the bat study for potatoes, vegetables and fruit

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Distribution: Restricted The BAT study for potatoes, vegetables and fruit processing industry April 2016 translated version of parts of the Dutch version BBT voor de aardappel-, groenten- en fruitverwerkende nijverheid (AGF) Liesbet Van den Abeele, Stella Vanassche, Reinhilde Weltens and Diane Huybrechts 2016/SMAT/R/0592 April 2016 TRANSLATION VERSION APRIL 2016

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The BAT study for potatoes, vegetables and fruit processing industry April 2016 translated version of parts of the Dutch version BBT voor de aardappel-, groenten- en fruitverwerkende nijverheid (AGF) Liesbet Van den Abeele, Stella Vanassche, Reinhilde Weltens and Diane Huybrechts 2016/SMAT/R/0592 April 2016

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All rights, amongst which the copyright, on the materials described in this document rest with the Flemish Institute for Technological Research NV (“VITO”), Boeretang 200, BE-2400 Mol, Register of Legal Entities VAT BE 0244.195.916. The information provided in this document is confidential information of VITO. This document may not be reproduced or brought into circulation without the prior written consent of VITO. Without prior permission in writing from VITO this document may not be used, in whole or in part, for the lodging of claims, for conducting proceedings, for publicity and/or for the benefit or acquisition in a more general sense. TRANSLA

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ABSTRACT

The Centre for Best Available Techniques (BAT) is founded by the Flemish Government, and is hosted by VITO. The BAT centre collects, evaluates and distributes information on environmentally friendly techniques. Moreover, it advises the Flemish authorities on how to translate this information into its environmental policy. Central in this translation is the concept “BAT” (Best Available Techniques). BAT corresponds to the techniques with the best environmental performance that can be introduced at a reasonable cost. To process potatoes, vegetables and fruit, large amounts of water and energy are used. By processing the potatoes, vegatables and fruit organic materials will migrate to the process water and cause waste water. The processes themselves and the storage of the processed fruit and vegetables use energy. These issues can cause a possible environmental impact. In the study, a distinction is made between companies that produce potatoes, vegetables or fruit. Vegetables and fruit should be processed as soon as possible after harvesting. The harvest periods of the different vegetables and fruits follow one another during the year. Each type of fruit or vegetable has its own (pre)processing steps with a different impact on water use and waste water contamination. The environmental impact therefore, varies during the year. Companies that process potatoes have a continuous process, as potatoes can be stored for a year. The environmental impact of these companies will therefore show less variation. Fruit processing into juices is limited in Flanders. Therefore, these activities are only described in chapters two, three and four. No specific BAT conclusions were developed for these companies. This study also distinguishes different preservation methods of potatoes, vegetables and fruit. Each preservation method has its own environmental impact. For canning, larger amounts of water and energy are needed than for the production of frozen or fresh products. The storage of canned vegetables or fruit is done at room temperature, allowing lower energy consumption in this phase than for frozen products ( -18 °C) or fresh products ( 4 to 6 ° C). The objective of this study was to determine the best available techniques to reduce water and energy consumption and emissions to wastewater and air (odor). An additional point of interest in this study is how the sector can efficiently handle its raw materials to maximize the use as food. In addition, we examined how the side streams can be become feed for livestock, soil improver or source for renewable energy. Based on the BAT conclusions, BAT associated emission levels for the fruit and vegetable sector were derived by the method of Polders et al. (2012). To come to this, emission data of VMM were used. Since the industrial waste water of various types potatoes, vegetables and fruit companies varies and not all proposed BAT are applicable in these companies, a proposal for differentiated BAT associated emission levels (BAT-AEL) was developed. This has been done for potato processing companies and vegetable processors and for larger companies (type frozen and canned products) and smaller companies (type processors of fresh potato and vegetables). The BAT selection in this study was based on plant visits, a literature survey, a technical and socio-economic study and discussions with industry experts and authorities,… The formal consultation was organised by means of an advisory committee.

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Table 1: Evaluation of available environmentally-friendly techniques and selection of BAT

Technique Technical feasibility Environmental benefit

Cost

feasib

ility

&

eff

ectiveness

BAT

Pro

ven

Safe

ty

Genera

lly

applicable

Quality

Overa

ll

Wate

r

consum

ption

Waste

wate

r

odour

Waste

ra

w

mate

rials

Energ

y

Chem

icals

Impact

on

the

chain

Overa

ll

Limiting raw materials

Limiting packaging + 01 - 0 +/- 0 0 0 + 0 0 0 + 0 cbc2

Intensive sorting of waste + 0 + 0 + 0 0 0 + 0 0 0 + 0 Yes

Accurate sorting machinery to limit raw

material losses + 0 + + + + + 0 + + 0 + + -

Yes

Automatic filling machinery for cans and glass

packaging + 0 + 0 + 0 + 0 + 0 + + + -

Yes

Good housekeeping in order to limit raw

material losses + 0 + 0 + 0 0 0 + 0 0 + + 0

Yes

Valorisation of secondary streams

Vegetable juice from vegetable residues + 0 - 0 +/- 0 0 0 + 0 0 + + -- No

Recovering starch from the potato processing

industry + 0 + 0 + 0 + 0 + 0 0 + 0 -/0

Yes

1 If the packaging is limited judiciously, this will not have any negative impact on safety or quality. 2 The adaptation or limitation of the packaging must be carefully considered and is not always possible due to quality requirements. TRANSLA

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Technique Technical feasibility Environmental benefit

