JP3106751B2 - Method for producing resin modifier - Google Patents
Method for producing resin modifierInfo
- Publication number
- JP3106751B2 JP3106751B2 JP04332396A JP33239692A JP3106751B2 JP 3106751 B2 JP3106751 B2 JP 3106751B2 JP 04332396 A JP04332396 A JP 04332396A JP 33239692 A JP33239692 A JP 33239692A JP 3106751 B2 JP3106751 B2 JP 3106751B2
- Authority
- JP
- Japan
- Prior art keywords
- gelatin
- powder
- degree
- reaction
- insolubilization
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000003607 modifier Substances 0.000 title claims description 13
- 229920005989 resin Polymers 0.000 title claims description 7
- 239000011347 resin Substances 0.000 title claims description 7
- 238000004519 manufacturing process Methods 0.000 title claims description 5
- 108010010803 Gelatin Proteins 0.000 claims description 64
- 239000008273 gelatin Substances 0.000 claims description 64
- 229920000159 gelatin Polymers 0.000 claims description 64
- 235000019322 gelatine Nutrition 0.000 claims description 64
- 235000011852 gelatine desserts Nutrition 0.000 claims description 64
- 239000000843 powder Substances 0.000 claims description 47
- 238000000034 method Methods 0.000 claims description 26
- 239000003431 cross linking reagent Substances 0.000 claims description 16
- 238000006243 chemical reaction Methods 0.000 claims description 15
- 239000003292 glue Substances 0.000 claims description 11
- 239000002245 particle Substances 0.000 claims description 11
- 239000007787 solid Substances 0.000 claims description 6
- 239000012530 fluid Substances 0.000 claims 1
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 16
- 229920003002 synthetic resin Polymers 0.000 description 10
- 239000000057 synthetic resin Substances 0.000 description 10
- 238000010521 absorption reaction Methods 0.000 description 9
- 229920001971 elastomer Polymers 0.000 description 9
- 239000005060 rubber Substances 0.000 description 9
- 239000000047 product Substances 0.000 description 7
- 238000004898 kneading Methods 0.000 description 6
- 239000000203 mixture Substances 0.000 description 6
- 229920003051 synthetic elastomer Polymers 0.000 description 6
- 239000005061 synthetic rubber Substances 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 239000012298 atmosphere Substances 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 239000010985 leather Substances 0.000 description 4
- SXRSQZLOMIGNAQ-UHFFFAOYSA-N Glutaraldehyde Chemical compound O=CCCCC=O SXRSQZLOMIGNAQ-UHFFFAOYSA-N 0.000 description 3
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 3
- 238000009835 boiling Methods 0.000 description 3
- 239000010419 fine particle Substances 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- 238000010298 pulverizing process Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000003925 fat Substances 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- 238000007696 Kjeldahl method Methods 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229940037003 alum Drugs 0.000 description 1
- 125000003277 amino group Chemical group 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- 210000000988 bone and bone Anatomy 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 238000007385 chemical modification Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 239000002612 dispersion medium Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000010828 elution Methods 0.000 description 1
- 238000006911 enzymatic reaction Methods 0.000 description 1
- 150000002118 epoxides Chemical class 0.000 description 1
- 125000003700 epoxy group Chemical group 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000000499 gel Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000010559 graft polymerization reaction Methods 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 230000001678 irradiating effect Effects 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 229930014626 natural product Natural products 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
- -1 polyethylene Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 238000007873 sieving Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 229920002803 thermoplastic polyurethane Polymers 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
- Jellies, Jams, And Syrups (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明はゼラチン粉末又は膠粉末
からなる樹脂改質材の製造方法に関する。本発明により
得られるゼラチン粉末及び膠粉末は、合成樹脂あるいは
ゴム組成物に配合あるいは付着させ改質材として用いら
れる。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a resin modifier comprising gelatin powder or glue powder. According to the present invention
The resulting gelatin powder and glue powder are blended or adhered to a synthetic resin or rubber composition and used as a modifier.
