Home About Us Products Projects Accessories Technical Services Flea Market Cooperations Contact us
Pharmaceutical Water-One Stage RO++EDI

 

Pharmaceutical water is usually produced by distillation, ion exchange, RO or other reasonable technologies, and there is not addtives in the permeate water at all..

We usually use the following three technologies to produce purified water:

Two stage RO

One stage RO + mixed bed(demineralization)

One stage RO + EDI

Mix bed must be periodically regenerated to remove contaminant ions sticking to the resin, that will be harmful to environment by using large quantity of chemicals (acid&alkali) and water during the regeneration. However, EDI is a technology which combines ion exchange,membrane filtration. EDI system replaces conventional mixed beds to produce deionized water,it does not require shutdowns for replacing resin beds or for resin regeneration using chemicals. So one stage RO+EDI is more superior to one stage RO+Mixed bed.

 

One Stage RO

Natural osmosis occurs when a semi-permeable membrane separates two fluids of different salinity. The fluid with the lower salinity will pass through the membrane until the salt solution becomes equal on both sides of the membrane.

 

Reverse osmosis ROis the reverse of normal osmosis processit occurs when the water is forced by pressure from higher salinity solution to permeated water side across a semi-permeable membranethe memebrane allows the passage of water, but not impurities, organics, ions etc. The rejection rate can usually reach above 97, and the highest will reach 99.8

 

The contaminants such as inorganic salt, bacterias,virus, glucides,amino acid will be removed through RO system. Therefore to get ideal purified water.

 

We use the membrane elements ESPA series from Hydranautics Company featuring high performance, ultra low pressure needs, high productivity and energy savings, 4 inches and 8 inches elements have been frenquently used.

 The Operating Conditions of One Stage RO System

Item

Run Conditions

Item

Run Conditions

Operating Pressure of Pretreatment System

0.3MPa

Operating Pressure of RO System

1.05MPa

Operating Temperature

5℃40

PH of Feed Water for RO System

49

Control Mode of  Main System 

manualautomatic (optional)

Power Requirements

Three-phase four-wire     AC380V/50HZ

Control Mode of  Pretreatment System 

Manual valvesfully automatic solenoid control valves, fully automatic multiport control valves  (optional)

 

 

 Spefications of JNB One Stage RO System

 

No

Model

Permeate Flowt/h

Power Consumptionkw/h

Control Mode

Specifications for    RO Membranes

1

JB-ROY300

0.3

2.5

manualautomatic (optional)

ESPA4040

2

JB-ROY500

0.5

3.0

manualautomatic (optional)

ESPA4040

3

JB-ROY750

0.75

3.0

manualautomatic (optional)

ESPA4040

4

JB-ROY1000

1.0

3.5

manualautomatic (optional)

ESPA4040

5

JB-ROY1500

1.5

4.5

manualautomatic (optional)

ESPA4040

6

JB-ROY2000

2.0

5.5

manualautomatic (optional)

ESPA4040

7

JB-ROY3000

3.0

6.5

manualautomatic (optional)

ESPA4040

8

JB-ROY4000

4.0

7.5

manualautomatic (optional)

ESPA4040

9

JB-ROY5000

5.0

8.5

manualautomatic (optional)

ESPA4040

10

JB-ROY6000

6.0

9.5

manualautomatic (optional)

ESPA4040ESPA8040  (optional)

11

JB-ROY8000

8.0

16.5

manualautomatic (optional)

ESPA4040ESPA8040  (optional)

12

JB-ROY10000

10.0

17.5

manualautomatic (optional)

ESPA4040ESPA8040  (optional)

 

2E D I Electrodeionization

EDIElectrodeionizationremoves ions from water using conventional ion-exchange resin. However, in EDI ,an electrical current is used to regenerate the resin continuously, eliminating the need for periodic chemical regeneration.

EDI stacks are the heart of an EDI system,a single stack has the basic structure of a deionization chamber. In the chamber, ion exchange resins are packed between ion exchange membranes (cationic and anionic),only the ions can pass through the membranes, the water is blocked in the dilute flowing out of the stack. When the system applies DC electrical field to the single EDI stack, charged ions are discharged to regenerate the ion exchange resins,all the processes of EDI have been regenerated through electricity continuously, so it’s also called CDIcontinuous deionization.

The EDI system is used to produce ultrapure water(conductivity <2μS/cm), the rejection rate of which is more than 99%. Weak electrolyte within the water, such as silicic acid, boric acid,carbonic acid,ammonia etc, can be removed effectively. The feed water to the EDI system must be one or two-stage RO permeate or better, and the conductivity of RO is usually 2-40μS/cm25℃.

                      Operating Conditions of EDI

Feed Water Pressure

0.4MPa

Feed Water PH Range

6.09.0

Hardness of Feed WateBased on CaCO3

  0.75 ppm

Total Oganic CarbonTOC

0.5 ppm

Dissolved Silicon

0.5 ppm

Residual chlorine

0.01 ppm

FeMnH2S

0.5 ppm

Operating Temperature

5℃35

Total Exchangebale Anions

25ppm

Total Exchangebale Cations

25ppm

Total Exchangebale Substances Based on CaCO3

50ppm

 

 

Specifications of EDI

Model

Voltage (V)

Electric Current(A)

Flow Rate (m3/h)

Weight (kg)

JB-200

1525

26

0.20.4

20

JB-500

3550

26

0.40.7

26

JB-1000

6090

26

0.91.2

32

JB-2000

115180

26

1.02.0

48

JB-3600

180300

26

2.03.5

74

Notes: Other flow rate available on request.