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The International Journal Of Engineering And Science (IJES) 
|| Volume || 3 || Issue || 8 || Pages || 77-83 || 2014 || 
ISSN (e): 2319 – 1813 ISSN (p): 2319 – 1805 
www.theijes.com The IJES Page 77 
Comparative Analysis on Sodium-Based and Polyethylene-Based Greases as Anti-Friction Agents 1, Iheme, C.; 2, Chukwuma, F.O; 1, Offurum, J.C. 1, Department of Chemical Engineering, Imo State Polytechnic, Umuagwo-Ohaji 2, Department of Chemical Engineering, University of Port-Harcourt ---------------------------------------------------------------ABSTRACT------------------------------------------------------ The activities of greases have been well utilized for regular lubrication purposes, as well as in friction control in machineries. These have, over the years, led to the increased demand for the product, which in turn have opened ways of livelihood to many. But the more attractive this business becomes to the dealers, the more sub- standard products fill up the market, especially in our localities. Many users of the products, thus, resorted to patronizing importers of these products, who deal mainly on Sodium-based greases that are after all not the best (in spite of their cost). The present study tends to draw attention to an alternative ‘friction controller’ – the Polyethylene Grease (otherwise called Copolymer greases) through a concise comparative analysis with the commonly used Sodium-based grease. The study samples were normally formulated by dispersion of low-density polyethylene in base oil at varying capacities, through saponification, evaporation, milling (homogenization) and filtration of the dispersed thickener in the base oil; Polypropylene was used as an additive to enhance the binding property of the product. A blend of the two grease samples (Sodium and Copolymer) was also obtained at the ratio of 1:3. Results of analysis conducted on the products showed that the Sodium-based grease has a higher dropping point (120-190oC) when compared with the Polyethylene and the blended greases, whose dropping points both fall between 120 – 185oC. The worked penetration for Polyethylene grease was found to be 280-340, while that of the Blended and Sodium are 275-340 and 230-340 respectively. Also, the copolymer grease appeared smooth and soft, while the Sodium grease appeared buttery and fibrous. However, it was demonstrated that the Copolymer grease is of better grade than the Sodium-based grease, and would resist water penetration very readily as well. Keywords: Comparative Analysis, Sodium-based, Polyethylene-based, Grease. --------------------------------------------------------------------------------------------------------------------------------------- 
Date of Submission: 02 June 2014 Date of Publication: 15 August 2014 --------------------------------------------------------------------------------------------------------------------------------------- 
I. INTRODUCTION 
Grease from the early Egyptian or Roman eras is thought to have been prepared by combining lime with olive oil. The lime saponifies some of the triglycerides that comprise oil to give calcium grease. In the middle of the middle of the 19th century, soaps were intentionally added as thickeners to oils. Over the centuries, all manner of materials have been employed as greases. For example, black slugs “Arion ater” were used as axle grease to lubricate wooden axle-trees or carts in Sweden (Svanberge, 2006). The oil Mist principle was developed by a bearing manufacturer in Europe during the 1930s. The problem that nurtured this development was the inability to satisfactorily lubricate high speed spindle bearings on grinders and similar equipment. The speed of these bearing was too high for grease lubrication, and liquid oil generated too much heat through fluid friction, necessitating an expensive recirculating system. Continuous thin-film lubrication with oil Mist provided a solution. The purging and slight cooling effects of the carrier air gave additional benefits. The oil Mist generator resulted later from this development and used a small amount of air to produce a less dense concentration of small oil particles. About 97% of these particles could be transmitted to the bearings without condensing in the piping, regardless of the distance of the bearings from the oil Mist generator itself. 
In some cases, the lubrication and high viscosity of grease are desired in situations where non-toxic, non-oil based materials are required. Carboxymethyl Cellulose (CMC) is one popular material used to create water-based analogue of greases. CMC serves both as a thickener to the solution, as well as to add a lubricating effect to the device, after which silicone-based lubricants could be added for additional lubrication. The most familiar example of this type of lubricant, used as a surgical and personal lubricant, is k-y Jelly. After a few decades, air heaters were developed because it was discovered that, by heating the air used to generate oil Mist, oils of just about any viscosity could be atomized. Many applications, subject to extremes in ambient temperature, use air heaters to ensure a constant oil/air ratio regardless of the oil viscosity. Today oil Mist is still used to lubricate high speed spindles in grinders. Included in the increasing range of oil Mist applications are systems applied to all types of other machine tools, web and sheet processing equipment, belt and chain conveyors rolling mills, vibrators, crushers, centrifuges, kilns, pulverizers, ball mills, dryers and liquid processing pumps.
