Differences of Dimensions in Analysis

AI Thread Summary
Zero-dimensional models treat a system as a single point with no spatial variation, while one-dimensional models incorporate variations along a single axis, allowing for more complexity in analysis. Quasi-one-dimensional models bridge the gap by simplifying multi-dimensional systems into a one-dimensional framework while retaining some spatial characteristics. The choice of dimensionality impacts the accuracy and applicability of thermochemical analyses, particularly in combustion modeling, where zero-dimensional models may overlook critical spatial dynamics. Understanding these differences is essential for effectively applying mathematical models to gaseous systems and improving predictive capabilities in thermochemical studies.
Magno
Messages
1
Reaction score
0
When analyzing/studying thermochemistry or any system with gases, i.e., combustion, fusion, fuel cells, often time in the literature the system is derived or modeled as being zero-dimensional or quasi-one dimensional.
Can anyone provide a good explanation as to the differences between 0, 1, and quasi-1 dimensions or explain what the use of this mathematics gains you in analyzing/studying gaseous systems?

As an example: concerning combustion modeling using turbulent kenetic energy densities and fuel concentrations where the author is using a zero-dimension for analysis.

"...this formulation based on the k-ε model commonly used in three-dimensional simulations is not particularly suitable for zero-dimensional models."

Again, can anyone provide a good explanation as to the differences between 0, 1, and quasi-1 dimensions or explain what the use of this mathematics gains you in analyzing/studying gaseous systems?
 
Last edited:
Engineering news on Phys.org
Hi all, I have a question. So from the derivation of the Isentropic process relationship PV^gamma = constant, there is a step dW = PdV, which can only be said for quasi-equilibrium (or reversible) processes. As such I believe PV^gamma = constant (and the family of equations) should not be applicable to just adiabatic processes? Ie, it should be applicable only for adiabatic + reversible = isentropic processes? However, I've seen couple of online notes/books, and...
I have an engine that uses a dry sump oiling system. The oil collection pan has three AN fittings to use for scavenging. Two of the fittings are approximately on the same level, the third is about 1/2 to 3/4 inch higher than the other two. The system ran for years with no problem using a three stage pump (one pressure and two scavenge stages). The two scavenge stages were connected at times to any two of the three AN fittings on the tank. Recently I tried an upgrade to a four stage pump...
Back
Top