JPH02298366A - Grinding adjuvant of mineral substance - Google Patents
Grinding adjuvant of mineral substanceInfo
- Publication number
- JPH02298366A JPH02298366A JP11862689A JP11862689A JPH02298366A JP H02298366 A JPH02298366 A JP H02298366A JP 11862689 A JP11862689 A JP 11862689A JP 11862689 A JP11862689 A JP 11862689A JP H02298366 A JPH02298366 A JP H02298366A
- Authority
- JP
- Japan
- Prior art keywords
- grinding
- glycol
- aqueous liquid
- ethylene
- adjuvant
- 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
- 238000000227 grinding Methods 0.000 title claims abstract description 37
- 229910052500 inorganic mineral Inorganic materials 0.000 title claims abstract description 15
- 239000011707 mineral Substances 0.000 title claims abstract description 15
- 239000000126 substance Substances 0.000 title abstract description 3
- 239000002671 adjuvant Substances 0.000 title abstract 4
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims abstract description 27
- 239000007788 liquid Substances 0.000 claims abstract description 16
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 claims abstract description 10
- UWHCKJMYHZGTIT-UHFFFAOYSA-N tetraethylene glycol Chemical compound OCCOCCOCCOCCO UWHCKJMYHZGTIT-UHFFFAOYSA-N 0.000 claims abstract description 9
- JLFNLZLINWHATN-UHFFFAOYSA-N pentaethylene glycol Chemical compound OCCOCCOCCOCCOCCO JLFNLZLINWHATN-UHFFFAOYSA-N 0.000 claims abstract description 8
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 claims description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- ZIBGPFATKBEMQZ-UHFFFAOYSA-N triethylene glycol Chemical compound OCCOCCOCCO ZIBGPFATKBEMQZ-UHFFFAOYSA-N 0.000 claims description 4
- BEVWMRQFVUOPJT-UHFFFAOYSA-N 2,4-dimethyl-1,3-thiazole-5-carboxamide Chemical compound CC1=NC(C)=C(C(N)=O)S1 BEVWMRQFVUOPJT-UHFFFAOYSA-N 0.000 claims description 2
- IIRDTKBZINWQAW-UHFFFAOYSA-N hexaethylene glycol Chemical compound OCCOCCOCCOCCOCCOCCO IIRDTKBZINWQAW-UHFFFAOYSA-N 0.000 claims description 2
- 238000000034 method Methods 0.000 abstract description 13
- 230000000694 effects Effects 0.000 abstract description 8
- 229920001223 polyethylene glycol Polymers 0.000 abstract description 7
- 239000011398 Portland cement Substances 0.000 abstract description 5
- 239000002893 slag Substances 0.000 abstract description 4
- 230000015572 biosynthetic process Effects 0.000 abstract description 2
- 238000003786 synthesis reaction Methods 0.000 abstract description 2
- 239000000843 powder Substances 0.000 description 11
- 239000000463 material Substances 0.000 description 8
- 239000002245 particle Substances 0.000 description 6
- 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
- 230000002776 aggregation Effects 0.000 description 3
- 238000010298 pulverizing process Methods 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
- GSEJCLTVZPLZKY-UHFFFAOYSA-N Triethanolamine Chemical compound OCCN(CCO)CCO GSEJCLTVZPLZKY-UHFFFAOYSA-N 0.000 description 2
- 238000005054 agglomeration Methods 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 239000010440 gypsum Substances 0.000 description 2
- 229910052602 gypsum Inorganic materials 0.000 description 2
- RZXMPPFPUUCRFN-UHFFFAOYSA-N p-toluidine Chemical compound CC1=CC=C(N)C=C1 RZXMPPFPUUCRFN-UHFFFAOYSA-N 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- -1 virol Chemical compound 0.000 description 2
- WZCQRUWWHSTZEM-UHFFFAOYSA-N 1,3-phenylenediamine Chemical compound NC1=CC=CC(N)=C1 WZCQRUWWHSTZEM-UHFFFAOYSA-N 0.000 description 1
- XADHLFVRTDESMR-UHFFFAOYSA-N 2-ethyl-3,4-dimethyl-1h-pyrrole Chemical compound CCC=1NC=C(C)C=1C XADHLFVRTDESMR-UHFFFAOYSA-N 0.000 description 1
- 229920001732 Lignosulfonate Polymers 0.000 description 1
- 235000019738 Limestone Nutrition 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
- 238000004220 aggregation Methods 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 239000010881 fly ash Substances 0.000 description 1
- 239000006028 limestone Substances 0.000 description 1
- 229940018564 m-phenylenediamine Drugs 0.000 description 1
- 229910052573 porcelain Inorganic materials 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
- 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
- 150000003839 salts Chemical class 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 150000008054 sulfonate salts Chemical class 0.000 description 1
- 230000002194 synthesizing effect Effects 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
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
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Disintegrating Or Milling (AREA)
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、保管にあたり再凝集することを防
ぐための鉱物質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 mineral substances to prevent reagglomeration during transportation and storage of powdered minerals.
