Rubber composition containing modified lignin and mixing method thereof

Abstract

The invention relates to the technical field of tire rubber manufacturing, and discloses a rubber composition containing modified lignin and a mixing method thereof, and the rubber composition is added with the modified lignin. The modified lignin is water-soluble lignin obtained by modifying lignin by grafting citric acid groups. Citric acid is adopted to modify lignin, a citric acid group is grafted on a lignin group under the catalytic action of sodium hypophosphite to enhance the hydrophilicity of the lignin group, and wet mixing is combined to effectively improve the dispersity of the lignin in rubber and reduce the rolling resistance of the rubber composition, and meanwhile, the added lignin can enhance the strength of a rubber network, so that the rolling resistance of the rubber composition is improved. The tensile property of the rubber is improved.

Description

Technical Field

[0001] The invention relates to the technical field of tire rubber manufacturing, in particular to a rubber composition containing modified lignin and a mixing method thereof. Background Art

[0002] Due to the non-renewable nature of fossil fuel resources and the environmental pollution and greenhouse gas emissions caused by their use, countries around the world are seeking new energy sources as a way out for sustainable development. Therefore, biomass energy, as a renewable energy source with a wide range of sources, and the development and utilization of biomass-based materials have also received widespread attention.

[0003] Lignin is one of the main components of higher plants. Using lignin as a filler to fill rubber can not only strengthen rubber, replace carbon black, and get rid of dependence on petroleum, but also reduce production costs. At the same time, it can give rubber excellent flame retardancy, UV resistance, and antioxidant properties, making the application and research and development of lignin in rubber very cutting-edge. However, due to the complexity and heterogeneity of the chemical and physical structures of lignin, it is difficult to truly form a nano-scale dispersion in the rubber matrix to achieve performance similar to that of carbon black-reinforced rubber, and sometimes even deteriorate the performance of the material. Therefore, there is still a very long way to go before lignin can completely replace carbon black and be used in most rubbers, especially general non-polar rubbers. In view of this, how to make lignin into a filler with the same reinforcing properties as traditional fillers and apply it to rubber will be a very promising direction.

[0004] The Chinese invention patent (publication number: CN117757159A, publication date: 2024-03-26) discloses a tire rubber composition, which is prepared by mixing the following raw materials by weight based on 100 parts by weight of raw rubber: 100 parts of raw rubber, 45-80 parts of reinforcing filler; and an appropriate amount of activator, antioxidant and vulcanizer; the raw rubber includes 5-15 parts of trans-isoprene rubber, and the reinforcing filler includes 5-20 parts of lignin-modified white carbon black, and the lignin-modified white carbon black is prepared by reacting the following raw materials based on 100 parts by weight of white carbon black: 100 parts of white carbon black, 10-60 parts of acetylated lignin. The composition solves the problem of increased heat generation after adding trans-isoprene rubber by modifying white carbon black with acetylated lignin. The prepared mining tire has good tear resistance, puncture resistance, cutting resistance, and chipping resistance, while reducing the heat generation of the rubber compound.

[0005] A Chinese invention patent (publication number: CN112831059B, publication date: 2021-11-26) discloses a modified lignin, a preparation method thereof, and an application in a rubber composite material. Lignin is reacted with an acetylenic compound in an organic solvent to obtain a reaction solution containing modified lignin. The present invention has the following advantages: (1) The acetylenic reagent structure contains an acyl chloride functional group, which is easy to undergo esterification reaction with the alcohol hydroxyl group and phenolic hydroxyl group in the lignin molecule to generate modified lignin grafted with unsaturated acetylenic functional groups. (2) Alkynylation modification reduces the hydroxyl content in the lignin molecule and reduces the molecular polarity, which helps to inhibit the self-aggregation tendency of lignin caused by hydrogen bonds, is conducive to grinding to obtain lignin powder with a smaller particle size, improves the compatibility and affinity of lignin with non-polar natural rubber, and promotes the dispersion of lignin in the natural rubber matrix.

[0006] In addition, in traditional dry mixing, the shearing and crushing effect of open mills and internal mixers is used to mix the compounding agent and the rubber material. This mixing method not only has problems such as dust pollution, high energy consumption, and high heat generation, but also has poor dispersibility for fillers that are easy to self-aggregate and difficult to disperse, such as lignin and white carbon black. The advantages of wet mixing are more significant. Summary of the invention

[0007] The present invention aims at the deficiencies of the prior art and provides a rubber composition containing modified lignin and a mixing method thereof. The modified lignin can effectively replace carbon black to prepare the rubber composition and improves the dispersibility of lignin in rubber.

[0008] In order to achieve the above-mentioned purpose, the present invention adopts the following technical solutions: A rubber composition containing modified lignin, wherein the rubber composition is obtained by wet mixing and comprises a rubber component, a reinforcing filler, modified lignin and a compounding agent, wherein based on 100 parts by weight of the rubber component, the reinforcing filler is 15.0-55.0 parts, the modified lignin is 5.0-20.0 parts, The modified lignin is water-soluble lignin obtained by modifying lignin by grafting citric acid groups.

