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i UNIVERSITI TUN HUSSEIN ONN MALAYSIA STATUS CONFIRMATION FOR MASTER’S THESIS DEVELOPMENT OF A MICROFLUIDIC DILUTION AND INFUSION PUMP SYSTEM ACADEMIC SESSION : 2015/2016 I, MUHAMMAD SHARIL BIN SARIPAN agree to allow this Master’s Thesis to be kept at the Library under the following terms: 1. This Master’s Thesis is the property of Universiti Tun Hussein Onn Malaysia. 2. The library has the right to make copies for educational purposes only. 3. The library is allowed to make copies of this report for educational exchange between higher educational institutions. 4. ** Please Mark (√) CONFIDENTIAL (Contains information of high security or of great importance to Malaysia as STIPULATED under the OFFICIAL SECRET ACT 1972) RESTRICTED (Contains restricted information as determined by the Organization/institution where research was conducted) FREE ACCESS _________________________ Approved by, __________________________ (WRITER’S SIGNATURE) (SUPERVISOR’S SIGNATURE) Students name MUHAMMAD SHARIL BIN SARIPAN Date: ___________________ Supervisor’s name PM.DR. SOON CHIN FHONG Date : ________________________ NOTE: ** If this Master’s Thesis is classified as CONFIDENTIAL or RESTRICTED, Please attach the letter from the relevant authority/organization stating reasons and duration for such classifications. 28 JANUARY, 2016 28 JANUARY, 2016

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i

UNIVERSITI TUN HUSSEIN ONN MALAYSIA

STATUS CONFIRMATION FOR MASTER’S THESIS

DEVELOPMENT OF A MICROFLUIDIC DILUTION AND INFUSION

PUMP SYSTEM

ACADEMIC SESSION : 2015/2016

I, MUHAMMAD SHARIL BIN SARIPAN agree to allow this Master’s Thesis to be kept at the

Library under the following terms:

1. This Master’s Thesis is the property of Universiti Tun Hussein Onn Malaysia.

2. The library has the right to make copies for educational purposes only.

3. The library is allowed to make copies of this report for educational exchange between

higher educational institutions.

4. ** Please Mark (√)

CONFIDENTIAL

(Contains information of high security or of great

importance to Malaysia as STIPULATED under the

OFFICIAL SECRET ACT 1972)

RESTRICTED

(Contains restricted information as determined by

the Organization/institution where research was

conducted)

FREE ACCESS

_________________________

Approved by,

__________________________

(WRITER’S SIGNATURE)

(SUPERVISOR’S SIGNATURE)

Student’s name

MUHAMMAD SHARIL BIN

SARIPAN

Date: ___________________

Supervisor’s name

PM.DR. SOON CHIN FHONG

Date : ________________________

NOTE:

** If this Master’s Thesis is classified as CONFIDENTIAL or RESTRICTED,

Please attach the letter from the relevant authority/organization stating

reasons and duration for such classifications.

28 JANUARY, 2016 28 JANUARY, 2016

DEVELOPMENT OF A MICROFLUIDIC DILUTION AND INFUSION PUMP

SYSTEM

MUHAMMAD SHARIL BIN SARIPAN

A thesis submitted in

Fulfillment of the requirement for the award of the

Degree of Master of Electrical Engineering

Faculty of Electrical & Electronic Engineering

Universiti Tun Hussein Onn Malaysia

JANUARY, 2016

ii

I hereby declare that the work in this thesis is my own except for quotations and

summaries which have been duly acknowledged.

Student : ………………………………………………..

Muhammad Sharil bin Saripan

Date : ……………………………………………….

Supervisor : ………………………………………………..

PM Dr Soon Chin Fhong

Date : ……………………………………………….

iii

ACKNOWLEDGEMENT

First of all, all grateful to Allah SWT, our creator for his merciful and bless to all

people. I would like to give a million thanks to my parents for all the support and

motivation for me during my Postgraduate program over past one years and six

months here. Without them, I can’t achieve my dream as I was here. I am very

pleased with all their sacrifice as the backbone to ensure that I can be a good person

for them and to graduate my studies soon. Special thanks also to PM Dr. Soon Chin

Fhong, with her supervision and guidance for these one year on my final year project,

the whole progress of my master project goes smoothly. The appreciation goes to my

supervisor for the cooperation to ensure my project work progress kept on the track.

Also a million thanks to the Suria Arts and MyBotic Company.

iv

ABSTRACT

In recent years, there are many biological studies that require a use of microfluidic

device in the experiment, one of the device used is dilution chip which it used to

separate the concentration of the fluid intensity for many application. One of the

application use the dilution chip is for cytochemical treatment. Thus, to separate the

fluid intensity in the microfluidic chip, an infusion pump has been developed with an

aim to drive fluid into the microfluidic device with different flow rate set. The flow

rate set in the infusion pump is 0.5, 1 and 2 ml/min. The purpose of applying

different flow rates used to test the efficiency of the dilution in microfluidic chip

with different flow rates. The infusion pump system built by using Arduino as the

main microcontroller to control the whole system operation including for both of

infuse and diffuse process by using bipolar stepper motor and motorized linear slider

to control the plunger movement.

