A DFT Insight into the Tuning Effect of Potassium Promoter on the Formation of Carbon Atoms via Carburization Gases Dissociation on Iron-Based Catalysts

: The research of the formation mechanism of iron carbides is significant to design the high-performance catalysts for the Fischer–Tropsch synthesis (FTS) process. In this paper, the effect of potassium promoter on the formation of atomic carbon via carburization gases dissociation on the iron-based catalyst, the C 2 H 4 , C 2 H 2 and CO/H 2 adsorption energies and dissociation paths as well as the rate constants of the corresponding elementary steps are investigated by DFT on the Fe(110), Fe(110)-K 2 O, Fe(211) and Fe(211)-K 2 O surfaces. The calculation results demonstrated that the K 2 O promoter can modify the capabilities of surface C formation via the thermodynamic method as well as the kinetical method. The K 2 O promoter can increase the CO adsorption energy while decreasing the C 2 H 4 adsorption energy both on Fe(110) and Fe(211) surfaces. Kinetically, via tuning the catalyst surfaces from Fe(110) to Fe(211), the K 2 O promoter can inhibit the ability of C 2 H 4 /C 2 H 2 dissociation to atomic carbon, while enhancing the ability of CO/H 2 decomposition to atomic carbon. The C 2 H 4 /C 2 H 2 dissociation rate constants on Fe(211) and Fe(211)-K 2 O are about 10 7 times slower than that on Fe(110) and Fe(110)-K 2 O, whereas the dissociation rate constants of CO/H 2 on Fe(211) are about 10 6 times faster than that on Fe(110), and about 10 7 times faster on Fe(211)-K 2 O than on Fe(110)-K 2 O.


Introduction
Owing to the lack of crude oil, Fischer-Tropsch synthesis (FTS), which converts syngas (CO and H2) into valuable chemicals and clean fuels, is of important academic and commercial significance in China. The catalyst is one of the most key factors account for the successes of the industrial FTS process, and the iron-based catalysts are extensively studied and used for decades due to their low cost and relative high activity [1][2][3][4][5]. It is well known that the main active phases are iron carbides in the iron-based FTS [6][7][8]. However, because of the complex phase transformations, numerous iron carbide phases can be formed during the carburization process, such as Fe2C, Fe5C2 and Fe3C, etc. [9][10][11][12][13][14]. Hence, the research of the formation mechanism of iron carbides is significant to design the highperformance catalysts for FTS process.
The formation of carbon atoms via carburization gases dissociation on iron-based catalyst surfaces is the precondition for generation the iron carbides. The carbon atoms decomposed from carburization gases would diffuse into the iron lattice when the carbon chemical potentials of carburization gases are greater than that of iron carbides phase. The most studied carburization gases are CO and syngas, because they have practical applications. Density Function Theory (DFT) calculations indicated that the presence of H2 could accelerate the CO dissociation on metallic Fe (111) surfaces, suggesting that the syngas (H2/CO) is an excellent carburization agent [15,16]. De Smit et al., using the in-situ setup (XAFS/XRD/Raman) under high pressure, investigated the carburization of α-Fe2O3 under different carbon chemical potentials (μc) in a syngas atmosphere and they found higher μc is beneficial to the formation of carbon-rich iron carbides [6]. Researchers also studied other carburization gases, such as C2H4 and C2H2 gas. These carbonaceous gases also could be partially dissociated into surface carbon and H2 under FTS conditions, the surface carbon is a carbon source for the carburization of the iron-based catalysts [17][18][19][20]. Although these researchers made great efforts to investigate the influence of carburization gases, the intrinsic mechanism of carburization are still ambiguous, e.g., how the carburization gases were decomposed to form the surface carbon atoms, and then how the surface carbon atoms were permeated into the iron crystal lattice-all these issues need to be illuminated. In view of the carburization of the iron catalyst, the first step is the carbon atoms' formation which has not been fully researched on the micro level, so it is considered that the dissociation of the carburization gases into atomic carbon is necessary to be calculated in detail.
