JPH02298367A - Grinding adjuvant - Google Patents
Grinding adjuvantInfo
- Publication number
- JPH02298367A JPH02298367A JP11862789A JP11862789A JPH02298367A JP H02298367 A JPH02298367 A JP H02298367A JP 11862789 A JP11862789 A JP 11862789A JP 11862789 A JP11862789 A JP 11862789A JP H02298367 A JPH02298367 A JP H02298367A
- Authority
- JP
- Japan
- Prior art keywords
- grinding
- adjuvant
- residual liquid
- ammonia
- ethylene oxide
- 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
Links
- 239000002671 adjuvant Substances 0.000 title abstract 6
- HZAXFHJVJLSVMW-UHFFFAOYSA-N 2-Aminoethan-1-ol Chemical compound NCCO HZAXFHJVJLSVMW-UHFFFAOYSA-N 0.000 claims abstract description 10
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims abstract description 8
- 239000007788 liquid Substances 0.000 claims abstract description 7
- GSEJCLTVZPLZKY-UHFFFAOYSA-N Triethanolamine Chemical compound OCCN(CCO)CCO GSEJCLTVZPLZKY-UHFFFAOYSA-N 0.000 claims abstract description 6
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 claims abstract description 4
- 229910021529 ammonia Inorganic materials 0.000 claims abstract description 4
- ZBCBWPMODOFKDW-UHFFFAOYSA-N diethanolamine Chemical compound OCCNCCO ZBCBWPMODOFKDW-UHFFFAOYSA-N 0.000 claims abstract 2
- 229910052500 inorganic mineral Inorganic materials 0.000 abstract description 10
- 239000011707 mineral Substances 0.000 abstract description 10
- 230000000694 effects Effects 0.000 abstract description 8
- 238000000034 method Methods 0.000 abstract description 6
- 239000011398 Portland cement Substances 0.000 abstract description 4
- 239000002893 slag Substances 0.000 abstract description 4
- 239000004568 cement Substances 0.000 abstract description 3
- 239000010440 gypsum Substances 0.000 abstract description 3
- 229910052602 gypsum Inorganic materials 0.000 abstract description 3
- 235000019738 Limestone Nutrition 0.000 abstract description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 abstract description 2
- 239000010881 fly ash Substances 0.000 abstract description 2
- 239000006028 limestone Substances 0.000 abstract description 2
- 239000002699 waste material Substances 0.000 abstract description 2
- 230000002708 enhancing effect Effects 0.000 abstract 1
- 150000002169 ethanolamines Chemical class 0.000 abstract 1
- 230000016615 flocculation Effects 0.000 abstract 1
- 238000005189 flocculation Methods 0.000 abstract 1
- 239000000843 powder Substances 0.000 description 11
- 239000000463 material Substances 0.000 description 8
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 6
- 238000005054 agglomeration Methods 0.000 description 5
- 230000002776 aggregation Effects 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- -1 dimethylethylvirol Chemical compound 0.000 description 4
- 238000010298 pulverizing process Methods 0.000 description 4
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- SJRJJKPEHAURKC-UHFFFAOYSA-N N-Methylmorpholine Chemical compound CN1CCOCC1 SJRJJKPEHAURKC-UHFFFAOYSA-N 0.000 description 3
- RWRDLPDLKQPQOW-UHFFFAOYSA-N Pyrrolidine Chemical compound C1CCNC1 RWRDLPDLKQPQOW-UHFFFAOYSA-N 0.000 description 3
- HPYNZHMRTTWQTB-UHFFFAOYSA-N 2,3-dimethylpyridine Chemical compound CC1=CC=CN=C1C HPYNZHMRTTWQTB-UHFFFAOYSA-N 0.000 description 2
- PAYRUJLWNCNPSJ-UHFFFAOYSA-N Aniline Chemical compound NC1=CC=CC=C1 PAYRUJLWNCNPSJ-UHFFFAOYSA-N 0.000 description 2
