WO2022191792A1

WO2022191792A1 - Wastewater recovery and technological treatment system

Info

Publication number: WO2022191792A1
Application number: PCT/TR2021/050353
Authority: WO
Inventors: Zeki CAKAR
Original assignee: Univermak Makine Muhendislik Sanayi Ve Ticaret Anonim Şirketi
Priority date: 2021-03-10
Filing date: 2021-04-15
Publication date: 2022-09-15

Abstract

The invention is related to the wastewater recovery and technological treatment system that eliminates the waste release to the environment without using chemicals with low energy consumption and high efficiency with dielectric heating system at low temperatures under vacuum of post-process wastewater in industrial plants.

Description

WASTEWATER RECOVERY AND TECHNOLOGICAL TREATMENT SYSTEM Technical Field

The present invention relates to a treatment system that is used in the treatment of wastes discarded after the completion of processes carried out in such fields as textile, food, heavy industry, paper industry, glass industry, etc., and in water recovery as well. in particular, the Invention relates to a wastewater recovery and technological treatment system that enables a high-efficiency and sustainable recovery of the wastewater stemming from a process carried out in industrial plants without using chemical agents and by eliminating the drawback of waste release to the environment and that also helps operational costs to be reduced.

Prior Art Water usage in the industry has immensely gained importance in recent years regarding both the quality of the water used and environmental outcomes of the wastes emerged as well. Particularly, in industrial sectors such as textile, paper, plastic, glass, metal, food, large quantifies of high-quality water is used in manufacturing processes of the plants, whiiehigh volume wastewater containing many chemical agents occurs.

In the current art, in the textile industry and other industrial plants, wastewater can be gained into reuse through recovery systems such as jacketed heating, electrocoagulation, and osmosis system while it is possible to subject the wastewater to biological and/or chemical treatment processes after use and then to introduce it into sewers.

Jacketed heating systems, which are one of the most prevalently used systems in the current applications, are generally systems that operate by vaporizing the wastewater contained in itself through the method of steam-heating. These systems consume a large amount of energy and have high installation costs. Furthermore, as they perform the recovery process at high temperatures, their cooling capacity is not sufficient. Therefore, the desired efficiency cannot be achieved in the system. In the electrocoagulation system, which is another commonly used system, a plurality of iron plates are used as being positioned parallel to one another. Said plates are provided with poles through which wastewater is allowed to be passed

between the plates. The wastewater passing through the plates is ionizated and impurities rises to the upper surface of the wastewater. Chemical and osmosis systems are used in the next processes in order in order to

wastewater to be reused. The drawback of these systems is the need for replacing the plates in very short periods. The piates incrementally fade out and become unserviceable as the required processes are carried out. In this system that operates by introducing electricity to the plates, high energy costs are a matter of concern. Chemicals are used in order in order to enable the water recovered to be reused. Such usage of chemicals also leads to additional costs and workloads. Furthermore, to be able to use the recovered water, the osmosis system is later required. This system also causes establishments to encounter the problem of extra cost and high energy consumption. Accordingly, recovery systems are not preferable due to their drawbacks of high installation and operational cost, low efficiency, and the requirement for using chemicals during processes. Therefore, in wastewater recovery, only biological treatment and draining into sewers are preferred. This nevertheless causes environmental pollution and serious disorders in living creatures. Thus, since current systems are not capable of meeting expectations and greater masses of wafer are required to be treated although industrial wastewater recovery is now becoming more common, it has recently been mandatory to develop novel treatment technologies that occupy a narrower area, apply to all types of wastewater, economical and quite efficient regarding effluent quality.