[0009] Preferably, the modified lignin is lignin in which citric acid groups are grafted onto lignin groups under the catalytic action of sodium hypophosphite to enhance its hydrophilicity.

[0010] Preferably, the preparation method of modified lignin comprises the following steps: 1) At room temperature, citric acid is dissolved in water to prepare a citric acid solution, sodium hypophosphite is added, and the solution is stirred to mix evenly; lignin nanoparticle powder is added, and stirring is continued for 0.5-1.5 hours to allow the lignin nanoparticles to fully contact with the citric acid aqueous solution to obtain a suspension; 2) Place the suspension in a vacuum drying oven and let it stand at room temperature for 11-13 hours after evacuating the vacuum; 3) placing the suspension in an air drying oven to remove excess water and colloidal substances, and then placing the remainder at 125-135° C. for 3.5-4.5 hours, and taking out the colloidal lignin nanoparticles after the reaction is completed; 4) re-dispersing the colloidal lignin nanoparticles in water and purifying the modified lignin nanoparticles by centrifugation, dialyzing the precipitate obtained after centrifugation in deionized water, diluting the modified lignin nanoparticle suspension to less than 1%, and dispersing it evenly in water after ultrasonic treatment; 5) Freeze drying to obtain modified lignin.

[0011] Preferably, the concentration of the citric acid solution is 4-6% (w / w); And / or, the sodium hypophosphite concentration is 0.8-2.0% (w / w); And / or, the vacuum degree of the vacuum drying oven is 0.5-0.7 Bar, and the suspension is placed for 1.5-2.5 hours; and / or, the air drying oven temperature is 55-65° C., and the suspension is placed for 46-50 hours; And / or, the freeze-drying temperature is -45°C to -55°C, and the vacuum degree is 0.11-0.13 mBar.

[0012] Preferably, the wet mixing comprises the following steps: mixing the reinforcing filler, the modified lignin and water to obtain a dispersion A, mixing the rubber and deionized water to obtain a dispersion B, mixing the dispersion A and the dispersion B, and then adding CaCl 2 The aqueous solution is used to flocculate to obtain a floc gel, and the floc gel is washed and dried to obtain a masterbatch. The masterbatch and the compounding agent are put into an open mixer and mixed to obtain a wet mixed rubber.

[0013] Preferably, the rubber component is a mixture of one or more of natural rubber, butadiene rubber, styrene-butadiene rubber, nitrile rubber, chloroprene rubber, ethylene-propylene rubber, butyl rubber and silicone rubber; The reinforcing filler is one or more of carbon black and white carbon black; The compounding agent is one or more of rubber processing oil, tackifying resin, activator, antioxidant, accelerator, vulcanizer, microsilica powder and paraffin.

[0014] Preferably, the carbon black particle size is 30-70 nm, preferably 30-40 nm; and / or, the active agent is one or more of zinc oxide and stearic acid; And / or, the accelerator is one or more of accelerator DM, accelerator DPG, accelerator CZ, and accelerator NS.

[0015] Preferably, the rubber processing oil is 1.0-20.0 parts, the tackifying resin is 1.0-5.0 parts, the activator is 1.0-5.0 parts, and the accelerator is 0.5-4.0 parts; Preferably, the rubber processing oil is 1.0-15.0 parts and the tackifying resin is 2.0-3.5 parts.

[0016] Furthermore, the present invention also provides a mixing method for the rubber composition containing modified lignin, which adopts wet mixing and comprises the following steps: 1) Preparation of masterbatch a. Put the reinforcing filler, modified lignin and water into a colloid mill and grind them to obtain a reinforcing filler aqueous dispersion; b. Add deionized water to the rubber to adjust the solid content to 10%, then transfer to a beaker and stir evenly with an electric stirrer at a speed of 450-550 rpm and a stirring time of 8-12 minutes; c. Add the reinforcing filler aqueous dispersion to the mixed rubber, continue stirring for 25-35 minutes, and drop 5% CaCl 2 The aqueous solution causes it to flocculate; d. Wash the flocculent gel in deionized water for 4-6 times, and then dry it in a vacuum oven at 55-65°C for 22-26 hours to obtain a masterbatch; 2) Mixing a. Heat the hot roll mill to 75-90℃, add the masterbatch into the mill and plasticize for 0.5-1.5min until it wraps around the roll; b. Add compounding agents in sequence, tap the rubber continuously to make the compounding agents evenly dispersed in the rubber, then adjust the roller distance to 0.15-0.25mm, make triangle packages and roll them in sequence, repeat three times, then adjust the roller distance to 1.5-2.0mm, produce sheets, and obtain wet mixed rubber.

[0017] Furthermore, the present invention also provides the use of the rubber composition containing modified lignin in tire tread, sidewall and base rubber.

