CN107540805A - A kind of process solvent and its application - Google Patents

A kind of process solvent and its application Download PDF

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Publication number
CN107540805A
CN107540805A CN201710796116.4A CN201710796116A CN107540805A CN 107540805 A CN107540805 A CN 107540805A CN 201710796116 A CN201710796116 A CN 201710796116A CN 107540805 A CN107540805 A CN 107540805A
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CN
China
Prior art keywords
solvent
slurry
application
polyurethane resin
leather
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
Application number
CN201710796116.4A
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Chinese (zh)
Inventor
叶昱文
姜辉
唐茂强
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.)
Yantai Blue Ocean Bolong Microfiber New Material Co Ltd
Original Assignee
Yantai Blue Ocean Bolong Microfiber New Material 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.)
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Publication date
Application filed by Yantai Blue Ocean Bolong Microfiber New Material Co Ltd filed Critical Yantai Blue Ocean Bolong Microfiber New Material Co Ltd
Priority to CN201710796116.4A priority Critical patent/CN107540805A/en
Publication of CN107540805A publication Critical patent/CN107540805A/en
Pending legal-status Critical Current

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Abstract

The present invention relates to a kind of process solvent, include the composition of following mass percent:Dimethylformamide (93~95) %;Sulfoxide type organic (5~7) %, the mixed solvent are used for the production of leather polyurethane resin.Compared with prior art, mixed solvent of the invention, in Synthetic Leather production, offer reaction environment is served, regulation slurry is sticky, carries the effect of slurry.The mixed solvent reduces the use of raw material in production process, reduces cost;Flash-point is improved, improves the security of production process;Make between slurry and base fabric combine it is even closer, improve product quality.

