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1030results about How to "Low acid value" patented technology

Mono-component aqueous metal baking paint and preparation method thereof

The invention discloses a mono-component aqueous metal baking paint and a preparation method thereof. The mono-component aqueous metal baking paint consists of the following components by weight: 40 to 57 percent of tap water, 28 to 34 percent of aqueous acrylic modified polyester resin, 7 to 8.5 percent of amino resin, 1.12 to 1.36 percent of amine modifier, 0.1 to 0.3 percent of wetting dispersing agent A, 0.1 to 0.3 percent of wetting dispersing agent B, 0.01 to 0.1 percent of defoaming agent, 0.5 to 1.2 percent of thickening agent, and 0.2 to 0.6 percent of levelling agent. The mono-component aqueous metal baking paint uses water as a solvent without adding an alcohol / ether cosolvent so that environmental protection is excellent; because of mono-component, the construction is simple and convenient, and the performance is stable; and a paint film is plumpy, the luster is high, the mechanical property is excellent, and the adhesive force is good. The mono-component aqueous metal baking paint is applicable to metal surface corrosion protection and decoration, and can be used as a finishing paint, a priming paint or a coating varnish; and when used for bottom surface integral coating, the mono-component aqueous metal baking paint still has excellent surface effect and protective action.
Owner:GUANGZHOU JOINTAS CHEM

Method for preparing biodiesel by lowering value of high acid palm oil

The invention provides a method which uses palm oil to prepare biologic diesel oil and can lower the high acid value. The method uses solid super acids of SO>4<2- > / ZrO2, SO4< 2- > / TiO2, and SO4< 2- > / xZrO<2- yTiO2 as catalyst, and uses low-carbon alcohol as esterifying agent to pre-treat the high acid value palm oil, can effectively lower the acid value of the oil, and can ensure the acid vale of the obtained biologic diesel oil to easily meet the standard (less than 0.8mgKOH / g, ASTM). The catalyst used by the invention has high catalytic activity, and is reusable. The process flow is simple, the production cost is decreased, and the environmental pollution is reduced greatly.
Owner:SICHUAN UNIV

Method for preparing polyol ester lubricating oil by using composite solid acid catalyst

The invention relates to a method for preparing polyol ester lubricating oil by using a composite solid acid catalyst. The method comprises the following steps of: adding a water carrying agent into polyol ester and monobasic fatty acid, performing esterification reaction under the action of the composite solid acid catalyst, and dehydrating and esterfying to obtain raw ester; performing filter pressing on the raw ester to separate the raw ester from the solid acid catalyst, wherein the catalyst can be recycled; and performing reduced pressure distillation on the raw ester to remove the residual fatty acid, and then deacidifying and decolorizing to refine with heating by using a refining adsorption bed layer respectively to obtain low-acid value polyol ester lubricating oil. The method has the advantages that the catalyst can be recycled, the esterification rate is high, an aftertreatment process is simple, and a product is low in acid value, high in purity, environment-friendly and suitable to be produced industrially. The reaction esterification rate can reach over 99 percent, and the acid value of the ester product obtained through refining can be controlled to be less than 0.01mg KOH/g. The product is excellent in visco-temperature performance, high in lubricity and thermal stability, strong in hydrolytic stability, low in volatility and excellent in electrical insulation property.
Owner:SHAANXI RES DESIGN INST OF PETROLEUM CHEM IND

Method for preparing acrylic aqueous dispersion with hydroxyl through two-step polymerization

InactiveCN101649098ALow acid valueReduce Amine Neutralizer DosageSolventWater resistance
The invention provides a method for preparing acrylic aqueous dispersions with hydroxyl through two-step polymerization and the method comprises the synthesis of hydroxy acrylic resin, the removal ofsolvent, the neutralization and salt-formation and the deionized water dispersion, wherein the synthesis of hydroxy acrylic resin adopts two-step feeding synthesis method instead of one-step feeding method in prior art, the composition of the first added monomer mixture is different from that of the second added monomer mixture and preferentially, the weight percent of the second added hydrophilicmonomer is higher than that of the first added monomer when feeding tends to end up. The aqueous dispersions obtained by the technical solution of the invention reduces the dosage of monomer with hydroxyl so as to increase the water resistance of coating which is formed by combining aqueous dispersions and curing agent, reduce the grain size of dispersions, lower the viscosity and increase the stability obviously.
Owner:ZHEJIANG HUANDA PAINT IND GROUP +1

