Installation for preparation of desalinated water for synthesis-gas production. RU patent 2506233.
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Method of sewage purification from cyanide-ions / 2501743 Method of sewage purification from cyanide-ions includes its processing with sulfate of bivalent iron in quantity 293 wt.p to 100 wt.p. CN-ions in presence in water of sorbent in form of fibrillated cellulose fibres, which contain in wt %: not less than 54% of fibres with length not more 0.63 mm and not less than 94% of fibres with length not more than 1.23 mm, with formation of reaction product in form of insoluble particles of iron cyanide. Reaction product is obtained in form of composite material, which consists of cellulose fibres with sorbed on them iron cyanide particles. Product of processing is discharged from water with application of pressured flotation. |
 Combined method of treating waste water containing organic contaminants / 2480423Invention relates to treatment of waste water containing organic contaminants in industry, agriculture and household conditions. The waste water treatment method involves treatment of the initial waste water with a coagulant and flocculant, separation thereof into sludge and clarified waste water. Further, the clarified waste water is treated with nanostructured boehmite until achieving a given degree of purity of the clarified waste water and then separated into purified waste water and a solid residue. The solid residue, which contains contaminated nanostructured boehmite, is collected and regenerated, while undergoing supercritical aqueous oxidation. The regenerated nanostructured boehmite is collected for subsequent recycling. |
 Method for precipitation of phosphorus from waste water / 2480422Invention can be used in small-size continuous purification plants for precipitating phosphorus from waste water, particularly household waste water. An apparatus, which is connected to the small-size purification plant, has a pumping tank (1), a discharge pump (2) for draining the pumping tank, a chemical reservoir (6) and a dosing pump (5) for the chemical coagulant which is meant for feeding the chemical coagulant from the chemical reservoir (6) into the waste water discharged from the pumping tank (1), wherein separation of the formed residue of chemical substance from water released from said purification plant takes place in the settling reservoir (12) of the small-size purification plant. The apparatus can entirely be placed inside the settling reservoir (12) of the small-size purification plant. The dosing pump (5) is configured to pump the chemical coagulant into a stream generated by the discharge pump (2) during the entire or almost entire operating cycle of the discharge pump (2). |
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Method for integrated treatment of industrial waste water formed when producing extra-pure quartz concentrate / 2480421 Invention can be used in production of extra-pure quartz concentrate which is one of the main sources of contamination by fluorine, chlorine and salts containing fluorine and chlorine. The method is realised via reactant treatment in two steps. The first step involves neutralisation of acidic waste water with 23% NH4OH with separation of the SiO2 precipitate and formation of NH4F solution. At the second step, said solution is treated with 20% lime milk. The formed CaF2 precipitate and previously separated SiO2 precipitate are washed, dehydrated and removed from the process as end products. The 7-8% NH4OH solution obtained after separating the CaF2 precipitate and flush water are returned to the first step for reactant treatment of waste water to prepare the starting NH4OH solution. The 7-8% NH4OH solution formed at the second step is concentrated by evaporation to 23% and returned to the first reactant treatment step. The condensate obtained during evaporation is directed for preparation of 20% lime milk, washing the SiO2 precipitate and into recycling cycle of the main production. |
 Method of removing hydrogen sulphide and impurities from water of underground sources and apparatus for realising said method / 2478577Group of inventions relates to treatment of underground water from gases dissolved therein and can be used in water treatment. Source water containing hydrogen sulphide and impurities is fed through a pipe 1. The water is then fed into a floatation plant 3, having at least two chambers. At the first floatation step, a hydrogen sulphide neutraliser is fed through a nozzle 2 and at the second step, a chemical which facilitates precipitation of sulphates and sulphides is added. The treated water enters a settling tank 4, from where it is fed into a contact flocculator 6, having a gravel filling. The contact flocculator 6 is connected to the settling tank 4 through a nozzle 5, needed for feeding a flocculant. |
 Method of water cleaning and decontamination / 2477707Set of intention relates to water treatment and may be used in various industries. First, chlorinated coagulant is subjected to electrochemical treatment at membrane or diaphragm electrolysis unit 3 with insoluble electrodes to produce high-basic coagulant and gaseous chlorine. High-basic coagulant is mixed with water flow fed into settler 4 for coagulation and flocculation of undissolved suspensions and mechanical impurities. Gaseous chlorine withdrawn from electrolysis unit is fed into chlorine proportioner 6 to make bleaching water. Said water is fed for decontamination in cleaned water flow between said settler 4 and mechanical filter 8. |
 Method purifying waste water from aluminium ions / 2468997Invention relates to waste water treatment techniques. The method involves treating water with sodium phosphate in the presence of fibrillated cellulose fibres in amount of 100 pts.wt per 100-900 pts.wt of the formed aluminium phosphate. Water can be pre-treated with sodium hydroxide solution in the presence of said fibres. The treatment product is separated by pressure flotation. |