従来、鉱物質、特にポルトランドセメントクリンカ−5
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。Conventionally, mineral materials, especially Portland cement clinker-5
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、!物質を粉砕すると、W、物質粒子の檗解が生
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(なることがある。in general,! Grinding the material causes disintegration of the W material particles and exposes fresh active surfaces. This surface probably has high energy due to the breaking of ionic bonds. The surface force of the crushed particles is maintained for a certain period of time after crushing, and if this force is not reduced or eliminated, the powder may become compacted or bank cent, resulting in poor flowability.
パンクセントとは、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「バックセット指数」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
ッパー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。Punccent refers to "powder agglomeration" in which, for example, when powder is stored or transported in bags, powder particles agglomerate and adhere to each other due to their surface forces. In the present invention, the ease with which agglomerated powder particles begin to reflow is expressed as a relative value called "backset index." For example, when mineral powder is loaded directly into a hopper car, the powder particles often become solid clumps. This agglomerated powder becomes particulate and does not flow unless a significant mechanical impact is applied to break this state.
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−
)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、ビロール、ピロリジン、ビロリン、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、ジメチルエチルピロール、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-
) Ribromoaniline, N-phenylhydroxyamine, β-phenethylamine, morpholine, pyridine, piperidine, virol, pyrrolidine, viroline, pyridazine, pyrimidine, N-methylmorpholine, dimethylpyridine, dimethylethylpyrrole, piperazine, pinzole resin, resorcin, lignin Sulfonate salts, oxycarboxylate salts, etc. are known.
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。However, the grinding aids that have been researched and used in the past have limitations in improving grinding efficiency, and if a large amount of grinding aids are used in order to improve the grinding effect, the problem is that grinding costs will increase. was there. 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、主要
成分としてテトラエチレングリコール、ペンタエチレン
グリコール、ヘキサエチレングリコール及びヘプタエチ
レングリコールの少なくとも1種を主成分とするエチレ
ングリコールの高縮合体を含有する水性液が鉱物質の粉
砕助剤として有効であり、しかもこの水性液は、いわゆ
る、酸化エチレン法により酸化エチレンと水からエチレ
ングリコール類を合成した後、該合成物を留去した残液
に含有され、これが優れた粉砕助剤として使用され得る
ことを見出し、本発明を完成するに至ったものである。The present inventors have conducted extensive research to solve the above-mentioned problems, and have developed a high condensate of ethylene glycol containing at least one of tetraethylene glycol, pentaethylene glycol, hexaethylene glycol, and heptaethylene glycol as a main component. The aqueous liquid it contains is effective as a grinding aid for mineral materials, and this aqueous liquid is the residual liquid obtained by distilling off the synthesized product after synthesizing ethylene glycols from ethylene oxide and water using the so-called ethylene oxide method. It has been discovered that this can be used as an excellent grinding aid, leading to the completion of the present invention.
本発明の鉱物質粉砕助剤は、一つの態様ではテトラエチ
レングリコールやペンタエチレングリコールの高縮合体
を水性液に調製したものである。In one embodiment, the mineral grinding aid of the present invention is an aqueous liquid prepared from a high condensate of tetraethylene glycol or pentaethylene glycol.
すなわち、テトラエチレングリコールやペンタエチレン
グリコールをそのまま或いは水で約2倍〜30倍程度に
希釈した水性液として使用される。That is, tetraethylene glycol or pentaethylene glycol is used as it is or as an aqueous liquid diluted with water to about 2 to 30 times.
