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85 results about "Di-t butyl peroxide" patented technology

Preparation of tert-butyl hydrogen peroxide and di-tert-butyl peroxide

The invention discloses a preparation method of tert-butyl hydroperoxide and di-t-butyl peroxide which includes the following steps: after mixing vitriol, oxyful and phosphotungstic acid with certain concentration, adding tertiary butyl alcohol into a mixed liquor or adding the mixed liquor into the tertiary butyl alcohol; reacting for 0.5 to 5 hours under 20 to 60 DEG C; obtaining an oil phase after carrying out liquid separation on the crude product of the reaction; obtaining the tert-butyl hydroperoxide and di-t-butyl peroxide products by carrying out decompressing and rectifying on the oil phase; the method has the advantages of simple and convenient operation, low manufacture cost, safety, high efficiency and high yield; in addition, the method of the invention can adjust the relative content of the two reaction products by changing the reaction conditions. The reaction products of tert-butyl hydroperoxide and di-t-butyl peroxide are separated by decompressing and rectifying, thus avoiding the working procedures of acid cleaning and caustic wash in the traditional technique, solving the defect of overlarge waste water amount in the traditional technique, being beneficial to protecting the environment, reducing the manufacture cost and being capable of greatly increasing the enterprise benefits.
Owner:ZHEJIANG JINKE CHEM

Synthesis of gamma-undecalactone

The invention discloses a method for synthesizing gamma-undecalactone, which belongs to a synthesis technology of the gamma-undecalactone. The method takes n-octanol as a solvent, boric acid or zinc bromide as a catalyst, acrylic acid as a raw material and di-t-butyl peroxide or dibenzoyl peroxide as an initiator, and comprises the following steps: firstly, adding partial n-octanol and the catalyst into a reaction kettle to be mixed and heated; secondly, mixing the remaining n-octanol, the initiator and the acrylic acid and dipping the mixture into the reaction kettle; thirdly, making the mixture react for a period; and finally obtaining reaction liquid containing the gamma-undecalactone. The method has the advantages that the reaction is carried out at normal pressure, byproducts of tert-butyl alcohol are easy to discharge from a system during the reaction process, and simultaneously the equipment used by the method is simple, the synthesis cost is low and the yield of the gamma-undecalactone is high.
Owner:TIANJIN UNIV

Anti-cracking silicone rubber cable material and preparation method thereof

The invention discloses an anti-cracking silicone rubber cable material and a preparation method of the material. The anti-cracking silicone rubber cable material is prepared by the following raw materials in parts by weight: 65-75 parts of methyl vinyl silicone rubber, 20-30 parts of nylon 66, 10-15 parts of isotactic polypropylene, 15-20 parts of magnesium hydrate, 5-10 parts of sodium molybdate, 8-12 parts of melamine cyanurate, 2-3 parts of magnesium oxide, 10-15 parts of diisononyl phthalate, 1.5-2.5 parts of methyl tin mercaptide, 5-8 parts of polyethene wax, 0.5-1.5 parts of antioxidant BHT (butylated hydroxytoluene), 0.8-1.2 parts of valcanizer DTBP (di-t-butyl peroxide), 1-2 parts of accelerator TETD (tetraethylthiuram disulfide), 0.5-1.5 parts of scorch retarder CTP (cytidine triphosphate), 15-20 parts of carbon black N660, 12-18 parts of vermiculite powder, 5-10 parts of nano aluminum oxide and 4-7 parts of composite packing. The cable material has excellent cracking resistance and mechanical properties, is free from cracking in a low temperature impact test at -30 DEG C, a high temperature impact test at 120 DEG C and a bending test, can be applied to harsh environments such as low temperature, salt mist, wetness, hot and mould, and is durable in use.
Owner:JING FENG GRP

Method for preparing polyacrylate rubber through continuous solution polymerization and devolatilization extrusion

The invention discloses a method for preparing acrylate rubber through continuous solution polymerization and devolatilization extrusion, belonging to synthetic technique of polyacrylate rubber and solving the problems in conventional preparation methods of polyacrylate rubber that the pressure during the polymerization process is high and that the solvent of the polymerisates cnnot be easily got rid of in later period. According to the method disclosed by the invention, acrylate monomer and a small amount of monomer with crosslinking active groups are taken as the raw materials to prepare polyacrylate rubber through the methods of continous solution polymerization and devolatilization extrusion in a solvent under the action of initiator. The acrylate monomer is one or the mixture of methyl acrylate, ethyl acrylate or butyl acrylate; the monomer with crosslinking active groups is epoxypropyl methacrylate; the initiator is benzoyl peroxide or di-t-butyl peroxide; and the solvent is toluene or ethyl acetate. The content of the residual volatile in the acrylate rubber prepared through the method disclosed by the invention is lower than 1% of the content of acrylate rubber.
Owner:CHANGCHUN UNIV OF TECH