v

ABSTRAK

Pada tahun terkini, banyak kajian penyelidikan dalam bidang biological yang

memerlukan penggunaan microfluidic cip dalam pengujian makmal, antara salah satu

contoh alatan yang digunakan adalah microfluidic cip pencairan yang digunakan

untuk proses mencairkan kelikatan cecair yang digunakan. Salah satu aplikasi

pencairan yang digunakan dalam pengujian adalah rawatan cytochemical. Oleh yang

demikian, untuk memisahkan kelikatan cecair didalam microfluidic cip, satu infusion

pam telah dibangunkan dan direka dengan tujuan untuk mengalirkan cecair ke dalam

microfluidic cip dengan kadar pengaliran yang berbeza. Kadar pengaliran yang telah

ditetapkan didalam system pam adalah 0.5, 1 dan 2 ml/min. Tujuan kadar pengaliran

yang berbeza untuk melihat keberkesanan pencairan di dalam microfluidic cip.

Infusion pam dibina dengan menggunakan Arduino sebagai pengawal utama

keseluruhan system operasi termasuk proses infuse dan diffuse dengan menggunakan

motor pelangkah jenis bipolar dan penggerak lurus bermotor untuk mengawal

pergerakan penarik picagari.

vi

TABLE OF CONTENTS

CHAPTER TITLE PAGE

DECLARATION i

ACKNOWLEDGEMENTS iii

ABSTRACT iv

ABSTRAK v

TABLE OF CONTENTS vi

LIST OF FIGURE ix

LIST OF TABLE xiii

CHAPTER 1 INTRODUCTION 1

1.1 Microfluidic background 1

1.2 Project background 1

1.3 Problem statement 2

1.4 Objectives of project 2

1.5 Project scopes 3

CHAPTER 2 LITERATURE REVIEW 4

2.1 Physics of microfluidic 4

2.1.1 Reynold’s number 4

2.1.2 Fluidic resistance 5

2.1.3 Beer’s lambert law 5

2.2 Fabrication of microfluidic 6

2.2.1 Photolitography 6

2.2.2 Master molding process 7

2.2.3 Advantages and disadvantages of PDMS 8

2.3 Types of infusion syringe pump 9

2.3.1 Neonatal syringe pump 9

2.3.2 In-line gear pump 10

vii

2.3.3 Self-aligning gas or liquid micropump 11

2.3.4 Micro-jet pump for microfluidic system 12

2.4 Micromixer dilution 13

2.4.1 Types of microfluidic mixer 14

(a) Single-target dilution microfluidic 14

(b) Digital microfluidic biochip 15

(c) Rectangular mixing channel 15

(d) Vibrating microplate mixer 16

(e) Serial dilution micromixer 16

(f) Straight, square wave and 3D

serpentine micromixer

17

(g) One channel micromixer 18

2.4.2 Applications of microfluidic mixers 18

2.5 Comparison of previous projects 19

CHAPTER 3 METHODOLOGY 24

3.1 The flow chart of the project 24

3.2 Development of the infusion pump system 26

3.2.1 Block diagram of the infusion syringe

pump system

26

3.2.2 Operation of the infusion pump system 28

3.3 Design and development of the infusion pump 29

3.3.1 Simulation of the electronic circuit

simulation

29

3.3.2 Prototype design of the infusion pump

device

31

3.4 Characterization of linear slider rotation speed 32

3.5 Design of the microfluidic mixer device 33

3.6 Design of microfluidic dilution chip using

COMSOL multiphysics version 5.1 software

34

3.7 Microfluidic fabrication process 36

3.8 Absorbance of the fluid dilution calculation 39

3.9 Arduino programming 39

viii

CHAPTER 4 RESULTS AND DISCUSSION 49

4.1 Introduction 49

4.2 Simulation of the mixing function at the merging

channel result

49

4.3 Main menu system interface functions 50

4.4 The infusion pump system model developed 51

4.5 Motorised linear slider produced 52

4.6 Flow rate calibrations test 53

4.7 Calibration result analysis 56

4.8 Calibration results of stepper motor speed 58

4.9 Dilution concentration result 60

4.10 Dilution spectrum 62

4.11 Determine the concentration of the green fluid dye

at wavelength of 330

63

(a) High concentrate dilution concentration 63

(b) Less concentrate dilution concentration 64

(c) Less diluted dilution concentration 64

(d) Much diluted dilution concentration 65

4.12 Drawbacks of the project development 66

CHAPTER 5 CONCLUSION 67

5.1 Future improvements and suggestions 67

REFERENCES 68

APPENDIX A (ZD-6560-V3 2.5A MOTOR DRIVER) 70

APPENDIX B (LCD DISPLAY) 71

APPENDIX C (FULL CODING) 72

ix

LIST OF FIGURE

Figure 2.1 (a) Tube channel of microfluidic 5

Figure 2.1 (b) Formula used to calculate fluid resistance 5

Figure 2.2 (a) Absorption sample of concentration 5

Figure 2.2 (b) Beer’s lambert law formula 5

Figure 2.3 Photolithography process 7

Figure 2.4 Master mold process 7

Figure 2.5 (a) Novel mechanical syringe pump design 9

Figure 2.5 (b) Measurement result 9

Figure 2.6 (a) Magnetic coupling structure of in-line gear pump 10

Figure 2.6 (b) Flow rate versus pump rotation speed for

theoretical and measurement in-line gear pump

10

Figure 2.7 (a) Measurement setup for micropump illustration 11

Figure 2.7 (b) Measurement result for the flow rate 11

Figure 2.7 (c) Measurement setup for gas pump 12

Figure 2.7 (d) Measurement result for gas pump 12

Figure 2.8 (a) Image of micro-jet pump fabricated 13

Figure 2.8 (b) Schematic diagram of micro-jet pump 13

Figure 2.9 Classification scheme of micromixer 14

Figure 2.10 Top and cross-sectional view of digital

microfluidic (DMF) biochip

