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The Effect of Inert Fuel Compounds on Flame Characteristics

Abstract

To describe the effects of inert compounds in gaseous fuel, experiments on three different process burners (staged fuel burner, staged air burner, and low-calorific burner) were carried out. The tested burners are commercially available, but they were specially designed for experimental usage. Tests were carried out in the semi-industrial burner testing facility to investigate the influence of inert gases on the flame characteristics, emissions, and heat flux to the combustion chamber wall. Natural gas was used as a reference fuel, and, during all tests, thermal power of 500 kW was maintained. To simulate the combustion of alternative fuels with lower LHV, N2 and CO2 were used as diluents. The inert gas in the hydrocarbon fuel at certain conditions can lower NOx emissions (up to 80%) and increase heat flux (up to 5%). Once incombustible compounds are present in the fuel, the higher amount of fuel flowing through nozzles affects the flow in the combustion chamber by increasing the Reynolds number. This can change the flame pattern and temperature field, and it can be both positive and negative, depending on actual conditions.

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The Effect of Inert Fuel Compounds on Flame Characteristics

Author: Hudák, Igor; Skryja, Pavel; Bojanovský, Jiří; Jegla, Zdeněk; Krňávek, Martin
Publisher: MDPI
Year: 2021
DOI: 10.3390/en15010262
Source: https://dspace.vut.cz/bitstreams/967a379c-8557-48a8-95d7-6fd8b85bd2f8/download
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Ci a ion: Hudák, I.; Sk yja, P.;
Bojano ský, J.; Jegla, Z.; K ˇná ek, M.
The E ec o Ine Fuel Compounds
on Flame Cha ac e is ics. Ene gies
2022,15, 262. h ps://doi.o g/
10.3390/en15010262
Academic Edi o : Fla io Ca esana
Recei ed: 29 No embe 2021
Accep ed: 27 Decembe 2021
Published: 31 Decembe 2021
Publishe ’s No e: MDPI s ays neu al
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Copy igh : © 2021 by he au ho s.
Licensee MDPI, Basel, Swi ze land.
This a icle is an open access a icle
dis ibu ed unde he e ms and
condi 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/).
ene gies
A icle
The E ec o Ine Fuel Compounds on Flame Cha ac e is ics
Igo Hudák1, Pa el Sk yja 1, Jiˇ íBojano ský1, Zdenˇek Jegla 1,* and Ma in K ˇná ek 2
1Ins i u e o P ocess Enginee ing, B no Uni e si y o Technology, Technická2896/2,
616 69 B no, Czech Republic; igo .hudak@ u b .cz (I.H.); [email p o ec ed].cz (P.S.);
Ji i.Bojano sky@ u b .cz (J.B.)
2E eco B no, s. .o., Hudco a 76d, 621 00 B no-Medlánky, Czech Republic; [email p o ec ed]
*Co espondence: [email p o ec ed]
Abs ac :
To desc ibe he e ec s o ine compounds in gaseous uel, expe imen s on h ee di e en
p ocess bu ne s (s aged uel bu ne , s aged ai bu ne , and low-calo i ic bu ne ) we e ca ied ou . The
es ed bu ne s a e comme cially a ailable, bu hey we e specially designed o expe imen al usage.
Tes s we e ca ied ou in he semi-indus ial bu ne es ing acili y o in es iga e he in luence o ine
gases on he lame cha ac e is ics, emissions, and hea lux o he combus ion chambe wall. Na u al
gas was used as a e e ence uel, and, du ing all es s, he mal powe o 500 kW was main ained. To
simula e he combus ion o al e na i e uels wi h lowe LHV, N
2
and CO
2
we e used as diluen s. The
ine gas in he hyd oca bon uel a ce ain condi ions can lowe NO
x
emissions (up o 80%) and
inc ease hea lux (up o 5%). Once incombus ible compounds a e p esen in he uel, he highe
amoun o uel lowing h ough nozzles a ec s he low in he combus ion chambe by inc easing
he Reynolds numbe . This can change he lame pa e n and empe a u e ield, and i can be bo h
posi i e and nega i e, depending on ac ual condi ions.
Keywo ds: low-calo i ic bu ne ; low NOxbu ne ; combus ion; ine gas; al e na i e gaseous uels
1. In oduc ion
To ul ill demands based on documen s such as he so-called g een deal o Eu ope [
1
],
i is necessa y o p o ide new design solu ions and op imize p ocess bu ne s o a ious
al e na i e uels. One o he possibili ies is he simul aneous o al e na e combus ion
o gaseous uels such as na u al gas and uels om al e na i e sou ces (biogas plan s,
py olysis plan s, algae [
2
]). Al e na i e uels p oduced, o example, in biogas s a ions and
py olysis uni s a e cha ac e ized by hei a iable composi ion. Thus, hei combus ion can
cause p oblems. Al e na i e uels wi h a lowe hea ing alue (LHV) a e usually combus ed
in bu ne s speci ically designed o he combus ion o a pa icula uel. The LHV in his
ype o uel is lowe ed by he p esence o ine gases (ni ogen, ca bon dioxide, and o he s).
To sus ain su icien ene gy powe in he u naces o boile s, i is necessa y o deli e a
highe amoun o uel in o he combus ion chambe (compa ed wi h he combus ion o
na u al gas). Usually, con en ional bu ne s ini ially designed o he combus ion o na u al
gas and uels wi h simila LHV a e no designed o be used along wi h low-calo i ic uels.
The e o e, i is usually necessa y o change he bu ne design. On he o he hand, a as
amoun o non-combus ible pa icles can be a eason o use al e na i e low-calo i ic uels
because o hei abili y o lowe empe a u e peaks and hus educe he e ec o he mal
NO
x
nuclea ion. The u iliza ion o al e na i e uels can also be a solu ion o abide by
inc easingly s ingen legisla i e limi s.
Exis ing esea ch ha deals wi h he combus ion o gaseous uels wi h ine com-
pounds (usually ca bon dioxide, ni ogen, a gon, wa e , and wa e apo ) and hei e ec s
on lame cha ac e is ics and CO and NO
x
emissions can be di ided in o wo basic ca ego ies.
The i s ca ego y is he dilu ion o he noble uel, such as me hane o na u al gas (including
esea ch wi h biogas—usually 60% ol. CH
4
, 40% ol. CO
2
), wi h he ine compound. On
Ene gies 2022,15, 262. h ps://doi.o g/10.3390/en15010262 h ps://www.mdpi.com/jou nal/ene gies
Ene gies 2022,15, 262 2 o 18
he o he hand, he second ca ego y con ains expe imen s wi h syn he ic gases (syngas) o
was e gases composed o combus ible compounds such as me hane, hyd ogen, and ca bon
monoxide and con aining incombus ible elemen s.
