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Low-temperature partial oxidation of methane over Pd–Ni bimetallic catalysts supported on CeO2

Fazlikeshteli, Shiva,Vendrell Villafruela, Xavier,Llorca Piqué, Jordi

Abstract

Monometallic Pd and Ni and bimetallic Pd–Ni catalysts supported on CeO2 are prepared via mechanochemical and conventional incipient wetness impregnation methods and tested for the production of syngas by the partial oxidation of methane. Compared with monometallic Ni/CeO2 and Pd/CeO2, bimetallic Pd–Ni/CeO2 catalysts show considerable higher methane conversion and syngas yield. Additionally, the bimetallic catalysts prepared by ball milling produce syngas at lower temperature. Different preparation parameters, such as metal loading, Pd/Ni ratio, milling energy, milling time and order of incorporation of the metals are examined. The best performance is obtained with a bimetallic catalyst prepared at 50 Hz for 20 min with only 0.12 wt% Pd and 1.38 wt% Ni. Stability tests demonstrate superior stability for bimetallic Pd–Ni/CeO2 catalysts prepared by a mechanochemical approach. From the characterization results, this is explained in terms of an impressive dispersion of metal species with a strong interaction with the surface of CeO2.

Full text

Low- empe a u e pa ial oxida ion o me hane o e PdeNi bime allic ca alys s suppo ed on CeO 2 Shi a Fazlikesh eli, Xa ie Vend ell ** , Jo di Llo ca * Ins i u e o Ene gy Technologies, Depa men o Chemical Enginee ing and Ba celona Resea ch Cen e in Mul iscale Science and Enginee ing, Uni e si a Poli  ecnica de Ca alunya, EEBE, Edua d Ma is any 16, 08019, Ba celona, Spain highligh s g aphical abs ac Bime allic PdeNi/CeO 2 p epa ed by ball milling show excellen pe - o mance o POM. Maximum me hane con e sion and syngas wi h 0.12 w % Pd and 1.38 w % Ni. Supe io s abili y o PdeNi/CeO 2 ball milled a 50 Hz o 20 min. Ball milling yields an imp essi e dispe sion o me al species on CeO 2 su ace. a icle in o A icle his o y: Recei ed 1 Feb ua y 2022 Recei ed in e ised o m 26 June 2022 Accep ed 3 July 2022 A ailable online 13 Augus 2022 Keywo ds: Me hane pa ial oxida ion Bime allic ca alys s Ce ia ca alys s Palladium Nickel Mechanochemis y abs ac Monome allic Pd and Ni and bime allic PdeNi ca alys s suppo ed on CeO 2 a e p epa ed ia mechanochemical and con en ional incipien we ness imp egna ion me hods and es ed o he p oduc ion o syngas by he pa ial oxida ion o me hane. Compa ed wi h mono- me allic Ni/CeO 2 and Pd/CeO 2 , bime allic PdeNi/CeO 2 ca alys s show conside able highe me hane con e sion and syngas yield. Addi ionally, he bime allic ca alys s p epa ed by ball milling p oduce syngas a lowe empe a u e. Di e en p epa a ion pa ame e s, such as me al loading, Pd/Ni a io, milling ene gy, milling ime and o de o inco po a ion o he me als a e examined. The bes pe o mance is ob ained wi h a bime allic ca alys p epa ed a 50 Hz o 20 min wi h only 0.12 w % Pd and 1.38 w % Ni. S abili y es s demons a e supe io s abili y o bime allic PdeNi/CeO 2 ca alys s p epa ed by a mechanochemical app oach. F om he cha ac e iza ion esul s, his is explained in e ms o an imp essi e dispe sion o me al species wi h a s ong in e ac ion wi h he su ace o CeO 2 . ©2022 The Au ho (s). Published by Else ie L d on behal o Hyd ogen Ene gy Publica ions LLC. This is an open access a icle unde he CC BY-NC-ND license (h p:// c ea i ecommons.o g/licenses/by-nc-nd/4.0/). *Co esponding au ho . ** Co esponding au ho . E-mail add esses: xa ie . end ell. illa [email p o ec ed] (X. Vend ell), [email p o ec ed] (J. Llo ca). A ailable online a www.sciencedi ec .com ScienceDi ec jou nal homepage: www.else ie .com/loca e/he in e na ional jou nal o hyd ogen ene gy 48 (2023) 12024e12035 h ps://doi.o g/10.1016/j.ijhydene.2022.07.020 0360-3199/©2022 The Au ho (s). Published by Else ie L d on behal o Hyd ogen Ene gy Publica ions LLC. This is an open access a icle unde he CC BY-NC- ND license (h p://c ea i ecommons.o g/licenses/by-nc-nd/4.0/). In oduc ion Me hane is a majo componen o na u al gas (>90%) and i s con e sion in o syngas (a aluable eeds ock composed by a mix u e o gases domina ed by he p esence o ca bon mon- oxide CO and hyd ogen) has a ac ed inc easing a en ion in he las ew decades o he