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Eur 40 electrodialysis stacks for the demineralization
of cheese whey.
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Dairy

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WHEY DEMINERALIZATION PROCESSES
In the dairy industry, whey is obtained
from the manufacturing of cheese and casein. There is a high demand
for demineralized whey for many applications in human and cattle
feed: these include instant formula (baby food; min. 90 % demin.),
confectionary, baking, meats, etc. Depending on the use for the end
product, the demineralization process has tbe tailored taking intaccount the complete composition of the raw whey: this includes the
ash profile and the equivalent acid content. Thus, the optimum
demineralization processes will be different for wheys produced from
two types of cheese, even if these belong to the same cheese
category.
In the case of cheese whey, there are two
main grades of whey:
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Sweet whey with a titrable acidity below
0.16 % or a pH above 6.0, from cooked cheeses
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Acid whey with a titrable acidity above
0.4 % or a pH below 4.0, from soft, fermented, and cottage cheeses.
In manufacturing, the whey obtained
after coagulation with HCl or H2SO4 has a titrable acidity between
0.4 and 0.45 %.
With more than 20 operating systems
worldwide, Eurodia / Ameridia has a unique expertise in whey
demineralization processes, either internally developed or licensed
form close partners. In accordance with our general process
development philosophy, the optimum process for each dairy customer
might combine several technologies adapted to its specific product:
these include electrodialysis reversal (EDR), ion exchange resins (IER),
and nanofiltration (NF). For instance, nanofiltration is not
attractive if used alone for any demineralization rates above 35 %
because of the high losses of lactose and divalent ions: therefore,
NF could be useful as a pretreatment or postreatment step.
Similarly, ion exchange resins are not economically attractive when
used alone because of the high volume of effluents, the high running
cots, and the heavy pollution load. For more details about the use
of nanofiltration only to demineralize whey, please go also to the
Technologies Section/ Nanofiltration of this website.
Following, are some general guidelines for
the expected optimized overall demineralization process for sweet
whey:
SWEET WHEY DEMINERALIZATION
Method to be used depends on the
required demineralization rate:
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DEMINERALIZATION RATE (ON ASHES)
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FEED
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30%
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50-70%
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90%
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DILUTED
SWEET WHEY
6% DS
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nanofiltration
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ion exchange resins + nanofiltration
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electrodialysis + ion exchange resins + nanofiltration
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PRECONCENTRATED SWEET WHEY
18-24% DS
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electrodialysis
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electrodialysis
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ion exchange
resins + electrodialysis
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Eurodia's design principles for a whey
demineralization plant:
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Achieve the demineralized whey specifications with the lowest operating costs and the most cost effective investment.
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Maintain the quality of the valuable product (proteins) by avoiding microbiological development and thermal shocks (by operating at acidic pH as much as possible).
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Keep the dry solid and valuable product yields as high as possible.
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Reduce the volume of waste effluent as well as the pollution load.
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Design the demineralization process taking into account the downstream process steps (i.e. evaporation, standardization, spray drying…) to optimize their operating and capital costs.
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Optimize the choices of technology, materials, and instruments.
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Look for easy maintenance.
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Design to meet FDA and 3A requirements.
EXAMPLE
6 % DS SWEET WHEY DEMINERALIZATION FOR
INSTANT FORMULA RUNNING COSTS in €/kg DS

WHEY DEMINERALIZATION
PERMANENT IMPROVEMENT OF TECHNOLOGY
1.ELECTRODIALYSIS
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Minimizes valuable products losses
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Lowers pollution load even after 10,000 hours of operation
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Improves the current efficiency and the power consumption
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Reduces the water consumption.
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Different thicknesses depending on of DS content and viscosity
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Different materials (all FDA approved grade) to operate at temperatures as high as 60°C
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Different types of netting to optimize flows and lower pressure drops.
2. ION EXCHANGE RESINS AND COLUMNS
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Strong cation gel type with high DVB content to improve the selectivity of resins when used as softeners before ED (SODIUM PROCESS® patented by the SAFIR Company).
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Adsorption of protein and complexed salts is dramatically reduced.
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Strong anion resins of special grade to be used with the above-mentioned strong cation resins in mixed beds (density, granulometry, swelling)
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Weak cation resins (carboxylic) adaped to reduce the divalent cations and adjust the pH.
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Weak anion resins with low swelling, no adsorption of proteins, and high capacity for phosphorous removal.
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Cost effective regarding feed distribution and chemicals (regenerants) consumption
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Adapted to resins swelling (if low).
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Easy to move when increasing resins volume for capacity increase
3. EASY MAINTENANCE AND OPTIMIZED
HYDRAULIC PIPING
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ED stacks can easily be handled,
disassembled and reassembled for on-site maintenance (in less than 2
hours per stack).
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Rod electrodes that can be replaced within
a few minutes (while hours are necessary for flat electrodes).
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Easy access to all key components (pumps,
valves, instruments).
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Selection of reliable instruments for
non-stop operation.
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Short hydraulic piping for both ED and IER
to optimize brine, chemicals, water and energy consumption.
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Specifically designed valve manifolds are
installed to avoid any risk of streams contamination (feed/product,
product/chemicals etc...)
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The on-line factor of our demineralization
plants is usually higher than 96 -98%.
EXAMPLE
SWEET WHEY DEMINERALIZATION FOR INSTANT
FORMULA