【0002】[0002]
【従来の技術】合成樹脂あるいはゴム組成物から成形さ
れたシート、フィルム、合成レザー、等は帯電により表
面が汚染され醜くなったり、吸放湿特性の不足、プラス
チック的な感触など使用者に対して違和感を与え、天然
物に比べて感触が好ましくない。 このような合成樹脂
の性質を改良するために特開昭53−121902号、
特開平1−197600号公報には、合成樹脂中に皮革
粉を配合することが開示されている。しかしながら、皮
革粉は繊維質で微粉砕が困難であり、流動性が低いため
樹脂に配合した場合、表面の平滑な製品や薄物製品を製
造することは困難である。また、皮革粉自体の吸放湿性
も低いため、得られた成型品の吸放湿特性は小さい。ま
た、油脂分が多く加熱成型する際、成型品表面に油脂が
ブリードしてべたつき感を生じたり、汚染の原因となり
吸湿性も低い。2. Description of the Related Art Sheets, films, synthetic leathers, and the like formed from synthetic resin or rubber compositions are contaminated by electrification and become ugly, lack of moisture absorption / desorption properties, and feel like plastic. Gives a sense of incongruity and is less pleasant to feel than natural products. In order to improve the properties of such synthetic resins, Japanese Patent Application Laid-Open No. 53-121902,
JP-A-1-197600 discloses that a leather powder is mixed in a synthetic resin. However, leather powder is fibrous and difficult to finely pulverize, and has low fluidity, so that when it is mixed with a resin, it is difficult to produce a product having a smooth surface and a thin product. In addition, since the moisture absorption / release properties of the leather powder itself are low, the moisture absorption / release properties of the obtained molded product are small. In addition, when a large amount of fats and oils are molded by heating, the fats and oils bleed on the surface of the molded product to give a sticky feeling, cause contamination, and have low hygroscopicity.
【0003】また、特開昭63−147635号、15
2480号及び152485号には同様の目的でゼラチ
ンを用いることが開示されている。ゼラチンは油脂分の
含有率も少なく、吸放湿性、帯電防止性、均一分散性が
皮革粉に比べて優れている。しかしながら、ゼラチンは
親水性が非常に大きく樹脂との親和性が悪い。このた
め、合成樹脂にゼラチンを多量に添加すると相分離を起
こしたり、表面のべたつき感が発生し、強度の低下も生
じやすい。Further, Japanese Patent Application Laid-Open No. 63-147635, 15
Nos. 2480 and 152485 disclose the use of gelatin for the same purpose. Gelatin has a low oil content, and is superior in moisture absorption / release properties, antistatic properties, and uniform dispersibility as compared with leather powder. However, gelatin has very high hydrophilicity and poor affinity with a resin. For this reason, when a large amount of gelatin is added to the synthetic resin, phase separation occurs, the surface becomes sticky, and the strength tends to decrease.
【0004】このようにゼラチン粉末は合成樹脂の改質
に好ましいが親水性の大きいことが問題である。このよ
うな欠点を回避すると共に通気性を付与するために、ゼ
ラチンを合成樹脂に配合した後、熱水処理を行い未反応
のゼラチンを溶出させる方法(特開昭63−15248
2号)も提案されている。しかしながらこのような方法
では工程が複雑となり加工費の上昇を招き、溶出条件に
よっては添加したゼラチンの90%以上が溶出してしま
うため排水処理が必要となる。As described above, gelatin powder is preferable for modifying a synthetic resin, but has a problem of high hydrophilicity. In order to avoid such drawbacks and to impart air permeability, a method of blending gelatin into a synthetic resin and subjecting it to hot water treatment to elute unreacted gelatin (Japanese Patent Application Laid-Open No. 63-15248).
No. 2) has also been proposed. However, such a method complicates the process and raises the processing cost, and depending on the elution conditions, 90% or more of the added gelatin elutes, so that wastewater treatment is required.
