPa in case of no changed load through technical reformation, 8 fans fully opened can be reduced to 5 fans only opened, electric power fee can be saved by 450 430.8 Yuan RMB annually.
