809 results about "Regenerative system" patented technology

A method and a system capable of removing carbon dioxide directly from ambient air, and obtaining relatively pure CO₂. The method comprises the steps of generating usable and process heat from a primary production process;

• • applying the process heat from said primary process to water to co-generate substantially saturated steam, alternately repeatedly exposing a sorbent to removal and to capture and regeneration system phases, wherein said sorbent is alternately exposed to a flow of ambient air during said removal phase, thereby enabling said sorbent to sorb, and therefore remove, carbon dioxide from said ambient air, and to a flow of the co-generated steam during the regeneration and capture phase, after the sorbent has adsorbed the carbon dioxide, thereby enabling regeneration of such sorbent, and the resultant capture in relatively pure form of the adsorbed carbon dioxide. This process can also be carried out in more efficient form by admixing with the air a minor amount of a flue gas or an effluent gas containing a higher concentration of carbon dioxide than exists in the atmosphere, most preferably following a pre-treatment. The carbon dioxide can be stored for further use, or sequestered permanently following the capture: The adsorbent is exposed to air at substantially ambient conditions and the adsorbent is exposed to the co-generated steam at a temperature in the range of not greater than about 130° C. The system provides the sorbent substrate and equipment for carrying out the above method, and provides for obtaining purified carbon dioxide for further use in agriculture and chemical processes, including manufacturing hydrocarbon fuels, or for permanent sequestration, as needed.

A system for providing regenerative power for an aircraft to sustain flight includes multiple energy cells disposed within the aircraft, the energy cells being configured to supply power to a propulsion motor and electronics of the aircraft, a fan generator harnessing propeller blast created by an aircraft propeller and converting kinetic energy of the propeller blast into electrical energy, a charger receiving the electrical energy generated by the fan generator and using the electrical energy to recharge one or more of the energy cells, and a power transfer switch selectively connecting one of the energy cells to the propulsion motor and electronics of the aircraft, such that the energy cells are rotated one at a time to power the propulsion motor and electronics. During recharging, the one or more of the energy cells are disconnected by the power transfer switch.

A nebulizer assembly for use in a fabrics revitalizing system having a fabric treatment chamber comprises a fluid reservoir configured to contain a fluid; an air flow channel in fluid communication with the fluid reservoir; a mist generator configured to generate a mist in the fluid reservoir; and a fan in fluid communication with the air flow channel to draw air through the air flow channel and transport the mist to the interior of the fabric treatment chamber. The nebulizer assembly can include a transitional assembly that communicates the nebulizer assembly with the fabric treatment chamber.

One aspect of the invention relates to a device for storing ammonia for use in SCR on board a vehicle. The device comprises an adsorption bed with a high capacity for storing ammonia. The device can be designed to hold a long-lasting charge of ammonia comparable to a urea tank, but will not release substantial amounts of ammonia into the environment even if the device is accidentally ruptured. In one embodiment, the devices are charged at stationary locations. In another embodiment, the devices are charged by vehicle-mounted ammonia synthesis plants. The device facilitate the use of small ammonia synthesis plants that operate at low pressures and give low conversions. Preferably, the devices are operated through temperature swing adsorption.

The embodiment of the invention discloses a building refuse treatment regeneration system, including a classification stacking, sorting processing system, a classification processing system and a plurality of storage bins, wherein, the classification processing system includes at least two parallel crushing screening process production lines and water circulating systems, each crushing screening process production line includes a feeder, crusher, as well as a screening machine connected in series in sequence, and a plurality of outlets of the screening machine are respectively connected to the plurality of storage bins through conveyor belts. By adoption of the building refuse treatment regeneration system of the embodiment of the invention, bricks, tiles, dust and sand and concrete blocks and the like in the building refuse can be divided into at least two production lines for parallel processing, which greatly enhancing the production efficiency and the purity of recycled aggregates, so that the recycled aggregates can be applied to a variety of uses, reproduced into a variety of high-quality recycled products, reducing the waste of resources and minimizing pollution that will be probably caused to the environment.

A method for revitalizing a fabric load with a revitalization system comprises selecting a revitalization program from a plurality of programs and operating the revitalization system in accordance with the selected revitalization program. The programs can include at least one of a fluid insertion step; a fabric relative motion step; a fluid extraction step; a fabric refreshing step; a fabric reshaping step; a light cleaning step; a water extraction operation, a relative motion operation; a fabric air flow operation; a cooling operation; a fluid insertion operation; and a fabric fluid absorption operation.

The invention relates to an on-line monitoring method for a heat rate of a steam turbine on the basis of a soft measurement technology. According to the method, an established expert performance knowledge base and a performance prediction model of a steam turbine regenerative system are used for calibrating data collected by measure point sensors on the operation site of the steam turbine regenerative system, and parameter data not collected on the operation site of the steam turbine regenerative system are predicted, so main steam flow can be calculated by utilizing the output power of the steam turbine, the on-line monitoring of the heat rate of the steam turbine regenerative system can be completed, and therefore accurate and reliable on-line monitoring results of the heat rate of a generator set can be obtained. The on-line monitoring method for the heat rate of the steam turbine on the basis of the soft measurement technology omits traditional condensed water flow measurement, a soft measurement method of the output power of the steam turbine is adopted to achieve on-line monitoring of the heat rate, and meanwhile the functions of calibration and prediction on field measured data are achieved.

