CN108003383B - A kind of PVC plastic preparation method for brightening winnofil - Google Patents

A kind of PVC plastic preparation method for brightening winnofil Download PDF

Info

Publication number
CN108003383B
CN108003383B CN201711259322.8A CN201711259322A CN108003383B CN 108003383 B CN108003383 B CN 108003383B CN 201711259322 A CN201711259322 A CN 201711259322A CN 108003383 B CN108003383 B CN 108003383B
Authority
CN
China
Prior art keywords
calcium carbonate
winnofil
brightening
sodium
pvc plastic
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.)
Active
Application number
CN201711259322.8A
Other languages
Chinese (zh)
Other versions
CN108003383A (en
Inventor
姚忠修
颜干才
杜年军
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shandong Yuxin Nano Technology Co ltd
Original Assignee
Qingzhou Yu Xingai Industry Limited-Liability Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Qingzhou Yu Xingai Industry Limited-Liability Co filed Critical Qingzhou Yu Xingai Industry Limited-Liability Co
Priority to CN201711259322.8A priority Critical patent/CN108003383B/en
Publication of CN108003383A publication Critical patent/CN108003383A/en
Application granted granted Critical
Publication of CN108003383B publication Critical patent/CN108003383B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K9/00Use of pretreated ingredients
    • C08K9/04Ingredients treated with organic substances
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/24Acids; Salts thereof
    • C08K3/26Carbonates; Bicarbonates
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K9/00Use of pretreated ingredients
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K9/00Use of pretreated ingredients
    • C08K9/02Ingredients treated with inorganic substances
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L27/00Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers
    • C08L27/02Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L27/04Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment containing chlorine atoms
    • C08L27/06Homopolymers or copolymers of vinyl chloride
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/24Acids; Salts thereof
    • C08K3/26Carbonates; Bicarbonates
    • C08K2003/265Calcium, strontium or barium carbonate
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K2201/00Specific properties of additives
    • C08K2201/002Physical properties
    • C08K2201/006Additives being defined by their surface area
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K2201/00Specific properties of additives
    • C08K2201/011Nanostructured additives
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/03Polymer mixtures characterised by other features containing three or more polymers in a blend
    • C08L2205/035Polymer mixtures characterised by other features containing three or more polymers in a blend containing four or more polymers in a blend

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Abstract

The invention discloses a kind of PVC plastic preparation methods for brightening winnofil, the following steps are included: Step 1: in the carbonation process for preparing winnofil, when carbonation rate reaches 60~80%, reducing agent and sodium isoascorbate is added, continues carbonization to pH less than 7.0;Step 2: calcium carbonate serosity that carbonization is completed is delivered to aging tank, still aging 12~for 24 hours;Step 3: opening the agitating device of aging tank, calcium carbonate serosity after ageing concentration is stirred evenly, it is then sent to activation kettle and heats, activation kettle is set to be warming up to 70~90 DEG C, ten diester of maleic acid list is added, stirs 20~40 minutes, then adds odium stearate and 4,4 '~bis- (sodium disulfonate styryl) biphenyl stir 20~40 minutes;Step 4: modified calcium carbonate serosity successively to be carried out to filters pressing, drying, crushing to get brightening winnofil.The winnofil production PVC plastic product glossiness produced by the present invention that brightens is good, small, the stable product quality of color difference fluctuation.

