WO2024004228A1 - Procédé de production de feuille de résine, cuir pvc et cuir végan - Google Patents
Procédé de production de feuille de résine, cuir pvc et cuir végan Download PDFInfo
- Publication number
- WO2024004228A1 WO2024004228A1 PCT/JP2022/037929 JP2022037929W WO2024004228A1 WO 2024004228 A1 WO2024004228 A1 WO 2024004228A1 JP 2022037929 W JP2022037929 W JP 2022037929W WO 2024004228 A1 WO2024004228 A1 WO 2024004228A1
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- WO
- WIPO (PCT)
- Prior art keywords
- leather
- resin sheet
- pvc
- manufacturing
- sheet
- Prior art date
Links
- 229920005989 resin Polymers 0.000 title claims abstract description 49
- 239000011347 resin Substances 0.000 title claims abstract description 49
- 239000010985 leather Substances 0.000 title claims abstract description 46
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 41
- 238000000034 method Methods 0.000 claims abstract description 43
- 239000002994 raw material Substances 0.000 claims abstract description 35
- 239000000463 material Substances 0.000 claims abstract description 30
- 239000000843 powder Substances 0.000 claims abstract description 26
- 238000010298 pulverizing process Methods 0.000 claims abstract description 15
- 235000013399 edible fruits Nutrition 0.000 claims description 16
- 238000002156 mixing Methods 0.000 claims description 15
- 239000002245 particle Substances 0.000 claims description 10
- 238000012545 processing Methods 0.000 claims description 8
- 238000007710 freezing Methods 0.000 claims description 3
- 230000008014 freezing Effects 0.000 claims description 3
- 238000010030 laminating Methods 0.000 claims description 3
- 239000000203 mixture Substances 0.000 abstract description 12
- 238000005096 rolling process Methods 0.000 abstract description 7
- 238000004898 kneading Methods 0.000 abstract description 6
- 230000008569 process Effects 0.000 description 24
- 239000002649 leather substitute Substances 0.000 description 19
- 239000004744 fabric Substances 0.000 description 13
- 241000196324 Embryophyta Species 0.000 description 12
- 239000013256 coordination polymer Substances 0.000 description 12
- 238000000227 grinding Methods 0.000 description 12
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 10
- 229920005749 polyurethane resin Polymers 0.000 description 9
- 239000000243 solution Substances 0.000 description 9
- 241000533293 Sesbania emerus Species 0.000 description 8
- 240000008790 Musa x paradisiaca Species 0.000 description 6
- 239000012790 adhesive layer Substances 0.000 description 6
- 239000010410 layer Substances 0.000 description 6
- 239000007788 liquid Substances 0.000 description 6
- 239000004570 mortar (masonry) Substances 0.000 description 6
- 244000105624 Arachis hypogaea Species 0.000 description 5
- 241000675108 Citrus tangerina Species 0.000 description 5
- 241000220225 Malus Species 0.000 description 5
- 238000002788 crimping Methods 0.000 description 5
- 229910052757 nitrogen Inorganic materials 0.000 description 5
- 235000020232 peanut Nutrition 0.000 description 5
- 235000010627 Phaseolus vulgaris Nutrition 0.000 description 4
- 244000046052 Phaseolus vulgaris Species 0.000 description 4
- 244000299461 Theobroma cacao Species 0.000 description 4
- 235000005764 Theobroma cacao ssp. cacao Nutrition 0.000 description 4
- 235000005767 Theobroma cacao ssp. sphaerocarpum Nutrition 0.000 description 4
- 241000219094 Vitaceae Species 0.000 description 4
- 235000021016 apples Nutrition 0.000 description 4
- 235000021015 bananas Nutrition 0.000 description 4
- 235000001046 cacaotero Nutrition 0.000 description 4
- 239000011248 coating agent Substances 0.000 description 4
- 238000000576 coating method Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 235000021021 grapes Nutrition 0.000 description 4
- 239000004814 polyurethane Substances 0.000 description 4
- 238000002360 preparation method Methods 0.000 description 4
- 238000011084 recovery Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 235000013305 food Nutrition 0.000 description 3
- 238000011160 research Methods 0.000 description 3
