Cost efficient integration of hydrothermal liquefaction and wet oxidation wastewater treatment
Aqueous wastewater from hydrothermal liquefaction (HTL) systems is typically high in chemical oxygen demand (COD), which renders classic aerobic wastewater treatment to be prohibitively expensive. HTL wastewater can be processed using thermochemical wet oxidation in a manner that is not only cost efficient but also contributes more heat than is required for the energetically demanding HTL process. Provided are methods and devices for integrated hydrothermal liquefaction of biomass and treatment of resulting wastewater.
1. A hydrothermal liquefaction (HTL) system for production of bio-crude oil comprising:
an inlet unit for aqueous slurries of biomass;
a high pressure pump providing an outlet pressure of at least 100 bar in fluid communication with the inlet unit;
a continuous hydrothermal liquefaction (HTL) reactor comprising one or more separate HTL reactors, adapted to produce bio-crude oil;
a heat exchanger, adapted to being heated directly or indirectly via a product stream of a hydrothermal liquefaction (HTL) reactor or a wet oxidation reactor;
a continuous wet oxidation reactor comprising one or more separate wet oxidation reactors adapted to process aqueous wastewater generated by the continuous hydrothermal liquefaction (HTL) reactor; and
a hydrothermal liquefaction (HTL) process heater that is adapted to receive thermal energy from a wet oxidation reactor,
wherein the one or more separate hydrothermal liquefaction (HTL) reactors and the one or more separate wet oxidation reactors are arranged co- or counter-current in direct thermal contact on opposite sides of a tubular heat exchanger optionally within a multitubular system.
2. The hydrothermal liquefaction (HTL) system according to claim 1 , wherein the hydrothermal liquefaction (HTL) system further comprises a separator that separates a product stream from the continuous hydrothermal liquefaction (HTL) reactor into a gaseous product phase, a product oil phase and an aqueous product phase.
3. The hydrothermal liquefaction (HTL) system of claim 2 , wherein the separator comprises a three-phase separator.
4. The hydrothermal liquefaction (HTL) system of claim 1 , further comprising a wet oxidation gas flow control system adapted to control a flow of air or an oxygen rich gas stream transported to the continuous wet oxidation reactor so as to ensure a desired conversion rate or heat production and to avoid overheating of the continuous wet oxidation reactor.
5. The hydrothermal liquefaction (HTL) system of claim 1 , wherein both the one or more separate wet oxidation and the one or more separate hydrothermal liquefaction (HTL) reactors have similar dimensions.
6. A method of hydrothermal liquefaction (HTL) comprising the steps of:
providing an HTL feed stream of biomass mixed with HTL product aqueous phase, and
conducting continuous HTL conversion of the HTL feed stream in such manner that some portion of the HTL product aqueous phase is recirculated to the HTL feed stream and some portion of the HTL product aqueous phase is subject to wet oxidation process, wherein heat produced by the wet oxidation process is used to heat the HTL feed stream,
wherein the HTL conversion and the wet oxidation process are conducted in separate reactors arranged co- or counter-current in direct thermal contact on opposite sides of a tubular heat exchanger.
7. The method of claim 6 , wherein a flow of air or oxygen rich gas stream supplied to the wet oxidation process is controlled so as to ensure a desired conversion rate or heat production and to avoid overheting of the wet oxidation reactor.