CN101220284A - A kind of preparation method of electrode impregnation pitch - Google Patents
A kind of preparation method of electrode impregnation pitch Download PDFInfo
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- CN101220284A CN101220284A CNA200710158909XA CN200710158909A CN101220284A CN 101220284 A CN101220284 A CN 101220284A CN A200710158909X A CNA200710158909X A CN A200710158909XA CN 200710158909 A CN200710158909 A CN 200710158909A CN 101220284 A CN101220284 A CN 101220284A
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- 238000002360 preparation method Methods 0.000 title claims description 5
- 238000005470 impregnation Methods 0.000 title abstract description 4
- 239000002904 solvent Substances 0.000 claims abstract description 29
- SMWDFEZZVXVKRB-UHFFFAOYSA-N Quinoline Chemical compound N1=CC=CC2=CC=CC=C21 SMWDFEZZVXVKRB-UHFFFAOYSA-N 0.000 claims abstract description 26
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 claims abstract description 16
- 238000010438 heat treatment Methods 0.000 claims abstract description 13
- 238000004821 distillation Methods 0.000 claims abstract description 12
- 238000003828 vacuum filtration Methods 0.000 claims abstract description 11
- 239000002994 raw material Substances 0.000 claims abstract description 6
- 239000000047 product Substances 0.000 claims abstract description 5
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 8
- 229910052802 copper Inorganic materials 0.000 claims description 8
- 239000010949 copper Substances 0.000 claims description 8
- 239000000706 filtrate Substances 0.000 claims description 8
- 238000000967 suction filtration Methods 0.000 claims description 5
- 238000003756 stirring Methods 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 3
- 230000006837 decompression Effects 0.000 claims 1
- 239000010426 asphalt Substances 0.000 abstract description 32
- 238000000034 method Methods 0.000 abstract description 25
- 239000011280 coal tar Substances 0.000 abstract description 7
- 238000004519 manufacturing process Methods 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract description 5
- 238000011084 recovery Methods 0.000 abstract description 4
- 239000012065 filter cake Substances 0.000 abstract description 2
- 238000011282 treatment Methods 0.000 abstract description 2
- 239000011295 pitch Substances 0.000 description 12
- 238000001914 filtration Methods 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 238000001816 cooling Methods 0.000 description 3
- 239000011259 mixed solution Substances 0.000 description 3
- 238000000638 solvent extraction Methods 0.000 description 3
- 239000011294 coal tar pitch Substances 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000012943 hotmelt Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000011338 soft pitch Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000012719 thermal polymerization Methods 0.000 description 1
Landscapes
- Working-Up Tar And Pitch (AREA)
Abstract
一种电极浸渍沥青的制取方法,采用中温沥青为原料,以脱酚酚油为溶剂,经过加热溶解、真空抽滤、溶剂蒸馏回收三项处理以脱除中温沥青中的喹啉不溶物,从而制得喹啉不溶物重量小于0.1%电极浸渍沥青产品。本发明电极浸渍沥青产率可达到80%以上;用后的脱酚酚油溶剂可再次使用,滤饼可作为重沥青处理;整个生产过程所需设备少,工艺简单易于控制,工序少,效果好;按每年处理中温沥青5000吨计算,可生产电极浸渍沥青4000吨,不失为煤焦油沥青加工的一种有效方法。A method for preparing electrode-impregnated asphalt, which uses medium-temperature asphalt as a raw material and dephenolized phenol oil as a solvent, and undergoes three treatments of heating and dissolving, vacuum filtration, and solvent distillation recovery to remove quinoline insolubles in the medium-temperature asphalt, Thereby, an electrode impregnation pitch product with less than 0.1% weight of quinoline insoluble matter can be obtained. The electrode impregnated asphalt yield of the present invention can reach more than 80%; the used dephenolized phenolic oil solvent can be used again, and the filter cake can be treated as heavy asphalt; the whole production process requires less equipment, the process is simple and easy to control, the process is less, and the effect is high. Good; based on the annual processing of 5,000 tons of medium-temperature asphalt, 4,000 tons of electrode-impregnated asphalt can be produced, which is an effective method for coal tar asphalt processing.
Description
技术领域technical field
本发明属于煤化工领域,尤其涉及一种利用中温沥青制取电极浸渍沥青的方法。The invention belongs to the field of coal chemical industry, and in particular relates to a method for preparing electrode-impregnated asphalt by using medium-temperature asphalt.
