Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Octanoic Acid | HCID 379 | — |
| Reactant | Decanoic Acid | HCID 2969 | — |
| Reactant | Glyceryl Monobehenate | HCID 5362585 | — |
| Product | Glyceryl Dibehenate | HCID 22477175 | — |
Reaction Steps
Typically, about 118 kg of a mixture of C10:0 and C8:0 fatty acids (55:45 weight ratio) is preheated to the esterification temperature and adjusted to the requisite pressure. This fatty acid mixture is used to esterify about 16.8 kg of monobehenin at an 18:1 acid to monobehenin mole ratio at esterification temperature 245° C. (The monobehenin is commercially produced by molecular distillation of behenic acid/glycerol reaction products and comprises 98.1% monoglyceride, 0.5% diglyceride, 0.1% free glycerol, and 0.3% diglycerol.) The monobehenin is added incrementally as a liquid over a 60 minute period to the melted fatty acids. The esterification pressure ranges from 700 mmHg to 1520 mmHg. A pressure of 700 mmHg is initially used, but is increased as necessary to prevent the mixture containing the fatty acids from boiling over.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US05589216 |
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| Source dataset | uspto-grants-1996_12 |
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| ORD ID | ord-35fe91295af94c65b12b5235cdffd3b6 |
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| Source note | uspto-grants-1996_12 |
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