用于Suzuki-Miyaura反应的阴离子交换树脂负载钯催化剂(英文)

以碱性阴离子交换树脂Amberlite IRA-900为载体,Pd(C3H5)(C5H5)为金属有机前体,采用金属有机气相沉积法在室温下制备了Pd@IRA-900多相催化材料.紫外-可见光谱分析证明前体和树脂骨架之间的化学作用以及树脂本身的孔道结构使得Pd纳米粒子均匀分散在载体上.透射电镜结果显示钯纳米粒子的平均尺寸为2.6 nm.在较温和的条件下Pd@IRA-900对多种卤代芳烃和苯硼酸的Suzuki偶联都具有良好的催化活性,并且催化剂重复使用5次之后依然具有很好的活性.此外,对树脂载体进行碱性交换处理后可得到一种双功能催化材料Pd@IRA-900(OH),该催化剂在不加入碱的条件下也可以催化碘苯和苯硼酸的Suzuki偶联反应.     

一步法合成Pt@ZIF-8及其在1,4-丁炔二醇选择加氢中的应用

1,4-丁炔二醇(BYD)部分加氢生成1,4-丁烯二醇(BED),BED进一步加氢生成1,4-丁二醇(BDO).此外,BYD,BED和BDO还会发生脱水反应生成单醇类产物.工业上BYD加氢反应主要用于生产BDO.由于传统的单金属加氢催化剂很难控制反应的加氢程度,因此一般通过提高反应温度和压力使BYD尽量转化为完全加氢产物BDO,以减少部分加氢产物BED对最终产品收率的影响.部分加氢产物BED在精细化工领域也具有重要的应用,所以选择合适的催化剂和反应条件来提高部分加氢产物BED的选择性具有重要的理论意义和潜在应用价值.文献中常采用Zn、微生物等活性抑制剂来降低贵金属催化剂的加氢活性.这些方法往往比较复杂,所使用的添加剂不仅存在毒性和污染产物,还会增加成本.这些方法得到的催化材料虽然可以提高烯醇的选择性,但是仍需要严格控制反应条件才能得到较高收率的部分加氢产物.本文基于MOFs材料独特的结构和性质,探索了MOFs负载型贵金属催化剂在选择加氢反应中的催化性能.首先制备了一种羧酸根保护的Pt纳米溶胶,并以水为溶剂,增加2-甲基咪唑的加入量,实现了室温下ZIF-8晶体的快速生成.在室温合成ZIF-8的过程中加入羧酸根保护的Pt纳米溶胶,通过羧酸根与ZIF-8之间存在的化学吸附力,实现ZIF-8对Pt纳米粒子的包覆.羧酸根不仅可以稳定溶液中的纳米粒子,同时还起着“桥梁”的作用.羧酸根中的C=O基团与ZIF-8中的Zn原子或有机骨架之间弱的配位作用,增加了纳米粒子和ZIF-8之间的亲和力,实现了金属纳米粒子被ZIF-8包围.Pt纳米粒子的引入对ZIF-8的形成也没有影响,得到的Pt@ZIF-8材料拥有良好的晶体结构和高的比表面积.采用XRD、N2吸附和TEM等表征揭示了Pt@ZIF-8的结构特点,并研究了其在水相1,4-丁炔二醇加氢反应中的催化性能.结果显示,该材料不仅具有很高的活性,还具有突出的部分加氢选择性.在5次循环反应中,BYD转化率没有明显变化,说明催化剂在反应过程中活性没有降低.在多次反应之后,反应产物的分布也没有发生明显变化,1,4-丁烯二醇选择性在5次反应中都保持在94％以上.结构表征结果则显示,在4次循环使用之后,催化剂的结构已经遭到破坏;5次循环使用之后,催化剂的XRD谱图中ZIF-8的特征衍射峰完全消失.其余谱峰为ZnO特征衍射峰,说明由于反应温度较高,催化剂在多次反应之后其载体ZIF-8发生了分解.循环寿命实验说明,ZIF-8中Zn离子和含氮有机骨架的抑制作用是导致1,4-丁烯二醇高选择性的重要原因.ZIF-8的分解虽然会使孔道塌陷,但是结构中的Zn和含氮的有机骨架组成依然存在,仍然可以达到抑制烯醇进一步加氢的效果,并且Pt纳米溶胶主要存在于外表面,所以催化剂的活性和选择性没有发生明显变化.     

