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45results about How to "Reduce energy consumption index" patented technology

Lead melting copper removal refining process for industrial frequency coreless-type electric induction furnace

The invention relates to a lead melting copper removal refining process for an industrial frequency coreless-type electric induction furnace. The process comprises the following steps: heating and melting a lead bullion raw material through the industrial frequency coreless-type electric induction furnace, pressing slag, and performing quick cooling to liquate copper from lead bullion; injecting the lead bullion obtained after copper removal into an anode casting unit to cast an anode plate, putting a lead anode plate into an electrolytic tank, applying direct current, and liquating anode lead on a cathode after the anode lead forms lead ions and enters an electrolyte; melting the liquated lead through the industrial frequency coreless-type electric induction furnace, sequentially performing oxidation refining and alkaline refining, dredging the slag, and then injecting a lead solution into a pouring unit to obtain an electrolytic lead ingot and oxidized slag; pumping the lead solution after slag dredging into a cathode sheet unit to enable a lead-solution-adhered roller to rotate so as to obtain a cathode lead sheet. The lead melting copper removal refining process for the industrial frequency coreless-type electric induction furnace is respectively applied to the working procedures such as lead melting copper removal, liquated lead refining ingot casting and cathode sheet manufacturing with electric energy, which is conveniently and easily obtained, through the industrial frequency coreless-type electric induction furnace, and has the advantages of reasonable process, low equipment investment, low energy consumption, great economic benefit, good environment-friendly effect and the like.
Owner:SHAANXI ZINC IND

Method for controlling furnace pressure of pulse furnace

An embodiment of the invention discloses a method for controlling the furnace pressure of a pulse furnace. The method includes the steps: arranging a test mechanism for testing the furnace pressure of the pulse furnace and a control mechanism for adjusting the furnace pressure of the pulse furnace in the pulse furnace; calculating feed-forward quantities including a first flue gas quantity, a second flue gas quantity and a third flue gas quantity and then summarizing the first flue gas quantity, the second flue gas quantity and the third flue gas quantity to serve as the adjusting feed-forward quantity of a gate valve position; correcting a valve characteristic curve of the gate valve position to reduce the influence of nonlinear factors, and adjusting the gate valve position according to the corrected valve characteristic curve; monitoring the state of a furnace door, closing the gate valve position by a preset angle when the furnace door is opened, and opening the gate valve position by the preset angle when the furnace door is closed; and monitoring the state of burners, and adjusting the number, the sequence and opening-closing action of the burners involved in combustion. The control mechanism comprises the adjustable gate valve position, first flue gas is generated by air and coal combustion, second flue gas is reduced by dilution wind extracted by a dilution fan, and third flue gas is extracted by a warm protection fan.
Owner:SHANGHAI BAOSIGHT SOFTWARE CO LTD

Device for extracting pure nitrogen from polluted nitrogen high in extraction rate and low in energy consumption and extracting method thereof

ActiveCN104048478AHigh extraction rateReduce the evaporating side temperatureSolidificationLiquefactionNitrogenTower
The invention discloses a method for extracting pure nitrogen from polluted nitrogen high in extraction rate and low in energy consumption. The method includes the following steps that polluted nitrogen enters a main tower and then conducts heat and mass transfer with top-to-bottom liquid on a tower plate or fillers in the main tower from bottom to top, part of pressure is pumped out at the tower top, and the polluted nitrogen serves as a product after being reheated through a main heat exchanger; after polluted liquid nitrogen discharged from the bottom of the main tower enters a subcooler to be cooled through the subcooler, polluted nitrogen evaporated from a main tower condenser is sent to a secondary tower, the polluted nitrogen conducts heat and mass transfer with top-to-bottom liquid on a tower plate or fillers in the secondary tower from bottom to top, the polluted nitrogen generated at the tower top is condensed through a secondary tower condenser, part of the condensed liquid returns to the secondary tower to serve as backflow liquid, and the other part of the liquid enters the main tower to serve as backflow liquid; the polluted nitrogen evaporated from the secondary tower condenser is reheated through the subcooler and the main heat exchanger, and then is sent to a polluted nitrogen compressor to be recycled and utilized. According to the method, the amount of the nitrogen extracted from the polluted nitrogen is higher than the amount of the nitrogen extracted from the air, and the nitrogen extraction rate reaches more than 90%.
Owner:ZHEJIANG DACHUAN AIR SEPARATION PLANT