Description

A kind of PVC plastic preparation method for brightening winnofil
Technical field
The present invention relates to the whitening technology field of winnofil more particularly to a kind of PVC plastics with brightening precipitating carbonic acid The preparation method of calcium.
Background technique
Winnofil has whiteness high, nontoxic, nonirritant, price is low as a kind of important chemical inorganic filler The features such as honest and clean, makes it be widely used in the industries such as plastics, rubber, coating, sealant, ink and papermaking.
In PVC plastic processing industry, as the maximum filler of usage amount, it is high-strength that winnofil can assign PVC plastic The characteristics such as degree, high rigidity, wear-resisting, ageing-resistant, fire retardant, corrosion-resistant, easy dyeing, however, color difference is unstable in white PVC product Fixed, fluctuation is always that the sector is difficult to the problem overcome greatly.Its reason is mainly from following two aspect:
First, the difference of calcium carbonate form and aspect.Winnofil generally uses lime stone as raw material, through calcining, digestion, old After the multiple tracks preparation sections such as change, carbonating, surface modification, press dewatering, drying, crushing, calcium carbonate finished product is obtained.However, by It is also different in the content of the intrinsic difference of different sources lime stone quality, the foreign metals such as magnesium, iron, manganese, thus prepare Calcium carbonate finished product form and aspect differ greatly.
The stability of second, PVC processability.Except the hue difference that calcium carbonate raw material impurity causes is unusual, PVC material itself Thermal decomposition behavior is the main factor for causing PVC product form and aspect and changing.When formula system mobility is poor, processing electric current When bigger than normal, PVC thermal decomposition aggravation often leads to the jaundice of product form and aspect, and this problem is generally also the surface by calcium carbonate Caused by science and engineering skill.
Chinese invention patent CN1544535A provides a kind of purification method of whitening of calcium carbonate especially winnofil, Ca (OH) is handled by chemical method2Suspension or CaCO3Clinker slurry, removing in slurries is in color base, to increase product brightness, Whiteness and purity are improved, while improving raw material grade and resource utilization.The purification method of whitening of this calcium carbonate are as follows: in alkalinity Under the conditions of into the suspension slurry of calcium carbonate be added be equivalent to its weight 0.01~0.5% reducing agent, screening agent, chelating agent its Middle one or more, pulp density 8~50%, 30~90 DEG C of temperature, stir process 30~120 minutes;Filtering is dried, sieving To obtain the final product.However, the preparation method can only inhibit the form and aspect of calcium carbonate itself to a certain extent, but in PVC material application, but It is difficult to improve the chromatic aberration caused by decomposing because of PVC.
Chinese invention patent CN101570342A is disclosed and a kind of is prepared silicone sealant using low-ore grade limestone wet-process The method of high-whiteness nanometer calcium carbonate special.Used technical solution are as follows: by limestone calcination and be crushed, calcium oxide is made: Sizing screening, good calcium oxide then enter next process;It takes quality oxide calcium by the digestion of revolution digestion machine, remove iron, change Brighten, heat preservation is aged, controls temperature and concentration and adds crystal control agent and carry out bubbling carbonizing, secondary ageing, then secondary carbon Change, wet process is twice-modified, finally obtains required nanometer calcium carbonate through filter-press dehydration, drying, crushing, classification, packaging again and produces Product.Chemical whitening described above is equally the binding mode using reducing agent and chelating agent, is only capable of inhibiting to a certain extent The form and aspect of calcium carbonate itself, but it is very little to the improvement result of PVC product form and aspect.
