KR20170026780A - Filter plate for filter press - Google Patents

Filter plate for filter press Download PDF

Info

Publication number
KR20170026780A
KR20170026780A KR1020150121232A KR20150121232A KR20170026780A KR 20170026780 A KR20170026780 A KR 20170026780A KR 1020150121232 A KR1020150121232 A KR 1020150121232A KR 20150121232 A KR20150121232 A KR 20150121232A KR 20170026780 A KR20170026780 A KR 20170026780A
Authority
KR
South Korea
Prior art keywords
ceramic filler
glass fiber
silica
tensile strength
range
Prior art date
Application number
KR1020150121232A
Other languages
Korean (ko)
Other versions
KR101818433B1 (en
Inventor
우현직
송태규
이민철
김영선
김영곤
심상은
Original Assignee
(주)동일캔바스엔지니어링
인하대학교 산학협력단
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by (주)동일캔바스엔지니어링, 인하대학교 산학협력단 filed Critical (주)동일캔바스엔지니어링
Priority to KR1020150121232A priority Critical patent/KR101818433B1/en
Publication of KR20170026780A publication Critical patent/KR20170026780A/en
Application granted granted Critical
Publication of KR101818433B1 publication Critical patent/KR101818433B1/en

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/12Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/121Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
    • C02F11/122Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering using filter presses
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D25/00Filters formed by clamping together several filtering elements or parts of such elements
    • B01D25/12Filter presses, i.e. of the plate or plate and frame type

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

The present invention provides a filter plate for a filter press made of a mixture of a ceramic filler and a polymer resin. The ceramic filler may be at least one selected from the group consisting of silica, glass fiber, calcium carbonate, carbon black, limestone powder and kaolin. The polymer resin may be at least one selected from the group consisting of polypropylene, polyethylene, polystyrene, polyester, acrylonitrile butadiene styrene , Polycarbonate, and nylon. The ceramic filler is dispersed in the course of mixing with the polymer resin, thereby improving the tensile strength of the filter plate for the filter press.

Description

{FILTER PLATE FOR FILTER PRESS}

The present invention relates to a filter plate for a filter press, and more particularly to a filter plate for a filter press having excellent mechanical strength and chemical resistance.

At present, the sewage discharged from homes and factories is sent to the sewage treatment plant and processed. The sewage treatment process includes a purification process and a sludge treatment process. In the purification process, the sewage is purified to a range where the self-purification of the river can be activated and discharged to a public water such as a river. In the sludge treatment process, The sludge is treated through processes such as concentration and dehydration.

A dehydrator, which is one of the devices used in the sludge treatment process, separates the filtrate from the sludge and is classified into a belt press, a filter press, a screw press, a centrifugal dehydrator, and an electroosmotic dehydrator according to the operation principle. Among them, the filter press is a device for removing the sludge cake (filtrate and separated sludge) from the compartment after pressurizing the compartment sludge provided between the filter plates which are in close contact with each other to separate the filtrate from the sludge.

In the filter press, the pressure of the sludge is applied to the filter plates during dehydration of the sludge, and the pressure input to the filter plates is released when the dehydration of the sludge is completed. Therefore, in the filter press, the action and release of high pressure on the filter plate are repeatedly performed, and the filter plate of the filter press needs to have a mechanical strength capable of withstanding repeated pressure changes. In addition, since the filter plate of the filter press is inevitably in constant contact with the organic / inorganic wastewater and air, it is also necessary to provide chemical resistance.

Korean Patent Laid-Open No. 10-2008-0018168 (Membrane plate for filter press) Korean Patent Laid-Open No. 10-2008-0018167 (Chamber Filter Plate) Korean Patent Laid-Open No. 10-2008-0011295 (heating and cooling filter plate)

SUMMARY OF THE INVENTION The present invention has been made in view of the above needs, and it is an object of the present invention to provide a filter plate for a filter press having excellent mechanical strength and chemical resistance, more specifically, a material for the filter plate.

The present invention provides a filter plate for a filter press made of a mixture of a ceramic filler and a polymer resin. The ceramic filler may be at least one selected from the group consisting of silica, glass fiber, calcium carbonate, carbon black, limestone powder and kaolin. The polymer resin may be at least one selected from the group consisting of polypropylene, polyethylene, polystyrene, polyester, acrylonitrile butadiene styrene , Polycarbonate, and nylon. The ceramic filler is dispersed in the course of mixing with the polymer resin, thereby improving the tensile strength of the filter plate for the filter press.