Se e al esea ch g oups ha e in es iga ed he combus ion o dilu ed gaseous uels
wi h hyd oca bons as he main combus ible componen . Fo example, Li e al. [
3
] conduc ed
expe imen s and nume ical simula ions o add ni ogen, ca bon dioxide, a gon, and wa e
apo in o me hane. The addi ion o s eam o he me hane lame was also examined
by Zhao e al. [
4
]. The in luence o supe hea ed wa e apo and CO
2
on me hane/ai
p emixed lames was expe imen ally in es iga ed by Kobayashi e al. [
5
,
6
]. To summa ize,
dilu ion by wa e and wa e apo , once added o he lame, signi ican ly lowe s NO
x
emissions in he lue gas. Mo eo e , a e s eam addi ion, a change was obse ed in he
decomposi ion o me hane in o OH adicals. Fu he mo e, he s eam added in o he lame
esul ed in a dec ease in he OH concen a ion in he lame; hus, a he same ime, i was
possible o obse e a dec ease in CH adicals, which esul ed in he supp ession o p omp
NO
x
. I was also obse ed ha he e ec o dilu ion by CO
2
is highe han dilu ion by
wa e , i.e., when ecycled lue gas is used, CO
2
is p edominan . Mo eo e , Pa k e al. [
7
]
e ealed ha he addi ion o H2O signi ican ly in luenced NO nuclea ion.
Mo e s udies ega ding he educ ion o NO
x
emissions whe e ine gases such as CO
2
and N
2
we e added o he uel we e conduc ed by Gla bo g e al. [
8
], Rang azi e al. [
9
],
De i e al. [
10
] (combus ion o biogas), and Sal ado e al. [
11
] (addi ion o N
2
). These
expe imen s e ealed ha he eac ion o CO
2
wi h hyd oca bons could con ibu e o
CO o ma ion, which can lead o nea -bu ne co osion and slagging. Mo eo e , i was
ound ha A dilu ion is less e ec i e han N
2
dilu ion ega ding educing NO
x
o ma ion.
Reduc ion o NO
x
can be achie ed by inc easing he ai su plus ( educ ion up o 30%), bu
when he ai is ully subs i u ed wi h ni ogen, he educ ion can be 60%. Fu he mo e,
du ing expe imen s wi h biogas, Dai e al. [
12
] e ealed ha a highe concen a ion o
CO
2
and lowe uel empe a u e c ea ed uns able condi ions o combus ion. Fu he mo e,
Hin on e al. [
13
] ound ou ha he highe p essu e o biogas led o a dec ease in bu ning
eloci y; howe e , a highe biogas empe a u e had he opposi e e ec .
Fo example, he combus ion o syngas and i s dilu ion was examined by
Chun e al. [14]
.
Among he esul s desc ibed abo e, i was disco e ed ha an inc ease in N adicals leads
o mo e signi ican NO
x
p oduc ion. Kied zynska e al. [
15
] used CFD o analyze he
co-combus ion o na u al gas and syngas in an unmodi ied bu ne . I was ound ha
i is possible o add only a small amoun o syngas (up o 10% o he mal sha e) be o e
eaching he bu ne limi . Fu he mo e, in e changeabili y be ween na u al gas and o he
enewable gases was s udied by Maznoy e al. [
16
]. The esea ch was mainly ocused on
s abili y limi s, adia ion e iciency, and CO/NO
x
emissions, which we e s udied du ing
he expe imen s. The addi ion o CO
2
educed NO
x
emissions bu o med a colde lame,
which esul ed in a CO emission inc ease. I was con i med ha uel in e changeabili y
is possible and can inc ease he adia ion e iciency in adial bu ne s. Dai e al. [
12
] also
examined lame s abili y, whe e i was disco e ed ha a lowe a io o me hane in uel
mo i a ed he lame li ing, while, on he o he hand, yellow ipping was mo i a ed by a
highe me hane con en . Flame s abili y was also pa ly in es iga ed by Song e al. [
17
]. A
as amoun o an ine compound can nega i ely a ec lame s abili y, and when a speci ic
limi is eached, he lame can ex inguish.
F om he e iew, i is possible o see he e ec on mul iple pa ame e s once an ine
compound is p esen in he gaseous uel. Howe e , mos s udies ha e been ca ied ou in
labo a o y condi ions, o hei esul s we e acqui ed by compu e simula ion, which used da a
om measu emen s on small-scale de ices. The au ho s o his s udy ca ied ou expe imen s
on a semi-indus ial acili y ha had simila pa ame e s o some o he smalle u naces. The
main con ibu ion o his s udy o he p e ious esea ch is he desc ip ion o he changes
in he hea lux, bu also he cla i ica ion and alida ion o p io esul s ega ding he NO
x
emissions and especially in lame empe a u es, which a e desc ibed by empe a u e p o iles.
Fu he mo e, h ee bu ne s wi h di e en designs we e used and compa ed ega ding he
Ene gies 2022,15, 262 3 o 18
emissions, lame cha ac e is ics, lame empe a u es, and hea lux. This s udy aimed o e eal
he possibili ies o uel in e changeabili y in con en ional p ocess bu ne s and o ind limi s
while inc easing he amoun o ine compounds in he uel.
2. Ma e ials and Me hods
2.1. Tes Equipmen
Combus ion es s we e ca ied ou a he bu ne es ing acili y (Figu e 1). The acili y
is designed o pe o m combus ion es s o bu ne s wi h he mal powe up o 1.8 MW and
collec expe imen al da a o he u he assessmen and e i ica ion o nume ical simula ion
esul s. Du ing he combus ion es wi h low-calo i ic uels, he bu ne s’ he mal ou pu
was se o 500 kW (and kep a his alue du ing each es ), and pa ame e s such as NO
x
and CO emissions, lue gas empe a u e, hea lux o he wall o he combus ion chambe
as a measu e o he mal e iciency, dis ibu ion o in- lame empe a u es in he ho izon al
symme y plane o he combus ion chambe , and he s abili y, shape, and dimensions o
he lame we e in es iga ed. In addi ion, he mal powe was eleased by he combus ion o
ansi na u al gas ( o a e age composi ion, see Table 1), u he dilu ed wi h ine gases
such as ni ogen and ca bon dioxide, o in es iga e hei e ec on he lame cha ac e is ics.
Ene gies 2022, 15, x FOR PEER REVIEW 3 o 18
compa ed ega ding he emissions, lame cha ac e is ics, lame empe a u es, and hea
lux. This s udy aimed o e eal he possibili ies o uel in e changeabili y in con en ional
p ocess bu ne s and o ind limi s while inc easing he amoun o ine compounds in he
uel.
2. Ma e ials and Me hods
2.1. Tes Equipmen
Combus ion es s we e ca ied ou a he bu ne es ing acili y (Figu e 1). The acili y
is designed o pe o m combus ion es s o bu ne s wi h he mal powe up o 1.8 MW and
collec expe imen al da a o he u he assessmen and e i ica ion o nume ical simula-
ion esul s. Du ing he combus ion es wi h low-calo i ic uels, he bu ne s’ he mal ou -
pu was se o 500 kW (and kep a his alue du ing each es ), and pa ame e s such as
NOx and CO emissions, lue gas empe a u e, hea lux o he wall o he combus ion
chambe as a measu e o he mal e iciency, dis ibu ion o in- lame empe a u es in he
ho izon al symme y plane o he combus ion chambe , and he s abili y, shape, and di-
mensions o he lame we e in es iga ed. In addi ion, he mal powe was eleased by he
combus ion o ansi na u al gas ( o a e age composi ion, see Table 1), u he dilu ed
wi h ine gases such as ni ogen and ca bon dioxide, o in es iga e hei e ec on he
lame cha ac e is ics.
Figu e 1. Semi-indus ial bu ne es ing acili y.
Table 1. A e age na u al gas composi ion du ing he combus ion es s.