p oduc ion o nume ous chemical p oduc s and uels [1e3]. Depending on he applica ion, he ca aly ic syngas p oduc ion om me hane can be ealized h ough h ee gene al ou es: (1) s eam e o ming o me hane (SRM) (Eq. (1)), (2) d y e o ming o me hane (DRM) (Eq. (2)), and (3) pa ial oxida ion o me hane (POM) (Eq. (3))[4e6]. CH 4 þH 2 O⟶CO þ3H 2 DH 298K ¼206 kJ mol 1 (Eq. 1) CH 4 þCO 2 ⟶2H 2 þ2CO DH 298K ¼247 kJ mol 1 (Eq. 2) CH 4 þ1/2O 2 /CO þ2H 2 DH 298K ¼36 kJ mol 1 (Eq. 3) In con as o SRM and DRM me hods, POM is a mildly exo he mic eac ion. Fo his eason, POM is seen as an ene gy-sa ing p ocess, and is conside ed he mos economic echnology o syngas p oduc ion [7,8]. Mo eo e , he mola a io o H 2 /CO in he POM eac ion is close o 2, which is sui able o he p oduc ion o me hanol and highe hyd o- ca bons h ough he Fische -T opsch p ocess [9,10]. Besides, POM can handle a la ge olume o he eed gas wi h only a small amoun o ca alys [11,12]. Usually, he POM p ocess in o syngas occu s in wo s eps [4,13]. In he i s s ep, CH 4 is combus ed by O 2 o p oduce CO 2 and H 2 O (Eq. (4)), and hen he emaining un eac ed CH 4 is e o med wi h wa e (Eq. (5)) and CO 2 (Eq. (6)) o p oduce CO and H 2 [13,14]. These eac ions a e always accompanied by he wa e gas-shi equilib ium (Eq. (7))[13]. CH 4 þ2O 2 %CO 2 þ2H 2 ODH 298 ¼803 kJ mol 1 (Eq. 4) CH 4 þH 2 O%CO þ3H 2 DH 298 ¼þ206 kJ mol 1 (Eq. 5) CH 4 þCO 2 %2CO þ2H 2 DH 298 ¼þ247 kJ mol 1 (Eq. 6) CO 2 þH 2 %CO þH 2 ODH 298 ¼41 kJ mol 1 (Eq. 7) A e nea ly 100 yea s o in es iga ion on he ca aly ic pa ial oxida ion o me hane in o syngas, nume ous ca alys o mula ions ha e been es ed. They can be di ided basically in o h ee main ypes: (1) nickel, cobal , o i on ca alys s, (2) ansi ion me al ca bide ca alys s, and (3) noble me al ca a- lys s [15,16]. Cu en ly, he indus ial ca alys s used o POM a e p ima ily nickel and noble me al suppo ed ca alys s [1]. Nickel-based ca alys s ha e been widely in es iga ed due o hei low cos ; howe e , hey a e easily deac i a ed owing o ca bon deposi ion and me al loss a empe a u es highe han 700 C[4,5,17]. To imp o e he mal s abili y and ac i i y and dec ease ca bon deposi ion, o he componen s like noble me als (Pd, P , Rh, Ru, e c.) a e added o Ni ca alys s. These noble me als a e mo e ac i e, less sensi i e o coke o ma ion and ha e highe capaci y o oxidize hyd oca bons, bu a e expensi e. The e o e, bime allic ca alys s wi h Ni and noble me als ha e been p oposed o p omo e me hane con e sion [15,17]. Palladium is one o he mos e ec i e noble me als used o me hane con e sion p ocesses [18e20]. The suppo plays also an impo an ole on he POM p ocess [21,22]. Mos ca alys s show high ac i i y when me als a e dispe sed on a educible oxide suppo [4]. Ce ium oxide (CeO 2 ) is one o he mos signi ican educible oxide suppo s used in indus ial ca alysis as i educes ca bon deposi ion and has a ema kable oxygen s o age/exchange capaci y due o acile oxygen a- cancy o ma ion and change o oxida ion s a es be ween Ce 3þ and Ce 4þ [19,23]. The main objec i e o he p esen in es iga ion is o de elop an e ec i e bime allic NiePd/CeO 2 ca aly ic sys em o POM o p oduce syngas a low empe a u e. To ha end, a se ies o monome allic Ni, Pd, and PdeNi bime allic ca alys s suppo ed on CeO 2 we e p epa ed, cha ac e ized and es ed. Two di e en me hods we e used o p epa e he ca alys s, d y ball milling (BM) and con en ional incipien we ness imp eg- na ion (IWI). The BM echnique is a g een echnology wi h eno mous po en ial o he p epa a ion o ca alys s; i has an easy ope a ion and i is as , cos -e ec i e and en i onmen- ally iendly [24e26]. Ma e ials and me hods P epa a ion o CeO 2 Ce ium ni a e hexahyd a e (Ce(NO 3 ) 3 $6H 2 O, 99.5%) and palladium (II) ni a e (Pd(NO 3 ) 2 , 93%) we e pu chased om Al a Aesa . Nickel (II) ni a e hexahyd a e (Ni(NO 3 ) 2 $6H 2 O, 98%) was ob ained om Fishe chemical. Ammonia solu ion (NH 3 , 28%) was ob ained om Scha lab. All eagen s we e used wi hou u he pu i ica ion. Ce ium dioxide (CeO 2 ) was ob ained by adding d opwise NH 3 o an aqueous solu ion o Ce(NO 3 ) 3 $6H 2 O un il he pH eached a alue be ween 9 and 10 and a yellowish p ecipi a e was ob ained. A e ha , he p ecipi a ed was il e ed and washed ho oughly wi h deion- ized wa e . The p ecipi a e was d ied