The invention provides a microalgae high-pressure continuous
tower-type liquefying process, which comprises the following steps of: pressurizing microalgae-containing suspension by using a high-pressure pump, making the
suspension flow through a
heat exchanger to exchange heat with liquefied liquid, heating to be between 180 and 250 DEG C according to a certain heating curve by using a
heating furnace, and preserving heat in a gelatinizing
tower for certain time to make
solid biomass changed into flowable
slurry; quickly heating gelatinized liquid to be between 270 and 350 DEG C at a certain heating rate by using a secondary
heating furnace, and adding into a liquefying
tower for hydrothermal liquefying to prepare a
liquid fuel; separating
coke slurry from a hydrothermal liquefying product by using a high-pressure
settling tank, discharging the
coke slurry from a
coke slurry outlet, and making liquefied gas liquid pass through the top of the high-pressure
settling tank, exchange heat with the microalgae suspension through the
heat exchanger and flow into a three-phase separator; separating the liquefied gas liquid into a water phase, an
oil phase and a
gas phase in the three-phase separator, circulating and discharging the water phase by connecting the water phase with the high-pressure pump and a discharging port from the lower part of the three-phase separator, concentrating to prepare a foliar
fertilizer, biological
gasoline or a
snow-melting agent and the like, discharging the
oil phase from a biological oil outlet in the middle of the three-phase separator to obtain a product, and discharging the
gas phase from a
tail gas outlet on the top of the three-phase separator to serve as a fuel; and discharging the
solid-phase coke slurry to serve as an
activated carbon material or a fuel.