大氮肥
大氮肥
대담비
LARGE SCALE NITROGENOUS FERTILIZER INDUSTRY
2011年
3期
169-170,193
,共3页
冷氨泵%汽化%流量%校核计算
冷氨泵%汽化%流量%校覈計算
랭안빙%기화%류량%교핵계산
cold ammonia pump%vaporization%flow%check calculation
分析冷氨泵低速运行时打量突然下降的主要原因是由于泵打量过低,不足以将热量带走,液氨在泵的某一级或几级入口过热汽化造成的。根据机组已知的设计参数计算实际工况下冷氨泵在2608r/min转速运转时,为保证泵内液氨不汽化,散热所需的最小流量为13.54m^3/h。
分析冷氨泵低速運行時打量突然下降的主要原因是由于泵打量過低,不足以將熱量帶走,液氨在泵的某一級或幾級入口過熱汽化造成的。根據機組已知的設計參數計算實際工況下冷氨泵在2608r/min轉速運轉時,為保證泵內液氨不汽化,散熱所需的最小流量為13.54m^3/h。
분석랭안빙저속운행시타량돌연하강적주요원인시유우빙타량과저,불족이장열량대주,액안재빙적모일급혹궤급입구과열기화조성적。근거궤조이지적설계삼수계산실제공황하랭안빙재2608r/min전속운전시,위보증빙내액안불기화,산열소수적최소류량위13.54m^3/h。
Aiming at a sudden drop of pumping capacity of cold-ammonia pump under running at a low speed, the analysis confirms that this is caused by an over-heat vaporization of liquid ammonia at the suction of one stage or at the suctions of some stages owing to a low pumping capacity insufficient to take the heat away. In order to ensure a non-vaporization of liquid ammonia in the pump, the minimum flow needed for heat release is 13.54 m^3/h calculated with the known design parameters of the cold-ammonia pump running at the actual condition of 2608r/min.