o e nigh a 90 C and calcined a 650 C o 4 h (5 C min 1 ). P epa a ion o ca alys s by mechanochemical me hod Monome allic Pd(x)/CeO 2 /BM (x ¼0.5, and 1 w %) and Ni(y)/ CeO 2 /BM (y ¼0.5 w %) ca alys s we e p epa ed ia ball mill (labeled as BM). Ni(NO 3 ) 2 $6H 2 O and Pd(NO 3 ) 2 we e used as Ni and Pd p ecu so s, espec i ely. The desi ed amoun s o me al ni a es we e mixed di ec ly wi h CeO 2 in a zi conium oxide essel using a F i sch Pul e ise e 23 mini-mill appa a us and one zi conium oxide ball o 15 mm diame e (ball o powde a io, BPR ¼10.2). Two di e en ou es we e used o p epa e he bime allic Pd(x)-Ni(y)/CeO 2 /BM ca alys s (x ¼0.06e1 w %, y¼0.5 o 1.44 w %; x þy¼1.5) by he BM me hod: (1) co-BM and (2) sequen ial-BM. In he co-BM me hod, he bime allic PdeNi/CeO 2 /BM ca alys s we e p epa ed in one-s ep by mill- ing oge he CeO 2 and he me al p ecu so s. In he sequen ial- BM me hod, i s ly, one o he me al p ecu so s was mixed wi h ce ium oxide by BM, and in he nex s ep he o he p e- cu so was added and subjec ed again o BM. These samples we e labeled as PdeCeO 2 /BM/Ni/BM o NieCeO 2 /BM/Pd/BM in e na ional jou nal o hyd ogen ene gy 48 (2023) 12024e12035 12025 depending i ce ia was i s milled wi h he Pd p ecu so o wi h he Ni p ecu so , espec i ely. The e ec o ball mill equency (15, 30 and 50 Hz) and milling ime (5e40 min) was also in es iga ed. All he esh ca alys s we e used wi hou any u he ea men . P epa a ion o ca alys s by incipien we ness imp egna ion Monome allic Pd, Ni, and bime allic PdeNi ca alys s we e also p epa ed by con en ional incipien we ness imp egna ion o compa ison (labeled as IWI). Fo he p epa a ion o mono- me allic Ni(y)/CeO 2 /IWI (y ¼0.5 w %) and Pd(x)/CeO 2 /IWI (x ¼0.5, and 1 w %), Ni(NO 3 ) 2 $6H 2 O and Pd(NO 3 ) 2 aqueous solu ions we e used as p ecu so s. Samples we e d ied a 90 C and calcined a 650 C o 4 h (5 Cmin 1 ). Two di e en ou es we e used o p epa e he bime allic Pd(x)-Ni(y)/CeO 2 /IWI ca - alys s (x ¼0.06e1 w %, y ¼0.5 o 1.44 w %; x þy¼1.5) by he IWI me hod: (1) co-IWI and (2) sequen ial-IWI. In he co-IWI me hod, he PdeNi/CeO 2 /IWI ca alys s we e p epa ed in one-s ep, while in sequen ial-IWI wo subsequen imp egna- ions we e ca ied ou , wi h a calcina ion s ep a 650 C o 2 h be ween each imp egna ion. These samples we e labeled as NieCeO 2 /IWI/Pd/IWI o PdeCeO 2 /IWI/Ni/IWI depending i he i s imp egna ion was ca ied ou wi h he Ni o he Pd p e- cu so , espec i ely. No u he ea men s we e pe o med on he calcined samples be o e he ca aly ic es . Ca aly ic es s The ca aly ic pe o mance o he ca alys s o he POM p ocess was e alua ed in a con inuous- low ixed-bed qua z ubula eac o . Reac ions we e ca ied ou a a mosphe ic p essu e be ween 300 and 550 C using a mix u e o CH 4 :ai :N 2 ¼4:11:85 (mola , CH 4 /O 2 ¼1.73) and F/W ¼60 L h 1 g 1 (gas hou ly space eloci y GHSV ¼12 10 3 h 1 ). Typically, 0.1 g o ca alys was mixed wi h silicon ca bide o ob ain a ixed bed olume o 0.5 cm 3 . The eac o was hea ed in an elec ical u nace (Ca boli e CTF) and he empe a u e in he cen e o he ca alys bed was measu ed wi h a ype K he mocouple; no axial he mal g adien s we e measu ed. CH 4 con e sion ðXCH4Þand syngas selec i i ies ðSH2;SCOÞwe e e alua ed om 300 C o 550 C in s eps o 50 C. A each empe a u e, a dwell ime o 45 min was applied, hus ensu ing s eady-s a e con- di ions. The eac ion p oduc s we e analyzed online e e y 4 min wi h a gas ch oma og aph (Va ian CP-4900) equipped wi h Molecula Sie e o 5  A, Plo U and S abilwax columns o a comple e analysis o p oduc s. The me hane con e sion ðXCH4Þ(Eq. (8)), selec i i y o hyd ogen ðSH2Þ(Eq. (9)), selec i i y o ca bon monoxide (SCO) (Eq. (10)), and yield o syngas ðYsgÞ (Eq. (11)) we e calcula ed acco ding o he ollowing equa ions: xCH4ð%Þ¼FinCH4Fou CH4 FinCH4 100 (Eq. 8) whe e FinCH4and Fou CH4a e he inle and ou le mola low o me hane, espec i ely SH2ð%Þ¼ moles o H2p oduced moles o ðH2þCO þCO2Þp oduced 100 (Eq. 9) SCOð%Þ¼ moles o CO p oduced moles o ðH2þCO þCO2Þp oduced 100 (Eq. 10) Ysgð%Þ¼xCH4ðSH2þSCOÞ 100 (Eq. 11) Ca alys cha ac e iza ion Cha ac e iza ion o he su ace was accomplished by X- ay pho oelec on spec oscopy (XPS) wi h a SPECS sys em equipped wi h a XR50 sou ce ope a ing a 250 W and a Phoibos 150 MCD-9 de ec o . The pass ene gy o he