14

Figure 2.11 Schematic design of digital microfluidic biochip 15

Figure 2.12 Block diagram of setup for mixing pressure-

driven microfluidic

15

Figure 2.13 Channel of microfluidic geometry and operating

parameter

16

Figure 2.14 Channel of microfluidic design using COMSOL 16

Figure 2.15 Graphical abstract for serial dilution experiments

of microorganisms’ growth in bacteriological

17

Figure 2.16 3 types of micro-channel used to determine the

fluid velocity in micro-channel

17

x

Figure 2.17 Schematic of two input reservoir of microfluidic

to mix two different fluid

18

Figure 3.1 Flow chart for project methodology 25

Figure 3.2 Block diagram of the mechanical system 26

Figure 3.3 Illustration block diagram of infusion pump 27

Figure 3.4 Flow chart operation of infusion pump system 28

Figure 3.5 The circuit controller, input switches and output

indicators

29

Figure 3.6 Direction and stepping pin connected to the

Arduino board from motor driver ZD-6560-V3

30

Figure 3.7 LCD display connection pin 31

Figure 3.8 Prototype infusion pump device 32

Figure 3.9 Digital laser tachometer 33

Figure 3.10 (a) Finished microfluidic dilution sticker template 34

Figure 3.10 (b) Paint illustration of microfluidic dilution device 34

Figure 3.11 Design of microfluidic dilution and mixing using

COMSOL software

35

Figure 3.12 Stick template to petri dish 36

Figure 3.13 Coating of microfluidic 36

Figure 3.14 Heating process was used to cure the PDMS and

vacuum process used to remove bubbles

37

Figure 3.15 Microfluidic pattern heated 37

Figure 3.16 Remove microfluidic pattern 38

Figure 3.17 Coated PDMS mixture and reheated 38

Figure 3.18 Create hole and tubing pipe installation 38

Figure 3.19 Complete microfluidic device 38

Figure 3.20 Absorbance formula for difference the dilution

result

39

Figure 3.21 Header files source code 39

Figure 3.22 Pin declaration for input and output port 40

Figure 3.23 Stepper pin configuration 40

Figure 3.24 Connection from ZD-6560-V3 motor driver to

Arduino pin

41

xi

Figure 3.25 Pin used to active the liquid crystal 41

Figure 3.26 Declaration for the push button 41

Figure 3.27 Startup program to initialize the LCD 42

Figure 3.28 Void function for slow speed 42

Figure 3.29 Void function for medium speed 43

Figure 3.30 Void function for high speed 43

Figure 3.31 Void reverse function 44

Figure 3.32 Void stop function 44

Figure 3.33 Loop process function 45

Figure 3.34 Selective program “A” 46

Figure 3.35 Selective program “B” 46

Figure 3.36 Selective program “C” 47

Figure 3.37 Selective program “D” 47

Figure 3.38 Selective program “E” 48

Figure 4.1 Simulation result for the velocity of the fluid flow

in the microfluidic channel

50

Figure 4.2 Main menu interface message 50

Figure 4.3 Flow rate of 0.5 ml/min button process 50

Figure 4.4 Flow rate of 1 ml/min button process 51

Figure 4.5 Flow rate of 2 ml/min button process 51

Figure 4.6 Linear slider move in reverse process 51

Figure 4.7 Model of the infusion pump designed 52

Figure 4.8 Structure design of the linear slider 53

Figure 4.9 Graph flow rate of 0.5 ml/min collected from the

repetition of 3 experiments

54

Figure 4.10 Graph flow rate of 1 ml/min collected from the

repetition of 3 experiments

55

Figure 4.11 Graph flow rate of 2 ml/min collected from the

repetition of 3 experiments

56

Figure 4.12 Graph shows the flow rate collected at different

step size

57

Figure 4.13 Graph analysis between the relationship of flow

rate with speed and step size measured

58

xii

Figure 4.14 RPM result comparison 59

Figure 4.15 Motor speed result with and without syringe

inserted

60

Figure 4.16 Dilute concentration of fluid in microfluidic chip 61

Figure 4.17 Different types of fluid concentration obtained

from the three outlets of microfluidic mixer device

for a flow rate of 2 ml/min

61

Figure 4.18 Light absorbed from different fluid concentration 63

Figure 4.19 Concentration obtained from the high concentrate

solution

64

Figure 4.20 Concentration obtained from the less concentrate

solution

64

Figure 4.21 Concentration obtained from the less diluted

solution

65

Figure 4.22 Concentration obtained from the much diluted

solution

65

Figure 4.23 Absorbance of different dilution with the

concentration collected

66

xiii

LIST OF TABLE

Table 2.1 Applications of Microfluidic mixer used in the previous

project developed

18

Table 2.2 Comparison of different syringe pump systems for use

with microfluidic device

20

Table 2.3 Comparison between project application techniques in

microfluidic device

21

Table 3.1 Parameter set on the microfluidic input channel 35

Table 3.2 Material parameter set for water in inlet channel 35

Table 3.3 Material parameter for the green food colouring dye 36

Table 4.1 Calibration result for 0.5 ml/min flow rate by using step

size of 280 with 3 different result

53

Table 4.2 Calibration result for 1 ml/min flow rate by using step

