ecogi pre- f biom ass for anaerobic - danetv - the danish ... · f biom and separ or biogas 2013...
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ECOPre-dige Mechaindust
Testr J.no.
VersionRevise
OGI -treatmestion anical pretry to obta
report
1004
n 1, Feb 12d version 5
ment o
treatment in a pulp f
2th 2013 5, may 6th
of biom
and separfor biogas
2013
mass f
ration of osification
for ana
organic wa
aerobi
aste from
ic
househollds and
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Table Intr1.
1.1. 1.2. 1.3. 1.4.
Tes2. 1.5.
1.51.51.5 1.6.
1.61.61.61.61.61.61.61.61.6
Tes3. 1.7. 1.8. 1.9. 1.10.
Ref4.AppeAppeAppe
of conteroduction ...
Name andName of tReferenceDeviation
st design ....Test site ..
.1. Type
.2. Addr
.3. DescrTests .......
6.1. Test m6.2. Test s6.3. Test s6.4. Test e6.5. Type6.6. Oper6.7. Oper6.8. Techn6.9. Healtst results ....
Test data Test PerfoTest quali
Ammenferences .....
endix 1 Tendix 2 Tendix 3
ents ..................
d contact of test centre/te to test planns to test pla....................................
es of test siteresses .........riptions ........................methods ....staff ...........schedule ....equipment .
e and numbeation conditation measunology maith, safety an..................summary ...
ormance obity assurancndments to ..................
Terms and dTest data repAmendmen
..................f proposer ...test responsin and specifan ...................................................es .............................................................................................................................................
er of sampletions ..........urements ....ntenance ....
nd wastes .......................................servation ...
ce summaryand deviatio..................
definitions .port ...........
nt and devia
...................
...................ible ............fic verificat.................................................................................................................................................................................................................es ....................................................................................................................................................
y incl. audit ons from te.........................................................ations repor
...................
...................
...................tion protoco.........................................................................................................................................................................................................................................................................................................................................................................results .......st plan .................................................................t for test .....
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2
4 4 4
7 7 7 7
9 9 0 0 0 0 0
4
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Intr1.This tesenvironguidelin
Na1.1. Propose KomtekContact
Na1.2.Danish DK-800Test resbmh@teInternallbfh@te
Re1.3.The testThe ver
De1.4. There wdescribe
Tes2.The testwaste in
• R• P• E• W
1 Organicapprox. 2mm are n
roductiost report is thnmental technes in EU ge
me and co
er
k Miljø af 20t: Bjarne La
ame of tesTechnologi
00, Aarhus, sponsible: Beknologisk.l reviewer: Leknologisk.d
ference tot plan is titlerification pr
viations towere minor ed in part 1.
st designt design is bn order to ev
Recovery oPurity of orEnergy conWater cons
c matter is def25-30 days of not included as
on he result of
hnology folleneral verif
ontact of p
012 A/S, Drarsen, phone
st centre/teical InstituteDenmark.
Bjørn Malmg.dk. Lotte Bjerrudk
o test planed: Ecogi, Totocol is tit
o test plandeviations .10.
n based on 3 rvaluate the
of organic mrganic mattensumption pumption pe
fined as materimesophilic ops they are not
f a test carrielowing the Efication prot
proposer
rivervej 8, De: +45 7020
est respone, Verificati
gren-Hanse
um Friis-Ho
n and specTestplan J.nled: Ecogi,
n of the meth
repeated tescustomer cl
matter for bioer for biogaer ton waste
er ton waste
ial which can peration and 1considered di
ed out for vETV methotocol versio
DK 6670 H0 54 89, e-m
nsible ion Centre,
en (BMH), p
olm (LBFH)
cific verifino.1004
Verification
hod in the te
t runs of thelaims conce
ogas producas productioe
be converted 18-21 days of igestible withi
verification ood. The formon 1.0 Decem
Holsted mail: Bjarne@
Life Scienc
phone: +45
), phone: +4
cation pro
n Protocol J
est plan for t
e ECOGI foerning the fo
ction1 in pun in pulp
into biogas wthermophilic in a normal op
of the perfomat used formber 15th 20
@komtek.d
ce Division,
72201810,
45 7220183
otocol
J.no.1004
the sorting p
or each of twollowing iss
lp
within a normaoperation . Wperation perio
ormance of r reporting f011.
dk
, Kongsvang
e-mail:
37, e-mail:
procedure a
wo differentsues:
al period of opWood pieces ofod in a biogas
3
an follows
g Allé 29,
as
t kinds of
peration f size >5*5*5 plant.
3
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The two
1. O2. F
Every teone test
Figure 1 CalculaPurity oRecoveRecover
Tes1.5.The test
1.5.1. The siteusing th
1.5.2. Test sit
o types of wOrganic fracFood waste f
est run const run sample
: test runs an
ation of purof biopulp isry of biopury of biopul
st site t site is Kom
Types of tee is a plant phe develope
Addresseste
waste are: ction from hfrom superm
sists of 3 bae (Figure 1)
nd sampling f
rity: s calculatedulp: lp is calcula
mtek A/S, D
est sites performing d ECOGI p
s
household wmarket 25 %
atch runs. Th. Three tons
for the two wa
d as given in
ated as given
Drivervej 8,
compostingrocess.
waste Vejle %, 25% dair
he samples s waste is p
aste types
n appendix 3
n in append
DK 6670 H
g operation
Kommune ry waste and
taken underrocessed pe
3
dix 3.
Holsted
with a sepa
(waste sortid 50% of (1
r the 3 batcher batch.
arate treatme
ing system)1)
hes are com
ent of organ
4
.
mbined to
nic waste
4
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Komtek
1.5.3. The ECbuildingseparate
Tes1.6.