本発明の鉱物質粉砕助剤の他の態様は、酸化エチレン法
によって酸化エチレンと水からエチレングリコール類を
合成する際、その合成後に該合成物を留去した残液を用
いる。本発明者らの研究によればその残液例の分析値の
1例は第1表の通りである。In another embodiment of the mineral grinding aid of the present invention, when ethylene glycols are synthesized from ethylene oxide and water by the ethylene oxide method, the residual liquid obtained by distilling off the synthesized product after the synthesis is used. According to the research conducted by the present inventors, an example of the analytical values of the residual liquid is shown in Table 1.
(以下余白) 第1表 (註)※1:浮秤り法による。(Margin below) Table 1 (Note) *1: Based on the floating scale method.
※2:B型粘度針による。*2: Based on B type viscosity needle.
第1表に示された結果から分かるように、抽出残液の主
成分はテトラエチレングリコール及びペンタエチレング
リコール(計−85重量%)である。As can be seen from the results shown in Table 1, the main components of the extraction residue were tetraethylene glycol and pentaethylene glycol (-85% by weight in total).
すなわち、酸化エチレン法では、酸化エチレンと水との
反応によりエチレングリコール、ジエチレングリコール
、トリエチレングリコール等を生成する外、テトラエチ
レングリコールやペンタエチレングリコールを副生ずる
ので、酸化エチレン法の主要な目的物であるエチレング
リコールやジエチレングリコール、トリエチレングリコ
ール等を蒸留により留去した後の残液には副生したテト
ラエチレングリコールやペンタエチレングリコールが大
量に残存しているのである。したがって、この酸化エチ
レン法における残液を使用する方法は産業上及び経済上
好ましい。In other words, in the ethylene oxide method, in addition to producing ethylene glycol, diethylene glycol, triethylene glycol, etc. through the reaction of ethylene oxide and water, tetraethylene glycol and pentaethylene glycol are also produced as by-products. After certain ethylene glycol, diethylene glycol, triethylene glycol, etc. are distilled off, a large amount of by-product tetraethylene glycol and pentaethylene glycol remain in the residual liquid. Therefore, the method of using the residual liquid in this ethylene oxide method is industrially and economically preferable.
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.
本発明の粉砕助剤は従来の粉砕助剤に比して分子量が大
きく、粉体の凝集防止に対し効果的であり、少量の添加
で充分な効果が得られる。The grinding aid of the present invention has a larger molecular weight than conventional grinding aids and is effective in preventing aggregation of powder, and a sufficient effect can be obtained by adding a small amount.
夫施開土ニュ
容量6.81の磁製ボールミルに粗砕された9通ポルト
ランドセメントクリンカ−2,5kg、二本石膏75g
を入れ、粉砕助剤として第2表に示した各種の粉砕助剤
を第2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l」〜「試料3」とした
。9 pieces of Portland cement clinker - 2.5 kg, 2 pieces of gypsum 75 g - crushed in a porcelain ball mill with a capacity of 6.81 kg
The various grinding aids shown in Table 2 were added as grinding aids at the addition rates shown in Table 2, and the grinding process was carried out for 6 hours. The obtained samples were designated as "Sample 1" to "Sample 3", respectively.
ル較拠A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。Comparison A: 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に準拠して行った。更に、パンクセント指数
を測定し、これらの結果を第2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 R5201. Furthermore, the punccent index was measured and these results are also listed in Table 2.
なお、パックセット指数は下記の方法で測定した。In addition, the pack set 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it250ml)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度回転の回数がパンクセット指数であ
る。したがって、パン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。Put 100 g of the powder sample into an Erlenmeyer flask (capacity: 250 ml) mounted on a variable vibrator, vibrate it for 15 seconds, remove the Erlenmeyer flask from the vibrator, and gently tilt it so that its center (center axis of the opening) ) was placed horizontally on the jig. Next, 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. This is the punk set index. Therefore, the smaller the Punxet index value is, the easier the powder is to handle with less agglomeration.
