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    • 专利摘要:
    Process of recovery of polyphenols from the fermentation brine of green table olives through membrane and adsorption technologies. This is the description of a process for the integral management of residual fermentation brine and water from the transport of table olives during their packaging. This process consists of a series of operations in series (prefiltration, ultrafiltration, nanofiltration and adsorption), whose objective is the separation of the polyphenols (mainly hydroxytorosol and tyrosol) as well as the reuse of the brine in the process of fermentation of the processing of the table olives. In addition, a direct osmosis process has been introduced to reduce the conductivity of the brine entering the nanofiltration process. Accordingly, this invention is framed in the area of wastewater treatment. (Machine-translation by Google Translate, not legally binding)
    公开号:ES2569002A1
    申请号:ES201431617
    申请日:2014-11-04
    公开日:2016-05-05
    发明作者:Laura PASTOR ALCAÑÍZ；Silvia DOÑATE HERNÁNDEZ；José Antonio MENDOZA ROCA；Silvia ÁLVAREZ BLANCO；Mª Cinta VINCENT VELA；Mª Amparo BES PIÁ
    申请人:Depuracion De Aguas Del Mediterraneo (dam)；
    IPC主号:
    专利说明:

    DESCRIPTION 5
    POLYPHENOL RECOVERY PROCESS OF GREEN TABLE OLIVES FERMENTATION SALMUERA THROUGH MEMBRANE AND ADSORTION TECHNOLOGIES

    SECTOR OF THE TECHNIQUE 10
    The invention falls within the technical sector of wastewater treatment and purification processes, more specifically in relation to the integral management of residual fermentation brine and water from the transportation of table olives during packaging, with recovery of polyphenols present in water (mainly hydroxytyrosol and tyrosol) and reuse of brine in the fermentation process of table olives processing.

    STATE OF THE TECHNIQUE
    As is already known, the global production of green table olives is mainly concentrated in the Mediterranean Region, and is very important for the economies of Spain, Italy, Greece, Turkey, Tunisia and Morocco (GC Kopsidas et al., 1992 ). In particular, Spain is the world's first producer of table olives, followed a long distance from other countries in the Mediterranean basin. The average world production in the campaigns from 2005 to 2011 amounts to 2,150,000 25 tons, of which 508,000 were produced in Spain, that is, 24% of the total.
    The objective of the processing of green table olives is to make them edible, and for this it is necessary to eliminate the natural bitterness of the fruit, mainly due to oleuropein, which is a polyphenol existing only in this fruit. First, the olives are placed in tanks and immersed in a 1-2% solution (w / v) of sodium hydroxide (8-12 hours). During this stage, the hydrolysis of oleuropein takes place, which is labile under alkaline conditions (Marsilio et al., 1998). Sodium hydroxide penetrates through three quarters of the meat, leaving a small volume around the bone that is not affected. This part of the meat provides the necessary sugars for subsequent fermentation. In the next step, the 35 olives are washed with water. Today, and due to environmental issues, washing is carried out only once and for 12-14 h. Operating this way will
    reduces the overall volume of wastewater. Finally, the olives are immersed in a brine solution with 4-8% (w / v) of sodium chloride and with lactic acid (added for pH control). The NaOH solution residues of the previous stage form a regulation solution with lactic acid, which improves the organoleptic properties of the olives. At the same time, it promotes the growth of bacteria of the genus Lactobacillus in brine, which perform the fermentation. The lactic fermentation process lasts about two months, after which, the olives are ready for commercial use. If the olives are to be transported to the packing centers, and in them by the different conveyor belts, the transport water has characteristics very similar to that of the fermentation water. fifteen
    Throughout the process, large quantities of wastewater are generated, between 3.9 and 7.5 m3 per tonne of olives, depending on the variety (G.C. Kopsidas et al., 1992). The purification of these waters constitutes an important concern for the environment in the Mediterranean countries and mainly the residual water of the fermentation stage with brine that, although they represent only 20% of the total volume of liquid generated, contain 80-85 % of total contaminant load. The corrosive nature of the salt in the brines and the fact that these waters contain non-biodegradable salts and organic solids, makes their elimination an especially difficult problem to solve. Exhausted brine, if discharged uncontrollably, may enter wells or streams used for irrigation, which decreases its quality and, in severe cases, can cause soil deterioration, so that they are no longer obtained satisfactory crops. In addition, organic acids, such as lactic acid, lower soil pH considerably. It has also been shown that sodium and chloride ions exert a specific toxicity on some plants. (Niaounakis and Halvadakis, 2006) 30
    Bibliography
    G.C. Kopsidas, Wastewaters from the preparation of table olives, Water Research 26 (5) (1992) 629–631.
    V. Marsilio, B. Lanza, Characterization of an oleuropein degrading strain of Lactobacillus plantarum. Combined effects of compounds present in olive fermenting 35 brines (phenols, glucose and NaCl) on bacterial activity, Journal of the Science of Food and Agriculture 76 (1998) 520-524.
    G. Moussavi, B. Barikbin, M. Mahmoudi. The removal of high concentrations of phenol 5 from saline wastewater using aerobic granular SBR. Chemical Engineering Journal 158 (2010) 498–504.
    M. Niaounakis, C.P. Halvadakis Olive processing waste management: literature review and patent survey. Second Edition 2006. Amsterdam; London: Elsevier.
    E. Reid, Xingrong Liu, S.J. Judd Effect of high salinity on activated sludge 10 characteristics and membrane permeability in an immersed membrane bioreactor. Journal of Membrane Science 283 (2006) 164-171.
    A. Uygur, F. Kargi. Salt inhibition on biological nutrient removal from saline wastewater in a sequencing batch reactor, Enzyme Microbiology and Technology 34 (2004) 313–318. fifteen