The important influence factor of the formation of carbon atoms via the dissociation of carburization gases is the catalyst promoter. The alkali metal and alkaline earth metal are the commonly studied promoters [21][22][23][24]. Thus far, the potassium promoter has been extensively applied in iron-based FTS catalysts, especially in commercial plants. It is well known that potassium promoter not only can increase the FTS activity, but also can increase the selectivity of higher molecular hydrocarbons and olefins [25][26][27][28][29][30][31]. It can be clearly found that all these researches mainly focused on the effect of potassium promoter to the catalytic performance of FTS [32][33][34][35], including the effect of the K2O promoter on the morphology control to pure iron (α-Fe) [32] and Hägg carbide (Fe5C2) [34], as well as the hydrogenation mechanism of surface carbon [33] and CO [35] on the Fe5C2 surface; while the effect of promoter to the formation of carbon atoms from carburization gases on iron-based catalyst surface is hardly studied. In other words, the effect of the K2O promoter on the decomposition ability of the carburization gases into the surface carbon atoms needs to be studied systematically on the iron catalysts' surfaces.
Using in situ XRD, Xu et al. recently studied the effect of varying carburization gases and potassium promoter on the carburization behaviors of α-Fe catalysts [36]. They reported that potassium could increase the carburization rate and in favor of the formation of carbon-rich iron carbides under CO or syngas, while the potassium promoter decreased the carburization rate and inhibited the formation of carbon-rich iron carbides under C2H4 or C2H2 atmosphere. Furthermore, via calculating the charge density difference, Bader charge and the adsorption energy of C2H4 and C2H2 on Fe(211) and Fe(211)-K2O surface, they concluded that the potassium promoter could weaken the adsorption ability of C2H4 and C2H2 thermodynamically, which finally reduced the carburization capabilities of C2H4 and C2H2.
It has been reported that the percentage of the Fe(110) facet is predominant for un-promoted α-Fe catalysts, while the Fe(211) facet is dominated for potassium promoted α-Fe catalysts [32]. Therefore, the comparison of the carburization gases adsorption energies on Fe(100), Fe(110)-K2O, Fe(211) and Fe(211)-K2O surfaces would make sense for understanding the effect of K2O promoter and designing the high-performance catalysts of FTS. In addition, the formation of atomic carbon via dissociation of carburization gases on these four facets also should be calculated, which is the precondition of carburization.
In this work, we used the GGA-PBE method to explore the adsorption energies and dissociation mechanisms of carburization gases on Fe(110), Fe(110)-K2O, Fe(211) and Fe(211)-K2O surfaces, respectively. Furthermore, on the basis of the calculation results, we identified the most favorable dissociation routes of carburization gases to form atomic carbon and gained the related rate constants. Our calculation results provide deep insights into the tuning effects of potassium promoter for the formation of carbon atoms via the dissociation process of CO/H2, C2H4 and C2H2 gases on metallic iron catalyst surfaces which well explained the experimental phenomenal [36], and broaden the fundamental understanding of carburization behaviors of iron-based catalysts in the FTS process.

