CN113402702B - Flame-retardant degradable PBS and preparation method thereof - Google Patents
Flame-retardant degradable PBS and preparation method thereof Download PDFInfo
- Publication number
- CN113402702B CN113402702B CN202110794585.9A CN202110794585A CN113402702B CN 113402702 B CN113402702 B CN 113402702B CN 202110794585 A CN202110794585 A CN 202110794585A CN 113402702 B CN113402702 B CN 113402702B
- Authority
- CN
- China
- Prior art keywords
- retardant
- flame
- pbs
- butanediol
- acid
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 239000003063 flame retardant Substances 0.000 title claims abstract description 42
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 title claims abstract description 40
- 238000002360 preparation method Methods 0.000 title claims abstract description 8
- KDYFGRWQOYBRFD-UHFFFAOYSA-N Succinic acid Natural products OC(=O)CCC(O)=O KDYFGRWQOYBRFD-UHFFFAOYSA-N 0.000 claims abstract description 104
- WERYXYBDKMZEQL-UHFFFAOYSA-N butane-1,4-diol Chemical compound OCCCCO WERYXYBDKMZEQL-UHFFFAOYSA-N 0.000 claims abstract description 42
- CDZXJJOGDCLNKX-UHFFFAOYSA-N 2,2,3,3-tetrafluorobutane-1,4-diol Chemical compound OCC(F)(F)C(F)(F)CO CDZXJJOGDCLNKX-UHFFFAOYSA-N 0.000 claims abstract description 39
- 239000001384 succinic acid Substances 0.000 claims abstract description 38
- YUDUFRYTKFGQCL-UHFFFAOYSA-N 2,2,3,3-tetrafluorobutanedioic acid Chemical compound OC(=O)C(F)(F)C(F)(F)C(O)=O YUDUFRYTKFGQCL-UHFFFAOYSA-N 0.000 claims abstract description 34
- KDYFGRWQOYBRFD-NUQCWPJISA-N butanedioic acid Chemical compound O[14C](=O)CC[14C](O)=O KDYFGRWQOYBRFD-NUQCWPJISA-N 0.000 claims abstract description 28
- 238000000034 method Methods 0.000 claims abstract description 24
- 238000006068 polycondensation reaction Methods 0.000 claims abstract description 19
- 238000006243 chemical reaction Methods 0.000 claims description 50
- KJIFKLIQANRMOU-UHFFFAOYSA-N oxidanium;4-methylbenzenesulfonate Chemical compound O.CC1=CC=C(S(O)(=O)=O)C=C1 KJIFKLIQANRMOU-UHFFFAOYSA-N 0.000 claims description 36
- 239000003054 catalyst Substances 0.000 claims description 30
- 238000005886 esterification reaction Methods 0.000 claims description 21
- YLQBMQCUIZJEEH-UHFFFAOYSA-N Furan Chemical compound C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 claims description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 14
- TXUICONDJPYNPY-UHFFFAOYSA-N (1,10,13-trimethyl-3-oxo-4,5,6,7,8,9,11,12,14,15,16,17-dodecahydrocyclopenta[a]phenanthren-17-yl) heptanoate Chemical compound C1CC2CC(=O)C=C(C)C2(C)C2C1C1CCC(OC(=O)CCCCCC)C1(C)CC2 TXUICONDJPYNPY-UHFFFAOYSA-N 0.000 claims description 12
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 12
- 229910021626 Tin(II) chloride Inorganic materials 0.000 claims description 12
- 229920000180 alkyd Polymers 0.000 claims description 12
- 235000011150 stannous chloride Nutrition 0.000 claims description 12
- 239000001119 stannous chloride Substances 0.000 claims description 12
- KSBAEPSJVUENNK-UHFFFAOYSA-L tin(ii) 2-ethylhexanoate Chemical compound [Sn+2].CCCCC(CC)C([O-])=O.CCCCC(CC)C([O-])=O KSBAEPSJVUENNK-UHFFFAOYSA-L 0.000 claims description 12
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 claims description 8
- 239000006227 byproduct Substances 0.000 claims description 8
- 229910052731 fluorine Inorganic materials 0.000 claims description 8
- 239000011737 fluorine Substances 0.000 claims description 8
- 230000032050 esterification Effects 0.000 claims description 7
- 239000012298 atmosphere Substances 0.000 claims description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 6
- 239000002131 composite material Substances 0.000 claims description 6
- 238000007599 discharging Methods 0.000 claims description 6
- 239000007789 gas Substances 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 6
- 229910052757 nitrogen Inorganic materials 0.000 claims description 6
- 239000001301 oxygen Substances 0.000 claims description 6
- 229910052760 oxygen Inorganic materials 0.000 claims description 6
- 229920000704 biodegradable plastic Polymers 0.000 abstract description 2
- 238000005265 energy consumption Methods 0.000 abstract description 2
- 239000002861 polymer material Substances 0.000 abstract description 2
- 238000012545 processing Methods 0.000 abstract description 2
- 230000035484 reaction time Effects 0.000 abstract description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 abstract 1
- 239000002253 acid Substances 0.000 abstract 1
- 230000000052 comparative effect Effects 0.000 description 10
- 229920000642 polymer Polymers 0.000 description 8
- 239000000047 product Substances 0.000 description 7
- 239000012299 nitrogen atmosphere Substances 0.000 description 6
- 239000000376 reactant Substances 0.000 description 6
- 239000001273 butane Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 4
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 4
- 238000006065 biodegradation reaction Methods 0.000 description 3
- 229920003023 plastic Polymers 0.000 description 3
- 239000004033 plastic Substances 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 2
- 102000004190 Enzymes Human genes 0.000 description 2
- 108090000790 Enzymes Proteins 0.000 description 2
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 2
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 2
- 229920006351 engineering plastic Polymers 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 238000005160 1H NMR spectroscopy Methods 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- 241000195493 Cryptophyta Species 0.000 description 1
- 241000233866 Fungi Species 0.000 description 1
- 229920002121 Hydroxyl-terminated polybutadiene Polymers 0.000 description 1
- 239000005062 Polybutadiene Substances 0.000 description 1
- 125000001931 aliphatic group Chemical group 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- CDQSJQSWAWPGKG-UHFFFAOYSA-N butane-1,1-diol Chemical compound CCCC(O)O CDQSJQSWAWPGKG-UHFFFAOYSA-N 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 229920002857 polybutadiene Polymers 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- KDYFGRWQOYBRFD-UHFFFAOYSA-L succinate(2-) Chemical compound [O-]C(=O)CCC([O-])=O KDYFGRWQOYBRFD-UHFFFAOYSA-L 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
- C08G63/68—Polyesters containing atoms other than carbon, hydrogen and oxygen
- C08G63/682—Polyesters containing atoms other than carbon, hydrogen and oxygen containing halogens
- C08G63/6824—Polyesters containing atoms other than carbon, hydrogen and oxygen containing halogens derived from polycarboxylic acids and polyhydroxy compounds
- C08G63/6826—Dicarboxylic acids and dihydroxy compounds
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
- C08G63/78—Preparation processes
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G2230/00—Compositions for preparing biodegradable polymers
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Polyesters Or Polycarbonates (AREA)
Abstract
Description
技术领域technical field
本发明涉及一种阻燃可降解及其制备方法,属于高分子材料加工技术领域。The invention relates to a flame retardant and degradable and a preparation method thereof, belonging to the technical field of polymer material processing.
