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38results about How to "Enables continuous synthesis" patented technology

Method for synthesizing 2,4-difluorobenzaldehyde by using micro-channel reactor

The invention discloses a method for synthesizing 2,4-dichlorophenol by using a micro-channel reactor. The method mainly comprises the following steps: with 2,4-dinitrobenzaldehyde and potassium fluoride as raw materials, carrying out a reaction in micro-channel reactor for 50-55 s at a temperature of 200-210 DEG C, and finally rectifying and purifying a product to obtain a refined 2,4-difluorobenzaldehyde product with a purity of more than or equal to 99%. According to the preparation method disclosed by the invention, micro-channel continuous synthesis of 2,4-difluorobenzaldehyde is realized, production cost is reduced by 10-15% compared with the production cost of a traditional intermittent tank method, yield can be increased by 1-2%, and production efficiency and yield are increased by30-35%. According to the method, the micro-channel continuous flow reactor is adopted, the micro-channel continuous flow reaction technology has the characteristics of continuous reaction process, good reaction liquid mixing effect, mild reaction conditions, short reaction time, good product consistency and the like, is particularly suitable for synthesis and preparation of 2,4-difluorobenzaldehyde, and provides a powerful technical support for large-batch low-cost continuous synthesis and production of 2,4-difluorobenzaldehyde.
Owner:NINGXIA DONGWU AGROCHEM

Method and device for quantum dot synthesis under auxiliary drive of capillary force

The invention discloses a method and a device for quantum dot synthesis under auxiliary drive of a capillary force. The device comprises a precursor liquid storage device (1), a magnetic pump (2), a flow meter (3), a micro-channel reactor (4) and a quantum dot collector (5). The method includes: pumping quantum dot precursor liquid into the micro-channel reactor (4), and enabling the precursor liquid to diffuse into capillary microgrooves (8) to react under capillary force drive of a first capillary liquid suction core (7) in an inlet area; enabling obtained quantum dot solution to flow out of the micro-channel reactor (4) under capillary force drive of a second capillary liquid suction core (9) in an outlet area and flow into a quantum dot collector (5) through a guide tube, so that the quantum dot solution is obtained. The method and the device for quantum dot synthesis under auxiliary drive of the capillary force have advantages that continuous synthesis of quantum dots under low-power or even powerless conditions is realized, uniformity of the quantum dots is effectively improved, and the synthesis method is simple in operation, low in process cost and beneficial for industrial production of the quantum dots.
Owner:SOUTH CHINA UNIV OF TECH

Method for synthesizing dihydrofuran containing 1, 3-indandione spiro skeleton by using micro-channel reaction device

The invention discloses a method for synthesizing a dihydrofuran compound containing a 1, 3-indandione spiro skeleton as shown in a formula III by using a micro-channel reaction device, which comprises the following steps: by using a 2-benzylidene-1, 3-indandione compound I and a benzoyl ethyl acetate compound II as reaction raw materials, carrying out continuous reaction by using the micro-channel reaction device to prepare the dihydrofuran compound containing a 1, 3-indandione spiro skeleton. The micro-channel reaction device comprises a feeding pump, a micro-mixer and a micro-reactor whichare sequentially connected through a pipeline. Compared with the prior art, the new dihydrofuran containing the 1, 3-indandione spiro skeleton is prepared by taking the 2benzylidene 1, 3-indandione compound as the substrate for the first time, and the method avoids multi-component reaction, uses a non-metal catalyst and a low-toxicity solvent, and is a quick, efficient, green and environment-friendly synthetic product, wherein R1 is selected from halogenated benzene, C1-C4 alkyl benzene, C1-C4 alkoxy benzene, nitrobenzene, furan or naphthalene, and R2 is selected from halogenated benzene, C1-C4 alkyl benzene, C1-C4 alkoxy benzene, nitrobenzene, furan, thiophene, pyridyl or naphthalene.
Owner:NANJING ADVANCED BIOLOGICAL MATERIALS & PROCESS EQUIP INST CO 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

