This document summarizes the results of computational modeling of gas flow in a Holweck pump. The pump geometry was modeled as 2D grooved channels with varying dimensions and rarefaction parameters. Discrete velocity methods were used to solve the Boltzmann equation for the gas distribution function. Mass flow rates were computed for 126 combinations of channel length, width, depth and rarefaction parameter. The results showed a Knudsen minimum in the mass flow rate around a rarefaction parameter of 1, consistent with theory. Normalizing the results matched published data, validating the computational approach.
Numerical methods in Transient-heat-conductiontmuliya
This file contains slides on Numerical methods in Transient heat conduction.
The slides were prepared while teaching Heat Transfer course to the M.Tech. students in Mechanical Engineering Dept. of St. Joseph Engineering College, Vamanjoor, Mangalore, India, during Sept. – Dec. 2010.
Contents: Finite difference eqns. by energy balance – Explicit and Implicit methods – 1-D transient conduction in a plane wall – stability criterion – Problems - 2-D transient heat conduction – Finite diff. eqns. for interior nodes – Explicit and Implicit methods - stability criterion – difference eqns for different boundary conditions – Accuracy considerations – discretization error and round–off error - Problems
Numerical methods in Transient-heat-conductiontmuliya
This file contains slides on Numerical methods in Transient heat conduction.
The slides were prepared while teaching Heat Transfer course to the M.Tech. students in Mechanical Engineering Dept. of St. Joseph Engineering College, Vamanjoor, Mangalore, India, during Sept. – Dec. 2010.
Contents: Finite difference eqns. by energy balance – Explicit and Implicit methods – 1-D transient conduction in a plane wall – stability criterion – Problems - 2-D transient heat conduction – Finite diff. eqns. for interior nodes – Explicit and Implicit methods - stability criterion – difference eqns for different boundary conditions – Accuracy considerations – discretization error and round–off error - Problems
Estados de Tensión y Deformación - Resolución Ejercicio N° 2.pptxgabrielpujol59
Dadas las tensiones correspondientes a los planos x, y, z ortogonales y pasantes por un punto A. Se pide:
1. Determinar los valores de las tensiones principales en el
citado punto.
2. Calcular los invariantes J1, J2 y J3.
3. Determinar los valores de las tensiones principales en el
citado punto.
4. Calcular los cosenos directores de los planos
principales.
5. Representar gráficamente el estado tensional mediante
el diagrama de Mohr y en base al mismo determinar:
5.1. Las componentes de tensión en un plano determinado por los ángulos fi1, fi2, fi3, respecto de la
dirección de su normal.
5.2. La tensión tangencial máxima y los planos donde se verifica.
we select cantilever beam having I,C,T section and we select material cast iron, stainless steel, steel and analyze base upon modal and static analysis.we see here deformation,stress ,strain and based upon it we conclude.
Fluid Dynamics (Continuity Equation - Bernoulli Equation - head loss - Appli...Safen D Taha
Outline:
-Continuity Equation
-Types of flow rate
-Bernoulli Equation
-Applications of Bernoulli principle
-Bernoulli equation and head loss
-Properties of ideal and real fluid
Temperature change in a material leaves it with
mechanical expansion & significance
Changes in material properties.
Expansion due to heat, induce
Strains internally.
Hence stress induced
Estados de Tensión y Deformación - Resolución Ejercicio N° 2.pptxgabrielpujol59
Dadas las tensiones correspondientes a los planos x, y, z ortogonales y pasantes por un punto A. Se pide:
1. Determinar los valores de las tensiones principales en el
citado punto.
2. Calcular los invariantes J1, J2 y J3.
3. Determinar los valores de las tensiones principales en el
citado punto.
4. Calcular los cosenos directores de los planos
principales.
5. Representar gráficamente el estado tensional mediante
el diagrama de Mohr y en base al mismo determinar:
5.1. Las componentes de tensión en un plano determinado por los ángulos fi1, fi2, fi3, respecto de la
dirección de su normal.
5.2. La tensión tangencial máxima y los planos donde se verifica.
we select cantilever beam having I,C,T section and we select material cast iron, stainless steel, steel and analyze base upon modal and static analysis.we see here deformation,stress ,strain and based upon it we conclude.