Adsorptions of C2H4, C2H2 and CO/H2-The Initial Step of Carburization
As is well-known, carburization behavior of α-Fe catalyst is closely related on the nature of the catalyst and the pretreatment conditions. In the introduction, it has been mentioned that the Fe(110) surface is predominant for pure α-Fe catalysts and the Fe(211) facet is dominated for potassiumpromoted α-Fe catalysts. Therefore, to understand the carburization behavior of the α-Fe catalyst at the atomic scale, we selected the Fe(110) and Fe(211) surfaces as the models of the α-Fe catalyst; firstly, we calculated the thermodynamic adsorption energies (Eads) of carburization gases (C2H4, C2H2 and CO/H2) on the Fe(110), Fe(110)-K2O, Fe(211) and Fe(211)-K2O surfaces. The corresponding Eads are listed in Table 1, and the top and side view configurations of C2H4, C2H2, CO and H2 adsorption on the four surface models are given in Figure 1. In Table 1, it can be clearly seen that the CO adsorption energies on Fe(110)-K2O and Fe(211)-K2O are more negative than that on Fe(110) (−2.28 vs. Totally, on the two surfaces of α-Fe catalysts, the CO and C2H4 adsorption can be stabilized and destabilized by the K2O promoter, respectively, which is probably to explain the Xu's et al. experimental results thermodynamicallythe K2O promoter can enhance and inhibit the carburization capabilities of CO and C2H4 on α-Fe catalysts [36]. Nevertheless, the C2H2 acts as a probable intermediate species of C2H4 dissociation, its adsorption energies on the two surfaces are changed oppositely by the K2O promoter. Therefore, it is inferred that, although the thermodynamic effect of K2O promoter can partially explain the experimental phenomena, the dynamic influence is probably more important for the carburization behavior of α-Fe catalyst, which needs to be performed in detail. In order to obtain a deep insight into the effect of the K2O promoter on the four surface models of Fe(110), Fe(110)-K2O, Fe(211) and Fe(211)-K2O, the total Bader charge differences of Fe atoms (∆q) covered with and without surface species of C2H4, C2H2, CO and H2 are analyzed in depth, and the detailed calculation method has been described in the Section 3.1. Meanwhile, the total Bader charge differences of Fe atoms in Fe(110) and Fe(211) covered with and without K2O are also calculated (see Table 2).
For the adsorptions of C2H4, C2H2, CO and H2, all the ∆q are negative on the four models, suggesting the electrons mainly transfer from Fe atoms to these surface species. In addition, it can be seen that the four ∆q of Fe atoms on Fe(110)-K2O and Fe(211)-K2O (adsorbed with C2H4, C2H2, CO and H2) are more negative than that of Fe(110) and Fe(211), suggesting the K2O can promote the electron transfer from the surfaces to the adsorbed species. Then, the positive value of ∆q (0.45 and 0.46) for K2O adsorption on Fe(110) and Fe(211) further indicate that the electrons will be transferred from K2O to Fe atoms, which has been proved indirectly by the experimental results that the catalyst surface basicity could be modified by potassium promoter [37,38]. Therefore, it can be concluded that the electrons of the K2O promoter will be transferred to the surface species via the Fe atoms in the catalyst surface. Furthermore, the same electronic transferring situation also can be seen from the charge density difference analysis of the surface adsorbed C2H4, C2H2, CO, H2 and K2O on the four models (see Figure 2). Via the above discussion, it is known that the K2O promoter can stabilize the adsorption of CO, but destabilize the adsorption of C2H4. However, in this part of work, the K2O promoter has the same electronic properties for the different adsorption species. In a word, although the K2O promoter as an electronic donor can afford electrons to all the different adsorbates, it has an obvious different effect for different adsorption species. Based on a previous study [39], the chemical interactions are very complicated between the transition metal (TM) and the compounds of carbonyl (CO), carbine (C=C) and carbine (C≡C). It was reviewed that the bonding model of TM-CO is obviously different from that of TM-C=C and TM-C≡C, e.g., the donor-acceptor interactions are considered as the dominant model of the TM-CO bond, while there is no electronic-back-donation in the bond of TM-C=C and TM-C≡C. Therefore, it is inferred that the different electronic interactions lead to the different effects of K2O promoter on the CO, C2H4, C2H2 and H2 adsorption.