US8801934 can be given as an example for the prior art in literature. Said document is related to an osmotic-assisted desalination system and a method thereof, Insaid invention, a system and a method, a system and method using a pressure purification process such as reverse osmosis in conjunction with a pressure delayed osmosis subsystem to provide desalination of low or high concentration brine from the sea, ocean or a similar body of water is mentioned. With said system, seawater is enabled to be desalinated and thus natural wafer sources are protected. Therefore, with said system and method, it is not possible in order to enable the wastewater formed from manufacturing processes in plants to be recovered. WO2018182435 can be another example of the prior art. Said document is related to a biological wastewater treatment plant. In said invention, a plant that enables the contaminations in wastewater to be removed is disclosed. However, as the wastewater cleaned by means of said plant is not applicable for being reused, it is released to the environment. This causes natural water sources to be intensively consumed and thereby resulting in a failure to achieve a sustainable recovery In plants. TR2020/10698 is another example of the prior art. Said document is related to a compact wastewater treatment plant. In said invention, a compact plant that enables wastewater to be cleansed of nitrogen and phosphorus together with carbon before if is discharged into receiving waters is disclosed. However, as the wastewater cleaned by means of said plant is not applicable for being reused, it is released to the environment. This causes naturai water sources to be intensively consumed and thereby resulting in a failure to achieve a sustainable recovery in plants.

EP2379452 can be given as yet another example for the prior art. Said document is related to a wastewater treatment system and a method thereof. In said invention, a system that enables the wastewater to be cleaned via an iminodiacetic ion exchange resin, a silica gel, a chemically modified silica gel, and an inorganic supporting material in a purification unit is disclosed. However, the system leads to extra costs and workloads due to chemical use in the recovery of wastewater. Consequently, the presence of the aforementioned problems and the inadequacy of current solutions has made it mandatory to develop a novelty in the related technical field.

Aim of the Invention

The present invention relates to a wastewater recovery and technological treatment system that eliminates the aforementioned drawbacks and provides novel advantages to the related technical field. The main aim of the invention is to achieve a wastewater treatment system that provides a high-efficiency sustainable recovery by eliminating the problem of releasing the wastewater resulted from the processes carried out in industrial plants to the environment without using chemicals.

An aim of the invention is in order to enable establishments to recover wastewater through an easy and low-cost method as well as in such a quality that enables them to directly use the wastewater in their processes after the process of recovery has been completed.

Another aim of the invention is in order to enable manufacturing costs to be reduced and to provide sustainable production by means of eliminating the problem of wastewater in plants with the recovery of wastewater as well as the applicable quality of the water obtained for other processes.

Yet another aim of the invention is to provide quality and environmentally friendly recycling together with sustainability through preventing wastewater from being released to the environment in plants by reducing the initial installation cost of treatment systems, by extending the use of the system, and by eliminating the use of chemicals in treatment processes.

Another aim of the invention is in order to enable the process of wastewater recovery to be completely implemented via the psychical methods without using chemical substances and thus to prevent wastewater from being released into the environment.

Yet another aim of the invention is to provide wastewater recovery with high efficiency and minimum energy consumption thanks to a heating system that consumes low energy and has a high heating capacity.

A further aim of the invention is in order to enable wastewater to be recovered without the need for any chemicals or osmosis systems by filtering the wastewater and minimizing the number of bacteria contained in itself in a sterilization system, and by vaporizing the wastewater under vacuum, at a low temperature, and with low energy consumption and then distilling it.

Another aim of the invention is in order to enable the process of recovery to be implemented with low energy consumption by vaporizing the wastewater under vacuum and at a low temperature after completing a pre-heating process and by distilling the wastewater after completing a pre-cooling process.

To be able to achieve all of the aims that are mentioned above and will be apparent from the detailed description below, the invention; is related to the treatment system that is used in cleaning the wastewater formed from the processes carried out in industrial plants and the recovery process of wastewater. The invention is characterized by comprising; a plant wastewater storage tank in which the wastewater formed as a result of manufacturing processes in an industrial plant is contained, at least a wastewater suction pump that enables the wastewater contained in the plant wastewater storage tank to be sucked into the treatment system, a dielectric sterilization system that performs a pre-sterilization process by disinfecting the water sucked out of the plant wastewater storage tank, a pre-filtration system that filters particles contained in the wastewater disinfected in the dielectric sterilization system, a filtered wastewater basin in which the wastewater filtered in the pre-filtration system is contained, a main unit that stores the wastewater stored in the wastewater basin through the vacuum obtained by means of a vacuum pump, a dielectric heating tube that vaporizes the wastewater stored in the main unit by heating with a dielectric fieldvia the capacitors, a horizontal heat exchanger that performs a pre-cooling process to the steam extracted out of the main unit through vacuum and a pre-heating process to the wastewater that passes therethroughand is introduced to the main unit in order to be heated, a vertical heat exchanger that enables the steam subjected to pre-cooling in the horizontal heat exchanger to be distilled, a distilled water reservoir that enables the water distilled in the vertical heat exchanger to be stored in order to be transferred to the plant water storage tank.