一步法合成Pt@ZIF-8及其在1,4-丁炔二醇选择加氢中的应用（英文）

1,4-丁炔二醇(BYD)部分加氢生成1,4-丁烯二醇(BED),BED进一步加氢生成1,4-丁二醇(BDO).此外,BYD,BED和BDO还会发生脱水反应生成单醇类产物.工业上BYD加氢反应主要用于生产BDO.由于传统的单金属加氢催化剂很难控制反应的加氢程度,因此一般通过提高反应温度和压力使BYD尽量转化为完全加氢产物BDO,以减少部分加氢产物BED对最终产品收率的影响.部分加氢产物BED在精细化工领域也具有重要的应用,所以选择合适的催化剂和反应条件来提高部分加氢产物BED的选择性具有重要的理论意义和潜在应用价值.文献中常采用Zn、微生物等活性抑制剂来降低贵金属催化剂的加氢活性.这些方法往往比较复杂,所使用的添加剂不仅存在毒性和污染产物,还会增加成本.这些方法得到的催化材料虽然可以提高烯醇的选择性,但是仍需要严格控制反应条件才能得到较高收率的部分加氢产物.本文基于MOFs材料独特的结构和性质,探索了MOFs负载型贵金属催化剂在选择加氢反应中的催化性能.首先制备了一种羧酸根保护的Pt纳米溶胶,并以水为溶剂,增加2-甲基咪唑的加入量,实现了室温下ZIF-8晶体的快速生成.在室温合成ZIF-8的过程中加入羧酸根保护的Pt纳米溶胶,通过羧酸根与ZIF-8之间存在的化学吸附力,实现ZIF-8对Pt纳米粒子的包覆.羧酸根不仅可以稳定溶液中的纳米粒子,同时还起着"桥梁"的作用.羧酸根中的C=O基团与ZIF-8中的Zn原子或有机骨架之间弱的配位作用,增加了纳米粒子和ZIF-8之间的亲和力,实现了金属纳米粒子被ZIF-8包围.Pt纳米粒子的引入对ZIF-8的形成也没有影响,得到的Pt@ZIF-8材料拥有良好的晶体结构和高的比表面积.采用XRD、N2吸附和TEM等表征揭示了Pt@ZIF-8的结构特点,并研究了其在水相1,4-丁炔二醇加氢反应中的催化性能.结果显示,该材料不仅具有很高的活性,还具有突出的部分加氢选择性.在5次循环反应中,BYD转化率没有明显变化,说明催化剂在反应过程中活性没有降低.在多次反应之后,反应产物的分布也没有发生明显变化,1,4-丁烯二醇选择性在5次反应中都保持在94%以上.结构表征结果则显示,在4次循环使用之后,催化剂的结构已经遭到破坏;5次循环使用之后,催化剂的XRD谱图中ZIF-8的特征衍射峰完全消失.其余谱峰为Zn O特征衍射峰,说明由于反应温度较高,催化剂在多次反应之后其载体ZIF-8发生了分解.循环寿命实验说明,ZIF-8中Zn离子和含氮有机骨架的抑制作用是导致1,4-丁烯二醇高选择性的重要原因.ZIF-8的分解虽然会使孔道塌陷,但是结构中的Zn和含氮的有机骨架组成依然存在,仍然可以达到抑制烯醇进一步加氢的效果,并且Pt纳米溶胶主要存在于外表面,所以催化剂的活性和选择性没有发生明显变化.     

酰胺羰基化反应中可重复使用的Pd/HZSM-5催化剂

 合成了非均相Pd/HZSM-5催化剂并将其用于酰胺羰基化反应. 结果表明,文献报道的Pd/C催化剂重复使用时其活性降为原来的一半,而Pd/HZSM-5催化剂重复使用4次后活性基本不变. 反应前后两种催化剂的TEM电镜照片表明, Pd/C上的金属钯粒子在反应后团聚并形成网络状结构,而Pd/HZSM-5上钯粒子在反应后仍保持与反应前相同的均匀分布状态.     

