Divalent ion removal from monoethylene glycol (MEG) feed streams
US-9469585-B2 · Oct 18, 2016 · US
US9868682B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9868682-B2 |
| Application number | US-201414912104-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 19, 2014 |
| Priority date | Aug 19, 2013 |
| Publication date | Jan 16, 2018 |
| Grant date | Jan 16, 2018 |
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The disclosure relates to a novel glycerol purification process that produces partially refined waste glycerol for a variety of industrial applications. The disclosure encompasses a salt-containing partially refined glycerol composition that is suitable as a fermentation grade glycerol.
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We claim: 1. A process of producing partially refined waste glycerol by refining crude glycerol containing organic impurities, said process comprising: subjecting crude glycerol to a hydrophobic solvent to produce a mixture of crude glycerol and hydrophobic solvent; separating the mixture of crude glycerol and hydrophobic solvent to produce a deoiled (DO) glycerol and a phase containing hydrophobic solvent and organic impurities; drying said DO glycerol to produce a deoiled and dewatered (DOW) glycerol; subjecting a polar solvent to said DOW glycerol to produce a mixture of polar solvent and DOW glycerol and precipitating a salt from the mixture of polar solvent and DOW glycerol; and separating the mixture of polar solvent and DOW glycerol into a light phase containing a deoiled, dewatered and desalted (DOWS) glycerol and the polar solvent and a heavy phase containing the salt, wherein said process further comprises: partially evaporating about 75 percent of said DOW glycerol as a glycerol distillate without salt; recovering a remaining portion of said DOW glycerol in an evaporation discharge bottom; and adding the polar solvent to said evaporation discharge bottom to precipitate salt and create a deoiled, dewatered and desalted (DOWS) glycerol. 2. The process of claim 1 , wherein said DOWS glycerol is a fermentation grade glycerol. 3. The process of claim 1 , wherein said DOW glycerol comprises less than about 0.5 percent water. 4. The process of claim 1 , further comprising partially evaporating the DOW glycerol before subjecting it to the polar solvent. 5. The process of claim 1 , further comprising the step of evaporating the polar solvent from the DOWS glycerol to produce a purified DOWS glycerol. 6. The process of claim 5 , wherein said evaporating comprises flash evaporation. 7. The process of claim 2 , wherein said fermentation grade glycerol is salt-containing glycerol. 8. The process of claim 1 , wherein said polar solvent is isopropanol.
by treatment giving rise to a chemical modification of at least one compound (chemisorption C07C29/76) · CPC title
Glycerol · CPC title
by liquid-liquid treatment · CPC title
by physical treatment · CPC title
Use of additives, e.g. for stabilisation · CPC title
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