When calcium carbonate and glass fiber are used as the ceramic filler, the weight of the calcium carbonate is preferably in the range of 1 to 6 times the weight of the glass fiber. Then, the tensile strength of the filter plate for the filter press can be set within the range of 48.72 MPa to 58.61 MPa, which is larger than the tensile strength of the filter plate for the filter press made of only polymer, which is 47.31 MPa. At this time, the content of the ceramic filler with respect to the mixture is preferably in the range of 10 wt% to 20 wt%, and if it is out of this range, the tensile strength may be lower than that of the filter plate made of only polymer.

The ceramic filler may be surface treated with a ceramic surface treatment agent selected from the group consisting of APS, EHTMS, MPA and VTMS. The ceramic surface treatment agent serves to help the ceramic filler to be more uniformly dispersed.

When the ceramic filler is a surface-treated silica, the content of the ceramic filler in the mixture is preferably 20 wt%. Then, the tensile strength of the filter plate for the filter press can be formed within the range of 51.86 MPa to 52.88 MPa, which is larger than the tensile strength of the filter plate for the filter press made of only polymer.

When the surface-treated silica and the glass fiber are used as the ceramic filler, the weight of the glass fiber is preferably in the range of 1 to 2 times the weight of the surface-treated silica. In this case, the tensile strength of the filter plate for the filter press can be formed within the range of 53.68 MPa to 81.46 MPa, which is larger than the tensile strength of the filter plate for the filter press made of only a polymer material. At this time, it is preferable that the content of the ceramic filler to the mixture is in the range of 10 wt% to 40 wt%, otherwise the tensile strength of the filter plate for the filter press made of only polymer may be lowered.

When the surface-treated silica and the glass fiber are used as the ceramic filler, the weight of the surface-treated silica may be in the range of 2 to 4 times the weight of the glass fiber. In this case, the tensile strength of the filter plate for the filter press can be formed within the range of 49.89 MPa to 65.56 MPa. At this time, it is preferable that the content of the ceramic filler in the mixture is in the range of 10 wt% to 30 wt%, otherwise the tensile strength of the filter plate for the filter press made of only polymer can be lowered.

The filter plate for a filter press according to the present invention has excellent tensile strength and chemical resistance as compared with a filter plate for a filter press made of only polymer water.

1 shows the results of tensile strength test and chemical resistance test of the composite specimen according to Example 1 of the present invention.
2 shows the results of the tensile strength test and the chemical resistance test of the composite specimen according to Example 2 of the present invention.
3 shows the results of tensile strength test and chemical resistance test of the composite specimen according to Example 3 of the present invention.
4 shows the results of the tensile strength test and chemical resistance test of the composite specimen according to Example 4 of the present invention.

Hereinafter, preferred embodiments of the filter plate for a filter press according to the present invention will be described in detail. It is to be understood that the terminology or words used herein are not to be construed in an ordinary sense or a dictionary, and that the inventor can properly define the concept of a term to describe its invention in the best possible way And should be construed in accordance with the meaning and concept consistent with the technical idea of the present invention.

Example  1 (surface treated silica / polypropylene composite)

160 g of methanol having a purity of 99.9%, 9 g of acetic acid, and 1 g of APS (N-2- (aminoethyl) -3-aminopropyltrimethoxysilane) as a ceramic surface treatment agent were stirred for 30 minutes to prepare a mixed solution. Then, 20 g of silica having a diameter of 6 micrometers was added to the mixed solution, stirred for 2 hours, and then silica was filtered out and dried. During the drying process, both methanol and acetic acid are vaporized, and APS chemically reacts with silica and remains on the surface of silica.

11 g of the surface-treated 6-micrometer-diameter silica was mixed with 44 g of pellet-shaped polypropylene in an airtight mixer at a temperature of 220 ° C and a screw rotation speed of 100 rpm for 15 minutes to form a composite And the silica content was 20 wt%). The composite was placed in a stainless steel mold, and thermocompression was performed at 220 ° C and 4600 psi to prepare a composite specimen. In addition, two composite specimens were further prepared by replacing only the ceramic surface treatment agent with EHTMS and MPA while keeping the other conditions intact.

