Tetracopper(II) Cores Driven by an Unexplored Trifunctional Aminoalcohol Sulfonic Acid for Mild Catalytic C–H Functionalization of Alkanes

Three new tetracopper(II) coordination compounds were easily generated from Cu(NO3)2, a trifunctional aminoalcohol sulfonic acid (H3bes, N,N-bis(2-hydroxyethyl)-2-aminoethanesulfonic acid) as a principal building block, and a benzene carboxylic acid as a supporting ligand (i.e., benzoic (Hba), 4-hydroxybenzoic (Hfba), or 3-hydroxybenzoic (Hthba) acid). The obtained microcrystalline products, [Cu4(µ-Hbes)3(µ-H2bes)(µ-L)]·2H2O (L = ba− (1), fhba− (2), and thba− (3)), were fully characterized by FTIR (Fourier-transform infrared spectroscopy), elemental analysis, ESI-MS (Electrospray Ionisation Mass Spectrometry), and single-crystal X-ray diffraction methods. Compounds 1–3 were applied as effective homogeneous catalysts in the oxidative C−H functionalization of alkanes (cycloalkanes and propane). Two different model reactions were explored: (1) mild oxidation of alkanes with hydrogen peroxide to give alcohols and ketones, and (2) mild carboxylation of alkanes with carbon monoxide, water, and potassium peroxodisulfate to give carboxylic acids. For these reactions, effects of different parameters, as well as mechanistic and selectivity characteristics, were studied.

The oxidation of C 6 H 12 was studied as a model reaction due to the relevance of cyclohexanol and cyclohexanone to nylon production [38][39][40][41]. Typical reactions were performed in acetonitrile/water medium at 50 • C and under atmospheric pressure, using hydrogen peroxide (50% in water) as a green oxidant and a small quantity of trifluoroacetic acid (TFA) as a promoter [13][14][15]. Compounds 1-3 catalyze the cyclohexane oxidation with hydrogen peroxide, resulting in the 12-16% total yields of cyclohexanol and cyclohexanone as final products ( Figure 2). Hereinafter, the product yields are relative to substrate ((moles of alcohol and ketone per mol of substrate) × 100%), and were obtained after the treatment of the reaction mixtures with triphenylphosphine for reduction of peroxides (cyclohexyl hydroperoxide to cyclohexanol and H 2 O 2 to water). The formation of cyclohexyl hydroperoxide as a primary (intermediate) product was confirmed following a method developed by Shul'pin [5,15], which is based on the GC (gas chromatography) analysis of the reaction mixtures before and after the treatment with solid PPh 3 . The maximum yield is attained after 90-120 min of the reaction. In some cases, a slight yield drop was observed due to an overoxidation that might occur at a prolonged reaction time. Influence of different reaction parameters was studied and is described below. The oxidation of C6H12 was studied as a model reaction due to the relevance of cyclohexanol and cyclohexanone to nylon production [38][39][40][41]. Typical reactions were performed in acetonitrile/water medium at 50 °C and under atmospheric pressure, using hydrogen peroxide (50% in water) as a green oxidant and a small quantity of trifluoroacetic acid (TFA) as a promoter [13][14][15]. Compounds 1-3 catalyze the cyclohexane oxidation with hydrogen peroxide, resulting in the 12-16% total yields of cyclohexanol and cyclohexanone as final products ( Figure 2). Hereinafter, the product yields are relative to substrate ((moles of alcohol and ketone per mol of substrate) × 100%), and were obtained after the treatment of the reaction mixtures with triphenylphosphine for reduction of peroxides (cyclohexyl hydroperoxide to cyclohexanol and H2O2 to water). The formation of cyclohexyl hydroperoxide as a primary (intermediate) product was confirmed following a method developed by Shul'pin [5,15], which is based on the GC (gas chromatography) analysis of the reaction mixtures before and after the treatment with solid PPh3. The maximum yield is attained after 90-120 min of the reaction. In some cases, a slight yield drop was observed due to an overoxidation that might occur at a prolonged reaction time. Influence of different reaction parameters was studied and is described below.  The oxidation of C6H12 was studied as a model reaction due to the relevance of cyclohexanol and cyclohexanone to nylon production [38][39][40][41]. Typical reactions were performed in acetonitrile/water medium at 50 °C and under atmospheric pressure, using hydrogen peroxide (50% in water) as a green oxidant and a small quantity of trifluoroacetic acid (TFA) as a promoter [13][14][15]. Compounds 1-3 catalyze the cyclohexane oxidation with hydrogen peroxide, resulting in the 12-16% total yields of cyclohexanol and cyclohexanone as final products ( Figure 2). Hereinafter, the product yields are relative to substrate ((moles of alcohol and ketone per mol of substrate) × 100%), and were obtained after the treatment of the reaction mixtures with triphenylphosphine for reduction of peroxides (cyclohexyl hydroperoxide to cyclohexanol and H2O2 to water). The formation of cyclohexyl hydroperoxide as a primary (intermediate) product was confirmed following a method developed by Shul'pin [5,15], which is based on the GC (gas chromatography) analysis of the reaction mixtures before and after the treatment with solid PPh3. The maximum yield is attained after 90-120 min of the reaction. In some cases, a slight yield drop was observed due to an overoxidation that might occur at a prolonged reaction time. Influence of different reaction parameters was studied and is described below.