Surface Atomic Carbon Formation-The Second Step of Carburization
In order to reveal essential role of the K2O promoter during the carburization process, the formation routes of the surface C atoms via carburization gases dissociation are necessary to be investigated. In Figure 3, the most favorable pathways for C2H4/C2H2 dissociation into surface C atom on the Fe(110), Fe(110)-K2O, Fe(211) and Fe(211)-K2O, as well as the configurations of the corresponding intermediates, are shown. In Figure 3, the optimum routes of CO/H2 dissociation into surface C atom on the four surfaces, as well as the corresponding structures of the intermediates are displayed. Meanwhile, for better comparing and understanding, all the barriers of the corresponding element steps, as well as the total effective barriers for C2H4/C2H2 and CO/H2 dissociation on the four surfaces are also listed in Table 3. Furthermore, all the possible mechanisms of C2H4/C2H2 and CO/H2 dissociation on the four surface models also have been given in the Supporting Information ( Figure  S1 to S8).

Surface Atomic Carbon Formation via the Dissociations of C2H4/C2H2
On Fe(110) and Fe(110)-K2O (see Figure 3 and Table 3), the most favorable steps of C2H4 dissociation begin with C2H4 dehydrogenation into the surface species of CHCH and two atomic H (C2H4→ CH2CH + H → CHCH + 2H), the calculation barriers of CH2CH formation are 0.37 and 0.39 eV on Fe(110) and Fe(110)-K2O, and the CHCH formation barriers are 0.16 and 0.19 eV, respectively. Furthermore, their total reaction energies of C2H4→ CHCH + 2H on Fe(110) and Fe(110)-K2O are −1.12 and −0.95 eV, suggesting the reaction can easily occur on two surfaces no matter from the view of thermodynamics or kinetics. After that, via the different paths, the C2H2 will be further dissociated into the surface 2C and 2H atoms (C2H2→ 2C + 2H) on the two surfaces.
For Fe(110), the C2H2 can directly dissociate into two CH species with a barrier of 0.81 eV, and the consequent decomposition of the two CH will form two surface C atoms with barriers of 0.72 and 1.17 eV. Here, we can clearly find that the second barrier of CH dissociation, as well as the adsorption properties of C+CH+3H to 2C+4H are significantly changed. Therefore, to explain about the differences, the Fe-Fe bond lengths and angles of the Fe(110) surface structures adsorbed with 2CH+2H, C+CH+3H and 2C+4H are compared in detail(see Figure S9). With the coverage increasing of the surface carbon atom, the structure of Fe(110) becomes distorted gradually, so it is considered that the changes of the second CH adsorption and reaction properties should be mainly attribute to the surface distortion. For Fe(110)-K2O, the most favorable path for C2H2 dissociation forming surface C atoms is C2H2→ CCH + H → C + CH +H → 2C + 2H, and the three barriers are 0.99, 0.53 and 1.08 eV, respectively.
As a contrast, on Fe(211) and Fe(211)-K2O, the favorable pathways ( Figure 3) and the corresponding barriers (Table 3) of C2H4/C2H2 dissociation are investigated systematically. For the clean surface of Fe(211), the calculation results shown that the C2H4 will be firstly transferred into the ravine site from the ridge site with a barrier of 0.92 eV, and it is endothermic by 0.31 eV. With that, through the pathway of C2H4→ CH2CH + H → CCH2 + 2H → CCH + 3H → C2 + 4H, the C2H4 in the ravine site can be further dissociated into a surface C2 and four H atoms with four lower barriers of 0.49, 0.17, 0.68 and 0.82 eV. However, the subsequent decomposition of the surface C2 is very difficult, which need a very high barrier of 1.95 eV, indicating the C-C bond cracking of the surface C2 species (C2→ 2C) is the rate-determining step. On Fe(211)-K2O, although the ridge site of C2H4 can be directly dehydrogenated into the ridge site of CH2CH and H atom (C2H4→ CH2CH + H) with a barrier of 0.65 eV, the ridge site of CH2CH also needs to be transferred into the ravine site with a barrier of 0.69 eV. After that, with the route of CH2CH + H → CHCH + 2H → CCH + 3H → C2 + 4H, the C2H3 in the ravine site can be further dehydrogenated into a surface C2 and four H atoms with three lower barriers of 0.25, 0.35 and 0.30 eV. Nevertheless, the C-C bond cracking of the C2 species (C2→ 2C) is also difficult because of the very high barrier of 1.75 eV. The formation of atomic carbons via C2H2 dissociation on Fe(211) facets are displayed in Figure S3, and the rated determining step is the C-C bond cracking of the C2 species (C2→ 2C) which is the same with that of C2H4 dissociation.
