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68 results about "P-Toluic acid" patented technology

P-Toluic acid (4-methylbenzoic acid) is a substituted benzoic acid with the formula CH₃C₆H₄CO₂H. It is a white solid that is poorly soluble in water but soluble in acetone. A laboratory route to p-toluic acid involves oxidation of p-cymene with nitric acid.

Microorganisms and methods for the biosynthesis of p-toluate and terephthalate

The invention provides non-naturally occurring microbial organisms having a (2-hydroxy-3-methyl-4-oxobutoxy)phosphonate pathway, p-toluate pathway, and / or terephthalate pathway. The invention additionally provides methods of using such organisms to produce (2-hydroxy-3-methyl-4-oxobutoxy)phosphonate pathway, p-toluate pathway or terephthalate pathway.
Owner:GENOMATICA INC

Method for recycling mother solid in PTA-refining wastewater

The invention discloses a method for recycling mother solid in PTA-refining wastewater, comprises the following steps: mixing PTA-refining wastewater and paraxylene in a prepositioned mixing tank, carrying out single-stage extraction and cooling on the wastewater, dissolving and extracting the solid in mother liquor into a PX phase, returning the extract phase PX discharged from a clarification tank to an oxidizing reaction system, and delivering the wastewater to an extraction tower to be subject to multistage countercurrent extraction; delivering the wastewater discharged from the bottom ofthe extraction tower to be subject to further treatment; and returning the extraction phase discharged from the top of the extraction tower to serve as extract liquor for single-stage extraction. By adopting the method in the invention, most of organic matters, such as p-toluic acid, terephthalic acid and the like in the wastewater can be recycled, thus the purpose of recycling wastes is achieved, and wasting of resources is avoided; and the invention omits the conventional filtering unit, saves the filter cloth-replacing cost, ensures that the extraction tower can operate at appropriate operating temperature, and has the advantages of investment saving, low energy consumption, high resource recovery rate and the like.
Owner:FUZHOU UNIV

Method for preparing terephthalic acid by oxidation refining process

The invention discloses a method for preparing terephthalic acid by an oxidation refining process. Terephthalic acid is prepared by implementing a liquid-phase catalytic oxidation reaction on p-xylene and oxygen in the presence of a catalyst, wherein the oxidation reaction is performed in a plurality of oxidation reaction zones by various steps; in a first oxidation reaction zone, Co-Mn-Ce is taken as a main body, and a catalytic system in which trace amount of bromide is added is applied to the liquid-phase catalytic oxidation; after adding a bromine catalyst to the product, the liquid-phase catalytic oxidation is further implemented in a second oxidation reaction zone; an oxidation product in the second oxidation reaction zone is directly, or after a liquid-solid separation, processed by a liquid-phase catalytic oxidation in a third oxidation reaction zone to purify, and the purified product is extracted to produce the terephthalic acid product. The method disclosed by the invention adopts different catalytic systems through a selectivity, in order to improve the selectivity of the oxidation process, reduce the catalytic combustion loss, and lower contents of p-toluic acid and p-carboxyl benzaldehyde; and meanwhile, the total amount of bromine in the oxidation process is reduced, so that the corrosion of the catalyst on the equipment is reduced.
Owner:CHINA PETROLEUM & CHEM CORP +1

Polyester fiber with low melting point and method for preparing polyester fiber

The invention relates to a polyester fiber with a low melting point and a method for preparing the polyester fiber. The polyester fiber with the low melting point is of a skin-core structure, skin layers are made of polyester with a low melting point, and core layers are made of PET (polyethylene terephthalate); the polyester with the low melting point comprises terephthalic acid chain segments, isophthalic acid chain segments, ethylene glycol chain segments, diethylene glycol chain segments and molecular weight regulator end-capping groups; corresponding molecular weight regulators of the molecular weight regulator end-capping groups particularly comprise benzoic acid, p-toluic acid or ethylbenzoic acid, or methyl ester or ethyl ester corresponding to the benzoic acid, the p-toluic acid or the ethylbenzoic acid, or saturated fatty acid or methyl ester or ethyl ester corresponding to the saturated fatty acid; the content of acetaldehyde in the polyester fiber with the low melting point is lower than 0.5 ppm. The method includes steps of polymerizing the polyester with the low melting point and carrying out composite spinning on skin and cores; carrying out back spinning by the aid of drafting-washing processes; carrying out oil-bath drafting by the aid of added sodium sulfite; carrying out crimping, cutting-off and drying to obtain the polyester fiber with the low melting point. The polyester fiber with the low melting point and the method have the advantages that the polyester fiber prepared by the aid of the method has the low melting point and is low in acetaldehyde content.
Owner:扬州富威尔复合材料有限公司

