Summary of the invention
The objective of the invention is to present these deficiencies or the weakness that exists of PDMDAAC laking agent; Further design is with cross-linkable monomer triallyl ammonio methacrylate (TAMAC) and monomer diallyldimethylammonChloride Chloride (DMDAAC) copolymerization; And through controlling the constructional feature and relative molecular mass (intrinsic viscosity) size of product; Thereby a kind of relative molecular mass and structure all controlled little copolymerzation with cross-linking modification PDMDAAC laking agent and compound method thereof have been obtained; For the printing and dyeing industry field provides one type of new laking agent product of novel polyquaternium hi-tech that dry fastness and fastness to wet rubbing all are improved, its reaction equation suc as formula shown in.
Ultimate principle of the present invention is according to being:
On the one hand, with regard to molecular structure, in little crosslinked its structure of PDMDAAC modification by copolymerization laking agent of gained possible crosslinking degree promptly wherein the molar content of cross-linkable monomer unit (TAMAC) be the key factor that influences its fixing property.Cross when low when its degree of crosslinking, the reach between dyestuff and laking agent is abundant inadequately, and this moment, its fixing property was relatively poor; And its degree of crosslinking is when too high; May destroy that modification laking agent agent structure PDMDAAC itself has with cotton fibre similarity structurally; Thereby the tight effect that influences between laking agent and cotton fabric is to each other got in touch; Simultaneously its degree of crosslinking crosses that roughly its spatial volume is excessive makes that also gained modification laking agent is difficult to penetrate into fibrous inside and dyestuff fully acts on, and thus its fixing property is also formed negative impact.Therefore, cross-linkable monomer unit (TAMAC) content in its structure within the specific limits the time its fixing property better.On the other hand; Experimental study is found; Resin type laking agent with certain intrinsic viscosity value can show outstanding fixing property; Simultaneously, consider PDMDAAC modification by copolymerization laking agent as one of resin type laking agent, its relative molecular mass (in intrinsic viscosity) estimates to have close related with its fixing property.When relative molecular mass is too small, the reactive force of itself and dyestuff a little less than, colour fixation is relatively poor; And relative molecular mass then forms gel or deposition easily and is difficult to penetrate into fibrous inside and the dyestuff effect when excessive.Therefore, can influence its colour fixation; Thereby control considers that PDMDAAC modification by copolymerization laking agent relative molecular mass then can improve its colour fixation within the specific limits.
In synthetic preparation process, the structure control of the little crosslinked PDMDAAC modification by copolymerization laking agent of gained can realize through the molar ratio of cross-linkable monomer (TAMAC) in the telo merization process and benchmark monomer (DMDAAC).Simultaneously; Its relative molecular mass control can realize according to following theory: for radical polymerization; The kinetic chain length of its resulting polymers is directly proportional with monomer concentration; With the square root of initiator concentration (initiator amount) be inverse ratio [Pan Zuren. polymer chemistry (third edition) [M]. Beijing: Chemical Industry Press, 2003:43,44]; The polymer kinetics chain length is big more, and the polymerization degree is just big more, and its relative molecular mass is just big more.Therefore, can be through regulating the relative molecular mass size that monomer concentration (initial monomer massfraction) and initiator concentration processing condition such as (initiator amounts) are controlled resulting polymers.The present invention comes effectively with this principle design through factors such as Collaborative Control reaction monomers concentration (initial monomer massfraction) and initiator amounts, and the relative molecular mass size of control gained laking agent is in the special characteristic range of viscosities; The molar ratio of cross-linkable monomer (TAMAC) and benchmark monomer (DMDAAC) is realized its structure control in the telo merization process simultaneously, to obtain corresponding micro-cross-linked PDMDAAC modification laking agent product.
Realize that technical solution of the present invention is:
According to the principle foundation, design following implementation step:
Step 1, cross-linkable monomer TAMAC and the benchmark monomer DMDAAC that gets metering joins in the reactor drum and is made into initial monomer solution;
Step 2 is filled nitrogen in reactor drum, join in the constant pressure funnel after initiator ammonium persulfate APS is made into dilute solution;
Step 3 heats up, and stirs evenly to drip initiator ammonium persulfate APS dilute solution down, drips off the back and keeps temperature to continue reaction;
Step 4, heat up back and slaking obtain the little crosslinked PDMDAAC modification laking agent of title product.
