制冷学报
製冷學報
제랭학보
JOURNAL OF REFRIGERATION
2014年
4期
25-33
,共9页
朱建鲁%季鹏%李玉星%王武昌%高嵩
硃建魯%季鵬%李玉星%王武昌%高嵩
주건로%계붕%리옥성%왕무창%고숭
板翅式换热器%封头结构%倾斜%气液两相%分配特性
闆翅式換熱器%封頭結構%傾斜%氣液兩相%分配特性
판시식환열기%봉두결구%경사%기액량상%분배특성
plate fin heat exchanger%header structure%tilt%two-phase%flow distribution
海上平台受到海浪的作用会发生晃动和倾斜,从而影响板翅式换热器的入口工质分配特性。通过空气-水两相工质分配实验系统,分别进行封头结构水平状态和倾斜状态下的单相以及气液两相实验,获得不同实验工况下的封头工质分配特性,研究倾斜对封头工质分配的影响,从而为换热器的安装及工艺的改进提供依据。结果表明:水平状态下工质分配受惯性力的影响,不均匀度随雷诺数和气液比的增加而增大;倾斜状态下流体受到惯性力和重力的双重影响,工质分配均匀程度显著低于水平状态,倾斜角越大工质分配越不均匀,气液比越大工质分配受倾斜影响程度越大;固定封头或安装换热器时应严格保证其水平/竖直状态,或者通过液化工艺及换热器设计的改进消除倾斜的影响。
海上平檯受到海浪的作用會髮生晃動和傾斜,從而影響闆翅式換熱器的入口工質分配特性。通過空氣-水兩相工質分配實驗繫統,分彆進行封頭結構水平狀態和傾斜狀態下的單相以及氣液兩相實驗,穫得不同實驗工況下的封頭工質分配特性,研究傾斜對封頭工質分配的影響,從而為換熱器的安裝及工藝的改進提供依據。結果錶明:水平狀態下工質分配受慣性力的影響,不均勻度隨雷諾數和氣液比的增加而增大;傾斜狀態下流體受到慣性力和重力的雙重影響,工質分配均勻程度顯著低于水平狀態,傾斜角越大工質分配越不均勻,氣液比越大工質分配受傾斜影響程度越大;固定封頭或安裝換熱器時應嚴格保證其水平/豎直狀態,或者通過液化工藝及換熱器設計的改進消除傾斜的影響。
해상평태수도해랑적작용회발생황동화경사,종이영향판시식환열기적입구공질분배특성。통과공기-수량상공질분배실험계통,분별진행봉두결구수평상태화경사상태하적단상이급기액량상실험,획득불동실험공황하적봉두공질분배특성,연구경사대봉두공질분배적영향,종이위환열기적안장급공예적개진제공의거。결과표명:수평상태하공질분배수관성력적영향,불균균도수뢰낙수화기액비적증가이증대;경사상태하류체수도관성력화중력적쌍중영향,공질분배균균정도현저저우수평상태,경사각월대공질분배월불균균,기액비월대공질분배수경사영향정도월대;고정봉두혹안장환열기시응엄격보증기수평/수직상태,혹자통과액화공예급환열기설계적개진소제경사적영향。
Offshore platforms will shake and tilt because of marine motion,which will influence flow distribution in the header of plate-fin heat exchanger. The distribution of pure water/air and air-water two-phase flow in horizontal and tilt state were conducted in the air-water two-phase flow distribution experimental apparatus. The effect of gas-liquid ratio and tilt angle on flow distribution in the header of plate-fin heat exchanger in tilt state were studied. The results show that flow distribution in static state is subject to the influence of the inertial force,and the flow distribution unevenness increases with the increase of the inlet flow and gas-liquid ratio. In tilt state,flow distribution is subject to the influence of both inertial force and gravity,and flow distribution evenness is much lower than the static state. Flow distri-bution unevenness increases with the increase of tilt angle,and is more sensitive to tilt when gas-liquid ratio increases. It is suggested that the header and heat exchanger should be fixed and installed strictly at horizontal/vertical state. Meanwhile the influence of tilt can be e-liminated through the improvement of liquefaction process and heat exchanger design.