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Case study of anaerobic digestion process stability detected by dissolved hydrogen concentration

Abstract

The paper presents the results of a laboratory experiment of mesophilic single-stage anaerobic digestion performed to verify the possibility of early detection of process instability and reactor overload by evaluating the course of dissolved hydrogen concentration of the main intermediate. The digestion process was run in a Terrafors IS rotary drum bioreactor for 230 days. The substrate dosed on weekdays was food leftovers from the university canteen. At an average temperature of 37 degrees C, an organic loading of volatiles of 0.858 kg m(-3) day(-1) and a theoretical retention time of 259 days, biogas production of 0.617 Nm(3) kg VS-1 was achieved with a CH4 content of 51.7 vol. %. The values of the established FOS/TAC stability indicator ranged from 0.26 to 11.4. The highest value was reached when the reactor was overloaded. The dissolved hydrogen concentration measured by the amperometric microsensor ranged from 0.039-0.425 mg dm(-3). Data were statistically processed using Pearson's correlation coefficient. The correlation of the hydrogen concentration with other parameters such as the concentration of organic acids was evaluated. The value of Pearson's correlation coefficient was 0.331 and corresponded to a p-value of 0. The results confirmed a very low limit of the hydrogen concentration at which the microbial culture, especially methanogens, was already overloaded. The amperometric microsensor proved to be rather unsuitable for operational applications due to insufficient sensitivity and short service life. The newly designed ratio of dissolved hydrogen concentration to neutralizing capacity was tested but did not work significantly better than the established FOS/TAC stability indicator.

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Case study of anaerobic digestion process stability detected by dissolved hydrogen concentration

Author: Platošová, Daniela
Publisher: MDPI
Year: 2021
DOI: 10.3390/pr9010106
Source: https://dspace.vsb.cz/bitstreams/97bed05b-0060-4a2f-8904-c9fb76c756c4/download
p ocesses
A icle
Case S udy o Anae obic Diges ion P ocess S abili y De ec ed
by Dissol ed Hyd ogen Concen a ion
Daniela Pla ošo á1,* , Jiˇ íRusín1, Jan Pla oš 2, Ka eˇ ina Smu ná3and Roman Bu yjan 4


Ci a ion: Pla ošo á, D.; Rusín, J.;
Pla oš, J.; Smu ná, K.; Bu yjan, R.
Case S udy o Anae obic Diges ion
P ocess S abili y De ec ed by
Dissol ed Hyd ogen Concen a ion.
P ocesses 2021,9, 106. h ps://
doi.o g/10.3390/p 9010106
Recei ed: 11 No embe 2020
Accep ed: 5 Janua y 2021
Published: 7 Janua y 2021
Publishe ’s No e: MDPI s ays neu-
al wi h ega d o ju isdic ional clai-
ms in published maps and ins i u io-
nal a ilia ions.
Copy igh : © 2021 by he au ho s. Li-
censee MDPI, Basel, Swi ze land.
This a icle is an open access a icle
dis ibu ed unde he e ms and con-
di ions o he C ea i e Commons A -
ibu ion (CC BY) license (h ps://
c ea i ecommons.o g/licenses/by/
4.0/).
1Ins i u e o En i onmen al Technology, VSB—Technical Uni e si y o Os a a, 17. Lis opadu 2172/15,
70800 Os a a, Czech Republic; [email p o ec ed]
2Depa men o Compu e Science, Facul y o Elec ical Enginee ing and Compu e Science,
VSB—Technical Uni e si y o Os a a, 17. Lis opadu 2172/15, 70800 Os a a, Czech Republic;
[email p o ec ed]
3Ins i u e o Languages, VSB—Technical Uni e si y o Os a a, 17. Lis opadu 2172/15,
70800 Os a a, Czech Republic; [email p o ec ed]
4GAS Con ol s. .o, No ýS ˇe 1407/59a, 73564 Ha íˇ o -P os ˇ edníSuchá, Czech Republic;
[email p o ec ed]
*Co espondence: [email p o ec ed]
Abs ac :
The pape p esen s he esul s o a labo a o y expe imen o mesophilic single-s age
anae obic diges ion pe o med o e i y he possibili y o ea ly de ec ion o p ocess ins abili y
and eac o o e load by e alua ing he cou se o dissol ed hyd ogen concen a ion o he main
in e media e. The diges ion p ocess was un in a Te a o s IS o a y d um bio eac o o 230 days.
The subs a e dosed on weekdays was ood le o e s om he uni e si y can een. A an a e age
empe a u e o 37
◦
C, an o ganic loading o ola iles o 0.858 kg m
−3
day
−1
and a heo e ical
e en ion ime o 259 days, biogas p oduc ion o 0.617 Nm
3
kg VS
−1
was achie ed wi h a CH4
con en o 51.7 ol. %. The alues o he es ablished FOS/TAC s abili y indica o anged om 0.26
o 11.4. The highes alue was eached when he eac o was o e loaded. The dissol ed hyd ogen
concen a ion measu ed by he ampe ome ic mic osenso anged om 0.039–0.425 mg dm
−3
. Da a
we e s a is ically p ocessed using Pea son’s co ela ion coe icien . The co ela ion o he hyd ogen
concen a ion wi h o he pa ame e s such as he concen a ion o o ganic acids was e alua ed. The
alue o Pea son’s co ela ion coe icien was 0.331 and co esponded o a p- alue o 0. The esul s
con i med a e y low limi o he hyd ogen concen a ion a which he mic obial cul u e, especially
me hanogens, was al eady o e loaded. The ampe ome ic mic osenso p o ed o be a he unsui able
o ope a ional applica ions due o insu icien sensi i i y and sho se ice li e. The newly designed
a io o dissol ed hyd ogen concen a ion o neu alizing capaci y was es ed bu did no wo k
signi ican ly be e han he es ablished FOS/TAC s abili y indica o .
