Gas flares configured to mix and burn multiple gasses are disclosed. According to one aspect, a gas flare head includes a first and second conduit one inside the other to form an interior region between the conduits. The interior region between the conduits is partitioned into multiple channels by a dividing structure. Each channel is configured to route a gas from a source to a mixing chamber where the gasses are mixed and burned.

One object is to generate, without the need for a motive power source and a high level of machining accuracy, micro-bubbles containing a large amount of fine air bubbles. Another object is to provide a micro-bubble generator that switches between micro-bubble water, which contains micro-bubbles, and foamed water containing a large amount of air and having a tender texture. The micro-bubble generator includes: a water passage that includes a smaller diameter portion and a larger diameter portion disposed on the downstream side of the smaller diameter portion; an air inlet disposed in the larger diameter portion and an elastic body disposed in the air inlet and configured to isolate the water passage from external air. The elastic body is compressible by negative pressure generated in the water passage, causing the external air to be sucked into the water passage through the air inlet and over the compressed elastic body.

Methods, systems, and devices, are developed for in-situ placement of a concrete mix that can have the thixotropy to hold vertical dimension without containment, while maintaining pliability to be pumped into place and manipulated to a desired shape, and can be combined with concrete set accelerators, allowing subsequent layers of this concrete mix to be continuously stacked in place to build tall walls and such without the use of forms. Concrete without these special properties is pumped toward the point of placement where it is modified by injecting and mixing, into that line of pumped concrete, an admixture containing thixotropes, thickeners and/or set accelerators or other modifiers to provide these properties and other improvements. This method allows conventional plant batching with commonly available constituent materials for batching an economical concrete that is delivered to a jobsite and then is pumped most of the way to a point of placement.

One aspect relates to a device for mixing two liquids including a tube having an open end, a main line connected to the tube in a liquid-permeable manner, a rubber-elastic body delimiting a line wall of the main line, at least one secondary line in the rubber-elastic body, wherein the at least one secondary line extends from at least one secondary opening up to the main line and opens via at least one mouth into the main line, a main connection for introducing a first liquid into the main line, at least one feed line for introducing a second liquid into the at least one secondary line, which is connected to the at least one secondary opening in a liquid-permeable manner. The at least one secondary line is closed in the rubber-elastic body without the action of a force and is hydraulically openable by a pressure being exerted on a second liquid fed to the at least one secondary line by an elastic deformation of the at least one rubber-elastic body. The open at least one secondary line closes without a pressure being exerted on the supplied second liquid by the restoring force of the elastically deformed rubber-elastic body.

A device for mixing a first fluid and a second fluid may include a primary conduit that may extend along a longitudinal axis of the primary conduit between a primary inlet port and a primary outlet port. The primary conduit may have a constant primary inner diameter for an entire length of the primary conduit. The primary inlet port may be connected to a pressurized source of the first fluid. The device may further include at least one secondary conduit that may extend parallel with the primary conduit. The secondary conduit may include a secondary inlet port and a secondary outlet port. The secondary conduit may have a constant secondary inner diameter. The secondary inner diameter may be smaller than the primary inner diameter. The primary conduit may encompass at least a portion of the secondary conduit. The secondary outlet portion may be disposed within the primary conduit. The secondary inlet port may be connected in fluid communication with a source of the second fluid.

A process for preparing an isocyanate product includes providing a phosgene inlet stream and an amine in solvent inlet stream to a phosgenation mixer, the amine in-solvent inlet stream including one or more amines and one or more inert solvents, and during steady state operation compensating for a fouling pressure drop increase by decreasing a pressure drop in the phosgenation mixer over a time period divided into at least a first period of time T1 and a second period of time T2 that is subsequent to the first period of time T1. During the second period of time T2 an amine concentration of the one or more amines in the amine-in-solvent stream is higher than during the first period of time T1, and during the second period of time T2 a phosgene-to-amine ratio value in the phosgenation mixer is higher than during the first period of time T1.

A bubble generating device is disclosed which includes: a bubble generator including a tubular body, a liquid introduction port, a gas introduction port, and a discharge port; and a gas supply unit including a gas supply port, a pressurized gas being supplied to the bubble generator through the gas supply port, wherein the flow passage of the bubble generator extends substantially along a same axis, a plurality of reduced diameter portions each having an inner diameter reduced are provided along a direction along which the liquid flows, and gas-liquid mixing portions are provided downstream of the respective reduced diameter portions in a contiguous manner, each of the gas-liquid mixing portions having an inner diameter larger than a minimum inner diameter of each of the plurality of reduced diameter portions, and the gas introduction port of the bubble generator is formed of a plurality of through holes.

A process for separation of a slurry by radially injecting a stream of a nanogas solution at a shear-focus volume within a pipe; passing an aqueous slurry through the pipe along a direction of flow and through the shear-focus volume; and shearing and/or admixing the slurry with the nanogas solution within the shear-focus volume.

The invention relates to the food industry. A method of saturating a beverage with CO2 comprises supplying the liquid and the gas under pressure, increasing the mass transfer surface, intensively mixing the components in a chamber, and subsequently feeding them into a storage tank. The mass transfer surface is increased abruptly prior to mixing by converting the liquid to a moist saturated vapor state, and the vapor-gas mixture is condensed before feeding into the storage tank. Also described is a device for saturating a beverage with CO2, which device is in the form of a water-air ejector.

Liquid treatment apparatus comprises at least two chambers being first and second chambers through which a fluid can flow. The two chambers are separated by at least one choke nozzle which has an entrance in the first chamber and an exit in the second chamber. The choke nozzle comprises a converging section at its entrance, a throat section, a backward-facing step immediately after the throat section, and an exit section at its exit wherein the exit section diverges from the step. Similarly constructed mixing nozzles may be included in the apparatus. The apparatus is especially useful in processes requiring a gas to be entrained in a fluid so that the gas is in the form of very small bubbles that do not tend to coalesce and flash off such as in the dissolution of gold and other precious metals from ore and in the removal of arsenic from an ore.