Comparative Analysis on Sodium-Based and Polyethylene-Based Greases as Anti-Friction Agents 
www.theijes.com The IJES Page 78 
Regrettably, sodium-based greases that are commonly used in our devices are no longer promising as they are readily soluble in water. However, classification and standards jointly developed by ASTM international, the National Lubricating Grease Institute (NLGI) and the Society for Automotive Engineers (SAE) International, for automotive service greases was first published in 1989 by American Society for Testing and Materials (ASTM) international. It categorizes greases suitable for the lubrication of chassis components and wheel bearing vehicles, based on performance requirements, using codes adopted from the NLGI’s “Chassis and wheel bearing service classification system”. The present study, therefore, tends to draw attention to comparative features of the water-soluble grease (sodium-based) with an alternative option (polyethylene-based) in their activities as lubricants. MATERIALS AND METHOD Materials Used for the Study The apparatus used in the study include the following: 
 Beakers 
 Conical Flasks 
 Constant temperature water batch 
 Electromagnetic hot plate 
 Thermometers (0-360oC range) 
 Burette and pipette 
 Weighing Balance 
 Flat bottom flask 
 Measuring cylinder 
 Electric grinder 
 Funnel and filter paper 
 Hydrometers (for low and high density liquid) 
 Penetrometer and Grease worker 
 Dropping point apparatus 
 Grease cup (seta cup) 
 Heat resistant glass test-tube 
 Spatula 
 Reactor (metal containers - 4 litres capacity jug) 
Reagents Used for the Study Similarly, the reagents used for the study include the following: * Sodium hydroxide (caustic soda) * Potassium hydroxide * Hydrochloric acid * Neutralized ethanol * Phenolphthalein and methyl orange indicators * Fatty materials/vegetable oils (i) Palm oil from Owerri (OHAJI) (ii) Shea butter from Ilorin (iii) Tallow from (cow) (iv) Soya - bean oil. * low density polyethylene * Base oil (i) 500N (ii) 650N (Bright stock) (iii) 100N (v) 150N
Comparative Analysis on Sodium-Based and Polyethylene-Based Greases as Anti-Friction Agents 
www.theijes.com The IJES Page 79 
Research Methodology Dispersion of Low-density Polyethylene in Base Oil (100N, 500N, 650N) Measured quantities of low density polyethylene was dispersed in separate grades of base oils (100N, 150N, 500N, 650N or B/S) by heating. Example: 5grams of polypropylene was transferred into five (5) beakers each containing about 300mls of base oil and the content of the beaker was heated, each to a temperature of about 170 to 1800c to melt. It was later allowed to cool to a room temperature of 300c as shown in the table 1 below: TABLE1: VARIATION OF DISPERSED WEIGHT OF POLYETHYLENE IN A FIXED VOLUME OF BASE OIL AT 180oC A: 100N (BASE OIL ) AT 180oC B: 150N (BASE OIL) AT 180oC 
MASS OF POLYETHYLENE(g) 
VOLUME OF BASE OIL (cm3) 
MASS OF POLYETHYLENE(g) 
VOLUME OF BASE OIL (cm3) 
5 
300 
5 
300 
10 
300 
10 
300 
15 
300 
15 
300 
20 
300 
20 
300 
30 
300 
30 
300 
C: 500N (BASE OIL) AT 180oC D: 650N (BRIGHT STOCK (B/S)) AT 180oC 
MASS OF POLYETHYLENE(g) 
VOLUME OF BASE OIL (cm3) 
MASS OF POLYETHYLENE(g) 
VOLUME OF BASE OIL (cm3) 
5 
300 
5 
300 
10 
300 
10 
300 
15 
300 
15 
300 
20 
300 
20 
300 
30 
300 
30 
300 
Production of Sodium Base Grease Grease production involves a batch process that incorporates a technology bounded by saponification, evaporation, dispersion in a mineral fluid (Base oil), Recycling/cut back, milling or homogenizing and filteration of dispersed thickener in a base oil mixed with additives and modifiers (Totten et al, 2006). SAPONIFICATION AND EVAPORATION Saponification is the alkali hydrolysis of fatty matters to form soap. 103 grams of caustic soda solution prepared by dilution to a concentration of 26% with the specific gravity of 1.275 at room temperature of about 30oC was weighed into the plastic container based on (S.V) of palm oil. The palm oil in the reactor was heated to a temperature of 600C (saponification temperature), followed by the gradual addition of already weighed caustic soda into the reactor. The mixture of the two components was stirred for a period of (5) minutes depending upon the volume of the reactants (fatty matter plus caustic soda solution) to saponify and form soap. The soap formed in the process was later heated up to a temperature of about (120oC to 130oC) (at atmospheric pressure) in other to remove water (by evaporation). That is the temperature at complete saponification, and the soap obtained at this stage was very thick and in a solid state.
