CN117210033A - Thermal cracking carbon black and preparation method thereof - Google Patents
Thermal cracking carbon black and preparation method thereof Download PDFInfo
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Abstract
Description
技术领域Technical field
本发明涉及一种热裂解炭黑及其制备方法,特别是一种低灰分和高比表面积的热裂解炭黑及其制备方法。The present invention relates to a thermal cracking carbon black and a preparation method thereof, in particular to a thermal cracking carbon black with low ash content and high specific surface area and a preparation method thereof.
技术背景technical background
轮胎自诞生起就在科学技术领域,特别是在交通领域起着重要作用。目前,全球废旧轮胎的数量庞大,年产量已达15亿条,且仍在持续增长。轮胎主要由由橡胶、炭黑、骨架材料以及添加剂组成。将废旧轮胎进行高温热裂解,可分解出热裂解油、热裂解炭黑、热裂解气体等物质。其中,热裂解油和热裂解气体可以有效地利用,如热裂解油具有较高的热值,可使其成为传统液体燃料的替代品;热裂解气体(如氢气)可以直接燃烧,为工业生产提供能量;热裂解炭黑则较难进行处理。废旧轮胎热裂解炭黑的主要化学成分是碳、氧、铜、锌、硅等,其灰分含量较高。另外,热裂解炭黑还沉积了一些热裂解过程中产生的焦油。与普通炭黑相比,热裂解炭黑由于灰分和焦油等杂质,导致化学性能有明显差异,对橡胶的补强效果较差,无法满足应用的需要。Since its birth, tires have played an important role in the field of science and technology, especially in the field of transportation. At present, the number of scrap tires in the world is huge, with annual output reaching 1.5 billion and continuing to grow. Tires are mainly composed of rubber, carbon black, skeleton materials and additives. The high-temperature pyrolysis of waste tires can decompose pyrolysis oil, pyrolysis carbon black, pyrolysis gas and other substances. Among them, pyrolysis oil and pyrolysis gas can be effectively utilized. For example, pyrolysis oil has a high calorific value, making it a substitute for traditional liquid fuels; pyrolysis gas (such as hydrogen) can be burned directly to provide industrial production. Provides energy; pyrolytic carbon black is more difficult to process. The main chemical components of waste tire pyrolysis carbon black are carbon, oxygen, copper, zinc, silicon, etc., and its ash content is relatively high. In addition, thermal cracking carbon black also deposits some tar produced during the thermal cracking process. Compared with ordinary carbon black, thermal cracking carbon black has obvious differences in chemical properties due to impurities such as ash and tar. Its reinforcing effect on rubber is poor and cannot meet the needs of applications.
现有技术公开了一些去除灰分等杂质的技术手段。CN110964350A记载了一种热裂解炭黑脱灰工艺,包括如下步骤:将热裂解炭黑、酸溶液、分散剂、络合剂混合,反应,固液分离,获得滤渣与滤液,滤渣清洗、造粒获得炭黑成品;使炭黑的灰分含量由18.1wt%降至5wt%左右。CN102504619A记载了一种废轮胎裂解炭黑净化工艺,包括经过酸洗碱洗的炭黑再次经过酸洗过程;制得的炭黑的灰分含量为约2.6wt%。然而,这样的去除杂质效果还是不够,灰分含量还比较高,无法单独作为补强炭黑用于橡胶材料。The prior art discloses some technical means for removing impurities such as ash. CN110964350A describes a thermal cracking carbon black deliming process, which includes the following steps: mixing thermal cracking carbon black, acid solution, dispersant, and complexing agent, reacting, solid-liquid separation, obtaining filter residue and filtrate, cleaning the filter residue, and granulating A finished carbon black product is obtained; the ash content of the carbon black is reduced from 18.1wt% to about 5wt%. CN102504619A records a waste tire cracking carbon black purification process, which includes acid-washing and alkali-washing carbon black and then undergoing an acid-washing process; the ash content of the carbon black produced is about 2.6wt%. However, this impurity removal effect is still not enough, and the ash content is still relatively high, so it cannot be used alone as reinforcing carbon black for rubber materials.
