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Productivity after acidizing

Heating nitroglycerine (particularly moist samples) at a temperature of 75°C brings about an apparent decomposition within 3-4 days characterized by the development of acid products. After 6 days the presence of HNO3 is clearly distinguishable. If the volatile products of decomposition are removed, e.g. by blowing with air, as quickly as they are developed, then only very slow decomposition of the nitroglycerine takes place. [Pg.47]

Counts of the number of S. mutans or L. casei are a poor measure of caries susceptibility because as noted above, they cannot account for ammonia production or differences in glycan production by other bacteria in the biofilms. Acid production after a 10% sucrose or glucose rinse after a 6 h or longer fast is a better measure of caries susceptibility, because it represents the balanced outcome of the factors that promote or prevent caries. Because this method requires time and skill, it is difficult to apply to many subjects. A simpler method of measuring caries susceptibility is past caries experience and age. The more teeth affected by caries in a child or adolescent, the greater is the likelihood that a new cavity will develop and, therefore, the greater is the need for preventive measures. Unfortunately, this measure is completely uninformative about what factors are present to promote or prevent caries. [Pg.280]

Aminopropanol Cleavage Weak acids Product after cleavage Ketone [33]... [Pg.173]

OZONOLYSIS OF POLYBUTADIENE (EXPECTED ACID PRODUCTS AFTER OZONE TREATMENT AND HYDROLYSIS AND OXIDATION OF OZONIDES FROM VARIOUS POLYBUTADIENE STRUCTURES) ... [Pg.117]

Such polymers contain repeat units based on ethylene glycol (and indeed other glycols such as 1, 4-butane diol) and terephthalic acid and proportions of isophthalic acid. Allen and co-workers [118] developed a precise quantitative method for determining such units in terylene. The sample is subject to an alkaline hydrolysis and glycol and acidic products after conversion to the trimethylsilyl derivatives are analysed by gas chromatography. [Pg.97]

In 1746 in Birmingham, John Roebuck adapted this method to produce sulfuric acid in lead-lined chambers, which were stronger, less expensive, and could be made larger than the previously used glass containers. This lead chamber process allowed the effective industrialization of sulfuric acid production. After several refinements, this method remained the standard for sulfuric acid production for almost two centuries. [Pg.133]

An excellent synthesis of myristic acid is thus achieved from readily accessible starting materials. An alternative synthesis of myristic acid utilises hexanoic acid (M-caproic acid n-hexoic acid) (X) (2 mols) and methyl hydrogen sebacate (XI) (1 mol) the products, after hydrolysis, are Ji-decane (XII), myristic acid (XIII) and hexadecane-1 16-dlcarboxylic acid (XIV) ... [Pg.938]

The solution leaving the flotation cell, containing about 0.4 g/L iodine, is sent to a kerosene solvent extraction process to recover the dissolved product. After neutralization with soda ash to the initial incoming alkalinity, the solution is returned to the nitrate lixiviation process. The iodine-chaiged kerosene is contacted with an acidic concentrated iodide solution containing SO2, which reduces the iodine to iodide. [Pg.362]

Fig. 1. Sulfonated and sulfated acid products viscosities after 98% conversions at varying temperatures where the vertical line indicates the maximum temperature for batch sulfonation using SO to minimi2e color deterioration lines A—C represent branched C 2 alkyl ben2ene (BAB) sulfonic acid from SO, oleum (settied), and oleum (whole mixture), respectively lines D and E, lauryl alcohol 3-ethoxylate sulfuric ester (SO ) and lauryl alcohol sulfuric ester... Fig. 1. Sulfonated and sulfated acid products viscosities after 98% conversions at varying temperatures where the vertical line indicates the maximum temperature for batch sulfonation using SO to minimi2e color deterioration lines A—C represent branched C 2 alkyl ben2ene (BAB) sulfonic acid from SO, oleum (settied), and oleum (whole mixture), respectively lines D and E, lauryl alcohol 3-ethoxylate sulfuric ester (SO ) and lauryl alcohol sulfuric ester...
Spent Sulfuric Field. Spent sulfuric acid recovered from petrochemical and refinery processes can be fed to a high temperature furnace at 870—1260°C, where it is transformed kito sulfur dioxide, water, and other gaseous products. After suitable scmbbkig and drykig, the gases are passed to a conventional contact sulfuric acid plant (263). [Pg.146]

After 30 hours, the maximum and critical fermentation is underway and the pH must remain above 4.0 for optimal fermentation. However, accompanying bacterial contamination from various sources such as yeast contamination, improper cleaning procedures, slow yeast growth, or excessive temperatures can result in a pH below 4.0. The remaining amylase enzymes, referred to as secondary conversion agents, are inactivated and can no longer convert the dextrins to maltose. Under these circumstances, the fermentor pH continues to drop because of acid production of the bacteria, and the pH can drop to as low as 3.0. The obvious result is a low ethanol yield and quaUty deterioration. [Pg.85]

