DISTILLING APPARATUS

Abstract: The invention relates to a distilling apparatus in which an evaporation section (10, 60) which heats raw water (100) and causes the generation of vapor (200) from said raw water (100), and a hydrophobic porous film (30) through which the thus generated vapor (200) is filtered are separately provided. Because vapor (200) separated from the raw water is supplied to one surface of the hydrophobic porous film, the proportion of the vapor relative to the fluid supplied to that surface of the film (30) can be increased, thereby enabling the efficient filtering of a large amount of vapor through the film (30). In addition, because the temperature of condensed water obtained by cooling the vapor (200) can be kept in the vicinity of the boiling point thereof, any gases and volatile substances contained in the raw water (100) are prevented from dissolving in the distilled water, there­ by enabling the production of extremely pure distilled water.

Description: The present invention relates to a distilling apparatus which is adapted to obtain extremely pure distilled water containing a very small amount of impurities from raw water. Description of the Prior Art: Distilled water of a high purity (also called "ultrapure water") which contains a very small amount of impurities is conventionally demanded by the electronics industry for manufacturing semiconductors and the pharmaceutical industry for manufacturing pharmaceutical substances. In particular, when manufacturing precise semiconductor devices such as integrated circuits (ICs) and large scale integrated circuits (LSIs), a large amount of distilled water is used in washing process and, therefore, the purity of the distilled water which is used can directly effect the production yield. For this reason, the stable production of extremely pure distilled water is an important point. In a conventional distilling apparatus, heated raw water is supplied to a hydrophobic porous film and is brought into contact therewith, and vapor generated from the raw water filters through the hydrophobic porous film. However, since the raw water is directly supplied to one surface of the hydrophobic porous film, the proportion of vapor generated on the side of that surface is small, thus making it difficult for a large amount of vapor to filter through the film. In addition, the hydrophobic porous film has a large number of small holes formed therein, and vapor which is generated from the surface of the raw water, which is in a state wherein it slightly penetrates the holes, filters therethrough. Thereafter, the filtered vapor is condensed by means of cooling water so as to obtain distilled water. However, when the vapor filters through the hydrophobic porous film, gases (e.g., carbonic dioxide gas and oxygen gas) as well as volatile substances which are dissolved in the raw water also evaporate and pass through the film. Therefore, the gases and volatile substances are dissolved in the condensed product, thus impeding the effort of increasing the degree of purity. In conventional apparatuses, no particular attention has been paid to this problem. One example of the prior art relating to this type of apparatus is that disclosed in US-A- 3,563,860. US-A-2 893 926 discloses a distilling apparatus according to the precharacterizing part of the claim, and claims an apparatus for the distillation of sea water and the production of electricity, comprising steam-generating means, a back-pressure steam turbine, an electrical generator driven by said steam turbine, a heat exchanger comprising a first side and a second side, a flash evaporator comprising a flash chamber and a condenser, first means to pass steam from said steam generating means to said back pressure steam turbine, second means to pass steam exhaust from said turbine to the first side of said heat exchanger, third means to pass sea water to the second side of said heat exchanger, fourth means to pass the sea water from the second side of said heat exchanger to the flash chamber of said flash evaporator, fifth means to pass steam from said steam generating means to said first side of said heat exchanger, and sixth means to regulate the amount of steam flowing through said fifth means to maintain the pressure in the first side of said heat exchanger at a predetermined value independent of fluctuations in electrical load. Since volatile gas and non-combustible gas are mixed into a pure water, it is difficult to produce ultrapure water. US-A-3 418 214 discloses a similar distilling apparatus, wherein part of volatile gas and non-condensable gas is discharged to the outside, but another part thereof is concentrated at a location of low temperature and, therefore dissolved in the raw water with the consequence that an ultrapure water cannot be produced. SUMMARY OF THE INVENTION An object of the invention is to provide a distilling apparatus which is capable of obtaining a large amount of distilled water from raw water at a high degree of efficiency. Another object of the invention is to provide a distilling apparatus which is capable of obtaining extremely pure distilled water. A further object of the invention is to provide a distilling apparatus which is designed to reduce its energy consumption. The above objects are achieved, according to the present invention, by a distilling apparatus for producing ultrapure water by condensing vapor generated from raw water, comprising a hydrophobic porous film which allows vapor to pass from an evaporation chamber to a condensation chamber but does not allow liquid to pass from said evaporation chamber to said condensation