Comparative Analysis on Sodium-Based and Polyethylene-Based Greases as Anti-Friction Agents 
www.theijes.com The IJES Page 80 
Fig. 1: Process Flow Sheet of Production of Sodium-Polyethylene (Co-Polymer) Greases. GREASE FORMATION AND MILLING OPERATION After saponification and evaporation at about 130oC, the soap formed is further heated to a temperature range of 170oC – 180oC. A little quantity of base oil was also added (depending on the mass of soap formed), so as to reduce friction or ease the stirring. At this temperature, the thickened soap melted to a liquid state and becomes gummy or sticky on little exposure to air. At this temperature (1800c) the soap was dispersed in base oil by gradual addition and stirring until the grease was formed. Here reasonable quantity of base oil was added (900m/s for 650N, 800mls for 500N and 500mls for 150N) in the respective production and dispersion of each of these base oil samples. NOTE: The total volume of base oil to be added per batch depends on the texture of the product sample on cooling to room temperature: say 30oC However, before allowing the grease to cool to room temperature, milling operation was performed by means of grinder at the temperature of 80oC (for homogenization). This method helped in reducing the particle size of the undispersed thickener in the base oil. BLENDING OPERATION Two hundred grams of dispersed polyethylene product and 200grams of the sodium grease were blended together at the temperature of 100oC by heating and stirring the two in a metal container (Reactor) for a period of 10–15 minutes, after which it was allowed for 24hours to cool.
Comparative Analysis on Sodium-Based and Polyethylene-Based Greases as Anti-Friction Agents 
www.theijes.com The IJES Page 81 
Quality Control Analysis of Grease 
WORKED PENETRATION 
400g of grease was cooled to 25oC and later transferred into the grease worker cup. The grease cup was 
Jared sharply on the bench to remove the air pockets. The grease cup was finally filled above the rim of the cup 
and scraped at an angle of 450c with the aid of spatula. The vent cock was closed and the grease inside the cup 
was subjected to 60 full double strokes of the plunger, completed in about one minute by timing it using a stop-watch, 
the plunger was finally returned to its top position at the end of one minute. 
The vent cock was opened and the top and plunger were removed. The plunger itself was scraped with 
spatula to remove all the grease that clings to it. The seta cup was used to fill the worked grease sample in 
readiness for penetration test. After loading the cup with grease, the excess grease was scrapped off above the 
rim of the cup by moving the blade of the spatula, held inclined towards the direction of the motion at an angle 
of 450, across the rim of the cup. 
PENETRATION MEASUREMENT 
400g of the test specimen was placed on the penetrometer table with one of the prepared faces upward. 
The mechanism was set to hold the cone in the “zero” position, and the apparatus was adjusted such that the tip 
of the cone just touched the surface at the centre of the test sample. Finally, the cone shaft was released rapidly 
and was allowed to drop for 5(five) seconds. The indicator shaft was gently depressed until it touched the cone 
shaft and penetration reading was taken from the indicator. The experiment was repeated up to three times. 
Hence the average result was recorded. 
DROPPING POINT OF LUBRICATING GREASE 
The Dropping Point is the temperature at which a conventional soap (thickened grease) passes from a 
semi–solid to a liquid state under the conditions of test; it is the temperature at which other non–soap (thickened 
greases), rapidly, separates from oil. This was determined by placing the grease sample in the cup, and a cone– 
shaped space created by means of a rod (manipulated through the orifice). A thermometer occupies the space, 
out of contact with the grease. Heating took place at specified rate and the temperature at which oil falls or drops 
(through the orifice of the cup) to the bottom of the test tube was noted. The operation was repeated as a check 
for consistency of the result, and the average reading was determined and recorded. 
RESULT AND DISCUSSION 
The results of analysis of the Samples are presented in figures 2 and 3, as well as tables 2–4 below. 
