Method for spraying and desalting through residual pressure of reverse osmosis concentrated water

26-05-2010 дата публикации
Номер:
CN0101712521A
Контакты:
Номер заявки: 07-10-20091167
Дата заявки: 05-11-2009

[1]

Technical Field

[2]

The invention belongs to the field of water treatment technology, relates to industrial water treatment, environmental pollution treatment, sea water and myoporum saltiest salt water desalination, reverse osmosis system in the field of purification of the condensed water. More specifically it is a kind of reverse osmosis practical knowledge -odd pressure spray desalination method.

[3]

Background Art

[4]

Reverse osmosis technology utilize the external force (overcome the osmotic pressure) and by means of a film trap function is selected, the solute in the solution separation with a solvent, so as to achieve the purpose of the pure water. This technology has now been widely applied in industrial water treatment, environmental pollution treatment, sea water and myoporum saltiest salt water desalination, etc., but in the process, the material of the membrane , the influence of factors such as the types of water quality, desalting fine water generating at the same time there are a large number of tracing thick salt water discharge, water quantity of about 1/3 the left and right. Reverse osmosis concentrated salt water has a salt-containing high, containing difficult to degrade the contaminants and the like, thus existing conventional method is difficult to carry out effective processing.

[5]

In addition to the purposes of the present method, can be mainly divided into: thermal energy law (multi-effect distillation, multi-stage flash evaporation, solar distillation, freezing, etc.), chemical (ion exchange method, solvent extraction, hydrate method, chemical precipitation method), electric-membrane (electric to ionic, electroosmosis chromatography), electric adsorption, pressure-film method (multi-stage reverse osmosis, nona) and other 5 types of. The desalting with the chemical method, a low level of salt, those can be removed only poorly soluble substances can be converted into salts, that is, calcium, magnesium, iron, manganese cation of the salt. As for the sodium, potassium, and the like has no cationic salt of. Especially in the ion concentration of chlorine in water is relatively high, the effect of precipitation thereof greatly discounted, large range of application of the constraint; electrical-membrane (electric to ionic, electrodialysis law) adsorption technology such as the initial equipment investment is large, the pre-treatment process is complicated, tedious management and operation, for reverse osmosis concentrated water processing will have a relatively high cost of water; in the thermal energy law , solar distillation, freezing france receives to the natural conditions, evaporation and crystallization rate is relatively low, the industrial field is very difficult to adapt to the requirements of the water treatment. Multi-effect distillation (MED), such as multi-stage flash distillation (MSF) method is to utilize low-grade waste heat in a plurality of ordered arrays of the container, heating and evaporation of the high-concentration saline water steam is generated, steam condensed to obtain the high-quality fresh water. Multi-stage flash distillation (MSF) to take step-down expansion method of flash evaporation of sea water, and the multi-effect distillation (MED) is used for the evaporation of sea water vapor direct heating steam, because the characteristics of the two process, than the progression of the MSF system MED counts of the system. In order to improve the energy utilization rate, reduce the cost, the search for high-efficient heat pump is still not solved.

[6]

Pressure-film method (multi-stage reverse osmosis, nona) from the 20 century 70 1990s. since put into application, has been the search for processing condensed water, the method of reducing the associated operating costs, but only depend on the development of multi-stage series of membrane technology to solve the problem of concentrated water is not enough, also need other method the cost is reduced. Unfortunately a large amount of energy used to provide high pressure of the system, and this partial pressure most of the losses are wasted, if in accordance with the usual 40% recovery rate calculation, the concentrated salt water accounts for about 60% of the energy feed pressure. Since there is not yet effective method for treating the concentrated water, the reverse osmosis device increased the cost of water, at the same time waste of a large amount of energy, concentrated salt water pollution to the environment is still the problem of unable to effectively solve the problem.

