DESC:
A. FIELD OF INVENTION:
The present invention relates to dual water purification technology. More particularly, the present invention discloses SensePure Advanced Dual Water Purification technology with SEAD water purification technology using Surface Electro-Adsorption Desorption (SEAD) unit along with Intelligent Rejuvenating Auto-cleaning (IRAC) unit, Auxiliary- recirculation Performance Booster (ARPB) unit, Performance Enhancement logic (PEL) unit, Smart Water Flow Algorithm (SWFA) encoded microprocessor unit technology with minimum quantity of drinking water wastage for point of use (POU) domestic water purifier.

B. BACKGROUND ART
Different systems have been developed to remove contaminants from water. Examples of such systems include various methods, such as filtration, physical adsorption, capacitive desalination and/or Advanced Oxidation Processes (AOPs), to treat organic, inorganic, and biological contaminants in water.

Filtration is a process in which contaminants are physically removed by size exclusion. Known filtration processes include, for example, reverse osmosis and microfiltration. Disadvantages of filtration include clogging of the filter pores with contaminants, often resulting in fouling and frequent replacement of the filter. In some applications, this may result in high maintenance costs.

Capacitive Deionization (CDI) is an electro-adsorption technology. When an electric potential is applied to the electrode, the ionic substances move and adsorb to the electrode surface by the adsorption reaction in the electric double layer formed on the electrode surface (ion adsorption reaction); when the adsorption capacity of the electrode reaches its limit, the electrode is regenerated by short-circuiting the charged electrode to desorb ionic materials (ion desorption reaction).

As such, the electro-adsorption technology is very easy to operate because it can adsorb and desorb ions by changing only the potential of the electrode. Also, since the applied potential is operated at a low voltage where electrolysis does not occur, the energy consumption is lower than that of the existing desalination process. There are features that can be significantly reduced.

In the prior art, a Chinese specification CN201132787Y discloses an Electro-adsorption demineralization water purifier, which comprises a high-precision pretreatment filter element, an electro-absorptive filter element, an electrical control circuit board, and a water quality probe capable of detecting the content of salinity in water. After suspended substances and particulate matters in raw water are removed through the high-precision pretreatment filter element, then the salinity in the water is removed through the electro-absorptive filter element, the water quality probe is arranged in a water outlet pipeline of the electro-absorptive filter element; the water outlet pipeline is divided into two paths behind the water quality probe; and one path is a freshwater pipeline communicated with a water purification tank, while the other path is a sewage pipeline which is communicated with a sewage tank or is emptied.

In another prior art, a Chinese specification CN203284279U discloses a Self-cleaning electric adsorption water purification device. The electric adsorption water purification device comprises a first electrolytic system and an electric absorption-desorption system. The first electrolytic system comprises a first electrode assembly comprising a first positive electrode and a first negative electrode. Harmful materials in water are ionized by ionizing and exciting the water with the powered-on first electrode assembly. The electric absorption-desorption system comprises at least one electric absorption-desorption unit, which is provided with an absorption material electrode therein. By turning on the power of the electric absorption-desorption unit, the harmful materials with the ions can be absorbed by the absorption material electrode, and by replacing the polarity of the absorption material electrode of the electric absorption-desorption unit by controlling the power supply, the harmful materials on the absorption material electrode can be desorbed. The first electrolytic system is connected with the electric absorption-desorption system. The self-cleaning electric adsorption water purification device can efficiently remove harmful materials without replacing filter cores and retain beneficial mineral substances.

Accordingly, it is desirable to provide water treatment systems and methods that overcome some of the aforementioned disadvantages and limitations of known water purification techniques.

C. OBJECTIVE OF THE INVENTION
The herein-disclosed SensePure Advanced Dual Water Purification technology includes a SEAD water purifier unit for point-of-use (POU) drinking water. In addition, said Surface Electro-Adsorption Desorption (SEAD) unit is used in synergism along with an Auxiliary recirculation Performance Booster (ARPB) unit, Performance Enhancement logic (PEL) unit, Intelligent Rejuvenating Auto-cleaning (IRAC) unit, and Smart Water Flow Algorithm (SWFA) encoded microprocessor unit purifier. A minimum quantity of drinking water wastage for point-of-use (POU) domestic water purifiers is needed.

Another object of the invention is to provide water purification by SWFA and electronic water conductivity sensor, with an instant water quality report of the input water.

It is another object of the invention is to provide a submersible programmable sensor with a purification tank that instantly provides a water quality report on output water.

It is another object of the invention to provide a longer life span of the filter through the performance enhancement logic (PEL) process and auxiliary recirculation performance booster (ARPB), which is configured to provide the best performance and life span filters compared to conventional RO and UV technology-based water purifiers.

It is another object of the invention to provide an auxiliary-recirculation performance booster (ARPB) purification process, which is adapted to retain minerals in the water without bypassing the core SEAD unit. So, the system effectively removes new-age containments like Heavy metals, etc.

It is another object of the invention to revitalize the SEAD unit using a cross-linked polymerized citric acid and citrate-based chelate solution and an exclusive pressure setup.

It is another object of the invention is to provide a different range of infusing voltage (12V to 60V) to SEAD based on the instant input or water quality measured by the SensePure programmable sensor.

It is another object of the invention is to provide a common pressurized setup for normal water flow through all filters and IARC units.

It is another object of the invention is to provide the specified time interval performance enhancement logic to improve the input water TDS reduction. This helps reduce the frequent revitalization cycle of SEAD membranes with minimum quantity use of the revitalization solution.

It is another object of the invention to provide an IARC with three parts: a revitalization solution unit, a storage unit for revitalizing SEAD, and a segment recirculation and electronic dispensing unit.

It is another object of the invention to provide a dual-path purification system containing a dual purification tank. This system doubles the electro-adsorption of ions, which results in less water wastage and longer filter life.

It is another object of the invention is to provide consistency in mineral reduction with respect to input water TDS and it is achieved by the dual auxiliary path purification, stimulating the output water flow rate & applying the input voltage to the SEAD cell membrane from 12V to 60V.

D. SUMMARY OF INVENTION:
The present invention relates to a fluid purification system, more particularly a water purification based on an electro-absorption technique system that infuses with advanced water flow algorithms, self-cleaning, double purification chamber in the water purification to the 60-80% water recovery with retain the mineral level in the water.

The said purification system comprises a water inlet unit, cartridge unit, SEAD (Surface Electro-Adsorption Desorption) unit, Intelligent Rejuvenating Auto-cleaning (IRAC) unit, Auxiliary recirculation Performance Booster (ARPB) unit, microbes deactivating unit, natural taste immunity fostering unit, Power supply (12V—60V), Smart Water Flow Algorithm (SWFA) encoded microprocessor unit, Water storage unit, and water outlet unit.

E. BRIEF DESCRIPTION OF THE FIGURES:
The following thorough description with reference to the drawing will help you understand the embodiments below.

Fig 1 illustrates a general block diagram of the said dual water purification in accordance with the present invention.

Fig 2 illustrates a flow diagram of SEAD's different treatment processes from Zone 1 to Zone 4 of the said dual water purification in accordance with the present invention.

Fig 3 illustrates an electro-adsorption chamber in a surface electro-adsorption desorption unit with a SEAD membrane, metal brase nylon spacer, and water flow channel SEAD purification, which is further divided in accordance with the present invention.

Fig 4 illustrates a relay in H – the bridge.

Fig 5 illustrates an ARBP chamber details.

Fig 6 illustrates an IRAC section details.

F. DETAILED DESCRIPTION
ELECTRO-ADSORPTION:
Conventional adsorption-desorption processes can be generated by altering the temperature and pressure (or concentration).

In the case of electro-absorption, when used with an electrode with a high surface area, the electrical potential of the electrode in the solution may be applied as a third control parameter, which may create new possibilities for separation processes.

The charging and discharging of the electrical double layer on the surface of electrodes is the fundamental process in electro-adsorption.

The embodiments herein and various features and advantage details are explained more fully with reference to the non-limiting embodiments illustrated in the accompanying drawing and tables, as well as in the following description. Descriptions of well-known components and processing techniques are excluded to avoid unduly obscuring the embossments presented.

