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Carbonate removal device

Carbon dioxide removal can be carried out with a CRD 300, which consists of a gas-permeable membrane with a silicone coating of about 1-2 pm thickness that is selective to carbon dioxide (Figure 3.113) [100]. The special selectivity of this membrane eliminates the possibility of the loss of volatile organic acids, which was characteristic of some older design carbonate removal devices. CRD 300 is plumbed between the membrane suppressor and the conductivity cell. The regenerant channel that encloses the CRD 300 membrane is flushed with a solution of c = 0.2 mol/L NaOH that aids the removal of carbon dioxide as carbonate. The CRD 300 removes carbonic acid as carbon dioxide from the suppressed eluent as per the following equilibrium... [Pg.166]

Phesatcha, T., Worawirunwong, W., and Rohrer, J. (2012) Application Note No. 208 Determination of Bromate in Bottled Mineral Water Using the CRD 300 Carbonate Removal Device. Thermo Fisher Scientific, Sunnyvale, CA,... [Pg.1462]

In spite of a few minor operating problems, the DSHS tests appeared to have been successful. All materials, pallets, carbon, and DPE suit material were reduced to the size specified for feeding to the SCWO system the metal removal devices appear to have performed well, and fugitive dust appears to have been controlled. The size reduction of the DPE suit material was of special interest because the technology for heavy polymeric composites is comparatively new. [Pg.134]

Adsorptive Processes. The use of activated carbon, sprayed into a dry/semi dry scrubbing unit along with lime or less frequently packed in an adsorption unit positioned after the particulate removal device and prior to the stack, has become a standard component in gas cleaning trains as a means of PCDD/F control on all sizes of plant fed with MSW or clinical waste. Other adsorptive media such as zeolites are also being tested. The inclusion of an adsorptive device in combustion systems fired with wood and agricultural wastes is not normally contemplated, and as noted above, an interesting issue to be resolved is whether different waste types generate flyash of different activities relative to PCDD/F formation. [Pg.176]

E. V. Pavlov, Y. A. Skryabin, Method for Removal of Impurity of Non-Diamond Carbon and Device for Its Realization, 1994 Russia.RU2019502... [Pg.389]

Cox, C.S., Zwischenberger, J.B., Traber, L.D., Traber, D.L., and Herndon, D.N. 1991. Use of an intravascular oxygenator/carbon dioxide removal device in an ovine smoke inhalation injury model. ASAIO Tram. 37(3) M411-13. [Pg.1577]

Livigni, S. et al. 2006. Efficacy and safety of a low-flow veno-venous carbon dioxide removal device Results of an experimental study in adult sheep. Crit Care 10(5) R151. [Pg.1578]

Zwischenberger, J.B., Tao, W. and Bidani, A. 1999. Intravascular membrane oxygenator and carbon dioxide removal devices A review of performance and improvements. ASAIO f 45(l) 41-46. [Pg.1581]

In a 1 litre round-bottomed flask provided with an efficient double surface condenser, place 40 g. (39 ml.) of aniline, 50 g. (40 ml.) of carbon sulphide CAUTION inflammable) (1), and 50 g. (63-5 ml.) of absolute ethyl alcohol (2). Set up the apparatus in the fume cupboard or attach an absorption device to the top of the condenser (see Fig. 11, 8, 1) to absorb the hydrogen sulphide which is evolved. Heat upon an electrically-heated water bath or upon a steam bath for 8 hours or until the contents of the flask sohdify. When the reaction is complete, arrange the condenser for downward distillation (Fig. 11, 13, 3), and remove the excess of carbon disulphide and alcohol (CA UTION inflammable there must be no flame near the receiver). Shake the residue in the flask with excess of dilute hydrochloric acid (1 10) to remove any aniline present, filter at the pump, wash with water, and drain well. Dry in the steam oven. The yield of crude product, which is quite satisfactory for the preparation of phenyl iao-thiocyanute (Section IV.95), is 40-45 g. Recrystalhse the crude thiocarbanihde by dissolving it, under reflux, in boiling rectified spirit (filter through a hot water funnel if the solution is not clear), and add hot water until the solution just becomes cloudy and allow to cool. Pure sj/m.-diphenylthiourea separates in colourless needles, m.p, 154°,... [Pg.642]

Another strategic device applies specifically to polycyclic compounds. In the interests of simplification we want to remove some of the rings and give an intermediate with a famihar ring structure. We can do this by the common atom approach. In TM 329, mark all the carbon atoms which belong to more than one ring - the common atoms . [Pg.107]

The scrubbing liquid must be chosen with specific reference to the gas being removed. The gas solubility in the liquid solvent should be high so that reasonable quantities of solvent are required. The solvent should have a low vapor pressure to reduce losses, be noncorrosive, inexpensive, nontoxic, nonflammable, chemically stable, and have a low freezing point. It is no wonder that water is the most popular solvent used in absorption devices. The water may be treated with an acid or a base to enhance removal of a specific gas. If carbon dioxide is present in the gaseous effluent and water is used as the scrubbing liquid, a solution of carbonic acid will gradually replace the water in the system. [Pg.478]

Catalytic Converter an air pollution abatement device that removes pollutants from motor vehicle exhaust either by oxidizing them into carbon dioxide and water or reducing them to nitrogen. A typical catalytic oxidizer for auto emission control is illustrated in the sidebar figure. [Pg.524]

The second method used to reduce exliaust emissions incorporates postcombustion devices in the form of soot and/or ceramic catalytic converters. Some catalysts currently employ zeolite-based hydrocarbon-trapping materials acting as molecular sieves that can adsorb hydrocarbons at low temperatures and release them at high temperatures, when the catalyst operates with higher efficiency. Advances have been made in soot reduction through adoption of soot filters that chemically convert CO and unburned hydrocarbons into harmless CO, and water vapor, while trapping carbon particles in their ceramic honeycomb walls. Both soot filters and diesel catalysts remove more than 80 percent of carbon particulates from the exliatist, and reduce by more than 90 percent emissions of CO and hydrocarbons. [Pg.335]

Both carbon tetrachloride, CC1, (used in dry cleaning and in some lire extinguishers) and mercury, Hg, are liquids whose vapors are poisonous to breathe. If CCh is spilled, the danger can be removed merely by airing the room overnight but if mercury is spilled, it is necessary to pick up the liquid droplets with a vacuum cleaner device. Explain. [Pg.82]


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Carbonate removal

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