Acid Promoter Effect
Since the Cu-catalyzed oxidation reactions require a minor quantity of an acid promoter, we tested the promoting effect of various acids, namely trifluoroacetic (TFA), nitric, sulfuric, or hydrochloric acids (Figures 3 and S8, Supplementary Materials). According to a literature background [15,40], the function of an acid promoter might consist of the following: (A) activation of catalyst via unsaturation of copper centers by protonation of ligands; (B) facilitation of proton transfer steps; (C) increase of the reaction rate of oxidation; (D) facilitation of the formation of peroxo Figure 2. Accumulation of products (cyclohexanol and cyclohexanone total yield) in Cu-catalyzed C 6 H 12 oxidation with H 2 O 2 . Conditions: catalyst 1-3 (2.5 µmol), C 6 H 12 (1 mmol), trifluoroacetic acid (TFA; 50 µmol), H 2 O 2 (5 mmol), CH 3 CN (up to 2.5 mL of total volume), 50 • C.

Acid Promoter Effect
Since the Cu-catalyzed oxidation reactions require a minor quantity of an acid promoter, we tested the promoting effect of various acids, namely trifluoroacetic (TFA), nitric, sulfuric, or hydrochloric acids ( Figure 3 and Figure S8, Supplementary Materials). According to a literature background [15,40] Kinetic curves of product accumulation in the cyclohexane oxidation catalyzed by 2 in the systems containing various acid promoters are shown in Figure 3. The oxidation is exceptionally fast when using HCl as a promoter, leading to a 16% yield of products already after 15 min of reaction (turnover frequency: TOF~250 h −1 ). Such a remarkable effect of hydrochloric acid on the reaction rate of cyclohexane oxidation was previously observed in other systems and can be associated with the participation of Cl − ions in the generation of catalytically active species bearing bridging or terminal chloride ligands [8]. TFA, HNO 3 , and H 2 SO 4 exhibit a slightly weaker promoting behavior with total yields of 14-11%, which are achieved at more prolonged reaction times relative to a system operating with HCl. We also studied the promoting effects of different acids for catalysts 1 and 3 which reveal a behavior similar to 2 ( Figure S8, Supplementary Materials).
complexes; (E) increase of hydrogen peroxide reactivity; (F) suppressing a decomposition of H2O2 to H2O and O2 (eventual catalase activity of catalyst can be suppressed in the presence of acid).
Kinetic curves of product accumulation in the cyclohexane oxidation catalyzed by 2 in the systems containing various acid promoters are shown in Figure 3. The oxidation is exceptionally fast when using HCl as a promoter, leading to a 16% yield of products already after 15 min of reaction (turnover frequency: TOF ~250 h −1 ). Such a remarkable effect of hydrochloric acid on the reaction rate of cyclohexane oxidation was previously observed in other systems and can be associated with the participation of Cl − ions in the generation of catalytically active species bearing bridging or terminal chloride ligands [8]. TFA, HNO3, and H2SO4 exhibit a slightly weaker promoting behavior with total yields of 14-11%, which are achieved at more prolonged reaction times relative to a system operating with HCl. We also studied the promoting effects of different acids for catalysts 1 and 3 which reveal a behavior similar to 2 ( Figure S8, Supplementary Materials). An influence of the TFA amount was also investigated for catalyst 2 ( Figure 4) that is barely active without an acid promoter. However, total yield of products gradually grew upon elevating the amount of acid promoter up to 20 equivalents relative to the catalyst.  An influence of the TFA amount was also investigated for catalyst 2 ( Figure 4) that is barely active without an acid promoter. However, total yield of products gradually grew upon elevating the amount of acid promoter up to 20 equivalents relative to the catalyst.
H2O and O2 (eventual catalase activity of catalyst can be suppressed in the presence of acid).
Kinetic curves of product accumulation in the cyclohexane oxidation catalyzed by 2 in the systems containing various acid promoters are shown in Figure 3. The oxidation is exceptionally fast when using HCl as a promoter, leading to a 16% yield of products already after 15 min of reaction (turnover frequency: TOF ~250 h −1 ). Such a remarkable effect of hydrochloric acid on the reaction rate of cyclohexane oxidation was previously observed in other systems and can be associated with the participation of Cl − ions in the generation of catalytically active species bearing bridging or terminal chloride ligands [8]. TFA, HNO3, and H2SO4 exhibit a slightly weaker promoting behavior with total yields of 14-11%, which are achieved at more prolonged reaction times relative to a system operating with HCl. We also studied the promoting effects of different acids for catalysts 1 and 3 which reveal a behavior similar to 2 ( Figure S8, Supplementary Materials). An influence of the TFA amount was also investigated for catalyst 2 ( Figure 4) that is barely active without an acid promoter. However, total yield of products gradually grew upon elevating the amount of acid promoter up to 20 equivalents relative to the catalyst.

