95-47-6 Usage
Xylene
Xylene refers to the aromatic hydrocarbon with the two hydrogen atoms on the benzene ring being substituted by two methyl groups. It has three isomers o-xylene (1, 2-Dimethylbenzene), m-xylene and p-xylene. The industrial products are the mixtures of the three isomers with 10% o-10%, 70% m-, and 20% p-. In the coking industry, it is one of crude benzene refined products.
Xylene is a kind of colorless flammable liquid; the melting point of o-, m-and p-xylene is-25.2 ℃,-47.9 ℃ and 13.3 ℃; the boiling points are respectively 144.4 ℃, 139.1 ℃ and 138.3 ℃ while the relative density is 0.8802, 0.8642 and 0.8611, respectively; It is not soluble in water but miscible with many kinds of organic solvents immiscibility. Upon catalytic oxidation, they respectively, generate phthalic anhydride, isophthalic acid and terephthalic acid.
Xylene is one kind of important raw materials of organic chemicals, naturally existing in coal tar and some kinds of petroleum. It can be obtained through the fractionation of the light oil part of the coal tar or catalytic reforming light gasoline. Industry mainly performs extracting using the C8 fraction in the naphtha reformates. It can be alternatively manufactured through the disproportionation reaction of toluene in the presence of catalyst and high temperature, high pressure. At present time, industry mainly applies the method of cryogenic crystallization, adsorption and formation of complexes or molecular sieves to separate them. O-xylene has a relatively high boiling point, being able to be separated using distillation. p-xylene also has a high melting point and can be purified through fractional crystallization purification. Mixed xylene without separation can be directly used as a solvent with being supplemented to the gasoline capable of improving the anti-explosive properties. They are components of aviation gasoline. O-xylene is mainly used for the preparation of phthalic anhydride, which is an important raw material for the manufacture of a variety of dyes and indicators (such as phenolphthalein). In addition, o-xylene can also be used for preparation of polyester resin, insect repellent, plasticizers and dyes. M-xylene, through nitration and reduction, can generate 4, 6-dimethyl-1, 3-phenylenediamine that is the intermediate for synthetic dyes. M-xylene can also be used as the raw materials for synthetic fragrances (such as xylene musk). P-xylene is mainly used in the manufacture of terephthalic acid, which is an important raw material for synthetic polyester fiber (polyester).
?
Figure 1 the chemical structure of the three isomers of xylene, ortho-xylene, m-xylene, p-xylene chemical structure.
The above information is edited by lookchem.
Precision Distillation for separation of O-xylene and p-xylene
Xylene is presented in coked crude benzene and petroleum cracked oil. Crude benzene, after initial distillation, sulfuric acid washing and distillation for separation of benzene and toluene, followed by distillation, we can obtain xylene, also known as coking xylene. The quality of the coked xylene depends on the separation capacity of the distillation column, the temperature at the top of the column and the reflux ratio. China has classified the coking xylene products into three levels. The coking xylene generally contains 16% if o-xylene, 50% of m-xylene, 21% of p-xylene and 7% of ethylbenzene. The xylene produced in the petroleum industry has a low content of m-xylene and a high content of ethylbenzene. Industrial xylene is not only the solvent and additive of rubber and coatings industry, but also the additives of aviation and power fuel. O-xylene, m-xylene and p-xylene separated from industrial xylene are the raw materials of phthalic acid, isophthalic acid and terephthalic acid, respectively. Phthalic acid and terephthalic acid are used in the production of plasticizers, polyester resins and polyester fibers. M-xylene can be used alone as solvent and fuel additives. The o-xylene contained in the industrial xylene has a over 5.2 ℃ difference with other isomers. With precision distillation, we can obtain o-xylene with a purity of over 95%, followed by using sulfonation and distillation for purification so we can get further purer o-xylene.?
Xylene belongs to Lewis base, which can form a polar complex with HF-BF3 (Lewis acid). The alkalinity of M-xylene is about 100 times as strong as that of other C8 aromatics. When the isomer mixture of xylene comes into contact with HF-BF3 solvent, m-xylene can form a complex with fluoride and is preferentially extracted into the fluoride phase. The m-xylene-containing fluoride phase is heated at a lower pressure to decompose the complex, thereby separating m-xylene from the mixture. HF-BF3 solvent can be recovered by distillation for recycling. If the raw material is a mixture of ortho-xylene, m-xylene and p-xylene, after the m-xylene is extracted, we can further use precision distillation to separate the o-xylene and p-xylene.