Description

A kind of process solvent and its application
Technical field
The present invention relates to polyurethane production field, and in particular to a kind of process solvent and its application.
Background technology
(N, N-Dimethylformamide, abbreviation DMF, hereinafter using referred to as, molecular structure is simple for dimethylformamide Formula O=CHN (CH3)2) because its molecular weight is small, dielectric constant is high, has electronq donor characteristic and forms the ability of complex compound, It is difficult to volatilize under normal temperature, physical property is stable with chemical property, has very strong solvability, is described as " alembroth ", existing Play the role of Synthetic Leather production process generally played in the form of process solvent it is irreplaceable.
But DMF solvent has the problem of to be solved in actual production there are still some.DMF nucleophilicities are not strong enough, poly- ammonia During ester resin polymerization so that the activity as the isocyanates of main material is not strong enough, can not react completely in proportion, therefore Need to be excessively added as the butanediol of chain extender and the PEPA of one of raw material, add the life of leather polyurethane resin Produce cost.
Secondly, DMF flash-points are relatively low (58 DEG C), have certain danger in storage and transport process is produced.
Again, because the DMF solvent polarity as slurry carried solvent is inadequate in wet polyurethane synthetic leather production process By force, as defective tightness is combined between oil phase carrier and aqueous phase, abscess is easily formed, influences final product quality.
The content of the invention
It is an object of the present invention to overcome the above-mentioned drawbacks of the prior art and provide a kind of activity is big, production peace Full process solvent and its application.
The purpose of the present invention can be achieved through the following technical solutions:A kind of process solvent, the process solvent include with The composition of lower mass percent:
Dimethylformamide (93~95) %;
Sulfoxide type organic (5~7) %.
Described sulfoxide type organic includes one kind in dimethyl sulfoxide (DMSO), diethyl sulfoxide or benzyl benzene sulfoxide.
Described sulfoxide type organic is dimethyl sulfoxide (DMSO).Dimethyl sulfoxide (DMSO), i.e. DMSO, it is same with DMF that there is molecular weight It is small, dielectric constant is high, is difficult to volatilize at normal temperatures, the characteristics of physical property and chemical property are stable.Compared with DMF, DMSO's Viscosity is higher, boiling point is higher, flash-point is higher, nucleophilicity is stronger, polarity is also stronger.DMSO flash-points are 95 DEG C, and DMF flash-points are 58 DEG C, the two mixture calculates according to Raoult laws and Le Chatelier equations, and flash-point is 62.8 DEG C.Use the DMF- The polyurethane resin of DMSO mixed solvents production is through flash(ing) test of remaining silent, and flash-point is 64 DEG C, the poly- ammonia relatively produced using DMF solvent 58 DEG C of ester resin flash-point has raised, and reduces the danger in whole production, storage and transport process.
A kind of application of process solvent as described above, the solvent are used for the production of leather polyurethane resin.
Preferably, described solvent is used for the polymerization process of leather polyurethane resin, and the solvent is polyalcohol, fourth two Alcohol, isocyanates provide reactive polymeric environment.DMSO nucleophilicities are much larger than DMF, and the isocyanate-reactive of in the mixed solvent is compared with DMF After isocyanates in solvent is coordinated by DMSO, activity is bigger, for the butanediol and PEPA for reaction is added completely Amount can suitably reduce.
Preferably, described solvent is used for the viscosity control process of leather polyurethane resin, the solvent and isocyanates The sliminess of common adjustment resin.DMSO nucleophilicities are much larger than DMF, and the isocyanate-reactive of in the mixed solvent is compared with DMF solvent In isocyanates be coordinated by DMSO after, activity it is bigger, adjust the better of sliminess.
Preferably, described solvent is used for dry method leather Polyurethane resin slurry production technology, and the solvent is as dilution Agent;Or sliminess of the solvent for adjusting finished product slurry.DMSO polarity is strong, in the production of wet polyurethane synthetic leather, DMF-DMSO mixed solvents are even closer as being combined between oil phase carrier and aqueous phase, and slurry attachment is close, is not easy to form abscess.
Preferably, the solvent stated is used for wet method leather Polyurethane resin slurry production technology, and the solvent is as diluent; Or sliminess of the solvent for adjusting finished product slurry.DMSO polarity is strong, in the production of wet polyurethane synthetic leather, DMF- DMSO mixed solvents are even closer as being combined between oil phase carrier and aqueous phase, and slurry attachment is close, is not easy to form abscess.
Preferably, described solvent is used for dry-process polyurethane synthetic leather production technology, and the solvent is as polyurethane resin Slurry carried solvent.DMSO polarity is strong, in the production of wet polyurethane synthetic leather, DMF-DMSO mixed solvents as oil phase carrier and Combine even closer between aqueous phase, slurry attachment is close, is not easy to form abscess.
Preferably, described solvent is used for wet polyurethane synthetic leather production technology, and the solvent is as polyurethane resin Slurry carried solvent.DMSO polarity is strong, in the production of wet polyurethane synthetic leather, DMF-DMSO mixed solvents as oil phase carrier and Combine even closer between aqueous phase, slurry attachment is close, is not easy to form abscess.
Compared with prior art, beneficial effects of the present invention are embodied in following several respects:
(1) mixed solvent of the invention is due to the addition of DMSO, and DMSO nucleophilicities are much larger than DMF, in the mixed solvent After isocyanate-reactive is coordinated compared with the isocyanates in DMF solvent by DMSO, activity is bigger, for the fourth for making reaction be added completely The amount of glycol and PEPA can be reduced suitably;
(2) for polyurethane resin of the mixed solvent through production of the invention through flash(ing) test of remaining silent, flash-point is 64 DEG C, is relatively used 58 DEG C of the polyurethane resin flash-point of DMF solvent production has raised, and reduces the danger in whole production, storage and transport process;
(3) mixed solvent of the present invention is even closer as being combined between oil phase carrier and aqueous phase, and slurry attachment is close, is not easy Form abscess.
Embodiment
Embodiments of the invention are elaborated below, the present embodiment is carried out lower premised on technical solution of the present invention Implement, give detailed embodiment and specific operating process, but protection scope of the present invention is not limited to following implementation Example.
Embodiment 1
Leather uses polyurethane resin production technology:PEPA, butanediol, DMF-DMSO mixed solvents etc. are measured respectively After put into reactor, wherein, the mass fraction that DMF mass fraction is 93%, DMSO is 7%, is stirred, formula ratio control Alcohol is excessive, to ensure that isocyanates reacts completely;The isocyanates of formula ratio is added to reactor, leads to steam from reacting kettle jacketing Heating, stirring heating carry out bunching reaction, and reaction stops heating after starting, to the logical circulation water management temperature of chuck at 75~80 DEG C Left and right;Auxiliary agent is added to reactor again, carries out chain-extension polymerization reaction, the reaction time is controlled in 3~5h;Inspection by sampling is simultaneously added DMF-DMSO mixed solvents or isocyanates carry out viscosity adjustment, wet method PU resins mixed solvent containing DMF-DMSO about 70%;Take Sample after the assay was approved, continues to be passed through cooling water being cooled down, finally discharging packaging to reacting kettle jacketing.
As a result show, replace former solvent by using mixed solvent, the usage amount of butanediol reduces by 8% left side than before The right side, save cost.
Embodiment 2
Dry method leather uses Polyurethane resin slurry production technology:By leather polyurethane resin, DMF-DMSO mixed solvents, fourth Ketone, acetone, mill base, auxiliary agent etc. measure according to the ratio of formula ratio above-mentioned substance putting into reactor, wherein DMF mass fraction It is 6% for 94%, DMSO mass fraction, is stirred;Reacting kettle jacketing leads to steam and is heated to 55~70 DEG C or so;Stirring point After dissipating uniformly, viscosity, sampling detection are adjusted with DMF-DMSO mixed solvents;After the assay was approved, filter, dispense.
As a result show, replace former solvent by using mixed solvent, the sticky regulating time of leather polyurethane resin is than it It is preceding to save 10% or so and better.
Embodiment 3
Wet method leather uses Polyurethane resin slurry production technology:By leather polyurethane resin, DMF-DMSO mixed solvents, color Slurry, auxiliary agent etc. measure according to the ratio of formula ratio above-mentioned substance putting into reactor, wherein, DMF mass fraction is 94%, DMSO mass fraction is 6%, is stirred;Reacting kettle jacketing leads to steam and is heated to 55~70 DEG C or so;It is dispersed with stirring uniformly Afterwards, viscosity, sampling detection are adjusted with DMF-DMSO mixed solvents;After the assay was approved, filter, dispense.
As a result show, replace former solvent by using mixed solvent, the sticky regulating time of leather polyurethane resin is than it It is preceding to save 8% or so and better.
Embodiment 4
Dry-process polyurethane synthetic leather production technology:Using release liners as carrier, smearing is mixed with DMF-DMSO and mixed in release liners The dry method leather slurry of bonding solvent, the mass fraction that DMF mass fraction is 95%, DMSO is 5%, is dried through heated-air drying; Again to coating slurry on epidermis after cooling, then dry;To coating leather slurry on epidermis after cooling;To the epidermis of film forming Upper coating mixed solution of adhesive layer, pasted with wet method chamois leather, extruding is batched after drying;Batch rear product curing 72h;Peel off again release Paper, the product after stripping carry out the post processings such as mill skin, glazing, embossing finishing by purposes requirement.
As a result show, replace former solvent by using mixed solvent, slurry attachment is even closer in production process, and is not easy Form abscess.
Embodiment 5
Wet polyurethane synthetic leather production technology:Base fabric after washing, shape, dry, be sent into by polyurethane resin and The wet method leather of DMF-DMSO mixed solvents is impregnated with pulp solution, and the mass fraction that DMF mass fraction is 95%, DMSO is 5%, make to be full of leather slurry and DMF-DMSO mixed solvents in base fabric;Then it is sent into coacervation groove and solidified, solidifying Gu during, DMF-DMSO mixed solvents are replaced by water in slurry, air-setting, and setting time is about 5 minutes;Coacervation is later Base fabric is sent into rinsing bowl and washed, and enters water-filling flushing, removing residual DMF-DMSO mixed solvents to epithelium abscess repeatedly;And then Extrude moisture content, drying epithelium the product of wet method half;The product of wet method half carries out the post processing finishing such as mill skin, glazing or embossing again Work.
As a result show, replace former solvent by using mixed solvent, slurry attachment is even closer in production process, and is not easy Form abscess.