[0018] The beneficial effects of the present invention are as follows: the present invention uses citric acid to modify lignin, grafts citric acid groups on lignin groups to enhance their hydrophilicity, and combines wet mixing to effectively improve the dispersibility of lignin in rubber. At the same time, the addition of lignin can enhance the strength of the rubber network and improve the tensile properties of the rubber.

[0019] In the rubber composition of the present invention, in addition to the above-mentioned components, different additives can be mixed, such as other fillers commonly used in tires and other rubber compositions, vulcanizing agents, vulcanization accelerators, different types of oils, antioxidants, plasticizers, etc. These additives are mixed in a common way to obtain a rubber composition that can be used for vulcanization. The amount of these additives can also be a conventional, usually mixed amount, provided that the purpose of the present invention is not adversely affected. BRIEF DESCRIPTION OF THE DRAWINGS

[0020] Figure 1 These are SEM images of the rubber compositions of Comparative Example 1 and Example 2, (a): Comparative Example 1, (b): Example 2. DETAILED DESCRIPTION

[0021] The following is a clear and complete description of the technical solutions in the embodiments of the present invention in conjunction with the embodiments of the present invention. Obviously, the described embodiments are only part of the embodiments of the present invention, not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the present invention.

[0022] 1. Application of lignin rubber composition in tread The formulations of Examples 1-3 and Comparative Examples 1-5 are shown in Table 1 (parts by weight).

[0023] Table 1 Comparative Example 1 Comparative Example 2 Comparative Example 3 Comparative Example 4 Comparative Example 5 Example 1 Example 2 Example 3 Natural rubber*1 100 100 100 100 100 100 100 100 Carbon black*2 30 30 38 30 30 30 30 30 White carbon black*3 25 25 25 25 25 25 25 25 Modified lignin 20 5 10 15 Lignin*4 10 Rubber operating oil*5 15 15 15 15 15 15 15 15 Stearic acid*6 2 2 2 2 2 2 2 2 Anti-aging agent*7 1 1 1 1 1 1 1 1 Petroleum resin*8 2.13 2.13 2.13 2.13 2.13 2.13 2.13 2.13 Zinc oxide*9 3 3 3 3 3 3 3 3 Paraffin*10 1.5 1.5 1.5 1.5 1.5 1.5 1.5 1.5 Accelerator*11 1 1 1 1 1 1 1 1 Accelerator*12 1 1 1 1 1 1 1 1 Accelerator*13 0.5 0.5 0.5 0.5 0.5 0.5 0.5 0.5 Oil-filled sulfur powder*14 2 2 2 2 2 2 2 2 Table 1 Footnotes *1: Natural rubber (solid content 60%), a product of China National Rubber Group; *2: N330, Cabot Chemicals; *3: 8113, product of Evonik Chemical Group Co., Ltd. *4: Lignin HS-L101, product of Hangshi Technology Development Co., Ltd.; *5: V500, product of Ningbo Hansheng Co., Ltd. *6: Stearic acid SA1801, a product of Yihai Kerry; *7: Antioxidant 4020 (6PPD), a product of Sinopec Nanjing Chemical Industry Co., Ltd.; *8: C5 / C9 resin, ExxonMobil product; *9: Zinc oxide, product of Qingdao Haiyan Chemical Co., Ltd.; *10: Microcrystalline wax H3236, a product of Yanggu Huatai; *11: Accelerator DPG (D), a product of Shandong Shangshun Chemical Co., Ltd.; *12: Accelerator DM, a product of Shandong Shangshun Chemical Co., Ltd.; *13: Accelerator CBS (CZ), a product of Shandong Shangshun Chemical Co., Ltd.; *14: Oil-filled sulfur powder, a product of Wuxi Huasheng Rubber New Material Technology Co., Ltd.

[0024] Comparative Example 1 adopts dry mixing, and the other comparative examples and embodiments adopt wet mixing.

[0025] The specific steps of dry mixing are as follows: 1) One-stage mixing: Mixing is carried out using an internal mixer; add natural rubber, press down the mass and keep it for 60 seconds; lift the mass, add white carbon black, carbon black, activator and antioxidant, press down the mass and keep it for 60 seconds; lift the mass and add rubber operating oil, petroleum resin and paraffin, press down the mass and keep it for 90 seconds; lift the mass and clean it; 2) Second stage mixing: Use open mill for mixing; discharge rubber to open mill, adjust the roller distance of double-roll open mill to 1.0mm, so that the rubber compound after mixing is wrapped around the roller; add accelerator and vulcanizer in sequence, cut the left and right knives three times each; make triangle wrapping passes five times when the roller is 0.20mm; adjust the roller distance to 2.0mm, remove the sheet and park.