背景技术Background technique
进入21世纪以来,白色污染越来越严重。随着生活水平的提高,人们开始越来越关注环 境问题。塑料作为我们日常生活中不可或缺的材料,它给人们带来方便的同时,也造成了严 重的环境污染。传统的工程塑料如PE、PP、PVC在我们的日常生活中已经得到了广泛的应 用。比如PE塑料袋,在我们的生活中随处可见,但是由于它们不可降解,在自然界中很难 分解,所以给环境带来了严重的污染。随着时间的流逝,环境问题变得越来越严重。解决环 境污染问题迫在眉睫,因此,必须寻找新的材料来替代传统的工程塑料。Since entering the 21st century, white pollution has become more and more serious. With the improvement of living standards, people have begun to pay more and more attention to environmental issues. As an indispensable material in our daily life, plastic not only brings convenience to people, but also causes serious environmental pollution. Traditional engineering plastics such as PE, PP, PVC have been widely used in our daily life. For example, PE plastic bags can be seen everywhere in our lives, but because they are not degradable, they are difficult to decompose in nature, so they have brought serious pollution to the environment. As time goes by, environmental problems become more and more serious. Solving the problem of environmental pollution is imminent, therefore, it is necessary to find new materials to replace traditional engineering plastics.
生物可降解材料是指一种可以被细菌、真菌、藻类、酶等自然界微生物降解的塑料,是 21世纪的新型材料。聚丁二酸丁二烯聚合(PBS)是一种具有良好生物降解性的脂肪族聚合物, 可被天然微生物或酶完全降解。高分子量PBS的机械性能与PE、PP相近,具有良好的耐热 性、耐化学腐蚀性和加工性,具有较高的机械强度。PBS由于其优异的综合性能,近年来受 到了广泛关注,越来越多的研究人员开始研究。目前,纯的PBS的合成方法主要是以丁二酸 和1,4-丁二醇直接缩聚得到PBS的直接酯化法。Biodegradable material refers to a plastic that can be degraded by natural microorganisms such as bacteria, fungi, algae, enzymes, etc. It is a new type of material in the 21st century. Polybutadiene succinate (PBS) is an aliphatic polymer with good biodegradability, which can be completely degraded by natural microorganisms or enzymes. The mechanical properties of high molecular weight PBS are similar to PE and PP, with good heat resistance, chemical resistance and processability, and high mechanical strength. Due to its excellent comprehensive properties, PBS has received extensive attention in recent years, and more and more researchers have begun to study it. At present, the synthesis method of pure PBS is mainly the direct esterification method of obtaining PBS by the direct polycondensation of succinic acid and 1,4-butanediol.
纯的PBS不具有超疏水以及阻燃性,使用过程中易燃易坏,使用范围因此受到一定的影 响。因此,开发阻燃、可降解、疏水的PBS具有十分重要的意义。Pure PBS does not have super-hydrophobicity and flame retardancy, and is flammable and easily damaged during use, which affects the scope of use. Therefore, the development of flame-retardant, degradable, and hydrophobic PBS is of great significance.
发明内容SUMMARY OF THE INVENTION
本发明的第一个目的是提供一种新的阻燃可降解PBS。The first object of the present invention is to provide a new flame-retardant and degradable PBS.
为达到本发明的第一个目的,本发明的阻燃可降解PBS采用如下方法制备得到:In order to achieve the first object of the present invention, the flame-retardant and degradable PBS of the present invention is prepared by the following method:
以丁二酸、四氟丁二酸、2,2,3,3-四氟-1,4-丁二醇、1,4-丁二醇缩聚得到PBS;PBS is obtained by polycondensation with succinic acid, tetrafluorosuccinic acid, 2,2,3,3-tetrafluoro-1,4-butanediol and 1,4-butanediol;
所述丁二酸、四氟丁二酸、2,2,3,3-四氟-1,4-丁二醇、1,4-丁二醇的醇酸摩尔比为1.1~ 1.5:1,且四氟丁二酸和2,2,3,3-四氟-1,4-丁二醇不同时为0。The alkyd molar ratio of succinic acid, tetrafluorosuccinic acid, 2,2,3,3-tetrafluoro-1,4-butanediol and 1,4-butanediol is 1.1-1.5:1, And tetrafluorosuccinic acid and 2,2,3,3-tetrafluoro-1,4-butanediol are not 0 at the same time.
