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Sulfation of Castor Oil with Development of Emulsifiers

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Al- satil Journal 61<br />

<strong>Sulfation</strong> <strong>of</strong> <strong>Castor</strong> <strong>Oil</strong> <strong>with</strong> <strong>Development</strong><br />

<strong>of</strong> <strong>Emulsifiers</strong><br />

Dr. Abdul Baset M. Elgellal <br />

Imad H. Al –Wahaib <br />

Abstract:<br />

The work is related to the field <strong>of</strong> preparation <strong>of</strong> emulsifiers for the<br />

use in asphalt emulsions, and formulating <strong>of</strong> solution type cooling – lubricating<br />

fluids. Thus, castor oil was reacted <strong>with</strong> gaseous sulfur trioxide at 25◦c using<br />

carbon tetrachloride as a solvent. Emulsification properties <strong>of</strong> the sulfurized<br />

castor oil were studied in relation to the content <strong>of</strong> combined SO3. The highest<br />

emulsification tendency was attained at approximate 8 percentages by weight <strong>of</strong><br />

SO3 content corresponding to the sulfation <strong>of</strong> one hydroxide group in castor oil.<br />

Introduction:<br />

Sulfonation <strong>of</strong> Aromatic hydrocarbons, petroleum oil and vegetable oil has<br />

great importance In industry, in which useful surfactants material could be<br />

produced. Such surfactants could be used as detergent, emulsifying agent,<br />

s<strong>of</strong>tening agents, de emulsifying agents etc. The sulfonation <strong>of</strong> aromatic<br />

hydrocarbons is used to induce the sulfonyl group (SO3H) while the sulfation <strong>of</strong><br />

aliphatic organic molecules such as alcohols and olefins produce sulfuric acid<br />

esters. The sulfated castor oil (Turkey red oil) is one <strong>of</strong> the most effective<br />

surfactants. The sulfated castor oil is used in fabric manufacture as a s<strong>of</strong>tening<br />

agent. This sulfated oil is classically prepared, in early 1970s, by gradual<br />

addition <strong>of</strong> sulfuric acid to castor oil under harsh condition <strong>of</strong> high temperature<br />

and long reaction time in addition to producing side products. 1-2<br />

Recently, the sulphated castor oil is prepared by using diluted gaseous sulfur<br />

trioxide 1 (diluted <strong>with</strong> 4% V in N2) under mild condition (i.g., at 45-50°C for<br />

20-25 min). The resulted sulphated castor oil should be:<br />

<br />

• Highly soluble in water, this makes it good surfactant and/or good<br />

emulsifying agent.<br />

Misurata University – Faculty <strong>of</strong> Science – Misurata – Libya.


<strong>Sulfation</strong> <strong>of</strong> <strong>Castor</strong> <strong>Oil</strong> <strong>with</strong> <strong>Development</strong> <strong>of</strong> <strong>Emulsifiers</strong>.<br />

• Stable under acidic conditions.<br />

The experimental data showed that the optimum reaction temperature was<br />

45-50 o c. 1 lowering the temperature below this range leads to increasing the<br />

viscosity <strong>of</strong> the reaction mixture resulting poor interaction between the gas and<br />

liquid phases. However, raising the reaetion thempeature higher than 50 o c could<br />

allow some oxidation reactions to take place producing sulphur dioxide.<br />

It has been proved that the sulfation reaction <strong>of</strong> the castor oil at < 50 o c<br />

occurs by a reaction between gaseous SO3 and the hydroxyl groups <strong>of</strong> esters <strong>of</strong><br />

ricinolic acid. 1<br />

There have been a number <strong>of</strong> studies focusing on the sulfation <strong>of</strong> fatty acids<br />

using SO3. 3-5<br />

According to these studies, the esters <strong>of</strong> the higher sulfonyl fatty acids.<br />

