CN106039796B - A kind of polymeric latex discharging filtration system - Google Patents
A kind of polymeric latex discharging filtration system Download PDFInfo
- Publication number
- CN106039796B CN106039796B CN201610476140.5A CN201610476140A CN106039796B CN 106039796 B CN106039796 B CN 106039796B CN 201610476140 A CN201610476140 A CN 201610476140A CN 106039796 B CN106039796 B CN 106039796B
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- China
- Prior art keywords
- latex
- finished product
- filter
- polymeric latex
- filtering
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 239000004816 latex Substances 0.000 title claims abstract description 82
- 229920000126 latex Polymers 0.000 title claims abstract description 82
- 238000001914 filtration Methods 0.000 title claims abstract description 58
- 238000007599 discharging Methods 0.000 title claims abstract description 16
- 238000004140 cleaning Methods 0.000 claims abstract description 30
- 239000000047 product Substances 0.000 claims abstract description 30
- 239000000463 material Substances 0.000 claims abstract description 28
- 239000011265 semifinished product Substances 0.000 claims abstract description 12
- 238000006116 polymerization reaction Methods 0.000 claims abstract description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 19
- 238000011010 flushing procedure Methods 0.000 claims description 8
- 229910001220 stainless steel Inorganic materials 0.000 claims description 4
- 239000010935 stainless steel Substances 0.000 claims description 4
- 238000004148 unit process Methods 0.000 claims description 4
- 239000003818 cinder Substances 0.000 claims description 2
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 description 7
- 239000002245 particle Substances 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 239000008399 tap water Substances 0.000 description 4
- 235000020679 tap water Nutrition 0.000 description 4
- 238000000889 atomisation Methods 0.000 description 3
- 239000011347 resin Substances 0.000 description 3
- 229920005989 resin Polymers 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 206010016825 Flushing Diseases 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000008237 rinsing water Substances 0.000 description 1
- 230000011218 segmentation Effects 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/01—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements
- B01D29/03—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements self-supporting
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/62—Regenerating the filter material in the filter
- B01D29/66—Regenerating the filter material in the filter by flushing, e.g. counter-current air-bumps
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Lubrication Details And Ventilation Of Internal Combustion Engines (AREA)
Abstract
The present invention discloses a kind of polymeric latex discharging filtration system, the system includes the polymeric latex slot for storing the polymeric latex semi-finished product produced after polymerization process, with the finished product bin for storing finished product latex material, blowpit is disposed between the polymeric latex slot and the finished product bin, filter, self-cleaning filter, latex slot, stripper and atomizer, the polymeric latex semi-finished product are successively through the blowpit, filter, self-cleaning filter, latex slot, finished product latex material is obtained after stripper and the processing of atomizer each processing unit, the finished product latex material storing is in the finished product bin.For solving the problems, such as that energy consumption is high in the prior art, at high cost, quality is low, have the advantages that structure is simple, easy-operating.
Description
Technical field
The present invention relates to the technological process of production of polymer and production equipment field, in particular to a kind of polymeric latex discharging
Filtration system.
Background technique
Flow chart shown in Figure 1 for polymeric latex discharge system in the prior art, it is known that aggregated process production
Latex semi-finished product are placed in polymeric latex slot, are entered latex delivery in blowpit by discharging pump, then ground machine is to latex object
Material is ground, rear successively to be handled by self-cleaning filter, stripper and atomizer by feeding engine conveying, obtains finished product glue
Newborn material.
The prior art has the following problems: the latex particle that ground pulverizer milled processed obtains has a large amount of fine slag,
When entering the strainer of self-cleaning filter, it will cause strainer deformation and damage, latex particle granule size caused not to be inconsistent symphysis
It produces and requires, the atomizing disk that next can be blocked in entering atomization drying process in atomizer causes atomization to be not thorough, and influences to paste
The quality of shape resin finished product；Grinding and crushing machine generally uses the gear pump of French import, and matched motor power (output) is 75KW, energy
Consume larger, production cost is higher.
