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42results about How to "Reduce the risk of reactions" patented technology

Gas-liquid phase vinyl chloride production process and device

The invention provides a gas-liquid phase vinyl chloride production process and a device, and belongs to the technical field of chemical product preparation. The production process comprises the following steps: raw materials are treated, wherein raw materials comprise a liquid catalyst and mixed gas composed of hydrogen chloride and acetylene; a hydrochlorination reaction is carried out on acetylene, wherein acetylene reacts with hydrogen chloride to generate vinyl chloride, and the reaction temperature is controlled by a heat exchanger during a reaction process; gas-liquid separation is carried out, wherein generated vinyl chloride gas flows out of a liquid catalyst, and when the vinyl chloride gas passes through a condenser, the liquid catalyst is cooled, liquefied and refluxed to a reaction zone for acting on the reaction again; the liquid catalyst is recovered, and a small amount of the liquid catalyst is separated again by a demister; and the acetylene conversion rate is detected, wherein the liquid catalyst is replaced when the acetylene conversion rate is lower than 95%, and the original liquid catalyst is continuously used for catalytic action when the conversion rate is higher than 95%. The invention aims to solve the problems of temperature runaway phenomenon, surface carbon deposition and low catalytic efficiency caused by a gas-solid reaction in the prior art.
Owner:河北美邦工程科技股份有限公司

A kind of early strengthening agent of calcium silicate hydrate gel solution and its preparation method by suction filtration

The invention discloses a calcium silicate hydrate gel solution early strength agent and a preparation method thereof, and relates to the technical field of construction material production. The early strength agent and the method are used for solving problems of complicated preparation process, high cost, storage difficulty, and poor early strength effect of traditional calcium silicate hydrate powder. The calcium silicate hydrate gel solution early strength agent comprises a calcareous material, a siliceous material, a gel dispersant, and water. A weight ratio of the calcareous material to the siliceous material is 0.3-3:1. A weight ratio of water to the total of the calcareous material and the siliceous material is 5-30:1. The mass percentage of the gel dispersant is 0.1-2.0%. The preparation method of the early strength agent comprises the following steps: reaction materials are weighed; a sodium silicate water solution and a calcium nitrate water solution are respectively prepared; the two are mixed and are subjected to a reaction, such that a gel mixture solution is obtained; suction filtration is carried out; and water and the dispersant are added for re-dispersion. The early strength agent is uniform and stable, and is convenient to store. The early strength agent is highly convenient to use, and has a good early strength effect. With the early strength agent, an alkali-aggregate reaction risk can be effectively reduced.
Owner:SHANGHAI CONSTRUCTION GROUP

Synthesis method of alkyl phosphinic acid and aluminium salt thereof under normal-pressure mild condition

The invention discloses a synthesis method of alkyl phosphinic acid and aluminium salt thereof under a normal-pressure mild condition. A hypophosphorous acid solution and alcohol are adopted as raw materials, by means of an organic solvent which has an azeotropy point with water, through in-situ reaction of olefin, the alkyl phosphinic acid is synthesized, after reaction is completed, the pH is adjusted, an aluminium salt solution is added, and alkyl aluminum hypophosphite precipitates as a white precipitate. According to the synthesis method of the alkyl phosphinic acid and the aluminium saltthereof under the normal-pressure mild condition, operation is simple and convenient, concentration of the hypophosphorous acid solution is avoided, energy consumption is reduced, and the efficiencyis improved; the alcohol not only can be used as the raw material for in-situ reaction of the olefin, but also can promote homogeneous system generation of the reaction, so that inconvenience of easyauto-agglutination brought by using acetic acid as a solvent and using olefin as an oligomer is eliminated; by using the solvent co-boiling with water, the purposes of solvent recovery and recycle areachieved, and it is easier to obtain the high-quality salt-forming product; the method is implemented under the normal-pressure mild condition, a security coefficient is high, the reaction risk is small, a synthesis technology is more energy-saving, environmentally friendly and efficient, and industrial production is easier to achieve.
Owner:JINAN TAIXING FINE CHEM

Retrievable hazardous waste rigid landfill system and operation method

The invention provides a retrievable hazardous waste rigid landfill system and an operation method. The retrievable hazardous waste rigid landfill system comprises a hazardous waste landfill reservoir area, a discharging channel, an overhauling interlayer, a portal crane, a steel-structured canopy and a personnel operation walkway plate. The hazardous waste landfill reservoir area is erected on the overhauling interlayer and composed of a plurality of landfill units. Each landfill unit comprises a reinforced concrete retaining wall and a bottom plate and is provided with a bottom plate anti-seepage system, a retaining wall anti-seepage system and a leachate collecting pipe, wherein pipe walking lines of the leachate collecting pipes are mainly located in the overhauling interlayer. The overhauling interlayer is an overhead layer and located below the hazardous waste landfill reservoir area. The portal crane is located above the landfill reservoir area. The steel-structured canopy is located on the upper portion of a crane. Personnel walkways are arranged on the periphery or/and in the landfill reservoir area. The retrievable hazardous waste rigid landfill system has more reliable safety, operable retrievable landfill is achieved, and management and maintenance are facilitated.
Owner:POWERCHINA HUADONG ENG COPORATION LTD