In conclusion the winnofil prepared using chemical whitening method, is typically only capable to increase calcium carbonate to a certain extent Whiteness, but can not improve and stablize the whiteness of product in PVC production process.
Summary of the invention
Technical problem to be solved by the invention is to provide one kind can effectively increase white PVC product whiteness, glossiness PVC plastic with brightening the preparation method of winnofil.
In order to solve the above technical problems, the technical scheme is that a kind of PVC plastic system for brightening winnofil Preparation Method, comprising the following steps:
Step 1:, when carbonation rate reaches 60~80%, reducing agent is added in the carbonation process for preparing winnofil And sodium isoascorbate, continue carbonization to pH less than 7.0;
Step 2: the calcium carbonate serosity that carbonization is completed is delivered to aging tank, and keep calcium carbonate serosity quiet in aging tank Ageing 12~for 24 hours is set, supernatant liquor is then transported to Sewage treatment pond with dredge pump and is handled;
Step 3: opening the agitating device of aging tank, the calcium carbonate serosity after ageing concentration is stirred evenly, is then conveyed To activation kettle, activation kettle is made to be warming up to 70~90 DEG C, ten diester of maleic acid list is added, stirred 20~40 minutes, then add Odium stearate and 4,4 '~bis- (sodium disulfonate styryl) biphenyl, continues stirring 20~40 minutes, completes activation modification processing;
Step 4: modified calcium carbonate serosity successively to be carried out to filters pressing, drying, crushing to get brightening winnofil.
As a preferred technical solution, the following steps are included:
Step 1: in the carbonation process for preparing winnofil, when carbonation rate reaches 70%, reducing agent and different is added Sodium ascorbate, continuing to be carbonized to pH is 6.8;
Step 2: the calcium carbonate serosity that carbonization is completed is delivered to aging tank, and keep calcium carbonate serosity quiet in aging tank Ageing 18h is set, supernatant liquor is then transported to Sewage treatment pond with dredge pump and is handled;
Step 3: opening the agitating device of aging tank, the calcium carbonate serosity after ageing concentration is stirred evenly, is then conveyed To activation kettle, activation kettle is made to be warming up to 85 DEG C, ten diester of maleic acid list is added, stirred 30 minutes, then add odium stearate With 4,4 '~bis- (sodium disulfonate styryl) biphenyl continue stirring 30 minutes, complete activation modification processing;
Step 4: modified calcium carbonate serosity successively to be carried out to filters pressing, drying, crushing to get brightening winnofil.
As a preferred technical solution, in the step 4, after calcium carbonate serosity carries out filters pressing, drying, crushing, using It is classified process.
The winnofil being prepared as a preferred technical solution, is nanometer grade calcium carbonate, the nanoscale The specific surface area of calcium carbonate is 16~30m2/g。
The winnofil being prepared as a preferred technical solution, is micron grade light-weight calcium carbonate, described micro- The settling volume of meter level precipitated calcium carbonate is 2.0~3.2ml/g.
As a preferred technical solution, the reducing agent be one of sodium hydrosulfite, sodium pyrosulfite, thiourea dioxide or Any several combinations.
As improvement to above-mentioned technical proposal, the dosage of the reducing agent is the 0.2 of raw material calcium carbonate butt quality ~0.5%;
The dosage of the sodium isoascorbate is the 0.1~0.3% of raw material calcium carbonate butt quality;
The dosage of ten diester of maleic acid list is the 0.5~2.0% of raw material calcium carbonate butt quality;
The dosage of the odium stearate is the 0.3~1.5% of raw material calcium carbonate butt quality;
The dosage of 4,4 '-bis- (sodium disulfonate styryl) biphenyl be raw material calcium carbonate butt quality 0.1~ 0.5%.
By adopting the above-described technical solution, the beneficial effects of the present invention are: using precipitating is brightened made from above-mentioned technique Calcium carbonate production PVC plastic product has the advantage that compared with calcium carbonate common in the market
