JPS60262849A - Production of amino resin molding material - Google Patents

Production of amino resin molding material

Info

Publication number
JPS60262849A
JPS60262849A JP11928484A JP11928484A JPS60262849A JP S60262849 A JPS60262849 A JP S60262849A JP 11928484 A JP11928484 A JP 11928484A JP 11928484 A JP11928484 A JP 11928484A JP S60262849 A JPS60262849 A JP S60262849A
Authority
JP
Japan
Prior art keywords
powder
fed
pulp
resin
tank
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.)
Pending
Application number
JP11928484A
Other languages
Japanese (ja)
Inventor
Tomio Takatsuka
高塚 富夫
Genichi Ishikawa
元一 石川
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Panasonic Electric Works Co Ltd
Original Assignee
Matsushita Electric Works Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Matsushita Electric Works Ltd filed Critical Matsushita Electric Works Ltd
Priority to JP11928484A priority Critical patent/JPS60262849A/en
Publication of JPS60262849A publication Critical patent/JPS60262849A/en
Pending legal-status Critical Current

Links

Landscapes

  • Compositions Of Macromolecular Compounds (AREA)

Abstract

PURPOSE:To obtain the titled molding material which can dispense with drying and kneading stages and save the cost of equipment, space and energy, by mixing a liquid amino resin having a low water content with pulp powder, crushing the mixture, coloring it and tableting it. CONSTITUTION:Urea or melamine (A) from a feed tank 1, 1.2-3mol (per mol of component A) of paraformaldehyde (B) from a feed tank 2 and a catalyst (C) such as NaOH from a catalyst tank 3 are fed through constant feeders 4, 5, 6 to a closed, complete discharge type reactor 7 where a continuous condensation reaction is carried out in a liquid state (at 65 deg.C) to obtain a liquid amino resin having a low water content (e.g. 3wt%). The resin is fed through a cooler 18 to a crusher 19, where the resin is mixed with pulp powder fed through a constant feeder 10 from a pulp tank 9 and the mixture is crushed into a powder having a particle size of 60 mesh or below. The powder is fed through a collector 20 and a constant feeder 21 to a coloring and mixing machine 22, where the powder is colored with a pigment fed through a constant feeder 14. The colored powder is tableted in a tableting machine 26.

Description

【発明の詳細な説明】 [技術分野1 本発明は乾燥工程及び混線工程を必要としないアミ7系
樹脂成形材料の製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Technical Field 1] The present invention relates to a method for producing an Ami7-based resin molding material that does not require a drying step or a crosstalk step.

[背景技術1 一般に7ミ7系樹脂成形材料の製造方法は綜合工程、混
練工程、乾燥工程、粉砕着色工程及び粒状化工程とから
成り、従来にあっては、縮合工程により含有水分率が約
30重量%の液状アミ/系樹脂を得、このものをシート
状のバルブに混合含浸させ、乾燥させた後、顔料及び可
塑剤、硬化剤、離型剤等の添加剤を混合分散させ、粉砕
し、次いで粒状化してアミ/系樹脂成形材料を製造して
いたが、液状アミノ系樹脂の含有水分率が高いためバル
ブに混合含浸させた後の乾燥に多大なエネルギーを必要
とし、設備が大きくなり、コストが」ユ昇してしまうも
のであり、しかも乾燥させるので、この段階で製造工程
を一旦中断しなければならなく、連続工程を採用できな
くて自動化、省人化が困難であり、又シート状のパルプ
を混練し、粉砕しなければならなく工数が多くなり生産
性が低いという問題があった。
[Background technology 1] In general, the manufacturing method for 7/7 resin molding materials consists of a synthesis process, a kneading process, a drying process, a pulverization coloring process, and a granulation process. Conventionally, the condensation process reduces the water content to approximately A 30% by weight liquid amyl/based resin is obtained, mixed and impregnated into a sheet-like bulb, dried, and then mixed and dispersed with additives such as pigments, plasticizers, curing agents, and mold release agents, and pulverized. This was then granulated to produce an amino-based resin molding material, but since the liquid amino-based resin has a high moisture content, it requires a lot of energy to dry after mixing and impregnating the valve, and the equipment is large. This increases costs, and since drying is required, the manufacturing process must be temporarily interrupted at this stage, making it difficult to automate and save labor as a continuous process cannot be adopted. In addition, the sheet-like pulp must be kneaded and pulverized, which increases the number of man-hours and reduces productivity.