【0005】これらの問題を解決するために、100μ
m以下の不溶化ゼラチン微粉末を、合成樹脂に配合する
ことも開示されている(特開平3−237165号)が、
ここで使用されている不溶化ゼラチンは、最も小さいも
のでも粒径45ミクロンほどであり、その不溶化方法
も、従来公知の加熱によるもの、あるいは溶液状での不
溶化反応によるものである。In order to solve these problems, 100 μm
It has also been disclosed that an insolubilized gelatin fine powder of m or less is compounded in a synthetic resin (Japanese Patent Application Laid-Open No. 3-237165).
The insolubilized gelatin used here has a particle size of about 45 microns even at the smallest, and the insolubilization method is a conventionally known heating method or a solution insolubilization reaction.
【0006】ゼラチンを不溶化する方法としては、ゼラ
チンの溶液をホルマリン、グルタルアルデヒド、クロム
明ばん等のゼラチンの架橋剤で処理する方法があるが、
この方法ではゼラチン自身が高分子でありその溶液の粘
度が高いため、不溶化度合をかなり高くした場合は、強
固なゲルを形成し、その後の処理に苦慮する場合があ
る。As a method of insolubilizing gelatin, there is a method of treating a gelatin solution with a gelatin crosslinking agent such as formalin, glutaraldehyde, chromium alum, etc.
In this method, since gelatin itself is a polymer and the viscosity of the solution is high, if the degree of insolubilization is considerably increased, a strong gel is formed, and it may be difficult to perform the subsequent treatment.
【0007】他の方法としては、100〜200℃の高
温で加熱したり、赤外線や紫外線照射する方法などがあ
るが、これらの方法では、ゼラチン自身が変性するため
問題の生じることがある。さらにゼラチンの親水性を調
整する方法として、ゼラチンのアミノ基、カシボキシル
基、水酸基などの官能基の反応を利用した化学修飾法、
酵素法、グラフト重合法等があるが、これらの方法では
工程が複雑になり、修飾度合、グラフト度合などの制御
が難しく品質安定性に問題があり、製造コストも高くな
るなどいずれも工業的実現性が困難である。Other methods include heating at a high temperature of 100 to 200 ° C. and irradiating infrared rays or ultraviolet rays. However, these methods may cause a problem because gelatin itself is denatured. Further, as a method for adjusting the hydrophilicity of gelatin, a chemical modification method using a reaction of a functional group such as an amino group, a casboxyl group, or a hydroxyl group of gelatin,
There are enzymatic methods, graft polymerization methods, etc., but these methods complicate the process, difficult to control the degree of modification, degree of grafting, etc., have problems with quality stability, and increase the manufacturing cost. Is difficult.
【0008】また、ゴム組成物においても、吸湿性及び
帯電防止性を有するゴム製品を製造する目的で、ゴム原
料配合物に膠を加えて混練する方法が従来より知られて
いる。この方法では、膠を一旦温水に溶解し、冷却によ
り膠をゲル化し、次いでゴムと混練していた。しかしな
がら、膠自身が高分子であるため、このような方法では
溶液状態での粘度が高く濃厚溶液を得る場合は、多くの
時間と手間を必要としていた。また、ゴム原料と膠とを
混練する場合、混練ローラーに対するこれら混合物の接
着性が悪いなどの問題もある。これらの問題を解決し、
得られるゴム製品の吸湿性を向上させ、帯電性を減少さ
せる方法として軽度に硬化してから微粉化し、次いで水
分で膨潤した状態の粉末をゴム配合物と混練する方法
(特公昭48−23661号)も知られているが粒径の違
いについては検討がなされておらず、硬化度合も低い。[0008] In addition, a method of kneading a rubber composition by adding glue to a rubber composition for the purpose of producing a rubber product having hygroscopicity and antistatic properties has also been known. In this method, glue was once dissolved in warm water, gelled by cooling, and then kneaded with rubber. However, since the glue itself is a polymer, such a method requires a lot of time and labor to obtain a concentrated solution having a high viscosity in a solution state. Further, when the rubber raw material and the glue are kneaded, there are also problems such as poor adhesion of the mixture to the kneading roller. Solve these issues,
As a method of improving the hygroscopicity of the obtained rubber product and reducing the chargeability, a method of lightly curing, pulverizing, and then kneading the powder swollen with water with a rubber compound.
