The present invention relates to the technical field of peroxide decomposition, and discloses a method for preparing phenol, which comprises the following steps: (1) mixing cumene hydroperoxide and liquid acid or solid acid with a solvent to form a homogeneous solution or uniformly dispersed system; (2) loading the homogeneous solution or uniformly dispersed system of cumene hydroperoxide with a homogeneous solution or uniformly dispersed system of acid into a preheating module and preheating in a micro-channel continuous flow mode, preliminarily mixing the preheated materials for reaction in a mixing module in a micro-channel continuous flow mode, and then further mixing the materials for reaction in a series of mixing and reaction module groups in a micro-channel continuous flow mode, to obtain phenol. The method provided in the present invention is easy, simple and safe to operate, can implement continuous production of phenol product at a high yield ratio; in addition, since the reaction in the present invention is a cracking reaction, which releases heat strongly, the safety factor of the process is significantly improved owing to the strong heat release characteristic in conjunction with the unique heat transfer property of the micro-channels. With the method provided in the present invention, the yield of the product is higher than 99%.

The present invention relates to the technical field of peroxide decomposition, and discloses a method for preparing phenol, which comprises the following steps: (1) mixing cumene hydroperoxide and liquid acid or solid acid with a solvent to form a homogeneous solution or uniformly dispersed system; (2) loading the homogeneous solution or uniformly dispersed system of cumene hydroperoxide with a homogeneous solution or uniformly dispersed system of acid into a preheating module and preheating in a micro-channel continuous flow mode, preliminarily mixing the preheated materials for reaction in a mixing module in a micro-channel continuous flow mode, and then further mixing the materials for reaction in a series of mixing and reaction module groups in a micro-channel continuous flow mode, to obtain phenol. The method provided in the present invention is easy, simple and safe to operate, can implement continuous production of phenol product at a high yield ratio; in addition, since the reaction in the present invention is a cracking reaction, which releases heat strongly, the safety factor of the process is significantly improved owing to the strong heat release characteristic in conjunction with the unique heat transfer property of the micro-channels. With the method provided in the present invention, the yield of the product is higher than 99%.

The disclosure concerns methods comprising forming a phenol and acetone mixture from decomposition of a cumene hydroperoxide or a phenol, acetone, and AMS from the decomposition of a mixture containing dicumyl peroxide in a system comprising one or more reactors where at least a portion of an inner surface of the one or more reactors has a polymer coating and wherein the coating inhibits build-up of a fouling precipitate on the coated inner surface of the one or more reactors as compared to such build-up in the absence of the coating.

The present invention provides a micro-reactor (1) adapted to host chemical reactions having at least one microfluidic layer, said micro-reactor (1) comprising a fluid inlet (2) and a fluid outlet (3); a plurality of micro-reaction chambers (10) arranged in rows (7) and columns (6), each micro-reaction chamber comprising a chamber inlet (10a) and a chamber outlet (10b); a plurality of supply channels (4) for supplying fluid to from said fluid inlet (2) to said micro-reaction chambers (10) and further arranged for draining said micro-reaction chambers (10) to said fluid outlet (3), said supply channels (10) extending in a first direction (D1) along the columns (6) of micro-reaction chambers (10) and arranged such that there is one supply channel (4) between adjacent columns (6). The micro-reaction chambers (10) in the columns (6) are arranged such that the chamber inlets (10a) of a column are in fluid contact with the same supply channel (4) and the chamber outlets (10b) are in fluid contact with the supply channel (4) adjacent to the supply channel (4) arranged in fluidic contact with the chamber inlets (10a). Further, the plurality of supply channels (4) comprises a first end supply channel (4a) arranged for supplying fluid to a first end column (6a) of the micro-reaction chambers (10) and a second end supply channel (4b) arranged for draining fluid from the second, opposite, end column (6b) of said micro-reaction chambers (10); and wherein the micro-reactor (1) further comprises at least one reagent inlet (8) in fluid contact with the first end supply channel 4a and a reagent outlet (9) in fluid contact with the second end supply channel such that reagents introduced to the at least one reagent inlet (8) fill the plurality of micro-reaction chambers (10) in a second direction (D2) along the rows (7) of micro-reaction chambers (10) to the reagent outlet (9).

An apparatus for depositing nanocomposite material comprising a nanocomposite-ink factory and inkjet printer. The nanocomposite-ink factory producing nanocomposite-ink and the inkjet printer receiving the nanocomposite-ink. The inkjet printer having a printhead and a positioning mechanism. The printhead having one or more nozzles to dispense nanocomposite-ink droplets.