Preparation method of (-)-di(p-toluoyl)tartaric acid

The invention discloses a preparation method of (-)-di(p-toluoyl)tartaric acid. The preparation method comprises the following steps of: adding certain quantity of para-toluylicacid, solvent and catalyst into a flask which is provided with a reflux condenser, simultaneously dropwise adding thionyl chloride; and then adding certain quantity of tartaric acid after heating for reflux for a while; then continuing to heat for reflux for a while; after reaction is finished, cooling to room temperature; adjusting pH value to be neutral by using an alkali solution; after finishing pH adjusting, heating for reflux for a while; after reaction, cooling to below 20 DEG C; filtrating to obtain a crystal; washing twice with a reactive solvent; and baking to obtain the product. The process has the characteristics of simple process, high efficiency, direct product obtaining without treating a semi-finished product, and adaptability to actual production.
Owner:南通欧通置业有限公司

Preparation method of novel fluorescent PVC wire/cable shield material

The invention provides a preparation method of a novel fluorescent PVC wire / cable shield material. The preparation method comprises the following steps: (1) heating and stirring a terbium chloride solution and a phenanthroline solution together, adding a p-toluic acid solution, further stirring, standing, filtering, washing, and drying to obtain white powder; dissolving the white powder in dimethyl fumarate, adding distilled water to form a suspension, then adding sodium chloride and stearic acid, stirring, taking out, filtering and drying to obtain fluorescent powder; (2) adding ACR to the fluorescent power, stirring and mixing, extruding, melt spinning to obtain fluorescent fibers; (3) adding PVC, nano-montmorillonite, a heat stabilizer, a plasticizer, calcium carbonate, a coupling agent and an antioxidant together into a high speed stirrer for stirring to obtain a mixed material; and (4) dissolving the mixed material into a solvent, adding the fluorescent fibers, uniformly stirring to obtain a prepreg, drying, transferring to a die, heating, pressurizing and insulating heat, and naturally cooling to room temperature to obtain the fluorescent PVC wire / cable shield material. The shield material prepared by the preparation method provided by the invention has a relatively good fluorescent performance.
Owner:SHAOGUAN YINGTIAN ENVIRONMENT FRIENDLY MATERIAL CO LTD

Extraction method for reducing emission of chemical oxygen demand (COD) in pure terephthalic acid (PTA) wastewater

The invention discloses an extraction method for reducing emission of chemical oxygen demand (COD) in pure terephthalic acid (PTA) wastewater. The method includes that a solvent is firstly used for extracting and removing a large amount of organic carboxylic acid of benzoic acid, p-toluic acid, p-carboxyl benzyl alcohol, p-carboxybenzaldehyde and terephthalic acid, and then a gas stripping method is used to remove a residual extracting agent in the wastewater so that COD concentration in the wastewater is greatly reduced; simultaneously, organic carboxylic acid which is extracted into an extracting agent phase returns to a PTA device with the extracting agent, and the p-toluic acid, the p-carboxyl benzyl alcohol, the p-carboxybenzaldehyde and the terephthalic acid in the organic carboxylic acid are finally converted into PTA products through the PTA device so that a large quantity of useful organic substances in the wastewater are recycled, and economic benefits are increased; and outlet gases of a gas stripping tower, which carry the extracting agent, are returned to the PTA device so that the extracting agent is recycled, and consumption of the extracting agent is low. The extraction method is high in efficiency, low in consumption and capable of reducing emission of COD, reducing loads of sewage treatment stations and partially achieving resource utilization of the wastewater.
Owner:浙江化安安全技术研究院有限公司

Method for preparing modified alkyd resin

The invention adopts the technical scheme that a method for preparing modified alkyd resin comprises the special steps as follows: (1) mixing 23 to 37 percent by weight of ricinoleic acid, 21 to 29 percent by weight of glycerin, 29 to 31percent by weight of phthalic anhydride, 10 to 18 percent by weight of crude p-toluic acid and adding the mixed liquor into a reaction vessel; and (2) adding xylene and hypophosphorous accounting for 0.06 to 0.1 percent by weight of the mixed liquor obtained from the step (1) into the reaction vessel, increasing the temperature to 190 to 201 DEG C for thermal insulation and esterification, and cooling and diluting as long as the acid value is below 21.5 mgKOH / g in esterification. In the invention, the cost is low; and polyurethane varnish made of alkyd resin prepared through the invention can reach requirements of various properties.
Owner:江苏三木化工股份有限公司

Recycling method of 2-(4-methyl phenyl)-benzoxazole synthetic process wastewater

The invention relates to a recycling and treating method of p-toluic acid and ortho-aminophenol in wastewater of a process for synthesizing 2-(4-methyl phenyl)-benzoxazole by taking the p-toluic acid and the ortho-aminophenol as raw materials. The method is characterized by comprising the steps that p-toluic acid precipitates are firstly precipitated out through acidification, and the p-toluic acid is recycled through filtration; filtrate is treated with a reducing agent, the pH value of the filtrate is regulated to be alkali, adsorption is performed with adsorbent resin, elution and analysis are performed, the pH of eluant is regulated to 8.5-9, concentrating and temperature lowering are performed to precipitate phenol out, and filtration is performed to obtain the ortho-aminophenol. According to the method, the p-toluic acid and the ortho-aminophenol in the process wastewater can be economically and effectively recycled, the purity of the p-toluic acid and the purity of the ortho-aminophenol can reach 94.5% or above and 95.8% or above respectively, and the p-toluic acid and the ortho-aminophenol can directly serve as the raw materials to be put and used over and over again in a condensation reaction; organic solvent is not related and used in the treatment process, secondary environmental pollution is not generated, cleanliness and environmental protection are achieved.
Owner:HUBEI HONGXIN CHEM CO LTD

