A process control method for pbo fiber production
A process control and fiber technology, which is applied in the control field of poly-p-phenylenebenzobisoxazole (PBO) fiber polymerization process production, can solve the problems of TPA solubility and high solution viscosity, etc., and achieve easy and feasible stirring , the effect of reducing solid content and shortening the process time
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Embodiment 1
[0033] The present embodiment proposes a process control method for PBO fiber production, the steps of the process control method are as follows:
[0034] A, degassing, after polyphosphoric acid is heated, drop into mixed degassing still, then drop into phosphorus pentoxide, 4,6-diaminoresorcinol hydrochloride and terephthalic acid, carry out degassing;
[0035] B, pre-polymerization, the material obtained by the degassing of step A is pre-polymerized, and terephthalic acid is added in the pre-polymerization process to obtain a prepolymer material;
[0036] C, post-polymerization, the pre-polymer material and terephthalic acid are sent into the screw reactor for post-polymerization to obtain the post-polymer material;
[0037] D. Spinning, the polymer material is spun to obtain PBO fiber.
[0038] In the above-mentioned steps, the ratio of the molar weight of the 4,6-diaminoresorcinol hydrochloride input in step A to the sum of the terephthalic acid molar weight input in step...
Embodiment 2
[0040] The present embodiment proposes a process control method for PBO fiber production, the steps of the process control method are as follows:
[0041] A, degassing, after polyphosphoric acid is heated, drop into mixed degassing still, then drop into phosphorus pentoxide, 4,6-diaminoresorcinol hydrochloride and terephthalic acid, carry out degassing;
[0042] B, pre-polymerization, the material obtained by the degassing of step A is pre-polymerized, and terephthalic acid is added in the pre-polymerization process to obtain a prepolymer material;
[0043] C, post-polymerization, the pre-polymer material and terephthalic acid are sent into the screw reactor for post-polymerization to obtain the post-polymer material;
[0044] D. Spinning, the polymer material is spun to obtain PBO fiber.
[0045] In the above-mentioned steps, the ratio of the molar weight of the 4,6-diaminoresorcinol hydrochloride input in step A to the sum of the terephthalic acid molar weight input in steps ...
Embodiment 3
[0047] The present embodiment proposes a process control method for PBO fiber production, the steps of the process control method are as follows:
[0048] A, degassing, after polyphosphoric acid is heated, drop into mixed degassing still, then drop into phosphorus pentoxide, 4,6-diaminoresorcinol hydrochloride and terephthalic acid, carry out degassing;
[0049] B, pre-polymerization, the material obtained by the degassing of step A is pre-polymerized, and terephthalic acid is added in the pre-polymerization process to obtain a prepolymer material;
[0050] C, post-polymerization, the pre-polymer material and terephthalic acid are sent into the screw reactor for post-polymerization to obtain the post-polymer material;
[0051] D. Spinning, the polymer material is spun to obtain PBO fiber.
[0052] In the above-mentioned steps, the ratio of the molar weight of the 4,6-diaminoresorcinol hydrochloride input in step A to the sum of the terephthalic acid molar weight input in step...
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