从而,现有技术仍然存在进一步降低废旧轮胎热裂解炭黑中的灰分等杂质,得到低灰分和高比表面积的热裂解炭黑。Therefore, the existing technology still exists to further reduce the ash and other impurities in the thermal cracking carbon black of waste tires to obtain thermal cracking carbon black with low ash content and high specific surface area.
发明内容Contents of the invention
本申请解决的技术问题是:提供一种低灰分和高比表面积的热裂解炭黑,与商用炭黑性能接近。The technical problem solved by this application is to provide a thermal cracking carbon black with low ash content and high specific surface area, which has properties close to those of commercial carbon black.
本发明提供了一种热裂解碳黑的制备方法,包括以下步骤:The invention provides a method for preparing thermal cracking carbon black, which includes the following steps:
(1)提供一种热裂解炭黑颗粒;(1) Provide a thermal cracking carbon black particle;
(2)配制碱金属碳酸盐饱和溶液,并将步骤(1)的炭黑浸泡到上述饱和溶液中;除去饱和溶液中的水分得到沉积有碱金属碳酸盐的炭黑;(2) Prepare a saturated alkali metal carbonate solution, and soak the carbon black in step (1) into the above saturated solution; remove the water in the saturated solution to obtain carbon black deposited with alkali metal carbonate;
(3)将沉积有碱金属碳酸盐的炭黑在超声下用酸进行处理;(3) The carbon black deposited with alkali metal carbonate is treated with acid under ultrasound;
(4)随后过滤、洗涤、干燥得到炭黑颗粒。(4) Then filter, wash and dry to obtain carbon black particles.
其中,所述热裂解炭黑颗粒是由废轮胎热裂解制得,然后粉碎,并利用磁力装置除去铁屑。使用的热裂解方法可以是:直接热裂解、熔盐热裂解、共热裂解、等离子热裂解等。例如,将去掉钢丝和纤维的废轮胎破碎为小块,洗净、干燥后放入热裂解炉中进行热裂解。热裂解终温为350-700℃,例如,400℃、450℃、500℃、550℃、600℃、650℃等,升温速率为5-30℃/min,例如,5℃/min、10℃/min、15℃/min、20℃/min、25℃/min、30℃/min等。终温维持时间为10-120min。随后将得到的炭黑研磨均匀,利用磁力装置除去铁屑,制得热裂解炭黑。Wherein, the thermal cracking carbon black particles are produced by thermal cracking of waste tires, and then crushed, and a magnetic device is used to remove iron filings. The thermal cracking methods used can be: direct thermal cracking, molten salt thermal cracking, co-thermal cracking, plasma thermal cracking, etc. For example, waste tires with steel wires and fibers removed are broken into small pieces, washed and dried, and then placed in a thermal cracking furnace for thermal cracking. The final temperature of thermal cracking is 350-700℃, for example, 400℃, 450℃, 500℃, 550℃, 600℃, 650℃, etc., and the heating rate is 5-30℃/min, for example, 5℃/min, 10℃ /min, 15℃/min, 20℃/min, 25℃/min, 30℃/min, etc. The final temperature maintenance time is 10-120min. The obtained carbon black is then ground evenly, and a magnetic device is used to remove iron filings to obtain thermal cracking carbon black.