The said purification SEAD (Surface Electro-Adsorption Desorption) unit, as shown in Fig 2, consists of monopolar or bipolar carbon-graphite electrode in the circular/Square form placed in the vertical direction (vertical stack) in the ABS/PP/Polycarbonate, Nylon or similar food grade chamber. The number of free caron-graphite varies from 16, 24, 32, 36, 37, 38, 40, 42, 48 in the electrode stack. Constant DC power is applied to two ends of the electrode in the range of 12V, 24V, 48V & 60V, and maximum capacity of peak current (A) of the input power device is from 5A to 15A and to achieve the 0.1A to 3A through the cell during the process. The electro-adsorption process takes place on the surface of the modified graphite electrode, and excess minerals/contaminants from the fluids/water are removed.

The said purification cartridge unit further comprises the purification system that includes the primary sediment filter or a series of sediment filters, carbon filters, and similar units to remove visible, invisible, dissolved solids or organic impurities from the water source.

Further, the said purification system comprises a microbe-deactivating unit, such as ultraviolet radiation from a UV lamp (253.7nm Wavelength), UV LED (275-280nm), UV LED—reactor-based, hollow, or Sheet membrane with a porosity of 0.01 micron.

Further, the said purification system comprises an ultra-filtration unit, which consists of hollow fiber UF filler (4 or 8''), sheet type UF membrane or specially designed SS 304 mesh (1 micron to 40 microns).

Further, the said purification system comprises a natural taste-fostering unit consisting of modified activated carbon with a pH balancer, micronutrients (Zinc and copper), and an Anti-Biocide Agent (Silver Ion). It is fixed in the post-purification process stage of the water purifier system.

Further, the said purification system comprises IARC & ARPB, a self-rejuvenating unit, and a recirculation segment. The rejuvenating unit includes a new compositional cross-linked polymerized citric acid and citrate-based chelate solution. The rejuvenating unit is connected to a gravity-based non-return valve, which will not allow the solution to be mixed with water.

Further, the said purification system comprises an auxiliary purification chamber, which is ABS/PP or the same type of food grade pressure withstanding cylindrical or square container, and it is ultrasound welded chamber has a fluid capacity of 500 to 1.5 L. One end of the container is fixed with a solenoid valve, and the other end is connected to a recirculation segment.

Further, each purification unit contains seven solenoid valves (6W—8W), which regulate the water/fluid flow to the purification process.

The present invention deals more with the smart water flow algorithm (SWFA). The water purification algorithmic process is explained in detail, as shown in Fig 1.

G. SEAD water purification process consists of the following stages.
1. Physico-chemical impurities particle removing filtration unit. It consists of a sediment filter, activated carbon filter, and Micro mesh SS filter.

2. The electro-adsorption chamber consists of a SEAD (Surface Electro-Adsorption Desorption) unit (SEAD Membrane, Metal Brase Nylon Spacer, Water flow channel SD purification), which is further divided as shown in Fig 3.

2.1 Annulus (Ring type/Square) shaped surface modified-Cation exchange & Anion Exchange Carbon-Graphite electrode with thickness range from (0.55 mm – 1.1 mm], Inner Diameter 10-25mm and electrode diameter size range from 100,125,150-200 mm as shown in Part No.1 of Fig 3 with spacer of nylon material type fiber mesh with thickness of 100 to 500 Micron as shown in Part No. 5 of Figure 3.

2.2 As shown in Part No. 2 of Figure 3, a metal brass terminal (+ve&-ve) with an outer diameter of 10-15mm is fixed.

2.3 SEAD Housing – Cylindrical or Square Shape; Made up of ABS/PP/PC/Nylon, etc., as shown in Part No.3 of Fig 3.

2.4 Electrode cell Membrane circular fluid/water filling phase, water filling from bottom to top through the ¼’’, 1/6’’, and 3/8'' connectors as shown in Part No.4 of Fig 3.

2.5 Direct Negative polarized desorption phase.

2.6 Zero Polarized desorption phase.

2.7 Reversed Positive Polarized adsorption phase.

3. Dual purification Path phase.

4. Performance Enhancement phase.

5. SEAD – Intelligent Rejuvenating Auto-cleaning (IRAC) controlled flow phase.

6. Microbes deactivating phase.
It consists of a (4W to 16W) UV lamp in a cylindrical aluminium camber and quartz glass tube that allows the water flow path or one or more UV LED composite cambers with UV wattages of 0.6mW to 1mW.

7. Natural Taste & immune (NTI) booster cartridge.

H. List of Essential Modules & Components in the present invention
Essential Module in the Invention: TABLE 1

Sl.No. Components Description/Series
1 SWFA encoded microprocessor unit & logic
2 ARPB unit
3 IARC Storage unit
4 PEL unit
5 SensePure Advanced Dual Water Purification technology with SEAD

Components list & specifications: TABLE 2

Sl.No. Components Description Specification
1 SEAD (Surface Electro-Adsorption Desorption) Module It consists of carbon-graphite electrodes of diameter 100mm, 125mm, 150mm or 200mm with specific numbers of electrodes, DC power applied to the cell (12V to 60 V)
2 Yarn Sediment Filter – 5-Micron Polypropylene 48mm or 55mm OD
3 Pre-Activated Carbon Filter - Granules or Block
4 Solenoid valves (V1) –[V1_Inlet] 6W or 7W or 8W; 24VDC
5 Solenoid valves (V2) –[V2_Pre] 6W or 7W or 8W; 24VDC
6 Solenoid valves (V3) –[V3_Rej] 6W or 7W or 8W; 24VDC
7 Solenoid valves (V4) -[V4_Clean] 6W or 7W or 8W; 24VDC
8 Solenoid valves (V5) -[V5_Recir1] 6W or 7W or 8W; 24VDC
9 Solenoid valves (V6) –[V6_Recir2] 6W or 7W or 8W; 24VDC
10 Solenoid valves (V7)—[V7_Citric] 6W or 7W or 8W; 24VDC
11 Booster Pump or Suction Pump Bypass pressure: 75PSI, 24CDC
12 ARPB Unit- Chamber Food Grade plastic; Fluid volume capacity 500 ml to 1.5L – with water inward and outward points
13 Gravity Based NRV- 2No.s Work in the Zero Pressure; Maximum pressure 7 Kg.cm2
14 NRV- 4 No. s Maximum pressure 7 Kg.cm2
15 IARC Storage unit Capacity Max. 1.5 L, Food grade PP
16 Flow Restrictor (FR) 1000ml, 800ml & 600ml
17 UF Membrane Pre Hollow Fiber (4’’ or 8’’) (Optional)
18 TDS Sensor Minimum TDS 10 PPM to 2000PPM
19 4W/8W/11W/16W UV Lamp, Quartz Glass (OD 10 mm to 25 mm with Aluminum Chamber (OD 61 x 63 mm to; or UV LED Reactor Cylindrical Shape. UV LED reactor shape as per the respective manufacturer's design
20 Natural Taste & immune (NTI) Booster cartridge Zinc/Copper impregnated carbon, pH Balancer, Natural minerals
21 PRV-Pressure Reducer Valve Max, 2Kg.cm2 output
22 LPS-Low Pressure Switch 0.3-3 Kg.cm2
23 UV LED – Waterproof 7MW
24 Water Level Sensor (5V) Float/Magnetic/Weight Based/Conductivity sensor
25 Purified Tank (2L – 10L) ABS/PP/SS-304
26 UF Membrane Post Hollow Fiber (4’’ or 8’’) (Optional)
27 SMPS 12V to 60V

I. ESSENTIAL MODULE IN THE INVENTION:
1. SMART WATER FLOW ALGORITHM (SWFA) PROCESS
Potential Difference on SEAD maintained by H – Bridge; [FIGURE 4]
• The operating voltage of SEAD is controlled using an electronic H-Bridge embedded in Micro Controller PCB.
• Initially, all the relays in H-Bridge will be off.
• To apply zero potential to both terminals of SEAD, we need to turn on both the lower relays of the H-bridge. (S2, S4).
• To apply a positive voltage to SEAD, you need to turn on the cross relays of the H bridge. (S3, S2).
• To apply a negative voltage to SEAD, turn on the other pair of cross relays on the H Bridge. (S1, S4).