1.6.1. Measurethe ECOtaken fr
Figure 2 • M1
• M2
• M3
• M4
Fee
Pure
Waste
M1
k Miljø af 20
DescriptioCOGI plant ig including ely from oth
sts
Test metho
ement of reOGI shown rom some of
Mass flows i
weight
weight (usi
weight (usi
weight will
eder
water
e
M2
012 A/S, Dr
ns is placed in necessary v
her facilities
ods
ecovery and in Figure 2f the mass f
in test
ing FT1 - flo
ing FT1 - flo
l decrease d
Pulper
FT1
2 for filling
rivervej 8, D
a separate cventilation is at Komtek
purity is ba and analys
flows.
ow transmit
ow transmit
during transp
Rejseparwas
M3 for
DK 6670 H
closed buildis run by elek.
ased on measis of a num
tter)
tter)
port for dra
ect-rator/hing
Collecti
r washing
FT
Holsted
ding at Komectrical pow
asuring all mmber of param
ainage
ion of washi
M4
V
T2
mtek. All equwer which ca
mass flows meters of re
Storage-tank
ing water M
Dewatering
quipment in an be logge
during operepresentativ
Soli
Pulp f
7
g
M5
M6
5
the ed
ration of ve samples
d fraction
for biogas
5
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• M5 sam
• M6 cont
• M7 samrese
The elecis operahall. Basicallsection Biopulp This tessample sieve. T Organi This tesbeing w Automafollowinsubsampmatter. Organifrom coThis tesbalancebecausestep and The TS The test
weight wimpled repres
weight, retent in biopu
volume (bymples will beervoir after e
ctricity conating in, bef
ly three test0 for detaile
p purity tes
st determineby sieving t
The inorgani
ic content t
st determinewashed of th
atic washingng filtrationples will be
ic content inollection tast determine reasons on
e the washind thus the co
(Total Soli
t methods a
ll be recorentatively f
epresentativulp.
y height meae taken aftereach test run
sumption isfore and afte
ts are perfored descripti
st (samplin
es the puritythe biopulpic residue is
est in solid
es the loss ohe solid frac
g in a specian in order toe dried, man
n washing nk)
es the organnly and will ng water is rontent of or
ds) and VS
are described
rded after dfor organic c
e sampling
asurement ir each test rn.
s measured ber every test
rmed on theion of the te
g position V
y of the biop, flushing ws dried and w
fraction (s
of organic mtion in the E
ally designe determine
nually sorted
water (sam
nic residue innot be inclurecycled to rganic matte
(Volatile S
d in detail in
drainage, 60content test
g of each b
in tank) beforun while pu
by reading t run. The E
e samples taests and sam
V)
pulp by sortwith warm wweighed.
sampling p
matter in theECOGI pro
ed washer isrest organicd for organi
mpling posit
n the washiuded as lossthe pulper i
er is not lost
Solids) is an
n appendix
0 liter of tt
batch while
fore and afteumping the
the electriciECOGI is th
aken out durmpling:
ting the inorwater and ha
osition M 5
ECOGI process.
s performedc matter in tic/inorganic
tion V duri
ing water. Ts of organicin normal opt.
nalysed from
3 of the tes
the solid fr
e pumping
er a test run.washing wa
ity-meter ofhe only oper
ring test for
rganic residand sorting
5)
ocess, whic
d repeatedlythe solid frac matters an
ing recircu
This test is pmaterial in
peration for
m representa
t plan.
raction per
for test of
. Representater out of t
f the hall, thrating mach
r one waste
dues out of tof organic r
ch is the biop
y on the soliaction. The nd analysed
ulation of co
performed fon our calcular reuse in ne
ative sample
6
test run is
f anorganic
ative the
he ECOGI hine in this
type, see
the biopulp rests on the
pulp not
d fraction
for dry
ontent
or mass ations, ext pulping
es.
6
s
c
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1.6.2. The testBjørn MSabine L
1.6.3. Task
Applicati
Verificati
Test
Analysis
Test repo
Verificati
Verificati
1.6.4. The testdifferensmall shplant. F
1.6.5. The typ sample
biosolid
Collec
In generwas use SamplinThe maiis stuckbucket i PreparaIn all sumaterial
Test staff t staff is
Malmgren-HLindholst (S
Test sched
ion definition
ion protocol w
phase
orting
ion
ion report
Test equipt equipment
nt mesh sizehovels, dryior further d
Type and npes and num
opulp fraction
ction tank
ral the folloed.
ng of mainin samples
k in the valvis used for s
ation of sububdividing ol may float
Hansen (BMSBL)
dule
document
with test plan
pment t includes bes, small whng ovens, c
details see A
number of mber of samp
Sampposit
VMV
owing practi
n sample froare taken frve. Before sampling th
bsamples of samples or sink.
MH) SS
Timing
August 201
November 2
December 2
December 2
January 201
January 201
April 2013
esides the Eheel loader, oncrete mix
Appendix 3 i
samples ples per typ
pling tion
V M5 V
ise for samp
om inlet anrom valves wobtaining te main sam
care was ta
Sampling, dSampling, a
12
2012
2012
2012-january 2
13
13
ECOGI sampitch-fork,
xer with attain the test p
pe of waste a
Numbebatch sam
9
pling, subsa
nd outlet with sufficithe sample
mples. For de
aken to prod
data analysisanalyses, da
2013
mpling contasorting tablached 40 m
plan.
are summar
r of mples
N
ampling and
ient dimensiat least 2 letails see Ap
duce represe
s and reportta analysis,
ainers, buckle with drainm sieve, we
rized in the
Number of samples
3 3
d sample han
ion (1”) to eitres are disppendix 3 in
entative sub
ting (TI) reporting (
kets, sieves wn for water eights, flow
following.
test s
Nusamw
ndling of su
ensure that scarded. A in Test plan
bsamples as
7
TI)
with collection,
wmeters in
umber of mples per aste type
3 3 3
uspensions
no material10-15 litre
.
some fibre
7
l e
e
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Dependfollowin
1) Ht
2) Ip
Used MIn the temethod All othe HandlinAll fibrlater ana
Used prSolid frthere be
1.6.6. Before efrom theand outp
1.6.7. • T• W
1.6.8. The testin the te
1.6.9. While teof splascontaineperform
ding on typeng way: Homogenioto subsampInhomogenperformed f
Methods ests the biopwas also us
er sampled m
ng of sampre material walysis.
reservation action samp
efore VS an
Operation
each test rue previous oput waste w
Operation Total powerWater consu
Technologt is a short test.