[0026] The specific steps of wet mixing are as follows: 1) Preparation of masterbatch a. Take carbon black, modified lignin, white carbon black and 500 mL of water and grind them in a colloid mill to obtain a carbon black aqueous dispersion; b. Add deionized water to natural rubber to adjust the solid content to 10%, then transfer to a beaker and stir evenly with an electric stirrer at a stirring speed of 500 rpm for 10 minutes; c. Add the carbon black aqueous dispersion to the mixed natural rubber, continue stirring for 30 minutes, and drop 650 mL of 5.0% CaCl 2 The aqueous solution causes it to flocculate; d. The flocculent gel was washed in deionized water for 5 times, and then dried in a vacuum oven at 60° C. for 24 h to obtain a masterbatch; 2) Mixing a. Heat the hot roll mill to 80℃, add the masterbatch into the mill and plasticize for 1.0min until it wraps around the roll; b. Add rubber operating oil, petroleum resin, paraffin, zinc oxide, stearic acid, antioxidant, accelerator and vulcanizer in sequence, tapping the rubber continuously to make the compounding agents evenly dispersed in the rubber, then reduce the roller distance to 0.20mm, make triangle packages and roll them in sequence, repeat three times, then adjust the roller distance to 2.0mm, produce sheets, and obtain wet mixed rubber.

[0027] The rubber compositions obtained in the examples and comparative examples were tested.

[0028] Vulcanization characteristics: According to GB / T 9869-1997 standard, the UR-2030 rotorless vulcanizer produced by Taiwan Uni-Con Company was used to measure the vulcanization curve and vulcanization characteristic parameters at 143°C and a swing angle of 1°.

[0029] Filler dispersion: The blended rubber was tested using the RPA2000 rubber processing analyzer from Alpha Corporation of the United States. 5-6g of the mixed rubber was placed in the mold cavity and tested at 60°C to analyze and study the effects of different mixing methods and different blending ratios on the filler network of the blended rubber.

[0030] Tensile properties: The tensile strength and tear strength of the composite materials are in accordance with GB / T 528-2009 and GB / T 529-2008 standards. The tensile specimen is dumbbell-shaped and the tearing specimen is right-angled. The test is carried out using a U-CAN UT-2060 electronic tensile testing machine at a rate of 500 mm / min.

[0031] The test data is shown in Table 2.

[0032] Table 2 Comparative Example 1 Comparative Example 2 Comparative Example 3 Comparative Example 4 Comparative Example 5 Example 1 Example 2 Example 3 T90(min) 100 100 96 94 99 99 99 99 Payne effect (%) 100 33 95 86 31 30 25 30 TB(MPa) 100 107 113 110 97 120 127 110 EB(%) 100 109 95 98 110 113 124 111 Analyzing Table 2, Example 2 is the best example with the best comprehensive performance. It can be seen from Comparative Examples 1 and 2 that the filler dispersibility of wet mixing is significantly higher, and the tensile properties of the rubber composition are better. Comparative Example 2 and Example 2 add an equal amount of carbon black, and Comparative Example 3 adds a sufficient amount of carbon black. It can be seen that the filler dispersibility of Example 2 is significantly improved, the network strength of the rubber is also significantly improved, the tensile properties are significantly enhanced, and lignin can effectively replace part of the carbon black. It can be seen from Comparative Example 4 and Example 2 that lignin modification can effectively improve hydrophilicity to better adapt to wet mixing and effectively improve the dispersibility of lignin in rubber. It can be seen from Comparative Example 5 and the examples that the amount of modified lignin added should not be too much.

[0033] 2. Application of lignin rubber composition in sidewall The formulations of Examples 4-6 and Comparative Examples 6-10 are shown in Table 3 (parts by weight).

