The hydraulic characteristics of flow through miniature slot orifices
Hydraulic characteristics of flow through miniature slot orifices for rocket engine injectors
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Hydraulic characteristics of flow through miniature slot orifices for rocket engine injectors
Orifice compensated hydrostatic face seal under pressure and thermal loading for aircraft gas turbine
Two dimensional potential flow representation of subsonic jet interference effects for jet orifice
Compressible flow of two component, two phase mixtures in nozzles and orifices
Near-free molecular flow through orifice measured for velocity distribution dependence on Knudsen number and angular position using time-of-flight technique
Liquid rocket engine injector elements design criteria, using noncircular orifice geometry to predict efficiency
Hydraulic characteristics of flow through miniature slot orifices for rocket engine injectors, observing stability of effluent liquid streams
Orifice length-to-diameter ratio effect on spray mixture uniformity from unlike impinging jets
Compressible flow of two component two phase mixtures through convergent nozzles and orifices, determining initially or annular dispersed flow patterns
Performance of simplex and dual orifice fuel nozzles with ambient and heated fuel in annular turbojet combustor
Test chambers with orifice and helium mass spectrometer for detecting leak rate of encapsulated semiconductor devices
A new geometry is described for low temperature diode heat pipes employing excess liquid to block the vapor space of the evaporator and part of the transport section during reverse mode conditions. An orifice plate is placed in the pipe at the blocking meniscus location, with the opening arranged to permit proper liquid distribution in both ground tests and zero 'g' operation. Parametric analytical results are presented for several fluids (carbon tetrafluoride, methane, and ethane). Experimental data is presented for a room temperature diode verifying feasibility, and a 1/4 in. O.D. cryogenic diode with methane working fluid.
The cold air flow field for a 1/27 cm orifice nozzle was determined for subsonic flow velocities. In addition, d.c. arc voltage, current, and diameter measurements were made for a range of velocities and arc gaps. Average voltage gradients increased rapidly as an arc extinguishing velocity was approached. Measured values of current and diameter were used as an input for relaxation solution of an energy balance equation to compute radial temperature profiles. Calculated arc voltage gradients compare favorably with measured average voltage gradients.
Module, consisting of transparent plastic cylinder containing separate suction and calibration chambers, allows static-pressure orifices to be calibrated, and rapidly checked for leaks. Device is compact, saves time, and improves accuracy, and reliability of pressure measurements.
Choked flow rate and pressure profile data were taken on sequential axially aligned inlets of the orifice and Borda type. The configuration consisted of from two to four inlets spaced at two nominal separation distances of 0.7 and 30 diameters. At the nominal 30 diameter spacing, the reduced flow rate follows a simple empirical relation based on the reduced flow rate for a single inlet. At the nominal 0.7 diameter spacing, fluid jetting was prevalent at low temperatures and flow rates were the same as for a single inlet.
Critical mass flux and axial pressure profile data for fluid nitrogen are presented for N = 20, 15, 10, and 7 N-sequential orifice inlet configurations uniformly spaced at 15.5 cm. These data correlate well over a wide range in reduced temperature (0.7 T sub r,o ambient) and reduced pressure (to P sub r = 2) and are in general agreement with studies of one to four inlets and labyrinth seal gas data for 33 tooth equivalent sequential inlets. Experimental and theoretical agreement is good for liquid and gas critical mass flux.
Choked flow rate and pressure profile data were taken on sequential axially aligned inlets of the orifice and Borda type. The configuration consisted of from two to four inlets spaced at two nominal separation distances of 0.7 and 30 diameters. At the nominal 30 diameter spacing, the reduced flow rate follows a simple empirical relation based on the reduced flow rate for a single inlet. At the nominal 0.7 diameter spacing, fluid jetting was prevalent at low temperatures and flow rates were the same as for a single inlet. Previously announced in STAR as N81-30391