CN109503306B - Styrene rectification polymerization inhibitor and production method thereof - Google Patents

Styrene rectification polymerization inhibitor and production method thereof Download PDF

Info

Publication number
CN109503306B
CN109503306B CN201910011402.4A CN201910011402A CN109503306B CN 109503306 B CN109503306 B CN 109503306B CN 201910011402 A CN201910011402 A CN 201910011402A CN 109503306 B CN109503306 B CN 109503306B
Authority
CN
China
Prior art keywords
styrene
polymerization inhibitor
silicon dioxide
nano silicon
water
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
CN201910011402.4A
Other languages
Chinese (zh)
Other versions
CN109503306A (en
Inventor
范啸
范毅
樊纪利
张洁
邵至央
缪淼
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.)
Anhui Zhuoyuan Chemical Technology Co ltd
Original Assignee
Anhui Zhuoyuan Chemical Technology Co ltd
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 Anhui Zhuoyuan Chemical Technology Co ltd filed Critical Anhui Zhuoyuan Chemical Technology Co ltd
Priority to CN201910011402.4A priority Critical patent/CN109503306B/en
Publication of CN109503306A publication Critical patent/CN109503306A/en
Application granted granted Critical
Publication of CN109503306B publication Critical patent/CN109503306B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00Purification; Separation; Use of additives
    • C07C7/04Purification; Separation; Use of additives by distillation
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00Purification; Separation; Use of additives
    • C07C7/20Use of additives, e.g. for stabilisation

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Water Supply & Treatment (AREA)
  • Polymerisation Methods In General (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

The invention discloses a styrene rectification polymerization inhibitor and a production method thereof, wherein the styrene rectification polymerization inhibitor comprises the following components in percentage by weight: 25-55% of di-tert-butyl nitroxide free radical, 10-15% of ethanol, 3-8% of composite water-soluble dispersant, 0.5-1% of nano silicon dioxide loaded polyacrylamide and the balance of water. The styrene rectification polymerization inhibitor can effectively inhibit polymerization reaction of styrene and reduce catalytic activity of iron ions, thereby reducing external induction factors of polymerization of styrene monomers from the source, dispersing and cleaning polymerized parts, improving polymerization inhibition effect through various ways and greatly improving the operation stability of a rectification system.