Effect of Catalyst Amount
We also studied the influence of the amount of catalyst 2 on the yield and W 0 (maximum initial reaction rate) in the oxidation of cyclohexane ( Figure 5). Blank experiments revealed that the cyclohexane oxidation products are not formed unless copper catalyst is added. An increase of the catalyst amount from 1.25 to 5 µmol results in an increase of both W 0 and total yield of products ( Figure 5a). The highest yield of 17% was obtained when using 5 µmol of catalyst. A linear trend between W 0 and the amount of catalyst was observed (Figure 5b), suggesting kinetics of the first order We also studied the influence of the amount of catalyst 2 on the yield and W0 (maximum initial reaction rate) in the oxidation of cyclohexane ( Figure 5). Blank experiments revealed that the cyclohexane oxidation products are not formed unless copper catalyst is added. An increase of the catalyst amount from 1.25 to 5 µmol results in an increase of both W0 and total yield of products ( Figure 5a). The highest yield of 17% was obtained when using 5 µmol of catalyst. A linear trend between W0 and the amount of catalyst was observed (Figure 5b), suggesting kinetics of the first order and supporting an eventual participation of a single type of copper species in a rate-limiting step of the oxidation reaction.

Substrate Scope
Apart from cyclohexane, oxidation of other cycloalkane substrates was also explored (Table 1, Figures 6 and S9, Supplementary Materials). For catalyst 2, more reactive substrates are cycloheptane and cyclooctane, which lead to the maximum total yields of 26 and 20%, respectively. In comparison, the oxidation of cyclohexane and cyclopentane is less efficient (13-9% product yield). This might be influenced by the stability of formed radicals (cycloalkyl radicals) that increases with the ring size. Moreover, cyclopentane is rather volatile (boiling point (bp): 49 °C) and, at typical reaction conditions (50 °C), can partially be present in the gas phase; this may explain its lower reactivity. Such a trend of substrate reactivity is also observed for catalytic systems based on 1 or 3 (Table 1, Figure S9, Supplementary Materials).

Substrate Scope
Apart from cyclohexane, oxidation of other cycloalkane substrates was also explored (Table 1, Figure 6 and Figure S9, Supplementary Materials). For catalyst 2, more reactive substrates are cycloheptane and cyclooctane, which lead to the maximum total yields of 26 and 20%, respectively. In comparison, the oxidation of cyclohexane and cyclopentane is less efficient (13-9% product yield). This might be influenced by the stability of formed radicals (cycloalkyl radicals) that increases with the ring size. Moreover, cyclopentane is rather volatile (boiling point (bp): 49 • C) and, at typical reaction conditions (50 • C), can partially be present in the gas phase; this may explain its lower reactivity. Such a trend of substrate reactivity is also observed for catalytic systems based on 1 or 3 (Table 1, Figure S9

Effect of Substrate and Oxidant Amount
In cyclohexane oxidation catalyzed by 2 ( Figure S10, Supplementary Materials), the reaction efficiency practically does not depend on the substrate amount within the studied range of loadings (0.5-2 mmol C6H12). In contrast, the amount of oxidant has a significant effect (Figure 7) and an excess of hydrogen peroxide is required for efficient oxidation of cyclohexane. An increase of the H2O2 amount from 1.5 to 7.5 mmol results in the growth of W0 (initial reaction rate) and product yield.

