Technology for creating a device for laminar flow of water in pipes | Результаты научных исследований в условиях пандемии (COVID-19)

Technology for creating a device for laminar flow of water in pipes

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Mengliyev, S., & Xamrayev, A. (2022). Technology for creating a device for laminar flow of water in pipes. Результаты научных исследований в условиях пандемии (COVID-19), 1(03), 182–189. извлечено от https://inlibrary.uz/index.php/scientific-research-covid-19/article/view/8271
Sh Mengliyev, Termez State University

Doctor of Philosophy in Technical Sciences

A Xamrayev, Termez State University

student

0
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Аннотация

The article discusses the mathematical modeling of the movement of viscous incompressible fluids through a bundle of tubes located inside the outer pipe. The laminar and turbulent modes of this movement are considered, and the physical meaning of their occurrence is also analyzed. The fluid flow through n tubes of length L and radius r located inside the outer tube is considered. Calculation formulas are derived for calculating the maximum velocity of this flow, the volume of fluid passing through the cross section of the tube, the coefficient of resistance to friction in the tube along the length of the flow, and also the maximum value of the tangential stress. The results of the study of the relationship of the coefficient of resistance to friction in the tube with the Reynolds number are presented. A description is given of a device created according to the results of a study that brings the disordered flow of liquids into a laminar state


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17.Сборник задач по методам вычислений. Учебное пособие / Под

ред. П.И.Монастырного. – 2-е изд. – Мн.: Университецкое, 2000. – 311 c.




Mengliyev Sh.A., Doctor of Philosophy in Technical Sciences

Termez State University (Ph.D)

Xamrayev A.B., student of Termez State University

TECHNOLOGY FOR CREATING A DEVICE FOR LAMINAR FLOW OF WATER

IN PIPES

Sh. Mengliyev A. Xamrayev

Abstract: The article discusses the mathematical modeling of the

movement of viscous incompressible fluids through a bundle of tubes
located inside the outer pipe. The laminar and turbulent modes of this
movement are considered, and the physical meaning of their occurrence is
also analyzed. The fluid flow through n tubes of length L and radius r located
inside the outer tube is considered. Calculation formulas are derived for
calculating the maximum velocity of this flow, the volume of fluid passing
through the cross section of the tube, the coefficient of resistance to friction
in the tube along the length of the flow, and also the maximum value of the
tangential stress. The results of the study of the relationship of the
coefficient of resistance to friction in the tube with the Reynolds number are
presented. A description is given of a device created according to the results
of a study that brings the disordered flow of liquids into a laminar state.

Keywords: Reynolds number, laminar flow, turbulent flow, parabolic

flow, friction force, integral, coordinate, pipe, viscosity, density, main flow
velocity, average speed, maximum speed, radius, Hooke, Gegin, Poiseuille,
Darcy-Weisbach, fluid volume, drag coefficient.

The motion of real fluids is often very different from that of laminar flow.

They have a special property called turbulence. As the Reynolds number
increases in real fluid flows in pipes, channels, and boundary layers, the
transformation of a laminar-shaped flow into a turbulent flow is clearly
observed. This transition of laminar flow to turbulent flow is sometimes
called turbulence, which is fundamental in the whole field of
hydrodynamics. Initially, such a transition was observed in the flow of
straight pipes and channels.

Information on the forces acting on a fluid for flow in a cylindrical tube

is given in the article [2; pp. 36-47].

Consider the motion of a tube of constant diameter along its entire

length and the flow of fluid through n tubes of length L and radius r placed


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183

inside the tube. In real liquids, the liquid sticks to the walls of the tubes and
exerts a repulsive stress on the flowing surface. This creates a force called
internal friction, which is the viscosity of liquids. Viscosity is the property of
gases and liquids to resist the action of external forces that cause the fluid to
move. The presence of experimental stresses and the adhesion of the fluid
to solid walls cause the real fluids in motion to be qualitatively different from
ideal fluids. We now calculate the forces acting on the fluid in the pipe, taking
into account the n tubes. Due to the adhesion, the velocity in the tube wall is
zero, and the velocity between the tubes reaches its maximum value. Some
concentric layers move so that the velocity is axial everywhere and the flow
is laminar. At a sufficiently long distance from the starting point of the tubes,
the velocity distribution of the flow in the tube does not depend on the
longitudinal coordinates along the radius.