Claims (10)

1. a kind of process solvent, it is characterised in that the process solvent includes the composition of following mass percent:
Dimethylformamide (93~95) %;
Sulfoxide type organic (5~7) %.
2. a kind of process solvent according to claim 1, it is characterised in that described sulfoxide type organic includes dimethyl One kind in sulfoxide, diethyl sulfoxide or benzyl benzene sulfoxide.
3. a kind of process solvent according to claim 2, it is characterised in that described sulfoxide type organic is that dimethyl is sub- Sulfone.
4. a kind of application of the process solvent as described in claims 1 to 3 is any, it is characterised in that the solvent is used to remove from office with poly- ammonia The production of ester resin.
5. the application of a kind of process solvent according to claim 4, it is characterised in that described solvent is used to remove from office with poly- ammonia The polymerization process of ester resin, the solvent is polyalcohol, butanediol, isocyanates provide reactive polymeric environment.
6. the application of a kind of process solvent according to claim 4, it is characterised in that described solvent is used to remove from office with poly- ammonia The viscosity control process of ester resin, the solvent adjust the sliminess of resin with isocyanates jointly.
7. the application of a kind of process solvent according to claim 4, it is characterised in that described solvent is used for dry method leather and used Polyurethane resin slurry production technology, the solvent is as diluent;Or the solvent is used to adjust the sticky of finished product slurry Degree.
8. the application of a kind of process solvent according to claim 4, it is characterised in that described solvent is used for wet method leather and used Polyurethane resin slurry production technology, the solvent is as diluent;Or the solvent is used to adjust the sticky of finished product slurry Degree.
9. the application of a kind of process solvent according to claim 4, it is characterised in that described solvent is used for the poly- ammonia of dry method Lipase absobed removes from office production technology, and the solvent carries solvent as Polyurethane resin slurry.
10. the application of a kind of process solvent according to claim 4, it is characterised in that described solvent gathers for wet method Urethane synthetic leather production technology, the solvent carry solvent as Polyurethane resin slurry.
CN201710796116.4A 2017-09-06 2017-09-06 A kind of process solvent and its application Pending CN107540805A (en)

