1020 results about "Octanol" patented technology

Described are controlled, time-release microparticulate active and bioactive compositions (including perfuming compositions) for targeted delivery to services such as skin, hair and fabric and the environment proximate thereto, where the active and bioactive materials have a calculated log10P values of between 1 and 8 (P being the n-octanol-water partition coefficient). Such compositions include the active or bioactive material in single phase, solid solution in a wax or polymer matrix also having coated thereon and/or containing a compatible surfactant. Also described are processes and apparatus for preparing such compositions and processes for using same. Furthermore, certain component(s) of the aforementioned compositions in combination with one another are novel, and other components have novel uses in increasing fragrance substantivity.

It is intended to provide a transdermal absorption patch which is highly excellent in transdermal absorption properties and long-lasting drug effect even in the case where a drug-effect component contained in the transdermal absorption patch is a basic drug hardly soluble in a pressure-sensitive adhesive base, has a high stability of the drug contained therein with the passage of time and can achieve improvement in the compliance and simplification of the administration method. These problems can be solved by providing a transdermal absorption patch which contains a basic drug having an octanol/water partition coefficient (logarithm) in the free state of 3 or above, a pressure-sensitive adhesive base and a (meth)acrylic copolymer having carboxyl group.

Mixed alcohols can be used as a fuel additive in gasoline, diesel, jet fuel or as a neat fuel in and of itself. The mixed alcohols can contain C₁-C₅ alcohols, or in the alternative, C₁-C₈, or higher, alcohols in order to boost energy content. The C₁-C₅ mixed alcohols contain more ethanol than methanol with amounts of propanol, butanol and pentanol. C₁-C₈ mixed alcohols contain the same, with amounts of hexanol, heptanol and octanol. A gasoline-based fuel includes gasoline and the mixed alcohols. A diesel based fuel includes diesel and the mixed alcohols. A jet fuel includes kerosene and the mixed alcohols. The neat fuel of the mixed alcohols has an octane number of at least 109 and the Reid Vapor Pressure is no greater than 5 psi. The gross heat of combustion is at least 12,000 BTU's/lb.

The invention discloses a preparation method of an alumina porous microsphere. The preparation method comprises the following steps: 1) dissolving a surfactant in deionized water, stirring the solution, and using the solution as a water phase; 2) mixing a chelating agent, an alumina precursor and octanol, stirring the materials, and using the mixture as an oil phase; 3) adding Span80 and a pore-forming agent to the oil phase, and stirring the materials; 4) pouring the clear oil phase obtained in the step 3) into the water phase, and continuously stirring and emulsifying the materials; 5) carrying out vacuum filtration on the product obtained in the step 4), and washing and then drying the obtained filter cake, thus obtaining the alumina porous microsphere. The microsphere has an internally closed macroporous structure and has a microsphere dimension of 1-100mu m and an internally closed pore diameter of 50nm-5mu m.

An exemplary printable composition of a liquid or gel suspension of diodes comprises a plurality of diodes, a first solvent and/or a viscosity modifier. In other exemplary embodiments a second solvent is also included, and the composition has a viscosity substantially between about 100 cps and about 25,000 cps at about 25° C. In an exemplary embodiment, a composition comprises: a plurality of diodes or other two-terminal integrated circuits; one or more solvents comprising about 15% to 99.9% of any of N-propanol, isopropanol, dipropylene glycol, diethylene glycol, propylene glycol, 1-methoxy-2-propanol, N-octanol, ethanol, tetrahydrofurfuryl alcohol, cyclohexanol, and mixtures thereof; a viscosity modifier comprising about 0.10% to 2.5% methoxy propyl methylcellulose resin or hydroxy propyl methylcellulose resin or mixtures thereof; and about 0.01% to 2.5% of a plurality of substantially optically transparent and chemically inert particles having a range of sizes between about 10 to about 50 microns.

The present invention provides a method of producing a fluoropolymer aqueous dispersion by which the fluorine-containing emulsifier contained in the fluoropolymer aqueous dispersion as obtained after polymerization can be efficiently removed as well as a fluoropolymer aqueous dispersion low in fluorine-containing emulsifier concentration. The present invention is a method of producing a fluoropolymer aqueous dispersion which comprises carrying out a concentration treatment comprising a concentration operation of a pretreatment fluoropolymer aqueous dispersion, wherein the pretreatment fluoropolymer aqueous dispersion is obtained by carrying out a polymerization in an aqueous medium in the presence of a fluorine-containing surfactant (A), the fluorine-containing surfactant (A) is a fluorine-containing surfactant having an octanol/water partition coefficient of 1.5 to 3.5.