Keywo ds:
anae obic diges ion; e men a ion; o a y bio eac o ; dissol ed hyd ogen; ampe ome -
ic senso
1. In oduc ion
Con olled anae obic diges ion wi h biogas p oduc ion is an es ablished and, in he
u u e, p omising way o ecological use o biomass and enewable ene gy p oduc ion. The
echnology o biogas plan s is based on he biological decomposi ion o o ganic subs ances
in an en i onmen wi hou access o ai . This is a bioene ge ic ans o ma ion o subs ances
in which he e is no signi ican educ ion in a e ilize alue. The p oduc s a e a biologically
s abilized ma e ial called diges a e, which is used mainly as a e ilize and biogas wi h a
me hane con en o 55–70% and a calo i ic alue o abou 18–26 MJ Nm−3.
Anae obic diges ion is a complex biochemical p ocess ha consis s o many pa s,
consecu i e and pa allel p ocesses; Guje and Zehnde illus a e his in a diag am [
1
]. To
simpli y he explana ion, mos au ho s di ide he p ocess in o ou p ima y phases [
2
]: hy-
d olysis is he i s s age o decomposi ion; mac omolecula o ganic subs ances a e b oken
P ocesses 2021,9, 106. h ps://doi.o g/10.3390/p 9010106 h ps://www.mdpi.com/jou nal/p ocesses
P ocesses 2021,9, 106 2 o 11
down in o low molecula weigh wa e -soluble subs ances. Decomposi ion akes place
using ex acellula hyd oly ic enzymes, which a e p oduced exclusi ely by e men a ion
bac e ia. In he second phase, acidogenesis, he p oduc s o hyd olysis decompose in o
simple o ganic subs ances, such as alcohols, acids, CO
2
, and hyd ogen, mainly by he
ac ion o bac e ia. The hi d phase is ace ogenesis, he o ma ion o ace ic acid. Syn ophic
ace ogenic mic oo ganisms decompose o ganic acids highe han ace ic acid, alcohols, and
a oma ic compounds. CO
2
and H
2
a e also p oduced. The las phase is me hanogenesis.
Commonly, p edominan ly ace o ophic me hanogenic mic oo ganisms decompose he
ace ic anion o o m me hane and CO
2
. Hyd ogeno ophic me hanogens consume H
2
and
CO
2
o p oduce me hane. CH
4
and CO
2
p edomina e in biogas om balanced diges ion in
a a io co esponding mainly o he composi ion o he incoming o ganic ma e in he sub-
s a e [
3
]. The in e ac ion o many g oups o mic oo ganisms is essen ial o he long- e m
main enance o he condi ions o e icien con e sion o o ganic ma e . Excess hyd ogen
in he whole sys em inhibi s he ac i i y o me hanogens, as well as ace ogenesis, and can
cause chaining p oblems leading o he collapse o he whole p ocess. The condi ions in
he e men e o he biogas plan wi h ega d o he one-s age p ocess a e main ained by
he ope a o so ha said diges ion phases a e in equilib ium o a long ime. I he e is a
mo e signi ican imbalance, es o ing equilib ium may no be easy a all o a sho pe iod.
1.1. Va iables Moni o ed du ing he Diges ion P ocess
I we conside a ma u e biogas echnology ensu ing minimal empe a u e luc ua ions
and minimal ai supply o he e men e , he ollowing a iables a e moni o ed o con inu-
ous e alua ion o p ocess s abili y: biogas p oduc ion is s ill some imes he only moni o ed
pa ame e . I does no desc ibe he s a e o he p ocess bu only i s esul , which depends
on he amoun o o ganic subs ances in oduced and on a high numbe o o he ac o s.
The concen a ion o CH
4
in biogas is also no he main indica o o p ocess s abili y. I is
a he a balance elemen . The amoun o CH
4
p oduced mus be in ela ion o he o ganic
load applied o o loads o he main g oups o subs a es, such as a s e sus ca bohy-
d a es e sus p o eins. A mo e sensi i e indica o o p ocess s abili y is he CH
4
/CO
2
concen a ion a io. This a io is de e mined by he composi ion o he eed mix u e and
does no change much du ing he s able ope a ion o he e men e . The hyd ogen con-
cen a ion in biogas is one o he mo e sensi i e indica o s o p ocess s abili y. In gene al,
i can be s a ed ha he appea ance o H
2
in biogas almos always signals he ins abili y
o he p ocess. Howe e , i is almos impossible o achie e an equilib ium dis ibu ion
o H
2
be ween he liquid and gas phases, which makes he e alua ion o his pa ame e
di icul . pH is no a su icien ly sensi i e indica o o p ocess s abili y. I he pH d ops,
his indica es dosing e o s made in he las ew days o weeks. I is necessa y o moni o
he pH, especially when diges ing subs a es ha do no p o ide su icien neu alizing
capaci y o he suspension in he e men e o subs a es ha a e oo ni ogenous. The
neu aliza ion capaci y (bu e ing capaci y) o he eac o consis s mainly o he equilib ium
sys em HCO
3−
/CO
2
oge he wi h he equilib ium sys em NH
4+
/NH
3
. Adequa ely high
neu aliza ion capaci y is he mos impo an ac o o p e equisi e o main aining he
s abili y o he p ocess a high o ganic loading. The con en o lowe ( ola ile) a y acids
(VFA) is one o he mos sensi i e indica o s o s abili y. Usually, he sum o C
2
–C
5
acids is
moni o ed, bu i is mo e app op ia e o moni o indi idual acids. E en a ela i ely high
concen a ion o ace ic acid can be emo ed quickly, bu highe acids usually pa alyze he
sys em o a longe ime [
4
]. The VFA/TIC (To al Ino ganic Ca bona e) pa ame e is he
a io o he sum o lowe a y acids exp essed by he equi alen o ace ic acid and he
neu alizing capaci y o med mainly by he bica bona e sys em. The i a ion pa ame e
de ec s a possible bu e de iciency and an excess o acids. I has become he mos aluable
indica o o p ocess s abili y, no only a he s a o he use o he echnology bu also
con inuously [
5
]. Méndez-Acos a e al. [
6
] used a Luenbe ge obse e o inc ease diges ion
s abili y by moni o ing ola ile a y acid (VFA) and o al alkalini y (TA) concen a ions in a
mul iple-inpu , mul iple-ou pu eedback con ol model. Fei kenhaue e al. [
7
] con i med
P ocesses 2021,9, 106 3 o 11
ha online ola ile a y acid (VFA) i a ion is a eliable me hod o measu ing subs a e
concen a ion wi hou he use o expensi e analy ical equipmen . They designed a eliable
measu ing cell o online i a ion o ola ile a y acids. Recalib a ion o he pH p obe
esis an o high sal concen a ions was only necessa y wice a week. Yuan and Zhu [
8
]
s udied a a ie y o inhibi o y subs ances and ound ha in e media e p oduc s a e he
p ima y cause o anae obic diges e upse o ailu e, including ee ammonia (FA), ola ile
a y acids (VFAs), and sul ide/sul a e. Howe e , hey a e essen ial nu ien s o bac e ial
g ow h and he anae obic diges ion p ocess.
