There is provided a gas solution supply apparatus capable of preventing bubbles from being generated in use at a point-of-use even if gas solution to be provided to a point-of-use has a high concentration. The gas solution supply apparatus 1 includes: a gas dissolving unit 4 that dissolves a source gas in a source liquid to produce a first gas solution; a first gas-liquid separator 10 that stores the first gas solution produced and produces a second gas solution through gas-liquid separation of the first gas solution; a pressure reducer 17 that depressurizes the second gas solution produced in the first gas-liquid separator 10; and a second gas-liquid separator 12 that stores the depressurized second gas solution and produces a third gas solution through gas-liquid separation of the second gas solution. The third gas solution is supplied to a point-of-use.

A method for manufacturing beverage or other liquid containing bubbles uses a system for manufacturing bubble-containing liquid that includes: a bubble generating unit that generates fine bubbles in a liquid; a bubble collapsing unit that is connected to the bubble generating unit to collapse the fine bubbles contained in the bubble-containing liquid supplied from the bubble generating unit by making the bubble-containing liquid pass through the bubble collapsing unit and irradiating the bubble-containing liquid with ultrasonic wave; and a storage unit that is connected to the bubble collapsing unit to store the bubble-containing liquid supplied from the bubble collapsing unit. The method includes: a bubble generating step of generating the fine bubbles in the liquid by the bubble generating unit; a bubble collapsing step of generating superfine bubbles by forming an ultrasonic field by the bubble collapsing unit to collapse the fine bubbles contained in the liquid; and a storage step of storing the bubble-containing liquid containing the superfine bubbles by the storage unit. Consequently, beverage or other liquid containing the superfine bubbles can be manufactured.

The present invention specifically relates to equipment and a method for preparing an aerogel thermal insulation mortar for a high-temperature kiln thereof. The equipment comprises a top box, a support frame platform, a processing mechanism, an agitation mechanism, a receiving mechanism and a docking mechanism, wherein the top box is provided with a partition frame capable of dividing an inner space thereof into a first material discharge cavity, a second material discharge cavity, a third material discharge cavity and a fourth material discharge cavity respectively; the receiving mechanism is mounted on an inner top of the support frame platform and docked with the top box; the docking mechanism is mounted on the receiving mechanism; an inner bottom of the support frame platform is provided with a collection box; one side of the top box is provided with a door panel.

According to one embodiment, the liquid crystal material processing device includes a syringe containing contents composed of a liquid crystal material and the like, having a distal end portion constituting a first discharge pipe, an agitation mechanism agitating the contents of the syringe, a vacuum chamber having a second discharge pipe penetrating the bottom to connect to the first discharge pipe of the syringe. The agitation mechanism agitates the liquid crystal material and the pure water in the syringe, and purifies the liquid crystal material by causing water-soluble impurities to transfer to the pure water. The agitation mechanism agitates the liquid crystal material remaining in the syringe after the water layer has been discharged. The evacuation mechanism evacuates the vacuum chamber and causes the liquid crystal material to be degassed while the remaining liquid crystal material is agitated.

A gas/liquid dissolution device includes: a dissolution case; an introduction port outside a side surface of the dissolution case; a gas/liquid separation inducing means in the dissolution case, the gas/liquid separation inducing means inducing the dissolution water and an insoluble gas introduced into the dissolution case; and a discharge port outside an end portion of the dissolution case. The introduction port includes: an introduction tube connected to the dissolution case; an insertion tube inserted into the introduction tube; and an intake tube connected to the insertion tube. The discharge port has a structure where a discharge flow path communicating with an interior of the dissolution case is formed therein. The gas/liquid separation inducing means includes: a first gas/liquid separation guide tube, one side end portion of the first gas/liquid separation guide tube contacting an end surface of a discharge portion of the dissolution case and an other side end portion of the first gas/liquid separation guide tube spaced apart from an opposite end surface of the dissolution case; and a second gas/liquid separation guide tube, one side end portion of the second gas/liquid separation guide tube spaced apart from the end surface of the discharge portion of the dissolution case and an other side end portion of the second gas/liquid separation guide tube contacting the opposite end surface of the dissolution case. A guide channel is formed on each of the first gas/liquid separation guide tube and the second gas/liquid separation guide tube, and the insoluble gas is separated from the dissolution water to flow by the guide channel. The different kinds of the soluble gases are easily introduced through the intake tube. As a result, the dissolution ability of the gas is improved and the separation ability of the insoluble gas is also improved. Therefore, the dissolution water including the microbubble is effectively generated, and a phenomenon that the flow state of the dissolution water is deteriorated by the insoluble gas is prevented.