The invention discloses a method for producing mixed butanol and coarse octanol by using waste liquid discharged from an octanol device as a raw material, which belongs to a method for preparing acyclic monohydric alcohols, and is characterized by using a raw material fractionation unit, a hydrogenation synthesis unit and a product distillation unit, wherein the raw material fractionation unit comprises three fractionation devices: a butyraldehyde fractionation tower, a butanol fractionation tower and a C8 fractionation tower; the hydrogenation synthesis unit and the product distillation unit are suitable for hydrogenating and distilling a butyraldehyde fraction and a C8 fraction from the raw material fractionation unit alternately; and the product distillation unit comprises a light component removing tower device and a heavy component removing tower device. The method for producing the mixed butanol and coarse octanol by using the waste liquid discharged from the octanol device as the raw material, which is energy-saving and environmentally-friendly, can realize the recycling of the waste liquid discharged from the octanol device, reduce the waste water treatment cost of the octanol device and improves the technical indexes of treated water.

The invention relates to a lanthanum-modified nickel-copper octanol hydrorefining catalyst, preparation and application thereof. The catalyst is prepared by taking Gamma-Al2O3 as a carrier, taking lanthanum as an auxiliary agent, taking nickel-copper as a active component and adopting an immersion method; and the aluminum oxide accounts for 40-90%in the terms of 100% by mass, the content of nickel is 1-40% in the terms of NiO, the content of copper is 1-30% in the terms of CuO, and the lanthanum as the auxiliary agent is 0.1-10% in the terms of La2O3; and a hydrogenation evaluation result indicates that the catalyst is reduced at a temperature of 350-550 DEG C, and under the conditions that the reaction temperature is 120 DEG C, the reaction pressure is 2.5MPa, the volume ratio of hydrogen to liquid is 8:1 and the volume air speed is 3.0h<-1>, the hydrogenation rates of unsaturated substances such as octylene aldehyde, isooctyl aldehyde and octylene alcohol are all more than 95%.

A two-stage process for reclaiming the waste alkaline solution discharged by octanol synthesizing system includes "after-heat self-extracting" and "activated carbon adsorption" stages, that is, usingthe afterheat and inorganic acid to acidify the waste alkaline solution, extracting the organic components from waste solution by 2-ethylhexanol as the product of said octanol synthesizing system, adsorbing the residual phase by granular activated carbon, neutralizing by alkali, biochemical treating, and regenerating the used activated carbon. Its advantagesa re high effect etc.

Provided is a pharmaceutical composition for permeabilizing fetal membranes including an active ingredient having a log K in the range of 2 to 4, where K is the octanol/water partition coefficient. The active ingredient may be, for example, bupivacaine, sodium lauryl sulfate or oleic acid. Further provided is a system for transfetal membrane transport. The system includes a probe unit adapted for insertion into a female reproductive tract and releasing a substance onto fetal membranes that permeabilizes the membranes. The system is also configured to apply ultrasound radiation to the fetal membranes to further increase the membrane permeability.

The invention provides a composition of a surfactant oil displacement system for anionic and nonionic oil displacement. The composition consists of 18% C18 sodium alkyl benzene sulfonate, C16 fatty acid, 25% C2 alkanolamide, 7% C8 alkylphenol polyoxyethylene ether phosphate, 17% ethanol, 3% octanol, 30% water; the alkyl is a hydrocarbyl group with linear chain, branched chain and ring structures in a calibrated carbon atom range, and also can be substituted by one or more halogens, alkyls or alkoxys; the sodium sulfonates are formed by sulfonating different alkanes or arenes by SO3 or chlorosulfonic acid in chloroalkane environment and then neutralizing the sulfonate and sodium hydroxide; and the esterification derivatives are sulfates or phosphates. The formulation has highoil displacement efficiency, strong oil deposit adaptability and good popularization prospect.

