CN102387994A - Water purification method and a device for carrying out said method - Google Patents
Water purification method and a device for carrying out said method Download PDFInfo
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- CN102387994A CN102387994A CN2009801576379A CN200980157637A CN102387994A CN 102387994 A CN102387994 A CN 102387994A CN 2009801576379 A CN2009801576379 A CN 2009801576379A CN 200980157637 A CN200980157637 A CN 200980157637A CN 102387994 A CN102387994 A CN 102387994A
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/22—Treatment of water, waste water, or sewage by freezing
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
- C02F9/20—Portable or detachable small-scale multistage treatment devices, e.g. point of use or laboratory water purification systems
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
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Abstract
The invention relates to water purification at home. The water purification method involves cooling water for the first time in a temperature-controlled tank by decreasing the temperature of the water in said container to a value equal to or greater than 3 DEG C at a rate of 0.1-0.3 DEG C/minute and subsequently freezing the water at a rate of 0.05-0.1 DEG C/minute to a temperature equal to or greater than -4 DEG C so that the pure water with heavy water admixtures is fully crystallised and a liquid brine with the admixtures is formed. Then, the brine is drained, the ice is heated by gradually increasing the temperature to a value equal to or less than 10 DEG C at a rate of 0.16-0.18 DEG C/minute and is kept in those conditions until it is totally melted. For the second time, the water is cooled at a rate of 0.1-0.3 DEG C/minute to a temperature equal to or greater than 2 DEG C and the heavy water is kept in those conditions until it is fully crystallized. The purified water is drained via a filter. A device for purifying water comprises a housing provided with a temperature-controlled working container that has a cover and an inclined bottom with a hole for draining water, a thermoelectric module for freezing water and melting ice, which module is provided with a control unit, a consumer tank for receiving the purified melt water and a tank for receiving water with admixtures and a high deuterium content. The device comprises pipes with a water drainage control means, which are connected to the drain hole in the inclined bottom of the working tank. The pipes are additionally interconnected by a pipe with a fine water filter.
Description
The present invention relates to method for purifying water and device at home; It rely on to remove the biological property that dissolved gases in carcinogenic and mutagenic material and the water improves water; And relying on freezing and crystallizing through closed volume to make to pollute feed water to be separated to be pure water and polluted water to come the concentration of heavy isotope (heavy hydrogen and tritium) in the remarkable minimizing water, the present invention is suitable in daily life, foodstuffs industry and medical science, using.
Biosystem is to water (H
2The reaction of effect O) depends on that the quality and quantity that the water isotropic substance constitutes is well-known.Have the water of high heavy isotope concentration, particularly heavy hydrogen, thereby cause limiting the application of water in treatment [referring to Kushner at the clear and legible toxic reaction of health aspect; D.J., Baker, F.; Dunstall; T.G., Can.J. physiology pharmacology (Physiol.Pharmacol.) in February, 1999,77 (2): 79-88].Simultaneously, the positive biological activity of the water that in some technical matters, produces classified as light isotope water and, find that in some biological projects to a certain extent, [referring to Somlyai, G. fights with cancer to come feed water to reduce heavy hydrogen concentration relatively! ), Akademiai Kiado, Budapest, 2001].
The biological activity that disclosed digital proof snow-broth or thawing water also arranged the effect of stimulation aspect plant-growth and the development be significantly [referring to Rodimov, B.N., " snow-broth is to the effect of active object "; Siberian and Far East agricultural crops, Omsk, 1965; 56-57 page or leaf (Agricultural Productions of the Siberia and Far East; Omsk, 1965, pp.56-57)].The increase of heavy isotope concentration has changed the normal path of Biochemical processes in human body, has therefore weakened the function of health.The result is exactly to increase at daily tap water
1H
2 16The amount of O.
A kind of method of disclosed treating water comprises from feed water produces ice, thaw it and collect thawing water.The production of ice realizes [referring to Denisov, I., and Matveev, S., " drinking pure water (Drink Pure Water) ", Rabotnitsa magazine, Moscow, 1991,11 phases, 34-36 page or leaf] through part cooling (approximately being 2/3rds volumes) feed water.Because water is all being stopped freezing and is being discharged not refrigerated residuum before freezing, melt the water that obtains through " ice cup (an ice cup) " and reduced heavy metal and some isotopic concentration.
Therefore, this method can not provide the reduction of heavy (heavy hydrogen and tritium) water molecules level in the thawing water; They have together become ice with light (light hydrogen) water.Further, above cited method does not provide water effective structurizing, does not provide the condition of the performance that influences gained water that it provides yet.
The device that is used for implementing this art methods is presented as family or industrial refrigerator (refrigerator); It comprises a case; Its mounted inside has the chamber of admittance feed water and the refrigerating unit of pond form, and [referring to technology dictionary (The Polytechnic Dictionary), Academician N.I.Artobolevsky edits, Moscow; 1977,546 pages].The defective of this art methods and this prior-art devices comprises that they can not provide separating and the biological nature that can not improve water significantly of the heavy water of having removed heavy water and light-water.
