membrane application in the recovery of gaharu …

24
MEMBRANE APPLICATION IN THE RECOVERY OF GAHARU ACTIVE MARKER COMPOUND FROM WATER MIXTURE CHIN WENG FOO Thesis submitted in partial fulfilment of the requirements for the award of the degree of Bachelor of Chemical Engineering Faculty of Chemical & Natural Resources Engineering UNIVERSITI MALAYSIA PAHANG FEBRUARY 2013

Upload: others

Post on 03-Oct-2021

2 views

Category:

Documents


0 download

TRANSCRIPT

MEMBRANE APPLICATION IN THE RECOVERY OF GAHARU ACTIVE

MARKER COMPOUND FROM WATER MIXTURE

CHIN WENG FOO

Thesis submitted in partial fulfilment

of the requirements for the award of the degree of

Bachelor of Chemical Engineering

Faculty of Chemical & Natural Resources Engineering

UNIVERSITI MALAYSIA PAHANG

FEBRUARY 2013

TABLE OF CONTENTS

PAGE

TITLE PAGE i

ACKNOWLEDGEMENT ii

TABLE OF CONTENTS iii

LIST OF TABLES vi

LIST OF FIGURES vii

LIST OF SYMBOLS xi

LIST OF ABBREVIATIONS xii

ABSTRACT xiii

ABSTRAK xiv

CHAPER 1 INTRODUCTION

1.1 Background of Study 1

1.2 Problem Statement 1

1.3 Objectives of Study 2

1.4 Scope of Study 2

CHAPTER 2 LITERATURE REVIEW

2.1 Introduction 4

2.2 History of Gaharu 5

2.3 Gaharu Marker Compound 6

2.3.1 Agarospirol 7

2.3.2 Jinkohol II 8

2.3.3 α-guaiene 9

2.3.4 Seline-3,11-dien-9-al 10

2.4 Membrane Separation 11

2.4.1 Introduction 11

2.4.2 Advantage of Membrane Separation 11

2.4.3 Nanofiltration 13

2.4.4 Ultrafiltration 14

2.4.5 Microfiltration 15

2.4.6 Factors that Affect the Membrane Performance 16

2.5 Mass Transfer in Membrane 18

2.5.1 Diffusion 18

2.5.2 Permeability and Selectivity 20

CHAPTER 3 Methodology

3.1 Membrane Selection 22

3.2 Milipore Stirred Ultrafiltration Cell Model 8200 23

3.3 Field Emission Scanning Electron Microscope 26

3.4 Preparative HPLC 26

3.5 Permeability Calculation 28

3.6 Experimental Procedure 28

3.6.1 List of Equipments 28

3.6.2 Experimental Procedure 29

CHAPTER 4 RESULT AND DISCUSSION

4.1 Results 33

4.2 Results for Membrane Filtration Experiment 34

4.3 Field Emission Scanning Electron Microscope Testing 39

4.3.1 SEM Image of TS40 Membrane Before Experiment 39

4.3.2 SEM Image of SB90 Membrane Before Experiment 42

4.3.3 SEM Image of TS40 after the Experiment for Run 1 44

4.3.4 SEM Image of TS40 after the Experiment for Run 2 48

4.4 Preparative HPLC Testing 52

CHAPTER 5 CONCLUSION AND RECOMMENDATION

5.1 Conclusion 59

5.2 Recommendation 60

REFERENCES 62

vi

LIST OF TABLES

PAGE

Table 2.1 Properties of Agarospirol 7

Table 2.2 Properties of Jinkohol II 8

Table 2.3 Properties of α-guainene 9

Table 2.4 Properties of Selina-3,11-dien-9-al 10

Table 2.5 Properties of Nanofiltration, Ultrafiltration and 16

Microfiltration Membrane

Table 3.1 Parts List for AMICON 8200 25

Table 4.1 Results for TS40 Run 1 34

Table 4.2 Results for TS40 Run 2 34

vii

LIST OF FIGURES

PAGE

Figure 2.1 Aquilaria Malaccensis Tree 6

Figure 2.2 Molecular Structure of Agarospirol 7

Figure 2.3 Molecular Structure of Jinkohol II 8

Figure 2.4 Molecular Structure of α-guainene 9

Figure 2.5 Molecular Structure of selina-3,11-dien-9-al 10

Figure 3.1 Molecular Structure of polypiperazine amide 23

