JPH03193986A - Deinking agent for reclaiming waste paper - Google Patents
Deinking agent for reclaiming waste paperInfo
- Publication number
- JPH03193986A JPH03193986A JP1333052A JP33305289A JPH03193986A JP H03193986 A JPH03193986 A JP H03193986A JP 1333052 A JP1333052 A JP 1333052A JP 33305289 A JP33305289 A JP 33305289A JP H03193986 A JPH03193986 A JP H03193986A
- Authority
- JP
- Japan
- Prior art keywords
- acid
- deinking agent
- deinking
- ink
- alcohol
- 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.)
- Granted
Links
- 239000002761 deinking Substances 0.000 title claims abstract description 40
- 239000003795 chemical substances by application Substances 0.000 title claims abstract description 34
- 239000010893 paper waste Substances 0.000 title claims description 10
- 239000002253 acid Substances 0.000 claims abstract description 34
- 150000002148 esters Chemical class 0.000 claims abstract description 20
- 239000000539 dimer Substances 0.000 claims abstract description 13
- 125000002947 alkylene group Chemical group 0.000 claims abstract description 12
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 10
- 150000004670 unsaturated fatty acids Chemical class 0.000 claims abstract description 9
- 235000021122 unsaturated fatty acids Nutrition 0.000 claims abstract description 9
- 125000004432 carbon atom Chemical group C* 0.000 claims description 10
- 238000004064 recycling Methods 0.000 claims description 4
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 abstract description 18
- GOOHAUXETOMSMM-UHFFFAOYSA-N Propylene oxide Chemical compound CC1CO1 GOOHAUXETOMSMM-UHFFFAOYSA-N 0.000 abstract description 16
- 229920000642 polymer Polymers 0.000 abstract description 8
- 238000005187 foaming Methods 0.000 abstract description 2
- 230000002708 enhancing effect Effects 0.000 abstract 1
- 150000007513 acids Chemical class 0.000 description 11
- 238000006243 chemical reaction Methods 0.000 description 10
- 235000014113 dietary fatty acids Nutrition 0.000 description 8
- 230000000694 effects Effects 0.000 description 8
- 239000000194 fatty acid Substances 0.000 description 8
- 229930195729 fatty acid Natural products 0.000 description 8
- 150000004665 fatty acids Chemical class 0.000 description 8
- 239000000203 mixture Substances 0.000 description 8
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 239000003054 catalyst Substances 0.000 description 6
- LQZZUXJYWNFBMV-UHFFFAOYSA-N dodecan-1-ol Chemical compound CCCCCCCCCCCCO LQZZUXJYWNFBMV-UHFFFAOYSA-N 0.000 description 6
- AMQJEAYHLZJPGS-UHFFFAOYSA-N N-Pentanol Chemical compound CCCCCO AMQJEAYHLZJPGS-UHFFFAOYSA-N 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 4
- 229920001131 Pulp (paper) Polymers 0.000 description 4
- -1 alkylbenzene sulfonates Chemical class 0.000 description 4
- 238000007664 blowing Methods 0.000 description 4
- 239000003518 caustics Substances 0.000 description 4
- 229910001873 dinitrogen Inorganic materials 0.000 description 4
- 230000032050 esterification Effects 0.000 description 4
- 238000005886 esterification reaction Methods 0.000 description 4
- GLDOVTGHNKAZLK-UHFFFAOYSA-N octadecan-1-ol Chemical compound CCCCCCCCCCCCCCCCCCO GLDOVTGHNKAZLK-UHFFFAOYSA-N 0.000 description 4
- 238000006116 polymerization reaction Methods 0.000 description 4
- 229910052700 potassium Inorganic materials 0.000 description 4
- 239000011591 potassium Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 239000012190 activator Substances 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 238000005188 flotation Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 239000000178 monomer Substances 0.000 description 3
- 230000035515 penetration Effects 0.000 description 3
- CFQZKFWQLAHGSL-FNTYJUCDSA-N (3e,5e,7e,9e,11e,13e,15e,17e)-18-[(3e,5e,7e,9e,11e,13e,15e,17e)-18-[(3e,5e,7e,9e,11e,13e,15e)-octadeca-3,5,7,9,11,13,15,17-octaenoyl]oxyoctadeca-3,5,7,9,11,13,15,17-octaenoyl]oxyoctadeca-3,5,7,9,11,13,15,17-octaenoic acid Chemical compound OC(=O)C\C=C\C=C\C=C\C=C\C=C\C=C\C=C\C=C\OC(=O)C\C=C\C=C\C=C\C=C\C=C\C=C\C=C\C=C\OC(=O)C\C=C\C=C\C=C\C=C\C=C\C=C\C=C\C=C CFQZKFWQLAHGSL-FNTYJUCDSA-N 0.000 description 2
- OYHQOLUKZRVURQ-NTGFUMLPSA-N (9Z,12Z)-9,10,12,13-tetratritiooctadeca-9,12-dienoic acid Chemical compound C(CCCCCCC\C(=C(/C\C(=C(/CCCCC)\[3H])\[3H])\[3H])\[3H])(=O)O OYHQOLUKZRVURQ-NTGFUMLPSA-N 0.000 description 2
- WRIDQFICGBMAFQ-UHFFFAOYSA-N (E)-8-Octadecenoic acid Natural products CCCCCCCCCC=CCCCCCCC(O)=O WRIDQFICGBMAFQ-UHFFFAOYSA-N 0.000 description 2
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 description 2
