KR20090008117A - Biodegradable Base Resin Composition Using Biodegradable Polymer and Fine Calcium Carbonate and Manufacturing Method Thereof - Google Patents
Biodegradable Base Resin Composition Using Biodegradable Polymer and Fine Calcium Carbonate and Manufacturing Method Thereof Download PDFInfo
- Publication number
- KR20090008117A KR20090008117A KR1020080050826A KR20080050826A KR20090008117A KR 20090008117 A KR20090008117 A KR 20090008117A KR 1020080050826 A KR1020080050826 A KR 1020080050826A KR 20080050826 A KR20080050826 A KR 20080050826A KR 20090008117 A KR20090008117 A KR 20090008117A
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- Prior art keywords
- calcium carbonate
- biodegradable
- weight
- starch
- resin composition
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- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 title claims abstract description 67
- 229910000019 calcium carbonate Inorganic materials 0.000 title claims abstract description 33
- 239000011342 resin composition Substances 0.000 title claims abstract description 32
- 229920002988 biodegradable polymer Polymers 0.000 title claims abstract description 23
- 239000004621 biodegradable polymer Substances 0.000 title claims abstract description 23
- 238000004519 manufacturing process Methods 0.000 title claims description 8
- 229920002472 Starch Polymers 0.000 claims abstract description 32
- 239000008107 starch Substances 0.000 claims abstract description 30
- 235000019698 starch Nutrition 0.000 claims abstract description 30
- 238000002156 mixing Methods 0.000 claims abstract description 14
- 239000000203 mixture Substances 0.000 claims abstract description 14
- 239000000314 lubricant Substances 0.000 claims abstract description 12
- 239000004014 plasticizer Substances 0.000 claims abstract description 12
- 229920005989 resin Polymers 0.000 claims abstract description 6
- 239000011347 resin Substances 0.000 claims abstract description 6
- 239000002994 raw material Substances 0.000 claims description 28
- 239000000463 material Substances 0.000 claims description 17
- 238000000034 method Methods 0.000 claims description 10
- 238000012545 processing Methods 0.000 claims description 10
- 229920000331 Polyhydroxybutyrate Polymers 0.000 claims description 9
- 239000005015 poly(hydroxybutyrate) Substances 0.000 claims description 9
- 229920002961 polybutylene succinate Polymers 0.000 claims description 9
- 239000004631 polybutylene succinate Substances 0.000 claims description 9
- 229920001610 polycaprolactone Polymers 0.000 claims description 9
- 239000004632 polycaprolactone Substances 0.000 claims description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- 239000002245 particle Substances 0.000 claims description 7
- 239000008188 pellet Substances 0.000 claims description 7
- 229920003232 aliphatic polyester Polymers 0.000 claims description 6
- 238000005520 cutting process Methods 0.000 claims description 6
- 239000012188 paraffin wax Substances 0.000 claims description 6
- 238000004898 kneading Methods 0.000 claims description 5
- 230000004048 modification Effects 0.000 claims description 5
- 238000012986 modification Methods 0.000 claims description 5
- 239000000843 powder Substances 0.000 claims description 5
- 229920002261 Corn starch Polymers 0.000 claims description 4
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 4
- 239000004372 Polyvinyl alcohol Substances 0.000 claims description 4
- 239000008120 corn starch Substances 0.000 claims description 4
- 239000004626 polylactic acid Substances 0.000 claims description 4
- 229920002451 polyvinyl alcohol Polymers 0.000 claims description 4
- 230000008569 process Effects 0.000 claims description 4
- 239000001993 wax Substances 0.000 claims description 4
- 239000004342 Benzoyl peroxide Substances 0.000 claims description 3
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical compound C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-N 0.000 claims description 3
- FBPFZTCFMRRESA-FSIIMWSLSA-N D-Glucitol Natural products OC[C@H](O)[C@H](O)[C@@H](O)[C@H](O)CO FBPFZTCFMRRESA-FSIIMWSLSA-N 0.000 claims description 3
- 240000003183 Manihot esculenta Species 0.000 claims description 3
- 235000016735 Manihot esculenta subsp esculenta Nutrition 0.000 claims description 3
- 235000019400 benzoyl peroxide Nutrition 0.000 claims description 3
- 239000011230 binding agent Substances 0.000 claims description 3
- 239000011256 inorganic filler Substances 0.000 claims description 3
- 229910003475 inorganic filler Inorganic materials 0.000 claims description 3
- 229940057995 liquid paraffin Drugs 0.000 claims description 3
- 239000005014 poly(hydroxyalkanoate) Substances 0.000 claims description 3
- -1 polybutylene succinate Polymers 0.000 claims description 3
- 239000000600 sorbitol Substances 0.000 claims description 3
- 239000000126 substance Substances 0.000 claims description 3
- 229940070710 valerate Drugs 0.000 claims description 3
- NQPDZGIKBAWPEJ-UHFFFAOYSA-N valeric acid Chemical compound CCCCC(O)=O NQPDZGIKBAWPEJ-UHFFFAOYSA-N 0.000 claims description 3
- XOOUIPVCVHRTMJ-UHFFFAOYSA-L zinc stearate Chemical compound [Zn+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O XOOUIPVCVHRTMJ-UHFFFAOYSA-L 0.000 claims description 3
- QMMJWQMCMRUYTG-UHFFFAOYSA-N 1,2,4,5-tetrachloro-3-(trifluoromethyl)benzene Chemical compound FC(F)(F)C1=C(Cl)C(Cl)=CC(Cl)=C1Cl QMMJWQMCMRUYTG-UHFFFAOYSA-N 0.000 claims description 2
- VBICKXHEKHSIBG-UHFFFAOYSA-N 1-monostearoylglycerol Chemical compound CCCCCCCCCCCCCCCCCC(=O)OCC(O)CO VBICKXHEKHSIBG-UHFFFAOYSA-N 0.000 claims description 2
- FBPFZTCFMRRESA-JGWLITMVSA-N D-glucitol Chemical compound OC[C@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-JGWLITMVSA-N 0.000 claims description 2
- 244000017020 Ipomoea batatas Species 0.000 claims description 2
- 235000002678 Ipomoea batatas Nutrition 0.000 claims description 2
- 235000013871 bee wax Nutrition 0.000 claims description 2
- 239000012166 beeswax Substances 0.000 claims description 2
- RWCCWEUUXYIKHB-UHFFFAOYSA-N benzophenone Chemical compound C=1C=CC=CC=1C(=O)C1=CC=CC=C1 RWCCWEUUXYIKHB-UHFFFAOYSA-N 0.000 claims description 2
- 239000012965 benzophenone Substances 0.000 claims description 2
- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical group [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 claims description 2
- 239000008116 calcium stearate Substances 0.000 claims description 2
- 235000013539 calcium stearate Nutrition 0.000 claims description 2
- 239000004204 candelilla wax Substances 0.000 claims description 2
- 235000013868 candelilla wax Nutrition 0.000 claims description 2
- 229940073532 candelilla wax Drugs 0.000 claims description 2
- 238000007599 discharging Methods 0.000 claims description 2
- 239000000839 emulsion Substances 0.000 claims description 2
- 235000011187 glycerol Nutrition 0.000 claims description 2
- IUJAMGNYPWYUPM-UHFFFAOYSA-N hentriacontane Chemical compound CCCCCCCCCCCCCCCCCCCCCCCCCCCCCCC IUJAMGNYPWYUPM-UHFFFAOYSA-N 0.000 claims description 2
- CKQVRZJOMJRTOY-UHFFFAOYSA-N octadecanoic acid;propane-1,2,3-triol Chemical compound OCC(O)CO.CCCCCCCCCCCCCCCCCC(O)=O CKQVRZJOMJRTOY-UHFFFAOYSA-N 0.000 claims description 2
- 239000007787 solid Substances 0.000 claims description 2
- 229940100445 wheat starch Drugs 0.000 claims description 2
- 229920001592 potato starch Polymers 0.000 claims 2
- 239000007788 liquid Substances 0.000 claims 1
- 229940100486 rice starch Drugs 0.000 claims 1
- 230000000704 physical effect Effects 0.000 abstract description 14
- 238000004806 packaging method and process Methods 0.000 abstract description 5
- 229920000642 polymer Polymers 0.000 abstract description 5