high- esolu ion spec a was se a 0.1 eV. Binding ene gy (BE) alues we e e e ed o he Ce 4þ 3d 5/2 peak a 916.9 eV. The mic os uc u e o he ca alys s was in es iga ed wi h high esolu ion ans- mission elec on mic oscopy (HRTEM) and ene gy-dispe si e X- ay analysis (EDX) using a FEI TECNAI F20 ins umen ope a ed a 200 kV. Raman spec oscopy was pe o med using a Renishaw inViaQon o con ocal Raman mic oscope equip- ped wi h a 532.1 ±0.3 nm lase wi h a nominal 100 mW ou pu powe di ec ed h ough a specially adap ed Leica DM2700 M mic oscope (x50 magni ica ion). Spec a we e acqui ed in wo anges, 50-800 cm 1 and 1000-2000 cm 1 , wi h an exposu e ime o 0.5 s, 1% o maximum lase powe and 18 epe i ions. Tempe a u e p og ammed educ ion (TPR-H 2 ) was pe o med wi h a Chems a appa a us wi h TCD de ec o . Samples we e i s ea ed a 450 C in A (50 mL min 1 ,10C min 1 ), and hen TPR was ca ied ou om 30 o 850 C (10 C min 1 ) unde 10% H 2 and kep a his empe a u e o 30 min. Resul s and discussion Cha ac e iza ion o esh ca alys s Raman spec oscopy The Raman spec a eco ded o he bime allic PdeNi/CeO 2 ca alys s p epa ed by BM and IWI me hods be o e he ca aly ic es s a e shown in Fig. 1. In all cases, he Raman we e domi- na ed by he symme ical s e ching mode o he CeO 2 la ice s uc u e (F 2g mode) a ~464 cm 1 [27]. Addi ionally, o he bime allic PdeNi/CeO 2 ca alys p epa ed by BM, Raman spec a indica ed a weak band a ~1050 cm 1 , which co e- sponds o he symme ic n 1 s e ching mode o he ni a e anion [28,29]. The NO 3band was absen in he bime allic ca alys s p epa ed by IWI because ni a e esidues dis- appea ed ollowing he calcina ion ea men pe o med a 650 C. Also, o he bime allic PdeNi/CeO 2 ca alys p epa ed by IWI, a b oad band om ~530 o 620 cm 1 is obse ed, which can be asc ibed o NiO species [29], al hough a de ec -induced ib a ional mode o ce ia la ice de ec s in he ce ia s uc u e, such as oxygen acancies, canno be disca ded (~595 cm 1 ,D band) [30]. T ansmission elec on mic oscopy (HRTEM) Wi h he aim o unde s anding he mic os uc u e o he ca alys s, he PdeNi dispe sion and he possible in e ac ions be ween me al and suppo , high esolu ion ansmission in e na ional jou nal o hyd ogen ene gy 48 (2023) 12024e1203512026 elec on mic oscopy (HRTEM) and ene gy-dispe si e X- ay analysis (EDX) we e used (Fig. 2). A ep esen a i e image o he monome allic Pd/CeO 2 ca alys p epa ed by BM is shown in Fig. 2a. The sample is e y homogeneous and con ains sub- nanome ic Pd en i ies (some o hem indica ed wi h a ows in he image), which a e well dispe sed o e he CeO 2 suppo . A la ge Pd pa icle is highligh ed wi h a dashed squa e. The Fou ie T ans o m (FT) image o his a ea is shown in he inse and shows spo s a 1.9  A om CeO 2 (220) planes and a 2.2  A om Pd (111) planes. The EDX spec um eco ded in he same a ea con i ms he na u e o he pa icle and shows he simul aneous occu ence o Ce, Pd and O ( he Cu signal o ig- ina es om he TEM g id). Fig. 2b co esponds o he bime allic PdeNi/CeO 2 ca alys s p epa ed by IWI me hod. I is di icul o dis inguish any Pd, Ni o PdeNi pa icle in TEM analysis, which indica es an excellen dispe sion o Ni and Pd on he CeO 2 suppo . The EDX spec um eco ded om he a ea enclosed by he squa e shows only weak Pd signals; no signals o Ni a e obse ed, p obably due o he low loading o Ni (0.5 w %). Fig. 2c shows he mic os uc u e o he bime allic PdeNi/ CeO 2 ca alys s p epa ed by he BM me hod. The mechano- chemical p epa a ion o PdeNi/CeO 2 c ea es an amo phous laye a ound he ce ia c ys alli es (ma ked be ween a ows). This shell exhibi s an a e age hickness o abou 2e4 nm. The EDX spec um eco ded om he a ea enclosed by he squa e conclusi ely iden i ied bo h Pd and Ni in his amo phous shell. The amo phous shell is simila o ha ecen ly epo ed in Pd/ CeO 2 ca alys s p epa ed by BM [31] and co esponds o an unp eceden ed a chi ec u e. X- ay pho oelec on spec oscopy (XPS) The su ace composi ion o he bime allic PdeNi/CeO 2 ca a- lys s p epa ed by ball milling was analyzed by X- ay Fig. 1 eRaman spec a o bime allic ca alys s wi h 1 w % Pd and 0.5 w % Ni suppo ed on CeO 2 p epa ed by BM a 50 Hz o 20 min (black), and IWI ( ed). (Fo in e p e a ion o he e e ences o colo /colou in his igu e legend, he eade is e e ed o he Web e sion o his a icle.) Fig. 2 