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Hemihydrate, 3.25

In this experiment students synthesize basic copper(ll) carbonate and determine the %w/w Gu by reducing the copper to Gu. A statistical analysis of the results shows that the synthesis does not produce GUGO3, the compound that many predict to be the product (although it does not exist). Results are shown to be consistent with a hemihydrate of malachite, Gu2(0H)2(G03) I/2H2O, or azurite, GU3(0H)2(G03)2. [Pg.97]

The selection of a process can be complex, requiring carehil evaluation of the many variables for each appHcation. The hemihydrate process is energy efficient, but this may not be an overriding consideration when energy is readily available from an on-site sulfuric acid plant. The energy balance in the total on-site complex may be the determining factor. [Pg.226]

Extensive hydrogen bonding takes place in phosphoric acid solutions. In concentrated (86% H PO solutions, as well as in the crystal stmctures of the anhydrous acid and the hemihydrate, the tetrahedral H PO groups are linked by hydrogen bonding. At lower (75% H PO concentrations, the tetrahedra are hydrogen-bonded to the water lattice. Physical properties of phosphoric acid solutions of various concentrations are Hsted in Table 2 the vapor pressure of aqueous H PO solutions at various temperatures is given in Table 3. [Pg.325]

Two main categories of the wet process exist, depending on whether the calcium sulfate is precipitated as the dihydrate or the hemihydrate. Operation at 70—80°C and 30% P20 in the Hquid phase results in the precipitation of CaSO 2 filterable form 80—90°C and 40% P20 provide a filterable CaSO O.5H2O. Operation outside these conditions generally results in poor filtration rates. A typical analysis of wet-process acid is given in Table 4. For more detailed discussion of the wet-process acid, see Fertilizers. [Pg.327]

The only clearly defined crystalline compositions are three forms of phosphoric acid and hemihydrate, pyrophosphoric acid, and crystalline P O q. The phosphoric acids obtained in highly concentrated solutions or by mixing phosphoric acid with phosphoms pentoxide are members of a continuous series of amorphous (excluding [Y OO]) condensed phosphoric acid mixtures. Mixtures having more than 86% P2O5 contain some cyclic metaphosphoric... [Pg.329]

Fig. 1. Solubility system of (—) Na2S04-H20 where R and M refer to rhombic and monoclinic Na2S04, respectively, ia H2O and represent Glauber s salt and sodium sulfate hemihydrate, Na2S04-7H20, respectively, at saturation ia H2O and (—) Na2S04-NaCl-H2 0 where and G represent the rhombic form and Glauber s salt, both saturated with NaCl. The dashed line represents a metastable form. Fig. 1. Solubility system of (—) Na2S04-H20 where R and M refer to rhombic and monoclinic Na2S04, respectively, ia H2O and represent Glauber s salt and sodium sulfate hemihydrate, Na2S04-7H20, respectively, at saturation ia H2O and (—) Na2S04-NaCl-H2 0 where and G represent the rhombic form and Glauber s salt, both saturated with NaCl. The dashed line represents a metastable form.
The iaterrelatioaship of nonalkaline scales (CaSO, CaSO /2H2O, CaSO 2H20) depeads oa temperature and the concentration of CaSO. To assure that no hemihydrate scale forms, MSF operators must mn their plants ia such a manner as to assure that the coaceatratioa of the total dissolved sohds does aot exceed 70,000 ppm at temperatures of 120°C. With average-salinity seawater, plants can operate at a concentration factor of 2, but in the Middle East where water salinity can be as high as 50,000 ppm, the concentration factor should not exceed 1.4. Under no circumstances should the total dissolved soHds exceed 70,000 ppm, ie, twice the concentration of normal seawater at 120°C. [Pg.241]

Arsenic Acids and the Arsenates. Commercial arsenic acid, corresponds to the composition, one mole of arsenic pentoxide to four moles of water, and probably is the arsenic acid hemihydrate [7774-41-6] H AsO O.5H2O. It is obtained by treatment of arsenic trioxide with concentrated nitric acid. Solutions of this substance or of arsenic pentoxide in water behave as triprotic acids with successive dissociation constants = 5.6 x 10 , ... [Pg.334]