The sohds are treated with hydrochloric acid at 70°C at pH 3—4. The thorium hydroxide [13825-36-0] remains iasoluble and can be filtered off. Small amounts of trace contaminants that carry through iato solutioa, such as uranium and lead as well as some thorium, are removed by coprecipitation with barium sulfate ia a deactivatioa step. The resultiag product, after SX-removal of the heavy La fractioa, is a rare-earth/lanthanide chloride,... [Pg.366]

Cesium isotopes can be recovered from fission products by digestion in nitric acid, and after filtration of waste the radioactive cesium phosphotungstate is precipitated using phosphotungstic acid. This technique can be used to prepare radioactive cesium metal or compounds. Various processes for removal of Cs isotopes from radioactive waste have been developed including solvent extraction using macrocycHc polyethers (62) or crown ethers (63) and coprecipitation with sodium tetraphenylboron (64). [Pg.379]

Monomer conversion (79) is followed by measuring the specific gravity of the emulsion. The polymerization is stopped at 91% conversion (sp gr 1.069) by adding a xylene solution of tetraethylthiuram disulfide. The emulsion is cooled to 20°C and aged at this temperature for about 8 hours to peptize the polymer. During this process, the disulfide reacts with and cleaves polysulfide chain segments. Thiuram disulfide also serves to retard formation of gel polymer in the finished dry product. After aging, the alkaline latex is acidified to pH 5.5—5.8 with 10% acetic acid. This effectively stops the peptization reaction and neutralizes the rosin soap (80). [Pg.541]

Many of these reactions occur in the course of synthesis of fully or partly unsaturated products after initial ring closure, giving rise to more unsaturated systems, e.g. in the pyrido[2,3-pipemidic acids (Section 2.15.4.1) and their derivatives, e.g. (16a) -> (17) (74JAP(K)7444000). Examples are also found in the pyrido[3,2-[Pg.205]

Amlnoacrldlne (6) 4 (37 g 0 2 mol) glycerol (150 g) formic acid (9 2 g, 0 2 mol) and cone HCI (17 ml) were healed to 155 C maintained at this temp (or 30 min and heated to 175 C (or 30 mm The product was treated with scdium acetate (10 g) in water (400 mL) After filtration of N N diphenylproflavine the filtrate was treated with NaOH solution and boiled to precipitate the crude product After recrystallization from alcohol there was obtained 6 23 g (59%), mp216°C... [Pg.32]

The reaction mixture is filtered with suction and the cake is washed thoroughly with two 200-ml. portions of glacial acetic acid (Note 4). The combined filtrate and washings are evaporated under reduced pressure on the steam bath until a thick oil, which generally partially crystallizes, remains. To purify the crude product, 100 ml. of water is added, and the flask is warmed on a steam bath until the solid melts. The mixture of water and oil is stirred rapidly in an ice bath, and diethyl acetamidomalonate crystallizes as a fine white product. After cooling in an ice bath for an additional hour, the product is collected by filtration, washed once with cold water, and dried in air at 50°. A second crop is obtained by concentrating the mother liquor under reduced pressure. The yield of diethyl acetamidomalonate, m.p. 95-97° (Note 5), is 52-53 g. (77-78%) based on malonic ester. [Pg.22]

As a preparative route to A -3-ketones, the anhydrous reaction in benzene at room temperature gives 40-55 % of product after chromatography and is inferior to a stepwise conversion (via A -3-ketone). The principal side reaction (which also occurs in the acid catalyzed reaction of A -3-ketones with two moles of DDQ) appears to be addition of the hydroquinone ... [Pg.312]


See other pages where Productivity after acidizing is mentioned: [Pg.272]    [Pg.386]    [Pg.87]    [Pg.87]    [Pg.256]    [Pg.95]    [Pg.340]    [Pg.139]    [Pg.272]    [Pg.386]    [Pg.87]    [Pg.87]    [Pg.256]    [Pg.95]    [Pg.340]    [Pg.139]    [Pg.618]    [Pg.878]    [Pg.976]    [Pg.178]    [Pg.449]    [Pg.339]    [Pg.301]    [Pg.34]    [Pg.38]    [Pg.49]    [Pg.51]    [Pg.23]    [Pg.58]    [Pg.834]    [Pg.444]    [Pg.275]    [Pg.206]    [Pg.611]    [Pg.297]    [Pg.222]    [Pg.50]    [Pg.233]    [Pg.152]    [Pg.280]   
See also in sourсe #XX -- [ Pg.50 ]

See also in sourсe #XX -- [ Pg.50 ]




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