Hlorogen Container Chlorination Station KHS3

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Hlorogen container on-site electrolytic system is the optimal solution when there is no adequate space to accommodate equipment for the disinfection of drinking water, as well as in the case when it is needed to place equipment for chlorination to a temporary location.
It consists of a storage container in which is the complete technological equipment installed, and as such is delivered to the buyer.
All the necessary equipment for remote monitoring and control is installed; therefore it can operate without a human crew. It is fast, reliable, efficient and cheap solution.

 

Characteristics of the system

Hlorogen Container Chlorination Station KDS3 – Characteristics of the system
KHS3 Container Station consists of : HLOROGEN H125 device, ADS – Automatic dosing system, PC for acquisition of sysstem data and remote control and managment by GSM or GPRS communication.
Hlorogen Container Chlorination Stations KHS3 capacity is 0,250 kg / h or 6,0 kg / day of equivalent chlorine.
Since no gaseous chlorine is present, water chlorination is absolutely safe due to system design. For production of sodium hypochlorite solution all that is needed is  common salt,  softened  water and electric energy. Production expenses are up to two times lower compared  to gaseous chlorine disinfection, or commercial sodium hypochlorite.

System is easy to use, demands only minimal maintenance and it is fully automated. Exploitation period is minimum 20 years.

E250 electrolyzers capacity to produce 250g/h, 6.0 kg/day is sufficient to disinfect the water with flow of 139 L / s in order to maintain the 0.5 mg/l residual prescribed by law.

The maximum water flow that can be disinfected with Hlorogen H125, depending on chlorine demand and desired residuals

 

Chlorine need (mg/l) 

Desired chlorine residual (mg/l) 

Chlorine consumption (g/min) 

NaOCl consumption (ml/min) 

Chlorine consumption (g/h) 

NaOCl consumption (l/h) 

Maximal water flow (l/s) 

0

0,3

4,16

416

249

24,9

231

0

0,4

4,15

415

249

24,9

173

0

0,5

4,17

417

250

25

139

0,1

0,5

4,14

414

248

24,8

115

0,2

0,5

4,16

416

249

24,9

99

0,3

0,5

4,13

413

248

24,8

86

0,4

0,5

4,16

416

249

24,9

77

0,5

0,5

4,14

414

248

24,8

69

0,6

0,5

4,16

416

249

24,9

63

0,7

0,5

4,10

410

246

24,6

57

0,8

0,5

4,13

413

248

24,8

53

0,9

0,5

4,12

412

247

24,7

49

1

0,5

4,14

414

248

24,8

46

 

 

 

Techical Data

KHS3 – 250 HLOROGEN CONTAINER SYSTEM – TECHNICAL DATA

Construction:

galvanized and painted steel profiles

The roof and walls:

polyurethane “sandwich” panel plastic coated galvanized steel sheet

Floor:

“Grill” of galvanized steel and colored profile, polyurethane “sandwich panel of 40mm, ceramic tiles

Dimension (W x D x H) mm:

4000 x 2410 x 2680

The weight of containers with equipment (kg):

2500

Installed power (W):

3500

Voltage (~V; 50Hz):

3×220/380

Water inlet (“):

1/2

Analyzer inlet (”):

1/2

Drain connections (“):

3 x 1/2

NaOCl outlet (”):

1/2

HLOROGEN H125gr  (pcs):

1

ADSR11 (pcs):

1

Main power cabinet GRO (pcs):

1

GSM communication cabinet ROGK (pcs):

1

Auxiliary tank for NaOCl RNHH50/250 (pcs):

1

Air conditioner (pcs):

1

HLOROGEN  H250 – TECHNICAL DATA

Capacity of equivalent chlorine (kg/h):

0,250

Saturated brine solution flow 30%(l/h):

2,50

Softened water flow (l/h):

22,50

Electrolyte flow (l/h):

25,0

Salt consumption (kg/h):

1,45

Power consumption (W):

1300

Voltage (~V; 50Hz):

170 – 250

NaOCl solution strength (%):

0,9 – 1

Electrolyzer E250 (pcs):

1

Hydraulic board with stand (pcs):

1

Water softener K180/20 (pcs):

1

Softened water tank ROMH50/250(pcs):

1

Saturator RSH50/250(pcs):

1

NaOCl tank RNHH50/250(pcs):

1

Brine pump Sigma Classic MTM2 (pcs):

1

Softened water pump Sigma Classic VGM (pcs):

1

Power supply OEH (pcs):

1

Ventilation system – Fan TD-160/100N (pcs):

1

Microprocessor control – Hlorogen PLC (pcs):

1

Electrolyzer Model E250

anodes

cathodes

capacity ekv. Cl2 (kg/h)

capacity ekv. Cl2 (kg/day)

pcs.

dim.(mm)

material

conn.

pcs.

dim. (mm)

material

conn.

0,250

6

8

150 x 100 x 2

Titanium

serial

5

150 x 100 x 2

Hastelloy

serial

Input electrolyte NaCl (gr/l)

Total electrolyte flow (l/h)

Conversion index (kg NaCl/1kg Cl2)

Current density (mA/cm²)

Input water temperature (˚C)

Allowed water hardness (mg/l CaCO3)

30

25

2,8 – 3

100

5 – 20

17

Working DC voltage (V)

Optimal DC current (A)

Switching power supply type

Allowed AC voltage (V)

Max. DC current (A)

Optimal power consumption (kWh)

14

60

PSP-1500-13,5

170 – 250

10

1.2

Produced solution concentration (%)

Optimal electrolyte temperature (˚C)

Salt consumption (kg/day)

Salt consumption (kg/month)

*Maximal water flow with keeping residual at  0,5 mg/l which can be disinfect (l/sec)

0,9 – 1

30

9

540

139

 

Operation Basics

 Hlorogen Container Chlorination Station KHS3 – Operation Basics

Water from the pipeline is filling water softener (4), calcium and magnesium ions are removed, and on the outlet of the softened water is obtained. Dosing pump (6) is transferring this water to the electrolyser where it is mixed with sodium chloride solution transferred from tank (3) by means of another dosing pump ( tank 3 contains saturated sodium chloride solution). Electrochemical reaction which results in conversion of sodium chloride into sodium hypochlorite is taking place in the electrolyser cell energized by direct electric current from energetic assembly (35) of the Hlorogen device Hypochlorite solution is stored in the tank (2). Hydrogen generated by conversion reaction is let in to atmosphere by means of ventilating system (28). Optimal hypochlorite production is achieved using system automatic arrangement (36). Sodium hypochlorite solution is injected by dosing membrane pumps (38) into pipeline with water to be disinfected. Residual chlorine analyzer (39) connected into regulation circuit with dosing pump keeps the concentration of residual chlorine in the water on the predetermined level. This is providing continuous production of disinfecting agent, automatic process control and automatic dosing and residual chlorine control.

Full system operation can be monitored through PC (37).

TECHNOLOGICAL SCHEME HLOROGEN PLANT

HLOROGEN_tehnoloska_sema

 

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