- 238000011144 upstream manufacturing Methods 0.000 description 3
- 241001465754 Metazoa Species 0.000 description 2
- 235000018290 Musa x paradisiaca Nutrition 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000004745 nonwoven fabric Substances 0.000 description 2
- 238000010792 warming Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 238000004804 winding Methods 0.000 description 2
- 239000002759 woven fabric Substances 0.000 description 2
- 241000219357 Cactaceae Species 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 235000009754 Vitis X bourquina Nutrition 0.000 description 1
- 235000012333 Vitis X labruscana Nutrition 0.000 description 1
- 240000006365 Vitis vinifera Species 0.000 description 1
- 235000014787 Vitis vinifera Nutrition 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003607 modifier Substances 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/40—Layered products comprising a layer of synthetic resin comprising polyurethanes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B9/00—Layered products comprising a layer of a particular substance not covered by groups B32B11/00 - B32B29/00
- B32B9/02—Layered products comprising a layer of a particular substance not covered by groups B32B11/00 - B32B29/00 comprising animal or vegetable substances, e.g. cork, bamboo, starch
-
- 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
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06N—WALL, FLOOR, OR LIKE COVERING MATERIALS, e.g. LINOLEUM, OILCLOTH, ARTIFICIAL LEATHER, ROOFING FELT, CONSISTING OF A FIBROUS WEB COATED WITH A LAYER OF MACROMOLECULAR MATERIAL; FLEXIBLE SHEET MATERIAL NOT OTHERWISE PROVIDED FOR
- D06N3/00—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06N—WALL, FLOOR, OR LIKE COVERING MATERIALS, e.g. LINOLEUM, OILCLOTH, ARTIFICIAL LEATHER, ROOFING FELT, CONSISTING OF A FIBROUS WEB COATED WITH A LAYER OF MACROMOLECULAR MATERIAL; FLEXIBLE SHEET MATERIAL NOT OTHERWISE PROVIDED FOR
- D06N7/00—Flexible sheet materials not otherwise provided for, e.g. textile threads, filaments, yarns or tow, glued on macromolecular material
- D06N7/0002—Wallpaper or wall covering on textile basis
Definitions
- the present invention relates to a method for manufacturing a resin sheet, PVC leather, and vegan leather.
- An object of the present invention is to provide a method for manufacturing a resin sheet that can improve tensile strength, as well as PVC leather and vegan leather.
- the method for producing a resin sheet of the present invention includes a first step of freezing and pulverizing plant-derived raw materials to generate powder, a second step of mixing the powder with a resin raw material to generate a mixed raw material, and a second step of generating a mixed raw material. and a third step of processing the material into a sheet material.
- the plant-derived raw materials may include seeds or seed-derived raw materials.
- the plant-derived raw materials may include fruits.
- the plant-derived raw material may include plant stems.
- the method for manufacturing a resin sheet of the present invention may include a fourth step of laminating the sheet material to the base material.
- the powder may be composed of particles that have been pulverized to have an average particle size of at least 250 ⁇ m or less.
- the PVC leather of the present invention is a PVC leather manufactured using a resin sheet manufactured by any of the resin sheet manufacturing methods described above.
- the vegan leather of the present invention is vegan leather manufactured using a resin sheet manufactured by any of the resin sheet manufacturing methods described above.
- a resin sheet can be manufactured using powder produced by freeze-pulverization. This makes it possible to improve the tensile strength of the resin sheet.
- FIG. 2 is a schematic diagram showing the flow of freeze-pulverization processing included in the pulverization process shown in FIG. 1.
- FIG. FIG. 2 is a schematic diagram showing the flow of each process in the adjustment step, kneading step, rolling step, compression bonding step, and recovery step included in FIG. 1.