The invention discloses a treatment process of 2-ethyl hexanol liquid waste. The treatment process is suitable for processing the 2-ethyl hexanol liquid waste discharged by a 2-ethyl hexanol device. The treatment process comprises the following steps: heating the 2-ethyl hexanol liquid waste to 60-100 DEG C and then leading to a middle section of a first rectifying tower; removing moisture and light components from the top of the first rectifying tower under the effect of an entrainer; enabling tower kettle liquid of the first rectifying tower to enter the middle section of a second rectifying tower, so as to obtain a butanol product of which the purity is greater than 98% from the top of the second rectifying tower; enabling the tower kettle liquid of the second rectifying tower to enter the middle section of a third rectifying tower; removing C5-C7 and an octenal component from the top of the third rectifying tower; and enabling the tower kettle liquid of the third rectifying tower to enter the middle section of a fourth rectifying tower, so as to obtain an octanol product of which the purity is greater than 98% from the top of the fourth rectifying tower. The treatment process does not need any fuel; butanol and octanol, of which the purity is greater than 98%, can be effectively recovered, so that the useful components in the 2-ethyl hexanol liquid waste can be fully utilized; the resources are saved; the environmental pollution is also reduced; the treatment process has good economical benefits and social benefits.

The invention discloses an octanol hydrorefining catalyst, which belongs to the field of hydrorefining catalytic materials. The prepared catalyst is used for modifying a carrier by using a rare earth element, reducing the amount of an active component of a nickel ion entering a carrier framework and improving the content of surface nickel species; the active component is loaded by adopting a hydrothermal deposition method, the dispersion of nickel salts on the surface of a carrier pore canal by using hydrothermal high-temperature and high-pressure conditions and forming nickel precipitation with proper size at the loading initial period of the active component by using a deposition reaction, so the invention can effectively control the amount of the nickel ions entering the carrier, improve the content of the surface nickel species and simultaneously can avoid the growth of nickel oxide particles; and the catalyst greatly increases the surface nickel active site, effectively improves the utilization rate of the active component of nickel and has higher catalytic reaction activity during hydrorefining the octanol at higher airspeed. The result shows that the hydrogenation rate of an unsaturated substance in crude octanol reaches over 90 percent when the temperature is 120DEG c, the pressure is 2.5MPa, the ratio of hydrogen to liquid for feeding is 8:1 and the airspeed is 30<-1>hour.

Hard surface cleaning compositions comprise: A. Surfactant, e.g., a nonionic ethoxylated alcohol; B. Solvent, e.g., propyleneglycol n-butyl ether; C. Low VOC, low odor, alkanolamine selected from the group consisting of tris(hydroxymethyl)amino methane; 2-amino-2-methyl-1,3-propanediol; 2-amino-2-ethyl-1,3-propanediol; 2-amino-2-methyl-1-propanol; N,N-dimethylamino-2-methyl-1-propanol; and 3-amino-4-octanol; D. Water, and E. Optionally, one or more of an alkaline agent, builder, fragrance, preservative, biocide, colorant, dye and rheology modifier.

The invention relates to production technology for cracking butyl octanol residual liquid into C4 and C8 by means of an alkaline liquid cracking agent. The technology is characterized by comprising the following steps of: preparing the alkaline liquid cracking agent, wherein the alkaline liquid cracking agent consists of sodium hydroxide, potassium hydroxide, water, isopropanol, ethylene glycol, potassium permanganate, ethanol, barium nitrate and diboron trioxide; preheating the alkaline liquid cracking agent and the butyl octanol residual liquid through a preheater and adding into a distilling still, wherein the tower bottom temperature of the distilling still is between 200 and 280 DEG C, the tower top temperature is between 130 and 190 DEG C, and the tower top pressure is between 0.08 and 0.1Mpa below zero; and extracting the C4 and C8 generated by cracking from the tower top of the distilling still, pumping the C4 and C8 into a fractionating column at the downstream for fractionation, and extracting a small amount of uncracked heavy components from a tower bottom pump. The production technology has the advantages of high production capacity, high cracking selectivity, high content of the cracked useful components, low cost, simple process, and batch distillation or continuous distillation.

The present invention is directed to a rinse-off conditioner composition for hair frizz reduction comprising from about 0.2% to about 20% of a moisture control material or mixture of moisture control materials wherein the moisture control material is selected from one or more of the following:

wherein R′ is —COOY, sulfonic acid, or C═CH—COOY, Y is hydrogen or a metal ion, R₁, R₂, R₃, R₄, R₅ is hydrogen, methyl, ethyl, propyl, vinyl, allyl, methoxy, ethoxy, hydroxyl, halogen, sulfate, sulfonate, nitro, or —CH═CH—COOR, and wherein the moisture control material is an acidic material and further wherein the moisture control material has a % Protein binding higher than 20 and Molecular Volume lower than 500 and Partition coefficient octanol to water (log P) lower than 3 and hydrogen binding higher than 10 and pKa lower than 5.0; and at least about a 4% fizz reduction vs. a control composition without the moisture control material.