1.2. Senso s and he Measu emen o he Pa ame e s
Many o he pa ame e s can be moni o ed, bu hey usually encoun e a mo e com-
plica ed ea men o he sludge sample be o e analysis. The esul s o e alua ion a e
a ailable wi h an imp ac ically long ime delay. I is ad isable o con inue looking o an
easily measu able and in o ma i e pa ame e , acco ding o which i would be possible o
eac immedia ely o he eme ging imbalance in he e men e . The p ocess biochemis y
sugges s he possibili y o apid cap u e o changes by moni o ing he dissol ed hyd ogen
concen a ion pa ame e . Acco ding o esea ch in he ield o was ewa e ea men and
om esea ch on e men e s o biogas plan s, he anae obic p ocess can be con olled in
connec ion wi h he measu emen o he concen a ion o he mos impo an chemical
in e media e-dissol ed dia omic hyd ogen H
2
(l). The li e a u e gi es se e al lab-scale
o pilo -scale examples, each using a di e en ype o H
2
(l) senso . H
2
(l) mos apidly
de ec s he upcoming o e load o he slowes g owing-me hanogenic mic obial biomass.
Dohányos s a es ha he as es de ec ion o o e load can be pe o med by measu ing H
2
(l)
in he ange o 0–200 mmol m
−3
, which co esponds o a pa ial equilib ium p essu e o H
2
up o 20,000 Pa [
9
]. Co d-Ruwisch e al. e i ied ha he pa ial p essu e o dissol ed H
2
in
he ange o 2–8 Pa co ela es linea ly wi h he o e load, and he no mal limi o s abili y
is no highe han 5–6 Pa. [
10
]. Pauss e al. indica e he common H
2
(l) concen a ion o
2–3.5
µ
mol dm
3
co ela ing o 200–350 Pa [
11
]. S ini asan ecommends in si u online
measu ing o he concen a ion o dissol ed H
2
wi h a Cla k oxygen p obe wi h e e sed
pola iza ion and a mo e powe ul elec ical signal ampli ie . I is a pola ized pla inum
elec ode, and he H
2
(l) sensi i i y should be linea be ween 1–50
µ
M co esponding o
100–5000 Pa [
12
]. The long- e m s abili y o he p obe and H
2
S in e e ence does no appea
o be known [
13
]. Al e na i ely, dissol ed hyd ogen can be en ained in he ca ie gas, and
he mix u e con inuously analyzed ch oma og aphically, bu his is no a sui able ope a ing
me hod o biogas plan ope a o s [
12
]. A che e al. e i ied he applicabili y o he
Exhaled Hyd ogen Moni o EHM (Gas Measu emen Ins umen s L d., Ren ew, Sco land)
in a biogas plan using a 6 m
3
e men e . The EHM can measu e gaseous hyd ogen in
biogas exac ly up o he limi o 0.1 Pa e en in indus ial condi ions. The esul s had o be
co ec ed acco ding o he H
2
S, CH
4
, and CO
2
c oss-sensi i i ies. Hyd ogen peaks in biogas
occu ed 3–6 h a e shock o e load. The esul s showed ha i would be mo e app op ia e
o measu e hyd ogen in he liquid phase [
14
]. S ong e al. desc ibed he cons uc ion and
use o a cheap senso , un o una ely wi h insu icien sensi i i y a he le el o 30 Pa [
15
].
Danne un e al. de eloped a sensi i e palladium me al-oxide-semiconduc o (Pd-MOS)
H
2
gas senso wi h a de ec ion limi o 0.1 Pa [
16
]. Appa en ly, his senso has no ye
been es ed o anae obic diges ion. Only a ew biogas plan s exis , which ely solely on
H
2
measu emen s o s abili y moni o ing. I hyd ogen is moni o ed a biogas plan s, i
is measu ed by elec ochemical senso s in he biogas. In he u u e, he measu emen s
o dissol ed H
2
could become an in e es ing al e na i e [
17
]. Wilcox e al. [
18
] es ed an
online bica bona e alkalini y (BA) senso and ecognized dis u bances by a neu al ne wo k.
They concluded ha he sys em is p ac ically usable and use ul in he case o an inle wi h
insu icien bu e ing capaci y. The au ho s [
19
] hypo hesize ha an imbalance in he AD
p ocess can lead o he accumula ion o sho -chain o ganic acids, as high concen a ions
o hese acids inhibi me hane o ma ion and, in ex eme cases, his can lead o he dea h
o he co esponding bac e ial popula ions. They a e based on he assump ion ha he e
P ocesses 2021,9, 106 4 o 11
is an analogy be ween he lo a o mic oo ganisms in he umen o a uminan and he
e men e eac o o a biogas plan . In a heal hy animal, he pan- lo a is p edominan ly
G am-nega i e and has a ious o ms. In he case o malnu i ion, his di e si y dec eases,
and G am-posi i e lac ic acid-p oducing s ep ococci soon p e ail and lac obacilli will
p edomina e. This condi ion is known as umen acidosis. Acco ding o he pa en , an
analogous change o he bac e ial popula ion om G am-nega i e o G am-posi i e in
he e men e is used as an indica o o p ocess in e up ion in a biogas plan . Bac e ial
de ec ion was pe o med by FT-MIR spec ome y.