The present invention provides a desulfurization agent mixing system for fuel oil used in harbors, the system including: a fuel oil tank for storing fuel oil; a desulfurization agent tank for storing a desulfurization agent; a line mixer receiving and mixing the fuel oil and the desulfurization agent from the fuel oil tank and the desulfurization agent tank; a droplet atomization unit for forming droplets of a mixture of the fuel oil and the desulfurization agent, the mixture being generated by the line mixer; a magnetization unit for magnetizing the mixture in which the droplets are contained; a vortex reaction unit for turning the mixture of the fuel oil and the desulfurization agent, which is magnetized by the magnetization unit; a gas separation unit configured to separate gas contained in the fuel oil and the desulfurization agent mixture in the vortex reaction unit; a collision emulsion unit configured to cause the mixture of the fuel oil and the desulfurization agent from which the gas is separated by the gas separation unit to collide against a collision target; and an emulsion tank for storing the mixture of the fuel oil and the desulfurization agent, which is collided by the collision emulsion unit.

Proposed is a method of emulsifying fuel oil and a desulfurization agent. The method includes (a) a step of adding a desulfurization agent to fuel oil for line mixing thereof, (b) a step of generating droplets in the resulting mixture of step (a), (c) a step of causing the resulting mixture of step (b) to pass through a magnetic field so that the mixture can be magnetized, (d) a step of subjecting the resulting mixture of step (c) to vortex mixing, and (e) a step of causing collision of the resulting mixture of step (d). The method uses fuel oil as a continuous phase and a water-based desulfurization agent as a disperse phase and emulsifies the desulfurization agent in the fuel oil through water-in-oil (W/o) emulsification so that the desulfurization agent can be stably dispersed in the fuel oil. Since the fuel oil and the desulfurization agent are burned together during combustion, sulfur oxides that may occur during the combustion are removed, whereby sulfur oxide emissions are reduced.

An ultrafine bubble water manufacturing device includes a whirlpool pump, an ejector, a cascade pump, a branch portion on the downstream side of the cascade pump, a return path which communicates from the branch portion between the ejector and the cascade pump, a flow rate adjusting valve and a first ultrafine bubble manufacturing unit interposed in the return path, an emission path which communicates with the branch portion, a second ultrafine bubble manufacturing unit interposed in the emission path and a control device. The control device controls an air amount adjusting valve, the whirlpool pump, the cascade pump and the flow rate adjusting valve based on the measurement values of a concentration meter for the emission path and first and second pressure gauges and on the downstream and upstream sides of the cascade pump.

Provided is a supply-liquid producing apparatus capable of producing a supply liquid by an amount needed at a use point.

A supply-liquid producing apparatus includes a mixer that mixes water and ozone gas to produce ozone water; a booster pump that increases the pressure of the water supplied to the mixer; a gas-liquid separation tank that separates the ozone water produced by the mixer into ozone water to be supplied to a use point and exhaust gas to be discharged from an exhaust port; a flowmeter that measures the flow rate of the ozone water supplied from the gas-liquid separation tank to the use point; a flow control unit that adjusts the flow rate of the water supplied to the mixer by controlling the booster pump in response to the flow rate of the ozone water measured by the flowmeter; and an exhaust pressure control unit that controls the exhaust pressure to keep constant the water level in the gas-liquid separation tank.

A gas solution production apparatus 1 includes a gas dissolving unit 5 that dissolves the gas of the second raw material into the liquid of the first raw material to generate a gas solution with a predetermined concentration, and a gas-liquid separation unit 8 that subjects the gas solution to gas-liquid separation into a supply liquid and an exhaust gas. The unit 5 includes a first nozzle 9 that atomizes the liquid of the first raw material, a mist mixing section 11 that mixes the liquid of the first raw material atomized by the nozzle 9 and the gas of the second raw material to generate a gas solution with a higher concentration than a predetermined concentration, and a liquid mixing section 12 that mixes the gas solution with the high concentration and the liquid of the first raw material to generate the gas solution with the predetermined concentration.