ZIF-8原位负载Pd纳米粒子及其在Suzuki-Miyaura反应中的应用(英文)

将PdCl2与ZIF-8的反应原料ZnO和2-甲基咪唑按照一定的比例,采用机械化学法原位将Pd2+负载在ZIF-8上(Pd2+/ZIF-8)。然后用NaBH4将Pd2+/ZIF-8进行还原,得到均匀分散的Pd纳米颗粒(Pd/ZIF-8)。通过XRD、N2吸附、透射电镜、ICP-AES、XPS等对Pd/ZIF-8的结构、形貌、价态等进行了表征。结果表明用机械化学法原位制备的Pd/ZIF-8具有分散均匀、容易大量制备的优点。该催化剂不仅能高效催化Suzuki-Miyaura交叉偶联反应,并且能够多次循环利用。     

氧化锌纳米线外延生长PdZn纳米粒子的制备及在甲醇水蒸气重整反应中的催化性能

以采用改进的气相沉积法制备的具有规整{1010}晶面的氧化锌纳米线为载体,合成了氧化锌纳米线负载钯催化剂,考察了还原温度和负载量对催化剂表面形成Pd Zn合金过程的影响,并通过适当的后处理过程制备了氧化锌纳米线外延生长Pd Zn纳米粒子催化体系.结果表明,当金属钯负载量较低(质量分数约为2%)时,经400℃还原后的催化剂表面会形成PdxZny(xy)合金,从而影响催化剂的CO选择性;提高钯负载量或还原温度有利于将PdxZny(xy)合金转化为Pd Zn合金,降低CO选择性.负载Pd Zn合金纳米粒子与氧化锌纳米线载体之间外延生长的界面关系使其在甲醇水蒸气重整反应中显示出优异的反应稳定性.     

具有分级结构的SiC纳米线负载的Pd纳米颗粒光催化芳基卤化物硼化反应（英文）

芳基硼酸酯作为一种重要的有机中间体,在C–C, C–N和C–O键的构筑以及C–X键的转换中有着广泛的应用,其传统合成方法主要是用格氏试剂或有机锂试剂,但该方法的官能团耐受性较差,且对反应环境敏感.在均相催化体系下,过渡金属催化芳烃的C–H和C–X键硼化反应成为合成芳基硼酸酯化合物的重要途径,虽然活性和选择性很高,但催化剂难于分离,且多数反应需要昂贵的配体,限制了其在工业上的大规模应用.多相催化剂体系虽然解决了分离回收的问题,但是催化效率大多较低.近年来,由于光催化能够有效利用太阳能,在温和条件下促使反应进行,并且能够定向的选择性合成目标产物,提高目标产物的产率,因此其在有机合成中的应用引起了广泛的关注.本文以具有分级结构且能够响应可见光的Si C纳米线为载体,并通过液相还原法制备负载量为3wt%的Pd/Si C催化剂.TEM照片可以看出, Pd纳米颗粒均地分散在Si C表面,平均粒径为3.7 nm.UV-Vis图谱表明, Si C负载Pd以后可明显提高其对可见光的吸收.Pd/Si C在可见光(400–800 nm)照射下,在30 oC和常压Ar氛围下即可实现碘苯脱碘硼化,苯硼酸频哪醇酯...     

复合碳载体负载Pd催化剂的乙醇电氧化性能

以石墨烯纳米片(GNP)和XC-72炭黑组成复合碳载体,制备了Pd/C-GNP催化剂,并考察了其乙醇电氧化性能.透射电子显微镜和X射线衍射分析结果表明,复合载体的采用改善了催化剂的结构,促进了Pd纳米粒子的分散.电化学测试结果表明,Pd/C-GNP催化剂具有较大的电化学活性表面积;在碱性介质中,Pd/C-GNP催化剂的乙醇氧化活性显著高于Pd/GNP和Pd/C催化剂;Pd/C-GNP催化剂还表现出优良的抗中毒能力,这可能得益于Pd/C-GNP催化剂中金属-载体的相互作用.     

Pd/SAPO-34催化剂上CO低温氧化反应

 采用水热法合成了小晶粒的 SAPO-34, MnSAPO-34 和 CuSAPO-34 分子筛, 并以它们为载体采用浸渍法制备了一系列不同 Pd 含量的催化剂用于催化 CO 氧化反应. 结果表明: 分子筛载体、催化剂制备条件、反应条件、Pd 含量及预还原等对催化剂的活性影响较大. 催化剂活性随焙烧温度的增加而降低, 而随着反应温度的升高而提高, 担载在 SAPO-34 上 Pd 含量为 1.35% 时性能最佳. X射线衍射和透射电镜结果表明 Pd 物种高度分散于催化剂上, 粒子粒径在 2~8 nm; X射线光电子能谱及氢气程序升温还原结果表明, 高度分散的 Pd2+ 物种是 CO 氧化反应活性位. 随着反应进行被还原为 Pd0 物种, 因而导致催化剂活性下降. H2 预还原处理催化剂致使活性下降的实验结果也支持了这一结论.     

