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Process for making esters

A technology of esters and triglycerides, applied in the field of biodiesel, which can solve the problems of undesirable fine particle formation and pressure drop

Inactive Publication Date: 2014-08-13
BASF CORP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Also (physical) degradation of the catalyst will occur, which may lead to undesirable fines formation and thus an undesirable pressure drop, especially in fixed beds

Method used

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  • Process for making esters
  • Process for making esters
  • Process for making esters

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] A 10 mL titanium silicate tablet was prepared according to the procedure of US-A-5 053 139, in particular according to its Example 9: by adding 569.11 g of TiCl 4 Add to enough deionized water to reach 2dm 3 , making 2dm 3 1.5M titanium chloride solution (Solution A). By adding 638.2g of Na 2 SiO 3.5 ·H 2 O is dissolved in sufficient 3M NaOH to reach 2dm 3 , making 2dm 3 1.5M sodium silicate solution (solution B). Solution B was added to solution A at a rate of 16 ml / min with very vigorous stirring. After the addition was complete, the mixture was allowed to continue mixing for an additional 15 minutes. The pH of the solution should fall between 7.5 and 7.9. Adjust pH with diluted HCl or diluted NaOH if necessary. Then, the samples were allowed to age for 2-4 days. After aging, any water on top of the gel was decanted off. Then filter the sample, every dm 3 1dm for gel 3 Wash with deionized water at 4-6dm 3 Reslurry in deionized water, filter and finally ...

Embodiment 2

[0031] 10 mL of titanium silicate tablets prepared according to the procedure of US-A-5 053 139 were loaded in a fixed bed reactor. The reactor was fed with MeOH (1.73 ml / h) and rapeseed oil (3.47 ml / h) containing 5 wt.% dodecanoic acid. After 284 hours on stream at 180°C, the reaction was stopped and the product stream and catalyst were analyzed. The product stream contains only trace amounts of titanium and silicon (several or tens of ppm (w / w)).

Embodiment 3

[0033] 10 mL titanium silicate tablets with different amounts of Na were prepared by treating the tablets prepared according to Example 1 with different amounts of HCl in water. The final Na content of the tablet can be controlled by controlling the pH of the aqueous phase. After 2 hours of HCl treatment, the tablets were washed thoroughly with demi-water and dried in an oven at 110° C. overnight. This process allowed the production of titanium silicate tablets with different Na contents, namely 6.0, 3.9, 3.2, 2.4 and 0.8 wt% Na, respectively.

[0034] Treated and untreated tablets were tested in a fixed bed reactor under similar conditions as described in Example 2. figure 1 The relationship between the amount of Na in the catalyst (wt.%) versus the amount of Si (ppm) and Ti in the product stream (XRF peak height) is shown (see figure 1 , respectively, the square line and the rhombus line). When measuring the amount of titanium and silicon in the final product by XRF (X-Ra...

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PUM

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Abstract

The invention relates to a process for making esters, in particular biodiesel, by using heterogeneous catalysts. The invention provides a process for making biodiesel, in particular FAME, which process is versatile and robust. The process can be carried out continuously, in particular in a fixed bed reactor or a slurry reactor and may be operated in a continuous fashion. In accordance with the process, the transesterification reaction of triglycerides is carried out by using a heterogeneous catalyst that comprises a Group 4 silicate and less than 3 wt% of Na in the presence of at least one acid compound.

Description

technical field [0001] The present invention relates to a method for preparing esters, especially biodiesel, using a heterogeneous catalyst. Background technique [0002] The most common forms of biodiesel include fatty acid methyl esters (FAME; H 3 COOR). Biodiesel, especially FAME, is becoming more and more important as a fuel, especially as a transportation fuel. [0003] Biodiesel has been produced in the prior art in batch reactors, where oil (usually vegetable oil or sometimes animal fat), short-chain alcohols, especially methanol, and a homogeneous catalyst such as NaOMe are combined and Stir at 50-80°C for 1 or 2 hours at ambient pressure. (trans)esterification reaction ((trans-)esterification reaction) to generate FAME and glycerol: [0004] [0005] where R 1 , R 2 and R 3 Each independently represents the long-chain portion of a triglyceride or the corresponding methyl ester (usually C 12 -C 20 , and more specifically C 16 -C 18 ). [0006] In this ...

Claims

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Application Information

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IPC IPC(8): C07C67/03C07C69/24C07C69/52C11C3/00
CPCC10L2200/0476C10L1/026Y02E50/13C07C67/03C10L2290/00C11C3/003C11C3/10C07C69/24C07C69/52Y02E50/10
Inventor 吉姆·阿洛伊修斯·马里亚·布兰茨
Owner BASF CORP