化肥设计
化肥設計
화비설계
CHEMICAL FERTILIZER DESIGN
2011年
4期
50-52
,共3页
邵士铭%卢海鹰%阿不都热合木·托乎提%张中亚
邵士銘%盧海鷹%阿不都熱閤木·託乎提%張中亞
소사명%로해응%아불도열합목·탁호제%장중아
弛放气%一段炉%高压蒸汽%压力下降%措施
弛放氣%一段爐%高壓蒸汽%壓力下降%措施
이방기%일단로%고압증기%압력하강%조시
releasing gas%primary reformer%high pressure steam%pressure drop%measures
分析了塔里木大型化肥装置因一段炉燃料气系统压力波动,导致高压蒸汽压力从10.7 MPa递减下降至8.92 MPa,并使整个系统接近高压蒸汽跳车的原因:①弛放气设定压力降低导致放空阀打开;②高压用户用汽量增加;③高压废锅产汽量下降。结果表明,通过提高一段炉温度、调整高压合成氨系统负荷、调整高压蒸汽透平抽气量、增加快装锅炉产气量等相应措施,高压蒸汽压力逐步稳定和提高,合成氨工况恢复了正常。
分析瞭塔裏木大型化肥裝置因一段爐燃料氣繫統壓力波動,導緻高壓蒸汽壓力從10.7 MPa遞減下降至8.92 MPa,併使整箇繫統接近高壓蒸汽跳車的原因:①弛放氣設定壓力降低導緻放空閥打開;②高壓用戶用汽量增加;③高壓廢鍋產汽量下降。結果錶明,通過提高一段爐溫度、調整高壓閤成氨繫統負荷、調整高壓蒸汽透平抽氣量、增加快裝鍋爐產氣量等相應措施,高壓蒸汽壓力逐步穩定和提高,閤成氨工況恢複瞭正常。
분석료탑리목대형화비장치인일단로연료기계통압력파동,도치고압증기압력종10.7 MPa체감하강지8.92 MPa,병사정개계통접근고압증기도차적원인:①이방기설정압력강저도치방공벌타개;②고압용호용기량증가;③고압폐과산기량하강。결과표명,통과제고일단로온도、조정고압합성안계통부하、조정고압증기투평추기량、증가쾌장과로산기량등상응조시,고압증기압력축보은정화제고,합성안공황회복료정상。
Author has analyzed the reason causing the whole system to approach trip of the high pressure steam due to pressure fluctuation of the fuel gas system of primary reformer in Talimu Large-sized chemical fertilizer plant,it made the pressure of high pressure steam decreased progressively from 10.7 MPa to 8.92 MPa,result indicates that decreasing the setting pressure makes the venting valve opened;the steam consume of the high pressure steam users is increased;the steam production is decreased for high pressure steam of waste heat boiler,that leads to pressure drop of the high pressure steam pipeline network.Through appropriate measures of elevating the temperature of primary reformer,adjusting the load of high pressure ammonia synthesis system,controlling the steam extraction of high pressure steam turbine and increasing the steam production of package boiler and so on,the pressure of the high pressure steam is gradually stabilized and increased,it makes operating condition restored to the normal state.