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D B Geselowitz

Publications and source records attributed to D B Geselowitz.

79 records · Page 5Linked to original sources

Mean velocity and Reynolds stress measurements in the regurgitant jets of tilting disk heart valves in an artificial heart environment.

Laser Doppler velocimetry, with a high temporal resolution (1 ms time windows), was used to measure the flow field in two regions (major and minor orifices) near the aortic and mitral valves (Bjork Shiley monostrut Nos. 25 and 27, respectively) of the Penn State artificial heart. The motion of each valve was also investigated using a 1000 frame/s video camera in order to estimate the valve's closing velocity. Fluid velocities in excess of and opposite to valve closing velocity were detected near the valve, providing evidence of "squeeze flow." Maximum Reynolds shear stresses of approximately 20,000 dyn/cm2 and time-averaged Reynolds shear stresses of approximately 2000 dyn/cm2 were observed during the regurgitant flow phase. These elevated Reynolds shear stresses suggest that regurgitant jets play a role in the hemolysis and thrombosis associated with tilting disk heart valves in an artificial heart environment.

Aortic Valve↗

Mean velocities and Reynolds stresses within regurgitant jets produced by tilting disc valves.

Fluid velocities were measured with a two-component laser Doppler anemometry system in the regurgitant jet regions of Bjork-Shiley Delrin monostrut tilting disc valves mounted within a Plexiglas model of the 70 cm3 Penn State electric left ventricular assist device. At each measurement location, 250 instantaneous velocity realizations were collected at times when regurgitation through the valves occurred. The maximum Reynolds shear and normal stresses were calculated after filtering the data. Results show that Reynolds shear and normal stresses proximal to the mitral valve were elevated to magnitudes of 9,000 dynes/cm2 and 20,000 dynes/cm2, respectively. The peak Reynolds stresses near the mitral valve occurred during early systole, when regurgitant jet velocities reached magnitudes as high as 440 cm/sec. The Reynolds shear and normal stresses proximal to the aortic valve reached magnitudes of 9,900 dynes/cm2 and 20,500 dynes/cm2, respectively. The peak Reynolds stresses near the aortic valve occurred during early diastole, when regurgitant jet velocities were as high as 280 cm/sec. These high Reynolds stresses created by turbulent regurgitant flow have the potential to cause significant blood damage.

Aortic Valve↗

Ventricular assist device volume compensation using a two phase fluid.

A two-phase fluid (TPF) volume compensation chamber (VCC), using Freon as a working fluid, has been developed to reduce pressure fluctuations created in electric ventricular assist devices (VADs) during emptying and filling of the blood sac. The advantages of a TPF VCC over the currently employed flexible compliance chambers are as follows: 1) the TPF VCC has rigid external walls, eliminating the deleterious effects of fibrous ingrowth; 2) the internal diaphragm is made of Saran HB, which has a permeability two orders of magnitude less than that of butyl rubber; and 3) the TPF VCC has an external volume of 477 ml, comparable to that of the flexible compliance chambers used for electric VADs with a stroke volume of 100 ml. Experiments were conducted with the VCC attached to an electric VAD operated in a mock circulatory system. The results show that the strong temperature sensitivity of Freon vapor pressure does not compromise VAD flow output over a temperature range of 6 degrees C. Since body temperature generally fluctuates no more than 5 degrees C, this result is promising. A compromise is seen, however, in VAD power consumption. As the temperature of the VCC drops 6 degrees C, the mean pressure of the system drops 95 mmHg, causing an increase in power consumption that may require introduction of a temperature control system.

Blood Pressure↗

Estimation of Reynolds stresses within the Penn State left ventricular assist device.

Fluid velocities were measured using a two-component laser Doppler anemometery (LDA) system at 129 locations within a Plexiglas model of a 70 cm3 Penn State electric Left Ventricular Assist Device (LVAD). The LVAD was driven by a pulsatile piston pump acting on an attached segmented polyurethane diaphragm. Bjork-Shiley tilting disc valves were used to provide unidirectional flow through the inlet and outlet ports. A seeded blood analog fluid, which matched the kinematic viscosity of blood at high shear rates and the refractive index of Plexiglas, was used to make the measurements. At each location, 250 instantaneous velocity realizations were collected at eight instances during the pump cycle. The maximum Reynolds shear and normal stresses were calculated for each pump cycle time and location after filtering the data. The results reveal that the highest Reynolds shear and normal stresses occur in the near wall region just proximal to the aortic valve during diastole, and reach values of 5,300 dynes/cm2 and 10,800 dynes/cm2, respectively. The elevated turbulent stresses are observed during the period of regurgitant flow through the aortic valve, with peak stress values arising during the period of peak regurgitant flow. This supports the hypothesis that a regurgitant turbulent jet is formed near the wall of the prosthetic aortic valve and may be contributing to blood damage.

Blood Flow Velocity↗

Relative blood damage in the three phases of a prosthetic heart valve flow cycle.

Blood flow through a prosthetic heart valve operating in a ventricular assist device can be subdivided into three phases: a) forward flow through an open valve, b) rapid valve closure, and c) regurgitant back flow through a closed valve. Recent studies of fluid stresses in the Penn State Electric Left Ventricular Assist Device (PS LVAD) operating under physiologic conditions indicate that Reynolds stresses of possibly hemolytic magnitude may exist in the valve area. Although several studies have been made of the fluid stresses seen in forward flow through an open valve, few have looked at valve closure or backflow, and none have related these stresses directly to blood damage. In this study, novel in vitro blood flow loops were developed to allow for the separate analysis of the three flow phases of a Bjork-Shiley monostrut Delrin disk valve operating in a PS LVAD. Forward flow through fully open aortic and mitral valves and backflow through closed valves are studied separately in flow loops driven by a roller pump with the LVAD acting as a valve housing and compliance vessel. Valve closure is investigated with a PS LVAD operating in a low volume mock circulatory loop characterized by cavitation potential through stroboscopic videography of this mock loop, using saline as the working fluid. Rate of hemolysis, characterized by the index of hemolysis, IH, is determined for each of the three flow loops charged with fresh porcine blood.(ABSTRACT TRUNCATED AT 250 WORDS)

Animals↗

Three-component laser Doppler velocimetry measurements in the regurgitant flow region of a Björk-Shiley monostrut mitral valve.

Three-dimensional laser Doppler velocimetry measurements were acquired in a mock-circulatory loop proximal to a Björk-Shiley monostrut valve in the mitral position, and synchronous ensemble-averaging was applied to form an "average" beat. Two axial locations in the regurgitant flow region of the valve (in the minor orifice) were mapped, and maximum Reynolds shear stresses were calculated. A large spike in regurgitant flow was noted at the beginning of systole, which may be the squeeze flow phenomenon computed by other researchers. A region of sustained regurgitant flow 50 msec later was the focus of this study. Maximum velocities of approximately 3.7 mps were noted, and maximum Reynolds shear stresses of approximately 10,000 dyne/cm2 were calculated. Comparisons were made of two-dimensional (ignoring tangential component) versus three-dimensional shear stresses, and, in this case, in regions of high stress, the differences were insignificant. This suggests that the tangential component of velocity can probably be ignored in similar measurements where the tangential velocity is likely to be small.

Blood Flow Velocity↗