Health, saf
esting, the pshes and if ner. Based on
med without
e of the hom
ous pulps: ale
nious pulpsfollowed by
pulp was vesed for wash
material wa
ples was refriger
and storagples were tralysis.
conditions
n of waste, operation co
was emptied
measuremr consumptioumption dur
gy maintenterm perform
fety and wa
personal wenecessary brn low tempebreathing p
mogeneity o
a subsample
s with floatiy proportion
ery homogenhing water i
as solid.
rated if test
ge of sampleansported to
s
the whole sould be obse
d. Each batch
ments on during trring treatme
ance mance test o
astes
ears a protecreathing proeratures durprotection.
of the bioma
e was made
ing layers onal weigh of
nious and cin the sortin
ts were perf
es: o Danish Te
system waserved any loh test uses 3
reatment waent was reco
of 2-3 days.
ctive suit anotection. Thring test (0-
ass pulp the
e by stirring
or fast sinkf solid and l
ould be subng step.
formed with
echnologica
flushed witonger. Furth30 minutes
as recordedorded
. Maintenan
nd gloves, sahe waste can5ºC) it was
e subsample
main samp
king layers: liquid fracti
bsampled us
hin 2-3 day
al Institute d
th clean wather all convpulping.
nce requirem
afety glassen be deposit
decided tha
es were obta
ple well dur
Sieving ofions into sub
sing method
ys or freeze
directly and
ter until no veyers for so
ments are no
es in case thted in a genat sorting co
8
ained in the
ing transfer
f fibres wasbsamples.
d 1). This
ed down for
d dried
visible rest olid input
ot covered
here is risk eral waste ould be
8
e
r
s
r
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Tes3.The testDANET
Tes1.7.Target a For the A: OrgaB: Food Parame OveralCapacityChemicPure Wa
Energy Electrici
TreatmPurity oparticles2-6 mm)15% Recover
st resultst report willTV Centre Q
st data suand measure
following tanic fractiond waste from
eters l performancy cals ater
ity consumpti
ment effects f pulps (nonds plastic, glas,) % in a pulp w
ry % VS
s l be includeQuality Man
ummary ed values of
types of wasn from housm supermark
Tce
on
egradable metal of with DM
9
9
d as an appnual.
f tested para
ste the perfosehold wastket 25 %, 2
Target Mea 5-6 Nonapprwas
20-3
95 % Test
pulpTestpulp
90 % TeststanTeststan
endix in the
ameters.
ormance pare Vejle Kom5% dairy w
asured value
ton organic wne rox. 1 ton wat
ste
30 kwh/ton wa
t with A >99.p with 15% TSt with B >99.p with 15% TSt with A: 94.8
ndard deviationt with B: 95.9
ndard deviation
e verificatio
rameters in mmune was
waste and 50
waste /h
ter/ton wet
aste
.86 % in S .96 % in S
8 % with n of 0.7 %
9 % with n 0.6 %
on report acc
the table beste sorting s0% of (A)
Method/com Based on tes Based on tes
based on contests
cording to t
elow were osystem.
mment
st.
st.
nsumption in
9
the
obtained:
the
9
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It is con• t
e• t
t
Tes1.8. The testconditiocycles uoperatio The plan
Tes1.9.For eachmeasurevalidate
1.10.The test The foll The handrying) the orga The orgnot enoumaterial
Ref4.
Appen Terms a Table 4.1
ncluded for the purity oetc. >2 mmthe recoverythe two test
st Perform
t was designons and withused in the tons of the eq
nt operated
st quality h batch run ements. Fure the accura
Ammendt plan was f
lowing devi
nd sorting oas this was
anic materia
ganic fractiough material was crush
ferences
dix 1 Term
and definitio
1 Terms and
ECOGI sysof pulp is hig
m) y is high (apts)
mance obs
ned to test th two differtest, the dataquipment.
well with n
assurancmass balan
rther mass bcy of the m
dments to followed exc
iations were
f the solid r judged a m
als (etc. veg
ons from 2 -al for the ched in a mor
s
ms and def
ons used in
definitions u
stem: gh (>99.8 w
pproximate
servation
he ECOGI rent sorts ofa observed c
no accidenti
e summarnces were cabalances weethod.
and deviacept from m
e made from
reject fractiomore securegetables like
- 40 mm wehain cruchertar for subs
finitions
the protoco
sed by the DA
weight %) w
ly 95% of t
equipmentf waste. By can be judg
ial operation
ry incl. aualculated to ere made for
ations fromminor adjust
m the test pl
ons was persorting met
e carrots wh
ere not crushr to work. Insampling.
ol are explai
ANETV test
when measur
the organic w
performancchoosing th
ged as being
n stops duri
udit resultsvalidate the
r the sorting
m test plantments in th
lan:
rformed direthod becaus
hich loose co
hed in the chnstead parts
ined in Tabl
centres.
ring the con
waste is rec
ce under reahe amount og representat
ing the 2 day
s e measured g and washin
n he sorting pr
ectly after wse it was moolor and for
hain crucheof the sorte
le 4.1.
ntent of plas
covered in th
alistic operaof replicate ative for mo
ay test
d mass and fng procedu
rocedure
washing (wiore easy to rrm when dry
er, because ted out organ
10
stic, glass
he pulp in
ating operating st
flow re to
ithout recognize ying).
there was nic
0
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se experts mayerts, QA experV systems or reerts
rices could beer, ground wat
n-house methhe absence of a
the proach
ay use an ory as
must be definedhat allows the verification toneeds are verification
nged, when the in the EU ET
be concentratiose in treatmentse etc
e item producethe item that averification
ogy is coverings, processes, ces.
y be technical rts for other egulatory
soil, drinkingter etc.
od may be usea standard, if
d
o
he TV
on t
ed a
g a
l
g
ed
11
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Word
Performaclaim
Performaparamete
Procedure
Producer
Proposer
Standard
Target
Test centsub-body
Test centrverificatiobody
Test/testin
DA
for
ance Theon inte
ance rs
Parquaprothe env
e Detstanbod
The
Anyoutpreenvverpro
Genconrecthatcha
Thepro
tre, test y
Subplan
re, on sub-
Subplan
ng Detof a
ANETV
tests or analy
e effects foresthe target (s) iended use
rameters that cantitatively in ovide the relev
performance vironmental te
tailed descriptndard or a medy
e party produc
y legal entity tside the Europesenting an innvironmental terification undeogramme
neric documennsensus and apognized standt provides rule
aracteristics fo
e property thaoduct
b-body of the ns and perform
b-body of the ns and perform
termination ofa product for p
ysis
seen by the vein the matrix o
can be documtests and that
vant informatioof an
echnology pro
tion of the usethod within on
cing the produ
established inpean Union novative echnology for er the EU ETV
nt establishedpproved by a dardization boes, guidelines
or tests or anal
at is affected b
test centre thams test
test centre thams the verific
f the performaparameters de
ComDAN
prepformstand
endor of
Non
mented t on on
oduct
The be esapplirequ(reguand v
e of a ne
The implmethequip
uct Non
n or
V pilot
Non
d by
dy or lysis
Non
by the Targconc
at Non
at ation
Non
ance efined
Non
mments on NETV app
ared in complmat and contendards.