[7]

Content of the invention

[8]

The purpose of the invention is to establish a set of reverse osmosis system used for processing of the high-concentrated salt water technique and apparatus, this method mainly utilizes the process of water in the reverse osmosis system of the self-produced form practical knowledge excess pressure high salt water fog, save the conventional atomizing the required power, the flow of fine small drops evaporate rapidly in the air, separation of impurities such as water and the salts, and, at the same time the organic matter contained in the water is oxidized to carbon dioxide, water vapor input condensation as pure water, and salt and the high water concentration of the bottom of the drop in the separating chamber, is mixed with the initial adopts after circulating water, continue to atomizing concentrated to saturation state, through the heat exchanging the salt-containing separation by crystallization after condensation, ultimately achieving reverse osmosis water purification and salinity removing condensed water. The invention changes the existing reverse osmosis operation of the device and its concentrated water treatment method, the cost of water-saving, generated by reverse osmosis can greatly reduce the high concentrated salt water emissions, reduce the concentrated salt water discharged to the peripheral environment of the negative impact caused by, suitable for all kinds of reverse osmosis system for purifying condensed water produced. The technical scheme of the present invention are as follows:

[9]

A kind of reverse osmosis practical knowledge -odd pressure spray desalination method, which is characterized in that according to the following steps:

[10]

1) the waste water under the high pressure of the reverse osmosis device (1) separating the waste water for the concentrated water;

[11]

2) the concentrated water through the heat exchanging system (2) after preheating, through the mixed exchanger (3) directly enters the atomization room (4), the energy of the concentrated water in through the pressure the rotary atomizer, the water in the spray nozzle on the front end of the disc, depending on the high-speed rotation of the disc will be made into a thin film the practical knowledge unfolds , by "centrifugal force spray" and "speed spray" comprehensive effect of the water droplet atomizing;

[12]

3) after the atomization the practical knowledge bubble passes through of the temperature control heating system (5) of the contact buckles, forming water vapor and water preparation over into the dense workpiece;

[13]

4) by the induced draft fan (7) the water vapor and air flow out of the evaporation chamber into the gas-powder separator (8), entrained in the air are removed salt powder, and then the condensed water collector (9) is condensed into fresh water and so as to be recovered;

[14]

5) the tail water entering into the tail water distribution system (11), the salinity and temperature of the on-line monitoring, feedback information: when the tail water salinity to approach or reach the saturation, the collector adopts the tail water of crystallization (10) cooling crystallization, the desalting; adopts the not yet reached saturation, directly flow back to the mixed exchanger (3) after being mixed with the condensed water re-entering the atomization room (4) circulation evaporation;

[15]

6) the crystallization is carried out by entering the salt salty dregs tail materialdregs tail material collector (12) centralized processing after storage.

[16]

The invention the reverse osmosis practical knowledge -odd pressure spray desalination method, in the step 3) the temperature in the heating system of the hot air from the air blower (6) and is blown in the room, the air source can be air and inferior goods heat steam, operating temperature is 50-100 the [...].

[17]

The invention the reverse osmosis practical knowledge -odd pressure spray desalination method, in the step 1) of the waste water in is referred to: industrial waste water, environmental pollution treatment of the waste water, sea water and myoporum saltiest salt water.

[18]

The invention the reverse osmosis practical knowledge -odd pressure spray desalination method, in the step 1) of the reverse osmosis device in discharged pressure is 1.5-20 MPa. The invention the reverse osmosis practical knowledge -odd pressure spray desalination method, in the step 1) of the salt in dregs tail material collector (12) is made of corrosion and a polytetrafluoroethylene material processing, collection utility rectangular box structure.

[19]

The invention the reverse osmosis practical knowledge -odd pressure spray desalination method for the principle of the invention:

[20]

Reverse osmosis system utilizes the high pressure of the water separation for desalting fine water and waste thick salt water (hereinafter referred to as: the concentrated water), wherein the concentrated water from the membrane reactor pressure is as high as 1.5-20 MPa. The invention will be the concentrated water after preheating by the heat exchange system, directly enters the atomization room, the energy of the concentrated water in through the pressure-operated rotary atomizer, concentrated indoor sprays atomized fog-shaped, and spiral track movement. At the same time its atomization is concentrated indoor, the water drops suspended in the air flow to a very small volume, the diameter generally the 100 within   m, specific surface area is very large, the heat transfer with the surrounding air, after the atomization of the contact and wiring terminal practical knowledge bubble , the moisture in the condensed water to evaporate rapidly become water vapor, in the middle part of the concentrated water is oxidized or volatile organic matter, the concentrated water from the concentrated to tail water is high. After the end of the evaporation process, the water vapor by the draft fan and air flow out of the evaporation chamber into the gas-powder separator, entrained in the air are removed salt powder, then through the heat exchange system of the fresh water of condensation and recovery. Concentrated rear tail water entering into the tail water distribution system, the salinity and temperature of the on-line monitoring, feedback information to the intelligent decision-making: when the tail water salinity to approach or reach the saturation, will enter heat exchange system adopts the cooling crystallization, the desalting; adopts the not yet reached saturation, direct return to the mixing exchanger, and the concentrated heat, energy and material content of the mixture, into the atomization room circulation evaporation. In this invention heat the steam by the blower blown into the atomization room, the air source can be air and inferior goods heat steam, generally in the operating temperature of the 50-90 [...] , can also be according to the actual need, in the temperature control heating system is improved in intake air temperature, enhanced oxidizing water desalination and the effect of organic matter.