A method and apparatus to improve regeneration efficiency when regenerating the energy of discharge fluid from a fluid pressure actuator as electrical energy. In a flow rate control line 15, which finctions as a discharge flow path for oil discharged from a head side oil chamber 1c of a hydraulic cylinder 1, is provided a displacement variable regenerating hydraulic motor 20, where controlling the displacement of the regenerating hydraulic motor 20 allows the flow rate of discharge oil from the hydraulic cylinder head side oil chamber 1c to be controlled. A generator 21, which generates electric power due to the rotation of the regenerating hydraulic motor 20, is further provided.

The invention relates to a method for flexibly adjusting catalytic cracking reaction-regeneration system heat balance. A conventional regenerated catalyst heat remover which is arranged beside a regenerator and a regenerated catalyst cooler which is arranged on a regenerated catalyst conveying pipe are coupled and linked so that the catalyst bed temperature in the regenerator is controlled in oneaspect to solve the problem of catalyst inactivation because of overhigh temperature caused by great scorching amount in a traditional heavy oil catalytic cracking device and too much heat in the regenerator, and the carried heat and the temperature of the regenerated catalyst entering a lifting pipe reactor are adjusted in the other aspect to adjust ratios of different catalyst and oil needed for raw materials with different properties in cracking reactions. The invention takes heat and adjusts the temperatures of high-temperature regenerated catalysts in different positions in a traditionalheavy oil catalytic cracking device and flexibly adjusts the reaction-regeneration system heat balance so as to optimize heavy oil catalytic cracking process conditions and remarkably improve the yield of light oil and liquid.

The invention discloses a desulfurization flue gas waste heat recovery system for a coal-fired generator set, which comprises at least a gas-water heat exchanger for exchanging heat energy between gas state and liquid state, a flue gas inlet channel and a flue gas outlet channel respectively independently communicated with the gas-water heat exchanger, and a condensation water inlet pipeline and a condensation water outlet pipeline; a flue gas inlet of the gas-water heat exchanger is communicated with a rear flue gas channel of a boiler flue gas dust remover in the coal-fired generator set; a flue gas outlet of the gas-water heat exchanger is communicated with the flue gas inlet of a desulfurization absorption tower in a desulfurization system; a condensation water inlet and a condensation water outlet of the gas-water heat exchanger can be in sereies or parallel with at least a first-stage low-pressure heater of a regenerative system. The desulfurization flue gas waste heat recovery system provided in the invention has the advantages of the high waste heat utilization ratio, saving energy and water, the obvious discharge reducing benefit and the high comprehensive utilization degree of abandoned resources.

The invention provides an adjustable feed water heat regenerative system for a turbo generator unit, which comprises a high pressure cylinder of a steam turbine, a final-stage extraction opening, a final-stage feed water heater, a steam extraction pipe and a regulating valve, wherein the final-stage extraction opening is additionally arranged on the high pressure cylinder; the steam extraction pressure of the final-stage extraction opening is much higher than the common highest extraction pressure; additionally extracted steam is used as a heat source of the final-stage feed water heater; the steam extraction pipe is connected with the final-stage extraction opening and the final-stage feed water heater; and the regulating valve is arranged on the steam extraction pipe. Part of steam which does work is guided to the feed water heater through the final-stage steam extraction pipe so as to further heat feed water of a boiler. The heat regenerative system provided by the invention is an elastic heat regenerative system. The temperature of the feed water can be maintained or changed under the variable load condition of the unit, so that the environmental friendliness, the economy and the safety of the unit are improved and the frequency modulation characteristic is perfected.

A particulate trap regeneration system is provided. The system may include a particulate trap configured to remove one or more types of particulate matter from an exhaust flow of an engine. The system may also include a regeneration device configured to reduce an amount of particulate matter in the particulate trap. The system may further include a controller configured to activate the regeneration device in response to the first to occur of at least three trigger conditions.

An energy storage system has a first pressurized tank for carrying water and hydrogen gas and a second pressurized tank for carrying water and oxygen gas. A first output line connects to the pressurized tank for carrying hydrogen gas from the tank. A second output line connects to the second pressurized tank for carrying oxygen gas from the second tank. The energy storage system has a differential-pressure relief valve connected to the output lines to maintain the gases within a defined pressure differential. A water line connects to both pressurized tanks for maintaining relative water levels in the tanks. An electrolyzer is maintained under pressure and receives water from at least one of the pressurized tanks and creates hydrogen gas and oxygen gas for storage in the pressurized tanks. An accumulator connects to the output lines and having a movable diaphragm that separates the gases and moves to adjust volume to equalize pressure. A regeneration system having the energy storage system and a fuel cell for generating electrical energy is connected to the output lines. A catalyst hood overlies the electrolyzer. In a preferred embodiment of the regeneration system, both the electrolyzer and the fuel cell have a proton exchange membrane. A solar array is connected to the electrolyzer in the regeneration system.