- QSBYPNXLFMSGKH-UHFFFAOYSA-N 9-Heptadecensaeure Natural products CCCCCCCC=CCCCCCCCC(O)=O QSBYPNXLFMSGKH-UHFFFAOYSA-N 0.000 description 2
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 2
- 239000005642 Oleic acid Substances 0.000 description 2
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 description 2
- BLRPTPMANUNPDV-UHFFFAOYSA-N Silane Chemical compound [SiH4] BLRPTPMANUNPDV-UHFFFAOYSA-N 0.000 description 2
- 239000004115 Sodium Silicate Substances 0.000 description 2
- 235000021355 Stearic acid Nutrition 0.000 description 2
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 2
- 238000004220 aggregation Methods 0.000 description 2
- 150000001298 alcohols Chemical class 0.000 description 2
- 150000005215 alkyl ethers Chemical class 0.000 description 2
- 125000000129 anionic group Chemical group 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- ZSIAUFGUXNUGDI-UHFFFAOYSA-N hexan-1-ol Chemical compound CCCCCCO ZSIAUFGUXNUGDI-UHFFFAOYSA-N 0.000 description 2
- ZXEKIIBDNHEJCQ-UHFFFAOYSA-N isobutanol Chemical compound CC(C)CO ZXEKIIBDNHEJCQ-UHFFFAOYSA-N 0.000 description 2
- QXJSBBXBKPUZAA-UHFFFAOYSA-N isooleic acid Natural products CCCCCCCC=CCCCCCCCCC(O)=O QXJSBBXBKPUZAA-UHFFFAOYSA-N 0.000 description 2
- GOQYKNQRPGWPLP-UHFFFAOYSA-N n-heptadecyl alcohol Natural products CCCCCCCCCCCCCCCCCO GOQYKNQRPGWPLP-UHFFFAOYSA-N 0.000 description 2
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 2
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 2
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N oleic acid Chemical compound CCCCCCCC\C=C/CCCCCCCC(O)=O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 description 2
- 235000011118 potassium hydroxide Nutrition 0.000 description 2
- 238000010926 purge Methods 0.000 description 2
- 229910000077 silane Inorganic materials 0.000 description 2
- 235000011121 sodium hydroxide Nutrition 0.000 description 2
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 2
- 229910052911 sodium silicate Inorganic materials 0.000 description 2
- 239000008117 stearic acid Substances 0.000 description 2
- 239000003784 tall oil Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- QPCDCPDFJACHGM-UHFFFAOYSA-N N,N-bis{2-[bis(carboxymethyl)amino]ethyl}glycine Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(=O)O)CCN(CC(O)=O)CC(O)=O QPCDCPDFJACHGM-UHFFFAOYSA-N 0.000 description 1
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 1
- FXXACINHVKSMDR-UHFFFAOYSA-N acetyl bromide Chemical compound CC(Br)=O FXXACINHVKSMDR-UHFFFAOYSA-N 0.000 description 1
- 238000007259 addition reaction Methods 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 238000007605 air drying Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 125000005233 alkylalcohol group Chemical group 0.000 description 1
- 239000007844 bleaching agent Substances 0.000 description 1
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000007872 degassing Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000002736 nonionic surfactant Substances 0.000 description 1
- 238000007645 offset printing Methods 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 235000019198 oils Nutrition 0.000 description 1
- 235000021313 oleic acid Nutrition 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000003352 sequestering agent Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000003549 soybean oil Substances 0.000 description 1
- 235000012424 soybean oil Nutrition 0.000 description 1
- 150000003871 sulfonates Chemical class 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000012719 thermal polymerization Methods 0.000 description 1
- 229920001187 thermosetting polymer Polymers 0.000 description 1
- DHCDFWKWKRSZHF-UHFFFAOYSA-L thiosulfate(2-) Chemical compound [O-]S([S-])(=O)=O DHCDFWKWKRSZHF-UHFFFAOYSA-L 0.000 description 1
- 239000013638 trimer Substances 0.000 description 1
- PHYFQTYBJUILEZ-IUPFWZBJSA-N triolein Chemical compound CCCCCCCC\C=C/CCCCCCCC(=O)OCC(OC(=O)CCCCCCC\C=C/CCCCCCCC)COC(=O)CCCCCCC\C=C/CCCCCCCC PHYFQTYBJUILEZ-IUPFWZBJSA-N 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
- 239000004711 α-olefin Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/64—Paper recycling
Landscapes
- Polyethers (AREA)
- Paper (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、新聞、雑誌、ちらし等の印刷古紙再生に用−
いられる脱墨剤に関する。さらに詳しくは新聞、雑誌等
をフローチーシラン法で脱墨処理するに際し、発砲性、
インキ捕集性を高め、高白色度で残インキの少ない脱墨
パルプを得ることができる脱墨剤に関する。[Detailed Description of the Invention] (Industrial Application Field) The present invention is applicable to the recycling of printed waste paper such as newspapers, magazines, flyers, etc.