[0034] Table 3 Comparative Example 6 Comparative Example 7 Comparative Example 8 Comparative Example 9 Comparative Example 10 Example 4 Example 5 Example 6 Natural rubber*1 40 40 40 40 40 40 40 40 Butadiene rubber*2 30 30 30 30 30 30 30 Butadiene rubber*3 60 30 30 30 30 30 30 30 Carbon black*4 5 Carbon black*5 35 35 48 35 35 35 35 35 Carbon black*6 5 5 5 5 5 5 5 Modified lignin 20 5 10 15 Lignin*7 10 Rubber operating oil*8 2 2 2 2 2 2 2 2 Stearic acid*9 1.5 1.5 1.5 1.5 1.5 1.5 1.5 1.5 Anti-aging agent*10 1.5 1.5 1.5 1.5 1.5 1.5 1.5 1.5 Antiaging agent*11 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 Zinc oxide*12 3 3 3 3 3 3 3 3 Paraffin*13 2 2 2 2 2 2 2 2 Tackifying resin*14 3 3 3 3 3 3 3 3 Accelerator*15 0.25 0.25 0.25 0.25 0.25 0.25 0.25 0.25 Accelerator*16 0.65 0.65 0.65 0.65 0.65 0.65 0.65 0.65 Oil-filled sulfur*17 2 2 2 2 2 2 2 2 Table 3 Footnotes *1: Natural rubber (solid content 60%), a product of China National Rubber Group; *2: BR1250H, a product of Japan ZEON Co., Ltd. *3: BR9000, a product of Zhejiang Chuanhua Company; *4: N330, a product of Cabot Chemical Company; *5: N550, product of Cabot Chemical Company; *6: N660, product of Cabot Chemical Company; *7: Lignin HS-L101, product of Hangshi Technology Development Co., Ltd.; *8: V500, product of Ningbo Hansheng Co., Ltd. *9: Stearic acid SA1801, a product of Yihai Kerry; *10: Antioxidant RD, a product of Sinopec Nanjing Chemical Industry Co., Ltd.; *11: Antioxidant 4020, a product of Sinopec Nanjing Chemical Industry Co., Ltd.; *12: Zinc oxide, product of Qingdao Haiyan Chemical Co., Ltd.; *13: Microcrystalline wax H3236, a product of Yanggu Huatai; *14: Tackifying resin SL-1801, Huaqi Chemical Products; *15: Accelerator CZ, a product of Shandong Shangshun Chemical Co., Ltd.; *16: Accelerator NS, a product of Shandong Shangshun Chemical Co., Ltd.; *17: Oil-filled sulfur powder, a product of Wuxi Huasheng Rubber New Material Technology Co., Ltd.

[0035] Comparative Example 6 adopts dry mixing, and the other comparative examples and embodiments adopt wet mixing.

[0036] The specific steps of dry mixing are as follows: 1) One-stage mixing: Use internal mixer for mixing; add rubber, press down the mass and keep it for 60 seconds; lift the mass, add carbon black, activator and antioxidant, press down the mass and keep it for 60 seconds; lift the mass and add rubber operating oil, tackifying resin and paraffin, press down the mass and keep it for 90 seconds; lift the mass and clean it; 2) Second stage mixing: Use open mill for mixing; discharge rubber to open mill, adjust the roller distance of double-roll open mill to 1.0mm, so that the rubber compound after mixing is wrapped around the roller; add accelerator and vulcanizer in sequence, cut the left and right knives three times each; make triangle wrapping passes five times when the roller is 0.20mm; adjust the roller distance to 2.0mm, remove the sheet and park.

[0037] The specific steps of wet mixing are as follows: 1) Preparation of masterbatch a. Put carbon black, modified lignin and 500 mL of water into a colloid mill and grind them to obtain a carbon black aqueous dispersion; b. Add deionized water to the rubber to adjust the solid content to 10%, then transfer to a beaker and stir evenly with an electric stirrer at a stirring speed of 500 rpm for 10 minutes; c. Add the carbon black aqueous dispersion to the mixed rubber, continue stirring for 30 minutes, and drop 650 mL of 5.0% CaCl2 The aqueous solution causes it to flocculate; d. The flocculent gel was washed in deionized water for 5 times, and then dried in a vacuum oven at 60° C. for 24 h to obtain a masterbatch; 2) Mixing a. Heat the hot roll mill to 80℃, add the masterbatch into the mill and plasticize for 1.0min until it wraps around the roll; b. Add rubber operating oil, tackifying resin, paraffin, zinc oxide, stearic acid, antioxidant, accelerator and vulcanizer in sequence, tapping the rubber continuously to make the compounding agents evenly dispersed in the rubber, then reduce the roller distance to 0.20mm, make triangle packages and roll them in sequence, repeat three times, then adjust the roller distance to 2.0mm, produce sheets, and obtain wet mixed rubber.

[0038] The rubber compositions obtained in the examples and comparative examples were tested.

[0039] Vulcanization characteristics: According to GB / T 9869-1997 standard, the UR-2030 rotorless vulcanizer produced by Taiwan Uni-Con Company was used to measure the vulcanization curve and vulcanization characteristic parameters at 143°C and a swing angle of 1°.

[0040] Filler dispersion: The blended rubber was tested using the RPA2000 rubber processing analyzer from Alpha Corporation in the United States. 5-6 g of the mixed rubber was placed in the mold cavity and tested at 60°C to analyze and study the effects of different mixing methods and different blending ratios on the filler network of the blended rubber.

[0041] Tensile properties: The tensile strength and tear strength of the composite materials are in accordance with GB / T 528-2009 and GB / T 529-2008 standards. The tensile specimen is dumbbell-shaped and the tearing specimen is right-angled. The test is carried out using a U-CAN UT-2060 electronic tensile testing machine at a rate of 500 mm / min.

[0042] Dynamic mechanical analysis (DMA) was performed in tensile mode on a DMA 242D dynamic mechanical analyzer produced by NETZSCH, Germany. The test conditions were: 12 Hz, 0.5% strain, temperature range: -100-100℃, heating rate 3℃ / min.

[0043] The test data is shown in Table 4.