所述丁二酸、四氟丁二酸、2,2,3,3-四氟-1,4-丁二醇、1,4-丁二醇的醇酸摩尔比为1.1~ 1.5:1,即2,2,3,3-四氟-1,4-丁二醇、1,4-丁二醇与丁二酸和四氟丁二酸的摩尔比为1.1~1.5:1。The alkyd molar ratio of succinic acid, tetrafluorosuccinic acid, 2,2,3,3-tetrafluoro-1,4-butanediol and 1,4-butanediol is 1.1-1.5:1, That is, the molar ratio of 2,2,3,3-tetrafluoro-1,4-butanediol and 1,4-butanediol to succinic acid and tetrafluorosuccinic acid is 1.1 to 1.5:1.
在一种具体实施方式中,所述阻燃可降解PBS采用如下方法制备得到:以丁二酸、2,2,3,3- 四氟-1,4-丁二醇缩聚得到PBS。In a specific embodiment, the flame-retardant and degradable PBS is prepared by the following method: PBS is obtained by polycondensation of succinic acid and 2,2,3,3-tetrafluoro-1,4-butanediol.
所述醇酸摩尔比是指羟基与羧基的摩尔比。The alkyd molar ratio refers to the molar ratio of hydroxyl groups to carboxyl groups.
在一种具体实施方式中,所述阻燃可降解PBS的结构式如下:In a specific embodiment, the structural formula of the flame-retardant and degradable PBS is as follows:
n为100~180。 n is 100-180.
在一种具体实施方式中,所述方法包括:In a specific embodiment, the method includes:
a.酯化:将丁二酸、四氟丁二酸、2,2,3,3-四氟-1,4-丁二醇、1,4-丁二醇、催化剂混合, 在氮气或惰性气体氛围下升温至120~130℃,待反应体系变透明后加热到150~160℃反应 1.5~2h;a. Esterification: Mix succinic acid, tetrafluorosuccinic acid, 2,2,3,3-tetrafluoro-1,4-butanediol, 1,4-butanediol, catalyst, under nitrogen or inert The temperature is raised to 120-130°C under a gas atmosphere, and the reaction system is heated to 150-160°C for 1.5-2h after the reaction system becomes transparent;
b.缩聚:在a步骤反应结束后,升温至220~240℃,压力为0~200Pa的条件下反应3~ 3.5h后得到阻燃可降解PBS;b. Polycondensation: after the reaction in step a, the temperature is raised to 220-240°C, and the pressure is 0-200Pa for 3-3.5 hours to obtain flame-retardant and degradable PBS;
优选还包括先将a步骤反应产生的水和含氟的呋喃副产物排出反应体系后再进行b步骤。Preferably, it also includes first discharging the water and fluorine-containing furan by-products produced in the reaction of step a out of the reaction system, and then performing step b.
在一种具体实施方式中,所述催化剂为氯化亚锡或辛酸亚锡中的至少一种和对甲苯磺酸 一水合物组成的复合催化剂。In a specific embodiment, the catalyst is a composite catalyst composed of at least one of stannous chloride or stannous octoate and p-toluenesulfonic acid monohydrate.
在一种具体实施方式中,所述氯化亚锡或辛酸亚锡的用量为丁二酸与四氟丁二酸摩尔总 量的1~1.2‰;所述对甲苯磺酸一水合物的用量优选为丁二酸与四氟丁二酸摩尔总量的1~ 1.5‰。In a specific embodiment, the dosage of the stannous chloride or stannous octoate is 1-1.2‰ of the total molar amount of succinic acid and tetrafluorosuccinic acid; the dosage of the p-toluenesulfonic acid monohydrate It is preferably 1 to 1.5‰ of the total molar amount of succinic acid and tetrafluorosuccinic acid.
在一种具体实施方式中,所述阻燃可降解PBS的极限氧指数为28以上,优选为28~31; 接触角105~110;结晶度40~43。In a specific embodiment, the limiting oxygen index of the flame-retardant and degradable PBS is above 28, preferably 28-31; the contact angle is 105-110; the crystallinity is 40-43.
本发明的第二个目的是提供一种上述的阻燃可降解PBS的制备方法。The second object of the present invention is to provide a method for preparing the above-mentioned flame-retardant and degradable PBS.
为达到本发明的第二个目的,所述的阻燃可降解PBS的制备方法包括:In order to achieve the second object of the present invention, the preparation method of the flame-retardant and degradable PBS includes:
a.酯化:将丁二酸、四氟丁二酸、2,2,3,3-四氟-1,4-丁二醇、1,4-丁二醇、催化剂混合, 在氮气或惰性气体氛围下升温至120~130℃,待反应体系变透明后加热到150~160℃反应 1.5~2h;a. Esterification: Mix succinic acid, tetrafluorosuccinic acid, 2,2,3,3-tetrafluoro-1,4-butanediol, 1,4-butanediol, catalyst, under nitrogen or inert The temperature is raised to 120-130°C under a gas atmosphere, and the reaction system is heated to 150-160°C for 1.5-2h after the reaction system becomes transparent;
b.缩聚:在a步骤反应结束后,升温至220~240℃,压力为0~200Pa的条件下反应3~3.5h后得到阻燃可降解PBS;b. Polycondensation: after the reaction in step a, the temperature is raised to 220 to 240 ° C, and the pressure is 0 to 200 Pa to react for 3 to 3.5 hours to obtain flame-retardant and degradable PBS;
优选还包括先将a步骤反应产生的水和含氟的呋喃副产物排出反应体系后再进行b步骤。Preferably, it also includes first discharging the water and fluorine-containing furan by-products produced in the reaction of step a out of the reaction system, and then performing step b.
在一种具体实施方式中,所述催化剂为氯化亚锡或辛酸亚锡中的至少一种和对甲苯磺酸 一水合物组成的复合催化剂。In a specific embodiment, the catalyst is a composite catalyst composed of at least one of stannous chloride or stannous octoate and p-toluenesulfonic acid monohydrate.
在一种具体实施方式中,所述氯化亚锡或辛酸亚锡的用量为丁二酸与四氟丁二酸摩尔总 量的1~1.2‰;所述对甲苯磺酸一水合物的用量优选为丁二酸与四氟丁二酸摩尔总量的1~ 1.5‰。In a specific embodiment, the dosage of the stannous chloride or stannous octoate is 1-1.2‰ of the total molar amount of succinic acid and tetrafluorosuccinic acid; the dosage of the p-toluenesulfonic acid monohydrate It is preferably 1 to 1.5‰ of the total molar amount of succinic acid and tetrafluorosuccinic acid.