 Method of bed fluid treatment and universal floater to this end / 2466100Invention relates to treatment of whatever effluents and may be used in oil production and processing industries, petrochemical industry, etc. Proposed device represents treatment system comprising intake chamber communicated with flotation assembly inlet and settling assembly as well as with unit distributing inert gas and gas-water mix communicated with flotation unit outlet and settling unit inlet. Note here that settling unit is composed of tight modules of thin-layer settlers while flotation unit is composed of a system of tight modules of flotation chamber with impeller-type dispersers. Note also that foam product collector assembly is equipped with inert gas feeder and communicates with flotation unit inlet, settling unit inlet and aforesaid distributing unit to make closed-circuit circulation system. |
 Mobile systems and methods for sufficient treatment of water for further use in well treatment operations / 2450980Methods are realised using a system comprising a mobile platform; an input pump for pumping a treatment stream through the system; a centrifugal separator operatively connected to the outlet of the input pump for treating the treatment stream under centrifugal forces; a borate filter operatively connected to the outlet of the centrifugal separator for filtering the treatment stream capable of removing at least a portion of borate when the treatment stream is at a pH of 8 or higher; and a chemical-additive subsystem capable of selectively adding one or more chemical agents to the treatment stream before the centrifugal separator, wherein the chemical agents can be selected so as to enable precipitation of dissolved ions selected from the group consisting of: sulphate, calcium, strontium or barium, magnesium, iron; and selectively adding a chemical agent to the treatment stream before the borate filter to increase the pH of the treatment stream to 8 or higher. |
 Method for cleaning of ground waters from arsenic / 2441846Invention can be used for cleaning of natural (ground and surface) and technogenic waters from arsenic. The method includes oxidation on psilomelane of trivalent arsenic to pentavalent and subsequent sorption of the later on brucite. The oxidation of trivalent arsenic is performed by filtration through psilomelane layer or by addition of psilomelane sized less than 0.1 mm into treated water, mixing for 30-60 minutes with subsequent sediment separation. The sorption is performed by the way of filtration of treated water through the layer of brusite or by the way of addition of brucite sized 10:50 μm to treated water, mixing for 30 minutes and subsequent sedimentation separation. |
 Method of inactivating viruses in water media / 2506232Invention can be used for preparation of ultra-pure water, safe for consumption by people, as a result of sorption purification of drinkable water from viruses. Method includes filtration of water through zones with sorption materials, where, at least, one of zones represents porous filtering element based on resins, obtained by condensation of aldehydes with aromatic phenols and amines. Sorption material possesses the following characteristics: ratio of absolute value of zeta potential of porous filtering element to value of effective radius of liquid flow canal constitutes not less than 104 V/m. Porous filtering element, based on resin, obtained by condensation of formaldehyde with resorcin or melamine, is used as such sorption material of, at least, one of zones. Porous filtering element can preferably contain onwashed layer of sorption material, characterised by ratio of absolute value of material zeta potential to value of effective radius of flow canal not less than 105 V/m. |
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Method of obtaining activated solutions / 2506231 Invention relates to methods of obtaining solutions with preliminarily specified properties, which can be applied in chemical technology, medicine, agriculture, in particular, in viticulture. Method includes influence on 0.6% solution of water-soluble sodium chloride salt in water with constant electric current in chambers of diaphragm electrolyser. Mixture, containing equal portions of 3 water-soluble substances in quantity making it possible to form two-phase system of saturated solution and equal in weight sediment is introduced into resulting from electrochemical processing of initial 0.6 sodium chloride solution anolyte and catholyte. Mixture of sodium silicate, potassium silicate and potassium nitrate with ratio of dry masses 1/1/1 is additionally introduced into activated 0.6% sodium chloride solution in amount 4.0% to solution mass. |
 Device for cleaning oil-bearing waters and effluents / 2506230Invention relates to oil-bearing effluents treatment and can be used for treatment of oil field effluents used in system for maintaining seam pressure at oil field flooding. This device comprises main tank, perforated pipelines, one to feed oil contact mass in water supply layer and another one intended for discharge, arranged at the tank top and bottom parts, respectively. Besides, said device incorporates extra tank composed of two parts. First part is equipped with hydrophobic filter arranged horizontally, sealed and locked along the perimetre, and feed perforated pipe arranged downstream of the filter. Second part is equipped with water discharge pipe at bottom section. Note here that said first and second parts are communicated above extra tank while main tank water discharge pipe communicates with extra tank feed pipe. Main tank and extra tank feed pipe are communicated under contact mass layer via appropriate valves and accessories with hydrocarbon solvent feed pipe. |
 System and method of bioretention / 2506229Invention relates to system of discharge flow purification, such as rain water and sewages, containing hard particles and dissolved substances. System of water purification contains, at least, one retention layer, constructed for receiving water, flowing into system, with retention layer containing media, which have composition, intended for retention of phosphorus, which contain residues of water purification; drainage layer, including drainage system under retention layer, with retention layer and drainage layer being constructed and placed in such a way that, at least, part of water, passing through retention layer will be received by drainage system. |
