Biodiesel via Ultrasonically Improved (Trans-)Esterification

Biodiesel is synthesized via transesterification using a base-catalyst. However, if the raw material such as low-grade waste vegetable with a high free fatty acid content are used, a chemical pre-treatment step of esterification using an acid-catatlyst is required. Ultrasonication and its sonochemical and sonomechanical effects contribute to both reaction types and increase the efficiency of biodiesel conversion dramatically. Ultrasonic biodiesel production is significantly faster than the conventional biodiesel synthesis, results in higher biodiesel yield and quality and saves reagents such as methanol and catalyst.

Biodiesel Conversion using Power Ultrasound

For biodiesel, fatty acid esters are produced by transesterification of vegetable oils as well as of animal fats (e.g., tallow). During the transesterification reaction, the glycerol component is replaced by another alcohol, such as methanol. Feedstocks with a high content of free fatty acids, e.g. waste vegetable oils (WVO), require a pre-treatment of acid esterification in order to avoid soap formation. This acid catalysis process is a very slow reaction, when carried out as conventional batch method. The solution for accelerating the slow esterification process is the application of power ultrasound. Sonication achieves a significant improvement in reaction speed, conversion and biodiesel yield as the sonochemical effects of high-power ultrasound promote and intensify the acid catalysis. Ultrasonic cavitation provides sonomechanical forces, i.e. high-shear mixing, as well as sonochemical energy. These both types of ultrasonic impact (sonomechanical and sonochemical) turn the acid-catalyzed esterification into a fast reaction requiring less catalyst.

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3x UIP1000hdT ultrasonicators for highly efficient biodiesel transesterification

Ultrasonic mixing improves biodiesel conversion rate, increases yield and saves excess methanol and catalyst.The picture shows the installation of 3x UIP1000hdT (each 1kW ultrasound power) for inline processing.


In this video tutorial we introduce you into the science of how ultrasonic biodiesel reactors significantly improve biodiesel production. Hielscher ultrasonic biodiesel reactors are established as a powerful tool to enhance the biodiesel production process, and in this tutorial, we delve into the working principle behind it and show various ultrasonic setups for any production scale. Enhance your biodiesel production in efficiency and cost-effectiveness and produce higher yields of high-quality biodiesel within a rapid conversion. At the same time, ultrasonic biodiesel reactors allow for the use of poor oils such as waste vegetable oils or spent cooking fats and help to save methanol and catalyst, contributing to an environmental-friendly and sustainable biodiesel manufacturing.

Biodiesel Production Using Hielscher Sonoreactors for More Yield, Higher Quality & Capacity

Video sīktēls


How Does Ultrasonic Biodiesel Conversion Work?

Ultrasonication between different phases in the transesterification (also sometimes called alcoholysis ) and esterification is based on the enhancement of mixing as well as on an increased heat and mass transfer. Ultrasonic mixing is based on the principle of acoustic cavitation, which occurs as result of imploding vacuum bubbles in the liquid. Acoustic cavitation is characterized by high-shear forces and turbulences, as well as very high pressure and temperature differentials. These forces promote the chemical reaction of transesterification / esterification and intensify mass and heat transfer, thereby improving the reaction of biodiesel conversion significantly.

Ultrasonic transesterification improves biodiesel conversion.

Transesterification of triglycerides into biodiesel (FAME) using sonication results in accelerated reaction and significantly higher efficiency.

The application of ultrasonics during biodiesel conversion has been scientifically and industrially proven to improve process efficiency. The improvement in process efficiency can be attributed to reduced energy consumption and operating costs, and the reduced use of alcohol (i.e., methanol), less catalyst, and significantly shortened reaction time. Energy cost for heating are eliminated since there is no requirement for external heating. Additionally, phase separation between biodiesel and glycerol is simpler with a shorter phase separation time. An important factor for the commercial use of ultrasound in biodiesel production is the simple scale-up to any volume, the reliable and safe operation as well as the robustness and reliability of the ultrasonic equipment (industrial standard, capable to run continuously 24/7/365 under full load).

Hielscher ultrasonic reactor for biodiesel transesterification with superior process efficiency

Ultrasonic industrial system with flow cell for inline biodiesel esterfication and transesterification.

Process chart showing the biodiesel process in continuous flow mode. Ultrasound can improve esterification and transesterification significantly.

Ultrasonic esterification and transesterification can be run as batch or continuous inline process. The chart shows the ultrasonic inline process for biodiesel (FAME) transesterfication.