A kind of disclosed through the freezing method that improves drinking water quality; Comprise that water-cooled freezes, ice is broken, and ice-out; Be characterised in that feed water is freezing to the 70-90% of original volume and the thawing of ice; Its through thermal isolation the ice of side and bottom surface account for the 30-55% that is removed volume subsequently [referring to russian patent No. 2077160, ICL C02F1/22, on April 10th, 1997 is open] until the thawing water that flows away.
The method of the high-quality tap water of known preparation comprises and removes undissolved mechanicalness impurity, removes chlorine, and is softening, removes organic substance and venting step; Their defective comprises the tap water that high purification can not be provided, and does not also have treatment characteristic (European patent 0249049, IC C02F 9/00,1987 in addition; European patent 0312079, IC C02F 9/00,1989).
Further, known preparation has the method for high purification tap water of treatment characteristic, except that comprising the water purifying step, also comprise water-cooled freeze step (referring to USP 1799367, IC C02F 9/00,1991; Russ P 2010772, IC C02F 9/00,1992; With Russ P 2031085, IC C02F 9/00,1992).
A kind ofly knownly freeze large-scale purification water method and the device that is used for implementing this method (referring to Lyubarsky through water-cooled; V.M., natural water deposition and handle their method (Precipitation in Nature Waters and Methods for Processing Them), Moscow; Stroyizdat; 1980, the 98-99 page or leaf, Figure 22).This device comprises in order to the pond that holds water with in order to cool off the technique device of (freezing) and heating (thawing) water.
A defective of above-mentioned quoting method possibly be since lack freezing and thawing mode that select to optimize (speed, time, and design temperature, and other) the low-level purification of water that causes.
Another kind of known (referring to " suggestion of making provision against emergencies (An Advice Just in Case) "; At Rabochaya Tribuna newspaper; Moscow, the 21st phase (321), on January 30th, 91) pass through the freezing method that purifies household drinking water and the device of implementing this method (referring to Russ P 2058262; IC C02F is open on April 20th, 1/22,96).This method comprises injects the pond with water, at first the pond is placed in the refrigeration chamber; Water coolant is until form the thick and heavy hydrogen ice sheet of 1-3mm on the surface; The pond is moved apart refrigeration chamber and removes the heavy hydrogen ice sheet; With the pond be placed on refrigeration chamber for the second time and be maintained until clean ice sheet and do not purify, chemistry is unclean, refrigerated water (residual brine) forms; The pond is moved apart refrigeration chamber and will totally icing with residual brine separates; Ice with melting totally.In second time refrigerating process, the feed water that contains with the impurity of dissolved salt, organism and agricultural chemicals form is separated into fresh clean ice and residual brine; The latter is concentrated in the central zone of refrigerated water for the first time.
The art methods that this water purifies has following defective:
-two independently water-cooled freeze step and two independences and increased the complicacy that water purifies from the separating step of ice and ice; It is not easy to remove heavy hydrogen (weight) water; Because need to move apart refrigeration chamber to the pond, pour into new (temporarily) pond to refrigerated water not, remove the upper surface of water and first ice sheet (1-3mm is thick) of bottom, main pond and peripheral formation; Pour into main pond to water from interim pond, be placed on main pond in the refrigeration chamber; And only remove first ice sheet from upper surface, do not pour water into interim pond, it uses in front the step sometimes, has increased the heavy water residual volume in the water purification.Because these defectives, although it is very high to obtain the issue requirement of " one glass of clean tap water ", the method for purifying waste water through freezing mode this obviously " simply " does not have widespread usage in the family.
One device (on April 20th, 1996 is open for USP 2058262, IC C02F1/22) through freezing purifying drinking water; This device comprises in order to place the pond (container) of water; Top cover is fluted to place freezing ice sheet for the first time, and the bottom is fluted to place water and the freezing ice sheet second time, heating unit; Sluice is providing bottom and lid to the pressure of container, and the packing ring between lid and container.
The defective that should have family's water treatment technology device now is following: complicated design; Because only remove heavy hydrogen ice, mean that removal quantity is insufficient from the top surface that is frozen water; Because the ice forming process occurs in whole internal surfaces of container, also be difficult even therefore only remove heavy hydrogen ice from top surface; And, therefore separate clean ice and residual brine is difficult through the removed bottom mode that a dark groove is arranged because ice for the second time that forming process occurs in the totality surface and be not from top to bottom.
The one known water purifier of drinking thawing water in order to production; It comprises the extension container; Its internal series-connection arranges with annular refrigeration chamber refrigerated water zone, and impurity is extruded in salt solution spissated zone and is equipped with annular heating unit from ice water is transformed into region of fluid (Russ P 23412817 from solid; IC C02F is open on December 20th, 1/22,2007).This water purifier has independently outlet pipe drink thawing water to remove like brinish impurity and removal; The separating unit that is placed on the refrigerator next door of two bottoms that all are set at container and extra assembling is to move refrigerated water rod and to be placed on the separating unit at refrigerated water rod center with the form of pipe.There is circular cutting part and its exit section to launch in this separating unit ingress to remove like brinish impurity.
