CN101358042B - Pigment carbon black products and preparation technique thereof - Google Patents
Pigment carbon black products and preparation technique thereof Download PDFInfo
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- CN101358042B CN101358042B CN 200810071476 CN200810071476A CN101358042B CN 101358042 B CN101358042 B CN 101358042B CN 200810071476 CN200810071476 CN 200810071476 CN 200810071476 A CN200810071476 A CN 200810071476A CN 101358042 B CN101358042 B CN 101358042B
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- 239000006229 carbon black Substances 0.000 title claims abstract description 98
- 239000000049 pigment Substances 0.000 title claims abstract description 19
- 238000000034 method Methods 0.000 title claims description 17
- 238000002360 preparation method Methods 0.000 title abstract description 4
- 239000002994 raw material Substances 0.000 claims abstract description 26
- 238000004519 manufacturing process Methods 0.000 claims abstract description 19
- 239000000654 additive Substances 0.000 claims abstract description 12
- 230000000996 additive effect Effects 0.000 claims abstract description 7
- 235000019241 carbon black Nutrition 0.000 claims description 91
- 239000003921 oil Substances 0.000 claims description 54
- 238000002485 combustion reaction Methods 0.000 claims description 37
- 239000000295 fuel oil Substances 0.000 claims description 33
- 238000006243 chemical reaction Methods 0.000 claims description 25
- MWPLVEDNUUSJAV-UHFFFAOYSA-N anthracene Chemical compound C1=CC=CC2=CC3=CC=CC=C3C=C21 MWPLVEDNUUSJAV-UHFFFAOYSA-N 0.000 claims description 22
- 239000011280 coal tar Substances 0.000 claims description 17
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 16
- 239000003546 flue gas Substances 0.000 claims description 16
- 239000007789 gas Substances 0.000 claims description 11
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical group [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims description 10
- TYJJADVDDVDEDZ-UHFFFAOYSA-M potassium hydrogencarbonate Chemical compound [K+].OC([O-])=O TYJJADVDDVDEDZ-UHFFFAOYSA-M 0.000 claims description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- 239000002918 waste heat Substances 0.000 claims description 6
- 239000002816 fuel additive Substances 0.000 claims description 5
- 239000000203 mixture Substances 0.000 claims description 5
- 239000003973 paint Substances 0.000 claims description 5
- 229910000027 potassium carbonate Inorganic materials 0.000 claims description 5
- 238000010248 power generation Methods 0.000 claims description 5
- 238000010791 quenching Methods 0.000 claims description 5
- 230000000171 quenching effect Effects 0.000 claims description 5
- 239000007787 solid Substances 0.000 claims description 5
- 238000005336 cracking Methods 0.000 claims description 4
- 239000000843 powder Substances 0.000 claims description 4
- 239000000779 smoke Substances 0.000 claims description 4
- 239000006185 dispersion Substances 0.000 abstract description 2
- 238000004040 coloring Methods 0.000 abstract 1
- 239000002245 particle Substances 0.000 description 3
- 239000012535 impurity Substances 0.000 description 2
- 238000009776 industrial production Methods 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 229910003481 amorphous carbon Inorganic materials 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000003776 cleavage reaction Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000002310 reflectometry Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
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Abstract
Description
技术领域 technical field
本发明属于炭黑工艺领域,更具体涉及一种C385系列炭黑产品及其生产工艺。 The invention belongs to the technical field of carbon black, and more specifically relates to a C385 series carbon black product and a production process thereof. the
背景技术Background technique
炭黑为一种无定形碳。轻、松而极细的黑色粉末,比表面积非常大,范围从10-3000m2/g,是有机物(天然气、重油、燃料油等)在空气不足的条件下经不完全燃烧或受热分解而得的产物,炭黑因为生产方法不同其表面化学性能各异。目前,色素炭黑产品质量参差不齐,制备工艺也不是十分成熟。 Carbon black is an amorphous carbon. Light, loose and extremely fine black powder with a very large specific surface area ranging from 10-3000m 2 /g, which is obtained by incomplete combustion or thermal decomposition of organic matter (natural gas, heavy oil, fuel oil, etc.) in the absence of air The product of carbon black has different surface chemical properties due to different production methods. At present, the quality of pigment carbon black products is uneven, and the preparation process is not very mature.