[21]

The invention the reverse osmosis practical knowledge -odd pressure spray desalination method of the detailed steps are as follows:

[22]

(1) according to the required evaporation of water, adjusting inflow gas flow rate and temperature, the atomization gas into the room.

[23]

The operation carried out mainly in the air circulation system, the air circulation system comprises a blower, a temperature control heater, gas source can be air and the hot steam inferior goods , the composed of a blower and gas enters the temperature control heater, according to the actual situation of the heater, the operating temperature of the inflow gas in general the 50-90 [...] , can also be according to the final processing requirements, the intake air temperature is raised, enhancing desalting efficiency and improve the effect of the oxidation of organic matter in the water mist. After the inflow gas to the temperature required, entering the atomization room, with the induced draft fan in the indoor structure is a whole under suction effect of the circling motion.

[24]

(2) the reverse osmosis of discharged concentrated water heat system preheating.

[25]

The operation step is carried out in the heat exchange system, the aim is to improve the temperature of the concentrated water when atomized, atomization evaporation time is shortened. The heat exchange system mainly the atomized water steam, the reverse osmosis and after concentrating the heat exchange between the condensed water, the water steam, after concentrating the heat of the concentrated water is transmitted to the reverse osmosis. The exchange of heat between the steam and the condensed water by using embedded steam-water heat exchanger to carry through, after concentrating with concentrated the water depends on the heat-pipe exchanger to achieve heat transfer.

[26]

(3) after preheating atomizing the room in the atomization of the condensed water.

[27]

The operation of the atomizing concentrating compartment, the concentrated water first enters the pressure the rotary atomizer, through the device, the front end of the disc in the nozzle the practical knowledge gushes in , rely on high-speed rotation of the disc will be made into a thin film the practical knowledge unfolds , by "centrifugal force spray" and "speed spray" comprehensive effect of the water droplet atomizing; the device can make the atomized droplets more narrow particle size distribution, more uniform, when the condensed water using reverse osmosis to produce the excess pressure of the concentrated water into a diameter of 100 the water drops within   m, and the rotating the spray nozzle to spray the same in the gas stream at the top of the concentration chamber, relying on the sprayed water mist suspended in the centrifugal action of a the top of the atomization room of the movement of the airflow in a spiral state, the movement track of the time the water droplet settling process, improving the atomization at the same time evaporating effect of the water globules.

[28]

(4) concentrated water atomized droplets contact with inflow air mixing, evaporation and concentration.

[29]

In the process for atomizing and concentrating, after the inflow air into the atomizing concentrating, guiding the inner wall under the action of drainage of the fan to Backpitch state flow, and the top of the dense water mist which the movement of the double-spiral flow around the structure, because the atomization of the suspension in the air flow to a very small volume practical knowledge bubble , specific surface area is very large, the inflow air for heat transfer, thus concentrated water most of the moisture to evaporate rapidly become water vapor, forming fine salt particles and adopts high power concentration, particle size minor salt dust floating in the air stream, and after concentrating concentrating fogdrops of formed at the bottom part of the tail water. Furthermore, in the contact process of evaporation of the contained practical knowledge bubble central is oxidation and volatilization of organic matter.

[30]

(5) the condensation of the hot steam.

[31]

After the end of the evaporation process, the step from an induced draft fan (4) the water vapor and air flow out of the vaporizing chamber in the form of gas-powder separator, through the separator to remove air entrained in the salt material powder, salt and other impurities can be used for keeps out the chamber after being collected, the snow melting in winter, the purified mixed gas to enter the heat exchange system, relying on the embedded heat exchanger for steam and water the gas condensation and reverse osmosis concentrated water preheating, for steam condensation enters the collector shui Dan and recovery, other gas is discharged into the air.

