CN107033183A - The preparation technology and its product of Methyl stannum mercaptide, application - Google Patents

The preparation technology and its product of Methyl stannum mercaptide, application Download PDF

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CN107033183A
CN107033183A CN201710318842.5A CN201710318842A CN107033183A CN 107033183 A CN107033183 A CN 107033183A CN 201710318842 A CN201710318842 A CN 201710318842A CN 107033183 A CN107033183 A CN 107033183A
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catalyst
reaction
stannum mercaptide
methyl stannum
aminoethyls
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CN107033183B (en
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杨学强
俞永峰
张建根
张冲
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Qidong Qiangqiang Trade Co.,Ltd.
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NANTONG ADVANCE CHEMICALS CO Ltd
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F7/00Compounds containing elements of Groups 4 or 14 of the Periodic Table
    • C07F7/22Tin compounds
    • C07F7/226Compounds with one or more Sn-S linkages
    • 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
    • C08K5/00Use of organic ingredients
    • C08K5/56Organo-metallic compounds, i.e. organic compounds containing a metal-to-carbon bond
    • C08K5/57Organo-tin compounds
    • C08K5/58Organo-tin compounds containing sulfur

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

The present invention relates to preparation technology and its product, the application of a kind of preparation method of organic tin material, more particularly to a kind of Methyl stannum mercaptide.The preparation technology of Methyl stannum mercaptide is specifically disclosed, is at least comprised the following steps:Step 1:Alkane halogenation;Step 2:Displacement reaction;Step 3:Esterification;Step 4:Distillation:Methyl stannum mercaptide is obtained by vacuum distillation drying;Mol ratio between the metallic tin powder, monochloro methane, isooctyl thioglycolate is:1:(1.2~1.5):5.

Description

The preparation technology and its product of Methyl stannum mercaptide, application
Technical field
The present invention relates to a kind of preparation method of organic tin material, more particularly to a kind of preparation technology of Methyl stannum mercaptide And its product, application.
Background technology
The method of production organotin mainly has Grignard, Wu Zifa, alkyl aluminum method and direct iodine method, grignard both at home and abroad at present Fado is used with American-European countries, and military hereby method has realized industrialized production in the U.S. and East Germany, and alkyl aluminum method is also adopted in East Germany With.Direct iodine method is in Japanese extensive use.Grignard advantage is that product form can be controlled at any time, but step is more, and grignard React for exothermic reaction, solvent boiling point is very low, thus must Cautious control temperature and reaction speed, to avoid blast;Though iodine method Right step is few compared with grignard, but must enter the recovery of professional etiquette, and two methods have in common that magnesium metal, iodine and feed metal tin Price is all more expensive, and wherein organic tin chloride toxicity is higher, therefore the method for not using iodide is sought in general industry production.ke Commissioning
Methyl tin is short due to its carbochain, no tertiary carbon, quaternary carbon atom, is difficult to be alkylated reaction or bar using the above method Part is extremely harsh, and the not scale application in actual production.Current industrial method mainly uses chemical raw material 1 and metal Tin direct alkylation reaction generation methyl chloride tin under high temperature, high pressure, catalysts conditions.This method has process simple, straight The advantage connect, but there is reaction controlling difficulty greatly, high shortcoming is required to reactor.ke Commissioning ke Commissioning
In organic tin heat stabilizer, conventional has tin octylate, butyl tin, ester group tin, methyl tin, although four kinds organic Tin respectively has its feature and advantage, but by contrast, methyl tin has distinctive feature:During with prominent suppression PVC product processing Early stage tinctorial property, remarkable UV resistant and long-time stability;With good mobility, color and luster retentivity during processing It is good, product excellent transparency;Particularly its photo and thermal stability is reached the international leading level, and can effectively realize that secondary operation is recycled Use;Because it does not have toxicity, consumption is few, and thermal stability is excellent, and compatibility is strong, good processability.In polyvinyl chloride resin only Add 1% or so amount, so that it may so that PVC product become water white transparency, it is sparkling and crystal-clear bright, therefore, use methyl tin used as stabilizers PVC sheet be widely used in the packaging of food, medicine and beverage.
Thiol methyl tin production technology is to add catalyst one-step synthesis production technology.Experimental studies have found that, use S class chemical combination Thing makees catalyst and there is problems with:Firstth, catalytic effect is not high, and a collection of reaction more than hour will could be completed at 8 substantially; Secondth, usage cycles are too short, fail too fast, general with one month or so, catalyst failure, it is necessary to remove bed material, cause tin A large amount of losses of material.Meanwhile, methyl tin (SM501) in the domestic market mainly contains the 20% trisulfides second of monomethyl tin The different monooctyl ester of acid and 80% stannous methide curing 2-ethyl hexyl ethanoate, need to adjust tri-thiol 2-ethyl hexyl ethanoate according to different situations The content of methyl tin and dimercapto 2-ethyl hexyl ethanoate stannous methide.For above-mentioned situation, it is necessary to the catalyst that selection is more applicable, Could preferably it solve the above problems.ke Commissioning
The content of the invention
In order to solve the above-mentioned technical problem, the first aspect of the invention provides the preparation technology of Methyl stannum mercaptide, extremely Comprise the following steps less:
Step 1:Alkane halogenation:Metallic tin powder, the first catalyst are added in reactor, then led into reactor Enter monochloro methane, rise reaction temperature carries out alkane 5~10h of halogenation, obtain dimethyltin chloride to 150~180 DEG C;
Step 2:Displacement reaction:Butter of tin is added into step 1, rise reaction temperature is forced into 220~230 DEG C 0.5MPa, enters line replacement reaction, obtains replacing reaction solution, then distills displacement reaction solution, obtains monomethyl tri-chlorination Tin and the dimethyltin chloride aqueous solution;
Step 3:Esterification:The monomethyl tin trichloride obtained in step 2 and the dimethyltin chloride aqueous solution are added Enter to sequentially add the second catalyst, isooctyl thioglycolate, 5~20min of stirring reaction in the case where reaction temperature is 20~30 DEG C, so After add N- (2- aminoethyls) -3- aminopropyl trimethoxysilane improved silicas, the stirring reaction 20 at 30~50 DEG C ~60min, and it is 7 to adjust the pH value of reaction, then at 40 DEG C, 4~5h of stirring reaction, static, cooling, layering;Isolate Organic layer, water-filling of going forward side by side is washed 1~3 time;Second catalyst is TBAB, bi-tristearin, dimethyl Asia The mixture of sulfone;
Step 4:Distillation:Methyl stannum mercaptide is obtained by vacuum distillation drying;
Mol ratio between the metallic tin powder, monochloro methane, isooctyl thioglycolate is:1:(1.2~1.5):5.
As a kind of preferred technical scheme of the present invention, first catalyst is hexadecyltrimethylammonium chloride and shell The weight ratio of glycan compound, hexadecyltrimethylammonium chloride and chitosan is 10:1.
As a kind of preferred technical scheme of the present invention, the metallic tin powder and the weight ratio of the first catalyst are:100: (0.1~5).
As a kind of preferred technical scheme of the present invention, in second catalyst, TBAB, double stearic acid are sweet Weight ratio between grease, the mixture of dimethyl sulfoxide (DMSO) is:1:(1~5):(10~15).