 Multisectional contact reservoir for water processing with ozone / 2505487Reservoir includes, at least, three communicating with each other hermetic reaction tanks, made preferably of concrete, each in form of parallelepiped, located between pressure compartment, connected with source of processed water, and discharge compartment, which has outlet for supplying water to consumers, as well as equipped with system of ozone-air mixture supply into each reaction section and its dispersion into water, system of removal and destruction of residual ozone in ozone-air mixture, inter-sectional relief compartments are installed between sections, and each section of contact reservoir is additionally equipped with devices of even water distribution on its transverse section, at the top in form of installed under water horizon level dead from one butt end perforated tubes. Open butt ends of tubes, installed in first section are connected with pressure compartment of contact reservoir, and open butt ends of tubes, installed in second and third sections, are connected respectively with cavities of first and second inter-sectional relief compartment, and at the bottom below ozone-air mixture dispersers or in form of similar perforated tubes. Open butt ends in first and second sections are connected respectively with cavity of first and second inter-sectional relief compartment, and open butt ends of tubes in third section are connected with discharge compartment, or horizontally installed perforated partition. Through canals are made in walls, separating first section from first relief compartment, second section from second relief compartment, third section from discharge compartment below perforated partition. |
 Method of drainage outflow purification and device for its realisation / 2505486Weed plants are preliminarily mowed in discharge canal to water level and is left to dry. After drying reed and rush plants are selected. Selected plants are used as sorbent. Filtering cassette net of cassette-holding device is filled with sorbent. Sorbent-containing device is fixed in discharge canal bed in monolithic manner and drainage outflow is passed through it. Plant mowing and replacement of filtering cassette are carried out when rice plant passes from one vegetation stage into another. |
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Method of purifying waste water from heavy metal cations / 2504518 Invention can be used in treating electroplating wastes. The method of purifying waste water from heavy metal cations with a low-frequency pulsed field involves treatment in a heterogeneous medium formed by at least 12 mmol/l of calcium hydroxide, in an electromagnetic apparatus using energy of an alternating electromagnetic field formed by magnetic elements made of hard-magnetic material moving under the effect of said field. |
 Filtration module incorporating capillary membranes / 2504428Invention relates to "from outside-to inside" filtration modules including capillary membranes intended for water or other turbid fluid treatment. Proposed device comprises membrane shutters, each being formed by one row of capillary membranes, lower manifold arranged nearby lower end of membrane shutters and connected therewith, and at least one membrane shutter. Appropriate top manifold arranged nearby upper end of membrane shutter and connected with its capillary membranes is arranged for every membrane shutter. Membrane shutters are arranged vertically while top manifolds are spaced apart to allow fluid flowing upward between membrane shutters and top manifolds. Top manifolds of at least two adjacent membrane shutters are located at different height while capillary membranes of adjacent shutters feature different length. |
 Pipeline transport method of multiphase multicomponent mixture / 2503878Method involves measurement, sampling of hydrocarbon gas-liquid mixture supplied from wells for analysis and supply to mixture flow in the beginning of the pipeline of composition of surface active substances, which converts multiphase multicomponent flow to pseudohomogeneous bubble system, and consisting of oil-soluble demulsifier and depressant or inhibitor of paraffin depositions taken in the weight ration of 1:7 to 7:1. The above composition is introduced in the amount of 0.01 to 0.02 or 0.2 to 0.5 wt % of hydrocarbon constituent of mixture liquid phase. |
 Method of deironing mineral drinking bottled water / 2503626Invention relates to method of removing bivalent iron from drinking, predominantly carbonic mineral waters. Method of deironing mineral drinking bottled water, includes pre-purification of mineral water from suspended admixtures, and deironing is realised by only one operation - processing mineral water with active granulated carbon sorbents in presence of natural humic acids in concentration not less than 1 mg/dm3. This method makes it possible to reduce content of bivalent iron to quantity 0.3 mg/dm3, and, as it has been found out, such residual concentration of iron does not worsen marketable state of bottled water in storage. |
 Device for purification of sewage / 2243941The invention is dealt with devices for purification of household and industrial sewage and intended for electrical and cavitational treatment of sewage containing a large quantity of organic compounds. The device for purification of sewage consists of a body made out of a dielectric material partitioned by diaphragms for two electrode chambers and one working chamber, that contains a filtering material. The electrode chambers have cavitational field sources installed and the working chamber is supplied with a the bubbler installed in it. The technical result consists in an increase of recuperation of the filtering material at the expense of application of a cavitational field to it, decrease of the microbiological semination, and an increase of cavitational effect on particles. |
FIELD: chemistry.