[32]

(6) concentration of tail water of regulation and processing.

[33]

The process is mainly the control system adopts, the heat exchange system in the mixed exchanger, can be divided into the following three sub-steps:

[34]

(1) control of water concentrated workpiece.

[35]

Step (4) is high times the drainage to concentrate the water distribution system, the system can be to the tail water concentration and the temperature of the salt in the on-line test and monitoring, according to the system feedback information to intelligent decision-making, according to the tail the temperature of the first decision-making, to assess the condition of the tail water saturation temperature the solubility of the salt, the salt content of the monitoring by a combination of the judge whether the system reached or is close to saturation, when the tail water salinity to approach or reach the saturation, will be deployed to adopts the heat exchange system; the saturation has not been attained, after being mixed directly with the condensed water, to re-enter the atomization room circulation evaporation.

[36]

(2) approach or reach saturation condensation of tail water of crystallization.

[37]

Saturated adopts are deployed to the heat exchange system, through the heat exchange pipe to reverse osmosis to discharge the initial concentrated water preheating, when the temperature is reduced to the set saturation solubility when the corresponding temperature, will be discharged to the collector adopts a large amount of condensation in the crystallization, the secondary removal of the salt.

[38]

(3) non-saturated tail water circulating concentrated

[39]

The non-saturated adopts direct reflux to the mixing exchanger, and the condensed water is mixed in the heat exchanger, energy and material content mixed, and then to re-enter the atomization room circulation evaporation.

[40]

Reverse osmosis practical knowledge -odd pressure spray desalination effect contrast table 1

[41]

   COD  The concentration is not limited to  ≤ 40  Potassium dichromate chlorine calibration method     GB/T   11914-1989     HJ/T70-2001
   BOD  The concentration is not limited to  ≤ 5  Dilution and inoculation method    GB7488-87
   TN  The concentration is not limited to  ≤ 10  Alkaline potassium persulphate-digestion by ultraviolet spectrophotometry    GB11894-89
 Ammonia nitrogen  The concentration is not limited to  ≤ 5  Distillation and titration    GB7478-87
   TP  The concentration is not limited to  ≤ 0.5  Ammonium molybdate spectrophotometry    GB11893-89
 The salt content  The concentration is not limited to  ≤ 1000    EDTA titration     GB   5750-1985
 Total hardness  The concentration is not limited to  ≤ 200    EDTA titration     GB   5750-1985
   TDS  The concentration is not limited to  ≤ 500  A gravimetric method     GB   5750-1985

[42]

The present invention further discloses the reverse osmosis practical knowledge -odd pressure spray desalination method for preparing various types of reverse osmosis system waste thick the application of the salt water, is not influenced by the concentrated water and reverse osmosis device categories of restricted, and can be jointly used with other processing method. Which comprises preparing a separation industrial waste water, environmental pollution treatment of the waste water, sea water and the application of the salt water.

[43]

This invention relates to reverse osmosis practical knowledge -odd pressure spray desalination method and the prior art has the technical characteristics and the positive effects:

[44]

(1) the excess pressure of concentrated water using reverse osmosis atomized, saving power for atomization, the structure is simple, the manufacturing cost is low.

[45]

(2) is not influenced by the concentrated water and reverse osmosis device categories of restricted, processing range is wide, it is easy to realize and the popularization and application, can be conveniently realized with traditional desalination method for coupling, improving the overall economic efficiency of the desalination desalination process.

[46]

(3) the device scale flexible, convenient dispersed using, in addition to nozzle components, the operating pressure is mostly atmospheric pressure, generally in the operating temperature of the 50-90 [...] , easy to use low level heat energy as a source of energy, which is cheap and easy to obtain the high-molecular material manufacturing equipment.

[47]

(4) the theoretical 99% more concentrated salt water evaporation processing, into the fresh water and concentrated of the discharge amount of the water is quite small, reducing secondary pollution of the environment, the tail water of the salt slurry of outputs can be used in chemical, building materials and other industries.

[48]

(5) the gasification process in the gas-liquid interface of the non-equipment wall surface and, therefore, the device the fouling tendency of small, feeding pre-processing requirement is low, the operation is simple, replacement and the maintenance is convenient.