As a kind of preferred technical scheme of the present invention, the isooctyl thioglycolate and N- (2- aminoethyls) -3- ammonia third Weight ratio between base trimethoxy silane improved silica is 100:(1~8).
As a kind of preferred technical scheme of the present invention, N- (2- the aminoethyls) -3- aminopropyl trimethoxysilanes change Property silica in, weight ratios of the N- (2- aminoethyls) between -3- aminopropyl trimethoxysilanes and silica for (1~ 10):3.
As a kind of preferred technical scheme of the present invention, N- (2- the aminoethyls) -3- aminopropyl trimethoxysilanes change Weight ratio between property silica and the second catalyst is:1:(0.1~1).
The second aspect of the invention provides Methyl stannum mercaptide, is obtained using above-mentioned preparation method.
The third aspect of the invention provides environment-friendly type PVC, and the environment-friendly type PVC in parts by weight, at least includes,
100 parts of polyvinyl chloride resin;
0.1~0.5 part of Methyl stannum mercaptide;
0.1~0.5 part of auxiliary agent;
The fourth aspect of the invention provides application of the Methyl stannum mercaptide in rubber, plastics, catalyst field.
The above-mentioned of the application and other features, aspect and advantage is more readily understood with reference to described further below.
Embodiment
The participation in the election detailed description of the invention below for being preferable to carry out method and including embodiment this public affairs can be more easily understood Open content.A large amount of terms can be referred in description below and claims, these terms are defined as following meanings.
As used herein term " by ... prepare " it is synonymous with "comprising".Term "comprising" used herein, " comprising ", " having ", " containing " or its any other deformation, it is intended that cover including for non-exclusionism.For example, the combination comprising listed elements Thing, step, method, product or device are not necessarily limited to those key elements, but can include not expressly listed other key elements or Such a composition, step, method, product or the intrinsic key element of device." optionally " or " optionally " refer to describe thereafter Item or event may or may not occur, and the description includes the situation and the situation that does not occur of event that event occurs.
Equivalent, concentration or other values or parameter are excellent with scope, preferred scope or a series of upper limit preferred values and lower limit During the Range Representation that choosing value is limited, this, which is appreciated that, specifically discloses by any range limit or preferred value and any scope All scopes that any pairing of lower limit or preferred value is formed, regardless of whether whether the scope separately discloses.For example, when open During scope " 1 to 5 ", described scope should be interpreted as including scope " 1 to 4 ", " 1 to 3 ", " 1~2 ", " 1~2 and 4~ 5 ", " 1~3 and 5 " etc..When number range is described herein, unless otherwise indicated, otherwise the scope is intended to include its end Value and all integers and fraction within the range.
In order to solve the above-mentioned technical problem, the first aspect of the invention provides the preparation technology of Methyl stannum mercaptide, extremely Comprise the following steps less:
Step 1:Alkane halogenation:Metallic tin powder, the first catalyst are added in reactor, then led into reactor Enter monochloro methane, rise reaction temperature carries out alkane 5~10h of halogenation, obtain dimethyltin chloride to 150~180 DEG C;
Step 2:Displacement reaction:Butter of tin is added into step 1, rise reaction temperature is forced into 220~230 DEG C 0.5MPa, enters line replacement reaction, obtains replacing reaction solution, then distills displacement reaction solution, obtains monomethyl tri-chlorination Tin and the dimethyltin chloride aqueous solution;
Step 3:Esterification:The monomethyl tin trichloride obtained in step 2 and the dimethyltin chloride aqueous solution are added Enter to sequentially add the second catalyst, isooctyl thioglycolate, 5~20min of stirring reaction in the case where reaction temperature is 20~30 DEG C, so After add N- (2- aminoethyls) -3- aminopropyl trimethoxysilane improved silicas, the stirring reaction 20 at 30~50 DEG C ~60min, and it is 7 to adjust the pH value of reaction, then at 40 DEG C, 4~5h of stirring reaction, static, cooling, layering;Isolate Organic layer, water-filling of going forward side by side is washed 1~3 time;Second catalyst is TBAB, bi-tristearin, dimethyl Asia The mixture of sulfone;
Step 4:Distillation:Methyl stannum mercaptide is obtained by vacuum distillation drying;
Mol ratio between the metallic tin powder, monochloro methane, isooctyl thioglycolate is:1:(1.2~1.5):5.
Step 1
The step 1 of the present invention is carries out alkane halogenation, and detailed process is:
Metallic tin powder, the first catalyst are added in reactor, monochloro methane is then passed through into reactor, rise is anti- Temperature is answered to 150~180 DEG C, alkane 5~10h of halogenation is carried out, obtains dimethyltin chloride;
In the application, the metallic tin powder can be different shape, can be tin flower, or glass putty;Preferably tin Powder.
In the application, first catalyst is hexadecyltrimethylammonium chloride and chitosan complexes;
Term " hexadecyltrimethylammonium chloride and chitosan complexes " refers to be grafted cetyl front three on chitosan Ammonium chloride, obtained compound.
In a preferred embodiment, the preparation side of the hexadecyltrimethylammonium chloride and chitosan complexes Method comprises the following steps:
100g water, 1g chitosans are added in a kettle., after stirring at room temperature, add 10g cetyl front threes Ammonium chloride, controlling reaction temperature be 20~45 DEG C, then add 0.1g sodium hydroxide, at 30~60 DEG C react 5~ After 12 hours, neutralized and used after ethanol cyclic washing with hydrobromic acid, suction filtration and dry hexadecyltrimethylammonium chloride and shell Glycan compound.
In first catalyst, the weight ratio of hexadecyltrimethylammonium chloride and chitosan is 10:1.
The chitosan refers to the chitosan that deacetylation is 80%.
In a preferred embodiment, the metallic tin powder and the weight ratio of the first catalyst are:100:0.1.
The specific chemical reaction occurred in step 1 is:
Inventor has found that the first catalyst of the application can improve the conversion ratio of metallic tin powder, to improve metallic tin powder Utilization rate, meanwhile, the present inventor is found surprisingly that, by adjust the first catalyst usage amount can adjust monomethyl trichlorine Change the weight ratio of tin and dimethyltin chloride, with the increase of the usage amount of the first catalyst, dimethyltin chloride contains Amount increase, and then the trisulfides 2-ethyl hexyl ethanoate of monomethyl tin and diformazan of product can be controlled by the usage amount of the first catalyst Base tin curing 2-ethyl hexyl ethanoate ratio.Meanwhile, it can also suppress side reaction using the first catalyst:Sn+SnCl4→2SnCl2 Generation.
Step 2
The step 2 of the present invention is that, into line replacement reaction, detailed process is:
Butter of tin is added into step 1, rise reaction temperature is forced into 0.5MPa, enters line replacement to 220~230 DEG C Reaction, obtains replacing reaction solution, then distills displacement reaction solution, obtains monomethyl tin trichloride and dimethyl dichloride The tin aqueous solution;
The specific chemical reaction occurred in step 2 is:
(CH3)2SnCl2+SnCl4→2CH3SnCl3
In the step 2 of the application, will not substantially occur side reaction, will not especially occur Sn+SnCl4→2 SnCl2, Substantially increase the utilization rate of raw material.