- FIG. It is a flowchart which shows the flow of the manufacturing method of the dry synthetic leather sheet in 2nd Embodiment. It is a figure which shows typically the flow of each process in a processing process, a pasting process, and a collection
- vegan leather is a material that artificially reproduces the appearance and texture of leather without using animal skin.
- Examples of vegan leather include PVC leather, artificial leather, and synthetic leather.
- FIG. 1 is a flowchart showing the flow of a method 10 for manufacturing vegan leather (PVC leather).
- FIG. 2 is a schematic diagram showing the flow of the freeze-pulverization process in the crushing step S1.
- the vegan leather manufacturing method 10 includes a pulverization step (first step) S1 of freezing and pulverizing coffee grounds CS, a preparation step S2 of a PVC resin mixed raw material Q, and a pulverization step.
- Coffee grounds CS is the residue (in other words, it can also be expressed as pomace) after extracting components from coffee beans or coffee bean powder using hot water or water.
- coffee grounds CS corresponds to a raw material derived from seeds.
- the coffee grounds CS put into the raw material tank 20 are pre-cooled using liquid nitrogen supplied from the liquid nitrogen tank 22 to the raw material tank 22 via the supply pipe P1. do. Then, the pre-cooled coffee grounds CS are conveyed to the freeze grinder 26 via the screw feeder 24. Liquid nitrogen is supplied to this freeze crusher 26 from a liquid nitrogen tank 22 via a supply pipe P2, and coffee grounds CS supplied from a screw feeder 24 via a supply pipe P3 are frozen at a predetermined low temperature. It has the function of crushing in the state. As the freeze crusher 26, it is preferable to use, for example, Linrex Mill (registered trademark) manufactured by Hosokawa Micron Corporation.
- coffee grounds CS is used as a plant-derived (in other words, it can also be expressed as seed-derived) raw material, but instead of coffee grounds CS, seeds such as coffee beans, cacao beans, peanuts, and peanuts may be used. Good too. Furthermore, fruits such as apples, tangerines, grapes, and bananas may be used as plant-derived raw materials. More specifically, all of these fruits may be used as they are, or only a portion of the fruit may be used. Examples of this fruit include apple peel, tangerine peel, grape skin, and banana peel. Furthermore, discarded fruit or fruit scheduled for disposal may be used as the plant-derived raw material. In this case, waste food can be effectively utilized. Furthermore, as a plant-derived raw material, plant fibers obtained from banana stems, cacti, etc. may be used.
- the inventor conducted a study and found that when attempting to powderize coffee grounds by grinding them using a mortar or mortar, the coffee grounds become paste-like due to the influence of oil contained in the coffee grounds. It turned out that it was difficult to make it into powder form. It was also found that when a PVC sheet material was produced by mixing the paste-like coffee grounds with a PVC resin raw material, the sheet material had an extremely low tensile strength and was not suitable for practical use.
- the inventor conducted extensive research and found that it is possible to powderize coffee grounds by performing a freeze-grinding process using liquid nitrogen or the like as in this embodiment. It has also been found that when PVC sheet material is manufactured using powdered coffee grounds, the tensile strength of the sheet is also improved.
- the inventor conducted extensive research and found that if coffee beans, cacao beans, peanuts, etc. are ground in place of coffee grounds using a mortar or mortar, they tend to become paste-like. It turns out that problems can easily occur. Therefore, the inventor conducted additional studies and found that the tensile strength of the PVC sheet can be improved by using freeze-grinding treatment, similar to the case of coffee grounds described above.
- the inventor conducted a study and found that when trying to crush fruits such as apples, tangerines, grapes, and bananas, or the skins of these fruits using a mortar or mortar, these fruits It has also been found that it is difficult to grind into fine powder (which can also be expressed as fine granulation) due to the influence of moisture contained in the skin of the fruit. However, we have found that even in these cases, it is possible to micronize (reduce particles) and improve the tensile strength of PVC sheets by performing freeze-grinding treatment in the same way as in the case of coffee grounds mentioned above. It's arrived.