Regarding the deinking agent that can be used. More specifically, when deinking newspapers, magazines, etc. using the flow-chie silane method,
This invention relates to a deinking agent that can improve ink collection ability and produce deinked pulp with high whiteness and little residual ink.
(従来の技術)
新聞、雑誌等の再生利用は古くから行われてきているが
、特に最近は森林資源の保護や脱墨パルプの用途拡大に
より、古紙の有効利用はその重要性を増してきている。(Conventional technology) Recycling of newspapers, magazines, etc. has been carried out for a long time, but in recent years, the effective use of waste paper has become increasingly important due to the protection of forest resources and the expansion of uses for deinked pulp. There is.
印刷古紙を再生するには、印刷古紙を通常離解機内で苛
性ソーダ、珪酸ソーダ等のアルカリ薬剤と脱墨剤、さら
に必要に応じて過酸化水素、次亜硫酸塩等の漂白剤、E
DTA、DTPA等の金属イオン封鎖剤と共に離解し、
パルプからインキを脱離させ、脱離したインキを水洗浄
処理やフローチーシラン処理によりパルプから分離する
方法が広く採用されている。To recycle waste printed paper, it is usually treated in a disintegrating machine with an alkaline agent such as caustic soda or sodium silicate, a deinking agent, and, if necessary, a bleaching agent such as hydrogen peroxide or hyposulfite.
Disintegrates with sequestering agents such as DTA and DTPA,
A widely used method is to desorb ink from pulp and then separate the desorbed ink from the pulp by water washing or flow-free silane treatment.
脱墨剤には、大別して、*I[したインキを細かく分散
させた状態で系外に除去することを目的とする分散系脱
墨剤と、脱離したインキをある程度凝集させた状態で系
外に除去することを目的とする凝集系脱墨剤があり、こ
のうち現在では再生パルプの白色度をより高めることの
できる凝集系脱墨剤が広(用いられている。Deinking agents can be roughly divided into *I[dispersion type deinking agents, which aim to remove the removed ink from the system in a finely dispersed state; There are agglomerated deinking agents whose purpose is to remove waste materials, and among these, agglomerated deinking agents that can further increase the whiteness of recycled pulp are widely used.
脱墨剤としては、アルキルベンゼンスルホン酸塩、高級
アルコール硫酸エステル、αオレフィンスルホン酸塩等
の陰イオン活性剤、ポリオキシアルキレンアルキルエー
テル、ポリオキシアルキレンアルキルアリルエーテル、
脂肪酸アルカノールアマイド等の非イオン活性剤あるい
は高級脂肪酸などが単独または2種以上配合されてきた
。しかしながら、従来の脱墨剤で高級脂肪酸系は、イン
キ凝集効果は高いが、パルプへの浸透、インキ剥離効果
が低く充分な脱墨効果が得られない問題がある一方、ポ
リオキシアルキレンアルキルエーテルなどアルキレンオ
キシド付加物系(例えば特公昭64−11756号、特
開昭63−303190号および特開平1−11108
6号)はパルプへの浸透、インキ剥離分散効果が高いが
インキとの親和性に劣るため、インキの凝集効果が未だ
充分でない。Examples of deinking agents include anionic activators such as alkylbenzene sulfonates, higher alcohol sulfates, α-olefin sulfonates, polyoxyalkylene alkyl ethers, polyoxyalkylene alkyl allyl ethers,
Nonionic surfactants such as fatty acid alkanolamides or higher fatty acids have been used alone or in combination of two or more. However, conventional deinking agents based on higher fatty acids have a high ink aggregation effect, but have the problem of poor penetration into pulp and ink removal effect, making it impossible to obtain a sufficient deinking effect. Alkylene oxide adduct systems (e.g., Japanese Patent Publication No. 11756/1983, 303190/1982, and 11108/1999)
No. 6) has a high ink penetration and ink removal and dispersion effect, but has poor affinity with the ink, so the ink aggregation effect is still insufficient.
