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Temperature carbon dioxide water solubility

Carbon dioxide (C02, melting point -56.6°C at 76 psi - 527 kPa, density 1.9769 gL at 0°C) is a colorless, odorless gas. Solid carbon dioxide sublimes at -79°C (critical pressure 1073 psi, 7397 kPa, critical temperature 31°C). High concentrations of the gas do cause stupefaction and suffocation because of the displacement of ample oxygen for breathing. Carbon dioxide is soluble in water (approximately 1 volume carbon dioxide in 1 volume water at 15°C), soluble in alcohol, and is rapidly absorbed by most alkaline solutions. [Pg.147]

At ambient temperature, carbon dioxide is three to five times more soluble in most organic solvents than in water (Table I). The differences among polar (e.g. methanol, = 0.139) and nonpolar (e.g. carbon tetrachloride, % = 0- 094) solvents are small. Two solvents which have recently been of practical interest in removing carbon dioxide from natural gas are propylene carbonate ( ) and monoethanolamine (10) - this last ought to be classified as an acid-base reaction. Judging from the number of entries in the 10th collective index to Chemical Abstracts, there is a substantial chemical engineering literature on this topic. [Pg.11]

Carbon dioxide, like sodium chloride, is also a compound, but its properties differ from those of sodium chloride. For example, salt is a solid at room temperature, but carbon dioxide is a colorless, odorless, and tasteless gas. When carbon dioxide is cooled below — 80°C, the gas changes directly to white, solid carbon dioxide without first becoming a liquid. Because the solid form of carbon dioxide does not melt to a liquid, it is called dry ice, as shown in Figure 4.4. Carbon dioxide is soluble in water, as anyone who has ever opened a carbonated beverage knows. A water solution of carbon dioxide is a weak conductor of electricity. You can make carbon dioxide from its elements by burning carbon in air. Coal and charcoal are mostly carbon. [Pg.124]

The carbon dioxide/water biphasic system is an example of binary mixtures consisting of components with widely separated critical temperatures. The critical properties of the pure compounds are given in Table 1. The typical phase diagram for such mixtures can be complex, including the possibility for areas of three-phase coexistence (LEV). For applications in biphasic catalysis, however, the key parameters to be discussed are solubility and cross-contamination, mass transfer, and chemical changes. [Pg.717]

Polylactic acid (PLA) is fully biodegradable when composted in a large-scale operation with temperatures of 60°C and above. The first stage of degradation of PLA (two weeks) is via hydrolysis to water soluble compounds and lactic acid, then metabolization by microorganisms into carbon dioxide, water and biomass proceeds [20]. [Pg.131]

Figure 1.3 Phase behaviour of carbon dioxide/water system at temperatures between the critical hydrate temperature and the upper critical solution temperature, (a) Typical pressure/composi-tion diagram for carbon dioxide/water (a Class B2 system) at temperatures below the critical temperature of carbon dioxide but above the critical hydrate formation temperature. Data for arms B and C are shown in (b) and (c) respectively, (b) Solubility of liquid CO2 in water as a function of temperature and pressure (arm C in (a)), (c) Solubility of water in liquid CO2 as a function of temperature and pressure (arm B in (a)), (d) The three phase pressure curve compared with the vapour pressure curve of carbon dioxide showing the critical locus CsU (i.e. locus of points such as C on (e) where vapour properties merge with those of solvent-rich liquid). (Data reference [75].) (e) Detail of the isothermal pressure/composition diagram at 25°C (on left) and at temperature between Tc and Tu (on right). Subscripts 1 and 2 denote water-rich and C02-rich phase. Critical point C is shown as blocked-in circle. (Data reference for (b) and (c) is [81].)... Figure 1.3 Phase behaviour of carbon dioxide/water system at temperatures between the critical hydrate temperature and the upper critical solution temperature, (a) Typical pressure/composi-tion diagram for carbon dioxide/water (a Class B2 system) at temperatures below the critical temperature of carbon dioxide but above the critical hydrate formation temperature. Data for arms B and C are shown in (b) and (c) respectively, (b) Solubility of liquid CO2 in water as a function of temperature and pressure (arm C in (a)), (c) Solubility of water in liquid CO2 as a function of temperature and pressure (arm B in (a)), (d) The three phase pressure curve compared with the vapour pressure curve of carbon dioxide showing the critical locus CsU (i.e. locus of points such as C on (e) where vapour properties merge with those of solvent-rich liquid). (Data reference [75].) (e) Detail of the isothermal pressure/composition diagram at 25°C (on left) and at temperature between Tc and Tu (on right). Subscripts 1 and 2 denote water-rich and C02-rich phase. Critical point C is shown as blocked-in circle. (Data reference for (b) and (c) is [81].)...
As seen in chapter 1 the system carbon dioxide/water is a Class B2 system (Figure 1.6) and this is almost certainly true also of mixtures of carbon dioxide with the natural oils (Figure 1.8). Such systems show low mutual solubilities with the liquid solvent below its critical temperature and form open loop pressure/composition diagrams for a small range of temperatures above the solvent critical temperature. [Pg.185]