chamber; a main distilling body separated into said evaporation chamber and said condensation chamber, said evaporation chamber including a raw water tank in a lower portion thereof, and said condensation chamber including a distilled water tank in a lower portion thereof; means to introduce raw water to said evaporation chamber; heating means for heating said raw water being introduced above a saturation temperature of said raw water; means for generating vapor from said heated raw water introduced to said evaporation chamber, said generating means including means for flash evaporating the raw water heated by the heating means; and means for condensing said vapor in said condensation chamber, characterized in that the distilling apparatus further includes a thermobar vaporization device connected with said main distilling body, said thermobar vaporization device comprising: a plurality of raw water chambers for receiving raw water; an air chamber located next to said plurality of raw water chambers; a cooling chamber located next to said air chamber, a hydrophobic porous film separating said plurality of raw water chambers and said air chamber; a cooling surface separating said air chamber and said cooling chamber; means for feeding raw water from said condensing means to said raw water chambers; means for feeding raw water from raw water chambers to said condensing means; an activated carbon absorption tower connected to said thermobar evaporation device; an ultraviolet sterilizer connected to said absorption tower; a polisher connected to said ultraviolet sterilizer; an ultrafilter connected to said polisher; means for feeding said distilled water from said air chamber to said absoprtion tower; means for feeding condensed vapor from said condensation chamber to said absorption tower; and an exhaust valve disposed on an upper portion of said condensation chamber. Fig. 1 is a view of the whole arrangement of a distilling apparatus in accordance with an embodiment of the invention; and Fig. 2 is a view of a more specific structure of a main body of the apparatus in accordance with the invention. DESCRIPTION OF THE PREFERRED EMBODIMENT A preferred embodiment of the present invention will now be described with reference to the drawings. In an embodiment shown in Fig. 1, the apparatus comprises a main distilling apparatus body 50, a heater 10, a recirculation pump 20, and a heat economizer 35. The main body 50 is divided into an evaporation chamber 51 and condensation chamber 52 by a hydrophobic porous film 30. A nozzle 60 which discharges heated raw water 100 is disposed in the evaporation chamber 51 whose bottom forms a raw water tank 61. A cooling pipe 80 is disposed in the condensation chamber 52 whose bottom is formed into a distilled water tank 81. The raw water 100 is introduced into the heat economizer 35 wherein it exchanges heat with distilled water 500 and is heated thereby, and is then led to the heater 10 through the pump 20 to be heated. In the heater 10, the raw water 100 is heated to a temperature which is a few degrees higher than the saturated vapor temperature within the evaporation chamber 51 (the difference between the water temperature and the saturated vapor temperature is called "the flash temperature" which is normally about 3 to 5°C, and the state of vapor in which it is heated to a temperature above the saturation temperature is called "the superheated state"). The thus heated raw water 100 is discharged into the evaporation chamber 51 through the nozzle 60 and instantly self-evaporates, generating a large amount of fine water droplets. Evaporation proceeds on the surface of the water droplets, and the temperature of the droplets drops to the vapor saturation temperature within the evaporation chamber 51. Vapor 200 generated in the chamber 51 flows into the condensation chamber 52 together with the water droplets 110, but when they filter through the hydrophobic porous film 30, the water droplets 110 are completely separated, so that the vapor 200 alone is introduced into the condensation chamber 52. In the chamber 52, the vapor 200 is cooled and allowed to condense on the surface of the cooling pipe 80 through which cooling water flows, so as to become distilled water 500 which is collected in the distilled water tank 81. As described above, the apparatus is arranged in such a manner that only vapor and water droplets which have been separated from the raw water are supplied to one surface of the hydrophobic porous film. Therefore, the proportion of vapor relative to the fluid supplied to that one surface of the film can be increased, thus enabling the efficient filtering of a large amount of the vapor through the film. In general, since the distilled water 500 stored in the tank 81 has a relatively high temperature on the order of several tens of degrees, it is cooled by utilizing the raw water 100 in the heat economizer 35. With this apparatus for producing distilled water, which is normally operated under a pressure which is approximately equal to atmospheric pressure, the raw water 100 in the evaporation chamber 51 has a temperature on the order of 100°C, having been heated to a temperature of about 105°C by the heater 10. Because the interior of the evaporation chamber 51 is filled with the saturated vapor 200 and the water droplets 110, the distilled water 500 within the adjacent distilled water tank 81 has a temperature of about 100°C which is the boiling point of water. In this way, since the apparatus is operated at an internal temperature in the vicinity of 100°C, any bacteria and the like contained in the raw water are killed by