Cyclohexanone to adipic acid. US3361806A 2022-10-15

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The Industrial Revolution, which took place from the 18th to 19th centuries, was a period of significant economic and social change. It marked a shift from an agrarian and handicraft economy to one dominated by industry and machine manufacturing. While the Industrial Revolution brought about many positive changes, it also had negative impacts on society and the environment.

One positive aspect of the Industrial Revolution was the increase in productivity and efficiency. The use of machinery and the division of labor allowed for goods to be produced more quickly and at a lower cost. This led to an increase in the standard of living for many people, as they were able to purchase more goods and services at lower prices. The Industrial Revolution also created new job opportunities and industries, allowing people to move from rural areas to urban centers in search of work.

Another positive impact of the Industrial Revolution was the development of new transportation and communication systems. The steam engine and the railroad allowed for the rapid movement of goods and people, and the telegraph allowed for faster communication over long distances. These advancements facilitated trade and helped to integrate global markets.

However, the Industrial Revolution also had negative impacts on society and the environment. One negative aspect was the exploitation of labor, as factory owners often paid low wages and provided poor working conditions for their employees. Children and women were often employed in factories, and they often worked long hours in hazardous conditions. The Industrial Revolution also led to the rise of urbanization, as people moved from rural areas to urban centers in search of work. This led to overcrowding and poor living conditions in cities, as there was often a lack of adequate housing and sanitation.

Another negative impact of the Industrial Revolution was the pollution of the environment. The use of coal as an energy source led to air pollution, and the disposal of waste in rivers and streams led to water pollution. The Industrial Revolution also had a negative impact on agriculture, as the demand for factory goods led to the enclosure of land, resulting in the displacement of small farmers.

In conclusion, the Industrial Revolution brought about many positive changes, such as increased productivity and efficiency, the development of new transportation and communication systems, and the creation of new job opportunities and industries. However, it also had negative impacts on society and the environment, including the exploitation of labor, overcrowding and poor living conditions in cities, and pollution of the environment.

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cyclohexanone to adipic acid

The first option is improvement for N 2 O decomposition in special designed boilers. The catalyst will, at least in part, be present as the cobalt salt of adipic, glutaric and succinic acids. Also, estimated atmospheric lifetime of N 2 O is 150 years. The time between the start of oxygen absorption and when the reaction mixture is withdrawn from the reaction conditions is defined as reaction time. Description This invention relates to a process for converting cyclohexane to adipic acid which comprises oxidizing cyclohexane with molecular oxygen in the presence of critical amounts of cobaltic ions and selected amounts of added water in an aliphatic monobasic acid while maintaining critical temperature and pressure in the reaction zone.

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US3361806A

cyclohexanone to adipic acid

Such pressures, moreover, are sufficient to maintain the reactants in the liquid phase. A process for converting cyclohexane to adipic acid in a system consisting essentially of cyclohexane, an aliphatic monobasic acid solvent, cobaltic ions and molecular oxygen, which comprises subjecting cyclohexane to oxidation with oxygen in the presence of cobaltic ions in an aliphatic monobasic acid having only primary and secondary hydrogen atoms and having two to eight carbon atoms, wherein at least about 25 millimols of cobalt are present per mol of cyclohexane, while maintaining a temperature of about 85° to about 105° C. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed. Estimated current global production of adipic acid is at 1. Another critical requirement herein in obtaining high conversions of cyclohexane to adipic acid is the partial pressure of oxygen over the reaction mixture. R Chin, PEP abstract: Adipic acid, September 1996.