(Japanese Patent Publication No. 48-23661) is also known, but the difference in particle size has not been studied, and the degree of curing is low.
【0009】[0009]
【発明が解決しようとする課題】本発明の目的は、吸放
湿性に優れ、不溶化後の状態が安定で凝集等の問題が起
こらず、取扱いが簡便なゼラチン粉末又は膠粉末からな
る樹脂改質材を製造するに当たって、簡便かつ低コスト
で、品質安定性にも優れた方法を提供することにある。OBJECTS OF THE INVENTION It is an object of the present invention is excellent in moisture sorption, state after insolubilization does not occur a problem such as a stable aggregate, handling simple gelatin powder or glue powder Tona
That the resin modifier order to manufacture, in a simple and low cost, is to provide a superior method in quality stability.
【0010】[0010]
【課題を解決するための手段】本発明者らは、前記の課
題について鋭意検討を重ねた結果、意外にも平均粒径5
〜30μmを有し、かつ架橋された不溶性のゼラチン粉
末又は膠粉末からなる樹脂改質材が上述の問題点を解決
し、かつゼラチン粉末を固体のまま架橋剤で処理するこ
とにより、そのゼラチン粉末が不溶化できることを見い
だし本発明を完成した。本発明は固体のゼラチン粉末ま
たは膠粉末を流体状態に保持した架橋剤と抵触させ、不
溶化反応を行うことを特徴とする(以下、膠粉末を含め
て単にゼラチン粉末と記載することがある)。Means for Solving the Problems The present inventors have conducted intensive studies on the above-mentioned problems, and as a result, surprisingly, the average particle diameter was 5
A resin modifier comprising an insoluble gelatin powder or glue powder having a cross-linkability of 30 to 30 μm solves the above-mentioned problems, and the gelatin powder is treated with a cross-linking agent while the gelatin powder remains solid. Have been found to be able to be insolubilized, and the present invention has been completed. The invention is conflict with the crosslinking agent held in the flow body condition gelatin powder or glue solid powder, and performing insolubilization reaction (hereinafter, including glue powder
Simply referred to as gelatin powder) .
【0011】不溶化反応に用いるゼラチン粉末の平均粒
径は、5〜30μm、好ましくは5〜25μm、更に好
ましくは10〜20μmである。本発明において「架橋
され、不溶化されてなる」とは、粉末の全部又は一部が
架橋され、このため不溶化されていることを意味し、一
部が架橋されている場合とは、粉末の粒子表面のみが架
橋された場合等、不均一な架橋状態を含むものとする。
ゼラチン粉末の架橋割合は目的に応じ任意に選択してよ
いが、不溶化度合が5%以上であればよい。更に好まし
くは、不溶化度合が80%以上であるものがよい。The average particle size of the gelatin powder used in the insolubilization reaction is 5 to 30 μm, preferably 5 to 25 μm, and more preferably 10 to 20 μm. In the present invention, "crosslinked and insolubilized" means that all or a part of the powder is crosslinked and thus insolubilized. This includes an uneven crosslinked state, such as when only the surface is crosslinked.
The cross-linking ratio of the gelatin powder may be arbitrarily selected depending on the purpose, but it is sufficient that the degree of insolubilization is 5% or more. More preferably, the degree of insolubility is 80% or more.
【0012】不溶化度合は、ゼラチン微粉末1gを99
mLの水に分散させ、70℃にて10分間撹拌後、遠心
分離(10000G×20分間)により、固液分離を行い、上
澄み液の窒素量をセミミクロケルダール法により求め、
以下の式より算出したものをいう。[0012] The degree of insolubility is determined by mixing 1 g of gelatin fine powder with 99 g.
Dispersed in mL of water, stirred at 70 ° C. for 10 minutes, and then separated into solid and liquid by centrifugation (10000 G × 20 minutes). The amount of nitrogen in the supernatant was determined by a semi-micro Kjeldahl method.
It is calculated by the following equation.