Yet it is big that this device is implemented complex structure and refrigeration chamber size and weight, stoped it to use in the family like this.
The one known water purifier that is used for drinking on a large scale thawing water from seawater production; It comprises the extension container; Its internal series-connection is arranged with annular refrigeration chamber refrigerated water zone; Impurity is extruded in salt solution spissated zone and is equipped with annular heating unit from ice water from solid be transformed into region of fluid and all be arranged on container than the independent outlet pipe of lower part with impurity in the discharging salt solution with drink thawing water (referring to FRP 2858607; IC C02F is open on February 11st, 1/22,2005).
Yet this device also has the large size refrigeration chamber and because the whole installation weight that is used for desalinizing seawater on a large scale is big, has stoped it to use in the family like this.Further, this device can not provide the chance of removing heavy (heavy hydrogen and tritium) water, has therefore weakened product gas purity and has therefore weakened application characteristic.
One knownly includes the lid and the pond of conical bottom in order to the device of purifying waste water, have in it be used for discharge water the hole and be used for refrigerated water and melt the electrothermal module of icing; The pond of pond that acceptance is purified waste water and the polluted water that receives the raising of heavy hydrogen level; The electrothermal module control unit; Be used for the conduit of discharge water; One end is connected to refrigerated water and is equipped with valve with the interior drain and the other end of the conical bottom in the pond of melting ice; Its pond that thawing water that is used to receive purification is installed respectively down and the pond that is used to receive the polluted water of the heavy hydrogen level that contains rising are (referring to Japanese Patent 5123668; IC C02F 1/22, F25B21/02, on May 21st, 1993 is open).
Yet this device has one cooling or heating unit in electrothermal module, and this unit is placed on the one side in pond, does not therefore allow water evenly to melt and reduced the quality of water decontamination with a large amount of evenly freezing or ice of rotational symmetry spiral tube form.In this device, can not allow this device between circulation, to prepare operation fast and the automated manner operation can not be provided in order to the blowdown system of emission purification water (thawing water) and polluted water, therefore reduced the operability of this device.Further, this device can not provide the removal of heavy (heavy hydrogen and tritium) water, has therefore weakened product gas purity and has therefore weakened application characteristic.
Maximally related art methods is included in the method (Russ P 2274607 of purifying waste water in the pond; IC C02F 1/22; On April 20th, 2006 is open); Comprise the heat abstraction through heat exchanger mode, this heat exchanger is arranged on the pond internal upper part apart from about 1/3 to 2/3 height of the top of liquid cylinder liquid level, with the equidistant position in center, pond and side; And 1 temperature head in (1) ℃ is provided, this temperature head surroundings provide ice crystal continuously, progressively with local volume (local-bulk) crystallisation process of the rapid refrigerated of multistep.For purifying waste water; Carry out following operation: continuously, progressively quenching is frozen to their amount and is no more than the size of the 50-70% of feed water total amount with multistep at the surroundings ice crystal; The refrigerated polluted water is not discharged from the pond; Ice unfreezes all, and filters through secondary filter when for the second time freezing amount and the discharging thawing water to thawing water sum 3-7% of part is in order to consumption.Polluted water is melted the back from the different levels part of the height along the pond and through different conduit dischargings with thawing water; Wherein polluted water is discharged through the conduit that is arranged on minimum base, bottom, pond, and thawing water is through being arranged on the conduit discharging of 0.5-2 centimetre of top, bottom, pond.
Thawing of ice through the enforcement of two steps; Wherein the first step comprises to separate to freeze to all containing the long-pending 90-95% of lower concentration heavy hydrogen isotropic substance ice body and second step and comprising thaw on heat exchanger residue crystalline and the ice that comprises high weight percentage hydrogen isotopes (heavy hydrogen and tritium) for the first time.Thawing through continuous elevated temperature of ice to reaching evaporating state and the vapor film convective transfer of heating being realized to the temperature that is not higher than 40-80 ℃.Through the pond side perimeters around shielding cable heating realize thawing of ice.
Maximally related prior-art devices comprises water-purification plant (Russ P 2274607; IC C02F is open on April 20th, 1/22,2006), comprise not purification water pool; Be installed in inside, pond to remove the heat exchanger of heat and freezing ice; Heating is also separated the device that freezes, and freezing unit and cooling system thereof have the conduit of the exhaust emission water of valve; Conduit with the discharging thawing water that valve is arranged; This device is characterised in that: heat exchanger be multistage coil form and be placed on top, pond, be approximately the pond height 1/3 to 2/3, to top 2-5 centimetre the distance in pond and with side, pond symmetry, the gap that has makes that ice refrigerated volume size maybe not can be blocked this gap because of crystal ice in the coil pipe ambient water, heat-insulating lid and tightness system are assembled in the pond; The pipe of exhaust emission water is installed in pond conical lower section apex portion, and discharging thawing water conduit is installed in conical base top, pond 0.5-2 centimeters.This device is equipped with secondary filter, and the water discharge spout of valve is arranged, and is used for circulating and transmits thawing water pump through secondary filter and have manual work or the control unit of operational mode automatically under pressure.