Summary of the invention
The present invention proposes a kind of polymeric latex discharging filtration system, and for solving, above-mentioned energy consumption is high, at high cost, quality is low
Problem has the advantages that structure is simple, easy-operating.
To achieve the above object, the invention adopts the following technical scheme: a kind of polymeric latex discharging filtration system, this is
System includes the polymeric latex slot for storing the polymeric latex semi-finished product produced after polymerization process, and for storing finished product latex
Finished product bin is disposed with blowpit, filter, self-cleaning filtering between the polymeric latex slot and the finished product bin
Device, latex slot, stripper and atomizer, the polymeric latex semi-finished product are successively through the blowpit, filter, self-cleaning filtering
Finished product latex material, the finished product latex material storing are obtained after device, latex slot, stripper and the processing of atomizer each processing unit
In the finished product bin.
Further, discharging pump is equipped between the polymeric latex slot and the blowpit, the discharging pump is for conveying
Polymeric latex semi-finished product in the polymeric latex slot enter in blowpit；
Between the filter and the self-cleaning filter and between the self-cleaning filter and the latex slot
It is equipped with feeding engine, latex of the feeding engine for after conveying a processing unit processes enters next processing unit.
Preferably, the filter includes tank body, and the tank body, which is equipped with, rinses water inlet, feeding inlet, discharge port and row
Cinder notch, the level height for rinsing water inlet, feeding inlet, discharge port and slag-drip opening successively reduce, and the tank interior is equipped with
For filtering the filtering baffle of latex, the tank interior is divided into filtering proparea and filtering back zone, institute by the filtering baffle
Flushing water inlet, feeding inlet and slag-drip opening is stated to join with filtering proparea connection, the discharge port and the filtering back zone
Logical, the feeding inlet is connected with the blowpit, and the discharge port is connected through the feeding engine with the self-cleaning filter.
Further, it is additionally provided with and is cleaned into hole on the tank body, it is described to clean the level height into hole lower than the pan feeding
The level height of mouth, it is described to clean into hole and filtering proparea connection higher than the level height of the slag-drip opening.
Preferably, the tank body is the cylindrical body that upper/lower terminal is equipped with end socket, that is, upper cover and lower head, the upper cover
It is equipped with and rinses water inlet, the lower head is equipped with slag-drip opening, and the flushing water inlet and the slag-drip opening are located at the circle
On the central axis of cylinder, the feeding inlet and it is described clean the side that the cylindrical body is located at into hole, the discharge port setting exists
The other side of the cylindrical body, the filtering baffle is disposed in proximity to the discharge port side and the central axis of the cylindrical body is flat
Row.
Preferably, the filtering baffle is the stainless steel plate with a thickness of 6mm, and the filtering baffle is equipped with filter hole, institute
The bore dia for stating filter hole is 7mm.
There is choosing, the tank base is equipped with two support columns.
The beneficial effects of the present invention are:
1) polymeric latex of the invention discharging filtration system connects filter by pipeline in blowpit rear end, makes blowpit
In material be directly entered filter carry out material particles filtering, ensure that the subsequent material particles into self-cleaning filter
The size of granularity further protects the strainer in self-cleaning filter, selects filter in this system, substantially reduce energy consumption, save
About cost, while meeting the requirement of paste naval stores quality, the loss for reducing latex material reaches the production for improving paste resin
The purpose of energy.
2) structure of filter is relatively simple in the present invention, filters out the material for meeting production requirement for the first time by filter
Grain graininess, it is possible to reduce energy loss simplifies field operation procedures, screens remaining undesirable material centralized recovery
It recycles, further reduces the cost, improve the quality of paste resin.