发明目的 Purpose of the invention
本发明的目的是提供一种C385系列炭黑产品及其生产工艺,该炭黑产品属于色素炭黑,具有黑度、着色力好,易于分散,光泽度较好等特点,而且原料合理,制备工艺成熟,适合工业化大生产。 The purpose of the present invention is to provide a C385 series carbon black product and its production process. The carbon black product belongs to pigment carbon black and has the characteristics of blackness, good tinting strength, easy dispersion, good gloss, etc., and the raw materials are reasonable and easy to prepare. The process is mature and suitable for large-scale industrial production. the
本发明的C385系列炭黑产品的原料包括:所述C385系列炭黑的原料包括:原料油和添加剂,所述原料油的用量与添加剂的用量重量比为:1500~1620∶0.6~0.9。 The raw materials of the C385 series carbon black products of the present invention include: the raw materials of the C385 series carbon blacks include: raw material oil and additives, and the weight ratio of the amount of the raw material oil to the amount of the additives is: 1500-1620: 0.6-0.9. the
本发明的C385系列炭黑产品采用炉法工艺色素炭黑生产工艺生产。 The C385 series carbon black product of the present invention is produced by a furnace process technology pigment carbon black production process. the
本发明的显著优点是:本发明以煤焦油为燃料油,在煤焦油中配以适当的蒽油为原料油,采用的原料比例合理,炭黑收率较高,所产炭黑产品粒径中等,粒径分布较窄,炭黑表面含氧官能团较高,结构较低,炭黑经微粉粉碎机,造粒机后,制得C385系列炭黑产品,因此生产的炭黑产品属于色素炭黑,具有黑度、着色力好,易于分散,杂质少等特点,而且原料合理,制备工艺成熟,适合工业化大生产,具有显著的经济效益。 The remarkable advantages of the present invention are: coal tar is used as fuel oil in the present invention, appropriate anthracene oil is mixed in coal tar as raw material oil, the proportion of raw materials adopted is reasonable, the yield of carbon black is high, and the particle size of the produced carbon black product is Medium, narrow particle size distribution, high oxygen-containing functional groups on the surface of carbon black, and low structure. After the carbon black is pulverized and granulated, the C385 series carbon black products are obtained, so the produced carbon black products belong to pigment carbon. Black, with good blackness and tinting strength, easy to disperse, less impurities, etc., and the raw materials are reasonable, the preparation process is mature, suitable for large-scale industrial production, and has significant economic benefits. the
附图说明Description of drawings
图1是本发明的炉法工艺色素炭黑新工艺生产工艺流程图,其中1燃烧室;2喉口;3反应室;4烟道;5余热锅炉;6高温空气预热器;7中温空气预热器;8低温空气预热器;9一级热补偿器;10一级旋风分离器;11二级热补偿器;12二级旋风分离器;13袋滤器;14袋滤器;15微粉粉碎机;16风送风机;17收集旋风分离器;18造粒机;19特种炭黑机;20原料油泵;21原料油过滤器;22罗茨鼓风机;23燃料油过滤器;24燃料油泵;25尾气风机;26冷却水泵。 Fig. 1 is the production process flow diagram of the new process of the furnace process pigment carbon black of the present invention, wherein 1 combustion chamber; 2 throat; 3 reaction chamber; 4 flue; 5 waste heat boiler; 6 high-temperature air preheater; Preheater; 8 low temperature air preheater; 9 primary thermal compensator; 10 primary cyclone separator; 11 secondary thermal compensator; 12 secondary cyclone separator; 13 bag filter; 14 bag filter; 15 fine powder crushing 16 air blower; 17 collection cyclone separator; 18 granulator; 19 special carbon black machine; 20 raw oil pump; 21 raw oil filter; 22 Roots blower; 23 fuel oil filter; 24 fuel oil pump; 25 tail gas Fan; 26 cooling water pumps. the
具体实施方式Detailed ways
所述原料油的用量与添加剂的用量重量比为:1500~1620∶0.6~0.9;原料油为煤焦油和蒽油的混合物,所述原料油中煤焦油和蒽油的用量配比为:重量比6∶4~7∶3;所述原料油的水分小于4%,密度为1.14~1.17g/ml,出油率大于70%。 The weight ratio of the amount of raw material oil to that of additives is: 1500-1620: 0.6-0.9; the raw material oil is a mixture of coal tar and anthracene oil, and the ratio of coal tar and anthracene oil in the raw material oil is: weight The ratio is 6:4-7:3; the water content of the raw material oil is less than 4%, the density is 1.14-1.17g/ml, and the oil yield is greater than 70%. the