the high temperature, thus providing a sterilization effect. In addition, the flash evaporation which takes place in the apparatus causes the small amounts of air and carbonic dioxide gas dissolved in the raw water to be discharged. In the evaporation chamber 51, when the vapor evaporates from the raw water at a temperature on the order of 100°C, a small amount of volatile organic substances (which have boiling points of below 100°C) are also discharged. However, since the distilled water 500 in the tank 81 has the same temperature as that within the evaporation chamber 51, as described before, the thus discharged volatile organic substances are not readily re-absorbed by the distilled water 500. The same is true for air and carbonic acid dissolved in the raw water and generated in the evaporation chamber 51; the air and carbonic acid are not readily dissolved, in the distilled water in the tank 81 and hence are not re-absorbed. Instead, they are discharged to the outside through an exhaust valve 70. This exhaust valve 70 is of the check valve type which has a body whose interior is pressurized to a pressure sightly higher than that of the outside so as to prevent any backward flow of air, etc., from the otuside. In this embodiment, part of the cooling water 600 may be used as the raw water. If it is necessary to discharge distilled water at a high pressure from the valve located at the point of use, a pump may be provided. As described above, according to this embodiment of the invention as described so far, the following advantages are provided: distilled water of a high degree of purity can be obtained by a single evaporation and condensation operation; at the same time, by virtue of the phenomenon of flash evaporation and the provision of the hydrophobic porous film, extremely pure distilled water can be obtained by means of a compact apparatus with a high evaporation efficiency. In order to reduce the heating capacity of the heater for achieving a reduction in energy consumption, the apparatus in accordance with this embodiment is adapted to recover the heat which is generated when vapor is cooled and condensed by means of the cooling pipe 80, and to produce distilled water 500' by further comprising a thermobar vaporization device 90. The thermobar vaporization device 90 comprises a hydrophobic porous film 31, a cooling surface 32, a number of raw water chambers 91, a cooling chamber 93, and an air chamber 92, the chambers being separated by the film 31 and the surface 32. Raw water 100 at a high temperature is introduced into the raw water chamber 91 and is supplied to a surface of the porous film 31 on which vapor 210 evaporates, and the vapor 210 thus generated from the water 100 passes through the air chamber 92 and is then cooled and condensed on the cooling surface 32, thereby producing distilled water 500'. The main body 50 and the thermobar vaporization device 90 are connected in the following manner. First, raw water 100 is heated by utilizing the cooling heat obtained from the cooling pipe 80 in the condensation chamber 52 of the main body 50, and the raw water 100 is sent to the raw water chamber 91 of the thermobar vaporization device 90 wherein the water 100 is allowed to evaporate on the surface of the hydrophobic porous film 31. Part of the raw water 100, whose temperature is now reduced, is drained away while the remainder is returned to the cooling pipe 80 of the main body 50, in which it is heated again by the condensation heat, and is then recirculated to the raw water chamber 91 by means of the pump 20. By incorporating the above device, the heat supplied to the apparatus is used in the flash evaporation in the main body, via the heater 10, so as to obtain distilled water 500 from the condensation of vapor resulting from the flash evaporation; and, at the same time, the condensation heat resulting from the above condensation is recovered by the cooling pipe 80 to heat the raw water 100 which is then allowed to evaporate in the thermobar vaporization device 90 so as to obtain distilled water 500'. With this arrangement, the amount of heat consumed can be reduced to a level which is about half as that without the device 90. In order to further adapt the apparatus for performing ultra-distillation to obtain an ultra-high degree of purity (which operation is normally called "ultra-ultra distillation"), a conventionally-known secondary pure water system is combined with the destilling apparatus described above. In order to obtain ultra-ultra-pure distilled water 510, distilled water 500 obtained by the main body 50 and the thermobar vaporization device 90 is further passed by means of a pump 22 through an activated carbon absorption tower 5, an ultraviolet sterilizer 7, a polisher 6, and an ultrafilter 8. One of the effects thereof is that ultra-ultra-pure water of an ultra-high degree of purity can be obtained. Further, the invention provides the following advantage. In general, the activated carbon absorption device, the polisher, and the ultrafilter, which are disposed downstream of the apparatus, need to be replaced periodically because of their limited effective life relative to their absorption and ion-exchange capacities and to the degree of clogging of the ultrafilter. However, in accordance with the embodiment of the invention, since these elements are disposed after the distilling apparatus which forms the main part of the invention, their effective life can be considerably lengthened. Fig. 2 shows an example of a specific structure of the main body 50 of the distilling apparatus. The main apparatus body 50 has a vertical structure in