Cost

feasib

ility

&

eff

ectiveness

BAT

Pro

ven

Safe

ty

Genera

lly

applicable

Quality

Overa

ll

Wate

r

consum

ption

Waste

wate

r

odour

Waste

ra

w

mate

rials

Energ

y

Chem

icals

Impact

on

the

chain

Overa

ll

Recovering oil in the production of fried potato

products + 0 + 0 + 0 + 0 + 0 0 0 + 0

Yes

Recovering vitamins and high-quality products

from waste substances of vegetables and fruit -3 0 - 0 - 0 0 0 + - 0 + + -/--

No4

Recovering fertilisers from waste water:

formation of struvite by a chemical process + 0 - 0 + 0 + 0 + 0 - + + --

No5

Recovering fertilisers from waste water:

formation of struvite by a biochemical process -6 0 - 0 - 0 ++ 0 + 0 0 + 0 -/--

No

Valorisation of coir in biofermentation + 0 - 0 +/- 0 + 0 + 0 0 + 0 -

cbc/

No7

Re-using slurry as soil + 0 + 0 + 0 0 0 + 0 0 + + 0 Yes

Valorisation of PVF residues as animal feed + 0 - 0 +/- 0 0 0 + 0 0 + 0 0 cbc8

Electrodialysis for recovering chlorides from

concentrate streams + 0 - 0 +/- + + 0 + - + 0 + -- No9

3 It usually concerns experiments or laboratory-scale installations. 4 This technique goes beyond the BAT. 5 This technique goes beyond the BAT and is eligible for the ecology premium. 6 Only proven on a laboratory scale. 7 Only at very low flow rates. The formation of deposits on the coir must be ensured. 8 If the nutritional value of the residues is sufficient for use as animal feed. 9 This technique goes beyond the BAT. TRANSLA

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Technique Technical feasibility Environmental benefit

Cost

feasib

ility

&

eff

ectiveness

BAT

Pro

ven

Safe

ty

Genera

lly

applicable

Quality

Overa

ll

Wate

r

consum

ption

Waste

wate

r

odour

Waste

ra

w

mate

rials

Energ

y

Chem

icals

Impact

on

the

chain

Overa

ll

Internal re-use of concentrate streams from

reverse osmosis plants lab 0 - 0 lab 0 + 0 0 0 + 0 + No10

Use of polymers of NON-petrogenic origin in

water treatment + 0 + 0 + 0 0 0 + 0 0 + + + Yes11

Limiting energy consumption: heat treatments

Pre-heating products when using a steam

peeler + 0 + - +/- 0 0 0 +/- + 0 0 + - No

Limiting microbial contamination during the

production process + + + + + - 0 0 + + - 0 + - Yes

Optimising heat treatment + 0 - + +/- 0 0 0 0 + 0 0 + - Yes12

Appropriate choice of type and size of blancher

and associated technologies + + + + + + 0 0 0 + 0 0 + 0 Yes

Heat treatment during sterilisation or

pasteurisation of cans or glass + + + 0 + 0 0 0 0 + 0 0 + 0 Yes

Limiting energy consumption: alternatives for heat treatments

Cold pasteurisation of drinks and juices using

UV-C -13 0 - + - 0 0 0 0 + 0 0 + -

No

10 This technique has not yet been tested at plant level but does have potential. 11 This is the BAT for plants that only process waste water from PVF plants in their water treatment facilities. 12 This measure must be viewed in the light of “continuous improvements” to the quality and the production process. 13 Has been tested in the lab and on pilot scale. TRANSLA

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Technique Technical feasibility Environmental benefit

Cost

feasib

ility

&

eff

ectiveness

BAT

Pro

ven

Safe

ty

Genera

lly

applicable

Quality

Overa

ll

Wate

r

consum

ption

Waste

wate

r

odour

Waste

ra

w

mate

rials

Energ

y

Chem

icals

Impact

on

the

chain

Overa

ll

Pulsed Electrical Field (PEF) -14 0 - + - 0 No

Limiting energy consumption: chilled chain

Differentiated chilling network + 0 - 0 + 0 0 0 0 + 0 0 + - - No15

Automated cold stores + 0 -16 0 +/- 0 0 0 0 + 0 0 + - (-) cbc16

Good housekeeping in chilling + 0 + 0 + 0 0 0 0 + 0 0 + - Yes

Limiting energy consumption: steam

Minimising spray

+ 0 - 0 +/- + 0 0 0 + + 0 + -(-) cbc17 by continuously measuring the conductivity of

the condensate

by using reverse osmosis for boiler feedwater

Differentiated steam network + 0 -18 0 +/- 0 0 0 0 + 0 0 + - cbc18

14 Has been tested in the lab and on pilot scale. 15 This system goes beyond the BAT. It is not feasible for small and micro businesses. For others, this must be taken into consideration

in the case of reinvestments, taking account of the investment costs and electricity consumption of the cooling installation. 16 Automated cold stores are only worthwhile in large cold rooms. The throughput volume and the number of modifications should also

be taken into account. 17 Not applicable to micro-businesses. 18 A thorough analysis of the pipeline network must be performed before introducing such a technology. TRANSLA

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Technique Technical feasibility Environmental benefit

Cost

feasib

ility

&

eff

ectiveness

BAT

Pro

ven

Safe

ty

Genera

lly

applicable

Quality

Overa

ll

Wate

r

consum

ption

Waste

wate

r

odour

Waste

ra

w

mate

rials

Energ

y

Chem

icals

Impact

on

the

chain

Overa

ll

Connecting the active boiler to the stand-by

boiler + 0 - 0 +/- 0 0 0 0 + 0 0 + - cbc19

Regular maintenance of the boiler, incinerator

and steam equipment + + - + + 0 0 0 0 + 0 0 + 0 Yes

Using the economiser on the steam boiler + 0 - 0 + 0 0 0 0 + 0 0 + - Yes

Limiting energy consumption: other energy consumption

No-load test + 0 + 0 + 0 0 0 0 + 0 0 + - Yes

Planning software in order to limit energy

consumption

+ 0 - + +/- + 0 0 0 + 0 0 + - cbc20

Insulation of pipelines and buffer tank for hot

water

+ 0 + 0 + 0 0 0 0 + 0 0 + - Yes

Recovery of heat for production of hot water + 0 + 0 0 0 0 0 0 + 0 0 + - Yes

Using a solar boiler + 0 - 0 +/- 0 0 0 0 + 0 0 + -(-) cbc

Using combined heat and power (CHP) and

trigeneration

+ 0 - 0 +/- 0 0 0 0 + 0 0 + -(-) cbc

Using a heat pump + 0 - 0 +/- 0 0 0 0 + 0 0 + -(-) cbc

19 Depending on the size of the installation and the existence of other energy measures applicable to and in relation to the steam

boiler. 20 The use of planning software presupposes that meters and a control system are present. This may well be the BAT for a new

installation. TRANSLATIO

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Technique Technical feasibility Environmental benefit

