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283results about How to "Reduce energy input" patented technology

Waste heat recovery device of air compressor and control method of waste heat recovery device

The invention discloses a waste heat recovery device of an air compressor and a control method of the waste heat recovery device. The waste heat recovery device comprises heat exchanging modules and enhanced heat exchanging modules, wherein the heat exchanging modules are arranged in parallel at the two ends of an oil-channel electric valve; the reinforcing heat exchanging modules are arranged in parallel at the two ends of the air-channel electric valve; the heat exchanging modules and the reinforcing heat exchanging modules are utilized to recover and store the heat energy in circulating oil and the heat energy in compressed air lost and wasted when the air compressor operates; the heat energy of the compressed air can be recycled at highest efficiency under the premise that the operation of the air compressor is not impacted. According to the waste heat recovery device of the air compressor and the control method of the waste heat recovery device, the collected data are analyzed and operated so as to realized effective high intelligent control; not only is the efficiency of the operation of the air compressor improved, but also the energy input of the heat energy utilizing modules can be reduced, the energy consumption or fuels for heating are lowered, and energy comprehensive utilizing degree is improved. Therefore, the waste heat recovery device has the advantages that the energy-saving effect is good, the intelligent degree is high, and the stability is excellent.
Owner:ZHEJIANG UNIV

Supercritical-water-oxidation energy recovery system

The invention discloses a supercritical-water-oxidation energy recovery system. The supercritical-water-oxidation energy recovery system disclosed by the invention has the beneficial effects that theoutlet end of a supercritical water oxidation reactor is connected with a high-pressure hydrocyclone, inorganic salts in reaction products in the supercritical water oxidation reactor are discharged from a sewage discharging port, high-pressure and high-pressure gas generated is exhausted into a buffering tank to carry out flat-pressing treatment, then the flatly-pressed gas passes through a high-pressure turboexpander and a low-pressure turboexpander in sequence to carry out residual-heat utilization for generating power, an outlet of the low-pressure turboexpander is connected with an evaporator, a Rankine circulation system is connected on the evaporator and is utilized for further utilizing residual heat of fluid passing through the evaporator, so that the energy input of the Rankine circulation system is reduced; the supercritical water oxidation system and a residual-heat and residual-pressure recovery system are fully combined, and heat energy and pressure energy of supercritical water oxidation products are fully utilized, so that the energy recovery and utilization rate of the supercritical water oxidation system is increased; carbon dioxide in the products is separated and recovered by utilizing a gas-liquid separator and a rectifying tower, so that the emission of greenhouse gas is reduced.
Owner:SHAANXI UNIV OF SCI & TECH

Method for extracting microalgae lipid through biological enzyme catalysis wall breaking

The invention discloses a method for extracting microalgae lipid through biological enzyme catalysis wall breaking. The method includes the steps that A, a phosphate buffer solution and a biological enzyme catalyst are sequentially added into wet algae mud, or algae slurry, or dry powder or fermentation liquor for culturing harvested lipid-generating microalgae, and the mixture is stirred and heated; B, after the enzyme catalysis degradation reaction is finished, the pH value of a reaction system is adjusted, and the temperature of enzyme catalysis degradation liquid is raised and kept; C, after the reaction is finished, the temperature of the enzyme catalysis degradation system is lowered, an extraction agent is added into the reaction system for lipid extraction, and then demulsifier is added to carry out layering through centrifugation; D, reduced pressure distillation or thin film evaporation concentration is carried out on the oil phase obtained through separation to obtain the microalgae lipid. The method is easy to implement and convenient to operate; due to efficient wall-breaking lipid extraction for the lipid-generating microalgae particularly photoautotroph lipid-generating microalgae, energy input in the microalgae lipid extraction process is reduced, the energy efficiency ratio of microalgae energy is increased, and then comprehensive production cost of microalgae biomass energy is greatly reduced.
Owner:INST OF AQUATIC LIFE ACAD SINICA
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