Willard E. Alexander - Midland MI Timothy L. Faley - Midland MI
Assignee:
The Dow Chemical Company - Midland MI
International Classification:
D01D 1002 D01D 1006
US Classification:
264184
Abstract:
Improved polybenzoxazole fibers are made by a process for finishing a spun and drawn dope fiber, which contains polybenzoxazole polymer and a solvent acid, including the steps of: (a) coagulating the dope fiber in an aqueous coagulant: (b) washing the coagulated fiber with an aqueous washing fluid for less than 72 hours under conditions such that the fiber contains no more than 8,000 ppm residual solvent acid (1 ppm=1 part per million, by weight); (c) drying the fiber at a temperature of no more than 300. degree. C. until it retains no more than about 2 weight percent residual moisture; and (d) heat-treating the fiber at a temperature of at least about 300. degree. C. under tension.
Rapid Heat-Treatment Method For Polybenzaole Fiber
Katsuya Tani - Shiga, JP Steven Rosenberg - Midland MI Willard E. Alexander - Midland MI
Assignee:
The Dow Chemical Company - Midland MI
International Classification:
D01D 1002 D01F 626
US Classification:
264 85
Abstract:
This invention aims at improvement of heat-treatment technology for manufacture of large amounts of polybenzazole fibers. The fibers are heat treated in a device that provides for a rapid, cocurrent, countercurrent or both cocurrent and countercurrent flow of heat treatment gas.
Process For Post-Spin Finishing Of Polybenzoxazole Fibers
Willard E. Alexander - Midland MI Timothy L. Faley - Midland MI
Assignee:
The Dow Chemical Company - Midland MI
International Classification:
D01D 1002 D01D 1006
US Classification:
264184
Abstract:
Improved polybenzoxazole fibers are made by a process for finishing a spun and drawn dope fiber, which contains polybenzoxazole polymer and polyphosphoric acid, including the steps of: (a) coagulating the dope fiber in an aqueous coagulant; (b) washing the coagulated fiber with an aqueous washing fluid for less than 72 hours under conditions such that the fiber contains no more than 8,000 ppm residual phosphorus (1 ppm=1 part per million, by weight); (c) drying the fiber at a temperature of no more than 300. degree. C. until it retains no more than about 3 weight percent residual moisture; and (d) heat-treating the fiber at a temperature of at least about 300. degree. C. under tension.
Louis C. Rubens - Midland MI Willard E. Alexander - Midland MI
Assignee:
The Dow Chemical Company - Midland MI
International Classification:
B29D 2704
US Classification:
53472
Abstract:
Pneumatic synthetic resinous foams are used as dunnage. Foams are added to a package under fluid pressure; the package closed, the pressure reduced to atmospheric, and particulate pneumatic foam expands to fill container.
Louis C. Rubens - Midland MI Willard E. Alexander - Midland MI
Assignee:
The Dow Chemical Company - Midland MI
International Classification:
B29D 2700
US Classification:
264 53
Abstract:
Shaped articles of organic polymer resins having cellular (foamed) structure are made from heat-expandable normally solid thermoplastic resin compositions in permeable molds particularly characterized by flooding the mold cavity and the expandable material therein with molten salt as heating medium. For example, a permeable mold, charged with pieces of polyethylene containing azobisformamide and crosslinked by electron irradiation, is immersed into a molten salt eutectic mixture of KNO. sub. 3, NaNO. sub. 2 and NaNO. sub. 3 at about 264. degree. C, removed, cooled and washed with water, thereby forming a coherent, unitary cellular resin molded article completely filling the mold cavity.
Process For The Preparation Of Polybenzoxazole And Polybenzothiazole Filaments And Fibers
Michael E. Mills - Midland MI Willard Alexander - Midland MI Timothy L. Faley - Midland MI
Assignee:
Toyobo Co., Ltd. - Osaka
International Classification:
D01F 626
US Classification:
264344
Abstract:
A continuous process for heating a polybenzazole or polybenzothiazole filament, which includes the step of heating the filament to a temperature of at least 100. degree. C. but no greater than 290. degree. C. while applying a tension thereto of at least 3. 5 grams per denier, which is carried out at a line speed of at least 100 m/minute; and there is no prior or subsequent heating of the fiber to any temperature greater than 300. degree. C. It has been discovered that placing tension on the filament while it is dried increases its tensile modulus without a significant decrease in its tensile strength.
Expandable Synthetic Resinous Thermoplastic Particles, Method For The Preparation Thereof And The Application Therefor
Louis C. Rubens - Midland MI Willard E. Alexander - Midland MI
Assignee:
The Dow Chemical Company - Midland MI
International Classification:
C08J 922 C08J 924
US Classification:
521 58
Abstract:
Resilient foam particles and moldings are obtained employing a lightly crosslinked polymer such as a styrene polymer with volatile fluid foaming agent that has low permeability through the polymer. Multiple expansion will permit low density particles for molding.
Method And Apparatus For The Preparation Of Foamed Thermoplastic Articles
Louis C. Rubens - Midland MI Willard E. Alexander - Midland MI Carl A. Raeck - Essexville MI
Assignee:
The Dow Chemical Company - Midland MI
International Classification:
C08J 922
US Classification:
264 454
Abstract:
Expandible synthetic resinous particles are molded by injecting heated air generally centrally into the mold cavity by means of a probe, withdrawing the probe and heating the surface of the mold. Low densities and rapid cycle times are obtained.
During a portage around the Missouri River Falls in July 1805, Alexander Willard was attacked by a "White Bear", Clark gathered three men and chased the ...