添加剂为碳酸钾。 The additive is potassium carbonate. the
本发明的C385系列炭黑为应用于油漆、油墨行业的粉末型色素炭黑。 The C385 series carbon black of the present invention is a powder-type pigment carbon black used in the paint and ink industries. the
本发明的C385系列炭黑产品采用炉法新工艺色素炭黑生产工艺具体如下: The C385 series carbon black product of the present invention adopts the furnace process new process pigment carbon black production process to be specific as follows:
1)将空气经过罗茨鼓风机压缩至压力为0.036~0.040Mpa,依次经过低温空气预热器、中温空气预热器和高温空气预热器,加热到600℃后送入燃烧室; 1) The air is compressed by a Roots blower to a pressure of 0.036-0.040Mpa, then passes through a low-temperature air preheater, a medium-temperature air preheater and a high-temperature air preheater in sequence, and is heated to 600°C before being sent into the combustion chamber;
2)将燃料油和添加剂送入燃烧室后与热空气混合燃烧,温度控制在1500~1520℃,将燃烧产生的热烟气经喉口进入反应室,将原料油经喉口喷入,在反应室内裂解反应;温度为1450℃,压力为20Kpa。 2) Fuel oil and additives are sent into the combustion chamber and mixed with hot air for combustion. The temperature is controlled at 1500-1520°C. The hot smoke generated by combustion enters the reaction chamber through the throat, and the raw material oil is injected through the throat. Cleavage reaction in the reaction chamber; the temperature is 1450°C and the pressure is 20Kpa. the
3)反应结束后,将反应的产物烟气经过急冷水急冷后进入余热锅炉,随后经过高温空气预热器、中温空气预热器和低温空气预热器,使产物烟气的温度降至340℃; 3) After the reaction, the product flue gas of the reaction is quenched by quenching water and then enters the waste heat boiler, and then passes through the high-temperature air preheater, medium-temperature air preheater and low-temperature air preheater to reduce the temperature of the product flue gas to 340 ℃;
4)将产物烟气经过一级热补偿器、一级旋风分离器、二级热补偿器和二级旋风分离器,温度降至200~250℃,进入袋滤器进行收集,收集到的炭黑通过微粉粉碎机,经风送风机送至收集旋风分离器; 4) The product flue gas passes through the primary thermal compensator, the primary cyclone separator, the secondary thermal compensator and the secondary cyclone separator, the temperature drops to 200-250°C, and it enters the bag filter for collection. The collected carbon black Through the fine powder pulverizer, it is sent to the collection cyclone separator through the air blower;
5)所述收集旋风分离器的炭黑经过造粒机造粒后,经过特种炭黑机加工,通过40~400目筛网后制成C385系列炭黑产品。 5) The carbon black collected in the cyclone separator is granulated by a granulator, processed by a special carbon black machine, and passed through a 40-400 mesh screen to make a C385 series carbon black product. the
所述一级旋风分离器、二级旋风分离器、袋滤器和收集旋风分离器中残留的固体炭黑通过微粉粉碎机,经风送风机至收集旋风分离器;收集旋风分离器的炭黑经过造粒机造粒后,经过特种炭黑机(微粒粉碎机)加工(粉碎研磨),通过40~400目筛网后制成C385系列炭黑产品。 The solid carbon black remaining in the first-stage cyclone separator, secondary cyclone separator, bag filter and collection cyclone separator passes through the micropowder pulverizer, and is collected by the wind blower to the collection cyclone separator; the carbon black of the collection cyclone separator is processed After being granulated by a granulator, it is processed (crushed and ground) by a special carbon black machine (particle pulverizer) and passed through a 40-400 mesh screen to make C385 series carbon black products. the
所述燃料油为煤焦油,所述燃料油经过燃料油过滤器后配以重量浓度10%的碳酸钾溶液一同进入燃烧室,所述碳酸钾溶液以每小时6~8升的流量进入燃烧室,所述燃料油以240kg/h的流量进入燃烧室。 The fuel oil is coal tar, and the fuel oil enters the combustion chamber together with potassium carbonate solution with a weight concentration of 10% after passing through the fuel oil filter, and the potassium carbonate solution enters the combustion chamber at a flow rate of 6-8 liters per hour , the fuel oil enters the combustion chamber at a flow rate of 240kg/h. the