eHRTEM images o (a) monome allic Pd (1)/CeO 2 ca alys p epa ed by BM a 50 Hz o 20 min; (b) bime allic Pd (1)-Ni(0.5)/CeO 2 ca alys p epa ed by IWI; (c) bime allic Pd (1)-Ni(0.5)/CeO 2 ca alys p epa ed by BM a 50 Hz o 20 min. in e na ional jou nal o hyd ogen ene gy 48 (2023) 12024e12035 12027 pho oelec on spec oscopy (XPS). Fig. 3a shows he Ce 3d spec um. The peaks ma ked as (882.7 eV), 2 (889 eV), 3 (899.8 eV), u (901.1 eV), u 2 (907.1eV) and u 3 (916.9 eV) co e- spond o he p esence o Ce 4þ species, and hose labeled as 0 (881.6 eV), 1 (885 eV), u 0 (898.4 eV), and u 1 (903 eV) co espond o Ce 3þ species [32,33]. Abou 40% o ce ium a he su ace appea s as Ce 3þ species. Fig. 3b shows he Pd 3d spec um. A single double co esponding o he 3d 5/2 and 3d 3/2 spli ing is p esen , wi h a binding ene gy o 3d 5/2 a 335.3 eV, which co esponds well o educed Pd. The su ace Pd/Ce and Ni/Ce a omic a ios a e 0.09 and 0.04, espec i ely, which poin s o an excellen dispe sion o he wo me als o e he ce ia suppo . Tempe a u e p og ammed educ ion (H 2 -TPR) The H 2 -TPR p o iles eco ded o he in es iga ed samples a e shown in Fig. 4. All he samples show a high- empe a u e educ ion peak loca ed abo e 700 C, which co esponds o he bulk educ ion o CeO 2 , as epo ed elsewhe e [34]. How- e e , i is wo h men ioning ha he high- empe a u e peak is shi ed o lowe empe a u es when samples a e p epa ed by he BM me hod wi h espec o analogous samples p epa ed by IWI. The Ni/CeO 2 /IWI ca alys shows a b oad H 2 con- sump ion a ~450 C, which co esponds o he educ ion o NiO s ongly in e ac ing wi h he CeO 2 suppo [35,36], ac- co ding o an enhanced me al-suppo in e ac ion ollowing calcina ion [37,38]. In con as , he H 2 consump ion on he Ni/ CeO 2 ca alys p epa ed by BM appea s a much lowe em- pe a u e (~185 C) and wi h highe in ensi y, which can be assigned o he educ ion o well-dispe sed NiO species [39]. I is in e es ing o no e ha he ball mill me hod no ably im- p o es he me al educibili y a lowe empe a u e. The monome allic ca alys Pd/CeO 2 p epa ed by BM me hod a b oad educ ion peak cen e ed a ~285 C, which can be assigned o he educ ion o PdO species ancho ed on CeO 2 [40,41]. The bime allic PdeNi/CeO 2 ca alys s p epa ed by bo h IWI and BM me hods show simila H 2 -TPR p o iles wi h a b oad H 2 consump ion a abou ~250 C, due o PdOeNiO educ ion. Compa ed o Pd/CeO 2 monome allic ca alys s, in he bime- allic PdeNi/CeO 2 ca alys s he educ ion appea s a a lowe empe a u e, indica ing ha he addi ion o Ni acili a es he educ ion o PdO. In o he wo ds, he e is a s ong syne gy be ween bo h me als, which is in acco dance o he HRTEM esul s (Fig. 2c). Fig. 3 eCe 3d (a) and Pd 3d (b) X- ay pho oelec on spec a o he bime allic Pd (1)-Ni(0.5)/CeO 2 /BM ca alys (50 Hz o 20 min). Fig. 4 eH 2 -TPR p o iles co esponding o Pd (1)/CeO 2 /BM (black), Ni(0.5)/CeO 2 /BM (g een), Ni(0.5)/CeO 2 /IWI (o ange), Pd (1)-Ni(0.5)/CeO 2 /IWI (blue) and Pd (1)-Ni(0.5)/CeO 2 /BM ( ed). Ball mill condi ions we e 50 Hz o 20 min. (Fo in e p e a ion o he e e ences o colo /colou in his igu e legend, he eade is e e ed o he Web e sion o his a icle.) in e na ional jou nal o hyd ogen ene gy 48 (2023) 12024e1203512028 Ca aly ic es s The empe a u e-dependen ca aly ic pe o mance o he di e en ca alys s p epa ed ollowed simila pa e ns. As a ep esen a i e example, Fig. 5 shows he mola low a es o eac an s (me hane and oxygen) and p oduc s (syngas, wa e and ca bon dioxide) om 300 o 550 C o bime allic PdeNi/CeO 2 ca alys s p epa ed by BM (Fig. 5a) and IWI (Fig. 5b) me hods. Acco ding o he modynamics, he con e sion o me hane in- c eases p og essi ely wi h empe a u e. Howe e , signi ican di e ences a e obse ed be ween BM and IWI ca alys s. Fo he bime allic ca alys p epa ed by BM, all he oxygen is consumed a 450 C and om his empe a u e he consump ion o me hane uns pa allel o he consump ion o wa e and he p oduc ion o syngas is obse ed. The e o e, his pe o mance below 450 C obeys o he equa ion: CH 4 þ2O 2 /CO 2 þ2H 2 O. A highe empe a u es, when all he oxygen is consumed, he eac ion ha akes place is he me hane s eam e o ming e- ac ion: CH 4 þH 2 O%CO þ3H 2 , whe e he con e sion o me hane is accompanied by he consump ion o H 2 Oand he p oduc ion o syngas inc eases d as ically. Simul aneously, he d