CN104910544A - Polyvinyl chloride (PVC) multipurpose inner lubricant - Google Patents
Polyvinyl chloride (PVC) multipurpose inner lubricant Download PDFInfo
- Publication number
- CN104910544A CN104910544A CN201510242676.6A CN201510242676A CN104910544A CN 104910544 A CN104910544 A CN 104910544A CN 201510242676 A CN201510242676 A CN 201510242676A CN 104910544 A CN104910544 A CN 104910544A
- Authority
- CN
- China
- Prior art keywords
- pvc
- polyvinyl chloride
- omnipotent
- higher alcohols
- internal lubricant
- 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
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L27/00—Compositions 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
- C08L27/02—Compositions 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
- C08L27/04—Compositions 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
- C08L27/06—Homopolymers or copolymers of vinyl chloride
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K13/00—Use of mixtures of ingredients not covered by one single of the preceding main groups, each of these compounds being essential
- C08K13/02—Organic and inorganic ingredients
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/16—Halogen-containing compounds
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/32—Phosphorus-containing compounds
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/04—Oxygen-containing compounds
- C08K5/05—Alcohols; Metal alcoholates
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/04—Oxygen-containing compounds
- C08K5/15—Heterocyclic compounds having oxygen in the ring
- C08K5/151—Heterocyclic compounds having oxygen in the ring having one oxygen atom in the ring
- C08K5/1535—Five-membered rings
- C08K5/1539—Cyclic anhydrides
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K2201/00—Specific properties of additives
- C08K2201/014—Additives containing two or more different additives of the same subgroup in C08K
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2201/00—Properties
- C08L2201/08—Stabilised against heat, light or radiation or oxydation
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
The invention discloses a polyvinyl chloride (PVC) multipurpose inner lubricant. The multipurpose inner lubricant comprises high alcohols, catalysts, color modifiers and phthalic anhydride. The high alcohols are composed of octadecanol and hexadecanol. The feeding weight ratio of the high alcohols and phthalic anhydride is 3.54-3.9:1. Compared with the prior art, the multipurpose inner lubricant has characteristics of speeding fusion, lowering the fusion viscosity, prolonging the processing life, improving fluidity, raising transparency and the like. The multipurpose inner lubricant has excellent compatibility with polyvinyl chloride, thus hard and soft PVC products achieve excellent thermal stability and transparency, safety, non-poison and environmental protection are achieved, and the multipurpose inner lubricant can be used in cooperation with stable systems of organic tin, calcium/zinc, barium/cadmium and lead salt and the like, has supper additive effect effects and raises the combination properties.
Description
Technical field
The present invention relates to igelite processing technique field, be specifically related to a kind of polyvinyl chloride (PVC) omnipotent internal lubricant.
Background technology
Lubricant is the important auxiliary agent of the class in plastic working, and can be described as is plastic working " catalyzer ".At present, in PVC plastic processing, ester lubricant range of product is less, and the leeway of selection is little, and product performance technology content is not high, and the lubricity of lubricant is not ideal enough.Also there is no or seldom have simultaneously inside and outside oilness, stability, the appearance of synergitic ester lubricant now in this field.PVC plastic processing enterprise in the urgent need to high-quality lubricant product, with the satisfied market requirement of producing high-grade plastics.
Summary of the invention
The object of the invention is to: for the above-mentioned technical problem existed in prior art, a kind of polyvinyl chloride (PVC) omnipotent internal lubricant is provided.
The present invention is achieved by the following technical solutions:
Polyvinyl chloride (PVC) omnipotent internal lubricant, comprise higher alcohols, catalyzer, modification of colour agent and phthalic anhydride, described higher alcohols are made up of stearyl alcohol and hexadecanol, and described higher alcohols are 3.54-3.9: 1 with the charged material weight ratio of phthalic anhydride.
As preferably, described catalyzer is tin protochloride, and with total charging capacity for benchmark, described catalyzer is pressed 0.2-0.3% and added.
As preferably, described modification of colour agent is inferior sodium phosphate, and the charging capacity of described modification of colour agent is the 0.05-0.1% of higher alcohols charging capacity.
The manufacture method of above-mentioned polyvinyl chloride (PVC) omnipotent internal lubricant, comprises the steps:
S1, the vacuum produced by vacuum pump successively by surge tank one and surge tank two, then cools in arrival reactor by surge tank two through prolong;
S2, under vacuum condition protection, higher alcohols, phthalic anhydride, catalyzer and modification of colour agent are put into reaction tower according to above-mentioned weight proportion, in control tower, temperature is at 210-240 DEG C, reaction times is from reaching temperature of reaction (namely 210 DEG C time meter), be as the criterion for < 3mgkoh/g to control sampling acid number, be generally 8 hours;
S3, the work in-process that step S2 is produced, then after scraping machine, pulverizer processing, be packaged into finished product, warehouse-in.
