EP 3946668 A2 20220209 - METHOD AND DEVICE FOR CONTROLLING THE PRODUCTION OF AN EXTRACT USING A SOLID-LIQUID EXTRACTION PROCESS
Title (en)
METHOD AND DEVICE FOR CONTROLLING THE PRODUCTION OF AN EXTRACT USING A SOLID-LIQUID EXTRACTION PROCESS
Title (de)
VERFAHREN UND VORRICHTUNG ZUR STEUERUNG DER HERSTELLUNG EINES EXTRAKTES DURCH FEST-FLÜSSIG-EXTRAKTION
Title (fr)
PROCÉDÉ ET DISPOSITIF DE CONTRÔLE DE LA PRODUCTION D'UN EXTRAIT PAR EXTRACTION SOLIDE-LIQUIDE
Publication
Application
Priority
- DE 102019002218 A 20190328
- EP 2020000045 W 20200219
Abstract (en)
[origin: WO2020192959A2] The invention relates to a method for controlling the production of an extract using a solid-liquid extraction process, preferably a hot solid-liquid extraction process, in particular for large-scale industrial applications and in particular for producing a tea concentrate, using at least one extraction container (10; 100; 1000) according to the preamble of claim 1. The aim of the invention is to improve the exchange of material during the extraction process in comparison to solutions according to the prior art and to allow a controlled dehumidification of a raffinate with residual moisture in order to obtain additional valuable extracts using the method according to the invention. According to the method, this is achieved by carrying out the following steps: (i) providing the first compound (M) in the extraction container (10; 100; 1000); (ii) supplying the specified second compound (m) to the provided first compound (M) without spatial constraints and distributing and mixing the second compound into and with the first compound (M); (iii) discharging a mixture ((C∞B)+A), consisting of the extract ((C∞B)) and the raffinate (A), out of the extraction container (10; 100; 1000); (iv) separating the mixture discharged according to step (iii) into the raffinate with residual moisture (A+) and an extract ((C°°B)**) released from the raffinate with residual moisture (A+); and (v) re-treating the raffinate with residual moisture (A+) at least such that the residual moisture consisting of the extract is at least partly removed from the raffinate with residual moisture (A+) by a dehumidification process and is supplied to the already separated extract ((C∞B)).
IPC 8 full level
B01D 11/02 (2006.01); A23F 3/18 (2006.01); A23F 3/22 (2006.01); A23F 3/42 (2006.01); B01D 37/04 (2006.01)
CPC (source: EP KR US)
A23F 3/18 (2013.01 - EP KR US); A23F 3/22 (2013.01 - EP KR); A23F 3/423 (2013.01 - EP KR); B01D 11/0207 (2013.01 - EP KR US); B01D 11/0223 (2013.01 - EP KR); B01D 11/0257 (2013.01 - EP KR US); B01D 11/0284 (2013.01 - EP KR US); B01D 11/0288 (2013.01 - US); B01D 37/043 (2013.01 - KR); B01D 37/043 (2013.01 - EP)
Citation (search report)
See references of WO 2020192959A2
Designated contracting state (EPC)
AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR
Designated extension state (EPC)
BA ME
DOCDB simple family (publication)
WO 2020192959 A2 20201001; WO 2020192959 A3 20201119; WO 2020192959 A4 20210107; DE 102019002218 A1 20201001; EP 3946668 A2 20220209; KR 20210143859 A 20211129; US 2022184524 A1 20220616
DOCDB simple family (application)
EP 2020000045 W 20200219; DE 102019002218 A 20190328; EP 20710422 A 20200219; KR 20217034357 A 20200219; US 202017598032 A 20200219