- the tensile strength of the sheet material SH by pulverizing the powdered coffee grounds CP so that the average particle size is 250 ⁇ m or less and then manufacturing the above-mentioned PVC sheet material SH. Do you get it. Furthermore, it is more preferable to pulverize the coffee grounds CS so that the average particle size of the coffee grounds powder CP is 150 ⁇ m or less. Thereby, the tensile strength of the PVC sheet material SH can be further improved. Furthermore, by pulverizing coffee grounds CS and incorporating it into PVC sheet material SH or PVC leather sheet PH, it is sufficient even when the content (ratio) of coffee grounds CS contained in the same sheet materials SH and PH is increased. It also has the advantage of being able to obtain a high tensile strength.
- coffee grounds powder CP can be used instead of coffee grounds CS.
- the inventor's research has revealed that the tensile strength of the PVC sheet material SH can be improved by making the particles finer (micronized). Specifically, when using seeds such as coffee grounds, coffee beans, cacao beans, and peanuts, fruits such as apples, tangerines, grapes, and bananas, and the skins of these fruits, the average particle size of the powder is 100 ⁇ m or less.
- the pulverization treatment it is preferable to carry out the pulverization treatment so that the following results are obtained. This makes it possible to sufficiently suppress variations in the tensile strength of the PVC sheet material SH.
- the above-mentioned powder may be pulverized so that the average particle size becomes 50 ⁇ m or less.
- steps S2 to S6 other than the above-mentioned crushing step S1 will be explained with further reference to FIG. 3.
- a stabilizer, a lubricant, a plasticizer, a coloring agent, a modifier, etc. are mixed with the PVC resin powder (resin) using a mixing device such as a ribbon blender (not shown) to form the PVC resin.
- a mixed raw material Q is produced.
- a Banbury mixer closed kneader
- a pair of mixing rolls (open kneader) 34A, 34B, a pair of warming rolls 36A, 36B, etc. are used.
- the PVC resin mixed raw material Q is made into a rice cake (gel)-like mixture R containing coffee grounds.
- the PVC resin mixed raw material Q is put into the Banbury mixer 32 and kneaded until it becomes gel-like, it is put into the mixing roll pair 34A, 34B and the coffee produced in the grinding step S1 (see FIG. 2)
- a mixture R containing coffee grounds is produced by adding and mixing the powdered coffee grounds CP.
- the coffee grounds-containing mixture R is conveyed to a pair of warming rolls 36A and 36B having a heating function, and the viscosity of the coffee grounds-containing mixture R is adjusted while heating the mixture R so as not to cool.
- the coffee grounds-containing mixture R is rolled by the calender device 38 and formed into a sheet to produce a PVC sheet material SH containing coffee grounds.
- the calender device 38 is a rolling device that includes a pair of nipping rollers 38A, 38B that nip the coffee grounds-containing mixture R, feed rollers 39A, 39B, and the like.
- the coffee grounds-containing PVC sheet material SH sent out from the upstream calendar device 38 and the base fabric BS fed from the feeding device 40 via the plurality of rollers 42 and 44 are rolled onto the rolling roller pair 52. , 54 and pressure bonding to produce a PVC leather sheet PH.
- the base fabric BS is made of, for example, a knitted fabric, a woven fabric, a nonwoven fabric, or the like.
- the base fabric BS and the PVC sheet material SH are bonded together in the crimping step S5, but the base fabric BS may be used as the PVC sheet material SH without being bonded together. In this case, there is no need to provide the crimping step S5.
- the PVC leather sheet PH sent out from the crimping step S5 is cooled while being transported between a plurality of transport rollers 61, 62, 63, and then wound up by a winding device 70. to recover.
- vegan leather (in other words, PVC leather sheet PH) is manufactured using coffee grounds powder CP generated by freeze-grinding. be able to. This makes it possible to improve the tensile strength of vegan leather.
- the method 10 for manufacturing vegan leather (PVC leather sheet PH) is described as an example, but the present invention is not limited thereto.