e
performance pstablished conication(s) of th
uirements of soulations), custvendor claims
procedure spelementing a sthod in terms opment used
e
e
e
gets could be ecentration
e
e
e
the proach
liance with thents required fo
parameters munsidering the he product, thociety tomers (needs)s
ecifies andard or a
of e.g.:
e.g.. contamin
e or
must
he
)
nant
12
2
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Word
Vendor
Verificati
AppenTest The test(see 3.4 Before tcalibrati Calibra All weig4.46 kg) Table 2 TWeight small w20 kg w30 kg w All weig The inpweighin CalibratThe are
DA
for
Thethe
ion Evaparappconassu
dix 2
t was perfor4).
the actual teing the equi
ation
ghts used w) which wer
Test results
weight (g) weight (kg) weight (kg)
ghts measur
put amount ong cells on K
tion of flowa of the bas
ANETV
the applicatio
e party delivercustomer
aluation of prorameters for a plication undenditions and adurance
Te
rmed as des
est, a prerunipment.
were calibratre weighed
red within t
of added waKomteks wh
w transmittersin was mea
on
ring the produ
oduct performspecified r defined dequate qualit
st data re
scribed in th
n was perfor
ted using prusing DTIs
reference129.08 4.46 4.46
the accuracy
aste and theheel loader.
rs was perfoasured to 1.4
ComDAN
uct to Can
mance
ty
Non
port
he test plan
rmed on 10
reweighed cs calibrated
e
y of reading
e output amo.
ormed by us4*11.7 = 16
mments on NETV app
be the produc
e
except mino
.dec 2012 f
calibration blaboratory w
g.
ount of reje
sing the bas6.38 m2.
the proach
cer
or deviation
for testing th
bottles with weights.
measured129 4.45 4.4
ct was weig
sin M7 for m
n in sorting
he method a
h water (129
d
ghed using c
measuring th
13
method
and
9.08 g and
calibrated
he amount.
3
![Page 14: ECOGI Pre- f biom ass for anaerobic - DANETV - The Danish ... · f biom and separ or biogas 2013 ass f ation of o ification or ana rganic wa erobi ... sed on mea sis of a num ter)](https://reader030.vdocument.in/reader030/viewer/2022013017/5c65a6ec09d3f29b6e8d145f/html5/thumbnails/14.jpg)
Table 3 Ttest 1 2 The resuarea me SortingBased oenough Based othe solidsorting m Tests peTests won 12.de The test
• R• Sa
• Sa
Docume Samplin3 subsammixing
Test of flow tadded FT6.1 2.4
ult is accepteasurement
g test on the preru
material fo
on drying trid reject fracmethod as m
erformed were perform
ecember us
t included thecording alampling of
o analo anal
metampling of
o subso waso sort
degro dryio Ana
entation pho
ng of produmples wereand subsam
ransmitter FT1 (m3)
table within(1 cm heigh
un it was decr the chain
ials and inspctions directmaterials w
med 11.deceing 50 % w
he followinl input and produced pulysis of VS lysis of purial, plastic) breject sampling ofhing of subing reject inradable mating subsampalysis of Vo
otos from se
uced pulp e taken durinmpling while
T1 by addingmeasured (39 14.8
n the uncertaht correspon
cided to runcrucher to w
pection of thtly after wasere more ea
ember usingwaste from V
g steps accooutput weigulp and TS of pity of pulp (by washing
f reject for tsample in s
n non-degratter and weiples of sortelatile solids
elected indi
ng pumpinge stirring.
g of water pe(cm) Calc
6.392.42
ainty of heinds to a volu
n without thwork.
he waste it shing withoasily recogn
g organic waVejle and 50
ording to teghts as well
pulp (amount of
g, sorting an
testing contspecial machadable matteighing (wet)ed reject ands content (or
ividual step
g to storage
rformed dec.culated addi9 2 ight measurume change
e chain crus
was decideout drying anized.
aste collecte0% waste fr
st plan: l as power c
non-degradnd weighing
ent of organhinery er (plastic, m) d weighingrganic matt
s in the test
tank and tra
.10th 2013 ition (m3)
ement of the of 0.164 m
sher, becaus
d to performs this was ju
ed from hourom industry
consumption
dable matter
nic waste
metal, glass
for dry mater)
are shown
ansferred to
Differen-4.5 -0.8
he basin (1 cm3).
se there was
m the hand sudged a mo
useholds in y.
n for each te
r > 2 mm –
s/stones) and
tter analysis
below.
o a large buc
14
nce %
cm) and
s not
sorting of ore secure
Vejle and
est run
glass,
d
s
cket for
4
![Page 15: ECOGI Pre- f biom ass for anaerobic - DANETV - The Danish ... · f biom and separ or biogas 2013 ass f ation of o ification or ana rganic wa erobi ... sed on mea sis of a num ter)](https://reader030.vdocument.in/reader030/viewer/2022013017/5c65a6ec09d3f29b6e8d145f/html5/thumbnails/15.jpg)
Figure 3 AnalysiA 1 litreparticles
Figure 4
Sampling of
is of purity e subsamples for drying
Washing of p
f pulp
of pulp e of the pulpg and weigh
pulp to estim
p was washhing.