Wherein, the temperature of reaction in described step S2 controls when 210-225 DEG C, and effect is best.
In sum, owing to have employed technique scheme, the invention has the beneficial effects as follows:
Compared with prior art, the present invention has acceleration melting, reduces melting viscosity, extends the processing life-span, improves liquidity and improve the features such as the transparency, itself and polyvinyl chloride have fabulous consistency to give thermostability and the transparency of hard and flexible PVC goods excellence, safety non-toxic environmental protection, and can coordinate to use with organic tin, calcium/zinc class, barium/stabilising system such as cadmium class and lead salts, there is super additive effect and improve over-all properties.
Accompanying drawing explanation
Examples of the present invention will be described by way of reference to the accompanying drawings, wherein:
Fig. 1 is preparation facilities structural representation of the present invention;
Mark in figure: 1-reactor, 2-prolong, 3-surge tank one, 4-surge tank two, 5-vacuum pump, 6-scraping machine, 7-pulverizer.
Embodiment
All features disclosed in this specification sheets, or the step in disclosed all methods or process, except mutually exclusive feature and (or) step, all can combine by any way.
Arbitrary feature disclosed in this specification sheets (comprising any accessory claim, summary and accompanying drawing), unless specifically stated otherwise, all can be replaced by other equivalences or the alternative features with similar object.That is, unless specifically stated otherwise, each feature is an example in a series of equivalence or similar characteristics.
Polyvinyl chloride (PVC) omnipotent internal lubricant, comprise higher alcohols, catalyzer, modification of colour agent and phthalic anhydride, described higher alcohols are made up of stearyl alcohol and hexadecanol, and described higher alcohols are 3.54-3.9: 1 with the charged material weight ratio of phthalic anhydride.
The proportioning calculation of parameter of above-mentioned higher alcohols and phthalic anhydride is as follows:
1, higher alcohols are made up of stearyl alcohol and hexadecanol, and its molecular-weight average is:
270 (C
18alcohol molecular weight) * 70%+242 (C
16alcohol molecular weight) * 30%=262
2, the calculating of stoichiometric
Calculate often to criticize 500kg higher alcohols gauge, the theoretical charging capacity of its phthalic anhydride is:
(148*500)/(2*262)＝141(kg)
The feed ratio of higher alcohols and phthalic anhydride is 3.54: 1 (weight)
3, the calculating of actual proportioning
Owing to considering the volatilization loss under hexadecanol and stearyl alcohol high temperature, the proportional quantity of general higher alcohols should suitably increase, and experimentally document is advisable with excessive 0.1-0.2mol.
(1), during the excessive 0.1mol of higher alcohols, throw 500kg higher alcohols, should throw phthalic anhydride amount is:
(148*500)/(2.1*262)＝134.5kg
Namely the ratio of components of higher alcohols and phthalic anhydride is 3.71: 1 (weight)
(2), during the excessive 0.2mol of higher alcohols, throw 500kg higher alcohols and should throw phthalic anhydride amount and be:
(148*500)/(2.2*262)＝128.3kg
Namely the ratio of components of higher alcohols and phthalic anhydride is 3.9: 1 (weight)
In the present invention, described catalyzer is tin protochloride, and with total charging capacity for benchmark, described catalyzer is pressed 0.2-0.3% and added, and described modification of colour agent is inferior sodium phosphate, and the charging capacity of described modification of colour agent is the 0.05-0.1% of higher alcohols charging capacity.
The manufacture method of above-mentioned polyvinyl chloride (PVC) omnipotent internal lubricant, comprises the steps:
S1, the vacuum produced by vacuum pump successively by surge tank one and surge tank two, then cools in arrival reactor by surge tank two through prolong;
S2, under vacuum condition protection, higher alcohols, phthalic anhydride, catalyzer and modification of colour agent are put into reaction tower according to above-mentioned weight proportion, in control tower, temperature is at 210-240 DEG C, and wherein, temperature of reaction controls when 210-225 DEG C, effect is best, reaction times, from reaching temperature of reaction (namely 210 DEG C time meter), is as the criterion for < 3mgkoh/g to control sampling acid number, is generally 8 hours;
S3, the work in-process that step S2 is produced, then after scraping machine, pulverizer processing, be packaged into finished product, warehouse-in.