【0013】 不溶化度合(%)={(a−x)/a}×100 a:比較試料1gのセミミクロケルダール値 X:上澄み液のセミミクロケルダール値 本発明の反応に供される原料ゼラチンとしては、牛皮、
豚皮、牛骨等のいずれから得られたものであってもよ
く、また、酸、アルカリのいずれによって処理されたゼ
ラチンであってもよい。Degree of insolubility (%) = {(a−x) / a} × 100 a: Semi-micro Kjeldahl value of 1 g of a comparative sample X: Semi-micro Kjeldahl value of a supernatant The raw material gelatin used in the reaction of the present invention is Cowhide,
It may be obtained from any of pig skin, cow bone, etc., and may be gelatin treated with any of acid and alkali.
【0014】用いるゼラチン粉末は、微粉砕の効果を考
えると細かいものが好ましいが、12メッシュ程度以下
の物であればよい。このようなゼラチン粉末は、例えば
12〜22メッシュパス程度の粒径のものをファインビ
クトリーミル、ジェット粉砕機などを用いて微粉砕した
後、フルイ分けして得られる。[0014] The gelatin powder used is preferably fine in consideration of the effect of fine pulverization, but may be finer than about 12 mesh. Such a gelatin powder is obtained by, for example, finely pulverizing a powder having a particle size of about 12 to 22 mesh pass using a fine victory mill, a jet pulverizer, or the like, and then sieving.
【0015】一方、架橋剤としては、ホルマリン、グル
タルアルデヒドのようなアルデヒド類、エポキシドなど
のエポキシ基を有する有機化合物、明ばん類などゼラチ
ンの架橋剤として従来公知のものがいずれも用いられて
もよい。これら架橋剤は前記のゼラチン粉末に対して気
体、液体、あるいは霧状などの流体状態で反応に供され
る。On the other hand, as the cross-linking agent, any of those conventionally known as gelatin cross-linking agents such as aldehydes such as formalin and glutaraldehyde, organic compounds having an epoxy group such as epoxide, and alums can be used. Good. These crosslinking agents are reacted in a flow material in gaseous, liquid, or mist, such as with respect to the gelatin powder.
【0016】例えば、ホルマリンのような低沸点の架橋
剤は気体で用いられる。また、常温で液状の架橋剤は、
空気中に浮遊した微粒子ゼラチンに対して、霧状にして
接触反応させてもよく、また分散媒体中に微粒子ゼラチ
ンを分散させ、これに架橋剤を添加して接触反応させ、
反応後に溶媒を蒸発させてもよい。For example, a low-boiling crosslinking agent such as formalin is used in gaseous form. In addition, the crosslinking agent that is liquid at room temperature is
The fine particle gelatin suspended in the air may be subjected to a contact reaction in the form of a mist, or the fine particle gelatin may be dispersed in a dispersion medium, and a cross-linking agent may be added thereto to cause a contact reaction,
After the reaction, the solvent may be evaporated.
【0017】ゼラチン微粒子と架橋剤の反応条件は、ゼ
ラチンの粒径、架橋剤の種類および反応方法により異な
るが常温〜150℃にて1時間〜1週間程度行うのが好
ましい。例えば、ゼラチンに対して架橋剤としてホルマ
リンを用いる場合は、ホルマリン上記の雰囲気中、常温
〜80℃にて1〜7日間処理する。従来よりホルマリ
ン、グルタルアルデヒドなどのゼラチンの架橋剤を用い
てゼラチンの親水性を調整する方法は知られているが、
いずれも前記のとおりゼラチン溶液との液相反応であ
る。本発明はゼラチン粉末を固形のまま、これらの架橋
剤とを反応させるものであり本質的に異なる。The reaction conditions of the gelatin fine particles and the crosslinking agent vary depending on the particle size of the gelatin, the kind of the crosslinking agent and the reaction method, but it is preferable to carry out the reaction at a normal temperature to 150 ° C. for about 1 hour to 1 week. For example, when formalin is used as a cross-linking agent for gelatin, the treatment is performed at room temperature to 80 ° C. for 1 to 7 days in the above-mentioned atmosphere. Conventionally, a method of adjusting the hydrophilicity of gelatin using a gelatin crosslinking agent such as formalin or glutaraldehyde is known,
All are liquid phase reactions with a gelatin solution as described above. In the present invention, the gelatin powder is reacted with these cross-linking agents in a solid state, which is essentially different.
