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Method for preparing polycarbonate powder

A technology for polycarbonate and powder materials, which is applied in the field of processing polycarbonate powder materials, can solve the problems of flocs easily sticking into large pieces, unsuitable for downstream use, low space utilization efficiency, etc., and achieves the advantages of process economy. , low moisture content, energy saving effect

Active Publication Date: 2021-04-16
WANHUA CHEM GRP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, this method requires a tower with a height of 25-30 meters and a huge space, and the space utilization efficiency is low, and the amount of hot water required to process the polycarbonate per unit weight is relatively large
[0007] In addition, these methods present additional problems when dealing with polycarbonate species with reduced crystallinity
The steam precipitation process is prone to wire drawing problems; the particle size of the powder prepared by kneading and crushing is usually too large, the bulk density is low, and it is not suitable for downstream use; the poor solvent precipitation usually results in a paste, and the powder cannot be obtained; the hot water tower The flocs generated by this method are easy to stick into large pieces, and there are also problems in the control of the particle size of the powder

Method used

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  • Method for preparing polycarbonate powder
  • Method for preparing polycarbonate powder

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0038] Such as figure 1 As shown, prepare a semi-closed stainless steel hot water tank with a width of 20cm, a depth of 10cm, and a length of 2m. At the bottom of one end of the water tank, there is a horizontal slit with the same width as the water tank, which has an adjustable opening function, and serves as a hot water inlet.

[0039] The hot water is introduced from the slit at a flow rate of 450L / h, the temperature of the hot water at the entrance is kept at about 80°C, and the opening of the slit is adjusted so that the flow rate of the hot water at the entrance is about 0.1m / s.

[0040] At 4mm above the slit, there is another horizontally centered, replaceable rectangular entrance with a length of 8.5cm and a height of 0.5cm. The length and height refer to the dimensions of the rectangular entrance in the horizontal and vertical directions.

[0041] Prepare polycarbonate obtained by copolymerization of 33% bisphenol A and 67% bisphenol TMC, the preparation method can r...

Embodiment 2

[0048] Main process with reference to embodiment 1.

[0049] The length of the hot water tank is 5m, and the hot water is introduced from the slit inlet at a flow rate of 450L / h. The temperature of the hot water at the inlet is kept at about 80°C, and the flow rate is adjusted to about 0.3m / s.

[0050] The composition of the copolycarbonate solution was consistent with that of Example 1. The solution was passed into the tank through a rectangular inlet with a flow rate of 150 L / h. The rectangular inlet had a width of 15 cm, a height of 0.1 cm, and a flow velocity of about 0.3 m / s at the inlet.

[0051] After the solution is added to the water tank, a gel layer is automatically formed on the water surface with a thickness of about 0.06cm. The linear velocity of the gel layer is basically the same as the flow velocity of the hot water, and the width is approximately equal to the width of the rectangular inlet. It is calculated that the projected area of ​​the unit volume of solu...

Embodiment 3

[0054] Main process with reference to embodiment 1.

[0055] The width of the hot water tank is 50cm, the depth is 10cm, and the length is 10m. The hot water is introduced from the slit inlet at a flow rate of 3000L / h. The temperature of the hot water at the inlet is kept at about 90°C, and the flow rate is adjusted to about 0.3m / s.

[0056] The composition of the copolycarbonate solution was consistent with that of Example 1. The solution was passed into the tank through a rectangular inlet with a flow rate of 3000 L / h. The rectangular inlet had a width of 30 cm and a height of 1 cm. The flow velocity at the inlet is about 0.3m / s.

[0057] After the solution is added to the water tank, a gel layer is automatically formed on the water surface with a thickness of about 0.7cm. The linear velocity of the gel layer is basically the same as the flow rate of the hot water. The measured width of the gel layer is about 120% of the width of the rectangular inlet, and the projected are...

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Abstract

The invention provides a method for processing a gel layer of polycarbonate from a solution and further preparing polycarbonate powder when the polycarbonate is prepared by an interfacial polycondensation method. The method comprises the following steps that a polycarbonate solution and hot water are conveyed into a container in the same direction, part of a solvent is heated and evaporated, polycarbonate forms gel with the density lower than that of water, the gel is continuously spread on the flowing water surface to form a gel layer under the driving effect of water flow, wherein the content of the residual solvent is 10-70% of the weight of carbonic ester; the gel layer is separated at an outlet of the container and then is crushed to obtain wet powder containing polycarbonate, a solvent and a small amount of water, and then the wet powder is dried to remove the residual solvent and water to obtain powder. The method is simple in process, the moisture content of the treated powder is low, energy consumption can be reduced during drying, good process economy is achieved, the dried powder has high stacking density, the fine powder content is low, and the method is suitable for being applied to the downstream industry.

Description

technical field [0001] The invention relates to a method for processing polycarbonate powder from a solution. Background technique [0002] The preparation of polycarbonate by the interfacial phosgene process requires the removal of the solvent, usually dichloromethane, in the post-treatment process. The method for removing methylene chloride in polycarbonate solution, disclosed main several categories include: [0003] US 4568418 discloses a steam precipitation process, that is, the polycarbonate solution and superheated steam are sprayed into the pipeline at high speed, the dichloromethane in the solution evaporates rapidly, and the polycarbonate is also sheared into powder by the high-speed steam. This process needs to consume a large amount of superheated steam, and the bulk density of the prepared powder is low, which is not conducive to downstream use. [0004] CN 1733819 discloses a method, crushing the gel obtained after concentrating the polycarbonate solution, an...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08J3/16C08L69/00
Inventor 李诚高俊民潘勇军王晓东李强隋东武
Owner WANHUA CHEM GRP CO LTD
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