Cost

feasib

ility

&

eff

ectiveness

BAT

Pro

ven

Safe

ty

Genera

lly

applicable

Quality

Overa

ll

Wate

r

consum

ption

Waste

wate

r

odour

Waste

ra

w

mate

rials

Energ

y

Chem

icals

Impact

on

the

chain

Overa

ll

Condensing boiler + 0 0 0 + 0 0 0 0 + 0 0 + - Yes

Fermenting biomass – generating steam + 0 - 0 +/- 0 0 0 --21 + 0 0 0 -- No

Good housekeeping to limit energy

consumption + + + + + 0 0 0 0 + 0 0 + + Yes

Limiting odour emissions

Condensing the steam plume from steam

peelers + 0 - 0 +/- + 0 + 0 (+) 0 0 + -(-) cbc22

Burning frying vapours + 023 + 0 + 0 0 + 0 - 0 0 + -(-)

Yes24 Biofiltration or bioscrubbing + 0 + 0 + - - + 0 0 0 0 + -

Enclosed chilling tunnel with indirect chilling + 0 + 0 + 0 0 + 0 - 0 0 + - Yes

Transporting emissions via a high chimney + 0 - 0 +/- 0 0 + 0 0 0 0 0 - cbc25

Good housekeeping to reduce odour + 0 + 0 + 0 0 + 0 0 0 0 + 0 Yes

Limiting water consumption

21 In many cases, the biomass may be used for a high-quality application instead of for generating energy. See also the cascade chart

of value retention. 22 If steam peelers are used continuously (e.g. in the potato industry), the released heat may be used for the production of hot water,

making it possible to recoup the investment costs. This is less likely or unlikely to be the case for vegetable processing plants. 23 If the technique is installed judiciously and monitored, this will not have any negative impact on safety. 24 The installation of either of the two techniques is BAT. No judgement is made on the choice of technique. 25 Only worthwhile and useful in the case of densely populated areas, and only if no other (additional) odour removal techniques are

possible. TRANSLATIO

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Technique Technical feasibility Environmental benefit

Cost

feasib

ility

&

eff

ectiveness

BAT

Pro

ven

Safe

ty

Genera

lly

applicable

Quality

Overa

ll

Wate

r

consum

ption

Waste

wate

r

odour

Waste

ra

w

mate

rials

Energ

y

Chem

icals

Impact

on

the

chain

Overa

ll

Transporting solid materials in dry form + 0 - 0/- +/- + + 0 - 0 0 + + - cbc26

Minimising the use of shallow or deep

groundwater and maximising the use of

rainwater

+ 0 + 0 0/- +27 0 0 0 0 0 0 + - Yes

Direct re-use of water + 0 -28 0 +/- + 0 0 0 0 - 0 + - Yes

Fitting start/stop systems on the water supply + 0 + 0 + + 0 0 0 0 0 0 + - Yes

Extending the service life of water baths at the

point of cutting blades by selectively removing

white starch – potato industry

+/- 0 - 0 +/- + 0 0 0 0 0 0 + -(-) No

Re-use of water after treatment – reverse

osmosis or sand filtration

+ 0 - 0 +/- +

0 0

- 0 + -(-) cbc29 Re-use after treatment – sand filtration 0 0

Re-use after treatment – reverse osmosis -30 -

Good housekeeping – general cleaning + 0 + 0 + + 0 0 0 0 0 0 + 0 Yes

Improving the quality of discharged waste water

26 This is possible for most PVF processing plants. In some cases, vegetable residues must be washed in order to be processed further,

in which case this is an essential production stage. 27 The environmental benefit is: limiting the use of shallow or deep groundwater. 28 This technique cannot be used on every water stream. The conditions described in Chapter 4 must always be taken into account. 29 The economic effect of implementation of the measure must be weighed up. 30 This has no effect on the total discharged load, but it does affect the concentration of chlorides. TRANSLA

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Technique Technical feasibility Environmental benefit

Cost

feasib

ility

&

eff

ectiveness

BAT

Pro

ven

Safe

ty

Genera

lly

applicable

Quality

Overa

ll

Wate

r

consum

ption

Waste

wate

r

odour

Waste

ra

w

mate

rials

Energ

y

Chem

icals

Impact

on

the

chain

Overa

ll

Steam peeling of salsify (instead of lye

peeling) + 0 - 0/- +/- 0 + 0 0 0 0 0 + 0 No

Limiting phosphate discharge by potato

processors – preventive measures + 0 + 0 + 0 + 0 0 0 + 0 + - Yes

Limiting phosphate discharge by vegetable

processors – preventively by adding milk of

lime

-

/+31 0 - 0 - 0 + 0 0 0 - 0 No32

Use of environmentally friendly cleaning agents

and disinfectants + 0 + 0 + 0 + 0 0 0 0 0 + - Yes

Limiting chloride discharge – preventively by

limiting softening + 0 + 0 + 0 + 0 0 0 + 0 + -- No

Limiting chloride discharge – by using softener

pellets + 0 - 0 +/- 0 + 0 0 0 + 0 + -- No

Limiting chloride discharge – by using

nanomembranes + 0 - 0 +/ 0 + 0 0 0 0 + + -- No

Limiting chloride discharge – by removing

brine stream + 0 + 0 + 0 + 0 0 0 0 0 + -- No

31 This has been proven for a number of vegetable types. It does not work for other types. 32 The process can only be controlled if only one type of vegetable is being processed at once. In practice, multiple types of vegetables

are processed at the same time. TRANSLATIO

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Technique Technical feasibility Environmental benefit