size of 560 with 3 different result

54

Table 4.3 Calibration result for 2 ml/min flow rate by using step

size of 1120 with 3 different result

55

Table 4.4 Collected data from calibrating test 57

Table 4.5 RPM measurement result comparison 59

Table 4.6 Motor speed test from flow rate result with load and

unloaded syringe

60

Table 4.7 Total absorbance of light for different dilution 62

Table 4.8 Concentration of green food colouring dye obtained

from different dilution result

65

1

CHAPTER 1

INTRODUCTION

1.1 Microfluidic Background

Microfluidic is a multidisciplinary field that investigates the behaviour of fluids itself

at the micro scale to pico scale of fluid [1] The application of microfluidic devices

are such as the chemical reaction, control volume of fluid or to manipulate small

samples volume such as for lab-on-chip application [1,2]. Channels in the

microfluidic device can be used to control the movement of fluids in micro or nano

metric volume. Polydimethylsiloxane (PDMS) is the main material used for the

manufacturing of micro-fluidic device [3,4]. In this project, a microfluidic device

will be used as an input for the fluid injected by the infusion pump.

1.2 Project background

In this part, the project of microfluidic fabricated for dilution of solvent purpose to

determine the force ex. The solvent injection system consists of a customized syringe

pump. The main important thing for this micro-fluidic device is the syringe pump

system that assembles together with it. The syringe pump act as an infusion to

control the flow rate of the fluid flow through a micro-fluidic devices channel.

2

The syringe pump will made up with 2 mode of microfluidic device, which will use

infusion process for both solvent and distilled water. The purpose for the project

develop to separate the concentration of chemical solution by infuse a volume of

distilled water then mix with an amount of chemical solution to find the

concentration of the solution by using dilution process. , the 2 tier of microfluidic

will design with 4 outlets for the dilution process. The 2 tier input will be the distilled

water and solvent, both of the substances will flow through the 4 flow channel of

microfluidic to mix both solution to separate the concentration obtain through the 4

outlet of the microfluidic device.

1.3 Problem Statement

Current problem occurred in the design of syringe pump system was the control of

speed and the volume flow in µl/min. The problem were not satisfies some user

when they handling some experiment for the micro-fluidic. In other word, the drive

of fluid will flow overload or not follow the specification as the accuracy for every

reading will affect the record taken. All this will result in micro-fluidic channel flow

from the liquid that drive in from the syringe pump system. This problem occurred

due to the fluid drive from the syringe pump which the speed of motor affects the

fluids driving to the micro-fluidic.

1.4 Objectives of the project

The main objectives of this project are:

To design and fabricate a microfluidic mixer that performs serial dilutions

To develop an infusion pump with various flow rates of 0.5, 1 and 2 ml/min

To separate the concentration of fluid intensity

To produce four dilutions of two different liquids

Determine the efficiency of the dilution from various flow rates and speed

RPM

3

1.5 Project scopes

The following are the scope of project which is:

Using Comsol Multiphysics version 5.1 for modelling the microfluidic

simulation design

Programming software microcontroller to control the current driver to a

motorised linear slides.

Design model of infusion pump using Sketchup software.

Design model of microfluidic using AutoCAD

Using spectrophotometer to measure the light absorbance of colour intensity

4

CHAPTER 2

LITERATURE REVIEW

The literature review covered the past research related to the background of flow

mechanic for microfluidics and electronics of different liquid pump system. The

physics of microfluidic were reviewed and reported in this chapter. Surveying the

past literature review from a sources like journal, conference proceeding, articles and

dissertations with a purpose for collecting data that related to the work field research

progress development to avoid reinventing the research already conducted on the

topic.

2.1 Physics of microfluidic

2.1.1 Reynolds’s number

In microfluidic, laminar flow in the micro channel is very important to predict the

flow of droplet or particle in the fluid stream in function of fluid density, velocity,

pressure and fluid viscosity. Thus, The Reynolds number (Re) formula is used to

describe the parameter involve for the fluid flows in a microfluidic channel. The

Reynolds number can be calculated by using equation 2.1,

𝑅𝑒 =⍴𝜐L

µ (2.1)

in which ⍴ is the fluid density, 𝜐 is the velocity of fluid, µ is the dynamic viscosity and

L is the material characteristic length scale.

