Abstract A flame resisting agent to be incorporated into an aqueous spinning dope containing chlorine-containing polymer as a main polymer ingredient for improving the flame resistant property of the fiber spun from the spinning dope which includes a stannic oxide hydrate being substantially amorphous with respect to X-ray diffraction and having a bound water in the range of about 0.5 to about 0.7 mole of H 2 O per 1 mole of SnO 2 . The flame resisting agent has a superior dispersibility in an aqueous spinning dope containing chlorine-containing polymer as a main polymer ingredient and the aqueous spinning dope in which the flame resisting agent is incorporated has a superior stability, filtering property and spinning property to give a uniform quality of fibers having a durable, superior flame resistant property.
A process for preparing stannic oxide hydrate substantially amorphous with respect to X-ray diffraction and having bound water in the range from about 0.5 to about 0.7 mole of H 2 O per 1 mole of SnO 2 which comprises a. forming a slurry containing β-stannic acid having a free water content of not more than 70% by weight, b. adjusting the slurry to a pH in the range of from about 2 to about 4.5, c. heating the slurry to a temperature in the range from 80° C. to 130° C. in an atmosphere having a humidity of not less than 0.5 kg. of steam/1 kg. of dry air, and d. recovering the resulting stannic oxide hydrate product, the product having a free water content of from 5% to 25% by weight and bound water in the range from about 0.5 to about 0.7 mole of H 2 O per 1 mole of SnO 2 .
Claim 2
Dependent Claim
157 words
A process for preparing stannic oxide hydrate substantially amorphous with respect to X-ray diffraction and having bound water in the range from about 0.5 to about 0.7 mole of H 2 O per 1 mole of SnO 2 which comprises a. forming a slurry containing β-stannic acid having a free water content of not more than 70% by weight, b. adjusting the slurry to a pH in the range of from about 2 to about 4.5, c. heating the slurry to a temperature in the range from 80° C. to 130° C. in an atmosphere having a humidity of not less than 0.5 kg. of steam/1 kg. of dry air, and d. recovering the resulting stannic oxide hydrate product, the product having a free water content of from 5% to 25% by weight and bound water in the range from about 0.5 to about 0.7 mole of H 2 O per 1 mole of SnO 2 .
Claim 3
Dependent Claim
18 words
The process of claim 1, wherein said β-stannic acid is prepared by oxidizing metallic tin with nitric acid.
Claim 4
Dependent Claim
18 words
The process of claim 1, wherein said β-stannic acid is prepared by hydrolyzing stannic chloride with an alkali.
Claim 5
Dependent Claim
24 words
The process of claim 1, wherein the β -stannic acid in the slurry has a free water content of 10 to 50% by weight.
Claim 6
Dependent Claim
29 words
The process of claim 1, wherein step (c) is carried out so as to give stannic oxide hydrate having a free water content of 7 to 15% by weight.