Method and device for continuously synthesizing spherical micro-nano cuprous oxide powder

ActiveCN102153129BNot easy to remixAvoid antimixingNanotechnologyCopper oxides/halidesMicro nanoOxide
The invention provides a method for continuously synthesizing spherical micro-nano cuprous oxide powder, and a segmented pipe type reactor for realizing the method, belonging to the technical field of nanometer materials. The method includes the steps as follows: fully mixing copper sulfate solution with sodium hydroxide solution by a pipeline and then leading the mixed solution to enter the pipetype reactor for preheating; adding glucose solution in the mixed solution; later leading the mixed system to pass through a segment or a serial-connection multi-pipe type reactor so as to raise temperature to 50-70 DEG C in a continuous or gradient way; and filtering the mixed system after oxidation reduction in the pipe type reactor, washing the mixed system with water and ethanol in sequence, conducting vacuum drying, and finally obtaining the spherical micro-nano cuprous oxide powder. The spherical micro-nano cuprous oxide powder obtained by the method is within the range of 0.5-2Mum in particle size and smooth on surface, has a cubic phase in crystal form, and has high uniformity of particle size distribution, excellent dispersivity, good sphericity and high purity. The method is easy to control in synthesizing process, low in cost, energy-saving and environment-friendly, and beneficial to industrialized production.
Owner:JINCHUAN GROUP LIMITED +1

Magnesium-silicide spiral cooling device

The invention discloses a magnesium-silicide spiral cooling device. The magnesium-silicide spiral cooling device comprises a motor, a cooler and a spiral propeller arranged in the cooler, wherein the spiral propeller mainly comprises a hollow shaft and spiral blades arranged on the hollow shaft; a cooling water introduction pipe is arranged in the hollow shaft; a cooling water return channel is formed in a gap between the inner wall of the hollow shaft and the outer wall of the cooling water introduction pipe; the first end of the cooling water return channel is connected with a cooling waterdelivery pipe; and a front end cylinder, a multi-level cooling water jacket and a tail end cylinder are arranged outside the cooler from the second end to the first end of the cooler in turn. The magnesium-silicide spiral cooling device has the advantages that: due to the combination of the spiral propeller and the cooler, continuous cooling of high-temperature magnesium silicide powder can be realized, and continuous synthesis of magnesium silicide is facilitated; and the high-temperature magnesium silicide powder moves forward with the turnover of the spiral propeller, and therefore the heat transfer is enhanced, the cooling of the magnesium silicide powder is uniform, the cooling rate is stable and a mild expansion condition is provided so as to ensure the reaction activity of the magnesium silicide and prevent the cooled magnesium silicide from caking.
Owner:SEDIN NINGBO ENG +1

Method for continuously synthesizing peracetic acid by using microreactor

The invention provides a method for continuously synthesizing peracetic acid by using a microreactor. According to the method, acetic anhydride (AA) is used as a raw material, concentrated sulfuric acid is used as a catalyst, and hydrogen peroxide (HP) is oxidized in a microreactor to generate peracetic acid (PAA). The concentration of the hydrogen peroxide is 30-50wt%, the molar ratio of the acetic anhydride to the hydrogen peroxide is (1-1.2): 1, the dosage of the catalyst concentrated sulfuric acid is 5-15mol%, the retention time is 3-20 minutes, and the reaction temperature is 30-80 DEG C. The method comprises the following steps: fully mixing acetic anhydride and concentrated sulfuric acid, mixing with hydrogen peroxide preheated by a micro preheater in a micro reactor to initiate a reaction, controlling the reaction temperature through a heat exchanger, and controlling the concentration of generated peracetic acid to be 21-35wt%. According to the invention, continuous preparation of peracetic acid is realized by adopting the microreactor, the process flow is simplified, the reaction period is short, the reaction is easy to control, peracetic acid can be rapidly and conveniently obtained when the device is used and opened, and the safety of the preparation process is improved.
Owner:DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI

