Vacuum condensation package
Multiple units for olefin, alcohol, ester and surfactant process streams against chilled brine.
Purpose-designed vapor passages, large nozzles and independent condensate and non-condensable outlets support stable recovery of valuable solvents.
Contact Engineering
In vacuum and low-pressure processes, excessive pressure drop can reduce production capacity or destabilize the upstream process. The vapor nozzle, plate pattern, channel arrangement and non-condensable gas path must therefore be designed as one system.
| Vapor composition | Each condensable and non-condensable component, preferably mass or molar fraction. |
|---|---|
| Flow rate | Total vapor flow and expected range / turndown. |
| Pressure | Absolute operating pressure at exchanger inlet and allowable pressure drop. |
| Temperature | Inlet temperature and required condensate outlet temperature. |
| Cooling medium | Fluid, flow, inlet temperature and available outlet temperature. |
| Recovery target | Required condensation percentage or residual vapor specification. |
Multiple units for olefin, alcohol, ester and surfactant process streams against chilled brine.
Atmospheric condensation around 65°C, using 7/12°C chilled water.
Butanol, ethyl acetate and air, with deep-vacuum operation and glycol cooling.
Two-stage cooling using demineralized water and cooling water.
Yes, provided the complete vapor-side pressure profile is evaluated. Nozzle size, channel resistance, condensate drainage and non-condensable gas flow are critical.
Non-condensable gases can blanket heat-transfer surfaces and restrict condensate drainage. A dedicated outlet helps maintain effective area and stable operation.
Depending on temperature profile and layout, cooling-water and chilled-water duties can be arranged in separate units or a custom multi-section system.