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CN102303885A - Method for refining white clay calcium carbonate from green solution produced in alkali recovery from grass pulp - Google Patents

Method for refining white clay calcium carbonate from green solution produced in alkali recovery from grass pulp Download PDF

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Publication number
CN102303885A
CN102303885A CN201110242298A CN201110242298A CN102303885A CN 102303885 A CN102303885 A CN 102303885A CN 201110242298 A CN201110242298 A CN 201110242298A CN 201110242298 A CN201110242298 A CN 201110242298A CN 102303885 A CN102303885 A CN 102303885A
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calcium carbonate
green liquor
reaction
white mud
straw pulp
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夏新兴
刘峰
吴盼
李金宝
李佩燚
罗清
殷学风
王建
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Shaanxi University of Science and Technology
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Shaanxi University of Science and Technology
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Abstract

一种草类制浆碱回收绿液精制白泥碳酸钙的方法,将生石灰加入水中使生石灰消化完全制成石灰溶液;将草浆绿液加到石灰溶液中发生苛化反应或将石灰溶液加入到草浆绿液中制成白泥碳酸钙。本发明通过对碱回收机理研究,改进现有的碱回收工艺条件,将消化反应和苛化反应分开进行,并控制反应条件,使苛化反应生产的白泥碳酸钙形貌为针形,使得碱回收产生的副产品白泥碳酸钙,白度高,晶型均一,能高质量的用于纸张加填,部分甚至全部代替商品碳酸钙,节约制浆企业成本,减少环境污染。A method for grass pulping soda to recover green liquor and refine white mud calcium carbonate. Quicklime is added to water to digest the quicklime to make a lime solution; add straw pulp green liquor to the lime solution for causticization reaction or add the lime solution to Make white mud calcium carbonate into the straw pulp green liquor. The present invention improves the existing alkali recovery process conditions by studying the alkali recovery mechanism, separates the digestion reaction and the causticization reaction, and controls the reaction conditions so that the appearance of the white mud calcium carbonate produced by the causticization reaction is needle-shaped, so that Calcium carbonate, a by-product of alkali recovery, has high whiteness and uniform crystal form. It can be used for paper filling with high quality, and can partially or even completely replace commercial calcium carbonate, saving pulping enterprises costs and reducing environmental pollution.

Description

一种草类制浆碱回收绿液精制白泥碳酸钙的方法A method for recovering green liquor from grass pulping alkali to refine white mud calcium carbonate

技术领域 technical field

本发明属于造纸工业领域,具体涉及一种草类制浆碱回收绿液精制白泥碳酸钙的方法。The invention belongs to the field of papermaking industry, and in particular relates to a method for recovering green liquor from grass pulping soda and refining lime mud calcium carbonate.

背景技术 Background technique

中国森林资源缺乏,大部分制浆厂还是利用草类原料制浆,在制浆过程中,碱回收是必不可少的工序,碱回收过程会产生大量白泥碳酸钙。传统的碱回收工艺是将生石灰直接加入到草浆绿液中,也就是消化反应和苛化反应同时进行。这种工艺条件生产的白泥碳酸钙由于质量问题,并不能很好的用于纸张加填,大多数企业只能选择堆放、填埋处理,造成了二次污染。China lacks forest resources, and most pulp mills still use grass raw materials for pulping. In the pulping process, alkali recovery is an essential process, and the process of alkali recovery will produce a large amount of white mud calcium carbonate. The traditional alkali recovery process is to add quicklime directly to the grass pulp green liquor, that is, the digestion reaction and the causticization reaction are carried out simultaneously. The white mud calcium carbonate produced under this technological condition cannot be used for paper filling due to quality problems. Most enterprises can only choose to stack and landfill it, causing secondary pollution.

发明内容 Contents of the invention

本发明的目的在于提供一种能够使得碱回收产生的副产品白泥碳酸钙,白度高,晶型均一,能高质量的用于纸张加填,部分甚至全部代替商品碳酸钙,节约制浆企业成本,减少环境污染的草类制浆碱回收绿液精制白泥碳酸钙的方法。The purpose of the present invention is to provide a white mud calcium carbonate, a by-product of alkali recovery, with high whiteness and uniform crystal form, which can be used for paper filling with high quality, partly or even completely replace commercial calcium carbonate, and save pulping enterprises. The method of recovering green liquor and refining white mud calcium carbonate by grass pulping soda which reduces environmental pollution.

为达到上述目的,本发明采用的技术方案是:In order to achieve the above object, the technical scheme adopted in the present invention is:

1)将生石灰加入水中反应10-120min,反应温度5-100℃,使生石灰消化完全制成质量浓度为10%-40%石灰溶液;1) adding quicklime into water to react for 10-120min at a reaction temperature of 5-100°C, so that the quicklime is completely digested and made into a lime solution with a mass concentration of 10%-40%;

2)按每克生石灰加入0.02-0.5ml的草浆绿液将草浆绿液加到石灰溶液中发生苛化反应;或按每ml草浆绿液加入0.01-0.5g生石灰的量将石灰溶液加入到草浆绿液中,反应温度10-100℃,搅拌速度为100-5000rpm制成白泥碳酸钙。2) Add 0.02-0.5ml of straw pulp green liquor per gram of quicklime, add grass pulp green liquor to lime solution for causticization reaction; or add 0.01-0.5g of straw pulp green liquor to lime solution Add it into the grass pulp green liquor, the reaction temperature is 10-100°C, and the stirring speed is 100-5000rpm to make white mud calcium carbonate.

