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384 results about "Precursor polymer" patented technology

Photosensitive resin compositions

A heat resistant negative working photosensitive composition that comprises
    • (a) one or more polybenzoxazole precursor polymers (I):
    • wherein x is an integer from about 10 to about 1000, y is an integer from 0 to about 900 and (x+y) is about less then 1000; Ar1 is selected from the group consisting of a tetravalent aromatic group, a tetravalent heterocyclic group, or mixtures thereof; Ar2 is selected from the group consisting a divalent aromatic, a divalent heterocyclic, a divalent alicyclic, a divalent aliphatic group that may contain silicon, or mixtures thereof; Ar3 is selected from the group consisting a divalent aromatic group, a divalent aliphatic group, a divalent heterocyclic group, or mixtures thereof; Ar4 is selected from the group consisting Ar1 (OH)2 or Ar2; G is an organic group selected from the group consisting groups having a carbonyl, carbonyloxy or sulfonyl group attached directly to the terminal NH group of the polymer;
    • (b) one or more photo-active compounds which release acid upon irradiation (PAGs);
    • (c) a latent crosslinker which contains at least two ˜N—(CH2OR)n units wherein n=1 or 2 and R is a linear or branched C1-C8 alkyl group, with the proviso that when a glycoluril is employed as the latent crosslinker, the G group in the polybenzoxazole precursor polymer is produced from the reaction of a cyclic anhydride; and
    • (d) at least one solvent that is not NMP.
Owner:FUJIFILM ELECTRONICS MATERIALS US

Method for preparing composite ceramic material through utilizing ceramic and precursor

The invention provides a method for preparing a composite ceramic material through utilizing ceramic and a precursor. The method comprises the steps that (1) ceramic powder and the precursor are mixed uniformly; (2) the mixture material is solidified, wherein the solidifying temperature is between 120 and 500 DEG C, and the thermal insulation time is between 0.5 and 10 hours; (3) the solidified product is subjected to die pressing so as to preform a body, and then, the body is further densified through isostatic pressing; (4) the body is subjected to net final dimension processing through adopting a mechanical processing mode; and (5) the processed product is sintered in a sintering furnace, so that the composite ceramic product is finally obtained, wherein the sintering pressure is between 100 pascals and 10 mega pascals, the sintering temperature is between 1600 and 2200 DEG C, and the sintering time is between 0.5 and 10 hours. A precursor polymer has plasticity and plays a role of a 'plasticizer' during the body forming process; and moreover, the 'plasticizer' can be directly converted into a component which is required by composite ceramic through cracking during the subsequent high-temperature processes, other impurities cannot be brought in, and the dispersion of all the components can be effectively improved.
Owner:AEROSPACE RES INST OF MATERIAL & PROCESSING TECH +1

Synthetic fiber nonwoven web and method

A nonwoven web and method of preparing a novel nonwoven web of synthetic fiber are disclosed. An aqueous solution amide crosslinked synthetic precursor polymer is extruded under defined conditions through a plurality of die orifices to form a plurality of threadlines. The threadlines are attenuated with a defined primary gaseous source to form fiber under conditions of controlled macro scale turbulence and under conditions sufficient to permit the viscosity of each threadline, as it leaves a die orifice and for a distance of no more than about 8 cm, to increase incrementally with increasing distance from the die, while substantially maintaining uniformity of viscosity in the radial direction, at a rate sufficient to provide fiber having,the desired attenuation and mean fiber diameter without significant fiber breakage. The attenuated threadlines are dried with a defined secondary gaseous source. The resulting fibers are deposited randomly on a moving foraminous surface to form a substantially uniform web. The moving foraminous surface is positioned about 10 to about 100 cm from the last gaseous source to contact the threadlines. The fibers have a mean fiber diameter in the range of about 0.1 to 30 mum and are substantially free of shot. The attenuating and drying steps are carried out under conditions of controlled macro scale turbulence.
Owner:KIMBERLY-CLARK WORLDWIDE INC
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