The method of the polyurethane polyol comprises (1) dissolving 2,3-epoxybutane and an acid catalyst in an inert solvent to obtain a solution A; dissolving triethylene glycol in an inert solvent to obtain a solution B; and dissolving epoxy vegetable oil in an inert solvent to obtain a solution C; (2) respectively and simultaneously pumping the solutions A and B into a first micromixer for mixing; (3) pumping the solution C and an effluent of the first microreactor into a second micromixer for mixing while carrying out step (2); and (4) dissolving the vegetable oil polyol in an inert solvent to obtain a solution D; dissolving epoxypropane and an alkaline catalyst in an inert solvent to obtain a solution E; and pumping the solution D and the solution E into a tank reactor for reaction, thereby obtaining the polyurethane polyol.

Systems and methods for synthesizing chemical products, including active pharmaceutical ingredients, are provided. Certain of the systems and methods described herein are capable of manufacturing multiple chemical products without the need to fluidically connect or disconnect unit operations when switching from one making chemical product to making another chemical product.

Systems and methods for synthesizing chemical products, including active pharmaceutical ingredients, are provided. Certain of the systems and methods described herein are capable of manufacturing multiple chemical products without the need to fluidically connect or disconnect unit operations when switching from one making chemical product to making another chemical product.

The invention relates to a fluidic purifying device designed to clean a fluid of at least one pollutant, comprising a fluidic purification network, characterized in that the fluidic purification network comprises a plurality of microfluidic channels, each microfluidic channel being defined by one or more fluidttight walls, each microfluidic channel comprising at least one zone on the interior surface of said microfluidic channel that exhibits at least one autonomous purifying agent and each microfluidic channel exhibiting, in such a zone, a height less than 60 m in a direction normal to the main direction of flow of the fluid, the purifying agent or agents, and the sizing of said zones, being configured in such a way as to allow at least 10% of the pollutants to be captured and/or broken down by said zones, for at least one flow rate of the fluid that is to be purified.

The invention generally provides systems and methods for producing a chemical product. In certain embodiments, the invention provides systems that include a chemical product production unit. The chemical production unit includes a plurality of microfluidic modules configured to be fluidically coupled to each other in an arrangement that produces a chemical product from an input of a plurality of starting reagents that react with each other due to conditions within the plurality of microfluidic modules through which the starting reagents flow. The system also includes a droplet dispenser fluidically coupled to the chemical product production unit that forms and dispenses droplets of the chemical product.

A flow reactor has a module having a process fluid passage with an interior surface, a portion of the passage including a cross section along the portion having a cross-sectional shape, and a cross-sectional area with multiple minima along the passage. The cross-sectional shape varies continually along the portion and the interior surface of the portion includes either no pairs of opposing flat parallel sides or only pairs of opposing flat parallel sides which extend for a length of no more than 4 times a distance between said opposing flat parallel sides along the portion and the portion contains a plurality of obstacles distributed along the portion.

A flow reactor has a module (12) that comprises at least first (20), second (30), and third (40) parallel plates stacked temporarily or permanently together and defining a first thermal fluid layer (25) between the first (20) and second plates (30) and a process fluid layer (35) between the second (30) and third plates (40), the process fluid layer (35) comprising a process fluid passage (32) having two or more U-bends and three or more successive process fluid passage segments joined by respective U-bends, the first thermal fluid layer (25) comprising at least two open thermal fluid channels (26) in the second plate (30), the at least two open channels (26) positioned, when viewed in a plan view of the module (12), between respective adjacent process fluid passage segments.

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 invention generally provides systems and methods for producing a chemical product. In certain embodiments, the invention provides systems that include a chemical product production unit. The chemical production unit includes a plurality of microfluidic modules configured to be fluidically coupled to each other in an arrangement that produces a chemical product from an input of a plurality of starting reagents that react with each other due to conditions within the plurality of microfluidic modules through which the starting reagents flow. The system also includes a droplet dispenser fluidically coupled to the chemical product production unit that forms and dispenses droplets of the chemical product.

A method comprises enabling epoxy vegetable oil to react with a compound of a formula III in a second microstructured reactor to obtain the vegetable oil polyol. Compared with the existing technology, the present invention adopts a novel, environment-friendly ring-opening agent, the obtained polyol is novel in structure, high in hydroxyl value, even in distribution and low in viscosity, and can completely replace traditional petrochemical polyol to be applied to the preparation of polyurethane foam materials.