Structural and characteristic properties together with all of the advantages of the invention will be more clearly understood with the help of the accompanying drawings and the detailed description written by making references to these drawings. Therefore, it will be appreciated that evaluations are made by taking these drawings and this detailed description into consideration.

Drawings of the Invention

Figure 1 :lt is a top view of the treatment system subject to the invention.

Figure 2: It is a perspective view of the treatment system subject to the invention. Figure 3: It is another perspective view of the treatment system subject to the invention.

Figure 4: It is a side view of the treatment system subject to the invention.

Definitions of the References of the Components

1. Plant wastewater storage tank

2. Wastewater suction line

3. Wastewater suction pump

4. Wastewater sterilization system suction line

5. Dielectric sterilization system

6. Wastewater pre-filtration system suction line

7. Pre-filtration system

8. Pre-filtration system chassis

9. Pre-filtration outlet line

10. Pre-filtration system sludge outlet line

11. Pre-filtration system sludge outlet line valve

12. Filtered wastewater basin

13. Vacuum pump

14. Vacuum pump suction line

15. Main unit

16. Filtered wastewater collector suction line

17. Filtered wastewater horizontal heat exchanger pre-heating intake collector

18. Suction line to filtered wastewater horizontal heat exchanger

19. Horizontal heat exchanger

20. Vertical heat exchanger

21. Subvacuum pump

22. Vacuum pump service water discharge vessel

23. Discharge vessel service water discharge line 24. Discharge vessel service water suction pump

25. Service water discharge line

26. Vertical cooling heat exchanger vacuum stabilization line

27. Electrical automation panel

28. Wastewater horizontal heat exchanger outlet line

29. Dielectric heating tube

30. Waste sludge discharge line

31. Waste sludge discharge pump

32. Distilled water reservoir

33. Heat exchanger cooling water intake line

34. Washing ball

35. Coldwater collector

36. Vertical cooling heat exchanger hot water outlet line

37. Vertical cooling exchanger hot water outlet line

38. Plant cold water line

Detailed Description of the Invention

In this detailed description, preferred alternative embodiments of the treatment system subject to the invention have been described, without any limitations, only in order to enable the subject matter to be better understood.

In Figure 1, a top view of the treatment system subject to the invention is illustrated. Accordingly, the treatment system basically comprises; a plant wastewater storage tank (1) in which the wastewater formed as a result of manufacturing processes in an industrial plant is contained, a dielectric sterilization system (5) that performs a

sterilization process by disinfecting the water sucked out of the plant wastewater storage tank (1), a pre-filtration system (7) that filters particles contained in the wastewater disinfected in the dielectric sterilization system (5), a filtered wastewater basin (12) in which the wastewater filtered in the pre-filtration system (7) is contained, a main unit (15) that stores the wastewater stored in the wastewater basin (12) through the vacuum obtained by means of a vacuum pump (13), a dielectric heating tube (29) that vaporizes the wastewater stored in the main unit (15) by heating with a dielectric fieldvia the capacitors, a horizontal heat exchanger (19) comprised of a vertical body having thereon pipe bundles that perform a pre-cooling process to the steam extracted out of the main unit (15) through vacuum and a pre- heating process to the wastewater that passes therethrough and is introduced to the main unit (15) in order to be heated, a vertical heat exchanger (20) comprised of a vertical body having thereon pipe bundles that enable the steam subjected to pre cooling in the horizontal heat exchanger (19) to be distilled, a distilled water reservoir (32) that enables the water distilled in the vertical heat exchanger (20) to be stored in order to be transferred to the plant water storage tank, a waste sludge discharge line (30) that discharges the waste sludge remaining in the main unit (15) during the vaporizing process, a washing ball (34) that automatically cleanse the waste sludge in the main unit (15).