- it may be realized as a dry synthetic leather sheet manufacturing method 80.
- a dry synthetic leather sheet manufacturing method 80 according to the second embodiment in this case will be described using FIGS. 4 and 5.
- dry synthetic leather seats are also included in vegan leather.
- FIG. 4 is a flowchart showing the flow of each step in the manufacturing method 80.
- FIG. 5 is a diagram schematically showing the flow of each process in the processing step S12, pasting step S13, and collection step S14 among the steps included in the flowchart shown in FIG.
- the dry synthetic leather sheet manufacturing method 80 includes the above-mentioned crushing step S1 (see FIG. 2), mixing step (second step) S11, and processing step (third step). ) S12, a pasting step (fourth step) S13, and a collecting step 14.
- the mixing step S11 for example, the coffee grounds powder CP produced in the grinding step S1 is mixed with a one-component polyurethane resin solution T1.
- the release paper U is transported downstream from the feed roller 81 via the transport roller 82 and the coating roller 83, and in the mixing step S11, the polyurethane resin mixed with coffee grounds powder CP is mixed.
- Solution T1 is applied (can also be expressed as coating). Thereby, the skin layer resin film PU1 is formed on the release paper U. Then, while conveying the release paper U on which the skin layer resin film PU1 is formed to the downstream side, a drying process is performed using the dryer HT1.
- a two-component polyurethane resin solution T2 is applied to the skin layer.
- the adhesive layer PU2 is formed by coating the adhesive layer PU2 on the resin film PU1. Thereby, the skin layer resin film PU1 and the adhesive layer PU2 can be laminated on the release paper U.
- the release paper U on which the skin layer resin film PU1 and the adhesive layer PU2 are laminated is passed through the dryer HT2 while being conveyed downstream. Thereby, the solvent and the like contained in the adhesive layer PU2 are volatilized.
- the base fabric TS (which can also be expressed as the base TS) sent out from the sending roller 88 and the release paper U that has passed through the dryer HT2 on the upstream side are sandwiched between a pair of heat press rolls 89A and 89B. Send it downstream. Thereby, the base fabric TS is bonded to the adhesive layer PU2 formed on the release paper U. As a result, a dry synthetic leather sheet PU is formed.
- the base fabric TS is a sheet material made of knitted fabric, woven fabric, nonwoven fabric, or the like.
- the release paper U on which the dry synthetic leather sheet PU has been formed is transported downstream by transport rollers 91A, 91B, 91C, and 91D, and is wound up and collected by the winding roller 92.
- the release paper U may be removed from the dry synthetic leather sheet PU after being collected by the take-up roller 92.
- a dry synthetic leather (resin) sheet PU having the same effects as the first embodiment can be obtained.
- the coffee grounds powder CP produced in the grinding step S1 is mixed with the polyurethane resin solution T1 in the mixing step S11, but the present invention is not limited to this.
- the coffee grounds powder CP produced in the grinding step S1 may be mixed with the polyurethane resin solution T2 instead of the polyurethane resin solution T1.
- the coffee grounds powder CP produced in the grinding step S1 may be mixed into both the polyurethane resin solution T1 and the polyurethane resin solution T2.
- the manufacturing method according to the present invention is not limited to the vegan leather manufacturing method 10 and the dry synthetic leather sheet manufacturing method 80 described above, but may be realized as a wet synthetic leather sheet manufacturing method.
- a mixed solution obtained by mixing the coating liquid (polyurethane resin solution) with the coffee grounds powder CP produced in the grinding step S1 described above is used.
