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Cyclohexane oxide

Figure 1.15 shows the product profiles for the mixture containing 2.5, 140 and 357.5 Torr of cyclohexane, H2 and O2 at 753 K. The results are typical of the quality of data obtained not only from cyclohexane but alkanes and related compounds in general. Primary and secondary products may be characterized from the shape of the profiles. Cyclohexane, 7-oxabi-cyclo(2,2,l)heptane (1,4 cyclohexane oxide), 1,2 epoxycyclohexane, CH2=CHCH2CH2CH2CH0 (hex-5-en-l-al), buta-1,3-diene and possible... [Pg.75]

High Peroxide Process. An alternative to maximizing selectivity to KA in the cyclohexane oxidation step is a process which seeks to maximize cyclohexyUiydroperoxide, also called P or CHHP. This peroxide is one of the first intermediates produced in the oxidation of cyclohexane. It is produced when a cyclohexyl radical reacts with an oxygen molecule (78) to form the cyclohexyUiydroperoxy radical. This radical can extract a hydrogen atom from a cyclohexane molecule, to produce CHHP and another cyclohexyl radical, which extends the free-radical reaction chain. [Pg.241]

Although many variations of the cyclohexane oxidation step have been developed or evaluated, technology for conversion of the intermediate ketone—alcohol mixture to adipic acid is fundamentally the same as originally developed by Du Pont in the early 1940s (98,99). This step is accomplished by oxidation with 40—60% nitric acid in the presence of copper and vanadium catalysts. The reaction proceeds at high rate, and is quite exothermic. Yield of adipic acid is 92—96%, the major by-products being the shorter chain dicarboxytic acids, glutaric and succinic acids,and CO2. Nitric acid is reduced to a combination of NO2, NO, N2O, and N2. Since essentially all commercial adipic acid production arises from nitric acid oxidation, the trace impurities patterns ate similar in the products of most manufacturers. [Pg.242]

Caprolactam [105-60-2] (2-oxohexamethyleiiiiriiQe, liexaliydro-2J -a2epin-2-one) is one of the most widely used chemical intermediates. However, almost all of the aimual production of 3.0 x 10 t is consumed as the monomer for nylon-6 fibers and plastics (see Fibers survey Polyamides, plastics). Cyclohexanone, which is the most common organic precursor of caprolactam, is made from benzene by either phenol hydrogenation or cyclohexane oxidation (see Cyclohexanoland cyclohexanone). Reaction with ammonia-derived hydroxjlamine forms cyclohexanone oxime, which undergoes molecular rearrangement to the seven-membered ring S-caprolactam. [Pg.426]

Dutch State Mines (Stamicarbon). Vapor-phase, catalytic hydrogenation of phenol to cyclohexanone over palladium on alumina, Hcensed by Stamicarbon, the engineering subsidiary of DSM, gives a 95% yield at high conversion plus an additional 3% by dehydrogenation of coproduct cyclohexanol over a copper catalyst. Cyclohexane oxidation, an alternative route to cyclohexanone, is used in the United States and in Asia by DSM. A cyclohexane vapor-cloud explosion occurred in 1975 at a co-owned DSM plant in Flixborough, UK (12) the plant was rebuilt but later closed. In addition to the conventional Raschig process for hydroxylamine, DSM has developed a hydroxylamine phosphate—oxime (HPO) process for cyclohexanone oxime no by-product ammonium sulfate is produced. Catalytic ammonia oxidation is followed by absorption of NO in a buffered aqueous phosphoric acid... [Pg.430]

Homogeneous Oxidation Catalysts. Cobalt(II) carboxylates, such as the oleate, acetate, and naphthenate, are used in the Hquid-phase oxidations of -xylene to terephthaUc acid, cyclohexane to adipic acid, acetaldehyde (qv) to acetic acid, and cumene (qv) to cumene hydroperoxide. These reactions each involve a free-radical mechanism that for the cyclohexane oxidation can be written as... [Pg.381]