In the treatment system having overall perspective views in Figures 2 and 3, the wastewater formed as a result of manufacturing processes in an industrial plant is stored in the plant wastewater storage tank (1). Plant wastewater storage tank (1) is connected to at least one wastewater suction line (2) and thus enables the wastewater contained in the plant wastewater storage tank (1) to be sucked into the treatment system through at least one wastewater suction pump (3).

The wastewater suction pump (3) is firstly connected to the wastewater sterilization system suction line (4) in an effort in order to enable the wastewater sucked out of the wastewater suction pump (3) to be disinfected, thereby enabling the wastewater to be transferred to the dielectric sterilization system (5). Said dielectric sterilization system (5) is basically comprised of the profiles that are operated through the capacitors placed within the electrical automation panel (27) in which the automation of the treatment system is provided, and that are interlocked to expose the wastewater to the dielectric field. Thus, the wastewater passed through the wastewater sterilization system suction line (4) is subjected to pre-sterilization process by means of the dielectric sterilization system (5) and thereby enabling the wastewater to be disinfected and ready to be filtered.

The wastewater treated with the pre-sterilization process in the dielectric sterilization system (5) is passed to the pre-filtration system (7) through the wastewater

filtration system suction line (6) connected to the dielectric sterilization system (5). The pre-filtration system (7) enables the sterilized wastewater to be made ready for the process by removing solid particles contained in the wastewater. Said

filtration system (7) has stainless wire gauze filters of different micron diameters in a through-narrowing form and is basically comprised of at least 7 groups in 3 individual lines that are positioned on the pre-filtration system chassis (8). Thus, the wastewater is enabled to be cleaned from solid materials as it passes through the pre-filtration system (7). Solid particles retained in the pre-filtration system (7) are introduced to a sewer of the plant or, if provided in the plant, to a sludge drying machine through the

filtration system outlet line (10) that is connected to the pre-filtration system (7). The pre-filtration system sludge outlet line valve (11) is also connected to the pre-filtration system (7), and thus solid particles filling inside of the pre-filtration system (7) are enabled to be automatically introduced to said sewer or sludge drying machine.

The wastewater cleaned out of solid particles in the pre-filtration system (7) is transferred to the filtered wastewater basin (12) through the pre-filtration system outlet line (9) connected to the pre-filtration system (7) and then is stored in the filtered wastewater basin (12).

The wastewater that is stored in the filtered wastewater basin (12) after being treated with pre-sterilization and pre-filtration processes is distributed to the filtered wastewater horizontal heat exchanger inlet collectors (17) by means of the filtered wastewater collector suction line (16) connected to the filtered wastewater basin (12). The wastewater distributed to the filtered wastewater horizontal heat exchanger inlet collectors (17) is introduced to the horizontal heat exchangers (19) through the suction line to the filtered wastewater horizontal heat exchanger (18). Said filtered wastewater collector suction line (16) provides a connection between the filtered wastewater basin (12) and the filtered wastewater horizontal heat exchanger inlet collectors (17) and thus enables the wastewater stored in the wastewater basin (12) to be distributed to the filtered wastewater horizontal heat exchanger inlet collectors (17). The filtered wastewater horizontal heat exchanger inlet collectors (17) are connected between the filtered wastewater collector suction line (16) and the suction line to the filtered wastewater horizontal heat exchanger (18). The suction line to the filtered wastewater horizontal heat exchanger (18) provides a connection between the filtered wastewater horizontal heat exchanger inlet collectors (17) and the horizontal heat exchangers (19) and thereby enabling the wastewater distributed to the filtered wastewater horizontal heat exchanger inlet collectors (17) to be introduced to each horizontal heat exchanger (19). The wastewater passing through the horizontal heat exchangers (19) passes through the wastewater horizontal heat exchanger outlet line (28) connected to the horizontal heat exchangers (19) and fills into the main unit (15) that forms the main structure of the treatment system. Said main unit (15) is the component in which the wastewater is stored to be vaporized by being heated up. The main unit (15) is kept under vacuum by means of the vacuum pump (13) through which it is connected to the vacuum pump suction line (14). Thus, the main unit (15) is enabled to perform vaporizing at low temperatures under a vacuum.