mate purity
hed on a 2 mmm sieve as shown belo
ow before c
15
ollection of
5
f
![Page 16: ECOGI Pre- f biom ass for anaerobic - DANETV - The Danish ... · f biom and separ or biogas 2013 ass f ation of o ification or ana rganic wa erobi ... sed on mea sis of a num ter)](https://reader030.vdocument.in/reader030/viewer/2022013017/5c65a6ec09d3f29b6e8d145f/html5/thumbnails/16.jpg)
SamplinThe rejeone batc
Figure 5 The 3 bweighin
Figure 6
ng of rejectect was collch was trans
Collection of
atches in a ng cells of th
Mixing of 3 b
t lected in a csferred to a
f reject from
test run werhe wheel lo
batches to on
container wiclean stora
one batch in
re mixed usader
ne sample rep
ith drainageage facility f
container
sing a large
presenting a t
e of water tofor mixing a
wheel load
test run and w
o floor tank.and weighin
er and weig
weighing with
. The containg.
ghed using t
h wheel loade
16
iner with
the
er
6
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From thand filli The squ The contogetherwash. T The use1: washcollectin2: washcollectin3: washinto a co4: remo
4am(F4b4c
5: The <amount 6: remo
6ahala6b6c
7: Fromthoroug 8: SampA repre
he mixed 3 bing a 60 litr
uare bucket
ntent was wr with wash
The amount
ed sorting prhing with 48ng bucket w
hing with 20ng bucket w
hing with 20ollecting bu
oval of >40 ma: The rejec
metal, glass, Figure 10) b: The matec: The non-o< 10 mm frawas small a
oval of 2 - 40a: Sorting a and in non-darger than 5*b: The matec: The non-o
m the organicgh mixing fo
pling of wassentative sa
batches a ree square bu
was now so
eighed and hing water (F
was washed
rocedure (ap8 litre cold wwith a 10 mm0 litre cold wwith a 10 mm0 litre hot wucket with amm reject f
ct fraction >bones and s
erial was weorganic mataction incluand it was s0 mm rejectrepresentat
degradable *5*5 mm anerial was weorganic mat
c fraction >or analysis o
shing water ample was t
epresentativucket.
orted accord
transferred Figure 7). Td in three st
ppendix 3, twater for apm screen water for apm screen ater (30-40º
a 10 mm scrfor sorting 40 mm wassticks with d
eighed (wet)terial was d
uding washinsorted togetht for sortingtive sample material (plnd organic meighed terial was d
> 40 mm andof TS and V
aken from w
ve sample w
ding to the p
d to a cemenThe averageteps while r
test plan) ispprox. 10 mi
pprox. 10 mi
ºC) for apprreen (Figure
s hand sortedimensions
) dried and weng water waher with the
g of approx.
lastics, metmaterial (Fi
dried and we
d 2 - 40 mmVS.
washing wa
was taken by
procedure in
nt mixer wite weight warotating.
s summarizeinutes, deca
inutes, deca
rox. 10 mine 8)
ed in non-de larger than
eighed as filtered oe 10-40 mm
20% of the al, glass, boigure 11)
eighed
m proportion
ater to furthe
y using a gra
n appendix
h a 40 mm s approxima
ed below anting of wa
anting of wa
utes, decant
egradable mn 5*5*5 mm
on a 2 mm sm fraction.
reject fractones and stic
nal subsamp
er analysis o
ab randomly
3 of the test
screen in frmately 15 kg
ater by tiltin
ater by tiltin
nting of wate
material (plam and organi
screen (Figu
tion 2 - 40 mcks with dim
ples were pr
of TS and V
17
y picking
t plan.
ront for each
ng into a
ng into a
er by tilting
stics, ic material
ure 9). The
mm by mensions
repared by
VS
7
g
![Page 18: ECOGI Pre- f biom ass for anaerobic - DANETV - The Danish ... · f biom and separ or biogas 2013 ass f ation of o ification or ana rganic wa erobi ... sed on mea sis of a num ter)](https://reader030.vdocument.in/reader030/viewer/2022013017/5c65a6ec09d3f29b6e8d145f/html5/thumbnails/18.jpg)
Figure 7
Figure 8
Washing in c
Collection of
cement mixer
f 10 - 40 mm
r with 40 mm
reject from w
m screen
washing
18
8
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Figure 9
Figure 10
Collection of
0 Sorting of >
f 2 - 10 mm r
> 40 mm was
eject from w
hed reject fra
ashing
action
19
9
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Figure 11 Total SoTS and possible The dryweight aused, as
1 Hand sortin
olids and VVS was ana
e by using a
ying methodafter 2 and s the drying
ng of 2-40 mm
Volatile solidalyzed on oa mortar.
d for organic3 days. Thewould have
m fraction on
ds analysisrganic samp
c fraction use low tempee been too t
n sorting tabl
ples that we
sed was 103erature optiotime consum
le
ere manually
3 °C for 4 don in test plming.
y homogeni
days, as theran appendix
ized as thor
re still was lx 3 (50 °C)
20
roughly as
loss of was not
0
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Test resDuring Table 9
• InTd
• A
T
• ToTt
• PuT
• W
Tw
• RTd
• PoTk
sults and Mall tests the.
nput of wastThe amoundistributed
Amount of wThe amoun
otal water fThe total amtransmitters
ulp to storagThe amoun
Washing watThe washinwater follow
eject The amoundistributed
ower consumThe power kWh counte
Mass Balance following p
te (waste in t was only wevenly betw
water to pulpt is added u
for Reject semount for res. This amou
ge tank t is measure
ter ng steps is dwed by 2.3
t was only wevenly betw
mption consumptioer before an
ces parameters
ton) weighed forween the 3 b
per using FT1
eparation eject separaunt is transf
ed using FT
divided in 2 m3 fresh wa
weighed forween the 3 b
on of the pland after the
were record
r the sum ofbatch tests
ation was meferred to the
T2
steps with aater
r the sum ofbatch tests
ant includincombined 3
ded as show
f 3 batch tes
easured by e pulp in the
approx. 1.5
f 3 batch tes
ng ventilatio3 batch tests
wn in Table
sts and there
reading amoe rejection s
m3 in first s
sts and there
on was recors in each tes
4 to
efore has be
mounts addedstep.
