Category filter:

Acronym	Definition
NU	University of Nebraska
NU	Northeast Utilities
NU	National University (various worldwide)
NU	Niue (The Country of Niue)
NU	Nicaragua
NU	Northwestern University (Evanston, IL, USA)
NU	Nunavut (Nunavut, Canada)
NU	Northeastern University (Boston, MA, USA)
NU	Niagara University (Niagara County, New York, USA)
NU	Newcastle United
NU	Next Up
NU	Nations Unies (French: United Nations)
NU	Nations Unies (United Nations)
NU	Naresuan University (Thailand)
NU	Naciones Unidas (Spanish: United Nations)
NU	Nações Unidas (Portuguese: United Nations)
NU	Northwood University
NU	Norton Utilities
NU	Nixon University (online university)
NU	Nahdlatul Ulama (Indonesia Islam organization)
NU	National Underwriter (Insurance Magazine)
NU	Name Unknown
NU	Nazioni Unite (Italian: United Nations)
NU	Niue Island (ISO country code)
NU	Nusselt Number (ratio of convective to conductive properties)
NU	Nagoya University (Japan)
NU	Nuoro, Sardegna (Italian province)
NU	Non-Uniformity
NU	Non-Ultra (Nvidia)
NU	Natural Uranium
NU	New Urbanist (architecture)
NU	Nova University
NU	Neuropathic Ulcer
NU	Nile University (Egypt)
NU	Number Unobtainable (telecommunications)
NU	Number Unobtainable
NU	Nikki-Universal Co., Ltd. (Japan)
NU	Neighborhood Unit
NU	NATO Unclassified
NU	NationsUniversity (online university)
NU	Normalized Unit
NU	Non Upset (thread end finish)
NU	Nationality Undetermined

References in periodicals archive

It is increasing nanoparticles volume fraction enhances the Nusselt number. By increasing the volume fraction of nanofluid the thermal conductivity of the fluid increases which enhanced the heat transfer.

Performance of the heat transfer behavior of Tri Ethylene Glycol (TEG) based cuo and sin nanofluids in a rectangular pipe under the turbulent flow condition

When no combustion takes place, it is known that the Nusselt number is proportional to [Re.sup.0.5] in the stagnation region, while [Re.sup.0.8] in the wall-jet region [21].

Modified Regression Rate Formula of PMMA Combustion by a Single Plane Impinging Jet

Using the temperature field, the heat transfer coefficient at the surface can be obtained, which, in the nondimensional form, in terms of the Nusselt number, is given by

On a Bivariate Spectral Homotopy Analysis Method for Unsteady Mixed Convection Boundary Layer Flow, Heat, and Mass Transfer due to a Stretching Surface in a Rotating Fluid

Friction factor of each flow rate for nanofluid which can be found in single-phase flow cannot be used for calculating friction factor as well as Nusselt number as presented by Hussein [13].

Improving the Hybrid Photovoltaic/Thermal System Performance Using Water-Cooling Technique and Zn-[H.sub.2]O Nanofluid

Nusselt Number. The nondimensional Nusselt number Nu = -([partial derivative][theta]/[partial derivative]R)[|.sub.R=1] is obtained from the temperature profile (11) as

Unsteady Natural Convection Flow past an Infinite Cylinder with Thermal and Mass Stratification

Table 3 and table 4 respectively presents the results for local Nusselt number for Prandtl number and Eckert number.

MHD MICROPOLAR FLUIDS FLOW AND HEAT TRANSFER OVER A STRETCHING SHEET

Based on the same approximations of the previous case and using the model for turbulence, the velocity, the temperature profiles, and the Nusselt number at the base wall have been predicted for three different temperatures on its right inclined wall.

Investigation of attic space airflow and temperature distribution using a computational fluid dynamics program

To validate present numerical results the local Nusselt number and the drag coefficient were compared with the earlier numerical results by (Bharti et al.

LOW REYNOLDS NUMBER CONVECTIVE HEAT TRANSFER ACROSS A CIRCULAR CYLINDER WITH UNIFORM VOLUMETRIC ENERGY DISSIPATION

Zarkadas (2005) proposed a relationship to calculate the internal mean Nusselt number of a thermal developing region based on the inside Nusselt number calculated by Hickman's approach and the incremental heat transfer number calculated by Hsu's approach:

Polymeric Hollow Fiber Heat Exchangers: Liquid-to-Gas Application

Using the geometric parameters L/D = 3 and H/D = 2 for circular cross-section, the normalized pressure drop ([DELTA][p.sup.*]), and Nusselt number for third module of the parallel plate channel, when compared with the values of Kundu et al.

Thermohydraulic performance of a series of in-line noncircular ducts in a parallel plate channel