CH4 C2H6 C3H8 i-C4H8 n-C4H8 i-C5H10 n-C5H10 C6+ CO2 N2
[% mol.] 96.486 2.593 0.127 0.043 0.021 0.005 0.003 0.024 0.333 0.365
The cen al appa a us o he acili y is a wo-shell ho izon al wa e -cooled combus-
ion chambe wi h an inne diame e o 1 m and an ou e leng h o 4 m. The on and he
ea side o he chambe a e insula ed wi h a high- empe a u e ib ous lining wi h a hick-
ness o 100 mm. The cooling shell o he combus ion chambe is di ided in o se en indi-
idual sec ions wi h an independen supply o cooling wa e . Each sec ion is equipped
wi h senso s o measu e he low a e, inle , and ou le empe a u e o cooling wa e . Wa-
e low a e is measu ed by u bine low me e s, and inle and ou le empe a u es a e
measu ed by esis ance he mome e s placed in he s eel shea h.
Be o e he lue gas is eleased in o he a mosphe e, i lows om he combus ion
chambe h ough he lue gas s ack. The e a e h ee measu emen and sampling spo s o
measu ing he p essu e in he combus ion chambe , lue gas empe a u e, and lue gas
composi ion. The lue gas analysis and lue gas empe a u e measu emen s a e p o ided
by he lue gas analyze TESTO 350-XL. The analysis box is equipped wi h elec ochemical
senso s o he eal- ime measu emen o O2, CO, CO2, NO, and NO2 concen a ions in he
d y lue gas. The lue gas empe a u e is measu ed using an R- ype he mocouple.
Figu e 1. Semi-indus ial bu ne es ing acili y.
Table 1. A e age na u al gas composi ion du ing he combus ion es s.
CH4C2H6C3H8i-C4H8n-C4H8i-C5H10 n-C5H10 C6+ CO2N2
[% mol.] 96.486 2.593 0.127 0.043 0.021 0.005 0.003 0.024 0.333 0.365
The cen al appa a us o he acili y is a wo-shell ho izon al wa e -cooled combus ion
chambe wi h an inne diame e o 1 m and an ou e leng h o 4 m. The on and he ea
side o he chambe a e insula ed wi h a high- empe a u e ib ous lining wi h a hickness
o 100 mm. The cooling shell o he combus ion chambe is di ided in o se en indi idual
sec ions wi h an independen supply o cooling wa e . Each sec ion is equipped wi h
senso s o measu e he low a e, inle , and ou le empe a u e o cooling wa e . Wa e low
a e is measu ed by u bine low me e s, and inle and ou le empe a u es a e measu ed
by esis ance he mome e s placed in he s eel shea h.
Be o e he lue gas is eleased in o he a mosphe e, i lows om he combus ion
chambe h ough he lue gas s ack. The e a e h ee measu emen and sampling spo s o
measu ing he p essu e in he combus ion chambe , lue gas empe a u e, and lue gas
composi ion. The lue gas analysis and lue gas empe a u e measu emen s a e p o ided
by he lue gas analyze TESTO 350-XL. The analysis box is equipped wi h elec ochemical
senso s o he eal- ime measu emen o O
2
, CO, CO
2
, NO, and NO
2
concen a ions in he
d y lue gas. The lue gas empe a u e is measu ed using an R- ype he mocouple.
Combus ion ai is supplied o he on o he combus ion chambe using a high-
p essu e an equipped wi h a equency con e e . The maximum an ou pu is app ox-
ima ely 4500 m
N3
/h wi h a maximum o e p essu e o 11.2 kPa. The ai duc is also
Ene gies 2022,15, 262 4 o 18
equipped wi h a p ehea ing uni o combus ion ai p e- ea men . The e o e, combus ion
ai can be p ehea ed up o 500 ◦C.
The es ing acili y is equipped wi h a sophis ica ed da a collec ion and sa e y sys em.
The sys em o da a collec ion enables au oma ic da a collec ion e e y second o
wo minu es
and da a collec ion upon he ope a o ’s eques . Collec ed da a include low a es, p essu es,
and empe a u es o combus ion ai , uel, ine gases, and cooling wa e . The sa e y sys em
ensu es he sa e and eliable ope a ion o he es ing acili y using he in o ma ion om he
senso s, e.g., i p e en s p ehea ing o cooling wa e and lame blow-o .
2.2. Me hodology
The expe imen was i s ca ied ou wi h he e e ence uel—in his case, na u al gas
(composi ion Table 1). All he esul s ob ained wi h low-calo i ic uels we e compa ed o
his e e ence uel. Low-calo i ic uels a e speci ic o hei con en o non-combus ible
compounds, which lowe he LHV, bu he e is a leas one lammable compound. Thus,
he ollowing combus ion es s o low-calo i ic uels equi ed a combus ible componen —in
his case, na u al gas. E en hough me hane is usually only combus ible in syngas o
biogas, me hane was subs i u ed wi h na u al gas du ing he expe imen due o i s simila
Wobbe’s numbe (me hane—50.7 MJ/m3, a ailable na u al gas—50.5 MJ/m3).
The mixing s a ion ensu ed p ope mixing o ine gases and combus ible componen s,
as shown in Figu e 2. The s a ion can mix ou s eams (me hane—up o 100 m
N3
/h,
hyd ogen—up o 500 m
N3
/h, ca bon dioxide—up o
300 mN3/h
, and ni ogen—up o
300 mN3/h
). Each s eam is egula ed and measu ed by B onkho s and M + W ins umen s
pilo al es; he low o gases can be p ecisely egula ed, measu ed, and eco ded. In
addi ion, uel pa ame e s can be egula ed by changing he uel composi ion. The e o e,
LHV can a y in he ange om 5 o 35 MJ/m3.
Ene gies 2022, 15, x FOR PEER REVIEW 4 o 18
Combus ion ai is supplied o he on o he combus ion chambe using a high-
p essu e an equipped wi h a equency con e e . The maximum an ou pu is app oxi-
ma ely 4500 mN3/h wi h a maximum o e p essu e o 11.2 kPa. The ai duc is also
equipped wi h a p ehea ing uni o combus ion ai p e- ea men . The e o e, combus ion
ai can be p ehea ed up o 500 °C.
The es ing acili y is equipped wi h a sophis ica ed da a collec ion and sa e y sys em.
The sys em o da a collec ion enables au oma ic da a collec ion e e y second o wo
minu es and da a collec ion upon he ope a o ’s eques . Collec ed da a include low a es,
p essu es, and empe a u es o combus ion ai , uel, ine gases, and cooling wa e . The
sa e y sys em ensu es he sa e and eliable ope a ion o he es ing acili y using he in o -
ma ion om he senso s, e.g., i p e en s p ehea ing o cooling wa e and lame blow-o .
2.2. Me hodology
The expe imen was i s ca ied ou wi h he e e ence uel—in his case, na u al gas
(composi ion Table 1). All he esul s ob ained wi h low-calo i ic uels we e compa ed o
his e e ence uel. Low-calo i ic uels a e speci ic o hei con en o non-combus ible
compounds, which lowe he LHV, bu he e is a leas one lammable compound. Thus,
he ollowing combus ion es s o low-calo i ic uels equi ed a combus ible componen —
in his case, na u al gas. E en hough me hane is usually only combus ible in syngas o
biogas, me hane was subs i u ed wi h na u al gas du ing he expe imen due o i s simila
Wobbe’s numbe (me hane—50.7 MJ/m3, a ailable na u al gas—50.5 MJ/m3).