其中,步骤(2)中所述碱金属碳酸盐是碳酸氢钠、碳酸钠、碳酸氢钾和碳酸钾中的一种或多种,优选,碳酸氢钠和碳酸钾的组合。配制碳酸氢钠和碳酸钾的混合溶液时,先分别制得碳酸氢钠和碳酸钾的饱和溶液,然后按一定体积比混合。两者的比例可以是任意配比,优选1:5-5:1,例如,1:5、1:4、1:3、1:2、1:1、2:1、3:1、4:1、5:1等;配制碱金属碳酸盐饱和溶液的温度为20-90℃,优选50-80℃。步骤(1)的炭黑颗粒和碱金属碳酸盐饱和溶液的固液比为1:0.1-4(g/mL),优选1:0.5-2.5(g/mL),使炭黑颗粒部分或完全浸入碱金属碳酸盐饱和溶液中。此时,可以通过搅动、翻动、振动等方式使得炭黑表面充分浸润碱金属碳酸盐饱和溶液。浸泡时间为2-48小时,优选12-36小时,例如,12小时、16小时、20小时、24小时、28小时、32小时、36小时等。Wherein, the alkali metal carbonate in step (2) is one or more of sodium bicarbonate, sodium carbonate, potassium bicarbonate and potassium carbonate, preferably a combination of sodium bicarbonate and potassium carbonate. When preparing a mixed solution of sodium bicarbonate and potassium carbonate, first prepare saturated solutions of sodium bicarbonate and potassium carbonate respectively, and then mix them according to a certain volume ratio. The ratio of the two can be any ratio, preferably 1:5-5:1, for example, 1:5, 1:4, 1:3, 1:2, 1:1, 2:1, 3:1, 4 :1, 5:1, etc.; the temperature for preparing the saturated alkali metal carbonate solution is 20-90°C, preferably 50-80°C. The solid-liquid ratio of the carbon black particles and the alkali metal carbonate saturated solution in step (1) is 1:0.1-4 (g/mL), preferably 1:0.5-2.5 (g/mL), so that the carbon black particles are partially or Completely immersed in a saturated solution of alkali metal carbonates. At this time, the carbon black surface can be fully infiltrated into the alkali metal carbonate saturated solution through stirring, turning, vibration, etc. The soaking time is 2-48 hours, preferably 12-36 hours, for example, 12 hours, 16 hours, 20 hours, 24 hours, 28 hours, 32 hours, 36 hours, etc.
其中,步骤(3)中所述酸液是本领域常见的无机酸,如盐酸、硝酸、硫酸和氢氟酸中的一种或多种;步骤(3)中,酸的浓度为1-30mol/L,超声处理的时间为0.5-50小时,优选4-24小时,处理温度为:50-90℃。碱金属碳酸盐和酸的摩尔比是1:4-40,优选1:8-20。Wherein, the acid solution in step (3) is a common inorganic acid in this field, such as one or more of hydrochloric acid, nitric acid, sulfuric acid and hydrofluoric acid; in step (3), the concentration of the acid is 1-30 mol /L, the ultrasonic treatment time is 0.5-50 hours, preferably 4-24 hours, and the treatment temperature is: 50-90°C. The molar ratio of alkali metal carbonate and acid is 1:4-40, preferably 1:8-20.
优选的,步骤(4)之后再进行步骤(5),步骤(5)为将步骤(4)的炭黑颗粒加入到酸液中并进行超声处理;随后过滤、洗涤和干燥处理。步骤(5)中所述酸液是本领域常见的无机酸,如盐酸、硝酸、硫酸和氢氟酸中的一种或多种。步骤(5)中,酸的浓度为1-30mol/L,炭黑颗粒和酸的固液比是1:5-30(g/mL),超声处理的时间为0.5-50小时,优选4-24小时,处理温度为:50-90℃。Preferably, step (5) is performed after step (4). Step (5) is to add the carbon black particles of step (4) into the acid solution and perform ultrasonic treatment; followed by filtration, washing and drying. The acid solution in step (5) is a common inorganic acid in the art, such as one or more of hydrochloric acid, nitric acid, sulfuric acid and hydrofluoric acid. In step (5), the concentration of the acid is 1-30 mol/L, the solid-liquid ratio of the carbon black particles and the acid is 1:5-30 (g/mL), and the ultrasonic treatment time is 0.5-50 hours, preferably 4- 24 hours, treatment temperature: 50-90℃.
优选,步骤(3)中使用硫酸或盐酸进行处理,步骤(5)中使用氢氟酸进行处理。Preferably, sulfuric acid or hydrochloric acid is used for treatment in step (3), and hydrofluoric acid is used for treatment in step (5).
可选的,本发明的一种废轮胎热裂解制得的炭黑的制备方法还包括使用强碱对炭黑颗粒进行处理的步骤。强碱可以是氢氧化钠、氢氧化钾等。Optionally, the method for preparing carbon black obtained by thermal cracking of waste tires of the present invention also includes the step of using a strong alkali to treat the carbon black particles. Strong bases can be sodium hydroxide, potassium hydroxide, etc.
