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43results about How to "Good spinnability" patented technology

Method for preparing mesophase pitch through catalytic cracking oil slurry hydrogenation reduction and co-carbonization

ActiveCN105238431ALow mesophase contentHigh content of mesophaseWorking-up pitch/asphalt/bitumen by chemical meansCarbonizationSlurry
The invention provides a preparation method of petroleum base mesophase pitch with even high mesophase content. The FCC oil slurry of naphthenic crude oil or intermediate base crude oil serves as the raw material, under the action of a catalyst, haloalkane is mixed with the raw material, the temperature is increased to range from 280 DEG C to 350 DEG C, the pressure ranges from 0 MPa to 2 MPa, reaction is conducted for 5-20 h, and modified oil is obtained. Distillate oil, obtained at the temperature higher than 400 DEG C, of the modified oil is taken, the distillate oil is mixed with a co-carbonization agent, the temperature ranges from 360 DEG C to 480 DEG C, the reaction pressure ranges from 4 MPa to 10 MPa, reaction is conducted for 2-10 h, and the high-quality mesophase pitch is obtained. According to the preparation method of the petroleum base mesophase pitch with the even high mesophase content, preparation technology is simple and easy to operate, the anisotropic structure of the prepared mesophase pitch is uniform, the mesophase content is high and larger than 96 percent, the softening point is low, the temperature ranges from 240 DEG C to 260 DGE C, and the spinnability is good.
Owner:CHINA UNIV OF PETROLEUM (EAST CHINA)

Production method of normal-pressure cation dyeable copolyester endless tow, chopped fiber and top wool

The invention relates to a production method of normal-pressure cation dyeable copolyester endless tow, chopped fiber and top wool. The normal-pressure cation dyeable copolyester endless tow is obtained by spinning normal-pressure cation dyeable copolyesters. A preparation method of the normal-pressure cation dyeable copolyesters comprises the following steps of: (1) carrying out an esterification reaction on ethylene glycol, terephthalic acid and m-phthalic acid; (2) adding ethylene glycol, mixing, adding an SIPE (5-Sodium Sulfonate Isophthalate Ethyl-ester) solution and carrying out an ester exchange reaction; and (3) adding a mixture obtained in the ester exchange reaction into binary fatty acid, mixing uniformly, and carrying out a condensation polymerization reaction to obtain the normal-pressure cation dyeable copolyesters, wherein the molar ratio of the terephthalic acid to the m-phthalic acid is 50:1-90:1; the ratio of the mole number of the ethylene glycol added in the step (2) to the total mole number of the terephthalic acid and the m-phthalic acid is 0.1:1-0.5:1; and the ratio of the total mole number of the terephthalic acid, the m-phthalic acid and the binary fatty acid to the total mole number of sulfonic acid groups in the SIPE solution is 9:1-28:1.
Owner:JIANGSU JIANGNAN HIGH POLYMER FIBER

Preparing method for ablation-resistant high-ortho phenolic fibers

The invention discloses a preparing method for ablation-resistant high-ortho phenolic fibers. A phenolic compound and formaldehyde are mixed according to a certain proportion, then a certain amount of citric acid as a catalyst is added, and a boiling reaction is carried out for 0.5-4 h; diluted concentrated sulfuric acid is added, and the reaction continues for 30-50 min; decompression and dehydration are carried out for 0.5-2.9 h, boric acid accounting for 1-8% by mass is added for a modification reaction after the temperature reaches 90-97 DEG C, and boiling is carried out for 2 h at the constant temperature; decompression and dehydration are carried out, and dehydration is stopped when the temperature of resin reaches 110 DEG C; the resin is subjected to melt spinning at 120-160 DEG C; nascent fibers are put into a prepared curing solution, the temperature is increased to 95 DEG C gradually from the room temperature, and the nascent fibers are naturally cooled to the room temperature after constant temperature is achieved; the temperature is gradually increased for thermosetting under the nitrogen condition. The fiber strength of the high-ortho phenolic fibers ranges from 3 cN/dtex to 36 cN/dtex, the modulus ranges from 40 cN/dtex to 400 cN/dtex, and the cross-linking degree ranges from 32% to 38%.
Owner:ZHONGYUAN ENGINEERING COLLEGE

Processing method of fibers for grid type purse net fishing net

The invention provides a processing method of fibers for a grid type purse net fishing net. The processing method is characterized by comprising the following steps: pre-mixing UHMWPE (Ultrahigh Molecular Weight Polyethylene) powder, silicone powder, nano silicon dioxide, HDPE (High-density Polyethylene) powder, a nano titanium dioxide silver-loaded antibacterial agent, an antioxidant B225, hydroxystearic acid, nano-grade diatomite, nano-grade white carbon black, nano-grade wollastonite and an ethylene-vinyl acetate copolymer, which are weighed according to a formula, and pouring the mixture into a high-speed kneading pot and carrying out high-speed kneading to obtain a UHMWPE modified material; fusing and extruding the UHMWPE modified material through a double-screw-rod extruder; fusing and extruding an extruded product from a spinneret hole through a metering pump which is additionally arranged on a double-screw-rod outlet; cooling, pre-stretching and hotly setting extruded freshly formed filaments and winding a fiber bundle through a fiber winding machine which utilizes a torque motor; dividing the fiber bundle into fibers through a fiber dividing machine, so as to obtain the fibers for the grid type purse net fishing net.
Owner:EAST CHINA SEA FISHERIES RES INST CHINESE ACAD OF FISHERY SCI

Special-shaped cross section viscose filament yarn and preparation method thereof

The invention provides a special-shaped cross section viscose filament yarn, wherein the cross section of the special-shaped cross section viscose filament yarn is in a C shape, and the special-shaped cross section viscose filament yarn has degree of hollowness of 20-65%, dry breaking strength of more than or equal to 2.00cN/ dtex, wet breaking strength of more than or equal to 0.90cN/ dtex, dry stretch rate of more than or equal to 19.0% and twist variation coefficient of more than or equal to 11.00%. The invention also provides a preparation method of the special-shaped cross section viscose filament yarn; the preparation method is characterized by comprising a spinning viscose preparation step; a viscose denaturant is added in the spinning viscose preparation step, and the amount of the added viscose denaturant is 0.2-5wt% of that of alpha cellulose in viscose. The special-shaped cross section viscose filament yarn can be produced without purchasing a special-shaped spinning jet, so that the utilization rate of the spinning jet is increased, and the production cost in a spinning exchange process is lowered. The special-shaped cross section viscose filament yarn is widely used for making underwear, clothing, home textiles, imitated silk fabric products and the like.
Owner:潍坊欣龙生物材料有限公司
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