y e o ming o me hane likely occu s: CH 4 þCO 2 %2CO þ 2H 2 . This mechanisms co esponds o he well-known “com- bus ion and e o ming eac ion (CRR)”mechanism ou lined in he in oduc ion sec ion [16,42], al hough a de ailed kine ic analysis ou o he modynamic con ol would be necessa y o discuss he eac ion mechanism in mo e de ail [43,44]. Simila end dis ibu ion and appea ance o p oduc s a e ob ained when he bime allic ca alys was p epa ed by he con en ional IWI me hod, con i ming ha a simila eac ion mechanism akes place independen ly o he p epa a ion me hod. Howe - e , all he eac ions occu a highe empe a u es, indica ing lowe ca aly ic ac i i y. Conside ing he wo consecu i e s eps in ol ed in he POM eac ion and gi en ha below 450 C he p oduc ion o syngas is no signi ican , only he pe o mance o he ca alys s a empe a u es abo e 450 C will be conside ed u he . Table 1 compiles he ca aly ic esul s o all p epa ed samples in e ms o me hane con e sion ðxCH4Þ,H 2 selec i i y ðSH2Þ, CO selec- i i y ðSCOÞand yield o syngas ðYsgÞ. Ba e CeO 2 esul s a e also included as a blank es , as well as chemical equilib ium alues. The CeO 2 suppo in he absence o Pd and Ni is o ally inac i e o POM unde he eac ion condi ions es ed. Mo e- o e , he ca aly ic ac i i y esul s o he ca alys s wi h 0.5 w % Ni suppo ed on CeO 2 p epa ed by ei he IWI o BM me hods showed low me hane con e sion and he o ma ion o syngas was no obse ed a all. On he o he hand, i is clea ha he ca aly ic ac i i y o Pd/CeO 2 is much g ea e han Ni/CeO 2 ,as he me hane con e sion alues o Pd/CeO 2 ca alys s a 550 C doubled hose ob ained o e Ni/CeO 2 ca alys s and he syngas yield was 42e48%. The milling pa ame e s had negligible e - ec on he ca aly ic pe o mance o he monome allic ca a- lys s, as me hane con e sion a 550 C oscilla ed be ween 51 and 55% and syngas yield om 42 o 47%. F om Table 1, i can be clea ly seen ha he coope a i e e ec be ween Pd and Ni in he bime allic ca alys s is ema kable, wi h a d ama ic inc ease in bo h he me hane con e sion and he syngas yield compa ed o monome allic ca alys s. A 550 C, bime allic PdeNi/CeO 2 ca alys s show me hane con e sion le els om 62 o 75%, selec i i y owa ds H 2 o 64e66%, selec i i y owa ds CO o 19e24%, and syngas yield be ween 52 and 67%. These esul s demons a e ha he syne gy be ween Pd and Ni suppo ed on CeO 2 yields ca alys s wi h imp o ed ac i i y and selec i i y in he POM wi h espec o monome allic Ni/CeO 2 and Pd/CeO 2 . The p epa a ion me hod (BM s. IWI), he o de o inco - po a ion o he me als (co-BM/co-imp egna ion s. sequen ial BM/IWI) play an impo an ole on he ca aly ic pe o mance o he bime allic PdeNi/CeO 2 ca alys s. Fig. 6a shows he me hane con e sion a di e en empe a u es o he bime- allic Pd (1)-Ni(0.5)/CeO 2 ca alys s p epa ed by co- imp egna ion and sequen ial-imp egna ion. In e es ingly, a low empe a u e (450 C) he me hane con e sion o he ca - alys s p epa ed by sequen ial imp egna ion is much highe han ha o he ca alys p epa ed by co-imp egna ion, ega dless o he o de o addi ion used o Pd and Ni. In con as , a high empe a u es (500 and 550 C), he me hane con e sion a ained by he ca alys p epa ed by co- imp egna ion is highe han hose o he ca alys s p epa ed Fig. 5 eMola low a es eco ded o bime allic ca alys s Pd (1)-Ni(0.5)/CeO 2 p epa ed by BM a 50 Hz o 20 min (a) and IWI (b) me hods. GHSV ¼12 £10 3 h ¡1 , F/W ¼60 L h ¡1 g ¡1 . in e na ional jou nal o hyd ogen ene gy 48 (2023) 12024e12035 12029 by sequen ial imp egna ion. No ema kable di e ences we e obse ed be ween bime allic ca alys s p epa ed by co-BM o sequen ial-BM (Fig. 6b). In all cases, he me hane con e sion was simila a each empe a u e. In any case, he addi ion o Pd i s gi es be e ca aly ic esul s han when Ni is i s inco po a ed, which poin s o a be e ca aly ic pe o mance when Pd in e ac s s ongly wi h CeO 2 , as opposed o Ni. On he o he hand, he e ec o milling condi ions ( e- quency and ime) on he ca aly ic ac i i y o bime allic PdeNi/ CeO 2 /BM ca alys a di e en empe a u es is shown in Fig. 6c and d. The ene gy applied du ing he ball milling in e ms o equency o ib a ion has a s ong e ec on ca aly ic ac i i y; he highe he ene gy he be e he ca aly ic ac i i y o he ca alys (Fig. 6c). The e o e, i is clea ha high-ene gy milling has a bene