本发明公开了一种废轮胎热裂解制得的炭黑的制备方法。通过该方法显著降低了灰分含量,提高了比表面积。该方法首先将碱金属碳酸盐沉积在炭黑的外表面和内孔的表面。随后浸入酸液中,碱金属碳酸盐和酸反应产生大量的二氧化碳气体,并配合超声作用可以使炭黑上的灰分,包括内孔中的灰分,脱离炭黑的表面,充分和酸反应转化为可溶的盐。在此过程中,沉积在炭黑上的焦油等有机物质也会部分脱离下来。另外,随后的第二次酸处理和可选的碱处理可以进一步降低灰分和有机物质的含量。The invention discloses a method for preparing carbon black obtained by thermal cracking of waste tires. This method significantly reduces the ash content and increases the specific surface area. This method first deposits alkali metal carbonate on the outer surface of carbon black and the surface of inner pores. Then it is immersed in the acid solution. The alkali metal carbonate reacts with the acid to produce a large amount of carbon dioxide gas. With the action of ultrasound, the ash on the carbon black, including the ash in the inner pores, can be separated from the surface of the carbon black and fully react with the acid for conversion. is a soluble salt. During this process, organic substances such as tar deposited on the carbon black will also be partially detached. In addition, a subsequent second acid treatment and optional alkali treatment can further reduce the ash and organic matter content.
具体实施方式Detailed ways
下面结合实施例对本发明作进一步描述,旨在帮助阅读者更好理解本发明的技术方案,并不对本发明技术方案的实施范围构成任何限定。The present invention is further described below in conjunction with the examples, which are intended to help readers better understand the technical solutions of the present invention, and do not limit the implementation scope of the technical solutions of the present invention in any way.
制备例Preparation example
将去掉钢丝和纤维的废轮胎破碎为1.5cm直径大小的小块,洗净、干燥后放入热裂解炉中进行热裂解。热裂解条件为:氮气气氛,初始温度为80℃,热裂解终温为500℃,升温速率为10℃/min,热裂解终温维持时间为50min。随后将得到的炭黑研磨均匀,利用磁力装置除去铁屑。最终,制得热裂解炭黑A。The waste tires with the steel wires and fibers removed are broken into small pieces with a diameter of 1.5cm, washed and dried, and then placed in a thermal cracking furnace for thermal cracking. The thermal cracking conditions are: nitrogen atmosphere, initial temperature is 80°C, final thermal cracking temperature is 500°C, heating rate is 10°C/min, and final thermal cracking temperature maintenance time is 50 min. The obtained carbon black is then ground evenly, and iron filings are removed using a magnetic device. Finally, thermal cracking carbon black A is obtained.
实施例1Example 1
称取制备例得到的热裂解炭黑A 100g;在80℃下配制碳酸钠饱和溶液,并将热裂解炭黑A在80℃碳酸钠饱和溶液中浸泡24小时,热裂解炭黑A和碳酸钠饱和溶液的固液比为1:1.5(g/mL);加热除去饱和溶液中的水得到沉积有碳酸钠的炭黑;将沉积有碳酸钠的炭黑投入5mol/L的硫酸中并超声处理5小时,碱金属碳酸盐和酸的摩尔比为1:16;随后过滤,用水在50℃下洗涤3次、真空干燥得到炭黑颗粒。Weigh 100g of the thermally cracked carbon black A obtained in the preparation example; prepare a saturated sodium carbonate solution at 80°C, and soak the thermally cracked carbon black A in the saturated sodium carbonate solution at 80°C for 24 hours. The solid-liquid ratio of the saturated solution is 1:1.5 (g/mL); heat to remove the water in the saturated solution to obtain carbon black with sodium carbonate deposited; put the carbon black with sodium carbonate deposited into 5 mol/L sulfuric acid and conduct ultrasonic treatment For 5 hours, the molar ratio of alkali metal carbonate and acid was 1:16; then filtered, washed three times with water at 50°C, and vacuum dried to obtain carbon black particles.
实施例2Example 2
参照实施例1的制备方法,和实施例1的区别在于:使用碳酸氢钠饱和溶液替换碳酸钠饱和溶液。Refer to the preparation method of Example 1, the difference from Example 1 is that a saturated solution of sodium bicarbonate is used instead of a saturated solution of sodium carbonate.