The mixing s a ion ensu ed p ope mixing o ine gases and combus ible compo-
nen s, as shown in Figu e 2. The s a ion can mix ou s eams (me hane—up o 100 mN3/h,
hyd ogen—up o 500 mN3/h, ca bon dioxide—up o 300 mN3/h, and ni ogen—up o 300
mN3/h). Each s eam is egula ed and measu ed by B onkho s and M + W ins umen s
pilo al es; he low o gases can be p ecisely egula ed, measu ed, and eco ded. In ad-
di ion, uel pa ame e s can be egula ed by changing he uel composi ion. The e o e,
LHV can a y in he ange om 5 o 35 MJ/m3.
Figu e 2. Model o a mixing s a ion.
Hyd ogen and ine gases we e supplied in bundles p essu ized up o 200 ba (300
ba in he case o ni ogen). Thei p essu e was educed o 8 ba ( he calib a ion p essu e
o he lowme e s) be o e lowing in o he mixing s a ion. Then, hese gases we e mixed,
c ea ing a combus ible mix u e. The limi a ion o he whole uni was he p essu e o he
na u al gas, which was a ailable only a he o e p essu e a 0.1 ba . The e o e, he p es-
su e o he hyd ogen and ine gas mix u e was u he dec eased be o e mixing wi h na -
u al gas and be o e en e ing he bu ne .
Figu e 2. Model o a mixing s a ion.
Hyd ogen and ine gases we e supplied in bundles p essu ized up o 200 ba (
300 ba
in he case o ni ogen). Thei p essu e was educed o 8 ba ( he calib a ion p essu e o he
lowme e s) be o e lowing in o he mixing s a ion. Then, hese gases we e mixed, c ea ing
a combus ible mix u e. The limi a ion o he whole uni was he p essu e o he na u al
gas, which was a ailable only a he o e p essu e a 0.1 ba . The e o e, he p essu e o he
hyd ogen and ine gas mix u e was u he dec eased be o e mixing wi h na u al gas and
be o e en e ing he bu ne .
A i s , o e i y he possibili y o uel in e changeabili y, es s we e ca ied ou on wo
di e en ypes o con en ional expe imen al bu ne s. This means ha se e al pa ame e s
can be easily changed on each bu ne o achie e he equi ed combus ion pa ame e s ( lame
shape, emissions, e c.). Each bu ne was adjus ed o he combus ion o he na u al gas o
Ene gies 2022,15, 262 5 o 18
achie e op imal esul s ega ding he NO
x
emission and lame s abili y. Each expe imen
was ca ied ou while combus ing a uel equi alen o 500 kW.
Fo he i s se ies o expe imen s, a low-NO
x
gas-s aged bu ne wi h al e able geom-
e y (deno ed as Bu ne A) was used. This bu ne can be ope a ed ei he in he p ima y
o seconda y egime wi h mo e uel po s. Fuel en e s he combus ion chambe h ough
12 po s in he p ima y egime, dis ibu ed on wo ci cula a cs. In he seconda y egime,
ou seconda y nozzles a e used o uel injec ion. These nozzles can be posi ioned in
axial, adial, and angen ial di ec ions. Bu ne A can be seen in Figu e 3a and is capable o
u ndown 1:7.
Ene gies 2022, 15, x FOR PEER REVIEW 5 o 18
A i s , o e i y he possibili y o uel in e changeabili y, es s we e ca ied ou on
wo di e en ypes o con en ional expe imen al bu ne s. This means ha se e al pa am-
e e s can be easily changed on each bu ne o achie e he equi ed combus ion pa ame e s
( lame shape, emissions, e c.). Each bu ne was adjus ed o he combus ion o he na u al
gas o achie e op imal esul s ega ding he NO
x
emission and lame s abili y. Each ex-
pe imen was ca ied ou while combus ing a uel equi alen o 500 kW.
Fo he i s se ies o expe imen s, a low-NO
x
gas-s aged bu ne wi h al e able geom-
e y (deno ed as Bu ne A) was used. This bu ne can be ope a ed ei he in he p ima y
o seconda y egime wi h mo e uel po s. Fuel en e s he combus ion chambe h ough
12 po s in he p ima y egime, dis ibu ed on wo ci cula a cs. In he seconda y egime,
ou seconda y nozzles a e used o uel injec ion. These nozzles can be posi ioned in axial,
adial, and angen ial di ec ions. Bu ne A can be seen in Figu e 3a and is capable o u n-
down 1:7.
The second bu ne (Bu ne B) used o es ing is shown in Figu e 3b. This bu ne is
designed as an ai -s aged bu ne . The a io be ween he p ima y and seconda y ai can be
changed due o he in e changeable inne placings. Modula ion o he ai low posi i ely
a ec s he lame dilu ion, and i can elimina e empe a u e peaks whe e he mal NO
x
is
o med. The p ima y uel head has 16 po s dis ibu ed in wo ci cula ields, whe e one
o he ields ( he closes o he lame holde ) s abilizes he lame, while he o he is de-
signed o deli e he maximal he mal ou pu . The bu ne is capable o u ndown 1:10.
Bo h bu ne s we e igni ed and s abilized wi h he injec o bu ne wi h a he mal ou -
pu o 18 kW.
(a) (b)
Figu e 3. Models o commonly used con en ional bu ne s: (a) bu ne wi h s aged uel dis ibu ion
(Bu ne A); (b) bu ne wi h s aged uel dis ibu ion (Bu ne B).
A e he expe imen s wi h he wo con en ional bu ne s and p elimina y da a e al-
ua ion, i was e iden ha in o de o combus low-calo i ic uels and achie e desi ed uel
low a es, a di e en bu ne had o be used. This s ep was necessa y mainly due o ope -
a ional p oblems (especially he abili y o each he desi ed he mal ou pu while com-
bus ing low-calo i ic uel) de ec ed using he abo e bu ne s. The used bu ne (Bu ne C,
Figu e 4) e lec s all he exis ing indings. The calcula ed dimensions and he inal geom-
e y we e designed o combus low-calo i ic uel wi h he minimal LHV o 6.9 MJ/m
N3
.
This alue is he minimum ( o he mal powe o 1500 kW) achie able using he p esen ed
mixing s a ion. Low-calo i ic uel wi h his LHV can deli e maximal he mal powe , ei-
he 750 o 1500 kW, depending on he geome y o he bu ne head and pa ame e s o
he uel. Bu ne C is designed o use he same windbox as Bu ne A. The e o e, i is pos-
sible o easily e o i a con en ional bu ne wi h he low-calo i ic bu ne by changing he
inne placing. This bu ne is designed as an expe imen al de ice; many pa s a e eplace-
able and modula . Fo example, di e en ypes o lame holde s and bu ne heads wi h
Figu e 3.
Models o commonly used con en ional bu ne s: (
a
) bu ne wi h s aged uel dis ibu ion
(Bu ne A); (b) bu ne wi h s aged uel dis ibu ion (Bu ne B).
The second bu ne (Bu ne B) used o es ing is shown in Figu e 3b. This bu ne is
designed as an ai -s aged bu ne . The a io be ween he p ima y and seconda y ai can be
changed due o he in e changeable inne placings. Modula ion o he ai low posi i ely
a ec s he lame dilu ion, and i can elimina e empe a u e peaks whe e he mal NO
x
is
o med. The p ima y uel head has 16 po s dis ibu ed in wo ci cula ields, whe e one o
he ields ( he closes o he lame holde ) s abilizes he lame, while he o he is designed
o deli e he maximal he mal ou pu . The bu ne is capable o u ndown 1:10.