Effect of Substrate and Oxidant Amount
In cyclohexane oxidation catalyzed by 2 ( Figure S10, Supplementary Materials), the reaction efficiency practically does not depend on the substrate amount within the studied range of loadings (0.5-2 mmol C 6 H 12 ). In contrast, the amount of oxidant has a significant effect (Figure 7) and an excess of hydrogen peroxide is required for efficient oxidation of cyclohexane. An increase of the H 2 O 2 amount from 1.5 to 7.5 mmol results in the growth of W 0 (initial reaction rate) and product yield. Furthermore, higher loadings of H 2 O 2 (up to 7.5 mmol) may lead to a yield drop due to the overoxidation at prolonged reaction times. The W 0 linearly depends on the amount of hydrogen peroxide (Figure 7b), suggesting reaction kinetics of the first order for the oxidant.

Effect of Substrate and Oxidant Amount
In cyclohexane oxidation catalyzed by 2 ( Figure S10, Supplementary Materials), the reaction efficiency practically does not depend on the substrate amount within the studied range of loadings (0.5-2 mmol C6H12). In contrast, the amount of oxidant has a significant effect ( Figure 7) and an excess of hydrogen peroxide is required for efficient oxidation of cyclohexane. An increase of the H2O2 amount from 1.5 to 7.5 mmol results in the growth of W0 (initial reaction rate) and product yield. Furthermore, higher loadings of H2O2 (up to 7.5 mmol) may lead to a yield drop due to the overoxidation at prolonged reaction times. The W0 linearly depends on the amount of hydrogen peroxide (Figure 7b), suggesting reaction kinetics of the first order for the oxidant.

Effect of Water
Recently, we reported an unexpected acceleration effect of H 2 O on cyclohexane oxidation catalyzed by other Cu catalytic systems [23,24]. Aiming at understanding whether H 2 O plays any role in the present Cu 4 catalytic systems, we investigated the influence of water quantity in the system H2O2 (1.5-7.5 mmol), CH3CN (up to 2.5 mL of total reaction volume), 50 °C.

Effect of Water
Recently, we reported an unexpected acceleration effect of H2O on cyclohexane oxidation catalyzed by other Cu catalytic systems [23,24]. Aiming at understanding whether H2O plays any role in the present Cu4 catalytic systems, we investigated the influence of water quantity in the system on both the W0 (maximum initial reaction rate) and product yield values in the C6H12 oxidation in the presence of catalyst 2 (Figure 8). Some water quantity (4.0 M) is already present in the reaction system that comes from the aqueous 50% H2O2. Addition of an extra portion of H2O (200 µL, 4.4 M; 8.4 M H2O total) into the reaction mixture results in an increase of the initial reaction rate W0 while not affecting the maximum yield of products. Addition of a double amount of water (400 µL, 8.4 M; 12.8 M H2O total) leads to further acceleration of W0 which, however, is accompanied by the decrease of total yield. The W0 values reveal a linear trend in the concentration of water within a studied range of concentrations (Figure 8b), thus suggesting an involvement of H2O in a rate-limiting step of the reaction. Such a promoting H2O behavior opens up a possibility of using the diluted H2O2 solutions (generated in situ) for cycloalkane oxidation.

Mild Cu-Catalyzed Oxidation of Propane
Development of the direct oxidation of propane constitutes a very promising approach in catalysis due to the abundance of this hydrocarbon as a C3 feedstock for the generation of valueadded oxidation products [1,2]. Hence, catalytic performance of compounds 1-3 was also evaluated the in the propane oxidation with H2O2 under mild conditions, resulting in a mixture of isopropanol, acetone, n-propanol, and propanal (Scheme 3, Table 2).

Mild Cu-Catalyzed Oxidation of Propane
Development of the direct oxidation of propane constitutes a very promising approach in catalysis due to the abundance of this hydrocarbon as a C 3 feedstock for the generation of value-added oxidation products [1,2]. Hence, catalytic performance of compounds 1-3 was also evaluated the in the propane oxidation with H 2 O 2 under mild conditions, resulting in a mixture of isopropanol, acetone, n-propanol, and propanal (Scheme 3, Table 2).

Effect of Water
Recently, we reported an unexpected acceleration effect of H2O on cyclohexane oxidation catalyzed by other Cu catalytic systems [23,24]. Aiming at understanding whether H2O plays any role in the present Cu4 catalytic systems, we investigated the influence of water quantity in the system on both the W0 (maximum initial reaction rate) and product yield values in the C6H12 oxidation in the presence of catalyst 2 (Figure 8). Some water quantity (4.0 M) is already present in the reaction system that comes from the aqueous 50% H2O2. Addition of an extra portion of H2O (200 µL, 4.4 M; 8.4 M H2O total) into the reaction mixture results in an increase of the initial reaction rate W0 while not affecting the maximum yield of products. Addition of a double amount of water (400 µL, 8.4 M; 12.8 M H2O total) leads to further acceleration of W0 which, however, is accompanied by the decrease of total yield. The W0 values reveal a linear trend in the concentration of water within a studied range of concentrations (Figure 8b), thus suggesting an involvement of H2O in a rate-limiting step of the reaction. Such a promoting H2O behavior opens up a possibility of using the diluted H2O2 solutions (generated in situ) for cycloalkane oxidation.