Nguyen e al. [
20
] s udied wo signi ican s a egies o p omo e he s able pe o mance
o he AD p ocess, including moni o ing and con ol o e he p ocess. While he e is a con-
s an deba e on he impo ance o ins umen a ion e sus con ol s a egy, he expe ience
on bo h aspec s is limi ed in indus ial-scale AD ope a ions. Wi h he apid de elopmen
o ins umen a ion and au oma ic con ol, he implemen a ion and ope a ion cos o his
ad anced sys em is expec ed o dec ease. The op imis ic ou look o he upcoming decades
is ha small-scale AD plan s will be equipped wi h an au oma ic con ol sys em o be e
pe o mance. Meanwhile, a cen alized AD plan is s ill a easible op ion. Liu e al. [
21
]
in oduced a new con ol s a egy o ope a ing anae obic diges ion p ocesses e icien ly a
high load. The con ol sys em includes a cascade con olle embedded in o a ule-based
supe iso y sys em based on ex emum-seeking con ol. The con ol sys em measu es pH
and biogas p oduc ion a e and a ies he o ganic load by manipula ing he in luen low.
Good con ol pe o mances we e achie ed du ing he s a -up and s eady-s a e unning
ope a ions and du ing he ejec ion o dis u bances. The con ol sys em can un he p ocess
unde a high load condi ion and e icien ly ejec dis u bances wi hou explici measu e-
men o he in luen cha ac e is ics (Gaida e al. [
22
]). O e he las 40 yea s, many di e en
con ol me hodologies o subs a e eed con ol o anae obic diges ion p ocesses ha e been
p oposed in o de o inc ease plan e iciency and sus ainable long- e m ene gy p oduc ion.
This e iew shows ha al hough sophis ica ed con olle s exis , ull-scale biogas plan s a e
mos ly s ill ope a ed wi hou a closed-loop eed con ol. No ma e which applica ion, such
con ol always has o ind a comp omise be ween maximizing economic yield, minimizing
he ecological oo p in , and minimizing he isk o p ocess ailu e. Fo anae obic was ewa-
e ea men , con ol sys ems ha come close o his ideal exis , bu o ag icul u al as well
as indus ial biogas plan s, such con ol has no ye been de eloped, and nei he has been
success ully implemen ed and alida ed a ull-scale. The main challenges a e a lack o
obus and eliable p ocess moni o ing using online ins umen a ion and a conse a i e
indus y ha is eluc an o implemen ully au oma ed p ocess con ol s a egies.
Ou wo k aimed o e i y he possibili y o ea ly de ec ion o diges ion p ocess ins a-
bili y and eac o o e load by e alua ing he cou se o dissol ed hyd ogen concen a ion
using an ampe ome ic mic osenso .
2. Labo a o y Tes ing
Tes ing ook place in he Ins i u e o En i onmen al Technologies a VSB—Technical
Uni e si y Os a a, Czech Republic. One 230-day single-s age mesophilic mono-diges ion
expe imen was pe o med. The p ocess was conduc ed in a Te a o s IS o a y d um
bio eac o (INFORS HT, Bo mingen, Swi ze land); see he appa a us diag am in Figu e 1.
The d um eac o wi h a o al olume o 0.0187 m
3
was illed wi h 15.0 kg (app oxima ely
0.015 m
3
) o liquid inoculum, anae obic slu y, om he lab-scale (0.2 m
3
) psych ophilic
eac o p ocessing ood le o e s om uni e si y can een a psych ophilic condi ions
(18–22
◦
C). The inoculum was eed o pa icles la ge han 5 mm o educe he o ma ion
o loa ing c us s. Du ing he expe imen , he slu y was con inuously s i ed. The s i ing
was secu ed by o a ion o he eac o d um a ound he ho izon al axis. The o a ion speed
was se o 0.5 min
−1
. Diges ion empe a u e was se o 37
◦
C
±
1
◦
C. The main pa ame e s
o he inoculum a e lis ed in Table 1.
P ocesses 2021,9, 106 5 o 11
P ocesses 2021, 9, x FOR PEER REVIEW 5 o 11
was se o 0.5 min−1. Diges ion empe a u e was se o 37 °C ± 1 °C. The main pa ame e s
o he inoculum a e lis ed in Table 1.
Table 1. Inoculum, Subs a e, and Diges a e Pa ame e s.
Pa ame e Symbol, Uni Inoculum Subs a e Diges a e
Po en ial o Hyd ogen pH-H2O, - 7.63 3.4–5.6; mean 4.2 3.4–7.9, mean 7.1
To al Solids (105 °C) TS, w . % 2.96 11.2–24.9; mean 16.4 2.2–5.4; mean 3.6
Vola ile Solids (550 °C) VS, w . %TS 59.79 86.00–96.10; mean 92.90 50.00–70.60; mean 61.30
Vola ile Fa y Acids VFA, mg dm−3 3050 - 1999–15,856; mean 5352
To al Ino ganic Ca bona e TIC, mg dm−3 13,650 - 1226–14,489; mean 9773
Diges ion S abili y Ra io VFA/TIC, - 0.223 - 0.161–11.431; mean 1.323
Figu e 1. Appa a us diag am. 1. Ro a y d um eac o . 2. S a o connec ed o he base. 3. Liquid ba ch le el. 4. Po o
subs a e dosing and diges a e sampling. 5. Biogas ou le ube. 6. The mocouple. 7. Dissol ed hyd ogen senso . 8. Two
al es o sampling and e u n o biogas. 9. Gas low me e . 10. Po able gas analyze . 11. Wa e hea ed jacke .