- 239000005022 packaging material Substances 0.000 description 7
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- 230000009467 reduction Effects 0.000 description 5
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- 238000003912 environmental pollution Methods 0.000 description 3
- 238000002347 injection Methods 0.000 description 3
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- 239000002952 polymeric resin Substances 0.000 description 3
- 238000011160 research Methods 0.000 description 3
- 229920001169 thermoplastic Polymers 0.000 description 3
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 3
- 229920002554 vinyl polymer Polymers 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 230000002411 adverse Effects 0.000 description 2
- 229920006167 biodegradable resin Polymers 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
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- 229910010272 inorganic material Inorganic materials 0.000 description 2
- 239000011147 inorganic material Substances 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 229920003002 synthetic resin Polymers 0.000 description 2
- 239000011882 ultra-fine particle Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 description 1
- 229920002749 Bacterial cellulose Polymers 0.000 description 1
- 229920002101 Chitin Polymers 0.000 description 1
- 229920001661 Chitosan Polymers 0.000 description 1
- 102000008186 Collagen Human genes 0.000 description 1
- 108010035532 Collagen Proteins 0.000 description 1
- 239000004594 Masterbatch (MB) Substances 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 208000034530 PLAA-associated neurodevelopmental disease Diseases 0.000 description 1
- 244000061456 Solanum tuberosum Species 0.000 description 1
- 235000002595 Solanum tuberosum Nutrition 0.000 description 1
- 229920006328 Styrofoam Polymers 0.000 description 1
- 241000209140 Triticum Species 0.000 description 1
- 235000021307 Triticum Nutrition 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 239000000783 alginic acid Substances 0.000 description 1
- 229920000615 alginic acid Polymers 0.000 description 1
- 235000010443 alginic acid Nutrition 0.000 description 1
- 229960001126 alginic acid Drugs 0.000 description 1
- 150000004781 alginic acids Chemical class 0.000 description 1
- 239000005016 bacterial cellulose Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000000861 blow drying Methods 0.000 description 1
- 239000000872 buffer Substances 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000010000 carbonizing Methods 0.000 description 1
- 235000013339 cereals Nutrition 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 229920001436 collagen Polymers 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000002860 competitive effect Effects 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
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- 235000005822 corn Nutrition 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 229920006237 degradable polymer Polymers 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- UKMSUNONTOPOIO-UHFFFAOYSA-N docosanoic acid Chemical class CCCCCCCCCCCCCCCCCCCCCC(O)=O UKMSUNONTOPOIO-UHFFFAOYSA-N 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 239000002657 fibrous material Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 230000003054 hormonal effect Effects 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 238000005461 lubrication Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 239000006259 organic additive Substances 0.000 description 1
- 229940056211 paraffin Drugs 0.000 description 1
- 239000013502 plastic waste Substances 0.000 description 1
- 229920001308 poly(aminoacid) Polymers 0.000 description 1
- 229920000747 poly(lactic acid) Polymers 0.000 description 1
- 229920000903 polyhydroxyalkanoate Polymers 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 239000004016 soil organic matter Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000008261 styrofoam Substances 0.000 description 1
- 230000009469 supplementation Effects 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
- 230000003313 weakening effect Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/18—Manufacture of films or sheets
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/01—Use of inorganic substances as compounding ingredients characterized by their specific function
- C08K3/013—Fillers, pigments or reinforcing additives
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/18—Oxygen-containing compounds, e.g. metal carbonyls
- C08K3/24—Acids; Salts thereof
- C08K3/26—Carbonates; Bicarbonates
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/0008—Organic ingredients according to more than one of the "one dot" groups of C08K5/01 - C08K5/59
- C08K5/0016—Plasticisers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/04—Oxygen-containing compounds
- C08K5/05—Alcohols; Metal alcoholates
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K7/00—Use of ingredients characterised by shape
- C08K7/16—Solid spheres
- C08K7/18—Solid spheres inorganic
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L3/00—Compositions of starch, amylose or amylopectin or of their derivatives or degradation products
- C08L3/02—Starch; Degradation products thereof, e.g. dextrin
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L67/00—Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/18—Oxygen-containing compounds, e.g. metal carbonyls
- C08K3/24—Acids; Salts thereof
- C08K3/26—Carbonates; Bicarbonates
- C08K2003/265—Calcium, strontium or barium carbonate
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2201/00—Properties
- C08L2201/06—Biodegradable
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- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Biological Depolymerization Polymers (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
본 발명은 미세 탄산칼슘을 주재료로 하여 초미세 탄산칼슘, 생분해성 고분자, 전분, 가소제, 윤활제, 상용화제를 이용하여 제조한 이용한 생분해 베이스 레진 조성물에 관한 것으로, 미세탄산칼슘 5 내지 50 중량%, 초미세 탄산칼슘 5 내지 40 중량%, 생분해성 고분자 5 내지 60 중량%, 전분 5 내지 50 중량%, 가소제 1 내지 15 중량%, 윤활제 0.1 내지 20 중량%, 상용화제 0.005 내지 5 중량%를 포함하는 것을 특징으로 한다. 기존 생분해성 조성물의 경우 내열성, 생산성, 성형성이 떨어지는 단점 이외에도 지나치게 고가인 관계로 산업상 이용 가능성이 떨어지고 여타 고분자와 상용성이 떨어지는 한계가 있었다. 본 발명에 따른 생분해성 베이스 레진 조성물은 패키징 완제품을 생산할 때, 간단하게 특성이 다른 생분해성 고분자 수지 등과 적당 비율로 혼합하여 패키징 완제품을 원하는 물성, 강도, 가격 등을 조절하여 생산할 수 있으며, 생산된 패키징 완제품은 자연 상태에서 선순환되어 환경에 부담을 주지 않고 썩어서 자연으로 돌아 간다.The present invention relates to a biodegradable base resin composition prepared using ultra-fine calcium carbonate, a biodegradable polymer, starch, a plasticizer, a lubricant, a compatibilizer, based on fine calcium carbonate, and 5 to 50% by weight of fine calcium carbonate, 5 to 40% by weight ultrafine calcium carbonate, 5 to 60% by weight biodegradable polymer, 5 to 50% by weight starch, 1 to 15% by weight plasticizer, 0.1 to 20% by weight lubricant, 0.005 to 5% by weight compatibilizer It is characterized by. In the case of the existing biodegradable composition, in addition to the disadvantages of low heat resistance, productivity, and moldability, there is a limit in the industrial availability due to the excessively expensive and incompatible with other polymers. The biodegradable base resin composition according to the present invention can be produced by controlling the desired physical properties, strength, price, etc. of the finished packaged product by simply mixing the biodegradable polymer resin with a suitable ratio and other properties when producing the finished product. Packaging finished products are virtuous in their natural state and rot and return to nature without straining the environment.
