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36results about How to "Subsequent separation is simple" patented technology

Method for preparing taurine by adopting sulfonation of ammonium sulfite

The invention discloses a method for preparing taurine by adopting sulfonation of ammonium sulfite. The method comprises the steps of: firstly carrying out esterification reaction to synthetize an intermediate 2-aminoethanol sulfate by taking concentrated sulfuric acid and ethanolamine as raw materials; carrying out sulfonation reaction to prepare taurine by taking ammonium sulfite and 2-aminoethyl sulfate as the raw materials, wherein ammonia is introduced to protect before the reaction, the temperature of the reaction solution is reduced after the sulfonation reaction is finished, and the conversion ratio of 2-aminoethyl sulfate is analyzed by adopting a sodium thiosulfate inverse titration method; cooling the reaction solution to room temperature, adding calcium hydroxide, heating, agitating and filtering to remove calcium sulfate, removing ammonia in mother liquor and repeatedly utilizing the mother liquor; then purifying the taurine by a cooling and crystallizing method to obtain crystal, carrying out suction filtration and baking the obtained crystal, and analyzing the taurine crystal by a thermal analysis method. The method disclosed by the invention is an integrated preparation method of combining the synthesis and separation of the taurine. The method is the preparation method of the taurine with simple operating process and mild reaction condition, wherein the primary conversion rate of 2-aminoethyl sulfate can be up to 79% and the desalination efficiency is 99.12%.
Owner:ZHENGZHOU UNIV

Method for vanadium extracting through low liquid-solid-ratio ammonification

The invention relates to the field of vanadium slag wet process metallurgy and vanadium chemical industry, in particular to a method for vanadium extracting through low liquid-solid-ratio ammonification. According to the method, after raw materials containing vanadium is roasted, clinkers, water and ammonium salt are mixed according to a certain proportion; materials with a low liquid-solid ratio are formed and subjected to the low-temperature ammonification reaction, the vanadium in the clinkers reacts with the ammonium salt to form ammonium metavanadate, and the ammonium metavanadate formed at the low temperature exists in mixed slurry in a crystalline mode; after the mixed slurry is subjected to hydrotherm dissolution, a solution rich in the ammonium metavanadate is obtained; and after slurry filtering, filtrate cooling and crystallizing and separating and ammonium vanadate roasting, vanadium pentoxide products are obtained. Compared with a conventional vanadium extracting through ammonification, according to the method for vanadium extracting through low liquid-solid-ratio ammonification, the using quantity of the water and the ammonium salt are greatly reduced in the ammonification process, and volatilization of ammonia gas is obviously inhibited; and the slurry can be directly subjected to hydrotherm leaching to obtain the ammonium metavanadate solution after ammonification, the process of vanadium extracting through ammonification is greatly simplified, the process is easy to operate and control, efficient and clean extracting of the vanadium can be achieved, and the extracting rate of the vanadium reaches 90% or more.
Owner:INST OF PROCESS ENG CHINESE ACAD OF SCI

Ultrasonic oxidation-extraction and deep desulfurization method for diesel oil

The invention discloses an ultrasonic oxidation-extraction and deep desulfurization method for diesel oil. The method comprises the steps: firstly, uniformly mixing an oxidizing agent, a cosolvent and a catalyst, then, mixing the mixture with sulfur-contained diesel oil on line, and next, carrying out ultrasonic oxidative desulphurization reaction in an ultrasonic reactor; delivering the mixture after reacting into a settling tank for separating to obtain a catalyst-contained solvent to be recycled and diesel oil to be subjected to solvent extraction, and separating organic sulfur in the diesel oil to obtain desulfurized diesel oil; carrying out reduced pressure distillation on the extracted solvent, recycling the separated solvent, and retreating the separated organic sulfur. By using the ultrasonic oxidation-extraction and deep desulfurization method, not only can the oxidation performance of the oxidizing agent to organic sulfur be improved, but also the cosolvent can be used for extracting organic sulfur in the diesel oil to obtain the solvent in the ultrasonic oxidation reaction, a phase transfer catalyst is not needed to be additionally added, the subsequent separation operation is easy, and the sulfur content of the desulfurized diesel oil is not higher than 10ppm. In addition, the ultrasonic oxidation-extraction and deep desulfurization method has the advantages of no adoption of organic acid capable of corroding equipment, short process route and low oil loss.
Owner:WUHAN GLT ENERGY & ENVIRONMENTAL TECH CO LTD