所述原料油经过原料油过滤器后以每分钟25~27kg的流量经喉口喷入。 The raw oil is sprayed through the throat at a flow rate of 25-27 kg per minute after passing through the raw oil filter. the
所述袋滤器中的尾气经尾气风机排出后用于发电。 The tail gas in the bag filter is used for power generation after being discharged by the tail gas blower. the
本发明的C385系列炭黑产品的指标如下: The index of C385 series carbon black product of the present invention is as follows:
本发明的C385系列炭黑产品主要根据经过特种炭黑机加工后通过筛网目数不同而区别成不同细度的C385炭黑产品。 The C385 series carbon black products of the present invention are mainly differentiated into C385 carbon black products of different finenesses according to the different meshes of the sieve after being processed by special carbon black machines. the
以下是本发明的几个实施例,进一步阐述本发明,但是本发明不仅限于此。 The following are several embodiments of the present invention to further illustrate the present invention, but the present invention is not limited thereto. the
实施例1 Example 1
原料油为煤焦油和蒽油的混合物,所述原料油中煤焦油和蒽油的用量配比为:重量比7∶3;所述原料油的水分小于4%,密度为1.17g/ml,出油率大于70%。 The raw material oil is a mixture of coal tar and anthracene oil, and the ratio of coal tar and anthracene oil in the raw material oil is: the weight ratio is 7:3; the moisture content of the raw material oil is less than 4%, and the density is 1.17g/ml. The oil yield is greater than 70%. the
添加剂为碳酸钾。 The additive is potassium carbonate. the
本发明的C385系列炭黑为应用于油漆、油墨行业的颗粒型色素炭黑。 The C385 series carbon black of the present invention is a granular pigment carbon black used in the paint and ink industries. the
本发明的C385系列炭黑产品采用炉法工艺色素炭黑生产工艺具体如下: C385 series carbon black product of the present invention adopts furnace process process pigment carbon black production process to be specific as follows:
1)将空气经过罗茨鼓风机压缩至压力为0.036Mpa,依次经过低温空气预热器、中温空气预热器和高温空气预热器,加热到600℃后送入燃烧室; 1) The air is compressed by a Roots blower to a pressure of 0.036Mpa, then passes through a low-temperature air preheater, a medium-temperature air preheater and a high-temperature air preheater in sequence, and is heated to 600°C before being sent into the combustion chamber;
2)将燃料油和添加剂送入燃烧室后与热空气混合燃烧,温度控制在1500℃,将燃烧产生的热烟气经喉口进入反应室,将原料油经喉口喷入,在反应室内裂解反应;温度为1450℃,压力为20Kpa。 2) Fuel oil and additives are sent into the combustion chamber and mixed with hot air for combustion. The temperature is controlled at 1500°C. The hot smoke generated by combustion enters the reaction chamber through the throat, and the raw material oil is sprayed into the reaction chamber through the throat. Cracking reaction; the temperature is 1450°C and the pressure is 20Kpa. the
3)反应结束后,将反应的产物烟气经过急冷水急冷后进入余热锅炉,随后经过高温空气预热器、中温空气预热器和低温空气预热器,使产物烟气的温度降至340℃; 3) After the reaction, the product flue gas of the reaction is quenched by quenching water and then enters the waste heat boiler, and then passes through the high-temperature air preheater, medium-temperature air preheater and low-temperature air preheater to reduce the temperature of the product flue gas to 340 ℃;
4)将产物烟气经过一级热补偿器、一级旋风分离器、二级热补偿器和二级旋风分离器,温度降至200℃,进入袋滤器进行收集,收集到的炭黑通过微粉粉碎机,经风送风机送至收集旋风分离器; 4) The product flue gas passes through the primary thermal compensator, the primary cyclone separator, the secondary thermal compensator and the secondary cyclone separator, the temperature drops to 200°C, and enters the bag filter for collection. The collected carbon black is passed through the micropowder The pulverizer is sent to the collection cyclone separator through the air blower;