Description
본 발명은 생분해성 베이스 레진 조성물에 관한 것으로, 미세탄산칼슘 5 내지 50 중량%, 초미세 탄산칼슘 5 내지 40 중량%, 생분해성 고분자 5 내지 60 중량%, 전분 5 내지 50 중량%, 가소제 1 내지 15 중량%, 윤활제 0.1 내지 20 중량%, 상용화제 0.005 내지 5 중량%를 포함하는 것을 특징으로 한다. 기존 생분해성 수지 조성물의 경우 내열성, 생산성, 성형성, 내수성이 떨어지고 또한 가격 경쟁력이 부족하여 산업상의 이용가능성이 부족한 단점을 보완하여 보다 경쟁성이 있는 생분해성 베이스 레진 조성물을 제공한다. 본 발명에 따른 생분해성 베이스 레진 조성물은 패키징 완제품을 생산할 때, 간단하게 특성이 다른 생분해성 고분자 수지 등과 적당 비율로 혼합하여 패키징 완제품을 원하는 물성, 강도, 가격 등을 조절하여 생산할 수 있으며, 생산된 패키징 완제품은 자연 상태에서 선순환되어 환경에 부담을 주지 않고 썩어서 자연으로 돌아 간다.The present invention relates to a biodegradable base resin composition, 5 to 50% by weight of fine calcium carbonate, 5 to 40% by weight of ultrafine calcium carbonate, 5 to 60% by weight of biodegradable polymer, 5 to 50% by weight of starch, 1 to 1 plasticizer 15 wt%, 0.1-20 wt% of lubricant, 0.005-5 wt% of compatibilizer. Existing biodegradable resin composition provides a more competitive biodegradable base resin composition by compensating for the disadvantages of lack of industrial availability due to lack of heat resistance, productivity, moldability, water resistance, and lack of price competitiveness. The biodegradable base resin composition according to the present invention can be produced by controlling the desired physical properties, strength, price, etc. of the finished packaged product by simply mixing the biodegradable polymer resin with a suitable ratio and other properties when producing the finished product. Packaging finished products are virtuous in their natural state and rot and return to nature without straining the environment.
본 발명에 따른 생분해성 베이스 레진 조성물을 이용하여 쉬트 생산, 진공성형, 압 진공, 사출 성형 등 일반적인 생산방식에 따라 식품용기, 산업용 포장재, 농업용 및 원예용 포장재의 원료로 사용할 수 있다. 또한 기존 생분해 에코 패키징 완제품에 물성 개선, 원가절감, 소각성 부여, 생산성 개선 효과가 기대되고, 완제품 포장재는 구조적으로 안정하면서도 표면 개선효과, 강도 증가, 고분자가 상용성이 개선되는 장점이 있다. 본 발명의 미세 탄산칼슘, 바인더로 사용되는 생분해성 고분자, 상용화제를 사용한 조성물은 여러 가지 고분자 물질과 상용성이 우수하여 필름 및 비닐 압출, 시트성형, 진공성형, 압진공성형, 사출 성형품의 원료로써 다양하게 적용시킬 수 있는 장점이 있다. The biodegradable base resin composition according to the present invention may be used as a raw material for food containers, industrial packaging materials, agricultural and horticultural packaging materials according to general production methods such as sheet production, vacuum molding, pressure vacuum, injection molding, and the like. In addition, properties of the existing biodegradable eco-packaging products are expected to improve properties, reduce cost, incineration, and improve productivity. The finished product packaging material is structurally stable, but has surface improvement effects, strength increase, and polymer compatibility. Biodegradable polymer used in the present invention as a fine calcium carbonate, a composition using a compatibilizer is excellent in compatibility with a variety of polymer materials, raw materials for film and vinyl extrusion, sheet molding, vacuum molding, vacuum molding, injection molding products There is an advantage that can be applied to various.
플라스틱 등 고분자 소재는 다양하고 내수성, 우수한 물성 및 저렴한 가격으로 현대인의 풍요로운 일상생활과 산업발달에 큰 공헌을 해 온 반면 대량으로 발생되는 각종 폐비닐, 스티로폼, 플라스틱 용기 등의 소각이나 매립에 따른 환경호르몬 누출, 맹독성의 다이옥신 검출 폐기물의 불완전 연소에 의한 대기오염 발생 등과 같은 심각한 환경오염의 원인으로 대두되고 있다. Polymer materials such as plastics have made great contributions to modern people's abundant daily life and industrial development with diverse, water resistance, excellent physical properties and low price, while environment caused by incineration or landfill of various waste vinyl, styrofoam, plastic containers, etc. It is emerging as a cause of serious environmental pollution such as hormonal leakage and air pollution caused by incomplete combustion of toxic dioxin detection waste.
이러한 플라스틱 폐기물의 문제를 해결하기 위하여 사용할 때는 플라스틱의 가공성, 내구성, 기계적 성질을 유지하면서 추가로, 분해성이라는 기능을 부가하여 플라스틱의 편리성과 환경오염 문제 해결을 할 수 있는 연구가 진행되고 있다. In order to solve the problem of the plastic waste, while maintaining the processability, durability, and mechanical properties of the plastic, in addition to the decomposability, the research has been conducted to solve the convenience and environmental pollution problems of plastics.