[0044] Table 4 Comparative Example 6 Comparative Example 7 Comparative Example 8 Comparative Example 9 Comparative Example 10 Example 4 Example 5 Example 6 T90(min) 100 95 93 92 90 93 91 90 Payne effect (%) 100 32 95 90 32 30 26 31 TB(MPa) 100 109 121 111 93 123 128 116 EB(%) 100 109 86 106 112 116 128 111 Tan delta 60℃ 100 83 96 86 78 72 73 76 Analyzing Table 4, Example 5 is the best example with the best comprehensive performance. It can be seen from Comparative Examples 6 and 7 that the filler dispersibility of wet mixing is significantly higher, the tensile properties of the rubber composition are better, and the rolling resistance is relatively low. Comparative Example 7 and Example 5 add an equal amount of carbon black, and Comparative Example 8 adds a sufficient amount of carbon black. It can be seen that the filler dispersibility of Example 5 is significantly improved, the network strength of the rubber is also significantly improved, the tensile properties are significantly enhanced, and the rolling resistance is relatively low. Lignin can effectively replace part of the carbon black. It can be seen from Comparative Example 9 and Example 5 that lignin modification can effectively improve hydrophilicity to better adapt to wet mixing and effectively improve the dispersibility of lignin in rubber. It can be seen from Comparative Example 10 and the examples that the amount of modified lignin added should not be too much.

[0045] 3. Application of lignin rubber composition in base rubber The formulations of Examples 7-10 and Comparative Examples 11-14 are shown in Table 5 (parts by weight).

[0046] Table 5 Comparative Example 11 Comparative Example 12 Comparative Example 13 Comparative Example 14 Example 7 Example 8 Example 9 Example 10 Natural rubber*1 80 80 80 80 80 80 80 80 Butadiene rubber*2 20 10 10 10 10 10 10 10 Butadiene rubber*3 10 10 10 10 10 10 10 Carbon black*4 50 35 45 35 35 35 35 35 Modified lignin 5 10 15 20 Lignin*5 5 Microsilica fume*6 10 15 15 15 15 15 15 15 Rubber operating oil*7 10 10 10 10 10 10 10 10 Stearic acid*8 1 1 1 1 1 1 1 1 Anti-aging agent*9 2 2 2 2 2 2 2 2 Anti-aging agent*10 1 1 1 1 1 1 1 1 Zinc oxide*11 3 3 3 3 3 3 3 3 Tackifying resin*12 3 3 3 3 3 3 3 3 Accelerator*13 1.4 1.4 1.4 1.4 1.4 1.4 1.4 1.4 Accelerator*14 0.2 0.2 0.2 0.2 0.2 0.2 0.2 0.2 Oil-filled sulfur*15 3 3 3 3 3 3 3 3 Table 5 Footnotes *1: Natural rubber (solid content 60%), a product of China National Rubber Group; *2: BR1250H, a product of Japan ZEON Co., Ltd. *3: BR9000, a product of Zhejiang Chuanhua Company; *4: N550, a product of Cabot Chemical Company; *5: Lignin HS-L101, product of Hangshi Technology Development Co., Ltd.; *6: Microsilica powder Sidistar R320u, a product of Eken Chemical Company; *7: V500, product of Ningbo Hansheng Co., Ltd. *8: Stearic acid SA1801, a product of Yihai Kerry; *9: Antioxidant RD, a product of Sinopec Nanjing Chemical Industry Co., Ltd.; *10: Antioxidant 4020, a product of Sinopec Nanjing Chemical Industry Co., Ltd.; *11: Zinc oxide, product of Qingdao Haiyan Chemical Co., Ltd.; *12: Tackifying resin SL-1801, Huaqi Chemical Products; *13: Accelerator CZ, a product of Shandong Shangshun Chemical Co., Ltd.; *14: Accelerator NS, a product of Shandong Shangshun Chemical Co., Ltd. *15: Oil-filled sulfur powder, a product of Wuxi Huasheng Rubber New Material Technology Co., Ltd.

[0047] Comparative Example 1 adopts dry mixing, and the other comparative examples and embodiments adopt wet mixing.

[0048] The specific steps of dry mixing are as follows: 1) One-stage mixing: Use internal mixer for mixing; add rubber, press down the mass and keep it for 60 seconds; lift the mass, add carbon black, activator and antioxidant, press down the mass and keep it for 60 seconds; lift the mass, add rubber operating oil, tackifying resin and microsilica powder, press down the mass and keep it for 90 seconds; lift the mass and clean it; 2) Second stage mixing: Use open mill for mixing; discharge rubber to open mill, adjust the roller distance of double-roll open mill to 1.0mm, so that the rubber compound after mixing is wrapped around the roller; add accelerator and vulcanizer in sequence, cut the left and right knives three times each; make triangle wrapping passes five times when the roller is 0.20mm; adjust the roller distance to 2.0mm, remove the sheet and park.