[発明の目的1 本発明は上記事情に鑑みて為されたものであり、その目
的とするところは、アミ/系樹脂成形材料の製造方法に
おいて、乾燥工程及びパルプの混練工程が不要で工程の
単純化及び合理化を図ることかでト、設備コストを押さ
えることができると共に省スペース、省エネルギー化が
可能で、しかも乾燥工程を必要としないので、連続工程
を採用でき、自動化、省人化が可能で生産性を高めるこ
とにある。
[Objective of the Invention 1 The present invention has been made in view of the above-mentioned circumstances, and its purpose is to eliminate the need for a drying step and a pulp kneading step in a method for producing an amide/based resin molding material, and to reduce the process time. Through simplification and rationalization, it is possible to reduce equipment costs, save space, and save energy.Moreover, since a drying process is not required, a continuous process can be adopted, allowing automation and labor savings. The aim is to increase productivity.

[発明の開示] 本発明の7ミ7系樹脂成形材料の製造方法は、縮合反応
により得られた低含有水分率の液状アミノ系樹脂に粉状
パルプを混合して粉砕着色し、次いで粒状化することを
特徴とし、この構成により上記目的を達成でき−たちの
である。即ち、低含有水分率の液状アミノ系樹脂を採用
することにより、乾燥工程が不要となり、又この液状ア
ミ7系樹脂に粉状パルプを混合させるので、パルプの混
線工程が必要でなく、工程を単純化、合理化できるもの
である。
[Disclosure of the Invention] The method for producing a 7-7 type resin molding material of the present invention involves mixing powdered pulp with a liquid amino resin with a low water content obtained by a condensation reaction, pulverizing and coloring the mixture, and then granulating it. With this configuration, the above object can be achieved. In other words, by using a liquid amino-based resin with a low moisture content, a drying process is not required, and since powdered pulp is mixed with this liquid amino-7 resin, there is no need for a pulp mixing process, and the process can be simplified. It can be simplified and streamlined.

以下、本発明の製造方法を添付の図面に示す一工程図に
基づいて説明する。本発明で用いる低含有水分率、たと
えば3重量%程度の液状アミノ系樹脂は、尿素又はメラ
ミンを原料タンク1から、又ホルムアルデヒドとしてパ
ラホルムアルデヒドを原料タンク2から、そして触媒の
水酸化ナトリウムのようなアルカリを触媒タンク3から
、それぞれ定量フィーダ4.5.6を通して反応8!7
に投入して縮合反応を行って得る。この縮合反応は、た
とえば尿素1モルにたいして1.2〜2.0モルのホル
ムアルデヒドをpH7〜8で、又はメラミン1モルに対
してして2.0〜3.0ホルムアルデヒドをpH8,9
〜9.0で液状(65℃)の反応温度で連続反応させる
。反応8!7は滞留時間の安定化、付着等のない密閉完
全排出型、たとえば二軸セル7クリーニング型を採用す
る。この低含有水分率の液状アミノ系樹脂を冷却機18
に投入し冷却する。この場合必要に応じて添加物タンク
12から硬化剤、離型剤、その他の添加剤を定量フィー
ダ8を介して冷却機18に投入しておいてもよい。この
後冷却した液状アミノ系樹脂を色彩管理計11によりそ
の彩度をチェックした後粉砕磯19に送る。それと共に
パルプタンク9から定量フィーダ10を介して色彩管理
計13によりその彩度をチェックした粉状パルプを粉砕
8!】9に投入して、液状アミノ系樹脂と粉状パルプを
混合すると共に粉砕機19により60メツシユ以下に粉
砕する。パルプとしてはアミノ系樹脂は美しい彩度のあ
る製品であることから通常a−セルローズを主成分とす
る白色の溶解パルプが好ましい。投入量は液状アミ7系
樹脂に対してパルプチップは20〜40重量%程度であ
る。尚、図中想像線で示すように、粉状パルプを粉砕8
!19に投入せずに、直接着色混合機22に投入しても
よい。この粉砕物を補集機20に送り、定量フィーダ2
1を介して一定量を着色混合t9122に投入する。そ
れと共に着色混合8!22に定量フィーダ14を介して
所定量の顔料、その他添加剤を投入し混合着色させる。
Hereinafter, the manufacturing method of the present invention will be explained based on one-step diagrams shown in the accompanying drawings. The liquid amino-based resin with a low moisture content, for example, about 3% by weight, used in the present invention is prepared by using urea or melamine from the raw material tank 1, paraformaldehyde as formaldehyde from the raw material tank 2, and a catalyst such as sodium hydroxide. The alkali is passed from the catalyst tank 3 to the quantitative feeder 4.5.6 for reaction 8!7.
and conduct a condensation reaction. In this condensation reaction, for example, 1 mole of urea is mixed with 1.2 to 2.0 moles of formaldehyde at pH 7 to 8, or 1 mole of melamine is mixed with 2.0 to 3.0 formaldehyde at pH 8,9.
Continuous reaction is carried out at a reaction temperature of ~9.0 and liquid (65°C). For reactions 8 and 7, a closed complete discharge type with stable residence time and no adhesion, such as a twin-screw cell 7 cleaning type, is used. This liquid amino resin with a low moisture content is transferred to a cooling device 18.
and cool it. In this case, a curing agent, a mold release agent, and other additives may be fed into the cooler 18 from the additive tank 12 via the quantitative feeder 8, if necessary. Thereafter, the cooled liquid amino resin is checked for chroma using a color control meter 11 and then sent to a crusher 19. At the same time, the powdered pulp is passed from the pulp tank 9 through the metering feeder 10 and whose color saturation is checked by the color control meter 13, and is crushed 8! 9, the liquid amino resin and the powdered pulp are mixed and crushed into 60 meshes or less by a crusher 19. As for the pulp, white dissolving pulp containing a-cellulose as a main component is generally preferred since amino resins are products with beautiful color saturation. The amount of pulp chips to be added is about 20 to 40% by weight based on the liquid Ami-7 resin. In addition, as shown by the imaginary line in the figure, the powdered pulp is crushed 8
! It is also possible to directly charge the color mixer 22 without charging the color mixer 19. This crushed material is sent to the collection machine 20, and the quantitative feeder 2
1 to the colored mixture t9122. At the same time, a predetermined amount of pigments and other additives are fed into the coloring mixer 8!22 via the quantitative feeder 14 to mix and color.