Based on that the sulfation <strong>of</strong> the castor oil takes place at relatively high<br />

temperature c > 60 o c producing free sulfonates <strong>with</strong>out the formation <strong>of</strong> sulfated<br />

glycerides. 6 The sulfated castor oil has wide industrial uses. It is used in leather<br />

industry as the aqueous filling material for leather contains about 3-4 % by<br />

weight <strong>of</strong> the saponifiied sulfated castor oil. 7<br />

The sulfated castor oil along <strong>with</strong> the coconut oil are used as a hydrating<br />

material. 8 It is also used in processing leather in which 20% by volume <strong>of</strong><br />

ethanol is added to an aqueous solution <strong>of</strong> the sulfated castor oil to form an<br />

emulsifier for so aching chrome – treated leather in order to enhance its<br />

flexibility. In the presence <strong>of</strong> 6% by weight sulfated castor oil, the hydrating<br />

and flexibility properties <strong>of</strong> the mixture have been improved. 9 The sulfated<br />

castor oil has been used to purify the asphaltic sand from the asphalt. 10 In<br />

addition, it has been involved <strong>with</strong> the lithium lipids for improving their thermal<br />

properties. 11 Further more, the sulfated castor oil has been utilized <strong>with</strong> other<br />

materials to form cooling – lubricating emulsifiers that are employed in cutting<br />

and polishing the glass. 12<br />

Other types <strong>of</strong> lubricating emulsifiers have been synthesized from the<br />

sulfated castor oil and other substances concentration ranging between 30 to<br />

50%. 13<br />

2. Experimental:<br />

2.1. Materials.<br />

Pure castor oil (B.P) was used ricinolic acid (C12------OH,9C ) was prepared<br />

by saponification pure castor oil using 20 % sodium hydroxide solution at 90-<br />

95◦C <strong>with</strong> stirring for 2 hr. the resulting mixture was acidified by dilute<br />

sulphuric acid. The resulted ricinolic acid was watched <strong>with</strong> hot water and<br />

dried.<br />

62


Al- satil Journal 63<br />

2. 2. <strong>Sulfation</strong>.<br />

Two methods have been used for sulfation: in the first method. Oleum<br />

containing 30% SO3 by weight was used. The oleum was added slowly over 30<br />

minutes <strong>with</strong> stirring at certain temperature. In the second method, the<br />

SO3diluted <strong>with</strong> nitrogen (approximate 4% by volume) was used .The excess<br />

SO3 <strong>of</strong> was liberated by heating the oleum and passing current <strong>of</strong> nitrogen. The<br />

sulfating agent (SO3 diluted <strong>with</strong> nitrogen) was passed through the gas<br />

distributor placed in bottom <strong>of</strong> reactor that contains oil. This was <strong>with</strong>in ±2°c.<br />

by heating the reactor. by using sulfation in this way, the unreacted residual gas<br />

was expelled at the end <strong>of</strong> reaction <strong>of</strong> reaction by heating to 70 ◦C.<br />

The reaction depth was determined by measuring the content <strong>of</strong> reacted SO3<br />

gas and also by measuring the acidity <strong>of</strong> the resulted sulfated oil. Hexane and<br />

CCl4 were used as solvents.<br />

2. 3. Method <strong>of</strong> test and extraction.<br />

2. 3.1. Acidity <strong>of</strong> sulfated oil.<br />

The acidity <strong>of</strong> sulfated oil was determined by titration <strong>with</strong> standard<br />

solution <strong>of</strong> KOH. The sulfated castor oil (1g) was dissolved in mixture<br />

(100cm 3 ) <strong>of</strong> toluene and iso propyl alcohol in ration <strong>of</strong> 2:1 V/V at high<br />

temperature.<br />

Acidity (mg KOH/g)<br />

V × N × 56<br />

=<br />

W<br />

V= volume <strong>of</strong> KOH (ml)<br />

N= normality <strong>of</strong> KOH solution<br />

W= weight <strong>of</strong> the sample (gm)<br />

2.4. Emulsification properties.<br />

The emulsification properties <strong>of</strong> sulfated castor oil and its derivatives were<br />

studied by forming <strong>of</strong> asphaltic emulsions. The asphaltic emulsions were<br />

prepared by mixing equal volumes <strong>of</strong> water, light asphalt and toluene in the<br />

presence <strong>of</strong> emulsifying agent. The stability <strong>of</strong> the resulted emulsions was<br />

monitored over 24 h. the amount <strong>of</strong> separated water gave indication to the<br />

stability <strong>of</strong> the emulsion. thin asphalt, and toluene and in presence <strong>of</strong> certain<br />

ration <strong>of</strong> emulsifier ,the stability <strong>of</strong> emulsion <strong>with</strong> time has been followed<br />

. Over night separated water ration was standard for stability <strong>of</strong> emulsion.