Cost

feasib

ility

&

eff

ectiveness

BAT

Pro

ven

Safe

ty

Genera

lly

applicable

Quality

Overa

ll

Wate

r

consum

ption

Waste

wate

r

odour

Waste

ra

w

mate

rials

Energ

y

Chem

icals

Impact

on

the

chain

Overa

ll

Limiting chloride discharge – clay bath for the

potato processing industry + -33 + 0 - 0 + 0 0 0 0 0 + 0 No

Thickening slurry using a cyclone or in a pool + 0 - 0 +/- 0 0 0 + 0 0 0 + - cbc34

Correct assessment to send streams to

anaerobic treatment or fermenter + 0 + + + 0 + 0 0 0 0 0 + 0 Yes

Limiting the strain on the anaerobic treatment

or fermenter with material that is difficult to

biodegrade

+ 0 - + +/- 0 + 0 0 0 0 0 + 0 cbc35

Heating/chilling the influent of the anaerobic

water treatment + 0 - + +/- 0 + 0 0 0/- 0 0 + - cbc36

Biofermentation + 0 - 0 +/- 0 + 0 + 0 0 0 0 - cbc/N

o37

Limiting phosphate discharges – end-of-pipe

+ 0

0

0 + 0 0 0

0 +

Biological phosphate removal - -/+ 0- - cbc38

Physico-chemical phosphate removal - -/+ - -(-) cbc39

33 Due to potential contamination of the used clay with dioxins. 34 BAT for plants that process PVF straight from the soil. Not applicable to plants that accept washed PVF. 35 BAT for plants that have an anaerobic water treatment facility. 36 BAT for plants that have an anaerobic water treatment facility. 37 Only at very low flow rates. The formation of deposits on the coir must be ensured. 38 Not for sewer dischargers. 39 BAT for large plants or plants that discharge into surface water TRANSLA

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Technique Technical feasibility Environmental benefit

Cost

feasib

ility

&

eff

ectiveness

BAT

Pro

ven

Safe

ty

Genera

lly

applicable

Quality

Overa

ll

Wate

r

consum

ption

Waste

wate

r

odour

Waste

ra

w

mate

rials

Energ

y

Chem

icals

Impact

on

the

chain

Overa

ll

Removal of P and N using algae – tertiary

treatment technique - -/+ 0 --

No40

Limiting chloride and phosphate discharges by

means of precise dosing of the flocculant –

end-of-pipe

+ 0 - 0 -/+ 0 + 0 0 0 + 0 + +

cbc41

Good housekeeping for water treatment + 0 + 0 + 0 + 0 0 + + 0 + 0 Yes

General measures

Introduction of environmental management

system + + + + + + + + + + + 0 + 0 Yes

Replacing machinery in good time + + + + + + + + + + + 0 + 0 Yes

Limiting noise pollution + + + 0 + 0 0 0 0 0 0 0 +42 0 Yes

40 This technique goes beyond the BAT. 41 This technique is BAT for frozen-produce plants and large plants. 42 Positive: will limit noise pollution. Noise pollution has not been included as a separate criterion in this table. TRANSLA

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BAT-AEL Discharge data provided by the Flanders Environment Agency (VMM) for 2008 to 2014 in relation to vegetable and potato processing plants have been used to determine the BAT-AEL43. The data was divided up by plant type. Separate BAT-AEL were derived for different types of plants.

- A distinction has also been made between vegetable processors and potato

processors. Potato processors operate a continuous process, in which the

composition of the raw material remains relatively stable throughout the year.

The differences in the varieties of potato available will only give rise to limited

changes to the composition of the waste water produced. In the case of

vegetable processors that process other types of vegetables depending on the

time of year, there are greater fluctuations in the composition of the waste

water. Every transition from one type of vegetable to the next requires time for

the biological water treatment system to adjust, as a result of which effluent

concentrations of various parameters may temporarily increase. For that reason,

two BAT-AEL are determined for the vegetable processors: one for the

maximum concentration, and one for an annual average value. With the

exception of the parameter P (see below), BAT-AEL were only determined for

the maximum concentrations for potato processors.

- A distinction is made within the potato processors group between frozen-

produce plants and processors of fresh potato products. These plants differ in

their procedures, which results in a different composition of the waste water.

There is also a difference in terms of scale, which enables larger plants (frozen-

produce plant type) to implement end-of-pipe measures, which in turn makes

for a favourable composition of the discharged waste water.

- A distinction is made within the vegetable processors group between frozen and

preserved food plants and prepared fruit and vegetable plants. The same

reasoning applies here as for the potato processors: there is a difference in

process and a difference in scale, which accounts for differentiated BAT-AEL.

- As only limited data sets were available from wholesalers (both of vegetables

and potatoes), it was not possible to determine the BAT-AEL for these plants.

As the study featured only one preserved food plant and only one crisp-producing plant, these data were not included separately in the study. The data were examined against those of the frozen-produce plants and of the frozen potato plants, however. For the purposes of dividing up the data, we used information from the websites of Vegebe and Belgapom, combined with information from the plants’ websites and information from LNE and VMM. This analysis has shown that certain plants also carry out other activities (e.g. catering). The data from plants with a different activity (that affects the waste water issue) were excluded from the analysis. In addition, a distinction was made between discharge data from plants that discharge into surface water and plants that discharge into sewers. This classification was based on information from the VMM database. In order to determine BAT-AEL for discharging into surface water, the analysis used data from plants that discharge directly and indirectly into surface water. The analysis showed that the discharge data from certain plants labelled “indirect discharger” still did not fulfil expectations. More specifically, it was possible to deduce that these plants potentially did not possess a water treatment facility that could be expected of a plant that discharges into surface water44. The data from these plants were removed from the analysis for surface water dischargers.