有益效果:Beneficial effects:
(1)本发明的PBS具有疏水和阻燃性。(1) The PBS of the present invention has hydrophobicity and flame retardancy.
(2)本发明的PBS和纯PBS一样具有良好的生物降解性,其拓宽了生物降解塑料的领 域。(2) The PBS of the present invention has good biodegradability like pure PBS, which broadens the field of biodegradable plastics.
(3)本发明工艺简单可控,反应时间短、能耗低,具有良好的工业应用前景。(3) The process of the invention is simple and controllable, the reaction time is short, the energy consumption is low, and the invention has a good prospect of industrial application.
附图说明Description of drawings
图1为本发产品的1H-NMR图。Figure 1 is the 1 H-NMR chart of the product of the present invention.
具体实施方式Detailed ways
为达到本发明的第一个目的,本发明的阻燃可降解PBS采用如下方法制备得到:In order to achieve the first object of the present invention, the flame-retardant and degradable PBS of the present invention is prepared by the following method:
以丁二酸、四氟丁二酸、2,2,3,3-四氟-1,4-丁二醇、1,4-丁二醇缩聚得到PBS;PBS is obtained by polycondensation with succinic acid, tetrafluorosuccinic acid, 2,2,3,3-tetrafluoro-1,4-butanediol and 1,4-butanediol;
所述丁二酸、四氟丁二酸、2,2,3,3-四氟-1,4-丁二醇、1,4-丁二醇的醇酸摩尔比为1.1~ 1.5:1,且四氟丁二酸和2,2,3,3-四氟-1,4-丁二醇不同时为0。The alkyd molar ratio of succinic acid, tetrafluorosuccinic acid, 2,2,3,3-tetrafluoro-1,4-butanediol and 1,4-butanediol is 1.1-1.5:1, And tetrafluorosuccinic acid and 2,2,3,3-tetrafluoro-1,4-butanediol are not 0 at the same time.
所述丁二酸、四氟丁二酸、2,2,3,3-四氟-1,4-丁二醇、1,4-丁二醇的醇酸摩尔比为1.1~ 1.5:1,即2,2,3,3-四氟-1,4-丁二醇、1,4-丁二醇与丁二酸和四氟丁二酸的摩尔比为1.1~1.5:1。The alkyd molar ratio of succinic acid, tetrafluorosuccinic acid, 2,2,3,3-tetrafluoro-1,4-butanediol and 1,4-butanediol is 1.1-1.5:1, That is, the molar ratio of 2,2,3,3-tetrafluoro-1,4-butanediol and 1,4-butanediol to succinic acid and tetrafluorosuccinic acid is 1.1 to 1.5:1.
在一种具体实施方式中,所述阻燃可降解PBS采用如下方法制备得到:以丁二酸、2,2,3,3- 四氟-1,4-丁二醇缩聚得到PBS。In a specific embodiment, the flame-retardant and degradable PBS is prepared by the following method: PBS is obtained by polycondensation of succinic acid and 2,2,3,3-tetrafluoro-1,4-butanediol.
所述醇酸摩尔比是指羟基与羧基的摩尔比。The alkyd molar ratio refers to the molar ratio of hydroxyl groups to carboxyl groups.
在一种具体实施方式中,所述阻燃可降解PBS的结构式如下:In a specific embodiment, the structural formula of the flame-retardant and degradable PBS is as follows:
n为100~180。 n is 100-180.
在一种具体实施方式中,所述方法包括:In a specific embodiment, the method includes:
a.酯化:将丁二酸、四氟丁二酸、2,2,3,3-四氟-1,4-丁二醇、1,4-丁二醇、催化剂混合, 在氮气或惰性气体氛围下升温至120~130℃,待反应体系变透明后加热到150~160℃反应 1.5~2h;a. Esterification: Mix succinic acid, tetrafluorosuccinic acid, 2,2,3,3-tetrafluoro-1,4-butanediol, 1,4-butanediol, catalyst, under nitrogen or inert The temperature is raised to 120-130°C under a gas atmosphere, and the reaction system is heated to 150-160°C for 1.5-2h after the reaction system becomes transparent;
b.缩聚:在a步骤反应结束后,升温至220~240℃,压力为0~200Pa的条件下反应3~ 3.5h后得到阻燃可降解PBS;b. Polycondensation: after the reaction in step a, the temperature is raised to 220-240°C, and the pressure is 0-200Pa for 3-3.5 hours to obtain flame-retardant and degradable PBS;
优选还包括先将a步骤反应产生的水和含氟的呋喃副产物排出反应体系后再进行b步骤。Preferably, it also includes first discharging the water and fluorine-containing furan by-products produced in the reaction of step a out of the reaction system, and then performing step b.
在一种具体实施方式中,所述催化剂为氯化亚锡或辛酸亚锡中的至少一种和对甲苯磺酸 一水合物组成的复合催化剂。In a specific embodiment, the catalyst is a composite catalyst composed of at least one of stannous chloride or stannous octoate and p-toluenesulfonic acid monohydrate.
在一种具体实施方式中,所述氯化亚锡或辛酸亚锡的用量为丁二酸与四氟丁二酸摩尔总 量的1~1.2‰;所述对甲苯磺酸一水合物的用量优选为丁二酸与四氟丁二酸摩尔总量的1~ 1.5‰。In a specific embodiment, the dosage of the stannous chloride or stannous octoate is 1-1.2‰ of the total molar amount of succinic acid and tetrafluorosuccinic acid; the dosage of the p-toluenesulfonic acid monohydrate It is preferably 1 to 1.5‰ of the total molar amount of succinic acid and tetrafluorosuccinic acid.
在一种具体实施方式中,所述阻燃可降解PBS的极限氧指数为28以上,优选为28~31; 接触角105~110;结晶度40~43。In a specific embodiment, the limiting oxygen index of the flame-retardant and degradable PBS is above 28, preferably 28-31; the contact angle is 105-110; the crystallinity is 40-43.