As shown in Figure 1, the manufacturing installation of polyvinyl chloride (PVC) omnipotent internal lubricant, comprise reactor, prolong, surge tank one, surge tank two, vacuum pump, scraping machine and pulverizer, the upper end of described reactor connects prolong, prolong connects surge tank one by pipeline, surge tank one connects surge tank two by pipeline, and surge tank two-way piping connects vacuum pump, and vacuum pump is provided with venting port; The lower end of described reactor connects scraping machine, between reactor and scraping machine, be provided with valve, and scraping machine connects pulverizer.Wherein, described reactor, surge tank one and surge tank two are equipped with vacuum meter, surge tank two is also provided with blow-off valve, described prolong has water-in and water outlet.
The present invention can be used in the techniques such as PVC rolls, extrudes, molding, and effectively reduce melt viscosity, continuous high temperature lubricates, and enhances productivity, and reduces energy consumption cost.
Above-described specific embodiment, further describes object of the present invention, technical scheme and beneficial effect, and institute it should be understood that and the foregoing is only specific embodiments of the invention, is not limited to the present invention.The present invention expands to any new feature of disclosing in this manual or any combination newly, and the step of the arbitrary new method disclosed or process or any combination newly.
Claims (7)
1. polyvinyl chloride (PVC) omnipotent internal lubricant, is characterized in that, comprise higher alcohols, catalyzer, modification of colour agent and phthalic anhydride, described higher alcohols are made up of stearyl alcohol and hexadecanol, and described higher alcohols are 3.54-3.9: 1 with the charged material weight ratio of phthalic anhydride.
2. polyvinyl chloride according to claim 1 (PVC) omnipotent internal lubricant, is characterized in that, described catalyzer is tin protochloride.
3. polyvinyl chloride according to claim 1 (PVC) omnipotent internal lubricant, is characterized in that, described modification of colour agent is inferior sodium phosphate.
4. polyvinyl chloride according to claim 1 and 2 (PVC) omnipotent internal lubricant, is characterized in that, with total charging capacity for benchmark, described catalyzer is pressed 0.2-0.3% and added.
5. polyvinyl chloride (PVC) the omnipotent internal lubricant according to claim 1 or 3, is characterized in that, the charging capacity of described modification of colour agent is the 0.05-0.1% of higher alcohols charging capacity.
6. the manufacture method of polyvinyl chloride according to claim 1 (PVC) omnipotent internal lubricant, is characterized in that, comprise the steps:
S1, the vacuum produced by vacuum pump successively by surge tank one and surge tank two, then cools in arrival reactor by surge tank two through prolong;
S2, under vacuum condition protection, higher alcohols, phthalic anhydride, catalyzer and modification of colour agent are put into reaction tower according to above-mentioned weight proportion, in control tower, temperature is at 210-240 DEG C, reaction times is from reaching temperature of reaction (namely 210 DEG C time meter), be as the criterion for < 3mgkoh/g to control sampling acid number, be generally 8 hours;
S3, the work in-process that step S2 is produced, then after scraping machine, pulverizer processing, be packaged into finished product, warehouse-in.
7. the manufacture method of polyvinyl chloride according to claim 6 (PVC) omnipotent internal lubricant, is characterized in that, the temperature of reaction in described step S2 controls when 210-225 DEG C, and effect is best.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510242676.6A CN104910544A (en) | 2015-05-07 | 2015-05-07 | Polyvinyl chloride (PVC) multipurpose inner lubricant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510242676.6A CN104910544A (en) | 2015-05-07 | 2015-05-07 | Polyvinyl chloride (PVC) multipurpose inner lubricant |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN104910544A true CN104910544A (en) | 2015-09-16 |
Family
ID=54080018
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510242676.6A Pending CN104910544A (en) | 2015-05-07 | 2015-05-07 | Polyvinyl chloride (PVC) multipurpose inner lubricant |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104910544A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105968628A (en) * | 2016-05-23 | 2016-09-28 | 张进 | PVC (Polyvinyl Chloride) lubricant and preparation method thereof |