High-acid value rice bran oil esterification depickling process

The invention relates to an esterification deacidification process for high acid number rice bran oil, and the process can well solve the problem of a low refining rate. The esterification deacidification process for high acid number rice bran oil comprises grease pretreatment, namely two steps of degumming and decolorizing. A decolorized substance is obtained after the decolorizing, and then esterification deacidification is carried out. The concrete operating method comprises the following steps of: adding glycerin after the decolorized substance is stirred and heated at a vacuum degree of 0.09 MPa; adding a catalyst of zinc oxide or zinc to carry out a catalytic reaction to generate low acid number rice bran oil with an acid number of 5-7mgKOH / g. The zinc oxide or zinc which is taken as the catalyst of the esterification deacidification of the high acid number bran oil can effectively boost the esterification reaction and rapidly reduce the acid number; simultaneously the process overcomes the problems of the low refining rate lying in a traditional refining method and a great deal of sewage produced by a chemical alkali refining method; the zinc oxide or zinc has a low price, thereby reducing production cost; compared with other chemical esterification catalysts, the zinc oxide or zinc has a very low toxity, thereby being very suitable for the production of edible grease.
Owner:HEFEI UNIV OF TECH

Nano-size incombustible polyether polyol polymer and its preparing process and application

A nano-size (10-200 nm) incombustible polyether polyol polymer (MPP) is prepared through dispersing or locally grafting tripolycyanamine, cyanoguanidine and formaldehyde on high-activity polyether polyol at 40-160 deg.C for 5-16 hr. Said MPP has viscosity lower than 2300 MPa.s / 25 deg.C and density of 1.120-1.126g / ml, and can be used along with high-activity polyether polyol and assistant to prepare high-resilience foam polyurethane plastics.
Owner:朱吕民

Preparation method of diethyl succinate

The invention discloses a preparation method of butane diacid dimethyl ester. The preparation process comprises the following steps of: (1) the rate of raw materials and a catalyst and dosage quality rate thereof is: butane diacid : industrial ethanol : absolute ethyl alcohol : the catalyst is equal to 1 : 0.8 to 1.1 : 0.1 to 0 : 0.01 to 0.02; 1) putting butane diacid, industrial ethyl alcohol of 20 percent of total amount and the catalyst into an esterification kettle and increasing temperature to 120 DEG C; 2) inputting residual industrial ethanol continuously for 8 hours to 9 hours, maintaining the temperature of the kettle at 115 DEG C to 120 DEG C and the temperature of the top of distillation device less than 105 DEG C; 4) sampling to detect acid value and inputting absolute ethyl alcohol when the acid value is 40mgKOH / g to 48mgKOH / g; 5) sampling to detect acid value after an hour and stopping heating when the acid value is 10mgKOH / g to 15mgKOH / g; 6) reducing the temperature to 80 DEG C after ethyl alcohol is withdrawn from the kettle by opening vacuum; 7) separating the catalyst from the materials cooled to 80 DEG C and putting the catalyst into an alkaline washing kettle; 8) inputting alkali solution of proper amount and mixing for 20 minutes to 40 minutes under temperature of 60 DEG C to 70 DEG C; 9) placing stilly for layering and emitting the lower water layer; 10) adding crude product after the alkaline washing into a rectification kettle, raising the temperature to 150 DEG C to 170 DEG C and dehydrating; 11) opening vacuum and collecting distillate of 160 DEG C to 190 DEG C which is the final product.
Owner:SHENZHEN FEIYANG IND CO LTD

Fluorene-based resin polymer and photo-sensitive resin composition comprising the same

ActiveUS20120196949A1Excellent adhesive propertyGood develop propertyImpression capsPhotomechanical apparatusPolymer chemistryFluorene
The present invention relates to a fluorene-based resin polymer, and a photosensitive resin composition including the same, and the fluorene-based resin polymer according to the exemplary embodiment of the present invention has a high molecular weight, a low acid value, and excellent developing property, adhesive property and stability.
Owner:LG CHEM LTD

Special lubricating oil for fuel gas engine of public transport automobile

The invention discloses special lubricating oil for a fuel gas engine of a public transport automobile. The special lubricating oil is prepared from blended base oil, binary ethylene-propylene rubber, polymethacrylate, alkylphenol calcium sulfide, high-base-number calcium alkylbenzenesulfonate, polyisobutylene succinimide, boronated polyisobutylene succinimide, alkylated phenyl-alpha-naphthylamine, p,p'-dioctyl diphenylamine, a hindered phenol type antioxidant, dialkyl molybdenum dithiocarbamate, copper nanoparticle anti-wear additives, methyl silicone oil and thiadiazole polysulfide. According to the lubricating oil composition oil product, the sulfate ash content is lower than 0.5%, the content of phosphorus is lower than 0.03%, and the base number is 3-8mgKOH/g. According to the special lubricating oil for the fuel gas engine of the public transport automobile, aiming at the special requirements of the public transport automobile on engine oil, different additive varieties and charging sequences are adopted, so that physical and chemical indicators and use performance of the special lubricating oil are better than natural gas engine lubricating oil of the same grade, and the special lubricating oil has excellent cleaning and dispersion properties, lubricating property, abrasion resistance and oxidation resistance.
Owner:陕西通用润滑科技有限公司