It is not enough that the main drawback of maximally related existing method and apparatus comprises that water purifies quality; Be because the heat exchanger in the equipment is positioned at work pool and the integral body that can not feed water provides freezing ice-out to form axisymmetric annular solid or to have uniformly, therefore reduced the quality of water purifying contaminated thing and heavy hydrogen.The size of equipment is big with the weight of freezing unit that has cooling system, and the useful volume part that water-cooled is frozen the pond occupied by heat exchanger, and heat exchanger is a coil form, has increased the size of equipment and made to use difficulty at home.
The technical result that requires protection to invent comprises the creation of method for purifying water and equipment; Therefore increased the quality of water purifying inorganic salt, organic matter and heavy (heavy hydrogen and tritium) water pollutant; Reduced and produced the time of finished product and the weight and the size of equipment, and improved the accessibility of using this equipment through the thawing water production technique fully automated that makes purification.
This technical result is through accomplishing in the method that purifies at water; Said comprising: first water cooling in the temperature control work pool and under the temperature of the Tc that surpasses the liquid brine contain organic and inorganic pollutant, little by little its freezing for some time is enough to make the complete crystallization of pure water of being polluted by heavy water and makes liquid brine formation subsequently; Discharge said salt solution, reaches temperature value heating ice cube with rising gradually, and ice is maintained under the said temperature thaw fully up to it above the Tc of heavy water; Be water-cooled to for the second time the Tc of heavy water; And it is maintained under the said temperature up to the complete crystallization of heavy water, and and through secondary filter it to be filtered simultaneously, discharging is with the finished product of the thawing water form that purifies; According to the present invention; The contacted thermoelectric element of thermal conduction wall in the heating of water, cooling and crystallization and ice thaw dependence and pond is arranged on outside the pond with automatic mode equably, during the water cooling first time, equals 0.1-0.3 ℃/minute value range through the medium temperature in the work pool with speed and changes; The medium temperature that reduces in the work pool is born 3 ℃ value to being not less than; The first water crystallization round-robin time utilization software begins to calculate from the moment that water changes with automatic mode, raises at least 0.5 ℃ with the side wall temperatures of work pool and discerns the moment that this water changes, during first time water crystallization; Equaling 0.05-0.1 ℃/minute value range through the medium temperature in the work pool with speed changes; Reduce medium temperature in the work pool to the value that is not less than negative 4.0 ℃, up to during it melts fully behind the discharging salt solution, equal 0.16-0.18 ℃/minute value range through the medium temperature in the work pool with speed and change in ice thaw; Medium temperature in the rising work pool is to not being higher than positive 10 ℃ value; During the water cooling second time and heavy water crystallization, with the value range variation that speed equals 0.1-0.3 ℃/minute, reduce the interior medium temperature of work pool to being not less than positive 2 ℃ value through the medium temperature in the work pool.
, and obtained to be no more than 480 minutes no longer than 360 minutes from the organic and inorganic pollutant of purifying waste water to the discharging brinish time with the full cycle of the finished product of the thawing water form that purifies.
The biological activity of the thawing water that keep to purify for the long term, keep for the second time that water crystallization is not higher than in temperature+2 ℃ be disposed to the user pond up to Jiang Shui at least 300 minutes.
The volume of pure thawing water is at least 65% of a former volume of water, and the total content of inorganic impurity reduces half at least.
Above-mentioned technical result also can be accomplished in the equipment that water purifies; Said equipment comprises the work pool at the bottom of the inclination that has the lid and the water discharge orifice is arranged; Be equipped with control unit in order to refrigerated water with make the device of ice thaw, contain the pond of water of the heavy hydrogen content of pollutent and raising in order to the pond that receives the thawing water that purifies with in order to reception; The pipe that wherein has the water emission control system; With link to each other in order to the discharge orifice at the bottom of the inclination of refrigerated water and the work pool that makes ice thaw; Wherein delivery pipe is installed in the top in pond of the water of the heavy hydrogen per-cent that contains pollutent and raising in order to the pond of the thawing water that receive to purify with in order to reception respectively; According to the present invention: water-cooled is frozen with the ice thaw device and is implemented to use electrothermal module; It comprises several thermoelectric elements that are positioned in order to outside the sidewall of refrigerated water and the work pool that makes ice thaw; Water emission control system in the pipe comprises four valves of mounted in pairs in it, and said water discharge spout interconnects through the pipe that is equipped with second water filter in addition, between the valve of this pipe and the water emission control system of tie point in managing of said water discharge spout.Water-cooled is frozen the electronic control unit that comprises electrothermal module with the control unit of ice thaw device; The control unit of the water discharging valve that links to each other with valve; Automatic programming device and having be installed in water-cooled freeze with the end in ice thaw pond and sidewall on the scatterer of electrothermal module on the temperature measurement unit of transmitter.Wherein automatic programming device links to each other with the electronic control unit of control unit, temperature measurement unit and the electrothermal module of valve.