5)所述收集旋风分离器的炭黑经过造粒机造粒后,经过特种炭黑机加工,通过40目筛网后制成C385系列炭黑产品。 5) The carbon black collected in the cyclone separator is granulated by a granulator, processed by a special carbon black machine, and passed through a 40-mesh screen to make a C385 series carbon black product. the
所述一级旋风分离器、二级旋风分离器、袋滤器和收集旋风分离器中残留的固体炭黑通 过微粉粉碎机,经风送风机至收集旋风分离器;收集旋风分离器的炭黑经过造粒机造粒后,经过特种炭黑机加工,通过40目筛网后制成C385炭黑产品。 The solid carbon black remaining in the first-stage cyclone separator, secondary cyclone separator, bag filter and collection cyclone separator passes through the micropowder pulverizer, and is collected by the wind blower to the collection cyclone separator; the carbon black of the collection cyclone separator passes through After granulation by the granulator, it is processed by a special carbon black machine and passed through a 40-mesh screen to make C385 carbon black products. the
所述燃料油为煤焦油,所述燃料油经过燃料油过滤器后配以重量浓度10%的碳酸钾溶液一同进入燃烧室,所述碳酸钾溶液以每小时6升的流量进入燃烧室,所述燃料油以240kg/h的流量进入燃烧室。 Described fuel oil is coal tar, and described fuel oil enters combustion chamber together with potassium carbonate solution of weight concentration 10% after described fuel oil passes through fuel oil filter, and described potassium carbonate solution enters combustion chamber with the flow rate of 6 liters per hour, so Said fuel oil enters the combustion chamber with a flow rate of 240kg/h. the
所述原料油经过原料油过滤器后以每分钟25kg的流量经喉口喷入。 The raw oil is sprayed through the throat at a flow rate of 25 kg per minute after passing through the raw oil filter. the
所述袋滤器中的尾气经尾气风机排出后用于发电。 The tail gas in the bag filter is used for power generation after being discharged by the tail gas blower. the
实施例2 Example 2
原料油为煤焦油和蒽油的混合物,所述原料油中煤焦油和蒽油的用量配比为:重量比6∶4;所述原料油的水分小于4%,密度为1.14g/ml,出油率大于70%。 The feedstock oil is a mixture of coal tar and anthracene oil, and the proportioning ratio of coal tar and anthracene oil in the feedstock oil is: weight ratio 6:4; the moisture content of the feedstock oil is less than 4%, and the density is 1.14g/ml. The oil yield is greater than 70%. the
添加剂为碳酸钾。 The additive is potassium carbonate. the
本发明的C385系列炭黑为应用于油漆、油墨行业的粉末型色素炭黑。 The C385 series carbon black of the present invention is a powder-type pigment carbon black used in the paint and ink industries. the
本发明的C385系列炭黑产品采用炉法工艺色素炭黑生产工艺具体如下: C385 series carbon black product of the present invention adopts furnace process process pigment carbon black production process to be specific as follows:
1)将空气经过罗茨鼓风机压缩至压力为0.040Mpa,依次经过低温空气预热器、中温空气预热器和高温空气预热器,加热到600℃后送入燃烧室; 1) The air is compressed by a Roots blower to a pressure of 0.040Mpa, then passes through a low-temperature air preheater, a medium-temperature air preheater and a high-temperature air preheater in sequence, and is heated to 600°C before being sent into the combustion chamber;
2)将燃料油和添加剂送入燃烧室后与热空气混合燃烧,温度控制在1520℃,将燃烧产生的热烟气经喉口进入反应室,将原料油经喉口喷入,在反应室内裂解反应;温度为1450℃,压力为20Kpa。 2) Fuel oil and additives are sent into the combustion chamber and mixed with hot air for combustion. The temperature is controlled at 1520°C. The hot smoke generated by combustion enters the reaction chamber through the throat, and the raw material oil is sprayed into the reaction chamber through the throat. Cracking reaction; the temperature is 1450°C and the pressure is 20Kpa. the
