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Preparation method for small grainsize polybutadiene latex

A technology of small particle size and latex, which is applied in the field of preparation of small particle size polybutadiene latex, can solve the problems that the particle size of large particle size latex cannot be accurately controlled, the difference in particle size is large, and the heat release of reaction is uneven. Achieve excellent agglomeration effect, short reaction time, uniform reaction heat release

Active Publication Date: 2008-02-20
BC P INC CHINA NAT PETROLEUM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

This patented technology describes methods used to prepare tiny particles (PB), called pebbles or bubbles). These fine particles have unique properties such as being able to stick together easily without sticking them into each other's hands like candy balls. They also allow for efficient cool down on their owners due to its ability to absorb excessive amounts of moisture quickly while still maintaining an even distribution throughout the entire volume they formulate. Overall, these technical features improve the performance and efficiency of producing minute sizes of Pb(II)-based materials.

Problems solved by technology

This patented technical problem addressed in this patents relating to improving the quality and consistency of synthetic rubber (SR), specifically high molecular weight type BS). Current processes involve either suspension or solution casting followed by aggregation, which results in variations in particle sizes among particles resulting in poor reproducibility across lots. Chemically modified starch may provide better uniformity and controllability compared to other types of chemistry. Additionally, current methods require longer periods of reaction while still producing good quality rubber without excessive thermal energy input.

Method used

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  • Preparation method for small grainsize polybutadiene latex

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0047] Polymerization is carried out according to the following components and weight ratios and operating conditions:

[0048] 1), get each component by weight percentage as:

[0049] Butadiene: 38.10

[0050] Styrene: 2.00

[0051] Emulsifier: 1.27

[0052] Tertiary dodecyl mercaptan: 0.18

[0053] Electrolyte: 0.19

[0054] K 2 S 2 o 8 (3%): 0.12

[0055] water: balance

[0056] 2), operating conditions and steps:

[0057] Mix potassium abietate and potassium oleate at a ratio of 2:1 to make an emulsifier, and the ratio of the composite electrolyte sodium pyrophosphate to potassium carbonate is 1:2. Except for the emulsifier, add all the above components into the reaction kettle , and add 88% emulsifier at the same time; control the reaction temperature according to the saddle-shaped temperature control curve, the early stage is 67°C, the middle stage is 63°C, and the late stage is 73°C. When the conversion rate reaches 30%, the remaining 12% emulsifier is added, ...

Embodiment 2

[0064] Polymerization is carried out according to the following components and weight ratios and operating conditions:

[0065] 1), get each component by weight percentage as:

[0066] Butadiene: 40.10

[0067] Acrylonitrile 0.01

[0068] Emulsifier: 1.27

[0069] tertiary dodecyl mercaptan: 0.18

[0070] Electrolyte: 0.19

[0071] K 2 S 2 o 8 (3%): 0.12

[0072] The balance is water

[0073] 2), operating conditions and steps:

[0074] Mix potassium abietate and potassium oleate in a weight ratio of 6:1 to make an emulsifier, and the ratio of the composite electrolyte sodium pyrophosphate to potassium carbonate is 1:4. Except for the emulsifier, add all the above components to the reaction kettle Add 88% emulsifier at the same time; control the reaction temperature according to the saddle-shaped temperature control curve, the early stage is 63°C, the middle stage is 60°C, and the late stage is 70°C. When the conversion rate reaches 30%, add the remaining 12% emulsif...

Embodiment 3

[0081] 1), select the following components by weight percentage:

[0082] Butadiene: 38.13

[0083] Methyl methacrylate: 6.00

[0084] Emulsifier: 1.18

[0085] tertiary dodecyl mercaptan: 0.18

[0086] Electrolyte: 0.18

[0087] K 2 8 2 o 8 (3%): 0.12

[0088] The balance is water:

[0089] 2) Potassium oleate and potassium abietate are mixed in a weight ratio of 1:0.2 to make an emulsifier. The composite electrolyte EDTA and potassium carbonate are in a weight ratio of 4:1. Except for the emulsifier, all the above components are added to the reaction In the kettle, add 88% emulsifier at the same time; control the reaction temperature according to the saddle-shaped temperature control curve, the early stage is 69°C, the middle stage is 66°C, and the later stage is 75°C. When the conversion rate reaches 30%, add the remaining 12% emulsifier for 7 hours Complete the polymerization reaction.

[0090] 3), the result:

[0091] Response time: 9 hours,

[0092] Latex par...

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Abstract

The invention relates to a preparation method of ABS polybutadiene rubber latex with small grain diameter, comprising components based on a proportioning rate by weight: butadiene 34.00-45.00 percent, secondary monomer 0.01-6.0 percent, thiol 0.12-0.22 percent, emulsion 0.80-2.60 percent, electrolyte 0.12-0.32 percent and desalted water, wherein, the emulsion is made by mixing potassium rosinate and potassium oleate; the electrolyte comprises sodium pyrophosphate or EDTA and potassium carbonate. The emulsion is added in two steps, the temperature is controlled based on a saddle-shaped temperature controlling curve with 63-69 DEG C at prophase, 60-64 DEG C at metaphase and 70-75 DEG C at anaphase, the reaction time is 7-9 hours under 0.8 MPa, or reaction speed at the prophase is accelerated to discharge more heat, then the reaction temperature is decrease when the conversion rate is at 40 percent-80 percent, the heat discharging speed at the metaphase is decreased, then the reaction temperature is raised to a highest point when the conversion rate is more than 80 percent, so as to change a violent heat discharging situation and realize in shortening the reaction time. Quadric adding of the emulsion is used, so as to realize the effects of concentration increasing and reaction pressure decreasing to stably control the polymerization of the polybutadiene, thereby reducing rubber evolution and adhesion of the rubber latex and the conversion rate is more than 97 percent.

Description

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Claims

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Application Information

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Owner BC P INC CHINA NAT PETROLEUM CORP
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