Accompanying drawing 1 has been described the synoptic diagram that requires the water correction plant of protection.Accompanying drawing 2 has shown the temperature-time schedule curve of the thawing water product that purifies.
Disclosing of the equipment of enforcement method for purifying water.This equipment comprises shell 1; Be provided with in it cover 3 with the work pool 2 that has at the bottom of the inclination of water discharge orifice 54; Be used to make water-cooled to freeze and make the electrothermal module 6 of ice thaw, be used to receive the pond 7 and the pond 8 that is used to receive the water of the heavy hydrogen content that contains pollutent and raising of the thawing water of purification.Pipe 9 and 10 comprises water emission control system 11, and links to each other with 4 interior holes 5 at the bottom of the inclination of work pool 2.The delivery pipe 12 and 13 of pipe 9 and 10 is installed in the top in order to the pond 7 that receives the thawing water that purifies and the pond 8 of the water that is used to receive the heavy hydrogen content that contains pollutent and raising respectively.Electrothermal module 6 comprises several thermoelectric elements 14, and it is positioned at and is used to make water-cooled to freeze and make outside the side surface of work pool 2 of ice thaw.Pipe 9 and 10 interior water emission control systems 11 comprise mounted in pairs in it and four valves 15,16,17 and 18 of closing usually, and said water discharge spout 9 and 10 interconnects through the pipe 19 that is equipped with second water filter 20 in addition.Pipe 19 lays respectively between the valve of closing usually 15,16 and 17,18 of the water emission control system 11 in the said pipe with the tie point of water discharge spout 9 and 10.Further; Said equipment has control unit 21; It comprises the electronic control unit 22 of the electrothermal module 6 that links to each other with wherein element 14, the control unit 23 of the valve 15-18 that links to each other with valve, automatic programming device 24; And have the sidewall that is installed in pond 2 respectively and and transmitter 26,27 on the scatterer of electrothermal module 6 and 28 temperature measurement unit at the end.Automatic programming device 24 links to each other with the control unit 22 of valve control unit, VCU 23, temperature measurement unit 25 and electrothermal module 6.In the embodiment of a housed device, pond 2,7 and 8 volume are 2 liters.Under the situation of empty pond, the weight of equipment is no more than 5kg, and consumed power is 350W, and size is not more than 300 * 320 * 270mm.
Disclosing of method for purifying water.Equipment through being shown among Fig. 1 is implemented this method for purifying water.The capacity of temperature control work pool 2, is toppled over 1.5 liters tap water by for example 2 liters.The water heating; Cooling, and the contacted thermoelectric element 14 of thermal conduction wall in dependence of all process steps of crystallization and ice thaw and pond is in order to outside work pool, accomplishing equably with the electronic control unit 21 and the automatic mode of the algorithm (program) of implementing water cleansing operation order.The progress chart of round-robin temperature-time is shown in Fig. 2.When electrothermal module 6 is opened into cooling, carry out the water cooling first time.During the water cooling first time, change with the value range that speed equals 0.1-0.3 ℃/minute (line 1 among Fig. 2) through the medium temperature in the work pool, the medium temperature that reduces in the work pool 2 is born 3 ℃ value to being not less than.Further, implemented water crystallization technology for the first time.Water crystallization round-robin time utilization software began to calculate automatically from the moment that water changes for the first time, and the moment that this water changes is that the sidewall medium temperature in detection operations pond raises 0.5 ℃ at least.During first time water crystallization; Change with the value range that speed equals 0.05-0.1 ℃/minute (line 2 among Fig. 2) through the medium temperature in the work pool, reduce the interior medium temperature of work pool to the value that is not less than negative 4.0 ℃ (temperature on the Tc of the liquid brine that contains organic and inorganic pollutant).Whole crystallizations of the pure water of annular solid (toroidal body) form of polluting with heavy water and be after about 360 minutes, to accomplish in the formation that said body includes the liquid brine of organic and inorganic pollutant.In several minutes, with amount discharging salt solution to the salt solution reception tank 8 of 300-550ml.Remain in the ice in the work pool through the heating of transition heat electric device 14 to heating mode., change with the value range that speed equals 0.16-0.18 ℃/minute (line 3 among Fig. 2) through the medium temperature in the work pool up to during it melts fully behind the discharging salt solution in ice thaw, the medium temperature in the rising work pool is to not being higher than positive 10 ℃ value.Implement the heating ice cube through elevated temperature gradually thawed up to it in about 85 minutes fully.Afterwards; Equal 0.1-0.3 ℃/minute value range through the medium temperature in the work pool with speed and be changed to and reach heavy water Tc (being not less than positive 2 ℃) and implement water cooling for the second time, and keep water and under said temperature, be not more than time of 45 minutes up to the complete crystallization of heavy water (line 4 among Fig. 2).Several minutes then is that the finished product of 950-1200ml is to user pond 7 along with filtering form quantity discharged with the thawing water that purifies through second strainer simultaneously.Next, connection equipment is to heating, and several minutes realizes not being higher than+and 10 ℃ temperature is so that the heavy water crystal that remains in the pond 2 melts (line 5 among Fig. 2).Quantity discharged is 50 to 100ml resistates to the pond 8 of being polluted by heavy water.Whole circulations of producing the finished product of the thawing water form that purifies are no more than 480 minutes.The amount of pure thawing water is the 65-80% at least of raw water volume, and the total content of inorganic pollutant descends half at least.