3)反应结束后,将反应的产物烟气经过急冷水急冷后进入余热锅炉,随后经过高温空气预热器、中温空气预热器和低温空气预热器,使产物烟气的温度降至340℃; 3) After the reaction, the product flue gas of the reaction is quenched by quenching water and then enters the waste heat boiler, and then passes through the high-temperature air preheater, medium-temperature air preheater and low-temperature air preheater to reduce the temperature of the product flue gas to 340 ℃;
4)将产物烟气经过一级热补偿器、一级旋风分离器、二级热补偿器和二级旋风分离器,温度降至250℃,进入袋滤器进行收集,收集到的炭黑通过微粉粉碎机,经风送风机送至收集旋风分离器; 4) The product flue gas passes through the primary thermal compensator, the primary cyclone separator, the secondary thermal compensator and the secondary cyclone separator, the temperature drops to 250°C, and it enters the bag filter for collection. The collected carbon black passes through the micropowder The pulverizer is sent to the collection cyclone separator through the air blower;
5)所述收集旋风分离器的炭黑经过造粒机造粒后,经过特种炭黑机加工后,通过400目筛网后制成C385炭黑产品。 5) The carbon black collected in the cyclone separator is granulated by a granulator, processed by a special carbon black machine, and passed through a 400-mesh screen to make a C385 carbon black product. the
所述一级旋风分离器、二级旋风分离器、袋滤器和收集旋风分离器中残留的固体炭黑通过微粉粉碎机,经风送风机至收集旋风分离器;收集旋风分离器的炭黑经过造粒机造粒后,经过特种炭黑机加工,通过400目筛网后制成C385炭黑产品。 The solid carbon black remaining in the first-stage cyclone separator, secondary cyclone separator, bag filter and collection cyclone separator passes through the micropowder pulverizer, and is collected by the wind blower to the collection cyclone separator; the carbon black of the collection cyclone separator is processed After being granulated by a granulator, it is processed by a special carbon black machine and passed through a 400-mesh screen to make a C385 carbon black product. the
所述燃料油为煤焦油,所述燃料油经过燃料油过滤器后配以重量浓度10%的碳酸钾溶液一同进入燃烧室,所述碳酸钾溶液以每小时8升的流量进入燃烧室,所述燃料油的以240kg/h的流量进入燃烧室。 Described fuel oil is coal tar, and described fuel oil enters combustion chamber together with potassium carbonate solution of weight concentration 10% after described fuel oil passes through fuel oil filter, and described potassium carbonate solution enters combustion chamber with the flow rate of 8 liters per hour, so The above-mentioned fuel oil enters the combustion chamber with a flow rate of 240kg/h. the
所述原料油经过原料油过滤器后以每分钟27kg的流量经喉口喷入。 After the raw oil passes through the raw oil filter, it is injected through the throat at a flow rate of 27 kg per minute. the
所述袋滤器中的尾气经尾气风机排出后用于发电。 The tail gas in the bag filter is used for power generation after being discharged by the tail gas blower. the
实施例3 Example 3
原料油为煤焦油和蒽油的混合物,所述原料油中煤焦油和蒽油的用量配比为:重量比6∶4~7∶3;所述原料油的水分小于4%,密度为1.14~1.17g/ml,出油率大于70%。 The raw material oil is a mixture of coal tar and anthracene oil, and the ratio of coal tar and anthracene oil in the raw material oil is: the weight ratio is 6:4 to 7:3; the water content of the raw material oil is less than 4%, and the density is 1.14 ~1.17g/ml, the oil yield is greater than 70%. the
添加剂为碳酸钾。 The additive is potassium carbonate. the
本发明的C385系列炭黑为应用于油漆、油墨行业的颗粒型色素炭黑。 The C385 series carbon black of the present invention is a granular pigment carbon black used in the paint and ink industries. the
本发明的C385系列炭黑产品采用炉法新工艺色素炭黑生产工艺具体如下: The C385 series carbon black product of the present invention adopts the furnace process new process pigment carbon black production process to be specific as follows:
1)将空气经过罗茨鼓风机压缩至压力为0.038Mpa,依次经过低温空气预热器、中温空气预热器和高温空气预热器,加热到600℃后送入燃烧室; 1) The air is compressed by a Roots blower to a pressure of 0.038Mpa, then passes through a low-temperature air preheater, a medium-temperature air preheater and a high-temperature air preheater in sequence, and is heated to 600°C before being sent into the combustion chamber;
