Category Archives: Extraction

Removal of aromatics from oil fractions

30

Aug 2022

Removal of aromatics from oil fractions

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In the processing of petroleum crude oils, vacuum distillates and de-asphalted oils (DAO) are among the partial streams. These can be further processed into high quality base oils.
The first step is the removal of aromatics by extraction, which produces Distillate Aromatic Extracts (DAE) and Residual Aromatic Extracts (RAE) as extracts. DAE and RAE are important process oils used in the production of rubber products (tyres, inner tubes, floor coverings).
The polycyclic aromatic hydrocarbons (PCA) contained in DAE and RAE are now classified as highly harmful to health.
EU Directive 2005/69/EC limits the permissible limit value for polycyclic aromatic hydrocarbons (PCA). Limit values are benzo(a)pyrene < 1 mg/kg and total PCA < 10 mg/kg.
In order to fall below these limits, DAE and RAE are further treated by means of a extraction step. The extracts obtained in this way are called Treated Distillate Aromatic Extracts (TDAE) and Treated Residual Aromatic Extract (TRAE).
The market for TDAE and TRAE is growing strongly while DAE and RAE are in decline.
Figure 1: Market development TDAE

A possible technical solution for the extractive removal of aromatics is the Asymmetric Rotating Disk Contactor (ARDC) from Technoforce Solutions. Here, the series counter current circuit of several mixers/settlers (see Fig. 2) of a conventional extraction is transferred to an extraction column.

Figure 2: Conventional arrangement of three mixers/settlers

Figure 3: Structure of the ARDC

The ARDC consists of an axis with rotating discs that ensure mixing of feed and solvent and flow- calmed settling zones in which raffinate and extract can separate. The separate settling zone of the ARDC has significant advantages even against symmetrically designed conventional rotary extractors. The separation is significantly more controlled and thus more effective, as unwanted flow entrainment is avoided.

Approximately 6 mixer/settler stages are realised in one ARDC. The name comes from the off-centre axis of rotation of the mixing zone.
For the removal of aromatics from the DAE, furfural or NMP are used as solvents. While the NMP tolerates higher process temperatures, the possible process temperature for furfural is limited due to the higher partial pressure. However, furfural has a higher selectivity towards mono-aromatics than NMP and can therefore be used in a lower solvent to feed ratio. The process-relevant data are determined in advance by piloting in pilot plants of Technoforce Solutions. Figure 4 shows the settling zones in a glass column, which is used to adjust the flow conditions. Figure 5 shows one of the piloting plants.

Figure 4: Settling zones in an experimental column

Figure 5: ARDC Pilot Plant in Geleen, The Netherlands

Even at lower temperatures, the removal of aromatics to values far below those required by EU Directive 2005/69/EC can be achieved by getting a good TDA yield.

Technoforce has already designed and built more than 60 Asymmetric Rotating Disk Column Units for Petrochemical industry, Fine chemistry, Pharma and other industrial sectors. Within the scope are also other extraction technologies as well as other technologies like Short Path Distillation, Agitated Thin Film Evaporation and Drying, Falling Film, Rising Film and Forced Circulation Evaporation, as well as Liquid-Liquid Extraction and Crystallization.

Our Expertise
Evaporation
Drying
Crystallization
Short Path Distillation
Zero Liquid Discharge Systems
Extraction


Crystallization of a Monomer from a Waste Depolymerization Process

12

Aug 2022

Crystallization of a Monomer from a Waste Depolymerization Process

It’s no secret that the digital industry is booming. From exciting startups to global brands, companies are reaching out to digital agencies, responding to the new possibilities available.

Recycling of polymer products (“plastics”) is an important contribution to reduce the amount of waste that can turn into microplastic and pollute the environment for decades, and for an improved carbon dioxide balance in production of new polymers. The latter can be achieved by depolymerization of polymers by either thermal pyrolysis or in case of polyesters by interesterification in a suitable medium. However, the recovered monomer usually must meet strict quality requirements. Therefore, besides yield, the purity achieved is an essential criterion for the economy of the overall process. Depending on the properties of the monomer, different separation processes are available for this purpose. In addition to distillation methods, crystallization is one possibility for achieving high quality products. Using crystallization, it is also possible to not only have a strict control of purity but also on the crystal morphology and size distribution. In addition, customers are looking for continuous processes rather than batchwise operation. This is where the Technoforce Plug Flow Crystallizer (TPFC) comes into play.

The Technoforce Plug Flow Crystallizer consists of a horizontal cylinder fitted with one or more separate double jackets. This allows the crystallizer to be individually tempered in different sections to create a graduated temperature profile. In cooling crystallization, for example, an 80°C solution could be cooled to 60°C, then to 40°C and further to 20°C to control crystallization. A specially designed rotor ensures good mixing within a section, however from section to section (i.e., from temperature level to subsequent temperature level) the system forces a plug flow without significant back-mixing. The rotor design also minimizes mechanical energy transfer into the crystal slurry to avoid breaking of mature crystals into fines. By this, unwanted secondary nucleation and uncontrolled crystal growth can be reduced considerably.
Technoforce Plug Flow Crystallizer with cross section

By optimizing the crystallization process with our pilot size Technoforce Plug Flow Crystallizer, we were able to maximize yield with a narrow crystal size distribution for the monomer. The solution was directly coming from the upstream depolymerization at elevated temperature and was gradually cooled down at two different cooling media temperatures in one single TPFC. Thus, in one step we achieved the desired separation, while for demands of even higher purity it is always possible to repeat the crystallization by using either the same or a different solvent, a process known as re-crystallization.
In our laboratories in Nashik/India or Geleen/The Netherlands we can offer our customers bench scale and pilot scale crystallization trials in our continuous Plug Flow Crystallizers. Choice of suitable solvent as well as some pre-investigations regarding solubility curves should be performed by the customer beforehand to speed-up the project.
Technoforce has already designed and built several hundred skids of process intensification technology for oils and fats applications, fine chemistry, polymers, food and pharma products and other industrial sectors. We also offer other evaporation technologies like Short Path Distillation, Agitated Thin Film Evaporation and Drying, Falling Film, Rising Film and Forced Circulation Evaporation, as well as Liquid-Liquid Extraction in columns or centrifugal systems.

Our Expertise
Evaporation
Drying
Crystallization
Short Path Distillation
Zero Liquid Discharge Systems
Extraction