An apparatus for preparing an oligomer including: a reactor supplied with a monomer stream and a solvent stream to perform an oligomerization reaction; a product discharge line provided on a lower portion of a side surface of the reactor; a washing liquid supply line connected to a first point of the product discharge line; and a washing liquid discharge line extending from a second point of the product discharge line, wherein the product discharge line includes a branch point at which the product discharge line is branched into two or more lines and a junction point at which the respective branched lines are joined, and the product discharge line includes pressure control devices provided in each of the two or more branched lines.

A process for manufacturing a dihydrogen-containing outlet gas, including injecting a hydrocarbon inlet gas into a reactor, an operation of cracking the inlet gas with a three-phase plasma torch, and then delivering the outlet gas. The manufacture is carried out from injecting the inlet gas into the reactor to delivering the outlet gas, without either the inlet gas or the outlet gas undergoing expansion.

The invention is directed to a process for the continuous preparation of a cycloadduct product from the reaction of a furanic with a dienophile, comprising heating a first liquid feed stream comprising the dienophile and a solvent in which the dienophile is dissolved; providing a second liquid feed stream comprising the furanic; leading the first liquid feed stream and the second liquid feed stream into a continuous reactor to produce a product solution stream comprising the cycloadduct product; and leading the product solution stream to an product isolation zone to produce an isolated cycloadduct product. A further aspect of the invention is an apparatus for carrying out this reaction.

A fluid supply device includes a condenser, a tank that stores the fluid, a pump that pressure-feeds the fluid toward a processing chamber, a main pipe connecting the tank and the pump and transferring the liquid stored in the tank to the pump using a weight of the liquid, and a discharging pipe that is connected to the main pipe at a lowest position of the main pipe at one end, is opened to the atmosphere at the other end, and vaporizes and discharges the liquid in the tank and the main pipe to the outside. The discharging pipe is formed so that, after the liquid in the tank and the main pipe is fully discharged, a liquid pool that separates a space on the atmosphere side and a space on the main pipe side of the discharging pipe is temporarily produced in the discharging pipe.

Disclosed herein is a synthetic method, apparatus, and system for the continuous-flow synthesis of 3,4-dinitropyrazole from pyrazole in a microfluidic environment. This synthetic strategy consist of three (3) synthetic steps, including (1) N-nitration of pyrazole, (2) thermal rearrangement into 3-nitropyrazole, and (3) 4-nitration of 3-nitropyrazole. The current technique produces 3,4-dinitropyrazole in yields up to 85% in particular embodiments, in comparison to 40-50% yields demonstrated by the current state of-the-art batch process for large scale synthesis from pyrazole.

The present invention relates to a microfluidic flow process for making monomers, monomers made by such processes, and methods of using such monomers. In such process, microfluidic reaction technology is used to synthesize cyanation reaction products orders of magnitude faster than is possible in batch and continuous syntheses. The aforementioned process does require strictly regulated, highly toxic cyanogen chloride. Thus the aforementioned process is more economically efficient and reduces the environmental impact of thermosetting resin monomer production, and produces thermosetting resin monomers in greater purity than obtained through typical processes.

Methods and systems for on-site, continuous generation of peracid chemistry, namely peroxycarboxylic acids and peroxycarboxylic acid forming compositions, are disclosed. In particular, an adjustable biocide formulator or generator system is designed for on-site generation of peroxycarboxylic acids and peroxycarboxylic acid forming compositions from sugar esters. Methods of using the in situ generated peroxycarboxylic acids and peroxycarboxylic acid forming compositions are also disclosed.

A gas reactor may include a reactor chamber having a first end, a second end, and a lateral surface that extends between the first end and the second end. The gas reactor may include a torch inlet positioned at the first end of the reactor chamber, and the torch inlet may be configured for input flow of a fuel in a first flow direction. The gas reactor may include a reactant inlet positioned at the second end of the reactor chamber and configured to cause a reactant to flow into the reactor chamber in a second flow direction. The fuel or the reactant may move through the reactor chamber in a vortex flow pattern. The gas reactor may include an outlet port positioned at the second end of the reactor chamber in which the outlet port is configured for output flow of a product from the reactor chamber.

A reactor and method for the conversion of hydrocarbon gases utilizes a reactor (12, 312, 412, 512, 612) having a unique feed assembly with an original vortex combustion chamber (40, 340, 436, 536, 636), a diverging conduit (48, 348, 448, 548, 648), and a cylindrical reactor chamber (40, 340, 436, 536, 636). This design creates a compact reaction zone and an inwardly swirling fluid flow pattern of the feed gases to form a swirling gas mixture that passes through a diverging conduit (48, 348, 448, 548, 648). The feed streams can be introduced into the reactor (12, 312, 412, 512, 612) at any angle (radial, axial, or something between, or a combination of the above forms) with swirling flow components. The feed streams comprise preheated steam and hydrocarbons for cracking. This system provides conditions suitable for efficient cracking of hydrocarbons, such as ethane, to form olefins.

A sulfuric acid generating system can include: a primary burn chamber; an exhaust pipe extending from the burn chamber at a first end to an opposite second end; a secondary burn chamber located between the first end and second end; and a primary venturi pump having a gas inlet coupled to an outlet at the second end of the exhaust pipe and having an aqueous media in let and having a fluid outlet. A method of producing sulfurous acid can include: providing sulfur to the primary burn chamber; burning a first portion of the sulfur in the primary burn chamber to form a first portion of sulfur dioxide; burning a second portion of the sulfur in the secondary burn chamber to form a second portion of sulfur dioxide; and mixing the first portion and second portion of sulfur dioxide with an aqueous composition so as to produce aqueous sulfurous acid.