Figure 2 the precision distillation method for separation of o-xylene and p-xylene.
Chemical properties
It appears as colorless transparent liquid with aromatic odor. It is miscible with ethanol, ethyl ether, acetone and benzene but insoluble in water.
Uses
Different sources of media describe the Uses of 95-47-6 differently. You can refer to the following data:
1. (1)? It is mainly used in the production of phthalic anhydride
(2)? O-xylene is the raw material for the production of germicide fenramine, tetrachlorophenyl peptide and the herbicide bensulfuron-methyl. It is used as intermediate for the manufacture of o-methyl benzoic acid.
(3)? It is mainly used as chemical raw materials and solvents. It can be used to produce phthalic anhydride, dyes, pesticides and drugs, such as vitamins. It can also be used as aviation gasoline additives.
(4)? Used as chromatographic standards and solvents
(5)? As raw materials of synthesis of anhydride and other organic synthesis;
2. Preparation of phthalic acid, phthalic anhydride, terephthalic acid, isophthalic acid; solvent
for alkyd resins, lacquers, enamels, rubber cements; manufacture of dyes, pharmaceuticals, and
insecticides; motor fuels.
3. o-Xylene is largely used in the production of phthalic anhydride, and is generally extracted by distillation from a mixed Xylene stream in a plant primarily designed for p-Xylene production.
4. Xylene, xylenes, and total xylenes are used interchangeably since xylene usually exists as a mixture of three
isomers: 1,2-dimethylbenzene, 1,3-dimethylbenzene, and 1,4-dimethylbenzene, i.e., o-, m-, and p-xylene, and
is usually used as a mixture of the three forms. The mixture
often also contains ethylbenzene. It is a high volume industrial
chemical used in the synthetic fiber, chemical and plastics
industries and as a solvent, cleaning agent and thinner for paints
and varnishes.
Production method
Industry applied super-distillation method to separate out the o-xylene from the mixed xylene. O-xylene has a over 5 ℃ difference in the boiling point compared with other components in the mixed xylene. For the distillation, the required tray number is about 150; the reflux ratio being 5-8 and consume relative much energy.
O-xylene was originally produced mainly from coal tar. Currently most of the domestic and foreign production of o-xylene is mainly via extraction from oil catalytic reforming and thermal cracking of aromatic hydrocarbon. Owing to that the structures of o-xylene, p-xylene, and m-xylene in the xylene are very similar; their physical parameters are also quite similar. Industrial o-xylene separation mainly adopts super-distillation method; first separate out the o-xylene and ethylbenzene from the mixed xylene which demands the using of 100~150 tray distillation tower; followed by separation of o-xylene and ethylbenzene to obtain pure o-xylene.
Acute toxicity
Oral-rat LDL0: 5000 mg/kg; abdominal injection-mouse LD50: 1364 mg/kg
EXPLOSIVES and HAZARDOUS CHARACTERISTICS
being explosive when mixed with air
Flammability and Hazardous characteristics
being flammable upon flame, heat, oxidant Flammable with combustion releasing irritant smoke
Storage and transportation characteristics
warehouse: ventilated, low temperature and dry; gently load and unload; store it separately from oxidants and acids.
Fire extinguishing agent
mist water, foam, sand, carbon dioxide, 1211 extinguishing agent
Occupational Standard
TLV-TWA 100 PPM (440 mg/m 3); STEL 150; PPM (655 mg/m 3)
Chemical Properties
colourless liquid
Physical properties
Clear, colorless liquid with an aromatic odor. An odor threshold concentration of 380 ppbv was
reported by Nagata and Takeuchi (1990).
Definition
ChEBI: A xylene substituted by methyl groups at positions 1 and 3.
Synthesis Reference(s)
Journal of the American Chemical Society, 97, p. 7262, 1975 DOI: 10.1021/ja00858a011The Journal of Organic Chemistry, 44, p. 2185, 1979 DOI: 10.1021/jo01327a032
General Description
A colorless watery liquid with a sweet odor. Less dense than water. Insoluble in water. Irritating vapor.