The movement of the fluid in the tube is due to the fact that the pressure

decreases along the axis of the tube, but the pressure does not change in the
cross section perpendicular to the axis of each tube. The motion of each
element of the fluid accelerates due to the pressure drop and slows down
due to the shear stress caused by friction [3; pp. 36-38]. The pressure p is
assumed to be constant, i.e., across the entire tube section [4; pp. 59-60].

There are compressive forces and effects on the cylinder along the main

axis, which correspond to the inlet and outlet bases of the cylinder,
respectively, and there is an actuating force acting on the side surface of the
cylinder. It is necessary to determine the maximum flow rate in this cylinder,
the volume of liquid flowing through the cross section of the pipe, the
coefficient of frictional resistance of the pipe along the length of the pipe,
and the maximum value of the test voltage.

By balancing the forces acting on the fluid in the tube (Figure 1), we

obtain the following equation as a condition of equilibrium in the direction
of motion:

. (1)

Figure 1. N tubes are placed inside the tube

n

i

n

i

l

n

i

yL

y

p

y

p

1

1

2

1

2

0

2


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184

The projection of the internal friction force is obtained with a positive

sign because the velocity gradient is negative (the flow velocity of the layer
decreases with increasing coordinate).

From formula (1) we can determine the test voltage

(2)

In this case, the flow rate decreases with increasing coordinate and

becomes zero due to the viscosity. Therefore, we can say that according to

Newton's law of

friction.

Substituting this expression into (3), we get:

Henceforth

(4)

Now, assuming that when

, it is

, we integrate Equation

(4) with this initial condition to form the following equation

, (5)

To find the constant C in Equation (5), we use the condition that the

velocity is

when

i.e.

henceforth

(6)

we find that Set this value of the constant to (6)

equation and so on

(7)

we have the equation
Thus, we have a parabolic distribution of velocities along the radii of the

tubes (Figure 2). This velocity reaches its maximum value in the middle of
the tube ( y=0 ) and has the following maximum value:

0

2

l

p

p

y

L

dy

du

0

2

l

p

p

du

y

dy

L

0

2

l

p

p

du

y

dy

L

 

r

y

0

)

(

y

u

2

0

( )

4

l

p

p

u y

y

C

L

 

r

y

( )

0

u r

2

0

( )

4

l

p

p

u r

r

C

L

 

2

0

4

l

p

p

C

r

L

2

2

0

0

( )

4

4

l

l

p

p

p

p

u y

y

r

L

L

 

2

2

0

( )

(

)

4

l

p

p

u y

r

y

L


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185

(8)

Figure 2. Flow motion for a single tube
The total fluid flow (fluid flow) through the tube section is defined as

the circulating paraboloid volume (Figure 2) and is defined as
follows.Equation (7) we have the following formula:

(9)

Using the Gagen-Poiseuille formula for the total flow of fluid through a

tube with a circular cross section, we determine:

that is, we have a formula for the flow rate

(10)

Enter the average flow velocity across the cross section of the tube:

(11)

Given formula (10), we write (11) as follows

Comparing the function

with

defined by formula (8), the

average velocity for the motion

is half the maximum velocity.

We determine the pressure difference

.

2

0

max

4

l

p

p

u

r

L

2

2

2

2

0

max

2

2

( )

(

)

1

4

l

p

p

r

y

y

u y

r

u

L

r

r

r

r

r

r

y

y

u

dy

r

y

y

u

ydy

y

u

Q

0

2

4

2

max

0

2

3

max

0

4

2

2

2

2

)

(





4

0

(

)

8

l

p

p r

Q

L

2

r

Q

u

2

0

(

)

8

l

p

p r

u

L

)

(

y

u

max

u

max

2

1

)

(

u

y

u

0

(

)

l

p

p

0

2

8

l

Lu

p

p

r


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186

Henceforth

(12)

where

the diameter of the tube.

The pressure lost along the length of the flow is found by the Darcy-

Weisbach equation [5-9]. Summarizing the above formula for one tube for -
ta tubes, we obtain the following formula

(13)

Substituting the value of

from formula (4.34) into (13) we

obtain the following formula

or more

(14)

where is the number of tubes, the coefficient of resistance decreases

with increasing number of tubes

.

