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38results about How to "Optimize energy usage" patented technology

Multi-purpose, multi-oxy-fuel, power burner/injector/oxygen lance device

A multi-purpose, multi-oxy-fuel High Temperature Power Burner/Injector/Oxygen Lance, Mechanical System Apparatus Device, for steelmaking from recycled scrap and/or virgin ferrous charge, which can be employed in multi-oxy-fuel (natural gas; pulverized carbonaceous matter; heavy oil), especially by Oxygen Combusted mixture of Natural Gas/Pulverized Carbonaceous Matter in High Temperature Power Burner Mode, for efficient and rapid melting of solid ferrous charge (cold or preheated) in a special steelmaking Metallurgical Furnace or Open Hearth Furnace, Tandem Furnace, BOF, EAF, as its augmenting or only source of thermal energy; more than one Device in Oxygen-Natural Gas/Pulverized Carbonaceous Matter Power Burner Mode, can be employed as the only source of thermal energy in a modified, originally Electric Arc Furnace, as total replacement of Graphite Electrodes and Electric Arc System, the replacement being noticeably more primary energy efficient than the thermal energy provided by Graphite Electrode/Arc System; it also can be employed in an Solid Particles Injector Mode, for injecting of adequately granulated carbonaceous materials or lime into the molten steel for its carburizing or for foamy slag control; further it can be employed in a natural gas shrouded, pulsating oxygen stream, for vertically to the charge oriented soft blow supersonic Oxygen Injection Lance Mode, for decarburization of the molten metal contained in the hearth of the metallurgical furnace and foamy slag control; in one of the embodiments-generally arcuate-pivotally mounted, liquid media cooled composite body, is pivoted into and out of a furnace vessel through a small opening in the shell wall for auto-regulated constant optimal positioning of the Composite Body Tip against solid or molten charge, in each and all multi-purpose modes; furthermore, when inserted into the furnace vessel, the arcuate composite body can be rotated about its longitudinal axis for directing the oxy-fuel high temperature flame towards unmolten charge in the furnace; in an other-generally linear-embodiment, the liquid cooled composite body is attached to the mast type carrier allowing vertical movement of the composite body which enters the furnace vessel through a small opening in the furnace roof; the bimetallic, liquid cooled special tip assembly of both-arcuate and linear embodiments-of the composite body includes easy replaceable, independent, multi-opening nozzles, mounted in a protective, retracted position inside of the liquid cooled special tip assembly.
Owner:EMPCO (CANADA) LTD

Chemical industry power multi-generation energy resource system and method for separating C02

The invention relates to the technical field of energy and environment and discloses a chemical engineering power multi-generation energy system and a method. Crude synthesis gas produced by carbon-rich raw material firstly enters a chemical engineering production flow, the synthesis gas can not carry out water-gas shift reaction to reduce the proportion of CO/H2, temperature reduction and purification are carried out for direct chemical engineering synthesis, the product of synthetic reaction is separated into unreacted gas and crude products by flash evaporation process, part of the unreacted gas circulates and carries out synthetic reaction again, while the other part of the unreacted gas carries out water-gas shift reaction and a CO2 separating unit for decarburization, the synthesis gas after decarburization is taken as fuel gas to be sent to a combined cycle power system for power generation. By adopting the invention, under the promise of ensuring that the active ingredient of new synthesis gas is fully transformed into chemical products, the energy utilization situation of the system can be improved; meanwhile, by adopting the way of separating CO2 after chemical engineering synthetic reaction, the energy consumption for separating CO2 can be lowered and the problem of the efficiency reduction of the energy system can be solved.
Owner:INST OF ENGINEERING THERMOPHYSICS - CHINESE ACAD OF SCI

Supply and return water temperature difference control system

The invention discloses a control system for temperature difference of supply and return water, relates to the technical field of air conditioners, and is used for solving the problem that energy oversupply is liable to occur, comfort requirements are hard to meet, or temperature difference of supply and return water is hard to effectively control due to the fact that supply water flow adjustment according to temperature difference is delayed. The control system for temperature difference of supply and return water comprises a temperature difference controller, a plurality of temperature control systems, a gain characteristic average computer and a gain controller, wherein the difference of supply water temperature and return water temperature is adopted as a measurement value of the temperature difference controller; the temperature control systems are used for controlling the room temperature; gain characteristic values of the temperature control systems are adopted as input of the gain characteristic average computer; gain characteristic average values are adopted as output of the gain characteristic average computer; output of the temperature difference controller is adopted as a set value of the gain controller; and output of the gain characteristic average computer is adopted as a measurement value of the gain controller. The control system for temperature difference of supply and return water is used for central air conditioning systems.
Owner:XINZHI ENERGY SYST CONTROL
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