Fluid Dynamics (Continuity Equation - Bernoulli Equation - head loss - Appli...Safen D Taha
Outline:
-Continuity Equation
-Types of flow rate
-Bernoulli Equation
-Applications of Bernoulli principle
-Bernoulli equation and head loss
-Properties of ideal and real fluid
Temperature change in a material leaves it with
mechanical expansion & significance
Changes in material properties.
Expansion due to heat, induce
Strains internally.
Hence stress induced
,friction pipe ,friction loss along a pipe ,pipe ,along a ,loss along ,loss along a ,friction loss ,friction loss along a ,loss along a pipe ,along a pipe ,friction loss alon ,friction loss along a p ,loss along a pip
Coarse CFD-DEM simulation of Rare Earth Element leaching reactor, FCC re-gen...Liqiang Lu
In past decades, the continuum approach was the only practical technique to simulate large-scale fluidized bed reactors because discrete approaches suffer from the cost of tracking huge numbers of particles and their collisions[1,. This study significantly improved the computation speed of discrete particle methods in two steps: First, the time-driven hard-sphere (TDHS) algorithm with a larger time-step is proposed allowing a speedup of 20-60 times; second, the number of tracked particles is reduced by adopting the coarse-graining technique gaining an additional 2-3 orders of magnitude speedup of the simulations. A new velocity correction term was introduced and validated in TDHS to solve the over-packing issue in dense granular flow. The TDHS was then coupled with the coarse-graining technique to simulate the heat transfer and chemical reaction mechanisms in an industrial FCC regenerator in a reasonable time with little computational resources. The simulation results compared well with available industrial data and proved that this new approach can be used for efficient and reliable simulations of industrial-scale fluidized bed systems.
References:
1. Lu, L., Liu, X., Li, T., Wang, L., Ge, W., Benyahia, S., 2017. Assessing the capability of continuum and discrete particle methods to simulate gas-solids flow using DNS predictions as a benchmark. Powder Technology 321, 301-309.
2. Lu, L.; Gopalan, B.; Benyahia, S., 2017. Assessment of different discrete particle methods ability to predict gas-particle flow in a small-scale fluidized bed. Industrial & Engineering Chemistry Research, 56, 7865–7876
3. Lu, L., Benyahia, S., Li, T., 2017. An efficient and reliable predictive method for fluidized bed simulation. AIChE Journal 63, 5320-5334.
4. Lu, L.; Konan, A.; Benyahia, S., 2017. Influence of grid resolution, parcel size and drag models on bubbling fluidized bed simulation. Chemical Engineering Journal, 326, 627-639.
5. Lu, L.; Morris, A.; Li, T.; Benyahia, S., 2017. Extension of a coarse grained particle method to simulate heat transfer in fluidized beds. Int. J. Heat Mass Transfer, 111, 723-735.
6. Lu, L., Yoo, K., Benyahia, S., 2016. Coarse-Grained-Particle Method for Simulation of Liquid–Solids Reacting Flows. Industrial & Engineering Chemistry Research 55, 10477-10491.
7. Lu, L., Xu, J., Ge, W., Gao, G., Jiang, Y., Zhao, M., Liu, X., Li, J., 2016. Computer virtual experiment on fluidized beds using a coarse-grained discrete particle method—EMMS-DPM. Chemical Engineering Science 155, 314-337.
8. Lu, L., Xu, J., Ge, W., Yue, Y., Liu, X., Li, J., 2014. EMMS-based discrete particle method (EMMS–DPM) for simulation of gas–solid flows. Chemical Engineering Science 120, 67-87.
OMAE2013-10454: Experimental Study on Flow Around Circular Cylinders with Low...Rodolfo Gonçalves
Experiments were carried out in a recirculating water channel regarding the flow around stationary circular cylinders with low aspect ratio piercing the water free surface. Eight different aspect ratios were tested, namely L/D= 0.1, 0.2, 0.3, 0.5, 0.75, 1.0, 1.5 and 2.0; this range corresponds to aspect ratio related to circular offshore systems, such as spar and monocolumn platforms. Force was measured using a six degree-of-freedom load cell and Strouhal number is inferred through the transverse force fluctuation frequency. The range of Reynolds number covers 10,000 < Re < 50,000. PIV measurements were performed in some aspect ratio cases, namely 0.3, 0.5, 1.0 and 2.0 for Reynolds number equal to 43,000. The results showed a decrease in drag force coefficients with decreasing aspect ratio, as well as a decrease in Strouhal number with decreasing aspect ratio. The PIV showed the existence of an arch-type vortex originated in the cylinder free end.