43 An overview of all data has been compiled in Annex 4. 44 The status of indirect surface water discharger means that the plant’s situation with regard to discharging will change in the future. The plant will be disconnected in the future (and will have to discharge into surface water) or the plant will be connected to the public sewer network in the future.

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Apart from these data manipulations, outliers were also excluded from the analysis. It is not so much cleaning up the statistics, but more of an expert judgement by VITO in consultation with VMM and LNE, whereby it was decided that certain values did not reflect reality. From the perspective of BAT, the following data were removed in relation to surface water dischargers:

- data related to suspended solid concentrations greater than 60 mg/l;

- data related to BOD concentrations greater than 25 mg/l;

- data related to ammonium values greater than 5 mg/l (current standard for

potato processors). The EPAS study (Desmet et al., 2005) confirms that these

values are feasible for the vegetable processing sector.

The first set indicates a poor separation of water and suspended particles, which will also affect the parameters COD, BOD and metals. This can be avoided by correctly applying the BAT. The second indicates a poorly functioning biological treatment facility, which is regarded as the BAT for all surface water dischargers. This will also have an effect on the parameters COD and N. The third set indicates a poorly functioning nitrification facility, which will also affect the parameter Ntot. Differentiated BAT-AEL were derived on the basis of this analysis and these are listed in the following tables. Annex 4 contains figures of the original and cleaned-up data sets. Potato processors The figures from the plant that produces crisps from potatoes were examined against those of frozen-produce plants, and the BAT-AEL could be set at the same level. There was too little background information to separate the data from processors of fresh potato products from those from wholesalers of potatoes, and consequently the figures contain data from both groups. The proposed BAT-AEL only relate to the processors, however. BOD The average BOD concentration of the frozen potato plants lies below the classification criterion (6 mg/l). The maximum measured value lies well below the value that is being proposed in the BREF. Based on the analysis on the Flemish frozen-produce plants, the BAT-AEL is < 25 mg/l (maximum concentration).

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Figure 1: COD, BOD and SS concentrations from frozen-produce plants (potatoes)

processed according to the method for determining the BAT-AEL.

The BAT-AEL for processors of fresh potato products is < 25 mg/l (maximum concentration).

0,

50,

100,

150,

200,

250,

300,

350,

0,

10,

20,

30,

40,

50,

60,

70,

80,

90,

100,

CO

D (

mg/

l)

SS, B

OD

(m

g/l)

ZS BZV CZV

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Figure 2: COD, BOD and SS concentrations from potato wholesalers and processors of

fresh potato products processed according to the method for determining the BAT-AEL.

COD The frozen potato plants have an average COD that lies just above the classification criterion (< 30 mg/l). Based on the analysis of the Flemish frozen-produce plants, the BAT-AEL is < 100 mg/l (maximum concentration). The BAT-AEL for COD for processors of fresh potato products is < 125 mg/l (maximum concentration). SS As stated earlier, it was assumed that with a properly functioning treatment facility, it is possible to limit suspended solid concentration to < 60 mg/l (= BAT-AEL for the maximum concentration). Ntotal

The frozen potato plants have an average Ntot that lies well above the classification criterion. The value of 10 mg/l proposed in the BREF is not being achieved in practice45. These high Ntot values may be attributed to poor nitrification (conversion of ammonium into nitrate) or denitrification (conversion of nitrate into nitrogen), which may indicate problems in the water treatment facility. However, it is not possible to filter out data linked to potentially poorly functioning treatment facilities entirely from the data set. For that reason, it has been assumed in determining the BAT-AEL that these values are unique to the sector. Based on the analysis of the Flemish frozen-produce plants, the BAT-AEL is < 20 mg/l (maximum concentration).

45 The BREF FDM only gives an indicative value. These have not been based on

measurements and the averaging period has not been specified.

0

50

100

150

200

250

300

350

400

0

10

20

30

40

50

60

CO

D (

mg/

l)

SS a

nd

BO

D (

mg/

l)

ZS BZV CZV

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Figure 3: COD, Ntot and Ptot concentrations from frozen-produce plants (potatoes) processed according to the method for determining the BAT-AEL.

The BAT-AEL for Ntotal for processors of fresh potato products is < 15 mg/l (maximum concentration).

0,

50,

100,

150,

200,

250,

300,

350,

0

5

10

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Figure 4: COD, Ntot and Ptot concentrations from potato wholesalers and processors of fresh potato products processed according to the method for determining the BAT-AEL. These concern direct dischargers.

Ptotal46

The frozen potato plants have an average Ptot that lies well above the classification criterion (0.14 mg/l). The value of 0.4 to 5 mg/l proposed in the BREF47 is not always being achieved in practice. The removal of phosphate is a physico-chemical process, in which the dosing of chemicals will determine the efficiency of treatment. The highest phosphate concentrations are linked to under-dosing of chemicals in the water treatment plant. Based on the current discharge data, the BAT-AEL is < 10 mg/l (maximum value) and < 2.5 mg/l (annual average value). It was not possible, however, to filter out the effect of the use of BAT of BAT 4.10.16 (Beperking van de chloride- en fosfaat lozing door precieze dosering van het vlokmiddel – end-of-pipe) from the data set. It is expected that the consistent use of this technique will make it possible to achieve lower maximum concentrations in this sector. It is therefore possible to opt for a lower standard for the maximum concentration when implementing the BAT-AEL into the VLAREM Regulation. This is a policy choice. The BAT-AEL for Ptot for processors of fresh potato products is < 10 mg/l (maximum concentration) and < 2.5 mg/l as the annual average value. The tables below summarise the measured emissions and the BAT-AEL for potato processing plants.

Table 2: measured emissions for the potato processing plants based on the VMM data,

processed according to the principle of BAT-AEL

Surface water dischargers

potato-processors – frozen wholesalers and processors of fresh potato products

mean median max. mean median max.