| CN106009366A (en) * | 2016-05-23 | 2016-10-12 | 张进 | High-transmittance PVC (Polyvinyl Chloride) lubricant and preparation method thereof |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1749235A (en) * | 2005-10-13 | 2006-03-22 | 华南理工大学 | Synthetic method for dioctadecyl phthalate |
| CN1785956A (en) * | 2005-10-13 | 2006-06-14 | 华南理工大学 | Synthesis method of dehexadecyl phthalate |
| CN101130608A (en) * | 2007-09-28 | 2008-02-27 | 厦门大学 | Dibasic acid monoester rare earth used for PVC stabilizing agent and method for preparing the same |
| US20100087350A1 (en) * | 2007-04-09 | 2010-04-08 | Sonnenschein Mark F | Capped polyester polyol lubricant composition |
| US20110312864A1 (en) * | 2009-01-08 | 2011-12-22 | Godwin Allen D | Processes Relating To Alcohols For The Production Of Esters |
-
2015
- 2015-05-07 CN CN201510242676.6A patent/CN104910544A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1749235A (en) * | 2005-10-13 | 2006-03-22 | 华南理工大学 | Synthetic method for dioctadecyl phthalate |
| CN1785956A (en) * | 2005-10-13 | 2006-06-14 | 华南理工大学 | Synthesis method of dehexadecyl phthalate |
| US20100087350A1 (en) * | 2007-04-09 | 2010-04-08 | Sonnenschein Mark F | Capped polyester polyol lubricant composition |
| CN101130608A (en) * | 2007-09-28 | 2008-02-27 | 厦门大学 | Dibasic acid monoester rare earth used for PVC stabilizing agent and method for preparing the same |
| US20110312864A1 (en) * | 2009-01-08 | 2011-12-22 | Godwin Allen D | Processes Relating To Alcohols For The Production Of Esters |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105968628A (en) * | 2016-05-23 | 2016-09-28 | 张进 | PVC (Polyvinyl Chloride) lubricant and preparation method thereof |
| CN106009366A (en) * | 2016-05-23 | 2016-10-12 | 张进 | High-transmittance PVC (Polyvinyl Chloride) lubricant and preparation method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105482218B (en) | A kind of composite thermal stabilizer production technology using cyanuric acid zinc calcium as matrix | |
| CN102702644B (en) | Cold bending electrical protective casing and manufacturing method thereof | |
| CN101914218A (en) | Powdered composite calcium zinc stabilizing agent and preparation method thereof | |
| CN102863711A (en) | Heat-resisting PVC high impact-resisting tubular product and preparation method thereof | |
| CN104845410B (en) | A kind of preparation and its application of plastic modifier | |
| CN107226967A (en) | Hidden pipe salt discharge modified PVC bellows | |
| CN104910544A (en) | Polyvinyl chloride (PVC) multipurpose inner lubricant | |
| CN102276892A (en) | Method for preparing polyethylene pipe resin | |
| CN102816392A (en) | Chlorinated polyvinyl chloride waterproof coiled material and preparation method thereof | |
| CN101831120B (en) | Compounding method for doping light rare-earth non-toxic heat stabilizer during processing polyvinyl chloride plastic | |
| CN102344623A (en) | Outdoor polymeric environment-friendly floor | |
| CN103328425B (en) | Process for preparing liquid overbased metal carboxylates, mixed metal stabilizers containing same, and stabilized halogen-containing polymers therewith | |
| CN104479246A (en) | Formula and preparation method of novel environment-friendly sectional materials | |
| CN102391544B (en) | Composite heat stabilizer and preparation method | |
| CN103739988A (en) | High-impact hydraulic-pressure-resistant PVC (polyvinyl chloride) irrigation pipe | |
| CN103694520B (en) | A kind of Non-phthalate nitrile rubber material and preparation method thereof | |
| CN103524851B (en) | A kind of underground coal mine feed pipe for mortar with flame-retardant and anti-static and preparation method thereof | |
| CN104962000A (en) | Preparation method for flame-retardant PVC-U drain pipe | |
| CN102051005A (en) | Flame-retardant polyvinyl chloride (PVC) plastic pipe | |
| CN103289257A (en) | Highly weather-resistant co-extruded material PVC (Poly Vinyl Chloride) section bar and production method thereof | |
| CN106117899A (en) | Porous grid type PVC/HDPE underground communication pipe and production method thereof | |
| CN104497422A (en) | Composition for enhancing dimensional stability of PPR pipe and preparation method thereof | |
| CN103012934A (en) | Polyethylene tube for mining and preparation method thereof | |
| CN102417679B (en) | External lubricant for polyvinyl chloride (PVC) resin forming and processing and production method thereof | |
| CN103951368A (en) | Sulfur-oxygen-magnesium slab and production method thereof |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| CB03 | Change of inventor or designer information |
Inventor after: Jie Hesheng Inventor after: Jie Hesheng Zhang Weijia Inventor before: Jie Hesheng |
|
| COR | Change of bibliographic data | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20150916 |