The amount of the water that is stored in the main unit (15) is controlled by means of adjustment sensors located in the main unit (15), and when the amount of water in the main unit (15) reaches the maximum level, wastewater intake to the main unit (15) is stopped and the process of vaporizing is initiated. When the amount of wastewater in the main unit (15) reaches back to the minimum level, water intake is restarted. During the vaporizing process in the main unit (15), waste sludge starts to gather.At least one sludge sensor is placed in the main unit (15) for detaching if this waste sludge reaches the maximum level in the main unit (15), and as shown in Figure 4, to discharge said sludge from the main unit (15), at least one waste sludge discharge line (30) is connected under the main unit (15) and the waste sludge discharge pump (31) is connected to the waste sludge discharge line (30). When the waste sludge in the main unit (15) reaches the maximum level, the sludge sensor detects it and the waste sludge is extracted by means of the waste sludge discharge pump (31) and is discharged through the waste sludge discharge line (30).

The washing ball (34) is thereon coupled with the main unit (15) to automatically clean the main unit (15). After the waste sludge in the main unit (15) is discharged, said washing ball (34) cleans the main unit automatically.

The process of vaporizing the wastewater stored in the main unit (15) by being heated up is performed by means of the dielectric heating tubes (29) that provides heating with a dielectric field by operating in conjunction with the capacitors located in the electrical automation panel (27) through which the automation of the treatment system is provided.

The steam obtained by means of the dielectric heating tubes (29) in the main unit (15) is introduced to the horizontal heat exchangers (19) by being vacuumed through the vacuum pump (13). Said horizontal heat exchangers (19) are consisting of a vertical body having pipe bundles therein. The steam obtained in the main unit (15) passes through the pipe bundles of the horizontal heat exchangers (19) while the wastewater introduced to the main unit (15) from the wastewater basin (12) passes through the body outside the pipe bundles. Accordingly, the steam passing through the pipe bundles interferes with the wastewater passing outside the pipe bundles and thus a heat exchange occurs in the horizontal heat exchangers (19). Thus, the wastewater introduced to the main unit (15) from the wastewater basin (12) is enabled to be subjected to pre-heating process with the effect of the steam obtained in the main unit (15) during the wastewater passes outside the pipe bundles as well as a pre-cooling process with the effect of the wastewater introduced to the main unit (15) from the wastewater basin (12) during the steam obtained in the main unit (15) passes through the pipe bundles. The steam-subjected to pre-cooling process in the horizontal heat exchange (19) passes to the vertical heat exchanger (20) that is consisting of a vertical body having pipe bundles therein and enables the steam to be distilled. The process of distilling in said vertical heat exchanger (20) is performed with the cooling water passing through the body outside the pipe bundles during the steam passes through the pipe bundles. To feed cooling water into the vertical heat exchanger (20) is performed by means of cooling water that enters the plant cold water line (38) and is distributed by the cold water collectors (35), and passes through the heat exchanger cold water intake line (33) connected to the vertical heat exchangers (20). The water heated up by interfering with the steam in the vertical heat exchangers (20) exits the vertical heat exchangers (20) through the vertical cooling heat exchanger hot water outlet line (36) by being extracted with air through the vacuum pump suction line (14) and fills into the vacuum pump service water discharge vessel (22) by being connected to the vertical cooling heat exchanger hot water outlet collectors (37) communicated with the vertical cooling heat exchanger hot water outlet line (36).

The vacuum pump service water discharge vessel (22) has a level sensor that detects the occupancy rate of the cooling water extracted with air through the vacuum pump suction line (14) and of the vacuum pump (13) service water in the vessel. The discharge vessel service water suction pump (24) is connected to the vacuum pump service water discharge vessel (22) by means of the discharge vessel service water discharge line (23). The maximum amount of water in the vacuum pump service water discharge vessel (22) is detected through said level sensors, and the excess water is automatically transferred to the plant storage tank over the service water discharge line (25) through the discharge vessel service water suction pump (24) depending on the occupancy rate.