5

2.1.2 Fluidic resistance

Fluidic resistance occurred in the channels of both input and output stream is

governed by a set of equations whole solutions are well known [17]. The flow rate

presence within the micro channel given by formula of Q= ΔP/R, where Q is the

flow rate, ΔP is the pressure drop occurred across the channel, and R is the channel

resistance. Meanwhile, the resistance of a circular geometry can be calculated by the

formula of,

Figure 2.1: (a) Tube channel of microfluidic, (b) Formula used to calculate fluid resistance

From the Figure 2.1 as shown, the fluid resistance on the microfluidic channel as

shown in (a) calculated by using the formula on (b) where µ is the fluid viscosity, L

is the channel length, and r is the channel radius and R is the total resistance in the

tube channel.

2.1.3 Beer’s lambert law

In the spectrophotometer, the efficiency of the microfluidic mixer can be tested by

measuring the light absorption or spectroscopy of each light in different dilution.

Figure 2.2: (a) Absorption sample of concentration, (b) Beer’s lambert law formula

(b) (a)

(b) (a)

𝑹 =𝟖µ𝑳

𝝅𝒓𝟒

L

r

6

Figure 2.2 shows the relationship between absorption of concentration sample the

wavelength transmittance of liquid in the microfluidic channel as shown in (a) can be

accessed by beer’s lambert law (b) with the formula given by Absorbance = εLc. In

this equation, ε is the molar extinction coefficient, L is the path length of light passed

and c is the liquid concentration from the outlet stream of micro channel.

2.2 Fabrication of microfluidic

In this section, method of microfluidic fabrication discussed which there are two

process of microfluidic fabrication which ise photolithography and molding [6].

2.2.1 Photolithography

Photolithography is a process of photopatterning the channels of PDMS using a

mask. Generally, photoresist will be spin coated on a silicon wafer in compressed air.

Negative or positive masks will be placed on the photoresists and the silicon wafer

with the photoresist coating will be exposed to the UV light. The photo resist

exposed to the UV light will be softened and ready for wet etching process. The

etchant will etch the area without the pattern of the mask and leaving template of the

design behind on the silicon wafer in which, the template function as a mould.

Next is the step process of creating PDMS by using photolithography method. The

process started from (1) the resin spread on the on the flat surface such as petri dish

with desired thickness. For this PDMS, a 500 nm thickness is used. Next process is

(2) in which the resin spread on the flat surface undergo the UV exposition is

protected by the photomask applied to the resin with micro channel pattern.

Next, mould is developed in a solvent that etches the areas of resin that were not

exposed to UV light (3). The last step of photolithography (4) is the remove the

microfluidic pattern with the resin mould pattern from the photomask. The mould

then treated using silane to facilitate the microfluidic device as illustrated in Figure

2.3.

7

Figure 2.3: Photolithography process

2.2.2 Master molding process

Molding process is a common process used in the fabricating of microfluidic in

PDMS. It is used the silicone polymer based at ambient temperature to fabricate the

microfluidic. Molding commonly is a fabricating process after the photolithography

process is done.

Figure 2.4: Master mold process

The moulding process of PDMS is as shown in Figure 2.4. This figure indicates the

sequences process in which the first process producing microfluidic chips from the

8

mould by pouring the PDMS onto the mould. Then, an elastomer silicone gel and

curing agent poured to the mould and heated at high temperature. Next process is to

remove the hardened PDMS from the mould to obtain the micro-pattern of the

PDMS chip. Then, the process continued to create a hole for the input and output

channels of the microfluidic by using the holes puncher with size of 2 mm is

commonly used. Next, the PDMS and the glass slide were treated using plasma

treatment. This is allow for both of the microfluidic and glass slide can be bonded.

2.2.3 Advantages and disadvantages of PDMS

From the technological point of view in developing and fabricating of PDMS in,

there are some advantages and disadvantages measured from the intrinsic properties

which is:

Advantages of PDMS

i. Cheap.

ii. Biocompatible to all field in science or biological field application.

iii. It contain low auto fluorescence.

iv. PDMS can be replicate by using plasma treatment to formed sealed

microfluidic device.

Disadvantages of PDMS

i. PDMS can absorb small hydrophobic molecules especially in cell biology

application.

ii. Sensitive to expose with certain chemicals.

iii. Difficult to integrate with small electrode.

iv. Permeability of PDMS when exposed to water vapour that lead to evaporation

on the micro-channel.

9

2.3 Types of infusion syringe pump

2.3.1 Neonatal syringe pump

The neonatal syringe pump is used to deliver proper neonatal IV therapy accessible.

This device is capable to produce a flow rate between 5cc/hr to 40cc/hr for standard

syringe used with error produced within 15% and the delivery of intravenous

operation and volume at low infusion rates of (<20ml/hr) used by control the over

flow rates of the fluid flows through microfluidic channel. The prototype design were

tested for 20cc, 30cc, and 60cc syringes at room temperature (25𝑜 C). These systems

operate by driving the plunger of a syringe at controlled velocity to dispense fluids

through Intravenous (IV) channel [5].

Figure 2.1: Volume dispensed during two runs of 15cc/hr with a 20cc syringe pump [6]

Figure 2.5: (a) Novel mechanical syringe pump design and (b) Measurement result

The neonatal syringe pump prototyped as shown in the Figure 2.5 discussed the (a)

flow rate delivered data for two different runs of 5 cc and 40 cc to determines the

volume dispensed (ml) within 60 seconds and (b) shows the prototype design for the

syringe pump with a driving mass to drive the plunger of the syringe for delivery of

fluid purpose.