Air & Water Reactions
Highly flammable. Insoluble in water.
Reactivity Profile
1,2-Dimethylbenzene may react with oxidizing materials. .
Flammability and Explosibility
Flammable
Safety Profile
Moderately toxic bj7
intraperitoneal route. Mldly toxic by
ingestion and inhalation. An experimental
teratogen. A common air contaminant. A
very dangerous fire hazard when exposed to
heat or flame. Explosive in the form of
vapor when exposed to heat or flame. To
fight fire, use foam, CO2, dry chemical.
Incompatible with oxidzing materials.
When heated to decomposition it emits
acrid smoke and irritating fumes. Emitted
from modern building materials (CENEAR
69,22,91). See also other xylene entries.
Source
Detected in distilled water-soluble fractions of 87 octane gasoline (3.83 mg/L), 94 octane
gasoline (11.4 mg/L), Gasohol (8.49 mg/L), No. 2 fuel oil (1.73 mg/L), jet fuel A (0.87 mg/L),
diesel fuel (1.75 mg/L), military jet fuel JP-4 (1.99 mg/L) (Potter, 1996), new motor oil (16.2 to 17.5 μg/L), and used motor oil (294 to 308 μg/L) (Chen et al., 1994). The average volume percent
and estimated mole fraction in American Petroleum Institute PS-6 gasoline are 2.088 and 0.01959,
respectively (Poulsen et al., 1992). Schauer et al. (1999) reported o-xylene in a diesel-powered
medium-duty truck exhaust at an emission rate of 830 μg/km. Diesel fuel obtained from a service
station in Schlieren, Switzerland contained o-xylene at a concentration of 223 mg/L (Schluep et
al., 2001).
California Phase II reformulated gasoline contained o-xylene at a concentration of 19.7 g/kg.
Gas-phase tailpipe emission rates from gasoline-powered automobiles with and without catalytic
converters were 5.41 and 562 mg/km, respectively (Schauer et al., 2002).
Thomas and Delfino (1991) equilibrated contaminant-free groundwater collected from
Gainesville, FL with individual fractions of three individual petroleum products at 24–25 °C for
24 h. The aqueous phase was analyzed for organic compounds via U.S. EPA approved test method
602. Average m+p-xylene concentrations reported in water-soluble fractions of unleaded gasoline,
kerosene, and diesel fuel were 8.611, 0.658, and 0.228 mg/L, respectively. When the authors
analyzed the aqueous-phase via U.S. EPA approved test method 610, average m+p-xylene
concentrations in water-soluble fractions of unleaded gasoline, kerosene, and diesel fuel were
lower, i.e., 6.068, 0.360, and 0.222 mg/L, respectively.
Based on laboratory analysis of 7 coal tar samples, o-xylene concentrations ranged from 2 to
2,000 ppm (EPRI, 1990). A high-temperature coal tar contained o-xylene at an average
concentration of 0.04 wt % (McNeil, 1983).
Schauer et al. (2001) measured organic compound emission rates for volatile organic
compounds, gas-phase semi-volatile organic compounds, and particle-phase organic compounds
from the residential (fireplace) combustion of pine, oak, and eucalyptus. The gas-phase emission
rate of o-xylene was 18.1 mg/kg of pine burned. Emission rates of o-xylene were not measured
during the combustion of oak and eucalyptus.
Drinking water standard (final): For all xylenes, the MCLG and MCL are both 10 mg/L. In
addition, a DWEL of 70 mg/L was recommended (U.S. EPA, 2000).
Environmental fate
Biological. Reported biodegradation products of the commercial product containing xylene
include α-hydroxy-p-toluic acid, p-methylbenzyl alcohol, benzyl alcohol, 4-methylcatechol, mand
p-toluic acids (Fishbein, 1985). o-Xylene was also cometabolized resulting in the formation of
o-toluic acid (Pitter and Chudoba, 1990). In anoxic groundwater near Bemidji, MI, o-xylene
anaerobically biodegraded to the intermediate o-toluic acid (Cozzarelli et al., 1990). In gasolinecontaminated
groundwater, methylbenzylsuccinic acid was identified as the first intermediate
during the anaerobic degradation of xylenes (Reusser and Field, 2002).