DROPPING POINT OF GREASE SAMPLES 
0 
50 
100 
150 
200 
650N 500N 150N 100N 
Capacity 
Dropping Point (oC) 
A 
B 
C 
Fig. 2: PLOT OF DROPPING POINT OF SAMPLS AT VARYING CAPACITIES 
WORKED PENETRATION OF THE GREASE SAMPLES 
0 
50 
100 
150 
200 
250 
300 
350 
400 
650N 500N 150N 100N 
Capacity 
Worked Penetration (%) 
A 
B 
C 
Fig. 3: PLOT OF WORKED PENETRATION OF SAMPLS AT VARYING CAPACITIES
Comparative Analysis on Sodium-Based and Polyethylene-Based Greases as Anti-Friction Agents 
www.theijes.com The IJES Page 82 
TABLE 2: ANALYSIS OF SODIUM-BASED GREASE (SAMPLE A) 
Sodium/polypropylene = 1:1 
Sodium plus polypropylene Grease with: 
PROPERTIES 
650N 
500N 
150N 
100N 
Dropping point (oC) 
190 
165 
150 
120 
Worked penetration 
230 
260 
320 
340 
Appearance 
Smooth and fibrous 
Smooth and fibrous 
Buttery and fibrous 
Buttery and fibrous 
Other Properties 
Adhesive and cohesive 
Adhesive and cohesive 
Adhesive and cohesive 
Adhesive and cohesive 
TABLE 3: ANALYSIS OF POLYETHYLENE CO-POLYMER GREASE (SAMPLE B) 
Polyethylene Grease 
PROPERTIES 
650N 
500N 
150N 
100N 
Dropping point (oC) 
185 
180 
150 
120 
Worked penetration 
280 
290 
330 
340 
Appearance 
Smooth and buttery 
Smooth and buttery 
Smooth and soft 
Smooth and soft 
Other Properties 
Cohesive 
Cohesive 
Cohesive 
Cohesive 
TABLE 4: Analysis Of Blended Sodium/Polyethylene Grease At 1:3 Ratio (Sample C) 
Sodium plus polypropylene Grease 
PROPERTIES 
650N 
500N 
150N 
100N 
Dropping point (oC) 
185 
175 
140 
130 
Worked penetration 
275 
290 
320 
340 
Appearance 
Smooth & fibrous 
Smooth & fibrous 
Buttery & fibrous 
Buttery & fibrous 
Other properties 
Adhesive 
Adhesive 
Adhesive 
Adhesive 
Pumpability(in centralized systems) 
Poor to fair 
Poor to fair 
Fair to good 
Fair to good 
Water resistance 
Fair to good 
Fair to good 
Fair to excellent 
Fair to excellent 
Oxidation stability 
Good 
Good 
Good 
Good 
The result of the analysis shows that there is higher dropping point in the Sodium-based grease (120- 190oC) when compared with those of Polyethylene copolymer and the blended greases, whose dropping points both fall between 120 – 185oC. This is traceable to the fact sodium concentration increases the gelatinization temperature, and as such reduces the intermolecular bonding between the molecules of the product (Astrom and Hoglund, 1990). It could be observed, also, that the Worked Penetration is best with the Polyethylene (Copolymer) grease sample (280-340), followed by the Blended sample (275-340), but least with the Sodium grease sample. This shows that the Polyethylene grease possesses greater ability of friction control as it will travel farer into the axles than its Sodium counterpart. The analysis also indicated that the lower cadre (100N and 150N) of the Polyethylene grease appears smooth and soft, unlike the Sodium-based grease that is buttery and fibrous. This feature goes a long way to demonstrate that the Copolymer grease is a better sample than the Sodium-based grease, and would resist water penetration very readily as well. CONCLUSION The present study shows that suitable and ideal concentration of caustic soda for soap manufacture is 26% and it corresponds with the specific gravity of (1.275) at the temperature of 30oC. The density of dispersed polyethylene/polypropylene in a fixed volume of base oil increases with increase in the mass of polyethylene/polypropylene dispersed. Even 10% of dispersed polypropylene in 650N ( Bright stock) base oil is ideal to fortify sodium grease in a good ratio (such as 3:1) in order to produce water resistance grease suitable for servicing bearings and other heavy duty equipment.
Comparative Analysis on Sodium-Based and Polyethylene-Based Greases as Anti-Friction Agents 
www.theijes.com The IJES Page 83 
REFERENCES 
[1]. Astrom .H. and Hoglund, E. (1990): Rheological Properties of Six Greases and their Base 
Oils; Technical report; Lulea University of technology, Sweden. 
[2]. Behling, R.D. and Tomahawk, W.I (1996): Ready Reference for Lubricant Fuel 
Performance of Lubricating Oils, pp 29-31; Lubrizol Corporation, U.S.A. 
[3]. Cheng, D.C.H (1999):The Art of Coarse Rheology; The British Society of Rheology; 3(1), 1–9. 
[4]. George T. Austin (1984): Shreve’s Chemical Process Industries; McGraw-Hill International Edition, New York. 
[5]. Gottlieb Hugo E, Kotlyar Vadim, and Nudelman Abraham (1997): NMR Chemical Shifts of Common Laboratory Solvents as Trace Impurities; The Journal of Organic Chemistry, 62 (21), 7512 – 7515. Kirk Othmer, (1983): Encyclopedia of Chemical Technology, John Willey and Sons, New York. 
[6]. Totten George E., Westbrook Steven R., and Shah Rajesh J. (2006): Fuels and Lubricants 
Handbook Technology, Properties, Performance and Testing; ASTM manual series, Vol. 37, Pp 498-560. 