step using t
efore has be
rded by reast run
21
een
d by flow
technical
een
ding the
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Table 4 T11.dec.1Waste inAmount Water leReject seTotal sepPulp to sWashingother waPure watReject oReject oMass baInput waOutput perror in kWh befkWh aftePower co
Exampl Input wOutput p
Test A test ru13 A‐T1 nput ton of water add
evel after wateeparation paration watestorage tank mg ater washing (ter for washinut ut ton alance aste + water pulp + reject mass balancefore er onsumption k
le calculatio
waste and wapulp and rej
un T1
ed to pulper (er addition (c
er added to pum3 FT2
(estimated) * ng m3
%
kWh
on of mass b
ater = 2.23 +ject = 9.3 +
b
(m3) FT1 m)
ulp
balance A-T
+ 2 + 6.5 =+ 0.48 = 9.78
batch 1 batc2.233
286
6.59.3
1.52.3
0.48
10.739.788.85
253515
T1, batch 1:
10.73 ton 8 ton
ch 2 b2.233
2104
6.79.2
1.52.3
0.48
10.939.68
11.43
batch 3 Sum2.233
2130
6.59.5
1.52.5
0.48
10.739.986.99
253709
194
m or average 6.76
19.728
4.57.1
1.45
32.4029.45 9.1
22
7 6
7 8
5 1
5
0 5 1
2
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Table 5 T11.dec.1Waste inAmount Water leReject seTotal sepPulp to sWashingother waPure watReject oReject oMass baInput waOutput perror in kWh befkWh aftePower co
Table 6 T11.dec.1Waste inAmount Water leReject seTotal sepPulp to sWashingother waPure watReject oReject oMass baInput waOutput perror in kWh befkWh aftePower co
Test A test ru13 A‐T2 nput ton of water add
evel after wateeparation paration watestorage tank mg ater washing ter for washinut ut ton alance aste + water pulp + reject mass balancefore er onsumption k
Test A test ru13 A‐T3 nput ton of water add
evel after wateeparation paration watestorage tank mg ater washing ter for washinut ut ton alance aste + water pulp + reject mass balancefore er onsumption k
un T2
ed to pulper (er addition (c
er added to pum3 FT2
ng m3
%
kWh
un T3
ed to pulper (er addition (c
er added to pum3 FT2
ng m3
%
kWh
bat
(m3) FT1 m)
ulp
2
bat
(m3) FT1 m)
ulp
2
tch 1 batch2.333 2.3
2104
7
9.3
1.32.3
0.52 0
11.33 109.82 9
13.38 1153752
tch 1 batch2.167 2.
2
6.89.5
1.42.3
0.49 0
10.97 109.99 98.94 5
53922
h 2 batch 3333 2.3332 2
6.1 6.558.7 8.4
2 1.652.3 2.3
0.52 0.52
0.43 10.889.22 8.921.66 18.07
253922
170
h 2 batch 3167 2.1672 2
6.4 6.69.5 9.4
1.5 1.32.3 2.3
0.49 0.49
0.57 10.779.99 9.895.49 8.17
254086
164
Sum or ave32
54 53
2
827
2 0
Sum or ave72
64
33
9
797
6 4
erage 76
19.6526.4
4.956.9
1.55
32.6527.95 14.4
erage 6.56
19.828.4
4.26.9
1.46
32.329.86 7.55
23
3
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Table 7 T12.dec.1Waste inAmount Water leReject seTotal sepPulp to sWashingother waPure watReject oReject oMass baInput waOutput perror in kWh befkWh aftePower co
* for this Table 8 T12.dec.1Waste inAmount Water leReject seTotal sepPulp to sWashingother waPure watReject oReject oMass baInput waOutput perror in kWh befkWh aftePower co
Test B test ru13 B‐T1 nput ton of water add
evel after wateeparation paration watestorage tank mg ater washing ter for washinut ut ton alance aste + water pulp + reject mass balancefore er onsumption ktest the powe
Test B test ru13 B‐T2 nput ton of water add
evel after wateeparation paration watestorage tank mg ater washing ter for washinut ut ton alance aste + water pulp + reject mass balancefore er onsumption k
un T1
ed to pulper (er addition (c
er added to pum3 FT2
ng m3
%
kWh er consumptionun T2
ed to pulper (er addition (c
er added to pum3 FT2
ng m3
%
kWh
bat
(m3) FT1 m)
ulp
n for the test
bat
(m3) FT1 m)
ulp
2
tch 1 batch2.267 2.2
2104.5
6.910.9
1.22.3
0.53 0
11.17 911.43 8‐2.39 9
0 2543
run was calcu
tch 1 batch2.783 2.7
2
710
1.32.3
0.50 0
11.78 1110.50 1010.89 1154538
h 2 batch 3267 2.2672 2
5.6 7.48.4 10
2.8 1.12.3 2.3
0.53 0.53
9.87 11.678.93 10.539.46 9.71399
254493141*
ulated from tw
h 2 batch 3783 2.7832 2
7 7.19.9 10.6
1.3 1.22.3 2.3
0.50 0.50
1.78 11.880.40 11.101.74 6.59
254693
155
Sum or ave72
40
13
3
731
3 *
wo batch runs
Sum or ave32
16
23
0
809
3 5
erage 6.86
19.929.3
5.16.9
1.6
32.730.9 5.5
erage 8.35
6
21.130.5
3.86.9
1.5
35.4532
9.73
24
4
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Table 9 T12.dec.1Waste inAmount Water leReject seTotal sepTo storaWashingother waPure watReject oReject oMass baInput waOutput perror in kWh befkWh aftePower co
The calcThe erroreading on the p Table 1 Table 10
Test teA A A B B B
The wattechnicaproduceoptimisebatch w
Test B test ru13 B‐T3 nput ton of water add
evel after wateeparation paration watege tank m3 FTg ater washing ter for washinut ut ton alance aste + water pulp + reject mass balancefore er onsumption k
culated masor may be derrors in FT
pulp.