    OBJECT OF THE INVENTION: TECHNICAL PROBLEM-PROPOSED SOLUTION
    Currently, the treatments used to purify this type of water are very burdensome from an environmental point of view, such as solar evaporation in rafts, which can lead to seepage in the soil, or burdensome from an economic point of view. , such as advanced oxidation treatments, among others. Biological treatments are very complicated due to high salinities, and in addition, if performed correctly, it would mean the destruction of valuable substances such as polyphenols. Therefore, due to the characteristics of wastewater, these treatments are difficult to apply as evidenced by 25 multiple works (Gholamreza Moussavi et al., 2010; E. Reid et al., 2006; A. Uygur et al. ., 2004).
    The proposed invention combines an integration of membrane processes with an adsorption process that allows, unlike other processes, the recovery of valuable substances (polyphenols tyrosol and hydroxytyrosol) and the reuse of residual brine.

    DETAILED DESCRIPTION OF THE INVENTION
    The proposed invention manages to obtain a polyphenol concentrate (tyrosol and hydroxytyrosol) and fermentation brine from the table olive process.
    a saline solution for reuse, also generating a final residue. The process consists of 5 operations: filtration (A), ultrafiltration (B), nanofiltration (C), adsorption (D) and direct osmosis (E) (Figure 1)
    The brine to be treated is conducted to a pre-treatment stage based on a series filtration (A), first by a 60 micron filter and then by a 5 micron filter in order to remove solids is larger suspension . The filtrate (1) is conducted to the ultrafiltration process (B), basically removing the rest of solids in suspension not eliminated in the pre-treatment, as well as oils and fats that the sample could contain. The rejection of ultrafiltration will mean between 10 and 15% of the volume of treated water and will be the only liquid waste (in the form of mud) of the system. The permeate (filtered) current of the ultrafiltration (2) will be conducted according to its conductivity to the direct osmosis stage (E) or directly to the nanofiltration stage (C).
    In the direct osmosis process, current (2) will be used as a drag solution (with a high concentration of salts still). In this way, this process serves to standardize the salt content of the water to be treated in the subsequent nanofiltration process (C), since depending on the time of the year the fermentation brine and the transport water of the olives can contain a conductivity between 65 and 95 mS / cm. Lowering the conductivity of water is a benefit in the nanofiltration process from the point of view of energy cost and membrane fouling. Direct osmosis requires another stream (5) that is concentrated while diluting the concentrated stream in salts (2). It is proposed that said stream be a biological sludge from a wastewater treatment plant (WWTP), which will concentrate on the process, constituting the stream (6). The concentration of this current is an additional benefit to the process as it reduces the costs of treating these sludge. 30
    Since the polyphenols present in stream 2 are predominantly hydroxytyrosol and tyrosol, the nanofiltration membrane (C) (membrane like Dow Chemical NF245) barely rejects them, as does the conductivity since they are mostly sodium chloride. However, the membrane rejects a percentage of organic matter, which basically consists of sugars from the fermentation process. Therefore, the permeate (filtering) of the nanofiltration (4) will basically consist of a mixture of polyphenols and sodium chloride. The rejection current (approximately 25%) will be recirculated (3) for mixing with the water from the pretreatment (1) for ultrafiltration.
    The permeate of nanofiltration (4) will lead to an adsorption stage (D) (in particular by resins such as MN200) for the separation of the polyphenols from the salt stream. The separated polyphenols will be subsequently recovered in the resin regeneration step by solvent.

    EXPLANATION OF FIGURE 10

    A: prefiltration 1: prefiltered brine
    B: ultrafiltration 2: permeate ultrafiltered brine
    C: nanofiltration 3: nanofiltration brine rejection
    D: adsorption 4: permeate nanofiltered brine 15
    E: direct osmosis 5: biological sludge WWTP
        6: concentrated WWTP biological sludge

    Brine to be treated: brine from the pickled olives
    Final waste: rejection of the ultrafiltration process 20
    Polyphenols: polyphenols recovered after the adsorption process
    To be reused: brine composed exclusively of sodium chloride
    权利要求:
    Claims (2)
    [1]
    CLAIMS 5
    1. Procedure for the purification of high saline wastewater from the olive processing industry, which includes fermentation brine and transport water in the packaging plant.
     10
    [2]
    2. Procedure that allows the recovery of polyphenols (tyrosol and hydroxytyrosol) from the wastewater of the olive processing and the reuse of brine. This procedure includes the following stages:
    - Pretreatment of wastewater consisting of a double filtration at 60 and 5 microns.
    - Ultrafiltration of filtered water with a 5 kDa membrane of molecular cut. The rejection of the ultrafiltration membrane will be the only residue of the combined membrane process. twenty
    - Application of a direct osmosis process to ultrafiltered water, using it as a drag solution. This process allows the concentration of a biological sludge from purification of an urban wastewater treatment plant at the same time that the conductivity of ultrafiltered water is adjusted before it enters the nanofiltration process.
    - Nanofiltration of ultrafiltered water, after passing through the direct osmosis stage or not, in order to separate the sugars present in the residual water from the polyphenols. The nanofiltration rejection current is recirculated at the ultrafiltration inlet.
    - Adsorption by resins of the permeate stream of the nanofiltration stage for the separation of the polyphenols from the brine, which can be reused.
    - Desorption of resin polyphenols for final recovery.







    image 1

    Figure 1. Scheme of the process object of the invention
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