[7]. Svanberg, I. (2006): Black slugs (Arion ater) as Grease: a Study of Technical Use of 
Gastropods; Journal of Ethnobiology; 26 (2), 229 – 309. 
[8]. Vinogradov. G.V., (1989): Rhelogical and Thermophysical Properties of Grease; Gordon 
and Breach Science publications, London. 
[9]. Webb, E.T. (1927): Modern Soap and Glycerine manufacture; Davis Brothers, London.

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Comparative Analysis on Sodium-Based and Polyethylene-Based Greases as Anti-Friction Agents

  • 1. The International Journal Of Engineering And Science (IJES) || Volume || 3 || Issue || 8 || Pages || 77-83 || 2014 || ISSN (e): 2319 – 1813 ISSN (p): 2319 – 1805 www.theijes.com The IJES Page 77 Comparative Analysis on Sodium-Based and Polyethylene-Based Greases as Anti-Friction Agents 1, Iheme, C.; 2, Chukwuma, F.O; 1, Offurum, J.C. 1, Department of Chemical Engineering, Imo State Polytechnic, Umuagwo-Ohaji 2, Department of Chemical Engineering, University of Port-Harcourt ---------------------------------------------------------------ABSTRACT------------------------------------------------------ The activities of greases have been well utilized for regular lubrication purposes, as well as in friction control in machineries. These have, over the years, led to the increased demand for the product, which in turn have opened ways of livelihood to many. But the more attractive this business becomes to the dealers, the more sub- standard products fill up the market, especially in our localities. Many users of the products, thus, resorted to patronizing importers of these products, who deal mainly on Sodium-based greases that are after all not the best (in spite of their cost). The present study tends to draw attention to an alternative ‘friction controller’ – the Polyethylene Grease (otherwise called Copolymer greases) through a concise comparative analysis with the commonly used Sodium-based grease. The study samples were normally formulated by dispersion of low-density polyethylene in base oil at varying capacities, through saponification, evaporation, milling (homogenization) and filtration of the dispersed thickener in the base oil; Polypropylene was used as an additive to enhance the binding property of the product. A blend of the two grease samples (Sodium and Copolymer) was also obtained at the ratio of 1:3. Results of analysis conducted on the products showed that the Sodium-based grease has a higher dropping point (120-190oC) when compared with the Polyethylene and the blended greases, whose dropping points both fall between 120 – 185oC. The worked penetration for Polyethylene grease was found to be 280-340, while that of the Blended and Sodium are 275-340 and 230-340 respectively. Also, the copolymer grease appeared smooth and soft, while the Sodium grease appeared buttery and fibrous. However, it was demonstrated that the Copolymer grease is of better grade than the Sodium-based grease, and would resist water penetration very readily as well. Keywords: Comparative Analysis, Sodium-based, Polyethylene-based, Grease. --------------------------------------------------------------------------------------------------------------------------------------- Date of Submission: 02 June 2014 Date of Publication: 15 August 2014 --------------------------------------------------------------------------------------------------------------------------------------- I. INTRODUCTION Grease from the early Egyptian or Roman eras is thought to have been prepared by combining lime with olive oil. The lime saponifies some of the triglycerides that comprise oil to give calcium grease. In the middle of the middle of the 19th century, soaps were intentionally added as thickeners to oils. Over the centuries, all manner of materials have been employed as greases. For example, black slugs “Arion ater” were used as axle grease to lubricate wooden axle-trees or carts in Sweden (Svanberge, 2006). The oil Mist principle was developed by a bearing manufacturer in Europe during the 1930s. The problem that nurtured this development was the inability to satisfactorily lubricate high speed spindle bearings on grinders and similar equipment. The speed of these bearing was too high for grease lubrication, and liquid oil generated too much heat through fluid friction, necessitating an expensive recirculating system. Continuous thin-film lubrication with oil Mist provided a solution. The purging and slight cooling effects of the carrier air gave additional benefits. The oil Mist generator resulted later from this development and used a small amount of air to produce a less dense concentration of small oil particles. About 97% of these particles could be transmitted to the bearings without condensing in the piping, regardless of the distance of the bearings from the oil Mist generator itself. In some cases, the lubrication and high viscosity of grease are desired in situations where non-toxic, non-oil based materials are required. Carboxymethyl Cellulose (CMC) is one popular material used to create water-based analogue of greases. CMC serves both as a thickener to the solution, as well as to add a lubricating effect to the device, after which silicone-based lubricants could be added for additional lubrication. The most familiar example of this type of lubricant, used as a surgical and personal lubricant, is k-y Jelly. After a few decades, air heaters were developed because it was discovered that, by heating the air used to generate oil Mist, oils of just about any viscosity could be atomized. Many applications, subject to extremes in ambient temperature, use air heaters to ensure a constant oil/air ratio regardless of the oil viscosity. Today oil Mist is still used to lubricate high speed spindles in grinders. Included in the increasing range of oil Mist applications are systems applied to all types of other machine tools, web and sheet processing equipment, belt and chain conveyors rolling mills, vibrators, crushers, centrifuges, kilns, pulverizers, ball mills, dryers and liquid processing pumps.