本发明的第二个目的是提供一种上述的阻燃可降解PBS的制备方法。The second object of the present invention is to provide a method for preparing the above-mentioned flame-retardant and degradable PBS.
为达到本发明的第二个目的,所述的阻燃可降解PBS的制备方法包括:In order to achieve the second object of the present invention, the preparation method of the flame-retardant and degradable PBS includes:
a.酯化:将丁二酸、四氟丁二酸、2,2,3,3-四氟-1,4-丁二醇、1,4-丁二醇、催化剂混合, 在氮气或惰性气体氛围下升温至120~130℃,待反应体系变透明后加热到150~160℃反应 1.5~2h;a. Esterification: Mix succinic acid, tetrafluorosuccinic acid, 2,2,3,3-tetrafluoro-1,4-butanediol, 1,4-butanediol, catalyst, under nitrogen or inert The temperature is raised to 120-130°C under a gas atmosphere, and the reaction system is heated to 150-160°C for 1.5-2h after the reaction system becomes transparent;
b.缩聚:在a步骤反应结束后,升温至220~240℃,压力为0~200Pa的条件下反应3~ 3.5h后得到阻燃可降解PBS;b. Polycondensation: after the reaction in step a, the temperature is raised to 220-240°C, and the pressure is 0-200Pa for 3-3.5 hours to obtain flame-retardant and degradable PBS;
优选还包括先将a步骤反应产生的水和含氟的呋喃副产物排出反应体系后再进行b步骤。Preferably, it also includes first discharging the water and fluorine-containing furan by-products produced in the reaction of step a out of the reaction system, and then performing step b.
在一种具体实施方式中,所述催化剂为氯化亚锡或辛酸亚锡中的至少一种和对甲苯磺酸 一水合物组成的复合催化剂。In a specific embodiment, the catalyst is a composite catalyst composed of at least one of stannous chloride or stannous octoate and p-toluenesulfonic acid monohydrate.
在一种具体实施方式中,所述氯化亚锡或辛酸亚锡的用量为丁二酸与四氟丁二酸摩尔总 量的1~1.2‰;所述对甲苯磺酸一水合物的用量优选为丁二酸与四氟丁二酸摩尔总量的1~ 1.5‰。In a specific embodiment, the dosage of the stannous chloride or stannous octoate is 1-1.2‰ of the total molar amount of succinic acid and tetrafluorosuccinic acid; the dosage of the p-toluenesulfonic acid monohydrate It is preferably 1 to 1.5‰ of the total molar amount of succinic acid and tetrafluorosuccinic acid.
下面结合实施例对本发明的具体实施方式做进一步的描述,并不因此将本发明限制在所 述的实施例范围之中。The specific embodiments of the present invention will be further described below in conjunction with the examples, and therefore the present invention is not limited to the scope of the described examples.
实施例1Example 1
在氮气氛围下,向装有搅拌器、温度计、分水器和球形冷凝管的反应系统中投入丁二酸、 2,2,3,3-四氟-1,4-丁二醇和催化剂,其中丁二酸的用量为2mol,2,2,3,3-四氟-1,4-丁二醇与丁二 酸摩尔比为1.1:1,即丁二酸为236.18g,2,2,3,3-四氟-1,4-丁二醇为356.58g,催化剂用量为 SnCl2·2H2O为丁二酸的1‰mol和对甲苯磺酸一水合物为丁二酸的1.5‰mol,常压下搅拌反 应,温度先升至120℃,反应物熔化至体系变透明,随后加热到150℃,开始酯化反应,反应 过程中生成的水和副产物含氟呋喃排出体系,酯化反应2h,酯化反应结束;Under a nitrogen atmosphere, succinic acid, 2,2,3,3-tetrafluoro-1,4-butanediol and a catalyst were put into a reaction system equipped with a stirrer, a thermometer, a water separator and a spherical condenser, wherein The dosage of succinic acid is 2mol, the molar ratio of 2,2,3,3-tetrafluoro-1,4-butanediol to succinic acid is 1.1:1, that is, succinic acid is 236.18g, 2,2,3 ,3-tetrafluoro-1,4-butanediol is 356.58g, the catalyst dosage is SnCl 2 ·2H 2 O is 1‰mol of succinic acid and p-toluenesulfonic acid monohydrate is 1.5‰mol of succinic acid , the reaction is stirred under normal pressure, the temperature is first raised to 120 ° C, the reactant is melted until the system becomes transparent, and then heated to 150 ° C to start the esterification reaction, the water and by-product fluorine-containing furan generated during the reaction process are discharged from the system, and the esterification Reaction 2h, esterification reaction finishes;
接着升温至230℃,压力100Pa的条件下进行缩聚反应,反应3h后,得到产物F-PBS-1, F-PBS-1的1H-NMR图详见图1。Then the temperature was raised to 230°C, and the polycondensation reaction was carried out under the pressure of 100Pa. After the reaction for 3 hours, the product F-PBS- 1 was obtained.
由图可见F-PBS-1的结构是n为140~160。It can be seen from the figure that the structure of F-PBS-1 is n is 140-160.