Step 3
The step 3 of the present invention is carries out esterification, and detailed process is:
The monomethyl tin trichloride obtained in step 2 and the addition of the dimethyltin chloride aqueous solution are sequentially added second and urged Agent, isooctyl thioglycolate, 5~20min of stirring reaction in the case where reaction temperature is 20~30 DEG C, then add N- (2- ammonia Ethyl) -3- aminopropyl trimethoxysilane improved silicas, 20~60min of stirring reaction at 30~50 DEG C, and adjust anti- The pH value answered is 7, then at 40 DEG C, 4~5h of stirring reaction, static, cooling, layering;Organic layer is isolated, water-filling of going forward side by side is washed 1~3 time;Second catalyst is TBAB, bi-tristearin, the mixture of dimethyl sulfoxide (DMSO);
Term " N- (2- aminoethyls) -3- aminopropyl trimethoxysilanes improved silica " refer to N- (2- aminoethyls) - 3- aminopropyl trimethoxysilanes are to silica surface graft modification.In the application, N- (2- aminoethyls) -3- aminopropyls are added In the esterification reaction, one side can interact trimethoxy silane improved silica with the second catalyst, improve The service life of second catalyst, the number of times that increase repetitive cycling is used, plays a part of co-catalysis;Second aspect can be carried The catalytic efficiency of high second catalyst, improves the conversion ratio of monomethyl tin trichloride and dimethyltin chloride, while can inhale The hydrogen chloride produced in reaction system is received, promotes reaction forward to carry out.
In a preferred embodiment, N- (2- the aminoethyls) -3- aminopropyl trimethoxysilanes are modified dioxy The preparation process of SiClx comprises the following steps:
In the reactor, solvent 100ml toluene and 1g nano silicons, ultrasonic disperse 10min are added, N- is then added (2- aminoethyls) -3- aminopropyl trimethoxysilanes, add the triethylamine solution that volumetric concentration is 10%, are flowed back at 100 DEG C 2h is reacted, filtering, ethanol is washed 3 times, be dried to obtain N- (2- aminoethyls) -3- aminopropyl trimethoxysilanes and be modified titanium dioxide Silicon.
In a preferred embodiment, the isooctyl thioglycolate and N- (2- aminoethyls) -3- aminopropyl front threes Weight ratio between TMOS improved silica is 100:(1~8).
In a preferred embodiment, N- (2- the aminoethyls) -3- aminopropyl trimethoxysilanes are modified dioxy In SiClx, the weight ratio between amino silicane coupling agent and silica is (1~10):3.
In a preferred embodiment, in second catalyst, TBAB, bi-tristearin, Weight ratio between the mixture of dimethyl sulfoxide (DMSO) is:1:(1~5):(10~15);Preferably, in second catalyst, four Weight ratio between butylammonium bromide, bi-tristearin, the mixture of dimethyl sulfoxide (DMSO) is:1:(2~4):(12~14); Most preferably, in second catalyst, between TBAB, bi-tristearin, the mixture of dimethyl sulfoxide (DMSO) Weight ratio be:1:3:13.
In a preferred embodiment, N- (2- the aminoethyls) -3- aminopropyl trimethoxysilanes are modified dioxy Weight ratio between SiClx and the second catalyst is:1:(0.1~1).
The specific chemical reaction occurred in step 3 is:
(CH3)2SnCl2+2HSCH2COOC8H17→(CH3)2Sn(SCH2COOC8H17)2+2HCl;
2CH3SnCl3+3HSCH2COOC8H17→CH3Sn(SCH2COOC8H17)3+3HCl。
Finally Methyl stannum mercaptide is obtained through the distillation in step 4, drying process;
Mol ratio between the metallic tin powder, monochloro methane, isooctyl thioglycolate is:1:(1.2~1.5):5.
The second aspect of the invention provides Methyl stannum mercaptide, is obtained using above-mentioned preparation method.
The third aspect of the invention provides environment-friendly type PVC, and the environment-friendly type PVC in parts by weight, at least includes,
100 parts of polyvinyl chloride resin;
0.1~0.5 part of Methyl stannum mercaptide;
0.1~0.5 part of auxiliary agent;
In the application, described Methyl stannum mercaptide synthesizes what is obtained using above-mentioned preparation method.
In the application, what described auxiliary agent can be enumerated has:Antioxidant, plasticizer, fire retardant, filler, ultraviolet radiation absorption Agent, antiseptic, pigment, enter delustering agent, weather resisting agent, antistatic agent, anti-coloring agent etc..
What the antioxidant can be enumerated has:Phenolic antioxidant, phosphite ester kind antioxidant, containing in sulphur ester antioxidant It is at least one.
Phenolic antioxidant can be enumerated:1- hydroxy-3-methyl -4- cumenes, 2,6- DI-tert-butylphenol compounds, the uncles of 2,6- bis- Butyl -4- ethyl -phenols, BHT, 2,6- di-t-butyl -4- normal-butyls phenol, 4- methylols -2,6- bis- Tert-butyl phenol, butylhydroxy anisole, 2- (1- methylcyclohexyls) -4,6- xylenols, the tertiary fourths of 2,4- dimethyl -6- Base phenol, 2- methyl -4,6- dinonyl phenol, 2,6- di-t-butyls-alpha, alpha-dimethyl amino-p-cresol, 2,4,6- tri-butyl benzenes Double (the octylsulfo) -1,3,5-triazines of phenol, 6- (4- hydroxyl -3,5- di-tert-butyls amido) -2,4-, 4,6- it is double (4- hydroxyl -3, 5- di-t-butyls phenoxy group) -2- n-octylthios -1,3,5-triazines, β-(3,5- di-tert-butyl-hydroxy phenyl) propionic acid first Ester, β-positive octadecanol ester of (4-hydroxyl-3,5-di-tert-butyl-phenyl) propionic acid, styrenated phenol, 4,4 '-dihydroxy connection Benzene, butylated octylated phenol, butylated stytrene cresols, 2,2 '-methylene bis (4- methyl-6-tert-butylphenols) or 2, 2 '-methylene bis (the 6- tert-butyl group -4- cresols), 2,2 '-methylene bis (4- ethyl -6- tert-butyl phenols), 2,2 '-methylene bis (4- first Base -6- cyclohexylphenols), 4,4 '-methylene bis (2,6- DI-tert-butylphenol compounds), 2, (6- α-methylbenzyls are to first for 2 '-methylene bis Phenol), 1,1- double (4- hydroxy benzenes) hexamethylene, 2,2 '-methylene bis (4- methyl -6- (Alpha-Methyl cyclohexyl) phenol) or 2,2 '-two Hydroxyl -3,3 '-two (Alpha-Methyl cyclohexyl) -5,5 '-dimethyl diphenylmethane, 1,3,5- trimethyls -2,4,6- tri- (3,5- bis- Tertiary butyl-4-hydroxy benzyl) benzene, 1,1,3- tri- (2- methyl -4- hydroxyl -5- tert-butyl-phenyls) butane, four (3- (3 ' 5 '-two uncles Butyl -4 '-hydroxy phenyl) propionic acid) pentaerythritol ester, 4,4 '-thiobis (the 6- tert-butyl group -3- methylphenols) or 4,4 '-thio Double (6- tert-butyl-m-cresols), 4,4 '-thiobis (2- methyl-6-tert-butylphenols) or 4,4 '-thiobis (6- tert-butyl o first Phenol), 2, the double (β-(3,5- di-tert-butyl-hydroxy phenyl) propionic acid of 2 '-thiobis (4- methyl-6-tert-butylphenols), hexylene glycol Ester), 2,2 '-thiobis (3 ,-(3,5- di-tert-butyl-hydroxy phenyl) ethyl propionate), N, double (3,5- bis- uncles of N '-hexamethylene Butyl-4- hydroxyls hydrocinnamamide), 1,3,5- tri- (the 4- tert-butyl group-3- hydroxyls-2,6- dimethyl benzyls) 1,3,5-triazine-2,4, 6- (1H, 3H, 5H)-triketone, 1,3,5- tri- (3,5- di-tert-butyl-4-hydroxyl benzyl) guanamines, 4,6- (1H, 3H, 5H) three Ketone or isocyanuric acid three (3,5- di-tert-butyl-4-hydroxyl benzyl ester), [β-(3,5- di-t-butyl -4- hydroxy benzenes of isocyanuric acid three Base) propionyloxy ethyl ester], double [3,3- double (3 '-tert-butyl group -4 '-hydroxy phenyl) butyric acid] glycol esters, 1,1 '-thiobis (2- Naphthols), double (3,5- di-tert-butyl-4-hydroxyl benzyl) thioethers, 2,5- di-tert-butyl hydroquinones, the tertiary pentyls of 2,5- bis- are to benzene two Phenol, 3,5- di-tert-butyl-4-hydroxyl benzyls di(2-ethylhexyl)phosphate (18) ester, 3,5- di-tert-butyl-4-hydroxyl benzyls diethyl phosphate, three One kind in glycol double -3- (3- tertiary butyl-4-hydroxy -5- aminomethyl phenyls) propionic ester, hydroquinone dibenzyl ethers.