The water distilled in the vertical heat exchangers (20) fills in the distilled water reservoir (32) located under the vertical heat exchangers (20) to be used in the plant. The distilled water reservoir (32) has thereon-level sensors that detect the level of water. Additionally, the subvacuum pump (21) is connected to the distilled water reservoir (32). Level sensors detect when the water amount in the distilled water reservoir (32) reaches the maximum level through the level sensors and the excess water is transferred to the plant storage tank through the subvacuum pump (21) in order to be used in the plant.

Operation principle of the treatment system subject to the invention is as the following;

The wastewater formed as a result of manufacturing processes in an industrial plant is stored in the plant wastewater storage tank (1). The wastewater contained in the plant wastewater storage tank (1) is sucked through the wastewater suction pump (3), and the wastewater is passed through the wastewater sterilization system suction line (4) and is transferred to the dielectric sterilization system (5). The wastewater subjected to the dielectric field created in the dielectric sterilization system (5) is disinfected.

The wastewater subjected to pre-sterilization process in the dielectric sterilization system (5) is introduced to the pre-filtration system (7) through the wastewater

filtration system suction line (6) connected to the dielectric sterilization system (5). Solid particles retained in the pre-filtration system (7) are introduced to a sewer of the plant or, if provided in the plant, to a sludge drying machine through the

filtration system outlet line (10) that is connected to the pre-filtration system (7).

The wastewater cleaned out of solid particles in the pre-filtration system (7) is stored in the filtered wastewater basin (12) through the pre-filtration system outlet line (9).

The main unit (15) is kept under vacuum by means of the vacuum pump (13) and the wastewater stored in the filtered wastewater basin (12) is sucked and distributed to the filtered wastewater horizontal heat exchanger inlet collectors (17) by means of the filtered wastewater collector suction line (16). The wastewater distributed to the filtered wastewater horizontal heat exchanger inlet collectors (17) is introduced to the horizontal heat exchangers (19) through the suction line to the filtered wastewater horizontal heat exchanger (18).

The wastewater passing through the horizontal heat exchangers (19) fills in the main unit (15) by passing through the horizontal heat exchanger outlet line (28). When the main unit (15) reaches the determined level of filling, the process of filling is completed and suction of the wastewater is stopped.

The capacitors located in the electrical automation panel (27) transfers power to the dielectric heating tubes (29). The wastewater contained in the main unit (15) is heated up and vaporized with the dielectric field created in each dielectric heating tube (29), and is introduced to the horizontal heat exchangers (19) by being extracted through the vacuum. At this point, the steam obtained in the main unit (15) passes through the pipe bundles of the horizontal heat exchangers (19) while the wastewater introduced to the main unit (15) from the wastewater basin (12) passes through the body outside the pipe bundles. Thus, the steam passing through the pipe bundles interferes with the wastewater passing outside the pipe bundles, and a

cooling process to the steam as well as a pre-heating process to the wastewater introduced to the main unit (15) is applied by performing a heat transfer in the horizontal heat exchangers (19). The steam-treated with the pre-cooling process in the horizontal heat exchangers (19) passes to the vertical heat exchangers (20). The steam in the vertical heat exchangers (20), while passing through the pipe bundles of the vertical heat exchangers (20), is cooled with the cooling water passing through the body of the vertical heat exchangers (20) outside the pipe bundles and thus is distilled.

The water distilled in the vertical heat exchangers (20) fills in the distilled water reservoir (32) located under the vertical heat exchangers (20) in order to be used in the plant. When the water amount in the distilled water reservoir (32) reaches the maximum level, the distilled water is transferred to the plant water storage tank through the subvacuum pump (21 ) in order to be used in the plant. The cooling water that is heated up during the distilling process in the vertical heat exchangers (20), and the vacuum pump (13) service water exit the vertical heat exchangers (20) through the vertical cooling heat exchanger hot water outlet line (36) by being extracted together with air through the vacuum pump suction line (14) and, fill in the vacuum pump service water discharge vessel (22) by being connected to the vertical cooling heat exchanger hot outlet collectors (37) communicated with the vertical cooling heat exchanger hot water outlet line (36). The water contained in the vacuum pump service water discharge vessel (22) is automatically transferred to the plant storage tank over the service water discharge line (25) through the discharge vessel service water suction pump (24).