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Preparation OF Adipic ACID FROM Cyclohexene

cyclohexanone to adipic acid

The large amount of adipic acid production per year, due to the common product that it produces, has led to an enormous amount of this greenhouse gas to be emitted. Above three hours only small amounts of additional conversion of cyclohexane was found and this was accompanied by the tendency of adipic acid to degrade to glutaric and succinic acid. Approximately 10% of the cyclohexane is converted to oil containing cyclohexanone, cyclohexanol and oxygenated compounds. Device for detecting formation of a second liquid phase US6288270B1 en 1996-06-24 2001-09-11 Rpc Inc. RESULTS AND ANALYSIS Tabulated results obtained from the procedure, including any necessary computations made with respect to the data is shown below. A process for the production of adipic acid from cyclohexane including the steps of contacting cyclohexane with molecular oxygen as the essential oxidant in a first oxida tion zone to produce a mixture of cyclohexanone, cyclohexanol and oxygenated products, separating unreacted cyclohexane and recycling it to said first contacting zone, oxidizing said mixture in a second oxidation zone with nitric acid and a catalyst or with molecular oxygen in the presence of a catalyst chosen from the group consisting of manganese and copper, and separating adipic acid therefrom, including the improvement which comprises conducting the first step for an initial period of from to about 45 min.

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US4263453A

cyclohexanone to adipic acid

Time between the moment when the reaction mixture is brought to the defined temperature and pressure levels and when oxygen absorption begins indicating the start of oxidation is defined as the induction period. In general, the reaction time will be at least about one hour but no more than about four hours. This cleavage of an alkene double bond, generally accomplished in good yield, is calledozonolysis. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed. To recover these acids from the catalyst, the catalyst is treated with sodium hydroxide to release the chemically-bound acids from the catalyst, at the same time converting the cobalt salt to its hydroxide or oxide state.

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Adipic Acid Production Cyclohexane Reaction, Sample of Essays

cyclohexanone to adipic acid

Chemical gas was used on both sides of the line, which turned out to be fatal for many. . It was observed in the experiment that the flask used was completely covered with the brown color Manganese dioxide MnO2. It is apparent from the above data that whatever additional water is introduced into the system by way of the cobalt salt that the addition of selected amounts of free water at the beginning of the operation is required to increase the yields of adipic acid. Another critical requirement herein in obtaining high conversions of cyclohexane to adipic acid is the partial pressure of oxygen over the reaction mixture.

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US4032569A

cyclohexanone to adipic acid

The main reaction is by the oxidation of cyclohexane into cyclohexanol and cyclohexanone. In order to assist in obtaining the high conversions herein, the amount of cobalt present in the reaction mixture is critical and must be in excess of about 25 millimols of cobalt per mol of cyclohexane, preferably in the range of about 50 to about 100 millimols of cobalt per mol of cyclohexane. This period of induction is believed to occur in order to oxidize the cobaltous ion to the active cobaltic ion and to promote the production of free radicals from the cyclohexane charge. Thus, either air or oxygen itself can be employed. In the present process, because of the presence of added water, reaction time is not critical and no appreciable degradation of adipic acid to glutaric or succinic acid occurs. Recovery of these acids is effected by evaporating the solution to dryness and then extracting the residue with acetone to separate the acids from sodium chloride. The flask was then rinsed with a second portion of 10 mL of 1% sodium hydroxide solution.

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cyclohexanone to adipic acid

The other possible use of NaOH is the neutralization of formic acid which was formed during the oxidation of methanol. Other industrial uses of adipic acid are the production of adhesives, plasticizers, gelatinizing agents,hydraulic fluids,lubricants,emollients, polyurethane foams,leather tanning, urethane and also as anacidulantin foods. The molar ratios of solvent to cyclohexane lie between about 1. The average concentration of oxygen in the vent gas during oxidation is 18%, an explosion hazard. When the reaction mixture is permitted to remain at reaction conditions for periods in excess of those defined, the amount of additional conversion obtained is small and there is a tendency for the desired adipic acid to degrade to glutaric and succinic acids.

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cyclohexanone to adipic acid

While the addition of even very small amounts of water to the reaction zone at the beginning of the process will be sufficient to obtain an increase in yield of adipic acid, we generally add at least about 0. The products obtained were then subjected to recovery procedures as defined above. There is a possibility that the pH was higher than required and therefore favoring oxidation of unsaturated groups rather than the target alcohol methanol. . The greenhouse gas is specifically N 2 O.

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cyclohexanone to adipic acid

The catalyst can also be treated with concentrated hydrochloric acid and on evaporation to dryness will result in the formation of free organic acids and inorganic salts. The acid was collected by vacuum filtration. The second temperature must be at least 5 C. . The amount of initiator can vary between about 0.

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