최근에는 반영구성이 요구되는 제품을 제외한 1회용 식품용기, 쓰레 기 봉투, 상업용품 포장용 완충재 등 사용기간이 짧은 플라스틱 제품의 경우 사용 후 단기간 내에 분해될 수 있는 친환경 분해성 고분자 신소재를 기존 난분해성 플라스틱의 대체물질로 활용하기 위한 연구가 활발히 이루어져 그 용도가 확대 일로에 있으며, 신규 신소재 개발이 활발하다. 특히 화석연료 유래의 원유 가격이 가파르게 상승하고, 석유자원 고갈, 지구 온난화, 이산화탄소 감량, 환경 오염에 대한 폐해를 우려하는 요즘은 석유자원 사용 감량, 석유자원 대체 신소재의 연구 개발이 더욱 요구되고 있다. 기존에 개발된 생분해성 물질의 경우에도 물성의 증가, 원가 절감, 유사 친환경 소재와 블랜딩, 컴파운드 등을 통한 추가 연구 개발이 매우 활발하다. 또한 사용 감량 및 대체 소재 개발 이외에도 재활용, 재사용을 통한 자원 절감도 그 중요성이 더욱 고조 되고 있다. Recently, in the case of plastic products, such as disposable food containers, garbage bags, and buffers for packaging commercial products, except for products that require reflection, new eco-friendly degradable polymer materials that can be decomposed within a short period of time are used. As research to utilize as substitute material is actively conducted, its use is expanding and new new materials are actively developed. In particular, the price of crude oil derived from fossil fuels has risen sharply and worries about the depletion of petroleum resources, global warming, carbon dioxide reduction, and environmental pollution are required. In the case of previously developed biodegradable materials, further research and development through the increase of physical properties, cost reduction, and similar eco-friendly materials and blending and compound are very active. In addition to reducing use and developing alternative materials, the importance of resource saving through recycling and reuse is becoming more important.
기존에 개발된 석유자원 대체 소재로 개발된 생분해성 물질은 천연물 유래의 생분해 수지로는 키틴, 키토산, 알긴산, 콜라겐, 박테리아 셀룰로오스, 폴리아미노산 등이 있다. 또 미생물 유래 또는 화학 합성된 것으로 폴리젖산(PLA), 폴리히드록시부티레이트발러레이트(PHBV), 폴리카프로락톤(PCL), 폴리부틸렌석시네이트(PBS), 폴리히드록시부티레이트(PHB), 폴리히드록시알카노에이트(PHA) 등과 같은 지방족 폴리에스테르(Aliphatic polyester; AP) 등이 개발되어 시판되고 있다. 그러나 가격이 고가인 단점이 있어 기존 소비자의 가격저항이 있고, 또한 내열성, 가공성, 생산성이 나빠 실제 산업현장에서 활발히 적용이 되지 못하고 있는 실정이다. 이에 따라 기존 개발된 생분해성 물질 2가지 이상을 복합사용하거나, 새로운 생분해성 물질 개발을 하여 기존 생분해 물질 대비 물성 개량, 성형성, 가공성을 높이기 위한 다양한 노력을 하고 있다. 현재까지 개발된 생분해 원료 물질은 물성이 약하여 쉽게 파손되는 단점이 있고, 또한 원료 가격이 고가인 관계로 경제성이 저하되고, 제품 생산후 냉각시간이 길어지는 등 생산성이 나빠 실제 산업 현장에서 사용되지 못하는 단점이 있다.Biodegradable materials developed as substitutes for petroleum resources previously developed include chitin, chitosan, alginic acid, collagen, bacterial cellulose, and polyamino acids. Also derived from microorganisms or chemically synthesized, polylactic acid (PLA), polyhydroxybutyrate valerate (PHBV), polycaprolactone (PCL), polybutylene succinate (PBS), polyhydroxybutyrate (PHB), polyhydrate Aliphatic polyesters (AP) such as oxyalkanoate (PHA) and the like have been developed and marketed. However, there is a disadvantage that the price is expensive, there is a price resistance of the existing consumer, and also heat resistance, processability, productivity is poor, the situation is not actively applied in the actual industrial field. Accordingly, various efforts have been made to improve the properties, formability, and processability of existing biodegradable materials by using two or more existing biodegradable materials in combination or developing new biodegradable materials. Biodegradable raw materials that have been developed so far have weaknesses that are easily damaged due to their weak physical properties. Also, due to the high cost of raw materials, the economic efficiency is lowered, and the cooling time is long after production. There are disadvantages.
이러한 제반 문제를 해결하기 위한 방법으로, 기존에 내열성이 66.5도로 온수에도 변형이 되는 PLA, 고가인 지방족폴리에스테르 이외의 물질을 활용하는 연구가 다양하게 이루어지고 있으며 상기 물질들의 상용성이 약하여 제품 성형시 결무늬 방향으로 쉽게 찢어지는 이지컷 현상을 해결하지 못하여 제품 물성이 약한 단점이 있었다. 한국 특허출원 10-2005-0032965은 옥수수 전분을 변성시키고, 무기물 필러를 사용하였으나 제조 공정이 복잡한 단점이 있다. 한국 특허출원 10-2002-0058408은 전분, 섬유질 소재를 주로 사용하여 강도 보강 기능이 기대된다. 또한 본 발명자들이 선발명한 한국 특허출원 10-2007-0089849 또한 여전히 고가인 단점을 가지고 있어 산업상 이용 가능성이 떨어지는 단점이 있었다. In order to solve these problems, various researches using materials other than PLA and expensive aliphatic polyester, which are deformed even in hot water, have been conducted in various ways. It could not solve the easy-cut phenomenon that is easily torn in the direction of the time pattern, there was a weak product properties. Korean Patent Application No. 10-2005-0032965 denatures corn starch and uses inorganic fillers, but the manufacturing process is complicated. Korean Patent Application No. 10-2002-0058408 mainly uses starch and fibrous materials to enhance strength. In addition, Korean patent application 10-2007-0089849, which the inventors have selected, also has a disadvantage that is still expensive, and thus has a disadvantage in that the industrial application is inferior.