BOD mg/l 4 3 16 6 5 19

COD mg/l 40 33 290 80 54 350

N total mg/l 14 6 210 11 7 83

P total mg/l 5.9 1.6 70 5 2 48

Suspended solids

mg/l 12 6 60 15 15 55

46 Belgapom does not agree with this section. Their comments have been included in

Annex 5. 47 The BREF FDM only gives an indicative value. These have not been based on

measurements and the averaging period has not been specified.

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Table 3: BAT-AEL for potato processing plants48

curr

ent

sect

ora

l

dis

char

ge

con

dit

ion

s: s

urf

. w

ate

r/se

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B

REF

: BA

T-A

EL*

gen

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con

dit

ion

s o

r IC

GS

BAT-AEL for surface water dischargers

frozen-produce plants and crisp producers

processors of fresh potato products

BOD mg/l 25 < 25 6 (1) < 25 < 25

COD mg/l 200 < 125 30 (1) < 100 < 125

N total mg/l < 10 2.4 to 4 (2)

< 20 < 15

P total49 mg/l < 0.4-4 0.14 (2) < 10 (maximum concentration) < 2.5 (annual

average concentration)

< 10 (maximum concentration) < 2.5 (annual

average concentration)

Suspended solids

mg/l < 60 60 < 60 < 60

* The BREF FDM dates back to 2005. With regard to these values, the BREF notes that they concern indicative values, which can be achieved using the BAT described in the BREF. They do not necessarily reflect the emission levels currently (in 2005) being achieved, but are based on expert judgement by TWG. The BREF does not state which averaging period the BAT-AEL relate to. 1: as 90th percentile value 2: mid-summer average 3: dependent on the receiving water

Vegetable processors BOD The average BOD concentration of the frozen-produce plants lies below the classification criterion of < 6 mg/l. Despite this, higher values are being frequently measured that cannot be linked to specific circumstances. Based on the analysis of the Flemish frozen-produce plants, the BAT-AEL is < 6 mg/l (annual average) and < 25 mg/l (maximum concentration).

48 Belgapom does not agree with the value for Ptotal. Their comments have been

included in Annex 5. 49 It is possible to opt for a lower standard for the maximum concentration when implementing the BAT-AEL into the VLAREM Regulation. This is a policy choice.

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Figure 5: COD, BOD and SS concentrations from frozen-produce plants (vegetables) processed according to the method for determining the BAT-AEL.

Ninety-five percent of all measured results from the prepared fruit and vegetable plants and the preserved foods sector lie below the classification criterion for BOD (6 mg/l). Based on the analysis of the Flemish prepared fruit and vegetable plants and preserved foods sector, the BAT-AEL is < 25 mg/l (maximum concentration).

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Figure 6: COD, BOD and SS concentrations from prepared fruit and vegetable plants processed according to the method for determining the BAT-AEL.

COD The COD values of the frozen-produce plants fluctuate significantly, depending on the conditions and the vegetables processed. Based on the analysis of the Flemish frozen-produce plants, the BAT-AEL is < 70 mg/l (annual average) and < 125 mg/l (maximum concentration). Apart from when salsify is being processed, the BAT-AEL during the period 1 January to 30 April is < 300 mg/l (maximum value). The increase in the BAT-AEL for the maximum concentration does not provide any reason to change the BAT-AEL for the annual average. The data set from the prepared fruit and vegetable plants and the preserved foods sector is too limited to enable the fluctuations in the COD to be linked to specific conditions. Based on the analysis, the BAT-AEL is < 125 mg/l (maximum concentration). SS As stated earlier, it was assumed that with a properly functioning treatment facility, it is possible to limit suspended solid concentration to < 60 mg/l (= BAT-AEL for the maximum concentration). Ntotal

The frozen-produce plants and preserved food sector have an average Ntot that lies well above the classification criterion (< 4 mg/l). The value of 10 mg/l proposed in the BREF is not always being achieved in practice. High Ntot values can be attributed to poor nitrification (conversion of ammonium into nitrate) or denitrification (conversion of nitrate into nitrogen), which may indicate problems in the water treatment facility. The pre-conditions for effective processing can be found in Section 4.10.17 and in the guide to water treatment techniques(Derden et al., 2010). Based on the analysis of the Flemish frozen-produce plants, the BAT-AEL is < 10 mg/l (annual average) and < 15 mg/l (maximum concentration). Under specific conditions, a higher BAT-AEL has been proposed

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for the maximum concentration. These do not give any grounds for changing the value for the average annual concentration.

Specific conditions BAT-AEL

Processing of leafy vegetables (start-up period) – 1 April to 31 May < 30 mg/l

Processing of peas (start-up period) – is not possible in combination with a deviation for leafy vegetables – 1 June to 15 July

< 30 mg/l

Figure 7: COD, Ntot and Ptot concentrations from frozen-produce plants (vegetables) processed according to the method for determining the BAT-AEL

Wildly fluctuating total nitrogen values were measured in the prepared fruit and vegetable plants. Due the limited data set, it is not possible to link the high values to the type of nitrogen (Kjeldahl, ammonium, nitrite, nitrate). Based on the data set, the BAT-AEL has been set at < 30 mg/l (maximum concentration).

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Figure 8: COD, Ntot and Ptot concentrations from prepared fruit and vegetable plants processed according to the method for determining the BAT-AEL.

Ptotal

The frozen-produce plants and preserved food sector have an average Ptot that lies well above the classification criterion (0.14 mg/l). The value of 0.4 to 5 mg/l proposed in the BREF is not always being achieved in practice. The removal of phosphate is a physico-chemical process, in which the dosing of chemicals will determine the efficiency of treatment. The highest phosphate concentrations are linked to under-dosing of chemicals in the water treatment plant. Based on the current discharge data, the BAT-AEL is < 3 mg/l (annual average) and < 10 mg/l (maximum concentration). It was not possible, however, to filter out the effect of the use of BAT 4.10.16 (Beperking van de chloride- en fosfaat lozing door precieze dosering van het vlokmiddel – end-of-pipe) from the data set. It is expected that the consistent use of this technique will make it possible to achieve lower maximum concentrations in this sector. It is therefore possible to opt for a lower standard for the maximum concentration when implementing the BAT-AEL into the VLAREM Regulation. This is a policy choice. It is also the case in the prepared fruit and vegetable plants that phosphate discharges can be kept under control by means of physico-chemical treatment. Based on the analyses, the BAT-AEL is the same as for the frozen-produce plants. Overview The tables below summarise the measured emissions and the BAT-AEL for vegetable processing plants.

