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Solvent Vapor Recovery
Gas Treatment & Drying

Solvent Vapor Recovery

Solvent vapor recovery using twin tower pellet activated carbon adsorbers with steam or vacuum regeneration to capture and recover volatile organic solvents from process and printing vents.

The Challenge
Solvent vents from coating, printing, pharmaceutical synthesis, and chemical processing carry valuable VOCs that contribute to regulated emissions and to the operator solvent purchase cost. Recovery captures the economic value and meets the regulator emission limit simultaneously.
Quick Answer

Solvent vapor recovery uses twin tower pellet activated carbon adsorbers to capture volatile organic solvents (acetone, ethanol, methanol, MEK, toluene, dichloromethane) from process and printing vents. Steam or hot inert gas regeneration releases the captured solvent for condensation and return to the process. Recovery rates above 95 percent.

Solvent Vapor Recovery

Solvent Vents Have Economic and Regulatory Pressure

Solvent vents from industrial coating lines, flexible packaging printing, pharmaceutical synthesis reactors, chemical batch processing, and degreasing operations carry volatile organic solvents at concentrations from 100 to 10,000 mg/m³. The vented solvent is both an economic loss (the solvent has to be replaced from new purchase) and an environmental liability (the vent stream contributes to regulated VOC emissions). Recovery captures both.

Twin Tower Carbon Adsorber Configuration

The SorbiTech vapour recovery unit uses twin pellet activated carbon adsorbers running 180 degrees out of phase. The pellet form is preferred over granular: lower pressure drop in the vent gas service, higher hardness through the regeneration cycles, and longer service life. One tower is on adsorption capturing the solvent; the other is on regeneration releasing the captured solvent for condensation.

Solvent Vapor Recovery process equipment

Steam or Hot Gas Regeneration

Two regeneration methods are offered. Steam regeneration heats the bed to 100 to 120 °C and uses the steam to strip the captured solvent; the solvent vapour is condensed in a downstream chiller and the recovered solvent and water are decanted. This route suits water miscible solvents (ethanol, methanol, acetone). Hot inert gas regeneration uses heated nitrogen at 100 to 180 °C and avoids the water contamination of the recovered solvent; this route suits water sensitive solvents (THF) or halogenated solvents (dichloromethane).

Delivery and Economics

Delivered as a complete vapour recovery unit by SorbiTech or SorbiTech. Recovery rates above 95 percent are routine; the avoided solvent purchase cost typically pays for the unit within 18 to 36 months. Sector coverage is petrochemicals, pharmaceutical, and chemical processing.

Selection Guidance

Twin pellet activated carbon adsorbers with steam regeneration (for water miscible solvents) or hot inert gas regeneration (for halogenated or oxidation sensitive solvents). Condenser downstream for solvent recovery.

A Specified, Verified Solution

Define the duty

We capture your process conditions: flow, composition, pressure, temperature, and the target outlet specification.

Select media & configuration

Our engineers recommend the adsorbent grade and system type that meet the duty with margin.

Size & engineer

Bed sizing, vessel design, and cycle parameters are engineered to your case and documented for approval.

Commission & verify

We support loading, start up, and performance verification against the guarantee.

Specify a Solution for This Application

Provide your process conditions and our team will recommend the grade, configuration, and sizing.