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State of art SO3 Falling Film Tube Reactor Plant comprising of following sections :
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Air Drying Unit
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Sulphur Melting & Metering Unit
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Sulphur Combustion and SO2 / SO3 Convert Unit
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Sulphonation / Sulpation Unit
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Ageing & Stabilizing Unit
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Neutralization Unit
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Exhaust Gas treatment with electrostatic precipilato.
LABSA |
97 |
Free Oil |
1.2 |
Colour |
less than 20 Klett |
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Linear Alkyle Benzene (LAB) & Sulphuric acid are fed in proportion & controlled manner through a recycle venturi by a reaction loop pump into battery of digestion tubes. Reaction is axothermic & temperature is controlled by cold water circulation through heat exchangers. Reacted mass is further digested & continuously diluted in dilutor & separated by continuous gravity separation.
| LABSA |
90 |
| Free Oil |
0.5 |
| Colour |
less than 10 Klett |
Size: 500kgs/hr to 4000kgs/hr.
There is no gaseous, liquid or solid affluent in this process.
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Linear Alkyle Benzene (LAB) & Sulphuric acid are dosed through a batch tank into a Reactor & recycled through Loop Pump through a Heat Exchanger till reaction is complete. Digested mass is transferred to a Batch Dilutor for addition of water & gravity separated in the same vessel.
| LABSA |
89 |
| Free Oil |
0.5 |
| Colour |
less than 10 Klett |
Size: 500kgs/hr to 4000kgs/hr.
There is no gaseous, liquid or solid affluent in this process.
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Linear Alkyle Benzene (LAB) & Sulphuric acid are fed into the Reactor through a Batch Tank, digested, diluted, & separated in the same vessel.
| LABSA |
89 |
| Free Oil |
0.7 |
| Colour |
less than 20 Klett |
Size: 500kgs/hr to 4000kgs/hr.
There is no gaseous, liquid or solid affluent in this process.
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Dilution process of sulphonated mass is extremely exothermic, highly corrosive & requires extensive cooling. It is achieved through water circulation through a lead bonded coil to withstand highly corrosive process.
Size: To Suit.
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Electrical control to meet safety & control legislations of the process.
Size: To Suit.
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