Phosphite ester kind antioxidant can be enumerated:Triphenyl phosphite, phosphorous acid three (nonyl phenyl ester), phosphorous acid three are different pungent Ester, triisodecyl phosphite ester, the isodecyl ester of phosphorous acid benzene two, trilauryl trithiophosphite, trilauryl phosphite, phosphorous acid Three (octadecyl esters), the isodecyl ester of diphosphorous acid pentaerythrite two, diphosphorous acid pentaerythrite distearyl alcohol ester, 4,4 '-fourth fork are double (sub- Phosphoric acid (3- methyl-6-tert butyl phenyl) two (tridecyl) esters), isooctyl diphenyl phosphite, phosphorous acid benzene di-isooctyl, Asia Diphenyl octyl phosphate, phosphorous acid hexichol isodecyl ester, dioctyl phosphite, phosphorous acid dilauryl, dimethylphosphite, phosphorous acid Double 13 esters of two oleyl alcohol esters, didecyl phosphite, dibutyl phosphite, phosphorous acid, phosphorous acid double 14 esters, phosphorous triethylenetetraminehexaacetic acids Ester, tributyl phosphite, triisopropyl phosphite, the monooctyl ester of phosphorous acid three or phosphorous acid three (2- ethylhexyls), phosphorous acid-benzene are double One kind in (nonyl benzene) ester, phosphorous acid hexichol nonyl phenyl ester, phosphorous acid three (2,4- di-tert-butyl-phenyl) ester.
It can be enumerated containing sulphur ester antioxidant:Dilauryl thiodipropionate, thio-2 acid 2 stearyl ester or thio Dipropionic acid two (octadecyl ester), β, β '-thio two butyric acid two (18) ester, thio-2 acid bay octadecyl ester, thio-2 acid two (13) ester, thio-2 acid two (14) ester are medium.
The plasticizer can be enumerated:Dioctyl phthalate, diisooctyl phthalate, terephthalic acid (TPA) two are pungent One or more in ester, trioctyl trimellitate (TOTM) or di-n-octyl sebacate.And then preferred cold resistant plasticizer DOS (decanedioic acid Dioctyl ester) or DOP (dioctyl phthalate) etc..
The fire retardant can be enumerated:It is brominated organic based flame retardant, phosphoric acid based flame retardant, antimony trioxide, magnesium hydroxide, red Phosphorus etc..
The filler can be enumerated:Silica, aluminum oxide, kaolinite, wollastonite, mica, talcum, clay, sericite, Magnesium carbonate, magnesium sulfate, calcium oxide, carborundum, antimony trisulphide, artificial gold, copper sulfide, iron sulfide, bismuth sulfide, zinc sulphide, metal Powder, glass powder, glass flake, montmorillonite, glass microballoon etc..
What the ultra-violet absorber can be enumerated has:2- (2- hydroxy-5-methyl bases phenyl) BTA, 2- (2- hydroxyls- 5- butyl phenyls) BTA, 2- (2- hydroxyl -5- octyl phenyls) BTA, 2- (the 3- tert-butyl group -2- hydroxy-5-methyl base benzene Base) the enumerate BTA system ultra-violet absorber such as -5- chlorobenzotriazoles, 2- (3,5- bis- tertiary pentyl -2- hydroxy phenyls) BTA; The benzophenone series ultra-violet absorbers such as ESCALOL 567,2- hydroxyl -4- n-octyl epoxide benzophenone; 2- [4,6- double (2,4- 3,5-dimethylphenyl) -1,3,5-triazines -2- bases] -5- (octyl group epoxide) phenol, 2- (4,6- diphenyl -1, 3,5- triazine -2- bases) the triazine system ultra-violet absorber such as -5- (hexyl epoxide) phenol;P-t-butylphenyl salicylate, salicylic acid The salicylate such as phenyl ester system ultra-violet absorber etc..
What the antiseptic can be enumerated has:Silver ion class antiseptic, zinc oxide, cupric oxide, ammonium dihydrogen phosphate, carbonic acid Lithium, anilid class, imidazoles, thiazoles, isothiazolone derivative, quaternary ammonium salt, double croak classes, phenols formic acid, sorbic acid, have Machine iodine, nitrile, sulphur cyanogen, copper agent, three halogenation allyl compounds, organic nitrogen sulfur compound, chitin, mustard, castor oil, horseradish Deng.
In a preferred embodiment, the preparation method of the environment-friendly type PVC, comprises the following steps:
By the polyvinyl chloride resin, Methyl stannum mercaptide, auxiliary agent of corresponding parts by weight, melting mixing is carried out at 140~190 DEG C, through screw rod Extruder for shaping.
In the application, the thermally-stabilised principle of Methyl stannum mercaptide is divided into lower two steps, first step reaction:The tin of organic tin stabilizer is former With polyvinyl chloride molecule unstable chlorine atom ligand complex occurs for son, while the sulphur atom carbon corresponding with PVC in organotin Atom is complexed;Second step reacts:The sulphur atom of organotin is replaced with unstable chlorine atom in ligand, is deposited when there is HC1 When, coordinate bond divides, and sulfydryl is securely joined with carbon atom in PVC molecules, thus inhibit further take off HCl formed The reaction of double bond.
The fourth aspect of the invention provides application of the Methyl stannum mercaptide in rubber, plastics, catalyst field.