Combined process for recycling organisms in PTA (Purified Terephthalic acid) refining waste water

The invention discloses a combined process for recycling organisms in PTA (Purified Terephthalic acid) refining waste water. The combined process combines an existing azeotropic rectification system in a PTA system with an extraction process. Firstly, by using a water-carrying agent in an acetic acid azeotropic rectification system as an extraction agent for the PTA refining waste water, the organisms (organic carboxylic acids such as a benzoic acid, a p-toluic acid, a terephthalic acid and the like) in the waste water are extracted out. An extraction phase containing the organic carboxylic acid is returned to an azeotropic rectification column, then the organic carboxylic acids are produced from a column reactor of the azeotropic rectification column and are returned to a PTA oxidative system together with acetic acid. A raffinate phase is sent to a solvent recovery tower, and an organic solvent is produced from a tower top so as to implement recover of the organic solvent in the waste water. One part of waste water produced from a column reactor of a solvent recovery tower is sent to a tail gas absorption system of the PTA oxidative system to be used as an absorbent, and the other part of the waste water is sent to a sewage treatment system. The combined process is simple in flow, implements recycling of the organic carboxylic acid and partial recycling of water in the PTA refining waste water, and is low in cost.
Owner:FUZHOU UNIV

Process of producing high purity terephthalic acid

A problem of the invention is to provide a process of producing high purity terephthalic acid by selectively recovering p-toluic acid in wastewater which has hitherto been discarded and using it as a raw material of terephthalic acid.The invention is concerned with a process of producing high purity terephthalic acid, which is characterized in that a p-toluic acid recovery step of recovering p-toluic acid from a primary mother liquor and feeding it into an oxidation reaction step includes the following respective steps of: (I) an adsorption step of feeding, as a liquid to be treated, the primary mother liquor or a secondary mother liquor obtained by subjecting the primary mother liquor as cooled to solid-liquid separation into an adsorption tower filled with an adsorbing agent in which the breakthrough time of p-toluic acid is longer than the breakthrough time of benzoic acid to adsorb p-toluic acid and benzoic acid in the liquid to be treated to the adsorbing agent, (II) a feed stopping step of stopping the feed of the liquid to be treated into the adsorption tower at an arbitrary point of time of exceeding the breakthrough time of benzoic acid, (III) a desorption step of feeding a desorbing agent into the adsorption tower to desorb adsorbed p-toluic acid, and (IV) a circulation step of feeding p-toluic acid contained in the desorbing agent flown out from the adsorption tower into the oxidation reaction step.
Owner:MITSUBISHI CHEM CORP

Process for producing high-purity terephthalic acid

The life of a reduction catalyst to be used in a reduction step where 4CBA is reduced with hydrogen to p-toluic acid is prolonged. The process for producing high-purity terephthalic acid is characterized in that, in the reduction step, the ratio of the amount of hydrogen to be fed to a hydrogenation reactor to the amount of 4CBA in a solution thereof to be fed to the reactor, hydrogen / 4CBA, is from 2 to 10 (by mole) and that the ratio of the amount of crude terephthalic acid to be treated in the reduction step to the amount of the reduction catalyst present in the hydrogenation reactor, [amount of terephthalic acid being treated (t / h)] / [amount of reduction catalyst (t)], is from 400 to 5,000 (1 / h).
Owner:MITSUBISHI RAYON CO LTD

Method for recycling mother solid in PTA-refining wastewater

The invention discloses a method for recycling mother solid in PTA-refining wastewater, comprises the following steps: mixing PTA-refining wastewater and paraxylene in a prepositioned mixing tank, carrying out single-stage extraction and cooling on the wastewater, dissolving and extracting the solid in mother liquor into a PX phase, returning the extract phase PX discharged from a clarification tank to an oxidizing reaction system, and delivering the wastewater to an extraction tower to be subject to multistage countercurrent extraction; delivering the wastewater discharged from the bottom ofthe extraction tower to be subject to further treatment; and returning the extraction phase discharged from the top of the extraction tower to serve as extract liquor for single-stage extraction. By adopting the method in the invention, most of organic matters, such as p-toluic acid, terephthalic acid and the like in the wastewater can be recycled, thus the purpose of recycling wastes is achieved, and wasting of resources is avoided; and the invention omits the conventional filtering unit, saves the filter cloth-replacing cost, ensures that the extraction tower can operate at appropriate operating temperature, and has the advantages of investment saving, low energy consumption, high resource recovery rate and the like.
Owner:FUZHOU UNIV
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