实施例3Example 3
参照实施例1的制备方法,和实施例1的区别在于:使用碳酸氢钾饱和溶液替换碳酸钠饱和溶液。Refer to the preparation method of Example 1, the difference from Example 1 is that a saturated solution of potassium bicarbonate is used instead of a saturated solution of sodium carbonate.
实施例4Example 4
参照实施例1的制备方法,和实施例1的区别在于:使用碳酸钾饱和溶液替换碳酸钠饱和溶液。Refer to the preparation method of Example 1, the difference from Example 1 is that a saturated solution of potassium carbonate is used instead of a saturated solution of sodium carbonate.
实施例5Example 5
参照实施例1的制备方法,和实施例1的区别在于:分别在80℃下配制碳酸氢钠和碳酸钾的饱和溶液,取体积比为1:1的两种溶液混合组成碱金属碳酸盐饱和溶液,替换碳酸钠饱和溶液。Referring to the preparation method of Example 1, the difference from Example 1 is that: prepare saturated solutions of sodium bicarbonate and potassium carbonate at 80°C, and mix the two solutions with a volume ratio of 1:1 to form an alkali metal carbonate. Saturated solution, replace the saturated solution of sodium carbonate.
实施例6Example 6
参照实施例1的制备方法,和实施例1的区别在于:分别在80℃下配制碳酸氢钠和碳酸钾的饱和溶液,取体积比为2:1的两种溶液混合组成碱金属碳酸盐饱和溶液,替换碳酸钠饱和溶液。Referring to the preparation method of Example 1, the difference from Example 1 is that: prepare saturated solutions of sodium bicarbonate and potassium carbonate at 80°C, and mix the two solutions with a volume ratio of 2:1 to form an alkali metal carbonate. Saturated solution, replace the saturated solution of sodium carbonate.
实施例7Example 7
参照实施例1的制备方法,和实施例1的区别在于:分别在80℃下配制碳酸氢钠和碳酸钾的饱和溶液,取体积比为1:2的两种溶液混合组成碱金属碳酸盐饱和溶液,替换碳酸钠饱和溶液。Referring to the preparation method of Example 1, the difference from Example 1 is that: prepare saturated solutions of sodium bicarbonate and potassium carbonate at 80°C respectively, and mix the two solutions with a volume ratio of 1:2 to form an alkali metal carbonate. Saturated solution, replace the saturated solution of sodium carbonate.
实施例8Example 8
参照实施例7的制备方法,和实施例7的区别在于:使用7mol/L的盐酸替换硫酸。Refer to the preparation method of Example 7, the difference from Example 7 is that 7 mol/L hydrochloric acid is used instead of sulfuric acid.
实施例9Example 9
参照实施例7的制备方法,和实施例7的区别在于:使用7mol/L的硝酸替换硫酸。Refer to the preparation method of Example 7, the difference from Example 7 is that 7 mol/L nitric acid is used instead of sulfuric acid.
实施例10Example 10
参照实施例7的制备方法,和实施例7的区别在于:使用5mol/L的氢氟酸替换硫酸。Refer to the preparation method of Example 7, the difference from Example 7 is that 5 mol/L hydrofluoric acid is used instead of sulfuric acid.
实施例11Example 11
参照实施例7的制备方法,和实施例7的区别在于:在第一次酸处理并过滤、洗涤和干燥后,进行二次酸处理,使用5mol/L的氢氟酸,炭黑颗粒和酸的固液比是1:10(g/mL)。具体为,将干燥后的炭黑加入到氢氟酸中,超声处理5小时,然后过滤,用水在50℃下洗涤3次、真空干燥得到炭黑颗粒。Refer to the preparation method of Example 7. The difference from Example 7 is that after the first acid treatment and filtering, washing and drying, a second acid treatment is performed, using 5 mol/L hydrofluoric acid, carbon black particles and acid The solid-liquid ratio is 1:10 (g/mL). Specifically, the dried carbon black was added to hydrofluoric acid, treated with ultrasonic for 5 hours, then filtered, washed three times with water at 50°C, and vacuum dried to obtain carbon black particles.