(a) (b)

Plunger

Syringe

Driving

mass

10

2.3.2 In-line gear pump

The experiment develops to determine the performance demonstrates a viable pump

to the syringe pumps for flowing fluid in micro-instrumentation by comparing the

first in-linear gear pump and second stage in-line gear pump [6]. The process of the

system to compare the flow rates of the flowing fluid from the syringe pump to the

different motor used in the experiment. One the pump used in the first experiment is

in-linear pump assemble at first stage demonstrated with 350 µl/min at 5000 rpm.

Other than that, when using fluid motor, the flow rates generates from the syringe

pump resulting of 200 ml/min at 4000 rpm [6].

Figure 2.6 (a): magnetic coupling structure of in-line gear pump [6]

Figure 2.6 (b): Flow rate versus pump rotation speed for theoretical and measurement in-line

gear pump [6]

11

2.3.3 Self-aligning gas or liquid micropump

In this section, a piezoelectric driven silicon membrane pump and passive dynamic

valve [7] developed to tolerant the relationship between the pump gases and liquid

with the gas bubble. The project development progress are used to reduce the dead

volume of fluid produced by the micropump thus increasing the compression ratio

from the gas pumping. The outcome of the project shows that the flow rate produced

a 1500 µl/𝑚𝑖𝑛−1 for liquid pump and 690 µl/𝑚𝑖𝑛−1 for gas pump.

Figure 2.7 (a): Measurement setup for Micropump illustration and (b) Measurement result

for the flow rate [7]

As shown in Figure 2.7, the setup for the micro-pump included the inlet and outlet

channel tube that connected between the micro-pump with a purpose to deliver the

fluid and the Perspex test jig is used to observe the presence of adhesive between the

inlet and outlet valve. Meanwhile for (b), it shows the result of measured pump rate

at zero backpressure over a frequency range between 0.5 KHz and 3.5 KHz. From

the result, the flow rate achieved at 1500 µl/𝑚𝑖𝑛−1 with frequency of 2.5 KHz.

Next, is the measurement setup discussed installation setup for the gas pump testing

with a water beaker included and the outlet valve placed 4 mm inside the water

beaker containing water. The setup proposed to measure the gas presence in the

beaker when the micropump started to infuse the fluid as illustrated in Figure 2.7 (c).

(a) (b)

12

Figure 2.7 (c): Measurement setup for gas pump [7]

Figure 2.7 (d): Measurement result for gas pump [7]

From the result as shown in the Figure 2.7 (d), the measurement for gas pump

repeated by 3 test with a result shows the gas started to pump at the frequency of 3.5

KHz. Thus, it resulting with approximate gas pump rate of 690 µl/min−1 at a

frequency of 3.4 kHz is calculated.

2.3.4 Micro-jet pump for microfluidic system

The developed pump system were used for sampling in microfluidic system under

gas actuation with the threshold gas actuation pressure of 2kPa at the initial and

increase to 42kPa during the suction process [8]. The architecture of the micro-jet

pump built with vacuum suction mode to decrease the air bubbles in the microfluidic

channel and also to overcome the interface tension between the liquid and solid wall

in the microfluidic system. The size dimension of the nozzle outlet is 100µm, width

of nozzle wall is 20 µm and depth of the micro-jet nozzle pump 80 µm and it is

fabricated by using one mask process.

13

Figure 2.8 (a): Image of micro-jet pump fabricated [8]

Figure 2.8 (b): Schematic diagram of micro-jet pump [8]

2.4 Micromixer dilution

Micro-dilution is an applications that widely used in the biological or science field

with a purpose of mixing a two or many different chemicals in a microfluidic device

through the channels built in the device. Applications such as reaction kinetics, rapid

crystallisation, drug delivery and nanoparticle synthesis. Micro-mixer designed for

millisecond or microsecond mixing by using fabrication method of PDMS. There are

two classification scheme of micro-mixer which is passive and active [9].

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Figure 2.9: Classification scheme of micro-mixer [9]

2.4.1 Types of microfluidic mixer

(a) Single – target dilution microfluidic

Digital microfluidic (DMF) biochip [10,11] was used to developed a single-target

dilution by using several reagent with different concentration level for a dilution

process and mapping lab-bench protocol for an automate process. This process of

dilution used to minimizing the number of mix split-step of fluid and to minimize the

waste droplet during the automated sample preparation. The project also developed a

new dilution algorithm called Improved Dilution/Mixing Algorithm (IDMA) to

maximize the reuse of intermediate droplet generated during process.

Figure 2.10: Top and cross-sectional view of digital microfluidic (DMF) biochip [10]

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(b) Digital microfluidic biochip

The project developed to design a chip and mapping lab-bench protocol [9] to carry

out dilution process of biochemical samples. Dilution/Mixing algorithm developed to

creation automation technique to reduce the production of waste droplets. The digital

microfluidic designed consists of two 0(n)-size rotary mixers and 0(n) storage

electrodes [10]. The droplet of fluids flows by applying the voltage control and

electrode adjacent at the same time. The patterns of control voltage varying the

merging, mixing and splitting of the biochemical droplet samples.