この場合、顔料の量は粉砕物が粉砕機19から補集fi
20に送る際に色彩管理計15によるチェックを受けて
CCM25(フンピユータカラーマツチング)により制
御している。この後、このようにして得た着色物を色彩
管理計23によりチェックし、顔料供給量をフィードバ
ックできるようにしている。この場合所望通りのものが
得られない場合にはCCMにより補正を行う。この後着
色物を製品化用混練磯24に投入して混練し、粉砕し、
打錠機26により粒状化し、次いで混合磯により混合し
てアミ7系成形材料を得る。このアミノ系成形材料を分
光光度計によりその色彩をチェックし所望通りであれば
製品とする。所望通りのものが得られない場合にはCC
M28により補正を行う。
In this case, the amount of pigment is determined by the amount of the pulverized material collected from the pulverizer 19.
20, it is checked by a color controller 15 and controlled by CCM 25 (Funputer Color Matching). Thereafter, the colored product thus obtained is checked by a color control meter 23, so that the amount of pigment supplied can be fed back. In this case, if the desired result cannot be obtained, correction is performed using CCM. After this, the colored material is put into the kneading rock for commercialization 24, kneaded, and pulverized.
The mixture is granulated using a tablet press 26, and then mixed using a mixing iron to obtain an Ami7-based molding material. The color of this amino-based molding material is checked using a spectrophotometer, and if the color is as desired, it is used as a product. CC if you can't get what you want
Correction is performed using M28.

]発明の効果1 本発明にあっては、縮合反応により得られた低含有水分
率の液状アミノ系樹脂に粉状パルプを混合して粉砕着色
し、次いで粒状化するので、乾燥工程及びパルプの混線
工程が不要で工程の単純化及び合理化を図ることができ
、設備コストを押さえることができると共に省スペース
、省エネルギー化が可能で、しかも乾燥工程を必要とし
ないので、連続工程を採用でき、自動化、省人化が可能
で生産性を高めることができるものである。
] Effect of the invention 1 In the present invention, powdered pulp is mixed with a liquid amino resin with a low moisture content obtained by a condensation reaction, pulverized and colored, and then granulated, so there is no drying process and pulp The process can be simplified and rationalized by eliminating the need for cross-wire processes, reducing equipment costs, saving space and energy, and not requiring a drying process, allowing for continuous processes and automation. , it is possible to save labor and increase productivity.