TAMAC monomer described in the step 1 and the monomeric mol ratio of DMDAAC are m
(TAMAC)/ n
(DMDAAC)=1/99 ~ 5/95, described initial monomer liquid quality fraction is 35%-50%;
Described cross-linkable monomer TAMAC processes through following method: being solvent with acetone, is that methyl NSC 20948 and the propenyl chloride of 1:1 reacts 24 h and make in about 30 ℃ with mol ratio.
Initiator ammonium persulfate APS described in the step 2 is the 4%-11% of total monomer quality (TAMAC and DMDAAC quality summation), and described initiator ammonium persulfate APS dilute solution concentration is 0.1-0.3g/ml.
Temperature of reaction described in the step 3 is 60-70 ℃, and the described dropping time is 2.0-3.0 h, and the described reaction times is 3.0-4.0 h.
Temperature of reaction described in the step 4 is 75-85 ℃; The described curing time is more than the 2h; Described little crosslinked PDMDAAC modification laking agent intrinsic viscosity value is 0.10-1.00 dL/g, and bridging property structural unit TAMAC is 1/99 ~ 5/95 with the molar content ratio of benchmark architecture cells D MDAAC in the structure.
Compared with prior art, laking agent product of the present invention has following characteristics:
(1) products obtained therefrom has specific intrinsic viscosity value scope (0.10-1.00 dL/g), has good fixing property;
(2) molar content of bridging property structural unit TAMAC and benchmark architecture cells D MDAAC is controlled at 1/99 ~ 5/95 than effectively in its structure;
(3) its metal to-metal contact of product can reach more than 4 grades, and fastness such as its wet friction preferably can reach 4 grades, are superior to 0.5 ~ 1.0 grade of domestic and international commercial like product, and its preparation technology and fixing property all have satisfactory stability property, and application prospect is better;
(4) the micro-cross-linked PDMDAAC modification laking agent of gained of the present invention can directly use, and its method of use is identical with the method for use of existing polyquaternium laking agent, is convenient to its wide popularization and application.
Embodiment
Come the present invention is described further through embodiment below, purpose is better to understand content of the present invention.But the example of being lifted does not limit protection scope of the present invention.
Micro-cross-linked Poly Dimethyl Diallyl Ammonium Chloride modification laking agent compound method is carried out according to the following steps:
The first step, (two kinds of monomeric mol ratios are m to get cross-linkable monomer TAMAC and the industrial DMDAAC monomer of metering
(TAMAC)/ n
(DMDAAC)=1/99 ~ 5/95) joins in the reactor drum and be made into the initial monomer solution that massfraction is 35%-50%;
Second step, in reactor drum, fill nitrogen, take by weighing and account for total monomer quality (TAMAC and DMDAAC quality summation) and join in the constant pressure funnel for the initiator ammonium persulfate APS of 4%-11% and after being made into the dilute solution of 0.1-0.3g/ml;
The 3rd step was warming up to 60-70 ℃, stirred evenly to drip initiator ammonium persulfate APS dilute solution down, and the dropping time is 2.0-3.0 h, and initiator solution drips off the back and keeps 60-70 ℃ of temperature to continue reaction 3.0-4.0 h;
The 4th step was warming up to 75-85 ℃ and more than slaking 2 h, obtained title product;
In the 5th step, measures above-mentioned product feature viscosity number through slaking to represent its relative molecular mass big or small.
Cross-linkable monomer TAMAC in the first step prepares as follows: being solvent with acetone, is that methyl NSC 20948 and the propenyl chloride of 1:1 reacts 24 h and make in about 30 ℃ with mol ratio.