For comparison, the K2O promoter decreased the total effective barriers of the C2H4/C2H2 dissociation from 1.17 eV to 1.08 eV on the Fe(110) facet and from 2.04 eV to 1.75 eV on the Fe(211) facet, respectively. It can be concluded that the K2O promoter can slightly improve the ability of forming atomic carbon via C2H4/C2H2 dissociation on Fe(110) and Fe(211) surface kinetically. However, this conclusion is contradictory with Xu et al.'s experimental results that the K2O promoter can inhibit the carburization capabilities of C2H4 and C2H2 on α-Fe catalysts [36].On the basis of the literature [32], it is known that the K2O promoter can modify the exposed surface proportion of α-Fe catalysts. As increasing of K/Fe ratio, the percentage of Fe(211) is increased continuously from 32% to 70%, while the Fe(110) percentage is decreased from 39% to 20%. Surprisingly, it can be clearly found that the ability of atomic carbon formation from C2H4/C2H2 dissociation on Fe(211) and Fe(211)-K2O are much harder than that on Fe(110) and Fe(110)-K2O kinetically (2.04/1.75 vs. 1.17/1.08 eV). Therefore, it is reasonably inferred that the Fe(211) surface, tuned by the K2O promoter, is attributed to the inhibiting of the carburization capabilities of C2H4 and C2H2 on α-Fe catalysts. In other words, the tuning effect of the K2O promoter increases the exposed proportion of Fe(211), while it is exactly unfavorable the C2H4/C2H2 dissociation, and inhibits the carburization capabilities of C2H4 and C2H2, which could well explain Xu et al.'s experimental results [36].

Surface Atomic Carbon Formation via the Dissociations of CO and CO/H2
On Fe(110) and Fe(110)-K2O surfaces ( Figure 4 and Table 3), through three element steps of CO + 2H → CHO + H → CH + O + H → C + O + 2H, the CO/H2 will be dissociated into the surface C, O and H atoms. The calculation results shown that the three barriers are 1.31, 0.46 and 0.70 eV, respectively, on the Fe(110), suggesting the rate determining step is the first step of CHO formation with a high barrier of 1.31 eV. Similarly, the three corresponding barriers are 1.65, 0.45 and 0.78 eV, and the formation of CHO also is the rate determining step on the Fe(110)-K2O.
The mechanism of CO/H2 dissociation on Fe(211) surfaces is significantly different from that on Fe(211)-K2O surfaces. For the clean surface of Fe(211), the most favorable route is completely the same with that on the Fe(110) surface, the surface C formation from CO/H2 decomposition needs three element steps of CO + 2H → CHO + H → CH + O + H → C + O + 2H, and the corresponding barriers are 0.72, 0.54 and 0.67 eV, respectively. For the K2O-promoted surface of Fe(211)-K2O, the optimal route is the direct dissociation of CO (CO + 2H → C + O + 2H), and the barrier is 0.77 eV.
In summary, it can be concluded that K2O promoter enhanced the total effective barrier from 1.31 eV to 1.89 eV on Fe(110) surface, while reduced the total effective barriers from 1.26 eV to 0.77 eV on Fe(211) surface. This calculation results indicate that K2O promoter has adverse effect on the ability of forming atomic carbon via CO/H2 dissociation on Fe(110) and Fe(211) surfaces kinetically, i.e., they can inhibit and promote the CO decomposing, respectively. Similar with the analysis of the effect of K2O promoter on the C2H4/C2H2 dissociation, it is inferred that the K2O promoter increases the exposed proportion of Fe(211), and it is just beneficial to the CO/H2 dissociation (1.26/0.77 vs. 1.31/1.89 eV), which enhances the carburization capability of CO/H2, thus well explains the Xu et al.'s experimental result that the K2O promoter can enhance the carburization capabilities of CO/H2 on α-Fe catalysts [36].