Food le o e s o meals se ed in he uni e si y can een we e used as complex mono-
subs a e. Those le o e s we e no like common ki chen biowas e. I consis ed o unea en
Figu e 1.
Appa a us diag am. 1. Ro a y d um eac o . 2. S a o connec ed o he base. 3. Liquid ba ch le el. 4. Po o
subs a e dosing and diges a e sampling. 5. Biogas ou le ube. 6. The mocouple. 7. Dissol ed hyd ogen senso . 8. Two
al es o sampling and e u n o biogas. 9. Gas low me e . 10. Po able gas analyze . 11. Wa e hea ed jacke .
Table 1. Inoculum, Subs a e, and Diges a e Pa ame e s.
Pa ame e Symbol, Uni Inoculum Subs a e Diges a e
Po en ial o Hyd ogen pH-H2O, - 7.63 3.4–5.6; mean 4.2 3.4–7.9, mean 7.1
To al Solids (105 ◦C) TS, w . % 2.96 11.2–24.9; mean 16.4 2.2–5.4; mean 3.6
Vola ile Solids (550 ◦C) VS, w . %TS 59.79
86.00–96.10; mean 92.90
50.00–70.60; mean 61.30
Vola ile Fa y Acids VFA, mg dm−33050 - 1999–15,856; mean 5352
To al Ino ganic Ca bona e TIC, mg dm−313,650 - 1226–14,489; mean 9773
Diges ion S abili y Ra io VFA/TIC, - 0.223 - 0.161–11.431; mean 1.323
Food le o e s o meals se ed in he uni e si y can een we e used as complex mono-
subs a e. Those le o e s we e no like common ki chen biowas e. I consis ed o unea en
po ions o lunches, wi hou bones. The subs a e ob ained om he can een was sup-

P ocesses 2021,9, 106 6 o 11
plemen ed wi h a small amoun o d inking wa e o dec ease he con en o solids o a
pumpable le el. Subsequen ly, he mix u e was homogenized wi h TS-32T400V sc ew mill
(RM Gas o L d., P ague, Czech Republic) h ough a ma ix wi h ound holes (3 mm in di-
ame e ). The subs a e slu y was s o ed in a e ige a o a 4–6
◦
C o supp ess acidi ica ion.
The subs a e was dosed in o he d um eac o once e e y wo king day. The expe imen
las ed o 230 days, so we dosed he eac o 165 imes. The a e age dose was abou 80 g o
he subs a e. The egula size was 50 g, bu o he o e loading, we used a much la ge
amoun —up o 300 g. The main pa ame e s o he subs a e a e lis ed in Table 1.
The slu y empe a u e was con inuously measu ed by a he mocouple passing
h ough he ho izon al sha o he eac o in he cen e o he eac o . Da a we e manually
eco ded once daily. The biogas s eam om he eac o passed h ough a ube passing
om he gas space axially h ough he ho izon al sha o he eac o . Biogas p oduc-
ion was con inuously measu ed wi h a TG05 o a y d um gas me e (RITTER GmbH,
Schwabmünchen, Ge many). Gas olume inc emen s we e manually eco ded once daily.
The biogas composi ion was measu ed wi h a Biogas5000 po able analyze (GEOTECH
L d., Co en y, G ea B i ain) once a day in wo king days, p io o diges a e sampling
and subs a e dosing. The analyze used CH
4
and CO
2
in a ed senso s and O
2
and H
2
S
elec ochemical senso s. Du ing he gas composi ion measu emen s, he eac o o a ion
was s opped. The biogas sample was sucked h ough one al e and e u ned o he gas
space o he eac o by an adjacen al e. Immedia ely a e he analysis o he biogas
composi ion, a dissol ed hyd ogen senso was inse ed in o he liquid phase. A al e
(32 mm diame e ), commonly used o diges a e sampling and subs a e dosing, was used
o inse he H
2
senso . The senso was sealed wi h silicone ubbe . I usually ook 15 min
o s abilize he senso in he anae obic slu y. The o a ion o he eac o was esumed only
a e emo ing he senso and inse ing a dose o he subs a e.
The dissol ed hyd ogen senso was he MS 08 ampe ome ic mic osenso (AMT Anal-
ysenmess echnik GmbH, Ros ock, Ge many) wi h a s a ed de ec ion limi o 0.2
µ
g dm
−3
H
2
(l) and a ange o up o 1.5 mg dm
−3
H
2
(l); see Figu e 2. The H
2
senso used i s own
sepa a e empe a u e senso . The ips o bo h senso s we e always placed app oxima ely
30 mm below he su ace o he slu y. A e measu ing H
2
(l), a diges a e sample (app oxi-
ma ely 0.9
×
he olume o he subs a e dose) was d ained o analysis, and a dose o he
subs a e was in oduced in o he eac o . Thus, he diges a e sampling was pe o med a
he same equency as he subs a e sampling.
P ocesses 2021, 9, x FOR PEER REVIEW 6 o 11
po ions o lunches, wi hou bones. The subs a e ob ained om he can een was supple-
men ed wi h a small amoun o d inking wa e o dec ease he con en o solids o a pump-
able le el. Subsequen ly, he mix u e was homogenized wi h TS-32T400V sc ew mill (RM
Gas o L d., P ague, Czech Republic) h ough a ma ix wi h ound holes (3 mm in diam-
e e ). The subs a e slu y was s o ed in a e ige a o a 4–6 °C o supp ess acidi ica ion.
The subs a e was dosed in o he d um eac o once e e y wo king day. The expe imen
las ed o 230 days, so we dosed he eac o 165 imes. The a e age dose was abou 80 g
o he subs a e. The egula size was 50 g, bu o he o e loading, we used a much la ge
amoun —up o 300 g. The main pa ame e s o he subs a e a e lis ed in Table 1.