Above (14), we present the results obtained on the basis of the formula

(Fig.

3).

Figure 3. The dependence of the coefficient of resistance in a smooth pipe

on the number of tubes n and Re:

1) n=200; 2) n=300; 3) n=400; 4) n=500.

0

2

8

32

32

(

)

2

2

l

Lu

u

L

u

L

p

p

r

r

r

D

D

2

D

r

n

i

i

l

D

L

u

p

p

1

2

0

)

(

2

0

l

p

p

2

32

2

64

n

u L

D

D

D

n L

uD n

u

 

64

Re

n

n

Re

uD


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Figure 3 shows the results of calculations showing that the resistance

coefficient

for a smooth tube depends on the Rnolds number

. A

comparison of the results shows that the theoretical formula (14) is valid
for all values of the number

. At larger values of the number

, the

resistance decreases due to the active activation of the turbulence
mechanisms.

In the computational experiment, the characteristic parameters

Reynolds number Re and

of the coefficient of resistance are studied in

the following quantities:

,

. The figure shows that as the

number of tubes increases, the coefficient of resistance decreases.

Based on the above results, it is possible to create a device that allows

the regulation of water flows. The device can be implemented in the
manufacturing process, it can be used to regulate the flow in water
fountains.

The proposed device allows you to make the fountains look beautiful

and enrich them with different colors.

The main purpose of the device is to maintain the flow of water in the

form of a uniform laminar flow with the help of its working bodies.

The device can be explained by the following diagrams, its working

elements are shown, Figure 4 shows the internal section of the device, where
the base legs holding the device at an acute angle and the device is firmly
attached to it, 2 tube-shaped housing, 3 -cylindrical section with inlet and
outlet holes mounted vertically from top to bottom, 4 small-diameter tubes,
which serve to convert the tubular flow into laminar flow, and 5-distributor,
which serves to evenly distribute the flow to small-diameter tubes by
reducing the flow rate, 6 -network holding small-diameter tubes, which in
turn serves for the orderly movement of the flow.

Figure 4. Device interior

n

n

Re

Re

Re

n

Re

500 5000

0.0001 0.0007

n


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The device that converts the flow to a laminar view works as follows:

the flow from the inlet 3 is directed to the flow 5, which reduces the flow
rate and the flow is evenly distributed in the small diameter tubes, the
current passing through the small diameter tubes 4 becomes laminar and It
is shot in a laminar view through 3 outlet holes.

The experimental study found that the optimal length for a set of tubes

placed inside a tube was 12–16 cm, and that the resistance coefficient
decreased as the tube set increased, resulting in a device for converting
chaotic flows into laminar flows.

The proposed device is an in-depth analysis of laminar flow in the

movement of incompressible viscous fluids in the pipe, which is important
in technical applications, when it is necessary to convert turbulent (chaotic)
flows into laminar (layered, ordered) flows, including in parks. They can be
used when there is a need to effectively control the flow of water, that is, to
create a variety of pleasant and colorful streams of water in the installed
fountains, to give people an aesthetic pleasure. Laminarization of water
flows in the pipe is very useful and cost-effective, ie it saves water.


References:
1.Reynolds O. On the experimental investigation of the circumstances

which determine whether the motion of water shall be direct or sinuous, and
the law of resistance in parallel channels Phil. Trans.roy.soc. 1883. № 174.
P. 935-982.

2.Mengliyev Sh.A. Trubada qisilmaydigan yopishqoq suyuqliklar

harakatini laminar oqimga aylantirish Xorazm ma’mun akademiyasi
axborotnomasi, Xiva-2018. №. 2. Б. 105-110.

3.Гордин В.А. Дифференциальные и разностные уравнения

Изд.М.:«Высшая школа экономики», 2016. 517 с.

4.Горшков-Кантакузен В.А. К вопросу вычисления коэффициента

Дарси

методом

регрессионного

анализа

Материалы

XXI

Международного симпозиума "Динамические и технологические
проблемы механики конструкций и сплошных сред" имени А.Г.
Горшкова, 16-20 февраля 2015, Вятичи. Том 1./МАИ.:ООО "ТРП",2015. С.
59-60.