Method for preparing styrene/isoprene/maleic anhydride multi-block polymer with polyolefin as carrier

The invention relates to a method for preparing a styrene / isoprene / maleic anhydride multi-block polymer through reactive extrusion. Raw materials for the polymer comprise polyolefin, maleic anhydride, styrene, isoprene and a peroxide initiator, i.e., a di-tert-butyl peroxide compound. The method is characterized in that: polypropylene is added from a main feeding inlet at a first section of a twin-screw extruder; maleic anhydride and the initiator are dissolved in acetone and are added from a liquid feeding inlet at a third section of the extruder through a pipeline and a metering pump; isoprene and styrene are simultaneously added from the liquid feeding inlet at the third section of the extruder through another pipeline and another metering pump, temperature of a reaction section of the extruder is controlled to be 170 to 230 DEG C, and then polymerization is carried out. Compared with the prior art, the invention has the advantage that bulk polymerization is carried out on monomers by directly using the twin-screw extruder as a reactor. Meanwhile, the reactive extrusion method provided by the invention can prepare the styrene / isoprene / maleic anhydride polymer grafted on polypropylene, and the polymer can be used as an adhesive.
Owner:EAST CHINA UNIV OF SCI & TECH

O-shaped seal ring for automobile fuel pump and manufacturing process of O-shaped seal ring

The invention provides an O-shaped seal ring for an automobile fuel pump and a manufacturing process thereof, and solves the technical problems that a conventional rubber seal ring cannot be normally used in low-temperature or high-temperature environments, is poor in high-low temperature resistance and has no manufacturing process. The O-shaped seal ring for the automobile fuel pump comprises a circular-ring-shaped seal ring body, wherein a sealing lip is arranged in the middle of the seal ring body and extends outwards; the seal ring body and the sealing lip adopt an integral structure; the seal ring body comprises butadiene-acrylonitrile rubber, sulfur, an antiager mercaptobenzimidazole, zinc oxide, stearic acid, paraffin oil, alumina powder, dibutyl phthalate, an acid-base balance agent, and a vulcanization accelerator di-t-butyl peroxide. The invention also provides a manufacturing process of the O-shaped seal ring. The O-shaped seal ring has the advantages of good high-low temperature resistance and high yield.
Owner:HAINING ZHONGTENG AUTOMOTIVE SEALS

Methanol gasoline additive

The invention discloses a methanol gasoline additive which is prepared from the following raw materials in parts by weight: 6-14 parts of di-tert-butyl peroxide, 3-8 parts of naphtha, 5-9 parts of hydroquinone, 4-7 parts of propyl alcohol, 6-11 parts of acetylacetone, 3-9 parts of methyl tertiary butyl ether, 4-6 parts of benzotriazole, 1-5 parts of octadecylamine, 4-7 parts of liquefied petroleum gas, 2-6 parts of butane, 3-5 parts of carbon 12, 3-5 parts of ethanol, 4-9 parts of diethyl ether and 1-5 parts of isopropyl alcohol. The methanol gasoline additive disclosed by the invention has the beneficial effects of improving the power, simultaneously increasing the utilization rate of fuel oil and reducing pollution to air.
Owner:QINGDAO KANGTAIXIN ENVIRONMENTAL PROTECTION TECH

Preparation of tert-butyl hydrogen peroxide and di-tert-butyl peroxide

The invention discloses a preparation method of tert-butyl hydroperoxide and di-t-butyl peroxide which includes the following steps: after mixing vitriol, oxyful and phosphotungstic acid with certain concentration, adding tertiary butyl alcohol into a mixed liquor or adding the mixed liquor into the tertiary butyl alcohol; reacting for 0.5 to 5 hours under 20 to 60 DEG C; obtaining an oil phase after carrying out liquid separation on the crude product of the reaction; obtaining the tert-butyl hydroperoxide and di-t-butyl peroxide products by carrying out decompressing and rectifying on the oil phase; the method has the advantages of simple and convenient operation, low manufacture cost, safety, high efficiency and high yield; in addition, the method of the invention can adjust the relative content of the two reaction products by changing the reaction conditions. The reaction products of tert-butyl hydroperoxide and di-t-butyl peroxide are separated by decompressing and rectifying, thus avoiding the working procedures of acid cleaning and caustic wash in the traditional technique, solving the defect of overlarge waste water amount in the traditional technique, being beneficial to protecting the environment, reducing the manufacture cost and being capable of greatly increasing the enterprise benefits.
Owner:ZHEJIANG JINKE CHEM