The slu y empe a u e was con inuously measu ed by a he mocouple passing
h ough he ho izon al sha o he eac o in he cen e o he eac o . Da a we e manually
eco ded once daily. The biogas s eam om he eac o passed h ough a ube passing
om he gas space axially h ough he ho izon al sha o he eac o . Biogas p oduc ion
was con inuously measu ed wi h a TG05 o a y d um gas me e (RITTER GmbH, Schwab-
münchen, Ge many). Gas olume inc emen s we e manually eco ded once daily. The
biogas composi ion was measu ed wi h a Biogas5000 po able analyze (GEOTECH L d.,
Co en y, G ea B i ain) once a day in wo king days, p io o diges a e sampling and sub-
s a e dosing. The analyze used CH4 and CO2 in a ed senso s and O2 and H2S elec o-
chemical senso s. Du ing he gas composi ion measu emen s, he eac o o a ion was
s opped. The biogas sample was sucked h ough one al e and e u ned o he gas space
o he eac o by an adjacen al e. Immedia ely a e he analysis o he biogas composi-
ion, a dissol ed hyd ogen senso was inse ed in o he liquid phase. A al e (32 mm
diame e ), commonly used o diges a e sampling and subs a e dosing, was used o inse
he H2 senso . The senso was sealed wi h silicone ubbe . I usually ook 15 min o s abi-
lize he senso in he anae obic slu y. The o a ion o he eac o was esumed only a e
emo ing he senso and inse ing a dose o he subs a e.
The dissol ed hyd ogen senso was he MS 08 ampe ome ic mic osenso (AMT
Analysenmess echnik GmbH, Ros ock, Ge many) wi h a s a ed de ec ion limi o 0.2 µg
dm−3 H2(l) and a ange o up o 1.5 mg dm−3 H2(l); see Figu e 2. The H2 senso used i s own
sepa a e empe a u e senso . The ips o bo h senso s we e always placed app oxima ely
30 mm below he su ace o he slu y. A e measu ing H2(l), a diges a e sample (app ox-
ima ely 0.9× he olume o he subs a e dose) was d ained o analysis, and a dose o he
subs a e was in oduced in o he eac o . Thus, he diges a e sampling was pe o med a
he same equency as he subs a e sampling.
Figu e 2. Ampe ome ic mic osenso and i s loca ion in he eac o .
Figu e 2. Ampe ome ic mic osenso and i s loca ion in he eac o .
The ollowing analyses we e egula ly pe o med on subs a e and diges a e sam-
ples: he de e mina ion o pH wi h a 340i me e a SenTix 41 p obe (WTW, Weilheim,
P ocesses 2021,9, 106 7 o 11
Ge many) [
23
], he de e mina ion o o al solids (TS, d ying a 105
◦
C in an O
2
a mosphe e
o cons an weigh , 2.0% RSD) by a DLB 160 3A mois u e analyze wi h a halogen lamp
(KERN, Balingen, Ge many) [
24
], he de e mina ion o he con en o o ganic subs ances,
namely loss on igni ion (Vola ile Solids, VS, igni ing a 550
◦
C in an O
2
a mosphe e o
cons an weigh , 5.0% RSD) by he mog a ime ic analyze TGA 701 (LECO, Ben on Ha -
bo , MI, USA) [
25
]. The VFA/TIC a io in he diges a e slu y was de e mined by a TIM
BIOGAS V02.2 au oma ic i a o (HACH Lange, Düsseldo , Ge many) [26].
3. Resul s and Discussion
Du ing he 230 days o mono-diges ion, he TS con en o he subs a e was mos
o en a ound 16%, wi h a loss on igni ion o abou 93% TS. The o ganic loading a e (OLR)
was pu pose ully changed so ha he e was a signi ican o e load wi h he e olu ion o
hyd ogen and subsequen eco e y. Calcula ed o all 230 days o he expe imen , he OLR
was a ied in he ange o 0–3.02 kg
VS
m
−3
d
−1
, wi h a mean o 0.858 kg
VS
m
−3
day
−1
.
Calcula ed jus o he days o eeding, he mean OLR was 1.396 kg
VS
m
−3
d
−1
, which is
s ill a a he low load o he mesophilic eac o . The mean alue o hyd aulic e en ion ime
(HRT) was 259 days. The ela ion be ween OLR and HRT is isible in Figu e 3. Due o he easy
o e load, i would be possible o conside sho ening he HRT only when co- e men ing
he subs a e in a mo e nu i ionally balanced mix u e.
P ocesses 2021, 9, x FOR PEER REVIEW 8 o 13
Figu e 3. Rela ion be ween o ganic loading and e en ion ime.
The no malized biogas p oduc ion om inoculum was high due o he ansi ion
om psych ophilic o mesophilic p ocess, bu wi hin 3 days i d opped apidly. This was
ollowed by a pe iod o g adual acclima iza ion and an inc ease in gas p oduc ion un il
day 107. The mos e icien p ocess ook place a a load o abou 2.5 kgVS m−3 d−1 and an
HRT o 65 days. Un il day 123, he CH4 con en emained high, bu gas p oduc ion was
al eady declining due o o e load. I was no un il a ound day 170 ha he p ocess s abi-
lized again due o he omission o subs a e doses and, subsequen ly, only low loading
(see Figu e 4). Sho ly a e ebalancing, CH4 p oduc ion was unusually high, which is
expec ed due o he me hana ion o accumula ed ola ile acids.
The main pa ame e s o he diges a e a e lis ed in Table 1. F om Figu e 5, i is clea
ha he pH alue in he eac o dec eased much la e han when o e loading s a ed, and
VFA accumula ion s a ed, which is also well-known in o ma ion. The VFA/TIC limi
alue de e mining s abili y o a gi en p ocess appea s o be app oxima ely 0.4. I is he e-
o e in line wi h he commonly s a ed ange [26].
Figu e 3. Rela ion be ween o ganic loading and e en ion ime.