Rate Constants of Elementary Steps
To get an in-depth understanding of the effect of potassium promoters on the formation process of surface atomic carbon on the metallic iron catalysts under different carburization gases, the rate constants (k, s −1 ) of each element steps, as well as the total effective rate constants (keff, s −1 ) of C2H4/C2H2 and CO/H2 dissociation on Fe(110), Fe(110)-K2O, Fe(211) and Fe(211)-K2O were computed on the basis of the transition state theory [40,41]. The calculation method of the rate constant has been depicted in Section 3.1, and corresponding results are summarized in Table 3.
In Table 3, it can be clearly found that the rate-determining step of C2H4/C2H2 dissociation is the dehydrogenation of the second CH species (C + CH + 3H → 2C + 4H) both on Fe (110)

Methods
In the Vienna Ab Initio Simulation Package (VASP) [42,43], the periodic plane wave-based method was used for all DFT calculations, in which the corresponding plane wave basis was set up to 400 eV, and the spin polarization was included. Specifically, the projector augmented wave (PAW) method was used to describe the electron-ion interaction [44,45], the generalized gradient approximation was adopted to deal with the electron exchange and correlation energies in the Perdew Burke Ernzerhof functional (GGA-PBE) [46]. Via the Methfessel-Paxton technique, the electron smearing width was set as 0.2 eV. Furthermore, the climbing image nudged elastic band method (CI-NEB) [47] was chosen to estimate the transition states, and their stretching frequencies were analyzed to evaluate whether the structure is a minimum or transition state without or with only one imaginary frequency.
According to Eads = EA/surf -[Esurf + EA], the adsorption energy of the adsorbates was calculated, where EA/surf, Esurf and EA is the total energy of the surface with adsorbates, the bare surface, and the free adsorbates in the gas phase. In a word, the more negative of Eads represents the stronger adsorption. According to ∆Er = EFS -EIS and Ea = ETS -EIS, the reaction energy (∆Er) and activation energy (Ea) are calculated, where EIS, ETS and EFS are the corresponding energies of the initial state (IS), transition state (TS) and final state (FS), respectively.
Based on the transition state theory [40,41] the rate constants (k) of C2H4/C2H2 and CO/H2 dissociation have been computed to distinguish the formation ability of surface atomic carbon from different carburization gases of C2H4/C2H2 and CO/H2 on the Fe surfaces covered with and without the potassium promoter (the optimized models are given in Figure 5). The rate constant for element steps of the dissociation was calculated using Equation (1), in which kB and h is the Boltzmann and Planck constant, T is the reaction temperature of 600 K, qTS,vib and qIS,vib are the harmonic vibrational partition functions of the transition and initial state, and Ea is the activation energy derived from DFT calculations. For qTS,vib and qIS,vib, they were obtained according to Equation (2), in which the νi is the corresponding vibrational frequency for each vibrational mode of the surface intermediate.
The total Bader charge difference of Fe atoms (∆q) covered with and without surface species was calculated according to Equation (3) as follows.
Where qA/surf is the total Bader charge of all the Fe atoms in the Fe(110), Fe(110)-K2O, Fe(211) and Fe(211)-K2O covered with surface species of C2H4, C2H2, CO and H2, while the qsurf is the total Bader charge of all the Fe atoms in the corresponding clean surface.