기존 생분해성 수지 조성물의 제품 성형성 저하, 내열성 저하, 생산성 저하, 고가인 단점이 있어 산업상 이용 가능성이 현저히 저하되는 문제점을 해결하기 위한 것으로, 생분해성이 우수하면서도 저가의 첨가제를 대량 사용함에 따라 제품의 원가를 저하시킬 수 있으며, 전분의 물성 개질을 통하여 내열성을 부여하고, 지방질 계열의 지방족 폴리에스테르화 상용성을 대단히 높여 제품 물성이 매우 개선되고, 또한 가격이 저렴한 생분해성 베이스 레진 조성물을 제공함에 그 목적이 있다. 본 발명의 다른 목적은 각종 고분자 물질들과 콤파운드를 하지 않고 포장재 완제품 생산전에 다른 원료 물질과 본 발명의 생분해성 베이스 레진을 간단하게 혼합하여 포장재 완제품을 생산할 수 있도록 마스터배치와 같은 용도로 사용을 할 수 있는 생분해성 베이스 레진 조성물을 제공하여 원가절감, 포장재 완제품 강도 보완, 물성 조절 등 소기의 목적을 용이하게 달성할 수 있는 생분해성 베이스 레진 조성물을 제공함에 그 목적이 있다. 본 발명의 또 다른 목적은 생분해성 베이스 레진 조성물의 제조방법을 제공하는 것이다.It is to solve the problem that the industrial applicability of the existing biodegradable resin composition is lowered due to the deterioration of product moldability, heat resistance, productivity reduction, and expensiveness. It can reduce the cost of the product, give heat resistance through the modification of the properties of starch, and greatly improve the compatibility of the fatty-based aliphatic polyesters to provide a very improved product properties and low-cost biodegradable base resin composition Has its purpose. Another object of the present invention is to use the same as the master batch to produce a finished product by simply mixing the raw material and the biodegradable base resin of the present invention before producing the finished product packaging material without compounding with various polymer materials. It is an object of the present invention to provide a biodegradable base resin composition which can easily achieve a desired purpose such as cost reduction, supplementation of finished product strength, and physical property control by providing a biodegradable base resin composition. It is another object of the present invention to provide a method for preparing a biodegradable base resin composition.
이러한 본 발명의 목적은, 하기의 단계를 포함하는 본 발명의 방법에 의해 달성된다:This object of the present invention is achieved by the method of the present invention comprising the following steps:
전분, 가소제, 무기 필러인 초미세 탄산칼슘, 미세 탄산칼슘, 윤활제, 상용화제를 혼합기에 투입하고 500~1,500 rpm으로 혼합하여 수분제거 및 혼합을 하는 1단계; Starch, plasticizer, ultrafine calcium carbonate, fine calcium carbonate, lubricant, and compatibilizer, which are inorganic fillers, are added to a mixer and mixed at 500 to 1,500 rpm to remove moisture and mix;
1단계의 분말원료의 바인더 역할을 하는 생분해성 고분자를 1단계의 혼합물에 추가로 투입한 후 500~1,500 rpm으로 혼합을 하는 2단계;Adding the biodegradable polymer, which serves as a binder of the powder raw material of the first step, into the mixture of the first step, and then mixing at 500 to 1,500 rpm;
혼합 과정까지 완료된 재료를 호퍼에 투입한 다음, 반죽부(Kneading zone) 1개 이상, 역방향 스크류부(Reverse screw)가 1개 이상 장착되고, 분말 원료 가공시 생성될 수 있는 수분 및 휘발성 물질을 배출할 수 있는 통기공(Vent hole)이 1개 이상 설치된 통상의 트윈 익스트루더를 통과시키면서 가공온도 100 내지 230도에서 가공하여 반죽, 혼합, 열화학 변성이 일어난 원료가 다이스를 통하여 토출되는 3단계;After completing the mixing process, the material is put into the hopper, and then one or more kneading zones and one or more reverse screws are installed, and water and volatile substances that can be generated during processing of powder raw materials are discharged. Three steps of discharging the raw material produced by kneading, mixing, and thermochemical modification by processing at a processing temperature of 100 to 230 degrees while passing through a conventional twin extruder having one or more vent holes installed therein;
다이스를 통하여 토출되는 생분해성 베이스 원료 스트랜드를 커팅하여 펠렛 형상의 생분해성 고분자 및 미세 탄산칼슘을 이용한 생분해성 베이스 레진 조성물을 제조한다. The biodegradable base raw material strand discharged through the die is cut to prepare a biodegradable base resin composition using pellet-shaped biodegradable polymer and fine calcium carbonate.
원료 스트랜드를 커팅하여 펠렛 형상으로 만드는 방법은 일반적으로 다이스를 통하여 토출되는 원료를 페이스 커팅후 송풍건조하거나, 토출되는 스트랜드를 컨베이어 벨트를 통하여 이송하면서 송풍건조후 커팅하거나, 갈라시스템을 이용한 페이스커팅 방법, 스트랜드를 수조에 통과시켜 표면 냉각후 커팅하는 일반적인 커팅 방법으로 펠렛 형상으로 제조할 수 있다.In general, a method of cutting raw material strands into pellets is generally carried out by blow-drying a raw material discharged through a die after face cutting, or by cutting and drying the blown strand while transferring the discharged strand through a conveyor belt, or by using a gala system. In addition, the strand may be manufactured in a pellet form by a general cutting method of cutting the surface after passing the strand through a water bath.
본 발명에 있어서, 각 원료의 사용량은 미세탄산칼슘 5 내지 50 중량%, 초미세 탄산칼슘 5 내지 40 중량%, 생분해성 고분자 5 내지 60 중량%, 전분 5 내지 50 중량%, 가소제 1 내지 15 중량%, 윤활제 0.1 내지 20 중량%, 상용화제 0.005 내 지 5 중량%일 수 있다. In the present invention, the amount of each raw material used is 5 to 50% by weight of fine calcium carbonate, 5 to 40% by weight of ultra fine calcium carbonate, 5 to 60% by weight of biodegradable polymer, 5 to 50% by weight of starch, and 1 to 15% by weight of plasticizer. %, Lubricant 0.1 to 20% by weight, compatibilizer 0.005 to 5% by weight.
본 발명에 따른 상기 마이크로급 미세 탄산칼슘은 입경이 3 내지 100㎛인 것을 사용할 수 있는데, 초미세 탄산칼슘만 사용하는 경우 강한 자체 응집력에 의해서 탄산칼슘이 덩어리지게 되어 완제품 포장재에 오히려 나쁜 영향을 미치게 된다. 예를 들면 표면상태 악화, 치수안정성 저하, 굴곡 탄성율 저하, 강도 등 물성 저하 및 생산성 저하 등의 단점이 증가하게 된다. 미세 탄산칼슘의 사용량은 조성물의 총 중량을 기준으로 5 내지 70 중량%, 바람직하게는 5 내지 50 중량%일 수 있다. The micro-grade fine calcium carbonate according to the present invention may be used having a particle diameter of 3 to 100㎛, when using only ultra-fine calcium carbonate, the calcium carbonate is agglomerated by a strong self-cohesive force to adversely affect the finished product packaging material do. For example, disadvantages such as deterioration of surface condition, lowering of dimensional stability, lowering of elastic modulus of elasticity, lowering of physical properties such as strength and lowering of productivity are increased. The amount of fine calcium carbonate may be 5 to 70% by weight, preferably 5 to 50% by weight based on the total weight of the composition.
