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443 results about "Benzole" patented technology

In the United Kingdom, benzole or benzol is a coal-tar product consisting mainly of benzene and toluene. It was originally used as a 'motor spirit', as was petroleum spirits. Benzole was also blended with petrol and sold as a motor fuel under trade names including "National Benzole Mixture" and "Regent Benzole Mixture".

Preparation process of benzoyl chloride

The invention discloses a preparation process of benzoyl chloride. The preparation process comprises the following steps of synthesis of benzotrichloride: carrying out temperature reaction on methylbenzene and chlorine under the catalytic action of a catalyst to synthetize a crude benzotrichloride product; synthesis of the benzoyl chloride: continuously stirring and heating the crude benzotrichloride product and benzoic acid to prepare a crude benzoyl chloride product after adding the catalyst; refining of the benzoyl chloride: carrying out reduced pressure distillation on the crude benzoyl chloride product to prepare a refined benzoyl chloride product; recovering benzoyl chloride raffinate, adding water to the benzoyl chloride raffinate which is subjected to the reduced pressure distillation, heating and stirring to transform the benzoyl chloride contained in the raffinate into the benzoic acid, cooling, then separating out benzoic acid. The preparation process disclosed by the invention is easy to safe to operate, effectively shortens the reaction time, achieves the purity of the prepared benzoyl chloride by 99.5%, reduces the environmental pollution by recycling residues, saves the resources, reduces the cost, meets the requirements of pharmaceutical chemicals and can carry out massive industrial production.
Owner:YIDU YOUYUAN IND CO LTD

Anticorrosive environment-friendly spray paint formula

The invention discloses an anticorrosive environment-friendly spray paint formula, and relates to the field of chemical industries. The anticorrosive environment-friendly spray paint formula comprises the following components in parts by weight: 28 to 35 parts of glacial acetic acid, 3 to 7 parts of organic fluorine epoxy resin, 7 to 12 parts of epoxy modified organic silicon resin, 2 to 6 parts of glycol monomethyl ether, 6 to 9 parts of dimethyl sulfoxide, 8 to 13 parts of zinc phosphate, 8 to 13 parts of barium chromate, 1 to 4 parts of ethanol, 2 to 7 parts of polyacrylate, 1 to 4 parts of alcohol soluble resin, 7 to 13 parts of diacetone alcohol, 6 to 9 parts of zinc oxide, 8 to 13 parts of toluene diisocynate, 3 to 7 parts of n-butyl acetate, 12 to 16 parts of benzophenone, 9 to 13 parts of triethanolamine and 3 to 7 parts of diphenyl polysiloxane. The paint is bright in color and good in air-curing resisting effect, can substitute medium chrome yellow in inorganic pigment, is applicable to the outer wall paint, and has no harm of heavy metals, no harmful substances, good environment protection effect, little odor, no peculiar smell after being smeared on the wall, good mechanical performance, excellent electric insulation performance, dampness and water resistance, rust and cold resistance and ozone aging resistance.
Owner:王海平

Fine purification system and method for carbonization crude benzol

The present invention relates to a refining system of coked crude benzole and a refining method thereof. The basic equipment consists of two benzene towers, a primary tower, a first pure benzene tower, a second pure benzene tower, a toluene tower and a xylene tower. The heat of the reboiler of the primary tower comes from toluene vapor on the top of the toluene tower; the heat of the reboiler of the first pure benzene tower comes from the pure benzene vapor on the top of the second pure benzene tower. The refining method comprises pre-distillation, refining of the pure benzene and separation of the toluene and the xylene. The method not only saves energy but also reduces the cost of investment. The process is simplified. Compared with the traditional sulfuric acid washing process, the method eliminates the acid-alkali washing and benzene blowing processes. The whole process generates no waste acid, acid residue, caustic dross or waste water, which can cause serious damage to the environment. Compared with the catalytic hydrogenation, the method has the advantages of simplifying the process, lowering the energy consumption, reducing the cost of investment and production, and improving the benefit of production, and thus being an excellent method for steel enterprises and coking enterprises to further process and make use of by-products.
Owner:天津凯赛特科技有限公司

Method for refining carbonization crude benzole

The present invention relates to a refining method of coking crude benzol. The method has four following sequential steps as follows: thepretreatment process of raw materials, the refining process of doffing non-arene and doffing othiophene, the deep desulfurization process of thiophene alkyl, and the refining process of toluene and xylene. The products of high-purity sulfur-free benzene, toluene and xylene can be made. The detailed technological process can be referred to the specification munual. Compared with the traditional pickling method, the present invention has the following advantages: the whole process has no production of acid tar, no serious pollution to the environment and no serious corrosion of equipment; at the same time, the present invention avoids sulfonate loss of arene, effectively improves the reclamation rate of arene and belongs to an environmental friendly technology. Besides, the products of coking benzene category are obviously superior in quality to the traditional pickling. Compared with the catalytic hydrogenation process, the process is simple and not only can save a substantial amount of investment costs, but also the operation cost of device is low. The quality of benzene products is equivalent to hydrogenated benzene. The present invention provides an environmentally protective and economical process for the reasonable development and utilization of coking benzene resources, and has quite broad application prospects.
Owner:BEIJING INSTITUTE OF PETROCHEMICAL TECHNOLOGY