电纺Pd纳米粒子/碳纳米纤维复合材料对甲醇的电催化氧化研究

利用静电纺丝技术制备了含有乙酰丙酮钯(Pd(Ac)2)前体的聚丙烯腈(PAN)纳米纤维,经H2还原和900℃碳化处理得到了Pd纳米粒子负载的碳纳米纤维复合材料(Pd/CNF).此方法中,CNF的制备和Pd纳米粒子的形成是同步进行的,无需对碳载体进行任何预处理,实现了纳米粒子负载CNF的一步制备,简化了实验步骤的同时确保CNF载体骨架的完整性.扫描电镜(SEM)和透射电镜(TEM)分析表明,大小均一的Pd纳米粒子牢固地分散在CNF表面,其粒径约为60 nm.X-射线衍射(XRD)和X-射线光电子能谱(XPS)表征了Pd/CNF的晶体结构.Pd纳米粒子以单质态形式存在,具有面心立方体结构.通过循环伏安法(CV)和计时电流法等电化学方法研究了Pd/CNF复合材料对甲醇的电催化氧化情况,Pd/CNF对甲醇氧化显示出优异的催化活性和稳定性,优于商业化Pd/C催化剂.     

Ultra‐small and highly dispersed Pd nanoparticles inside the pores of ZIF‐8: Sustainable approach to waste‐minimized Mizoroki–Heck cross‐coupling reaction based on reusable heterogeneous catalyst

The rapid development of nanomaterials, particularly advanced hybrid nanoparticles, has made new opportunities for the design and fabrication of high‐performance metal‐based catalysts. However, generating metal nanoparticles of desired size without aggregation is an important challenge for enhancing the catalytic activity of metal nanoparticles supported in the host matrix. In this work, a hybrid nanoporous material, namely Pd nanoparticles@N‐heterocyclic carbene@ZIF‐8, with a high internal surface area was successfully prepared using a dispersed anionic sulfonated N‐heterocyclic carbene–Pd(II) precursor inside the cavities of zeolitic imidazolate framework (ZIF‐8) using an impregnation approach followed by reduction with NaBH₄. The anionic sulfonated N‐heterocyclic carbene was found to be a superb ligand for the stabilization of Pd nanoparticles in the pores of ZIF‐8. The resulting system was applied to the Mizoroki–Heck cross‐coupling reaction, in which the catalyst showed high catalytic activity under mild reaction conditions.     

Mechanically fabricated Metal–organic framework/resin composite nanoparticles for efficient basic catalysis

Zeolitic imidazolate framework‐8 (ZIF‐8) was successfully composited with an anionic basic resin 201 × 7 (717‐resin) to provide a novel ZIF‐8/717‐resin composite. Its catalytic activity toward the Knoevenagel condensation reaction was evaluated. Results showed that ZIF‐8/717‐resin composite could efficiently catalyze this reaction, affording the corresponding products in good to excellent yields. Good functional group tolerance, mild reaction conditions, good stability and reusability of the catalyst are the major features of present protocol.     

Effect of Hydrohalogenation of Metal/Zeolite Catalysts for Cyclohexene Hydroconversion ‐Part 3‐ Pd/H‐ZSM‐5 Catalysts

Cyclohexene (CHE) hydroconversion was performed in a flow reactor at atmospheric pressure and temperatures of 50–400 °C using: Pd/H‐ZSM‐5, Pd/H‐ZSM‐5(HCl), and Pd/H‐ZSM‐5(HF) catalysts. These catalysts were characterized for acid site strength distribution via NH₃ TPD, Pd dispersion via H₂ chemisorption, TPR via reduction of the metal oxide in the catalysts and XRD for tracing crystallinity The hydroconversion steps proceeded as follows: CHE → Cyclohexane (CHA); CHE → Methylcyclopentenes (MCPEs) → Methylcyclopentane (MCPA); CHE → Cyclohexadienes (CHDEs) → Benzene → Alkylbenzenes; CHE and others → Hydrocrackedproducts. The overall hydroconversion of CHE was achieved in the catalyst order: Pd/H‐ZSM‐5 > Pd/H‐ZSM‐5(HF) > Pd/H‐ZSM‐5(HCl). CHE hydrogenation step was the major reaction at low temperatures which significantly inhibited via HCl treatment, but slightly enhanced via HF treatment. At medium temperatures, on all catalysts, isomerisation to MCPEs and MCPA increase to a maximum then a decline with a further increase of temperature. The overall isomerisation of CHE was highest on the untreated catalyst. During the higher temperature range, dehydrogenation, alkylation and hydrocracking were increased with temperature. Dehydrogenation of CHE always yielded larger amounts of 1,3‐CHDE than 1,4‐CHDE. These cyclohexadienes were produced in the catalyst order: Pd/H‐ZSM‐5(HF) > Pd/H‐ZSM‐5(HCl) > Pd/H‐ZSM‐5. In general, benzene alkylation to toluene exceeded that of xylenes, indicating that the second methylation is more difficult than the first. However, the catalytic activities for benzene and toluene production were in the order: Pd/H‐ZSM‐5 » Pd/H‐ZSM‐5(HCl) > Pd/H‐ZSM‐5(HF), whereas for xylenes production, Pd/H‐ZSM‐5 » Pd/H‐ZSM‐5(HF) > Pd/H‐ZSM‐5(HCl). Intrapore diffusion plays an important role during the dehydrogenation reactions as well as during the interconversion of individual aromatic hydrocarbons.     