The present invention is specifically described below by embodiment.It is necessarily pointed out that, following examples are only used In the invention will be further described, it is impossible to be interpreted as limiting the scope of the invention, professional and technical personnel in the field Some the nonessential modifications and adaptations made according to the content of the invention described above, still fall within protection scope of the present invention.
In addition, if without other explanations, it is raw materials used be all it is commercially available,
Embodiment 1:
The present embodiment 1 provides a kind of Methyl stannum mercaptide, and the preparation technology of the Methyl stannum mercaptide comprises the following steps:
Step 1:Alkane halogenation:Metallic tin powder, the first catalyst are added in reactor, then led into reactor Enter monochloro methane, rise reaction temperature carries out alkane halogenation 8h, obtain dimethyltin chloride to 150 DEG C;Described first urges Agent is hexadecyltrimethylammonium chloride and chitosan complexes;
Step 2:Displacement reaction:Butter of tin is added into step 1, rise reaction temperature is forced into 220 DEG C 0.5MPa, after entering line replacement reaction 3 hours, obtains replacing reaction solution, then distills displacement reaction solution, obtains monomethyl Tin trichloride (boiling point is 148 DEG C) and dimethyltin chloride (188-190 DEG C) aqueous solution;
Step 3:Esterification:The monomethyl tin trichloride obtained in step 2 and the dimethyltin chloride aqueous solution are added Enter to sequentially add the second catalyst, isooctyl thioglycolate, the stirring reaction 5min in the case where reaction temperature is 30 DEG C, then add N- (2- aminoethyls) -3- aminopropyl trimethoxysilane improved silicas, the stirring reaction 20min at 30 DEG C, and adjust anti- The pH value answered is 7, then at 40 DEG C, stirring reaction 1h, static, cooling, layering;Organic layer is isolated, water-filling of going forward side by side washes 3 It is secondary;
Second catalyst is chitosan, bi-tristearin, the mixture of dimethyl sulfoxide (DMSO);
Step 4:Distillation:Methyl stannum mercaptide is obtained by vacuum distillation drying;
Mol ratio between the metallic tin powder, monochloro methane, butter of tin, isooctyl thioglycolate is:1:1.2:2: 5。
The metallic tin powder and the weight ratio of the first catalyst are:100:0.1;
The preparation process of first catalyst is as follows:
100g water, 1g chitosans are added in a kettle., after stirring at room temperature, add 10g cetyl front threes Ammonium chloride, controlling reaction temperature is 45 DEG C, then adds 0.1g sodium hydroxide, after being reacted 5 hours at 30 DEG C, uses hydrogen Bromic acid is neutralized simultaneously to be washed after 3 times with ethanol, suction filtration and dry hexadecyltrimethylammonium chloride and chitosan complexes.
In second catalyst, between TBAB, bi-tristearin, the mixture of dimethyl sulfoxide (DMSO) Weight ratio is:1:1:10.
The preparation method of second catalyst is as follows:At 50 DEG C, TBAB is dissolved in dimethyl sulfoxide (DMSO), After stirring, bi-tristearin is added in dimethyl sulfoxide (DMSO), the second catalyst is uniformly mixing to obtain.
The preparation process of N- (2- the aminoethyls) -3- aminopropyl trimethoxysilane improved silicas is as follows:Add Then solvent 100ml toluene and 3g nano silicons, ultrasonic disperse 10min add 1g N- aminoethyl -3- aminopropyltriethoxies Dimethoxysilane, adds 10% triethylamine solution that volumetric concentration is 10ml, the back flow reaction 2h at 100 DEG C, filtering, second Alcohol is washed 3 times, is dried to obtain N- (2- aminoethyls) -3- aminopropyl trimethoxysilane improved silicas.The silica It is purchased from extra large moral foundation (Beijing) bio tech ltd;
In N- (2- the aminoethyls) -3- aminopropyl trimethoxysilane improved silicas, N- (2- aminoethyls) -3- ammonia Weight ratio between propyl trimethoxy silicane and silica is 1:3.
Weight of the N- (2- aminoethyls) between -3- aminopropyl trimethoxysilanes improved silica and the second catalyst Measuring ratio is:1:0.1.
Between isooctyl thioglycolate and N- (2- the aminoethyls) -3- aminopropyl trimethoxysilane improved silicas Weight ratio be 100:1.
Embodiment 2:
The present embodiment 2 provides a kind of Methyl stannum mercaptide, and the preparation technology of the Methyl stannum mercaptide comprises the following steps:
Step 1:Alkane halogenation:Metallic tin powder, the first catalyst are added in reactor, then led into reactor Enter monochloro methane, rise reaction temperature carries out alkane halogenation 8h, obtain dimethyltin chloride to 150 DEG C;Described first urges Agent is hexadecyltrimethylammonium chloride and chitosan complexes;
Step 2:Displacement reaction:Butter of tin is added into step 1, rise reaction temperature is forced into 220 DEG C 0.5MPa, after entering line replacement reaction 3 hours, obtains replacing reaction solution, then distills displacement reaction solution, obtains monomethyl Tin trichloride (boiling point is 148 DEG C) and dimethyltin chloride (188-190 DEG C) aqueous solution;
Step 3:Esterification:The monomethyl tin trichloride obtained in step 2 and the dimethyltin chloride aqueous solution are added Enter to sequentially add the second catalyst, isooctyl thioglycolate, the stirring reaction 5min in the case where reaction temperature is 30 DEG C, then add N- (2- aminoethyls) -3- aminopropyl trimethoxysilane improved silicas, the stirring reaction 20min at 30 DEG C, and adjust anti- The pH value answered is 7, then at 40 DEG C, stirring reaction 1h, static, cooling, layering;Organic layer is isolated, water-filling of going forward side by side washes 3 It is secondary;
Second catalyst is chitosan, bi-tristearin, the mixture of dimethyl sulfoxide (DMSO);
Step 4:Distillation:Methyl stannum mercaptide is obtained by vacuum distillation drying;
Mol ratio between the metallic tin powder, monochloro methane, butter of tin, isooctyl thioglycolate is:1:1.2:2: 5。
The metallic tin powder and the weight ratio of the first catalyst are:100:0.3;
The preparation process of first catalyst is as follows:
100g water, 1g chitosans are added in a kettle., after stirring at room temperature, add 10g cetyl front threes Ammonium chloride, controlling reaction temperature is 45 DEG C, then adds 0.1g sodium hydroxide, after being reacted 5 hours at 30 DEG C, uses hydrogen Bromic acid is neutralized simultaneously to be washed after 3 times with ethanol, suction filtration and dry hexadecyltrimethylammonium chloride and chitosan complexes.
In second catalyst, between TBAB, bi-tristearin, the mixture of dimethyl sulfoxide (DMSO) Weight ratio is:1:1:10.
The preparation method of second catalyst is as follows:At 50 DEG C, TBAB is dissolved in dimethyl sulfoxide (DMSO), After stirring, bi-tristearin is added in dimethyl sulfoxide (DMSO), the second catalyst is uniformly mixing to obtain.