  • 2. Comparative Analysis on Sodium-Based and Polyethylene-Based Greases as Anti-Friction Agents www.theijes.com The IJES Page 78 Regrettably, sodium-based greases that are commonly used in our devices are no longer promising as they are readily soluble in water. However, classification and standards jointly developed by ASTM international, the National Lubricating Grease Institute (NLGI) and the Society for Automotive Engineers (SAE) International, for automotive service greases was first published in 1989 by American Society for Testing and Materials (ASTM) international. It categorizes greases suitable for the lubrication of chassis components and wheel bearing vehicles, based on performance requirements, using codes adopted from the NLGI’s “Chassis and wheel bearing service classification system”. The present study, therefore, tends to draw attention to comparative features of the water-soluble grease (sodium-based) with an alternative option (polyethylene-based) in their activities as lubricants. MATERIALS AND METHOD Materials Used for the Study The apparatus used in the study include the following:  Beakers  Conical Flasks  Constant temperature water batch  Electromagnetic hot plate  Thermometers (0-360oC range)  Burette and pipette  Weighing Balance  Flat bottom flask  Measuring cylinder  Electric grinder  Funnel and filter paper  Hydrometers (for low and high density liquid)  Penetrometer and Grease worker  Dropping point apparatus  Grease cup (seta cup)  Heat resistant glass test-tube  Spatula  Reactor (metal containers - 4 litres capacity jug) Reagents Used for the Study Similarly, the reagents used for the study include the following: * Sodium hydroxide (caustic soda) * Potassium hydroxide * Hydrochloric acid * Neutralized ethanol * Phenolphthalein and methyl orange indicators * Fatty materials/vegetable oils (i) Palm oil from Owerri (OHAJI) (ii) Shea butter from Ilorin (iii) Tallow from (cow) (iv) Soya - bean oil. * low density polyethylene * Base oil (i) 500N (ii) 650N (Bright stock) (iii) 100N (v) 150N
  • 3. Comparative Analysis on Sodium-Based and Polyethylene-Based Greases as Anti-Friction Agents www.theijes.com The IJES Page 79 Research Methodology Dispersion of Low-density Polyethylene in Base Oil (100N, 500N, 650N) Measured quantities of low density polyethylene was dispersed in separate grades of base oils (100N, 150N, 500N, 650N or B/S) by heating. Example: 5grams of polypropylene was transferred into five (5) beakers each containing about 300mls of base oil and the content of the beaker was heated, each to a temperature of about 170 to 1800c to melt. It was later allowed to cool to a room temperature of 300c as shown in the table 1 below: TABLE1: VARIATION OF DISPERSED WEIGHT OF POLYETHYLENE IN A FIXED VOLUME OF BASE OIL AT 180oC A: 100N (BASE OIL ) AT 180oC B: 150N (BASE OIL) AT 180oC MASS OF POLYETHYLENE(g) VOLUME OF BASE OIL (cm3) MASS OF POLYETHYLENE(g) VOLUME OF BASE OIL (cm3) 5 300 5 300 10 300 10 300 15 300 15 300 20 300 20 300 30 300 30 300 C: 500N (BASE OIL) AT 180oC D: 650N (BRIGHT STOCK (B/S)) AT 180oC MASS OF POLYETHYLENE(g) VOLUME OF BASE OIL (cm3) MASS OF POLYETHYLENE(g) VOLUME OF BASE OIL (cm3) 5 300 5 300 10 300 10 300 15 300 15 300 20 300 20 300 30 300 30 300 Production of Sodium Base Grease Grease production involves a batch process that incorporates a technology bounded by saponification, evaporation, dispersion in a mineral fluid (Base oil), Recycling/cut back, milling or homogenizing and filteration of dispersed thickener in a base oil mixed with additives and modifiers (Totten et al, 2006). SAPONIFICATION AND EVAPORATION Saponification is the alkali hydrolysis of fatty matters to form soap. 103 grams of caustic soda solution prepared by dilution to a concentration of 26% with the specific gravity of 1.275 at room temperature of about 30oC was weighed into the plastic container based on (S.V) of palm oil. The palm oil in the reactor was heated to a temperature of 600C (saponification temperature), followed by the gradual addition of already weighed caustic soda into the reactor. The mixture of the two components was stirred for a period of (5) minutes depending upon the volume of the reactants (fatty matter plus caustic soda solution) to saponify and form soap. The soap formed in the process was later heated up to a temperature of about (120oC to 130oC) (at atmospheric pressure) in other to remove water (by evaporation). That is the temperature at complete saponification, and the soap obtained at this stage was very thick and in a solid state.