Description

Styrene rectification polymerization inhibitor and production method thereof
Technical Field
The invention relates to the technical field of petrochemical industry, in particular to a styrene rectification polymerization inhibitor and a production method thereof.
Background
Styrene is an important basic organic chemical raw material, is mainly used for producing synthetic resins such as polystyrene and SBS, ion exchange resin, synthetic rubber and the like in industry, and has wide application. At present, the production of styrene mainly adopts an ethylbenzene dehydrogenation process, which is divided into a alkylation working section, an ethylbenzene rectification working section, an ethylbenzene dehydrogenation working section and a styrene rectification working section.
Styrene monomers have self-polymerizing properties and can be polymerized at room temperature, with higher temperatures and faster polymerization rates. Because a small amount of impurities exist in the dehydrogenation reaction liquid in the ethylbenzene dehydrogenation section, the dehydrogenation reaction liquid needs to be treated by a subsequent styrene rectification section. In the rectification process, styrene monomers are easy to polymerize, which not only affects normal production, but also increases energy consumption and even causes large-area production stop in severe cases. In order to reduce the polymerization loss of styrene monomers in the rectification process and ensure the normal operation of a rectification system, a polymerization inhibitor for inhibiting the polymerization of styrene must be added in the rectification process.
The polymerization of styrene is a free radical polymerization, and the influencing factors include monomer concentration, system temperature, impurities and the like. The existing styrene rectification polymerization inhibitor has the formula that single di-tert-butyl nitroxide radical (DTBNO) is dissolved in water in proportion, the components and the performance of the formula are single, the external inducing factor of styrene monomer polymerization cannot be reduced, the polymerization control effect is limited, and the improvement is needed.
Disclosure of Invention
The invention aims to make up the defects of the prior art and provides a styrene rectification polymerization inhibitor and a production method thereof.
The invention is realized by the following technical scheme:
a styrene rectification polymerization inhibitor comprises the following components in percentage by weight: 25-55% of di-tert-butyl nitroxide free radical, 10-15% of ethanol, 3-8% of composite water-soluble dispersant, 0.5-1% of nano silicon dioxide loaded polyacrylamide and the balance of water.
The composite water-soluble dispersant is prepared from 30D of alkali-modified sodium lignosulphonate, span S-40 and an anionic surfactant AEO-9 in a weight ratio of (3-5): (1-2): (1-2) mixing.
The preparation method of the nano silicon dioxide loaded polyacrylamide comprises the following steps: adding nano silicon dioxide into water, dispersing uniformly to obtain a nano silicon dioxide suspension with the solid content of 1-1.5%, then adding a proper amount of polyacrylamide aqueous solution with the mass fraction of 0.5-1%, stirring for 12-24h, centrifuging, and drying to obtain the nano silicon dioxide loaded polyacrylamide.
The volume ratio of the nano silicon dioxide suspension to the polyacrylamide aqueous solution is 1: (0.5-1).
The production method of the styrene rectification polymerization inhibitor comprises the following steps:
(1) adding the composite water-soluble dispersant and the nano-silica-loaded polyacrylamide into water, and uniformly stirring and dispersing to obtain a mixed solution;
(2) adding di-tert-butyl nitroxide free radical into ethanol, then uniformly mixing with the mixed solution, and filtering to remove impurities to obtain the product.
The invention has the advantages that:
on the basis of the formula of the conventional styrene rectification polymerization inhibitor, the composite water-soluble dispersing agent consisting of the alkali modified sodium lignosulfonate 30D, the span S-40 and the anionic surfactant AEO-9 is added, so that a good dispersion and cleaning effect can be achieved on a polymerized part under a high-temperature condition, and a good clean state in the styrene rectification process is kept; by adding the nano silicon dioxide loaded polyacrylamide, iron ions can be complexed, and the catalytic activity of the iron ions is reduced, so that the catalytic polymerization reaction participated by the iron ions is relieved. Through the compounding and synergism of the raw materials, the produced styrene rectification polymerization inhibitor can effectively inhibit the polymerization reaction of styrene and reduce the catalytic activity of iron ions, so that the external induction factor of polymerization of styrene monomers is reduced from the source, the polymerized parts are dispersed and cleaned, the polymerization inhibition effect is improved through various ways, and the operation stability of a rectification system is greatly improved.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention more apparent, the present invention is further described in detail with reference to the following embodiments. It should be understood that the specific embodiments described herein are merely illustrative of the invention and are not intended to limit the invention.
A styrene rectification polymerization inhibitor comprises the following components in percentage by weight: 25% of di-tert-butyl nitroxide free radical, 10% of ethanol, 3% of composite water-soluble dispersant, 0.5% of nano silicon dioxide loaded polyacrylamide and the balance of water.
The composite water-soluble dispersant is prepared from 30D alkali-modified sodium lignosulfonate, span S-40 and an anionic surfactant AEO-9 in a weight ratio of 3: 1: 1 are mixed.
The preparation method of the nano silicon dioxide loaded polyacrylamide comprises the following steps: adding nano silicon dioxide into water, dispersing uniformly to obtain a nano silicon dioxide suspension with the solid content of 1%, then adding a proper amount of polyacrylamide aqueous solution with the mass fraction of 0.5%, stirring for 12h, centrifuging, and drying to obtain the nano silicon dioxide loaded polyacrylamide.
The volume ratio of the nano silicon dioxide suspension to the polyacrylamide aqueous solution is 1: 0.5.
the production method of the styrene rectification polymerization inhibitor comprises the following steps:
(1) adding the composite water-soluble dispersant and the nano-silica-loaded polyacrylamide into water, and uniformly stirring and dispersing to obtain a mixed solution;
(2) adding di-tert-butyl nitroxide free radical into ethanol, then uniformly mixing with the mixed solution, and filtering to remove impurities to obtain the product.
100ppm of the polymerization inhibitor is added into 100g of styrene, oil bath treatment is carried out at 110 ℃ for 2h, the polymer is eluted by ethanol, the weight of the polymer is weighed after drying, and the weight of the polymer is 0.3 g.

Claims (3)

1. The styrene rectification polymerization inhibitor is characterized by comprising the following components in percentage by weight: 25-55% of di-tert-butyl nitroxide free radical, 10-15% of ethanol, 3-8% of composite water-soluble dispersant, 0.5-1% of nano silicon dioxide loaded polyacrylamide and the balance of water;
the preparation method of the nano silicon dioxide loaded polyacrylamide comprises the following steps: adding nano silicon dioxide into water, uniformly dispersing to obtain a nano silicon dioxide suspension with the solid content of 1-1.5%, then adding a proper amount of polyacrylamide aqueous solution with the mass fraction of 0.5-1%, stirring for 12-24h, centrifuging, and drying to obtain nano silicon dioxide loaded polyacrylamide;
the composite water-soluble dispersant is prepared from 30D of alkali-modified sodium lignosulphonate, span S-40 and an anionic surfactant AEO-9 in a weight ratio of (3-5): (1-2): (1-2) mixing.
2. The styrene rectification polymerization inhibitor according to claim 1, wherein the volume ratio of the nano silica suspension to the polyacrylamide aqueous solution is 1: (0.5-1).
3. The production method of a styrene rectification polymerization inhibitor as claimed in claim 1, characterized by comprising the steps of:
(1) adding the composite water-soluble dispersant and the nano-silica-loaded polyacrylamide into water, and uniformly stirring and dispersing to obtain a mixed solution;
(2) adding di-tert-butyl nitroxide free radical into ethanol, then uniformly mixing with the mixed solution, and filtering to remove impurities to obtain the product.
CN201910011402.4A 2019-01-07 2019-01-07 Styrene rectification polymerization inhibitor and production method thereof Active CN109503306B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201910011402.4A CN109503306B (en) 2019-01-07 2019-01-07 Styrene rectification polymerization inhibitor and production method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201910011402.4A CN109503306B (en) 2019-01-07 2019-01-07 Styrene rectification polymerization inhibitor and production method thereof