Switching from linear to cyclic δ‐Polyvalerolactone synthesized via zeolitic imidazolate framework as a catalyst: A promising approach

A series of spray dried zeolitic imidazolate frameworks (ZIFs = ZIF‐8, ZIF‐67, and Zn/Co‐ZIF) are used as a catalyst for the bulk ring‐opening polymerization of δ‐valerolactone without any co‐catalyst to generate polyvalerolactone. Interestingly, using the same catalyst under the same reaction conditions could manipulate the structure of the product polymer, and thus its physical properties. Thus, using a dried substrate leads to the formation of the cyclic polymer while a linear polymer was formed on using the commercially available substrate. An activated monomer mechanism has been suggested where the propagating zinc alkoxide undergoes an intramolecular transesterification to release cyclic or linear polyvalerolactone. The ROP of δ‐VL without drying shows that the polymeric zwitterions have little tendency to cyclize in the presence of moisture. At 140 °C, ZIF‐8 shows a superior catalytic activity resulting in the production of cyclic polyvalerolactone having a high molecular weight as compared to ZIF‐67 or Zn/Co‐ZIF due to the presence of highly active sites. The catalyst could be recycled and reused without any significant loss of catalytic activity.     

Influence of Metallic Modification on Ethylbenzene Dealkylation over ZSM‐5 Zeolites

A series of metal‐modified HZSM‐5 catalysts were prepared by impregnation and were used for ethylbenzene dealkylation of the mixed C8 aromatics (ethylbenzene, m‐xylene and o‐xylene). The effects of different supported metals (Pt, Pd, Ni, Mo) on catalytic performance, including reaction conditions, were investigated. The physicochemical properties of catalysts were characterized by means of XRD, BET, TEM and NH₃‐TPD. Experimental results showed that metallic modification obviously increased the ethylbenzene conversion and reduced the coke deposition, greatly improving the catalyst stability. The distinction of ethylbenzene conversion depended on the interaction between hydrogenation reactivity and acidic cracking of bifunctional metal‐modified zeolites. Compared with Pt and Ni, Pd and Mo were easier to disperse into HZSM‐5 micropores during loading metals. The acidic density of different metal‐modified HZSM‐5 declined in the following order: HZSM‐5>Pt/HZSM‐5>Pd/HZSM‐5>Ni/HZSM‐5>Mo/HZSM‐5. The activity of ethylene hydrogenation decreased with Pt/HZSM‐5>Pd/HZSM‐5>Ni/HZSM‐5>Mo/HZSM‐5. In comparison, Pd/HZSM‐5 showed the best catalytic performance with both high activity and high selectivity, with less cracking loss of m‐xylene and o‐xylene. Moreover, the following reaction conditions were found to be preferable for ethylbenzene dealkylation over Pd/HZSM‐5: 340°C, 1.5 MPa H₂, WHSV 4 h^?1, H₂/C8 4 mol/mol.     