Process chart showing the biodiesel process in batch mode. Ultrasound can improve esterification and transesterification significantly.

Ultrasonic esterification and transesterification can be run as batch or continuous inline process. This chart shows the ultrasonic batch process for biodiesel conversion.

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Ultrasonically-Assisted Two Step Biodiesel Conversion Applying Acid- and Base-Catalyzed Reaction Steps

For feedstocks with a high FFA content, the biodiesel production is carried out as acid or base-catalyzed reaction in a two stage process. Ultrasound contributes two both types of reactions, the acid-catalyzed esterification as well as the base-catalyzed transesterification:

Acid-catalyzed esterification using Ultrasound

To treat an excess of free fatty acids in the feedstock, the process of esterification is needed. Sulfuric acid is commonly used as acid catalyst.

  • Prepare feedstock by filtering and refining from contaminants and water.
  • Dissolve the catalyst, namely sulfuric acid, in methanol. Feed stream of catalyst/ methanol and the feedstock through a heat exchanger and a static mixer to obtain a crude pre-mix.
  • The pre-mix of catalyst and feedstock goes directly into the ultrasonic reaction chamber, where the ultra-fine mixing and sonochemistry take effect and the free fatty acids are converted to biodiesel.
  • Finally, dewater the product and feed it to the second stage – the ultrasonic transesterification. The acidic wet methanol is after recovery, drying and neutraliziation ready for reuse.
  • For very high FFA containing feedstocks, a recirculation setup maybe required to lower the FFA to a reasonable level before the transesterification step.

Esterification Reaction using an Acid Catalyst:
FFA + Alcohol → Ester + Water

Base-Catalyzed Transesterification using Ultrasound

The feedstock, which now has only small amounts of FFAs, can be directly fed to the transesterification stage. Most commonly sodium hydroxide or potassium hydroxide (NaOH, KOH) is used as base catalyst.

  • Dissolve the catalyst, namely potassium hydroxide, in methanol and feed the streams of catalyst/ methanol and pretreated feedstock through a static mixer to obtain a crude pre-mix.
  • Feed the pre-mix directly into the ultrasonic reaction chamber for the cavitational high-shear mixing and the sonochemical treatment. The products of this reaction are alkyl esters (i.e., biodiesel) and glycerin. The glycerin can be separated by settling-out or by centrifuging.
  • The ultrasonically produced biodiesel is of high quality and manufactured fast, energy-efficient and cost-efficient by saving methanol and catalyst.

Transesterification Reaction using a Base Catalyst:
Oil / Fat + Alcohol → Biodiesel + Glycerol

Methanol Use & Methanol Recovery

Methanol is a key component during biodiesel production. The ultrasonically driven biodiesel conversion allows for a significantly reduced use of methanol. If you are now thinking “I don’t care about my methanol use, since I recover it anyway”, you might re-think and consider the exorbitant high energy cost that apply for the evaporation step (e.g. using a distillation column), which is necessary to separate and recycle the methanol.
Methanol is usually removed after the biodiesel and glycerin have been separated into two layers, preventing reaction reversal. The methanol is then cleaned and recycled back to the beginning of the process. Producing biodiesel via ultrasonically-driven esterification and transesterification, you are able to reduce your methanol use dramatically, thereby reducing the exorbitant high energy expenditure for methanol recovery. The use of Hielscher ultrasonic reactors reduces the required amount excess methanol by up to 50%. A molar ratio between 1:4 or 1:4.5 (oil : methanol) is sufficient for most feedstock, when using Hielscher ultrasonic mixing.

Process chart showing the biodiesel processing steps. Ultrasound can improve esterification and transesterification significantly.

Ultrasonic esterification is a pretreatment step, which reduced low-grade feedstock high in FFAs into esters. In the 2nd step of ultrasonic transesterification, the triglycerides are converted into biodiesel (FAME).

