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从高通量分级催化剂设计看氨合成的反应机理、动力学和改进型催化剂

Reaction Mechanisms, Kinetics, and Improved Catalysts for Ammonia Synthesis from Hierarchical High Throughput Catalyst Design.

机构信息

Department of Chemical and Materials Engineering, University of Nevada, Reno, Nevada 89577, United States.

Materials and Process Simulation Center (MSC), California Institute of Technology, Pasadena, California 91125, United States.

出版信息

Acc Chem Res. 2022 Apr 19;55(8):1124-1134. doi: 10.1021/acs.accounts.1c00789. Epub 2022 Apr 6.

DOI:10.1021/acs.accounts.1c00789
PMID:35387450
Abstract

The Haber-Bosch (HB) process is the primary chemical synthesis technique for industrial production of ammonia (NH) for manufacturing nitrate-based fertilizer and as a potential hydrogen carrier. The HB process alone is responsible for over 2% of all global energy usage to produce more than 160 million tons of NH annually. Iron catalysts are utilized to accelerate the reaction, but high temperatures and pressures of atmospheric nitrogen gas (N) and hydrogen gas (H) are required. A great deal of research has aimed at increased performance over the last century, but the rate of progress has been slow. This Account focuses on determining the atomic-level reaction mechanism for HB synthesis of NH on the Fe catalysts used in industry and how to use this knowledge to suggest greatly improved catalysts via a novel paradigm of catalyst rational design.We determined the full reaction mechanism on the two most active surfaces for the HB process, Fe(111) and Fe(211)R. We used density functional theory (DFT) to predict the free-energy barriers for all 12 important reactions and the 34 most important 2 × 2 surface configurations. Then we incorporated the mechanism into kinetic Monte Carlo (kMC) simulations run for several hours of real time to predict turnover frequencies (TOFs). The predicted TOFs are within experimental error, indicating that the predicted barriers are within 0.04 eV of experiment.With this level of accuracy, we are poised to use DFT to improve the catalyst. Rather than forming bulk alloys with uniform concentration, we aimed at finding additives that strongly prefer near-surface sites so that minor amounts of the additive might lead to dramatic improvements. However, even for a single additive, the combinations of surface species and reactions multiplies significantly, with ∼48 reaction steps to examine and nearly 100 surface configurations per 2 × 2 site. To make it practical to examine tens of dopant candidates, we developed the (HHTCS) approach, which we applied to both the Fe(111) and Fe(211) surfaces. For HHTCS, we identified the most important 4 reaction steps out of 12 for the two surfaces to examine >50 dopant cases, where we required performance at each step no worse than for pure Fe. With HHTCS, the computational cost is about 1% of that for doing the full reaction mechanism, allowing us to do ≈50 cases in about 1/2 the time it took to do pure Fe(111). The new leads identified with HHTCS are then validated with full mechanistic studies.For Fe(111), we predict three high-performance dopants that strongly prefer the second layer: Co with a rate 8 times higher, Ni with a rate 16 times higher, and Si with a rate 43 times higher, at 400 °C and 20 atm. We also found four dopants that strongly prefer the top layer and improve performance: Pt or Rh 3 times faster and Pd or Cu 2 times faster. For Fe(211), the best dopant was found to be second-layer Co with a rate 3 times faster than that for the undoped surface.The DFT/kMC data were used to predict reshaping of the catalyst particles under reaction conditions and how to tune dopant content so as to maximize catalytic area and thus activity. Finally, we show how to validate our mechanistic modeling via a comparison between theoretical and experimental operando spectroscopic signatures.

摘要

Haber-Bosch (HB) 工艺是工业生产氨 (NH) 的主要化学合成技术,用于制造硝酸盐基肥料和作为潜在的氢载体。仅 HB 工艺就负责全球超过 2%的能源消耗,每年生产超过 1.6 亿吨 NH。铁催化剂用于加速反应,但需要大气氮气 (N) 和氢气 (H) 的高温和高压。在过去的一个世纪里,人们进行了大量的研究以提高性能,但进展速度缓慢。本账户重点介绍确定 HB 合成 NH 在工业中使用的 Fe 催化剂上的原子级反应机制,以及如何利用这一知识通过催化剂合理设计的新范例来建议大大改进的催化剂。

我们确定了 HB 过程中在最活跃的两个表面(Fe(111)和 Fe(211)R)上的完整反应机制。我们使用密度泛函理论 (DFT) 预测了所有 12 个重要反应和 34 个最重要的 2×2 表面构型的自由能垒。然后,我们将机制纳入动力学蒙特卡罗 (kMC) 模拟中,运行几个小时的实时模拟以预测周转率 (TOF)。预测的 TOF 在实验误差范围内,表明预测的势垒与实验相差 0.04 eV 以内。

有了这种准确性,我们就可以使用 DFT 来改进催化剂。我们的目标不是形成具有均匀浓度的块状合金,而是寻找强烈优先于近表面位置的添加剂,以便少量添加剂可能会导致显著改善。然而,即使对于单一添加剂,表面物种和反应的组合也会显著增加,需要检查的反应步骤约为 48 个,每个 2×2 位有近 100 个表面构型。为了使检查数十种掺杂剂候选物变得切实可行,我们开发了 (HHTCS) 方法,我们将其应用于 Fe(111)和 Fe(211)表面。对于 HHTCS,我们确定了两个表面上最重要的 4 个反应步骤,以检查超过 50 个掺杂情况,其中我们要求每个步骤的性能不低于纯 Fe。使用 HHTCS,计算成本约为全反应机制的 1%,使我们能够在大约一半的时间内完成大约 50 个案例,而完成纯 Fe(111)则需要这么长时间。然后使用全机制研究验证 HHTCS 中识别的新线索。

对于 Fe(111),我们预测了三种强烈优先于第二层的高性能掺杂剂:钴的速率提高 8 倍,镍的速率提高 16 倍,硅的速率提高 43 倍,在 400°C 和 20 大气压下。我们还发现了四种强烈优先于顶层并提高性能的掺杂剂:铂或铑快 3 倍,钯或铜快 2 倍。对于 Fe(211),发现最好的掺杂剂是第二层的钴,其速率比未掺杂表面快 3 倍。

DFT/kMC 数据用于预测催化剂颗粒在反应条件下的重塑以及如何调整掺杂剂含量以最大限度地提高催化面积和活性。最后,我们展示了如何通过理论和实验原位光谱特征之间的比较来验证我们的机制建模。

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