2)将燃料油和添加剂送入燃烧室后与热空气混合燃烧,温度控制在1510℃,将燃烧产生的热烟气经喉口进入反应室,将原料油经喉口喷入,在反应室内裂解反应;温度为1450℃,压力为20Kpa。 2) Fuel oil and additives are sent into the combustion chamber and mixed with hot air for combustion. The temperature is controlled at 1510°C. The hot flue gas generated by combustion enters the reaction chamber through the throat, and the raw material oil is sprayed into the reaction chamber through the throat. Cracking reaction; the temperature is 1450°C and the pressure is 20Kpa. the
3)反应结束后,将反应的产物烟气经过急冷水急冷后进入余热锅炉,随后经过高温空气预热器、中温空气预热器和低温空气预热器,使产物烟气的温度降至340℃; 3) After the reaction, the product flue gas of the reaction is quenched by quenching water and then enters the waste heat boiler, and then passes through the high-temperature air preheater, medium-temperature air preheater and low-temperature air preheater to reduce the temperature of the product flue gas to 340 ℃;
4)将产物烟气经过一级热补偿器、一级旋风分离器、二级热补偿器和二级旋风分离器,温度降至230℃,进入袋滤器进行收集,收集到的炭黑通过微粉粉碎机,经风送风机送至收集旋风分离器; 4) The product flue gas passes through the primary thermal compensator, the primary cyclone separator, the secondary thermal compensator and the secondary cyclone separator, the temperature drops to 230°C, and it enters the bag filter for collection, and the collected carbon black passes through the micropowder The pulverizer is sent to the collection cyclone separator through the air blower;
5)所述收集旋风分离器的炭黑经过造粒机造粒后,经过经过特种炭黑机加工,通过40~400目筛网后制成C385炭黑产品。 5) The carbon black collected in the cyclone separator is granulated by a granulator, processed by a special carbon black machine, and passed through a 40-400 mesh screen to make a C385 carbon black product. the
所述一级旋风分离器、二级旋风分离器、袋滤器和收集旋风分离器中残留的固体炭黑通过微粉粉碎机,经风送风机至收集旋风分离器;收集旋风分离器的炭黑经过造粒机造粒后,经过特种炭黑机加工,通过40~400目筛网后制成C385炭黑产品。 The solid carbon black remaining in the first-stage cyclone separator, secondary cyclone separator, bag filter and collection cyclone separator passes through the micropowder pulverizer, and is collected by the wind blower to the collection cyclone separator; the carbon black of the collection cyclone separator is processed After being granulated by a granulator, it is processed by a special carbon black machine and passed through a 40-400 mesh screen to make a C385 carbon black product. the
所述燃料油为煤焦油,所述燃料油经过燃料油过滤器后配以重量浓度10%的碳酸钾溶液一同进入燃烧室,所述碳酸钾溶液以每小时7升的流量进入燃烧室,所述燃料油的以240kg/h的流量进入燃烧室。 Described fuel oil is coal tar, and described fuel oil enters combustion chamber together with potassium carbonate solution of weight concentration 10% after described fuel oil passes through fuel oil filter, and described potassium carbonate solution enters combustion chamber with the flow rate of 7 liters per hour, so The above-mentioned fuel oil enters the combustion chamber with a flow rate of 240kg/h. the
所述原料油经过原料油过滤器后以每分钟26kg的流量经喉口喷入。 After the raw oil passes through the raw oil filter, it is injected through the throat at a flow rate of 26 kg per minute. the
所述袋滤器中的尾气经尾气风机排出后用于发电。 The tail gas in the bag filter is used for power generation after being discharged by the tail gas blower. the
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| CN112048196B (en) * | 2020-08-26 | 2022-02-22 | 茂名环星新材料股份有限公司 | Carbon black and production process thereof |
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| CN113527915B (en) * | 2021-08-25 | 2022-04-01 | 乌海黑猫炭黑有限责任公司 | Production method of pigment carbon black applied to leather color paste |
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