Bo h bu ne s we e igni ed and s abilized wi h he injec o bu ne wi h a he mal
ou pu o 18 kW.
A e he expe imen s wi h he wo con en ional bu ne s and p elimina y da a e alua-
ion, i was e iden ha in o de o combus low-calo i ic uels and achie e desi ed uel low
a es, a di e en bu ne had o be used. This s ep was necessa y mainly due o ope a ional
p oblems (especially he abili y o each he desi ed he mal ou pu while combus ing low-
calo i ic uel) de ec ed using he abo e bu ne s. The used bu ne (Bu ne C, Figu e 4) e lec s
all he exis ing indings. The calcula ed dimensions and he inal geome y we e designed o
combus low-calo i ic uel wi h he minimal LHV o 6.9 MJ/m
N3
. This alue is he minimum
( o he mal powe o 1500 kW) achie able using he p esen ed mixing s a ion. Low-calo i ic
uel wi h his LHV can deli e maximal he mal powe , ei he 750 o 1500 kW, depending on
he geome y o he bu ne head and pa ame e s o he uel. Bu ne C is designed o use he
same windbox as Bu ne A. The e o e, i is possible o easily e o i a con en ional bu ne
wi h he low-calo i ic bu ne by changing he inne placing. This bu ne is designed as an
expe imen al de ice; many pa s a e eplaceable and modula . Fo example, di e en ypes o
lame holde s and bu ne heads wi h di e en geome ies and uel dis ibu ion can be used.
The main ea u e o he bu ne is ha uel and ai a e no s aged, bu bo h a e deli e ed as a
single s eam. Once mixed in he combus ion chambe , hey appea as homogenous lames.
Bo h bu ne s’ head and swi l gene a o we e designed o gene a e a u bulen low o ensu e
p ope low-calo i ic uel and ai mixing, i.e., pe ec combus ion.

Ene gies 2022,15, 262 6 o 18
Ene gies 2022, 15, x FOR PEER REVIEW 6 o 18
di e en geome ies and uel dis ibu ion can be used. The main ea u e o he bu ne is
ha uel and ai a e no s aged, bu bo h a e deli e ed as a single s eam. Once mixed in
he combus ion chambe , hey appea as homogenous lames. Bo h bu ne s’ head and
swi l gene a o we e designed o gene a e a u bulen low o ensu e p ope low-calo i ic
uel and ai mixing, i.e., pe ec combus ion.
Figu e 4. Model o low-calo i ic bu ne designed a e he i s expe imen s (deno ed as Bu ne C).
Di e en ope a ional pa ame e s we e obse ed in he expe imen . In he i s es
(TEST A), he in luence o CO2 and N2 addi ion in o he noble uel on NOx emissions, lue
gas empe a u e, and lame s abili y was in es iga ed. Due o he di e en bu ne geom-
e ies, which limi ed he o e all uel amoun ha could be bu ned unde ce ain condi-
ions, an expe imen al ma ix o each es was c ea ed o show he di e ences be ween
he expe imen s. A e each change in he combus ion pa ame e s, he combus ion cham-
be ope a ed o 30 min be o e he measu emen s we e eco ded in o de o elimina e he
luc ua ions in he da a and ensu e op imal esul s. Fu he mo e, all he s a ed emission
esul s we e measu ed a 3% O2 in he lue gas a he sampling spo in he lue gas duc
be o e connec ing o he chimney. The echnological scheme o he combus ion chambe
is shown in Figu e 5.
Figu e 4. Model o low-calo i ic bu ne designed a e he i s expe imen s (deno ed as Bu ne C).
Di e en ope a ional pa ame e s we e obse ed in he expe imen . In he i s es
(TEST A), he in luence o CO
2
and N
2
addi ion in o he noble uel on NO
x
emissions,
lue gas empe a u e, and lame s abili y was in es iga ed. Due o he di e en bu ne
geome ies, which limi ed he o e all uel amoun ha could be bu ned unde ce ain
condi ions, an expe imen al ma ix o each es was c ea ed o show he di e ences
be ween he expe imen s. A e each change in he combus ion pa ame e s, he combus ion
chambe ope a ed o 30 min be o e he measu emen s we e eco ded in o de o elimina e
he luc ua ions in he da a and ensu e op imal esul s. Fu he mo e, all he s a ed emission
esul s we e measu ed a 3% O
2
in he lue gas a he sampling spo in he lue gas duc
be o e connec ing o he chimney. The echnological scheme o he combus ion chambe is
shown in Figu e 5.
Ene gies 2022, 15, x FOR PEER REVIEW 7 o 18
Figu e 5. Model o low-calo i ic bu ne designed a e he i s expe imen s (deno ed as Bu ne C).
TEST B was ocused on he lame empe a u e. Fo his es , R- ype he mocouples
we e used o measu e he empe a u e in he ho izon al plane o he lame. In o al, eigh
R- ype he mocouples we e used o co e he empe a u es along he ho izon al plane o
symme y. Measu ing poin s we e loca ed 50 cm om each o he along he whole com-
bus ion chambe . Each he mocouple was connec ed o he G aph ec midi LOGGER
GL220, which eco ded he measu ed alues. Tempe a u es we e measu ed a six di e -
en posi ions: nea he wall (5 cm), 10, 20, 30, 40, and 50 cm om he wall.
TEST C was ocused on measu emen s o hea lux in o he wall o he combus ion
chambe . This was allowed due o he unique cons uc ion o he combus ion chambe ,
di ided in o se en di e en sec ions and equipped wi h he mocouples and lowme e s
o measu e cooling wa e p ope ies o calcula e he o e all hea lux.
Du ing TEST A, limi s (bo h in design and echnological) o each bu ne we e e-
ealed. Thus, o TEST B and TEST C, only a ew di e en uel composi ions we e selec ed,
which we e adjus ed acco ding o he esul s ob ained du ing TEST A and o ob ain da a
desc ibing he end wi hou unnecessa y was e o he uel. Be o e each es , condi ions in
he combus ion we e s abilized; i was i al o con ol he low a e o uel and combus ion
ai o achie e s able condi ions. Al hough measu emen s we e conduc ed in exac in e -
als, maximum e o was used o ensu e he epea abili y and accu acy o each es .
3. Resul s
3.1. TEST A—Emissions, Flame S abili y, Flue Gas Tempe a u e
The expe imen s wi h Bu ne A e ealed ha he cons uc ion o his bu ne is no
su icien o a dilu ion highe han 10 m
N3
/h (LHV 28.67 MJ/m
3
) o CO
2
and 20 m
N3
/h (LHV
24.58 MJ/m
3
) o N
2
, as is e iden om he expe imen al ma ix o TEST A (Table 2). The
limi a ion was ha he bu ne head, o iginally designed o noble uels, could no dis ib-
u e mo e uel. I was e iden ha i would be possible o achie e a highe low a e wi h
highe o e p essu e o uel, bu his change would a ec he compa ison o he esul s.