【図面の簡単な説明】[Brief explanation of drawings]

添付図は本発明の一実施例の工程を装置と共に示す説明
図であって、1.2は原料タンク、3は触媒タンク、7
は反応磯、8は混練浸透機、9はパルプタンク、19は
粉砕機、22は着色混合機である。
The attached drawing is an explanatory diagram showing the process of an embodiment of the present invention together with equipment, in which 1.2 is a raw material tank, 3 is a catalyst tank, and 7
8 is a kneading infiltration machine, 9 is a pulp tank, 19 is a crusher, and 22 is a coloring mixer.

Claims (1)

【特許請求の範囲】[Claims] (1)縮合反応により得られた低含有水分率の液状アミ
ン系樹脂に粉状バルブを混合して粉砕着色し、次いで粒
状化することを特徴とするアミ/系樹脂成形材料の製造
方法。
(1) A method for producing an amine/based resin molding material, which comprises mixing a powdered bulb into a liquid amine-based resin with a low moisture content obtained by a condensation reaction, pulverizing and coloring it, and then granulating it.
JP11928484A 1984-06-11 1984-06-11 Production of amino resin molding material Pending JPS60262849A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11928484A JPS60262849A (en) 1984-06-11 1984-06-11 Production of amino resin molding material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11928484A JPS60262849A (en) 1984-06-11 1984-06-11 Production of amino resin molding material

Publications (1)

Publication Number Publication Date
JPS60262849A true JPS60262849A (en) 1985-12-26

Family

ID=14757578

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11928484A Pending JPS60262849A (en) 1984-06-11 1984-06-11 Production of amino resin molding material

Country Status (1)

Country Link
JP (1) JPS60262849A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102101895A (en) * 2009-12-22 2011-06-22 日东电工株式会社 Resin production apparatus and resin production method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102101895A (en) * 2009-12-22 2011-06-22 日东电工株式会社 Resin production apparatus and resin production method
EP2338590A1 (en) * 2009-12-22 2011-06-29 Nitto Denko Corporation Resin production apparatus and resin production method
US8771602B2 (en) 2009-12-22 2014-07-08 Nitto Denko Corporation Resin production apparatus and resin production method

Similar Documents

Publication Publication Date Title
CN102351588B (en) Production method of novel chemically synthesized ammoniated sulfur-base composite fertilizer
CN102018150B (en) Processing technique of sheep feed
CN102249777B (en) Production method for ammoniated sulfur-based compound fertilizer by chemical synthesis
CN100354235C (en) Spray pelleting process of compound fertilizer
CN101648838A (en) Method for producing granular ammonium sulfate by using crystalline ammonium sulfate or powdery ammonium sulfate
JPS60262849A (en) Production of amino resin molding material
CN211358820U (en) Reation kettle of chemical fertilizer anti-caking agent production usefulness
CN103641969A (en) Method of preparing high-viscosity urea formaldehyde slow release fertilizer emulsion by use of two-step method
JPS60262848A (en) Production of amino resin molding material
CN103230582A (en) Preparation method of duramycin premix
CN105132052A (en) Biomass water-coal-slurry and preparation method thereof
CN107053517B (en) A kind of compound amino film plastics grain granulation Processes and apparatus
CN206748796U (en) A kind of new color masterbatch mixing equipment
CN208449248U (en) Dry granulating machine mixing feeding system
CN210171370U (en) Premixing device of trace feed additive
CN206872692U (en) The production equipment of steam-pressing brisk
CN207202004U (en) A kind of production system for preparing the uniform pig feed of each component
CN204727816U (en) Mixing equipment is pulverized before a kind of modified starch production retort
CN204746433U (en) A high -speed pulverizer for modified starch production
CN214288039U (en) Auxiliary material machine for mixing granulation
CN112237885A (en) Prilling granulator is used in fertilizer production
CN206843336U (en) A kind of ammonium sulfate high-tower granulation sulfur-bearing compound fertilizer system
CN203904236U (en) Automatic coating and caking preventing device for compound fertilizer
JPS6135907A (en) Manufacture of resin molding material
CN112619548A (en) Auxiliary material machine for mixing granulation