The sludge sensor detects when the waste sludge reaches the maximum level in the main unit (15) and wastewater intake to the main unit (15) is stopped. The waste sludge in the main unit (15) is extracted by means of the waste sludge discharge pump (31) and is discharged through the waste sludge discharge line (30). After the waste sludge in the main unit (15) is discharged, the main unit (15) is automatically cleaned by means of the washing ball (34).

Claims

1. A treatment system used in the treatment of the wastewater formed as a result of the manufacturing processes in an industrial plant as well as in the recovery of water, characterized by comprising; a plant wastewater storage tank (1) in which the wastewater formed as a result of manufacturing processes in an industrial plant is stored, at least one wastewater suction pump (3) that allows the wastewater contained in the plant wastewater storage tank (1) to be sucked into the treatment system, a dielectric sterilization system (5) that performs a pre-sterilization process by disinfecting the water sucked out of the plant wastewater storage tank (1), - a pre-filtration system (7) that filters the particles contained in the wastewater disinfected in the dielectric sterilization system (5), a filtered wastewater basin (12) in which the wastewater filtered in the pre-filtration system (7) is contained, a main unit (15) that stores the wastewater stored in the wastewater basin (12) through the vacuum obtained by means of a vacuum pump (13), a dielectric heating tube (29) that vaporizes the wastewater stored in the main unit (15) by heating with a dielectric medium via the capacitors, - a horizontal heat exchanger (19) that performs a pre-cooling process to the steam extracted from the main unit (15) through vacuum as well as performs a pre-heating process to the wastewater that is introduced to the main unit (15) in order to be heated by passing therethrough, - a vertical heat exchanger (20) that enables the steam subjected to pre-cooling in the horizontal heat exchanger(19) to be distilled, a distilled water tank (32) that allows the water distilled in the vertical heat exchanger (20) to be stored in order to be transferred to the plant water storage tank.

2. The treatment system according to claim 1, characterized by comprising at least a wastewater suction line (2) connected to the plant wastewater storage tank (1 ) to enable the wastewater contained in the said wastewater storage tank (1) to be sucked into the treatment system through the wastewater suction pump (3).

3. The treatment system according to claim 1 , characterized by comprising a wastewater sterilization system suction line (4) that is connected to said wastewater suction pump (3) and allows the wastewater to be transferred to the dielectric sterilization system (5).

4. The treatment system according to claim 1 , characterized in thatsaid dielectric sterilization system (5) comprises the profiles that are operated via the capacitors placed in the electrical automation panel (27) through which the automation of the treatment system is provided, and that are interlocked to expose the wastewater to the dielectric medium.

5. The treatment system according to claim 1 , characterized by comprising a pre-filtration system suction line (6) that is connected to said dielectric sterilization system (5) and enables the wastewater to be passed to the

filtration system (7).

6. The treatment system according to claim 1, characterized in thatsaid

filtration system (7) comprises stainless gauze filters of different micron diameters in a through-narrowing form.

7. The treatment system according to claim 1 , characterized by comprising a pre-filtration system outlet line (10) that is connected to said pre-filtration system (7) and enables the solid particles retained in the pre-filtration system (7) to be transferred to a sewer or sludge drying maching of the plant.

8. The treatment system according to claim 1 , characterized by comprising a pre-filtration system sludge outlet line valve (11 ) that is connected to said

filtration system (7) and enables the solid particles filled inside of the

filtration system (7) to be automatically introduced to a sewer or sludge drying machine of the plant.

9. The treatment system according to claim 1 , characterized by comprising a filtered wastewater collector suction line (16) that is connected to the filtered wastewater basin (12) in order to allow the wastewater stored in said filtered wastewater basin (12) to be introduced to the horizontal heat exchanger (19), and a filtered wastewater horizontal heat exchanger inlet collectors (17) that is connected to the filtered wastewater collector suction line (16).

