Glycerine recovery from spent soap lye
Table Of Contents
Chapter ONE
INTRODUCTION
- 1.1Introduction
- 1.2Background of Study
- 1.3Problem Statement
- 1.4Objectives of Study
- 1.5Limitations of Study
- 1.6Scope of Study
- 1.7Significance of Study
- 1.8Structure of the Research
- 1.9Definition of Terms
Chapter TWO
LITERATURE REVIEW
- 2.1Overview of Glycerine Recovery
- 2.2Chemical Properties of Glycerine
- 2.3Traditional Methods of Glycerine Recovery
- 2.4Modern Techniques for Glycerine Recovery
- 2.5Environmental Impact of Glycerine Recovery
- 2.6Economic Aspects of Glycerine Recovery
- 2.7Global Trends in Glycerine Recovery
- 2.8Case Studies on Glycerine Recovery
- 2.9Future Prospects in Glycerine Recovery
- 2.10Summary of Literature Review
Chapter THREE
RESEARCH METHODOLOGY
- 3.1Research Design and Methodology
- 3.2Sampling Techniques
- 3.3Data Collection Methods
- 3.4Data Analysis Procedures
- 3.5Research Instruments
- 3.6Ethical Considerations
- 3.7Validity and Reliability
- 3.8Limitations of Methodology
Chapter FOUR
DATA PRESENTATION AND ANALYSIS
- 4.1Overview of Research Findings
- 4.2Analysis of Data
- 4.3Comparison with Existing Studies
- 4.4Interpretation of Results
- 4.5Discussion on Key Findings
- 4.6Implications of Findings
- 4.7Recommendations for Practice
- 4.8Suggestions for Future Research
Chapter FIVE
SUMMARY, CONCLUSION AND RECOMMENDATIONS
- 5.1Conclusion and Summary
- 5.2Recap of Objectives
- 5.3Key Findings Recap
- 5.4Contributions to Knowledge
- 5.5Practical Implications
- 5.6Recommendations for Action
- 5.7Areas for Future Research
- 5.8Closing Remarks
Thesis 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.
Thesis Overview
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</p><p><strong>1.0 INTRODUCTION</strong></p><p><strong>1.1 BACKGROUND OF THE STUDY</strong></p><p>Glycerine, (otherwise known as propan 1, 2, 3 triol) is found dissolved in the soap lye and also as an impurity in the crude soap during the saponification of fats and oils with caustic soda. Customarily, the process of soap manufacture, from fats and oil yields glycerol to about 10% of the value of the soap formed and due to its varied uses, its recovery is pertinent to the manufacturing cost analysis for any soap making business. Glycerol being an important bye product of soap manufacture, many small scale and medium scale soap manufacturers normally discards the lye as an unwanted product.</p><p>Glycerol occurs in nature combined in the form of triglycerides (fats and oil) and is obtained during the saponification of these triglycerides. This process was the only means of producing glycerol commercially, until 1949 when synthetic glycerol was produced as the compound recovered as by-product from the soap manufacture was sufficient for the world consumption. Alternatively, glycerol is synthesized from propene by the alternate chlorination and hydroxylation process. It is also obtained from the fermentation of various sugars. Glycerine is also produced by various routes from propylene. The epichlorohydrin process is the most important; it involves the chlorination of propylene to give ally chloride which is oxidized with a strong base to give epichlorohydrin. This epichlorohydrin is then oxidized to give glycerine.</p><p>In biodiesel, glycerine is a waste, as a result, the market for glycerol is depressed and the old epichlorohydrin process for glycerol synthesis is no more economically viable.</p><p>Fats and oils are esters of glycerine with long-chain fatty acid such as stearic acid (C17H35COOH) Palmitic acid (C15H31COOH) and oleic acid (C17H33COOH). Since glycerine contains three –OH groups, it can form three series of esters thus;</p><p>Mono-ester di-ester and tri-esters</p><p>CH2.OH CH2.OH CH2.O.OC.R</p><p>CH.OH CH.O.OC.R CH.O.OC.R</p><p>CH2.O.OC.R CH2.O.OC.R CH2.O.OC.R</p><p>Mono=-ester di-ester tri-ester</p><p>Some of the major industrial applications of glycerol include the manufacture of alkyd resins and flexible polyurethane for the plastic industry. It is also an important ingredient in cosmetics and adhesive manufacture. Many pharmaceutical preparations such as glycerol phenol mixture which serves as tranquilizers utilize glycerol.</p><p>Glycerol residue has been reported to contain 20.2% glycerol, 6.6% fatty acids (as soap) and 64.3% salt. Thus 91.1% of it is potentially useful. It is obviously advantageous, both environmentally and economically, to recover the glycerol in the waste material from soap industries as a potential alternative for the production of glycerol using chemical methods.</p><p><strong>1.2 PROBLEM STATEMENT</strong></p><p>The method of analyzing glycerine is greatly varied due to the fact that glycerine contained impurities which acted so much like glycerine as to introduce serious errors in the determination of crude glycerine. This however led to the appointment of committees in the United States and Europe to investigate the method of glycerine analysis. It was concluded in the meeting of the International Committee set for this purpose, that acetin method should control the buying and selling of glycerine, but the more convenient bichromate method in a standardized form might be used in factory control and other technical purposes.</p><p>The quantity of recovered residual salt is dependent on the point of recovery and nature of lye treatment. Neutralizes of the acid and alkaline content of the soap lye helps to reduce the amount of salt originally combined with soap by precipitation, coagulation and flocculation. This is done through their pH adjustments.</p><p>The whole process becomes entirely cumbersome as absolute care is taken to ensure that glycerine passes through all the stages required to obtain pure glycerine devoid of impurities.</p>
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