EHTMS (2- (3, 4epoxycyclohexyl) ethyltrimethoxysilane)

MPA (3-methacryloxypropyltrimethoxysilane)

The tensile strength test and the chemical resistance test were performed on the three composite specimens prepared as described above, and the results are shown in FIG. The tensile strength test was conducted according to ASTM D638-10. In the chemical resistance test, if the tensile strength of the composite specimen immersed in anaerobic wastewater for 2 months decreased to within 7% of the tensile strength of the composite specimen before immersing, it was judged to pass or fail.

Referring to FIG. 1, it can be seen that the composite specimens according to the present embodiment have a tensile strength in the range of 51.86 MPa to 52.58 MPa. Also, referring to FIG. 1, it can be seen that the chemical compositions of the composite specimens according to the present embodiment are all acceptable.

Example  2 (silica / polypropylene / Surface treatment agent  Complex)

11 g of silica having a diameter of 6 micrometers, 44 g of polypropylene in the form of pellets, and 0.55 g of APS were mixed in a closed mixer at a temperature of 220 DEG C and a screw rotating speed of 100 rpm for 15 minutes and then dried to form a composite. APS chemically reacts with silica in the mixing process and remains on the surface of silica, and unreacted APS is vaporized during the drying process.

The composite (20 wt% silica content of the composite) was put into a stainless steel mold and thermocompression bonded at 220 ° C and 4600 psi to prepare a composite specimen. In addition, two composite specimens were further prepared by replacing only the ceramic surface treatment agent with EHTMS and MPA while keeping the other conditions intact.

The tensile strength test and the chemical resistance test were carried out on the three composite specimens prepared as described above, and the results are shown in Fig. The tensile strength test and the chemical resistance test were carried out in the same manner as in Example 1.

Referring to FIG. 2, the composite specimens according to the present embodiment have a tensile strength in the range of 51.99 MPa to 52.88 MPa. In addition, referring to FIG. 2, it can be seen that the chemical resistance of the composite specimens according to the present embodiment is all acceptable.

Example  3 (silica / glass fiber / polypropylene / Surface treatment agent  Complex)

6 g of silica with a diameter of 6 micrometers, 12 g of glass fiber glass strand masterbatch (90% of glass fiber weight), 42 g of polypropylene in the form of pellets and 0.3 g of APS were mixed in a closed mixer at a temperature of 220 캜 and a screw rotation speed of 100 rpm Minute, followed by drying to form a complex. APS chemically reacts with silica in the mixing process and remains on the surface of silica, and unreacted APS is vaporized during the drying process.

These composites (silica and glass fiber weight ratio 1: 2, silica and glass fiber content 30wt% to the composite) were placed in a stainless steel mold and thermocompression bonded at 220 ° C and 4600 psi to produce composite specimens. Three composite specimens were further prepared by replacing only the ceramic surface treatment agent with EHTMS, MPA, and VTMS (Vinyltrimethoxysilane) while the other conditions remained unchanged.

The tensile strength test and the chemical resistance test were carried out on the four composite specimens thus prepared in the same manner as in Example 1, and the results are shown in Fig. Referring to FIG. 3, it can be seen that the above four composite specimens have a tensile strength in the range of 68.18 MPa to 73.15 MPa, and the chemical resistance is all acceptable.

On the other hand, in the present embodiment, the ceramic surface treatment agent was changed to APS and the 11 kinds of silica-glass fibers having a silica diameter of 6 micrometers and a weight ratio of silica and glass fiber, Composite specimens were further prepared, and tensile strength tests and chemical resistance tests were carried out for each composite specimen in the same manner as in Example 1.

Of these 11 composite specimens, the silica and glass fiber contents were 40 wt%, the weight ratio of silica to glass fiber was 2: 1, the content of silica and glass fiber was 40 wt%, and the weight ratio of silica and glass fiber was 4: 1, the tensile strength in the range of 49.89 MPa to 81.46 MPa is shown in FIG. In addition, it can be seen that the chemical resistance of the above 11 composite specimens are all acceptable.