Electrochemical Synthesis and Catalytic Properties of Encapsulated Metal Clusters within Zeolitic Imidazolate Frameworks

It is very interesting and also a big challenge to encapsulate metal clusters within microporous solids to expand their application diversity. For this target, herein, we present an electrochemical synthesis strategy for the encapsulation of noble metals (Au, Pd, Pt) within ZIF‐8 cavities. In this method, metal precursors of AuCl₄^2?, PtCl₆^2?, and PdCl₄^2? are introduced into ZIF‐8 crystals during the concurrent crystallization of ZIF‐8 at the anode. As a consequence, very small metal clusters with sizes around 1.2 nm are obtained within ZIF‐8 crystals after hydrogen reduction; these clusters exhibit high thermal stability, as evident from the good maintenance of their original sizes after a high‐temperature test. The catalytic properties of the encapsulated metal clusters within ZIF‐8 are evaluated for CO oxidations. Because of the small pore window of ZIF‐8 (0.34 nm) and the confinement effect of small pores, about 80 % of the metal clusters (fractions of 0.74, 0.77, and 0.75 for Au, Pt, and Pd in ZIF‐8, respectively) retain their catalytic activity after exposure to the organosulfur poison thiophene (0.46 nm), which is in contrast to their counterparts (fractions of 0.22, 0.25, and 0.20 for Au, Pt, and Pd on the SiO₂ support). The excellent performances of metal clusters encapsulated within ZIF‐8 crystals give new opportunities for catalytic reactions.     

Pd Nanocubes@ZIF‐8: Integration of Plasmon‐Driven Photothermal Conversion with a Metal–Organic Framework for Efficient and Selective Catalysis

Composite nanomaterials usually possess synergetic properties resulting from the respective components and can be used for a wide range of applications. In this work, a Pd nanocubes@ZIF‐8 composite material has been rationally fabricated by encapsulation of the Pd nanocubes in ZIF‐8, a common metal–organic framework (MOF). This composite was used for the efficient and selective catalytic hydrogenation of olefins at room temperature under 1 atm H₂ and light irradiation, and benefits from plasmonic photothermal effects of the Pd nanocube cores while the ZIF‐8 shell plays multiple roles; it accelerates the reaction by H₂ enrichment, acts as a “molecular sieve” for olefins with specific sizes, and stabilizes the Pd cores. Remarkably, the catalytic efficiency of a reaction under 60 mW cm^?2 full‐spectrum or 100 mW cm^?2 visible‐light irradiation at room temperature turned out to be comparable to that of a process driven by heating at 50 °C. Furthermore, the catalyst remained stable and could be easily recycled. To the best of our knowledge, this work represents the first combination of the photothermal effects of metal nanocrystals with the favorable properties of MOFs for efficient and selective catalysis.     

Preparation and decomposition of C60H36

C(60)H(36) was prepared by the Benkeser reaction with a much milder procedure. Thermal dehydrogenation of C(60)H(36) with IrCl(CO)(PPh(3))(2), Pd/C, and Ni-Al alloy and photochemical catalytic dehydrogenation with RhCl(CO)(PPh(3))(2) were studied. Pd/C catalyst was more effective for the thermal decomposition of C(60)H(36) till now.     

Chiral Metal–Organic Framework Hollow Nanospheres for High‐Efficiency Enantiomer Separation

Chiral ZIF‐8 hollow nanospheres with d ‐histidine as part of chiral ligands (denoted as H‐d ‐his‐ZIF‐8) were prepared for separation of (±)‐amine acids. Compared to bulk d ‐his‐ZIF‐8 without a hollow cavity, the prepared H‐d ‐his‐ZIF‐8 showed 15 times higher separation capacity and higher ee values of 90.5 % for alanine, 95.2 % for glutamic acid and 92.6 % for lysine, respectively.     

Tuning the Surface Chemistry of Pd by Atomic C and H: A Microscopic Picture

Palladium is crucial for industry‐related applications such as heterogeneous catalysis, energy production, and hydrogen technologies. In many processes, atomic H and C species are proposed to be present in the surface/near‐surface area of Pd, thus noticeably affecting its chemical activity. This study provides a detail and unified view on the interactions of the H and C species with Pd nanoparticles (NPs), which is indispensable for insight into their catalytic properties. Density functional calculations of the interplay of C and H atoms at various concentrations and sites on suitable Pd NPs have been performed, accompanied by catalysis‐relevant experiments on oxide‐supported bare and C‐modified Pd NPs. It is shown that on a Pd₇₉ NP a subsurface C atom destabilizes nearby atoms H at low coverage. Our experiments confirm that H atoms bind more weakly on C‐containing Pd NPs than on C‐free NPs. Various factors related to the presence of both H and C atoms on a Pd₇₉ surface, which may influence the penetration of H atoms from the surface into the subsurface area, have been investigated. Carbon atoms facilitate the subsurface penetration of atomic H both thermodynamically and kinetically when the surface is densely covered by H atoms. Moreover, subsurface H atoms are also energetically favored, even in the absence of C atoms, when several facets of the NP are covered by H atoms.