CN1752188A - 一种燃料油的生产方法 - Google Patents
一种燃料油的生产方法 Download PDFInfo
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- CN1752188A CN1752188A CN 200510048454 CN200510048454A CN1752188A CN 1752188 A CN1752188 A CN 1752188A CN 200510048454 CN200510048454 CN 200510048454 CN 200510048454 A CN200510048454 A CN 200510048454A CN 1752188 A CN1752188 A CN 1752188A
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- hydrogenator
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- oil
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- 239000000295 fuel oil Substances 0.000 title claims abstract description 23
- 238000000034 method Methods 0.000 title description 43
- 238000006243 chemical reaction Methods 0.000 claims abstract description 38
- 239000003054 catalyst Substances 0.000 claims abstract description 34
- 229910017318 Mo—Ni Inorganic materials 0.000 claims abstract description 26
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 24
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims abstract description 18
- 238000004519 manufacturing process Methods 0.000 claims abstract description 17
- 239000003921 oil Substances 0.000 claims description 48
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 44
- 239000000446 fuel Substances 0.000 claims description 40
- 238000005984 hydrogenation reaction Methods 0.000 claims description 37
- 239000011280 coal tar Substances 0.000 claims description 30
- 239000001257 hydrogen Substances 0.000 claims description 30
- 229910052739 hydrogen Inorganic materials 0.000 claims description 30
- 239000007788 liquid Substances 0.000 claims description 29
- 238000007670 refining Methods 0.000 claims description 26
- 239000007789 gas Substances 0.000 claims description 25
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 21
- 239000005864 Sulphur Substances 0.000 claims description 21
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 18
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 15
- 150000002431 hydrogen Chemical class 0.000 claims description 13
- 239000011148 porous material Substances 0.000 claims description 12
- 239000012535 impurity Substances 0.000 claims description 10
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 claims description 9
- 229910021529 ammonia Inorganic materials 0.000 claims description 9
- 239000010763 heavy fuel oil Substances 0.000 claims description 9
- 229910000037 hydrogen sulfide Inorganic materials 0.000 claims description 9
- 150000004945 aromatic hydrocarbons Chemical class 0.000 claims description 5
- 238000001816 cooling Methods 0.000 claims description 4
- 238000005194 fractionation Methods 0.000 claims description 4
- 229920006395 saturated elastomer Polymers 0.000 claims description 4
- 238000005520 cutting process Methods 0.000 claims description 3
- 238000000926 separation method Methods 0.000 claims description 2
- 229910052717 sulfur Inorganic materials 0.000 abstract description 4
- 229910052593 corundum Inorganic materials 0.000 abstract 2
- 229910001845 yogo sapphire Inorganic materials 0.000 abstract 2
- 239000000047 product Substances 0.000 description 43
- 238000009833 condensation Methods 0.000 description 13
- 230000005494 condensation Effects 0.000 description 13
- 238000009835 boiling Methods 0.000 description 9
- 238000012360 testing method Methods 0.000 description 9
- 239000003245 coal Substances 0.000 description 7
- 238000002360 preparation method Methods 0.000 description 6
- 238000012545 processing Methods 0.000 description 6
- 239000002994 raw material Substances 0.000 description 6
- 239000003381 stabilizer Substances 0.000 description 6
- 239000003208 petroleum Substances 0.000 description 5
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 239000006227 byproduct Substances 0.000 description 3
- 239000012263 liquid product Substances 0.000 description 3
- 238000011017 operating method Methods 0.000 description 3
- 238000000197 pyrolysis Methods 0.000 description 3
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 2
- 206010067482 No adverse event Diseases 0.000 description 2
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 2
- 239000010426 asphalt Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000008157 edible vegetable oil Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000011049 filling Methods 0.000 description 2
- 239000003350 kerosene Substances 0.000 description 2