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Citations (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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JP2005171226A (en) * 2003-11-18 2005-06-30 Sanyo Chem Ind Ltd Polyurethane resin for synthetic leather and porous sheet material
CN1706998A (en) * 2004-06-10 2005-12-14 香港理工大学 Shape memory fiber and its prepn process
JP2007099992A (en) * 2005-10-06 2007-04-19 Nissan Motor Co Ltd Material for ordinary-temperature-drying solvent-based topcoating, coating obtained by using the same and coating film
CN101306329A (en) * 2007-05-17 2008-11-19 深圳市龙澄高科技环保有限公司 Preparation method of polyurethane hollow fiber filter membrane
CN101322922A (en) * 2008-07-21 2008-12-17 天津工业大学 Hollow fiber film and method for producing the same
CN101391113A (en) * 2008-11-07 2009-03-25 四川大学 Polyurethane medical compound film and preparation method thereof
CN101775119A (en) * 2010-02-08 2010-07-14 湖南科技大学 Preparation method of environmental sensitivity polyurethane film
CN101787136A (en) * 2010-01-19 2010-07-28 东南大学 Method for preparing polyurethane function material with surface modified by polyvinyl pyrrolidone
CN102071542A (en) * 2011-02-22 2011-05-25 天津工业大学 Method for preparing polymeric nano-micro fiber non-woven fabric
CN102230236A (en) * 2011-05-17 2011-11-02 上海瑞贝卡纤维材料科技有限公司 Color paste for modified acrylic fiber wet raw liquor coloring system and preparation method thereof
CN102627847A (en) * 2012-04-11 2012-08-08 东华大学 Bendable unsupported carbon nanotube gas-sensitive film and preparation method thereof
CN103360737A (en) * 2013-08-07 2013-10-23 华东理工大学 Thermoplastic-polymer-base lamellar-structure composite material, and preparation method and application thereof
CN105085866A (en) * 2015-09-02 2015-11-25 西安交通大学 Hyperbranched polyurethane containing epoxy groups as well as preparation method and application thereof
CN106702759A (en) * 2016-12-14 2017-05-24 上海华峰超纤材料股份有限公司 Tea fragrance type polyurethane synthetic leather and preparation method thereof

Patent Citations (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1401700A (en) * 2002-10-17 2003-03-12 天津工业大学 Polyurethane/inorganic particle blended composite film and mfg. method thereof
JP2005171226A (en) * 2003-11-18 2005-06-30 Sanyo Chem Ind Ltd Polyurethane resin for synthetic leather and porous sheet material
CN1706998A (en) * 2004-06-10 2005-12-14 香港理工大学 Shape memory fiber and its prepn process
JP2007099992A (en) * 2005-10-06 2007-04-19 Nissan Motor Co Ltd Material for ordinary-temperature-drying solvent-based topcoating, coating obtained by using the same and coating film
CN101306329A (en) * 2007-05-17 2008-11-19 深圳市龙澄高科技环保有限公司 Preparation method of polyurethane hollow fiber filter membrane
CN101322922A (en) * 2008-07-21 2008-12-17 天津工业大学 Hollow fiber film and method for producing the same
CN101391113A (en) * 2008-11-07 2009-03-25 四川大学 Polyurethane medical compound film and preparation method thereof
CN101787136A (en) * 2010-01-19 2010-07-28 东南大学 Method for preparing polyurethane function material with surface modified by polyvinyl pyrrolidone
CN101775119A (en) * 2010-02-08 2010-07-14 湖南科技大学 Preparation method of environmental sensitivity polyurethane film
CN102071542A (en) * 2011-02-22 2011-05-25 天津工业大学 Method for preparing polymeric nano-micro fiber non-woven fabric
CN102230236A (en) * 2011-05-17 2011-11-02 上海瑞贝卡纤维材料科技有限公司 Color paste for modified acrylic fiber wet raw liquor coloring system and preparation method thereof
CN102627847A (en) * 2012-04-11 2012-08-08 东华大学 Bendable unsupported carbon nanotube gas-sensitive film and preparation method thereof
CN103360737A (en) * 2013-08-07 2013-10-23 华东理工大学 Thermoplastic-polymer-base lamellar-structure composite material, and preparation method and application thereof
CN105085866A (en) * 2015-09-02 2015-11-25 西安交通大学 Hyperbranched polyurethane containing epoxy groups as well as preparation method and application thereof
CN106702759A (en) * 2016-12-14 2017-05-24 上海华峰超纤材料股份有限公司 Tea fragrance type polyurethane synthetic leather and preparation method thereof

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