2. ARPB [Auxiliary Recirculation Performance Booster] Unit. – [FIGURE – 5]
In the current invention, the main differentiation generated by the accurate location of the ARPB unit is the water flow diagram. As the name suggests, the ARPB unit acts as a secondary water storage and recirculation place and enhances water purification with consistency in the mineral content in each purification zone.

ARPB unit is an empty food grade plastic (ABS/PP/PC, HDPE, etc.)/steel (SS 304)/glass closed container with five different purpose opening interfaces in the shape of cylindrical/rectangular/square with a water volume capacity minimum 200 ml to maximum capacity with respect to the dimensions of the point of use domestic water purifier [In the present invention it considered as 800ml volume] and also air vent placed at the lid of the container to provide the free flow in the gravity.

• The first open interface is named Auxiliary Inlet [1]: ¼’’, 5/16’’ & 3/8’’ Male connector used to fix in the container [By this interface, the SEAD purified water fills into the ARPB container. This inlet is connected to the Solenoid valve – V5, which is connected to the water output of the SEAD unit. Water flow to the ARPB container is controlled by the flow restrictor (FR) in the 200 ml to 1000 ml range. In the present designed water purifier, 800ml FR is used. The water filling time/intervals are controlled by the SWFA-encoded microprocessor unit & logic.

• The second open interface is named Suction Point [2]: ¼'', 5/16'' & 3/8'' Male connector used to fix in the container. This interface is connected to the inlet of the booster pump, and water flow is continued towards the outlet of the booster pump, and it is connected to the inlet of the solenoid valve V6 and outlet of the V6 connected the Pressure Reducer Valve (PRV) and it is connected to the inlet of SEAD unit. The Not Return Valve (NRV) avoided reverse flow in an accurate place as per the water flow diagram.

As mentioned above, the booster sucks the water from the ARPB unit; water passes through SV -V6, PRV and reaches to inlet port of the SEAD. This proves that double purification of water will occur; it provides dual water purification and maintains the water TDS level in the final purifier tank, and it maintains the consistency of minerals in the purified tank throughout the purification process.

And this suction interface acts as a Recirculation Zone in the purification stage by circulating the water in the same water loop (Suction Point ?Booster Pump? SV6?PRV? SEAD? SV5 ? Auxiliary Inlet). So, it helps in the double purification by maintaining the water mineral in the ARPB container in a short time sequence (Minimum recirculation time is 20 Sec required).

• The Third open is named Overflow Point [3]: ¼’’,5/16’’ & 3/8’’ Male connector used to fix in the container: This interface to avoid the over follow from the ARPB container and this interface directly connected to the drain line of the water purifier, so it will not allow the water spillage inside the unit. The LLDPE tube with size (¼’’/3/8’’/5/16'') with NRV (Non Return Valve) is connected to the interface, and another end of the tube is connected to the drain line.

• The Fourth open is named an Inlet for Rejuvenating liquid [4]: ¼'', 5/16'' & 3/8'' Male connector used to fix in the container. This interface, with a size of ¼'', is connected to a solenoid valve – V7. SV-V7 connected to the IARC Storage unit (1L). At the time-periodic SEAD cell rejuvenating cycle, the Solenoid valve – V7 opens for the specified time and rejuvenating liquid with a restricted quantity falls into the ARPB container, which is already filled with water. The Fourth open interface of ARPB controls the inlet flow of the rejuvenating liquid to the ARBP container.

• The Fifth open is named as Air Release Vent [5] for the ARPB tank ,it help release the air in the ARPB tank, the air release controlled by the silicon stopper, which can pass only air no water from the container.

3. IARC [Intelligent Rejuvenating Auto-cleaning] unit. – [FIGURE 6]
The role of the IARC unit is to rejuvenate the SEAD electrode by dissolving the scaling from its inter- and intra-surface. The IARC Storage unit consists of a rejuvenating solution with a low or high pH range that can remove the scaling from the SEAD electrode.

The Specially designed chamber with one opening interface [1] with ¼’’/5/16’’/3/8’’ male connector is connected to the ARPB chamber. The top of the container lid with an air vent [2] is placed to get the gravitational flow of the liquid without any pressure.

The rejuvenating liquid based on citric acid or citrate water is stored in a sealed or refillable plastic container. The container has an outlet interface and is connected to the inlet of solenoid valve V7, and SV7 is connected to the ARPB unit chamber. The minimum volume of the IRAC unit is 1L.

The IARC unit process has two different segments. The first one is the rejuvenating liquid with low pH (3-4) or with High pH (10-12). In the rejuvenating periodic sequence cycle (Every 200 cycle or after 250L permeate water usage or manual cleaning), a sequence minimum of 10-20 ml of the rejuvenating liquid is mixed with purified water which is stored in the ARPB unit, and the pH of the water in the ARPB unit chamber become 4 to 10 with respect to the pH of the rejuvenating liquid . The mixed solution of ARPB is passed through the SEAD electrode and rejuvenated the electrode. The pH 4 to 10 solution was recirculated through the SEAD module by the ARBP unit open interface (suction point & Auxiliary inlet). The minimum time required to rejuvenate the SEAD electrode is 5 minutes to 30 minutes.

Using the specially designed IARC unit container helps control the temperature and avoid the rejuvenating liquid's evaporation. If 20 ml of the liquid is used for every 250L purification, it works 50 times for each 250L purification, i.e., for 12500L purification or more than two years.

In the present invention, the rejuvenating process is integrated with the main water purifier, and the microprocessor controls its processing sequence. So, it is fully automated, and no human intervention is required. The rejuvenating program sequence explained in the section part 2 – Step 12.

4. SensePure Advanced Dual Water Purification technology with SEAD
As mentioned, “SensePure” is the built-in water quality sensing unit integrated with the main water purifier unit. It helps diagnose water quality and also adapts SWFA's different purification sequence programs to suit the input water. SensePure technology adapts the SEAD-based water purifier to purify input water from 0 to 2000 PPM.

In the present invention, two possibilities of SensePure are discussed, and details are mentioned below.

4.1 SensePure Water Quality Conductivity sensor in the input line:
In this sequence, it is divided into two conditions.

a. Input Water Less than 200 PPM:
First Method: The SEAD unit is the main purification to reduce the TDS of the water; if the SEAD voltage (48V/60V) continues throughout the purification, more TDS reduction in the input water will occur, leading to less TDS water. To get the mineral-rich purified water, control the SEAD voltage by reducing the voltage to less than 48V/ 60V in the purification zone and increasing the maintenance voltage to 48V/60V. It helps to maintain the minerals in purified water.

The SWFA-encoded microprocessor unit and logic controlled the unit's process with reference to the storage purification program sequence. SEAD voltage control and the purification program independently performed the purification process.

Second method: At the specific time of the purification zone cycle, the input voltage to the SEAD is switched off, i.e., at the sequence of Reversed Positive Polarized adsorption phase. This maintains the mineral level in the output water.
Considered Purified Tank: 5L Voltage to the SEAD Tank TDS, PPM Cycle (Desorption + Adsorption) Time
Input Water TDS
Filling Cycle Desorption Phase Adsorption Phase No. of Cycle
<200 PPM Tank Filling Part 1 Part 2
1L 0V -48V/60V *48V/60V 0V 1 <200 One full cycle 4min; In each one cycle approximately 800ml to 1000ml of water filling in the Purification Tank.
2L 0V -48V/60V 0V +48V/60V 2 <200
3L 0V -48V/60V +48V/60V +48V/60V 3 <200
4L 0V -48V/60V 0V 0V 4 <200
5L 0V -48V/60V 0V +48V/60V 5 <200

b. Input Water Greater than 200 – 2000 PPM:
In this case, Sensepure senses the input water TDS and maintains the SEAD input voltage 48V/60V throughout the purification zone sequence. SWFA encoded microprocessor unit & logic controlled the process of the unit with reference to the storage purification program sequence. SEAD voltage controlling, and purification program independently performs the purification process.

In two case a & b category, Sensepure sensor will decode the input water TDS continuously and send the decoded date to micro controller. Micro controller will control the entire process and process explained.