[49]

Description of drawings

[50]

The invention offers a structure diagram of the measuring device. On the drawings, 1-reverse osmosis device, 2-heat exchange system, 3-mixed exchanger, 4-atomization room, 5-temperature control heating system, 6-blower, 7-an induced draft fan, 8-powder-gas separator, 9-condensed water collector, 10-crystalline tail water collector, 11-concentrated tail water distribution system, 12-salt dregs tail material collector.

[51]

Mode of execution

[52]

The following embodiments to help understanding of the invention, and is not used for also should not be construed as in any way to the requirements set out in the right limit of the invention.

[53]

Embodiment 1

[54]

1) the waste water under the high pressure of the reverse osmosis device (1) separating the waste water for the concentrated water; a gas source (may be air and hot vapor inferior goods) by the blower (6) into the temperature-controlled heater (5), the heater according to the required evaporation of the concentrated water quantity and temperature, and other practical situation, the inflow gas control in the general operating temperature (the 50-90 [...]), rely on an induced draft fan (7) into the suction effect of the atomization room;

[55]

2) the concentrated water through the heat exchanging system (2) preheating, heat exchange system (2) is mainly the atomized water steam, the reverse osmosis and after concentrating the heat exchange between the condensed water, the water steam, after concentrating the heat of the concentrated water is transmitted to the reverse osmosis. The exchange of heat between the steam and the condensed water by using embedded steam-water heat exchanger to carry through, after concentrating with concentrated the water depends on the heat-pipe exchanger to achieve heat transfer.

[56]

3) through the mixed exchanger (3) directly enters the atomization room (4), the energy of the concentrated water in through the pressure the rotary atomizer, the front end of the water spray into the disc, rely on high-speed rotation of the disc will be made into a thin film the practical knowledge unfolds , by "centrifugal force spray" and "speed spray" comprehensive effect of the water droplet atomizing;

[57]

4) after the atomization the practical knowledge bubble passes through of the temperature control heating system (5) of the contact buckles, guiding the inner wall under the action of drainage of the fan to Backpitch state flow, and the top of the dense water mist which the movement of the double-spiral flow around the structure, forming water vapor and water preparation over into the dense workpiece;

[58]

5) by the induced draft fan (7) the water vapor and air flow out of the evaporation chamber into the gas-powder separator (8), entrained in the air are removed salt powder, and then the condensed water collector (9) is condensed into fresh water and so as to be recovered;

[59]

6) concentrating the tail of the water entering into the tail water distribution system (11), the salinity and temperature of the on-line monitoring, feedback information: when the tail water salinity to approach or reach the saturation, the collector adopts the tail water of crystallization (10) cooling crystallization, the desalting; adopts the not yet reached saturation, directly flow back to the mixed exchanger (3) after being mixed with the condensed water re-entering the atomization room (4) circulation evaporation;

[60]

7) in the process of atomizing, evaporating, the crystallization is carried out by entering the salt salty dregs tail materialdregs tail material collector (12) centralized processing after storage.

[61]

Embodiment 2

[62]

1) waste water in the high-pressure 2.5 MPa by the reverse osmosis device (1) for separating the waste water desalting fine water and waste thick salt water (concentrated water);

[63]

2) the concentrated water through the heat exchanging system (2) after preheating (the 40 [...]), through the mixed exchanger (3) directly enters the atomization room (4), in use the energy of the concentrated water through the improved pressure type rotary atomizer;

[64]

3) after the atomization the practical knowledge bubble passes through of the temperature control heating system (the 90 [...]) processing the contact buckles, forming water vapor and water preparation over into the dense workpiece;

[65]

4) by the induced draft fan (7) the water vapor and air flow out of the evaporation chamber into the gas-powder separator (8), entrained in the air are removed salt powder, and then the condensed water collector (9) is condensed into fresh water and so as to be recovered;

[66]

5) the tail water entering into the tail water distribution system (11), the salinity and temperature of the on-line monitoring, feedback information: when the tail water salinity to approach or reach the saturation, the collector adopts the tail water of crystallization (10) cooling crystallization, the desalting; adopts the not yet reached saturation, directly flow back to the mixed exchanger (3) after being mixed with the condensed water re-entering the atomization room (4) circulation evaporation;

[67]

6) in the process of atomizing, evaporating, the crystallization is carried out by the apparatus for storing the collection salty dregs tail material centralized processing.