  • 4. Comparative Analysis on Sodium-Based and Polyethylene-Based Greases as Anti-Friction Agents www.theijes.com The IJES Page 80 Fig. 1: Process Flow Sheet of Production of Sodium-Polyethylene (Co-Polymer) Greases. GREASE FORMATION AND MILLING OPERATION After saponification and evaporation at about 130oC, the soap formed is further heated to a temperature range of 170oC – 180oC. A little quantity of base oil was also added (depending on the mass of soap formed), so as to reduce friction or ease the stirring. At this temperature, the thickened soap melted to a liquid state and becomes gummy or sticky on little exposure to air. At this temperature (1800c) the soap was dispersed in base oil by gradual addition and stirring until the grease was formed. Here reasonable quantity of base oil was added (900m/s for 650N, 800mls for 500N and 500mls for 150N) in the respective production and dispersion of each of these base oil samples. NOTE: The total volume of base oil to be added per batch depends on the texture of the product sample on cooling to room temperature: say 30oC However, before allowing the grease to cool to room temperature, milling operation was performed by means of grinder at the temperature of 80oC (for homogenization). This method helped in reducing the particle size of the undispersed thickener in the base oil. BLENDING OPERATION Two hundred grams of dispersed polyethylene product and 200grams of the sodium grease were blended together at the temperature of 100oC by heating and stirring the two in a metal container (Reactor) for a period of 10–15 minutes, after which it was allowed for 24hours to cool.
  • 5. Comparative Analysis on Sodium-Based and Polyethylene-Based Greases as Anti-Friction Agents www.theijes.com The IJES Page 81 Quality Control Analysis of Grease WORKED PENETRATION 400g of grease was cooled to 25oC and later transferred into the grease worker cup. The grease cup was Jared sharply on the bench to remove the air pockets. The grease cup was finally filled above the rim of the cup and scraped at an angle of 450c with the aid of spatula. The vent cock was closed and the grease inside the cup was subjected to 60 full double strokes of the plunger, completed in about one minute by timing it using a stop-watch, the plunger was finally returned to its top position at the end of one minute. The vent cock was opened and the top and plunger were removed. The plunger itself was scraped with spatula to remove all the grease that clings to it. The seta cup was used to fill the worked grease sample in readiness for penetration test. After loading the cup with grease, the excess grease was scrapped off above the rim of the cup by moving the blade of the spatula, held inclined towards the direction of the motion at an angle of 450, across the rim of the cup. PENETRATION MEASUREMENT 400g of the test specimen was placed on the penetrometer table with one of the prepared faces upward. The mechanism was set to hold the cone in the “zero” position, and the apparatus was adjusted such that the tip of the cone just touched the surface at the centre of the test sample. Finally, the cone shaft was released rapidly and was allowed to drop for 5(five) seconds. The indicator shaft was gently depressed until it touched the cone shaft and penetration reading was taken from the indicator. The experiment was repeated up to three times. Hence the average result was recorded. DROPPING POINT OF LUBRICATING GREASE The Dropping Point is the temperature at which a conventional soap (thickened grease) passes from a semi–solid to a liquid state under the conditions of test; it is the temperature at which other non–soap (thickened greases), rapidly, separates from oil. This was determined by placing the grease sample in the cup, and a cone– shaped space created by means of a rod (manipulated through the orifice). A thermometer occupies the space, out of contact with the grease. Heating took place at specified rate and the temperature at which oil falls or drops (through the orifice of the cup) to the bottom of the test tube was noted. The operation was repeated as a check for consistency of the result, and the average reading was determined and recorded. RESULT AND DISCUSSION The results of analysis of the Samples are presented in figures 2 and 3, as well as tables 2–4 below. DROPPING POINT OF GREASE SAMPLES 0 50 100 150 200 650N 500N 150N 100N Capacity Dropping Point (oC) A B C Fig. 2: PLOT OF DROPPING POINT OF SAMPLS AT VARYING CAPACITIES WORKED PENETRATION OF THE GREASE SAMPLES 0 50 100 150 200 250 300 350 400 650N 500N 150N 100N Capacity Worked Penetration (%) A B C Fig. 3: PLOT OF WORKED PENETRATION OF SAMPLS AT VARYING CAPACITIES