The preparation process of N- (2- the aminoethyls) -3- aminopropyl trimethoxysilane improved silicas is as follows:Add Then solvent 100ml toluene and 3g nano silicons, ultrasonic disperse 10min add 1g N- aminoethyl -3- aminopropyltriethoxies Dimethoxysilane, adds 10% triethylamine solution that volumetric concentration is 10ml, the back flow reaction 2h at 100 DEG C, filtering, second Alcohol is washed 3 times, is dried to obtain N- (2- aminoethyls) -3- aminopropyl trimethoxysilane improved silicas.The silica It is purchased from extra large moral foundation (Beijing) bio tech ltd;
In N- (2- the aminoethyls) -3- aminopropyl trimethoxysilane improved silicas, N- (2- aminoethyls) -3- ammonia Weight ratio between propyl trimethoxy silicane and silica is 1:3.
Weight of the N- (2- aminoethyls) between -3- aminopropyl trimethoxysilanes improved silica and the second catalyst Measuring ratio is:1:0.1.
Between isooctyl thioglycolate and N- (2- the aminoethyls) -3- aminopropyl trimethoxysilane improved silicas Weight ratio be 100:1.
Embodiment 3:
The present embodiment 3 provides a kind of Methyl stannum mercaptide, and the preparation technology of the Methyl stannum mercaptide comprises the following steps:
Step 1:Alkane halogenation:Metallic tin powder, the first catalyst are added in reactor, then led into reactor Enter monochloro methane, rise reaction temperature carries out alkane halogenation 6h, obtain dimethyltin chloride to 180 DEG C;Described first urges Agent is hexadecyltrimethylammonium chloride and chitosan complexes;
Step 2:Displacement reaction:Butter of tin is added into step 1, rise reaction temperature is forced into 220 DEG C 0.5MPa, after entering line replacement reaction 3 hours, obtains replacing reaction solution, then distills displacement reaction solution, obtains monomethyl Tin trichloride (boiling point is 148 DEG C) and dimethyltin chloride (188-190 DEG C) aqueous solution;
Step 3:Esterification:The monomethyl tin trichloride obtained in step 2 and the dimethyltin chloride aqueous solution are added Enter to sequentially add the second catalyst, isooctyl thioglycolate, the stirring reaction 5min in the case where reaction temperature is 30 DEG C, then add N- (2- aminoethyls) -3- aminopropyl trimethoxysilane improved silicas, the stirring reaction 20min at 30 DEG C, and adjust anti- The pH value answered is 7, then at 40 DEG C, stirring reaction 1h, static, cooling, layering;Organic layer is isolated, water-filling of going forward side by side washes 3 It is secondary;
Second catalyst is chitosan, bi-tristearin, the mixture of dimethyl sulfoxide (DMSO);
Step 4:Distillation:Methyl stannum mercaptide is obtained by vacuum distillation drying;
Mol ratio between the metallic tin powder, monochloro methane, butter of tin, isooctyl thioglycolate is:1:1.2:2: 5。
The metallic tin powder and the weight ratio of the first catalyst are:100:0.5;
The preparation process of first catalyst is as follows:
100g water, 1g chitosans are added in a kettle., after stirring at room temperature, add 10g cetyl front threes Ammonium chloride, controlling reaction temperature is 45 DEG C, then adds 0.1g sodium hydroxide, after being reacted 5 hours at 30 DEG C, uses hydrogen Bromic acid is neutralized simultaneously to be washed after 3 times with ethanol, suction filtration and dry hexadecyltrimethylammonium chloride and chitosan complexes.
In second catalyst, between TBAB, bi-tristearin, the mixture of dimethyl sulfoxide (DMSO) Weight ratio is:1:1:10.
The preparation method of second catalyst is as follows:At 50 DEG C, TBAB is dissolved in dimethyl sulfoxide (DMSO), After stirring, bi-tristearin is added in dimethyl sulfoxide (DMSO), the second catalyst is uniformly mixing to obtain.
The preparation process of N- (2- the aminoethyls) -3- aminopropyl trimethoxysilane improved silicas is as follows:Add Then solvent 100ml toluene and 3g nano silicons, ultrasonic disperse 10min add 1g N- aminoethyl -3- aminopropyltriethoxies Dimethoxysilane, adds 10% triethylamine solution that volumetric concentration is 10ml, the back flow reaction 2h at 100 DEG C, filtering, second Alcohol is washed 3 times, is dried to obtain N- (2- aminoethyls) -3- aminopropyl trimethoxysilane improved silicas.The silica It is purchased from extra large moral foundation (Beijing) bio tech ltd;
In N- (2- the aminoethyls) -3- aminopropyl trimethoxysilane improved silicas, N- (2- aminoethyls) -3- ammonia Weight ratio between propyl trimethoxy silicane and silica is 1:3.
Weight of the N- (2- aminoethyls) between -3- aminopropyl trimethoxysilanes improved silica and the second catalyst Measuring ratio is:1:0.1.
Between isooctyl thioglycolate and N- (2- the aminoethyls) -3- aminopropyl trimethoxysilane improved silicas Weight ratio be 100:1.
Embodiment 4:
The present embodiment 4 provides a kind of Methyl stannum mercaptide, and the preparation technology of the Methyl stannum mercaptide comprises the following steps:
Step 1:Alkane halogenation:Metallic tin powder, the first catalyst are added in reactor, then led into reactor Enter monochloro methane, rise reaction temperature carries out alkane halogenation 6h, obtain dimethyltin chloride to 180 DEG C;Described first urges Agent is hexadecyltrimethylammonium chloride and chitosan complexes;
Step 2:Displacement reaction:Butter of tin is added into step 1, rise reaction temperature is forced into 220 DEG C 0.5MPa, after entering line replacement reaction 3 hours, obtains replacing reaction solution, then distills displacement reaction solution, obtains monomethyl Tin trichloride (boiling point is 148 DEG C) and dimethyltin chloride (188-190 DEG C) aqueous solution;
Step 3:Esterification:The monomethyl tin trichloride obtained in step 2 and the dimethyltin chloride aqueous solution are added Enter to sequentially add the second catalyst, isooctyl thioglycolate, the stirring reaction 5min in the case where reaction temperature is 30 DEG C, then add N- (2- aminoethyls) -3- aminopropyl trimethoxysilane improved silicas, the stirring reaction 20min at 30 DEG C, and adjust anti- The pH value answered is 7, then at 40 DEG C, stirring reaction 1h, static, cooling, layering;Organic layer is isolated, water-filling of going forward side by side washes 3 It is secondary;
Second catalyst is chitosan, bi-tristearin, the mixture of dimethyl sulfoxide (DMSO);
Step 4:Distillation:Methyl stannum mercaptide is obtained by vacuum distillation drying;
Mol ratio between the metallic tin powder, monochloro methane, butter of tin, isooctyl thioglycolate is:1:1.2:2: 5。
The metallic tin powder and the weight ratio of the first catalyst are:100:0.7;
The preparation process of first catalyst is as follows:
100g water, 1g chitosans are added in a kettle., after stirring at room temperature, add 10g cetyl front threes Ammonium chloride, controlling reaction temperature is 45 DEG C, then adds 0.1g sodium hydroxide, after being reacted 5 hours at 30 DEG C, uses hydrogen Bromic acid is neutralized simultaneously to be washed after 3 times with ethanol, suction filtration and dry hexadecyltrimethylammonium chloride and chitosan complexes.
In second catalyst, between TBAB, bi-tristearin, the mixture of dimethyl sulfoxide (DMSO) Weight ratio is:1:1:10.