Mild Cu-Catalyzed Oxidation of Propane
Development of the direct oxidation of propane constitutes a very promising approach in catalysis due to the abundance of this hydrocarbon as a C3 feedstock for the generation of valueadded oxidation products [1,2]. Hence, catalytic performance of compounds 1-3 was also evaluated the in the propane oxidation with H2O2 under mild conditions, resulting in a mixture of isopropanol, acetone, n-propanol, and propanal (Scheme 3, Table 2). All catalysts 1-3 exhibit a comparable level of activity regarding the total product yield, which is in the 7-9% range (based on propane). As expected, the oxidation at the secondary C(2) atom is preferable, resulting in the generation of i-propanol and acetone as major products, due to an easier activation of the secondary carbon in propane in comparison with the two primary ones. Thus, n-propanol and propanal are formed in minor quantities (Table 2). Despite not being very high, such a level of total yields (up to 9%) in propane oxidation can be considered as significant given the high inertness of propane, its low solubility in the reaction medium, and the mild reaction conditions applied (50 • C, low-pressure reaction).

Selectivity Parameters and Mechanistic Considerations in Alkane Oxidation
Catalysts 1-3 were also tested in oxidation reactions of other alkanes, including a linear alkane (n-heptane), polycyclic alkane (adamantane), and cycloalkanes with methyl functionality (methylcyclohexane, cis-dimethylcyclohexane), aiming at establishing various selectivity parameters (Table 3) Table 3). Oxidation of cis-dimethylcyclohexane provides the information about stereoselectivity through the determination trans/cis ratio between the isomeric tertiary alcohol products. The observed trans/cis values are 0.9, 0.8, and 1.1 for 1-3, respectively; these suggest that the reactions are non-stereoselective. Herein, all selectivity parameters were calculated on the basis of the molar ratios of the alcohol product isomers after the treatment of the reaction mixtures with solid PPh 3 (to reduce to alcohols, the alkyl hydroperoxides formed as primary products) followed by normalization (the number of hydrogen atoms at each carbon atom was taken into consideration). b Parameters C(1):C(2):C(3):C(4) refer to the reactivity of hydrogen atoms at C(1), C(2), C(3), and C(4) atoms of n-C 7 H 16 . c Parameters 1 • :2 • :3 • refer to the reactivity of hydrogen atoms at primary, secondary, and tertiary carbon atoms of methylcyclohexane. d Parameters 2 • :3 • refer to the reactivity of hydrogen atoms at secondary and tertiary carbon atoms of adamantane. e Parameters trans/cis refer to the ratio of the formed tertiary alcohol isomers with trans and cis orientation of CH 3 groups.
The obtained selectivity parameters, the generation of alkyl hydroperoxides as primary intermediate products (detected by Shul'pin's method [5,15]), and the analysis of the relevant literature [1-15] support a radical-type mechanism that involves indiscriminate oxidizing species such as hydroxyl radicals. Hence, we can propose a simplified mechanism for the Cu-catalyzed alkane oxidation with H 2 O 2 . It involves the following steps [8]: (1) formation of HO • radicals upon the interaction of H 2 O 2 with Cu catalyst; (2) reaction of HO • radicals with alkane, abstracting H atom and forming R • (alkyl radicals); (3) formation of ROO • radicals in the reaction of alkyl radicals with O 2 ; (4) transformation of ROO • radicals to ROOH (alkyl hydroperoxides) as a primary intermediate product; (5) decomposition of ROOH (via Cu-catalyzed processes), leading to alcohols (ROH) and ketones (R'=O) as final oxidation products.