which a flash evaporation nozzle 60 and a tank 61 for storing water which has not yet been evaporated are disposed in a lower portion, and a condensation chamber 52 including a hydrophobic porous film 30, a cooling pipe 80 for condensation, and a distilled water tank 81 are disposed in an upper portion. The main body 50 is thus adapted to achieve the advantages and effects hereinbefore described, as well as to require a minimum of mounting area. The nozzle 60 comprises one or more pipes which have the following dimensions determined from fundamental experiments: a diameter which is suitable for realizing a flow speed of the fluid being discharged of not more than 30 m/s., and a length of not more than 300 mm. Although the direction of the discharge is not specifically limited, it is not preferable, at least, to have it in a direction that helps to increase the speed at which the generated spray advances upward in the direction of the condensation chamber 52. In this case, it is possible to use a member for reversing the direction of advancement. In order to increase the efficiency of the film 30 which is made of a hydrophobic porous material, the film 30 should have a wider area within a smaller volume. From this view point, the film 30 should preferably have a pleated structure which is disposed vertically. By virtue of this structure, spray accompanying the vapor can be separated therefrom on the surface of the hydrophobic porous film 30 and can immediately drop downward in the vertical direction, and be received in the tank 61 for storing unvaporized water. Therefore, a condition which enables the filteration of the vapor can always be maintained on the surface of the hydrophobic film 30. The cooling pipe 80 may either be of a winding type or a straight type, but basically, an extraction pipe 7l should be disposed in a region at which the temperature is lowest in the condensation chamber 52. In addition, the surfaces of members which are in contact with the distilled water, such as the distilled water tank 8l, should have a surface roughness of not more than 0.l µm in order to prevent any microscopic retention of fluid and thus to prevent any reduction in the degree of purity. Therefore, such members should preferably be made of a material which is either SUS304 or SUS3l6, subjected to surface finishing and the formation of an oxidation film. Although not illustrated, the nozzle 60 and the condensation chamber 52 may be arranged in the horizontal direction. As described above, according to the present invention, a large amount of vapor can be efficiently filtered through the hydrophobic porous film, whereby the efficiency of the production of ultrapure distilled water can be enhanced. In addition, since any gases and volatile substances contained in the raw water can be removed, advantages such as the possibility of obtaining distilled water of a high degree of purity can be ensured.

Claims: A distilling apparatus for producing ultrapure water by condensing vapor generated from raw water, comprising a hydrophobic porous film (30) which allows vapor to pass from an evaporation chamber (51) to a condensation chamber (52) but does not allow liquid to pass from said evaporation chamber (51) to said condensation chamber (52); a main distilling body (50) separated into said evaporation chamber (51) and said condensation chamber (52), said evaporation chamber (51) including a raw water tank (61) in a lower portion thereof, and said condensation chamber (52) including a distilled water tank (81) in a lower portion thereof; means to introduce raw water (100) to said evaporation chamber (51); heating means (10) for heating said raw water (100) being introduced above a saturation temperature of said raw water (100); means (60) for generating vapor (200) from said heated raw water (100) introduced to said evaporation chamber (51), said generating means (60) including means for flash evaporating the raw water (100) heated by the heating means; and means (80) for condensing said vapor in said condensation chamber (52); characterized in that the distilling apparatus further includes: a thermobar vaporization device (90) connected with said main distilling body (50), said thermobar vaporization device comprising: a plurality of raw water chambers (91) for receiving raw water (100); an air chamber (92) located next to said plurality of raw water chambers (91); a cooling chamber (93) located next to said air chamber (92); a hydrophobic porous film (31) separating said plurality of raw water chambers (91) and said air chamber (92); a cooling surface (32) separating said air chamber (92) and said cooling chamber (93); means for feeding raw water from said condensing means (80) to said raw water chambers (91); means for feeding raw water from raw water chambers (91) to said condensing means (80); an activated carbon absorption tower (5) connected to said thermobar evaporation device (90); an ultraviolet sterilizer (7) connected to said absorption tower (5); a polisher (6) connected to said ultraviolet sterilizer (7); an ultrafilter (8) connected to said polisher (7); means (22) for feeding distilled water (500) from said air chamber (92) to said absorption tower (5); means for feeding condensed vapor from said condensation chamber (52) to said absorption tower (5); and an exhaust valve (70) disposed on an upper portion of said condensation chamber (52).

Inventors: EBARA, KATSUYA, HAYASHI, NOBUATSU, KOSEKI, YASUO, KUROKAWA, HIDEAKI, TAKAHASHI, SANKICHI, YAMADA, AKIRA
Applicants: HITACHI, LTD.
Application year: 1986
Main classification: B01D3
IPC codes: B01D1, B01D5, B01D3, B01D61, C02F1