3) structure of filtering baffle is simple in the present invention, and the filtering gear of different pore size filters can be replaced according to product requirement
Plate, the present invention in cleaning water inlet can be used for tap water cleaning filter interior, guarantee filter interior cleannes, filter
Being equipped with to clean can be used for manually cleaning filter interior into hole, when tap water equipment goes wrong and can not work normally, according to
Filter can so be cleaned, ensure that the normal work of filter in several situations, filter of the invention uses
Range is relatively broad, easy to operate, easy to maintenance.
Detailed description of the invention
Fig. 1 is the flow diagram for crossing polymeric latex filtering and discharging system in the prior art.
Fig. 2 is flow chart of the invention.
Fig. 3 is the structural schematic diagram of filter in the present invention.
The meaning of label symbol is as follows in figure:
10-14-feeding inlets of filter 11-tank body, 12-filtering baffle, 13-filter hole 15-clean into hole
16-17-slag-drip opening of discharge port, 18-flushing, 19-support columns of water inlet.
Specific embodiment
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation description, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.
The filtration system as shown in Fig. 2, a kind of polymeric latex discharges, which includes for producing after storing polymerization process
The polymeric latex slot of polymeric latex semi-finished product, and the finished product bin for storing finished product latex material, the polymeric latex slot with
Blowpit, filter, self-cleaning filter, latex slot, stripper and atomizer, institute are disposed between the finished product bin
It is successively each through the blowpit, filter, self-cleaning filter, latex slot, stripper and atomizer to state polymeric latex semi-finished product
Finished product latex material is obtained after processing unit processes, the finished product latex material storing is in the finished product bin.
Discharging pump is equipped between the polymeric latex slot and the blowpit, the discharging pump is for conveying the polymeric gel
Polymeric latex semi-finished product in newborn slot enter in blowpit；
Between the filter and the self-cleaning filter and between the self-cleaning filter and the latex slot
It is equipped with feeding engine, latex of the feeding engine for after conveying a processing unit processes enters next processing unit.
As shown in figure 3, the filter 10 includes tank body 11, the tank body 11, which is equipped with, rinses water inlet 18, feeding inlet
14, it cleans into hole 15, discharge port 16 and slag-drip opening 17, the flushing water inlet 18, is cleaned into hole 15, discharge port at feeding inlet 14
16 and the level height of slag-drip opening 17 successively reduce, the filtering baffle 12 for filtering latex, institute are equipped with inside the tank body 11
State filtering baffle 12 by the tank body 11 segmentation in filtering proparea and filtering back zone, the flushings water inlet 18, feeding inlet 14, clearly
Wash hole 15 and slag-drip opening 17 with filtering proparea connection, the discharge port 16 and filtering back zone connection, it is described enter
Material mouth 14 is connected with the blowpit, and the discharge port 16 is connected through the feeding engine with the self-cleaning filter.
The tank body 11 is the cylindrical body that upper/lower terminal is equipped with end socket, that is, upper cover and lower head, is set on the upper cover
Have and rinse water inlet 18, the lower head is equipped with slag-drip opening 17, and the flushing water inlet 18 is located at institute with the slag-drip opening 17
It states on the central axis of cylindrical body, the feeding inlet 14 and described cleans the side for being located at the cylindrical body into hole 15, the discharging
The other side of the cylindrical body is arranged in mouth 16, and the filtering baffle 12 is disposed in proximity to 16 side of discharge port and the circle
The central axis of cylinder is parallel.
The filtering baffle 12 is the stainless steel plate with a thickness of 6mm, and the filtering baffle 12 is equipped with filter hole 13, described
The bore dia of filter hole 13 is 7mm.
11 bottom of tank body is equipped with two support columns 19.
The course of work of the invention is as follows: in the latex semi-finished product storage polymeric latex slot obtained after polymerization process, through going out
Material pump is conveyed into blowpit, connects filter 10 by pipeline in blowpit rear end, the material in blowpit was directly entered
In filter, the material for obtaining meeting production requirement granular size after being filtered is pumped into self-cleaning filter through feeding
In, the material being obtained by filtration further is cleaned through self-cleaning filter to be pumped into latex slot through feeding, the material in latex slot
It is delivered in atomizer after stripper is handled, latex material finished product is obtained after the processing of atomizer atomization drying, and store extremely
In finished product bin.