Figure 3.2 Molecular Structure of cellulose acetate 23

Figure 3.3 AMICON 8200 Model 24

Figure 3.4 Parts List for AMICON 8200 25

Figure 3.5 Methodology for Preparative HPLC 27

Figure 3.6 Flow of Experimental Procedure 29

Figure 3.7 Experimental Set Up of Membrane Separation 32

Figure 4.1 Graph of Permeate Flux vs Pressure for TS40 Run 1 34

viii

Figure 4.2 Graph of Permeate Flux vs Pressure for TS40 Run 2 35

Figure 4.3 Water flux for unmodified and modified membranes 36

Figure 4.4 Molecular Structure of Cellulose Acetate 37

Figure 4.5 Circular stain on SB90 Membrane 37

Figure 4.6 Yellowish Stain on SB90 Membrane 38

Figure 4.7 Two Yellowish Stain on SB90 Membrane 38

Figure 4.8 Upper Coating of TS40 at 60x 40

Figure 4.9 Upper Coating of TS40 at 7000x 40

Figure 4.10 Rough Surface of TS40 at 200x 41

Figure 4.11 Rough Surface of TS40 at 500x 41

Figure 4.12 Rough Surface of TS40 at 1000x 42

Figure 4.13 Rough Surface of SB90 at 200x 43

Figure 4.14 Rough Surface of SB90 at 500x 43

Figure 4.15 Rough Surface of SB90 at 1000x 44

Figure 4.16 Gaharu Extract on the Surface of TS40 at 100x 45

ix

Figure 4.17 Gaharu Extract on the Surface of TS40 200x 45

Figure 4.18 Gaharu extract on the surface of TS40 750x 46

Figure 4.19 Gaharu extract on the surface of TS40 5000x 47

Figure 4.20 Gaharu Extract on the Surface of TS40 at 10000x 47

Figure 4.21 Gaharu Extract on the Surface of TS40 at 30000x 48

Figure 4.22 Gaharu Extract on the Surface of TS40 1000x 49

Figure 4.23 Gaharu Extract on the Surface of TS40 5000x 49

Figure 4.24 Gaharu Extract on the Surface of TS40 10000x 50

Figure 4.25 Gaharu Extract on the Surface of TS40 20000x 50

Figure 4.26 Gaharu extract on the surface of TS40 30000x 51

Figure 4.27 HPLC Result for Gaharu Water Mixture from Industry 53

Figure 4.28 HPLC Result for TS40 1 Bar Run 1 Permeate 54

Figure 4.29 HPLC Result for TS40 3 Bar Run 1 Permeate 54

Figure 4.30 HPLC Result for TS40 4 Bar Run 1 Permeate 55

Figure 4.31 HPLC Result for TS40 2 Bar Run 2 Permeate 55

x

Figure 4.32 HPLC Result for TS40 3 Bar Run 2 Permeate 56

Figure 4.33 HPLC Result for TS40 4 Bar Run 2 Permeate 56

Figure 4.34 HPLC Result for TS40 2 Bar Run 1 Permeate 57

Figure 4.35 HPLC Result for TS40 1 Bar Run 2 Permeate 58

xi

LIST OF SYMBOLS

V Volume of permate

A Effective area of membrane

P Pressure of nitrogen gas

t Time to collect permeate

xii

LIST OF ABBREVIATIONS

FESEM - Field Emission Scanning Electron Microscope

HPLC - High Performance Liquid Chromatography

MF - Microfiltration

NF - Nanofiltration

UF - Ultrafiltration

xiii

MEMBRANE APPLICATION IN THE RECOVERY OF GAHARU ACTIVE

MARKER COMPOUND FROM WATER MIXTURE

ABSTRACT

This study focuses the membrane application in the recovery of gaharu active

marker compound from water mixture. The objective of this study is to design the

separator process using membrane technique to recover gaharu active marker

compound from water mixture and to analyse the recovered gaharu marker

compound using membrane separation. The gaharu marker compounds that needed

to be separated are agarospirol, jinkohol, α-guainene and selina-3,11-dien-9-al.