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Ultrasonic Increased Biodiesel Conversion EfficiencyScientifically Proven

Numerous researcher group have investigated the mechanism and effects of ultrasonic transesterification of biodiesel. For instance, the research team of Sebayan Darwin demonstrated that ultrasonic cavitation increased the chemical activity and reaction rate resulting in a significantly increased ester formation. The ultrasonic technique reduced the transesterification reaction time to 5 minutesin comparison to 2 hours for mechanical stirring processing. Conversion of triglyceride (TG) to FAME under ultrasonication obtained 95.6929%wt with a methanol to oil molar ratio of 6:1 and 1%wt sodium hydroxide as catalyst. (cf. Darwin et al. 2010)

Gholami et al. (2021) demonstrated the superior efficiency of ultrasonically assisted biodiesel transesterification in comparison to mechanical agitation. The research team therefore compared two biodiesel plants based on the conventional mechanical stirring and ultrasonic cavitation, which were were designed using Aspen HYSYS V8.4. Total investment, costs of products, net present value, and internal rate of return were used to compare the two processesultrasonicator and mechanical strirrerwith each other. The total investment in the ultrasonic cavitation process was lower than that of the mechanical stirring process by approximately 20.8%. Compared to the conventional process, using ultrasonic reactors also caused products’ costs to reduce by 5.2%. Owing to a positive net present value and an internal rate of return of 18.3%, the ultrasonic cavitation process was a better choice. Moreover, ultrasonic cavitation resulted in a meaningful decrease in both consumed energy and the production of wastes. The overall energy consumption was reduced by 6.9% when ultrasonic cavitation was employed. The amount of waste produced in the ultrasound-assisted process was one-fifth of that in the mechanical stirring process.

Mid-Size and Large-Scale Ultrasonicators for Biodiesel Processing

Hielscher Ultrasonics’ supplies small to mid-size as well as large scale industrial ultrasonic processors for the efficient production of biodiesel at any volume. Offering ultrasonic system at any scale, Hielscher can offer the ideal solution for both small producers and large companies. Ultrasonic biodiesel conversion can be operated as batch or as continuous inline process. The installation and operation is simple, safe and gives reliably high outputs of superior biodiesel quality.
Below you will find recommended reactor setups for a range of production rates.

1x UIP500hdT
0.25 to 0.5
80 to 160
1x UIP1000hdT
0.5 to 1.0
160 to 320
1x UIP1500hdT
0.75 to 1.5
240 to 480
2x UIP1000hdT
1.0 to 2.0
320 to 640
2x UIP1500hdT
1.5 to 3.0
480 to 960
4x UIP1500hdT
3.0 to 6.0
960 to 1920
6x UIP1500hdT
4.5 to 9.0
1440 to 2880

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Literatūra / Atsauces

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Biodiesel Production

Biodiesel is produced when trigycerides are converted into free fatty methyl ester (FAME) via a chemical reaction known as transesterification. During the reaction of transesterification, trigylcerides in vegetable oils or animal fats react in presence of a catalyst (e.g., potassium hydroxide or sodium hydroxide) with a primary alcohol (e.g., methanol). In this reaction, alkyl esters are formed from from the feedstock of vegetable oil or animal fat. Triglycerides are glycerides, in which the glycerol is esterfied with long chain acids, known as fatty acids. These fatty acids are abundantly present in vegetable oil and animal fats. Since biodiesel can be produced from various different feedstocks such as virgin vegetable oils, waste vegetable oils, used frying oils, animal fats such as tallow and lard, the amount of free fatty acids (FFAs) can vary heavily. The percentage of free fatty acids of the triglycerides is a crucial factor that influences the biodiesel production process and the resulting biodiesel quality drastically. A high amount of free fatty acids can interfere with the conversion process and deteriorate the final biodiesel quality. The main problem is that free fatty acids (FFAs) react with alkali catalysts resulting in the formation of soap. Soap formation subsequently causes glycerol separation problems. Therefore, feedstocks containing high amounts of FFAs mostly require a pretreatment ( a so-called esterification reaction), during which the FFAs are transformed into esters. Ultrasonication promotes both reactions, transesterification and esterification.

Chemical Reaction of Esterification

Esterification is the process of combining an organic acid (RCOOH) with an alcohol (ROH) to form an ester (RCOOR) and water.

Methanol Use in Acidic Esterification

When acid esterification is used to reduce FFAs in feedstock, the immediate energy requirements are relatively low. However, water is created during the esterification reactioncreating wet, acidic methanol, which must be neutralized, dried and recovered. This methanol recovery process is expensive.
If starting feedstocks have 20 to 40 % or even higher percentages of FFAs, multiple steps may be necessary in order to bring them down to acceptable levels. This means, even more acidic, wet methanol is created. After neutralizing the acidic methanol, drying requires multistage distillation with significant reflux rates, resulting in very high energy use.

High performance ultrasonics! Hielscher's product range covers the full spectrum from the compact lab ultrasonicator over bench-top units to full-industrial ultrasonic systems.

Hielscher Ultrasonics manufactures high-performance ultrasonic homogenizers from lab to industrial size.

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