(本発明が解決しようとする問題点)
特に、最近の古紙は印刷技術の向上、特に印刷インキの
オフセット化でインキ組成が変化し、乾性油や熱硬化性
樹脂が用いられている現状においては、このためインキ
皮膜が強固に硬化しており、従来の脱墨剤ではインキを
脱離し、パルプから分離することが難しく、高品質の脱
墨パルプを得ることができなかった。(Problems to be solved by the present invention) In particular, in recent years, the ink composition of waste paper has changed due to improvements in printing technology, especially offset printing ink, and drying oil and thermosetting resin are used. As a result, the ink film is strongly cured, and it is difficult to remove the ink and separate it from the pulp using conventional deinking agents, making it impossible to obtain high-quality deinked pulp.
また、脱墨バルブの用途拡大にともない、より高白色度
、残存インキの少ない脱墨バルブが求められている。Additionally, as the uses of deinking valves expand, there is a demand for deinking valves with higher whiteness and less residual ink.
そこで、本発明はこれら脱離、分離の難しくなった古紙
についても容易に高説墨の可能な脱墨剤を提供すること
を目的とする。Therefore, it is an object of the present invention to provide a deinking agent that can easily remove high quality ink from waste paper that is difficult to remove and separate.
(課題を解決するための手段)
そこで、本発明者らは上記目的を達成するためにはイン
キ剥離効果が大きいと同時に、インキ凝集効果および発
泡性が大きい脱墨剤であることが必要であることに鑑み
、鋭意研究を重ねた結果、高級不飽和脂肪酸のダイマー
酸および/またはポリマー酸とアルコールからの部分エ
ステルにアルキレンオキシドを付加させたものは上記必
要な物性を備えることを見出し、本発明を完成した。(Means for Solving the Problems) Therefore, in order to achieve the above object, the present inventors found that it is necessary to create a deinking agent that has a high ink removal effect, as well as a high ink coagulation effect and foaming property. In view of this, as a result of extensive research, it was discovered that alkylene oxide is added to partial esters of dimer acids and/or polymer acids of higher unsaturated fatty acids and alcohols, and the present invention completed.
すなわち、本発明は炭素数16〜20の高級不飽和脂肪
酸のダイマー酸および/またはポリマー酸と炭素数1〜
18のアルコールとからの部分エステルにアルキレンオ
キシドの1種または2種以上を300モル以下付加した
付加物を主成分とすることを要旨とする古紙再生用脱墨
剤にある。That is, the present invention relates to a dimer acid and/or a polymer acid of a higher unsaturated fatty acid having 16 to 20 carbon atoms and a higher unsaturated fatty acid having 1 to 20 carbon atoms.
The deinking agent for waste paper recycling is characterized in that the main component is an adduct obtained by adding one or more alkylene oxides in an amount of 300 moles or less to a partial ester of No. 18 alcohol.
本発明において使用される炭素数16〜20の高級不飽
和脂肪酸のダイマー酸およびポリマー酸は高級脂肪酸モ
ノエン酸またはジエン酸などの多量化により得られる0
例えばオレイン酸、リノール酸、リルン酸などの不飽和
脂肪酸単量体を熱重合、またはその他の方法により得ら
れるものが挙げられるが、現在一般に市販され入手し易
いものはオレイン酸とリノール酸の熱重合による炭素数
36のダイマー酸および炭素数54のトリマー酸、また
はこれらの混合物である。その分子構造は明確でなく、
種々の異性体の混合物として工業的に提供されており、
トール油脂肪酸の重合により得られるハリダイマー(播
磨化成工業製)、大豆油脂肪酸の重合により得られるも
のなどが好適例である0本発明は少量のモノマー酸の混
入を制限するものではない。Dimer acids and polymer acids of higher unsaturated fatty acids having 16 to 20 carbon atoms used in the present invention are obtained by polymerizing higher fatty acid monoenoic acids or dienoic acids.
Examples include those obtained by thermal polymerization of unsaturated fatty acid monomers such as oleic acid, linoleic acid, and linoleic acid, or by other methods. It is a dimer acid having 36 carbon atoms and a trimer acid having 54 carbon atoms obtained by polymerization, or a mixture thereof. Its molecular structure is not clear;
It is commercially available as a mixture of various isomers,
Suitable examples include haridimer (manufactured by Harima Kasei Kogyo) obtained by polymerization of tall oil fatty acids and those obtained by polymerization of soybean oil fatty acids.The present invention does not limit the incorporation of small amounts of monomer acids.
また、部分エステル化用の炭素数1〜18のアルコール
としては通常の一級、二級、三級のアルキルアルコール
で、メタノール、エタノール、イソプロパツール、n−
ブタノール、イソブタノール、5ec−ブタノール、t
ert−ブタノール、アミルアルコール、ヘキシルアル
コール、ラウリルアルコール、オキソ合成その他の合成
アルコール混合物、ステアリルアルコールなどが挙げら
れる。In addition, alcohols having 1 to 18 carbon atoms for partial esterification include ordinary primary, secondary, and tertiary alkyl alcohols such as methanol, ethanol, isopropanol, n-
Butanol, isobutanol, 5ec-butanol, t
Examples include ert-butanol, amyl alcohol, hexyl alcohol, lauryl alcohol, oxo-synthesized and other synthetic alcohol mixtures, and stearyl alcohol.