- YNAVUWVOSKDBBP-UHFFFAOYSA-N Morpholine Chemical compound C1COCCN1 YNAVUWVOSKDBBP-UHFFFAOYSA-N 0.000 description 2
- GLUUGHFHXGJENI-UHFFFAOYSA-N Piperazine Chemical compound C1CNCCN1 GLUUGHFHXGJENI-UHFFFAOYSA-N 0.000 description 2
- NQRYJNQNLNOLGT-UHFFFAOYSA-N Piperidine Chemical compound C1CCNCC1 NQRYJNQNLNOLGT-UHFFFAOYSA-N 0.000 description 2
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 description 2
- KAESVJOAVNADME-UHFFFAOYSA-N Pyrrole Chemical compound C=1C=CNC=1 KAESVJOAVNADME-UHFFFAOYSA-N 0.000 description 2
- RZXMPPFPUUCRFN-UHFFFAOYSA-N p-toluidine Chemical compound CC1=CC=C(N)C=C1 RZXMPPFPUUCRFN-UHFFFAOYSA-N 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- WZCQRUWWHSTZEM-UHFFFAOYSA-N 1,3-phenylenediamine Chemical compound NC1=CC=CC(N)=C1 WZCQRUWWHSTZEM-UHFFFAOYSA-N 0.000 description 1
- RSEBUVRVKCANEP-UHFFFAOYSA-N 2-pyrroline Chemical compound C1CC=CN1 RSEBUVRVKCANEP-UHFFFAOYSA-N 0.000 description 1
- 229920001732 Lignosulfonate Polymers 0.000 description 1
- JLTDJTHDQAWBAV-UHFFFAOYSA-N N,N-dimethylaniline Chemical compound CN(C)C1=CC=CC=C1 JLTDJTHDQAWBAV-UHFFFAOYSA-N 0.000 description 1
- AFBPFSWMIHJQDM-UHFFFAOYSA-N N-methyl-N-phenylamine Natural products CNC1=CC=CC=C1 AFBPFSWMIHJQDM-UHFFFAOYSA-N 0.000 description 1
- CKRZKMFTZCFYGB-UHFFFAOYSA-N N-phenylhydroxylamine Chemical compound ONC1=CC=CC=C1 CKRZKMFTZCFYGB-UHFFFAOYSA-N 0.000 description 1
- BHHGXPLMPWCGHP-UHFFFAOYSA-N Phenethylamine Chemical compound NCCC1=CC=CC=C1 BHHGXPLMPWCGHP-UHFFFAOYSA-N 0.000 description 1
- CZPWVGJYEJSRLH-UHFFFAOYSA-N Pyrimidine Chemical compound C1=CN=CN=C1 CZPWVGJYEJSRLH-UHFFFAOYSA-N 0.000 description 1
- 239000004480 active ingredient Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 150000001875 compounds Chemical group 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 229940018564 m-phenylenediamine Drugs 0.000 description 1
- 229910052573 porcelain Inorganic materials 0.000 description 1
- 239000011802 pulverized particle Substances 0.000 description 1
- PBMFSQRYOILNGV-UHFFFAOYSA-N pyridazine Chemical compound C1=CC=NN=C1 PBMFSQRYOILNGV-UHFFFAOYSA-N 0.000 description 1
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 description 1
- ZVJHJDDKYZXRJI-UHFFFAOYSA-N pyrroline Natural products C1CC=NC1 ZVJHJDDKYZXRJI-UHFFFAOYSA-N 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- GHMLBKRAJCXXBS-UHFFFAOYSA-N resorcinol Chemical compound OC1=CC=CC(O)=C1 GHMLBKRAJCXXBS-UHFFFAOYSA-N 0.000 description 1
- 229960001755 resorcinol Drugs 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 150000004684 trihydrates Chemical class 0.000 description 1
- ODHXBMXNKOYIBV-UHFFFAOYSA-N triphenylamine Chemical compound C1=CC=CC=C1N(C=1C=CC=CC=1)C1=CC=CC=C1 ODHXBMXNKOYIBV-UHFFFAOYSA-N 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B7/00—Hydraulic cements
- C04B7/36—Manufacture of hydraulic cements in general
- C04B7/48—Clinker treatment
- C04B7/52—Grinding ; After-treatment of ground cement
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明はポルトランドセメント、高炉スラグ、アルミナ
セメント、フライアッシュ、石灰石、石膏などの水硬性
鉱物の粉砕工程において粉砕効率を向上させ、更に、粉
砕された粉末の輸送、保管にあたり凝集することを防ぐ
ための粉砕助剤に関する。[Detailed Description of the Invention] [Field of Industrial Application] The present invention improves the pulverization efficiency in the pulverization process of hydraulic minerals such as Portland cement, blast furnace slag, alumina cement, fly ash, limestone, and gypsum. This invention relates to a grinding aid for preventing agglomeration during transportation and storage of powder.