<strong>Sulfation</strong> <strong>of</strong> <strong>Castor</strong> <strong>Oil</strong> <strong>with</strong> <strong>Development</strong> <strong>of</strong> <strong>Emulsifiers</strong>.<br />

3. Results and discussion:<br />

3.1. <strong>Sulfation</strong> <strong>of</strong> castor oil using SO3 and studying the properties <strong>of</strong> the<br />

resulting emulsion.<br />

3.1.1. The relation ship between the depth <strong>of</strong> sulfation and acidity <strong>of</strong> the<br />

sulfated castor oil.<br />

The sulfation was carried out at 45 using different ratios <strong>of</strong> sulphur trioxide<br />

and the castor oil after which the acidity <strong>of</strong> the products was determined.<br />

The theoretical values <strong>of</strong> the acidity <strong>of</strong> the sulfated oil were calculated bored<br />

or a comparison between the theoretical and experimental data.<br />

The content <strong>of</strong> SO3 in the product when one hydroxide group was sulfated<br />

= 8.<br />

6%<br />

80 × 100<br />

=<br />

932<br />

Mwt.<br />

<strong>of</strong>SO3×<br />

100<br />

= Is:<br />

Mwt.<br />

0 f<strong>Castor</strong>oil<br />

This means that the molecular weight <strong>of</strong> the product is 1012 and the<br />

acidity <strong>of</strong> product is 55mg KOH ⁄ gm.<br />

The experimental and theoretical correlation (Figure 1), Show the sulfation<br />

<strong>of</strong> castor oil <strong>with</strong>out observing any side products. More over, the experimental<br />

results are in accordance <strong>with</strong> the theoretical calculation <strong>with</strong> error percentage<br />

<strong>of</strong> 3.5%.<br />

Figure 1: The relationship between sulphation's depths and the acidity <strong>of</strong> the<br />

product (sulphation was carried out at 45 °C)<br />

3.1.2 .Optimization <strong>of</strong> the sulfation <strong>of</strong> the castor oil.<br />

A range <strong>of</strong> chlorinated hydrocarbons and other low-poiling hydrocarbon<br />

were used as solvent in the sulfation process. These solvents are in reactive<br />

64


Al- satil Journal 65<br />

towards sulfur trioxide. In addition, such solvents are easy to remove by<br />

evaporation where the sulfation is complete. The ration <strong>of</strong> solvent to caster oil<br />

was (2:1w/w). The temperature <strong>of</strong> the sulfation reaction was reduced to 25◦C<br />

due to the use <strong>of</strong> such Low-boiling solvents.<br />

The rate <strong>of</strong> the sulfation reaction in carbon tetrachloride was found to be<br />

much faster than the reaction rate when the sulfation was carried out on neat<br />

castor oil or in hexane. The rate <strong>of</strong> the sulfation, in carbon tetrachloride,<br />

increased by 2.4 times (Table 1).<br />

Table 1: The effect <strong>of</strong> solvents on the rate <strong>of</strong> the sulfation <strong>of</strong><br />

Solvent<br />

NO Solvent<br />

Hexane<br />

Carbon tetrachloride<br />

castor oil using SO3<br />

Temperature <strong>of</strong> Reaction rate (increase <strong>of</strong><br />

the sulfation (°C) acidity/h) (mgKOH/gr/h)<br />

50<br />

19<br />

25<br />

5<br />

25<br />

46<br />

3.1.3. Study <strong>of</strong> the Emulsification properties <strong>of</strong> sulfated <strong>Castor</strong> oil.<br />