Production method of feed-grade tricalcium phosphate

InactiveCN106698377AFacilitate the decomposition and defluorinationDecomposition defluorination promotionEnergy inputPhosphorus compoundsDecompositionPhosphate product
The invention discloses a production method of feed-grade tricalcium phosphate. The method comprises the following steps: 1, drying of phosphorus rock powder; 2, mixing and ball milling; 3, disc granulation; 4, calcination defluorination; 5, cooling, crushing and sieving; 6, ball-milling of a semi-finished product; 7, screening deironing; and 8, product packaging. The method has the following advantages: 1, the raw material component and the granularity range of the phosphorus rock powder are prescribed; 2, addition of a sodium salt to raw materials facilitates decomposition defluorination of phosphorus rocks; 3, addition of phosphoric acid to the raw materials improves the content of phosphorus in the above product and facilitates granulation and calcination defluorination; 4, addition of steam in the calcining process promotes decomposition defluorination of the phosphorus rocks; 5, the product goes through the area of an electromagnet or a permanent electromagnet to remove iron fillings and other metal impurities, so operation control is simple, and the impurity removal efficiency is high; and 6, calcination tail gas is fully used to produce saturated steam and superheated steam, so energy is saved, and the energy consumption and the production cost are reduced. The method is suitable for producing the feed-grade tricalcium phosphate product.
Owner:WENGFU (GRP) CO LTD

Device and method of recycling C2 from refinery dry gas

The invention discloses a device of recycling C2 from refinery dry gas, which includes a PSA unit, a compression unit and an oil absorption unit. The PSA unit includes a first-section PSA device. The compression unit includes a compressor and a liquid separation pot. An inlet of the first-section PSA device is communicated with the raw material dry gas and an outlet of the first-section PSA device is communicated with the inlet of the compressor. The outlet of the compressor is communicated with the inlet of the liquid separation pot. The invention is advantaged in that firstly the raw material dry gas is subjected to primary concentration in the first-section PSA device being low in energy consumption, and then the PSA concentrated gas is further concentrated through an adsorption/desorption method being high in recycle rate and product purity, wherein the temperature of fed gas material, an absorbent and top reflux are all 40 DEG C in the absorption unit. By means of circulated cooling water, the cooling condensation temperature can be achieved without any refrigerating device. By means of the compressed condensate as the absorbent, it is unnecessary to feed a C4 absorbent from other apparatus. The invention also discloses a method of recycling C2 from the refinery dry gas.
Owner:BEIJING YANSHAN YULONG PEC

Wet desulfurization system with electrostatic humidifier and anode demister

The invention provides a wet desulfurization system with an electrostatic humidifier and an anode demister, which relates to a purification apparatus in a thermal power plant, particularly an apparatus for lowering dust content in spray-type desulfurization absorption tower wet desulfurization fume. The wet desulfurization system comprises an absorption tower, wherein a spray layer and a demister are arranged in the tower; a humidification sprayer is arranged 0.3-1.0m behind the demister; the humidification sprayer is connected with a high-voltage electrostatic power supply; a last stage demister is arranged in a flue which is 4-10m behind the humidification sprayer; a flush sprayer for flushing the last stage demister is arranged in front of the last stage demister; an electrostatic demister is arranged behind the last stage demister and connected with the high-voltage electrostatic power supply. The wet desulfurization system effectively lowers the smoke dust discharge amount of the thermal power plant chimney, has the advantages of low energy consumption, lower investment, convenient maintenance of equipment, long service life, short construction cycle, extremely low equipment failure rate, simple operation regulation and high equipment safety, and can effectively collect fine particles, escape ammonia, heavy metal, organic pollutants and the like.
Owner:王利国 +2