Energy losses in Bends, loss coefficient related to velocity head.Pelton Whee...Salman Jailani
In this slide you learn the how to make the lablayout and the study the Energy losses, Pelton Wheel. Kaplan TURBINE, Franices TURBine And its Efficiency of Mecahanical Power Plants..
00923006902338
The objective of this project was to identify various methods for well test in horizontal wells. Well test analysis in horizontal wells is applied to find the reservoir parameters like permeability and skin factor and the result from the chosen methods will be compared to the result of some famous software like Kappa Saphir, PanSystem, etc which are used in oil and gas industries.
Recruiting in the Digital Age: A Social Media MasterclassLuanWise
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3.0 Project 2_ Developing My Brand Identity Kit.pptxtanyjahb
A personal brand exploration presentation summarizes an individual's unique qualities and goals, covering strengths, values, passions, and target audience. It helps individuals understand what makes them stand out, their desired image, and how they aim to achieve it.
Cracking the Workplace Discipline Code Main.pptxWorkforce Group
Cultivating and maintaining discipline within teams is a critical differentiator for successful organisations.
Forward-thinking leaders and business managers understand the impact that discipline has on organisational success. A disciplined workforce operates with clarity, focus, and a shared understanding of expectations, ultimately driving better results, optimising productivity, and facilitating seamless collaboration.
Although discipline is not a one-size-fits-all approach, it can help create a work environment that encourages personal growth and accountability rather than solely relying on punitive measures.
In this deck, you will learn the significance of workplace discipline for organisational success. You’ll also learn
• Four (4) workplace discipline methods you should consider
• The best and most practical approach to implementing workplace discipline.
• Three (3) key tips to maintain a disciplined workplace.
RMD24 | Debunking the non-endemic revenue myth Marvin Vacquier Droop | First ...BBPMedia1
Marvin neemt je in deze presentatie mee in de voordelen van non-endemic advertising op retail media netwerken. Hij brengt ook de uitdagingen in beeld die de markt op dit moment heeft op het gebied van retail media voor niet-leveranciers.
Retail media wordt gezien als het nieuwe advertising-medium en ook mediabureaus richten massaal retail media-afdelingen op. Merken die niet in de betreffende winkel liggen staan ook nog niet in de rij om op de retail media netwerken te adverteren. Marvin belicht de uitdagingen die er zijn om echt aansluiting te vinden op die markt van non-endemic advertising.
B2B payments are rapidly changing. Find out the 5 key questions you need to be asking yourself to be sure you are mastering B2B payments today. Learn more at www.BlueSnap.com.
What is the TDS Return Filing Due Date for FY 2024-25.pdfseoforlegalpillers
It is crucial for the taxpayers to understand about the TDS Return Filing Due Date, so that they can fulfill your TDS obligations efficiently. Taxpayers can avoid penalties by sticking to the deadlines and by accurate filing of TDS. Timely filing of TDS will make sure about the availability of tax credits. You can also seek the professional guidance of experts like Legal Pillers for timely filing of the TDS Return.
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𝐓𝐉 𝐂𝐨𝐦𝐬 (𝐓𝐉 𝐂𝐨𝐦𝐦𝐮𝐧𝐢𝐜𝐚𝐭𝐢𝐨𝐧𝐬) is a professional event agency that includes experts in the event-organizing market in Vietnam, Korea, and ASEAN countries. We provide unlimited types of events from Music concerts, Fan meetings, and Culture festivals to Corporate events, Internal company events, Golf tournaments, MICE events, and Exhibitions.
