Method for preparing white clay calcium carbonate by performing low-temperature two-step causticization on non-wood pulp alkali recovery green liquid

A non-wood pulp and calcium carbonate technology, applied in the direction of calcium carbonate/strontium/barium, etc., can solve the problems of unsatisfactory preferential reaction effect and unsatisfactory selective silicon removal effect, and achieve the effect of resource utilization

Active Publication Date: 2015-06-10
YOUBIAOYIZHAN (SUZHOU) E-COMMERCE CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

According to Dr. Rao of India et al. 2 SiO 3 with Ca(OH) 2 The reactivity and rate are greater than that of Na 2 CO 3 with Ca(OH) 2 The characteristics of the reaction, the bamboo pulp green liquor is treated by high temperature two-step causticization method, the research found that the first step causticizing lime addition is 30% (relative to the total lime addition), the reaction temperature is 90~95°C, and the reaction time is 1.5 hrs, the white mud only brings out about 56% of the total silicon contained in the green liquor, and the selective removal of silicon is not ideal
It can be seen that high temperature increases Na 2 CO 3 with Ca(OH) 2 The reaction rate, so that Na 2 SiO 3 with Ca(OH) 2 The priority response effect is not ideal

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0015] The first step of causticization: Add the green liquor recovered from non-wood pulping alkali to the completely digested lime water to cause causticization reaction. The amount of lime is 5% of the total amount of causticized lime, and the green liquor addition rate per gram of quicklime is 0.02ml / min; the reaction temperature is 10°C, the stirring speed is 50rpm, and the reaction time is 100min. After the specified reaction time was reached, the precipitate was separated and removed by filtration.

[0016] The second step of causticization: adding the remaining 95% lime to the filtered filtrate to continue causticization, the reaction temperature is 60°C to increase the causticization reaction speed, continue to react for 30 minutes, or continue to react for 5 hours at the original temperature, filter and separate, wash , get white mud calcium carbonate with regular shape.

Embodiment 2

[0018] The first step of causticization: add the green liquor recovered from non-wood pulping alkali to the completely digested lime water to cause causticization reaction. The amount of lime used is 20% of the total amount of causticized lime, and the green liquor addition rate per gram of quicklime is 0.8ml / min; the reaction temperature is 5°C, the stirring speed is 2000rpm, and the reaction time is 5min. After the specified reaction time was reached, the precipitate was separated and removed by filtration.

[0019] The second step of causticization: adding the remaining 80% lime to the filtered filtrate to continue causticization, the reaction temperature is 80°C to increase the causticization reaction speed, continue to react for 86 minutes, or continue to react for 2 hours at the original temperature, filter and separate, wash , get white mud calcium carbonate with regular shape.

Embodiment 3

[0021] The first step of causticization: add the green liquor recovered from non-wood pulping alkali to the completely digested lime water to cause causticization reaction. The amount of lime is 40% of the total amount of causticized lime, and the green liquor addition rate per gram of quicklime is 1ml / min; the reaction temperature is 39° C., the stirring speed is 20 rpm, and the reaction time is 180 min. After the specified reaction time was reached, the precipitate was separated and removed by filtration.

[0022] The second step of causticization: adding the remaining 60% lime to the filtered filtrate to continue causticizing, the reaction temperature is 100°C to increase the causticizing reaction speed, continue to react for 120 minutes, or continue to react for 12 hours at the original temperature, filter and separate, wash , get white mud calcium carbonate with regular shape.

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Abstract

The invention relates to a method for preparing white clay calcium carbonate by performing low-temperature two-step causticization on a non-wood pulp alkali recovery green liquid. According to the method, in a first step, a less amount of Ca(OH)2 is added into the non-wood pulp alkali recovery green liquid to perform low-temperature causticization at the temperature of below 39 DEG C to ensure that Na2SiO3 in the green liquid is subjected to prior reaction to produce CaSiO3, and precipitation on CaSiO3 is carried out and a part of precipitants are removed in a separating manner; and in a second step of causticization, the high-quality white clay calcium carbonate is prepared. According to the method, the problem of silicon interference in the causticization process of the white clay calcium carbonate can be effectively solved, and the resourceful utilization of the white clay calcium carbonate is realized.

Description

technical field [0001] The invention relates to a method for preparing white mud calcium carbonate by low-temperature two-step causticization of green liquor recovered from non-wood pulp alkali. Background technique [0002] Due to the shortage of wood resources, many countries in Asia and Europe still use a large number of non-wood fiber raw materials for pulp and paper, such as wheat straw, reed, bagasse, bamboo, etc. my country has a long history of pulping and papermaking from non-wood raw materials. It is the country with the largest non-wood pulp production in the world, with an annual output of about 10 million tons and about 5 to 6 million tons of lime mud. However, for a long time, the high silicon content of non-wood raw materials has caused serious "silicon interference" to the pulping process, and it has also made it difficult to recycle caustic lime mud (Since the main component of white mud is calcium carbonate, it is also called white mud calcium carbonate), ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01F11/18
CPCC01F11/18
Inventor 夏新兴郭爱莲郭大亮胡谦孙珊王芳
Owner YOUBIAOYIZHAN (SUZHOU) E-COMMERCE CO LTD
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