エステル化反応性、アルキレンオキシド付加した後の性
質から炭素数5〜12が特に好ましい。In view of esterification reactivity and properties after addition of alkylene oxide, carbon atoms having 5 to 12 carbon atoms are particularly preferred.
部分エステルとしては、ダイマー酸およびポリマー酸1
分子につき、少なくとも1個のカルボン酸が残るだけの
エステル化量とするのが好ましい。As partial esters, dimer acids and polymer acids 1
Preferably, the amount of esterification is such that at least one carboxylic acid remains per molecule.
ダイマー酸およびポリマー酸の上記アルコールによる部
分エステル化の反応は公知の方法を利用できる。A known method can be used for partial esterification of dimer acid and polymer acid with the above alcohol.
また、本発明において用いられるアルキレンオキシドと
してはエチレンオキシド、プロピレンオキシド、ブチレ
ンオキシドが挙げられ、1種または2種以上を付加して
良く、2種以上の付加はランダム付加もしくはブロック
付加によって行うことができるが、エチレンオキシドと
プロピレンオキシドの組み合わせでランダムまたはブロ
ック付加が最も好適である。アルキレンオキシドの付加
モル数は300モル以下であり、300モル以上では脱
墨でのフローテーション工程の発砲性が低下し、また剥
離したインキの凝集性を損ない、高品質の再生パルプが
得られない。アルキレンオキシドの付加モル数は10〜
200モルが特に好適である。付加反応は特に限定され
るものでな(、常法で行うことができる0例えば、上記
ダイマー酸および/またはポリマー酸の部分エステルに
触媒としてのアルカリの存在下100〜200°Cに加
熱して1〜5kg/cdでアルキレンオキシドを吹き込
み、数時間反応し、付加生成物を得ることができる。Furthermore, the alkylene oxide used in the present invention includes ethylene oxide, propylene oxide, and butylene oxide, and one or more types may be added, and the addition of two or more types can be performed by random addition or block addition. However, random or block addition with a combination of ethylene oxide and propylene oxide is most preferred. The number of moles of alkylene oxide added is 300 moles or less; if it is more than 300 moles, the foamability of the flotation step during deinking will decrease, and the cohesiveness of the peeled ink will be impaired, making it impossible to obtain high-quality recycled pulp. . The number of moles of alkylene oxide added is 10~
200 mol is particularly preferred. The addition reaction is not particularly limited (it can be carried out in a conventional manner, for example, by heating the partial ester of the dimer acid and/or polymeric acid to 100 to 200°C in the presence of an alkali as a catalyst). An addition product can be obtained by blowing alkylene oxide at a rate of 1 to 5 kg/cd and reacting for several hours.
本発明の脱墨剤の添加場所についてはパルパーまたは熟
成タワー前の工程が好ましいが、フローテータ−に添加
使用することもできる。また木脱墨剤は単独で充分効果
的であるが、その他の脱墨剤、例えば陰イオン活性剤や
ポリオキシアルキレンアルキルエーテルなどの非イオン
活性剤、高級脂肪酸などを併用することも差し支えない
。The deinking agent of the present invention is preferably added before the pulper or aging tower, but it can also be added to the floatator. Although the wood deinking agent alone is sufficiently effective, other deinking agents such as anionic activators, nonionic activators such as polyoxyalkylene alkyl ether, higher fatty acids, etc. may be used in combination.
(作用効果)
本発明の脱墨剤は高級不飽和脂肪酸のダイマー酸および
/またはポリマー酸とアルコールとからの部分エステル
にアルキレンオキシドを付加しているため、インキへの
浸透、剥離性に優れ、また、インキの捕集性が従来の脱
墨剤に比べ非常に優れるため、高品質の再生パルプを容
易に得ることができる。(Effect) The deinking agent of the present invention has an alkylene oxide added to a partial ester of dimer acid and/or polymer acid of higher unsaturated fatty acid and alcohol, so it has excellent ink penetration and releasability. Furthermore, since the ink collection property is much better than that of conventional deinking agents, high-quality recycled pulp can be easily obtained.
(実施例) 以下、本発明を実施例に基づき具体的に説明する。(Example) Hereinafter, the present invention will be specifically explained based on Examples.
〔実施例1〕
ポリマー酸として、トール油脂肪酸の重合により得られ
たダイマー酸79%、トリマー118%、モノマー酸3
%で酸価193、平均分子量605のハリダイマー25
0(横磨化成工業製)とnアミルアルコールを130〜
160°Cで反応させ、酸価90、平均分子量675の
部分エステルを得た。このエステル675gを耐圧反応
容器に入れ、触媒として苛性カリ3.4gを加え、17
0″Cに加熱し、容器内を脱気後窒素ガスで置換し、エ
チレンオキシド440.5gを圧力1〜5 kg/cd
で3時間かけて吹き込み反応させてエチレンオキシド1
0モル付加の脱墨剤を得た。[Example 1] Polymer acids include 79% dimer acid, 118% trimer, and 3 monomer acids obtained by polymerization of tall oil fatty acids.