The invention relates to a solution regeneration unit for a solution dehumidification air-conditioning system based on the membrane distillation technology, which mainly comprises a diluted solution reservoir, a concentrated solution reservoir, a solution heating device, a regenerative circulating pump, a water vapor treatment module and a membrane distillation component. By utilization of the characteristic in the membrane distillation technology that the temperature of driving heat source is low, the heat source temperature required by the solution regeneration process is greatly reduced, and the available temperature difference range of heat energy is increased; meanwhile, by utilization of the large contact area provided by a membrane component under unit volume and the expandability of the membrane component, the volume and the weight of a solution regeneration system are greatly reduced. Compared with the prior packed tower solution regeneration unit, the solution regeneration unit has low operating temperature and the heat energy during the operating process is only used for transmembrane latent heat transfer of water vapor, so that the energy consumption is small.

Disclosed are a movable cleaning and regenerating device and a cleaning and regenerating method for SCR (selective catalytic reduction) denitration catalysts. The device comprises a soot blowing system, a cleaning and regenerating system and a drying and calcining system. The complete offline cleaning and regenerating system for the SCR catalysts is highly integrated to be mobile, can be transported to a user via railway or road traffic to clean the SCR catalysts according to the degree of catalyst poisoning, and the catalysts are regenerated by adding catalytic ingredients while sediments, pore blockage, alkali metal and other soluble toxic substances on surfaces of the catalysts are removed. The device and the method have the advantages that activity of the catalysts is improved, the service lives of the catalysts are prolonged, a full cleaning and regenerating process can be completed without long-distance transportation, the catalysts can be regenerated to the greatest extent, cleaning cycle of the catalysts is shortened, and cost is saved for the user of the SCR denitration catalysts.

The invention relates to a method for saving energy and producing more propylene in an absorption-stabilization system by catalytic cracking. A liquid phase of a vapor-liquid equilibrium tank exchanges heat with stable gasoline on the bottom of a desorber T305 through a heat exchanger E301, exchanges heat with stable gasoline on the bottom of a stabilization tower T304 through a heat exchanger E302, and then enters a desorber T302; deethanized gasoline on the bottom of the desorber T302 exchanges heat with the stable gasoline on the bottom of a stabilization tower T304 through a heat exchanger E305, and then enters the stabilization tower T304; the stable gasoline on the bottom of the stabilization tower T304 is cooled by the heat exchanger E305 and the heat exchanger E302, a part of the stable gasoline enters a reaction-regeneration system for recycling, the rest stable gasoline is cooled by a heat exchanger E303, and a part of the rest stable gasoline enters an absorption tower T301; and the stable gasoline on the bottom of the desorber T305 is subjected to two-stage cooling of the heat exchanger E301 and a heat exchanger E304, serves as a stable gasoline product and is discharged from the device. The thermal load is reduced by 15.8 to 17.7 percent; and the alkene content in the stable gasoline product is reduced by 34.3 percent.

Methods and apparatuses for superregenerative system are disclosed, including an oscillator circuit for a superregenerative receiver. The oscillator circuit includes an RF oscillator, incorporating a self-biased transistor and a positive feedback circuit; and an external quench oscillator, for providing a quench signal to the RF oscillator; wherein the quench signal is coupled to the RF oscillator through a reversed-biased diode. The arrangement improves the performance of conventional superregenerative receivers by providing high selectivity and optimum receiver sensitivity, which is insusceptible to variations in supply voltage, temperature and device parameters.

The invention discloses a coal-fired power plant flue gas heat regenerative system and an energy-saving water-saving ultra-clean discharging method. The temperature of the flue gas is reduced to about 90-110 DEG.C through a low-temperature coal economizer, and the recycled flue gas heat heats primary and secondary wind entering a boiler through a steam air heaters, so that the first stage of heat regenerative cycles is achieved. The temperature of the flue gas at the outlet of a desulfurization tower is reduced to 30-40 DEG.C through a vacuum flash evaporation and solidification device and a low-temperature heat pump heat exchange device, and a part of water vapor of the flue gas is condensed and collected, so that water is saved. The low-temperature heat pump heat exchange device absorbs the latent heat released in flue gas sensible heat and condensation processes, and dry as-fired coal and air are heated, so that the second stage of heat regenerative cycles is achieved. A boiler slag discharge system recycles the waste heat of heat slag, and the as-fired coal is heated, so that the third stage of heat regenerative cycles is achieved. When the waste heat is not used up, the remained waste heat can be utilized, so that energy is saved. Low-temperature desulphurization slurry led out from the vacuum flash evaporation and solidification device is injected into the desulfurization tower, so that the desulphurization efficiency is improved, and an ultra-clean discharging objective is achieved.