Models
The lattice constant of cubic Fe cell (bcc) is calculated; Its value is well in agreement with that of the experiment (2.831 vs. 2.866 Å), and the Fe-Fe bond length is 2.452 Å. In Figure 5

Conclusions
In this work, in order to illuminate the essential effect of the potassium promoter on the generation of atomic carbon via carburization gases dissociation on the iron-based catalyst, the C2H4, C2H2 and CO/H2 adsorptions and decompositions, as well as the rate constants of the corresponding elementary steps, are investigated by Density Function Theory on the Fe(110), Fe(110)-K2O, Fe(211) and Fe(211)-K2O surfaces. The calculation results suggest that the K2O promoter can modify the capabilities of surface C formation under different carburization gases via the thermodynamic method as well as the kinetical method, which also can explain the experiment results well [36].
Thermodynamically, the K2O promoter can increase the CO adsorption energy while decreasing the adsorption energy of the C2H4 molecule on both the Fe(110) and Fe(211) surfaces, which can explain the experiment results that the K2O promoter can enhance and inhibit the carburization capabilities of CO and C2H4 on α-Fe catalysts. Nevertheless, the adsorption energies of C2H2 and H2 were decreased on the Fe(110), while their adsorption energies were increased on Fe(211) by the K2O promoter. Therefore, it is inferred that the thermodynamic and kinetic effects of K2O promoter can jointly controlled the carburization behavior of α-Fe catalysts.
Kinetically, comparing with Xu's et al. experimental results, although the calculations originally obtain a contradictory conclusion that the K2O promoter can slightly improve the ability of forming atomic C via C2H4/C2H2 dissociation on Fe(110) and Fe(211), while suppressing the atomic C formation via CO/H2 decomposition on Fe(110). However, via the detailed analysis of the literature [32] and calculation results, it is finally inferred that the tuning effect of the K2O promoter on the catalyst surfaces increases the exposed proportion of Fe(211), which exactly inhibits the C2H4/C2H2 dissociation, while enhancing the CO/H2 decomposition, and the conclusion could well explain the experimental results of Xu et al. [36].
It is believed that different surfaces of iron carbides have different reactivity in the FTS process, i.e., high-performance catalysts could be designed via catalyst-preparing technology which could control exposing facets of the iron-based catalyst. Hence, there are some potential routes which could be suggested based on our calculations and the literature for designing high-performance catalysts in the FTS process: a) controlling the proportion of exposed surfaces of iron-based catalysts by the surface science and technology; b) changing the composition and proportion of carburization gases; c) modulating the order of carburization and K2O promoter addition during the catalysts' preparation process; d) adding some other metal oxide replacing the K2O promoter, such as the reported Na2O [24].
Supplementary Materials: The following are available online at www.mdpi.com/2073-4344/10/5/527/s1, Figure  S1. The energy profiles of C2H4 dissociation on Fe(110), as well as the top and side view of the configurations for the corresponding intermediates. Figure S2. The energy profiles of C2H4 dissociation on Fe(110)-K2O, as well as the top and side view of the configurations for the corresponding intermediates. Figure S3. The energy profiles of C2H4 dissociation on Fe(211), as well as the top and side view of the configurations for the corresponding intermediates. Figure S4. The energy profiles of C2H4 dissociation on Fe(211)-K2O, as well as the top and side view of the configurations for the corresponding intermediates. Figure S5. The energy profiles of CO/H2 dissociation on Fe(110), as well as the top and side view of the configurations for the corresponding intermediates. Figure S6. The energy profiles of CO/H2 dissociation on Fe(110)-K2O, as well as the top and side view of the configurations for the corresponding intermediates. Figure S7. The energy profiles of CO/H2 dissociation on Fe(211), as well as the top and side view of the configurations for the corresponding intermediates. Figure S8. The energy profiles of CO/H2 dissociation on Fe(211)-K2O, as well as the top and side view of the configurations for the corresponding intermediates. Figure S9. The top and side view structures of 2CH+H, C+CH+3H and 2C+4H on Fe(110). Table S1. The distances between the two atoms (d, Å) be dissociated in the transition states of the element steps for C2H4 and CO/H2 dissociation on Fe (110)