Photolytic. Cox et al. (1980) reported a rate constant of 1.33 x 10-11 cm3/molecule?sec for the
reaction of gaseous o-xylene with OH radicals based on a value of 8 x 10-12 cm3/molecule?sec for
the reaction of ethylene with OH radicals.
Surface Water. The evaporation half-life of o-xylene in surface water (1 m depth) at 25 °C is
estimated to be 5.18 h (Mackay and Leinonen, 1975).
Groundwater. Nielsen et al. (1996) studied the degradation of o-xylene in a shallow,
glaciofluvial, unconfined sandy aquifer in Jutland, Denmark. As part of the in situ microcosm study, a cylinder that was open at the bottom and screened at the top was installed through a cased
borehole approximately 5 m below grade. Five liters of water was aerated with atmospheric air to
ensure aerobic conditions were maintained. Groundwater was analyzed weekly for approximately
3 months to determine o-xylene concentrations with time. The experimentally determined firstorder
biodegradation rate constant and corresponding half-life following a 7-d lag phase were
0.1/d and 6.93 d, respectively.
Photolytic. When synthetic air containing gaseous nitrous acid and o-xylene was exposed to
artificial sunlight (λ = 300–450 nm) biacetyl, peroxyacetal nitrate, and methyl nitrate formed as
products (Cox et al., 1980). A n-hexane solution containing o-xylene and spread as a thin film (4
mm) on cold water (10 °C) was irradiated by a mercury medium pressure lamp. In 3 h, 13.6% of
the o-xylene photooxidized into o-methylbenzaldehyde, o-benzyl alcohol, o-benzoic acid, and omethylacetophenone
(Moza and Feicht, 1989). Irradiation of o-xylene at ≈ 2537 ? at 35 °C and 6
mmHg isomerizes to m-xylene (Calvert and Pitts, 1966). Glyoxal, methylglyoxal, and biacetyl
were produced from the photooxidation of o-xylene by OH radicals in air at 25 °C (Tuazon et al.,
1986a).
Chemical/Physical. Under atmospheric conditions, the gas-phase reaction of o-xylene with OH
radicals and nitrogen oxides resulted in the formation of o-tolualdehyde, o-methylbenzyl nitrate,
nitro-o-xylenes, 2,3-and 3,4-dimethylphenol (Atkinson, 1990). Kanno et al. (1982) studied the
aqueous reaction of o-xylene and other aromatic hydrocarbons (benzene, toluene, m- and p-xylene,
and naphthalene) with hypochlorous acid in the presence of ammonium ion. They reported that the
aromatic ring was not chlorinated as expected but was cleaved by chloramine forming cyanogen
chloride. The amount of cyanogen chloride formed increased at lower pHs (Kanno et al., 1982). In
the gas phase, o-xylene reacted with nitrate radicals in purified air forming the following products:
5-nitro-2-methyltoluene and 6-nitro-2-methyltoluene, o-methylbenzaldehyde, and an aryl nitrate
(Chiodini et al., 1993).
Purification Methods
o-Xylene (4.4Kg) is sulfonated by stirring for 4hours with 2.5L of conc H2SO4 at 95o. After cooling, and separating the unsulfonated material, the product is diluted with 3L of water and neutralised with 40% NaOH. On cooling, sodium o-xylene sulfonate separates and is recrystallised from half its weight of water. [A further crop of crystals is obtained by concentrating the mother liquor to one-third of its volume.] The salt is dissolved in the minimum amount of cold water, then mixed with the same amount of cold water, and with the same volume of conc H2SO4 and heated to 110o. o-Xylene is regenerated and steam distils. The distillate is saturated with NaCl, the organic layer is separated, dried and redistilled. [Beilstein 5 H 362, 5 I 179, 5 II 281, 5 III 807, 5 IV 917.]
Check Digit Verification of cas no
The CAS Registry Mumber 95-47-6 includes 5 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 2 digits, 9 and 5 respectively; the second part has 2 digits, 4 and 7 respectively.
Calculate Digit Verification of CAS Registry Number 95-47:
(4*9)+(3*5)+(2*4)+(1*7)=66
66 % 10 = 6
So 95-47-6 is a valid CAS Registry Number.