Table 1
Raw material composition, sweet
whey analysis
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Raw material to process/day
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400 000 L/d
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408 840 kg
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Total solid
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6.30%
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25 757 kg
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Density
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1.0221
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1.0221
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Processing time per
day
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16 h/d
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Annual production time
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250d/year
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Inlet temperature
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4°C
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Note : Material balance is expressed in true proteins +
NPN, and not in total proteins.
Client data (or literature data)
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RAW MATERIAL |
SWEET WHEY FROM CHEESE MAKING |
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CLIENT'S
DATA
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%
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Solid/Day
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Equivalents
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Equivalents
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Molecular
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cations
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anions
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weight
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(equivalent)
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PH
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6.5
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Density (abacus).
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1.0221
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Solids
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6.300%
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25
757 kg
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Total protein
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13.250%
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3
413 kg
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Nitrogen from casein.
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0.040%
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10
kg
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120
mg/L
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Whey proteins (estimated)
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9.765%
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2
515 kg
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NPN (as Nitrogen)
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0.540%
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139
kg
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6,38
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Ash
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8.900%
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2
292 kg
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70,5
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Lactose
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74.400%
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19
163 kg
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Fats
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1.100%
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283
kg
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Ca++
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0.625%
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161
kg
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8
049 eq.
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20
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Mg++
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0.146%
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38
kg
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3
134 eq.
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12
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Na+
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0.970%
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250
kg
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10
863 eq.
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23
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K+
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2.100%
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541
kg
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13
869 eq.
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39
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NH3+
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0.380%
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98
kg
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5
438 eq.
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18
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Fe++
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0.010%
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3
kg
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92
eq.
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27.93
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Cu++
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0.010%
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3
kg
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81
eq.
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31.77
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Cl-
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2.163%
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557
kg
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15
694 eq.
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35.5
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P
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0.600%
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155
kg
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4
989 eq.
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31
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NO3-
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0.030%
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8
kg
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125
eq.
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62
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S
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0.165%
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42
kg
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1
328 eq.
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32
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CO3--
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30
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Lactic acid
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1.400%
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361
kg
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4
007 eq.
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90
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acetic acid
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0.196%
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50
kg
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841
eq.
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60
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Citric acid
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1.800%
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464
kg
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2
634 eq.
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176
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Other 1
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Other 2
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Checking
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24
764 kg
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41
525 eq.
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29
618 eq.
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Other, by difference
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96.10%
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993 kg
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41 525 eq.
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29 618 eq.
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Table 2
Raw material composition,
standard sweet whey
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Adjusted
data
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%
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Solid/Day
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Equivalents
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Equivalents
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Molecular
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cations
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anions
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weight
1
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equ
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PH
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6.5
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Density (abacus).
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1.0221
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Solid
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6.30%
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25
757 kg
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Total protein
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13.25%
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3
413 kg
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Nitrogen from casein.
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0.04%
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10
kg
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Whey proteins (estimated)
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9.76%
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2
515 kg
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NPN (as Nitrogen)
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0.54%
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139
kg
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6.38
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Ash
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8.28%
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2
133 kg
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70.5
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Lactose
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76,88%
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19
801 kg
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Fats
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1.10%
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283
kg
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Ca++
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0.63%
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161
kg
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8
049 equ
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20
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Mg++
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0.15%
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38
kg
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3
134 equ
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12
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Na+
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0.97%
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250
kg
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10
863 equ
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23
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K+
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2.10%
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541
kg
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13
869 equ
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39
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NH3+
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0.38%
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98
kg
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5
438 equ
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18
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Fe++
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0.01%
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3
kg
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92
equ
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27.93
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Cu++
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0.01%
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3
kg
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81
equ
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31.77
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Cl-
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2.16%
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557
kg
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15
694 equ
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35.5
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P
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0.60%
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155
kg
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4
989 equ
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31
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NO3-
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0.03%
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8
kg
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125
equ
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62
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S
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0.17%
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42
kg
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1
328 equ
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32
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CO3--
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30
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Lactic acid
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1.40%
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361
kg
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4
007 equ
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90
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acetic acid
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0.20%
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50
kg
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841
equ
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60
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Citric acid
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1.80%
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464
kg
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2
634 equ
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176
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Other 1
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