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POLYOL PRODUCTS & PENTAERYTHRITOL PROCESSES

PENTAERYTHRITOL or PE is a tetrahydric alcohol which has found widespread use in the Resin, Plastics, Lubricants and Explosive industries.

It is a white crystalline solid which has four methylol groups arranged symmetrically around a central carbon atom as shown in the structural formula below:

Pentaerythritol Structure

POLYOL PRODUCTS’ PROCESSES

PENTAERYTHRITOL PRODUCT SPECIFICATIONS
PROPERTY SPECIFICATIONS
AppearanceWhite coarse free flowing
Monopentaerythritol content (Wt % Min.)98
Hydroxyl number (Mg KOH/g)1625 – 1650
Melting Point (Min. degree C)257
Moisture content (Wt % Max.)0.1
Ash content as Na (PPM Max.)15
Colour as Phthalate (Gardner Max.)1.4
SODIUM FORMATE SPECIFICATIONS
Melting point (water–free salt)255°c
Melting Heat244.5 kJ/Kg
Specific Heat1.21 kJ/Kg K
Amino Phenolic Resin Process Amino Phenolic Resin Process

NEO PENTYL GLYCOL (N. P. G.)

ATEC offers the “State of the Art” Process Technology for production of Neo Pentyl Glycol (NPG) under a special licensing Agreement with a renowned European licensor.

NEO PENTYL GLYCOL
Characteristics Standard Limit
Purity99% min
Hydroxyl number1065 mg KOH/g min
Acidity number0.1 mg KOH/g max
Colour (APHA)max 15 mg Pt/l
Water (molten product)0.3% max
Solidification point124 to 130°C
Amino Phenolic Resin Process

N.P.G Process

Amino Phenolic Resin Process

N.P.G Process-2

N. P. G. Process Description

Neo Pentyl Glycol (NPG) Plants

Plant 1
  1. The raw materials, from the general storage, are charged to the reactor.
  2. The reaction is accomplished batch wise.
  3. The reaction liquors are concentrated in a multistage evaporation plant.
  4. The condensate is sent to methanol recovery unit.
  5. The concentrated reaction liquors are extracted by solvent and washed with water.
  6. The raffinate product - sodium formate solution - is sent to storage for direct use in other plant.
  7. The extracted product - NPG and solvent - is treated by multistage distillation plant.

T. M. P. PROCESS

Tri Methylol Propane (T.M.P.) is a type of Polyhydric Alcohol, resulting from mixed Aldol Condensation reaction between Formaldehyde and Acetaldehyde, Isobutyraldehyde and Butyraldehyde. Initially an Aldehydic intermediate is formed which must be reduced to Polyhydric Alcohol.

TMP is produced by reaction of Butyraldehyde, Formaldehyde and a base Sodium Hydroxide in aqueous medium. The reaction takes place according to the following equation:

C2H5CH2CHO + 3HCHO + NaOH → C2H5C(CH2OH)3 + HCOONa

Sodium Formate equivalent to each mole of TMP is produced as a byproduct. Finally the excess alkali is neutralized with Formic Acid and the pH is brought down to 6.8 and unreacted Formaldehyde is distilled off and this is followed by recovery of Tri Methylol Propane from the residual solution. The reaction is vigorous and the reaction temperature is maintained between 50–60°C. The rise of temperature is about 30°C.

TMP is recovered by extraction with Ethyl Acetate. The extract is distilled to evaporate the solvent and any water. The residue from this distillate is crude TMP containing minor amounts of less volatile impurities. Crude TMP is purified by vacuum distillation of this product at 142°C and 3 mm Hg absolute pressure.

TMP Plant