従来、鉱物質、特にポルトランドセメントクリンカ−1
高炉スラグ等の粉砕に際しては、粉砕効率を上げるため
、ジエチレングリコールやトリエタノールアミンなどの
粉砕助剤が用いられている。Traditionally, mineral materials, especially Portland cement clinker-1
When grinding blast furnace slag and the like, grinding aids such as diethylene glycol and triethanolamine are used to increase grinding efficiency.
粉砕工程においては鉱物質をできるだけ能率良く、比較
的早い速度で所望の粒径にすることが望ましい。In the grinding process, it is desirable to reduce the mineral material to the desired particle size as efficiently as possible and at a relatively fast rate.
一般に、鉱物質を粉砕すると、鉱物質粒子の臂解が生じ
、新鮮な活性のある表面が露出する。この表面は恐らく
イオン結合の破断によって高いエネルギーをもっている
ものと思われる。粉砕された粒子の表面の力は粉砕後あ
る時間保持され、それが減少、消滅しない場合には粉体
には緊密化あるいはバンクセントが起こり、流動性が悪
くなることがある。Generally, crushing mineral material causes the mineral particles to disintegrate, exposing fresh active surfaces. This surface probably has high energy due to the breaking of ionic bonds. The surface force of the pulverized particles is maintained for a certain period of time after pulverization, and if it is not reduced or eliminated, the powder may become compacted or bank cent, resulting in poor flowability.
パックセットとは、例えば粉末を袋詰めして貯蔵または
移送する場合、粉末粒子がその表面力によりアグロメレ
ーションを起こして相互に付着する「粉末の塊状化−」
を意味する。本発明においては、塊状化した粉末粒子が
再流動を開始するし易さを「バッジセット指数jと称す
る相対的な値で示している。例えば、鉱物質粉末を直接
ホソバ−車に積載したような場合には、その粉末粒子は
しばしば固い塊状になる。この塊状化した粉末はこの状
態を破壊するかなり大きい機械的衝撃を加えない限り、
粒子状態となって流動しない。A pack set is a "powder agglomeration" in which, for example, when powder is stored or transported in bags, the powder particles cause agglomeration and stick to each other due to their surface forces.
means. In the present invention, the ease with which agglomerated powder particles start reflowing is indicated by a relative value called the badge set index j. In such cases, the powder particles often form a solid agglomerate, and this agglomerated powder will not survive unless subjected to a significant mechanical shock that disrupts this state.
It becomes particulate and does not flow.
近時、ポルトランドセメントクリンカ−や高炉スラグの
粉砕においては各種の粉砕助剤が積極的に使用されてい
る。そして従来、例えばセメント製造時の粉砕助剤とし
ては、トリエタノールアミン、ジエチレングリコール、
アニリン、p−トルイジン、m−フェニレンジアミン、
ジメチルアニリン、ジフェニルアニリン、2,4.6−
ドリブロモアニリン、N−フェニルヒドロキシアミン、
β−フェネチルアミン、モルホリン、ピリジン、ピペリ
ジン、ピロール、ピロリジン、ピロリン、ピリダジン、
ピリミジン、N−メチルモルホリン、ジメチルピリジン
、ジメチルエチルビロール、ピペラジン、ピンゾルレジ
ン、レゾルシン、リグニンスルホン酸塩、オキシカルボ
ン酸塩などが知られている。Recently, various grinding aids have been actively used in the grinding of Portland cement clinker and blast furnace slag. Traditionally, triethanolamine, diethylene glycol,
Aniline, p-toluidine, m-phenylenediamine,
Dimethylaniline, diphenylaniline, 2,4.6-
Dolibromoaniline, N-phenylhydroxyamine,
β-phenethylamine, morpholine, pyridine, piperidine, pyrrole, pyrrolidine, pyrroline, pyridazine,
Known examples include pyrimidine, N-methylmorpholine, dimethylpyridine, dimethylethylvirol, piperazine, pinzole resin, resorcin, lignin sulfonate, and oxycarboxylate.