0 shows wa
0 Waste amou
est run Inputon
1 2 3 1 2 3
ter consumpal water (reced by dewated. Based o
which is appr
un T3
ed to pulper (er addition (c
er added to puT2
ng m3
%
kWh
ss balances due to an errT1 and 2. It
aste in- and
unts and powut waste (wet)
Oto
6.70 7.00 6.50 6.80 8.35 7.90
ption of purcycled fromtering of theon the test 2roximately
bat
(m3) FT1 m)
ulp
2
for the 3 tesror in readint was not pr
-outputs an
er consumptiOutput Pulp on(wet)
2826.428.429.330.529.6
re water is am earlier pule pulp by a d.3 ton of puthe same as
tch 1 batch2.633 2.6
2
710
1.32.3
0.54 0
11.63 1110.54 109.40 11
54706
sts have aveng of FT2 oractically po
nd power co
ion Output reton (wet)
844356
at present unlpings) is usdewatering
ure water was the added
h 2 batch 3633 2.6332 2
7 79.8 9.8
1.3 1.32.3 2.3
0.54 0.54
1.63 11.630.34 10.341.12 11.12
254877
171
erage errorsof approximossible to ca
onsumption
eject kWh u
1.451.551.461.61.5
1.62
nder improvsed for new technology
as needed foamount of w
Sum or ave32
78
33
4
342
7 1
s between 5 ately -10 %
alibrate the f
for each tes
used kWh/194170164141155171
vement. In npulpings. T
y which is pror washing wet waste.
erage 7.96
2129.6
3.96.9
1.62
34.931.22 10.5
and 14 wei% or a combi
flow transm
st run.
/ton input w222212
normal operThe technicaresently beithe reject o
25
ight %. ination of
mitter FT2
et 29.024.325.220.718.621.6
ration al water is ing
of each
5
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Analy Purity In Figur
Figure 12 The tabTS as th Test te
r
A 1A 2A 3B 1B 2B 3
The imp
ysis resu
re 12 the co
2 Inorganic
le below shhis is the typ
est un
biopuweigh(g)
1 1000.2 1000.3 1000.1 1000.2 1000.3 1000.purities >2 m
ults
ontent of res
dried residue
hows the anapical produc
lp hed
TS pul
00 4.99 00 5.88 00 6.13 00 6.41 00 6.93 00 6.8 mm amount
sidue (2-6 m
e (2 - 6 mm) o
alysis data fct quality af
lp % TSco‐ 60.0.0.0.0.0.
ts to
mm) in 1 lit
of 1 liter pulp
for calculatifter dewater
S inorganic omponents 6 mm (g) .4555 .7909 .3125 .1623 .1969 .1958
ter pulp from
p from test ru
ing purity. Tring using a
2 % inorganin pulp
0.05 0.08 0.03 0.02 0.02 0.02
m the purity
uns
The purity ia screw pres
nic % inorpulp wDM 0.14 0.20 0.08 0.04 0.04 0.04
y analysis i
is recalculatss.
rganic in with 15%
26
s shown.
ted to 15 %
6
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A averaB avera The par The purA > 99.B > 99.9in a pulp Recover The tabaccordinfrom 2 -biogasifwashing In the so Non deg
• M• Pl• ot• w
Fraction
• or
age: 0.14 % age: 0.04 %
rticles have
rity (amount86 % 96 % p with a cal
ry
le below shng to the pr- 40 mm. Thfication andg water cont
orting proce
grable fractMetal
lastic, rubbether inorgan
wood pieces,
ns degradabrganic waste
standard destandard de
to pass a 6
t of non-deg
lculated TS
hows resultsrocedure usihe hand sor
d organic fratained parti
edure the m
ions in biog
er and textilnic material, sticks and
ble in biogase from hous
eviation 0.0eviation 0.0
mm sieve in
gradable ma
of 15 wt %
from weighing washingrting producactions whiccles and sol
material is di
gasification
les s like stonebones with
sification inseholds and
06 % 02 % when
n the rejecti
aterial like p
%
hing of the g and hand sced a numbech are degralubilized or
ivided into :
including:
s ,ceramics dimensions
ncluding: d industry
n recalculate
ion separato
plastics, gla
reject sampsorting of frer of fractioadable in birganics < 2 m
:
and glass s >5*5*5 m
ed to 15 % T
or and there
ass and meta
ples. The samractions largons which arogasificatiomm.
mm
TS.
efore cannot
al) are
mples wereger than 40 re nondegraon. Further t
27
t be larger.
e treated mm and
adable in the
7
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Table 11
Test
teru
A 1A 2A 3B 1B 2B 3
The wei There is The madeviatio Figure 13testrun A A A B B B
The watin the so An exam In Figur
Weighing of
est un
Sample input (kg wet)
1 15.1
2 14.1
3 14.1
1 10.95
2 13.95
3 13.1
ights for 2 -
s a minor lo
ss balance oons.
3 Mass balanbatch
123123
ter loss of 0orting proce
mple of the
re 15 the no
reject
wash water
input (kg)
Da
79 76 75 75 75 79.5
- 40 mm are
oss of water
of input (be
nce before andinput
1 94.10 2 90.10 3 89.10 1 85.95 2 88.95 3 92.60
0.6 -6 % is aedure.
sorted fract
on plastic an
Drained reject after washing
(kg wet)
17.42 17.49 17.10 12.70 15.20 16.52
e based on s
during drai
fore washin
d after washioutput d
89.9788.3788.6981.9486.2486.78
acceptable w
tion > 40 m
nd textile co
Non‐degrabiogasifica
wet
> 40 mm
9.27 6.82 4.76 5.24 6.18 5.02
sorting and w
inage and so
ng) and outp
ing deviation %
‐4.4‐1.9‐0.5‐4.7‐3.1‐6.3
when taking
mm, textile a
ontent in a >
adable in tion (kg t)
Dbio
2 ‐ 40 mm
>m
3.01 04.54 04.60 03.03 03.16 04.30 0
weighing o
orting.
put (after w
g into accou
and plastics
>40 mm sor
Degradable inogasification (
wet)
> 40 mm
2 ‐ 40mm
0.52 4.570.26 4.650.29 5.740.29 2.790.48 3.120.38 4.56
f 20 % of th
ashing) sho
unt the large
s is shown in
ting fraction
n (kg
0 m
wash watdrained o
(kg) 7 72.60 5 72.10 4 73.30 9 70.60 2 73.30 6 72.53
he wet samp
ows the follo
e number of
n Figure 14
n is shown.
28
ter off organic
wet (%)29.3 30.2 39.2 27.1 27.8 34.6
ple.
owing
f operations
4.