The sulfated castor oil <strong>with</strong> different levels <strong>of</strong> sulfation was emulsified <strong>with</strong><br />

petroleum asphalt in which the content <strong>of</strong> the emulsifying agent (sulfated caster<br />

oil) was 2% by weight. The stability <strong>of</strong> the resulting emulsions was evaluated<br />

according to the content <strong>of</strong> SO3 in the sulfated castor oil (Figure 2). The pure<br />

caster oil showed on emulsification properties, however, the sulfation <strong>of</strong> one<br />

hydroxide group in the oil (8-10 , by wt <strong>of</strong> SO3) ,improved dramatically the<br />

emulsification properties. <strong>Sulfation</strong> <strong>of</strong> a second hydroxyl group decreased the<br />

emulsification ability <strong>of</strong> the product.<br />

Figure 2: Changing the emulsification properties <strong>of</strong> the sulphated oil by<br />

changing the acidity.


<strong>Sulfation</strong> <strong>of</strong> <strong>Castor</strong> <strong>Oil</strong> <strong>with</strong> <strong>Development</strong> <strong>of</strong> <strong>Emulsifiers</strong>.<br />

3-2. Study <strong>of</strong> Emulsification Properties <strong>of</strong> the sulfated Ricinolic Acid<br />

and its salts.<br />

3-2-1. The sulfated ricinolic acid and its salts as emulsifiers.<br />

Ricinolic acid showed no ability to product emulsion <strong>with</strong> petroleum asphalt.<br />

This was observed when ricinolic acid was combined <strong>with</strong> water and petroleum<br />

asphalt (diluted <strong>with</strong> toluene) in ration <strong>of</strong> (1: 1: 1 w/ w) <strong>with</strong> concentration<br />

between 0.5 and 2.0%. An immediate separation <strong>of</strong> the layers was occurred.<br />

However, when the ricinolic acid was sulfated, using diluted SO3 (diluted <strong>with</strong><br />

N2) in which different levels <strong>of</strong> sulfation were obtained, the resulting products<br />

showed emulsification properties. The most stable emulsion resulted from the<br />

use <strong>of</strong> sulfated ricinolic acid containing 2.3% <strong>of</strong> SO3. The emulsification<br />

property decreased as the SO3 content increased (Figure 3).<br />

Figure 3: Stability <strong>of</strong> asphalitic emulsions <strong>of</strong> the sulphated ricinolic acid<br />

(concentration <strong>of</strong> emulsifying agent is 2.0% by weight).<br />

This due to the fact that the sulfated ricinolic acid became a detergent rather<br />

than emulsifying agent as the content <strong>of</strong> SO3 increased. The initial stability<br />

sulfated <strong>of</strong> ricinoleic acid emulsion changed as the depth <strong>of</strong> sulfation<br />

increases from 2.3 to 10 % (Figure 4).<br />

66


Al- satil Journal 67<br />

Figure 4: The relationship between the initial stability <strong>of</strong> asphaltic emulsions<br />

and the depths <strong>of</strong> the sulphation <strong>of</strong> ricinolic acid (concentration <strong>of</strong> ricinolic acid<br />

is 2.0% by weight).<br />

The sodium salt <strong>of</strong> ricinoleic acid showed no emulsification properties.<br />

However, partial emulsification properties were seen when the sodium salt <strong>of</strong><br />

sulfated ricinolic acid was used (Figure 5). The emulsification properties <strong>of</strong> the<br />

latter case decreased as the content <strong>of</strong> SO3 increased which means that the<br />

sodium salt <strong>of</strong> the sulfated ricinolic acid became a detergent rather than<br />

emulsifying agent.<br />

Figure 5: The stability <strong>of</strong> asphaltic emulsion that contain sodium salt <strong>of</strong><br />

sulphated ricinolic acid (concentration <strong>of</strong> emulsifying agent 2.0% by weight).