背景技术Background technique
电极浸渍沥青的制取方法按生产原料分有煤焦油、软沥青、中温沥青等。按生产方法分有煤焦油过滤法、煤焦油溶剂抽提法、煤焦油(软沥青)热聚合法、煤沥青溶剂沉降法、中温沥青溶剂过滤法。采用中温沥青制取电极浸渍沥青生产的关键是脱除喹啉不溶物含量,脱除喹啉不溶物的的方法有以下几种。The preparation method of electrode impregnated asphalt is divided into coal tar, soft asphalt, medium temperature asphalt and so on according to the production raw materials. According to the production method, there are coal tar filtration method, coal tar solvent extraction method, coal tar (soft pitch) thermal polymerization method, coal tar pitch solvent precipitation method, and medium temperature pitch solvent filtration method. The key to the production of electrode impregnated asphalt by using medium-temperature pitch is to remove the content of quinoline insolubles. There are several methods for removing quinoline insolubles.
静置沉降分离:主要依靠重力沉降来分离所含杂质。本方法特点是投资小、工艺简单,但净化效果差。Static sedimentation separation: mainly rely on gravity sedimentation to separate the contained impurities. This method is characterized by small investment and simple process, but poor purification effect.
离心分离:使用高速离心机离心脱除原生喹啉不溶物,该装置设备庞大,金属耗费大,能耗高。Centrifugal separation: Use a high-speed centrifuge to centrifugally remove the insoluble matter of primary quinoline. The equipment is huge, the metal consumption is large, and the energy consumption is high.
热溶过滤:首先在釜中融料粗滤,粗滤釜配有加热炉,加压阀、放空阀;然后采用高效滤材把粗滤的原料进入精滤釜过滤,此方法净化效果好,工艺简单,但对滤网要求苛刻。Hot-melt filtration: First, melt the material in the kettle for coarse filtration. The coarse filter kettle is equipped with a heating furnace, a pressure valve, and a vent valve; then use high-efficiency filter materials to filter the coarsely filtered raw materials into the fine filter kettle. The process is simple, but the filter screen is demanding.
溶剂萃取:加入溶剂后进行溶剂萃取,此方法投资小,净化效果好,但溶剂用量大,收率低。Solvent extraction: Solvent extraction is carried out after adding solvent. This method has small investment and good purification effect, but the amount of solvent is large and the yield is low.
目前我国电极浸渍沥青的生产尚处于开发试制阶段,用中温沥青生产电极浸渍沥青的方法尚没有实现工业化。因此经检索,尚未见与本发明相同或相近似的专利文献及相关的资料报道。At present, the production of electrode impregnated pitch in our country is still in the stage of development and trial production, and the method of producing electrode impregnated pitch with medium temperature asphalt has not yet been industrialized. Therefore search, as yet identical with the present invention or similar patent document and relevant data report.
发明内容Contents of the invention
本发明的目的是提供一种投资省,见效快,工艺简单,能有效脱除中温沥青中的喹啉不容物,从而获得高品质电极浸渍沥青的方法。The purpose of the present invention is to provide a method with low investment, quick effect, simple process, which can effectively remove the quinoline content in medium-temperature asphalt, so as to obtain high-quality electrode-impregnated asphalt.