实施例2Example 2
氮气氛围下,向装有搅拌器、温度计、分水器和球形冷凝管的反应系统中投入丁二酸、 2,2,3,3-四氟-1,4-丁二醇和催化剂,其中丁二酸的用量为2mol,2,2,3,3-四氟-1,4-丁二醇与丁二 酸摩尔比为1.2:1,即丁二酸为236.18g,2,2,3,3-四氟-1,4-丁二醇为388.99g,催化剂用量为 SnCl2·2H2O为丁二酸的1‰mol和对甲苯磺酸一水合物为丁二酸的1.5‰mol,常压下搅拌反 应,温度先升至120℃,反应物熔化至体系变透明,随后加热到150℃,开始酯化反应,反应 过程中生成的水和副产物含氟呋喃排出体系,酯化反应2h,酯化反应结束;Under nitrogen atmosphere, put succinic acid, 2,2,3,3-tetrafluoro-1,4-butanediol and catalyst into the reaction system equipped with stirrer, thermometer, water separator and spherical condenser, among which butane The amount of diacid is 2mol, and the molar ratio of 2,2,3,3-tetrafluoro-1,4-butanediol to succinic acid is 1.2:1, that is, succinic acid is 236.18g, 2,2,3, 3-tetrafluoro-1,4-butanediol is 388.99g, the catalyst dosage is SnCl 2 ·2H 2 O is 1‰mol of succinic acid and p-toluenesulfonic acid monohydrate is 1.5‰mol of succinic acid, The reaction was stirred under normal pressure, the temperature was first raised to 120°C, the reactants were melted until the system became transparent, and then heated to 150°C to start the esterification reaction. 2h, the esterification reaction ends;
接着升温至230℃,压力100Pa的条件下进行缩聚反应,反应3h后,得到产物F-PBS-2。 其中n为140~160。Then, the temperature was raised to 230° C. and the polycondensation reaction was carried out under the condition of a pressure of 100 Pa. After the reaction for 3 hours, the product F-PBS-2 was obtained. Among them, n is 140~160.
实施例3Example 3
氮气氛围下,向装有搅拌器、温度计、分水器和球形冷凝管的反应系统中投入丁二酸、 2,2,3,3-四氟-1,4-丁二醇和催化剂,其中丁二酸的用量为2mol,2,2,3,3-四氟-1,4-丁二醇与丁二 酸摩尔比为1.3:1,即丁二酸为236.18g,2,2,3,3-四氟-1,4-丁二醇为421.41g,催化剂用量为 SnCl2·2H2O为丁二酸的1‰mol和对甲苯磺酸一水合物为丁二酸的1.5‰mol,常压下搅拌反 应,温度先升至120℃,反应物熔化至体系变透明,随后加热到150℃,开始酯化反应,反应 过程中生成的水和副产物含氟呋喃排出体系,酯化反应2h,酯化反应结束;Under nitrogen atmosphere, put succinic acid, 2,2,3,3-tetrafluoro-1,4-butanediol and catalyst into the reaction system equipped with stirrer, thermometer, water separator and spherical condenser, among which butane The amount of diacid is 2mol, the molar ratio of 2,2,3,3-tetrafluoro-1,4-butanediol to succinic acid is 1.3:1, that is, succinic acid is 236.18g, 2,2,3, 3-tetrafluoro-1,4-butanediol is 421.41g, the catalyst dosage is SnCl 2 ·2H 2 O is 1‰mol of succinic acid and p-toluenesulfonic acid monohydrate is 1.5‰mol of succinic acid, The reaction was stirred under normal pressure, the temperature was first raised to 120°C, the reactants were melted until the system became transparent, and then heated to 150°C to start the esterification reaction. 2h, the esterification reaction ends;
接着升温至230℃,压力100Pa的条件下进行缩聚反应,反应3h后,得到产物F-PBS-3。 其中n为140~160。Then, the temperature was raised to 230° C., and the polycondensation reaction was carried out under the condition of a pressure of 100 Pa. After the reaction for 3 hours, the product F-PBS-3 was obtained. Among them, n is 140~160.
实施例4Example 4
氮气氛围下,向装有搅拌器、温度计、分水器和球形冷凝管的反应系统中投入丁二酸、 2,2,3,3-四氟-1,4-丁二醇和催化剂,其中丁二酸的用量为2mol,2,2,3,3-四氟-1,4-丁二醇与丁二 酸摩尔比为1.4:1,即丁二酸为236.18g,2,2,3,3-四氟-1,4-丁二醇为453.82g,催化剂用量为 SnCl2·2H2O为丁二酸的1‰mol和对甲苯磺酸一水合物为丁二酸的1.5‰mol,常压下搅拌反 应,温度先升至120℃,反应物熔化至体系变透明,随后加热到150℃,开始酯化反应,反应 过程中生成的水和副产物含氟呋喃排出体系,酯化反应2h,酯化反应结束;Under nitrogen atmosphere, put succinic acid, 2,2,3,3-tetrafluoro-1,4-butanediol and catalyst into the reaction system equipped with stirrer, thermometer, water separator and spherical condenser, among which butane The amount of diacid is 2mol, and the molar ratio of 2,2,3,3-tetrafluoro-1,4-butanediol to succinic acid is 1.4:1, that is, succinic acid is 236.18g, 2,2,3, 3-tetrafluoro-1,4-butanediol is 453.82g, the catalyst dosage is SnCl 2 ·2H 2 O is 1‰mol of succinic acid and p-toluenesulfonic acid monohydrate is 1.5‰mol of succinic acid, The reaction was stirred under normal pressure, the temperature was first raised to 120°C, the reactants were melted until the system became transparent, and then heated to 150°C to start the esterification reaction. 2h, the esterification reaction ends;
接着升温至230℃,压力100Pa的条件下进行缩聚反应,反应3h后,得到产物F-PBS-4。 其中n为140~160。Then, the temperature was raised to 230° C., and the polycondensation reaction was carried out under the condition of a pressure of 100 Pa. After the reaction for 3 hours, the product F-PBS-4 was obtained. Among them, n is 140~160.
