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1053 results about "Tert-Butyl alcohol" patented technology

Tert-Butyl alcohol (TBA), also called tert-butanol or t-butanol, is the simplest tertiary alcohol, with a formula of (CH₃)₃COH (sometimes represented as t-BuOH). It is one of the four isomers of butanol. tert-Butyl alcohol is a colorless solid, which melts near room temperature and has a camphor-like odor. It is miscible with water, ethanol and diethyl ether.

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

Blocking remover for reservoir of oil well

The invention discloses a blocking remover for a reservoir of an oil well. The blocking remover is applied to the technical field of oil extraction in an oil field, comprises an agent A and an agent B, and is characterized in that the weight percentage of the agent A is 25-35%; the weight percentage of the agent B is 65-75%; the agent A comprises the following components by weight: 45-50% of petroleum mixed xylene, 1-2% of nonyl phenol polyoxyethylene (4) ether, and the balance of 0# diesel oil; the agent B comprises the following components by weight: 6-10% of glacial acetic acid or sulfamic acid, 2-2.5% of ammonium bifluoride, 2% of ammonium chloride, 1-2% of citric acid, 1.5-2% of corrosion inhibitor 7801, 3-5% of tertiary butanol, 0.5-1% of octyl phenol polyoxyethylene (10) ether and the balance of water. The blocking remover has the following effects that: the agent A and the agent B are respectively prepared so as to be beneficial to storing the blocking remover for a long time, the agent A of the blocking remover has strong dissolving capacity on crude oil heavy components, such as wax colloid asphalt, and the washing oil efficiency on oil sand is more than 90%. The dissolving rate of the agent B of the blocking remover on carbonate is more than 80%, and the corrosion speed on N80 steel is low and is smaller than 2 g/m<2>.h.
Owner:PETROCHINA CO LTD

Paclitaxel albumin subparticles for injection and preparation method thereof

The invention discloses a paclitaxel alhumin submicron for injection. The paclitaxel alhumin submicron comprises 1-10% (W / W) of paclitaxel, 10-80%(W / W) of alhumin and 10-85% (W / W) of freeze-drying protective agent. The invention also discloses a preparation method of the paclitaxel alhumin submicron. The method comprises the following steps of 1) adding paclitaxel into tert-butyl alcohol, stirring and dissolving to be used as an organic phase; 2) adding the alhumin and the freeze-drying protective agent to water or a buffer with a pH within 6.0-8.5, stirring and dissolving to be used as a water phase; 3) adding the organic phase into water with stirring, stirring and dissolving, filtering and degerming through a millipore filtration method, and placing in a clean container; 4) freezing at-30- -50 DEG C, removing tert-butyl alcohol and water through freeze-drying by a lyophilizer to obtain freeze-drying powder with good profile and loosening quality. During usage, the freeze-drying powder is added to a solvent for injection and redissolved, so that paclitaxel alhumin submicrons with an average particle size of 100-600nm are formed. The paclitaxel alhumin submicron for injection ofthe invention has advantages of a simple preparation technology, no high toxic organic solvent and long-term storage, etc.
Owner:SHANGHAI MODERN PHARMA ENG INVESTIGATION CENT

Method for preparing inorganic oxide aerogel by taking biomass nanometer fibrillation cellulose as template

The invention relates to a method for preparing inorganic oxide aerogel by taking biomass nanometer fibrillation cellulose as a template, relating to a preparation method of the inorganic oxide aerogel. The method aims at solving the problems of complex process, high cost and low yield of the traditional method for preparing the inorganic oxide aerogel. The method comprises the following steps of: 1, preparing a biomass nanometer fibrillation cellulose water solution; 2, preparing a biomass nanometer fibrillation cellulose absolute ethyl alcohol solution; 3, mixing to obtain an inorganic / biomass nanometer fibrillation cellulose mixed solution; 4, preparing an inorganic / biomass nanometer fibrillation cellulose composite material dispersion solution; 5, displacing and concentrating to obtain an inorganic / biomass nanometer fibrillation cellulose composite material / tert-butyl alcohol suspension; 6, carrying out drying treatment to obtain a tert-butyl alcohol / inorganic / biomass nanometer fibrillation cellulose composite material; and 7, carrying out template stripping treatment to obtain the inorganic oxide aerogel. The method disclosed by the invention is mainly used for preparing the inorganic oxide aerogel.
Owner:NORTHEAST FORESTRY UNIVERSITY