Embodiment 1
The present invention's design comes effectively through factors such as Collaborative Control reaction monomers concentration (initial monomer massfraction) and initiator amounts, and the relative molecular mass size of the micro-cross-linked PDMDAAC modification by copolymerization laking agent of control is in the special characteristic range of viscosities; The molar ratio of cross-linkable monomer (TAMAC) and benchmark monomer (DMDAAC) is realized its structure control in the telo merization process simultaneously; And obtain corresponding micro-cross-linked PDMDAAC modification laking agent product; Cross-linkable monomer TAMAC used among each embodiment makes as stated above, and concrete steps are following:
The first step, (two kinds of monomeric mol ratios are m to get cross-linkable monomer TAMAC and the industrial DMDAAC monomer of metering
(TAMAC)/ n
(DMDAAC)=1/99) joining in the reactor drum and being made into massfraction is 35% initial monomer solution;
Second step, open the nitrogen introducing valve door, to remove the air in the reaction flask, stop logical nitrogen behind 30 min than atm number;
The 3rd the step, take by weighing account for total monomer quality (TAMAC and DMDAAC quality summation) be 11% initiator ammonium persulfate APS and be made into the dilute solution that concentration is 0.1g/ml after join in the constant pressure funnel;
In the 4th step, solution temperature rises to 60 ℃, stirs evenly to drip initiator ammonium persulfate APS dilute solution down, and the dropping time is 2 h, and initiator solution drips off the back and keeps 60 ℃ of temperature to continue reaction 4 h;
The 5th step was warming up to 75 ℃ of slaking 2 h (further improve the monomer conversion of product, help improving the colour fixation of products obtained therefrom), obtained title product.
Measure its intrinsic viscosity size through the Ubbelohde viscometer method; Recording its intrinsic viscosity value is 0.10 dL/g, and bridging property structural unit TAMAC is 1/99 with the molar content ratio of benchmark architecture cells D MDAAC in the micro-cross-linked PDMDAAC modification of the title product laking agent structure.
Embodiment 2
The present invention's design comes effectively through factors such as Collaborative Control reaction monomers concentration (initial monomer massfraction) and initiator amounts, and the relative molecular mass size of the micro-cross-linked PDMDAAC modification by copolymerization laking agent of control is in the special characteristic range of viscosities; The molar ratio of cross-linkable monomer (TAMAC) and benchmark monomer (DMDAAC) is realized its structure control in the telo merization process simultaneously; And obtain corresponding micro-cross-linked PDMDAAC modification laking agent product, concrete steps are following:
The first step, (two kinds of monomeric mol ratios are m to get cross-linkable monomer TAMAC and the industrial DMDAAC monomer of metering
(TAMAC)/ n
(DMDAAC)=1/99) joining in the reactor drum and being made into massfraction is 50% initial monomer solution;
Second step, open the nitrogen introducing valve door, to remove the air in the reaction flask, stop logical nitrogen behind 30 min than atm number;
The 3rd the step, take by weighing account for total monomer quality (TAMAC and DMDAAC quality summation) be 5% initiator ammonium persulfate APS and be made into the dilute solution that concentration is 0.2g/ml after join in the constant pressure funnel;
In the 4th step, the reaction soln temperature rises to 70 ℃, stirs evenly to drip initiator ammonium persulfate APS dilute solution down, and the dropping time is 2 h, and initiator solution drips off the back and keeps 70 ℃ of temperature to continue reaction 4 h;
The 5th step was warming up to 85 ℃ of slaking 2h, obtained title product.
Measure its intrinsic viscosity size through the Ubbelohde viscometer method; Recording its intrinsic viscosity value is 0.52 dL/g, and bridging property structural unit TAMAC is 1/99 with the molar content ratio of benchmark architecture cells D MDAAC in the micro-cross-linked PDMDAAC modification of the title product laking agent structure.
Embodiment 3
The present invention's design comes effectively through factors such as Collaborative Control reaction monomers concentration (initial monomer massfraction) and initiator amounts, and the relative molecular mass size of the micro-cross-linked PDMDAAC modification by copolymerization laking agent of control is in the special characteristic range of viscosities; The molar ratio of cross-linkable monomer (TAMAC) and benchmark monomer (DMDAAC) is realized its structure control in the telo merization process simultaneously; And obtain corresponding micro-cross-linked PDMDAAC modification laking agent product, concrete steps are following:
The first step, (two kinds of monomeric mol ratios are m to get cross-linkable monomer TAMAC and the industrial DMDAAC monomer of metering
(TAMAC)/ n
(DMDAAC)=3/97) joining in the reactor drum and being made into massfraction is 46% initial monomer solution;
Second step, open the nitrogen introducing valve door, to remove the air in the reaction flask, stop logical nitrogen behind 30 min than atm number;
The 3rd the step, take by weighing account for total monomer quality (TAMAC and DMDAAC quality summation) be 4% initiator ammonium persulfate APS and be made into the dilute solution that concentration is 0.3g/ml after join in the constant pressure funnel;
In the 4th step, the reaction soln temperature rises to 60 ℃, stirs evenly to drip initiator ammonium persulfate APS dilute solution down, and the dropping time is 2 h, and initiator solution drips off the back and keeps 60 ℃ of temperature to continue reaction 4 h;
The 5th step was warming up to 85 ℃ of slaking 2 h, obtained title product.