The preparation method of second catalyst is as follows:At 50 DEG C, TBAB is dissolved in dimethyl sulfoxide (DMSO), After stirring, bi-tristearin is added in dimethyl sulfoxide (DMSO), the second catalyst is uniformly mixing to obtain.
The preparation process of N- (2- the aminoethyls) -3- aminopropyl trimethoxysilane improved silicas is as follows:Add Then solvent 100ml toluene and 3g nano silicons, ultrasonic disperse 10min add 1g N- aminoethyl -3- aminopropyltriethoxies Dimethoxysilane, adds 10% triethylamine solution that volumetric concentration is 10ml, the back flow reaction 2h at 100 DEG C, filtering, second Alcohol is washed 3 times, is dried to obtain N- (2- aminoethyls) -3- aminopropyl trimethoxysilane improved silicas.The silica It is purchased from extra large moral foundation (Beijing) bio tech ltd;
In N- (2- the aminoethyls) -3- aminopropyl trimethoxysilane improved silicas, N- (2- aminoethyls) -3- ammonia Weight ratio between propyl trimethoxy silicane and silica is 1:3.
Weight of the N- (2- aminoethyls) between -3- aminopropyl trimethoxysilanes improved silica and the second catalyst Measuring ratio is:1:0.1.
Between isooctyl thioglycolate and N- (2- the aminoethyls) -3- aminopropyl trimethoxysilane improved silicas Weight ratio be 100:1.
Embodiment 5:
The present embodiment 5 provides a kind of Methyl stannum mercaptide, and the preparation technology of the Methyl stannum mercaptide comprises the following steps:
Step 1:Alkane halogenation:Metallic tin powder, the first catalyst are added in reactor, then led into reactor Enter monochloro methane, rise reaction temperature carries out alkane halogenation 6h, obtain dimethyltin chloride to 180 DEG C;Described first urges Agent is hexadecyltrimethylammonium chloride and chitosan complexes;
Step 2:Displacement reaction:Butter of tin is added into step 1, rise reaction temperature is forced into 220 DEG C 0.5MPa, after entering line replacement reaction 3 hours, obtains replacing reaction solution, then distills displacement reaction solution, obtains monomethyl Tin trichloride (boiling point is 148 DEG C) and dimethyltin chloride (188-190 DEG C) aqueous solution;
Step 3:Esterification:The monomethyl tin trichloride obtained in step 2 and the dimethyltin chloride aqueous solution are added Enter to sequentially add the second catalyst, isooctyl thioglycolate, the stirring reaction 5min in the case where reaction temperature is 30 DEG C, then add N- (2- aminoethyls) -3- aminopropyl trimethoxysilane improved silicas, the stirring reaction 20min at 30 DEG C, and adjust anti- The pH value answered is 7, then at 40 DEG C, stirring reaction 1h, static, cooling, layering;Organic layer is isolated, water-filling of going forward side by side washes 3 It is secondary;
Second catalyst is chitosan, bi-tristearin, the mixture of dimethyl sulfoxide (DMSO);
Step 4:Distillation:Methyl stannum mercaptide is obtained by vacuum distillation drying;
Mol ratio between the metallic tin powder, monochloro methane, butter of tin, isooctyl thioglycolate is:1:1.2:2: 5。
The metallic tin powder and the weight ratio of the first catalyst are:100:1;
The preparation process of first catalyst is as follows:
100g water, 1g chitosans are added in a kettle., after stirring at room temperature, add 10g cetyl front threes Ammonium chloride, controlling reaction temperature is 45 DEG C, then adds 0.1g sodium hydroxide, after being reacted 5 hours at 30 DEG C, uses hydrogen Bromic acid is neutralized simultaneously to be washed after 3 times with ethanol, suction filtration and dry hexadecyltrimethylammonium chloride and chitosan complexes.
In second catalyst, between TBAB, bi-tristearin, the mixture of dimethyl sulfoxide (DMSO) Weight ratio is:1:1:10.
The preparation method of second catalyst is as follows:At 50 DEG C, TBAB is dissolved in dimethyl sulfoxide (DMSO), After stirring, bi-tristearin is added in dimethyl sulfoxide (DMSO), the second catalyst is uniformly mixing to obtain.
The preparation process of N- (2- the aminoethyls) -3- aminopropyl trimethoxysilane improved silicas is as follows:Add Then solvent 100ml toluene and 3g nano silicons, ultrasonic disperse 10min add 1g N- aminoethyl -3- aminopropyltriethoxies Dimethoxysilane, adds 10% triethylamine solution that volumetric concentration is 10ml, the back flow reaction 2h at 100 DEG C, filtering, second Alcohol is washed 3 times, is dried to obtain N- (2- aminoethyls) -3- aminopropyl trimethoxysilane improved silicas.The silica It is purchased from extra large moral foundation (Beijing) bio tech ltd;
In N- (2- the aminoethyls) -3- aminopropyl trimethoxysilane improved silicas, N- (2- aminoethyls) -3- ammonia Weight ratio between propyl trimethoxy silicane and silica is 1:3.
Weight of the N- (2- aminoethyls) between -3- aminopropyl trimethoxysilanes improved silica and the second catalyst Measuring ratio is:1:0.1.
Between isooctyl thioglycolate and N- (2- the aminoethyls) -3- aminopropyl trimethoxysilane improved silicas Weight ratio be 100:1.
Comparative example 1:
The detailed process be the same as Example 5 of comparative example 1, difference is, not including the first catalyst in step 1, other portions Divide be the same as Example 5.
Comparative example 2:
The detailed process be the same as Example 5 of comparative example 2, difference is, the first catalyst in step 1 is changed into cetyl Trimethyl ammonium chloride, other parts be the same as Example 5.
Comparative example 3:
The detailed process be the same as Example 5 of comparative example 3, difference is, the first catalyst in step 1 is changed into chitosan, Other parts be the same as Example 5.
Comparative example 4:
The detailed process be the same as Example 5 of comparative example 4, difference is, the first catalyst in step 1 is changed into dimethyl disulfide Ether, other parts be the same as Example 5.
Comparative example 5:
The detailed process be the same as Example 5 of comparative example 5, difference is, the second catalyst, other portions will not be included in step 2 Divide be the same as Example 5.
Comparative example 6:
The detailed process be the same as Example 5 of comparative example 6, difference is, N- (2- aminoethyls) -3- ammonia will not be included in step 2 Propyl trimethoxy silicane improved silica, other parts be the same as Example 5.
Comparative example 7:
The detailed process be the same as Example 5 of comparative example 7, difference is, by step 2 by N- (2- aminoethyls) -3- aminopropyls Trimethoxy silane improved silica is changed to N- (2- aminoethyls) -3- aminopropyl trimethoxysilanes, and other parts are with real Apply example 5.
Comparative example 8:
The detailed process be the same as Example 5 of comparative example 8, difference is, N- (2- aminoethyls) -3- ammonia will not be included in step 2 Propyl trimethoxy silicane improved silica is changed to silane coupler kh560 improved silicas, and other parts are with implementation Example 5.