In contact with the atmosphere, water dissolves a certain number of gases, mainly oxygen and carbon dioxide. Their solubility decreases with increasing temperature (Table D.1.2). Sulphur dioxide (SO2), hydrogen sulphide (H2S), and ammonia (NH3) can also be found, in general as minute traces, except in wastewater where they are in high concentrations. [Pg.301]

As with the hydroxides, we find that whilst the carbonates of most metals are insoluble, those of alkali metals are soluble, so that they provide a good source of the carbonate ion COf in solution the alkali metal carbonates, except that of lithium, are stable to heat. Group II carbonates are generally insoluble in water and less stable to heat, losing carbon dioxide reversibly at high temperatures. [Pg.132]

To obtain crystalline perbenzoic acid, dry the moist chloroform solution with a little anhydrous sodium or magnesium sulphate for an hour, filter, and wash the desiccant with a little dry chloroform. Remove the chloroform under reduced pressure at the ordinary temperature whilst carbon dioxide is introduced through a capillary tube. Dry the white or pale yellow residue for several hours at 30-35° under 10 mm. pressure. The yield of crystalline perbenzoic acid, m.p. about 42°, which is contaminated with a little benzoic acid, is 22 g. It is moderately stable when kept in the dark in a cold place it is very soluble in chloroform, ethyl acetate and ether, but only shghtly soluble in cold water and in cold hght petroleum. [Pg.809]

The use of accurate isotope ratio measurement is exemplified here by a method used to determine the temperature of the Mediterranean Sea 10,000 years ago. It is known that the relative solubility of the two isotopic forms of carbon dioxide COj) in sea water depends on temperature... [Pg.340]

One method for measuring the temperature of the sea is to measure this ratio. Of course, if you were to do it now, you would take a thermometer and not a mass spectrometer. But how do you determine the temperature of the sea as it was 10,000 years ago The answer lies with tiny sea creatures called diatoms. These have shells made from calcium carbonate, itself derived from carbon dioxide in sea water. As the diatoms die, they fall to the sea floor and build a sediment of calcium carbonate. If a sample is taken from a layer of sediment 10,000 years old, the carbon dioxide can be released by addition of acid. If this carbon dioxide is put into a suitable mass spectrometer, the ratio of carbon isotopes can be measured accurately. From this value and the graph of solubilities of isotopic forms of carbon dioxide with temperature (Figure 46.5), a temperature can be extrapolated. This is the temperature of the sea during the time the diatoms were alive. To conduct such experiments in a significant manner, it is essential that the isotope abundance ratios be measured very accurately. [Pg.341]

Triiodoacetic acid [594-68-3] (I CCOOH), mol wt 437.74, C2HO2I3, mp 150°C (decomposition), is soluble in water, ethyl alcohol, and ethyl ether. It has been prepared by heating iodic acid and malonic acid in boiling water (63). Solutions of triiodoacetic acid are unstable as evidenced by the formation of iodine. Triiodoacetic acid decomposes when heated above room temperature to give iodine, iodoform, and carbon dioxide. The sodium and lead salts have been prepared. [Pg.90]

Basic zirconium carbonate reacts with sodium or ammonium carbonate solutions to give water-soluble double carbonates. The ammonium double carbonate is nominally NH4[Zr20(0H)2(C02)3]. These solutions are stable at room temperature, but upon heating they lose carbon dioxide and hydrous zirconia precipitates. [Pg.437]

The solubility of carbon dioxide in water is given in Figure 1 (11). Over the temperature range 273—393 K, the solubiUties at pressures below 20 MPa (200 atm) decrease with increasing temperature. From 30 to 70 MPa (300—700 atm) a solubiUty minimum is observed between 343 and 353 K, with solubihties increasing as temperature increases to 393 K. Information on the solubiUty of carbon dioxide in pure water and synthetic seawater over the range 268 to 298 K and 101—4,500 kPa pressure (1—44 atm) is available (12,13). [Pg.19]

