A method and apparatus for producing a biocide from a hypochlorite oxidant and an ammonium salt are provided. The method includes monitoring a control parameter to optimize the ratio between the hypochlorite oxidant and the ammonium salt. The control parameter may be oxidation-reduction potential, conductivity, induction or oxygen saturation.

A cytometric mechanism includes: a flow path through which a cell suspension is made to flow; a liquid drive unit for sending the cell suspension which is in the flow path; and a computation unit for irradiating, with irradiation light from a light source, a cell suspension flowing through a flow cell, and for finding a cell survival rate in the cell suspension on the basis of a resulting forward scattered light intensity and transmittance and/or side scattered light intensity. The invention is provided with a calibration curve database for storing, in advance, respective calibration curves indicative of a relationship between viable cell concentration and forward scattered light intensity, a relationship between dead cell concentration and the transmittance, and a relationship between a cell survival rate and the side scattered light intensity.

Disclosed is a boron recovering device including: an aeration-type water-channel reactor including a water channel; at least one aeration unit disposed in the water channel and aerating a boron-containing solution by passing it through the water channel to deposit boron in the form of borax; and a precipitation bath precipitating the deposited borax in the boron-containing solution having passed through the aeration-type water-channel reactor and separating a filtrate by overflowing, a boron recovering device, a method of recovering boron, and a boron recovering system.

An apparatus and method for delivery of additives(s), e.g., catalyst, co-catalyst, scavengers, and/or other reaction- or product-modifying agents, to a reaction or mixing site, such as a reaction vessel, offers the capability for multi-additive delivery and customization of additive selection, flow and flow rate, and if desired, mixing thereof, without production train shutdowns. The invention includes at least two additive sources that are detachably connected, with conduit, to the reaction or mixing site, and a process control means, preferably automated, that is capable of initiating, terminating, and determining the rate of flow from the additive sources.

Fuel tank inerting systems for aircraft are provided. The systems include a fuel tank, a catalytic reactor arranged to receive a first reactant from a first reactant source and a second reactant from a second reactant source to generate an inert gas that is supplied to the fuel tank to fill an ullage space of the fuel tank, a heat exchanger arranged between the catalytic reactor and the fuel tank and configured to at least one of cool and condense an output from the catalytic reactor to separate out the inert gas, and a controller configured to perform a light-off operation of the catalytic reactor by controlling at least one light-off parameter and, after light-off occurs, adjusting the at least one light-off parameter to an operating level, wherein the at least one light-off parameter comprises a temperature of the catalytic reactor.

The invention concerns a method for controlling at least one gas bubble produced in a localised manner in a medium (3′) allowing the movement of said at least one gas bubble, characterised in that it comprises a step consisting of generating at least one ultrasound burst towards said at least one gas bubble, said at least one burst being emitted for a burst duration at least partially covering a duration during which said gas is effectively being produced.

A device for treating crude oil or heavy fuel oil with a method that can lower the pour point to at least 0° C. Crude oil or heavy fuel oil treated thusly maintains this property for at least one year. The device for lowering the pour point of crude oil or heavy fuel oil uses a specific ionization method. The method is conducted by passing a heated medium through the main ionization device which is grounded and which includes three parallelly connected segments whereby each segment includes a protective copper tube inside which a protective insulating shell is situated, inside which a copper housing is situated. In each copper housing there is one cylindrical-shaped external core in which an internal core is placed, and the external core and internal core are manufactured as two different alloys by composition. Also described is a process for casting the external core and internal core.

A flow reaction facility 10 includes a reaction section 23, a collecting section 26, a system controller 15, a first flow velocimeter to a third flow velocimeter 35a to 35c, a thermometer 35d, and a soft sensor 38. The first flow velocimeter to the third flow velocimeter 35a to 35c and the thermometer 35d detect reaction conditions in the reaction section 23, and output the detected reaction conditions as detection information. The soft sensor 38 applies the above detection information to a prediction function generated in advance using measurement data, and calculates a reaction result in the reaction section 23 as an arithmetic reaction result. The system controller 15 controls the reaction section 23 on the basis of the arithmetic reaction result.

A control system of a full-automatic cold plasma seed processor comprises a human-machine interaction interface, a PLC, a transport module, a vacuum degree module, an ionization module, and an energy supply module. The human-machine interaction interface is in a communications connection with the PLC by using a serial port. The energy supply module supplies a power source required by another module in a system. The PLC controls a transport rate of seeds by using the transport module, controls, by using the vacuum degree module, the vacuum degree of the system to reach a dynamic balance, and at last, controls the ionization time and the ionization power by using the ionization module, so as to adapt to processing requirements of different seeds and achieve an optimal processing effect. The control system can automatically process seeds of various grains, and brings short processing time and low cost.

A polyolefin manufacturing system and method including polymerizing olefin in a first reactor to form a polyolefin, transferring the polyolefin to a second reactor, polymerizing olefin in the second reactor, and discharging a product polyolefin from the second reactor. The system and method including operating the first reactor with a first reactor pressure relief system and the second reactor with a second reactor pressure relief system, both pressure relief systems to discharge to a flare system, and wherein a relief instrumented system (RIS) is configured to direct at least one process interlock that mitigates an excess reaction scenario as an overpressure relief scenario.