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. 2021 Apr 15;19(4):e06511. doi: 10.2903/j.efsa.2021.6511

Table 1.

Comparison of processing parameters of the approved method in the legislation (Commission Regulation (EU) No 142/2011) and the alternative methods (submitted by the applicant in 2017 and 2020)

Methods and their parameters
Commission Regulation (EU) No 142/2011 Section 2 D, Chapter IV, Annex IV RepCat® process, 2017 RepCat® process 2020
Process pH T t p pH T t p pH T t p
Pressure sterilisation a n.s. 133 20 3 bar n.s. 133 20 3 bar n.s. 133 20 3 bar
Removal of insoluble impurities b n.s. n.s. n.s. n.s. n.s. n.s. n.s. n.s. n.s. n.s. n.s. n.s.
Esterification c < 1d 72 ≥ 120e n.s. n.s. ≥ 220 ≥ 30h ≥ 80 bar n.s. ≥ 200 ≥ 15i ≥ 70 bar
Transesterification c 14f 35–50 ≥ 15g n.s.
Vacuum distillation n.s. 150 n.s. n.s. n.s. ≥ 150 n.s. ≤ 10 mbar n.s. ≥ 150 n.s. ≤ 10 mbar

n.s: not specified; T: temperature in centigrade; t: time in minutes; p: pressure in bar or mbar as indicated.

a

According to method 1 as specified in Commission Regulation (EU) No 142/2011.

b

To obtain cleaned raw material with solid content < 0.15% w/w.

c

For the RepCat® method, esterification and transesterification are combined into a single step.

d

By addition of sulfuric acid or equivalent acid.

e

Mixed intensely.

f

By addition of potassium hydroxide or an equivalent base.

g

Carried out twice using a new base solution.

h

Mixing with addition of methanol to 15% w/w.

i

Mixing with addition of methanol to 10–15% w/w and traces of MgO as catalyst.