The diluted emulsions are subjected to flashing at emulsion-breaking conditions after which the oil is recovered from the various streams created in the flashing steps.

The flashed vapors are transferred to the direct contact condenser.

After a rough flash, a more pure diesel can be produced.

At least a portion of the first flash stage bottoms product (30.1) is heated to a temperature in excess of 150°C to form a heated first flash stage bottoms product (30.2).

Exothermic heat generated in the first compartment of the autoclave is abstracted in the flashing process.

An oil feedstock (6) is upgraded by hydrocracking and flashing and/or distilling.

An anti-flash wick (18) support (16) for candles having a candle floor.

for electricity generation using dry steam or high enthalpy brine after flashing

for electricity generation using dry steam or high enthalpy brine after flashing

for electricity generation using dry steam or high enthalpy brine after flashing

for electricity generation using dry steam or high enthalpy brine after flashing

Steam flashes off from seawater downstream of heat exchange (32B) within a flash tank (33).

From the pre-flasher/post reaction vessel the acetic acid enriched mixture is (d) withdrawn and fed to a flash vessel.

A flash boiler (10, 100) or steam generator includes a shell (12) defining a combustion chamber (105).

The salt and/or particulate matter are removed in the liquid bottoms stream from the flash separation vessel.