1, there is good workability, excellent in mechanical performance good with polyvinyl chloride resin compatibility in PVC plastic processing;
2, there is good brightening effect to white PVC product, glossiness is good;
3, color difference fluctuates small, stable product quality in PVC product production process;
4, present invention process is simple and effective, and cost of investment is low, has preferable economic benefit and social benefit.
Specific embodiment
Below with reference to embodiment, the present invention is further explained.In the following detailed description, it is only retouched by way of explanation Certain exemplary embodiments of the invention are stated.Undoubtedly, those skilled in the art will recognize, without departing from In the case where the spirit and scope of the present invention, the described embodiments may be modified in various different ways.Therefore, Description is regarded as illustrative in nature, and is not intended to limit the scope of the claims.
The invention discloses a kind of PVC plastic preparation methods for brightening winnofil, comprising the following steps:
Step 1:, when carbonation rate reaches 60~80%, reducing agent is added in the carbonation process for preparing winnofil And sodium isoascorbate, continue carbonization to pH less than 7.0;
Step 2: the calcium carbonate serosity that carbonization is completed is delivered to aging tank, and keep calcium carbonate serosity quiet in aging tank Ageing 12~for 24 hours is set, supernatant liquor is then transported to Sewage treatment pond with dredge pump and is handled;
Step 3: opening the agitating device of aging tank, the calcium carbonate serosity after ageing concentration is stirred evenly, is then conveyed To activation kettle, activation kettle is made to be warming up to 70~90 DEG C, ten diester of maleic acid list is added, stirred 20~40 minutes, then add Odium stearate and 4,4 '~bis- (sodium disulfonate styryl) biphenyl, continues stirring 20~40 minutes, completes activation modification processing;
Step 4: modified calcium carbonate serosity successively to be carried out to filters pressing, drying, crushing to get brightening winnofil.
The reducing agent in the present embodiment is one of sodium hydrosulfite, sodium pyrosulfite, thiourea dioxide or any several Kind combination, and said components, when being applied in combination, constituent content can be adjusted arbitrarily.
The dosage of heretofore described reducing agent is the 0.2~0.5% of raw material calcium carbonate butt quality;It is described different anti-bad The dosage of hematic acid sodium is the 0.1~0.3% of raw material calcium carbonate butt quality;The dosage of ten diester of maleic acid list is former material Expect the 0.5~2.0% of calcium carbonate butt quality;The dosage of the odium stearate be raw material calcium carbonate butt quality 0.3~ 1.5%;The dosage of 4,4 '-bis- (sodium disulfonate styryl) biphenyl be raw material calcium carbonate butt quality 0.1~ 0.5%.
Below by specific embodiment, the present invention is described in detail.
Embodiment one:
The present embodiment is to prepare micron grade light-weight calcium carbonate carbon, it is specific the preparation method comprises the following steps:
Step 1:, when carbonation rate reaches 70%, the two of 0.3% are added in the carbonation process for preparing winnofil Aminoiminomethanesulfonic acid and 0.1% sodium isoascorbate, continue carbonization to pH be 6.8 when complete reaction, be made product settling volume It is 2.6;
Step 2: the calcium carbonate serosity that carbonization is completed is delivered to aging tank, and keep calcium carbonate serosity quiet in aging tank Ageing 18h is set, supernatant liquor is then transported to Sewage treatment pond with dredge pump and is handled;
Step 3: opening the agitating device of aging tank, the calcium carbonate serosity after ageing concentration is stirred evenly, is then conveyed To activation kettle, the heating function of activation kettle is opened, activation kettle is made to be warming up to 85 DEG C, 0.6% ten diester of maleic acid list is added, stirs It mixes 30 minutes, then adds 0.4% odium stearate and the 4 of 0.3%, 4 '~bis- (sodium disulfonate styryl) biphenyl, after Activation modification processing is completed in continuous stirring 30 minutes;