Measure its intrinsic viscosity size through the Ubbelohde viscometer method, recording its intrinsic viscosity value is 1.00 dL/g, and bridging property structural unit TAMAC and the molar content of benchmark architecture cells D MDAAC are than 3/97 in the micro-cross-linked PDMDAAC modification of the title product laking agent structure.
Embodiment 4
The present invention's design comes effectively through factors such as Collaborative Control reaction monomers concentration (initial monomer massfraction) and initiator amounts, and the relative molecular mass size of the micro-cross-linked PDMDAAC modification by copolymerization laking agent of control is in the special characteristic range of viscosities; The molar ratio of cross-linkable monomer (TAMAC) and benchmark monomer (DMDAAC) is realized its structure control in the telo merization process simultaneously; And obtain corresponding micro-cross-linked PDMDAAC modification laking agent product, concrete steps are following:
The first step, (two kinds of monomeric mol ratios are m to get cross-linkable monomer TAMAC and the industrial DMDAAC monomer of metering
(TAMAC)/ n
(DMDAAC)=5/95) joining in the reactor drum and being made into massfraction is 37% initial monomer solution;
Second step, open the nitrogen introducing valve door, to remove the air in the reaction flask, stop logical nitrogen behind 30 min than atm number;
The 3rd the step, take by weighing account for total monomer quality (TAMAC and DMDAAC quality summation) be 10% initiator ammonium persulfate APS and be made into the dilute solution that concentration is 0.2g/ml after join in the constant pressure funnel;
In the 4th step, the reaction soln temperature rises to 60 ℃, stirs evenly to drip initiator ammonium persulfate APS dilute solution down, and the dropping time is 2.5h, and initiator solution drips off the back and keeps 60 ℃ of temperature to continue reaction 3.5 h;
The 5th step was warming up to 85 ℃ of slaking 4h, obtained title product.
Measure its intrinsic viscosity size through the Ubbelohde viscometer method, recording its intrinsic viscosity value is 0.18 dL/g, and bridging property structural unit TAMAC and the molar content of benchmark architecture cells D MDAAC are than 5/95 in the micro-cross-linked PDMDAAC modification of the title product laking agent structure.
Embodiment 5
The present invention's design comes effectively through factors such as Collaborative Control reaction monomers concentration (initial monomer massfraction) and initiator amounts, and the relative molecular mass size of the micro-cross-linked PDMDAAC modification by copolymerization laking agent of control is in the special characteristic range of viscosities; The molar ratio of cross-linkable monomer (TAMAC) and benchmark monomer (DMDAAC) is realized its structure control in the telo merization process simultaneously; And obtain corresponding micro-cross-linked PDMDAAC modification laking agent product, concrete steps are following:
The first step, (two kinds of monomeric mol ratios of monomer are m to get cross-linkable monomer TAMAC and the industrial DMDAAC of metering
(TAMAC)/ n
(DMDAAC)=5/95) joining in the reactor drum and being made into massfraction is 41% initial monomer solution;
Second step, open the nitrogen introducing valve door, to remove the air in the reaction flask, stop logical nitrogen behind 30 min than atm number;
The 3rd the step, take by weighing account for total monomer quality (TAMAC and DMDAAC quality summation) be 9% initiator ammonium persulfate APS and be made into the dilute solution that concentration is 0.2g/ml after join in the constant pressure funnel;
In the 4th step, the reaction soln temperature rises to 60 ℃, stirs evenly to drip initiator ammonium persulfate APS dilute solution down, and the dropping time is 3 h, and initiator solution drips off the back and keeps 60 ℃ of temperature to continue reaction 3 h;
The 5th step was warming up to 85 ℃ of slaking 2 h, obtained title product.