The no malized biogas p oduc ion om inoculum was high due o he ansi ion
om psych ophilic o mesophilic p ocess, bu wi hin 3 days i d opped apidly. This was
ollowed by a pe iod o g adual acclima iza ion and an inc ease in gas p oduc ion un il day
107. The mos e icien p ocess ook place a a load o abou 2.5 kg
VS
m
−3
d
−1
and an HRT
o 65 days. Un il day 123, he CH
4
con en emained high, bu gas p oduc ion was al eady
declining due o o e load. I was no un il a ound day 170 ha he p ocess s abilized again
due o he omission o subs a e doses and, subsequen ly, only low loading (see Figu e 4).
Sho ly a e ebalancing, CH
4
p oduc ion was unusually high, which is expec ed due o
he me hana ion o accumula ed ola ile acids.
The main pa ame e s o he diges a e a e lis ed in Table 1. F om Figu e 5, i is clea ha
he pH alue in he eac o dec eased much la e han when o e loading s a ed, and VFA
accumula ion s a ed, which is also well-known in o ma ion. The VFA/TIC limi alue
de e mining s abili y o a gi en p ocess appea s o be app oxima ely 0.4. I is he e o e in
line wi h he commonly s a ed ange [26].
P ocesses 2021,9, 106 8 o 11
P ocesses 2021, 9, x FOR PEER REVIEW 8 o 13
Figu e 3. Rela ion be ween o ganic loading and e en ion ime.
The no malized biogas p oduc ion om inoculum was high due o he ansi ion
om psych ophilic o mesophilic p ocess, bu wi hin 3 days i d opped apidly. This was
ollowed by a pe iod o g adual acclima iza ion and an inc ease in gas p oduc ion un il
day 107. The mos e icien p ocess ook place a a load o abou 2.5 kgVS m−3 d−1 and an
HRT o 65 days. Un il day 123, he CH4 con en emained high, bu gas p oduc ion was
al eady declining due o o e load. I was no un il a ound day 170 ha he p ocess s abi-
lized again due o he omission o subs a e doses and, subsequen ly, only low loading
(see Figu e 4). Sho ly a e ebalancing, CH4 p oduc ion was unusually high, which is
expec ed due o he me hana ion o accumula ed ola ile acids.
The main pa ame e s o he diges a e a e lis ed in Table 1. F om Figu e 5, i is clea
ha he pH alue in he eac o dec eased much la e han when o e loading s a ed, and
VFA accumula ion s a ed, which is also well-known in o ma ion. The VFA/TIC limi
alue de e mining s abili y o a gi en p ocess appea s o be app oxima ely 0.4. I is he e-
o e in line wi h he commonly s a ed ange [26].
Figu e 4. Biogas p oduc ion and i s CH4con en .
P ocesses 2021, 9, x FOR PEER REVIEW 9 o 13
Figu e 4. Biogas p oduc ion and i s CH4 con en .
Figu e 5. VFA and TIC e sus pH.
Thanks o a signi ican educ ion in dosing, he ex eme o e load (VFA/TIC peak o
11.4) was o e come in abou 55 days. The cou se o he dissol ed hyd ogen concen a ion
is shown in Figu e 6. The dissol ed hyd ogen concen a ion measu ed by he ampe ome -
ic mic osenso anged om 0.039 mg dm−3 o 0.425 mg dm−3. Apa om o e load, he
ypical H2(l) concen a ion was 0.12 ± 0.04 mg dm−3, co esponding o abou 6000 Pa pa ial
p essu e. When o e loaded, i eached 0.40 mg dm−3 H2(l), co esponding o abou 20,000
Pa pa ial p essu e. Simila ly, high alues we e measu ed e en a e he ini ial hea ing o
he inoculum a he beginning o he expe imen . I he inc eased hyd ogen pe sis ed o
se e al days, he acid con en inc eased apidly. The maximum H2(l) concen a ion meas-
u ed by us he e o e app oxima ely co esponds o he alue gi en by Dohányos [6]. The
small peak o he H2(l) ha appea s a ound day 105 was caused by he ou days o eac o
s a a ion due o Eas e b eak ollowed by he high doses o subs a e.
Figu e 5. VFA and TIC e sus pH.
Thanks o a signi ican educ ion in dosing, he ex eme o e load (VFA/TIC peak o
11.4) was o e come in abou 55 days. The cou se o he dissol ed hyd ogen concen a ion is
shown in Figu e 6. The dissol ed hyd ogen concen a ion measu ed by he ampe ome ic
mic osenso anged om 0.039 mg dm
−3
o 0.425 mg dm
−3
. Apa om o e load, he
ypical H
2
(l) concen a ion was 0.12
±
0.04 mg dm
−3
, co esponding o abou 6000 Pa
pa ial p essu e. When o e loaded, i eached 0.40 mg dm
−3
H
2
(l), co esponding o abou
20,000 Pa pa ial p essu e. Simila ly, high alues we e measu ed e en a e he ini ial hea -
ing o he inoculum a he beginning o he expe imen . I he inc eased hyd ogen pe sis ed
o se e al days, he acid con en inc eased apidly. The maximum H
2
(l) concen a ion
measu ed by us he e o e app oxima ely co esponds o he alue gi en by Dohányos [
6
].
The small peak o he H
2
(l) ha appea s a ound day 105 was caused by he ou days o
eac o s a a ion due o Eas e b eak ollowed by he high doses o subs a e.
