Polyamide synthesis including multiple back-ends
A polyamide and post-condensation technology, which is applied in the field of synthetic polyamide, can solve the problems of limited size, and achieve the effects of avoiding capacity bottlenecks, high overall throughput, and economic cost
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[0081] The present invention may be better understood with reference to the following examples, provided by way of illustration. The invention is not limited to the examples given herein.
[0082] Throughout the examples, X represents the same cost. Throughout the examples, Z represents the same cost.
Embodiment 3a
[0121] Example 3a. Continuous process with multiple finishers.
[0122] The method described in Example 1a was followed, using a system comprising cells approximately three times the size and handling three times the flow rate, similar to Example 1c. However, instead of the single finisher of Example 1c, two finishers in parallel are used, with the flow from the flasher being split evenly between the finishers.
[0123] The salt pond delivers material to the evaporator at about 315 L / min, has a volume of about 12,000 L, costs about 3*Z to buy and build into the system, and costs about 3*X / h to run. The evaporator delivers material into the reactor at about 225 L / min, has a volume of about 12,000 L, costs about 9*Z to buy and build into the system, and costs about 12*X / h to run. The reactor delivers material to the flasher at about 180 L / min, has a volume of about 4,500 L, costs about 15*Z to purchase and build into the system, and costs about 12*X / h to run. The flasher del...
Embodiment 3b
[0125] Example 3b. Continuous process with multiple finishers.
[0126] The method of Example 3 was followed except that one finisher was configured to produce polymer having a relative viscosity of about 60 and the other finisher was configured to produce polymer having a relative viscosity of about 50.
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