实施例5Example 5
氮气氛围下,向装有搅拌器、温度计、分水器和球形冷凝管的反应系统中投入丁二酸、 2,2,3,3-四氟-1,4-丁二醇和催化剂,其中丁二酸的用量为2mol,2,2,3,3-四氟-1,4-丁二醇与丁二 酸摩尔比为1.5:1,即丁二酸为236.18g,2,2,3,3-四氟-1,4-丁二醇为486.24g,催化剂用量为 SnCl2·2H2O为丁二酸的1‰mol和对甲苯磺酸一水合物为丁二酸的1.5‰mol,常压下搅拌反 应,温度先升至120℃,反应物熔化至体系变透明,随后加热到150℃,开始酯化反应,反应 过程中生成的水和副产物含氟呋喃排出体系,酯化反应2h,酯化反应结束;Under nitrogen atmosphere, put succinic acid, 2,2,3,3-tetrafluoro-1,4-butanediol and catalyst into the reaction system equipped with stirrer, thermometer, water separator and spherical condenser, among which butane The amount of diacid is 2mol, and the molar ratio of 2,2,3,3-tetrafluoro-1,4-butanediol to succinic acid is 1.5:1, that is, succinic acid is 236.18g, 2,2,3, 3-tetrafluoro-1,4-butanediol is 486.24g, the catalyst dosage is SnCl 2 ·2H 2 O is 1‰mol of succinic acid and p-toluenesulfonic acid monohydrate is 1.5‰mol of succinic acid, The reaction was stirred under normal pressure, the temperature was first raised to 120°C, the reactants were melted until the system became transparent, and then heated to 150°C to start the esterification reaction. 2h, the esterification reaction ends;
接着升温至230℃,压力100Pa的条件下进行缩聚反应,反应3h后,得到产物F-PBS-5。 其中n为140~160。Then the temperature was raised to 230°C, and the polycondensation reaction was carried out under the condition of a pressure of 100Pa. After the reaction for 3 hours, the product F-PBS-5 was obtained. Among them, n is 140~160.
对比例1Comparative Example 1
氮气氛围下,向装有搅拌器、温度计、分水器和球形冷凝管的反应系统中投入丁二酸、 1,4-丁二醇和催化剂,其中丁二酸的用量为2mol,1,4-丁二醇与丁二酸摩尔比为1.3:1,即丁 二酸为236.18g,1,4-丁二醇为234.31g,催化剂用量为SnCl2·2H2O为丁二酸的1‰mol和对甲 苯磺酸一水合物为丁二酸的1.5‰mol,常压下搅拌反应,温度先升至120℃,反应物熔化至 体系变透明,随后加热到150℃,开始酯化反应,反应过程中生成的水和副产物四氢呋喃排 出体系,酯化反应2h,酯化反应结束;Under nitrogen atmosphere, put succinic acid, 1,4-butanediol and catalyst into the reaction system equipped with stirrer, thermometer, water separator and spherical condenser, wherein the consumption of succinic acid is 2mol, 1,4- The molar ratio of butanediol and succinic acid is 1.3:1, that is, succinic acid is 236.18g, 1,4-butanediol is 234.31g, and the catalyst dosage is SnCl 2 ·2H 2 O is 1‰mol of succinic acid and p-toluenesulfonic acid monohydrate is 1.5‰mol of succinic acid, and the reaction is stirred under normal pressure. The temperature first rises to 120 ° C, the reactant melts until the system becomes transparent, and then heated to 150 ° C to start the esterification reaction, the reaction The water and by-product tetrahydrofuran generated in the process are discharged from the system, and the esterification reaction is 2h, and the esterification reaction ends;
接着升温至230℃,压力100Pa的条件下进行缩聚反应,反应3h后,得到产物纯PBS。Then the temperature was raised to 230° C., and the polycondensation reaction was carried out under the condition of a pressure of 100 Pa. After the reaction for 3 hours, the product pure PBS was obtained.
本发明实施例1-5得到含氟PBS结晶度分别为42.3,41.5,40.6,40.8,42.1,具有良好 的生物降解性。对比例1制备得到的纯PBS结晶度41。实施例1-5与对比例1的特性粘度结果如下表1所示:The crystallinity of the fluorine-containing PBS obtained in Examples 1-5 of the present invention are 42.3, 41.5, 40.6, 40.8, and 42.1, respectively, and have good biodegradability. The crystallinity of pure PBS prepared in Comparative Example 1 was 41. The intrinsic viscosity results of Examples 1-5 and Comparative Example 1 are shown in Table 1 below:
表1实施例1-5与纯PBS的特性粘度Table 1 Intrinsic Viscosity of Examples 1-5 and Pure PBS
以上特性粘度测试:以氯仿为溶剂,配制浓度为0.5g/dL的PBS或PBS/HTPB溶液,使用内径0.38mm乌氏粘度计在25℃下测定。实验结果采用“一点法”计算:The above intrinsic viscosity test: use chloroform as a solvent to prepare a PBS or PBS/HTPB solution with a concentration of 0.5g/dL, and use an Ubbelohde viscometer with an inner diameter of 0.38mm to measure at 25°C. The experimental results are calculated using the "one-point method":
式中,t与t0分别为聚合物溶液与纯溶剂的流出时间;C为聚合物溶液的浓度。In the formula, t and t 0 are the outflow time of the polymer solution and the pure solvent, respectively; C is the concentration of the polymer solution.
实施例1-5与对比例1的纯PBS极限氧指数结果如下表2所示:The pure PBS limiting oxygen index results of Examples 1-5 and Comparative Example 1 are shown in Table 2 below:
表2实施例1-5与对比例1的纯PBS的极限氧指数Table 2 Limiting oxygen index of pure PBS of Examples 1-5 and Comparative Example 1
实施例1-5与纯PBS的接触角测试结果如下表3所示:The contact angle test results of Examples 1-5 and pure PBS are shown in Table 3 below:
表3实施例1-5与对比例1纯PBS的接触角测试结果The contact angle test result of table 3 embodiment 1-5 and comparative example 1 pure PBS
实施例1-5与对比例1的纯PBS的结晶度如下表4所示:The crystallinity of the pure PBS of Examples 1-5 and Comparative Example 1 is shown in Table 4 below:
表4实施例1-5与对比例1的纯PBS的结晶度Table 4 Crystallinity of pure PBS of Examples 1-5 and Comparative Example 1
实施例1-5与对比例1的纯PBS的生物降解性能如下表5所示:The biodegradation properties of the pure PBS of Examples 1-5 and Comparative Example 1 are shown in Table 5 below:
表5实施例1-5与对比例1的纯PBS的生物降解性能Table 5 Biodegradation properties of pure PBS of Examples 1-5 and Comparative Example 1
生物降解性能测试是将10g样品埋入土壤里,30天后取出洗净烘干称取质量。The biodegradation performance test is to bury 10g of the sample in the soil, take it out after 30 days, wash it, dry it, and weigh it.
