CN101775238B - Active extra-fine grinding calcium carbonate processing method - Google Patents

Active extra-fine grinding calcium carbonate processing method Download PDF

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Publication number
CN101775238B
CN101775238B CN 201010103151 CN201010103151A CN101775238B CN 101775238 B CN101775238 B CN 101775238B CN 201010103151 CN201010103151 CN 201010103151 CN 201010103151 A CN201010103151 A CN 201010103151A CN 101775238 B CN101775238 B CN 101775238B
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CN
China
Prior art keywords
calcium carbonate
fine grinding
processing method
grinding calcium
active extra
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Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN 201010103151
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Chinese (zh)
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CN101775238A (en
Inventor
徐方祥
隋亚娜
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DALIAN YOULAN ENTERPRISE GROUP Co Ltd
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DALIAN YOULAN ENTERPRISE GROUP Co Ltd
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Priority to CN 201010103151 priority Critical patent/CN101775238B/en
Publication of CN101775238A publication Critical patent/CN101775238A/en
Application granted granted Critical
Publication of CN101775238B publication Critical patent/CN101775238B/en
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Abstract

The invention discloses an active extra-fine grinding calcium carbonate processing method which belongs to the technical calcium carbonate processing field. In the active extra-fine grinding calcium carbonate processing method, stearic acid is used as an activating agent for activating and modifying calcium carbonate. The active extra-fine grinding calcium carbonate produced by using the processing method has the grain size being up to 1.7 mum and has advanced powder fineness. The activating agent modifies inorganic padding, plays a role of bridging an interface of the inorganic material and a high polymer material, improves the compatibility of the inorganic material and the high polymer material, and has the efficacy which can not be matched by singly modifying triple superphosphate and precipitated calcium carbonate.

Description

Active extra-fine grinding calcium carbonate processing method
Technical field
The invention belongs to the technical field of calcium carbonate processing superfine, modification, specifically refer to calcium carbonate powder modification processing treatment.
Background technology
In the inorganic chemicals industry product, calcium carbonate is to belong to the Chemicals that turnout is very big, purposes is extremely wide, the consumption maximum is paper-making industry in the world, next is as weighting agent, strengthening agent, extender, especially for the polyvinyl chloride plastic material products, such as being used for plastic-steel door and window, upper and lower conduit, cable, pipe etc. for plastics.Calcium carbonate also is used as a kind of filler of tackiness agent, seal gum, coating, paint.Water-ground limestone is one take natural calcite as raw material, with its ink powder, reaches certain fineness standard with the method for machinery.It is different that water-ground limestone is pressed particle diameter, is divided into particulate calcium carbonate, micro mist calcium carbonate, fine calcium carbonate, calcium carbonate superfine powder, super fine calcium carbonate.
Summary of the invention
The purpose of this invention is to provide a kind of calcium carbonate active working method, i.e. a kind of active extra-fine grinding calcium carbonate processing method.
The present invention to achieve these goals, the technical scheme that adopts is: a kind of active extra-fine grinding calcium carbonate processing method is provided, and described active extra-fine grinding calcium carbonate processing method uses stearic acid as activator.
Active extra-fine grinding calcium carbonate processing method one preferred version of the present invention: described active extra-fine grinding calcium carbonate complete processing is,
(1) with the calcite of supplied materials less than 400mm, respectively through jaw crusher, hammer crushing crusher machine, the calcite particle diameter that obtains advances storage bin and stores less than 5mm;
(2) through three grades of pulverizing, grading machine classification, classification is not up to standard sends storage bin back to material by storage bin;
(3) classification material up to standard carries out the activator activation modification in the turbine mill.
Active extra-fine grinding calcium carbonate processing method one preferred version of the present invention: described active extra-fine grinding calcium carbonate complete processing turbine mill rotating speed is 3000 rev/mins, and Heating temperature is 100-110 ℃.
Active extra-fine grinding calcium carbonate processing method beneficial effect of the present invention is:
1, the calcite particle diameter after classified can reach 1.7 μ m, and powder fineness is leading.
2, calcium carbonate do super-refinement can improve filled articles snappiness, improve to stretch, impact property.
3, activator modified inorganic filler plays the effect of on inorganic materials and macromolecular material interface " bridge formation ", improves the consistency of inorganic materials and macromolecular material.
4, the active extra-fine grinding calcium carbonate that utilizes working method of the present invention to produce has simple modified heavy calcium carbonate, the simple incomparable effect of modification fine particle calcium carbonate.
Embodiment
Embodiment
A kind of complete processing of using stearic acid to produce active extra-fine grinding calcium carbonate as activator is:
(1) with the calcite of supplied materials less than 400mm, respectively through jaw crusher, hammer crushing crusher machine, the calcite particle diameter that obtains advances storage bin and stores less than 5mm;
(2) through three grades of pulverizing, grading machine classification, classification is not up to standard sends storage bin back to material by storage bin;
(3) classification material up to standard carries out the activator activation modification in the turbine mill, turbine mill rotating speed is 3000 rev/mins, and Heating temperature is 100-110 ℃.
The above; only be the better embodiment of the present invention; but protection scope of the present invention is not limited to this; anyly be familiar with those skilled in the art in the technical scope that the present invention discloses; be equal to replacement or change according to technical scheme of the present invention and inventive concept thereof, all should be encompassed within protection scope of the present invention.