[68]

Embodiment 3

[69]

1) waste water in the high-pressure 7 MPa by the reverse osmosis device (1) for separating the waste water desalting fine water and waste thick salt water (concentrated water);

[70]

2) the concentrated water through the heat exchanging system (2) after preheating (the 40 [...]), through the mixed exchanger (3) directly enters the atomization room (4), in use the energy of the concentrated water through the improved pressure type rotary atomizer;

[71]

3) after the atomization the practical knowledge bubble passes through of the temperature control heating system (the 90 [...]) treated with dry hot air, forming water vapor and water preparation over into the dense workpiece;

[72]

4) by the induced draft fan (7) the water vapor and air flow out of the evaporation chamber into the gas-powder separator (8), entrained in the air are removed productivity salts substances, and then the condensed water collector (9) is condensed into fresh water and so as to be recovered;

[73]

5) the tail water entering into the tail water distribution system (11), the salinity and temperature of the on-line monitoring, feedback information: when the tail water salinity to approach or reach the saturation, the collector adopts the tail water of crystallization (10) cooling crystallization, the desalting; adopts the not yet reached saturation, directly flow back to the mixed exchanger (3) after being mixed with the condensed water re-entering the atomization room (4) circulation evaporation;

[74]

6) in the process of atomizing, evaporating, the crystallization is carried out by the apparatus for storing the collection salty dregs tail material centralized processing.

[75]

Embodiment 4 (steel waste water reclamation and reuse embodiment)

[76]

A iron and steel group internal non-conventional sources of water supply, therefore the production of waste water, rain water and domestic sewage water source such as the centralized processing method for regenerating and recycling provide supplementary water circulating water and the production and use, by the treatment of the waste water, biochemical processing and microfiltration processing enters the reverse osmosis (RO) system, the high-concentration salt water produced by the system of the invention perform the following processing:

[77]

1) waste water in the 1.6 MPa under the high pressure of the reverse osmosis device (1) separated into desalted fine water and waste thick salt water (concentrated water), the concentrated water outlet pressure reaches the 1.54 MPa left and right;

[78]

2) the concentrated water enters the heat exchange system (2), and after the atomization of the water steam, after concentrating the heat exchange tube, and the, water vapor and concentrating the heat can be transferred to the reverse osmosis concentrated water, after having been preheated to 50 the left and right [...] , through the mixed exchanger (3) directly enters the atomization room (4), its own lubricator using concentrated water, atomized through pressure-operated rotary atomizer;

[79]

3) after the atomization the practical knowledge bubble passes through of the temperature control heating system (the 90 [...]) treated is contacted with the dry hot air, forming water vapor and water preparation over into the dense workpiece;

[80]

4) by the induced draft fan (7) the water vapor and air flow out of the evaporation chamber into the gas-powder separator (8), entrained in the air are removed salt powder, and then the condensed water collector (9) is condensed into fresh water and so as to be recovered;

[81]

5) the tail water entering into the tail water distribution system (11), the salinity and temperature of the on-line monitoring, feedback information: when the tail water salinity to approach or reach the saturation, the collector adopts the tail water of crystallization (10) cooling crystallization, the desalting; adopts the not yet reached saturation, directly flow back to the mixed exchanger (3) after being mixed with the condensed water re-entering the atomization room (4) circulation evaporation;

[82]

6) in the process of atomizing, evaporating, the crystallization is carried out by the apparatus for storing the collection salty dregs tail material centralized processing;

[83]

7) concentrated water and atomization obtained by the processing of fresh water quality are shown in table 2

[84]

Steel waste water through the reverse osmosis resulting concentrated water Classic -odd pressure spray desalination effect contrast table 2

[85]

   COD    214    38.5  Potassium dichromate chlorine calibration method     GB/T   11914-1989     HJ/T70-2001
   BOD    10.1    4.2  Dilution and inoculation method    GB7488-87
   TN    28.5    9  Alkaline potassium persulphate-digestion by ultraviolet spectrophotometry    GB11894-89
 Ammonia nitrogen    1.23    0.95  Distillation and titration    GB7478-87
   TP    1.32    0.4  Ammonium molybdate spectrophotometry    GB11893-89
 The salt content    9580    458    EDTA titration     GB   5750-1985
 Total hardness    1448    150    EDTA titration     GB   5750-1985
   TDS    9320    450  A gravimetric method     GB   5750-1985

[86]

In the detailed description following of the preferred embodiment, those familiar with the art can clearly understand, without deviating from the scope and spirit of the above-mentioned Patent application can be carried out under various changes and modifications, where according to the invention the technical essence to the above embodiment any simple modification the, equivalent to change and modification, are the scope of the technical scheme of the invention. The invention also is not influenced by the example in the specification of the example embodiment.