Step 4: modified calcium carbonate serosity successively to be carried out to filters pressing, drying, crushing are brightened to get PVC plastic is dedicated Winnofil.
Embodiment two:
The present embodiment is to prepare micron grade light-weight calcium carbonate carbon, it is specific the preparation method comprises the following steps:
Step 1: in the carbonation process for preparing winnofil, when carbonation rate reaches 70%, be added 0.2% also Former agent and 0.2% sodium isoascorbate, continue carbonization to pH be 6.8 when complete reaction, be made product settling volume be 3.0;
Step 2: the calcium carbonate serosity that carbonization is completed is delivered to aging tank, and keep calcium carbonate serosity quiet in aging tank Ageing 18h is set, supernatant liquor is then transported to Sewage treatment pond with dredge pump and is handled;
Step 3: opening the agitating device of aging tank, the calcium carbonate serosity after ageing concentration is stirred evenly, is then conveyed To activation kettle, the heating function of activation kettle is opened, activation kettle is made to be warming up to 85 DEG C, 0.8% ten diester of maleic acid list is added, stirs It mixes 30 minutes, then adds 0.3% odium stearate and the 4 of 0.2%, 4 '~bis- (sodium disulfonate styryl) biphenyl, after Activation modification processing is completed in continuous stirring 30 minutes;
Step 4: modified calcium carbonate serosity successively to be carried out to filters pressing, drying, crushing are brightened to get PVC plastic is dedicated Winnofil.
Embodiment three:
The present embodiment is to prepare nanometer grade calcium carbonate, it is specific the preparation method comprises the following steps:
Step 1:, when carbonation rate reaches 60%, the two of 0.5% are added in the carbonation process for preparing winnofil Aminoiminomethanesulfonic acid and 0.2% sodium isoascorbate, continue carbonization to pH be 6.8 when complete reaction, the ratio table of nanometer grade calcium carbonate Area is 18.9m2/g;
Step 2: the calcium carbonate serosity that carbonization is completed is delivered to aging tank, and keep calcium carbonate serosity quiet in aging tank It sets ageing for 24 hours, supernatant liquor is then transported to Sewage treatment pond with dredge pump and is handled;
Step 3: opening the agitating device of aging tank, the calcium carbonate serosity after ageing concentration is stirred evenly, is then conveyed To activation kettle, the heating function of activation kettle is opened, activation kettle is made to be warming up to 85 DEG C, 1.5% ten diester of maleic acid list is added, stirs It mixes 30 minutes, then adds 0.6% odium stearate and the 4 of 0.5%, 4 '~bis- (sodium disulfonate styryl) biphenyl, after Activation modification processing is completed in continuous stirring 30 minutes;
Step 4: modified calcium carbonate serosity successively to be carried out to filters pressing, drying, crushing are brightened to get PVC plastic is dedicated Winnofil.
Example IV:
The present embodiment is to prepare nanometer grade calcium carbonate, it is specific the preparation method comprises the following steps:
Step 1:, when carbonation rate reaches 60%, the two of 0.4% are added in the carbonation process for preparing winnofil Aminoiminomethanesulfonic acid and 0.2% sodium isoascorbate, continue carbonization to pH be 6.8 when complete reaction, the ratio table of nanometer grade calcium carbonate Area is 23.4m2/g;
Step 2: the calcium carbonate serosity that carbonization is completed is delivered to aging tank, and keep calcium carbonate serosity quiet in aging tank It sets ageing for 24 hours, supernatant liquor is then transported to Sewage treatment pond with dredge pump and is handled;
Step 3: opening the agitating device of aging tank, the calcium carbonate serosity after ageing concentration is stirred evenly, is then conveyed To activation kettle, the heating function of activation kettle is opened, activation kettle is made to be warming up to 85 DEG C, 1.5% ten diester of maleic acid list is added, stirs It mixes 30 minutes, then adds 1% odium stearate and the 4 of 0.5%, 4 '~bis- (sodium disulfonate styryl) biphenyl continue Activation modification processing is completed in stirring 30 minutes;
