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ABSTRACT
The recovery of glycerine from spent soap lye has been done using soap lye samples obtained from the hot process of soap production using palm kernel oil (P.K.O). The main advantage of hot process is that exact concentration of the lye solution is not known, but to perform this with adequate success, the lye and fat are boiled together at 80 – 1000C at times above 1000C until saponification occurs. The overall weight of glycerine recovered per 100g of oil used was 9.0g. The quantity of spent soap lye obtained was 250ml, Acid value was 555.39, percentage free acid value was 5.6%, total fatty acid = 7.131, percentage free caustic acid = 0.14%, percentage free fatty acid obtained was 0.07131%, the specific gravity was 1.059, purity of glycerine was 92%. These parameters obtained were measured relatively to international standards with negligible error due to the type of equipment used. From the result, it is evident that the amount of glycerine recovered depends largely on the quantity of spent soap lye. Other processes the spend soap lye and the glycerine undergo as may be seen in other chapters includes, salting out, filtration, splitting and others.
TABLE OF CONTENTS
Title page i
Letter of Transmittal ii
Approval page/certification iii
Approval page iv
Dedication v
Acknowledgement vi
Abstract vii
Table of Contents viii
List of Figures/Tables xii
Definition of Terms/Nomenclature xiii
CHAPTER ONE
1.0 Introduction 1
1.1 Background of the study 1
1.2 Statement of the problem 4
1.3 Scope and limitation of the study 6
1.4 Purpose/aim/objectives of the study 6
1.5 Method of Research 7
1.6 Significance of the study 8
CHAPTER TWO
2.0 Literature Review 10
2.01 History of glycerine 13
2.02 Lye clarification 16
2.03 Recovery of glycerine from spent lye 25
2.04 Twitchel process 38
2.05 Autoclave saponification 48
2.06 Lime saponification 49
2.07 Acid saponification 52
2.08 Aqueous saponifictaion 54
2.09 Splitting fats with ferments 55
2.10 Krebitz porcess 59
2.11 Distillation of fatty acids 62
2.12 Glycerol detection and estimation 66
2.13 Glycerine as a by-product of soap
manufacture 75
2.14 Process description of soap production 78
2.15 Process summary 79
2.16 Step 1: oil preparation 79
2.17 Ion exchange 81
2.18 Soap removal 82
2.19 Composition of glycerine production 83
2.20 Physical properties of glycerine 87
2.21 Chemical properties of glycerine 88
2.22 Sources and types of lipids 90
2.23 Distinction between fats and oils 91
2.24 Uses of glycerine 93
2.25 Major types of saponification 95
2.26 Separation of glycerine and free fatty acid 99
2.27 Quantifying the phosphoric acid to be used 100
2.28 Metabolism 102
2.29 Application of glycerine in food 103
2.30 Application of glycerine in urethane polymers 104
2.31 Application of glycerine in drugs and cosmetics 104
2.32 Application of glycerine as a lubricant. 106
2.33 Application of glycerine in snuffs 106
2.34 Other uses of glycerine 107
2.35 Hyper osmotic effects 108
2.36 Basic raw material for flycerine production. 108
CHAPTER THREE
3.0 Experimental Procedure 111
3.01 The Saponification Process 112
3.02 Splitting Method 115
3.03 Determination of the viscosity of Glycerine 116
3.04 Titration 117
3.05 Percentage Free Alkaline (FCA) 118
3.06 Bleaching of Crude Glycerine 119
CHAPTER FOUR
4.0 Experimental Result and Analysis 121
CHAPTER FIVE
5.0 Discussion 128
5.1 Conclusion 128
5.2 Recommendation 129
References 131
Appendices 132
LIST OF FIGURES/TABLE
Table 2.0: Properties of glycerine 87
Table 2.1: Physical properties of glycerine 86
Table 4A: Glycerine producer association standard for Glycerine recovery 121
Table 4B: Estimation consumption of glycerol in various industries 122
Table 4C: Order of increment of the amount of % glycerine in all the samples. 124
Table 4D: Standard deviation table for percentage (%) salt and percentage glycerine 127
DEFINITION OF TERM/NOMENCLATURE
% = Percentage
N/4 = Quarter normal
Lbs = Pounds
C.C = Cubic centimeter
PZ = Paterson Zochonis
IEA = International Equitable Association
KSI =
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