The invention discloses a microencapsulated water-based fire retardant coating. The coating is prepared from an epoxy-modified water-based polyurethane emulsion, melamino-formaldehyde resin microencapsulated ammonium polyphosphate, polyurethane microencapsulated inorganic particles, hydroxyethyl cellulose, a dispersing agent, a defoaming agent, a mildewproof agent, n-octanol and water. According to the microencapsulated water-based fire retardant coating, a carbon source and an air source are subjected to resinification, the total adding amount of fire retardant is reduced, and due to that fact that too much fire retardant is added, physical damage to obtained materials is reduced; microencapsulation treatment is conducted on ammonium polyphosphate, hygroscopicity and water solubility of hydrophilic fire retardant are reduced, migration of APP is blocked, and the durability of the coating is increased; microencapsulation to inorganic filler is achieved, compatibility of the inorganic filler and a high polymer material is enhanced, the defects of being prone to agglomeration and migration are overcome, and the mechanical property of fire retardant composite material is improved; the obtained coating has the advantages of being green, environmentally friendly, efficiency, durable, stable, attractive and the like, and a related preparation method is simple and suitable for application and popularization.

The invention discloses a method for chlorine from solution of zinc sulfate, which mainly comprises the following: 1, a step of extraction, in which tributylamine is used as an extractant, kerosene or para-octanol is used as diluent, clear liquid of zinc sulfate is mixed with an organic phase for extraction, and chlorine in a water phase is transferred to an organic phase; 2, a step of back extraction, in which back extraction is performed by using ammonia water or solution of sodium hydroxide, chlorine in the organic phase is retransferred to the water phase, and the organic phase is recycled; 3, a step of organic phase regeneration, in which 5 to 10 percent solution of sodium hydroxide is mixed with the organic phase which ages after being used for a certain period of time in a ratio of 1:0.9 to 1:2.5, and the mixture is stirred by an electromagnetic siterr at a high speed for 8 to 15 minutes for regenerating the organic phase; and 4, a step of deoiling, in which raffinate is subjected to active carbon absorption or ultrasonic demulsification so as to remove the organic phase in the raffinate. In the invention, the organic phase and the raffinate can be used circularly, the dechlorination rate is over 85 percent, the electrolytic operation environment is improved, the process flow is simple, and the method can be used for dechlorinating solution of zinc sulfate from wet-method zinc smelting plants and can also be used for dechlorinating wastewater.

The invention discloses an extraction process for preparing electronic-grade cobalt sulfate from a cobalt-containing waste material, and relates to an extraction method for cobalt salt. The process comprises the following steps of: performing acidolysis; filtering and separating; removing iron and copper; preparing rough Co material liquid; removing impurities by P204 extraction; and separating Co and Ni by P507 extraction; and the process is characterized in that an N235 extracting agent is prepared from 8 to 12 volume percent of N235, 8 to 12 volume percent of 2-octanol and 76 to 84 volume percent of 206 solution oil; and the prepared N235 extracting agent is added into raffinate of the P204 extraction and is subjected to six stages of extraction, two stages of hydrochloric acid washing, six stages of washing, three stages of ammonia water washing and one stage of sulfuric acid washing. The process has good impurity removal effect; compared with the prior art, the process has the advantages that: one order of magnitude is reduced, particularly, impurities such as cadmium, lead and the like which are difficult to remove are removed by P204 extraction and the P507 extraction, and the impurities reach an extremely low degree. The process has short flow, the comprehensive recovery rate of cobalt is high and the production cost is lower than the average cost of the same domestic industry.

The invention discloses a liquid phase hydrogenation method for residual liquids of butanol and octanol. The liquid phase hydrogenation method is characterized by comprising the steps of firstly, carrying out fixed bed liquid catalytic hydrogenation reaction on the residual liquids of butanol and octanol, and then, rectifying and separating to obtain butanol and octanol, wherein a rectifying unit comprises a dehydrating tower, a butanol tower and an octanol tower. A catalyst for the hydrogenation reaction is composed of a carrier and active components, wherein the carrier is one of silicon dioxide and silica sol, the active components include Ni and Zn, Ni accounts for 10-50wt% of the total mass of the catalyst, and Zn accounts for 5-30wt% of the total mass of the catalyst; the catalyst is prepared by using a co-precipitation method. The catalyst used in the method is simple in component and preparation, the residual liquids of butanol and octanol are simple in treatment process and high in utilization ratio, and the purity of a product is high.