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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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940 Phillip J. Wakelyn, Peter J. Wan<br />

clude neutral clay, acid activated clay, and activated carbon. The choice <strong>of</strong> adsorbent will<br />

depend on a balance between activity <strong>of</strong> the adsorbent, oil retention loss, and adsorbent cost.<br />

The process is generally carried out via batch or continuous bleaching. Adsorbent is<br />

mixed with the refined oil creating a slurry that is agitated to enhance contact between the<br />

oil and the adsorbent. This is generally carried out under a vacuum at 90-95ºC (194-203ºF)<br />

for 15-30 minutes. Vacuum bleaching <strong>of</strong>fers the advantages <strong>of</strong> an oil with improved oxidative<br />

and flavor stability. Finally the adsorbent is filtered from the oil using pressure leaf filters<br />

precoated with diatomaceous earth. Spent clay is steamed for efficient oil recovery.<br />

Deodorization: Deodorization, which removes the volatile compounds along with residual<br />

FFA, is a critical step in ensuring the purity <strong>of</strong> any vegetable oil and improves flavor,<br />

odor, color, and oxidative stability. Many <strong>of</strong> the volatile compounds removed are formed by<br />

the auto-oxidation <strong>of</strong> fat, which produces aldehydes, ketones, alcohols, and hydrocarbons<br />

that are associated with undesirable flavors and odors. The process also is effective in removing<br />

any remaining pesticide residues or metabolites that may be in the oil.<br />

Deodorization, which can be conducted as a batch operation in smaller plants or as a<br />

continuous or semicontinuous process by larger deodorizing facilities, consists <strong>of</strong> a steam<br />

distillation process in which the oil is heated to 230ºC (446ºF) under a vacuum <strong>of</strong> 2-10 mm<br />

Hg. Steam is sparged through the oil to carry away the volatiles and provide agitation. The<br />

odor and flavor compounds, which are more volatile than the triglycerides, are preferentially<br />

removed. After deodorization and during the cooling stage, 0.005-0.01% citric acid is<br />

generally added to chelate trace metals, which can promote oxidation. Deodorized oils preferably<br />

are stored in an inert atmosphere <strong>of</strong> nitrogen to prevent oxidation. Tocopherols and<br />

sterols are also partially removed in the deodorization process. Tocopherols can be recovered<br />

from the deodorizer distillate in a separate operation.<br />

14.10.4 REVIEW OF SOLVENTS STUDIED FOR EXTRACTION EFFICIENCY<br />

Research on solvents for extraction has been carried out for more than 150 years and has intensified<br />

since the first patent was issued to Deiss <strong>of</strong> France in 1855. 1,3,48 In the early effort <strong>of</strong><br />

selecting an extraction solvent, the availability, operation safety, extraction efficiency,<br />

product quality and cost were the major concerns. In recent decades, toxicity, bio-renewability,<br />

environmental friendliness have been added to the solvent selection criteria. Among<br />

the solvents tested, a majority <strong>of</strong> the candidate solvents were excluded on the ground <strong>of</strong> toxicity<br />

and safety. Only a handful <strong>of</strong> solvents are used to any degree. These are acetone, alcohol,<br />

hexanes, heptane, and water. 1,4-7,49 Water is used in rendering <strong>of</strong> fat from animal tissues<br />

and fish and in coconut processing, 49 alcohol for spice and flavorants extraction, 5,49 acetone<br />

for lecithin separation and purification. 4 For commodity oils derived from vegetable<br />

sources, only hydrocarbon solvents have been used since 1930’s. Acetone was used by an<br />

Italian cottonseed oil mill during the 1970’s. 4 Aqueous acetone and acetone-hexane-water<br />

azeotrope were studied by the scientists at the Southern Regional Research Center <strong>of</strong> Agricultural<br />

Research Service, USDA during the 1960’s and 1970’s. 4 The effort was stopped<br />

due to the cost <strong>of</strong> retr<strong>of</strong>it required, the difficulties in managing the mixture <strong>of</strong> solvents with<br />

the presence <strong>of</strong> water and product quality concerns - a strong undesirable odor associated<br />

with the acetone extracted meals. 4 Ethanol and isopropanol were studied in the 1980’s as a<br />

potential replacement <strong>of</strong> hexane for oil extraction. Both were proven technically feasible<br />

but economically unacceptable. 5,6 n-Hexane is listed as a HAP under the CAA 14,15 (See Section<br />

14.10.2.2.1 CAA) and there are other regulatory requirements. As a way to meet envi-

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