Bendamustine hydrochloride compound

The invention relates to a bendmustine hydrochloride compound and a method for preparing the same. The bendmustine hydrochloride compound prepared by the method can be used for treating chronic lymphocytic leukemia (CLL) and inertia B-cell non-Hodgkin's lymphoma (B-cell NHL). The bendmustine hydrochloride compound contains bendmustine hydrochloride and hydroxyproyl beta-cyclodextrin, wherein the mass ratio of bendmustine hydrochloride to hydroxyproyl beta-cyclodextrin is 1:1-20. During the preparation process, mixed solvent of tertiary butanol and water for injection can be used, wherein the concentration of bendmustine hydrochloride in the mixed solvent is 5-10mg/mL; the ratio in the solvent (100%) by volume is as follows: 5-50% of tertiary butanol and the balance of water. The preparation process comprises the following steps of: weighing the tertiary butanol, sequentially adding the solvent and the hydroxyproyl beta-cyclodextrin, dissolving, evenly mixing and cooling the mixture to 2-15 DEG C, maintaining the temperature, then adding the bendmustine hydrochloride, stirring until bendmustine hydrochloride dissolves, filtering, filling, stoppering, dishing-up, freeze-drying, corking, out-box, covering and packaging, and finally, the bendmustine hydrochloride compound is obtained.
Owner:JIANGSU AOSAIKANG PHARMA CO LTD

Batch extractive distillation separation method of methylal-methanol azeotropic mixture

Belonging to separation technologies of methylal-methanol azeotropic mixtures, the invention discloses a batch extractive distillation separation method of a methylal-methanol azeotropic mixture. The method takes propanol, isopropanol, butanol, tert-butyl alcohol, 1, 3-propylene glycol or dimethyl sulfoxide as the extracting agent. An extractive distillation tower are operated according to the operation conditions that, under normal pressure or reduced pressure, the extracting agent and an overhead product are in a mass ratio of 0.5:1-10:1, the feed temperature of the extracting agent is 20-40DEG C, and the extractive distillation tower top is controlled at different temperatures and reflux ratios, so that a methylal product, a methylal-methanol transition section I, a methanol product and a methanol-extracting agent transition section II can be obtained from the extractive distillation tower top respectively. When composition of the extracting agent of a heating kettle meets requirements, the extracting agent is pumped into a high storage tank, and feeding is conducted for next batch of extractive distillation separation. The method of the invention has the advantages of low cost of single-tower equipment, flexible operation, adoption of an extracting agent to destroy a methylal-methanol azeotropic system, and can obtain high purity methanol and methylal products.
Owner:UNIV OF JINAN

Recovering process of solvent tertiary butanol in production process of ammoximation

The invention discloses a recovering process of a solvent tertiary butanol in a production process of ammoximation. The process comprises the following steps of: combining a rectifying system by a plurality of rectifying towers and configuring corresponding re-boiler, cooling system, reverse-flow system and compressing system; recovering ammonia and tertiary butanol in a reaction liquid of a reactor by a double-effect or multi-effect rectifying tower; using the overhead gas phase of the previous rectifying tower as a heat source of the re-boiler of the next rectifying tower by setting different operating pressures of the rectifying towers so as to utilize the previous gas phase condensing heat energy, wherein the operating pressure of one rectifying tower is 0.08-0.6MPa (absolute pressure) while the operating pressure of the last rectifying tower is 0.001-0.1MPa (absolute pressure), the overhead temperature of one rectifying tower is 60-140 DEG C, while the overhead temperature of the previous rectifying tower is 10-40 DEG C higher than that of the next rectifying tower; condensing the overhead gas phases by the cooling system, controlling the discharge temperature at 10-80 DEG C, the condensate enters into the reverse-flow system, and is pressurized by a pump, and part of the condensate is fed to the rectifying tower to reverse-flow, while the other condensate is fed outside the rectifying system; and feeding noncondensable gases in the cooling system to the compressing system to be compressed and feeding outside the rectifying system. According to the tertiary butanol recovering process flow, steam consumed is just 45-65% of that consumed by a single rectifying tower.
Owner:HUNAN BAILI ENGINEERING SCIENCE AND TECHNOLOGY CO LTD
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