实施例12Example 12
参照实施例8的制备方法,和实施例8的区别在于:在第一次酸洗并过滤、洗涤和干燥后,进行二次酸处理,使用5mol/L的氢氟酸,炭黑颗粒和酸的固液比是1:10(g/mL)。具体为,将干燥后的炭黑加入到氢氟酸中,超声处理5小时,然后过滤,用水在50℃下洗涤3次、真空干燥得到炭黑颗粒。Refer to the preparation method of Example 8. The difference from Example 8 is that after the first pickling and filtering, washing and drying, a second acid treatment is performed, using 5 mol/L hydrofluoric acid, carbon black particles and acid The solid-liquid ratio is 1:10 (g/mL). Specifically, the dried carbon black was added to hydrofluoric acid, treated with ultrasonic for 5 hours, then filtered, washed three times with water at 50°C, and vacuum dried to obtain carbon black particles.
对比例1Comparative example 1
称取制备例得到的热裂解炭黑A 100g;在80℃下配制碳酸钠饱和溶液,并将热裂解炭黑A在80℃碳酸钠饱和溶液中浸泡并超声5小时,热裂解炭黑A和碳酸钠饱和溶液的固液比为1:5(g/mL);随后过滤,用水在50℃下洗涤3次、真空干燥;将得到的炭黑投入5mol/L的硫酸中并超声处理5小时;随后过滤,用水在50℃下洗涤3次、真空干燥得到炭黑颗粒。Weigh 100g of the thermally cracked carbon black A obtained in the preparation example; prepare a saturated sodium carbonate solution at 80°C, soak the thermally cracked carbon black A in the saturated sodium carbonate solution at 80°C, and sonicate for 5 hours. The thermally cracked carbon black A and The solid-to-liquid ratio of the saturated sodium carbonate solution is 1:5 (g/mL); it is then filtered, washed three times with water at 50°C, and dried under vacuum; the obtained carbon black is put into 5 mol/L sulfuric acid and sonicated for 5 hours. ; Then filter, wash three times with water at 50°C, and dry under vacuum to obtain carbon black particles.
对比例2Comparative example 2
称取制备例得到的热裂解炭黑A 100g;在80℃下配制10mol/L的氢氧化钠溶液,并将热裂解炭黑A在80℃的氢氧化钠饱和溶液中浸泡并超声5小时,热裂解炭黑A和氢氧化钠饱和溶液的固液比为1:5(g/mL);随后过滤,用水在50℃下洗涤3次、真空干燥;将得到的炭黑投入5mol/L的硫酸中并超声处理5小时;随后过滤,用水在50℃下洗涤3次、真空干燥得到炭黑颗粒。Weigh 100g of the thermally cracked carbon black A obtained in the preparation example; prepare a 10 mol/L sodium hydroxide solution at 80°C, and soak the thermally cracked carbon black A in the saturated sodium hydroxide solution at 80°C and sonicate for 5 hours. The solid-liquid ratio of thermal cracking carbon black A and saturated sodium hydroxide solution is 1:5 (g/mL); then filter, wash with water 3 times at 50°C, and dry in vacuum; put the obtained carbon black into 5 mol/L in sulfuric acid and sonicated for 5 hours; then filtered, washed three times with water at 50°C, and dried under vacuum to obtain carbon black particles.
对比例3Comparative example 3
称取制备例得到的热裂解炭黑A 100g;将得到的炭黑投入5mol/L的硫酸中并超声处理5小时;随后过滤,用水在50℃下洗涤3次、真空干燥;在80℃下配制氢氧化钠饱和溶液,并将热裂解炭黑A在80℃的10mol/L的氢氧化钠溶液中浸泡并超声5小时,热裂解炭黑A和氢氧化钠饱和溶液的固液比为1:5(g/mL);随后过滤,用水在50℃下洗涤3次、真空干燥得到炭黑颗粒。Weigh 100g of the thermally cracked carbon black A obtained in the preparation example; put the obtained carbon black into 5 mol/L sulfuric acid and conduct ultrasonic treatment for 5 hours; then filter, wash with water 3 times at 50°C, and dry in vacuum; at 80°C Prepare a saturated solution of sodium hydroxide, soak the thermally cracked carbon black A in a 10mol/L sodium hydroxide solution at 80°C, and sonicate for 5 hours. The solid-liquid ratio of the thermally cracked carbon black A and the saturated sodium hydroxide solution is: 1:5 (g/mL); then filtered, washed three times with water at 50°C, and dried under vacuum to obtain carbon black particles.