icial in luence on he numbe and quali y o he ac i e si es [45,46]. This wo k adds an addi ional e idence ha ball milling is able o c ea e unp eceden ed a chi ec u es ha can exhibi ou s anding ca aly ic ac i i y. The ball milling ime is ano he impo an ac o ha can a ec ca aly ic pe o mance. Fig. 6d shows he e ec o he milling ime ( om 5 o 40 min) on he me hane con e sion alues. A good comp omise be ween me hane con e sion and milling ime is ound o he ca alys p epa ed using 20 min o milling ime. Acco dingly, a ball milling equency o 50 Hz o 20 min ap- pea s as he op imal syn hesis condi ions. An impo an aspec ega ding bime allic ca alys s is he ela i e amoun o he wo me als in ol ed. In ou case, i should be also conside ed ha he cos o Pd is much highe han ha o Ni, which ob iously has a di ec impac on he inal cos o he ca alys . Fig. 7 shows he me hane con e sion and syngas yield a 450 C and 550 C exhibi ed by PdeNi/ CeO 2 /BM and PdeNi/CeO 2 /IWI ca alys s con aining di e en amoun s o Pd and Ni bu keeping he o al me al loading a 1.5 w % (Pd w .% om 0.06 o 1% and Ni w .% om 0.5 o 1.44%). Two aspec s me i pa icula a en ion. Fi s , i is e y in e es ing o obse e ha a 450 C bo h he me hane con- e sion and syngas yield a e much highe o all he ca alys s p epa ed by BM wi h espec o hei espec i e coun e pa s p epa ed by he IWI me hod. This clea ly demons a es ha e y eac i e and speci ic ac i e si es a e c ea ed by he BM me hod, which a e highly ac i e o he POM p ocess a low empe a u e. A 550 C, he ca aly ic pe o mance o PdeNi/ CeO 2 /BM and PdeNi/CeO 2 /IWI ca alys s a e simila . Second, he e ec o he Pd amoun on he ca aly ic pe o mance is lowe han expec ed and depends also on he p epa a ion me hod. Fo he PdeNi/CeO 2 /IWI ca alys s, a end is obse ed Table 1 eMe hane con e sion, hyd ogen and ca bon monoxide selec i i y alues and syngas yields ob ained o e ba e CeO 2 , Ni/CeO 2 , Pd/CeO 2 and PdeNi/CeO 2 bime allic ca alys s p epa ed by incipien we ness imp egna ion (IWI) and d y ball milling (BM) using di e en syn hesis pa ame e s and me al loading alues. Reac ion condi ions: CH 4 :ai :N 2 ¼4:11:85, F/ W¼60 L h ¡1 g ¡1 , GHSV ¼12 £10 3 h ¡1 . Sample Hz min w .%Pd w .%Ni x450C CH4x550C CH4S550C H2S550C CO Y550C syngas Equilib ium - - - - 51.3 77.9 67.2 26.3 70.9 CeO 2 /BM 50 10 0 0 0 0 0 0 0 Ni/CeO 2 /BM 50 10 0 0.5 3.2 22 0 0 0 Ni/CeO 2 /IWI - - 0 0.5 3 18.6 0 0 0 Pd/CeO 2 /BM 50 10 0.5 0 32.6 52.7 63.3 17.7 42.7 Pd/CeO 2 /IWI - - 0.5 0 39.7 51 63.8 23 44.5 Pd/CeO 2 /BM 50 10 1 0 30.5 53.2 64.8 19.3 44.8 Pd/CeO 2 /IWI - - 1 0 34.5 57.4 64.5 19.4 48.2 Pd/CeO 2 /BM 50 20 1 0 32.7 55.6 65.2 20.2 47.6 Pd/CeO 2 /BM 15 10 1 0 35.2 54.9 63.5 18 44.7 Pd/CeO 2 /BM 30 10 1 0 31.4 51 64 18.2 41.9 PdeNi/CeO 2 /BM 15 10 1 0.5 36.4 62.4 64.2 19.2 52.1 PdeNi/CeO 2 /BM 30 10 1 0.5 39.9 67.1 64.9 20.5 57.4 PdeNi/CeO 2 /BM 50 10 1 0.5 44 71.8 65.5 21.7 62.7 PdeCeO 2 /BM/Ni/BM 50 10 1 0.5 42.5 71.6 65.5 22 62.6 NieCeO 2 /BM/Pd/BM 50 10 1 0.5 41.6 68 64.9 20.5 58.1 PdeNi/CeO 2 /BM 50 5 1 0.5 37.5 67.2 65.5 20.7 57.9 PdeNi/CeO 2 /BM 50 15 1 0.5 38 66.3 65.5 21.2 57.5 PdeNi/CeO 2 /BM 50 20 1 0.5 42.1 72.4 66 22 63.7 PdeNi/CeO 2 /BM 50 40 1 0.5 41.4 71.5 65.8 21.7 62.6 PdeNi/CeO 2 /BM 50 20 0.75 0.75 37.9 67.4 65.4 21.7 58.7 PdeNi/CeO 2 /BM 50 20 0.5 1 35.5 68.2 65.3 21.7 59.4 PdeNi/CeO 2 /BM 50 20 0.25 1.25 37.7 70.6 65.9 23.8 63.4 PdeNi/CeO 2 /BM 50 20 0.12 1.38 40.8 69.5 65.9 23.6 62.2 PdeNi/CeO 2 /BM 50 20 0.06 1.44 36.6 69.5 66 23.1 62 NieCeO 2 /IWI/Pd/IWI - - 1 0.5 38.5 51.5 64.6 19.5 54 PdeCeO 2 /IWI/Ni/IWI - - 1 0.5 42.2 71.7 66 21.8 63 PdeNi/CeO 2 /IWI - - 1 0.5 12.6 75.8 66.1 22.8 67.4 PdeNi/CeO 2 /IWI - - 0.75 0.75 11.6 74.8 66.2 22.5 66.3 PdeNi/CeO 2 /IWI - - 0.5 1 7.7 74.4 66.3 22.8 66.3 PdeNi/CeO 2 /IWI - - 0.25 1.25 6.9 70 66 21.8 63 PdeNi/CeO 2 /IWI - - 0.12 1.38 2.8 67.7 65.8 23 60.2 PdeNi/CeO 2 /IWI - - 0.06 1.44 3.3 65.4 66 22.9 62.6 in e na ional jou nal o hyd ogen ene gy 48 (2023) 12024e1203512030 be ween me hane con e sion and Pd con en : he highe he Pd amoun he highe he con e sion o me hane. This is no he case o he PdeNi/CeO 2 /BM ca alys s, whe e bo h he me hane con e sion and syngas yield a e a he unsensi i e o he ela i e amoun s o Pd and Ni in he ange s udied. I should be highligh ed ha he Ni/CeO 2 /BM sample