| Market price | 10,310 | Upper limit price | 13,460 | |
|---|---|---|---|---|
| High price | 10,930 | Lower limit price | 7,260 | |
| Low price | 10,310 | EPS | 3233 | |
Stock Price Status
COPYRIGHT ISU CHEMICAL. ALL RIGHTS RESERVED.
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| Market price | 10,310 | Upper limit price | 13,460 | |
|---|---|---|---|---|
| High price | 10,930 | Lower limit price | 7,260 | |
| Low price | 10,310 | EPS | 3233 | |
COPYRIGHT ISU CHEMICAL. ALL RIGHTS RESERVED.
Features of the NP process
Raw Material Reservoirs
Receiving and storing Kerosene, the raw material for Normal Paraffin, from S-Oil
Prefractionation process
The light cut of the preheated material flows to the overhead of the column. Raw material moved to the Bottom enters the Hydrotreating Unit
Hydrotreating process
Kerosene is reacted by adding hydrogen to remove sulfur, oxygen, nitrogen compounds, etc. which reduces the activity of the Molecular Sieve of the Molex process
Hydrogen unit
Rerun Column
The column that removes heavy oil from kerosene separates the oil with a high boiling point from the bottom of the column and sends it to the heavy-cut reservoir, and the upper oil proceeds to the Molex process
Extraction Process MOLEX
Extraction of Kerosene from the hydrotreating process by selective adsorption into Normal Paraffin and Raffinate
Fractionation process POST
The process to categorize incoming Normal Paraffin from Molex processes by carbon number
Features and Advantages of SS Process
Raw Material Sorage
Store Crude Oil, the raw material for SS products.
Reaction Effect
Effect Crude Oil and H2 at appropriate temperature and pressure and remove Aromatic.
Fractionation Distillation
Produce the SS product meeting customer's needs through Distillation.
Features and Advantages of TDM Process
Raw Material Storage
Store Propylene Tetramer, the Raw materials for TDM products.
Reaction Effect
Effect the raw material and the H2S, the byproduct of NP process at appropriate temperature and pressure.
Fractionation Distillation
produce the TDM product meeting customer's needs through Distillation.
Features and Advantages of IPA Process
Raw Material Storage
Store Acetone, the raw material for IPA products
Reaction Effect
Effect Acetone, and H2 at appropriate temperature and pressure
Fractionation Distillation
Produce the IPA product meeting customer's needs through Distillation
Features of the LAB process
Raw Material Input Process
Processes required to reliably supply Normal Paraffin to the 'Dehydrogenation Process'
Pacol Process
The dehydrogenation process to convert Normal Paraffin to Olefin by heating it to a high temperature of 470~484oC and passing it through a fixed bed reactor, the PACOL Reactor
Alkylation Process
Process of reacting Olefin with Benzene under HF catalyst to produce Alkylate
Fractionation Process
The excess benzene in the Alkylation process and the NPs remaining after the reaction in the dehydrogenation process are separated by distillation and recycled to the Alkylation process and raw material stabilization tower, respectively. The final remaining Alkylate is then separated in a distillation column to spec
Export Terminal
Features of the BAB process
Raw Material Input Process
After PT and Benzene are fed into the Feed Drying Column, dissolved oxygen and moisture are removed
Alkylation Process
Process of reacting PT with Benzene under HF catalyst to prepare Alkylate
Fractionation process
The process of separating the produced Alkylate to specification in a distillation column