Method for flocculating and removing blue algae through dual-polymer composition and application of dual-polymer composition

The invention discloses a method for flocculating and removing blue algae through a dual-polymer composition. The dual-polymer composition is prepared from a natural cationic polymer A and a natural anionic polymer B; the polymer A is a mixture formed by one or two of chitosan and chitin according to a mass ratio of (1 : 200) to (100 : 1); the polymer B is a mixture formed by one or two of xanthan gum and pullulan according to a mass ratio of (1 : 500) to (300 : 1). The method for flocculating and removing the algae through the dual-polymer composition is characterized by comprising the following steps: firstly adding the polymer A into blue algae water according to a final concentration ratio of 0.2mg/L to 10mg/L, uniformly mixing, then adding the polymer B into the blue algae water according to a final concentration ratio of 0.2mg/L to 30mg/L, the adding ratio range of the polymer A and the polymer B being (1 : 1) to (1 : 3), adjusting pH of the algae water to be 3-7, stirring for 0.5-5 minutes under 100-500 rpm, standing or stirring for 0.5-10 minutes at a low speed to form massive dense blue algae floccules, and removing the algae floccules via a filtering or fishing manner.
Owner:TIANJIN ACADEMY OF ENVIRONMENTAL SCI

System and method for producing fuel chemicals by conducting solar high-temperature thermal-coupling on methane

The invention provides a system and method for producing fuel chemicals by conducting solar high-temperature thermal-coupling on methane. The method includes the steps of introducing CO2-enriched gasinto a first high-temperature thermochemical reactor, carrying out a thermochemical decomposition reaction to produce a gas mixture of CO and CO2 and first oxygen under irradiation of first sunlight,and making the gas mixture of CO and CO2 sequentially pass a first temperature reducing device and a CO2 removal device to become CO-enriched gas; introducing water vapor into a second high-temperature thermochemical reactor, carrying out a thermochemical decomposition reaction to produce a gas mixture of water vapor and H2 and second oxygen under irradiation of second sunlight, and making the gasmixture of water vapor and H2 sequentially pass a second temperature reducing device and a dewatering device to become H2-enriched gas; after mixing methane-enriched gas with the first oxygen and thesecond oxygen, carrying out a reaction in a methane partial-oxidation reactor to produce synthesis gas; mixing the synthesis gas, the CO-enriched gas and the H2-enriched gas to be introduced into a fuel chemical synthesis tower for reacting to obtain the fuel chemicals.
Owner:SHANGHAI ADVANCED RES INST CHINESE ACADEMY OF SCI +1

Ultrasonic oxidation-extraction and deep desulfurization method for diesel oil

The invention discloses an ultrasonic oxidation-extraction and deep desulfurization method for diesel oil. The method comprises the steps: firstly, uniformly mixing an oxidizing agent, a cosolvent and a catalyst, then, mixing the mixture with sulfur-contained diesel oil on line, and next, carrying out ultrasonic oxidative desulphurization reaction in an ultrasonic reactor; delivering the mixture after reacting into a settling tank for separating to obtain a catalyst-contained solvent to be recycled and diesel oil to be subjected to solvent extraction, and separating organic sulfur in the diesel oil to obtain desulfurized diesel oil; carrying out reduced pressure distillation on the extracted solvent, recycling the separated solvent, and retreating the separated organic sulfur. By using the ultrasonic oxidation-extraction and deep desulfurization method, not only can the oxidation performance of the oxidizing agent to organic sulfur be improved, but also the cosolvent can be used for extracting organic sulfur in the diesel oil to obtain the solvent in the ultrasonic oxidation reaction, a phase transfer catalyst is not needed to be additionally added, the subsequent separation operation is easy, and the sulfur content of the desulfurized diesel oil is not higher than 10ppm. In addition, the ultrasonic oxidation-extraction and deep desulfurization method has the advantages of no adoption of organic acid capable of corroding equipment, short process route and low oil loss.
Owner:WUHAN GLT ENERGY & ENVIRONMENTAL TECH CO LTD