Pillar aromatic hydrocarbon and pillar aromatic hydrocarbo-like compound with aggregation-induced emission effect as well as preparation method and application thereof

ActiveCN112079684AExcellent aggregation-induced luminescence effectHigh quantum yieldOrganic non-active ingredientsHydrocarbonsImidePharmaceutical drug
The invention provides a pillar aromatic hydrocarbon and pillar aromatic hydrocarbon-like compound with an aggregation-induced emission effect as well as a preparation method and application thereof.The pillar aromatic hydrocarbon and the pillar aromatic hydrocarbon-like compound have the following structural general formula, or in the structural general formula, R1 is equal to OCH2CH2Br or H; and R2 is equal to OCH2CH2Br or H. The preparation method comprises the following steps: reacting a compound 1 with N-bromo succinimide to obtain a compound 2; then carrying out oxidation reaction to obtain a compound 3, and reacting the compound 3 with benzophenone to obtain the pillar aromatic hydrocarbon and pillar aromatic hydrocarbon-like compound 4 shown in a formula (a); and if the compound 3reacts, obtaining a compound 5 shown as a formula (b). The obtained pillar aromatic hydrocarbon and pillar aromatic hydrocarbon-like compound has an excellent AIE effect, contains a plurality of recognition sites and an electricity-rich cavity, can realize accurate fluorescence regulation and control by utilizing the AIE effect and supramolecular assembly of the pillar aromatic hydrocarbon and pillar aromatic hydrocarbon-like compound, and has wide application in the fields of nano-drug delivery, diagnosis and treatment and the like.
Owner:NANJING UNIV OF AERONAUTICS & ASTRONAUTICS

Preparation method of ultraviolet absorbent intermediate etocrilene (ETO)

The invention relates to a preparation method of an ultraviolet absorbent intermediate etocrilene (ETO). The preparation method comprises the following steps of: 1, adding benzophenone, ethyl cyanoacetate, a catalyst and a water-insoluble solvent into a condensation reaction kettle, carrying out backflow water distribution reaction for 12-15h, and then, cooling to 50-55 DEG C, wherein the excessive equivalent of the ethyl cyanoacetate relative to the benzophenone is 0.2-5; 2, washing the reaction liquid by using water, and separating the liquid to respectively obtain a water layer and an organic layer; distilling the recycled water at the water layer at normal pressure, dissolving distillation tailings by using a solvent same as the solvent used in the step 1, and then, replenishing a proper quantity of catalyst to obtain a product, wherein the distilled recycled water is used in the step 2, and the product is used in the step 1; and distilling the recycled solvent at the organic layer at normal pressure, and carrying out reduced pressure distillation to recycle the excessive ethyl cyanoacetate, wherein the recycled solvent and ethyl cyanoacetate are used in the step 1; 3, carrying out reduced pressure distillation on the distillation tailings, adding 75-100% of ethanol for crystallizing, and filtering to obtain the etocrilene; and 4, filtering a mother solution obtained in the step 3, recycling the ethanol at normal pressure, and carrying out reduced pressure recycle on the benzophenone and the etocrilene, wherein the recycled ethanol is used in the step 3, and the recycled benzophenone and etocrilene are used in the step 1. The preparation method has the advantages of simplicity in operation, short production period, little environment pollution, low energy consumption, realization of material recycling, and the like.
Owner:ANHUI SHENGNUOBEI CHEM TECH

Method for measuring distillate quantity of crude benzole before 180 DEG C

The invention discloses a method for measuring distillate quantity of crude benzol before 180 DEG C. The method comprises the following steps of: 1, selection of a measuring device; 2, selection of a chromatographic column: for the analysis of the benzene serial matters, the ratio of a fixation fluid Apiezon L to a supporter(6201) is 10 percent, and the length of the chromatographic column is 3m; 3, calculation of components of the crude benzol: the area normalization method is selected for calculation; 4, apparatus conditions: the column temperature is the temperature programming and is raised from 140 to 180 DEG C, the vaporizing and the conversion temperatures are 180 DEG C, the carrier gas and the fuel gas are highly purified hydrogen gas, the pressure of the hydrogen gas is 0.20MPa, the pre-column pressure is 0.05MPa, the air pressure is 0.20MPa, and the sample size is 1.5 microliter; and 5, a large number of qualitative and quantitative analysis tests on the crude benzol according to the conditions: the benzene serial matters are completely distilled before 5 minutes, and the calculation method adopts that the distillate quantity (percent) of the crude benzol before 180 DEG C is equal to 100 minus the summation of area percents of all chromatographic peaks after 5 minutes.
Owner:新疆八一钢铁股份有限公司炼钢厂
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