4.2 SensePure Water Quality Conductivity sensor in the purified water storage container/tank:
In this sequence, the water quality sensor is immersed in the purification tank, and the TDS level of the purified tank is always sensed. As the unit starts as per the pre-programmed SWFA encoded microprocessor logic, purified water begins filling the purified water storage container and, simultaneously, water contact with the Senspure sensor. If the water TDS is less than pre stored value (for example <20PPM ± 10), the sensor provides the signal to the SWFA microprocessor to control the SEAD input voltage (Shut down or reduce the input voltage ) in the respective adsorption cycle, so there is no high TDS reduction, and the unit works as a UV purifier. When the TDS of the purified tank is> 20PPM±10, the sensor provides the signal to the SWFA microprocessor to switch on the input voltage to SEAD, which leads to the TDS reduction. This voltage regulation with purification continues as the purification tank gets filled. The sensor always senses the water quality, compares it with the stored TDS value, and decides the program logic using voltage control.

J. Purification Sequence in the ONE Purification Cycle: Mentioned below. – TABLE 3

a Purification Zone – Part 1 in the ONE CYCLE
1 SEAD Membrane water Filling cycle
2 Direct polarized desorption phase. - section 1 &2
3 Fast Flushing Zero Voltage Polarized Phase 1&2
4 Reversed Positive Polarized adsorption phase1,2 & 3
b Purification Zone – Part 2 in the ONE CYCLE
1 Zero voltage Polarized Phase 1
2 Direct polarized desorption phase. - section 1 & 2
3 Fast Flushing Zero Voltage Polarized Phase 1 & 2
4 Dual Path Purification ARPB Chamber filling zone
5 Reversed Positive Polarized adsorption phase- Section 4
c Purification Zone – Part 3 in the ONE CYCLE
1 PE- Logic cycle
d Intelligent Rejuvenating Auto-cleaning (IRAC) flow phase zone. Part 4

Time for the one purification cycle (a+b) is ~ 4 – 5 minutes.

J.1: Explanation of the Purification Sequence of the ONE Purification cycle on SEAD
Purification Process Zone - Part 1 & Part 2
1. Purification Process Zone – Part 1
Step 1: SEAD Membrane water-filling cycle
a) Cell Terminals (T1 & T2) are short and have no voltage & current across the membrane. -Natural Desorption.

b) All Seven Solenoid valves (V1 to V7) & Pumps are in the off position & there is no water flow through the SEAD.

c) At this time, checking the whole electronic functionality of a system & error identification.

d) At specified intervals at T1 terminals (Anion Exchange side of carbon –graphite cell) -vDC voltage applied & T2 Terminal (Cation Exchange side of carbon-graphite cell) +vDC voltage applied: Desorption begins.

e) At that time, Valve 1, and Valve 2 & Pump open & water filling to the SEAD.

f) The minimum time required for the phase is 10 Sec.

Step 2: Direct polarized desorption phase or -Ve Terminal on SEAD - section 1 & 2
a) T1 Terminal (Anion Exchange side of carbon -graphite cell) is -vDC & T2 Terminal (Cation Exchange side of carbon -graphite cell) +VDC; Desorption of the ion from the carbon-graphite cell takes place.

b) The surface adsorbed +ve & -ve ions penetrate into the pre-treated source water & mineral SEAD cavity source water increase.

c) At this phase -section 1 solenoid Valve V1, V2, V3, V4, V5, V6, V7 & Pump are off for the specific time interval.

d) At this phase, in the section 2 solenoid valves V1, V2, and V3 and the Pump are ON, allowing the high TDS water in SEAD module to be removed from the cell through the drain line by Solenoid valve V3.

e) Flow control valve (FCV)/Flow Restrictor (FR) or without FCV/Flow Restrictor (FR) for better system water recovery management.

f) The time intervals for sections 1 and 2 are prerecorded in the microprocessor, and they range from 5 Seconds to 60 minutes.

Step 3: Fast Flushing Zero Voltage Polarized Phase- Section 1 & Section 2
a) Cell Terminals (T1 & T2) is short and have no voltage & current across the membrane.

b) Specified time intervals in the zero-voltage phase help facilitate the fast peak voltage up in the cell membrane at the positive adoption zone.

c) In section 1, all valves and pumps are off for a certain time (5 Sec is minimum). In Section 2, Solenoid Valves V1, V2, and V3 and the pump are open, the pretreated water entered in to the SEAD module and which helps drain out the high TDS water of the previous phase from the SEAD module & tube. Which help to avoid the cross -mixing of water in the next step (4).

Step 4: Reversed Positive Polarized adsorption phase or +Ve Terminal on SEAD - Section 1, Section 2 & Section 3
a) T1 Terminal (Anion Exchange side of carbon -graphite cell) is +vDC & T2 Terminal (Cation Exchange side of carbon-graphite cell) is -vDC. Adsorption of -ve & +ve ions in the water into the carbon-graphite cell takes place. The input water TDS reduction & inorganic contaminants adsorbed on the surface of the cell.

b) At this phase, pre-filtered water passes to the inlet of the SEAD cell through the PRV (Pressure Reducer Valve).

c) This step is further divided into three sections.

d) Section 1: It works at the initial stage of the process (Unit Switch on time). At this time, +Ve terminal voltage applied on the SEAD module (Adsorption Phase) Solenoid Valves V1, V2, and V5 are open for a specified time (minimum 30 Sec), and the ARPB chamber starts to fill.

e) After finishing the Reversed Positive Polarized adsorption phase – Section 1 – unit restart the cycle from step 1 to Step 3.

f) In the section 2: +ve terminal to SEAD module & solenoid Valve V1,V2, V4 & Pump open–water passes through the SEAD.

g) SEAD water treated passes to the microbes deactivating phase & Natural Taste & immune (NTI) booster cartridge and fill in to the storage tank.

h) The time duration for section 2 is the 30 Sec to 90 Sec.

i) In Section 3, after the specified intervals (30 Sec to 90 Sec), solenoid valve V4 gets closed, solenoid valve V5 opens along with V1, V2 & ARPB storage purified purification tank gets filled in either partial or full.

j) The time duration for the section 3 is 30 Sec to 90 Sec.

SEAD - Dual purification Path Zone: Part 2
This purification process is the continuity of part 1.

Step 5: Zero voltage Polarized Phase.
a) Cell Terminals (T1 & T2) are short and have no voltage & current across the membrane.

b) Specified time intervals in the zero voltage phase help to achieve a fast peak voltage up in the cell membrane at the positive adsorption zone.

c) All valves & pumps are off at this condition.

d) The time duration for the phase is 10 Sec, which is the minimum.

Step 6: Direct polarized desorption phase. - section 1 & 2
a) T1 Terminal (Anion Exchange side of carbon -graphite cell) is -vDC & T2 Terminal (Cation Exchange side of carbon -graphite cell) +vDC; Desorption of the ion from the carbon-graphite cell takes place.

b) The adsorbed +ve & -ve ions dissolve in the pre-treated source water & mineral SEAD cavity source water increase.

c) At this phase-section 1 Valve V1, V2, V3, V4, V5, V6, V7 & Pump closed for the specific time interval.

d) At this phase, section 2 Valves V1, V2, and V3 and the Pump are open, allowing the high TDS water to be removed from the cell through the drain line.

e) Flow control valve (FCV)/Flow Restrictor (FR) or without FCV/Flow Restrictor (FR) for better system water recovery management.

f) Section 1 and Section 2 are time intervals prerecorded in the microprocessor, and they range from 5 Seconds to 60 minutes.

Step 7: Fast Flushing Zero Voltage Polarized Phase- Section 1 & Section 2
a) Cell Terminals (T1 & T2) is short and have no voltage & current across the membrane.

b) Specified time intervals in the zero-voltage phase help facilitate the fast peak voltage up in the cell membrane at the positive adoption zone.

c) In section 1, all valves and pumps are off for a certain time (5 Sec is minimum). In Section 2, Valves V1, V2, V3 and the pump are open, which helps drain out the high TDS water of the previous phase from the tube line.

d) In section 1, all valves and pumps are off for a certain time (5 Sec is minimum). In Section 2, Valves V1, V2, V3 and the pump are open, which helps drain out the high TDS water of the previous phase from the tube line.