本发明通过对碱回收机理研究,改进现有的碱回收工艺条件,将消化反应和苛化反应分开进行,并控制反应条件,使苛化反应生产的白泥碳酸钙形貌为针形,使得碱回收产生的副产品白泥碳酸钙,白度高,晶型均一,能高质量的用于纸张加填,部分甚至全部代替商品碳酸钙,节约制浆企业成本,减少环境污染。The present invention improves the existing alkali recovery process conditions by studying the alkali recovery mechanism, separates the digestion reaction and the causticization reaction, and controls the reaction conditions so that the appearance of the white mud calcium carbonate produced by the causticization reaction is needle-shaped, so that Calcium carbonate, a by-product of alkali recovery, has high whiteness and uniform crystal form. It can be used for paper filling with high quality, and can partially or even completely replace commercial calcium carbonate, saving pulping enterprises costs and reducing environmental pollution.

附图说明 Description of drawings

图1是本发明制备的针形白泥碳酸钙扫描电镜图。Fig. 1 is the scanning electron micrograph of the needle-shaped white mud calcium carbonate prepared by the present invention.

具体实施方式 Detailed ways

下面结合附图及实施例对本发明作进一步详细说明。The present invention will be described in further detail below in conjunction with the accompanying drawings and embodiments.

实施例1,将生石灰加入水中使生石灰消化完全制成质量浓度为10%石灰溶液;按每克生石灰加入0.02ml的草浆绿液将草浆绿液加到石灰溶液中发生苛化反应,反应温度10℃,搅拌速度为5000rpm制成白泥碳酸钙。Embodiment 1, quicklime is added in water and quicklime is digested and made mass concentration completely and is 10% lime solution; Add 0.02ml straw pulp green liquor by every gram of quicklime, straw pulp green liquor is added in lime solution and causticizing reaction occurs, reaction The temperature is 10°C, and the stirring speed is 5000rpm to make white mud calcium carbonate.

实施例2,将生石灰加入水中使生石灰消化完全制成质量浓度为30%石灰溶液;按每克生石灰加入0.08ml的草浆绿液将草浆绿液加到石灰溶液中发生苛化反应,反应温度50℃,搅拌速度为100rpm制成白泥碳酸钙。Embodiment 2, quicklime is added in water and quicklime is digested and made mass concentration completely and is 30% lime solution; Add the straw pulp green liquor of 0.08ml by every gram of quicklime, straw pulp green liquor is added in the lime solution and causticizing reaction occurs, reaction The temperature is 50°C, and the stirring speed is 100rpm to make white mud calcium carbonate.

实施例3,将生石灰加入水中使生石灰消化完全制成质量浓度为20%石灰溶液;按每克生石灰加入0.3ml的草浆绿液将草浆绿液加到石灰溶液中发生苛化反应,反应温度80℃,搅拌速度为2000rpm制成白泥碳酸钙。Embodiment 3, quicklime is added in water and quicklime is digested and made mass concentration completely and is 20% lime solution; Add the straw pulp green liquor of 0.3ml by every gram of quicklime, straw pulp green liquor is added in the lime solution and causticizing reaction occurs, reaction The temperature is 80°C, and the stirring speed is 2000rpm to make white mud calcium carbonate.

实施例4,将生石灰加入水中使生石灰消化完全制成质量浓度为40%石灰溶液;按每克生石灰加入0.5ml的草浆绿液将草浆绿液加到石灰溶液中发生苛化反应,反应温度100℃,搅拌速度为3500rpm制成白泥碳酸钙。Embodiment 4, quicklime is added in water and quicklime is digested and made mass concentration completely and is 40% lime solution; Add the straw pulp green liquor of 0.5ml by every gram of quicklime, straw pulp green liquor is added in the lime solution and causticizing reaction occurs, reaction The temperature is 100°C, and the stirring speed is 3500rpm to make white mud calcium carbonate.

实施例5,将生石灰加入水中使生石灰消化完全制成质量浓度为25%石灰溶液;按每ml草浆绿液加入0.01g生石灰的量将石灰溶液加入到草浆绿液中,反应温度30℃,搅拌速度为500rpm制成白泥碳酸钙。Example 5, adding unslaked lime into water to make the unslaked lime fully digested makes a lime solution with a mass concentration of 25%; add 0.01 g of unslaked lime per ml of straw pulp green liquor and add the lime solution to the straw pulp green liquor at a reaction temperature of 30°C , the stirring speed is 500rpm to make white mud calcium carbonate.