〔発明が解決しようとする課題〕
しかしながら、従来研究され、使用されている粉砕助剤
は粉砕効率の向上にも限度があり、粉砕効果を高めるた
めにその粉砕助剤の使用量を多量にすると、粉砕コスト
の上昇を招くという問題があった。そこで、より入手し
やすく、少量で顕著な効果を有する粉砕助剤が求められ
ていた。[Problem to be solved by the invention] However, the grinding aids that have been researched and used in the past have limitations in improving the grinding efficiency, and if the amount of grinding aids used is increased to improve the grinding effect, However, there was a problem in that the grinding cost increased. Therefore, there has been a need for a grinding aid that is more easily available and has significant effects in small amounts.
本発明者らは上述の課題を解決すべく研究を重ね、酸化
エチレンとアンモニアを反応させてモノエタノールアミ
ン、ジェタノールアミン及びトリエタノールアミンを合
成し、生成したこれら3種のエタノールアミンの60重
量%以上を留去させた後の残液中の成分、特に比較的分
子量の大きいエタノールアミン系物質が、鉱物質の粉砕
助剤として有効であることを見出し本発明を完成するに
至った。The present inventors have conducted repeated research to solve the above-mentioned problems, and synthesized monoethanolamine, jetanolamine, and triethanolamine by reacting ethylene oxide and ammonia. The present inventors have discovered that components in the residual liquid after distilling off more than % of the mineral content, particularly ethanolamine-based substances with relatively large molecular weights, are effective as grinding aids for mineral materials, and have completed the present invention.
本発明の粉砕助剤は、鉱物質の粉砕前或いは粉砕時に被
粉砕物に対して滴下或いはスプレーにより添加する。ま
た被粉砕物に対して0.002〜0.1重量%添加する
が、好ましくは0.005〜0.05重量%添加する。The grinding aid of the present invention is added dropwise or by spraying to the material to be ground before or during the grinding of the mineral material. Further, it is added in an amount of 0.002 to 0.1% by weight, preferably 0.005 to 0.05% by weight, based on the material to be crushed.
本発明粉砕助剤の有効成分はモノエタノールアミン、ジ
ェタノールアミン及びトリエタノールアミン留去後の残
液であるため、未だ化合物基を特定することができない
。しかしながら、従来の粉砕助剤に比して分子量が大き
いアミン系の化合物やその縮合体の複合物であると考え
られる。しかも、粉体の凝集防止効果が高く、被粉砕物
に対する添加量が少量でありながら充分なパックセット
指数が得られ、経済性の点でも優れている。Since the active ingredients of the grinding aid of the present invention are the residual liquid after distilling off monoethanolamine, jetanolamine, and triethanolamine, the compound group cannot yet be identified. However, it is thought that it is a composite of an amine compound or a condensate thereof, which has a larger molecular weight than conventional grinding aids. Moreover, it has a high effect of preventing agglomeration of powder, and even though the amount added to the material to be crushed is small, a sufficient pack set index can be obtained, and it is also excellent in economical efficiency.
脂1
容量6.81の磁製ボールミルに粗砕されたtill!
ボルトランドセメントタリンカー2.5kg、三水石膏
75gを入れ、粉砕助剤として第1表に示した各種の粉
砕助剤を第1表記載の添加率で添加し、6時間粉砕処理
を行った。得られた試料を各々「試料1」〜F試料3」
とした。Fat 1 Till crushed in a porcelain ball mill with a capacity of 6.81!
2.5 kg of Boltland Cement Talinker and 75 g of gypsum trihydrate were added, and the various grinding aids shown in Table 1 were added at the addition rates shown in Table 1, and the grinding process was carried out for 6 hours. . The obtained samples were divided into "Sample 1" to "F Sample 3" respectively.
And so.
ル較拠へ二旦
粉砕助剤として従来のエチレングリコール及び水を使用
した以外は、上記実施例と同様に粉砕実験を行った。得
られた試料を「試料A」及び「試料B」とした。Grinding experiments were conducted in the same manner as in the above examples, except that conventional ethylene glycol and water were used as grinding aids. The obtained samples were designated as "Sample A" and "Sample B."
上記の実施例及び比較例で得られた試料について、粉末
度試験、フロー試験及び圧縮強度試験をJ I S −
R5201の規定に準拠して行った。更に、パックセン
ト指数を測定し、これらの結果を第1表に併記した。The samples obtained in the above Examples and Comparative Examples were subjected to a fineness test, a flow test, and a compressive strength test according to JIS-
It was carried out in accordance with the regulations of R5201. Furthermore, the pack cent index was measured and these results are also listed in Table 1.
