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Control of fluorination

This method of low-temperature, direct fluorination involves very precise control of fluorine concentrations during the reaction, and initial high dilution of the fluorine with helium. The reaction of elemental fluorine with organometallic compounds is conducted (27) in a cryogenic-zone reactor (see Fig. 8) at temperatures in the range of - 78 to... [Pg.197]

We cannot predict the act for the highly exothermic attack of fluorine atoms on methane, but we would certainly not expect it to be any larger than for the attack of chlorine atoms on methane. It appears actually to be smaller (about 1 kcal), thus permitting even longer chains. Because of the surprising weakness of the fluorine-fluorine bond, fluorine atoms should be formed faster than chlorine atoms thus there should be not only longer chains in fluorination but also more chains. The overall reaction is extremely exothermic, with a A// of —102 kcal, and the difficulty of removing this heat is one cause of the difficulty of control of fluorination. [Pg.61]

Robertson, F.N. (1984) Solubility controls of fluorine, barium and chromium in ground water in alluvial basins of Arizona. Geological Survey Tucson, Water Resources Division. In First Canadian/American Conference on Hydrogeology Practical Applications of ground water geochemistry, 22-26 June 1984, Banff, Alberta, Canada, pp. 96-102. [Pg.73]

Fig. 5 Process control of fluorine treatment. Pressure Unit 1000mbar= 14.7 psi. Stage I Evacuation. Stage II Inlet Fluorine. Stage III Treatment, and Stages IV, V, VI Flushing. (Courtesy of Fluor Technik GmbH, Lauterbach, Germany.)... Fig. 5 Process control of fluorine treatment. Pressure Unit 1000mbar= 14.7 psi. Stage I Evacuation. Stage II Inlet Fluorine. Stage III Treatment, and Stages IV, V, VI Flushing. (Courtesy of Fluor Technik GmbH, Lauterbach, Germany.)...
The overall reaction under controlled conditions provides a method for the disposal of fluorine by conversion to a salt ... [Pg.124]

Ammonia. Ammonia (qv) reacts with excess fluorine ia the vapor phase to produce N2, NF, N2F2, HF, and NH F. This reaction is difficult to control ia the vapor phase because of the iatense heat of reaction, and ia some cases only N2 and HF are produced. Nitrogen trifluoride was obtained ia 6% yields ia a gas-phase reaction over copper (42). Yields of ca 60% are achieved by the reaction of fluorine and ammonia ia a molten ammonium acid fluoride solution (43,44). [Pg.124]

The large amount of fluorine values released from phosphate rock in the manufacture of fertilisers (qv) gives a strong impetus to develop fluorine chemicals production from this source (see Phosphoric acid and the phosphates). Additional incentive comes from the need to control the emission of fluorine-containing gases. Most of the fluorine values are scmbbed out as fluorosiUcic acid, H2SiPg, which has limited useflilness. A procedure to convert fluorosihcic acid to calcium fluoride is available (61). [Pg.173]

Chlorine Trifluoride. Chlorine trifluoride is produced commercially by the continuous gas-phase reaction of fluorine and chlorine ia a nickel reactor at ca 290°C. The ratio of fluorine to chlorine is maintained slightly in excess of 3 1 to promote conversion of the chlorine monofluoride to chlorine trifluoride. Sufficient time ia the reactor must be provided to maintain high conversions to chlorine trifluoride. Temperature control is also critical because the equiHbrium shift of chlorine trifluoride to chlorine monofluoride and fluorine is significant at elevated temperatures. [Pg.186]

Molybdenum hexafluoride can be prepared by the action of elemental fluorine on hydrogen-reduced molybdenum powder (100—300 mesh (ca 149—46 l-lm)) at 200°C. The reaction starts at 150°C. Owing to the heat of reaction, the temperature of the reactor rises quickly but it can be controlled by increasing the flow rate of the carrier gas, argon, or reducing the flow of fluorine. [Pg.212]

Chemical precipitation and solvent extraction are the main methods of purifying wet-process acid, although other techniques such as crystallisa tion (8) and ion exchange (qv) have also been used. In the production of sodium phosphates, almost all wet-process acid impurities can be induced to precipitate as the acid is neutralized with sodium carbonate or sodium hydroxide. The main exception, sulfate, can be precipitated as calcium or barium sulfate. Most fluorine and siUca can be removed with the sulfate filter cake as sodium fluorosiUcate, Na2SiFg, by the addition of sodium ion and control of the Si/F ratio in the process. [Pg.328]