Step 4: modified calcium carbonate serosity successively to be carried out to filters pressing, drying, crushing are brightened to get PVC plastic is dedicated Winnofil.
The present invention in the course of the research, additionally uses other components to calcium carbonate serosity into activation modification processing is carried out, such as Sodium isoascorbate is replaced using EDETATE SODIUM, two comparative examples and various embodiments of the present invention is now taken to carry out test data comparison Explanation.
Comparative example 1:
Replace sodium isoascorbate to prepare micron grade light-weight calcium carbonate carbon using EDETATE SODIUM, it is specific the preparation method comprises the following steps:
Referring to the manufacturing condition of embodiment one, the micron order light calcium carbonate serosity that settling volume is 2.6 is prepared, so 0.3% thiourea dioxide and 0.1% EDETATE SODIUM are added afterwards, stirs 30 minutes;Then be added 1.3% odium stearate into Row is activated, and activation time is 30 minutes;Again by the defeated successively progress filters pressing of modified slurries, drying, classification to get heavy to brightening Shallow lake calcium carbonate product.
Comparative example 2:
Referring to the manufacturing condition of example IV, preparation specific surface area is 23m2The nanometer calcium carbonate slurries of/g or so, Then 0.4% thiourea dioxide and 0.2% EDETATE SODIUM is added, stirs 30 minutes;Then 3.3% odium stearate is added It is activated, activation time is 30 minutes;It is again that the defeated successively progress filters pressing of modified slurries, drying, classification is heavy to get brightening Shallow lake calcium carbonate product.
Winnofil product will be brightened made from above four embodiments and two comparative examples to be formulated according to table -1 respectively Prepare hard PVC product.
Table -1
Raw material title Mass fraction/part
PVC 100
Calcium-zinc composite stabilizing agent 5.0
ACR 2.0
CPE 8.0
Paraffin 0.5
Stearic acid 0.3
Monoglyceride 0.3
Calcium carbonate 50
Table -2 is to carry out Mechanics Performance Testing to hard PVC referring to GB1040-79 and GB1043-79 standard, as a result As shown in table -2:
Table -2
The results show that using winnofil prepared by the present invention, either micron grade light-weight calcium carbonate or nanoscale Calcium carbonate brightens calcium carbonate compared to conventional method preparation, in PVC plastic application, not only has preferable mechanical property, And color difference b* value is smaller, is conducive to the PVC for preparing white article.
It is described to receive when the winnofil being prepared is nanometer grade calcium carbonate in each embodiment of the invention The specific surface area of meter level calcium carbonate is 16~30m2/g.The winnofil being prepared is micron grade light-weight calcium carbonate When, the settling volume of the micron grade light-weight calcium carbonate is 2.0~3.2ml/g.
The present invention is and common in the market using brightening winnofil production PVC plastic product made from above-mentioned technique Calcium carbonate is compared, and is had the advantage that
1, there is good workability, excellent in mechanical performance good with polyvinyl chloride resin compatibility in PVC plastic processing;
2, there is good brightening effect to white PVC product, glossiness is good;
3, color difference fluctuates small, stable product quality in PVC product production process;
4, present invention process is simple and effective, and cost of investment is low, has preferable economic benefit and social benefit.The above display With describe basic principles and main features and advantages of the present invention of the invention.It should be understood by those skilled in the art that this hair Bright to be not restricted to the described embodiments, the above embodiments and description only illustrate the principle of the present invention, is not taking off Under the premise of from spirit and scope of the invention, various changes and improvements may be made to the invention, these changes and improvements, which are both fallen within, to be wanted It asks in the scope of the invention of protection.The scope of the present invention is defined by the appended claims and its equivalents.