The oxidation of cyclohexane to a mixture of cyclohexanol and cyclohexanone, known as KA-od (ketone—alcohol, cyclohexanone—cyclohexanol cmde mixture), is used for most production (1). The earlier technology that used an oxidation catalyst such as cobalt naphthenate at 180—250°C at low conversions (2) has been improved. Cyclohexanol can be obtained through a boric acid-catalyzed cyclohexane oxidation at 140—180°C with up to 10% conversion (3). Unreacted cyclohexane is recycled and the product mixture is separated by vacuum distillation. The hydrogenation of phenol to a mixture of cyclohexanol and cyclohexanone is usually carried out at elevated temperatures and pressure ia either the Hquid (4) or ia the vapor phase (5) catalyzed by nickel. [Pg.425]

Vapor-phase oxidation of cyclohexane is commercially feasible, but the preferred route is Hquid-phase cyclohexane oxidation (2). In the latter... [Pg.425]

The alternative route involves the air oxidation of cyclohexane and proceeds via the production of a mixture of cyclohexanol and cyclohexanone often known as KA oil. It was in the cyclohexane oxidation section of the caprolactam plant of Nypro Ltd that the huge explosion occurred at Flixborough, England in 1974. [Pg.483]

B. T. Matusz and D. L. Sadler, A Comprehensive Program for Preventing Cyclohexane Oxidation Process Piping Failures, Paper presented at AIChE Loss Prevention Symposium, Houston, Texas, Mar./Apr. 1993. [Pg.164]

The production of alcohols by the catalytic hydrogenation of carboxylic acids in gas-liquid-particle operation has been described. The process may be based on fixed-bed or on slurry-bed operation. It may be used, for example, for the production of hexane-1,6-diol by the reduction of an aqueous solution of adipic acid, and for the production of a mixture of hexane-1,6-diol, pentane-1,5-diol, and butane-1,4-diol by the reduction of a reaction mixture resulting from cyclohexane oxidation (CIO). [Pg.76]

Another reaction which enjoys much commercial interest is the production of adipic acid from cyclohexane oxidation. The two types of processes that are employed commercially are outlined in Figure 24. [Pg.299]

Obviously, there is a definite need for cleaner, more efficient routes to adipic acid. The question which immediately arises is, naturally, what does the Amoco system do in cyclohexane oxidation In this context it is interesting to compare the relative oxidizabilities of toluene, cyclohexane, cyclohexanol and cyclohexanone (Table 2). [Pg.300]

Zaidi (ref. 28) has reported the autoxidation of cyclohexane in acetic acid, at 60-80 °C and 1 bar, in the presence of a Co(OAc)2/NaBr catalyst (4). Adipic acid was obtained in 31% yield. Based on the results obtained in alkylaromatic oxidations it would be interesting to try the Co/Mn/Br /HOAc system in cyclohexane oxidation. It is, however, difficult to believe that this has not already been done. [Pg.300]

CFD modeling was conducted as a real industrial ALR taken as a background -a cyclohexane oxidation airlift loop reactor. The CFD software FLUENT6.0 was used to study two-phase flow in the reactor. [Pg.525]

A schematic diagram of cyclohexane oxidation airlift loop reactor is illustrated in Fig.l. This reactor consists of outer vessel (riser), coneentric draft-tube(downcomer) and gas... [Pg.525]

Eulerian two-fluid model coupled with dispersed itequations was applied to predict gas-liquid two-phase flow in cyclohexane oxidation airlift loop reactor. Simulation results have presented typical hydrodynamic characteristics, distribution of liquid velocity and gas hold-up in the riser and downcomer were presented. The draft-tube geometry not only affects the magnitude of liquid superficial velocity and gas hold-up, but also the detailed liquid velocity and gas hold-up distribution in the reactor, the final construction of the reactor lies on the industrial technical requirement. The investigation indicates that CFD of airlift reactors can be used to model, design and scale up airlift loop reactors efficiently. [Pg.528]