InChI:InChI=1/C8H10/c1-7-5-3-4-6-8(7)2/h3-6H,1-2H3
95-47-6Relevant articles and documents
Evidence for a Bimolecular Isomerization of Xylenes on Some Large Pore Zeolites
Corma, A.,Sastre, E.
, p. 594 - 596 (1991)
Use of deuteriated p-xylene as reactant shows that alkyl isomerization takes place by both uni- and bi-molecular mechanisms on faujasite and mordenite, but only by a unimolecular 1,2-methyl shift on β-zeolite.
Selective catalytic synthesis of bio-based high value chemical of benzoic acid from xylan with Co2MnO4@MCM-41 catalyst
Fan, Minghui,He, Yuting,Li, Quanxin,Luo, Yuehui,Yang, Mingyu,Zhang, Yanhua,Zhu, Lijuan
, (2021/12/20)
The efficient synthesis of bio-based chemicals using renewable carbon resources is of great significance to promote sustainable chemistry and develop green economy. This work aims to demonstrate that benzoic acid, an important high added value chemical in petrochemical industry, can be selectively synthesized using xylan (a typical model compound of hemicellulose). This novel controllable transformation process was achieved by selective catalytic pyrolysis of xylan and subsequent catalytic oxidation. The highest benzoic acid selectivity of 88.3 % with 90.5 % conversion was obtained using the 10wt%Co2MnO4@MCM-41 catalyst under the optimized reaction conditions (80 °C, 4 h). Based on the study of the model compounds and catalyst's characterizations, the reaction pathways for the catalytic transformation of xylan to bio-based benzoic acid were proposed.
Rational Design of Zinc/Zeolite Catalyst: Selective Formation of p-Xylene from Methanol to Aromatics Reaction
Chen, Biaohua,Chen, Congmei,Chen, Xiao,Hou, Yilin,Hu, Xiaomin,Li, Jing,Qian, Weizhong,Sun, Wenjing,Wang, Ning,Yang, Yifeng,Zhang, Lan
supporting information, (2022/02/16)
The production of p-xylene from the methanol to aromatics (MTA) reaction is challenging. The catalytic stability, which is inversely proportional to the particle size of the zeolite, is not always compatible with p-xylene selectivity, which is inversely proportional to the external acid sites. In this study, based on a nano-sized zeolite, we designed hollow triple-shelled Zn/MFI single crystals using the ultra-dilute liquid-phase growth technique. The obtained composites possessed one ZSM-5 layer (≈30 nm) in the middle and two silicalite-1 layers (≈20 nm) epitaxially grown on two sides of ZSM-5, which exhibited a considerably long lifetime (100 % methanol conversion >40 h) as well as an enhanced shape selectivity of p-xylene (>35 %) with a p-xylene/xylene ratio of ≈90 %. Importantly, using this sandwich-like zeolite structure, we directly imaged the Zn species in the micropores of only the ZSM-5 layer and further determined the specific structure and anchor location of the Zn species.
Comparison of Physicochemical Properties and Catalytic Activity in the m-Xylene Isomerization of Catalysts Based on ZSM-12 Zeolites Prepared at Hydrothermal Conditions and under the Action of Microwave Radiation
Tsaplin,Ostroumova,Kulikov,Naranov,Egazar’yants,Karakhanov
, p. 1292 - 1301 (2021/12/29)
The properties of ZSM-12 zeolites prepared under hydrothermal conditions and microwave radiation influence were investigated. The prepared zeolites were characterized by various physicochemical methods of analysis, e.g., X-ray diffraction analysis, low-temperature nitrogen adsorption/desorption, scanning electron microscopy, solid-state 27Al and 29Si NMR spectroscopy, IR spectroscopy, temperature-programmed desorption of ammonia, IR spectroscopy of adsorbed pyridine, and X-ray fluorescence elemental analysis. The calcined zeolites were impregnated with 0.5 wt.% Pt, which performed the hydrogenation function in the reaction under study. The obtained materials were evaluated in the m-xylene isomerization reaction under the following conditions: Т = 300°С–440°С, WHSV = 1/hr, Р(Н2) = 10 atm. On the ZSM-12 MW catalyst, due to its high acidity and fine particles, which promoted high mass transfer, it is possible to increase the yields of m-xylene isomers, in particular p-xylene, to 36%–65%.