Claims (7)

1. a kind of PVC plastic preparation method for brightening winnofil, which comprises the following steps:
Step 1: in the carbonation process for preparing winnofil, when carbonation rate reaches 60~80%, reducing agent and different is added Sodium ascorbate continues carbonization to pH less than 7.0;
Step 2: the calcium carbonate serosity that carbonization is completed is delivered to aging tank, and it is old to stand calcium carbonate serosity in aging tank Change 12~for 24 hours, supernatant liquor is then transported to Sewage treatment pond with dredge pump and is handled;
Step 3: opening the agitating device of aging tank, the calcium carbonate serosity after ageing concentration is stirred evenly, work is then sent to Change kettle, activation kettle is made to be warming up to 70~90 DEG C, ten diester of maleic acid list is added, stirs 20~40 minutes, then add tristearin Sour sodium and 4,4 '~bis- (sodium disulfonate styryl) biphenyl, continues stirring 20~40 minutes, completes activation modification processing;
Step 4: modified calcium carbonate serosity successively to be carried out to filters pressing, drying, crushing to get brightening winnofil.
2. a kind of PVC plastic preparation method for brightening winnofil as described in claim 1, which is characterized in that including Following steps:
Step 1: in the carbonation process for preparing winnofil, when carbonation rate reaches 70%, reducing agent and different anti-bad is added Hematic acid sodium, continuing to be carbonized to pH is 6.8;
Step 2: the calcium carbonate serosity that carbonization is completed is delivered to aging tank, and it is old to stand calcium carbonate serosity in aging tank Change 18h, supernatant liquor is then transported to Sewage treatment pond with dredge pump and is handled;
Step 3: opening the agitating device of aging tank, the calcium carbonate serosity after ageing concentration is stirred evenly, work is then sent to Change kettle, activation kettle made to be warming up to 85 DEG C, ten diester of maleic acid list is added, stirs 30 minutes, then add odium stearate and 4, 4 '~bis- (sodium disulfonate styryl) biphenyl continue stirring 30 minutes, complete activation modification processing;
Step 4: modified calcium carbonate serosity successively to be carried out to filters pressing, drying, crushing to get brightening winnofil.
3. a kind of PVC plastic preparation method for brightening winnofil as claimed in claim 1 or 2, which is characterized in that institute It states in step 4, after calcium carbonate serosity carries out filters pressing, drying, crushing, using classification process.
4. a kind of PVC plastic preparation method for brightening winnofil as claimed in claim 1 or 2, which is characterized in that system The standby obtained winnofil is nanometer grade calcium carbonate, and the specific surface area of the nanometer grade calcium carbonate is 16~30m2/g。
5. a kind of PVC plastic preparation method for brightening winnofil as claimed in claim 1 or 2, which is characterized in that system The standby obtained winnofil is micron grade light-weight calcium carbonate, and the settling volume of the micron grade light-weight calcium carbonate is 2.0 ~3.2ml/g.
6. a kind of PVC plastic preparation method for brightening winnofil as claimed in claim 1 or 2, which is characterized in that institute Stating reducing agent is one of sodium hydrosulfite, sodium pyrosulfite, thiourea dioxide or any two or more combination.
7. a kind of PVC plastic preparation method for brightening winnofil as claimed in claim 1 or 2, which is characterized in that institute The dosage for stating reducing agent is the 0.2~0.5% of raw material calcium carbonate butt quality;
The dosage of the sodium isoascorbate is the 0.1~0.3% of raw material calcium carbonate butt quality;
The dosage of ten diester of maleic acid list is the 0.5~2.0% of raw material calcium carbonate butt quality;
The dosage of the odium stearate is the 0.3~1.5% of raw material calcium carbonate butt quality;
The dosage of 4,4 '-bis- (sodium disulfonate styryl) biphenyl be raw material calcium carbonate butt quality 0.1~ 0.5%.
CN201711259322.8A 2017-12-04 2017-12-04 A kind of PVC plastic preparation method for brightening winnofil Active CN108003383B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201711259322.8A CN108003383B (en) 2017-12-04 2017-12-04 A kind of PVC plastic preparation method for brightening winnofil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201711259322.8A CN108003383B (en) 2017-12-04 2017-12-04 A kind of PVC plastic preparation method for brightening winnofil