Mild Cu-Catalyzed Carboxylation of C 5 -C 8 Cycloalkanes
In addition to the oxidation reactions, catalysts 1-3 were tested in the single-pot carboxylation of cycloalkanes under mild conditions [8]. This reaction consists of the treatment of C n cycloalkane with a carbonyl source (CO), a hydroxyl source (H 2 O), and an oxidant (potassium peroxodisulfate) to directly generate a C n+1 cycloalkane carboxylic acid as the main product (Scheme 4); in addition, cyclic alcohols and ketones are formed as minor oxidation products.
The obtained selectivity parameters, the generation of alkyl hydroperoxides as primary intermediate products (detected by Shul'pin's method [5,15]), and the analysis of the relevant literature [1-15] support a radical-type mechanism that involves indiscriminate oxidizing species such as hydroxyl radicals. Hence, we can propose a simplified mechanism for the Cu-catalyzed alkane oxidation with H2O2. It involves the following steps [8]: (1) formation of HO • radicals upon the interaction of H2O2 with Cu catalyst; (2) reaction of HO • radicals with alkane, abstracting H atom and forming R • (alkyl radicals); (3) formation of ROO • radicals in the reaction of alkyl radicals with O2; (4) transformation of ROO • radicals to ROOH (alkyl hydroperoxides) as a primary intermediate product; (5) decomposition of ROOH (via Cu-catalyzed processes), leading to alcohols (ROH) and ketones (R'=O) as final oxidation products.

Mild Cu-Catalyzed Carboxylation of C5-C8 Cycloalkanes
In addition to the oxidation reactions, catalysts 1-3 were tested in the single-pot carboxylation of cycloalkanes under mild conditions [8]. This reaction consists of the treatment of Cn cycloalkane with a carbonyl source (CO), a hydroxyl source (H2O), and an oxidant (potassium peroxodisulfate) to directly generate a Cn+1 cycloalkane carboxylic acid as the main product (Scheme 4); in addition, cyclic alcohols and ketones are formed as minor oxidation products.
Compounds 1-3 show very high activity (total product yields up to 46%) in the carboxylation of cycloalkanes (cyclooctane, cycloheptane, cyclohexane, and cyclopentane) to form cycloalkane carboxylic acid as a main product ( Table 4). The catalytic activity of 1-3 is rather similar. In comparison to the oxidation reactions of cycloalkanes with H2O2, the Cu-catalyzed alkane carboxylation reactions proceed in the absence of an acid promoter.
C5 and C6 cycloalkanes represent the highest reactivity, resulting in cyclopentane carboxylic and cyclohexane carboxylic acids with yields of 31 and 43%, respectively (hereinafter, yields are relative to alkane substrate). Corresponding ketones and alcohols are also formed in low amounts (0.3-3.5%) as by-products of oxidation.
Carboxylation of cycloheptane and cyclooctane results in cyclooctane carboxylic (up to 27% yield) and cyclononane carboxylic (up to 14% yield) acids. Herein, the formation of alcohol and ketone by-products is more appreciable, especially in the case of C8H16 with the yields of cyclooctanol and cyclooctanone of up to 12% (Table 4). Compounds 1-3 show very high activity (total product yields up to 46%) in the carboxylation of cycloalkanes (cyclooctane, cycloheptane, cyclohexane, and cyclopentane) to form cycloalkane carboxylic acid as a main product ( Table 4). The catalytic activity of 1-3 is rather similar. In comparison to the oxidation reactions of cycloalkanes with H 2 O 2 , the Cu-catalyzed alkane carboxylation reactions proceed in the absence of an acid promoter. C 5 and C 6 cycloalkanes represent the highest reactivity, resulting in cyclopentane carboxylic and cyclohexane carboxylic acids with yields of 31 and 43%, respectively (hereinafter, yields are relative to alkane substrate). Corresponding ketones and alcohols are also formed in low amounts (0.3-3.5%) as by-products of oxidation.
Carboxylation of cycloheptane and cyclooctane results in cyclooctane carboxylic (up to 27% yield) and cyclononane carboxylic (up to 14% yield) acids. Herein, the formation of alcohol and ketone by-products is more appreciable, especially in the case of C 8 H 16 with the yields of cyclooctanol and cyclooctanone of up to 12% (Table 4).

Mild Cu-Catalyzed Carboxylation of Propane
Compounds 1-3 were also applied as catalysts for the carboxylation of propane (Table 5, Scheme 5) to give iso-butyric acid (main product, 23-33% yield) and n-butyric acid (minor product, 5-7% yield), as expected for the superior reactivity of the C(2) atom in propane. Total yields of butyric acids attain 40.1% (catalyst 3), followed by 33.9 and 27.9% when using catalysts 1 and 2, respectively.