Publications (2)

Publication Number Publication Date
CN109503306A CN109503306A (en) 2019-03-22
CN109503306B true CN109503306B (en) 2021-06-11

Family

ID=65757378

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201910011402.4A Active CN109503306B (en) 2019-01-07 2019-01-07 Styrene rectification polymerization inhibitor and production method thereof

Country Status (1)

Country Link
CN (1) CN109503306B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110330404A (en) * 2019-07-02 2019-10-15 宜兴市中大凯水处理有限公司 A kind of polymerization inhibitors for styrene rectification and preparation method thereof

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103467230B (en) * 2013-07-24 2015-11-18 金浦新材料股份有限公司 A kind of Water-soluble styrene polymerization inhibitor
US9399622B2 (en) * 2013-12-03 2016-07-26 Ecolab Usa Inc. Nitroxide hydroxylamine and phenylenediamine combinations as polymerization inhibitors for ethylenically unsaturated monomer processes
CN104447182B (en) * 2014-12-05 2016-02-10 天津科技大学 Can Magneto separate solid phase stopper and preparation method thereof and application
CN108341737B (en) * 2017-01-23 2021-08-10 中国石油化工股份有限公司 Rectification polymerization inhibitor of aromatic olefin monomer, preparation method and application method thereof

Also Published As

Publication number Publication date
CN109503306A (en) 2019-03-22

Similar Documents

Publication Publication Date Title
CN109824822B (en) Temperature response type high-temperature retarder suitable for oil-gas well cementation, preparation method thereof and well cementation cement slurry
CN109503306B (en) Styrene rectification polymerization inhibitor and production method thereof
CN114736659A (en) Preparation method of high-temperature high-density water-based drilling fluid filtrate reducer composition
CN111635497B (en) Underwater concrete anti-dispersant and preparation method thereof
CN115321873A (en) Inorganic modified polycarboxylate ceramic water reducer and preparation method thereof
CN109678528A (en) A kind of ceramics degumming agent and its preparation method and application
CN104910315A (en) Method for preparing polycarboxylate-type ceramic dispersant by use of normal temperature method
CN106565537B (en) A kind of water soluble disperse antisludging agent and its application in production device for acrylic nitrile
CN114213597A (en) Slow-release polycarboxylate superplasticizer with high water reducing rate and preparation method thereof
AU2008217538B2 (en) Redispersible polymers including a protective colloid system
CN105273111B (en) A kind of method of stripper plant fouling in reduction Production of PVC
CN116553996A (en) Polymerization inhibitor and application thereof
CN110981264A (en) Nano bulk concrete anti-cracking agent and preparation method thereof
CN113968689B (en) High-efficiency concrete water reducing agent and preparation method thereof
CN116239729A (en) Low-sensitivity concrete slump retaining agent and preparation method thereof
CN116621495A (en) Preparation method and application of silicate high-alkali wastewater activator for stirring station
CN115043977A (en) Composition, preparation and application of amphoteric ionic polymer retarder for aluminate cement for well cementation
CN106498803A (en) A kind of paper grade (stock) sterilization antiseptic and preparation method thereof
CN102976658B (en) Special additive for water-permeable concrete and preparation method of special additive
CN114940722B (en) High-temperature-resistant and high-alkali-resistant solid flocculating agent, and preparation method and application thereof
CN110668745A (en) Low-slump loss concrete and preparation method thereof
CN114634589B (en) Concrete water-retaining viscosity reducer and preparation method thereof
Wang et al. Synthesis and the effects of new melamine superplasticizer on the properties of concrete
CN109867758A (en) A kind of research work of air entrained type polycarboxylate water-reducer and its synthesis technology
CN103601396B (en) A kind of Aminosulfonic-acid high-efficiency water reducer

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