An al e na i e p ocess s abili y pa ame e was p oposed as he a io o dissol ed
hyd ogen concen a ion o neu aliza ion capaci y; see Figu e 7. Howe e , so a , his
pa ame e does no appea o be signi ican ly mo e sensi i e han he VFA/TIC a io
used. A e he heigh co ec ion o he peaks, he on o bo h peaks is si ua ed on he
same days o he p ocess. I will be necessa y o es his beha io in se e al di e en
co- e men a ion p ocesses. In he case o he p ocess moni o ed he e, eaching he alue
o 1.0 o he new pa ame e (H
2
(l)/TIC) * 48,000 announced he onse o ins abili y, bu
his happened app oxima ely on he same day when he VFA/TIC a io inc eased abo e
P ocesses 2021,9, 106 9 o 11
0.4. The acid o ma ion is a apid p ocess. Some p ocesses a e likely o equi e o e load
supp ession a an ea ly s age. Gi en ha he de ec ion limi o H
2
(l) o he ampe ome ic
senso is 0.5
µ
g dm
−3
, which co esponds o a pa ial p essu e o H
2
(g) o 10 Pa, and
some li e a u e epo s an incipien o e load no mally om 2 Pa [
9
], i is app op ia e
o sea ch o he mo e sensi i e senso . Fu he mo e, he obus ness and se ice li e o
he ampe ome ic senso in he sludge en i onmen is no e y sa is ac o y. The he mal
conduc i i y de ec o should mee he equi emen s, bu he e may be a p oblem wi h
sensi i i y. Fu he mo e, he cou se o H
2
(l) concen a ion should be co ela ed wi h he
concen a ion o acids de e mined by GC-MS o iso achopho esis.
P ocesses 2021, 9, x FOR PEER REVIEW 10 o 13
Figu e 6. Dissol ed H2 concen a ion.
An al e na i e p ocess s abili y pa ame e was p oposed as he a io o dissol ed hy-
d ogen concen a ion o neu aliza ion capaci y; see Figu e 7. Howe e , so a , his pa-
ame e does no appea o be signi ican ly mo e sensi i e han he VFA/TIC a io used.
A e he heigh co ec ion o he peaks, he on o bo h peaks is si ua ed on he same
days o he p ocess. I will be necessa y o es his beha io in se e al di e en co- e -
men a ion p ocesses. In he case o he p ocess moni o ed he e, eaching he alue o 1.0
o he new pa ame e (H2(l)/TIC) * 48,000 announced he onse o ins abili y, bu his hap-
pened app oxima ely on he same day when he VFA/TIC a io inc eased abo e 0.4. The
acid o ma ion is a apid p ocess. Some p ocesses a e likely o equi e o e load supp es-
sion a an ea ly s age. Gi en ha he de ec ion limi o H2(l) o he ampe ome ic senso is
0.5 μg dm−3, which co esponds o a pa ial p essu e o H2 (g) o 10 Pa, and some li e a u e
epo s an incipien o e load no mally om 2 Pa [9], i is app op ia e o sea ch o he
mo e sensi i e senso . Fu he mo e, he obus ness and se ice li e o he ampe ome ic
senso in he sludge en i onmen is no e y sa is ac o y. The he mal conduc i i y de ec-
o should mee he equi emen s, bu he e may be a p oblem wi h sensi i i y. Fu he -
mo e, he cou se o H2(l) concen a ion should be co ela ed wi h he concen a ion o ac-
ids de e mined by GC-MS o iso achopho esis.
Figu e 6. Dissol ed H2concen a ion.
P ocesses 2021, 9, x FOR PEER REVIEW 10 o 11
Figu e 7. Dissol ed H
2
e sus VFA/TIC a io.
The g aph in Figu e 7 depic s he alues o he VFA/TIC and H
2(l)
a iables du ing
he expe imen . We ha e compu ed he Pea son co ela ion coe icien o hese a iables,
and he esul is 0.331, wi h he p- alue almos 0. The linea co ela ion be ween hese wo
a iables is e y weak, as may be seen om he g aph. The alues o he H
2
(l)
a iable do
no ollow he VFA/TIC a iable cou se. The amoun o dissol ed hyd ogen is no a ec ed
by he eac o o e loading, and o he ac o s play a ole in i s concen a ion change.
4. Conclusions
The labo a o y expe imen con i med he possibili y o using an ampe ome ic mi-
c osenso o dissol ed hyd ogen o de ec he ins abili y o he anae obic diges ion p o-
cess. Un o una ely, he de ec ion limi o he speci ic senso used was no low enough o
ully e eal he beginnings o o e loading. So a , i has no been possible o p o e ha
he newly p oposed p ocess s abili y pa ame e in he o m o he a io o dissol ed hy-
d ogen concen a ion and neu aliza ion capaci y would signi ican ly help o de ec o e -
load. The i s s a is ical e alua ion o he ela ionship shows ha he e should be a linea
co ela ion be ween he VFA/TIC and H
2
(l), bu i is a ec ed by he o e loading o he
eac o . Deep expe imen s need o be pe o med o e alua e he ela ionships.
Au ho Con ibu ions: D.P. was esponsible o he labo a o y wo k, pe o ming he expe imen s.
J.R. is esponsible o he s udy design and he main ideas. J.P. was esponsible o da a analysis,
K.S. was esponsible o he o e all pape p epa a ion and language, R.B. ocused on he o e all
expe imen and i s ele an ness. All au ho s ha e ead and ag eed o he published e sion o he
manusc ip .
Funding: The wo k was suppo ed by he Minis y o Educa ion, You h and Spo s o he Czech
Republic unde he p ojec s ERDF “Ins i u e o En i onmen al Technology—Excellen Resea ch”
[No. CZ.02.1.01/0.0/0.0/16_019/0000853], La ge Resea ch In as uc u e ENREGAT [No.
LM2018098], and he Ope a ional P og amme Resea ch, De elopmen and Educa ion [No.
CZ.02.1.01./0.0/0.0/17_049/0008419 COOPERATION.
Ins i u ional Re iew Boa d S a emen : No applicable.
In o med Consen S a emen : No applicable.
Figu e 7. Dissol ed H2 e sus VFA/TIC a io.
The g aph in Figu e 7depic s he alues o he VFA/TIC and H
2(l)
a iables du ing
he expe imen . We ha e compu ed he Pea son co ela ion coe icien o hese a iables,
and he esul is 0.331, wi h he p- alue almos 0. The linea co ela ion be ween hese wo
a iables is e y weak, as may be seen om he g aph. The alues o he H
2
(l) a iable do
no ollow he VFA/TIC a iable cou se. The amoun o dissol ed hyd ogen is no a ec ed
by he eac o o e loading, and o he ac o s play a ole in i s concen a ion change.