본 발명에 따른 상기 나노급 초미세 탄산칼슘은 입경이 50 내지 200 nm의 것을 사용하는데, 그 사용량은 조성물의 총 중량을 기준으로 3.0 내지 70 중량%, 바람직하게는 5.0 내지 50 중량%일 수 있다. 초미세 탄산칼슘은 고분자 물질의 단량체과 결합을 이루고, 초미세 미립자가 고분자간 빈 공간을 채워주게 되어 강도 등 물성개선 및 표면 개선효과를 보여준다. 3.0 중량% 이하로 사용하는 경우 완제품 포장재에 적용했을 때 제품의 상용성 저하, 표면 개질, 물성 증가 등의 효과를 기대하기 어렵고, 50 중량% 이상 사용하는 경우에는 생산성 저하, 원가 상승, 재료가 뭉침 현상 등 생분해성 베이스 레진 조성물 물성에 악영향을 미치게 된다. 이러한 초미세 탄산칼슘을 사용하는 경우에 초미세 입자에 의해 표면적이 증가하고 그 표면에 놓이는 이온의 비율이 증가된다. 따라서 결합력, 응집력 등 고분자 물성에 매우 큰 역할을 하게 되어 물성 개선, 표면 개질, 강도 증가 등 현저한 효과 상승을 하게 된다. The nano-grade ultra-fine calcium carbonate according to the present invention uses a particle size of 50 to 200 nm, the amount may be 3.0 to 70% by weight, preferably 5.0 to 50% by weight based on the total weight of the composition. . The ultra fine calcium carbonate forms a bond with the monomer of the high molecular material, and the ultra fine particles fill the void space between the polymers, thereby improving physical properties such as strength and improving the surface. When it is used at less than 3.0% by weight, it is difficult to expect the effects of product compatibility, surface modification, and physical property increase when applied to the finished product packaging material, and when it is used at more than 50% by weight, productivity decreases, cost increases, and materials aggregate. It will adversely affect the properties of the biodegradable base resin composition such as development. In the case of using such ultrafine calcium carbonate, the surface area is increased by the ultrafine particles and the proportion of ions placed on the surface is increased. Therefore, it plays a very large role in the physical properties of the polymer such as bonding strength, cohesion, and the like, a remarkable effect of physical properties improvement, surface modification, strength increase.
본 발명에 따른 상기 생분해성 고분자는 폴리히드록시부티레이트발러레이트(PHBV), 폴리카프로락톤(PCL), 폴리부틸렌석시네이트(PBS), 폴리유산(PLA), 폴리히드록시부티레이트(PHB), 폴리히드록시알카노에이트(PHA), 지방족폴리에스테르, 전분 수지를 단독 또는 혼합하여 사용할 수 있다. 이는 원료간의 바인더 역할을 하는 것으로 조성물 원료간의 결합력을 증진시켜 펠렛 형성에 중요한 역할을 하게 되는 것으로 멜트인덱스(Melt Index; MI)가 높을수록 사용상에 편리하다. 그 사용량은 3.0 내지 70 중량%, 바람직하게는 5.0 내지 50 중량%일 수 있다. 5 중량% 미만으로 첨가되는 경우 결합력 약화에 의해 펠렛 형성이 어렵고, 50 중량% 이상 사용하는 경우 특별한 문제는 없으나 제품 단가가 상승하는 단점이 있다. The biodegradable polymer according to the present invention is polyhydroxybutyrate valerate (PHBV), polycaprolactone (PCL), polybutylene succinate (PBS), polylactic acid (PLA), polyhydroxybutyrate (PHB), poly Hydroxyalkanoate (PHA), aliphatic polyester, and starch resin can be used alone or in combination. This is to act as a binder between the raw materials is to play an important role in the formation of pellets by improving the binding force between the raw materials of the composition, the higher the Melt Index (MI) is more convenient for use. The amount used may be 3.0 to 70% by weight, preferably 5.0 to 50% by weight. If it is added less than 5% by weight, it is difficult to form pellets by weakening the binding force, there is no particular problem when using more than 50% by weight, but there is a disadvantage that the product cost increases.
본 발명에 따른 상기 전분은 당 업계에서 통상 사용되는 전분, 예를 들어 옥수수, 감자, 타피오카, 고구마, 밀, 쌀 및 곡류 등 각종 식물로부터 추출된 전분이다. 전분은 식물의 종류나 저장 부위에 따라 지상전분과 지하전분으로 구분된다. 각각의 전분은 입자의 형태, 입자의 크기가 모두 다르며 전분입자의 형상, 입경, 외형의 고유한 특성을 가지고 있는데, 품종에 따라 이화학적 특성에 많은 차이가 있기 때문에 적절한 선택 후 직접 이용하는 경우, 또는 물성을 변성시킨 후 이용 가치를 높여 사용하는 경우가 많으나, 본 발명에서는 옥수수 전분, 타피오카 전분, 밀전분 으로 구성되는 그룹에서 선택되는 한가지 또는 그 이상의 혼합물을 생전분 형태로 그대로 이용하였다. 그 사용량은 조성물 총 중량을 기준으로 5.0 내지 70 중량%, 바람직하게는 5 내지 50 중량%일 수 있다. 전분을 50% 이상 사용시 특별한 문제는 없으나 탄산칼슘 사용량이 저하되어 원가가 상승되는 단점이 있다.The starch according to the present invention is a starch commonly used in the art, for example, starch extracted from various plants such as corn, potato, tapioca, sweet potato, wheat, rice and grains. Starch is divided into ground starch and underground starch according to the type of plant and storage area. Each starch has different shape, particle size, and unique characteristics of starch particle shape, particle size, and appearance, and there are many differences in physicochemical properties according to varieties. In many cases, one or more mixtures selected from the group consisting of corn starch, tapioca starch and wheat starch were used as raw starch in the present invention. The amount used may be 5.0 to 70% by weight, preferably 5 to 50% by weight based on the total weight of the composition. There is no particular problem when the starch is used more than 50%, but the cost of the calcium carbonate is lowered and the cost is increased.