Implementation method of kerosene-based fuel for scramjet engine started by low Mach number

An implementation method of kerosene-based fuel for a scramjet engine started at a low Mach number comprises the following steps of: adding a borane triethylamine complex into a mixed fuel of 1-octene and RP-3 kerosene, and carrying out hydroboration reaction to obtain initial modified kerosene; and mixing the initial modified kerosene with di-tert-butyl peroxide serving as a free radical ignition enhancer and benzoquinone serving as a free radical stabilizer to obtain kerosene-based fuel. Starting of the scramjet engine when the incoming flow Mach number is 1.5 can be achieved through electric spark ignition, and good stability is achieved during contact with air in a normal-temperature environment. Starting and stable combustion of the scramjet engine under the low Mach number are achieved by synthesizing the kerosene-based fuel, the operation is easy, and the practicability is high.
Owner:SHANGHAI JIAO TONG UNIV

PP flow master batch

The invention relates to the technical field of master batch preparation, in particular to a PP flow master batch. The master batch comprises, by weight, 90-100 parts of polypropylene resin, 2.5-7.5 parts of an initiator and 0.5-1.5 parts of light calcium carbonate, wherein the flowing speed of a polypropylene resin melt is 19-27 g / 10 min, and the initiator is composed of di-tert-butyl peroxide and tert-butyl hydroperoxide in the ratio of 1:(1.2-1.5). The master batch has the advantages that the PP flow master batch is applied to polypropylene thin-wall injection molding, the fluidity of the polypropylene melt is improved, and meanwhile, an injection molded polypropylene thin-wall injection molding finished product has good mechanical properties.
Owner:东莞市恒彩塑胶颜料有限公司

The preparation method of di-tert-butyl peroxide

A method of preparing di-tert-butyl peroxide is disclosed and belongs to the technical field of organic synthesis. The method includes a step of adding tert-butyl alcohol and sulfuric acid into a first reaction device, reacting under stirring, and controlling the temperature and reaction time of the reaction under stirring in the first reaction device to obtain a tert-butyl hydrogen sulfate liquid, a step of adding a recovered mother liquor into a second reaction device, adding crude tert-butyl alcohol and the tert-butyl hydrogen sulfate liquid into the second reaction device, and controlling the temperature and reaction time of a reaction under stirring in the second reaction device to obtain a reaction product, a step of feeding the reaction product to a liquid separating tank, and performing liquid separating to obtain an upper oil phase that is the di-tert-butyl peroxide and a lower water phase that is a mother liquor adopted as a recovery mother liquor for a next turn of reactions. The method is simple and short in process steps, and can allow the content of the di-tert-butyl peroxide in the upper oil phase to be 97.5% or above, thus meeting requirements on industrial scaled-up production. The method avoids environment pollution, saves raw materials, reduces the cost and achieves circular economy.
Owner:江苏强盛功能化学股份有限公司

Preparation method of di-tert-butyl peroxide

The invention discloses a preparation method of di-tert-butyl peroxide. The preparation method comprises the following steps of: adding hydrogen peroxide and sulfuric acid into a reaction kettle, sufficiently mixing the hydrogen peroxide and the sulfuric acid under an ice bath condition to obtain a mixed solution, and continuously stirring the mixed solution for 30 minutes; dropwise adding tert-butyl alcohol after violently stirring the mixed solution, controlling the dropwise adding speed, and ensuring that the reaction temperature does not exceed 5 DEG C; after dropwise adding the tert-butylalcohol, naturally heating the solution to room temperature, and continuously stirring the solution for 4 hours to obtain a reaction crude product solution; and making the solution stand still, introducing the solution into a liquid separation tank for liquid separation to obtain an upper-layer organic phase, washing the organic phase with a 30% NaOH solution, washing the organic phase with water, and drying the organic phase with anhydrous MgSO4 to obtain stimulated colorless liquid which is di-tert-butyl peroxide. The preparation method has the advantages of simplified operation, higher yield, shortened reaction time, effectively controlled reverse reaction decomposition and raw material-saving performance/ Waste gas mother liquor is recycled, so that raw materials are saved, the production cost is reduced; and the discharge of the waste liquor is reduced, the subsequent treatment cost is saved, and the environmental protection is achieved; and the sustainable development is realized, and the production profits of enterprises are greatly improved.
Owner:宁夏顺邦达新材料有限公司
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