E en hough he amoun o he added ine gases was low and he educ ion o NO
x
in
he lue gas was lowe , i was possible o obse e signs o dependence. The di e ence
be ween he e ec o N
2
and CO
2
is also e iden . CO
2
as a la ge molecule can abso b much
Figu e 5. The echnological scheme o he combus ion chambe .
TEST B was ocused on he lame empe a u e. Fo his es , R- ype he mocouples
we e used o measu e he empe a u e in he ho izon al plane o he lame. In o al, eigh
R- ype he mocouples we e used o co e he empe a u es along he ho izon al plane
o symme y. Measu ing poin s we e loca ed 50 cm om each o he along he whole
Ene gies 2022,15, 262 7 o 18
combus ion chambe . Each he mocouple was connec ed o he G aph ec midi LOGGER
GL220, which eco ded he measu ed alues. Tempe a u es we e measu ed a six di e en
posi ions: nea he wall (5 cm), 10, 20, 30, 40, and 50 cm om he wall.
TEST C was ocused on measu emen s o hea lux in o he wall o he combus ion
chambe . This was allowed due o he unique cons uc ion o he combus ion chambe ,
di ided in o se en di e en sec ions and equipped wi h he mocouples and lowme e s o
measu e cooling wa e p ope ies o calcula e he o e all hea lux.
Du ing TEST A, limi s (bo h in design and echnological) o each bu ne we e e-
ealed. Thus, o TEST B and TEST C, only a ew di e en uel composi ions we e selec ed,
which we e adjus ed acco ding o he esul s ob ained du ing TEST A and o ob ain da a
desc ibing he end wi hou unnecessa y was e o he uel. Be o e each es , condi ions in
he combus ion we e s abilized; i was i al o con ol he low a e o uel and combus ion
ai o achie e s able condi ions. Al hough measu emen s we e conduc ed in exac in e als,
maximum e o was used o ensu e he epea abili y and accu acy o each es .
3. Resul s
3.1. TEST A—Emissions, Flame S abili y, Flue Gas Tempe a u e
The expe imen s wi h Bu ne A e ealed ha he cons uc ion o his bu ne is no
su icien o a dilu ion highe han 10 m
N3
/h (LHV 28.67 MJ/m
3
) o CO
2
and 20 m
N3
/h
(LHV 24.58 MJ/m
3
) o N
2
, as is e iden om he expe imen al ma ix o TEST A (Table 2).
The limi a ion was ha he bu ne head, o iginally designed o noble uels, could no
dis ibu e mo e uel. I was e iden ha i would be possible o achie e a highe low a e
wi h highe o e p essu e o uel, bu his change would a ec he compa ison o he esul s.
E en hough he amoun o he added ine gases was low and he educ ion o NO
x
in he
lue gas was lowe , i was possible o obse e signs o dependence. The di e ence be ween
he e ec o N
2
and CO
2
is also e iden . CO
2
as a la ge molecule can abso b much mo e
hea , i.e., educe he lame empe a u e, educing NO molecules’ nuclea ion. The e o e,
bo h ine gases had a di ec impac on lame cha ac e is ics. A highe amoun o ine gas
in he uel inally esul ed in he ins abili y o he lame. A low a es o 20 m
N3
/h o CO
2
and 30 m
N3
/h o N
2
, he lame co e became much colde , and a high amoun o CO was
measu ed in he lue gas. I could also be no iced ha he lame wi h mo e ine gas in
he uel changed i s colo om yellow o blue and became much mo e s able ( he lame
was isually sha pe ) un il i eached he u ning poin , and he lame had he endency o
quench. Resul s o TEST A o Bu ne A a e shown in Table 3.
Table 2. Expe imen al ma ix—TEST A—Bu ne A (•indica es ha he es was ca ied ou ).
Amoun o N2[mN3/h] 0 10 20 30 40 50 60 0 0 0 0 0 0
Amoun o CO2[mN3/h] 0 0 0 0 0 0 0 10 20 30 40 50 60
Fuel/Ine gas a io [% ol.]
100/0 83/17 71/29 62/38 56/44 50/50 45/55 83/17 71/29 62/38 56/44 50/50 45/55
Bu ne A P ima y egime • • -----•-----
Bu ne A Seconda y egime • • • - - - - •-----
Table 3. Expe imen al ma ix—TEST A—Bu ne A.
Regime CO2Addi ion
[mN3/h]
N2Addi ion
[mN3/h] NOx[ppm] NOx[mg/mN3]Flue Gas
Tempe a u e [◦C]
P ima y 0 0 72 147 629
P ima y 0 10 63 129 647
P ima y 10 0 53 109 654
Seconda y 0 0 46 94 683
Seconda y 0 10 39 79 676
Seconda y 0 20 27 56 692
Seconda y 10 0 29 60 682
Ene gies 2022,15, 262 8 o 18
The geome y o Bu ne B was designed o a highe he mal ou pu han ha o Bu ne
A. The e o e, i is possible o add mo e ine gases in o he uel. This bu ne combus s all he
uel in he p ima y egime, and, o NO
x
educ ion, he seconda y ai dis ibu ion is used. In
bo h p ima y and seconda y egimes, up o 60 m
N3
/h (LHV 15.64 MJ/m
3
) o CO
2
and N
2
was
added. All he uel was in a single s eam, c ea ing be e bu ning condi ions o low-calo i ic
uel compa ed o Bu ne A. Hence, i was possible o achie e highe low a es wi h good
lame s abili y. The educ ion o NO
x
was apid, and i s end was appa en . Assump ions
om he measu emen wi h Bu ne A we e con i med. CO
2
a ec s he educ ion mo e han
N
2
, as is e iden om he esul s in Table 4. In bo h cases, a highe con en o non-combus ible
compound esul ed in highe ou le nozzle eloci ies. This phenomenon imp o ed he lame
s abili y and in ensi ied he mixing o uel and combus ion ai . Al hough he lame was s able
du ing he whole p ocess/ es , he colo o he lame u ned om yellow o blue as he lame
empe a u e d opped. The expe imen al ma ix o Bu ne B is shown in Table 4, while he
measu ed alues a e summa ized in Table 5.
Table 4. Expe imen al ma ix—TEST A—Bu ne B (•indica es ha he es was ca ied ou ).
Amoun o N2[mN3/h] 0 10 20 30 40 50 60 0 0 0 0 0 0
Amoun o CO2[mN3/h] 0 0 0 0 0 0 0 10 20 30 40 50 60
Fuel/Ine gas a io [% ol.]
100/0 83/17 71/29 62/38 56/44 50/50 45/55 83/17 71/29 62/38 56/44 50/50 45/55
Bu ne B P ima y egime •••••••••••••
Bu ne B Seconda y egime •••••••••••••
Table 5. Expe imen al ma ix—TEST A—Bu ne B.