5.Кочен Н.Е., Кибель И.А., Розе Н.В.Теоретическая гидромеханика

М: Физматлиз, 1963. 728 с.

6.Лойцянский Л.Г. Ламинарный пограничный слой М: Физматлиз,

1962.479с.

7.Шлихтинг Г. Теория пограничного слоя. М.: Наука, 1974. 571 с.
8.Гольдштик М.А., Штерн В.Н. Гидродинамической устойчивость и

турбулентность. Hовосибирск: Наука, Сиб. Отд-ние, 1977. 366 с.


background image

Scientific research results in pandemic conditions (COVID-19)

189

9.Дразин Ф. Введение в теорию гидродинамической устойчивости.

М.:Физматлит, 2005. 88 с.




Baxodir Khamrokulov Independent researcher of UWED, PhD in law,

Tashkent, Uzbekistan

Compensation for moral damage caused by violation of the author's right

B. Khamrokulov


Abstract: Nowadays, there are many cases of using works protected by

copyright without obtaining the appropriate permission of the author or the
owner of such rights. The most common types of copyright infringement
include copying, distribution of the work, mass demonstration, mass
execution of works in concert halls, theatrical productions, translation of the
work into other languages, processing of the work (plagiarism), etc. As a
result of committing such an illegal act, not only material damage, but also
moral damage can be caused to the author of the work. In this article, the
issue of compensation for moral damage caused by violation of the rights of
the author has been studied.

Keywords: copyright law, intellectual property, moral damage, material

damage, mental calmness, anguish, feeling uncomfortable.


With the development of modern information and communication

technologies, the illegal users of literary works (literary-artistic, scientific,
educational, publicist and other works), dramatic and scenario works,
works of text and non-text music, musical-dramatic works, choreographic
works and pantomime, audiovisual works, painting, sculpture, graphics,
design works and other fine arts, works of landscape-applied and stage
decoration art, architecture, urban planning and garden-park development
works of art, photographic works and works created in similar ways to
photography are often encountered. As a result of this, personal non-
property and property rights of the author are violated.

We can say that our main laws aimed at protecting copyright are the

Civil Code of the Republic of Uzbekistan and the law of the Republic of
Uzbekistan "On copyright and related rights", the Criminal Code of the
Republic of Uzbekistan and other normative-legal acts. The result of the
reforms carried out in this area was the signing of the law of the Republic of
Uzbekistan "On the Accession of the Republic of Uzbekistan to the Treaty of
the World Intellectual Property Organization on Copyright (Geneva,
December 20, 1996)" on February 2, 2019.

Библиографические ссылки

Reynolds 0. On the experimental investigation of the circumstances which determine whether the motion of water shall be direct or sinuous, and the law of resistance in parallel channels Phil. Trans.roy.soc. 1883. № 174. P. 935-982.

Mengliyev Sh.A. Trubada qisilmaydigan yopishqoq suyuqliklar harakatini laminar oqimga aylantirish Xorazm ma’mun akademiyasi axborotnomasi, Xiva-2018. №. 2. Б. 105-110.

Гордин B.A. Дифференциальные и разностные уравнения Изд.М.:«Высшая школа экономики», 2016. 517 с.

Горшков-Кантакузен В.А. К вопросу вычисления коэффициента Дарси методом регрессионного анализа Материалы XXI Международного симпозиума "Динамические и технологические проблемы механики конструкций и сплошных сред" имени А.Г. Горшкова, 16-20 февраля 2015, Вятичи. Том 1./МАИ.:ООО "ТРП",2015. С. 59-60.

Кочен Н.Е., Кибель И.А., Розе Н.В.Теоретическая гидромеханика М: Физматлиз, 1963. 728 с.

Лойцянский Л.Г. Ламинарный пограничный слой М: Физматлиз, 1962.479с.

Шлихтинг Г. Теория пограничного слоя. М.: Наука, 1974. 571 с.

Гольдштик М.А., Штерн В.Н. Гидродинамической устойчивость и турбулентность. Новосибирск: Наука, Сиб. Отд-ние, 1977.366 с.

Дразин Ф. Введение в теорию гидродинамической устойчивости. М.:Физматлит, 2005. 88 с.

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