[0049] The specific steps of wet mixing are as follows: 1) Preparation of masterbatch a. Put carbon black, modified lignin and 500 mL of water into a colloid mill and grind them to obtain a carbon black aqueous dispersion; b. Add deionized water to the rubber to adjust the solid content to 10%, then transfer to a beaker and stir evenly with an electric stirrer at a stirring speed of 500 rpm for 10 minutes; c. Add the carbon black aqueous dispersion to the mixed rubber, continue stirring for 30 minutes, and drop 650 mL of 5.0% CaCl 2 The aqueous solution causes it to flocculate; d. The flocculent gel was washed in deionized water for 5 times, and then dried in a vacuum oven at 60° C. for 24 h to obtain a masterbatch; 2) Mixing a. Heat the hot roll mill to 80℃, add the masterbatch into the mill and plasticize for 1.0min until it wraps around the roll; b. Add rubber operating oil, tackifying resin, microsilica powder, zinc oxide, stearic acid, antioxidant, accelerator and vulcanizer in sequence, tapping the rubber continuously to make the compounding agents evenly dispersed in the rubber, then reduce the roller distance to 0.20mm, make triangle packages and rolls in sequence, repeat three times, then adjust the roller distance to 2.0mm, produce sheets, and obtain wet mixed rubber.

[0050] The rubber compositions obtained in the examples and comparative examples were tested.

[0051] Vulcanization characteristics: According to GB / T 9869-1997 standard, the UR-2030 rotorless vulcanizer produced by Taiwan Uni-Con Company was used to measure the vulcanization curve and vulcanization characteristic parameters at 143°C and a swing angle of 1°.

[0052] Filler dispersion: The blended rubber was tested using the RPA2000 rubber processing analyzer from Alpha Corporation in the United States. 5-6 g of the mixed rubber was placed in the mold cavity and tested at 60°C to analyze and study the effects of different mixing methods and different blending ratios on the filler network of the blended rubber.

[0053] Tensile properties: The tensile strength and tear strength of the composite materials are in accordance with GB / T 528-2009 and GB / T 529-2008 standards. The tensile specimen is dumbbell-shaped and the tearing specimen is right-angled. The test is carried out using a U-CAN UT-2060 electronic tensile testing machine at a rate of 500 mm / min.

[0054] Dynamic mechanical analysis (DMA) was performed in tensile mode on a DMA 242D dynamic mechanical analyzer produced by NETZSCH, Germany. The test conditions were: 12 Hz, 0.5% strain, temperature range: -100-100℃, heating rate 3℃ / min.

[0055] The test data is shown in Table 6.

[0056] Table 6 Comparative Example 11 Comparative Example 12 Comparative Example 13 Comparative Example 14 Example 7 Example 8 Example 9 Example 10 T90(min) 100 100 94 90 95 94 96 99 Payne effect (%) 100 31 96 83 28 26 26 27 TB(MPa) 100 101 102 101 119 126 122 120 EB(%) 100 104 95 105 116 128 112 113 Tan delta 60℃ 100 38 93 85 36 32 34 33 Analyzing Table 2, Example 9 is the best example with the best comprehensive performance. It can be seen from Comparative Examples 11 and 12 that the filler dispersibility of wet mixing is significantly higher, the tensile properties of the rubber composition are better, and the rolling resistance is relatively lower. Comparative Example 2 and Example 9 add equal amounts of carbon black, and Comparative Example 13 adds a sufficient amount of carbon black. It can be seen that the filler dispersibility of Example 9 is significantly improved, the network strength of the rubber is also significantly improved, the tensile properties are significantly enhanced, the rolling resistance is relatively lower, and lignin can effectively replace part of the carbon black. It can be seen from Comparative Example 14 and Example 9 that lignin modification can effectively improve hydrophilicity to better adapt to wet mixing and effectively improve the dispersibility of lignin in rubber.

[0057] The above is a description of the embodiments of the present invention. Through the above description of the disclosed embodiments, professionals and technicians in the field can implement or use the present invention. Various modifications to these embodiments will be apparent to professionals and technicians in the field. The general principles defined herein can be implemented in other embodiments without departing from the spirit or scope of the present invention. Therefore, the present invention will not be limited to these embodiments shown in this article, but will conform to the widest range consistent with the principles and novelties disclosed herein.

Claims

1. A rubber composition containing modified lignin, characterized in that: The rubber composition is obtained by wet mixing and comprises a rubber component, a reinforcing filler, a modified lignin and a compounding agent. Based on 100 parts by weight of the rubber component, the reinforcing filler is 15.0-55.0 parts, the modified lignin is 5.0-20.0 parts, The modified lignin is water-soluble lignin obtained by modifying lignin by grafting citric acid groups.

2. A rubber composition containing modified lignin according to claim 1, characterized in that: The modified lignin is prepared by grafting citric acid groups onto the lignin groups under the catalytic action of sodium hypophosphite to enhance the hydrophilicity of the lignin.