根据国家标准测量制备例、实施例1-12和对比例1-3制得的炭黑颗粒的灰分含量和比表面积:The ash content and specific surface area of the carbon black particles prepared in the preparation examples, Examples 1-12 and Comparative Examples 1-3 were measured according to national standards:
1)灰分含量:依据GB/T 3780.10-2017的操作步骤进行检测;1) Ash content: Tested according to the operating procedures of GB/T 3780.10-2017;
2)比表面积:依据GB/T 3780.5-2017的操作步骤进行检测。2) Specific surface area: Tested according to the operating procedures of GB/T 3780.5-2017.
具体测量结果列于表1中。Specific measurement results are listed in Table 1.
表1Table 1
实施例1-12采用本申请的制备方法,其中实施例1-4采用单独的碱金属碳酸盐,实施例5-10采用碳酸氢钠和碳酸钾的组合,实施例11和12附加使用了第二次酸处理。对比例1和实施例1的区别主要在于:将炭黑碱金属碳酸盐饱和溶液超声处理,随后过滤、洗涤和干燥;而非将碱金属碳酸盐沉积在炭黑上。对比例2和实施例1的区别主要在于:不使用碱金属碳酸盐溶液对炭黑进行超声处理,而是采用现有技术中常用的氢氧化钠对炭黑进行碱洗处理。对比例3在对比例2的基础上调换了酸处理和碱处理的顺序。通过表1的数据可以看到,采用本申请的制备方法的实施例1-12,特别是实施例5-10,更特别是实施例11-12制得的炭黑的灰分含量和比表面积显著优于对比例1-3和制备例。对比例1的碱金属碳酸盐没有沉积在炭黑表面并随后和酸反应,其效果较差,甚至不如使用氢氧化钠的对比例2和3。可见,将碱金属碳酸盐沉积在炭黑表面并随后和酸反应是非常关键的。另外,根据实施例1-7可以看出,不同的碱金属碳酸盐的效果不同,碳酸氢钠和碳酸钾的组合的效果较好。更进一步的,采用二次酸处理可以进一步降低灰分含量,提高比表面积。Examples 1-12 adopt the preparation method of the present application, wherein Examples 1-4 adopt a single alkali metal carbonate, Examples 5-10 adopt a combination of sodium bicarbonate and potassium carbonate, and Examples 11 and 12 additionally use Second acid treatment. The main difference between Comparative Example 1 and Example 1 is that the carbon black alkali metal carbonate saturated solution is sonicated, followed by filtration, washing and drying; instead of depositing the alkali metal carbonate on the carbon black. The main difference between Comparative Example 2 and Example 1 is that an alkali metal carbonate solution is not used for ultrasonic treatment of carbon black, but sodium hydroxide commonly used in the prior art is used for alkali washing treatment of carbon black. Comparative Example 3 is based on Comparative Example 2 and exchanges the order of acid treatment and alkali treatment. It can be seen from the data in Table 1 that the ash content and specific surface area of the carbon black prepared in Examples 1-12, especially Examples 5-10, and more especially Examples 11-12, using the preparation method of the present application are significantly Better than Comparative Examples 1-3 and Preparation Examples. The alkali metal carbonate in Comparative Example 1 did not deposit on the surface of carbon black and subsequently react with acid, and its effect was poor, even inferior to Comparative Examples 2 and 3 using sodium hydroxide. It can be seen that it is very critical to deposit alkali metal carbonate on the surface of carbon black and then react with acid. In addition, according to Examples 1-7, it can be seen that different alkali metal carbonates have different effects, and the combination of sodium bicarbonate and potassium carbonate has a better effect. Furthermore, secondary acid treatment can further reduce the ash content and increase the specific surface area.
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