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Method for controlling double-screw reactor to produce TPU by reaction temperature rising and gel time

A twin-screw reactor and gel time technology, applied in the field of material temperature control, can solve the problems of difficult production of adhesive TPU, slow reaction, flexible production technology, etc., to improve batch-to-batch stability, high production efficiency, The effect of suppressing the occurrence of side reactions

Inactive Publication Date: 2010-11-03
洛阳吉明化工有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The invention discloses a method for controlling the production of TPU in a twin-screw reactor through reaction temperature rise and gel time. The main problems to be solved by the invention are: the setting of TPU production process parameters with different formulas; how to set the twin-screw reaction The process conditions and parameters of the extruder have always been a major problem in the production of TPU by this process method. They have been set based on experience for a long time, which is more difficult for the production of adhesive TPU with variable formulations; The reaction temperature rise and "gel time" are used to determine the activity of the reaction system and the speed of the reaction rate, and find out its correlation with the process parameters of the twin-screw reaction extruder to produce adhesive TPU. This method has been tested in the laboratory It is relatively easy and accurate to set the process parameters of the twin-screw reaction extruder (material temperature, feed ratio, temperature of each area of ​​the screw, speed of the cutting machine and water flow temperature, etc.) with a little experiment; the production technology is flexible and can produce many Adhesive TPU products with different reactivity and properties are especially suitable for the production of TPU with special formulas such as particularly fast or slow reaction, high or low hardness, and non-crystalline (easy to stick) TPU. It is at the leading level in China and has basically reached the advanced level of similar foreign technologies

Method used

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  • Method for controlling double-screw reactor to produce TPU by reaction temperature rising and gel time

Examples

Experimental program
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Effect test

Embodiment 1

[0019] highly reactive system

[0020] 1mol of polymer polyol with a molecular weight of 500-1000, 1-10mol of small molecule chain extender, the molar number of isocyanate is the sum of the former two, and the isocyanate index is about 1; the total amount of materials is about 100g; Add the molecular chain extender into the reactor equipped with a stirrer, heat and melt, and dehydrate under reduced pressure for 2 hours at 120°C, return to normal pressure, cool down to 60°C and turn off the heater, add isocyanate, and the temperature rise of the reaction can be measured If it is >50°C / 3 minutes, and the gel time is <90 seconds / 200°C, it can be judged as a high-reactivity system.

[0021] Setting of screw parameters for high reactivity system: material temperature is 60°C-70°C, screw feeding section is set from room temperature to 120°C, reaction section is set at 120-180°C, and output section is set at 180°C; screw speed 20~25HZ; the cutting machine speed is set to fast; the c...

Embodiment 2

[0023] Medium reactive system

[0024] 2000-3000 molecular weight polymer polyol 1mol, small molecule chain extender 0.5-5mol, isocyanate mole number is the sum of the former two, isocyanate index is about 1; the total amount of materials is about 100g; polymer polyol, small Molecular chain extender is added to the reactor equipped with a stirrer, heated and melted, and dehydrated under reduced pressure for 2 hours at 120°C, then returned to normal pressure, cooled to 80°C and turned off the heater, and the reaction temperature can be measured by adding isocyanate 20-50°C / 10 minutes, gel time 90-300 seconds / 200°C, it can be judged as a medium reactive system.

[0025] Setting of medium reactive screw parameters: material temperature is 70°C-80°C, screw feed section is set from 120-140°C, reaction section is set at 160-200°C, discharge section is set at 190°C; screw speed 16 ~20HZ; the cutting machine speed is set to medium; the cooling water temperature is set to 15 ~ 25 ℃. ...

Embodiment 3

[0027] low reactivity system

[0028] 1 mol of polymer polyol with a molecular weight above 3000, 0.5-5 mol of small molecule chain extender, the molar number of isocyanate is the sum of the former two, and the isocyanate index is about 1; the total amount of materials is about 100g; Add the chain extender into the reactor equipped with a stirrer, heat and melt, and dehydrate under reduced pressure for 2 hours at 120°C, return to normal pressure, cool down to 80°C and turn off the heater, add isocyanate, the reaction temperature can be measured as 300 seconds / 200°C, it can be judged as a low reactivity system.

[0029] Setting of screw parameters with low reactivity: material temperature is 80°C-100°C, screw feeding section is set from 120-160°C, reaction section is set at 160-210°C, discharge section is set at 200°C; screw speed 12 ~16HZ; the cutting machine speed is set to low speed; the cooling water temperature is set to 10 ~ 15 ℃.

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Abstract

The invention relates to a method which utilizes reactive temperature raising and gelation time to control a double-screw reactor to produce TPU. The method is characterized as follows: Molecular weight selected between 500 and 5000 in polyol; Chain extender including small-molecular diol and diamine; Isocyanate including aromatic series and aliphatic diisocyanate; Promoter; Screw parameter settings including control of material temperature, tempeature setting of material-feeding section of screws, temperature setting of reaction section and tempeature setting of material-discharging section;Rotational speed setting of screws; Rotational speed setting of a segmenting machine; Temperature setting of cooling water. The invention is particularly applied to the production of TPU in the relatively special formulation system, such as ultra-fast or ultra-slow reaction, ultra-high or ultra-low rigidity, non-crystallization (easy conglutination), etc.

Description

【Technical field】 [0001] The invention relates to a material temperature control method, in particular to a production method for controlling a reactor through reaction temperature rise and gel time. 【Background technique】 [0002] In 1958, Goodrich Company of the United States first launched commercialized TPU, and developed rapidly in developed countries in the following decades, mainly including Goodrich and Morton in the United States, Bayer and Basf in Germany, Merquinsa in Spain, and Townsend in Australia. Most of them are produced by the twin-screw body method, and the scale is that a single production line can reach an annual output of 1,000 tons. Our country started late, and most manufacturers still stay at the level of 100 tons / year batch method or even solution method. There are also domestic manufacturers who have purchased advanced twin-screw extrusion equipment from abroad, but due to lack of formula, process technology and supporting auxiliary equipment The ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08G18/48B29C47/92B29C47/40B29C48/40B29C48/92
CPCB29C48/92B29C2948/92704B29C48/04B29C48/40B29C48/9185B29C48/919B29C2948/9259B29C2948/92695B29C2948/92885B29C2948/92895
Inventor 唐亚夫朱长春牛杰峰詹中贤吴炳峰张应超孟晓琳
Owner 洛阳吉明化工有限公司
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