- a wet synthetic leather sheet or a wet artificial leather sheet having the following effects can be obtained.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Textile Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Materials Engineering (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Casting Or Compression Moulding Of Plastics Or The Like (AREA)
- Treatment And Processing Of Natural Fur Or Leather (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
Le problème à résoudre par la présente invention est de fournir : un procédé de production d'une feuille de résine, le procédé permettant d'atteindre une amélioration de la résistance à la traction ; un cuir en PVC ; et un cuir végan. La solution selon l'invention concerne un procédé (10) de production d'un cuir végan comprenant : une étape de pulvérisation S1 dans laquelle du marc de café est pulvérisé à l'état congelé pour produire une poudre ; une étape de malaxage S3 dans laquelle la poudre produite à l'étape de pulvérisation S1 est mélangée avec une résine PVC brute produite au cours d'une étape de régulation S2 pour obtenir un mélange de matières premières ; et une étape de laminage S4 dans laquelle le mélange de matières premières obtenu à l'étape de malaxage S3 est traité pour obtenir un matériau en feuille.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
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CN202280005198.5A CN117693548A (zh) | 2022-06-30 | 2022-10-11 | 树脂片的制造方法以及聚氯乙烯皮革、纯素皮革 |
JP2022573551A JP7387127B1 (ja) | 2022-06-30 | 2022-10-11 | 樹脂シートの製造方法、および樹脂シート |
KR1020227042035A KR20240003693A (ko) | 2022-06-30 | 2022-10-11 | 수지시트의 제조방법 및 염화비닐레더, 비건레더 |
JP2023042390A JP2024006946A (ja) | 2022-06-30 | 2023-03-16 | 樹脂シートの製造方法、および、塩ビレザー、ヴィ―ガンレザー |
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JPS56129157A (en) * | 1980-03-15 | 1981-10-09 | Hiroshi Takaoka | Molded body using used coffee grounds as main material and production thereof |
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JPH10314286A (ja) * | 1997-05-15 | 1998-12-02 | U C C Ueshima C0Ffee Kk | 塩基性悪臭ガス吸着剤入りシート材 |
JP2000264734A (ja) * | 1999-03-17 | 2000-09-26 | Nihon University | 湿潤状態の植物絞り滓を用いた固形炭化物及びその製造方法 |
JP2010121002A (ja) * | 2008-11-18 | 2010-06-03 | Sanyo Chem Ind Ltd | スラッシュ成形用樹脂粉末組成物及び成形品 |
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JP2015073462A (ja) * | 2013-10-08 | 2015-04-20 | 大阪瓦斯株式会社 | 食味強化用コーヒー粉末の製造方法及び食味強化用コーヒー粉末 |
JP7138980B1 (ja) * | 2021-05-06 | 2022-09-20 | 株式会社冨田商店 | 樹脂組成物、接着剤、樹脂成形品及び樹脂成形品の製造方法 |
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2022
- 2022-10-11 WO PCT/JP2022/037929 patent/WO2024004228A1/fr active Application Filing
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JPS56129157A (en) * | 1980-03-15 | 1981-10-09 | Hiroshi Takaoka | Molded body using used coffee grounds as main material and production thereof |
JPH05277460A (ja) * | 1991-06-15 | 1993-10-26 | Unie Kafue:Kk | コーヒー残渣組成物 |
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JP2010121002A (ja) * | 2008-11-18 | 2010-06-03 | Sanyo Chem Ind Ltd | スラッシュ成形用樹脂粉末組成物及び成形品 |
JP2010121003A (ja) * | 2008-11-18 | 2010-06-03 | Sanyo Chem Ind Ltd | スラッシュ成形用樹脂粉末組成物及び成形品 |
JP2015511648A (ja) * | 2012-03-13 | 2015-04-20 | テックスチェム ポリマーズ エスディーエヌ ビーエイチディー | 農業廃棄物から得られる熱可塑性デンプン組成物 |
JP2015073462A (ja) * | 2013-10-08 | 2015-04-20 | 大阪瓦斯株式会社 | 食味強化用コーヒー粉末の製造方法及び食味強化用コーヒー粉末 |
JP7138980B1 (ja) * | 2021-05-06 | 2022-09-20 | 株式会社冨田商店 | 樹脂組成物、接着剤、樹脂成形品及び樹脂成形品の製造方法 |
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