[1]

The invention establishes a method for treating waste concentrated saltwater of reverse osmosis systems. The method mainly comprises the following steps that: the residual pressure of concentrated water produced by the self of a reverse osmosis system during water production is utilized to form high-salt spray so as to save power needed by conventional atomization; tiny water droplets quickly evaporate in floating air so as to separate water, salt and other impurities; meanwhile, organic matter contained by the water is oxidized to be carbon dioxide; vapor is input into a condensing chamber to turn into pure water, while salt and high-power tail water fall to the bottom of a separation chamber; the tail water and initial inflow water are mixed and circulated and then continue to be atomized and concentrated to a saturation state; the contained salt is subjected to heat-exchange condensation and then crystallization and precipitation; and water purification and salinity removal of reverse osmosis concentrated water are finally realized. The desalting and pollutant-reducing method for reverse osmosis concentrated water is suitable for the separation of the waste concentrated saltwater produced by every type of reverse osmosis systems.



1. A kind of reverse osmosis practical knowledge -odd pressure spray desalination method, which is characterized in that according to the following steps:

1) the waste water under the high pressure of the reverse osmosis device (1) separating the waste water for the concentrated water;

2) the concentrated water through the heat exchanging system (2) after preheating, through the mixed exchanger (3) directly enters the atomization room (4), the energy of the concentrated water in through the pressure the rotary atomizer, the water in the spray nozzle on the front end of the disc, depending on the high-speed rotation of the disc will be made into a thin film the practical knowledge unfolds , by "centrifugal force spray" and "speed spray" comprehensive effect of the water droplet atomizing;

3) after the atomization the practical knowledge bubble passes through of the temperature control heating system (5) of the contact buckles, the water preparation over into the dense workpiece;

4) by the induced draft fan (7) the water vapor and air flow out of the evaporation chamber into the gas-powder separator (8), entrained in the air are removed salt powder, and then the condensed water collector (9) is condensed into fresh water and so as to be recovered;

5) the tail water entering into the tail water distribution system (11), the salinity and temperature of the on-line monitoring, feedback information: when the tail water salinity to approach or reach the saturation, the collector adopts the tail water of crystallization (10) cooling crystallization, the desalting; adopts the not yet reached saturation, directly flow back to the mixed exchanger (3) after being mixed with the condensed water re-entering the atomization room (4) circulation evaporation;

6) the crystallization is carried out by entering the salt salty dregs tail materialdregs tail material collector (12) centralized processing after storage.

2. Reverse osmosis practical knowledge -odd pressure spray desalination method according to Claim 1, wherein step 3) the temperature in the heating system of the hot air from the air blower (6) and is blown in the room, the air source can be air and inferior goods heat steam, operating temperature is 50-100 the [...].

3. Reverse osmosis practical knowledge -odd pressure spray desalination method according to Claim 1, wherein step 1) of the waste water in is referred to: industrial waste water, environmental pollution treatment of the waste water, sea water and myoporum saltiest salt water.

4. Reverse osmosis practical knowledge -odd pressure spray desalination method according to Claim 1, wherein step 1) of the condensed water in the means: for separating the waste water desalting fine water and waste thick salt water.

5. Reverse osmosis practical knowledge -odd pressure spray desalination method according to Claim 1, wherein step 1) of the reverse osmosis device in discharged pressure is 1.5-20 MPa.

6. Claim 1-5 to any one of the reverse osmosis practical knowledge -odd pressure spray desalination method for preparing various types of reverse osmosis system waste thick the application of the salt water.

7. Applications include preparing a separation industrial waste water according to Claim 6, environmental pollution treatment of the waste water, sea water and the application of the salt water.

8. Reverse osmosis practical knowledge -odd pressure spray desalination method according to Claim 1, wherein step 1) of the salt in dregs tail material collector (12) is made of corrosion and a polytetrafluoroethylene material processing, collection utility rectangular box structure.