【0018】つぎに本発明を実施例にもとづきさらに具
体的に説明するが、本発明はこれらに限定されるもので
はない。Next, the present invention will be described more specifically based on examples, but the present invention is not limited to these examples.
【0019】[0019]
【実施例】[実施例1] アルカリ処理したオセインより得られたゼラチン粉末
(12メッシュパス)をさらにジェットミル粉砕機にて微
粉砕し、平均粒径15μmのゼラチン微粉末を得た。こ
のゼラチン微粉末各50gを5つの密閉式ポリエチレン
性容器(16×23×9cm)中に薄く敷いた。ガラスビ
ーカー(30ml)にホルマリン(37%濃度)5mlを入
れたものを4つ用意し、これを前記密閉式ポリ容器内に
一緒に入れ密閉状態(25℃)にて各々24時間、48時
間、72時間及び96時間静置した。残りの1つは比較
試料とした。EXAMPLES Example 1 Gelatin Powder Obtained from Alkaline Treated Ossein
(12 mesh pass) was further pulverized with a jet mill pulverizer to obtain a fine gelatin powder having an average particle size of 15 μm. 50 g of each of the gelatin fine powders was thinly spread in five closed polyethylene containers (16 × 23 × 9 cm). Prepare four glass beakers (30 ml) containing 5 ml of formalin (37% concentration), put them together in the above-mentioned closed plastic container in a sealed state (25 ° C.) for 24 hours each. , 48 hours, 72 hours and 96 hours. The other one was a comparative sample.
【0020】それぞれ所定時間経過後ゼラチン微粉末を
取り出し、よく混合してサンプリングし、前記の方法に
より不溶化度を調べた。また、反応時間96時間の不溶
化ゼラチン粉末については、沸騰水中で5分間及び10
分間撹拌した後、同様の方法を用いて不溶化度合(%)を
測定した。これらの結果を表1に示す。After a lapse of a predetermined time, the gelatin fine powder was taken out, mixed well and sampled, and the degree of insolubilization was examined by the method described above. In addition, the insolubilized gelatin powder having a reaction time of 96 hours was treated in boiling water for 5 minutes and 10 minutes.
After stirring for minutes, the degree of insolubility (%) was measured using the same method. Table 1 shows the results.
【0021】 [表1] ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ 反応時間(時間) 24 48 72 96 ──────────────────────────────────── 不溶化 70℃ 10分間 22 48 75 88 度 合 沸騰水中 5分間 − − − 78 (%) 〃 10分間 − − − 55 ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ この結果からゼラチン粉末とホルマリンガスとの気固反
応でも充分に不溶化反応が進行することがわかる。ま
た、不溶化後もゼラチン粉末同士の凝集は見られず取り
扱いも容易であった。[Table 1] ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ Reaction time (hour) 24 48 72 96 ──────────────────────────────────── Insolubilized 70 ° C for 10 minutes 22 48 75 88 ° C Boiling 5 minutes in water---78 (%) 〃 10 minutes---55 ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ ━━━ The results show that the gas-solid reaction between the gelatin powder and formalin gas sufficiently promotes the insolubilization reaction. In addition, even after insolubilization, aggregation of the gelatin powders was not observed, and the handling was easy.
【0022】[実施例2]実施例1と同様のゼラチン粉
末(12メッシュパス)をジェットミル粉砕機にて微粉砕
し、平均粒径が5、15、25、35、100μmの5
種類のゼラチン微粉末を得た。これらのゼラチン微粉末
を各々実施例1と同様にして40℃にて96時間ホルマ
リン雰囲気中に静置し不溶化度合96%のゼラチンを得
た。Example 2 The same gelatin powder (12 mesh pass) as in Example 1 was finely pulverized by a jet mill pulverizer, and the average particle size was 5, 15, 25, 35, and 100 μm.