Regime CO2Addi ion
[mN3/h]
N2Addi ion
[mN3/h] NOx[ppm] NOx[mg/mN3]Flue Gas
Tempe a u e [◦C]
P ima y 0 0 92 189 678
P ima y 0 10 89 182 639
P ima y 0 20 78 159 619
P ima y 0 30 66 135 597
P ima y 0 40 54 110 558
P ima y 0 50 40 82 554
P ima y 0 60 34 70 547
P ima y 10 0 55 113 622
P ima y 20 0 40 83 615
P ima y 30 0 28 58 568
P ima y 40 0 20 42 552
P ima y 50 0 16 33 552
P ima y 60 0 15 31 551
Seconda y 0 0 58 118 634
Seconda y 0 10 53 108 607
Seconda y 0 20 49 100 577
Seconda y 0 30 45 92 574
Seconda y 0 40 42 86 567
Seconda y 0 50 37 77 566
Seconda y 0 60 32 66 566
Seconda y 10 0 47 97 611
Seconda y 20 0 38 77 580
Seconda y 30 0 28 57 570
Seconda y 40 0 22 45 569
Seconda y 50 0 18 38 564
Seconda y 60 0 15 31 550
Bu ne C was designed o high low a es a he bu ne head; he e o e, he lame was
uns able du ing he combus ion o na u al gas wi hou any ni ogen o ca bon dioxide. As
a esul , uel mixing wi h combus ion ai was insu icien , and i was possible o obse e
a long lame (3 m). The addi ion o ni ogen and ca bon dioxide changed he lame
Ene gies 2022,15, 262 9 o 18
cha ac e is ics, he lame became sho e , and almos all he yellow colo in he lame was
subs i u ed wi h he blue colo . Wi h he addi ion o 120 m
N3
/h o N
2
in he uel, he lame
was only 1.5 m long, o 1 m o CO
2
. Due o he high eloci y a he ip o he bu ne head,
p ope mixing o uel and combus ion ai was ensu ed because o he high u bulen low.
Ne e heless, he bu ne was designed e en o highe low a es. I was impossible
o inc ease he a io o ine compounds in he uel because o he insu icien low om he
bundles. The egime wi h CO
2
addi ion was e alua ed as highly p oblema ic; a high low
a es, such as 120 m
N3
/h o CO
2,
he emaining CO
2
in he cylinde s comple ely oze o ,
and a u he inc ease in low a e was no possible. The expe imen al ma ix o Bu ne C
is shown in Table 6, and he measu ed alues a e displayed in Table 7.
Table 6. Expe imen al ma ix—TEST A—Bu ne C (•indica es ha he es was ca ied ou ).
Amoun o N2[mN3/h] 0 30 60 90 120 0 0 0 0
Amoun o CO2[mN3/h] 0 0 0 0 0 30 60 90 120
Fuel/Ine gas a io [% ol.] 100/0 62/38 45/55 36/64 29/71 62/38 45/55 36/64 29/71
Bu ne C •••••••••
Table 7. Expe imen al ma ix—TEST A—Bu ne C.
Regime CO2Addi ion
[mN3/h]
N2Addi ion
[mN3/h]
NOx
[ppm]
NOx
[mg/mN3]
Flue Gas
Tempe a u e [◦C]
P ima y 0 0 73 149 701
P ima y 0 30 61 125 673
P ima y 0 60 56 115 669
P ima y 0 90 49 101 662
P ima y 0 120 43 88 656
P ima y 30 0 45 92 653
P ima y 60 0 36 73 633
P ima y 90 0 28 58 632
P ima y 120 0 20 40 620
The measu ed alues o all egimes indica ed in he p e ious ma ixes we e displayed
in g aphs in o de o unde s and he acqui ed da a be e . In all igu es, a simila end
is isible. When ine gas was added, measu ed NO
x
in he lue gas s a ed o d op,
co esponding wi h he empe a u e dec ease. The alues o he bu ne wi h s aged uel
dis ibu ion can be seen in Figu e 6a. Since added ine gases we e ela i ely low, he
change was also mild. Figu e 6b shows a mo e signi ican dec ease, whe e measu ed da a
o he bu ne wi h s aged ai a e p esen ed. A simila pa e n can be obse ed in Figu e 6c,
displaying measu ed alues on a low-calo i ic bu ne .
Tempe a u es o he lue gas a e also p esen ed in he g aphs in Figu e 7. As men ioned
abo e, when ine gas is p esen in he uel, i immedia ely impac s he empe a u e, which,
in gene al, dec eases. The alues o he bu ne wi h s aged uel dis ibu ion can be seen in
Figu e 7a. In his case, he opposi e end is e iden . The empe a u e is inc easing wi h
added ine gas. The cause o his could be he highe ou le speed o he uel, which leads
o enhanced mixing and a mo e in ensi e eac ion. Figu e 7b shows a dec ease, whe e
measu ed da a o he bu ne wi h s aged ai a e p esen ed. A simila pa e n can be
obse ed in Figu e 7c, displaying measu ed alues on a low-calo i ic bu ne .
Ene gies 2022,15, 262 16 o 18
Ene gies 2022, 15, x FOR PEER REVIEW 16 o 18
E alua ion o he da a collec ed in he Bu ne C combus ion es e ealed simila
ends a e bo h N
2
and CO
2
addi ion. The mos signi ican di e ence was isible a e
adding 30 m
N3
/h o CO
2
. A u he inc ease in ine gas low did no cause a signi ican
di e ence. I was essen ial o s abilize he lame e en wi h a small amoun o enla gemen
o he uel o imp o e he ou le eloci ies. Al hough mo e ine gas was added o he uel,
i did no cause a signi ican luc ua ion in he hea lux abso p ion in single sec ions. The
e alua ed da a a e shown in Figu e 13.
(a) (b)
Figu e 13. In luence o ine gas addi ion on hea lux dis ibu ion—low-calo i ic bu ne —Bu ne
C: (a) addi ion o N
2
; (b) addi ion o CO
2
.
The e o analysis o hea lux was pe o med acco ding o Equa ion (1) o he s and-
a d de ia ion 𝜎󰇗

o calcula ed hea lux o he wall o he i- h chambe ’s sec ion [kW/m
2
].
Va iables in he equa ions a e hea lux, 𝜎

—s anda d de ia ion o wa e low a e
h ough he i- h chambe ’s sec ion [m
3
/h], 𝑉— olume ic low a e o cooling wa e
h ough he i- h chambe ’s sec ion [m
3
/h], 𝜎
,
— he s anda d de ia ion o he ou le
empe a u e o cooling wa e ou o he i- h chambe ’s sec ion [°C], 𝜎

— he s anda d
de ia ion o he inle empe a u e o cooling wa e in he chambe [°C], ∆𝑡— he ou le
empe a u e o cooling wa e ou o he i- h chambe ’s sec ion [°C].
𝜎󰇗

𝑞󰇗∙󰇩𝜎

𝑉𝜎
,
𝜎


∆𝑡󰇪
𝑓
𝑜𝑟 𝑖1,2,…,7 (1)
Fo he i s sec ion, he mos signi ican e o in all measu emen s was less han ±5%,
while i was usually less han ±3% in he o he sec ions.
4. Conclusions
The use o al e na i e uels in s anda dized bu ne s wi hou any modi ica ion is lim-
i ed. I is possible o injec he al e na i e low-calo i ic uel in o he nobble one, bu he
amoun has o be speci ied be o ehand so ha he ope a ing condi ions can emain s able.
The bu ne can usually handle he uel combus ion wi h a signi ican ly lowe LHV han
ini ially designed, bu i s abili y o deli e he mal powe will dec ease. This is mainly
due o he highe amoun o uel lowing h ough nozzles ini ially designed o p ocess
uel wi h a much highe LHV. Mo eo e , o p o ide s able combus ion condi ions on con-
en ional bu ne s while combus ing low-calo i ic uel, i is necessa y o suppo he lame
co e o s abilize he lame, which could blow o due o he inc eased pa ial p essu e o
incombus ible componen s.
