CN203174013U - Uniform ion exchange resin particle production equipment - Google Patents
Uniform ion exchange resin particle production equipment Download PDFInfo
- Publication number
- CN203174013U CN203174013U CN 201320110706 CN201320110706U CN203174013U CN 203174013 U CN203174013 U CN 203174013U CN 201320110706 CN201320110706 CN 201320110706 CN 201320110706 U CN201320110706 U CN 201320110706U CN 203174013 U CN203174013 U CN 203174013U
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- monomer
- tank
- heating tank
- fluidization
- exchange resin
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Abstract
The utility model discloses uniform ion exchange resin particle production equipment which belongs to the field of resin production equipment. The equipment comprises a monomer production system and a monomer forming system, wherein the monomer production system comprises a monomer box and a fluidization pipeline; a fluidization pipeline is connected with the top end of the monomer box; a raw material inlet and a liquid discharge are formed in the bottom end of the monomer box; a view mirror is arranged on the outer wall of the monomer box; a shower nozzle is arranged inside the monomer box; the monomer box is connected with a vibration motor; a ripple compensator is arranged at the joint of the monomer box and the fluidization pipeline; the monomer forming system comprises a fluidization tank and a heating tank; the fluidization tank is provided with an upper cover; a gas discharge hole is formed in the upper cover; the heating tank is connected with the bottom of the fluidization tank through a flange; fluid circulation pipelines are arranged on the fluidization tank and the heating tank; a circulation motor is connected with the fluid circulation pipelines; and a discharge hole is formed in the bottom of the heating tank. By utilizing the equipment, the diameter uniformity of ion exchange resin monomer particles is improved, the product ball yield is improved, the cost is lowered, and the production efficiency is improved.
Description
Technical field
The utility model relates to the production of resins equipment technical field, is specifically related to a kind of ion-exchange resin particles homogeneous production unit.
Background technology
Ion exchange resin is widely used in industry such as material purification, water treatment, catalyzed reaction, medicine Separation ﹠ Purification and the scientific research field, and its matrix is the pearl body that is generated by suspension copolymerization by vinylbenzene, divinylbenzene.Ion exchange resin bead footpath in the practical application all must be according to service requirements control in certain scope.
In present industrial suspension polymerization technology, the main reactor that adopts stirs shearing generation monomer particle, owing to stirring reasons such as the shearing force spatial distribution is inhomogeneous in the reactor, can cause the monomer granularity that produces inhomogeneous and have quite a few Archon granularity undesirable.Can increase production cost like this, increase energy consumption, waste resource, and can cause bigger environmental pollution.
The utility model content
Technical problem to be solved in the utility model is to provide a kind of structure perfect, the ion-exchange resin particles homogeneous production unit that result of use is good.
Technical problem to be solved in the utility model realizes by the following technical solutions:
A kind of ion-exchange resin particles homogeneous production unit, comprise that monomer produces system and monomer formation system, is characterized in that: described monomer produces system and the monomer formation system passes through pipe connection;
Described monomer generation system comprises one-piece box and fluidisation pipeline, described one-piece box top is connected with the fluidisation pipeline, the bottom is provided with feed(raw material)inlet, leakage fluid dram, outer wall is provided with visor, be used for observing monomer, inside is provided with shower nozzle, and described one-piece box is connected with vibration motor, and described one-piece box and fluidisation pipeline junction are provided with FlexbleJoint;
Described monomer formation system comprises streaming tank and heating tank, described streaming tank is provided with loam cake, on cover and be provided with venting port, described streaming tank bottom is connected with heating tank by flange, streaming tank and heating tank are provided with fluid circulation pipe, be connected with circulation motor on the fluid circulation pipe, described heating tank bottom is provided with discharge port, is equipped with visor on described heating tank and the streaming tank.
The beneficial effects of the utility model are: the utility model can improve the diameter homogeneity of ion exchange resin monomer particle, improves product and gets the ball rate, reduces cost, and enhances productivity.
Description of drawings
Fig. 1 is a kind of ion-exchange resin particles homogeneous of the utility model production unit structural representation.
Wherein: the 1-monomer produces system; 2-monomer formation system; The 3-one-piece box; 4-fluidisation pipeline; The 5-feed(raw material)inlet; The 6-leakage fluid dram; The 7-visor; The 8-shower nozzle; The 9-vibration motor; The 10-FlexbleJoint; The 11-streaming tank; The 12-heating tank; The 13-loam cake; The 14-venting port; The 15-flange; The 16-fluid circulation pipe; The 17-circulation motor; The 18-discharge port.
Embodiment
For technique means, creation characteristic that the utility model is realized, reach purpose and effect is easy to understand, below in conjunction with concrete diagram, further set forth the utility model.