Figure 2.11: Schematic design of digital microfluidic biochip [11]

(c) Rectangular mixing channel

A method of mixing process in the micro-channel flows of microfluidic developed

measured and analysed the pressure during drive the fluid. Thus both of the two fluid

streams in pressure driven rectangular microfluidic channel [12]. Spectral method

were used in three dimensional equation to determine the non-uniform and uniform

mixing process for both fluids. The project carries out by analyse and measure the

mix of two fluids on silicon and poly (methyl methacrylate) (PMMA) based T-type

micro mixers.

Figure 2.12: Block diagram of setup for mixing pressure-driven microfluidic [12]

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(d) Vibrating micro-plate mixer

Mixing concept based on a vibrating micro-plate in microfluidic channel [13,14]

project developed to determine and to find the efficient mixing of solvent in

microfluidic. It done by decrease the diffusion path and increase the contact area

between fluids to be mixed. It used numerical investigation conducted by COMSOL

to determine the parameter of flow velocity, amplitude and frequency of vibrating

plate. Method used for this project by design two fluid streams with different

concentration flow into upper and down half of microfluidic channel. The channel

design with 250µm length and 50µm depth, meanwhile the micro-plate dimension is

20µm length and 5µm depth.

Figure 2.13: Channel of microfluidic geometry and operating parameter [13]

Figure 2.14: Channel of microfluidic design using COMSOL [13]

(e) Serial dilution micro-mixer

One of technique project developed to determine the estimation of microbial counts

obtained by using the serial dilution technique [14]. The techniques used to

investigate the microorganisms’ growth on bacteriological media and develop into

colony. The method used Agar plate to estimate the microbial counts of colony size

and plate area. The dilution ratios used from 2 to 100 ml and microbial counts

between 104 and 1012 microns of colony-forming units and 6.25 to 200 of size ratio

for plate size. This method proposed to shows the relative accuracy within ± 0.1

𝑙𝑜𝑔10 reading from computer simulations.

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Figure 2.15: Graphical abstract for serial dilution experiments of microorganisms’ growth in

bacteriological [14]

(f) Straight, square wave and 3D serpentine micro-mixer

The other applications that used in microfluidic is mixing [13]. This project

developed to study about the computational of mixing a fluids in micro-channel to

define the mixing efficiency of fluid in straight, square-wave and three dimensional

(3D) serpentine micro-channels [1]. This project used COMSOL Multiphsyics [15]

to determine the velocity of fluids flow and use CATIA v6 software. To

characterized the mixing efficiency of fluids, this project used fluid concentration

from 0mol/𝑚3 and 50mol/𝑚3 with water and dilute with two different inlets in the

micro-channel.

Figure 2.16: 3 types of micro-channel used to determine the fluid velocity in micro-channel

[15]

Figure 2.16 shows the design of the micro-channel used to study about the

differences of mixing efficiency in the micro-channels. For experiment 1, then test

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was handled by using (a) straight micro-mixer, then the test repeated by using (b)

square wave micro-mixer and lastly (c) Serpentine micro-mixer.

(g) One channel micro-mixer

The project developed to studies about the fundamental concept of mixing fluids

with the microfluidic devices. The studies taking the consideration for the design of

the mixing application performances such as mixing index and residence time [16].

The gradient of the concentration of the species of fluid mixed called Fick’s Law

[17] defined to relate it with the proportional of flux to the gradient between two

reservoirs in the microfluidic devices to carry out the process of random motion for

fluid and the instantaneous state during the process.

Figure 2.17: Schematic of two input reservoir of microfluidic to mix two different fluid [16]

2.4.2 Applications of microfluidic mixers

From the previous literature review for the microfluidic mixers, the Table 2.1 shows

the summarization concluded from the previous literature review to define the

applications of various type the microfluidic mixer used in the microfluidic project.

Table 2.1: Applications of Microfluidic mixer used in the previous project developed

Types of Micromixer Application

i. Single – Target Dilution Microfluidic a) To minimize number of mix

split-step of fluid.

b) To minimize waste droplet.

c) Develop IDMA [9] algorithm to

maximize the reuse of

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intermediate droplet.

ii. Digital Microfluidic Biochip a) Dilution for biochemical droplet

sample.

b) To reduce the production of

waste droplet.

iii. Rectangular Mixing Channel a) Determine the non-uniform and

uniform mixing process.

b) Measure pressure of fluid in

channel.

iv. Vibrating Microplate Mixer a) Find the efficient mixing of

solvent in microfluidic with two

fluid streams with different

concentration flow into upper and

down half of microfluidic

channel.

v. Serial Dilution Micromixer a) To determine the estimation of

microbial counts obtained

b) Investigate the microorganisms’

growth on bacteriological media.

vi. Straight, Square – Wave & 3D

Serpentine

a) To define the mixing efficiency

of fluid

vii. One Channel Micromixer a) Define the mixing index and

residence time gradient of the

concentration of the fluid mixed

2.5 Comparison of previous projects

From the research done for the previous project done relate to the syringe pump and

microfluidic, this is important to make a conclusion from the literature review done

to compare the previous project done to collect some data for analysing.

