The amount of styrene in the resin, rubber and coating industry is not small, but its exhaust characteristics are easy to be ignored: the boiling point is moderate, there is obvious volatilization at room temperature, and it is easy to polymerize when heated or in contact with impurities. Styrene vapor will be brought out from the storage tank breathing, loading and exhausting of the polymerization kettle. If only simple collection and discharging are done, materials will be lost and the burden of back-end management will become heavier. The recovery of styrene waste gas should consider both recovery efficiency and polymerization risk.
The size and respiration of atmospheric storage tanks are intermittent emissions, and the concentration changes with temperature and liquid level. Exhaust in loading process is concentrated and large in short time. The exhaust of polymerization or reaction kettle may bring mist and a small amount of polymer particles. The common point of these types of gas sources is that the components are relatively single. The mainstream practice is to first condense and liquefy the recovery, and then further process the residual low concentration exhaust gas. Since the boiling point of styrene is not very low, conventional refrigerants can generally meet most of the liquefaction requirements. Whether to add cryogenic cooling depends on the exhaust gas concentration and the actual recovery target, and it is not necessary to add cryogenic cooling.
Exhaust comparison of different links
| Comparison item | Tank Size Breathing | Loading exhaust | Reaction kettle exhaust |
|---|---|---|---|
| Emission mode | Intermittent, liquid level changes with temperature | Concentrated, short-term flow | Fluctuation with lot |
| Component characteristics | Single, low concentration | High concentration with few droplets | Possible mist and particles |
| Configuration focus | Closed collection and anti-dilution | Load adaptation and condensate discharge | Front-end separation and anti-scaling |
The condensation outlet temperature and the amount of condensate are the two most direct observation indicators, and the simultaneous decline of both usually indicates that the heat exchange surface is fouled or the cooling capacity is reduced. The collection effect of the tank area is assisted by the odor and pressure state around the tank area, which is more intuitive than just looking at the instrument. The quality of the recovered condensate should be analyzed regularly. When the moisture content or added components change, the reuse method needs to be reconfirmed.
The air volume, concentration, temperature and daily emission period of each point are clearly sorted out, and the total load is estimated in combination with the volume of the storage tank and the loading frequency, so that the scale of the device is not easy to deviate too much.