  • 6. Comparative Analysis on Sodium-Based and Polyethylene-Based Greases as Anti-Friction Agents www.theijes.com The IJES Page 82 TABLE 2: ANALYSIS OF SODIUM-BASED GREASE (SAMPLE A) Sodium/polypropylene = 1:1 Sodium plus polypropylene Grease with: PROPERTIES 650N 500N 150N 100N Dropping point (oC) 190 165 150 120 Worked penetration 230 260 320 340 Appearance Smooth and fibrous Smooth and fibrous Buttery and fibrous Buttery and fibrous Other Properties Adhesive and cohesive Adhesive and cohesive Adhesive and cohesive Adhesive and cohesive TABLE 3: ANALYSIS OF POLYETHYLENE CO-POLYMER GREASE (SAMPLE B) Polyethylene Grease PROPERTIES 650N 500N 150N 100N Dropping point (oC) 185 180 150 120 Worked penetration 280 290 330 340 Appearance Smooth and buttery Smooth and buttery Smooth and soft Smooth and soft Other Properties Cohesive Cohesive Cohesive Cohesive TABLE 4: Analysis Of Blended Sodium/Polyethylene Grease At 1:3 Ratio (Sample C) Sodium plus polypropylene Grease PROPERTIES 650N 500N 150N 100N Dropping point (oC) 185 175 140 130 Worked penetration 275 290 320 340 Appearance Smooth & fibrous Smooth & fibrous Buttery & fibrous Buttery & fibrous Other properties Adhesive Adhesive Adhesive Adhesive Pumpability(in centralized systems) Poor to fair Poor to fair Fair to good Fair to good Water resistance Fair to good Fair to good Fair to excellent Fair to excellent Oxidation stability Good Good Good Good The result of the analysis shows that there is higher dropping point in the Sodium-based grease (120- 190oC) when compared with those of Polyethylene copolymer and the blended greases, whose dropping points both fall between 120 – 185oC. This is traceable to the fact sodium concentration increases the gelatinization temperature, and as such reduces the intermolecular bonding between the molecules of the product (Astrom and Hoglund, 1990). It could be observed, also, that the Worked Penetration is best with the Polyethylene (Copolymer) grease sample (280-340), followed by the Blended sample (275-340), but least with the Sodium grease sample. This shows that the Polyethylene grease possesses greater ability of friction control as it will travel farer into the axles than its Sodium counterpart. The analysis also indicated that the lower cadre (100N and 150N) of the Polyethylene grease appears smooth and soft, unlike the Sodium-based grease that is buttery and fibrous. This feature goes a long way to demonstrate that the Copolymer grease is a better sample than the Sodium-based grease, and would resist water penetration very readily as well. CONCLUSION The present study shows that suitable and ideal concentration of caustic soda for soap manufacture is 26% and it corresponds with the specific gravity of (1.275) at the temperature of 30oC. The density of dispersed polyethylene/polypropylene in a fixed volume of base oil increases with increase in the mass of polyethylene/polypropylene dispersed. Even 10% of dispersed polypropylene in 650N ( Bright stock) base oil is ideal to fortify sodium grease in a good ratio (such as 3:1) in order to produce water resistance grease suitable for servicing bearings and other heavy duty equipment.
  • 7. Comparative Analysis on Sodium-Based and Polyethylene-Based Greases as Anti-Friction Agents www.theijes.com The IJES Page 83 REFERENCES [1]. Astrom .H. and Hoglund, E. (1990): Rheological Properties of Six Greases and their Base Oils; Technical report; Lulea University of technology, Sweden. [2]. Behling, R.D. and Tomahawk, W.I (1996): Ready Reference for Lubricant Fuel Performance of Lubricating Oils, pp 29-31; Lubrizol Corporation, U.S.A. [3]. Cheng, D.C.H (1999):The Art of Coarse Rheology; The British Society of Rheology; 3(1), 1–9. [4]. George T. Austin (1984): Shreve’s Chemical Process Industries; McGraw-Hill International Edition, New York. [5]. Gottlieb Hugo E, Kotlyar Vadim, and Nudelman Abraham (1997): NMR Chemical Shifts of Common Laboratory Solvents as Trace Impurities; The Journal of Organic Chemistry, 62 (21), 7512 – 7515. Kirk Othmer, (1983): Encyclopedia of Chemical Technology, John Willey and Sons, New York. [6]. Totten George E., Westbrook Steven R., and Shah Rajesh J. (2006): Fuels and Lubricants Handbook Technology, Properties, Performance and Testing; ASTM manual series, Vol. 37, Pp 498-560. [7]. Svanberg, I. (2006): Black slugs (Arion ater) as Grease: a Study of Technical Use of Gastropods; Journal of Ethnobiology; 26 (2), 229 – 309. [8]. Vinogradov. G.V., (1989): Rhelogical and Thermophysical Properties of Grease; Gordon and Breach Science publications, London. [9]. Webb, E.T. (1927): Modern Soap and Glycerine manufacture; Davis Brothers, London.