USRE49610EActiveUtility
Heterogeneous catalyst for transesterification and method of preparing same
Est. expiryApr 17, 2035(~8.8 yrs left)· nominal 20-yr term from priority
B01J 35/613B01J 35/643B01J 35/647C07C 67/02B01J 21/066B01J 23/04B01J 27/1806B01J 35/1014B01J 35/1057B01J 35/1061C07C 67/03C10L 1/026C10M 105/34C11C 3/003B01J 37/031B01J 37/036B01J 37/04B01J 37/08C10L 2200/0476C10L 2270/026C10L 2290/543C10L 2290/547Y02E50/10Y02P20/582C07C 69/52
69
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Cited by
83
References
12
Claims
Abstract
A transesterification catalyst that is heterogeneous and a method for preparing said transesterification catalyst are provided. The catalyst can be used in a variety of transesterification reactor configurations including CSTR (continuous stirred tank reactors), ebullated (or ebullating) beds or any other fluidized bed reactors, and PFR (plug flow, fixed bed reactors). The catalyst can be used for manufacturing commercial grade biodiesel, biolubricants and glycerin.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1. A method of preparing alkyl ester using a transesterification catalyst, the method comprising:
providing a transesterification catalyst having the formula Z x Q y (PO 4 ) n H 2 O, wherein: Z is selected from the group consisting of sodium and lithium, Q is selected from the group consisting of calcium and barium, x is a rational number in the range from 0.5 to 4, y is a rational integer in the range from 2 to 8, and n is a rational integer in the range from 4 to 8; and wherein the transesterification catalyst having the formula Z x Q y (PO 4 ) n H 2 O is supported on a ceramic substrate; and reacting one or more triglycerides and an alcohol in the presence of the catalyst and converting the triglycerides and alcohol to alkyl ester and glycerin.
2. The method of claim 1 , wherein the triglycerides comprise triglyceride-containing fats and/or oils.
3. The method of claim 1 , wherein the converting of triglycerides comprises producing essentially complete conversion of the triglycerides to alkyl ester and glycerin.
4. The method of claim 1 , further comprising:
separating the glycerin from the alkyl ester and catalyst; iltering the alkyl ester to recover the catalyst; and distilling the unreacted alcohol from the alkyl ester and the glycerin.
5. The method of claim 1 , wherein the method is at least partially performed in a continuous stirred tank reactor.
6. The method of claim 1 , wherein the method is at least partially performed in a fixed bed reactor.
7. The method of claim 1 , wherein the method is at least partially performed in a fluidized bed reactor.
8. The method of claim 1 , wherein the alkyl ester is capable of being used as biodiesel fuel.
9. The method of claim 1 , wherein the alkyl ester is capable of being used as biodiesel additive to conventional diesel fuel.
10. The method of claim 1 , wherein the alkyl ester is capable of being used as a biolubricant additive to other lubricants.
11. The method of claim 1 , wherein the alkyl ester is capable of being used as a biolubricant.
12. A method of facilitating a transesterification reaction comprising:
using a reusable transesterification catalyst in the transesterification reaction, wherein the reusable transesterification catalyst is recovered from a transesterification product comprising an alkyl ester, and wherein the reusable transesterification catalyst is supported on a ceramic substrate, and wherein the reusable transesterification catalyst comprises a double metal salt having the formula Z x Q y (PO 4 ) n H 2 O, wherein:
Z consists of potassium,
Q consists of calcium,
x is a rational number in the range from 0.5 to 4,
y is a rational integer in the range from 2 to 8, and
n is a rational integer in the range from 4 to 8.Cited by (0)
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