%, acid value 193, average molecular weight 605 Hallidimer 25
0 (manufactured by Yokoma Kasei Kogyo) and n amyl alcohol from 130 to
The reaction was carried out at 160°C to obtain a partial ester with an acid value of 90 and an average molecular weight of 675. Put 675 g of this ester into a pressure-resistant reaction vessel, add 3.4 g of caustic potassium as a catalyst, and
Heating to 0''C, degassing the inside of the container and purging it with nitrogen gas, and adding 440.5g of ethylene oxide at a pressure of 1 to 5 kg/cd.
The reaction was carried out by blowing over 3 hours to produce 1 ethylene oxide.
A deinking agent with 0 mole addition was obtained.
〔実施例2〕
ハリダイマー250とラウリルアルコールを200〜2
50°Cで反応して酸価79、平均分子量773の部分
エステルを得た。このエステル386.5gを耐圧容器
に入れ、触媒として苛性カリ1゜9gを加え、170°
Cに加熱し、容器内を脱気後窒素ガスで置換し、エチレ
ンオキシド881gを圧力1〜5 kg / cdで5
時間かけて吹き込み反応させてエチレンオキシド40モ
ル付加の脱墨剤を得た。[Example 2] Haridimer 250 and lauryl alcohol 200-2
The reaction was carried out at 50°C to obtain a partial ester having an acid value of 79 and an average molecular weight of 773. 386.5 g of this ester was placed in a pressure container, 1.9 g of caustic potassium was added as a catalyst, and the mixture was heated to 170°.
The inside of the container was degassed and replaced with nitrogen gas, and 881 g of ethylene oxide was heated at a pressure of 1 to 5 kg/cd.
A deinking agent containing 40 moles of ethylene oxide was obtained by blowing and reacting over a period of time.
〔実施例3〕
実施例2で得られた部分エステルに実施例2と同様にし
てエチレンオキシドを吹き込み反応させ、次いでプロピ
レンオキシド580.8gを1〜5kg/ cdで5時
間かけて吹き込み反応させ、エチレンオキシド40モル
およびプロピレンオキシド20モル付加の脱墨剤を得た
。[Example 3] Ethylene oxide was blown into the partial ester obtained in Example 2 in the same manner as in Example 2, and then 580.8 g of propylene oxide was blown into the partial ester obtained in Example 2 at a rate of 1 to 5 kg/cd for 5 hours to react. A deinking agent containing 40 mol and 20 mol of propylene oxide was obtained.
(実施例4〕
実施例2と同様にして得られたハリダイマー250ラウ
リルアルコールエステル193.3g’H4圧容器に大
容器触媒として苛性カリ1.0gを加え、170°Cに
加熱し、容器内を脱気後窒素ガスで置換し、エチレンオ
キシド881gを1〜5 kg / c4で5時間かけ
て吹き込み反応させ、次いでプロピレンオキシド290
.4gを3時間かけて吹き込み反応させ、プロピレンオ
キシド80モルおよびプロピレンオキシド20モルラン
ダム付加の脱墨剤を得た。(Example 4) 1.0 g of caustic potash was added as a large container catalyst to a large container catalyst, 193.3 g of Halidimer 250 lauryl alcohol ester obtained in the same manner as in Example 2, and the container was degassed. After the air was replaced with nitrogen gas, 881 g of ethylene oxide was blown into the reactor at a rate of 1 to 5 kg/c4 over 5 hours, and then 290 g of propylene oxide was added.
.. 4 g was blown into the solution over a period of 3 hours and reacted to obtain a deinking agent containing 80 moles of propylene oxide and 20 moles of propylene oxide randomly added.
〔実施例5〕
反応条件として、エチレンオキシドとプロピレンオキシ
ドを同時に8時間かけて反応させた以外は実施例4と同
様にしてエチレンオキシド80モルおよびプロピレンオ
キシド20モルランダム付加の脱墨剤を得た。[Example 5] A deinking agent with random addition of 80 moles of ethylene oxide and 20 moles of propylene oxide was obtained in the same manner as in Example 4, except that the reaction conditions were that ethylene oxide and propylene oxide were reacted simultaneously over 8 hours.
〔実施例6〕
反応条件として、プロピレンオキシド吹き込み反応させ
、次いでエチレンオキシド吹き込み反応させた以外は実
施例4と同様にしてプロピレンオキシド20モルおよび
エチレンオキシド80モル付加物の脱墨剤を得た。[Example 6] A deinking agent of an adduct of 20 moles of propylene oxide and 80 moles of ethylene oxide was obtained in the same manner as in Example 4, except that the reaction conditions were that propylene oxide was blown into the reactor and then ethylene oxide was blown into the reactor.