Step 8: Recirculation of Purified Water of ARPB Chamber
a) At this sequence, solenoid Valve V1, V2, V3, V4 are closed.

b) Solenoid Valve V5, V6 & Pump are open.

c) Cell Terminals (T1 & T2) are short and have no voltage & current across the membrane.

d) The pump withdraws the water from the ARPB chamber and passes through the valve V6, SEAD unit Valve V5 and the same quantity of water reenter the ARPB chamber (1L).

e) This sequence will continue at specified time intervals (20 Sec-100 Sec).

Step 9: Reversed Positive Polarized adsorption phase- Section 4
a) T1 Terminal (Anion Exchange side of carbon -graphite cell) is +vDC & T2 Terminal (Cation Exchange side of carbon -graphite cell) is -vDC; ion adsorption into the carbon-graphite cell takes place.

b) The time duration for step 9 – section 4 is 30 Sec to 90 Sec.

c) At this phase Valve V1, V2 ,V3 & V5 closed.

d) Valve V6, Pump & V4 open at this phase.

e) Initially, the pump draws water from the ARBP unit chamber through the suction point.

f) The pump output connected the solenoid valve V6 open, and water passed through the PRV and reached the positive polarized SEAD, adsorbing excess minerals adsorbing excess minerals at the surface of the SEAD.

g) At this phase, Valve V6 and pump open, and all the other valves close. Water is drawn from the ARPB chamber, passes through SEAD, and recirculates, maintaining the constant water TDS in the ARPB chamber.

h) The SEAD outlet is connected to Valve V4. It is opened, and water fills the purified water tank after passing through the microbes deactivating phase and NTI Natural Taste and Immune (NTI) booster cartridge.

SEAD – Performance Enhancement Zone: Part 3

Step 10: PEL – Cycle
a) This zone helps to improve the SEAD performance and life.

b) The performance enhancement zone appears only after the completion of one full cycle.

c) The PEL cycle takes place after the 10L purification of the feed water.

d) More time is needed for the desorption process to take place, which helps to activate the porosity of the carbon electrode.

e) T1 Terminal (Anion Exchange side of carbon -graphite cell) is -vDC & T2 Terminal (Cation Exchange side of carbon -graphite cell)) +vDC: Desorption of the ion from the carbon-graphite cell takes place.

f) The adsorbed +ve and -ve ions discharge from the SEAD electron and dissolve in the pre-treated source water, increasing the minerals in the SEAD cavity source water.

g) At this phase, Valves V1, V2, V3, and the Pump are open, allowing the removal of high TDS water from the cell through the drain line.

h) Timing & Intervals for the PEL vary from 30S to 60S & every 5L to 10L purification.

SEAD: Intelligent Rejuvenating Auto-cleaning (IRAC) flow phase zone. Part 4

STEP: 11: SEAD cell Rejuvenation cycle
a) This phase helps the enhancement of carbon-electrode by activating all inter & intra voids of the electrode.

b) The cross-linked polymerized citric acid & citrate-based chelate solution activates the pores.

c) A rejuvenating liquid is a mixture of one chemical compound or two or more chemical compounds, which is food-grade and the common ingredient.

d) This phase has 14 different sub-phases (stage).

e) In the 1st stage (EAC)-Empty Auxiliary Chamber, Empty the ARPB chamber with a direct negative polarized desorption phase. At this time, valves V6, Pump, and V3 open. ARBP stored water is removed through the drain line. The time interval for this is prerecorded in the microprocessor and is in the range of 30 Sec to 1 min.

f) In the 2nd stage (FAC), Refill the ARPB chamber with reversed positive adsorption phase. At this stage, valves V1, V2, V5, and the pump are also used. The time interval is prerecorded in the microprocessor and ranges from 50 Sec to 1 min.

g) In the 3rd stage – (ARAC), the Rejuvenating liquid, which is stored in the IARC container, enters the ARBP chamber by opening Valve V7. The volume of rejuvenating liquid in one cycle will be in the range of 5ml to 50ml. The open& close time sequence of Valve V7 controls the volume of rejuvenating liquid. The time interval for this is prerecorded in the microprocessor and is in the range from 1Sec to 1min.

h) In the 4th stage [A-ST]—Stagnation of the ARPB liquid, all valves and pumps are closed with Zero Voltage Polarized through the SEAD module. This helps mix the rejuvenating liquid with water and achieve a water pH of 4 to 6, which is used to remove the mineral deposit from the SEAD electrode. The Time interval for this is recorded in the microprocessor, and it is in the range from 30 Sec to 5 min.

i) In the 5th stage [MARC] – Mix the rejuvenating liquid recirculation of the mixed water from the ARPB unit. Valve V5, V6, & Pump open with Zero Voltage Polarized through the SEAD module. This helps the mixing of the rejuvenating liquid with water and helps to achieve a water pH of 4 to 6, which is used for removing the mineral deposit from the SEAD electrode. The Time interval for this is recorded in the microprocessor, and it is in the range from 30 Sec to 5 min.

j) In the 6th stage [MARC-Neg] – Mix the rejuvenating liquid by recirculating the mixed water from the ARPB unit with a direct negative polarized phase through the SEAD module. Mixing the liquid at a negative polarized phase leads to dissolving a larger quantity of adsorbed minerals in the liquid. In this stage valve V1, V2, V3, V4 are closed, valve V5, V6 & pump opened. The time interval for this is prerecorded in the microprocessor, and it is in the range from 30 Sec to 10 min.

k) In the 7th stage, [Rinsing- Neg] – Rinsing the SEAD by opening the valve V3, V6 & Pump with direct negative polarized phase. The time interval is prerecorded in the microprocessor and ranges from 50 sec to 70 Sec. It helps to clean the surface of the SEAD cell.

l) In the 8th stage (ARAC -2), open Valve V7 and add the Rejuvenating liquid, which is stored in the IARC container, to the ARBP chamber. The volume of rejuvenating liquid in one cycle will range from 5ml to 20ml. The open and close time sequence of Valve V7 controls the volume of rejuvenating liquid. The time interval is prerecorded in the microprocessor and ranges from 0.5 sec to 20 Sec. This step is categorized as optional.

m) In the 9th stage – [MARC-2] – Repeat Mixing the rejuvenating liquid recirculation of the mixed water from the ARPB unit. Valve V5, V6, & Pump open with Zero Voltage Polarized through the SEAD module. The time interval is prerecorded in the microprocessor and ranges from 30 Sec to 5 min. This step is categorized as optional.

n) In the 10th stage – [Rinsing – Zero] – Rinsing the SEAD by opening the valve V3, V6 & Pump with a direct negative polarized phase. The time interval is prerecorded in the microprocessor and ranges from 50 sec to 70 Sec. It helps to clean the surface of the SEAD cell. This step is categorized in optional.

o) In the 11th stage -[FAC-2]- Refill the ARPB chamber with zero voltage phase. At this stage, valve V1, V2, V5 & pump. The time interval for this is prerecorded in the microprocessor and ranges from 50 Sec to 1 min.

p) In the 12th stage— [Back wash 1]—backwash the SEAD unit using the ARPB chamber stored water by opening valves V3, V6, and the pump with zero terminal. This helps to remove the liquid's residue.

q) In the 13th stage— [Back wash 2]—backwash the SEAD unit using feed water by opening the valves V1, V3, V6, and the pump. This helps to remove the residue and maintain the pH of the SEAD cell. The time interval for this is prerecorded in the microprocessor and ranges from 1 to 5 min.

r) In the 14th stage—[Backwash 3]—backwash the SEAD by opening the valves V1, V2, V3, and the pump. Water passes through the pre-carbon, completely removing any residue of the rejuvenating liquid and maintaining the pH of the SEAD cell.

s) Sequence for the IARC flow phase after each 250L or 200-cycle purification of the feed water.

t) In the 15th Stage – After finishing the IRAC phase, the unit restarts with purification zone part 1.

STEP 12:
a) Completing Steps 1 to 10 is called one purification cycle, and it continues the sequence, which is controlled by the microcontroller.

b) Step 11 cycles is defined as per the defined frequency to maintain the system's performance and efficiency, which is called the Auto cleaning mode.

c) SWPA also has a special provision to run the Auto cleaning mode instantly at a non-defined frequency.