One-Pass Conversion of Benzene and Syngas to Alkylbenzenes by Cu–ZnO–Al2O3 and ZSM-5 Relay
Dong, Jinxiang,Ge, Hui,Han, Tengfei,Li, Xuekuan,Liu, Jianchao,Xu, Hong,Zhou, Ligong
, (2021/05/21)
Alkylbenzenes have a wide range of uses and are the most demanded aromatic chemicals. The finite petroleum resources compels the development of production of alkylbenzenes by non-petroleum routes. One-pass selective conversion of benzene and syngas to alkylbenzenes is a promising alternative coal chemical engineering route, yet it still faces challenge to industrialized applications owing to low conversion of benzene and syngas. Here we presented a Cu–ZnO–Al2O3/ZSM-5 bifunctional catalyst which realizes one-pass conversion of benzene and syngas to alkylbenzenes with high efficiency. This bifunctional catalyst exhibited high benzene conversion (benzene conversion of 50.7%), CO conversion (CO conversion of 55.0%) and C7&C8 aromatics total yield (C7&C8 total yield of 45.0%). Characterizations and catalytic performance evaluations revealed that ZSM-5 with well-regulated acidity, as a vital part of this Cu–ZnO–Al2O3/ZSM-5 bifunctional catalyst, substantially contributed to its performance for the alkylbenzenes one-pass synthesis from benzene and syngas due to depress methanol-to-olefins (MTO) reaction. Furthermore, matching of the mass ratio of two active components in the dual-function catalyst and the temperature of methanol synthesis with benzene alkylation reactions can effectively depress the formation of unwanted by-products and guarantee the high performance of tandem reactions. Graphic Abstract: [Figure not available: see fulltext.]
Synergistic effect for selective hydrodeoxygenation of anisole over Cu-ReOx/SiO2
Wang, Xiaofei,Zhou, Wei,Wang, Yue,Huang, Shouying,Zhao, Yujun,Wang, Shengping,Ma, Xinbin
, p. 223 - 234 (2020/04/27)
Selective hydrodeoxygenation (HDO) of lignin derived oxygenated aromatic compounds has great significance for lignin utilization and chemicals production. Hereby, bifunctional catalysts of Cu-MOx/SiO2 (M = Re, Mo or W) were prepared to study the synergistic effect of Cu and MOx on the performance of anisole HDO. Characterizations indicated that Cu interacted strongly with the second metal species. As a result, more efficient sites exposed on catalysts surface, and metal dispersion and surface properties both were improved. Besides, adsorption strength for both oxygen atom and aromatic ring in reactant were all adjusted due to Cu-MOx interaction. Bimetallic catalyst Cu-ReOx/SiO2 showed the highest HDO activity, while Cu-MoOx/SiO2 and Cu-WOx/SiO2 both preferred transmethylation because of their prominent acid properties. The Cu-ReOx composition was found to evidently affect the anisole conversion and selectivity of benzene, toluene and xylene (BTX). The highest BTX yield of 50.5 % could be achieved when Cu/Re ratio was 3.
A chemiresistive methane sensor
Bezdek, Máté J.,Luo, Shao-Xiong Lennon,Ku, Kang Hee,Swager, Timothy M.
, (2021/01/12)
A chemiresistive sensor is described for the detection of methane (CH4), a potent greenhouse gas that also poses an explosion hazard in air. The chemiresistor allows for the low-power, low-cost, and distributed sensing of CH4 at room temperature in air with environmental implications for gas leak detection in homes, production facilities, and pipelines. Specifically, the chemiresistors are based on single-walled carbon nanotubes (SWCNTs) noncovalently functionalized with poly(4-vinylpyridine) (P4VP) that enables the incorporation of a platinum-polyoxometalate (Pt-POM) CH4 oxidation precatalyst into the sensor by P4VP coordination. The resulting SWCNT-P4VP-Pt-POM composite showed ppm-level sensitivity to CH4 and good stability to air as well as time, wherein the generation of a high-valent platinum intermediate during CH4 oxidation is proposed as the origin of the observed chemiresistive response. The chemiresistor was found to exhibit selectivity for CH4 over heavier hydrocarbons such as n-hexane, benzene, toluene, and o-xylene, as well as gases, including carbon dioxide and hydrogen. The utility of the sensor in detecting CH4 using a simple handheld multimeter was also demonstrated.
