Hlorogen H2000

hlorogen_mali150Hlorogen is device for electrolytic production of chlorine in the form of sodium hypochlorite (NaOCl) solution.
Capacity is 2 kg/h or 48 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.

Characteristics of the system

Hlorogen H2000 – Characteristics of the system

Two E1000 electrolyzers capacity to produce 2000g/h, 48.0 kg/day is sufficient to disinfect the water with flow of 1111 l/s in order to maintain the 0.5 mg/l residual prescribed by law.

Maximum water flow that can be disinfected with Hlorogen H2000, depending on chlorine needs 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

33,33

3333

2000

200

1852

0

0,4

33,33

3333

2000

200

1389

0

0,5

33,33

3333

2000

200

1111

0,1

0,5

33,33

3333

2000

200

926

0,2

0,5

33,31

3331

1998

199,8

793

0,3

0,5

33,31

3331

1999

199,9

694

0,4

0,5

33,32

3332

1999

199,9

617

0,5

0,5

33,3

3330

1998

199,8

555

0,6

0,5

33,33

3333

2000

200

505

0,7

0,5

33,33

3333

2000

200

463

0,8

0,5

33,31

3331

1998

199,8

427

0,9

0,5

33,26

3326

1996

199,6

396

1

0,5

33,3

3330

1998

199,8

370

1,2

0,5

33,25

3325

1995

199,5

326

1,4

0,5

33,29

3329

1997

199,7

292

1,6

0,5

33,26

3326

1996

199,6

264

1,8

0,5

33,26

3326

1996

199,6

241

2

0,5

33,3

3330

1998

199,8

222

2,2

0,5

33,21

3321

1993

199,3

205

2,4

0,5

33,23

3323

1994

199,4

191

2,6

0,5

33,29

3329

1998

199,8

179

2,8

0,5

33,26

3326

1996

199,6

168

3

0,5

33,18

3318

1991

199,1

158

3,5

0,5

33,12

3312

1987

198,7

138

4

0,5

33,21

3321

1993

199,3

123

4,5

0,5

33,3

3330

1998

199,8

111

5

0,5

33,33

3333

2000

200

101

 

 

Techical Data

HLOROGEN  H2000 – TECHNICAL DATA

Capacity of equivalent chlorine (kg/h):

2

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

20

Softened water flow (l/h):

180

Electrolyte flow (l/h):

200

Salt consumption (kg/h):

6

Power consumption (W):

12000

Voltage (~V; 50Hz):

170 – 250

NaOCl solution strength (%):

0,9 – 1

Electrolyzer E1000 (pcs):

2

Hydraulic board with stand (pcs):

2

Water softener K180/30 (pcs):

2

Softened water tank ROMH500/1000(pcs):

2

Saturator RSH500/1000(pcs):

1

NaOCl tank RNHH500/1000(pcs):

1

Brine pump Sigma Classic MTM (pcs):

2

Softened water pump Sigma Classic MGM (pcs):

4

Power supply OEH (pcs):

1

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

2

Microprocessor control – Hlorogen PLC (pcs):

2

Electrolyzer Model E1000 – 2 pieces

anodes

cathodes

capacity ekv. Cl2 (kg/h)

capacity ekv. Cl2 (kg/day

pcs.

dim.(mm)

material

conn.

pcs.

dim.(mm)

material

conn.

1

24

16

200 x 250 x 2

Titanum

serial

24

200 x 250 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

100

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)

27

180

PSP-1500-13,5

170 – 240

20

5

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

72

1728

556

 

Operation Basics

Hlorogen H2000 – 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 OF HLOROGEN PLANT

HLOROGEN_tehnoloska_sema

 

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