Claims (2)

1. active extra-fine grinding calcium carbonate processing method is characterized in that: described active extra-fine grinding calcium carbonate processing method uses stearic acid as activator; Described active extra-fine grinding calcium carbonate complete processing is:
(1) with the calcite of supplied materials less than 400mm, respectively through jaw crusher, hammer crushing crusher machine, the calcite particle diameter that obtains advances storage bin and stores less than 5mm;
(2) through three grades of pulverizing, grading machine classification, classification is not up to standard sends storage bin back to material by storage bin;
(3) classification material up to standard carries out the activator activation modification in the turbine mill.
2. active extra-fine grinding calcium carbonate processing method according to claim 1 is characterized in that: described active extra-fine grinding calcium carbonate complete processing turbine mill rotating speed is 3000 rev/mins, and Heating temperature is 100-110 ℃.
CN 201010103151 2010-01-29 2010-01-29 Active extra-fine grinding calcium carbonate processing method Expired - Fee Related CN101775238B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201010103151 CN101775238B (en) 2010-01-29 2010-01-29 Active extra-fine grinding calcium carbonate processing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201010103151 CN101775238B (en) 2010-01-29 2010-01-29 Active extra-fine grinding calcium carbonate processing method

Publications (2)

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CN101775238A CN101775238A (en) 2010-07-14
CN101775238B true CN101775238B (en) 2013-01-09

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Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103804953B (en) * 2013-12-10 2015-09-09 辽宁亿龙矿业股份有限公司 The preparation method of ultra-fine surface modification rhombspar
CN103804957B (en) * 2014-02-24 2015-02-25 哈尔滨工程大学 Modification method of ferric oxide corrosion-resistant pigment
CN104744971A (en) * 2015-03-04 2015-07-01 江西科越科技有限公司 Preparation process of wet-process superfine modified calcium carbonate
CN104743598A (en) * 2015-03-04 2015-07-01 江西科越科技有限公司 Preparation method of coarse whiting special for papermaking
CN105482501A (en) * 2015-11-26 2016-04-13 恩平燕怡新材料有限公司 Wet airflow crushing dispersion method of nanometer calcium carbonate
CN108948792A (en) * 2018-05-10 2018-12-07 桂林永福恒达实业有限公司 A kind of preparation method of the micro mist calcium carbonate suitable for polymer production

Citations (3)

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Publication number Priority date Publication date Assignee Title
CN1451695A (en) * 2003-04-25 2003-10-29 李柏荣 Method for dry producing micron and submicron organic nonmetal mineral functional mother stock
CN1803937A (en) * 2005-12-20 2006-07-19 中国地质大学(武汉) Dry process mechanical force and chemical modification method of superfine calcium carbonate
CN1962766A (en) * 2006-12-08 2007-05-16 中南大学 Process for preparing superfine modified inorganic powder by dry method

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1451695A (en) * 2003-04-25 2003-10-29 李柏荣 Method for dry producing micron and submicron organic nonmetal mineral functional mother stock
CN1803937A (en) * 2005-12-20 2006-07-19 中国地质大学(武汉) Dry process mechanical force and chemical modification method of superfine calcium carbonate
CN1962766A (en) * 2006-12-08 2007-05-16 中南大学 Process for preparing superfine modified inorganic powder by dry method

Non-Patent Citations (2)

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郑水林.非金属矿物粉体表面改性技术及应用.《2007年全国粉体工业技术大会论文集》.2007,47-57. *

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Address after: Xinglongtai District of Liaoning city in Panjin province 124010 Huibin Street No. 91

Applicant after: Dalian Youlan Enterprise Group Co., Ltd.

Address before: 116103, Liaoning Dalian District, Jinzhou province thirty mile town friends LAN Industrial Zone

Applicant before: Dalian Youlan Enterprise Group Co., Ltd.

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Granted publication date: 20130109

Termination date: 20150129

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