Preparation method of N-(4-(2-ethylhexyloxy) phenyl)-1, 1-dioxothiomorpholino

The invention relates to a preparation method of N-(4-(2-ethylhexyloxy) phenyl)-1, 1-dioxothiomorpholino. The method is characterized by comprising the following steps of: adding 10 parts by weight of thiodiglycol and 10 parts by weight of water to a reaction kettle, then adding 1-2 parts by weight of quaternary ammonium salt as a catalyst, adding 65-75 parts by weight of hydrogen peroxide dropwisely into the reaction kettle, after dropping, preserving the heat of the mixture and allowing it to stand for one hour so as to generate bishydroxyethylsulfone, adding p-aminophenol to conduct a condensation reaction for 3 hours, then adding bromoisooctane for a further condensation reaction for 3 hours, pouring n-heptane into a product stock solution, stirring the solution and allowing it to stand, taking out the extraction phase and evaporating the solvent to dryness, thus obtaining a finished product. Application of the method provided in the invention can prepare products with an overall yield of over 86% and effective content of more than 98%, so the method is completely applicable to large scale industrial production. With substantial economic benefit, social benefit and ecological benefit, the method provided in the invention fully meets the requirements of safety, environmental protection and high efficiency that are advocated by the nation in developing low carbon economy.
Owner:XIANTAO WYLSON CHEM

Sterilizing technology used for sterile filling production line

The invention discloses a sterilizing technology used for a sterile filling production line. A first pipeline is arranged between a high-temperature hot water circulation system and a sterile water circulation system; pre-cleaning is conducted on a material circulation system, the high-temperature hot water circulation system, the sterile water circulation system and the first pipeline, and afterwards, all the systems run and communicate with the first pipeline; in the high-temperature hot water circulation system, when the high-temperature hot water is heated to the first sterilizing temperature, heat insulation is conducted for the first time period, the high-temperature hot water is sterilized, and the sterile high-temperature hot water is obtained; and along with the situation that thefirst pipeline supplements the sterile high-temperature hot water into the sterile water circulation system gradually, the flow of sterile water supplied by the sterile water circulation system in the sterile water circulation system is reduced gradually, and meanwhile normal-temperature pure water is supplemented into the high-temperature hot water circulation system. By means of the sterilizingtechnology used for the sterile filling production line, energy consumption of steam, ice water and tower water used during running of the sterile water circulation system is effectively reduced, andenergy consumption of tower water and ice water at the rear end of the material circulation system is effectively reduced.
Owner:JIANGSU NEWAMSTAR PACKAGING MACHINERY

Secondary network intelligent adjustment system based on room temperature monitoring

The invention relates to a secondary network intelligent adjustment system based on room temperature monitoring. The system comprises: a room temperature monitoring and data collecting system used formonitoring the room temperature of a typical user in real time and obtaining an effective average room temperature; a meteorological data acquisition system used for acquiring outdoor meteorologicaldata, wherein the outdoor meteorological data comprises outdoor temperature data; and an intelligent adjustment heat supply platform used for establishing a heat supply operation curve according to the outdoor temperature, the room temperature monitoring data and a preset indoor temperature, correcting the water supply temperature of the secondary network according to the established heat supply operation curve and issuing the corrected water supply temperature of the secondary network to each heat exchange station for automatic operation of the heat exchange stations. The internet of things is combined with big data, self-sensing and self-optimizing operation of the heat supply system is achieved through self-adaptive regulation of intelligent means, energy consumption indexes such as heat and electricity are reduced, and the energy utilization rate is increased.
Owner:DATANG DONGBEI ELECTRIC POWER TESTING & RES INST +1

Marine temperature self-adaptive air-cooled cabinet

The invention discloses a marine temperature-adaptive air-cooled cabinet, the cabinet is a three-area cabinet composed of an air supply area, an equipment area and an air return area, the air supply area and the equipment area are further divided into a plurality of sub-areas in the vertical height, and the air supply sub-areas and the equipment sub-areas at the same height form a relatively independent heat dissipation unit; the public air return area collects hot air flowing out of the heat dissipation units. Through an air flow stabilizing and distributing mechanism composed of an air supply area cavity, an air supply pipe, a proportioning valve and a flow guide plate, air flow organization in the cabinet is clear, and heat exchange efficiency is improved. And the heat dissipation unit is combined with the multi-loop temperature control unit to form a temperature self-adaptive air cooling system with complete functions. According to the system, zoned control of temperature is realized, and the running condition of equipment in each heat dissipation unit is matched. And according to the temperature set value and the actual temperature feedback value, the branch cold air conveying amount is controlled as required, regional refined refrigeration management is achieved, and the energy consumption index of unit load is further reduced.
Owner:708TH RES INST OF CSSC