3. The rubber composition containing modified lignin according to claim 1, characterized in that: The preparation method of modified lignin comprises the following steps: 1) At room temperature, citric acid is dissolved in water to prepare a citric acid solution, sodium hypophosphite is added, and the solution is stirred to mix evenly; lignin nanoparticle powder is added, and stirring is continued for 0.5-1.5 hours to allow the lignin nanoparticles to fully contact with the citric acid aqueous solution to obtain a suspension; 2) Place the suspension in a vacuum drying oven and let it stand at room temperature for 11-13 hours after evacuating the vacuum; 3) placing the suspension in an air drying oven to remove excess water and colloidal substances, and then placing the remainder at 125-135° C. for 3.5-4.5 hours, and taking out the colloidal lignin nanoparticles after the reaction is completed; 4) re-dispersing the colloidal lignin nanoparticles in water and purifying the modified lignin nanoparticles by centrifugation, dialyzing the precipitate obtained after centrifugation in deionized water, diluting the modified lignin nanoparticle suspension to less than 1%, and dispersing it evenly in water after ultrasonic treatment; 5) Freeze drying to obtain modified lignin.

4. A rubber composition containing modified lignin according to claim 3, characterized in that: The concentration of the citric acid solution is 4-6% (w / w); And / or, the sodium hypophosphite concentration is 0.8-2.0% (w / w); And / or, the vacuum degree of the vacuum drying oven is 0.5-0.7 Bar, and the suspension is placed for 1.5-2.5 hours; and / or, the air drying oven temperature is 55-65° C., and the suspension is placed for 46-50 hours; And / or, the freeze-drying temperature is -45°C to -55°C, and the vacuum degree is 0.11-0.13 mBar.

5. The rubber composition containing modified lignin according to claim 1, characterized in that: The wet mixing comprises the following steps: mixing a reinforcing filler, a modified lignin and water to obtain a dispersion A, mixing rubber and deionized water to obtain a dispersion B, mixing the dispersion A and the dispersion B evenly, then adding a CaCl2 aqueous solution to flocculate the dispersion to obtain a flocculent gel, washing and drying the flocculent gel to obtain a masterbatch, and placing the masterbatch and a compounding agent in an open mill for mixing to obtain a wet mixed rubber.

6. The rubber composition containing modified lignin according to claim 1, characterized in that: The rubber component is a mixture of one or more of natural rubber, butadiene rubber, styrene-butadiene rubber, nitrile rubber, chloroprene rubber, ethylene-propylene rubber, butyl rubber and silicone rubber; The reinforcing filler is one or more of carbon black and white carbon black; The compounding agent is one or more of rubber operating oil, tackifying resin, activator, antioxidant, accelerator, vulcanizer, microsilica powder and paraffin.

7. The rubber composition containing modified lignin according to claim 6, characterized in that: The carbon black particle size is 30-70nm, preferably 30-40nm; and / or, the active agent is one or more of zinc oxide and stearic acid; And / or, the accelerator is one or more of accelerator DM, accelerator DPG, accelerator CZ, and accelerator NS.

8. The rubber composition containing modified lignin according to claim 6, characterized in that: The rubber processing oil is 1.0-20.0 parts, the tackifying resin is 1.0-5.0 parts, the activator is 1.0-5.0 parts, and the accelerator is 0.5-4.0 parts; Preferably, the rubber processing oil is 1.0-15.0 parts and the tackifying resin is 2.0-3.5 parts.

9. A mixing method for a rubber composition containing modified lignin according to any one of claims 1 to 8, characterized in that: The wet mixing method includes the following steps: 1) Preparation of masterbatch a. Put the reinforcing filler, modified lignin and water into a colloid mill and grind them to obtain a reinforcing filler aqueous dispersion; b. Add deionized water to the rubber to adjust the solid content to 10%, then transfer to a beaker and stir evenly with an electric stirrer at a speed of 450-550 rpm and a stirring time of 8-12 minutes; c. Add the reinforcing filler aqueous dispersion into the uniformly mixed rubber, continue stirring for 25-35 minutes, and drop 5% by mass CaCl2 aqueous solution into the mixed solution to make it flocculate; d. Wash the flocculent gel in deionized water for 4-6 times, and then dry it in a vacuum oven at 55-65°C for 22-26 hours to obtain a masterbatch; 2) Mixing a. Heat the hot roll mill to 75-90℃, add the masterbatch into the mill and plasticize for 0.5-1.5min until it wraps around the roll; b. Add compounding agents in sequence, tap the rubber continuously to make the compounding agents evenly dispersed in the rubber, then adjust the roller distance to 0.15-0.25mm, make triangle packages and roll them in sequence, repeat three times, then adjust the roller distance to 1.5-2.0mm, produce sheets, and obtain wet mixed rubber.

10. Use of the rubber composition containing modified lignin according to any one of claims 1 to 8 in tire tread, sidewall and base rubber.

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