<strong>Sulfation</strong> <strong>of</strong> <strong>Castor</strong> <strong>Oil</strong> <strong>with</strong> <strong>Development</strong> <strong>of</strong> <strong>Emulsifiers</strong>.<br />

3-2-2. The Formation <strong>of</strong> Emulsifying Agent By the Partial<br />

Neutralization <strong>of</strong> Sulfated Ricinolic Acid<br />

The possibility <strong>of</strong> preparing some emulsions by partial neutralization <strong>of</strong> high<br />

molecular weight carboxylic acids has been mentioned in the literature, This<br />

technique leads to the formation <strong>of</strong> emulsions consisting <strong>of</strong> free carboxylic acid<br />

and their salts (e.g sodium salts) in the same time. Based on that, an attempt was<br />

made to form an asphaltic emulsion containing an emulsifying agent prepared<br />

by the partial neutralization <strong>of</strong> sulfated ricinolic acid. The emulsifying agent<br />

was prepared by the sulfation <strong>of</strong> ricinolic acid up to 2.3 % (by weight) <strong>of</strong> SO3<br />

content. Partial neutralization <strong>of</strong> the resulting sulfated acid was carried out using<br />

a concentrated solution <strong>of</strong> sodium hydroxide to afford 25% neutralization. This<br />

allowed a good level <strong>of</strong> solubility in water. An asphaltic emulsion was prepared<br />

from water, toluene and liquid petroleum asphalt in ration <strong>of</strong> 1 : 1 : 1 (by<br />

weight) in the presence <strong>of</strong> 2.0 % (by weight) <strong>of</strong> the emulsifying agent. This<br />

emulsion showed high level <strong>of</strong> stability. For comparison, the partial<br />

neutralization <strong>of</strong> ricinolic acid resulted to no emulsification properties.<br />

Conclusion:<br />

1- The sulfation <strong>of</strong> castor oil <strong>with</strong> gaseous sulfur trioxide was studied by using<br />

carbon tetrachloride as solvent, therefore, the rate <strong>of</strong> the reaction was very<br />

fast and the sulfation process was carried out low temperature.<br />

2- the properties <strong>of</strong> emulsified sulfated castor oil changes according to the<br />

depth <strong>of</strong> sulfation <strong>with</strong> the enhancement <strong>of</strong> the concentration <strong>of</strong> sulfur<br />

trioxide in emulsifier up to (8%w). this percentage lead to sulfation <strong>of</strong> one<br />

hydroxyl group in caster oil and the ability <strong>of</strong> the emulsifier increases,<br />

whereas if it is more than this percentage the ability <strong>of</strong> the emulsifier<br />

decrease and lead to formation <strong>of</strong> bisulfonic acids.<br />

3- Stable tar emulsion was formed by using prepared emulsifier through<br />

molecular neutralization <strong>of</strong> sulfated ricinolic acid. This emulsifier contains<br />

free sulfuric acids and their salts.<br />

68


Al- satil Journal 69<br />

References<br />

1. F. J. Kremers, JAOCS, 48, No. 7, 314 (1971).<br />

2. E. E. Gilbert, Sulfonation and Related Reactions, Interscience Publishers,<br />

P.363 (1965).<br />

3. Japan Paten 7802, 419 (1978); Chem. Abs., 88:172294.<br />

4. Japan Patent 77. 156, 817 (1977); Chem. Abs.; 88:152044.<br />

5. B. L. Kapur, J. M. Solomon and B. R. Bluestein, JAOCS, 55, No. 6, 549<br />

(1978).<br />

6. B. M. Milwidsky and S. Holtzman, Soap, Cosmet., Chem. Spec., 48, No. 6,<br />

446 (1972); Chem. Abs., 77:116345.<br />

7. USSR Patent 977, 496 (1982); Chem. Abs., 98:74236.<br />

8. K. J. Kedlaya, K. Vijayalakshmi, S. C. Sumathi and V. V. Rao, Leather Sci.,<br />

20, No. 6, 199 (1973); Chem. Abs., 80:97359.<br />

9. S. Alberto and V. Victor D; Jaco La Plata, No. 1, 63 (1973); Chem. Abs.,<br />

80:49296.<br />

10. U. S. Patene 3, 951, 778 (1976); Chem. Abs., 85:49177.<br />

11. P. N. Vdovichenko, V. A. Dagaev and A. I. Petlitskii; Neftepererab.<br />

Neftekhim (Kiev) 17, 74 (1979); Chem. Abs., 92:8603.<br />

12. Czech. Patent 254, 462 (1988); Chem. Abs., 110:196190.<br />

13. Rom. Patent 84, 989 (1985); Chem. Abs., 104:150747.

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