Radical induced disproportionation of alcohols assisted by iodide under acidic conditions
Huang, Yang,Jiang, Haiwei,Li, Teng,Peng, Yang,Rong, Nianxin,Shi, Hexian,Yang, Weiran
supporting information, p. 8108 - 8115 (2021/10/29)
The disproportionation of alcohols without an additional reductant and oxidant to simultaneously form alkanes and aldehydes/ketones represents an atom-economical transformation. However, only limited methodologies have been reported, and they suffer from a narrow substrate scope or harsh reaction conditions. Herein, we report that alcohol disproportionation can proceed with high efficiency catalyzed by iodide under acidic conditions. This method exhibits high functional group tolerance including aryl alcohol derivatives with both electron-withdrawing and electron-donating groups, furan ring alcohol derivatives, allyl alcohol derivatives, and dihydric alcohols. Under the optimized reaction conditions, a 49% yield of 5-methyl furfural and a 49% yield of 2,5-diformylfuran were obtained simultaneously from 5-hydroxymethylfurfural. An initial mechanistic study suggested that the hydrogen transfer during this redox disproportionation occurred through the inter-transformation of HI and I2. Radical intermediates were involved during this reaction.
Bipyridinium and Phenanthrolinium Dications for Metal-Free Hydrodefluorination: Distinctive Carbon-Based Reactivity
Burton, Katherine I.,Elser, Iris,Waked, Alexander E.,Wagener, Tobias,Andrews, Ryan J.,Glorius, Frank,Stephan, Douglas W.
supporting information, p. 11730 - 11737 (2021/07/16)
The development of novel Lewis acids derived from bipyridinium and phenanthrolinium dications is reported. Calculations of Hydride Ion Affinity (HIA) values indicate high carbon-based Lewis acidity at the ortho and para positions. This arises in part from extensive LUMO delocalization across the aromatic backbones. Species [C10H6R2N2CH2CH2]2+ (R=H [1 a]2+, Me [1 f]2+, tBu [1 g]2+), and [C12H4R4N2CH2CH2]2+ (R=H [2 a]2+, Me [2 b]2+) were prepared and evaluated for use in the initiation of hydrodefluorination (HDF) catalysis. Compound [2 a]2+ proved highly effective towards generating catalytically active silylium cations via Lewis acid-mediated hydride abstraction from silane. This enabled the HDF of a range of aryl- and alkyl- substituted sp3(C?F) bonds under mild conditions. The protocol was also adapted to effect the deuterodefluorination of cis-2,4,6-(CF3)3C6H9. The dications are shown to act as hydride acceptors with the isolation of neutral species C16H14N2 (3 a) and C16H10Me4N2 (3 b) and monocationic species [C14H13N2]+ ([4 a]+) and [C18H21N2]+ ([4 b]+). Experimental and computational data provide further support that the dications are initiators in the generation of silylium cations.
Alkali Metal Adducts of an Iron(0) Complex and Their Synergistic FLP-Type Activation of Aliphatic C-X Bonds
Tinnermann, Hendrik,Sung, Simon,Csókás, Dániel,Toh, Zhi Hao,Fraser, Craig,Young, Rowan D.
supporting information, p. 10700 - 10708 (2021/07/31)
We report the formation and full characterization of weak adducts between Li+ and Na+ cations and a neutral iron(0) complex, [Fe(CO)3(PMe3)2] (1), supported by weakly coordinating [BArF20] anions, [1·M][BArF20] (M = Li, Na). The adducts are found to synergistically activate aliphatic C-X bonds (X = F, Cl, Br, I, OMs, OTf), leading to the formation of iron(II) organyl compounds of the type [FeR(CO)3(PMe3)2][BArF20], of which several were isolated and fully characterized. Stoichiometric reactions with the resulting iron(II) organyl compounds show that this system can be utilized for homocoupling and cross-coupling reactions and the formation of new C-E bonds (E = C, H, O, N, S). Further, we utilize [1·M][BArF20] as a catalyst in a simple hydrodehalogenation reaction under mild conditions to showcase its potential use in catalytic reactions. Finally, the mechanism of activation is probed using DFT and kinetic experiments that reveal that the alkali metal and iron(0) center cooperate to cleave C-X via a mechanism closely related to intramolecular FLP activation.