Publications (2)

Publication Number Publication Date
CN108003383A CN108003383A (en) 2018-05-08
CN108003383B true CN108003383B (en) 2019-06-25

Family

ID=62056131

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201711259322.8A Active CN108003383B (en) 2017-12-04 2017-12-04 A kind of PVC plastic preparation method for brightening winnofil

Country Status (1)

Country Link
CN (1) CN108003383B (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102154926A (en) * 2010-12-09 2011-08-17 山东轻工业学院 Method for improving whiteness of paper
CN103370383A (en) * 2011-02-18 2013-10-23 瓦克化学公司 Paper coating compositions

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102154926A (en) * 2010-12-09 2011-08-17 山东轻工业学院 Method for improving whiteness of paper
CN103370383A (en) * 2011-02-18 2013-10-23 瓦克化学公司 Paper coating compositions

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
轻质碳酸钙增白研究;胡庆福 等;《非金属矿》;20021130;第10-12页

Also Published As

Publication number Publication date
CN108003383A (en) 2018-05-08

Similar Documents

Publication Publication Date Title
TWI545085B (en) Production of high purity precipitated calcium carbonate
CN109796632A (en) A kind of preparation method of the high white winnofil of core-shell structure
CN109650431A (en) A kind of preparation method of MS glue nanometer calcium carbonate
WO2020010689A1 (en) Preparation method for nanoprecipitated calcium carbonate having core-shell structure
CN106928753A (en) A kind of preparation method for PVC automobile chassis stone-impact-proof paint modified calcium carbonates
CN110372024A (en) A kind of preparation method of plastics submicron order rice particle shape calcium carbonate
CN108069452B (en) Preparation method of chain calcite type calcium carbonate
CN107416884A (en) A kind of production method of high-quality superfine light calcium carbonate
CN1641100A (en) Method for recovering superfine calcium carbonate by clean causticization of green liquor
CN111137911A (en) Method for preparing high-purity superfine aluminum hydroxide flame retardant by decomposition method
CN108003383B (en) A kind of PVC plastic preparation method for brightening winnofil
CN1249176C (en) Method for purifying and whitening calcium carbonate
CN1200049C (en) Method for preparing high-white ness nano calcium carbide
CN1386710A (en) Process for preparing superfine iron oxide
CN113697831A (en) Method for purifying and removing magnesium from industrial wastewater with high sodium-magnesium ratio and preparing magnesium hydroxide fire retardant
CN109467112A (en) A kind of aragonitic seed and aragonitic precipitated calcium carbonate and preparation method thereof
CN1408666A (en) process for producing magnesium oxide from waste magnesite ore
CN108085740A (en) A kind of preparation method of anhydrous calcium sulfate whisker
CN107445188A (en) A kind of preparation method of rod-like precipitates calcium carbonate
JP2004238232A (en) Method for producing calcium carbonate
CN110697754A (en) Method for preparing industrial precipitated calcium carbonate by recycling nano calcium carbonate filter pressing water
CN106350870A (en) Disposal and utilization method for sulfuric acid waste liquid
CN110395748A (en) The method that lithium carbonate causticizing process prepares lithium hydroxide
KR101232633B1 (en) The synthesis method of in-situ precipitated calcium carbonate(pcc) for improving the quality of old corrugated container(occ)
JP5021344B2 (en) Method for concentrating light calcium carbonate

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
PE01 Entry into force of the registration of the contract for pledge of patent right
PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of invention: A preparation method of whitening precipitated calcium carbonate for PVC plastics

Effective date of registration: 20201130

Granted publication date: 20190625

Pledgee: Qingzhou Jinding sub branch of Weifang Bank Co.,Ltd.

Pledgor: QINGZHOU YUXIN CALCIUM INDUSTRIAL Co.,Ltd.

Registration number: Y2020980008603

PC01 Cancellation of the registration of the contract for pledge of patent right
PC01 Cancellation of the registration of the contract for pledge of patent right

Date of cancellation: 20220915

Granted publication date: 20190625

Pledgee: Qingzhou Jinding sub branch of Weifang Bank Co.,Ltd.

Pledgor: QINGZHOU YUXIN CALCIUM INDUSTRIAL CO.,LTD.

Registration number: Y2020980008603

TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20221213

Address after: 262503 Dianzi Industrial Park, Miaozi Town, Weifang City, Shandong Province

Patentee after: Shandong Yuxin Nano Technology Co.,Ltd.

Address before: 262503 nanzhudian village, Miaozi Town, Qingzhou City, Weifang City, Shandong Province

Patentee before: QINGZHOU YUXIN CALCIUM INDUSTRIAL CO.,LTD.