实施例6,将生石灰加入水中使生石灰消化完全制成质量浓度为15%石灰溶液;按每ml草浆绿液加入0.2g生石灰的量将石灰溶液加入到草浆绿液中,反应温度60℃,搅拌速度为1000rpm制成白泥碳酸钙。Example 6, adding unslaked lime into water to make the unslaked lime fully digested makes a lime solution with a mass concentration of 15%; add 0.2 g of unslaked lime per ml of straw pulp green liquor and add the lime solution to the grass pulp green liquor at a reaction temperature of 60°C , the stirring speed is 1000rpm to make white mud calcium carbonate.

实施例7,将生石灰加入水中使生石灰消化完全制成质量浓度为35%石灰溶液;按每ml草浆绿液加入0.5g生石灰的量将石灰溶液加入到草浆绿液中,反应温度20℃,搅拌速度为4200rpm制成白泥碳酸钙。Example 7, adding unslaked lime into water to make the unslaked lime completely digested to make a lime solution with a mass concentration of 35%; adding 0.5 g of unslaked lime per ml of grass pulp green liquor to add lime solution to the grass pulp green liquor at a reaction temperature of 20°C , the stirring speed is 4200rpm to make white mud calcium carbonate.

由如图1可以看出本发明将消化反应和苛化反应分开进行,并控制反应条件,使苛化反应生成的白泥碳酸钙形貌为针形。As can be seen from Figure 1, the present invention separates the digestion reaction and the causticizing reaction, and controls the reaction conditions so that the appearance of the white mud calcium carbonate generated by the causticizing reaction is needle-shaped.

Claims (1)

1. a grass type slurrying alkali reclaims the method that green liquor is made with extra care white mud calcium carbonate, it is characterized in that:
1) unslaked lime is added to make quicklime slaking process mass concentration fully in the entry be the 10%-40% lime solution;
2) the straw pulp green liquor that adds 0.02-0.5ml by every gram unslaked lime is added to the straw pulp green liquor causticizing reaction takes place in the lime solution, and temperature of reaction 10-100 ℃, stirring velocity is that 100-5000rpm processes white mud calcium carbonate; Or by the amount that every ml straw pulp green liquor adds 0.01-0.5g unslaked lime lime solution is joined in the straw pulp green liquor, temperature of reaction 10-100 ℃, stirring velocity is that 100-5000rpm processes white mud calcium carbonate.
CN201110242298A 2011-08-23 2011-08-23 Method for refining white clay calcium carbonate from green solution produced in alkali recovery from grass pulp Pending CN102303885A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102730736A (en) * 2012-06-28 2012-10-17 陕西科技大学 Method for preparing granular white mud calcium carbonate by using green liquor from straw pulp base recovery
CN103215849A (en) * 2013-04-28 2013-07-24 陕西科技大学 Method for recycling white-clay refined paper calcium carbonate filler by improved soda-process pulping alkali
CN104695270A (en) * 2015-02-14 2015-06-10 浙江理工大学 Method for controlling silicon in non-wood pulping alkali recovery green liquor low-temperature causticizing process
CN109650433A (en) * 2019-02-13 2019-04-19 广东鼎丰纸业有限公司 The method of slurrying alkali collection green liquor purification manufacture high-purity calcium carbonate

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1436894A (en) * 2002-02-09 2003-08-20 艾天召 Improved alkali recovering process from paper-making black liquor
CN1641100A (en) * 2004-07-20 2005-07-20 上海东升新材料有限公司 Method for recovering superfine calcium carbonate by clean causticization of green liquor
CN101700901A (en) * 2009-11-25 2010-05-05 王冬生 Novel method for producing light calcium carbonate (CaCO3) from white clay generated from alkali recovering in paper-making industry

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1436894A (en) * 2002-02-09 2003-08-20 艾天召 Improved alkali recovering process from paper-making black liquor
CN1641100A (en) * 2004-07-20 2005-07-20 上海东升新材料有限公司 Method for recovering superfine calcium carbonate by clean causticization of green liquor
CN101700901A (en) * 2009-11-25 2010-05-05 王冬生 Novel method for producing light calcium carbonate (CaCO3) from white clay generated from alkali recovering in paper-making industry

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102730736A (en) * 2012-06-28 2012-10-17 陕西科技大学 Method for preparing granular white mud calcium carbonate by using green liquor from straw pulp base recovery
CN103215849A (en) * 2013-04-28 2013-07-24 陕西科技大学 Method for recycling white-clay refined paper calcium carbonate filler by improved soda-process pulping alkali
CN104695270A (en) * 2015-02-14 2015-06-10 浙江理工大学 Method for controlling silicon in non-wood pulping alkali recovery green liquor low-temperature causticizing process
CN109650433A (en) * 2019-02-13 2019-04-19 广东鼎丰纸业有限公司 The method of slurrying alkali collection green liquor purification manufacture high-purity calcium carbonate
CN109650433B (en) * 2019-02-13 2019-12-03 广东鼎丰纸业有限公司 The method of slurrying alkali collection green liquor purification manufacture high-purity calcium carbonate

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Application publication date: 20120104