Method for preparing SIPE from SIPA by direct esterification method

The invention discloses a method of preparing m-phthalic acid diglycol ester-5-sulphonate by directly esterifying m-phthalic acid-5-sulphonate. The m-phthalic acid-5-sulphonate (SIPA) and glycol (EG) are used as raw material and are directly esterified to prepare the m-phthalic acid diglycol ester-5-sulphonate (SIPE); the esterification rate is more than 99 percent, the acid value is less than 1(mgKOH/g), and the content of diglycol (DEGA) is less than 2.0 percent. Therefore, the m-phthalic acid diglycol ester-5-sulphonate (SIPE) which is manufactured by adopting the method is almost esterified completely; the disadvantages of high equipment investment, high recovery cost of methanol, and going against environment protection are elminated when the m-phthalic acid diglycol ester-5-sulphonate (SIPE) is prepared by using dimethyl-m-phthalate-5-sulphonate (SIPM) through an interesterification method; the m-phthalic acid diglycol ester-5-sulphonate (SIPE) has the characteristics of low acid value, high purity, less byproducts, etc.; the m-phthalic acid diglycol ester-5-sulphonate (SIPE) is used as a dye modifier or a third monomer and is added in polyester, so that the mass-producing demand is achieved; the method is a preparation method with stable way and excellent quality.
Owner:厦门翔鹭化纤股份有限公司

Technological process of preparing biological diesel oil with vegetable oil niger

The present invention is technological process of preparing biological diesel oil with vegetable oil niger, and features that vegetable oil niger is prepared into biological diesel oil through acidifying with 50 % concentration sulfuric acid solution to obtain acidified oil, adding methanol to react and separating out esterified resultant, adding 20 % concentration methanol solution to obtain crude methyl fatty ester product, molecular distilling the crude methyl fatty ester product to obtain light methyl fatty ester component as the biological diesel oil product with purity up to 95 %. The present invention adopts twice esterification to convert high acid value oil into methyl fatty ester and molecular distilling to refine, and has raised reaction efficiency, short reaction time, product purity over 98 %, recovery of side product glycerin and low technological cost.
Owner:HEFEI UNIV OF TECH

Method for preparing low acid-value fatty acid methyl ester

The invention relates to a method for synthesizing low acid-value fatty acid methyl ester by esterification reaction and aims at providing the method with the characteristics that a process is simple; a catalyst and a product are easy to separate and can be recycled; the reaction conversion rate is high; and the obtained fatty acid methyl ester has low acid value. The method for preparing the lowacid-value fatty acid methyl ester sequentially comprises the following steps of: 1, feeding fatty acid and a resin catalyst together or feeding the fatty acid and a solid acid catalyst together, andthen heating the mixture with stirring; 2, after a temperature of a reaction system is raised to 50 to 80 DEG C, dropwise adding methanol into the reaction system, distilling the methanol and water generated in the reaction process, sampling and monitoring the reaction conversion rate in the reaction process and finishing the reaction until the acid value reaches below 0.5mgKOH/g, wherein the pressure of the reaction system is in the range of 10 to 101Kpa and the reaction time is in the range of 4 to 6 hours; and 3, after finishing the reaction, filtering out the catalyst, carrying out reduced pressure distillation on filtrate to separate out excessive methanol and water to obtain a finished product and directly recycling the resin catalyst or the solid acid catalyst.
Owner:ZANYU TECH GRP CO LTD

Method for preparing maize germ oil through enzymatic degumming

The invention relates to a method for preparing maize germ oil through enzymatic degumming. Specifically, phosphatidase is employed for a degumming treatment of maize crude oil during the refining process. Then after deacidification, decoloration, dewaxing and deodorization, refined maize germ oil can be obtained. Wherein, the degumming treatment comprises acid reaction, alkali neutralization, enzyme reaction, and separation, dehydration and drying; the acid in the acid reaction is citric acid, and the enzyme in the enzyme reaction is phosphatidase. In the invention, the key technology for maize germ oil refining is overcome, and the optimum technological conditions for the enzymatic degumming of maize germ oil are optimized. The maize germ oil prepared through enzymatic degumming has the obvious advantages of: low operation temperature and low energy consumption; obviously superior quality of the obtained oil to the quality of oil prepared by traditional methods, and increased product oil yield by over 1%; reduced consumption of acid and alkali chemicals, and reduced waste water generation by 70%-90%, substantially reduced environmental protection cost and markedly improved economic benefit.
Owner:SHANDONG XIWANG FOOD
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