SUBSTANCE: invention relates to technologies of purification of water from natural springs for their further application as initial water for obtaining vapour in processes of steam or vapour-oxygen conversion of hydrocarbon gases (synthesis-gas production). Installation for preparation of desalinated water contains successively connected heat exchanger for heating initial water, unit of preliminary clarification, unit of ultrafiltration, unit of ultraviolet decontamination, unit of filters with filtration degree not more than 5 mcm and unit of two-step reverse osmosis.
EFFECT: invention ensures increase of service term of ultrafiltration and reverse osmosis membranes, water decontamination.
5 cl, 1 dwg
The invention refers to the technology of water purification natural sources for their further use as initial water for steam generation in the processes of vapor or steam-oxygen conversion of hydrocarbon gases (synthesis gas production).
In the technologies of the production of synthesis-gas feedstock is a mixture of hydrocarbon gases and water vapor. To produce steam, you must use water of a high degree of purification. There are many methods of water purification, but currently are the most effective methods are based on membrane technologies (ultrafiltration, reverse osmosis).
As a source of initial water use natural water, as a rule, the nearest river or groundwater. The qualitative and quantitative indicators of pollution inherent to considerable seasonal fluctuations. During periodic worsening of quality of natural water in flood periods may experience problems with the production of synthesis-gas desalted water. In this case, some cleaning technology with the use of membranes may not provide the proper quality, or the necessary amount, or will work on critical loads with a high consumption of filter elements, chemicals, reduction of the life of the membrane, and also increase of process effluent.
In addition it is worth noting that during the production of synthesis-gas from economic considerations, water treatment should be carried out directly in the installations for the production of synthesis gas and served by the personnel of these same facilities. When choosing a water treatment technology, it imposes additional requirements. First, there must be maximum compactness of the equipment, secondly, simplicity of exploitation and service without attraction of specialists of narrow profile of water treatment.
Known plant for the preparation of demineralized water (EN 78183 U), consisting of a sequence of modules included preliminary preparation of water, reverse osmosis module, decarbonization, hearth, module ion-exchange softening and EDI. Module decarbonization can be made, in particular, in the form of a system of membrane degassing.
Known membrane unit for the preparation of water (EN 56374 U), consisting of the module ultrafiltration, the module first stage reverse osmosis module of the second stage reverse osmosis module electrodeionization, control softener, pumps and systems membrane .
Known equipment for water (EN 62923 U), consisting of a block of preliminary preparation of water (installation of direct-flow coagulation with filtration at multilayer, granular downloading or installing UF), nanofiltration unit, block reverse osmosis unit softening nanofiltration unit, block adjustment of the pH.
The disadvantages of these schemes are:
- complex technological scheme, as a result, difficulties in maintenance and operation, large geometrical dimensions;
- high cost of treated water;
- high production costs due to water the rapid breakdown of expensive membranes, because there is no pre-clarification of water (for example, methods of coagulation and sedimentation) in front of the ultrafiltration unit;
- the use of certain types of flocculants leads to reduced service life of ultrafiltration membranes;
- low reliability of the technology, in the period of deterioration in the quality of source water;
Known water treatment system (EN 79096 U)containing pipelines from the water intake to the consumer on the flow of purified water, tank cumulative buffer, the capacity of the gas removal, block membrane flow-through filters reaction chamber ozonization, camera, the capacity of the chemical treatment of metal oxides, filter clarifying, second buffer tank, tank of clean water and block ultraviolet disinfection, between the second buffer tank and reservoir of pure water laid parallel pipeline on which consistently placed an additional block ultraviolet disinfection and block reverse osmosis membrane separation.