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Table 4: measured emissions for the vegetable processing plants based on the VMM

data, processed according to the principle of BAT-AEL

Surface water dischargers

frozen produce prepared fruit and vegetables

mean median max. mean median max.

BOD mg/l 5 4 22 3 3 9

COD mg/l 61 50 290 33 29 103

N total mg/l 8 5 72 11 4 72

P total mg/l 3 2 28 2.3 1.4 11.5

Suspended solids

mg/l 14 10 56 10 7 42

Table 5: BAT-AEL for vegetable processing plants

sect

ora

l d

isch

arge

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ate

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wer

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: BA

T-A

EL*

gen

era

l

con

dit

ion

s o

r IC

GS

BAT-AEL for surface water dischargers

frozen produce plants prepared fruit and vegetables

annual average

maximum concentration

annual average

maximum concentration

BOD mg/l 25 < 25 6 (1) < 25 < 25

COD mg/l 200 < 125 30 (1) < 70 < 125 (300**)

< 125

N total mg/l < 10 2.4 to 4 (2)

< 10 < 15 (30***)

< 30

P total50 mg/l < 0.4-4

0.14 (2) < 3 < 10 < 3 < 10

Suspended solids

mg/l < 60 60 < 60 < 60

* The BREF FDM dates back to 2005. With regard to these values, the BREF notes that they concern indicative values, which can be achieved using the BAT described in the BREF. They do not necessarily reflect the emission levels currently (in 2005) being achieved, but are based on expert judgement by TWG. 1: as 90th percentile value 2: mid-summer average 3: dependent on the receiving water ** only when processing salsify, during the period 1 January to 30 April *** only when processing leafy vegetables (start-up period: from 1 April to 31 May) of when processing peas (start-up period: from 1 June to 15 July), deviations cannot be used in combination with one another

Proposal for sectoral discharge standards Table 6 below contains a proposal for sectoral discharge standards based on the BAT-AEL shown in Table 3 and Table 5. Table 6: Proposal for sectoral discharge standards for PVF processing plants that discharge into surface water

50 It is possible to opt for a lower standard for the maximum concentration when implementing the BAT-AEL into the VLAREM Regulation. This is a policy choice.

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Potato processors51

Vegetable processors

frozen-produce plants and crisp producers

processors of fresh potato products

frozen produce plants

prepared fruit and vegetables

mg/l annual average value

maximum concentration

annual average value

maximum concentration

annual average value

maximum concentration

annual average value

maximum concentration

BOD 25 25 25 25

COD 100 125 70 125 (300)1

125

N total 20 15 10 15 (30)2 30

P total52

2.5 10 2.5 10 3 10 3 10

Suspended solids

60 60 60 60

Conditions for the values between brackets: 1: Whenever the plant processes salsify, the maximum value is increased to 300 mg/l for the period from 1 January to 30 April. The increase in the maximum value does not provide any reason to change the BAT-AEL for the annual average. 2: During the start-up of the leafy vegetable or pea season, the permitted maximum is increased to 30 mg/l. There are two possible options: (a) during the processing of leafy vegetables, from 1 April to 31 May OR (b) during the processing of peas, from 1 June to 15 July. Plants may only avail themselves of one of the proposed deviation periods, but not a combination of both. The increase in the maximum value does not provide any reason to change the BAT-AEL for the annual average.

A proposal for BAT-AEL for wholesalers was not developed due to the absence of discharge data. Recommendations for monitoring Whenever annual averages are included in the VLAREM regulation, a uniform measuring method must also be included. A range of measurement or calculation methods can be used to determine the annual average. The proposal below already forms part of the specific environmental permit conditions of various plants. The annual average is the progressive arithmetic average of the available analysis results from the previous twelve months. The analysis results are these results from the waste water levy scheme and the 24 samples from the mandatory self-testing programme. The self-testing programme consists of sampling in proportion to the flow rate and the analysis of the effluent in accordance with Article 4.2.5.2 of the VLAREM II regulation. The sampling and the analysis may be conducted by the operator or by an accredited laboratory. If the sampling is conducted by the operator, the first samples from the even months (February, April, June, ...) must be taken and analysed by an accredited laboratory. The samples are taken according to the frequency below and on the proposed dates, or the day after if the date in question falls on an official public holiday. month 1 1st Wednesday and 3rd Saturday of the month month 2 1st Monday and 3rd Thursday of the month month 3 1st Friday and 3rd Monday of the month

51 Belgapom does not agree with the value for Ptotal for the potato processing plants.

Their comments have been included in Annex 5. 52 The proposal for P is based on the current measurement data. It is expected that using BAT 4.10.16 (Beperking van de chloride- en fosfaat lozing door precieze dosering van het vlokmiddel – end-of-pipe) will make lower P values feasible. It is therefore possible to opt for a lower P standard. This is a policy choice.

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month 4 1st Wednesday and 3rd Thursday of the month month 5 1st Wednesday and 3rd Tuesday of the month month 6 1st Monday and 3rd Thursday of the month month 7 1st Friday and 3rd Monday of the month month 8 1st Wednesday and 3rd Tuesday of the month month 9 1st Wednesday and 3rd Sunday of the month month 10 1st Wednesday and 3rd Tuesday of the month month 11 1st Monday and 3rd Saturday of the month month 12 1st Friday and 3rd Monday of the month The results must be forwarded to the Flemish Environment Agency within 30 days of taking the samples and must be kept available by the Environment Inspectorate. It is only feasible to impose the aforementioned monitoring regime on plants with sufficiently large turnover. From the perspective of BAT, we consider this feasible for frozen-produce, preserved food and crisp plants. With regard to plants that carry out reverse osmosis on their waste water with the aim of reducing water consumption, the number of measurements must be sufficiently representative. Sampling during dry periods combined with high activity levels may affect the average. It is a matter of policy choice to regulate this specific issue on the basis of the VLAREM regulation or on the basis of the special environmental permit conditions. This issue has been described in this study in the section on indicative reference volumes (1.1.1).