As shown in Figure 1, a kind of ion-exchange resin particles homogeneous production unit comprises that monomer produces system 1 and monomer formation system 2, and monomer produces system 1 and passes through pipe connection with monomer formation system 2; Monomer produces system 1 and comprises one-piece box 3 and fluidisation pipeline 4, one-piece box 3 tops are connected with fluidisation pipeline 4, the bottom is provided with feed(raw material)inlet 5, leakage fluid dram 6, outer wall is provided with visor 7, be used for observing monomer, inside is provided with shower nozzle 8, and one-piece box 3 is connected with vibration motor 9, and one-piece box 3 is provided with FlexbleJoint 10 with fluidisation pipeline 4 junctions;
Monomer formation system 2 comprises streaming tank 11 and heating tank 12, streaming tank 11 is provided with loam cake 13, loam cake 13 is provided with venting port 14, streaming tank 11 bottoms are connected with heating tank 12 by flange 15, streaming tank 11 is provided with fluid circulation pipe 16 with heating tank 12, be connected with circulation motor 17 on the fluid circulation pipe 16, heating tank 12 bottoms are provided with discharge port 18, are equipped with visor 7 on heating tank 12 and the streaming tank 11.
Principle of work of the present utility model is: raw material is 5 injection shower nozzles 8 from the feed(raw material)inlet, shower nozzle 8 connects vibrating motor 9, control the size that shower nozzles 8 eject monomer by regulating vibrating motor 9, the monomer that forms enters streaming tank 11 through fluidisation pipeline 4, by regulating the flow velocity of the liquid in the circulation motor 17 control streaming tanks 11, provide optimal temperature by the temperature of regulating liquid in the heating tank 12 control heating tanks 12 for monomer reaction.Because the density before the monomer reaction is less than fluid density in the streaming tank 11, therefore monomer can flow to the upper end of streaming tank 11 because of buoyancy function, and the monomer that has the liquid of certain flow rate and come-up in the streaming tank 11 produces reactive force, thereby make monomer stays form finished product in streaming tank 11 internal fixing zones to finish monomer reaction, finished product density behind the monomer reaction is greater than the fluid density in the streaming tank 11, finished product sinks to the bottom of heating tank 12 gradually, and draws off from discharge port 18.
More than show and described ultimate principle of the present utility model and principal character and advantage of the present utility model.The technician of the industry should understand; the utility model is not restricted to the described embodiments; that describes in above-described embodiment and the specification sheets just illustrates principle of the present utility model; under the prerequisite that does not break away from the utility model spirit and scope; the utility model also has various changes and modifications, and these changes and improvements all fall in claimed the utility model scope.The claimed scope of the utility model is defined by appending claims and equivalent thereof.
Claims (1)
1. an ion-exchange resin particles homogeneous production unit comprises monomer generation system and monomer formation system, and it is characterized in that: described monomer produces system and the monomer formation system passes through pipe connection;
Described monomer generation system comprises one-piece box and fluidisation pipeline, described one-piece box top is connected with the fluidisation pipeline, the bottom is provided with feed(raw material)inlet, leakage fluid dram, outer wall is provided with visor, inside is provided with shower nozzle, described one-piece box is connected with vibration motor, and described one-piece box and fluidisation pipeline junction are provided with FlexbleJoint;
Described monomer formation system comprises streaming tank and heating tank, described streaming tank is provided with loam cake, on cover and be provided with venting port, described streaming tank bottom is connected with heating tank by flange, streaming tank and heating tank are provided with fluid circulation pipe, be connected with circulation motor on the fluid circulation pipe, described heating tank bottom is provided with discharge port, is equipped with visor on described heating tank and the streaming tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320110706 CN203174013U (en) | 2013-03-12 | 2013-03-12 | Uniform ion exchange resin particle production equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320110706 CN203174013U (en) | 2013-03-12 | 2013-03-12 | Uniform ion exchange resin particle production equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203174013U true CN203174013U (en) | 2013-09-04 |
Family
ID=49070745
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320110706 Withdrawn - After Issue CN203174013U (en) | 2013-03-12 | 2013-03-12 | Uniform ion exchange resin particle production equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203174013U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103145904A (en) * | 2013-03-12 | 2013-06-12 | 蚌埠市天星树脂有限责任公司 | Uniform ion exchange resin granule production equipment |
-
2013
- 2013-03-12 CN CN 201320110706 patent/CN203174013U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103145904A (en) * | 2013-03-12 | 2013-06-12 | 蚌埠市天星树脂有限责任公司 | Uniform ion exchange resin granule production equipment |
| CN103145904B (en) * | 2013-03-12 | 2015-04-29 | 蚌埠市天星树脂有限责任公司 | Uniform ion exchange resin granule production equipment |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20130904 Effective date of abandoning: 20150429 |