Disadvantages of the known installation are:
- the use of coagulants low concentration in the block clarifier, which leads to excess transportation costs;
- absence of effective scheme of separation of the flakes with coagulated particles in a block of lightening;
- absence of schemes of automatic regulation of pH environment in the block of preliminary clarification of water;
- absence block ultrafiltration, which leads to premature failure of the reverse osmosis unit.
Closest to the proposed a unit for the desalination of water, carrying out coagulation/flocculation with the settlement of colloidal particles and impurities, pre-filtering, ultrafiltration and processing of reverse osmosis. The installation includes a series-connected capacity for coagulation and sedimentation, pre-filter, ultrafiltration unit, office of the reverse osmosis (CN 101973655, pub. 16.02.2011).
Disadvantages of the known installation are:
- the use of certain types of flocculants leads to reduced service life of ultrafiltration membranes;
- inefficient mode of coagulation and sedimentation of colloidal particles in the block of preliminary clarification of water due to the lack of aeration of the water and the effective scheme of separation of the flakes with coagulated particles in a block of lightening;
- absence of schemes of automatic regulation of pH environment in the block of preliminary clarification of water;
- lack of stage disinfection of water;
- lack of filters in front of the entrance of water in block reverse osmosis (possible «overshoot» colloidal particles)
The technical result of the proposed group of inventions is increase of term of service of ultrafiltration and reverse osmosis membranes; provision of water disinfection.
The technical result is achieved by the installation for preparation of desalinated water contains a series-connected system of preliminary clarification and block ultrafiltration and reverse osmosis unit, wherein is equipped with a heat exchanger for heating water source connected with the entrance of the block of preliminary clarification, connected in a block ultraviolet disinfection and block filters with filtration level no more than 5 mkm established between the block of ultrafiltration and reverse osmosis unit, which is a unit of the two-stage reverse osmosis.
Also, the yield to concentrate first stage unit for two-stage reverse osmosis connected to the backwashing membranes, United with actuator ultrafiltration that line filing of the leaching water is connected to the input of the block of preliminary clarification.
Also, the yield to concentrate second stage unit for two-stage reverse osmosis is connected between the unit ultrafiltration and block ultraviolet disinfection.
In addition, the block of preliminary clarification includes serially connected aeration tank, a tank of coagulation and Dodge.
Moreover Dodge preferably made in the form of capacity with tapered bottom and separation device in the upper part, has through channels with an inclination to the horizon 40 to 70 degrees.
Figure 1 shows a diagram of the installation for preparation of desalinated water.
Installation for preparation of desalinated water contains consistently connected plate-type heat exchanger 1 for heating water source with regulating valve 2, the block of preliminary clarification, which includes serially connected tank 3 aeration tank 4 coagulation and Dodge 5 with slime pump 6, hereinafter reception tank, 7, 8 pumps, block 9 of ultrafiltration, intermediate tank 10, pumps 11 block ultraviolet disinfection (UV sterilizer 12), block 13 roll filters with filtration level 5 microns (not more), unit 14-stage reverse osmosis, tank 15 for desalinated water pumps and 16.
Output of the first stage unit 14-stage reverse osmosis to concentrate connected with the module backwashing membranes (washing capacity of 18), United with actuator 9 ultrafiltration that line filing of leaching water is connected via a tank 17 to the entrance of the block of preliminary clarification.
Output to concentrate second stage in block 14 of the two-stage reverse osmosis is connected to intermediate tank 10 between the block 9 of ultrafiltration and block 13 roll filters.
Installation works as follows.
Source water, passing the plate-type heat exchanger 1, heated to a temperature of 20-25°C heating water from the packaging machine circuit. Temperature of initial water is maintained constant with the help of automatic control valve 2, installed on the by-pass of the plate heat exchanger line 1 of the district heating water. Keeping a constant temperature in a given interval is a necessary condition for the coagulation process. In the line of source water consistently dosed coagulant solution (for example, aluminium oxychloride mark «Aqua-Aurat 30») and a solution of alkali, such as sodium hydroxide. The number of coagulant selected experimentally, on the basis of laboratory studies. One of the main conditions of the coagulation process is to maintain a specific pH-values. Dosage of sodium hydroxide is necessary to adjust the pH of the water and is in automatic mode for given values of pH in the range of 5,5-7,5.
