化工学报
化工學報
화공학보
JOURNAL OF CHEMICAL INDUSY AND ENGINEERING (CHINA)
2014年
10期
3798-3804
,共7页
梁法春%杨桂云%王金龙%于皓
樑法春%楊桂雲%王金龍%于皓
량법춘%양계운%왕금룡%우호
气液两相流%分配%数值模拟%相分离%控制%临界流
氣液兩相流%分配%數值模擬%相分離%控製%臨界流
기액량상류%분배%수치모의%상분리%공제%림계류
gas-liquid flow%distribution%numerical simulation%phase splitting%control%critical flow
提出了一种新型气液两相流分配器,主要由旋流叶片、整流器、分流喷嘴以及分配腔室组成。通过采用“流型调整”与“临界分流”控制相分离。为研究不同分流比下的分配特征,设计了2喷嘴和4喷嘴两种分配结构。建立了气液两相流数值模型,模拟了气液两相流在分配器内流动特性。在气液两相流实验环道上进行了测试,气相折算速度范围为5.0~25.0 m·s-1,液相折算速度范围为0.012~0.14 m·s-1,实验中出现的流型包括波浪流、段塞流以及环状流。结果表明,在临界分流条件下,气液相分流系数主要取决于与侧支管相连通的分流喷嘴数目与总喷嘴数目的比值,不受流型、气液流速等参数波动的影响。对于2喷嘴分配器分流系数接近理论值0.5,对于4喷嘴气液分流系数约为0.25。
提齣瞭一種新型氣液兩相流分配器,主要由鏇流葉片、整流器、分流噴嘴以及分配腔室組成。通過採用“流型調整”與“臨界分流”控製相分離。為研究不同分流比下的分配特徵,設計瞭2噴嘴和4噴嘴兩種分配結構。建立瞭氣液兩相流數值模型,模擬瞭氣液兩相流在分配器內流動特性。在氣液兩相流實驗環道上進行瞭測試,氣相摺算速度範圍為5.0~25.0 m·s-1,液相摺算速度範圍為0.012~0.14 m·s-1,實驗中齣現的流型包括波浪流、段塞流以及環狀流。結果錶明,在臨界分流條件下,氣液相分流繫數主要取決于與側支管相連通的分流噴嘴數目與總噴嘴數目的比值,不受流型、氣液流速等參數波動的影響。對于2噴嘴分配器分流繫數接近理論值0.5,對于4噴嘴氣液分流繫數約為0.25。
제출료일충신형기액량상류분배기,주요유선류협편、정류기、분류분취이급분배강실조성。통과채용“류형조정”여“림계분류”공제상분리。위연구불동분류비하적분배특정,설계료2분취화4분취량충분배결구。건립료기액량상류수치모형,모의료기액량상류재분배기내류동특성。재기액량상류실험배도상진행료측시,기상절산속도범위위5.0~25.0 m·s-1,액상절산속도범위위0.012~0.14 m·s-1,실험중출현적류형포괄파랑류、단새류이급배상류。결과표명,재림계분류조건하,기액상분류계수주요취결우여측지관상련통적분류분취수목여총분취수목적비치,불수류형、기액류속등삼수파동적영향。대우2분취분배기분류계수접근이론치0.5,대우4분취기액분류계수약위0.25。
A novel distributor consisting of a swirl vane, nozzles and fluid splitting rooms was proposed to distribute gas-liquid two-phase flow evenly. The swirl van was used to change upstream flow patterns into annular flow with uniform film thickness to make sure all the nozzles have same inlet condition and the nozzles were used to accelerate the gas-liquid mixture to achieve critical flow. In order to investigate the distributor behavior under different extraction ratios, a 2-nozzle and a 4-nozzle distributor were designed. A numerical model was developed to simulate the gas and liquid velocity vector distribution in the distributor. The simulation results showed that all the nozzles had similar flow behavior if their outlet pressures were equal. Experiments were conducted in an air-water two-phase flow loop, with the distributor horizontally installed. Superficial gas velocity varied from 5.0 m·s-1 to 25.0 m·s-1, liquid superficial velocity was in the range of 0.012-0.14 m·s-1. The flow patterns observed during the tests included wavy flow, annular flow and slug flow. It was found that gas and liquid splitting ratio was determined by the number of the nozzles and was independent of flow patterns, gas and liquid superficial velocity and resistance characteristic of the downstream pipeline. The splitting ratios of the 2-nozzle and 4-nozzle distributors were 0.5 and 0.25 respectively.