showed Fig. 6 eCon e sion o me hane a 450, 500 and 550 C o e PdeNi/CeO 2 ca alys s p epa ed by IWI (a), PdeNi/CeO 2 ca alys s p epa ed by BM a 50 Hz o 10 min (b), PdeNi/CeO 2 /BM p epa ed a di e en milling equency o 10 min (c), and PdeNi/ CeO 2 /BM p epa ed a 50 Hz o di e en milling ime (d). GHSV ¼12 £10 3 h ¡1 , F/W ¼60 L h ¡1 g ¡1 . Fig. 7 eCon e sion o me hane (a) and yield o syngas (b) o he bime allic Pd(x)-Ni(y)/CeO 2 ca alys s con aining di e en amoun s o Pd and Ni p epa ed by BM (black) and IWI ( ed) me hods a 450 C and 550 C. All ca alys s con ain a o al me al loading o 1.5 w %. GHSV ¼12 £10 3 h ¡1 , F/W ¼60 L h ¡1 g ¡1 . (Fo in e p e a ion o he e e ences o colo /colou in his igu e legend, he eade is e e ed o he Web e sion o his a icle.) in e na ional jou nal o hyd ogen ene gy 48 (2023) 12024e12035 12031 low me hane con e sion (3.2% a 450 C and 22% a 550 C, Table 1) and no syngas p oduc ion, whe eas wi h only 0.06 w % Pd he me hane con e sion inc eased up o 36.6 and 69.5% a 450 and 550 C, espec i ely, and syngas yield was 62%. Ce ainly, he bime allic PdeNi sys em appea s as a pa icu- la ly appealing me al combina ion o POM. I has ecen ly been shown by using DFT calcula ions ha he subs i u ion o Ce by Pd ions in he su ace o he ca alys s o igina es highly ac i e and s able species based on Pd x Ce 1-x O d which a e highly e ec i e in he apid CeH bond ac i a ion [47,48]. F om he HRTEM images, we canno conclude i Pd subs i u es Ce in he ce ia s uc u e bu , in any case, we ha e e idence ha bo h Pd and Ni a e highly dispe sed a he subnanome ic le el. A low empe a u e (450 C), whe e he bime allic PdeNi ca alys s p epa ed by BM exhibi a pa icula high ac i i y o POM as ou lined abo e, he bes pe o mance (bo h me hane con e sion and syngas yield) was obse ed o PdeNi/CeO 2 / BM wi h 0.12 w % Pd and 1.38 w % Ni. Cha ac e iza ion o he ca alys s a e eac ion The Raman spec a eco ded on he samples PdeNi/CeO 2 /BM, and PdeNi/CeO 2 /IWI a e he ca aly ic es discussed abo e a e shown in Fig. 8. In all cases, he posi ion o he F 2g band o CeO 2 did no shi a e he ca aly ic es wi h espec o he alues eco ded be o e eac ion (Fig. 1), and he esidual ni- a e signals in he sample PdeNi/CeO 2 /BM disappea ed a e eac ion due o decomposi ion. In addi ion, he wo cha ac- e is ic g aphi e D and G bands a abou ~1345 and ~1595 cm 1 [49,50] we e obse ed in he Raman spec a o he ca alys s a e eac ion, being hei ela i e con ibu ion in he spec a conside ably mo e in ense in he case o he bime allic sample p epa ed by imp egna ion. The e o e, less coke deposi ion occu ed on he bime allic sample p epa ed by ball milling. Ca alys PdeNi/CeO 2 /BM was s udied by HRTEM and EDX (Fig. 9). In e es ingly, a la ge numbe o oids a e iden i ied in he ce ia c ys alli es, which we e no isible in he sample be o e eac ion (Fig. 2c). These a e en a i ely asc ibed o clus e s o oxygen acancies, p obably in con ac wi h he me als, c ea ed unde he educing en i onmen c ea ed by syngas du ing POM. On he o he hand, e en i he amo phous shell is no longe obse ed a e he ca aly ic es , Pd and o Ni pa icles escape de ec ion in HRTEM bu a e p esen in EDX analyses, indica ing ha he high dispe sion o he me als is main ained du ing he ca aly ic eac ion. Also, and in acco - dance wi h he Raman esul s, coke is iden i ied by i s cha - ac e is ic spacing a 3.8  A, which co esponds o he (0001) in e plana spacing o poo ly o de ed g aphi e. Howe e , he amoun o deposi ed coke is a he low. S abili y es s In o de o p o e he long- e m pe o mance o he ca alys s, s abili y es s o mo e han 100 h a 550 C we e ca ied ou . Since bime allic ca alys s showed good me hane con e sion and selec i i y o syngas (Table 1), PdeNi/CeO 2 ca alys s wi h 1 w % Pd and 0.5 Ni loading p epa ed by bo h IWI and BM Fig. 8 eRaman spec a o bime allic Pd (1)-Ni(0.5)/CeO 2 ca alys s p epa ed by BM a 50 Hz o 20 min (black), and IWI ( ed) a e eac ion (CH 4 :ai :N 2 ¼4:11:85, F/ W¼60 L h ¡1 g ¡1 , GHSV ¼12 £10 3 h ¡1 ). (Fo in e p e a ion o he e e ences o colo /colou in his igu e legend, he eade is e e ed o he Web e sion o his a icle.) Fig. 9 eHRTEM images o he bime allic Pd (1)-Ni(0.5)/CeO 2 /BM ca alys (50 Hz o 20 min) a e he ca aly ic es . in e na ional jou nal o hyd ogen ene gy 48 (2023) 12024e1203512032