본 발명에 따른 상기 가소제는 글리세린, 글리세롤모노스테아레이트(GMS), 솔비톨을 단독 또는 혼합하여 사용할 수 있는데, 그의 사용량은 0.5 내지 30 중량 %, 바람직하게는 1 내지 15 중량%일 수 있다. 가소제는 전분의 유동성, 가공성을 향상시키는 효과가 있는데, 과량 사용시 표면으로 이동 용출되는 단점이 있다. 가소제는 전분을 변성시키는 목적으로 사용되는데, 고분자 물질에 가소제를 첨가 가공하면, 그 혼화물은 유연성, 탄성, 휨성이 증가하여 가공성, 성형성 등이 개선된다. 전분 등 고분자 물질 자체는 분자량이 커서 쉽게 변형이 되지 않지만 거기에 가소성을 부여하면 외력에 의해 쉽게 변형시킬 수 있다. 열에 의해 가소성을 보이는 것을 열가소성이라 부르는데, 본 발명에서는 열을 가하면 탄화하는 전분에 열가소성을 부여하기 위해 전분을 가소화시켜 사용한다. The plasticizer according to the present invention may be used alone or in combination with glycerin, glycerol monostearate (GMS), sorbitol, the amount of the use may be 0.5 to 30% by weight, preferably 1 to 15% by weight. The plasticizer has an effect of improving the fluidity and processability of the starch, and has a disadvantage in that it is eluted to the surface when used in excess. The plasticizer is used for the purpose of denaturing starch. When the plasticizer is added to the polymer material, the blend is increased in flexibility, elasticity and warpage, thereby improving workability and formability. Polymeric material such as starch itself is not easily deformed due to its large molecular weight, but plasticity can be easily deformed by external force. Thermoplastic plastics are called thermoplastics. In the present invention, starch is plasticized to impart thermoplasticity to the carbonized starch when heat is applied.
본 발명에 따른 상기 윤활제는 칼슘스테아레이트, 아연스테아레이트, 글리세린스테아레이트, 부틸스테아레이트, 고체상 파라핀 왁스, 유동 파라핀 왁스, 밀납, 몰다 왁스, 이멀시파잉 왁스, 칸데릴라 왁스, 파라핀, 유동 파라핀을 단독 또는 혼합하여 사용할 수 있는데, 그의 사용량은 0.2 내지 20 중량 %, 바람직하게는 0.5 내지 15 중량%일 수 있다. 윤활제는 윤활효과가 우수한 탄소수 22의 베헤닌산 계열을 사용하면 재료원가가 높아지는 단점이 있어, 가격 대비 생분해제에 분산효과가 우수하고 윤활 효과가 좋은 탄소수 18인 스테아린산 계열을 사용하는 쪽이 경제성 측면에서 장점이 있다. 또한 지방산 계열 윤활제를 사용하는 경우, 필러같은 무기물에 친화성을 보이는 장점이 있으며 표면이 친수성인 무기물을 코팅하여 표면 개질이 되는 장점이 있다. 윤활제는 문자 그대로 원료간의 마찰을 적게하고 매끄럽게 하기 위해 사용하는 첨가제이다. 모든 마찰이 나쁘다는 것은 아니지만, 원료 혼합, 용융, 가공시 마찰에 의한 열이 원료를 필요 이상으로 가열하여 분해시키기도 하고, 원료중 전분등 유기 첨가제를 탄화시키기도 하며, 트윈 익스트루더 같은 금속가공기의 표면에 눌러붙기도 하여 불량이 발생하는 것을 해소하기 위해 사용한다. The lubricant according to the present invention is calcium stearate, zinc stearate, glycerin stearate, butyl stearate, solid paraffin wax, liquid paraffin wax, beeswax, drive wax, emulsion wax, candelilla wax, paraffin, liquid paraffin. It may be used alone or in combination, the amount thereof may be 0.2 to 20% by weight, preferably 0.5 to 15% by weight. Lubricants have a disadvantage in that the cost of materials increases when using behenic acid series with 22 carbon atoms, which have good lubrication effects. There is an advantage in In addition, when using a fatty acid-based lubricant, there is an advantage in showing the affinity to the inorganic material, such as filler, there is an advantage that the surface is modified by coating a hydrophilic inorganic material. Lubricants are additives that are used to literally reduce and smooth the friction between raw materials. Not all frictions are bad, but the heat of friction during mixing, melting, and processing of the raw materials causes the raw materials to be heated and decomposed more than necessary, carbonizing organic additives such as starch in the raw materials, and It is used to eliminate the occurrence of defects by pressing on the surface.
본 발명에 따른 상기 상용화제는 과산화벤조일, 폴리비닐알코올(PVA), 벤조페논을 단독 또는 혼합하여 사용할 수 있는데, 그의 사용량은 0.001 내지 1 중량 %, 바람직하게는 0.005 내지 2 중량%일 수 있다. 상용화제는 사용되는 원료간에 계면활성적 작용으로 원료간의 계면에 존재하여 계면장력을 저하시키기도 하고, 원료 상호간 반응성을 개선시켜 원료간 상용성을 개선시키고, 최종 제품 생산시, 융점의 차이에 따른 생산 불량률, 물성 저하를 개선시킨다.The compatibilizer according to the present invention may be used alone or mixed with benzoyl peroxide, polyvinyl alcohol (PVA), benzophenone, the amount of the amount may be 0.001 to 1% by weight, preferably 0.005 to 2% by weight. The compatibilizer is present at the interface between the raw materials due to the interfacial action between the raw materials used, thereby lowering the interfacial tension, and improving the compatibility between the raw materials by improving the reactivity between the raw materials. Improve the defective rate, lowering the physical properties
본 발명에 따라 제조된 생분해성 베이스 레진 조성물은 생분해성 고분자와 상용성이 있어, 에코 패키징 완제품을 제조하는데 별 문제점이 발견되지 않았고, 제품의 생산성이 우수하고 제품 강도가 증가하였다. 또한 본 발명의 생분해성 베이스 레진 조성물을 이용하여 다양한 고분자와 용이하게 혼합하여 다양한 물성의 생분해 완제품을 생산할 수 있게 되어 바이어가 원하는 물성의 제품을 간단한 방법으로 생산 공급이 용이하다. 본 발명의 제품을 산업화에 적용함에 따라 자연 상태에서 쉽게 분해되어 토양 유기물을 증가시키고 환경을 오염시키지 않는 장점이 있다. 본 발명의 생분해성 베이스 레진 조성물을 이용하여 제품 생산시 기존 생산현장의 기계를 그대로 사용할 수 있는 장점이 있고, 고가의 생분해성 고분자의 원가 절감을 이룰수 있게 되어 산업상 이용가능성이 매우 높다.The biodegradable base resin composition prepared according to the present invention is compatible with the biodegradable polymer, so that no problems were found in preparing the eco-packaging finished product, and the productivity of the product was excellent and the product strength was increased. In addition, by using the biodegradable base resin composition of the present invention can be easily mixed with a variety of polymers to produce a biodegradable finished product of various physical properties it is easy to produce and supply a product of the physical properties desired by the buyer in a simple way. As the product of the present invention is applied to industrialization, there is an advantage in that it is easily decomposed in the natural state to increase soil organic matter and does not pollute the environment. By using the biodegradable base resin composition of the present invention there is an advantage that can be used as a production machine in the existing production site as it is, it is possible to achieve a cost reduction of expensive biodegradable polymer is very high industrial applicability.