10. The treatment system according to claim 9, characterized by comprising a suction line to the filtered wastewater horizontal heat exchanger (18) that provides a connection between said filtered wastewater horizontal heat exchanger inlet collectors (17) and the horizontal heat exchangers (19).

11. The treatment system according to claim 1 , characterized by comprising a wastewater horizontal heat exchanger outlet line (28) that is connected to the horizontal heat exchangers (19) in order to allow the wastewater passing through said horizontal heat exchangers (19) to fill into the main unit (15).

12. The treatment system according to claim 1 , characterized by comprising a level sensor placed in the main unit (15) in order to enable the wastewater intake to be stopped when the water amount in the main unit (15) reaches the maximum level and to be initiated the water intake when the water amount reaches the minimum level.

13. The treatment system according to claim 1, characterized by comprising a sludge sensor that is placed in said main unit (15) and detects when the waste sludge reaches the maximum level in the main unit (15).

14. The treatment system according to claim 1 , characterized by comprising a waste sludge discharge line (30) that allows the discharge of the waste sludge in the main unit (15) by being coupled to the bottom of said main unit (15).

15. The treatment system according to claim 14, characterized by comprising, a waste sludge discharge pump (31) that is connected to said waste sludge discharge line (30) and enables the waste sludge in the main unit (15) to be extracted.

16. The treatment system according to claim 1 , characterized by comprising a washing ball (34) that enables the automatic cleaning of said main unit (15).

17. The treatment system according to claim 1 , characterized by comprising dielectric heating tubes (29) that operate by means of the capacitors placed in the electrical automation panel (27) through which the automation of the treatment system is provided, and that provide heating with a dielectric medium in order to allow the wastewater stored in said main unit (15) to be vaporized by heating.

18. The treatment system according to claim 1 , characterized by comprising the horizontal heat exchanger (19) that is consisted of a vertical body having pipe bundles and enables the wastewater introduced from the wastewater basin (12) to the main unit (15) to be subjected to a pre-heating process with the effect of the steam obtained in the main unit (15) during passing outside the pipe bundles as well as a pre-cooling process with the effect of the wastewater introduced from the wastewater basin (12) to the main unit (15) during the steam obtained in the main unit (15) passes through the pipe bundles.

19. The treatment system according to claim 1 , characterized by comprising the vertical heat exchanger (20) that is consisted of a vertical body having pipe bundles and provides the distillation of the steam introduced from the horizontal heat exchanger (19) with the cooling water passing through the body such that it passes outside the pipe bundles.

20. The treatment system according to claim 1 , characterized by comprising a heat exchanger cold water intake line (33) that is connected to the vertical heat exchangers (20) in order to feed cooling water to said vertical heat exchangers (20).

21. The treatment system according to claim 1 , characterized by comprising a vertical cooling heat exchanger hot water outlet line (36) that allows the water heated up by interfering with the steam in said vertical heat exchangers (20) to exit the vertical heat exchangers (20) through the vacuum pump suction line (14) by being extracted together with air by means of the wastewater vacuum pump (13).

22. The treatment system according to claim 1 , characterized by comprising a vacuum pump service water discharge vessel (22) that enables the cooling water heated up by interfering with the steam in said vertical heat exchangers (20) and extracted together with air through the vacuum pump suction line

(14) as well as the vacuum pump (13) service water to be stored.

23. The treatment system according to claim 22, characterized by comprising the level sensors that detect the occupancy rate in said vacuum pump service water discharge vessel (22).

24. The treatment system according to claim 22, characterized by comprising z discharge vessel service water suction pump (24) that is connected to said vacuum pump service water discharge vessel (22) by means of the discharge vessel service water discharge line (23) and allows the water contained in the vacuum pump service water discharge vessel (22) to be automatically transferred to the plant storage tank over the service water discharge line (25).

25. The treatment system according to claim 1 , characterized by comprising the level sensor that detects the water level of said distilled water tank (32).

26. The treatment system according to claim 1 , characterized by comprising the sub-vacuum pump (21) that is connected to said distilled water reservoir (32) and enables the water contained in the distilled water reservoir (32) to be transferred to the plant storage tank in order to be used in the plant.