Method for producing feed-grade tricalcium phosphate by utilizing low-calorific-value tail gas

PendingCN111377423AReduce processing costsFacilitate the decomposition and defluorinationDrying solid materials with heatEnergy inputExhaust gasChemistry
The invention discloses a method for producing feed-grade tricalcium phosphate by utilizing low-calorific-value tail gas. The method comprises the following steps: (1) burning ground phosphate rock byutilizing the low-calorific-value tail gas and drying; (2) mixing and ball milling; (3) performing disc granulation; (4) calcining and defluorinating the low-calorific-value tail gas; (5) air heat storage and temperature rise; (5) cooling, crushing and sieving; (6) circularly crushing and screening, and ball-milling a semi-finished product; (7) screening and removing iron; and (8) packaging products. The method has the following advantages: (1) the raw material components and the particle size range of the ground phosphate rock are specified; (2) low-calorific-value tail gas combustion is fully utilized for heat storage and temperature rise of combustion-supporting air; (3) a low-calorific-value tail gas combustion technology and a co-combustion technology are fully utilized; (4) steam isadded in the calcining process to promote decomposition and defluorination of the phosphate ore; and (5) saturated steam and superheated steam are produced by fully utilizing calcined tail gas, so that energy is saved, and energy consumption and production cost are reduced. The method is very suitable for being popularized and used in enterprises producing feed-grade tricalcium phosphate products.
Owner:WENGFU (GRP) CO LTD

Unpowered automatic liquid-transferring method in production and evaporation procedures of tanning extracts

The invention relates to the field of tanning extracts and particularly relates to an unpowered automatic liquid-transferring method in the production and evaporation procedures of the tanning extracts. A triple-effect evaporator is connected with a scratching-plate type evaporator to form a quadruple-effect down-flow evaporation system. The unpowered automatic liquid-transferring method is characterized in that liquid-level difference exists between the triple-effect evaporator (5) and the scratching-plate type evaporator (7), and simultaneously the boiling circulation speed of glue solution in the triple-effect evaporator is accelerated, so that the vacuum degree of the triple-effect evaporator is less than that of the scratching plate type evaporator, a water column between the triple-effect evaporator and the scratching plate type evaporator and with the vacuum-degree pressure difference being more than or equal to 100mm forms differential pressure; and glue solution in the triple-effect evaporator is automatically transferred into the scratching type evaporator under the action of pressure difference power. The unpowered automatic liquid-transferring method has the advantages that concentrated glue is suctioned to the scratching type evaporator for further evaporation and concentration from the triple-effect evaporator by utilizing the power formed by vacuum pressure difference, and automatic liquid transferring between the triple-effect evaporator and the scratching-plate type evaporator in the evaporation procedure without mechanical power is realized, so that the energy consumption in the production process of the tanning extracts is reduced and the production efficiency is improved.
Owner:陈晓程

Lead melting copper removal refining process for industrial frequency coreless-type electric induction furnace

The invention relates to a lead melting copper removal refining process for an industrial frequency coreless-type electric induction furnace. The process comprises the following steps: heating and melting a lead bullion raw material through the industrial frequency coreless-type electric induction furnace, pressing slag, and performing quick cooling to liquate copper from lead bullion; injecting the lead bullion obtained after copper removal into an anode casting unit to cast an anode plate, putting a lead anode plate into an electrolytic tank, applying direct current, and liquating anode lead on a cathode after the anode lead forms lead ions and enters an electrolyte; melting the liquated lead through the industrial frequency coreless-type electric induction furnace, sequentially performing oxidation refining and alkaline refining, dredging the slag, and then injecting a lead solution into a pouring unit to obtain an electrolytic lead ingot and oxidized slag; pumping the lead solution after slag dredging into a cathode sheet unit to enable a lead-solution-adhered roller to rotate so as to obtain a cathode lead sheet. The lead melting copper removal refining process for the industrial frequency coreless-type electric induction furnace is respectively applied to the working procedures such as lead melting copper removal, liquated lead refining ingot casting and cathode sheet manufacturing with electric energy, which is conveniently and easily obtained, through the industrial frequency coreless-type electric induction furnace, and has the advantages of reasonable process, low equipment investment, low energy consumption, great economic benefit, good environment-friendly effect and the like.
Owner:SHAANXI ZINC IND

