Abstract:Experiments were performed with water discharging into air from horizontal and vertical tubes of several diameters. The horizontal tubes discharged into a variable space between vertical plates. The effects of length/diameter ratio and the shape of the end of the tube were investigated for the case of vertical tubes. In each case the conditions for the pipes to run full were associated with the formation and washout of large gas bubbles resembling those occurring in the slug flow regime of two-phase flow. The … Show more
“…As mentioned earlier, complete condensation was always achieved in the test section before discharging the flow into the separation tank where liquid and vapor existed with a stable interface. For the horizontal orientation and the three of complete condensation, the exit condition of stratified or full-tube was found to be independent of the rate of cooling and dependent only on the discharge flow rate (Wallis et al, 1977). The boundary between stratified and full tube shifted THE CANADIAN JOURNAL OF CHEMICAL ENGINEERING, VOLUME 71, FEBRUARY, 1993 to higher mass flow rates as the inclination angle increased (G = 128 kg/m2 .…”
Section: Flow Condition At the Condenser Exitmentioning
Flow regime data of condensing steam inside an inclined 13.4 mm ID tube are presented. The effect of upward and downward inclinations within ± 10° on the different transition lines is discussed. In all test runs, complete condensation has been achieved inside the condenser, with or without full tube at exit depending on the total mass flow rate and inclination angle. It is shown that the zones occupied by the wavy and slug regimes experience significant shifts, whereas the effect on the annular flow boundary appears to be insignificant at the present small inclination angles. The present data sets are compared with adiabatic gas‐liquid flow regime maps developed analytically and experimentally for horizontal and inclined tubes. Deviations due to the condensation process are observed; however, consistent trends are identified among the two types of flow.
“…As mentioned earlier, complete condensation was always achieved in the test section before discharging the flow into the separation tank where liquid and vapor existed with a stable interface. For the horizontal orientation and the three of complete condensation, the exit condition of stratified or full-tube was found to be independent of the rate of cooling and dependent only on the discharge flow rate (Wallis et al, 1977). The boundary between stratified and full tube shifted THE CANADIAN JOURNAL OF CHEMICAL ENGINEERING, VOLUME 71, FEBRUARY, 1993 to higher mass flow rates as the inclination angle increased (G = 128 kg/m2 .…”
Section: Flow Condition At the Condenser Exitmentioning
Flow regime data of condensing steam inside an inclined 13.4 mm ID tube are presented. The effect of upward and downward inclinations within ± 10° on the different transition lines is discussed. In all test runs, complete condensation has been achieved inside the condenser, with or without full tube at exit depending on the total mass flow rate and inclination angle. It is shown that the zones occupied by the wavy and slug regimes experience significant shifts, whereas the effect on the annular flow boundary appears to be insignificant at the present small inclination angles. The present data sets are compared with adiabatic gas‐liquid flow regime maps developed analytically and experimentally for horizontal and inclined tubes. Deviations due to the condensation process are observed; however, consistent trends are identified among the two types of flow.
“…This parameter was used successfully by Wallis et al (1977) in correlating the data of the onset of bubble formation in small-diameter tubes when the data deviated substantially from the theoretical predictions. Also, the Kutateladze-Tien empirical correlation for flooding (Tien et al 1980) uses C as a correction factor.…”
A mechanism is proposed suggesting that the wavy‐slug transition during horizontal condensation is initiated by a hydraulic jump. Based on this mechanism, a simple empirical correlation is developed and shown to be consistent in magnitude and trend with data for different fluids and different tube diameters. Further, a theoretical model is constructed for stratified two‐phase flow near the end of the condensation path utilizing the principles of mass, momentum and energy conservation. Results from the model together with the proposed slugging mechanism succeeded in defining a theoretical wavy‐slug transition line which agrees well with experimental flow regime data for a wide range of operating conditions.
“…Wallis et al [10] clearly demonstrated that the ow rate needed for a tube to run full at the exit when discharging a liquid into a gas-lled space is given by the following equation:…”
Section: Controlling Mechanism Of the Intermittent And Separated-flowmentioning
confidence: 99%
“…The impact of the parameters that control the type of exit condition can be easily quanti ed for any passage con guration or heat exchanger type by conducting relatively simple adiabatic experiments. This approach was adopted by Wallis et al [10] and Rabas [11].…”
Section: Parameters Affecting the Boundary Between The Intermittent-amentioning
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