LiB02 2H20 or Li20 20 4H2O, becomes the stable soHd phase. Dihydrate crystals are orthorhombic having a density of 1.825 g/mL and a stmctural formula Li[B(OH)4]. In solution above 150°C a hemihydrate, LiB02 1 /2H2O, forms and the anhydrous salt crystallizes above 225°C. [Pg.206]

About 23 million metric tons of gypsum are consumed aimuaHy. About 80% is processed into the commercially usable hemihydrate. Uses of gypsum are ia fabricated and/or formulated building materials (see Building materials, survey), Pordand cement (qv) set regulation, and agricultural soil conditioning. [Pg.418]

Hemihydrate is formed. Anhydrous material is formed. Compound decomposes. [Pg.418]

Anhydrite also has several common classifications. Anhydrite I designates the natural rock form. Anhydrite 11 identifies a relatively insoluble form of CaSO prepared by high temperature thermal decomposition of the dihydrate. It has an orthorhombic lattice. Anhydrite 111, a relatively soluble form made by lower temperature decomposition of dihydrate, is quite unstable converting to hemihydrate easily upon exposure to water or free moisture, and has the same crystal lattice as the hemihydrate phase. Soluble anhydrite is readily made from gypsum by dehydration at temperatures of 140—200°C. Insoluble anhydrite can be made by beating the dihydrate, hemihydrate, or soluble anhydrite for about 1 h at 900°C. Conversion can also be achieved at lower temperatures however, longer times are necessary. [Pg.419]

P-Hemihydrate. The dehydration of gypsum, commonly referred to as calcination in the gypsum industry, is used to prepare hemihydrate, or anhydrite. Hemihydrate is generally called stucco in North America and plaster in many other continents. In North America, plaster is differentiated from hemihydrate or stucco by the inclusion of additives to control intended use properties, eg, rehydration time, density, coverage, strength, and viscosity. [Pg.419]

OC-Hemihydrate. Three processing methods are used for the production of a-hemihydrate. One, developed in the 1930s, involves charging lump gypsum rock 1.3—5 cm in size into a vertical retort, sealing it, and applying steam at a pressure of 117 kPa (17 psi) and a temperature of about 123°C (6). After calcination under these conditions for 5—7 h the hot moist rock is quickly dried and pulverized. [Pg.421]

Calcined Anhydrite. Soluble anhydrite, or second-settle stucco, has physical properties similar to those of gypsum plaster. It hydrates to the dihydrate rapidly in water. Its outstanding property is its extreme affinity for any moisture, which makes it a very efficient drying agent (see Desiccants). In ambient moisture-laden air, it readily hydrates to hemihydrate. Soluble anhydrite, under the trade name Drierite, is widely used as a desiccant in the laboratory and in iadustry. A small amount is also used as an insecticide carrier. Small amounts of soluble anhydrite are unintentionally produced in most commercial calciners during hemihydrate production. [Pg.422]


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Alpha-hemihydrate gypsum plaster

Arsenic acid hemihydrate

Calcium hemihydrate, 3.25

Calcium sulfate hemihydrate

Calcium sulfate.hemihydrate CaSO

Calcium sulphate hemihydrate

Cellotetraose hemihydrate

Cobalt hemihydrate

Cupric Oxalate Hemihydrate

Hemihydrate Analysis

Hemihydrate Physical characteristics

Hemihydrate addition

Hemihydrate cement hydration

Hemihydrate crystal characteristics

Hemihydrate dissolution rate

Hemihydrate gypsum

Hemihydrate precursors

Hemihydrates

Hydrazinium perchlorate hemihydrate

Levofloxacin hemihydrates

P-Hemihydrate

Phosphoric acid hemihydrate

Phosphoric acid hemihydrate process

Phosphoric hemihydrate processes

Synthesis hemihydrate

Vanadium . hemihydrate

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