〔実施例7〕
反応条件として、エチレンオキシド881gとブチレン
オキシド90.1gを用いた以外は実施例4と同様にし
てエチレンオキシド80モルおよびブチレンオキシド5
モル付加の脱墨剤を得た。[Example 7] The reaction conditions were the same as in Example 4 except that 881 g of ethylene oxide and 90.1 g of butylene oxide were used.
A molar addition deinking agent was obtained.
(実施例8]
ハリダイマー250とステアリルアルコールを200〜
250 ”Cで反応して酸価71、平均分子量858の
部分エステルを得た。このエステル171.6gを耐圧
容器に入れ、触媒として苛性カリ0.9gを加え、17
0 ’Cに加熱し、脱気後窒素ガスで置換し、エチレン
オキシド1321.5gを1〜5 kg/dで7時間か
けて吹き込み反応させ、次いでプロピレンオキシド58
0.8gを7時間かけて吹き込み反応させて、エチレン
オキシド150モルおよびプロピレンオキシド60モル
付加の脱墨剤を得た。(Example 8) Halidimer 250 and stearyl alcohol are mixed at 200~
A partial ester having an acid value of 71 and an average molecular weight of 858 was obtained by reacting at 250"C. 171.6g of this ester was placed in a pressure vessel, 0.9g of caustic potassium was added as a catalyst,
After heating to 0'C and purging with nitrogen gas, 1321.5g of ethylene oxide was blown in at a rate of 1 to 5 kg/d for 7 hours, and then 58g of propylene oxide was added.
By blowing 0.8 g over 7 hours and causing a reaction, a deinking agent containing 150 moles of ethylene oxide and 60 moles of propylene oxide was obtained.
(実施例9〕
ダイマー酸25%、トリマー酸75%からなる酸価19
0、平均分子量774のハリダイマー500(横磨化成
工業製)とn−アミルアルコールを130〜160 ’
Cで反応して酸価72、平均分子1879の部分エステ
ルを得た。このエステル175.8g、苛性カリ0.9
gを用いた以外は実施例8と同様に反応して、エチレン
オキシド150モルおよびプロピレンオキシド50モル
付加の脱墨剤を得た。(Example 9) Acid value 19 consisting of 25% dimer acid and 75% trimer acid
0, Haridimer 500 (manufactured by Yokoma Kasei Kogyo) with an average molecular weight of 774 and n-amyl alcohol of 130 to 160'
A partial ester having an acid value of 72 and an average molecular weight of 1,879 was obtained by reacting with C. This ester 175.8g, caustic potassium 0.9
A deinking agent containing 150 moles of ethylene oxide and 50 moles of propylene oxide was obtained by reacting in the same manner as in Example 8, except that g was used.
〔実施例10]
ハリダイマー500とラウリルアルコールを200〜2
50°Cで反応して酸価97、平均分子量942の部分
エステルを得た。このエステル235.5gと苛性カリ
1.2gを用いた以外は実施例4と同様にして、エチレ
ンオキシド80モルおよびプロピレンオキシド20モル
付加の脱墨剤を得た。[Example 10] Haridimer 500 and lauryl alcohol 200-2
The reaction was carried out at 50°C to obtain a partial ester having an acid value of 97 and an average molecular weight of 942. A deinking agent containing 80 moles of ethylene oxide and 20 moles of propylene oxide was obtained in the same manner as in Example 4, except that 235.5 g of this ester and 1.2 g of caustic potash were used.
〔比較例2〜4〕
上記ポリマー酸の代わりにオレイン酸、ステアリン酸、
ラウリルアルコールを用い、実施例と同様の反応により
オレイン# (EO) 、i。(PO)+6、ステアリ
ン酸(Eo)z。(po) 、。、ラウリルアルコール
(EO)2゜(PO)+oを得た。[Comparative Examples 2 to 4] Oleic acid, stearic acid,
Olein # (EO), i., was obtained by the same reaction as in Example using lauryl alcohol. (PO)+6, stearic acid (Eo)z. (po),. , lauryl alcohol (EO) 2°(PO)+o was obtained.