The course of work of filter in the present invention: feeding inlet 14 and the discharge port 16 for being set to 11 two sides of filter tank body are logical
Piping is connect with blowpit and self-cleaning filter respectively, and material enters inside tank body 11 from feeding inlet 14, by being set to
Filtering proparea will be divided into inside tank body 11 between feeding inlet 14 and discharge port 16 and filter the filtering baffle filtering of back zone, general mistake
Filter gear 12 is the stainless steel plate with a thickness of 6mm, and filtering baffle 12 is equipped with the filter hole 13 that diameter is 7mm, from discharge port 16
Outflow enters next processing unit, and the cleaning water inlet 18 for being set to 11 top of tank body enters pipe with external tap water and connect, and makes
It can guarantee filter inner clean with tap water flush filter, be set to 11 bottom of filter tank body and setting and pushed up in tank body 11
Slag-drip opening 17 at the opposite position of cleaning water inlet 18 in portion is connect with scum pipe, remaining big from the discharge filtering of slag-drip opening 17
The processing of bulky grain latex centralized collection is set to and is located at the clear of 14 underface of feeding inlet on filter tank body 11 by particle latex
Hole 15 is washed for artificial cleaning filter interior.
Claims (5)
- The filtration system 1. a kind of polymeric latex discharges, the system include for store the polymeric latex produced after polymerization process half at The polymeric latex slot of product, and the finished product bin for storing finished product latex material, it is characterised in that: the polymeric latex slot and institute It states and is disposed with blowpit, filter, self-cleaning filter, latex slot, stripper and atomizer between finished product bin, it is described Polymeric latex semi-finished product successively through the blowpit, filter, self-cleaning filter, latex slot, stripper and atomizer everywhere Finished product latex material is obtained after reason cell processing, the finished product latex material storing is in the finished product bin；The filter (10) includes tank body (11), and the tank body (11), which is equipped with, rinses water inlet (18), feeding inlet (14), goes out Material mouth (16) and slag-drip opening (17), it is described rinse water inlet (18), feeding inlet (14), discharge port (16) and slag-drip opening (17) water Flat height successively reduces, and the filtering baffle (12) for filtering latex, the filtering baffle are equipped with inside the tank body (11) (12) by the tank body (11) inside division at filtering proparea and filtering back zone, the flushing water inlet (18), feeding inlet (14), With slag-drip opening (17) with filtering proparea connection, the discharge port (16) and filtering back zone connection, the feeding inlet (14) it is connected with the blowpit, the discharge port (16) is connected through feeding engine with the self-cleaning filter；The filtering baffle (12) is the stainless steel plate with a thickness of 6mm, and the filtering baffle (12) is equipped with filter hole (13), institute The bore dia for stating filter hole (13) is 7mm.
- The filtration system 2. polymeric latex as described in claim 1 discharges, it is characterised in that:Discharging pump is equipped between the polymeric latex slot and the blowpit, the discharging pump is for conveying the polymeric latex slot Interior polymeric latex semi-finished product enter in blowpit；It is all provided between the filter and the self-cleaning filter and between the self-cleaning filter and the latex slot There is feeding engine, latex of the feeding engine for after conveying a processing unit processes enters next processing unit.
- The filtration system 3. polymeric latex as described in claim 1 discharges, it is characterised in that: be additionally provided on the tank body (11) clear It washes hole (15), it is described to clean the level height for being lower than the feeding inlet (14) into the level height of hole (15), it is higher than the row The level height of cinder notch (17), it is described to clean into hole (15) and filtering proparea connection.
