Technologies
From hydrocarbon fractionation to waste solvent recovery engineered around your feed.
Balaji Consultants designs and supplies batch and continuous specialty-solvent distillation systems for the separation, fractionation, recovery and purification of valuable hydrocarbon and solvent streams. Unlike crude-oil topping, where the objective is to produce a broad slate of petroleum fractions, specialty-solvent distillation is generally designed to produce narrower boiling-range products with tighter quality specifications or to recover and purify solvents from contaminated process or waste streams.
Typical applications include kerosene fractionation into different grades of white spirit, diesel-range feed fractionation into white-spirit cuts, recovery of spindle-oil-range base fractions, specialty naphtha fractionation, aromatic solvent separation and purification, and recovery of reusable solvents from contaminated industrial streams — including waste-solvent recovery from pharmaceutical, chemical, paint, resin, coating and other process industries. The technology may be configured as either a batch system or a continuous distillation system, depending on feed quantity, feed variability, number of required products, operating hours and product specifications.
Every specialty-solvent system is designed around the actual feed composition and target product specification. The required number of theoretical stages, reflux ratio, operating pressure, column diameter, reboiler duty and internals are determined specifically for the separation being performed. Heating may be provided by direct-fired heaters or reboiler systems using thermic fluid or steam, depending on the required process temperature and available utilities.
The first step is a detailed evaluation of the feed stream, covering component composition, ASTM or laboratory distillation data, gas-chromatography analysis, density, viscosity, water content, flash point, solids or suspended contaminants, boiling-range distribution, feed quantity and variability, and the required finished-product specifications. This information establishes the separation difficulty and determines the appropriate process configuration. For solvent-recovery applications, the analysis must identify both the valuable solvent components and the contaminants that must be rejected.
The feed may require conditioning before entering the main distillation system — which may include settling, filtration, water removal, light-end removal, preheating, separation of gross contaminants and buffer storage with feed equalisation. For waste-solvent streams from pharmaceutical and chemical industries, pretreatment is particularly important where the feed contains water, dissolved solids, resins, pigments, reaction by-products or high-boiling contaminants. Proper feed preparation reduces fouling, improves fractionation stability and lowers the load on downstream equipment.
In a batch system, a defined quantity of feed is charged into the distillation vessel and heated progressively; the different boiling-range fractions — light solvent, white-spirit cuts, kerosene-range and diesel-range products, spindle-oil-range fractions, heavy solvents and final residue — are recovered sequentially into separate receivers. For heavier fractions, vacuum can be applied after the atmospheric cuts have been recovered, allowing high-boiling material to be distilled at lower temperatures. In continuous plants, feed is introduced continuously into the fractionation system, which may incorporate single or multiple atmospheric columns, atmospheric followed by vacuum fractionation, dedicated vacuum columns, side draws, side strippers and multiple condensers and product receivers.
The vapours leaving the column are condensed and directed to dedicated receivers. Products may include light naphtha, specialty naphtha, white spirit, multiple white-spirit grades, kerosene-range and diesel-range fractions, spindle-oil-range fractions, aromatic solvent cuts, recovered process solvents and heavy hydrocarbon fractions. Cut points are controlled by column temperature profile, operating pressure, reflux ratio, product density, distillation characteristics and laboratory product analysis. Off-specification material can be recycled or reprocessed until the desired specification is achieved.
Vacuum operation is used where the desired product has a sufficiently high boiling point that atmospheric operation would create excessive process temperatures. Reducing the operating pressure lowers the boiling temperature and helps minimise thermal degradation, product discolouration, cracking, coke formation and unwanted chemical reactions — particularly important when recovering heavy white-spirit fractions, spindle-oil-range products, heavy specialty solvents and valuable fractions from waste-solvent residues. Depending on the required vacuum level and separation duty, the column may use trays or structured packing.
Balaji Consultants also designs solvent-recovery systems for contaminated and mixed solvent streams from pharmaceutical manufacturing, fine chemicals, paints and coatings, resins, adhesives, printing and packaging, specialty chemicals, agrochemicals, industrial cleaning and general chemical processing. The objective is to recover a reusable solvent fraction while concentrating the unwanted contaminants — water, light impurities, heavy organic contaminants, reaction by-products, dissolved solids, resins, pigments and high-boiling residue — into a smaller residue stream. Depending on the feed, the recovery system may use batch distillation, continuous distillation, vacuum distillation, fractionation, partial condensation, Wiped Film Evaporation or multiple-column separation.
A batch of feed is heated and individual fractions are recovered sequentially into separate receivers. The system may begin under atmospheric conditions and subsequently operate under vacuum for the heavier fractions. Suitable for variable feedstocks, multiple products, smaller and medium capacities, campaign production and waste-solvent recovery.
Feed is continuously processed through one fractionation column, producing an overhead and bottoms stream or one or more side draws. Suitable where feed composition is reasonably stable, separation duty is moderate and a limited number of products are required.
Two or more columns are used where several narrow-boiling products are required, with each column performing a defined separation duty to produce tighter product specifications than a single column could achieve. Suitable for multiple white-spirit grades, specialty naphtha, kerosene and diesel fractionation, high-purity solvent cuts and more demanding product specifications.
Lighter products are recovered under atmospheric conditions and the heavier fraction is subsequently processed under vacuum — using separate atmospheric and vacuum columns in continuous plants, or transitioning between atmospheric and vacuum operation in the same batch system. Suitable for wide-boiling solvent feeds, white-spirit production, diesel-to-solvent fractionation and spindle-oil-range recovery.
Contaminated process solvent is distilled to recover the reusable fraction while water, light contaminants and heavy residues are separated. The system is developed specifically around the composition of the waste solvent and the quality required for reuse, and may incorporate batch distillation, vacuum distillation, multiple columns, partial condensation, WFE and drying or polishing.
Yield estimates and product cut-point guarantees are only issued after receipt of a complete characterisation of the specific crude source and target product slate. Generic crude assumptions are not used as the basis for equipment sizing.
Commissioned projects where this technology is part of the installed plant.
Process selection depends on feedstock composition, required product quality, capacity, utilities, operating philosophy and project economics. Share your available feedstock data with our engineering team for an initial technical evaluation.
Submit Feedstock InformationConnect with our engineering team to review your feedstock, required capacity, and process objectives.