Various types of gelatin fine powder were obtained. Each of these fine gelatin powders was allowed to stand in a formalin atmosphere at 40 ° C. for 96 hours in the same manner as in Example 1 to obtain gelatin having a degree of insolubilization of 96%.
【0023】つぎに得られたゼラチン微粉末を改質剤と
して用い改質合成ゴムシートを成型した。成型は、合成
ゴム(SBR)100部を混練ローラーで練りながら、前
記各ゼラチン改質剤20部、カーボンブラック50部お
よび硫黄2部、軟化剤8部、老化防止剤1部を添加し、
均一に混練して行った。得られたゴムシートを、相対湿
度90%(30℃)の雰囲気下にて、10、20、3
0、60分間保持したときの吸湿性(g/m2)を測定し
た。結果を表2に示す。Next, a modified synthetic rubber sheet was molded using the obtained fine gelatin powder as a modifier. For molding, while kneading 100 parts of synthetic rubber (SBR) with a kneading roller, 20 parts of each of the above gelatin modifiers, 50 parts of carbon black and 2 parts of sulfur, 8 parts of a softener, and 1 part of an antioxidant were added,
The kneading was carried out uniformly. The obtained rubber sheet was subjected to 10, 20, 3 in an atmosphere of a relative humidity of 90% (30 ° C.).
The hygroscopicity (g / m 2 ) after holding for 0 and 60 minutes was measured. Table 2 shows the results.
【0024】 [表2] ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ 時 間 (分) ゼラチン粒径 ───────────────────── (μm) 10 20 30 60 ──────────────────────────────────── 5 1.42 1.61 1.82 2.31 15 1.39 1.58 1.80 2.30 25 1.36 1.56 1.79 2.30 35 1.13 1.49 1.70 2.28 100 0.80 1.05 1.40 2.15 ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ 表2より明らかなごとく、本発明のゼラチン改質剤を用
いた合成ゴムシートは、特に優れた吸湿性を示す。[Table 2] Time (minutes) Gelatin grains Diameter ───────────────────── (μm) 10 20 30 60 ───────────────────── ─────────────── 5 1.42 1.61 1.82 2.31 15 1.39 1.58 1.80 2.30 25 1.36 1.56 1.79 2.30 35 1.13 1.49 1.70 2.28 100 0.80 1.05 1.40 2.15 ━━━━━━━━━━く As is clear from Table 2, the synthetic rubber sheet using the gelatin modifier of the present invention is particularly excellent. It shows hygroscopicity.
【0025】[実施例3]実施例1で製造した不溶化度
合の異なる4種類のゼラチン粉末(不溶化度合:22、
48、75、88%;平均粒径15μm)および比較試
料(不溶化度合:0%)を各々改質剤として用いて6種類
の改質合成樹脂フィルムを成型した。Example 3 Four kinds of gelatin powders having different insolubilization degrees produced in Example 1 (insolubility degree: 22,
48, 75, and 88%; average particle size of 15 μm) and a comparative sample (degree of insolubility: 0%) were used as modifiers to mold six types of modified synthetic resin films.
【0026】成型は、ウレタン樹脂剤50部、ジメチル
ホルムアミド50部および改質剤10部を撹拌混合し、
その混合液を離型紙上に厚さ50μmにコーティングし
て行った。これを乾燥した後、離型紙よりコーティング
皮膜を剥がしてフィルムを得た。得られたフィルムを裁
断し、試料No.1〜5については、80℃の温水中に
1時間保持した後、50℃で乾燥し吸湿性試験を行っ
た。For molding, 50 parts of a urethane resin agent, 50 parts of dimethylformamide and 10 parts of a modifier are mixed with stirring.
The mixture was coated on release paper to a thickness of 50 μm. After drying, the coating film was peeled off from the release paper to obtain a film. The obtained film was cut, and samples Nos. 1 to 5 were kept in hot water at 80 ° C. for 1 hour, then dried at 50 ° C. and subjected to a moisture absorption test.