Example  4 (calcium carbonate / glass fiber / polypropylene composite)

6 g of calcium carbonate, 6 g of a glass fiber cord strand master batch (90% of glass fiber weight) and 48 g of pellet-shaped polypropylene were mixed in a closed type mixer at 220 캜 and 100 rpm screw rotation speed for 15 minutes to form a composite. Then, this composite (calcium carbonate and glass fiber weight ratio 1: 1, calcium carbonate and glass fiber content 20wt% for the composite) was placed in a stainless steel mold and thermocompression bonded at 220 ° C. and 4600 psi to prepare a composite specimen. In addition, one composite specimen was prepared by changing the content of calcium carbonate and glass fiber to 10 wt%, while keeping the other conditions intact. Six composite specimens were also prepared by changing the weight ratio of calcium carbonate to glass fiber to 2: 1, 4: 1 and 6: 1 for each of the two composites.

The tensile strength test and the chemical resistance test were conducted on the eight composite specimens thus prepared in the same manner as in Example 1, and the results are shown in FIG. Referring to FIG. 4, it can be seen that the above eight composite specimens have a tensile strength in the range of 48.72 MPa to 58.61 MPa, and the chemical resistance is all acceptable.

Comparative Example  (Polypropylene)

52 g of pelletized polypropylene was mixed in a closed mixer at a temperature of 220 ° C and a screw rotation speed of 100 rpm for 7 minutes. The mixture was placed in a stainless steel mold and thermocompression-bonded at 220 ° C. and 4600 psi to prepare a polypropylene sample.

The tensile strength test and the chemical resistance test were carried out on the polypropylene sample thus prepared in the same manner as in Example 1. As a result, it was confirmed that the polypropylene sample had a tensile strength of 47.31 MPa and the chemical resistance was confirmed to be acceptable .

The tensile strength of the polypropylene specimen is smaller than the tensile strength of the three composite specimens of Example 1, the tensile strength of the three composite specimens of Example 2 and the tensile strength of the eight composite specimens of Example 4. The tensile strengths of the polypropylene specimens were the same as in Example 3 except that two of the fifteen composite specimens of Example 3 (having a silica and glass fiber content of 40 wt% and a weight ratio of silica to glass fiber of 2: 1, Is 40 wt% and the weight ratio of silica to glass fiber is 4: 1) than the tensile strength of the 13 composite specimens.

While the present invention has been particularly shown and described with reference to exemplary embodiments thereof, it is to be understood that the invention is not limited to the disclosed exemplary embodiments. It is to be understood that various changes and modifications may be made without departing from the scope of the appended claims.

none

Claims (9)

A mixture of a ceramic filler and a polymer resin,
Wherein the ceramic filler is at least one selected from the group consisting of silica, glass fiber, calcium carbonate, carbon black, limestone powder and kaolin, and the polymer resin is selected from the group consisting of polypropylene, polyethylene, polystyrene, polyester, acrylonitrile butadiene styrene, A filter plate for a filter press employing one or more of the group consisting of carbonates and nylons.
The method according to claim 1,
Wherein when calcium carbonate and glass fiber are used as the ceramic filler, the weight of the calcium carbonate is in the range of 1 to 6 times the weight of the glass fiber.
3. The method of claim 2,
Wherein the content of the ceramic filler in the mixture is in the range of 10 wt% to 20 wt%.
The method according to claim 1,
Wherein the ceramic filler is surface treated with a ceramic surface treatment agent selected from the group consisting of APS, EHTMS, MPA and VTMS.
5. The method of claim 4,
Wherein when the ceramic filler is a surface-treated silica, the content of the ceramic filler relative to the mixture is 20 wt%.
5. The method of claim 4,
Wherein when the surface-treated silica and glass fiber are used as the ceramic filler, the weight of the glass fiber is in the range of 1 to 2 times the weight of the surface-treated silica.
The method according to claim 6,
Wherein the content of the ceramic filler in the mixture is in the range of 10 wt% to 40 wt%.
5. The method of claim 4,
Wherein when the surface-treated silica and glass fiber are used as the ceramic filler, the weight of the surface-treated silica is in the range of 2 to 4 times the weight of the glass fiber.
9. The method of claim 8,
Wherein the content of the ceramic filler in the mixture is in a range of 10 wt% to 30 wt%.
KR1020150121232A 2015-08-27 2015-08-27 Filter plate for filter press KR101818433B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1020150121232A KR101818433B1 (en) 2015-08-27 2015-08-27 Filter plate for filter press