K. Tabular Form of Program flow chart for the Unit working in the present invention.

Case 1: Integrated path:
Sensepure_SWFA_SEAD_ARPB_IRAC_Pre/Post filters – Time Based
• Applicable for 200mm, 150mm, 125mm & 100mm domestic SEAD module.
• Input water TDS range 0-2000PPM.
• Input water Hardness Max. 600PPM.
• The unit consists of pre-stage filters like outer sediment filters, inner sediment filters Pre, activated carbon filters & UF filters.
• The unit comprises post-stage filters like Post immune booster cartridge, UF filters, 11 W UV, and UV-LED.
• Only one Booster Pump.
• For the normal purification, 6 No. of Solenoid valves & one pump acting on the process.
• Water recovery ranges 60-80%.
• Input Water TDS Reduction – 75-95%.
• Unit water delivery flow rate – 10 to 60 LPH.
• Purification Process Zone Part 1, Part 2 & Part 3.
• SWFA – Program mentioned below mentioned TABLE 4. Time duration can vary with respect to the program.
• SEDA regeneration cycle - Intelligent Rejuvenating Auto-cleaning (IRAC) flow phase zone. Part 4 will happen after every 200 cycles, or 250L permeate water collection; the cycle interval/litre can change w.r.t the input water TDS & Hardness level. The detailed process is explained under Step 11, Intelligent Rejuvenating Auto-cleaning (IRAC) flow phase zone.

? Remarks:

1a SEAD Membrane water Filling cycle
2a Direct polarized desorption phase Section 1
2b Fast Flushing Zero Voltage Polarized Phase-Section 1
3a Fast Flushing Zero Voltage Polarized Phase-Section 1
3b Fast Flushing Zero Voltage Polarized Phase-Section 2
4a Initial Reversed Positive Polarized adsorption phase - Section 1
4b Reversed Positive Polarized adsorption phase - Section 2 -
4c Reversed Positive Polarized adsorption phase - Section 3
5a Zero voltage Polarized Phase
6a Direct polarized desorption phase Section 1
6b Direct polarized desorption phase Section 2
7a Fast Flushing Zero Voltage Polarized Phase-Section 1
7b Fast Flushing Zero Voltage Polarized Phase-Section 2
8a Recirculation of Purified Water of ARPB Chamber
9a Reversed Positive Polarized adsorption phase- Section 4
10a SEAD Membrane water Filling cycle
10b Direct polarized desorption phase Section 1
10c Direct polarized desorption phase Section 2

TABLE 4

Sequence Time duration , Seconds SEAD–Voltage Solenoid Vavles (SV) Pump ARPB Unit UV Lamp Flow Restrictor Process
Shunt/Negative/Positive ON Mode OFF Mode ON/OFF Mode Filling /Not Filling /emptying ON/OFF Mode
Purification Process Zone - Part 1
1a 10 Zero V1,V2,V3,V4,V5,V6,V7 OFF Not Filling OFF Natural Discharge
2a 5 Negative V1,V2,V3,V4,V5,V6,V7 OFF Not Filling ON Desorption
2b 12 Negative V1,V2,V3 V4,V5,V6,V7 ON Not Filling ON NO DRAIN FR Desorption
3a 5 Zero V1,V2,V3,V4,V5,V6,V7 OFF Not Filling ON Natural Discharge
3b 5 Zero V1,V2,V3 V4,V5,V6,V7 ON Not Filling ON Natural Discharge
4a 30 Positive V1,V2,V5 V3,V4,V6,V7 ON Filing ON 1000ml FR Adsorption
After finishing 4a Reversed Positive Polarized adsorption phase - Section 1 - unit restart the cycle from step 1 and Step 4a skip from the sequence
4b 35 Positive V1,V2,V4 V3,V5,V6,V7 ON Not Filling Adsorption
4c 65 Positive V1,V2,V5 V3,V4,V6,V7 ON Filling ON Adsorption
Purification Process Zone - Part 2
5a 10 Zero V1,V2,V3,V4,V5,V6,V7 OFF Not Filling OFF Natural Discharge
6a 5 Negative V1,V2,V3,V4,V5,V6,V7 OFF Not Filling ON Desorption
6b 12 Negative V1,V2,V3 V4,V5,V6,V7 ON Not Filling ON NO DRAIN FR Desorption
7a 5 Zero V1,V2,V3,V4,V5,V6,V7 OFF Not Filling ON Natural Discharge
7b 5 Zero V1,V2,V3 V4,V5,V6,V7 ON Not Filling ON Natural Discharge
8a 20 Zero V5,V6 V1,V2,V3,V4,V7 ON Not Filling ON 800ml FR Recirculation
9a 60 Positive V6,V4 V1,V2,V3,V5,V7 ON Emptying ON 1000 ml FR Adsorption
Purification Process Zone(Performance Enhancement Zone) - Part 3 – After Every 7 cycle or
10a 10 Zero V1,V2,V3,V4,V5,V6,V7 OFF Not Filling OFF Natural Discharge
10b 10 Negative V1,V2,V3,V4,V5,V6,V7 OFF Not Filling ON Desorption
10c 35 Negative V1,V2,V3 V4,V5,V6,V7 ON Not Filling ON NO DRAIN FR Desorption
Intelligent Rejuvenating Auto-cleaning (IRAC) flow phase zone. Part 4- after 200 cycle or 250 L

Case 2: Integrated Dual path:
Sensepure_SWFA_SEAD_ARPB_IRAC_Pre/Post filters – Time Based + Drain FR added.
• Applicable for 200mm, 150mm, 125mm & 100mm domestic SEAD module.
• Input water pressure 0 to 3 Kg/cm2.
• Input water TDS range 0-2000PPM.
• Input water Hardness Max. 600PPM.
• The unit consists of pre-stage filters, such as outer sediment filters, sediment filters pre, activated carbon filters, and UF filters.
• The unit consists of post-stage filters, such as a post-immune booster cartridge, UF filters, 11 W UV, and UV-LED.
• For the normal purification, 6 Nos. of Solenoid valves & one pump acting on the process.
• FR 800 ml added in the Auxiliary Inlet, FR 1000ml / 800ml / 600ml / 550ml / 400ml / 200ml added in the outlet of the UV chamber & FR 1000ml / 800ml / 600ml / 450ml / 300ml / 200ml / 100ml added in the reject line with respect to the performance requirements.
• Water Recovery of not less than 70%.
• Input Water TDS Reduction - 80-95%.
• Unit water delivery flow rate – 5 to 16LPH.
• Purification Process Zone Part 1, Part 2 & Part 3.
• SWFA -Program mentioned in the TABLE 5.
• SEDA regeneration cycle – Intelligent Rejuvenating Auto-cleaning (IRAC) flow phase zone. Part 4 will happen after every 200 cycles or 250L permeate water collection; the cycle interval/litre can change w.r.t the input water TDS & Hardness level. The detailed process is explained under Step 11, the Intelligent Rejuvenating Auto-cleaning (IRAC) flow phase zone. Part 4 heading.