第2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 2, 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、パックセント指数も良好であり、酸化エチレン法に
よりエチレングリコール、ジエチレングリコール及びト
リエチレングリコール製造後の残液を利用することがで
き、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, a sufficient pulverizing effect can be obtained with a small addition rate, the pack cent index is also good, and the residual liquid after producing ethylene glycol, diethylene glycol, and triethylene glycol can be used by the ethylene oxide method. This is an extremely useful invention that helps in the effective use of resources.
(以下余白)(Margin below)
Claims (2)
コール、ヘキサエチレングリコール及びヘプタエチレン
グリコールの少なくとも1種を含有する水性液からなる
鉱物質の粉砕助剤。(1) A mineral grinding aid consisting of an aqueous liquid containing at least one of tetraethylene glycol, pentaethylene glycol, hexaethylene glycol, and heptaethylene glycol.
ル、ジエチレングリコール及びトリエチレングリコール
を合成し、該合成物を留去させた残液からなる鉱物質の
粉砕助剤。(2) A mineral grinding aid consisting of the residual liquid obtained by reacting ethylene oxide and water to synthesize ethylene glycol, diethylene glycol, and triethylene glycol, and distilling off the synthesized products.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11862689A JPH02298366A (en) | 1989-05-15 | 1989-05-15 | Grinding adjuvant of mineral substance |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11862689A JPH02298366A (en) | 1989-05-15 | 1989-05-15 | Grinding adjuvant of mineral substance |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH02298366A true JPH02298366A (en) | 1990-12-10 |
Family
ID=14741190
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11862689A Pending JPH02298366A (en) | 1989-05-15 | 1989-05-15 | Grinding adjuvant of mineral substance |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02298366A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004002165A (en) * | 2002-03-28 | 2004-01-08 | Kansai Electric Power Co Inc:The | Cement admixture and its production method |
| WO2008038732A1 (en) * | 2006-09-28 | 2008-04-03 | Sumitomo Osaka Cement Co., Ltd. | Method of brake fluid disposal and grinding aid for cement material |
| JP2009234820A (en) * | 2008-03-26 | 2009-10-15 | Sumitomo Osaka Cement Co Ltd | Cement composition, cement hardened body, and production method of cement |
| JP2010517915A (en) * | 2007-02-07 | 2010-05-27 | ユニミン コーポレーション | Method of processing nepheline syenite powder to produce ultrafine particle size products |
| CN114956649A (en) * | 2022-07-01 | 2022-08-30 | 吉林省希普水泥助磨剂有限公司 | Cement grinding aid and preparation method thereof |
-
1989
- 1989-05-15 JP JP11862689A patent/JPH02298366A/en active Pending
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004002165A (en) * | 2002-03-28 | 2004-01-08 | Kansai Electric Power Co Inc:The | Cement admixture and its production method |
| WO2008038732A1 (en) * | 2006-09-28 | 2008-04-03 | Sumitomo Osaka Cement Co., Ltd. | Method of brake fluid disposal and grinding aid for cement material |
| US8083850B2 (en) | 2006-09-28 | 2011-12-27 | Sumitomo Osaka Cement Co., Ltd. | Method of brake fluid disposal and grinding aid for cement material |
| JP5228230B2 (en) * | 2006-09-28 | 2013-07-03 | 住友大阪セメント株式会社 | Brake fluid treatment method and cement-based material grinding aid |
| KR101402572B1 (en) * | 2006-09-28 | 2014-05-30 | 스미토모 오사카 세멘토 가부시키가이샤 | Method of brake fluid disposal and grinding aid for cement material |
| JP2010517915A (en) * | 2007-02-07 | 2010-05-27 | ユニミン コーポレーション | Method of processing nepheline syenite powder to produce ultrafine particle size products |
| JP2009234820A (en) * | 2008-03-26 | 2009-10-15 | Sumitomo Osaka Cement Co Ltd | Cement composition, cement hardened body, and production method of cement |
| CN114956649A (en) * | 2022-07-01 | 2022-08-30 | 吉林省希普水泥助磨剂有限公司 | Cement grinding aid and preparation method thereof |
| CN114956649B (en) * | 2022-07-01 | 2023-02-10 | 吉林省希普水泥助磨剂有限公司 | Cement grinding aid and preparation method thereof |
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