When being necessary the biological activity of the thawing water that the long period keep to purify, the running of actuating equipment up to the thawing water of emission purification to user pond 7, thereby keep for the second time that the water crystallization operation is not higher than in temperature+2 ℃ at least 300 minutes.
Disclosing of water correction plant operation
1. linking device is to power supply.
2. open and cover 3, and the water of the liter of falling 1.5-1.7 (tap water or the tap water that meet Russian national standard (GOST)) is to work pool 2.Close the lid 3.
3. press the power button on the switchboard (not shown), it links to each other with electronic control unit 21.Power light is bright.
4. by starting the operation button.
The following algorithm of the automatic programming device 24 completion equipment operation in electronic control unit 21:
4.1. the control unit 23 of valve is opened valve 15 and 18 ( valve 16 and 17 cuts out).Use from the amount of work pool 2 as the water filter rinsed 20 of 20-50ml and manage 9,10 and 19, and waste discharge to pond 8.
4.2. shut-off valve 15 and 18.
4.3. the electronic control unit 22 of electrothermal module 6 is opened thermoelectric element 14 to cooling mode.Electronic control unit 21 is opened temperature measuring equipment 25, and it provides temperature survey through sidewall that is installed in pond 2 respectively and the TP 26,27 and 28 that reaches on the scatterer of electrothermal module 6 at the end.
4.4. with the Tc that is water-cooled in the pond 2.Subsequently along with in 1 minute, the raising naturally to detect mutually and change of temperature 0.5-1.0 ℃; In other words, temperature 0.5-1.0 ℃ rapid rising is the telltale that changes mutually.Further, carry out crystallization (water-cooled is frozen) technology, it is by providing ice and cool ice to bearing 4-5 ℃ and keep and formed in 4-5 hour.From the direction at wall to the center of work pool 2 formation of ice takes place, it cools off through thermoelectric element 14.Dependence utilizes fan to carry out refrigerative scatterer (not shown) and removes the heat from thermoelectric element 14.
During ice forms, be dissolved in impurity in the water (metal-salt, organic pollutant and other) and be extruded the volume that is positioned at work pool 2 centers, therefore provide brinish to form, it is the water of salt and the rising of all contaminations content.According to given data, these brinish freezing temps are negative 6-7 ℃.
4.5. valve control unit, VCU 23 is opened valve 17 and 18 (shut-off valve 15 and 16).Carried out 2-3 minute from work pool 2 discharging salt solution to ponds 8 through managing 10.Shut-off valve 17 and 18.
4.6. the control unit 22 of electrothermal module 6 is opened thermoelectric element 14 and is got into heating mode.The temperature of the ice in the work pool 2 is increased to 0 ℃, ice-out under this temperature, subsequently one section equal 85 minutes time after, the thawing water of the purification that heating is polluted by heavy water is to+10 ℃.
4.7. then, the control unit 22 of electrothermal module 6 is opened thermoelectric element 14 and is got into cooling mode.Ice temperature in the work pool 2 is reduced to+2 ℃ (stable mode).Then, the control unit 22 of electrothermal module 6 is opened thermoelectric elements 14 and is got into the temperature master modes and be set in the temperature of keeping the thawing waters that purify in the work pool 2 in 2-3 ℃ the scope.Be contained in the heavy water (D in the thawing water
2O) have+3.8 ℃ freezing temp; Like this, when keeping thawing water in+2-+3 ℃ scope the time, the heavy water crystallization is meticulous heavy water crystal.
4.8. after 45 minutes, " EP on the switchboard.Thawing water is ready " marker light indicator bright.In bright back 300 minutes of marker light indicator, can discharge thawing water and closing device.
5. push and dissolve the water button.Valve control unit, VCU 23 is opened valve 16 and 17 (shut-off valve 15 and 18), and discharges thawing waters 3-5 minute through strainer 20 to pond 7 along pipe 9 and 10.Thawing water makes meticulous heavy water (D through the passage of strainer 20
2O) crystal settling is on strainer.Valve control unit, VCU 23 shut-off valves 16 and 17.
6. further, the control unit 22 unlatching thermoelectric elements 14 entering short-terms of electrothermal module 6 heat with the sidewall in heating work pond 2 and the heavy water crystal are melted.Valve control unit, VCU 23 is opened valve 17 and 18 with discharging residual water to pond 8.The control unit 22 of electrothermal module 6 is closed thermoelectric element 14.Electronic control unit 21 closing temperature measuring units 25, and close self.