Mild Cu-Catalyzed Carboxylation of Propane
Scheme 5. Single-pot Cu-catalyzed carboxylation of propane to butyric acids.
Compounds 1-3 were also applied as catalysts for the carboxylation of propane (Table 5, Scheme 5) to give iso-butyric acid (main product, 23-33% yield) and n-butyric acid (minor product, 5-7% yield), as expected for the superior reactivity of the C(2) atom in propane. Total yields of butyric acids attain 40.1% (catalyst 3), followed by 33.9 and 27.9% when using catalysts 1 and 2, respectively. On the basis of experimental data and taking into consideration prior literature background for related reactions catalyzed by copper compounds [8,[34][35][36], we can propose a simplified mechanism (free-radical type) which includes several steps as follows: (1) homolysis of K2S2O8 to give sulfate radical SO4 •− ; (2) interaction of SO4 •− with alkane to abstract a hydrogen atom and generate R • (alkyl radical); (3) formation of RCO • (acyl radical) via carbonylation of R • with CO; (4) generation of RCO + (acyl cation) by oxidation of acyl radical (with an involvement of Cu II /Cu I redox couple; Cu II form is then regenerated through the oxidation with peroxodisulfate); (5) formation of a carboxylic acid product via hydrolysis of acyl cation by water.

Materials and Methods
All reagents and solvents were acquired from commercial suppliers. FTIR spectra were recorded (4000-400 cm −1 , KBr pellets) on a JASCO FT/IR-4100 Type A or Shimadzu IRAffinity-1S apparatus (abbreviations: vs-very strong, s-strong, m-medium, w-weak, br-broad, sh-shoulder). Elemental analyses (EA) were carried out on a Perkin Elmer PE 2400 Series II analyzer (Laboratory On the basis of experimental data and taking into consideration prior literature background for related reactions catalyzed by copper compounds [8,[34][35][36], we can propose a simplified mechanism (free-radical type) which includes several steps as follows: (1) homolysis of K 2 S 2 O 8 to give sulfate radical SO 4 •− ; (2) interaction of SO 4 •− with alkane to abstract a hydrogen atom and generate R • (alkyl radical); (3) formation of RCO • (acyl radical) via carbonylation of R • with CO; (4) generation of RCO + (acyl cation) by oxidation of acyl radical (with an involvement of Cu II /Cu I redox couple; Cu II form is then regenerated through the oxidation with peroxodisulfate); (5) formation of a carboxylic acid product via hydrolysis of acyl cation by water.

Materials and Methods
All reagents and solvents were acquired from commercial suppliers. FTIR spectra were recorded (4000-400 cm −1 , KBr pellets) on a JASCO FT/IR-4100 Type A or Shimadzu IRAffinity-1S apparatus (abbreviations: vs-very strong, s-strong, m-medium, w-weak, br-broad, sh-shoulder). Elemental analyses (EA) were carried out on a Perkin Elmer PE 2400 Series II analyzer (Laboratory of Analyses, IST). ESI-MS spectra were obtained on an LCQ Fleet apparatus equipped with an electrospray (ESI) ion source (Thermo Scientific, San Jose, CA, USA). Gas chromatography (GC) analyses were carried out on an Agilent Technologies 7820A series gas chromatograph (Flame ionization detector; capillary column: BP20/SGE; carrier gas: He;).

Synthetic Procedure and Analytical Data for 1-3
Firstly, N,N-bis(2-hydroxyethyl)-2-aminoethanesulfonic acid (H 3 bes, 1 mmol, 213 mg) was added to an aqueous solution of Cu(NO 3 ) 2 ·3H 2 O (1 mmol, 0.1 M, 10 mL) with stirring under aerobic conditions at room temperature (reaction solution A). Then, benzene carboxylic acid (1 mmol; benzoic acid for 1 (Hba, 122 mg), 4-hydroxybenzoic acid for 2 (Hfhba, 138 mg), or 3-hydroxybenzoic acid for 3 (Hthba, 138 mg)) was dissolved in aqueous NH 4 OH (25% m/m, 4-12 mmol, up to 1.87 mL) to produce reaction solution B. This was slowly added to solution A and the obtained solution was further stirred least-squares refinement was used with anisotropic thermal parameters. In 3, water O atoms were refined with 0.5 occupancy. A twin matrix was applied to 3. All the hydrogen atoms bonded to carbon atoms were inserted in idealized positions and allowed to refine at the parent carbon atom. H atoms on the aminoalcohol moieties were localized by the electron density map and their positions were fixed. Regarding the hydroxyl groups in the benzene carboxylate in 3 and 2, the hydrogen atoms were inserted in idealized positions and allowed to refine at the parent O atom. With the exception of 2, the water hydrogen atoms were not possible to locate. Despite several attempts to recrystallize the compounds and several data collections for each sample, crystals of 1 and 3 were of low quality and the refinement of these crystal structures resulted in high R int and final R 1 and wR 2 values or completeness issues (for 3). The structure of 2 represents the best refinement parameters (Table S1, Supplementary Materials) and, thus, is discussed in detail as a representative example. The structural data for 1-3 were deposited as CIF files within the Cambridge Crystallographic Data Base (CCDC 1899840-1899842).