〔脱墨試験例]
J、TAPP紙パルプ試験法No、39−82に準じて
、オフセット印刷新聞古紙80%とちらし20%からな
る原料古紙を3 X 3 cyaに細断し、一定量をバ
ルブ離解機に入れ、温水を入れ、古紙重量に対して苛性
ソーダ1.5%、3号珪酸ソーダ3.0%、30%過酸
化水素水3,0%、第1表に示す各脱墨剤0.3%を加
え、バルブ濃度4.0%、50°Cで30分離解した後
、50°Cで1時間熟成した。その抜水を加えてバルブ
濃度1.0%に希釈し、30℃で10分間フローテーシ
ョン処理を行った。フローテーション後のバルブスラリ
ーを80メツシユワイヤーで脱水し5.0%にi4m後
、水を加えてバルブ濃度1.0%に希釈し、角型シート
マシンにて坪量100 g/rrrのバルブシートを調
製した。[Example of deinking test] According to J, TAPP Paper Pulp Test Method No. 39-82, raw material waste paper consisting of 80% offset printed newspaper waste paper and 20% flyer was shredded into 3 x 3 cya, and a certain amount was cut into pieces by valve. Place in a disintegrating machine, add hot water, and add 1.5% caustic soda, 3.0% No. 3 sodium silicate, 3.0% hydrogen peroxide solution, and 0 each deinking agent shown in Table 1 based on the weight of the waste paper. .3% was added, the bulb concentration was 4.0%, and the mixture was dissolved at 50°C for 30 minutes, and then aged at 50°C for 1 hour. The drained water was added to dilute the bulb concentration to 1.0%, and a flotation treatment was performed at 30° C. for 10 minutes. The valve slurry after flotation was dehydrated with an 80 mesh wire to 5.0%, after 4 m, water was added to dilute it to a valve concentration of 1.0%, and a valve with a basis weight of 100 g/rrr was prepared using a square sheet machine. A sheet was prepared.
得られたバルブシートの白色度はJIS P8123
に準じハンター白色光度計で測定した。The whiteness of the obtained valve seat is JIS P8123.
It was measured using a Hunter white photometer according to .
また残カーボンの表示は、脱墨バルブ中のカーボンの簡
易測定法により、得られたバルブシートを家庭用ミキサ
ーで粉砕し、この100■をアセチルブロマイド/酢酸
(1/3容量比)混合液に入れ、65〜70°C,2時
間でセルロースを溶解し、アトバンチツク東洋製グラス
ファイバーフィルター(GS25、直径55m+a)で
濾過し、フィルタを風乾後、色差計にて測定した。得ら
れた再生バルブシートの残存インキが少ないほど残カー
ボンL値は大きい値を示す。In addition, to display the remaining carbon, use a simple method for measuring carbon in deinking valves.The resulting valve sheet is ground in a household mixer, and 100 ml of this is mixed with acetyl bromide/acetic acid (1/3 volume ratio) mixture. The cellulose was dissolved at 65 to 70° C. for 2 hours, and the mixture was filtered using a glass fiber filter (GS25, diameter 55 m+a) manufactured by Atobanchiku Toyo Co., Ltd. After air-drying the filter, measurement was performed using a color difference meter. The smaller the residual ink on the obtained recycled valve seat, the larger the residual carbon L value.
その結果を併せて第1表に示す。The results are also shown in Table 1.
Claims (1)
酸および/またはポリマー酸と炭素数1〜18のアルコ
ールとからの部分エステルに、アルキレンオキシドの1
種また2種以上を300モル以下付加してなる付加物を
主成分とする古紙再生用脱墨剤。(1) A partial ester of a dimer acid and/or a polymeric acid of a higher unsaturated fatty acid having 16 to 20 carbon atoms and an alcohol having 1 to 18 carbon atoms is added with 1 of alkylene oxide.
A deinking agent for waste paper recycling whose main component is an adduct obtained by adding 300 moles or less of a species or two or more species.
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP33305289A JP2838423B2 (en) | 1989-12-22 | 1989-12-22 | Deinking agent for recycled paper |
US07/568,881 US5158697A (en) | 1989-10-26 | 1990-08-17 | Deinking agent for reproduction of printed waste papers |
FR9104061A FR2674871B1 (en) | 1989-10-26 | 1991-04-03 | DEINKING AGENT FOR THE REGENERATION OF OLD PRINTED PAPERS. |
DE19914110762 DE4110762C2 (en) | 1989-10-26 | 1991-04-03 | Decolorizing agent for the processing of printed waste paper |
GB9108623A GB2255111B (en) | 1989-10-26 | 1991-04-23 | Deinking agent |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP33305289A JP2838423B2 (en) | 1989-12-22 | 1989-12-22 | Deinking agent for recycled paper |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH03193986A true JPH03193986A (en) | 1991-08-23 |
JP2838423B2 JP2838423B2 (en) | 1998-12-16 |
Family
ID=18261730
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP33305289A Expired - Fee Related JP2838423B2 (en) | 1989-10-26 | 1989-12-22 | Deinking agent for recycled paper |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2838423B2 (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0324126A (en) * | 1989-06-21 | 1991-02-01 | Ajinomoto Co Inc | Polymerized fatty acid ester and deinking of waste-paper by using same |
-
1989
- 1989-12-22 JP JP33305289A patent/JP2838423B2/en not_active Expired - Fee Related
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0324126A (en) * | 1989-06-21 | 1991-02-01 | Ajinomoto Co Inc | Polymerized fatty acid ester and deinking of waste-paper by using same |
Also Published As
Publication number | Publication date |
---|---|
JP2838423B2 (en) | 1998-12-16 |
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