7. do not have closing device in bright back 300 minutes if do not discharge the marker light indicator of thawing water and " EP; thawing water is ready "; Automatic programming device 24 is kept temperature positive 2 ℃ in the work pool (in order to preserve the structure of thawing water); And after this past time, it sends signal and gives electronic control unit 21, and it says the word for valve control unit, VCU 23.Valve 17 and 18 is opened (shut-off valve 15 and 17).To user pond 7 discharging thawing waters.
8. shut-off valve 17 and 18 is turned off valve to control unit 23, turns off the control unit 22 of electrothermal module 6, turns off temperature measurement unit 25, turns off automatic programming device 24 and turns off electronic control unit 21.Equal total time 480 minutes of the technology of thawing water are provided.
9. push the power-off button.
Table 1 has shown that the water of the inorganic pollutant that is undertaken by Russian Academy Of Sciences siberian branch's geology and Institute of Analysis of mineralogical study institute (Analytical Center of the Institute for Geology and Mineralogy of the Siberian Branch of the Russian Academy of Sciences) purifies the property detection result.
Table 1 water purifies the result of property detection
The inspection of table 1 shown through the method that requires to protect, and the equipment of its request for utilization protection after water purified, has reduced the content of inorganic pollutant.Calcium contents reduces 1/1.8-1/1.5, and magnesium reduces 1/2, and potassium reduces 1/1.7-1/2.7.Sodium content reduces more than half.Therefore, analytical results has proved the appreciable degree of water purifying inorganic impurity.
Therefore; Compare with correlation technique with the prior art state; Be used for requirement method of protecting and the equipment that requires protection that water purifies; Owing to the axial at work pool has concentrated removable organic thawing water of having traped the heavy water crystal and purification is provided with inorganic pollutant, dependence secondary filter in+2 ℃ storage, therefore improved the character of water purification impurity and heavy (heavy hydrogen and tritium) water; Size and weight that thermoelectric original paper, equipment are moderate and the automated operation that runs through water purification process have improved the accessibility that equipment uses.Automatically water purification process since selected best freezing with melt progress chart (speed, time, temperature and other) and also reduced the time that finished product needs that obtains.
Claims (7)
1. method for purifying water; Be included in the water cooling first time in the temperature control work pool and little by little refrigerated water for some time is enough to make the complete crystallization of pure water of being polluted by heavy water and makes by organic liquid brine formation of polluting with inorganic pollutant under the temperature of the Tc that surpasses the liquid brine of being polluted by organic and inorganic pollutant subsequently; Discharge said salt solution; Using rises gradually reaches the temperature value heating ice cube above the Tc of heavy water; And make ice maintain under the said temperature and thaw fully up to it, be water-cooled to the Tc of heavy water for the second time, and it is maintained under the said temperature up to the complete crystallization of heavy water; Make finished product be disposed to the user pond its filtration through secondary filter simultaneously with the snowmelt form that purifies; It is characterized in that: the contacted thermoelectric element of thermal conduction wall in the heating of water, cooling and crystallization and ice thaw dependence and pond is implemented outside work pool with automatic mode equably, during the water cooling first time, equals 0.1-0.3 ℃/minute value range through the medium temperature in the work pool with speed and changes; The medium temperature that reduces in the work pool is born 3 ℃ value to being not less than; For the first time water crystallization round-robin time utilization software begins to calculate from the moment that water changes with automatic mode, and the side wall temperatures that the moment that this water changes is detected as work pool raises time of 0.5 ℃ at least, during first time water crystallization; Equaling 0.05-0.1 ℃/minute value range through the medium temperature in the work pool with speed changes; Reduce medium temperature in the work pool to the value that is not less than negative 4.0 ℃, up to during it melts fully behind the discharging salt solution, equal 0.16-0.18 ℃/minute value range through the medium temperature in the work pool with speed and change in ice thaw; Medium temperature in the rising work pool is to not being higher than positive 10 ℃ value; And during second water cooling and heavy water crystallization, with the value range variation that speed equals 0.1-0.3 ℃/minute, reduce the interior medium temperature of work pool to being not less than positive 2 ℃ value through the medium temperature in the work pool.
2. according to the method for purifying water of claim 1, it is characterized in that: no longer than 360 minutes, and the full cycle of producing as the finished product of the thawing water that purifies was no more than 480 minutes from the organic and inorganic pollutant of purifying waste water to the discharging brinish time.
3. according to the method for purifying water of claim 1, it is characterized in that: the biological activity of the thawing water that keep to purify for the long term, keep for the second time that water crystallization is not higher than in temperature+2 ℃ be disposed to the user pond up to Jiang Shui at least 300 minutes.
4. according to the method for purifying water of claim 1, it is characterized in that: the volume of pure snowmelt is at least 65% of a former volume of water, and the total content of inorganic impurity reduces at least 50%.