Preparation method and device of diiodosilane

The invention relates to a preparation method and device of diiodosilane, and relates to the field of synthesis methods of semiconductor materials, the preparation method comprises the following steps: 1, mixing and dissolving iodine with at least one of chloroform, dichloromethane and dichloroethane according to a volume ratio of 1: (2-5); the phenylsilane is mixed with at least one of ethyl acetate, tert-butyl acetate and butyl acetate according to the mass ratio of 100: (1-5); pre-cooling the iodine solution and the phenylsilane solution at-40 to 0 DEG C; then pumping the mixture into a microchannel reactor, carrying out mixed reaction for 100-300 seconds in a low-temperature microchannel at-40-10 DEG C, and then introducing the mixture into a room-temperature microchannel at 20-30 DEG C to react for 100-400 seconds, so as to obtain a reaction mixture; and 2, carrying out vacuum rectification on the reaction mixture obtained in the step 1, and collecting the product with the fraction temperature of 35-40 DEG C under 20 +/-3 mmHg to obtain the high-purity diiodosilane. The diiodosilane is synthesized through the microchannel reactor, the original synthesis period can be shortened to be within 700 seconds, and the obtained mixture product is high in content and low in impurity metal ion content.
Owner:安徽敦茂新材料科技有限公司

Ferronickel slag aggregate treatment method

The invention discloses a ferronickel slag aggregate treatment method. The ferronickel slag aggregate treatment method comprises the steps of: (1) soaking ferronickel slag aggregate in a mixed aqueoussolution of sodium hydroxide and water glass; (2) adjusting the temperature of the mixed solution obtained in the step (1) to 40-60 DEG C, and keeping the temperature for 1-6 hours; (3) after the heat preservation is finished, quickly stirring the solution for 10-60 seconds; (4) adding sodium carbonate and cement powder, and performing uniform stirring; (5) standing and precipitating the solutionfor 1-2 hours, and performing separating to obtain precipitate and clarified liquid; and (6) screening out ferronickel slag aggregate with the particle size of more than 5mm in the precipitate, naturally air-drying the ferronickel slag aggregate to be used as concrete aggregate, drying and grinding the part with the particle size of less than 5mm in the precipitate to be used as a concrete admixture, and using the clarified liquid as alkali-activated material mixing water. Through treatment of the method, air holes and active ingredients on the surface of the ferronickel slag aggregate are destroyed, and the problems that the ferronickel slag aggregate is high in crushing value and has potential alkali aggregate reaction are solved.
Owner:HUAIYIN INSTITUTE OF TECHNOLOGY

Method for synthesizing 4-chloro-2, 5-dimethoxynitrobenzene by using microreactor

The invention relates to a method for synthesizing 4-chloro-2, 3, 5-tetramethylpiperidine by using a microreactor. According to the method, intermediate 2, 5-dimethoxychlorobenzene of 4-chloro-2, 5-dimethoxynitrobenzene and nitric acid are used as raw materials, 4-chloro-2, 5-dimethoxynitrobenzene is synthesized through the microreactor, in the reaction process, the mass fraction of nitric acid is50%-95%, and the mass fraction of a 2, 5-dimethoxychlorobenzene solution is 15%-50%; the feeding molar ratio of nitric acid to 2, 5-dimethoxychlorobenzene is (1.0-1.5): 1, the reaction temperature is50-85 DEG C, the feeding temperature is not higher than 50 DEG C, and the reaction retention time is 30-120 seconds. According to the method, on one hand, the process conditions such as the materialratio and the reaction temperature are accurately controlled, the dosage of nitric acid is reduced, the method is environmentally friendly, the conversion rate of 2, 5-dimethoxychlorobenzene reaches 99.98%, and the yield of 4-chloro-2, 5-dimethoxynitrobenzene reaches 99.5% or above; on the other hand, the key problems of corrosivity of nitric acid, difficulty in controlling the reaction temperature, poor mass and heat transfer effect, poor safety and the like in the conventional synthesis process are solved, and the reaction risk is low; strong operability.
Owner:LILY GRP CO LTD

Gas-liquid phase vinyl chloride production process and equipment

The invention provides a gas-liquid phase vinyl chloride production process and device, belonging to the technical field of chemical product preparation, comprising the following steps: raw material treatment, the raw material includes a liquid catalyst and a mixed gas composed of hydrogen chloride and acetylene; acetylene hydrochlorination reaction, acetylene React with hydrogen chloride to generate vinyl chloride, and control the reaction temperature through a heat exchanger during the reaction; gas-liquid separation, the generated vinyl chloride gas flows out of the liquid catalyst, and the liquid catalyst cools and liquefies when the vinyl chloride gas passes through the condenser and flows back to The reaction zone acts on the reaction again; the liquid catalyst is recovered, and a small amount of liquid catalyst is separated again by means of a demister; the conversion rate of acetylene is detected. When the conversion rate is lower than 95%, the liquid catalyst is replaced. When the conversion rate is greater than 95%, it is used The original liquid catalyst continues to catalyze, aiming to solve the problems of overheating phenomenon, surface area carbon and low catalytic efficiency caused by gas-solid reaction in the existing process.
Owner:河北美邦工程科技股份有限公司
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