为此,本发明所采取的技术解决方案是:For this reason, the technical solution that the present invention takes is:
本发明电极浸渍沥青的制取方法,采用中温沥青为原料,以脱酚酚油为溶剂,经过加热溶解、真空抽滤、溶剂蒸馏回收三项加工以脱除中温沥青中的喹啉不溶物,从而制得电极浸渍沥青产品。其具体操作步骤为:The method for preparing electrode-impregnated asphalt of the present invention adopts medium-temperature asphalt as a raw material, and uses dephenolized phenolic oil as a solvent, and undergoes three processes of heating and dissolving, vacuum filtration, and solvent distillation recovery to remove quinoline insolubles in the medium-temperature asphalt, Thus, an electrode-impregnated pitch product is obtained. The specific operation steps are:
1、加热溶解:将中温沥青与脱酚酚油溶剂按1∶2~5混合后加热,保持溶解温度在70℃~110℃之间,并连续搅拌至中温沥青全部溶解于脱酚酚油溶剂中;然后采取小火加热,溶解10~30分钟后,停止加热;1. Heating and dissolving: Mix the medium-temperature asphalt and dephenolized phenolic oil solvent at a ratio of 1:2 to 5, then heat, keep the dissolving temperature between 70°C and 110°C, and continuously stir until the medium-temperature asphalt is completely dissolved in the dephenolized phenolic oily solvent Medium; then heat on low heat, dissolve for 10 to 30 minutes, then stop heating;
2、真空抽滤:将热混合溶液在室温下冷却到15~45℃后,缓慢倒入预先安装好的真空抽滤装置的漏斗中,边倒入边进行真空抽滤,抽滤后的滤液倒入铜壶中;2. Vacuum suction filtration: After cooling the hot mixed solution to 15-45°C at room temperature, slowly pour it into the funnel of the pre-installed vacuum suction filtration device, and carry out vacuum suction filtration while pouring, and the filtrate after suction filtration poured into a copper pot;
3、溶剂蒸馏回收:将铜壶中的滤液在减压的方式下进行蒸馏,蒸馏终温保持在160℃~230℃,馏出液为溶剂,可重复使用;蒸馏后壶底倒出的试样即为电极浸渍沥青。且电极浸渍沥青中喹啉不溶物重量小于0.1%。3. Solvent distillation recovery: distill the filtrate in the copper pot under reduced pressure, keep the final temperature of distillation at 160°C-230°C, and the distillate is a solvent, which can be reused; The sample is the electrode impregnated pitch. And the weight of the quinoline insoluble matter in the electrode impregnated asphalt is less than 0.1%.
本发明电极浸渍沥青的制取方法的有益效果是:The beneficial effect of the preparation method of electrode impregnated pitch of the present invention is:
一是收得率高,中温沥青处理后其电极浸渍沥青产率可达到80%以上;二是利用率高,使用过后的脱酚酚油溶剂可全部回收再次使用,过滤后所产生的滤饼可以作为重沥青处理;三是处理效率高,整个生产过程所需设备不多,工艺方法易于掌握和控制,工序少,效果好;四是综合效益可观,煤焦油沥青是煤焦油加工过程中分离出的大宗产品,约占煤焦油总量的50~60%,以年处理中温沥青5000吨、产率为80%计算,每年就可生产电极浸渍沥青4000吨,为煤焦油沥青的处理找出了一条行之有效的途径。First, the yield is high. After medium-temperature asphalt treatment, the yield of the electrode-impregnated asphalt can reach more than 80%. Second, the utilization rate is high. The used dephenolized phenolic oil solvent can be fully recovered and reused, and the filter cake produced after filtration It can be treated as heavy asphalt; third, the processing efficiency is high, the equipment required for the whole production process is not much, the process method is easy to master and control, there are few procedures, and the effect is good; fourth, the comprehensive benefits are considerable, coal tar pitch is separated from coal tar in the process of processing The bulk products produced account for about 50-60% of the total amount of coal tar. Based on the annual processing of 5,000 tons of medium-temperature pitch and a yield of 80%, 4,000 tons of electrode-impregnated pitch can be produced each year. an effective way.
具体实施方式Detailed ways
下面结合实施例对本发明作进一步说明。The present invention will be further described below in conjunction with embodiment.
本发明电极浸渍沥青的制取方法,选用中温沥青为原料,以脱酚酚油为溶剂,经过加热溶解、真空抽滤、溶剂蒸馏回收三项加工,从而制取喹啉不溶物重量小于0.1%的电极浸渍沥青产品。The method for preparing electrode-impregnated asphalt of the present invention uses medium-temperature asphalt as a raw material, uses dephenolized phenolic oil as a solvent, and undergoes three processes of heating and dissolving, vacuum filtration, and solvent distillation recovery, thereby producing quinoline insolubles with a weight less than 0.1% Electrode impregnated pitch products.
实施例1:Example 1:
将中温沥青与脱酚酚油溶剂按1∶2的比例混合,混合后将混合物进行加热,并且不间断搅拌,保持溶解温度在110℃,使中温沥青全部溶解于脱酚酚油溶剂中;然后采取小火加热,溶解10分钟后,停止加热。Mix the medium-temperature asphalt and the dephenolized phenolic oil solvent in a ratio of 1:2, heat the mixture after mixing, and stir continuously to keep the dissolution temperature at 110°C, so that all the medium-temperature asphalt is dissolved in the dephenolized phenolic oil solvent; then Take low heat to heat, after dissolving for 10 minutes, stop heating.