Table 21.22 Saturated solubilities of atmospheric gases in sea-water at various temperatures Concentrations of oxygen, nitrogen and carbon dioxide in equilibrium with 1 atm (lOI 325 N m ) of designated gas... Table 21.22 Saturated solubilities of atmospheric gases in sea-water at various temperatures Concentrations of oxygen, nitrogen and carbon dioxide in equilibrium with 1 atm (lOI 325 N m ) of designated gas...
The solubility of carbon dioxide in water depends on the pressure and temperature. The relationship between temperature and pressure for 3.5 and 5 volumes is shown in Figure 17.4. It will also be affected by the amount of air already dissolved in the water. The raw water is therefore carefully filtered and de-oxygenated under vacuum before the sugars and flavourings are added. [Pg.199]

The deprotection of carbobenzyloxy protected phenylalanine was carried out in a low-pressure test unit (V= 200 ml) equipped with a stirrer, hydrogen inlet and gas outlet. The gas outlet was attached to a Non Dispersive InfraRed (NDIR) detector to measure the carbon dioxide. During the reaction the temperature was kept at 25 °C at a constant agitation speed of 2000 rpm. In a typical reaction run, 10 mmol of Cbz protected phenylalanine and 200 mg of 5%Pd/C catalyst were stirred in a mixture of 70 ml ethanol/water (1 1). The Cbz protected phenylalanine is not water-soluble but is quite soluble in alcoholic solvents conversely, the water-soluble deprotected phenylalanine is not very soluble in alcoholic solvents. Thus, the two solvent mixture was used in order to keep the entire reaction in the solution phase. Twenty p.1 of the corresponding modifier was added to the reaction mixture, and hydrogen feed was started. The hydrogen flow into the reactor was kept constant at 500 ml/minute and the progress of the reaction was monitored by the infrared detection of C02 in the off-gas. [Pg.497]

Figure 3.1.1 The solubility of gaseous carbon dioxide in water as a function of both temperature and pressure. The CO2 solubility is expressed in terms of the mole fraction of carbon dioxide in the liquid solution. Figure 3.1.1 The solubility of gaseous carbon dioxide in water as a function of both temperature and pressure. The CO2 solubility is expressed in terms of the mole fraction of carbon dioxide in the liquid solution.
Both of these facts are employed in the carbonation process of sodas and beer and some sparkling wines. Low-temperature conditions and CO2 pressures of 3 to 4 atm are used to enhance the dissolution of carbon dioxide gas in water. The graph in Fig. 3.1.1 presents the solubility of carbon dioxide in water at various temperatures and pressures. The parameter used to express CO2 solubility is... [Pg.12]

Solubility of Carbon Dioxide in Water at Various Temperatures and Pressures, in Handbook of Chemistry and Physics, 74th ed., ed. David R. Lide (Boca Raton, FL, CRC Press 1993), 6-7. [Pg.13]

If global warming raises the temperature of surface waters and carbon dioxide continues to build up in the atmosphere, the carbon dioxide is less soluble in warmer water. The dissolved carbon dioxide can easily move back into the atmosphere unless it is taken up by marine plants or combines with a molecule of carbonate. But, the ocean s supply of carbonate is limited and is replenished only slowly as it is washed into the oceans by rivers that erode carbonate-containing rocks such as limestone. By absorbing two billion tons of carbon from the atmosphere each year, the ocean is depleting its buffer carbonate supply. [Pg.59]


See other pages where Temperature carbon dioxide water solubility is mentioned: [Pg.1057]    [Pg.5]    [Pg.595]    [Pg.448]    [Pg.513]    [Pg.8]    [Pg.17]    [Pg.499]    [Pg.386]    [Pg.389]    [Pg.137]    [Pg.2339]    [Pg.1042]    [Pg.1327]    [Pg.33]    [Pg.292]    [Pg.829]    [Pg.25]    [Pg.401]    [Pg.12]    [Pg.924]    [Pg.325]    [Pg.334]    [Pg.750]    [Pg.122]    [Pg.5]    [Pg.191]    [Pg.256]   


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Carbon dioxide solubility

Carbon dioxide temperatures

Carbon solubility

Carbon temperature

Carbonated waters

Dioxide - Water

Solubility of Carbon Dioxide in Water Various Temperatures and

Solubility of Carbon Dioxide in Water at Various Temperatures and Pressures

Solubility temperature

Temperature soluble

Temperature water solubility

Water carbon dioxide

Water carbon)

Water temperatures

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