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Sports events - Golf competitions/billiards competitions/company sports events: dynamic and challenging
⭐ 𝐅𝐞𝐚𝐭𝐮𝐫𝐞𝐝 𝐩𝐫𝐨𝐣𝐞𝐜𝐭𝐬:
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"𝐄𝐯𝐞𝐫𝐲 𝐞𝐯𝐞𝐧𝐭 𝐢𝐬 𝐚 𝐬𝐭𝐨𝐫𝐲, 𝐚 𝐬𝐩𝐞𝐜𝐢𝐚𝐥 𝐣𝐨𝐮𝐫𝐧𝐞𝐲. 𝐖𝐞 𝐚𝐥𝐰𝐚𝐲𝐬 𝐛𝐞𝐥𝐢𝐞𝐯𝐞 𝐭𝐡𝐚𝐭 𝐬𝐡𝐨𝐫𝐭𝐥𝐲 𝐲𝐨𝐮 𝐰𝐢𝐥𝐥 𝐛𝐞 𝐚 𝐩𝐚𝐫𝐭 𝐨𝐟 𝐨𝐮𝐫 𝐬𝐭𝐨𝐫𝐢𝐞𝐬."
Digital Transformation and IT Strategy Toolkit and TemplatesAurelien Domont, MBA
This Digital Transformation and IT Strategy Toolkit was created by ex-McKinsey, Deloitte and BCG Management Consultants, after more than 5,000 hours of work. It is considered the world's best & most comprehensive Digital Transformation and IT Strategy Toolkit. It includes all the Frameworks, Best Practices & Templates required to successfully undertake the Digital Transformation of your organization and define a robust IT Strategy.
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Implicitly or explicitly all competing businesses employ a strategy to select a mix
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involves recognizing relationships between elements of the marketing mix (e.g.,
price and product quality), as well as assessing competitive and market conditions
(i.e., industry structure in the language of economics).
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As an Army veteran dedicated to lifelong learning, I bring a disciplined, strategic mindset to my pursuits. I am constantly expanding my knowledge to innovate and lead effectively. My journey is driven by a commitment to excellence, and to make a meaningful impact in the world.
The key differences between the MDR and IVDR in the EUAllensmith572606
In the European Union (EU), two significant regulations have been introduced to enhance the safety and effectiveness of medical devices – the In Vitro Diagnostic Regulation (IVDR) and the Medical Device Regulation (MDR).
https://mavenprofserv.com/comparison-and-highlighting-of-the-key-differences-between-the-mdr-and-ivdr-in-the-eu/
RMD24 | Retail media: hoe zet je dit in als je geen AH of Unilever bent? Heid...BBPMedia1
Grote partijen zijn al een tijdje onderweg met retail media. Ondertussen worden in dit domein ook de kansen zichtbaar voor andere spelers in de markt. Maar met die kansen ontstaan ook vragen: Zelf retail media worden of erop adverteren? In welke fase van de funnel past het en hoe integreer je het in een mediaplan? Wat is nu precies het verschil met marketplaces en Programmatic ads? In dit half uur beslechten we de dilemma's en krijg je antwoorden op wanneer het voor jou tijd is om de volgende stap te zetten.
3. 3
Vacuum:
the pressure of the
gas is much lower
than the one of its
environment
Pump:
device that is used
to move fluids
Vacuum pump:
movement of gas
molecules due to flow
induced by a vacuum
system
Was invented in:
1650
by:
Otto von Guericke
4. General Terminology:
4
• Pressure:
• Ideal gas equation:
• Mean free path:
• Reynolds number:
• Knudsen number:
mfp:
F
p
A
B
mRT
pV Nk T
M
2 2
1 1
2 2n d n d
where: 8kT
m
Re
ud
v
1
2
Kn
d
Absolute vacuum:
density of
molecules=0
5. 5
Vacuum Terminology:
• Mass flow:
• Pumping speed:
• Pump throughput:
• Conductance/Conductivity:
• Compression ratio:
m
M
t
[kg/h, g/s]
dV
S
dt
[m3/s, m3/h]
pV
V mRT
Q p
t tM
pV
dV
Q S p p
dt
[Pa m3/s =W]
pVQ
C
