Sisitɛm de kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ Sistɛm kënë ye luɔ̈ɔ̈i në luɔɔi de kɔc ye kɔc ye kɔc ye kɔc ye kɔc ye kɔc ye kɔc ye kɔc ye kɔc ye kɔc ye kɔc ye kɔc ye kɔc ye kɔc ye kɔc ye kɔc ye kɔc ye kɔc ye kɔc ye kɔc

Process specific: buffer tank to condense oil by lifting pump to pressurize, into the heat exchanger to preheat, then into the stable tower, stable tata bottom temperature stable at around 120°C, so that the condensed oil contained gas fully distilled.

Condensate oil distilled at the bottom of the tower is cooled first through a heat exchanger, then into the air cooler, through the air cooler to control the temperature of condensate oil at 20 ℃ ~ 40 ℃, ensuring the stable after crude oil's temperature and saturated steam pressure to meet the output requirements, then into the buffer tank, finally through the exit lift pump will stabilize the condensate oil output pressure to 0.4-0.6MPa output.

Oil and gas distilled at the top of the tower is cooled by air cooler to enter the separation tank, gas is released from the top of the tank to the vacuum system or recycling system, light oil is released from the bottom of the tank, to return to the tower or directly recycled. Oil and gas distilled at the top of the tower is cooled by air cooler to enter the separation tank, gas is released from the top of the tank to the vacuum

Lɔ̈ɔ̈m ye kɔnɔ̈ɔ̈th ye kɔnɔ̈ɔ̈th ye kɔnɔ̈ɔ̈th ye kɔnɔ̈ɔ̈th ye kɔnɔ̈ɔ̈th ye kɔnɔ̈ɔ̈th ye kɔnɔ̈ɔ̈th ye kɔnɔ̈ɔ̈th ye kɔnɔ̈ɔ̈th ye kɔnɔ̈ɔ̈th ye kɔnɔ̈ɔ̈th ye kɔnɔ̈ɔ̈th ye kɔnɔ̈ɔ̈th ye kɔnɔ̈ɔ̈th