Preparative High Performance Liquid Chromatography was used as the qualitative

analysis of the gaharu active marker compound in the mixture. The membrane was

applied to separate the marker compound from the water mixture. Milipore Stirred

Ultrafiltration Cell Model 8200 was used as the membrane separation proces unit.

Field Emission Scanning Electron Microscopy was used to capture microscope

image of the TS40 and SB90 nanofiltration membrane used in the experiment. At the

end of the experiment, TS40 nanofiltration membrane was able to separate the

gaharu marker compounds at the average flux value of 0.45 ml/cm2.h to 2.00

ml/cm2.h with varying pressure from 1 bar to 4 bar.

xiv

APLIKASI MEMBRAN DALAM PEMULIHAN SEBATIAN KIMIA

GAHARU YANG TERDAPAT DALAM CAMPURAN AIR

ABSTRAK

Kajian ini berfokus pada aplikasi membran untuk pemulihan sebatian kimia

gaharu yang terdapat dalam campuran air gaharu. Objektif kajian ini adalah untuk

mereka bentuk satu proses pemisahan menggunakan teknik membran untuk

pemulihan sebatian kimia gaharu dalam campuran air and juga untuk menganalisis

sebatian kimia gaharu yang telah melalui proses pemulihan menggunakan proses

pemulihan membran. Sebatian kimia gaharu yang ingin dipisahkan adalah

agarospirol, jinkohol, α-guainene dan selina-3,11-dien-9-al. Kromatografi Cecair

Berprestasi Tinggin telah digunakan kualiti analisis untuk sebatian kimia gaharu

dalam campuran air. Membran telah digunakan untuk memisahkan sebatian kimia

gaharu dalam campuran air. "Milipore Stirred Ultrafiltration Cell Model" telah

digunakan sebagai proses unit untuk pemisahan membran. "Field Emission Scanning

Electron Microscopy" digunakan untuk menangkap imej mikroskop membran TS40

dan membran SB90. Di akhir experimen ini, membran TS40 dapat memisahkan

sebatian kimia gaharu dengan nilai fluks purata dari 0.45 ml/cm2.h hingga 2.00

ml/cm2.h dengan tekanan dari 1 bar hingga 4 bar.

1

CHAPTER 1

INTRODUCTION

1.1 Background of Study

Gaharu or agarwood is one of the most famous incenses in the East. Gaharu

are mainly produced by trees of Aquilaria and Gyrinops. The most popular species of

Aquilaria in Peninsular Malaysia is Aquilaria Malaccensis. Gaharu oil is formed by

mixtures of sesqiuternes, sesquiternes alcohol, chromone derivatives and resin

(Adam et al. 2011). The important key components that contribute the aroma of

gaharu are agarospirol, jinkohol-eremol, jinkohol and kusenol.

1.2 Problem Statement

Nowadays, membrane separation is one of the most popular methods of

separation because of its capability. The use of membrane for separation is becoming

increasingly important in the process industries. In this study, membrane is applied to

2

separate the gaharu marker compound from the gaharu water mixture. A suitable set

of membrane are needed to separate these marker compounds. The membranes are

selected based on their pore size, permeability and selectivity.

The selected membrane to be used must be made up of compound that can

have molecular interaction with the marker compounds that present inside the gaharu

marker compounds. By using the correct compound, the membrane can pull the

marker compounds into its surface and thus separating them from the gaharu water

mixture.