p
in row:
1/Ctot = 1/C1 + 1/C2
parallel:
Ctot = C1 + C2 + …
2
0
1
p
K
p
P1: inlet pressure
P2: outlet pressure
6. 6
vacuum
(mfp range)
rough vacuum:
mfp << 10-4 m
medium vacuum:
10-4 m - 10-1 m
high vacuum:
10-1 m - 103 m
ultra high vacuum:
mfp >> 103 m
vacuum
(pressure range)
rough vacuum:
105 Pa - 100 Pa
fine vacuum:
100 Pa - 10-1 Pa
high vacuum:
10-1 Pa - 10-5 Pa
ultra high vacuum (UHV):
10-5 Pa - 10-10 Pa
extreme high vacuum(XHV):
10-10 Pa - 10-12 Pa
Definition of vacuum
ranges:
Gas flow regimes:
Kn > 0.5:
Free Molecular
-Equation of Boltzmann
(without the collision term)
-ultra, extreme high
vacuum
0.01 < Kn < 0.5:
Transition regime
-Equation of Boltzmann
(empirical approaches)
- fine, medium vacuum
Kn << 0.01:
Viscous or continuum flow
(laminar or turbulent)
-Described by the equations NS
- rough vacuum
7. 7
fluid displaced
by a space and is
forwarded to
another
gases are removed
by extracting them
in the atmosphere
change of the
kinetic state of
the moving fluid
cause condensation
or chemical
trapping of gas
Pump tree:
8. Gas transfer: Positive displacement
8
• Diaphragm pump:
- Well known for
environmental reasons
- low maintenance cost
- noiseless
Rotary pumps
• Roots pump:
- design principle was discovered:
in 1848 by Isaiah Davies
- implemented in practice:
Francis and Philander Roots
- in vacuum science: only since 1954
Reciprocating pumps
9. 9
Gas transfer: Kinetic
- 1913 :Gaede - molecular
- 1957 :Dr.W.Becker - turbomolecular
• (Turbo) molecular pump:
Entrapment pumps
• Cryopump:
- concentration on cold
surface
- profitable for some
gases
Drag pumps
11. Holweck pump:
11
Invented by:
Fernand Holweck
Constructed by:
Charles Beaudouin
Molecular pump:
- Outer cylinder with
grooves, spiral form
- Inner cylinder with
smooth surface
The rotation of the
smooth cylinder causes
the gas flow
Fernand Holweck
(1890-1941)
12. 3D problem
12
Simulation: much computational effort
Neglect: end effects and the curvature
of the geometry
(total effect = 0.05 )
4 independent problems: 2D flow
in grooved channel
region of solution:
13. Geometry:
13
H : distance between plates
W x D : groove cross section
W : groove width
D : groove depth
L : period
Isothermal walls:
Τ=Τ0
Characteristic length:
Η
Boundaries of flow domain:
- Inlet: (x΄= -L/2)
- Outlet: (x΄= L/2)
- Top wall: (y΄= Η)
- Bottom wall: (y΄=-D)
14. General description of
individual problems:
14
1. Longitudinal Couette flow
2. Longitudinal Poiseuille flow
3. Transversal Couette flow
4. Transversal Poiseuille flow( , )i
f f
Q f f
t i
Boltzmann equation:
BGK model:
( )M
i
f f
v f f
t i
23
[ ( , )]
2
2 ( , )
( , )
2 ( , )
i i
B
m u i t
k T i tM
B
m
f n i t e
k T i t
Maxwell distribution function:
Steady state flow:
Taylor expansion:( )M
i
f
v f f
i
0
0
n n
n
0
0
T T
T
2
0
0 0
3
1
2 2
M i iu
f f
RT RT
where:
Polar system coordinates:
2 2
x yc c
1
tan y
x
c
c
cos sinx y
d
c c
x y x y ds
Linear differentiation of distribution function
15. 15
Longitudinal Couette: Longitudinal Poiseuille:
Fluid flow: in direction z’
Cause of flow: moving wall
in direction z’
Cause of flow: pressure gradient
in direction z’
0,0, ,zu u x y
0 0
1
o
U
f f h
u
0
1
o
U
u
Linearization0
1f f hXp z Xp 1Xp
x
x
H
y
y
H 0
x
xc
u 0
y
yc
u 0
z
zc
u
0
0
P
v 0
0 0
P H
u 02ou RT
Non dimensional
variables
'
0
z
z
u
u
U
0
0
u
U 0
ou
U
'