A method for extracting vanadium by ammonification with low liquid-solid ratio

The invention relates to the field of vanadium slag wet process metallurgy and vanadium chemical industry, in particular to a method for vanadium extracting through low liquid-solid-ratio ammonification. According to the method, after raw materials containing vanadium is roasted, clinkers, water and ammonium salt are mixed according to a certain proportion; materials with a low liquid-solid ratio are formed and subjected to the low-temperature ammonification reaction, the vanadium in the clinkers reacts with the ammonium salt to form ammonium metavanadate, and the ammonium metavanadate formed at the low temperature exists in mixed slurry in a crystalline mode; after the mixed slurry is subjected to hydrotherm dissolution, a solution rich in the ammonium metavanadate is obtained; and after slurry filtering, filtrate cooling and crystallizing and separating and ammonium vanadate roasting, vanadium pentoxide products are obtained. Compared with a conventional vanadium extracting through ammonification, according to the method for vanadium extracting through low liquid-solid-ratio ammonification, the using quantity of the water and the ammonium salt are greatly reduced in the ammonification process, and volatilization of ammonia gas is obviously inhibited; and the slurry can be directly subjected to hydrotherm leaching to obtain the ammonium metavanadate solution after ammonification, the process of vanadium extracting through ammonification is greatly simplified, the process is easy to operate and control, efficient and clean extracting of the vanadium can be achieved, and the extracting rate of the vanadium reaches 90% or more.
Owner:INST OF PROCESS ENG CHINESE ACAD OF SCI

Lactic acid-producing streptococcus bovis and separation method thereof

The invention provides lactic acid-producing streptococcus bovis and a separation method thereof, and relates to the technical field of streptococcus bovis separation. The separation method of the lactic acid-producing streptococcus bovis comprises the following steps: S1, preparation of raw materials: taking 100 grams of normal cattle manure, diluting the normal cattle manure, filtering out impurities, leaving a filtrate, filling a sterile anaerobic sealing bag with the filtrate, and sealing the sterile anaerobic sealing bag; and S2, preparation of a culture medium: with water as a solute, adding, in parts by mass, 2.0 to 4.0 grams of soluble starch, 10 to 30 grams of glucose, 0.5 to 1.5 grams of dipotassium phosphate, 3 to 5 grams of calcium carbonate, 0.2 to 0.4 gram of magnesium sulfate, 0.4 to 0.6 gram of yeast powder, 20 to 40 grams of agar and 1 milliliter of a crystal violet solution with a concentration of 1% into the water. According to the invention, starch and agar are added into common culture medium components, so the growth rate of streptococcus bovis can be increased and is higher than the growth rates of other bacteria, rapid proliferation can be achieved, dominant flora can be formed, and follow-up separation is easier; and the crystal violet solution is added into the common culture medium components, so colors are easy to distinguish, and the streptococcus bovis can be quickly selected from other bacteria.
Owner:TARIM UNIV

Separation system and method for preparing acetaldehyde product from ethanol

The invention discloses a separation system for preparing acetaldehyde products from ethanol, which comprises a reactor and an ethanol absorption tower, the reactor is connected with the bottom side wall of the ethanol absorption tower, and the tower top of the ethanol absorption tower is sequentially connected with a compressor, a first cooler and a first gas-liquid separation tank; a tower bottom outlet of the ethanol absorption tower is connected with an acetaldehyde rectifying tower through a booster pump, the tower top of the acetaldehyde rectifying tower is sequentially connected with a second cooler, a second gas-liquid separation tank and a reflux pump, and the reflux pump is further connected with the side wall of the top of the acetaldehyde rectifying tower; the tower bottom of the acetaldehyde rectifying tower is respectively connected with the top side wall of the ethanol absorption tower and the inlet of the reactor; and the tower bottom of the acetaldehyde rectifying tower is also provided with an ethanol outlet. Meanwhile, the invention also discloses a method for preparing an acetaldehyde product by separating ethanol by using the system. By adding the ethanol absorption tower, the main product acetaldehyde, the by-product hydrogen and the unreacted ethanol can be efficiently separated, the separation precision is high, and the utilization efficiency of raw materials is high.
Owner:SHAANXI YANCHANG PETROLEUM GRP +1
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