본 발명에 따른 상기 생분해성 베이스 레진 조성물은, 통상의 헨셀 믹서, 슈퍼 믹서 등 혼합기를 사용하여 혼합을 하고, 통상의 이축 압출기(Twin Extruder)를 이용한 용융 압출 성형과정을 통해 2-8mm 정도 크기를 갖는 펠렛 상태로 만들어 사용하게 된다. 용도에 따라 요구되는 통상의 고분자 수지와 첨가제 조성물을 즉석에서 혼합하여 제조하고자 하는 제품으로 성형할 수 있다. 또는, 요구되는 열가소성 중합체 수지와 다른 성분들을 용도에 따라 적절한 비율로 혼합하여 미리 콤파운드를 제조한 후 원하는 제품을 제조할 수 있다. 제조할 수 있는 포장재 완제품은 필름, 비닐, 쉬트, 진공성형제품, 사출성형품 등 알려진 다양한 형태로 제조될 수 있다. 이러한 생분해성 베이스 레진 조성물은 통상의 고분자 수지의 총 중량에 대하여 약 5% 내지 75% 정도의 비율로 혼합되어 사용할 수 있는 정도로 제조되는 것이 적당하나, 본 발명은 이에 제한되는 것이 아니다. The biodegradable base resin composition according to the present invention is mixed using a mixer such as a conventional Henschel mixer, a super mixer, and has a size of about 2-8 mm through a melt extrusion process using a conventional twin extruder. It is made into a pellet state having. The conventional polymer resin and the additive composition required according to the use can be molded into a product to be prepared by mixing immediately. Alternatively, the required thermoplastic polymer resin and the other components may be mixed in an appropriate ratio according to the use to prepare a compound beforehand to prepare a desired product. Packaging materials that can be manufactured can be manufactured in a variety of known forms such as films, vinyl, sheets, vacuum molded products, injection molded products. Such biodegradable base resin composition is suitably prepared to the extent that it can be mixed and used in a ratio of about 5% to 75% with respect to the total weight of the conventional polymer resin, but the present invention is not limited thereto.
이하, 본 발명을 실시예에 의해 더욱 상세히 설명한다. 하기 실시예는 본 발명을 설명하기 위한 것이며 본 발명이 그에 의해 한정되는 것은 아니다.Hereinafter, the present invention will be described in more detail with reference to Examples. The following examples are intended to illustrate the invention and are not intended to limit the invention thereto.
< 실시예 1 ><Example 1>
미세 탄산칼슘 28 중량%, 초미세 탄산칼슘 25 중량%, 옥수수 전분 15 중량%, 솔비톨 2 중량%, 스테아린산아연 2 중량%, 피이왁스 1.97 중량%, 과산화벤조일 0.03 중량%를 혼합기에 투입하고 1,000 rpm으로 수분제거 및 혼합하였다. 혼합된 원료에 PBS 10 중량%, PCL 16 중량%을 추가로 혼합기에 투입하고, 800 rpm으로 추가 혼합하였다. 혼합 과정까지 완료된 재료를 호퍼에 투입한 다음, 반죽부(Kneading zone) 1개 이상, 역방향 스크류부(Reverse screw)가 1개 이상 장착되고, 분말 원료 가공시 생성될 수 있는 수분 및 휘발성 물질을 배출할 수 있는 통기공(Vent hole)이 1개 이상 설치된 통상의 트윈 익스트루더를 통과시키면서 가공온도 175도, 스크류 950 rpm으로 가공하여 반죽, 혼합, 열화학 변성이 일어난 원료가 다이스를 통하여 토출되는 스트랜드를 커팅하여 생분해성 베이스 레진 조성물을 제조하였다. 28 wt% of fine calcium carbonate, 25 wt% of ultra fine calcium carbonate, 15 wt% of corn starch, 2 wt% of sorbitol, 2 wt% of zinc stearate, 1.97 wt% of pywax, and 0.03 wt% of benzoyl peroxide were added to the mixer and 1,000 rpm. Moisture removal and mixing. 10% by weight of PBS and 16% by weight of PCL were further added to the mixer, and the mixture was further mixed at 800 rpm. After completing the mixing process, the material is put into the hopper, and then one or more kneading zones and one or more reverse screws are installed, and water and volatile substances that can be generated during processing of powder raw materials are discharged. Strand through which the raw material, which is kneaded, mixed and thermochemically modified, is discharged through the die by processing at a processing temperature of 175 ° C and a screw 950 rpm while passing through a conventional twin extruder equipped with one or more vent holes. Was cut to prepare a biodegradable base resin composition.
< 실시예 2 ><Example 2>
실시예 1에서 제조한 생분해성 베이스 레진 조성물 60 중량%, PCL 20 중량%, PBS 20 중량%를 혼합하여 통상의 시트 압출기를 이용하여 시트를 제조하였다. 60 wt% of the biodegradable base resin composition prepared in Example 1, 20 wt% of PCL, and 20 wt% of PBS were mixed to prepare a sheet using a conventional sheet extruder.
< 실시예 3 ><Example 3>
실시예 2에서 제조한 시트를 이용하여 통상의 진공 성형기를 이용하여 진공성형품을 제조 하였다. Using the sheet prepared in Example 2, a vacuum molded article was manufactured using a conventional vacuum molding machine.
< 실시예 4 ><Example 4>
실시예 1에서 제조한 생분해성 베이스 레진 조성물 60 중량%, PLA 20 중량%, 전분 수지 20 중량%를 혼합하여 통상의 사출성형기에서 사출성형품을 제조하였다. 60 wt% of the biodegradable base resin composition prepared in Example 1, 20 wt% PLA, and 20 wt% of starch resin were mixed to prepare an injection molded article in a conventional injection molding machine.
< 실시예 5 ><Example 5>
실시예 1에서 제조한 생분해성 베이스 레진 조성물 100 중량%를 이용하여 통상의 사출성형기에서 사출 성형품을 제조하였다. Injection molded articles were manufactured in a conventional injection molding machine using 100 wt% of the biodegradable base resin composition prepared in Example 1.
< 실시예 6 ><Example 6>
실시예 1에서 제조한 생분해성 베이스 레진 조성물 60 중량%, PCL 20 중량%, PBS 20 중량%를 혼합하여 통상의 필름 압출기를 이용하여 필름을 제조하 였다. 60 wt% of the biodegradable base resin composition prepared in Example 1, 20 wt% of PCL, and 20 wt% of PBS were mixed to prepare a film using a conventional film extruder.
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