8
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Figure 14
Figure 15 An exam
4 Sorted frac
5 Sorted frac
mple of the
ction >40 mm
ction >40 mm
sorted fract
m textile and p
m metal, organ
tion 2 - 40 m
plastics
nic residue an
mm is show
nd non bioga
wn in Figure
s degradable
e 16 to Figur
e woodsticks a
re 18
29
and bones
9
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Figure 16
Figure 17
6 Sorted frac
7 Sorted frac
ction 2-40 mm
ction 2-40 mm
m organic fra
m plastic frac
action
ction
30
0
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Figure 18 The conconsidedevelop The conthe total In Tableare show
8 Sorted frac
ntent of stickred to be de
ped or instal
ntent was bel amount of
e 12 Total Swn.
ction 2-40 mm
ks, bones wegradable inlled at full s
etween 6-12f sorted was
Solids and V
m textile, met
with dimensin biogasificascale biogas
2% of the orste (Wet wei
Volatile soli
als, bones an
ions >5*5*5ation withou
s plants.
rganic food ight).
ids of the so
nd sticks
5 mm was mut severe pr
waste (wet
orted organi
measured inretreatment
t weight) or
ic fractions
n test B. Thewhich is ye
between 2-
and the was
31
ese are not et not
-3.3 % of
shing water
r
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Table 12
BiopulpA A A B B B Reject 2mm A A A B B B Washinwater A A A B B B
Table 1
TS and VS o
p test
2‐40
g
3 and Table
of organic con
t run TS % 1 42 3 1 2 3
1 142 13 11 142 13 1
1 2 3 1 2 3
e 14 show c
ntent in fractStandadev. %
4.99 05.88 06.13 06.41 06.93 06.80 0
4.49 15.63 05.38 04.71 05.10 05.36 0
0.16 00.17 00.22 00.18 00.14 00.15 0
alculations
tions ard % VS % .52 88.4.44 88.4.06 88.3.09 90.3.11 90.4.11 90.2
.12 81.3
.16 83.3
.62 90.6
.09 87.0
.51 92.2
.45 87.8
.00 69.6
.01 74.8
.01 73.8
.01 74.2
.00 73.6
.00 76.6
of recovery
Standarddev. %
43 0.1748 0.0936 0.9233 0.6642 0.6127 0.46
37 4.1537 4.6160 3.0905 0.2426 1.8984 5.05
63 0.5386 2.1684 1.9625 2.7266 2.6760 2.06
y.
d
792616
519495
366276
32
2
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Table 13Test runBiopulpTS % VS % BiopulpReject tOrganicOrganicOrganicOrganicOrganicOrganic% recov
% recov Exampl Biopulp OrganicOrganicton WashinInput = washing OrganicOrganic Thus fowater or As the b0.057)/1
Results for tn p tons Input
p VS ton Inputons c % (wet) c ton (wet) c DM % c VS % c VS ton excluc VS ton incluvery
very for test
le calculatio
p in VS = 28
c reject wet c reject excl
ng water add17.42 kg or
g water = 72
c content (exc content wa
or T1 we havr in total 0.0
biopulp con1.23*100 =
test A
ut
uding washinuding washin
t A: 94.8 %
on T1:
8 * 4.99 * 8
= 1.45 * 29luding wash
dition T1 rganic wet c
2.6 kg with
xcl. washinashing wate
ve additiona057 ton VS
ntains 1.23 t95.4%.
1
ng water ng water
with standa
88.43/100/10
9.3/100 = 0.hing water V
content 0.52
TS = 0.16%
g water) in er in VS = 7
al 50 *0.081in the rejec
on VS the r
1 228
4.9988.431.231.45
29.300.42
14.4981.370.0500.05795.41
ard deviatio
00 = 1.23 to
.42 ton VS ton = 1.4
2 + 4.57 = 5
% VS = 69.6
VS = (0.5272.6*0.16*6
1/0.6 = 6.75ct
recovery for
3 26.45.88
88.481.371.55
30.180.47
15.6383.370.0610.07094.93
on = 0.68 %
on
45*29.3/100
5.09 kg with
63%
+4.57)*14.469.63/100/10
5 kg VS to t
r batch 1 ca
28.46.13
88.361.541.46
39.160.57
15.3890.600.0800.09194.07
0*14.49*81
h DM 14.49
49*81.37/100 = 0.081
the 50 kg ex
n be calcula
1.37/100/10
9% VS = 81
00/100 = 0.kg
xcluding wa
ated to (1.23
33
0=0.050
1.37%
.60 kg
ashing
3-
3
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Table 14 Test runBiopulpTS % VS % BiopulpReject tOrganicOrganicOrganicOrganicOrganicOrganic% recov
% recov Discuss The resu
• a l
• a The recoallowpapeproc Somremdepe
AppenNo ame
4 Results for t
n p tons Input
p VS ton Inputons c % (wet) c ton (wet) c TS % c VS % c VS ton excluc VS ton incluvery
very for test
sion and co
ults show high purity larger than recovery >9
organic maovery it is exw most of ter like dryincess and no
me sticks anmoved with t
end on the c
dix 3 Ameendments an
test B
ut
uding washinuding washin
t B: 95.9 %
nclusion
of the prod2 mm. 94.8% of or
aterial will bxpected thathe material ng paper foridentifiable
d bones andthe reject. Tcomposition
endment and deviation
1
ng water ng water
with standa
duced pulp w
rganic mater
be in the fort the organito pass the
r kitchen use larger part
d wood piecThe amount n of collecte
and deviatns are descri
1 229.36.41
90.331.701.6
27.130.43
14.7187.050.060.07
95.96
ard deviatio
with less tha
rial
rm of food wic material i 6 mm scree
se is also exts of paper w
ces are too sof these pared waste.
tions repoibed here (d
3 30.56.93
90.421.911.5
27.800.42
15.1092.260.060.07
96.49
on = 0.6 %
an 0.14% pa
waste from is partly dowen holes in pected be dwas found i
solid to be drts was limi
ort for testdeviations to
29.66.80
90.271.821.62
34.620.56
15.3687.840.080.09
95.31
articles of p
householdswnsized in tthe sorting
disintegratedn sorted fra
down sized ited in the te
t o test plan a
plastic, glass
s. Based on the pulping unit. Loose
d by the pulactions.
in the proceests but will
are given in
34
s, metal
the high process to
ely bound lping
ess and are l of course
n part 3.4)
4