Catalytic Oxidation of Cycloalkanes
Catalytic tests were performed in glass reactors (equipped with a condenser) under aerobic conditions and under vigorous stirring at 50 • C, using MeCN as a solvent (up to 2.5 mL of total reaction volume). Total volume refers to all reagents and solvent (H 2 O 2 , alkane, GC standard, H 2 O, and MeCN). The typical procedure was as follows: catalyst 1-3 (2.5 µmol) was introduced into a MeCN solution, followed by the addition of an acid promoter (50 µmol) and GC internal standard (MeNO 2 , 250 µL). Then, an alkane substrate (1 mmol) and hydrogen peroxide (50% in H 2 O, 5 mmol) were added. The oxidation reactions were followed by withdrawing small aliquots of the reaction mixture at different time periods. Prior to GC (gas chromatography) analysis, the aliquots were treated with solid PPh 3 for reducing alkyl hydroperoxides (primary products in cycloalkane reactions) and remaining H 2 O 2 ; all the product yields were calculated based on GC data after the treatment with solid PPh 3 . Generation of alkyl hydroperoxides as primary products was corroborated by doing the GC analyses of selected samples twice, before and after the treatment with solid PPh 3 (Shul'pin's method) [5,15]. Peaks were attributed by comparing the obtained chromatograms with those of commercially available samples of products.

Catalytic Oxidation of Propane
The typical procedure was as follows: catalyst 1-3 (2.5 µmol) was introduced in an acetonitrile solution, and then an acid promoter (50 µmol), MeNO 2 (GC internal standard, 250 µL), and hydrogen peroxide (50% in H 2 O, 5 mmol) were added. A stainless-steel autoclave (total volume of 20.0 mL) was closed, pressurized with 3 atm of propane substrate, and kept under stirring at 50 • C (oil bath and magnetic stirrer) for 4 h. The autoclave was then cooled down and degassed. Samples of the reaction mixture were treated with PPh 3 and analyzed by GC for quantification of products (internal standard method).

Catalytic Carboxylation of Alkanes
The typical procedure was as follows: catalyst 1-3 (2.5 µmol), H 2 O (2.0 mL), MeCN (4.0 mL), cycloalkane (1.0 mmol), and K 2 S 2 O 8 (1.50 mmol) were introduced into a stainless-steel autoclave (total volume of 20.0 mL). Then, the autoclave was closed and flushed three times with CO for air removal and pressurized with carbon monoxide (20 atm). In the case of propane carboxylation, the reactor was first flushed and pressurized with propane followed by the addition of CO. The reaction mixture was stirred at 60 • C for 4 h (oil bath and magnetic stirrer). After this period, the autoclave was cooled in an ice bath, degassed, and opened. The reaction mixture was transferred to a glass flask. Et 2 O (9.0 mL) and GC internal standard (cycloheptanone, 45 µL) were introduced; cyclohexanone was the GC standard in the carboxylation of cycloheptane. After stirring the obtained mixture for 10 min, the aliquots were taken from an organic layer. These were subjected to GC analysis for the quantification (internal standard method) of carboxylic acids as principal products (ketones and alcohols were also formed as by-products in minor amounts). Peaks were attributed by comparing the obtained chromatograms with those of commercially available samples of products.
In fact, the obtained compounds 1-3 act as efficient and versatile homogeneous catalysts for the oxidation of cycloalkanes with hydrogen peroxide to produce cyclic alcohols and ketones, with total yields attaining 27% (yields are based on cycloalkane substrate). Propane oxidation into a mixture of the C 3 oxidation products was also achieved. The influence of various parameters of the oxidation reaction was investigated in detail, in addition to mechanistic and selectivity features. Moreover, compounds 1-3 also catalyze the mild carboxylation of propane and C 5 -C 8 cycloalkanes to give carboxylic acids in as high as 41% yield (based on alkane substrate). The obtained yields are remarkable considering the inertness of alkane substrates and mild reaction conditions applied [1][2][3][4][5][6][7][8].
Given the multicopper nature of active sites in some enzymes (i.e., multicopper oxidases, particulate methane monooxygenase) [20][21][22]48], the mild oxidative functionalization of alkanes using such bioinspired multicopper catalysts represents a particularly interesting research direction. Future research will also focus on the design of new structurally related coordination compounds and their application as catalysts in the mild functionalization of saturated hydrocarbons. The search for more efficient systems, optimization of reaction parameters, and widening of the substrate scope will be pursued.