- The filtration system 4. polymeric latex as claimed in claim 3 discharges, it is characterised in that: the tank body (11) is upper and lower two End is equipped with the cylindrical body of end socket, that is, upper cover and lower head, and the upper cover, which is equipped with, rinses water inlet (18), the lower head It being equipped with slag-drip opening (17), flushing water inlet (18) and the slag-drip opening (17) are located on the central axis of the cylindrical body, The feeding inlet (14) and it is described clean the side that the cylindrical body is located at into hole (15), the discharge port (16) is arranged described The other side of cylindrical body, the filtering baffle (12) are disposed in proximity to the center of the discharge port (16) side and the cylindrical body Axis is parallel.
- The filtration system 5. polymeric latex as described in claim 1 discharges, it is characterised in that: tank body (11) bottom is equipped with two Support column (19).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610476140.5A CN106039796B (en) | 2016-06-23 | 2016-06-23 | A kind of polymeric latex discharging filtration system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610476140.5A CN106039796B (en) | 2016-06-23 | 2016-06-23 | A kind of polymeric latex discharging filtration system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106039796A CN106039796A (en) | 2016-10-26 |
| CN106039796B true CN106039796B (en) | 2019-05-21 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610476140.5A Active CN106039796B (en) | 2016-06-23 | 2016-06-23 | A kind of polymeric latex discharging filtration system |
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| Country | Link |
|---|---|
| CN (1) | CN106039796B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111760377A (en) * | 2020-07-09 | 2020-10-13 | 唐山三友氯碱有限责任公司 | Latex conveying system and method in production process of special resin for polyvinyl chloride |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202962028U (en) * | 2012-09-26 | 2013-06-05 | 吴旭东 | Sewage filter |
| CN204202019U (en) * | 2014-10-24 | 2015-03-11 | 南京优能空调系统有限公司 | A kind of mixed water pot |
| CN104497178A (en) * | 2014-12-15 | 2015-04-08 | 天津渤天化工有限责任公司 | Method for preparing low-viscosity paste resin |
| CN105622825A (en) * | 2016-04-06 | 2016-06-01 | 辽宁方大工程设计有限公司 | Device and technique for producing polyvinyl chloride copolymer paste resin and application of polyvinyl chloride copolymer paste resin |
-
2016
- 2016-06-23 CN CN201610476140.5A patent/CN106039796B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202962028U (en) * | 2012-09-26 | 2013-06-05 | 吴旭东 | Sewage filter |
| CN204202019U (en) * | 2014-10-24 | 2015-03-11 | 南京优能空调系统有限公司 | A kind of mixed water pot |
| CN104497178A (en) * | 2014-12-15 | 2015-04-08 | 天津渤天化工有限责任公司 | Method for preparing low-viscosity paste resin |
| CN105622825A (en) * | 2016-04-06 | 2016-06-01 | 辽宁方大工程设计有限公司 | Device and technique for producing polyvinyl chloride copolymer paste resin and application of polyvinyl chloride copolymer paste resin |
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| Publication number | Publication date |
|---|---|
| CN106039796A (en) | 2016-10-26 |
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| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of invention: Polymerizing latex discharge material filtering system Effective date of registration: 20191205 Granted publication date: 20190521 Pledgee: Huizhou merchant bank, Hefei Taihu Road Branch Pledgor: ANHUI TIANCHEN CHEMICAL Co.,Ltd. Registration number: Y2019980000884 |
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Date of cancellation: 20220721 Granted publication date: 20190521 Pledgee: Huizhou merchant bank, Hefei Taihu Road Branch Pledgor: ANHUI TIANCHEN CHEMICAL Co.,Ltd. Registration number: Y2019980000884 |
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Address after: 230000 North side of Hongtu Avenue, Hefei Circular Economy Demonstration Park, Feidong County, Hefei City, Anhui Province Patentee after: China Salt Anhui Tianchen Chemical Co.,Ltd. Address before: 230000 North side of Hongtu Avenue, Hefei Circular Economy Demonstration Park, Feidong County, Hefei City, Anhui Province Patentee before: ANHUI TIANCHEN CHEMICAL Co.,Ltd. |
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