Bo h ine gases (N
2
and CO
2
) can dec ease peak empe a u es in he lame, esul ing
in lowe NO
x
emissions. Howe e , CO
2
can abso b mo e hea han N
2,
and i can be mo e
bene icial o NO
x
emission-wise. When combus ing in he bu ne wi h a s aged gas dis-
ibu ion, e en a mino uel dilu ion wi h 16% ol. o N
2
(26% w ) o CO
2
(34% w ) can
educe NOx up o 30%. When he uel dilu ion is highe , he educ ion can be e en mo e
apid. This was p o en on he bu ne wi h seconda y ai -s aged dis ibu ion, whe e he
Figu e 13.
In luence o ine gas addi ion on hea lux dis ibu ion—low-calo i ic bu ne —Bu ne C:
(a) addi ion o N2; (b) addi ion o CO2.
The e o analysis o hea lux was pe o med acco ding o Equa ion (1) o he
s anda d de ia ion
σ.
qi
o calcula ed hea lux o he wall o he i- h chambe ’s sec ion
[kW/m
2
]. Va iables in he equa ions a e hea lux,
σVi
—s anda d de ia ion o wa e low
a e h ough he i- h chambe ’s sec ion [m
3
/h],
Vi
— olume ic low a e o cooling wa e
h ough he i- h chambe ’s sec ion [m
3
/h],
σ ou ,i
— he s anda d de ia ion o he ou le
empe a u e o cooling wa e ou o he i- h chambe ’s sec ion [
◦
C],
σ in
— he s anda d
de ia ion o he inle empe a u e o cooling wa e in he chambe [
◦
C],
∆ i
— he ou le
empe a u e o cooling wa e ou o he i- h chambe ’s sec ion [◦C].
σ.
qi
=.
qi·
u
u
"σVi
Vi2
+
σ2
ou ,i+σ2
in
∆ 2
i# o i =1, 2, . . . , 7 (1)
Fo he i s sec ion, he mos signi ican e o in all measu emen s was less han
±
5%,
while i was usually less han ±3% in he o he sec ions.
4. Conclusions
The use o al e na i e uels in s anda dized bu ne s wi hou any modi ica ion is
limi ed. I is possible o injec he al e na i e low-calo i ic uel in o he nobble one, bu
he amoun has o be speci ied be o ehand so ha he ope a ing condi ions can emain
s able. The bu ne can usually handle he uel combus ion wi h a signi ican ly lowe
LHV han ini ially designed, bu i s abili y o deli e he mal powe will dec ease. This
is mainly due o he highe amoun o uel lowing h ough nozzles ini ially designed o
p ocess uel wi h a much highe LHV. Mo eo e , o p o ide s able combus ion condi ions
on con en ional bu ne s while combus ing low-calo i ic uel, i is necessa y o suppo he
lame co e o s abilize he lame, which could blow o due o he inc eased pa ial p essu e
o incombus ible componen s.
Bo h ine gases (N
2
and CO
2
) can dec ease peak empe a u es in he lame, esul ing
in lowe NO
x
emissions. Howe e , CO
2
can abso b mo e hea han N
2,
and i can be
mo e bene icial o NO
x
emission-wise. When combus ing in he bu ne wi h a s aged gas
dis ibu ion, e en a mino uel dilu ion wi h 16% ol. o N
2
(26% w ) o CO
2
(34% w ) can
educe NOx up o 30%. When he uel dilu ion is highe , he educ ion can be e en mo e
apid. This was p o en on he bu ne wi h seconda y ai -s aged dis ibu ion, whe e he
educ ion in NO
x
was ca. 80% (dilu ion o he uel 55% ol. o N
2
(67% w ) o CO
2
(
74% w
)
can signi ican ly a ec NO
x
educ ion up o 80%). A simila pa e n was also appa en wi h
he combus ion es s in he low-calo i ic bu ne .
A c ucial ac o ha has o be conside ed is he lame shape. When he ine gas
is added o he uel, i s olume inc eases, and he ou le nozzle eloci y inc eases; his
p ocedu e can also be used o modi y he lame shape and di ec ly in luence he he mal
s ess o he de ice.

Ene gies 2022,15, 262 17 o 18
The addi ion o ine gas in o he con en ional uel can be bene icial; i can imp o e he
e iciency o s eam mixing, which di ec ly impac s he he mal e iciency, bu i is challenging
o ind he u ning poin . A u he inc ease in he ine gas a io has a nega i e e ec . The
e alua ion o he expe imen s e ealed ha he imp o emen o hea lux could each up
o 5% compa ed o he combus ion o na u al gas in a con en ional bu ne . Howe e , he
e ec in he new low-calo i ic bu ne was negligible. An inc eased hea lux ansi ion in o he
walls can be explained by he imp o ed mixing e iciency, bu a change in he pa ial p essu e
o CO
2
o N
2
can also play a ole. Fu he mo e, a highe uel olume also esul s in highe
ou le eloci ies, which in ensi y he u bulen lue in he combus ion chambe . Thus, un il he
u ning poin is eached, i can imp o e he hea lux owa ds he walls.
When co-combus ing uels, such as na u al gas and biogas, i is mo e bene icial o equip
he bu ne wi h wo di e en se s o nozzles (i he same he mal powe is expec ed). Howe e ,
i a sligh dec ease in he mal powe is no an issue, one se o nozzles could be used.
Fu u e wo k will be ocused on he da a alida ion and op imiza ion o he low-
calo i ic bu ne .
5. Pa en s
Sk yja, P.; Hudák, I.; Bˇeloh adský, P.; S ehlík, P.; Vu B nˇe, B no. Czech Republic:
Bu ne Fo Low Calo i ic Fuels. EP3364105 (B1). (2018).
Sk yja, P.; Hudák, I.; Bˇeloh adský, P.; S ehlík, P.; Vu B nˇe, B no. Czech Republic:
Bu ne Head o Low Calo i ic Fuels. US2018231245A1. (2018).
Au ho Con ibu ions:
Concep ualiza ion, I.H. and P.S.; me hodology, I.H.; alida ion, I.H., J.B.
and Z.J.; o mal analysis, P.S.; in es iga ion, I.H. and J.B.; w i ing—o iginal d a p epa a ion, I.H.;
w i ing— e iew and edi ing, I.H., P.S. and J.B.; isualiza ion, I.H.; supe ision, M.K. and Z.J.; p ojec
adminis a ion, Z.J. All au ho s ha e ead and ag eed o he published e sion o he manusc ip .
Funding:
This esea ch was unded by he Czech Minis y o Educa ion, You h, and Spo s/EU Ope a-
ional P og amme Resea ch, De elopmen and Educa ion, g an no. CZ.02.1.01/0.0/0.0/16_026/0008413
“S a egic pa ne ship o en i onmen al echnologies and ene gy p oduc ion”. Fu he mo e, he au ho s
g a e ully acknowledge he inancial suppo p o ided by he Technology Agency o he Czech Republic
(TACR) wi hin he esea ch p ojec Na ional Cen e s o Compe ence, speci ically h ough he p ojec
Na ional Cen e o Ene gy (TN1000007).
Ins i u ional Re iew Boa d S a emen : No applicable.
Da a A ailabili y S a emen :
The da a p esen ed in his s udy a e a ailable on eques om he
co esponding au ho .
Con lic s o In e es : The au ho s decla e no con lic o in e es .
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