A centrifugal microfluidic chip and a method for continuously synthesizing janus particles

The invention discloses a centrifugal micro-fluidic chip and a method for continuously synthesizing Janus particles. The chip consists of an upper-layer substrate, a middle-layer substrate and a lower-layer substrate, wherein an upper-layer central round hole, a circular solution tank, multiple upper-layer round dispersion channels and multiple first-level straight channels which communicate are formed in the upper-layer substrate; a middle-layer central round hole is formed in the middle-layer substrate; a central solution tank, a lower-layer round dispersion channel, multiple second-level straight channels and multiple third-level straight channels are formed in the lower-layer substrate. The method comprises steps as follows: 1) the centrifugal micro-fluidic chip is fixed on a suction cup of a spin coater; 2) different test solutions are injected into the central solution tank and the circular solution tank, the spin coater is started for spin centrifugation, and bi-phase droplets are formed at channel outlets; 3) the bi-phase droplets are spun into the external circular solution tank to form the Janus particles. With the adoption of the method, continuous introduction of the test solutions is guaranteed and continuous synthesis of the bi-phase particles is realized; the synthesis rate of the Janus particles is increased due to the arrayed synthesis channels, drive solutions rotating at the high speed and continuous synthesis.
Owner:NORTHEASTERN UNIV LIAONING

Active metal-modified oxide catalyst, preparation method and application thereof

The invention provides an active metal-modified oxide catalyst as well as a preparation method and application thereof, and the active metal-modified oxide catalyst comprises active metal, a first auxiliary agent, a second auxiliary agent and a modified oxide load, the preparation method of the active metal-modified oxide catalyst comprises the four steps of oxide loading modification, magnesium nitrate treatment, catalyst material preparation and active metal-modified oxide catalyst preparation, and the finally prepared active metal-modified oxide catalyst can be used as a catalyst for 2-methyl-1, 3, 4-trimethyl-1, 3-pentanediol monoisobutyrate. The catalyst is used in 1, 2-propane diamine synthesis reaction. The active metal-modified oxide catalyst disclosed by the invention is good in stability and excellent in catalytic performance, and the conversion rate of reaction raw materials and the high selectivity of products can be improved by applying the catalyst to a synthetic reaction of 2-methyl-1, 2-propane diamine, namely the synthetic efficiency of 2-methyl-1, 2-propane diamine can be improved.
Owner:XIAN MODERN CHEM RES INST

Magnesium-silicide spiral cooling device

The invention discloses a magnesium-silicide spiral cooling device. The magnesium-silicide spiral cooling device comprises a motor, a cooler and a spiral propeller arranged in the cooler, wherein the spiral propeller mainly comprises a hollow shaft and spiral blades arranged on the hollow shaft; a cooling water introduction pipe is arranged in the hollow shaft; a cooling water return channel is formed in a gap between the inner wall of the hollow shaft and the outer wall of the cooling water introduction pipe; the first end of the cooling water return channel is connected with a cooling waterdelivery pipe; and a front end cylinder, a multi-level cooling water jacket and a tail end cylinder are arranged outside the cooler from the second end to the first end of the cooler in turn. The magnesium-silicide spiral cooling device has the advantages that: due to the combination of the spiral propeller and the cooler, continuous cooling of high-temperature magnesium silicide powder can be realized, and continuous synthesis of magnesium silicide is facilitated; and the high-temperature magnesium silicide powder moves forward with the turnover of the spiral propeller, and therefore the heat transfer is enhanced, the cooling of the magnesium silicide powder is uniform, the cooling rate is stable and a mild expansion condition is provided so as to ensure the reaction activity of the magnesium silicide and prevent the cooled magnesium silicide from caking.
Owner:SEDIN NINGBO ENG +1
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