TABLE 5

Sequence Time duration , Seconds SEAD–Voltage Solenoid Vavles (SV) Pump ARPB Unit UV Lamp Flow Restrictor Process
Shunt/Negative/Positive ON Mode OFF Mode ON/OFF Mode Filling /Not Filling /emptying ON/OFF Mode
Purification Process Zone - Part 1
1a 10 Zero V1,V2,V3,V4,V5,V6,V7 OFF Not Filling OFF Natural Discharge
2a 5 Negative V1,V2,V3,V4,V5,V6,V7 OFF Not Filling ON Desorption
2b 12 Negative V1,V2,V3 V4,V5,V6,V7 ON Not Filling ON 1000ml DrainFR Desorption
3a 5 Zero V1,V2,V3,V4,V5,V6,V7 OFF Not Filling ON Natural Discharge
3b 5 Zero V1,V2,V3 V4,V5,V6,V7 ON Not Filling ON Natural Discharge
4a 30 Positive V1,V2,V5 V3,V4,V6,V7 ON Filing ON 1000ml FR Adsorption
After finishing 4a Reversed Positive Polarized adsorption phase - Section 1 - unit restart the cycle from step 1 and Step 4a skip from the sequence
4b 35 Positive V1,V2,V4 V3,V5,V6,V7 ON Not Filling Adsorption
4c 65 Positive V1,V2,V5 V3,V4,V6,V7 ON Filling ON 800ml FR Adsorption
Purification Process Zone - Part 2
5a 10 Zero V1,V2,V3,V4,V5,V6,V7 OFF Not Filling OFF Natural Discharge
6a 5 Negative V1,V2,V3,V4,V5,V6,V7 OFF Not Filling ON Desorption
6b 12 Negative V1,V2,V3 V4,V5,V6,V7 ON Not Filling ON 1000ml DrainFR Desorption
7a 5 Zero V1,V2,V3,V4,V5,V6,V7 OFF Not Filling ON Natural Discharge
7b 5 Zero V1,V2,V3 V4,V5,V6,V7 ON Not Filling ON Natural Discharge
8a 20 Zero V5,V6 V1,V2,V3,V4,V7 ON Not Filling ON 800ml FR Recirculation
9a 60 Positive V6,V4 V1,V2,V3,V5,V7 ON Emptying ON 1000 ml FR Adsorption
Purification Process Zone(Performance Enhancement Zone) - Part 3 – After Every 7 cycle or
10a 10 Zero V1,V2,V3,V4,V5,V6,V7 OFF Not Filling OFF Natural Discharge
10b 10 Negative V1,V2,V3,V4,V5,V6,V7 OFF Not Filling ON Desorption
10c 35 Negative V1,V2,V3 V4,V5,V6,V7 ON Not Filling ON 800ml FR Desorption
Intelligent Rejuvenating Auto-cleaning (IRAC) flow phase zone. Part 4- after 200 cycle or 250 L

Case 3: Integrated Dual path:
Sensepure_SWFA_SEAD_ARPB_IRAC_Pre/Post filters – Single line purified water output + Time Based + Flow Restricted added.
• Applicable for 200mm, 150mm, 125mm & 100mm domestic SEAD module.
• Input water pressure 0 to 3 Kg/cm2.
• Input water TDS range 0-2000PPM.
• Input water Hardness Max. 600PPM.
• The unit consists of pre-stage filters, such as outer sediment filters, sediment filters pre, activated carbon filters, and UF filters.
• The unit consists of post-stage filters, such as a post-immune booster cartridge, UF filters, 11 W UV, and UV-LED.
• For the normal purification, 6 No. of Solenoid valves & one pump acting on the process.
• FR 800ml is added in the Auxiliary Inlet in the present invention; FR 1000ml, 800ml, 600ml, 550ml or 400ml is added in the outlet of the UV chamber, and FR 1000ml, 800ml, 600ml, 450ml, 300ml, 200ml or 100ml is added in the reject line.
• Water Recovery of not less than 70%.
• Input Water TDS Reduction - 80-95%.
• Unit water delivery flow rate – 5 to 16LPH.
• SWFA -Program mentioned below TABLE 6.
• SEDA regeneration cycle - Intelligent Rejuvenating Auto-cleaning (IRAC) flow phase zone Part 4 will happen after every 200 cycles, or 250L permeate water collection; the cycle interval/litre can change w.r.t the input water TDS & Hardness level. The detailed process is explained under Step 11, Intelligent Rejuvenating Auto-cleaning (IRAC) flow phase zone. Part 4 heading.
• Note V1, V2, V3, V4, V5, V6 & V7: Solenoid Valve.
• Note the Sequence & Time duration in second can be change according to the requirements of the product performance and it covered in the present invention.

TABLE 6
Sequence Time duration , Seconds SEAD–Voltage Solenoid Vavles (SV) Pump ARPB Unit UV Lamp Flow Restrictor Process
Shunt/Negative/Positive ON Mode OFF Mode ON/OFF Mode Filling /Not Filling /emptying ON/OFF Mode
Purification Process Zone - Part 1
1a 10 Zero V1,V2,V3,V4,V5,V6,V7 OFF Not Filling OFF Natural Discharge
2a 5 Negative V1,V2,V3,V4,V5,V6,V7 OFF Not Filling ON Desorption
2b 12 Negative V1,V2,V3 V4,V5,V6,V7 ON Not Filling ON 1000ml DrainFR Desorption
3a 5 Zero V1,V2,V3,V4,V5,V6,V7 OFF Not Filling ON Natural Discharge
3b 5 Zero V1,V2,V3 V4,V5,V6,V7 ON Not Filling ON Natural Discharge
4a 30 Positive V1,V2,V5 V3,V4,V6,V7 ON Filing ON 1000ml FR Adsorption
After finishing 4a Reversed Positive Polarized adsorption phase - Section 1 - unit restart the cycle from step 1 and Step 4a skip from the sequence
4c 65 Positive V1,V2,V5 V3,V4,V6,V7 ON Filling ON 800ml FR Adsorption
Purification Process Zone - Part 2
5a 10 Zero V1,V2,V3,V4,V5,V6,V7 OFF Not Filling OFF Natural Discharge
6a 5 Negative V1,V2,V3,V4,V5,V6,V7 OFF Not Filling ON Desorption
6b 12 Negative V1,V2,V3 V4,V5,V6,V7 ON Not Filling ON 1000ml DrainFR Desorption
7a 5 Zero V1,V2,V3,V4,V5,V6,V7 OFF Not Filling ON Natural Discharge
7b 5 Zero V1,V2,V3 V4,V5,V6,V7 ON Not Filling ON Natural Discharge
8a 20 Zero V5,V6 V1,V2,V3,V4,V7 ON Not Filling ON 800ml FR Recirculation
9a 60 Positive V6,V4 V1,V2,V3,V5,V7 ON Emptying ON 1000 ml FR Adsorption
Purification Process Zone (Performance Enhancement Zone) - Part 3 – After Every 7 cyle or
10a 10 Zero V1,V2,V3,V4,V5,V6,V7 OFF Not Filling OFF Natural Discharge
10b 10 Negative V1,V2,V3,V4,V5,V6,V7 OFF Not Filling ON Desorption
10c 35 Negative V1,V2,V3 V4,V5,V6,V7 ON Not Filling ON 800ml FR Desorption
Intelligent Rejuvenating Auto-cleaning (IRAC) flow phase zone. Part 4- after 200 cycle or 250 L

Case 4: Integrated: Intelligent Rejuvenating Auto-cleaning (IRAC) flow phase zone. Part
This rejuvenating cycle is the common of SEAD purification process. SEDA regeneration cycle – Intelligent Rejuvenating Auto-cleaning (IRAC) flow phase zone Part 4 will happen after every 200 cycles, or 250L permeate water collection; the cycle interval/litre can change w.r.t the input water TDS & Hardness level. The detailed process is explained under Step 11, Intelligent Rejuvenating Auto-cleaning (IRAC) flow phase zone. Step 11; the simplified & tabular format mentioned below in the TABLE 7

Sequence Time duration , Seconds SEAD–Voltage Solenoid Vavles (SV) Pump ARPB Unit UV Lamp Flow Restrictor Process
Shunt/Negative/Positive ON Mode OFF Mode ON/OFF Mode Filling /Not Filling /emptying ON/OFF Mode
EAU 30 Negative V3,V6 V1,V2,,V4,V5,V7 ON Emptying OFF Desorption

FAU 80 Positive V1,V2,V5 V3,V4,,V6,V7 ON Filling OFF 800ml FR Adsorption
ARAC 20 Zero V7 V1,V2,V3,V4,V5,V6 OFF Filling OFF Rejuvenating liquid filling to ARPB
A-ST 30 Zero V1,V2,V3,V4,V5,V6,V7 OFF ON Stagnation
MARC -1 360 Zero V5,V6, V7(for 10Sec) V1,V2,V3, V4,V7( off after 10 Sec) ON Not Filling ON Recirculation
MARC-2 360 Negatives V5,V6 V1,V2,V3,V4,V7 ON ON Recirculation
Rinsing –Neg 70 Negatives V3,V6, V1,V2,V4,V5,V7 ON Filling ON 1000ml/NO FR Rinsing – 1
FAU -2 80 Zero V1,V2,V5 V3,V4,,V6,V7 ON Filling OFF Filling
Back wash 1 80 Zero V3,V6 V1,V2,V4,V5,V7 On Not filling ON 1000ml/NO FR Back wash 1
Back Wash 2 80 Zero V1,V3 V2,V4,V5,V6,V7 ON Not Filling ON 1000ml/NO FR Back wash 2
Back wash 3 300 Zero V1,V2,V3 V4,V5,V6,V7 ON Not Filling ON 1000ml/NO FR Back wash 3

INVENTIVE STEP
1) A SEAD-based water purification system for infusing with SensePure Advanced dual water purification into drinking water comprising a water inlet, Intelligent Rejuvenating Auto-cleaning (IRAC) unit, Auxiliary- recirculation Performance Booster (ARPB) unit, Performance Enhancement logic (PEL) unit, Smart Water Flow Algorithm (SWFA), double microbial disinfection unit, natural Taste immune (NTI) cartridge, a water storage unit and a water outlet unit.