将热混合溶液在室温下冷却到15℃后,缓慢倒入预先安装好的真空抽滤装置的漏斗中,边倒入边进行真空抽滤,抽滤后的滤液倒入铜壶中。After cooling the hot mixed solution to 15°C at room temperature, slowly pour it into the funnel of the pre-installed vacuum filtration device, perform vacuum filtration while pouring, and pour the filtered filtrate into a copper pot.
将铜壶中的滤液在减压的方式下进行蒸馏,蒸馏终温为230℃。馏出液为脱酚酚油溶剂,回收以便重复使用。蒸馏后壶底倒出的试样即可获得喹啉不溶物重量小于0.1%电极浸渍沥青。The filtrate in the copper pot was distilled under reduced pressure, and the final distillation temperature was 230°C. The distillate is dephenolized phenol oil solvent, which is recovered for reuse. After distillation, the sample poured out from the bottom of the kettle can obtain quinoline insoluble matter with a weight less than 0.1% electrode impregnation pitch.
实施例2:Example 2:
将中温沥青与脱酚酚油溶剂按1∶5的比例混合,混合后将混合物进行加热,并且不间断搅拌,保持溶解温度在70℃,使中温沥青全部溶解于脱酚酚油溶剂中;然后采取小火加热,溶解30分钟后,停止加热。Mix the medium-temperature asphalt and the dephenolized phenolic oil solvent in a ratio of 1:5, heat the mixture after mixing, and stir continuously, keeping the dissolution temperature at 70°C, so that all the medium-temperature asphalt is dissolved in the dephenolized phenolic oil solvent; then Take low heat to heat, after dissolving for 30 minutes, stop heating.
将热混合溶液在室温下冷却到45℃后,缓慢倒入预先安装好的真空抽滤装置的漏斗中,边倒入边进行真空抽滤,抽滤后的滤液倒入铜壶中。After cooling the hot mixed solution to 45°C at room temperature, slowly pour it into the funnel of the pre-installed vacuum filtration device, perform vacuum filtration while pouring, and pour the filtered filtrate into a copper pot.
将铜壶中的滤液在减压的方式下进行蒸馏,蒸馏终温为160℃。馏出液为脱酚酚油溶剂,回收以便重复使用。蒸馏后壶底倒出的试样即可获得喹啉不溶物重量小于0.1%电极浸渍沥青。The filtrate in the copper pot was distilled under reduced pressure, and the final distillation temperature was 160°C. The distillate is dephenolized phenol oil solvent, which is recovered for reuse. After distillation, the sample poured out from the bottom of the kettle can obtain quinoline insoluble matter with a weight less than 0.1% electrode impregnation pitch.
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101445740A (en) * | 2009-01-04 | 2009-06-03 | 北京石油化工学院 | A preparation method of dipping agent pitch |
| CN101787298A (en) * | 2009-01-23 | 2010-07-28 | 北京石油化工学院 | Coal art pitch purification method |
| CN101880542A (en) * | 2010-06-24 | 2010-11-10 | 山西潞安环保能源开发股份有限公司 | A method for removing organic sulfur in coal tar pitch |
| CN104031669A (en) * | 2013-03-07 | 2014-09-10 | 神华集团有限责任公司 | Electrode pitch and preparation method thereof |
-
2007
- 2007-12-14 CN CN200710158909XA patent/CN101220284B/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101445740A (en) * | 2009-01-04 | 2009-06-03 | 北京石油化工学院 | A preparation method of dipping agent pitch |
| CN101787298A (en) * | 2009-01-23 | 2010-07-28 | 北京石油化工学院 | Coal art pitch purification method |
| CN101787298B (en) * | 2009-01-23 | 2014-05-28 | 北京石油化工学院 | Coal art pitch purification method |
| CN101880542A (en) * | 2010-06-24 | 2010-11-10 | 山西潞安环保能源开发股份有限公司 | A method for removing organic sulfur in coal tar pitch |
| CN101880542B (en) * | 2010-06-24 | 2013-01-23 | 山西潞安环保能源开发股份有限公司 | Method for removing organic sulfur in coal pitch |
| CN104031669A (en) * | 2013-03-07 | 2014-09-10 | 神华集团有限责任公司 | Electrode pitch and preparation method thereof |
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