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1020150121232A KR101818433B1 (en) 2015-08-27 2015-08-27 Filter plate for filter press

Publications (2)

Publication Number Publication Date
KR20170026780A true KR20170026780A (en) 2017-03-09
KR101818433B1 KR101818433B1 (en) 2018-01-22

Family

ID=58402788

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1020150121232A KR101818433B1 (en) 2015-08-27 2015-08-27 Filter plate for filter press

Country Status (1)

Country Link
KR (1) KR101818433B1 (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20080011295A (en) 2005-04-22 2008-02-01 여트파우카 필트라치온 지스템스 게엠베하 Filter plate that can be cooled and heated
KR20080018168A (en) 2005-04-25 2008-02-27 여트파우카 필트라치온 지스템스 게엠베하 Membrane plate for a filter press
KR20080018167A (en) 2005-04-20 2008-02-27 여트파우카 필트라치온 지스템스 게엠베하 Chamber filter plate

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000000407A (en) * 1998-06-17 2000-01-07 Mitsubishi Plastics Ind Ltd Thermoplastic-resin filter plate

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20080018167A (en) 2005-04-20 2008-02-27 여트파우카 필트라치온 지스템스 게엠베하 Chamber filter plate
KR20080011295A (en) 2005-04-22 2008-02-01 여트파우카 필트라치온 지스템스 게엠베하 Filter plate that can be cooled and heated
KR20080018168A (en) 2005-04-25 2008-02-27 여트파우카 필트라치온 지스템스 게엠베하 Membrane plate for a filter press

Also Published As

Publication number Publication date
KR101818433B1 (en) 2018-01-22

Similar Documents

Publication Publication Date Title
Goes et al. Polyurethane foams synthesized from cellulose-based wastes: Kinetics studies of dye adsorption
WO2014014458A1 (en) Recycling carbon fibers from epoxy using solvent cracking
CN107082962A (en) Automotive trim is with low VOC PP composite materials
CN107855118A (en) A kind of environment-friendly dye sewage-treating agent and preparation method thereof
Cao et al. Wool graft polyacrylamidoxime as the adsorbent for both cationic and anionic toxic ions from aqueous solutions
Selambakkannu et al. Modification of radiation grafted banana trunk fibers for adsorption of anionic dyes
KR101818433B1 (en) Filter plate for filter press
Velu et al. Removal of organic and inorganic substances from industry wastewaters using modified aluminosilicate‐based polyethersulfone ultrafiltration membranes
CN114080402A (en) Acrylic rubber having excellent water resistance
CN109824804B (en) Preparation method of chlorinated polyethylene rubber
CN107376670A (en) A kind of nano-TiO2Modified PE O/PVDF composite hyperfiltration membranes and preparation method
Zhu et al. Microfluidic synthesis of renewable biosorbent with highly comprehensive adsorption performance for copper (II)
KR101712813B1 (en) Method for preparing filter
Herrera-Gonzalez et al. Adsorption of anionic dyes using composites based on basic polyelectrolytes and physically activated carbon
Dai et al. High hydrophilicity and excellent adsorption ability of a stretched polypropylene/graphene oxide composite membrane achieved by plasma assisted surface modification
CN106984289B (en) A kind of preparation method of porous ceramic surface perfluoro caprylic acid molecular imprinting adsorbing agent
EP3277626B1 (en) Treating sulfuric acid
Xue et al. Synthesis of polyurethane containing carbon–carbon double bonds to prepare functionalizable ultrafine fibers via electrospinning
George et al. Separation of alkane–acetone mixtures using styrene–butadiene rubber/natural rubber blend membranes
CN106939086B (en) A kind of purification process of aged resin
Mangindaan et al. Diaminoethane-crosslinked polyetherimide nanofiltration membrane for textile wastewater dye removal
CN112125375A (en) Preparation method of palladium-wood film capable of synchronously performing oil-water separation and dye degradation
Samad et al. Preparation of ENR/PVC/RH Composite Membrane for Water Permeation Application
KR101746583B1 (en) The method of manufacturing cellulose fiber with bagasse
JPH11181328A (en) Additive for resin

Legal Events

Date Code Title Description
A201 Request for examination
E902 Notification of reason for refusal