Jökull


Jökull - 01.12.1961, Blaðsíða 63

Jökull - 01.12.1961, Blaðsíða 63
vacuum evaporators. The present equipment is too small for an economical operation. Mizu- tani (G/7) mentions the possibility o£ using geo- thermal energy for the production of special types of salt. (ii) The projectecl salt-plant at Krýsuvik, Iceland. Lindal (G/27) has, in cooperation with Dr. M. S. Patel of Bombay, India, and Mr. W. A. Tobey, Mantistee Engineering Associates, U. S. A. made a comprehensive study o£ the possi- bilities of the production of salt front sea-water by means o£ geothermal energy in Iceland. A geothermal salt-plant has been projected at Krysuvik some 30 km south of Reykjavik. The projected capacity of the plant is 60,000 metric tons/year of salt. Sea-water is to be piped over a distance of 7 krn and concentrated in triple-effect vacuum evaporators. The concen- trated brine flows to a settler where bicarbonates and calcium sulphate are precipitated. The salt is to be crystallized in double effect equipment, dewatered, dried, compacted and briquetted. The evaporators are to be operated by natural- steam at pressure of 1.4 to 1.7 atmospheres abs. The consumption of steam is about 16 units weight of steam per unit weight of salt. The estimated total cost of production is 15.23 S/metric ton of salt. Lindal’s cost estimate is based on a relatively low cost of the natural- steam. In the view of the present writer, the total cost is more likely to be about 17.00 |/metric ton of salt. This is above the price o£ imported salt. Lindal (G/27) consiclers also further process- ing of sea-water for the production of gypsum ancl other materials dissolvecl in the sea. (d) Drying and processing of various materials. (i) Diatomite. Lindal (G/59) discusses brief- ly the possibility of using geothermal energy in tlie recovering and refining of diatomite front an underwater deposit in Iceland. Natural- steam at a temperature of 150° C is to be used, and the consumption of steam appears to be around 8 units weight of steam per unit weight of product. (ii) Alumina. Lindal (G/59) discusses also the jDossible use of geothermal energy in the conversion of bauxite to alumina. The possi- bilities in this field appear rather remote due to the fact that it is more economical to pro- duce the alumina at the bauxite-mine. (III) Grass, seaweeds and peat. The use of geothermal energy for the drying of these mater- ials is possible. But the very low transportability of the raw materials presents the main difficulty. (iv) Paper, pulp and sugar. The paper and pulp industry as well as the sugar refining indu- stry are heavy consumers of heat. The use of natural-steam is no doubt of advantage in loca- tions where the raw materials are available in the vicinity o£ the geothermal resources. One paper-mill in New Zealand uses natural-steam as process steam. (v) Refrigeration and air-conditioning. Ab- sorption refrigeration systems can be operated with natural steam. Kerr et al. (G/52) report that some experimental work has been carried out in New Zealand in order to study the possi- ble uses of geothermal energy for this purpost (6) RECOVERY OF MATERIALS FROM GEOTHERMAL AREAS. (a) Geochemist.ry of thermal areas. Geothermal activitý is caused by an upward permeation of hot fluids and gases where water generally is the predominant component. This water is in most areas of meteoric origin but there may in some cases, mainly in high-temp- erature areas, also be some water of juvenile origin. The fluids and gases ascend through variable physical and chemical environment. Tempera- ture and pressure are high at depth, but de- crease gradually on the way upward. This leads to the selective transport of chemical compon- ents which is of great importance. Sorne com- ponents are soluble at depth but are precipita- ted at higher levels. For example, both silica and calcium carbon- ate take part in the selective transport. The solubility of silica increases with increasing temperature. This component is therefore dissolved at depth and precipitated near to, or on, the surface where the temperature of the fluid drops. The solubility of calcium carbon- ate depends mainly on the amount of carbon dioxyde present. This component is also dissol- ved at depth and is precipitated near to the surface or in geothermal boreholes. The behaviour of these two components has an important effect on the hydrological condi- tion in thermal areas. The precipitation of silica 61
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