1.1.1 Recommendations for special permit conditions

Not all BAT lend themselves to direct translation into environmental legislation. However, it may well be useful for the permitting authority to also take account of other measures in the permit, and to impose special permit conditions in this regard if required. The sections below describe in detail a proposal for

- chloride standards depending on specific conditions

- the effect of water-saving measures on discharge standards

- areas for attention in relation to raw materials, auxiliary substances and waste

substances

- areas for attention in relation to water quality (sensitive watercourses, additional

discharge parameters).

Issue of chlorides versus phosphates for frozen-produce plants, preserved

foods plants and crisp plants

Annex 3 examines the associated issue between chlorides and phosphates. Depending on the desired water quality of the receiving water course and the dilution factor (this being the ratio between the discharged flow rate and the flow rate of the water course), different standards are desirable with regard to phosphates and chlorides. Water consumption will decrease as a result of using the BAT “Re-use of water after treatment – reverse osmosis or sand filtration”. This may have an impact on the discharged P and chlorides concentrations.

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Table 7: BAT-AEL for chlorides depending on the technology used and required P

concentration.

P-concentration without reverse osmosis with reverse osmosis

max.: 10 mg/l 1000 mg/l 2000 mg/l

max.: 5 mg/l 2000 mg/l 5000 mg/l

average: 2 to 3 mg/l (1) 2000 mg/l 5000 mg/l (1) In the case of a maximum value and an average value, this must be followed by the average value

in relation to the chloride standard.

If lower phosphate or chloride standards are desired, then technologies other than BAT must be used.

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1.2 Material and energy streams in the chain

The PVF sector is inextricably linked to a number of other sectors in the product chain. Energy and material streams are exchanged within this chain and the output of one sector forms the input for another. The source of environmental issues that arise in one sector may be found in another sector (which also determines their solution). With a view to making the economy greener, it is extremely important not only to devote attention to the direct environmental impact of the sector, but to also take account of the interactions in the chain. An overview of the energy, water and material streams of which the production of vegetables, potatoes and fruit forms part, is shown in Figuur 43. This overview may be regarded as a general representation. Additional specific streams may also arise that have not been included in it. By charting these energy, water and material streams, we gain an insight into how the sector is connected with other sectors, where loops can be closed, and how certain environmental issues can be resolved in the interaction between sectors.

1.2.1 Degree of loop closure

At first glance, the materials loop appears to be closed. However, this is not the case if the aspects of location and time are taken into account.

- A variety of fertilisers are manufactured on the basis of ores and oil, and these

are not replenished.

- In addition, energy is used from fossil fuels, which are finite.

- An excess of (useful) nutrients (carbon, nitrogen, phosphorus) is removed or

broken down in the water treatment facility and these substances are not fed

back to the chain. Another part ends up in watercourses and results in pollution

of surface water.

1.2.2 Environmental issues in other sectors whose causes are found in the

PVF processing sector

- Drying up and salinisation of ground water as a result of high water

consumption.

1.2.3 Environmental issues in the PVF sector whose causes are found in

other sectors

- The use of pesticides results in contamination of the waste water used by the

PVF processing plants (see 3.14.2).

- The use of trace elements in feed for animals whose dung is used for the

cultivation of PVF results in contamination of waste water (see 1.3.1).

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1.3 Measures within the chain

The study in Chapter three, and more specifically section 1.2 show that some environmental issues are caused by activities that precede those of the food industry. These problems can be more effectively tackled within other sector studies or at a higher level.

1.3.1 Limiting copper and zinc in animal feed

description of measure

Pigs, cattle and calves need copper and zinc for growth and development. These elements are added to the compound feedstuffs for these animals. In order to be certain that the animals take in sufficient quantities of these elements, an excess amount is added to the feedstuffs. Measurements have shown that only 10% of the added copper and zinc are removed via the meat. The rest of the copper and zinc is excreted and some of it ends up in the manure (NN, 2008). Limiting the copper and zinc in feedstuffs will have a favourable effect on the composition of the manure that is later used as fertiliser on fields in which vegetables and potatoes are grown. If the manure contains lower levels of copper and zinc, the crops that are grown on these fields will also contain less copper and zinc. As a result, it is less likely that excessive concentrations of copper and zinc will be found in the waste water of PVF processing plants.

place within the chain

Agriculture: livestock production.

1.3.2 Supply of soft water by suppliers of mains water or grey water

description of measure

Section 3.10 shows that the hardness of the water used by PVF processors for their production process will determine the chloride concentration in the waste water. The chloride concentration will decrease if soft water is supplied to these plants (but also other plants). If drinking water or grey water is produced from hard water, it is better to soften it centrally at sites where increased salt concentrations have No harmful effects upon the receiving watercourse.

place within the chain

Drinking water producers.

1.3.3 Reuse of waste water in other sectors

description of measure

One line of thinking is the use of waste water from PVF plants in farming. Farms that produce PVF need to pump up ground or surface water during dry spells in order to meet their needs. The

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pumping up of (deep) groundwater is generally not desirable, because these water layers are already under pressure. Vegetable processing plants discharge effluent water throughout the year. These flow rates are greatest during the months of most intensive activity: spring and summer. These plants often discharge into small watercourses, in which case the discharged flow rate is often greater than that of the watercourse. The vegetable processing plants are usually located in the area surrounding farms that supply to the PVF sector. By linking the demand for water of one to the supply of another, we create a win-win situation throughout the chain.

place within the chain

Agriculture: crop production.

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