1.3 Objective of Study

In this study, the objectives which aims to be achieved are :

1. To design the separator process using membrane technique to recover gaharu

active marker compound from water mixture

2. To analyse the recovered gaharu marker compound using membrane separation

3. To make comparison between membranes that were used

1.4 Scope of Study

In this study, there are a few parameters that are needed to be controlled. The

parameters include permeability and selectivity of the membrane, permeate flux and

3

the pressure where these parameters will affect the membrane's performance in the

separation process.

During the experiment, the membrane performance can affect how the marker

compounds of gaharu are being separated and filter out. Therefore, it is important to

know the concept of permeability, selectivity, mass transfer and diffusion process in

a membrane system.

4

CHAPTER 2

LITERATURE REVIEW

2.1 Introduction

One of the objectives of this chapter is to explain the gaharu and its marker

compound. Explanation on gaharu will be more detailed in the Aquilaria Malaccensis

species which are found in Peninsular Malaysia. Then this chapter will explain the

types of membrane that can be used in membrane separation.

The literature review is done based on the journals that are related Aquilaria

Malaccensis species of gaharu. The literature review will cover the origins, types and

characteristics of Aquilaria Malaccensis. This chapter will also cover the gaharu

marker compound in its essential oils

The membrane application will also be covered in the scope of this chapter.

Types of membranes, properties and their application will be explained in this

5

chapter. There are three types of membrane that will be discussed here which are

ultrafiltration, microfiltration and nanofiltration.

This chapter will let the reader to know the importance of gaharu and its

marker compound. The concept of membrane separation will be explained to the

reader.

2.2 History of Gaharu

Gaharu is a fragnant wood that is derived from the diseased timber of the

genus Aquilaria. It is often occurs as dark coloured patches or streaks in the tree.

Gaharu oil is greatly valued as perfume ingredient and incense because of its strong,

unique scent and medical properties (Nor Azah et al. 2008).

Aquilaria genus is an aromatic plant that is commonly known as “Gaharu

Wood” in South East Asia. The Aquilaria species is found mostly in Malaysia,

Indonesia, India, Iran, Singapore, Bangladesh, Myanmar, Philippines and Thailand.

One of the species, Aquilaria Malaccensis produces valuable resin marinate in the

heartwood (Ibrahim et al. 2011).

6

Figure 2.1 Aquilaria Malaccensis Tree

Gaharu are classified into various grades such as Grade A, Grade B, Grade C

and Grade D. Gaharu is graded according to their physical properties, formation and

their unique scent (Nor Azah et al. 2008). Aquilaria Malaccensis produces valuable

resin marinate in the heartwood which originates as a consequences of natural

immune response towards fungal attack. One of the fungus, endophyte lives inside

healthy plant tissues. Some of these endophytes have found to have anticancer and

antidiabetic properties. Essential oils of Aquilaria Malaccensis is safe and simple to

use. It is produced and commonly used in traditional medicine to relieve pain, fever,

rheumatism, and asthma (Ibrahim et al. 2011).

2.3 Gaharu Marker Compound

The lower grades of gaharu such as Grade C are often distilled to get gaharu

oil (Nor Azah, 2008). In an extraction process, the presence of main components

such as agarospirol, jingkohol-eremol, jingkohol and eremol are found in gaharu

essential oils. In this study, it is desired to separate four compounds from the gaharu

water mixture using membrane separation. The four compounds are agarospirol,

jinkohol, guainene and selina.

7

2.3.1 Agarospirol

Agarospirol is a chemical compound that consists of fifteen carbon atoms,

twenty six hydrogen atoms and one oxygen atom. The molecular weight and volume

are 222.366 and 183.5 respectively. This compound has five methyl groups and a

functional group of hydroxyl.

Agarospirol is reported as one of the main marker compound that contribute

to the scent of gaharu. Figure 2.2 represent the molecular structure of agospirol.

Table 2.1 shows the chemical formula and molecular weight of agarospirol.