The significance of such rudimentary probes of mechanistic pathways rests with their dispelling the myth of fluorine s unpredictability In fact, fluorine, though highly reactive and with few activation barriers is highly predictable if the energy density (exothermicity per unit volume) of its reactions can be controlled so as not to disturb the integrity of the substrates with which it reacts Precise control of... [Pg.108]

The strength of the carbon-carbon bond adjacent to a difluoromethylene group IS hardly affected by the presence of fluorine on the cyclopropyl ring When heated, 2,2 difluoromethylenecyclopropane undergoes methylene-cyclopropane rearrangement [/2 ] Under kinetic control, 2,2 difluoro 1 methylenecyclopropane and (difluoromethylene)cyclopropane are formed in a 2 1 ratio, although the latter IS slightly more stable [129] (equation 27)... [Pg.922]

Enzyme-controlled transformations of fluorinated heterocycles 97MI32. [Pg.208]

The introduction of the halogens onto aromatic rings by electrophilic substitution is an important synthetic procedure. Chlorine and bromine are reactive toward aromatic hydrocarbons, but Lewis acid catalysts are normally needed to achieve desirable rates. Elemental fluorine reacts very exothermically and careful control of conditions is required. Molecular iodine can effect substitution only on very reactive aromatics, but a number of more reactive iodination reagents have been developed. [Pg.1008]

The use of plant extracts for insect control dates into antiquity the use of Paris green as an insecticide for control of the Colorado potato beetle in 1867 probably marks the beginning of the modern era of chemical control of injurious insects. The development of lead arsenate followed later in the nineteenth century for gypsy moth control. The commercial production of nicotine insecticides, the production of calcium arsenate at the time of the first world war, and the use of fluorine, arsenical, and cyanide compounds, as well as other inorganic chemicals for insect control, were important steps in pest control. These chemicals were applied largely by dilute high pressure sprays or dusts. [Pg.218]

Lipophilicity is an important consideration in the design of biologically active compounds because it often controls absorption, transport, or receptor binding that is, it is a property that can enhance the bioavailability of a compound. The presence of fluorine in a substituent gives rise to enhanced lipophilicity. [Pg.16]

Ans. The only oxidation state of fluorine in a compound is -1 it is the most electronegative element. (It always has control of any shared electrons, except in the element, F2.)... [Pg.227]

Dining the fluorination of organic materials by passing hydrogen fluoride into a vigorously stirred suspension of the oxide (to form transiently mercury difluoride, a powerful fluorinator), it is essential to use adequate and effective cooling below 0°C to prevent loss of control of the reaction system. [Pg.1506]

Dining interaction at ambient temperature in a bomb to produce poly (carbon monofluoride), admission of fluorine beyond a pressure of 13.6 bar must be extremely slow and carefully controlled to avoid a violently exothermic explosion [1], Previously it had been shown that explosive interaction of carbon and fluorine was due to the formation and decomposition of the graphite intercalation compound, poly (carbon monofluoride) [2], Presence of mercury compounds prevents explosion during interaction of charcoal and fluorine [3], Reaction of surplus fluorine with graphite or carbon pellets was formerly used as a disposal method, but is no longer recommended. Violent reactions observed when an exhausted trap was opened usually involved external impact on the metal trap, prodding the trap contents to empty the trap, or possibly ingress of moist air... [Pg.1513]


See other pages where Control of fluorination is mentioned: [Pg.194]    [Pg.570]    [Pg.36]    [Pg.883]    [Pg.540]    [Pg.194]    [Pg.570]    [Pg.36]    [Pg.883]    [Pg.540]    [Pg.124]    [Pg.124]    [Pg.125]    [Pg.127]    [Pg.128]    [Pg.268]    [Pg.269]    [Pg.275]    [Pg.276]    [Pg.277]    [Pg.278]    [Pg.283]    [Pg.290]    [Pg.462]    [Pg.102]    [Pg.954]    [Pg.956]    [Pg.454]    [Pg.98]    [Pg.997]    [Pg.303]    [Pg.277]    [Pg.117]    [Pg.86]   


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