Claims (14)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110794585.9A CN113402702B (en) | 2021-07-14 | 2021-07-14 | Flame-retardant degradable PBS and preparation method thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110794585.9A CN113402702B (en) | 2021-07-14 | 2021-07-14 | Flame-retardant degradable PBS and preparation method thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
CN113402702A CN113402702A (en) | 2021-09-17 |
CN113402702B true CN113402702B (en) | 2022-07-15 |
Family
ID=77686306
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202110794585.9A Active CN113402702B (en) | 2021-07-14 | 2021-07-14 | Flame-retardant degradable PBS and preparation method thereof |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN113402702B (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113372543B (en) * | 2021-04-20 | 2022-07-19 | 四川轻化工大学 | Low-crystallinity PBS (Poly Butylene succinate) and preparation method thereof |
CN114149576A (en) * | 2021-11-26 | 2022-03-08 | 南京桐君新材料科技有限公司 | Fluorine-containing polycarbonate diol and preparation method thereof |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103788346A (en) * | 2012-10-29 | 2014-05-14 | 中国石油化工股份有限公司 | Biodegradable polyester and preparation method thereof |
CN104693428A (en) * | 2015-03-17 | 2015-06-10 | 江苏钟腾化工有限公司 | Preparation method of high-molecular weight poly(butylene succinate) |
CN113025008A (en) * | 2021-03-19 | 2021-06-25 | 厦门峰百塑胶有限公司 | Wear-resistant plastic bag and preparation method thereof |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2395036A1 (en) * | 2010-05-17 | 2011-12-14 | Bayer MaterialScience AG | Polyurethane dispersions with an acid-base mixture as an additive |
KR20160069324A (en) * | 2014-12-08 | 2016-06-16 | 에스케이이노베이션 주식회사 | Composition and manufacture method of excellent biodegradable and selectively permeable films |
CN108203498A (en) * | 2016-12-20 | 2018-06-26 | 青岛祥智电子技术有限公司 | The preparation method of the poly butylene succinate of high molecular weight |
CN113372543B (en) * | 2021-04-20 | 2022-07-19 | 四川轻化工大学 | Low-crystallinity PBS (Poly Butylene succinate) and preparation method thereof |
CN114479026B (en) * | 2022-02-11 | 2023-07-28 | 山东元利科技有限公司 | PBS preparation method without by-product tetrahydrofuran |
-
2021
- 2021-07-14 CN CN202110794585.9A patent/CN113402702B/en active Active
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103788346A (en) * | 2012-10-29 | 2014-05-14 | 中国石油化工股份有限公司 | Biodegradable polyester and preparation method thereof |
CN104693428A (en) * | 2015-03-17 | 2015-06-10 | 江苏钟腾化工有限公司 | Preparation method of high-molecular weight poly(butylene succinate) |
CN113025008A (en) * | 2021-03-19 | 2021-06-25 | 厦门峰百塑胶有限公司 | Wear-resistant plastic bag and preparation method thereof |
Also Published As
Publication number | Publication date |
---|---|
CN113402702A (en) | 2021-09-17 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN113402702B (en) | Flame-retardant degradable PBS and preparation method thereof | |
CN110746457B (en) | Ionic monomer containing phosphonate structure, flame-retardant and smoke-suppressing ionomer catalyzed and synthesized by the same, and their preparation method and application | |
WO2022126812A1 (en) | Biodegradable aliphatic-aromatic copolyester and synthesis method therefor | |
CN112920385B (en) | Preparation method of poly (butylene succinate) and copolymer thereof | |
CN103524722B (en) | A kind of fluorine-containing PBT atactic polyester and preparation method thereof | |
CN104725615A (en) | Poly butylene glycol ester synthesis process by biologic organic guanidine catalysis method | |
CN109575257B (en) | Poly-2,5-furandicarboxylic acid-1,4-succinic acid neopentyl glycol ester and preparation method and product thereof | |
CN103556294A (en) | Creep-resistant hydrolysis-resistance polyester and its preparation method | |
CN103556289B (en) | Creep-resistant polyester and its preparation method | |
CN113372543B (en) | Low-crystallinity PBS (Poly Butylene succinate) and preparation method thereof | |
CN114456565B (en) | Carbon dioxide-based polylactic acid copolymer modified cellulose material and preparation method thereof | |
CN103467718B (en) | A kind of fluorine-containing PET-PTT copolyesters and preparation method thereof | |
CN109293907B (en) | A kind of high molecular weight polyester based on biomass as monomer, preparation method and use | |
CN108623795B (en) | A kind of polyester based on whole biomass monomer, preparation method and use | |
CN103435774A (en) | Method for modifying polyester bioelastomer | |
CN103467722B (en) | A kind of fluorine-containing PTT-PBT copolyesters and preparation method thereof | |
CN116199871A (en) | All-bio-based polyester and preparation method thereof | |
CN114702656B (en) | A kind of carbon dioxide-based lactic acid copolymer and preparation method thereof | |
CN103469358B (en) | A kind of preparation method of fluorine-containing PTT-PTT core-skin composite fiber | |
CN103469356B (en) | A kind of preparation method of fluorine-containing PET-PET core-skin composite fiber | |
JP2022146911A (en) | Polyester and method for producing the same | |
CN103467721B (en) | A kind of preparation method of fluorine-containing PTT polyester | |
CN118085250B (en) | Poly(terephthalate-adipate-carbonate-butylene glycol) and preparation method thereof | |
CN115785429B (en) | Flame-retardant carbon dioxide-based polycarbonate and preparation method thereof | |
CN115785416B (en) | A kind of polyoxalate (ethylene glycol-co-diethylene glycol) ester and its preparation method |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant | ||
TR01 | Transfer of patent right | ||
TR01 | Transfer of patent right |
Effective date of registration: 20230526 Address after: 610400 No.3 Guangdong Road, Chengdu ABA Industrial Development Zone, Jintang County, Chengdu City, Sichuan Province Patentee after: Sichuan xinghuiteng Group Co.,Ltd. Address before: No. 180, Huidong Xueyuan street, Zigong, Sichuan, 643033 Patentee before: Sichuan University of Science & Engineering |