2) The integrated controlling or regulating of the voltage polarity between two terminals of the SEAD unit, like regulating the up and down voltage in the ranges 24V to 60V or shutting down the voltage in the reversed positive adsorption phase for mineral richness in the purified water.

3) Integrated Intelligent Rejuvenating Auto-cleaning (IRAC) chamber [Rejuvenating Storage unit – is filled with new compositional cross-linked polymerized citric acid or citrate-based chelate solution with a pH range of 2-4 acidic or 8-12 basic raw rejuvenating liquid] connected to ARPB unit through Inlet for Rejuvenating liquid. The electro-magnetic valve controls this loop and helps enhance the SEAD membrane's life (more than 5 Years).

4) Integrated Auxiliary- recirculation performance Booster (ARPB) unit, including food grade polymer container (cylindrical/square) with fluid capacity maximum 1L with four ¼’’ or 5/16’’ or 3/8’’ size openings – (1. Auxiliary inlet, 2. Suction inlet, 3. Over flow & 4. Inlet for rejuvenating liquid). With the help of the ARPB unit, double purification of SEAD feed water helps retain the minerals in the purified.

5) The integrated Double Recirculation—purification loop [ARPB ? Booster Pump ? SV6 ? PRV ? SEAD ? SV5 ? ARPB] helps maintain the consistency of mineral levels in the purified water. It double removes excess impurities and reduces scaling on the surface of the SEAD electrode.

6) The integrated Performance Enhancement Logic (PEL), with a pre-programmed sequence (after 10L purification) and enhancement logic, enhances the adsorption capacity of the SEAD electrode, reduces mineral deposition in the SEAD, and increases the SEAD's life.

7) The integrated Pressure reducer valve (PRV) is connected to the inlet of the SEAD. It always reduces the input water pressure into the SEAD to not more than 2.5 Kg/cm2.

8) The integrated Smart Water Flow Algorithm (SWFA), operating in different SEAD purification sequences, maintains the purified water quality as per IS:10500:2012 and reduces water wastage.

9) The present invention provides the water purifier with water Recovery >= 60-80%, hence low water wastage.

10) The present invention provides water that Delivers 70-90% TDS reduction relative to the input water condition.

11) The system can deliver a flow rate of 5 LPH (Litre per Hour) to 60 LPH, depending on the selected SEAD configuration and system configuration.

12) The system delivers consistent mineral (TDS) levels in the purified water with the help of all combined units.

13) The integrated automatic control of the inbuilt IARC unit flow phase zone in the water purifier reduces manual intervention.

14) Forward purification, recirculation & double purification arising by only one number of Booster Pump there no second pump used in the invention and which is inter connected with seven number of electrically controlled valve (SV).

15) Suitable for all types of zone water (municipal water, groundwater, saline water, mixed water) with water TDS up to 2000 ppm.

While the present invention has been described with reference to a specific preferred embodiment, it will be apparent that various modifications and changes could be made to this embodiment without departing from the scope of the invention. The above-mentioned descriptions are provided to clarify the aspects of the invention, and it will be apparent to one skilled in the art that they do not serve to limit the scope of the invention. By way of example, the total process is customized. The above-mentioned process example is just one of the many configurations that the mentioned components can take on. All modifications and improvements have been incorporated herein for the sake of conciseness and readability but are properly within the scope of the present invention.

,CLAIMS:
1. A Surface Electro-Adsorption Desorption (SEAD) based water purification system for infusing with SensePure Advanced dual water purification into drinking water comprising of:
a water inlet;
an Intelligent Rejuvenating Auto-cleaning (IRAC) unit;
an Auxiliary- recirculation Performance Booster (ARPB) unit;
a Performance Enhancement logic (PEL) unit;
a Smart Water Flow Algorithm (SWFA);
a double microbial disinfection unit;
a natural Taste immune (NTI) cartridge;
a water storage unit and a water outlet unit;
wherein the said purification SEAD unit consists of monopolar or bipolar carbon-graphite electrode in the circular/Square form placed in the vertical direction (vertical stack) in the ABS/PP/Polycarbonate, Nylon or similar food grade chamber and wherein the number of free carbon-graphite varies from 16, 24, 32, 36, 37, 38, 40, 42, 48 in the electrode stack;

2. The SEAD-based water purification system, as claimed in claim 1, wherein said SEAD unit includes controlling or regulating the voltage polarity between two terminals of the SEAD unit, like regulating the up and down voltage in the ranges 24V to 60V or shutting down the voltage in the reversed positive adsorption phase for mineral richness in the purified water.

3. The SEAD-based water purification system, as claimed in claim 1, wherein said Intelligent Rejuvenating Auto-cleaning (IRAC) chamber [Rejuvenating Storage unit – is filled with compositional cross-linked polymerized citric acid or citrate-based chelate solution with a pH range of 2-4 acidic or 8-12 basic raw rejuvenating liquid connected to ARPB unit through Inlet for Rejuvenating liquid; and wherein the said loop is controlled by the electro-magnetic valve configured to enhance the life of the SEAD membrane.

4. The SEAD-based water purification system, as claimed in claim 1, wherein said Auxiliary- recirculation performance Booster (ARPB) unit, includes a food-grade polymer container (cylindrical/Square) with a fluid capacity maximum of 1L with four ¼'' or 5/16’’ or 3/8’’ size opening; and wherein the said ARPB unit includes double purification of SEAD feed water to retain the minerals in the purified.

5. The SEAD-based water purification system, as claimed in claim 1, wherein said integrated Double—Recirculation—Purification loop includes ARPB ? Booster Pump ? SV6 ? PRV ? SEAD ? SV5 ? ARPB], which is configured for the consistency of mineral levels in the purified water. The booster pump double removes excess impurities and reduces scaling on the surface of the SEAD electrode.

6. The SEAD-based water purification system, as claimed in claim 1, wherein said integrated Performance Enhancement Logic (PEL), with pre-programmed sequence and enhancement logic, enhances the adsorption capacity of the SEAD electrode, reduces mineral deposition in the SEAD and increases the life of the SEAD.

7. The SEAD-based water purification system, as claimed in claim 1, wherein said integrated Pressure reducer valve (PRV), which is connected to the inlet of SEAD and wherein said PRV reduces the input water pressure to the SEAD by not more than 2.5 Kg/cm2.

8. The SEAD-based water purification system, as claimed in claim 1, wherein said integrated Smart Water Flow Algorithm (SWFA) is configured to operate in different SEAD purification sequences, maintain the purified water quality as per IS:10500:2012, and reduce water wastage.

9. The SEAD-based water purification system, as claimed in claim 1, wherein said water purifier with water Recovery is more than equal to 60-80%, hence low water wastage.

10. The SEAD-based water purification system, as claimed in claim 1, wherein the water delivery percentage of TDS reduction is 70-90% based on the input water condition.

11. The SEAD-based water purification system as claimed in claim 1, wherein the integrated automatic controller of the inbuilt IARC unit flow phase zone in the water purifier reduces the manual intervention in the water purifier.

12. The SEAD-based water purification system, as claimed in claim 1, wherein said forward purification, recirculation, and double purification arise from only one Booster Pump, which is interconnected with seven electrically controlled valves (Solenoid Valve).