Results of the cyclohexane oxidation tests are shown in Table 41.4. Mono-oxygenated products are cyclohexanone, cyclohexanol and cyclohexyl hydroperoxide. Cu and Cr were very active, but subsequent tests showed considerable leaching for both metals, whereas Co-Si-TUD-1 did not show ai r leaching. Tests with different Co loadings indicate that the lowest Co concentration has the best conversion and ketone selectivity. Isolated cobalt species are most efficient for the conversion of cyclohexane, as agglomeration of Co reduces... [Pg.374]

Selective transformations Selective styrene ring opening [103] One-pot domino process for regioselective synthesis of a-carbonyl furans [104] Tandem process for synthesis of quinoxalines [105] Atmospheric oxidation of toluene [106] Cyclohexane oxidation [107] Synthesis of imines from alcohols [108] Synthesis of 2-aminodiphenylamine [109] 9H-Fluorene oxidation [110] Dehydrogenation of ethane in the presence of C02 [111] Decomposition of methane [112] Carbon monoxide oxidation [113]... [Pg.228]

Kumar, R., Sithambaram, S. and Suib,S.L. (2009) Cyclohexane oxidation catalyzed by manganese oxide octahedral molecular sieves - effect of acidity of the catalyst. Journal of Catalysis, 262,304—313. Sithambaram, S., Kumar, R., Son, Y. and Suib, S.L. (2008) Tandem catalysis direct catalytic synthesis of imines from alcohols using manganese octahedral molecular sieves. Journal of Catalysis, 253, 269-277. [Pg.239]

LG Galimova. Mechanism of Cyclohexane Oxidation by Ozone, Thesis Dissertation, BSU, Ufa, 1975 pp 3-25 [in Russian]. [Pg.163]


See other pages where Cyclohexane oxide is mentioned: [Pg.51]    [Pg.52]    [Pg.77]    [Pg.77]    [Pg.1875]    [Pg.139]    [Pg.234]    [Pg.235]    [Pg.235]    [Pg.271]    [Pg.496]    [Pg.732]    [Pg.240]    [Pg.241]    [Pg.242]    [Pg.242]    [Pg.242]    [Pg.244]    [Pg.523]    [Pg.168]    [Pg.10]    [Pg.268]    [Pg.269]    [Pg.8]    [Pg.51]    [Pg.52]    [Pg.147]    [Pg.263]    [Pg.2340]    [Pg.243]    [Pg.98]    [Pg.143]    [Pg.235]    [Pg.410]   
See also in sourсe #XX -- [ Pg.51 , Pg.159 ]




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Adipic acid oxidizing cyclohexane

Cobalt -catalyzed oxidation of cyclohexane

Cyclohexane direct oxidation

Cyclohexane electrochemical oxidation

Cyclohexane oxidation

Cyclohexane oxidation

Cyclohexane oxidation pressure requirements

Cyclohexane oxidation process

Cyclohexane oxidation product distribution

Cyclohexane oxidation products

Cyclohexane oxidation, vanadium

Cyclohexane oxidizing

Cyclohexane photocatalytic oxidation

Cyclohexane selective oxidation

Cyclohexane, 1,2-dimethyloxidation oxidation

Cyclohexane, oxidation photochemical

Cyclohexane, oxidative dehydrogenation

Cyclohexane, oxidative dehydrogenation catalysts

Cyclohexane, oxidative dehydrogenation product selectivity

Cyclohexane-1,2-diol, oxidation

Cyclohexane-1,2-diol, oxidation adipic acid

Cyclohexane-1,3-dione, oxidation

Direct Oxidation of Cyclohexane with Air

Mesityl oxide reaction with cyclohexane

Nylon cyclohexane oxidation

Oxidation of Cyclohexane to Adipic Acid

Oxidation of cyclohexane

Oxidation of cyclohexane and cyclopentane

Oxidative Dehydrogenation of Butane and Cyclohexane

Selective oxidation of cyclohexane

Special Features of Cyclohexane Oxidation

Special Features of Cyclohexane and p-Xylene Oxidations

The Noncatalyzed DSM Oxanone Cyclohexane Oxidation Process

Traditional catalyzed cyclohexane oxidation

Traditional catalyzed cyclohexane oxidation process

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