Figure 2.2 Molecular Structures of Agarospirol

Table 2.1 Properties of Agarospirol

Chemical Formula Molecular Weight

C15H26O 222.366

8

2.3.2 Jinkohol II

Jinkohol II is a chemical compound that consists of fifteen carbon atoms,

twenty six hydrogen atoms and one oxygen atom. The molecular weight and volume

are 222.366 and 176.64 respectively. It has three methyl group and the functional

group of one hydroxyl group.

Similar with agarospirol, jinkohol II is classified as the main marker

compound in gaharu. Jinkohol II also contributes to the characteristic aroma of

gaharu. Figure 2.3 represent the molecular structure of jinkohol II. Table 2.2 lists the

chemical formula and molecular weight of the compound.

Figure 2.3 Molecular Structure of Jinkohol II

Table 2.2 Properties of Jinkohol II

Chemical Formula Molecular Weight

C15H26O 222.366

9

2.3.3 α-guaiene

α-guaiene is a chemical compound that consists of five carbon atoms, five

hydrogen atoms, five nitrogen atoms and an oxygen atom. The molecular weight and

volume are 151.126 and 83. It has three double bonds.

α-guaiene is one of the main marker compound in the gaharu water mixture.

Therefore it is one of the most important compound that present in the gaharu water

mixture. Figure 2.4 represent the molecular structure of α-guaiene. Table 2.3 lists the

chemical formula and molecular weight of α-guaiene.

Figure 2.4 Molecular Structures of α-guaiene

Table 2.3 Properties of α-guaiene

Chemical Formula Molecular Weight

C5H5N5O 151.126

10

2.3.4 Selina-3,11-dien-9-al

Selina-3,11-dien-9-al is a chemical compound consists of hydrogen bonds

and methyl groups. Similarly with other compounds that were explained above,

selina-3,11-dien-9-al is also one of the main marker compound that present inside the

gaharu.

The molecular structure of selina-3,11-dien-9-al has the functional group of

hydroxyl. Figure 2.5 represent the molecular structure of selina-3,11-dien-9-al. Table

2.4 lists the chemical formula and molecular weight of selina-3,11-dien-9-al.

Figure 2.5 Molecular Structure of Selina-3,11-dien-9-al

Table 2.4 Properties of Selina-3,11-dien-9-al

Chemical Formula Molecular Weight

C15H24O 220.35

11

2.4 Membrane Separation

2.4.1 Introduction

Membrane separation is becoming increasingly important in process

industries. In this process, the membrane acts as a semi permeable barrier. The

separation process occurs by the membrane controlling the rate of the movement of

various molecules between two liquid phases, two gas phases, or a liquid or a gas

phase (Geankoplis et al. 2003)

In this study, three types of membrane separation process will be discussed

which are ultrafiltration, nanofiltration and microfiltration.

2.4.2 Advantage of Membrane Separation

Membrane separation can be used in a number of applications. One of the

them is the separation of two chemical compounds in a mixture that have narrow

boiling points. In the field of hydrocarbon separations, the separation of condensed

olefin from corresponding paraffins is complicated process. Separation of paraffin

and olefin by conventional distillation is expensive and difficult as the two

substances has a narrow temperature ranges.

Therefore, membrane separation can be offered as an alternative for the

separation process. In the polymeric matrix membranes, the introduction of

12

chemically active sites can offer increase membrane selectivity and permeability.

This can therefore improve in the efficiency of olefin and paraffin separations

(Bessarabov et al. 1999).

Besides that, membrane separation can also be applied in the water and waste

water treatment plant. A number of advantages can be offered by membrane

processes over conventional water and waste water treatment processes. The

advantages include reduced environmental impact of effluents, land requirement

reduce, higher standards of final product and the potential of the mobile treatment

units of membrane process.

In the water and waste water treatment, membranes can used in a few

applications. The applications include removal of colour, trihalomethanes and other

disinfection by product removal and also iron removal.

Membrane processes are also reported to be cost effective in a few situations

and applications. It can be used as an alternative to conventional softening plant and

as a pretreatment plant for reverse osmosis (Owen et al. 1995).