【0027】吸湿試験は相対湿度90%(30℃)の雰囲
気下にて、1、6、12、18時間保持した後、フィル
ムの重量を測定した。フィルムの吸湿量(g/m2)を以
下に示す。In the moisture absorption test, the film was held for 1, 6, 12, and 18 hours in an atmosphere having a relative humidity of 90% (30 ° C.), and then the weight of the film was measured. The moisture absorption (g / m 2 ) of the film is shown below.
【0028】 [表3] ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ 試料 時 間 No 不溶化度合(%) 1 6 12 18 ──────────────────────────────────── 1 0 0.91 2.93 3.18 3.52 2 22 2.02 3.25 3.44 3.80 3 48 2.31 3.38 3.61 3.93 4 75 2.40 3.50 3.86 4.18 5 88 2.72 3.72 3.99 4.42 6 無添加 0.22 0.28 0.29 0.31 ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ 上記の結果より比較試料(No.1)を用いたフィルム及
びゼラチン粉末を配合しないフィルム(No.6)は、本
発明の改質剤を配合したフィルムに比べて吸湿性が劣
る。また、不溶化度合80%を越える試料No.5の改質
剤は非常に優れた効果を示す。[Table 3] 試 料 Sample time No Degree of insolubility ( %) 1 6 12 18 ──────────────────────────────────── 10 0.91 2.93 3.18 3.52 2 22 2.02 3.25 3.44 3.80 3 48 2.31 3.38 3.61 3.93 4 75 2.40 3.50 3.86 4.18 5 88 2.72 3.72 3.99 4.42 6 No additive 0.22 0.28 0.29 0.31 ━━━━━━━━━━━━━━━━━━━━━よ り From the above results, the film using the comparative sample (No. 1) and the film (No. 6) containing no gelatin powder were the modifiers of the present invention. Is inferior to the film containing the compound. Further, the modifier of Sample No. 5 having a degree of insolubilization exceeding 80% shows a very excellent effect.
【0029】[0029]
【発明の効果】本発明によれば、不溶化されたゼラチン
が簡便にしかも低コストで製造することができる。本発
明の不溶化されたゼラチンを配合した合成樹脂及びゴム
成型物は従来のものに比べ、吸湿性に優れる。不溶化ゼ
ラチンの粒径が5〜25μmであると、特に吸湿速度が
速く吸湿性に優れる。According to the present invention, insolubilized gelatin can be produced simply and at low cost. The synthetic resin and the rubber molded product containing the insolubilized gelatin of the present invention are superior in hygroscopicity to the conventional one. When the particle size of the insolubilized gelatin is 5 to 25 μm, the moisture absorption rate is particularly high, and the moisture absorption is excellent.
Claims (2)
剤と接触させて不溶化反応を行うことを特徴とする樹脂
改質材の製造方法。 1. A method for producing a resin modifier, wherein solid gelatin powder or glue powder is brought into contact with a crosslinking agent to carry out an insolubilization reaction.
粉末を流体状態の架橋剤と接触させる請求項1の製造方
法。 2. The method according to claim 1, wherein the particle size of the powder is 5 to 30 μm, and the powder is brought into contact with a crosslinking agent in a fluid state.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP04332396A JP3106751B2 (en) | 1992-11-17 | 1992-11-17 | Method for producing resin modifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP04332396A JP3106751B2 (en) | 1992-11-17 | 1992-11-17 | Method for producing resin modifier |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH06157991A JPH06157991A (en) | 1994-06-07 |
| JP3106751B2 true JP3106751B2 (en) | 2000-11-06 |
Family
ID=18254509
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP04332396A Expired - Fee Related JP3106751B2 (en) | 1992-11-17 | 1992-11-17 | Method for producing resin modifier |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3106751B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007002084A (en) * | 2005-06-23 | 2007-01-11 | Electric Power Dev Co Ltd | Natural adhesive and method for producing the same |
| JP4786728B2 (en) * | 2009-03-27 | 2011-10-05 | 新田ゼラチン株式会社 | Viscosity agent and liquid food |
-
1992
- 1992-11-17 JP JP04332396A patent/JP3106751B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH06157991A (en) | 1994-06-07 |
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