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Table 2.2: Comparison of different syringe pump systems for use with microfluidic device

Associated Project Flow Rate Material Use Reference

i) Novel

Mechanical

Syringe Pump

i. Flow rate from

5cc/hr to 40cc/hr

i) electric motor

ii) Neonatal Syringe

Pump (NeoSyP)

iii) Syringe Plunger

Cynthia Sung et al.

2011 [5]

ii) In Line Gear

Pump

i) 350 µl/min at

5000 rpm

ii) 200 ml/min at

4000 rpm

i) Microfabricated

pump

ii) In-linear gear

pump

Andrew S.Dewa et

al. 1997 [6]

iii) Self-

Aligning/ Liquid

Micropump

i) 1500

µl/𝑚𝑖𝑛−1 for

liquid pump

ii) 690 µl/𝑚𝑖𝑛−1

for gas pump

i) Micropump

C.G.J Schabmuller

et al. 2002 [7]

iv) Micro-Jet Pump i) Pressure of

2kPa

i) Vacuum suction Xiuhan Li et al.

2006 [8]

As shown in Table 2.2 is the comparison of the differences between the associated

project by taking the flow rate reading of the fluid flow and materials from the

previous related to the infusion pump The pump developed which is neonatal syringe

pump, micro-fabricated pump, in-line gear pump, micro-pump and vacuum suction

pump were used during the project development on the previous project.

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Table 2.3: Comparison between project application techniques in microfluidic device

Associated

Project

Project Description Method References

i) Waste-aware

Single-target

Dilution of a

Biochemical

Fluid Using

Digital

Microfluidic

(DMF)

Biochips

i) Dilution process of

a biochemical by

using a digital

microfluidic (DMF)

biochips [9] and

mapping lab-bench

protocol for an

automate process.

i) Digital

microfluidic

(DMF) biochips

ii) Improved Dilution/

Mixing Algorithm

(IDMA)

Sudip Roy et al.

2015 [10,11]

ii) Analysis and

Measurement

of Mixing in

Pressure-

Driven

Microchannel

Flows

i) Determine the non-

uniform and

uniform mixing

process for both

fluids

ii) Analyse and

measure the mix of

two fluids on silicon

and poly (methyl

methacrylate)

(PMMA) based T-

type micro mixers

i) Spectral method 1. Jerry M. Chen et

al. 2006 [12]

iii) Simulation of a

Vibrating-Plate

based

Micromixer

i) To studies a mixing

concept based on a

vibrating microplate

in microfluidic

channel to achieve

an efficient mixing

i) COMSOL Software 1. Hongwei Sun et

al. 2006 [13]

iv) Estimation

Method for

i) To determine the

estimation of

i) Agar Plate used

from 2 to 100 ml

1. Avishai Ben-

David et al.

22

Serial Dilution

Experiments

microbial counts

obtained with the

serial dilution

technique

ii) The techniques to

investigate the

microorganisms’

growth on

bacteriological

media and develop

into colony

ii) Amicrobial counts

between 104 and

1012 microns of

colony-forming

units

iii) 6.25 to 200 of size

ratio for plate size

2014 [14]

v) Computational

Analysis for

Mixing of

Fluids Flowing

through Micro-

Channels of

Different

Geometries

i) To define the

mixing efficiency of

fluid in straight,

square-wave and

three dimensional

(3D) serpentine

micro-channels.

ii) Fluid concentration

from 0 mol/𝑚3 and

50 mol/𝑚3 with

water and dilute

with two different

inlets in the micro-

channel.

i) COMSOL software

ii) Catia v6 software

1. Sankha Shuvra

Das et al. 2014

[15]

vi) A Review on

Mixing in

Microfluidics

i) To studies about the

fundamental

concept of mixing

fluids with the

microfluidic devices

i) Using two reservoir

on microfluidic

technique

1. Yong Kweon

Suh et.al, 2010

[16]

23

As shown in Table 2.3 shows the few methods used for dilution and mixing the

chemical solution in the microfluidic channels. Based on the previous studies, the

microfluidic mixer basically used for cell culture, determine the mixed solution in

different channel design and etc. All the mixer used as a main application widely in

the biochemical studies.

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CHAPTER 3

METHODOLOGY

This chapter included the discussion on the design and simulation for the

microfluidic dilution device, the development of the infusion pump, and verification

of the performance of the infusion pump and the fabrication of the device. The flow

and pressure formed in the microfluidic mixer designed for dilution purpose was

studied in the Comsol Multiphysic version 5.1 software. While the infusion pump

was customised to provide suitable flow rates to achieve the four dilutions required

by the project. The calibration steps for the infusion pump to work together with the

microfluidic is required in order to prevent problems such as spillage and wastage of

fluid from the syringe while performing the desire functions. The design of the

microfluidic influenced the flow process when fluid was injected from the infusion

pump to the microfluidic device. Thus, the outcome of the project is to produce fluid

in different dilution concentrations at the output channel of the microfluidic mixer.

3.1 The flow chart of the project

In this part, the project progress was discussed for the related project development

progress for the simulation, fabrication and design of the microfluidic dilution and

infusion pump system.