Method of testing:
1st, using obtaining monomethyl tin trichloride and the dimethyltin chloride aqueous solution in liquid chromatography for measuring step 2 In, the content of monomethyl tin trichloride and dimethyltin chloride, wherein, the condition of liquid chromatogram is:Chromatographic column:C18, flowing It is mutually methanol, flow velocity is 1mL/min, and 35 DEG C of column temperature, wavelength is 300nm, and sampling volume is 10 microlitres;The model of liquid chromatogram Agilent 1100;
The standard sample of monomethyl tin trichloride and dimethyltin chloride is prepared respectively, is made standard curve, is measured guarantor It is 2.689min and 3.581min to stay the time;
The product that 1~embodiment of embodiment 5 and 1~comparative example of comparative example 8 are obtained measures monomethyl tri-chlorination respectively The content of tin and dimethyltin chloride.
2nd, the presence of stannous chloride is detected according to analysis method specified in HG/T 2526-93.
3rd, the second catalyst repetitive cycling service life number of times is tested, when the conversion ratio of reactant is less than 80%, catalysis Agent end of life, records the access times of the second catalyst.
The characterization test of table 1
From table 1 it follows that from embodiment 1 into embodiment 5, with the increase of the first catalyst usage amount, step 2 In obtain the percetage by weight increase of dimethyltin chloride, can basis when it is added in PVC plastic as heat stabilizer Actual conditions adjust the content of different component in Methyl stannum mercaptide.In addition, also found by experiment, N- (2- ammonia second is added Base) -3- aminopropyl trimethoxysilanes improved silica can greatly improve the service life of the second catalyst.
Embodiment 6
Embodiments herein 6 provide a kind of environment-friendly type PVC resin, the environment-friendly type PVC, in parts by weight, at least Including,
100 parts of polyvinyl chloride resin;
0.1 part of Methyl stannum mercaptide described in embodiment 5;
2,6- 0.5 part of DI-tert-butylphenol compounds.
The preparation method of the environment-friendly type PVC resin is:By the polyvinyl chloride resin under molten condition, Methyl stannum mercaptide, 2,6- bis- Tert-butyl phenol is added in screw extruder, extrusion molding.
After polyvinyl chloride resin is placed in into outdoor application 1 year, observation outward appearance does not occur by the transformation of white to yellow, brown, And hydrogen chloride is not detected.Illustrate that the present invention has good thermostable effect.
Foregoing example is merely illustrative, some features of the feature for explaining the disclosure.Appended claim The scope as wide as possible for requiring to be contemplated that is intended to, and embodiments as presented herein is only according to all possible embodiment Combination selection embodiment explanation.Therefore, the purpose of applicant is appended claim not by the explanation present invention Feature example selectional restriction.And the progress in science and technology by formed language performance it is inaccurate due to and not The possible equivalent or son being presently considered are replaced, and these changes should also be interpreted by appended in the conceived case Claim is covered.

Claims (10)

1. a kind of preparation technology of Methyl stannum mercaptide, it is characterised in that at least comprise the following steps:
Step 1:Alkane halogenation:Metallic tin powder, the first catalyst are added in reactor, one is then passed through into reactor Chloromethanes, rise reaction temperature carries out alkane 5~10h of halogenation, obtains dimethyltin chloride to 150~180 DEG C;
Step 2:Displacement reaction:Butter of tin is added into step 1, rise reaction temperature is forced into 220~230 DEG C 0.5MPa, enters line replacement reaction, obtains replacing reaction solution, then distills displacement reaction solution, obtains monomethyl tri-chlorination Tin and the dimethyltin chloride aqueous solution;
Step 3:Esterification:By the monomethyl tin trichloride obtained in step 2 and the dimethyltin chloride aqueous solution add according to The second catalyst of secondary addition, isooctyl thioglycolate, stirring reaction 5~20min, Ran Houzai in the case where reaction temperature is 20~30 DEG C Add N- (2- aminoethyls) -3- aminopropyl trimethoxysilane improved silicas, at 30~50 DEG C stirring reaction 20~ 60min, and it is 7 to adjust the pH value of reaction, then at 40 DEG C, 4~5h of stirring reaction, static, cooling, layering;Isolate Machine layer, water-filling of going forward side by side is washed 1~3 time;Second catalyst is TBAB, bi-tristearin, dimethyl sulfoxide (DMSO) Mixture;
Step 4:Distillation:Methyl stannum mercaptide is obtained by vacuum distillation drying;
Mol ratio between the metallic tin powder, monochloro methane, isooctyl thioglycolate is:1:(1.2~1.5):5.
2. the preparation technology of Methyl stannum mercaptide as claimed in claim 1, it is characterised in that first catalyst is hexadecane The weight ratio of base trimethyl ammonium chloride and chitosan complexes, hexadecyltrimethylammonium chloride and chitosan is 10:1.
3. the preparation technology of Methyl stannum mercaptide as claimed in claim 1, it is characterised in that the metallic tin powder and the first catalysis The weight ratio of agent is:100:(0.1~5).
4. the preparation technology of Methyl stannum mercaptide as claimed in claim 1, it is characterised in that in second catalyst, four fourths Weight ratio between base ammonium bromide, bi-tristearin, dimethyl sulfoxide (DMSO) is:1:(1~5):(10~15).
5. the preparation technology of Methyl stannum mercaptide as claimed in claim 1, it is characterised in that the isooctyl thioglycolate and N- Weight ratio between (2- aminoethyls) -3- aminopropyl trimethoxysilane improved silicas is 100:(1~8).
6. the preparation technology of Methyl stannum mercaptide as claimed in claim 1, it is characterised in that N- (2- the aminoethyls) -3- ammonia In propyl trimethoxy silicane improved silica, N- (2- aminoethyls) -3- aminopropyl trimethoxysilanes and silica it Between weight ratio be (1~10):3.
7. the preparation technology of Methyl stannum mercaptide as claimed in claim 1, it is characterised in that N- (2- the aminoethyls) -3- ammonia Weight ratio between propyl trimethoxy silicane improved silica and the second catalyst is:1:(0.1~1).
8. a kind of Methyl stannum mercaptide, it is characterised in that the Methyl stannum mercaptide is using the methyl mercaptan described in claim 1~7 What the preparation technology of tin was prepared.
9. a kind of environment-friendly type PVC resin, it is characterised in that the environment-friendly type PVC, in parts by weight, at least includes,
100 parts of polyvinyl chloride resin;
0.1~0.5 part of Methyl stannum mercaptide described in claim 8;
0.1~0.5 part of auxiliary agent.
10. application of the Methyl stannum mercaptide in rubber, plastics, catalyst field described in claim 8.
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CN1270961A (en) * 1999-04-19 2000-10-25 张麟 Preparation of tin methyl mercaptide
CN102250136A (en) * 2011-05-13 2011-11-23 浙江海普顿化工科技有限公司 Preparation method of methyltin mercaptide
CN106008589A (en) * 2016-06-25 2016-10-12 安徽升华新奥特化工有限公司 Green methyl tin mercaptide compound
CN106117263A (en) * 2016-06-25 2016-11-16 安徽升华新奥特化工有限公司 A kind of Methyl stannum mercaptide stabilizer of environmental protection

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CN113816987A (en) * 2021-10-08 2021-12-21 广东先导微电子科技有限公司 Preparation method of dibutyltin oxide
CN113816987B (en) * 2021-10-08 2024-05-24 广东先导微电子科技有限公司 Preparation method of dibutyl tin oxide

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