0
z
z
u
u
u Xp Xp Xp
reduced
BGK equations
after projection
x y zc c u
x y
where:
21
, , , , , , , zc
x y x y z z zx y c c h x y c c c c e dc
1
2
x y zc c u
x y
Macroscopic velocity:
16. 1616
Fluid flow: in direction x’
Cause of flow: moving wall
in direction x’
Cause of flow: pressure gradient
in direction x’
Linearization
x
x
H
y
y
H 0
x
xc
u 0
y
yc
u 0
z
zc
u
0
0
P
v 0
0 0
P H
u 02ou RT
Non dimensional
variables
( , ), ( , ),0x yu u x y u x yTransversal Couette: Transversal Poiseuille:
0 0
1
o
U
f f h
u
0
1
o
U
u
0
1f f hXp x Xp 1Xp
0
0
u
U 0
ou
U Xp Xp
where:
'
0
x
x
u
u
U
'
0
y
y
u
u
U
'
0
x
x
u
u
u Xp
'
0
y
y
u
u
u Xp
2
1 2 cos sinx yu u
x y
2
1 2 cos sin cosx yu u
x y
2
x yc c
x y
21
, , , , , , , zc
x y x y z zx y c c h x y c c c e dc
2
21 1
, , , , , , ,
2
zc
x y x y z z zx y c c h x y c c c c e dcand
reduced
BGK equations
after projection
Macroscopic velocity:
17. Macroscopic quantities:
17
Longitudinal flows:
22
0 0
1
,zu x y e d d
22
0 0
1
, sinyzP x y e d d
1
0
2 ,
2
z
L
G u y dy
H
/2
/2
2
( ,1)
L H
yz
L H
H
Cd P x dx
L
Transversal flows:
2
2
0 0
1
,x y e d d
2
2
2
0 0
1 2
, 1
3
x y e d d
2
2
2
0 0
1
, cosxu x y e d d
2
2
2
0 0
1
, sinyu x y e d d
2
2
3
0 0
1
, sin cosxyP x y e d d
/2
/2
2
,1
L
xyL
H
Cd P x dx
L
1
0
2 ,
2
x
L
G u y dy
H
Density deviation:
Temperature deviation:
Macroscopic velocity:
Stress tensor:
Flow rate:
Drag coefficient:
18. 18
Boundary conditions:
Couette
Poiseuille
eq
wf f
2
02
3
2
02
wu
RTeq w
w
n
f e
RT
, , , , , ,
2 2
L L
y y
H H
Inlet – Outlet: Periodic
Interface gas-wall: Maxwell - diffusion
0 0ncStationary walls:
Moving wall: 2 zc 0yc
Stationary walls:
2 coswn 0yc
Longitudinal
Transversal Stationary walls:
Moving wall:
0 0nc
0 0nc
wnStationary walls: 0nc
where
0
0
Longitudinal
Transversal
where nw is defined by the no-penetration condition: 0u n
19. • Discretization:
- Physical space [ (x,y) or (x,z)] : (i,j)
where i=1,2,…,I and j=1,2,…,J
- Molecular velocity space (μm,θn) : (ζm , θn)
where 0 < ζm < ∞ and 0 < θn < 2π
m=1,2,…,M and n=1,2,…N
19
Discrete Velocity Method
DVM
Set consists of:
Μ × Ν discrete velocities
(16 × 50 × 4)
3200
• Discretized kinetic equations:
(e.g. transversal Couette flow)
, ,
, , , 2
, , , , , 1 2 cos sini j i j
i j m n
m i j m n i j i j m m x n y n
d
u u
ds
, , , ,
, , ,
2
i j m n i j
m i j m n
d
ds
Set of
algebraic equations:
2 × Μ × Ν
equations/node
20. Algorithm:
20
Parameters:
δ μm θn Ny_cha
D (D/H) W (W/H) L (L/H)
Couette: U0 / Poiseuille: Χp
• Grid format :
Channel and Cavity
• Grid reverse:
Scan of grid:
1st 2nd
3rd
4th
end of scanning
21. • Geometries:
21
L = 2:
L = 2.5:
L = 3:
• Rarefaction parameter:
δ 0 10-3
10-
² 10-
¹ 1 10 100
Total runs:
18 geometries 7 δ
=
126
• Results:
Mass flow rate
Drag coefficient
Macroscopic velocities
28. • Four different flow configurations have been examined:
1. Longitudinal Couette flow
2. Longitudinal Poiseuille flow
3. Transversal Couette flow
4. Transversal Poiseuille flow
• Results have been obtained in the whole range of Knudsen number
and for various values of the geometrical parameters: L/H , W/H
, D/H.
• Synthesizing these results in a proper manner designed parameters
such as pumping speed and throughput can be obtained.
• Optimization of the Holweck pump will follow soon!!!
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