Measure its intrinsic viscosity size through the Ubbelohde viscometer method; Recording its intrinsic viscosity value is 0.65 dL/g; Bridging property structural unit TAMAC and the molar content of benchmark architecture cells D MDAAC are than 5/95 in the micro-cross-linked PDMDAAC modification of the title product laking agent structure; Through ir spectra and nucleus magnetic resonance its structure is characterized, the result is shown in Fig. 2 and 3.
Application examples
According to related method among GB GB/T 3920-2008 and the GB GB/T 3921-2008, the micro-cross-linked PDMDAAC modification laking agent of mensuration and more different relative molecular mass size and constructional feature is to the fixing property of various dyestuffs on the cotton fabric (reactive scarlet 3BS and reactive brilliant bule KNR etc.).
Comparative Examples 1
The micro-cross-linked PDMDAAC modification laking agent of different relative molecular mass sizes and constructional feature is listed in table 1 to the colour fixation of reactive scarlet 3BS dyestuff on the cotton fabric.Wherein product is No. 1, No. 8, No. 16; Be respectively synthetic the obtaining of condition of embodiment 1 ~ 5 for No. 17 and No. 21; Laking agent LYPF is the commercially available PDMDAAC laking agent product that Shandong chemical industry ltd provides; Laking agent PDAC is the commercially available PDMDAAC laking agent product that Jiangsu chemical industry ltd provides, and laking agent Fix is certain external BA-SF company cationic fixing agent, and blank value is each dyestuff colour fastness value of (before the fixation) during fixation not.
Its dry fastness of the micro-cross-linked PDMDAAC modification of gained laking agent all reaches 4 grades, and fastness to wet rubbing all can reach more than 3 grades, and calico staining all reaches the 4-5 level, and former state is faded and all reached the 4-5 level; It is better that wherein intrinsic viscosity scope cross-linkable monomer unit (TAMAC) molar content in 0.16-0.30 dL/g and structure thereof is controlled at 1% o'clock its fixing property; Its fixing property to dyestuffs such as reactive scarlet 3BS on the cotton fabric is: dry fastness reaches 4 grades respectively; Fastness to wet rubbing preferably all can reach 4 grades; Calico staining all reaches the 4-5 level; Former state is faded and is all reached the 4-5 level, obviously is superior to homemade unmodified PDMDAAC laking agent and external similar cationic laking agent (laking agent Fix) commonly used; Before and after the fixation, its dry fastness, soap calico staining and the former state fastness of fading can improve 0.5 grade, and its fastness to wet rubbing can improve 1 grade, thereby it should have a good application prospect as new class polyquaternium modification laking agent.
Comparative Examples 2
The micro-cross-linked PDMDAAC modification laking agent of different relative molecular mass sizes and constructional feature is listed in table 2 to the colour fixation of reactive brilliant bule KNR dyestuff on the cotton fabric.Wherein product is No. 1, No. 8 No. 16; Be respectively synthetic the obtaining of condition of embodiment 1 ~ 5 for No. 17 and No. 21; Laking agent LYPF is the commercially available PDMDAAC laking agent product that Shandong chemical industry ltd provides; Laking agent PDAC is the commercially available PDMDAAC laking agent product that Jiangsu chemical industry ltd provides, and laking agent Fix is certain external BA-SF company cationic fixing agent, and blank value is each dyestuff colour fastness value of (before the fixation) during fixation not.
The micro-cross-linked PDMDAAC modification of gained laking agent dry fastness all reaches the 4-5 level; Fastness to wet rubbing all can reach more than 3 ~ 4 grades; Calico staining all reaches the 4-5 level; Former state is faded and is all reached the 4-5 level, and it is better that wherein intrinsic viscosity scope cross-linkable monomer unit (TAMAC) molar content in 0.16-0.30 dL/g and structure thereof is controlled at 1% o'clock its fixing property, and its fixing property to dyestuffs such as reactive brilliant bule KNR on the cotton fabric is: dry fastness reaches the 4-5 level respectively; Fastness to wet rubbing preferably all can reach 4 grades; Calico staining all reaches the 4-5 level, and former state is faded and all reached the 4-5 level, obviously is superior to homemade unmodified PDMDAAC laking agent and similar cationic laking agent (laking agent Fix) commonly used; Before and after the fixation, its dry fastness, soap calico staining and the former state fastness integral body of fading can improve 0.5 grade, and its fastness to wet rubbing can improve 1 grade, thereby it should have a good application prospect as new class polyquaternium modification laking agent.