Then the heated water is mixed with clean water block 9 of ultrafiltration (from the tank 17) and sent to the block of preliminary clarification, which consists of a tank 3 aeration tank 4 coagulation and clarifier 5. Initial water enters the bottom point of the aeration tank 3 (agitator), which served process air of network for the removal of dissolved gases, oxidation of dissolved iron and improve the mixing of reagents with water. In the same tank 3 is the initial coagulation (consolidation particles coagulant and pollution). Then the water flows under gravity in the bottom point of the tank 4 coagulation (agitator), where the degassing of water and the final coagulation. water from the upper point of the tank 4 coagulation two parallel flows by gravity comes from opposite sides in the bottom of the clarifier 5, which is designed for deposition and removal of the resulting sludge (major connections coagulant and pollution in the form of flakes). Water upward flow rises from below upward. At the top of the clarifier 5 established the thin-layer separation unit, consisting of profiled plates, forming a cross section of channels in the form of a honeycomb. The slope of the plates is 40-70 degrees to the horizon. Separation of suspended particles occurs due to changes in the direction of the water flow in the channel of the device. In the middle part of the clarifier 5 formed a weighted layer of coagulated particles in the form of flakes, which is a contact medium, when the water passes through the layer of pollution are deposited. The presence of the fluidized flakes significantly speeds up the deposition process and make it more effective. When the rate of sedimentation in the form of flakes becomes higher than the velocity of water flow, they are deposited in the bottom of the clarifier 5 pyramidal form and with the periodicity of 8-12 hours deleted slime pump 6.
Effective water clarification in the block of preliminary clarification protects the membrane block 9 of the ultrafiltration from early failure.
The clarified water is collected in the receiving chute at the top of the clarifier 5 and gravity is served in the reception tank 7 block 9 of the ultrafiltration. From the receiving tank 7 8 pumps, one business and one reserve) water is served in the apparatus block 9 of ultrafiltration, one business and one reserve), where there is a clearing of suspended solids, colloid and organic impurities. In block 9 of ultrafiltration is also integrated module backwashing membranes with the washing capacity of 18. The clarified water is collected in the intermediate tank 10, where pumps 11, one business and one reserve) is served on the processing in ultra-violet sterilizer 12 for disinfection, then passes the unit 13 roll filters with filtration level 5 microns (one working and one reserve), which retained colloidal particles, «» through the block 9 of ultrafiltration, which can lead to early failure of membranes in block 14 of the reverse osmosis.
Then disinfected, and free from suspended matter, water enters the stage of two-stage osmosis unit 14, membrane units I and II levels which are connected in series by filtrate. Filtrate the first stage is input stage II for purification and concentrate stage I sent a capacity of 18 for leaching block 9 of the ultrafiltration. Concentrate grade II returned to the intermediate tank 10 for re-treatment.
For pH correction and removal of carbonic acid at the entrance of the second stage unit 14 is dosing of sodium hydroxide solution. Membrane units I and II levels assembled on one frame in the form of a monoblock and have a common module of leaching.
After cleaning on the reverse osmosis membranes desalted water is collected in a tank 15, where pumps 16, one business and one reserve) is fed to the production of synthesis-gas.
In the case of routine maintenance or flush on all stages of reverse osmosis remaining in the work of the stage continues to produce water and supplying it synthesis gas production.
Advantages of the proposed invention are:
- the most optimal conditions of the coagulation process, as the temperature and pH of water are held constant at the expense of automatic control;
- large deposition efficiency of colloidal particles thanks to the use of aeration of the water and the separation devices in a block of lightening;
- extended lifetime of ultrafiltration and reverse osmosis membranes;
- presence of stages of water disinfection.
1. Installation for preparation of desalinated water containing consistently United system of preliminary clarification and block ultrafiltration and reverse osmosis unit, wherein is equipped with a heat exchanger for heating water source connected with the entrance of the block of preliminary clarification, connected in a block ultraviolet disinfection block of filters with filtration level no more than 5 mkm established between the block of ultrafiltration and reverse osmosis unit, which is a unit of the two-stage reverse osmosis.