5. water correction plant; Comprise shell (1); The work pool (2) of (4) at the bottom of being provided with lid (3) in it and the inclination of water discharge orifice (5) being arranged; Be equipped with control unit (21) in order to refrigerated water with make the device of ice thaw, contain the pond (8) of water of the heavy hydrogen content of pollutent and raising in order to the user pond (7) that receives the thawing water that purifies with in order to reception; The pipe (9 and 10) that wherein has water emission control system (11); Link to each other with discharge orifice (5) in order to (4) at the bottom of the inclination of refrigerated water and the work pool that makes ice thaw (2); Wherein delivery pipe (13 and 12) is installed in the top in pond (8) of the water of the heavy hydrogen content that contains pollutent and raising in order to the user pond (7) of the thawing water that receive to purify with in order to reception respectively; It is characterized in that: water-cooled is frozen with the ice thaw device and is presented as electrothermal module (6), comprises being positioned in order to refrigerated water and outer several thermoelectric elements (14) of the sidewall of the work pool (2) that makes ice thaw, and the interior water emission control system (11) of pipe (9 and 10) comprises the valve of usually closing (15 of mounted in pairs in it; 16; 17 and 18), and said water discharge spout (9 and 10) interconnects through the pipe (19) that has second water filter (20) in addition, and this pipe and the tie point of water discharge spout (9 and 10) are positioned at the valve (15 of the water emission control system of said pipe (9 and 10); 16,17 and 18) between.
6. according to the equipment of claim 5, it is characterized in that: work pool (2) is made as the orthogonal shape, and the ratio of height and length and width be respectively be not less than 1.0 be not more than 1.2.
7. according to the equipment of claim 5, it is characterized in that: water-cooled is frozen the electronic control unit (22) that comprises electrothermal module (6) with the control unit (21) of ice thaw device; The control unit (23) of the water discharging valve (15-18) that links to each other with said valve (15-18); Automatic programming device (24); And have be installed in water-cooled freeze with the end (4) of ice thaw pond (2) and sidewall on and transmitter (26 on the scatterer of electrothermal module (6); 27 and 28) temperature measurement unit (25), wherein automatic programming device (24) links to each other with the electronic control unit (22) of control unit (23), temperature measurement unit (25) and electrothermal module (6) of valve (15-18).
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PCT/RU2009/000028 WO2010087731A1 (en) | 2009-01-29 | 2009-01-29 | Water purification method and a device for carrying out said method |
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CN (1) | CN102387994A (en) |
UA (1) | UA101430C2 (en) |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
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CN105217708A (en) * | 2015-10-28 | 2016-01-06 | 湖北华巳新能源环保工程有限公司 | A kind of cryogenic freezing Sewage treatment systems |
WO2017071039A1 (en) * | 2015-10-31 | 2017-05-04 | 深圳市易特科信息技术有限公司 | Water purifier for filtering heavy water |
CN110156106A (en) * | 2019-05-28 | 2019-08-23 | 深圳鼎邦健康科技有限公司 | A kind of preparation method of low deuterium-oxide |
CN113631518A (en) * | 2018-12-29 | 2021-11-09 | 普里斯蒂南有限责任公司 | System for purifying water by recrystallization and heat exchange device for realising same (variants) |
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CN117907163B (en) * | 2024-03-19 | 2024-05-24 | 四川沃耐稀新材料科技有限公司 | Lanthanum chloride cooling crystallization screening is with survey device |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
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JPH02194888A (en) * | 1989-01-20 | 1990-08-01 | Toshiba Corp | Pure water producing apparatus |
JP3028666B2 (en) * | 1991-11-05 | 2000-04-04 | 東陶機器株式会社 | Water purification method and apparatus |
RU2221201C2 (en) * | 2002-02-26 | 2004-01-10 | Малахов Анатолий Иванович | Liquid freezing device |
RU2274607C2 (en) * | 2003-02-17 | 2006-04-20 | Евгений Николаевич Высоцкий | Method of purification of water and the installation for its realization |
RU2344092C2 (en) * | 2006-07-31 | 2009-01-20 | Евгений Николаевич Высоцкий | Water treatment method and plant |
-
2009
- 2009-01-29 UA UAA201110387A patent/UA101430C2/en unknown
- 2009-01-29 WO PCT/RU2009/000028 patent/WO2010087731A1/en active Application Filing
- 2009-01-29 CN CN2009801576379A patent/CN102387994A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
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CN105217708A (en) * | 2015-10-28 | 2016-01-06 | 湖北华巳新能源环保工程有限公司 | A kind of cryogenic freezing Sewage treatment systems |
WO2017071039A1 (en) * | 2015-10-31 | 2017-05-04 | 深圳市易特科信息技术有限公司 | Water purifier for filtering heavy water |
CN113631518A (en) * | 2018-12-29 | 2021-11-09 | 普里斯蒂南有限责任公司 | System for purifying water by recrystallization and heat exchange device for realising same (variants) |
CN110156106A (en) * | 2019-05-28 | 2019-08-23 | 深圳鼎邦健康科技有限公司 | A kind of preparation method of low deuterium-oxide |
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UA101430C2 (en) | 2013-03-25 |
WO2010087731A1 (en) | 2010-08-05 |
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