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Method of producing uniform, fine polymer beads by vibration jetting

一种聚合物珠、聚合单体的技术,应用在使原料颗粒化的方法、抖动/振荡/振动混合机、化学仪器和方法等方向,能够解决板喷射法整体生产率低、能量损失大、难以实施商业操作等问题

Active Publication Date: 2015-11-18
PUROLITE CORP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, these conventional methods such as stirred batch polymerization often produce bead products exhibiting large particle size distributions, mainly due to problems with coalescence and / or breakdown of suspended monomer droplets
Current spraying methods also suffer from high cost and low output of products with a particle size below 300 μm
For example, the platejetting method has low overall productivity and is limited by large energy losses during the vibration generation step
In addition, methods that require injection into a gaseous medium require very sophisticated equipment and complex polymer formation methods
The use of cross-flow membranes for the generation of fine droplets using metal or glass sintered or electro-formed membranes is suitable for small-scale applications but difficult to implement in commercial operations
Furthermore, the low productivity per unit area of ​​cross-flow membranes requires complex and bulky equipment, which is unreliable and requires high capital and operating costs

Method used

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  • Method of producing uniform, fine polymer beads by vibration jetting
  • Method of producing uniform, fine polymer beads by vibration jetting
  • Method of producing uniform, fine polymer beads by vibration jetting

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0047] Preparation of Homogeneous Gel Polymer Beads (Volume Average Diameter 166 μm)

[0048] Polymeric beads of uniform particle size are used as image 3 A device of the configuration shown is manufactured. An aqueous phase with a viscosity of 1 to 1.2 centipoise comprising distilled water (4 kg) and polyvinyl alcohol (20 g) was prepared at neutral pH. The aqueous solution was fed to the collection column 30 at a rate of 16 l / hour. A monomer phase was prepared comprising styrene (2.25 kg), divinylbenzene (80%; 0.25 g) and tert-butyl peroxy-2-ethylhexanoate (5 g). The monomer phase was prepared under agitation in a monomer mix tank. The monomer phase was then fed to the monomer reservoir feed line 16 at a flow rate of 12.6 1 / hour. The membrane was then vibrated at 60 Hz and a peak-to-peak amplitude of 1.82 mm.

[0049] The membrane used in this example was a 4×4 cm (L / d) nickel-based membrane (pure nickel) including thousands of 40 μm through-holes connecting the suspend...

Embodiment 2

[0059] Preparation of uniform macroporous polymer beads (volume mean diameter 180 μm) of embodiment 2

[0060] Polymeric beads of uniform particle size are used as image 3 A device of the configuration shown is manufactured. An aqueous phase with a viscosity of 1 to 1.5 centipoise comprising distilled water (4 kg) and polyvinyl alcohol (20 g) was prepared at neutral pH. The aqueous solution was added to the disperser unit 30 and stirred to mix at room temperature. A monomer phase was prepared comprising styrene (1.8 kg), divinylbenzene (63%; 122.1 g), isooctane (1.9 kg) and tert-butyl peroxy-2-ethylhexanoate (56 g). The monomer phase was prepared under agitation in a monomer mix tank (not shown). The monomer phase was then fed to the membrane 12 at a flow rate of 13.2 l / hour. The membrane 12 was then vibrated at 48 Hz and an amplitude of 2.76 mm to provide 180 μm droplets, 90% of which were in the range of 136 to 202 μm. A droplet formation productivity in the range of 1...

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Abstract

Speriodal polymer beads having a uniform size are prepared by polymerizing uniformly sized monomer droplets formed by dispersing a polymerizable monomer phase over double-walled cylindrical cross-flow membrane into an aqueous phase. A shear force is provided at a point of egression of the polymerizable monomer phase into the aqueous phase, the direction of shear substantially perpendicular to the direction of egression of the monomer phase. The polymer beads can be employed in applications where beads having uniform diameters of 10 to 200 μm are useful.

Description

technical field [0001] The present invention relates generally to the preparation of spherical polymeric beads, and more particularly, to spherical polymeric beads having a substantially uniform particle size. Such beads are useful in the manufacture of ion exchange resins. Background technique [0002] Spherical polymer beads in the size range of about 1 μm to 300 μm in diameter are useful for various applications. For example, such polymer beads have been used in various chromatographic applications as matrices for ion exchange resins, seeds for the preparation of larger sized polymer particles, calibration standards for hemocytometers, aerosol Instrumentation, pollution control equipment, and among other uses as spacers for photographic emulsions. [0003] Unfortunately, however, the preparation of uniformly sized polymer beads using known methods is generally not suitable for large-scale production. Typically, polymer beads can be prepared by suspension polymerization...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08J3/12B01J2/00
CPCB01J2/12B01J2/06B01J19/18B01J19/185B01J4/004B01J4/007C08F2/01B01F27/80B01F31/441B01F33/82B01F35/71755
Inventor S·R·康斯维特斯
Owner PUROLITE CORP
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