なお、バックセット指数は下記の方法で測定した。In addition, the backset index was measured by the following method.
粉末試料100gを可変振動機上に取りつけた三角フラ
スコ(容量250rnff)中に入れ、これを15秒間
振動させた後、その三角フラスコを振動機から取外し、
静かに傾けてその中心(開口の中心軸)を水平にして治
具に装着した。次いでその状態で(中心を水平に保った
まま)フラスコをその中心を軸にして100回転/分の
割合で180度の角度で回転させ、内部の試料を崩れさ
せるに要する180度回転の回数がバックセット指数で
ある。したがって、パックセット指数の値が小さい方が
凝集の少ない扱い易い粉末である。100 g of the powder sample was placed in an Erlenmeyer flask (capacity 250 rnff) mounted on a variable vibrator, and after vibrating it for 15 seconds, the Erlenmeyer flask was removed from the vibrator.
It was gently tilted so that its center (the central axis of the opening) was horizontal and then mounted on the jig. Then, in this state (while keeping the center horizontal), rotate the flask at an angle of 180 degrees around its center at a rate of 100 revolutions per minute, and calculate the number of 180 degree rotations required to collapse the sample inside. It is a backset index. Therefore, the smaller the value of the pack set index is, the easier the powder is to handle with less agglomeration.
第1表に記載された各試料についての試験結果から、本
発明による粉砕助剤は少量でより優れた性能を発現する
ことが認められた。From the test results for each sample listed in Table 1, it was found that the grinding aid according to the present invention exhibits better performance in small amounts.
本発明によれば、少ない添加率で充分な粉砕効果が得ら
れ、パンクセット指数も良好であり、残液は従来廃棄物
に近い安価なものであるので、資源の有効利用に役立つ
きわめて有用な発明である。According to the present invention, sufficient pulverization effect can be obtained with a small addition rate, the puncture set index is also good, and the residual liquid is a low-cost substance that is close to conventional waste, so it is extremely useful for effective use of resources. It is an invention.
(以下余白)(Margin below)
Claims (1)
アミン、ジエタノールアミン及びトリエタノールアミン
を合成し、生成した3種のエタノールアミンの60重量
%以上を留去させた残液からなる粉砕助剤。A grinding aid consisting of a residual liquid obtained by reacting ethylene oxide and ammonia to synthesize monoethanolamine, diethanolamine, and triethanolamine, and distilling off 60% by weight or more of the three types of ethanolamine produced.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11862789A JPH02298367A (en) | 1989-05-15 | 1989-05-15 | Grinding adjuvant |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11862789A JPH02298367A (en) | 1989-05-15 | 1989-05-15 | Grinding adjuvant |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH02298367A true JPH02298367A (en) | 1990-12-10 |
Family
ID=14741215
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11862789A Pending JPH02298367A (en) | 1989-05-15 | 1989-05-15 | Grinding adjuvant |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02298367A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003509191A (en) * | 1999-09-13 | 2003-03-11 | ダブリュ・アール・グレイス・アンド・カンパニー・コネテイカット | Method for improving cement clinker milling in mills using rollers |
JP2004002165A (en) * | 2002-03-28 | 2004-01-08 | Kansai Electric Power Co Inc:The | Cement admixture and its production method |
JP4796770B2 (en) * | 2002-10-09 | 2011-10-19 | ダブリュー・アール・グレイス・アンド・カンパニー−コネチカット | Amine-containing cement processing additive |
KR20190094758A (en) * | 2018-02-06 | 2019-08-14 | 롯데케미칼 주식회사 | Additive composition for cement |
-
1989
- 1989-05-15 JP JP11862789A patent/JPH02298367A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003509191A (en) * | 1999-09-13 | 2003-03-11 | ダブリュ・アール・グレイス・アンド・カンパニー・コネテイカット | Method for improving cement clinker milling in mills using rollers |
JP2004002165A (en) * | 2002-03-28 | 2004-01-08 | Kansai Electric Power Co Inc:The | Cement admixture and its production method |
JP4796770B2 (en) * | 2002-10-09 | 2011-10-19 | ダブリュー・アール・グレイス・アンド・カンパニー−コネチカット | Amine-containing cement processing additive |
KR20190094758A (en) * | 2018-02-06 | 2019-08-14 | 롯데케미칼 주식회사 | Additive composition for cement |
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