Precipitated Silica (Anti Blocking Grade)

PLANT PARAMETERS

Capacity

2.5 MT/day or 750MT/annum

No.  of Shifts  per day

3

Working days per Year.

300

Land Area, m2

10000

Covered Area, m2

1350

MANPOWER

Managerial

1

Skilled

19

Unskilled

9

RAW MATERIAL/DAY

Sodium Silicate (Glass)

 3.125 MT

Sulfuric Acid(Oleum)

1.25 MT

Sodium Sulfate

 

UTILITIES/DAY

Power

1000 KWH

Water  

75 KL

Steam

5 Tons

Fuel (Kerosene)

1000 Lits

PLANT & MACHINERY

 Fluidised bed coal fired boiler

1

Digestor for sodium silicate glass

1

Silicate storage tanks

3

SS 316 reactor jacked

1

Instrumentation & flow controls

--

Plate & frame type filter press

1

Flash drier having water evaporation

1

Alpine fluidized bed opposed jet mill

1

Pumps with motors

8

Air compressors

2

Weighing scale

1

ECONOMICS

Know-how/turnkey fees

Negotiable

Consultancy fees

Negotiable

Operating experience

Proven

The above figures are for budgetary purpose only and subject to change in subsequent offers

 

USE  USES 

The Product  is used in all polyethelene and polypropelene plastic films raw materials manufacturers i.e. Petrochemicals units producing PE & PP granules.

SPECIFICATIONS

S.No.

Properties

Unit

Specified Limit

1.

Appearance

-

White free flowing powder

2.

Moisture Content (105oC, 2 hrs)

%

4.0 max

3.

Loss on Ignition (100oC, 2 hrs) (Anhydrous basis)

%

4.0 max

4.

Bulk Density (tapped 50)

gm/lit

80-120

5.

pH Value(5% aq. Slurry)

--

5.5-7.5

6.

Water Absorption Value

%

200-250

7.

Si2O Content (Anhydrous basis)

%

98.50 min

8.

Soluble Salts (Sulfates+Chlorides)

%

0.50 max

9.

Iron Content, (As FE+3 )

Ppm

200 max

10.

Average particle size (Malvern)

Micron

4-6

11.

Surface Area

M2/gm

325 ± 25

12.

Heavy Metals, (Expressed as Pb)

ppm

15 max

PROCESS

 Sodium silicate glass is digested in a digestor at high temp. and pressure and desired concentration of sodium silicate solution is obtained. Using above sodium silicate solution and dilute-sulfuric acid, reaction is carried out in a reactor in presence of optimised quantity of electrolyte at elevated temp and in the optimised quantity of electrolyte at elevated temp and in the optimised pH range of the reaction medium.

After completion of reaction in stipulated time, product slurry is filtered and washed with water to remove soluble salts generated during the reaction. The washed cake is again reslurried before it is flash dried in flash drying system.

The product is then milled to get the desired particle size distribution of the finished product. The finished product is then packed in 15 kgs. HDPE/paper bags as per the requirement of the user industry.

 

NRDC

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National Research Development Corporation
( A Government of India Enterprise )
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New Delhi 110 048. India
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