A device and method for recovering C2 in refinery dry gas

The invention discloses a device of recycling C2 from refinery dry gas, which includes a PSA unit, a compression unit and an oil absorption unit. The PSA unit includes a first-section PSA device. The compression unit includes a compressor and a liquid separation pot. An inlet of the first-section PSA device is communicated with the raw material dry gas and an outlet of the first-section PSA device is communicated with the inlet of the compressor. The outlet of the compressor is communicated with the inlet of the liquid separation pot. The invention is advantaged in that firstly the raw material dry gas is subjected to primary concentration in the first-section PSA device being low in energy consumption, and then the PSA concentrated gas is further concentrated through an adsorption / desorption method being high in recycle rate and product purity, wherein the temperature of fed gas material, an absorbent and top reflux are all 40 DEG C in the absorption unit. By means of circulated cooling water, the cooling condensation temperature can be achieved without any refrigerating device. By means of the compressed condensate as the absorbent, it is unnecessary to feed a C4 absorbent from other apparatus. The invention also discloses a method of recycling C2 from the refinery dry gas.
Owner:BEIJING YANSHAN YULONG PEC

A precise gas concentration control device for injection-assisted sintering method and its control method

A fuel concentration accurate control device for a blowing auxiliary sintering method comprises a sintering machine trolley (1) and a blowing cover (2). The blowing cover (2) is located on the upper portion of the sintering machine trolley (1) and combines into a sealing body with the sintering machine trolley (1). The fuel concentration accurate control device is characterized in that the devicefurther comprises a fuel blowing device (3) and a material face detecting device (5) which are arranged on the blowing cover (2), the fuel blowing device (3) comprises a fuel blowing master pipe (301), a fuel blowing branch pipe (302) and a fuel blowing pipe (303), and the material face CO detecting device (5) penetrates through the blowing cover (2), is located above the sintering machine trolley(1) and is lower than the fuel blowing pipe (303). According to the fuel concentration accurate control device, the material face fuel volume concentration value can be rapidly detected and controlled when the work condition is changed and thus fluctuation occurs, and thus returns to the normal range, and thus it is effectively guaranteed that disadvantageous condition that the material face fuelvolume concentration is over high or over low for a long time in the production process can be avoided.
Owner:ZHONGYE-CHANGTIAN INT ENG CO LTD

Equipment and method for purifying nitrogen from polluted nitrogen with high extraction rate and low energy consumption

ActiveCN104048478BHigh extraction rateReduce the evaporating side temperatureSolidificationLiquefactionNitrogenTower
The invention discloses a method for extracting pure nitrogen from polluted nitrogen high in extraction rate and low in energy consumption. The method includes the following steps that polluted nitrogen enters a main tower and then conducts heat and mass transfer with top-to-bottom liquid on a tower plate or fillers in the main tower from bottom to top, part of pressure is pumped out at the tower top, and the polluted nitrogen serves as a product after being reheated through a main heat exchanger; after polluted liquid nitrogen discharged from the bottom of the main tower enters a subcooler to be cooled through the subcooler, polluted nitrogen evaporated from a main tower condenser is sent to a secondary tower, the polluted nitrogen conducts heat and mass transfer with top-to-bottom liquid on a tower plate or fillers in the secondary tower from bottom to top, the polluted nitrogen generated at the tower top is condensed through a secondary tower condenser, part of the condensed liquid returns to the secondary tower to serve as backflow liquid, and the other part of the liquid enters the main tower to serve as backflow liquid; the polluted nitrogen evaporated from the secondary tower condenser is reheated through the subcooler and the main heat exchanger, and then is sent to a polluted nitrogen compressor to be recycled and utilized. According to the method, the amount of the nitrogen extracted from the polluted nitrogen is higher than the amount of the nitrogen extracted from the air, and the nitrogen extraction rate reaches more than 90%.
Owner:ZHEJIANG DACHUAN AIR SEPARATION PLANT
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