- 231100000252 nontoxic Toxicity 0.000 description 2
- 230000003000 nontoxic effect Effects 0.000 description 2
- 238000003672 processing method Methods 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- 239000011269 tar Substances 0.000 description 2
- 238000004073 vulcanization Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000002253 acid Substances 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 238000006136 alcoholysis reaction Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000007806 chemical reaction intermediate Substances 0.000 description 1
- 235000019219 chocolate Nutrition 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- -1 ignition dope Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000004449 solid propellant Substances 0.000 description 1
- 238000002560 therapeutic procedure Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Description
项目 | |
密度,20℃,kg/m3 | 1138.6 |
残炭,w% | 1.35 |
凝点,℃ | -1 |
粘度,40℃,mm2/s | 13.50 |
硫含量,μg/g | 6754 |
氮含量,μg/g | 8865 |
芳烃含量,w% | 72.5 |
馏程(D2887),℃ | |
IBP/10% | 115/239 |
50%/90% | 336/425 |
95%/FBP | 458/497 |
气味 | 刺激性臭味 |
外观 | 黑褐色 |
项目 | 4号轻燃料油 | 4号重燃料油 | 5号重燃料油 |
密度,20℃,kg/m3 | ≮872 | - | - |
闭口闪点,℃ | ≮38 | ≮55 | ≮55 |
凝点,℃ | ≯-6 | ≯-6 | - |
粘度,mm2/s | |||
40℃ | 1.9~5.5 | 5.5~24.0 | - |
100℃ | - | - | 9.0~14.9 |
灰分,w% | ≯0.05 | ≯0.10 | ≯0.15 |
项目 | 实施例1 | 实施例2 | 实施例3 | 实施例4 |
第一加氢反应器(R1)和第二加氢反应器(R2)的加氢工艺操作条件 | ||||
氢分压(R1/R2),MPa | 9.0/9.0 | 11.0/11.0 | 13.0/13.0 | 14.0/14.0 |
反应温度(R1/R2),℃ | 390/380 | 380/370 | 370/360 | 360/360 |
体积空速(R1/R2),h-1 | 0.7/0.5 | 0.9/0.7 | 1.0/0.8 | 0.8/0.6 |
氢油体积比(R1/R2) | 1000/1000 | 800/800 | 1200/1200 | 1000/1000 |
加氢改质后的液体产物的主要性质 | ||||
收率(对进料),w% | 98.5 | 99.1 | 98.8 | 98.2 |
密度,20℃,kg/m3 | 972.5 | 974.5 | 973.4 | 971.7 |
残炭,w% | 0.03 | 0.05 | 0.04 | 0.02 |
闭口闪点,℃ | 49 | 54 | 51 | 48 |
凝点,℃ | <-30 | <-30 | <-30 | <-30 |
粘度,40℃,mm2/s | 4.354 | 4.425 | 4.386 | 4.328 |
灰分,w% | 0.013 | 0.017 | 0.015 | 0.011 |
硫/氮含量,μg/g | 82/256 | 112/288 | 97/275 | 74/242 |
芳烃含量,w% | 32.8 | 33.5 | 33.1 | 32.6 |
馏程(D2887),℃ | ||||
IBP/10% | 89/216 | 98/224 | 93/219 | 87/214 |
50%/90% | 298/383 | 313/393 | 306/387 | 295/380 |
95%/FBP | 418/483 | 430/488 | 425/485 | 416/482 |
色度 | 7.5 | 7.5 | 7.5 | 7.5 |
气味 | 无异味 | 无异味 | 无异味 | 无异味 |
外观 | 橙红色 | 橙红色 | 橙红色 | 橙红色 |
项目 | 馏分 | ||
<320℃ | 320~360℃ | >360℃ | |
密度,20℃,kg/m3 | 948.8 | 1015.4 | 1064.5 |
闭口闪点,℃ | 40 | 152 | 211 |
凝点,℃ | <-30 | <-30 | 13 |
粘度,mm2/s | |||
40℃ | 2.157 | 14.25 | - |
100℃ | - | - | 12.28 |
灰分,w% | <0.001 | <0.001 | 0.042 |
色度 | 0.5 | 1.5 | >8.0 |
外观 | 浅黄色 | 橙色 | 红黑色 |
气味 | 无异味 | 无异味 | 无异味 |
Claims (2)
Priority Applications (1)
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CNB2005100484547A CN100348702C (zh) | 2005-10-28 | 2005-10-28 | 一种燃料油的生产方法 |
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CNB2005100484547A CN100348702C (zh) | 2005-10-28 | 2005-10-28 | 一种燃料油的生产方法 |
Publications (2)
Publication Number | Publication Date |
---|---|
CN1752188A true CN1752188A (zh) | 2006-03-29 |
CN100348702C CN100348702C (zh) | 2007-11-14 |
Family
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CNB2005100484547A Expired - Fee Related CN100348702C (zh) | 2005-10-28 | 2005-10-28 | 一种燃料油的生产方法 |
Country Status (1)
Country | Link |
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CN (1) | CN100348702C (zh) |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100532509C (zh) * | 2006-08-03 | 2009-08-26 | 湖南长岭石化科技开发有限公司 | 一种煤焦油加氢改质生产燃料油的方法 |
CN101760238A (zh) * | 2008-10-16 | 2010-06-30 | 何巨堂 | 一种不同沸程煤焦油馏份的联合加氢转化方法 |
CN101250433B (zh) * | 2008-03-28 | 2012-02-15 | 湖南长岭石化科技开发有限公司 | 一种煤焦油加氢工艺 |
CN102477310A (zh) * | 2010-11-25 | 2012-05-30 | 邵素英 | 一种煤焦油制燃料油的方法 |
CN102476055A (zh) * | 2010-11-25 | 2012-05-30 | 邵素英 | 一种煤焦油制燃料油催化剂及生产工艺 |
CN101724461B (zh) * | 2009-12-07 | 2012-10-03 | 中国科学院山西煤炭化学研究所 | 一种多产轻质清洁燃料油的煤焦油催化加氢处理方法 |
CN103122260A (zh) * | 2013-01-29 | 2013-05-29 | 沈阳三聚凯特催化剂有限公司 | 重质苯与洗油混合物的加氢精制工艺 |
CN101633851B (zh) * | 2008-10-14 | 2014-01-01 | 何巨堂 | 一种不同沸程煤焦油馏份的联合加氢转化方法 |
CN104927914A (zh) * | 2014-03-23 | 2015-09-23 | 何巨堂 | 包含使用供氢烃的低氢油比预加氢过程的高芳烃加氢方法 |
CN106687565A (zh) * | 2014-09-16 | 2017-05-17 | 托普索公司 | 从高沸点芳香性碳质材料生产高品质柴油燃料和润滑剂 |
CN108300510A (zh) * | 2017-01-12 | 2018-07-20 | 中国石油化工股份有限公司 | 一种煤焦油加氢生产燃料油的方法 |
CN113528184A (zh) * | 2020-04-20 | 2021-10-22 | 广元市天森煤化有限公司 | 一种煤焦油制燃料油的方法 |
CN113583756A (zh) * | 2021-08-13 | 2021-11-02 | 北京化工大学 | 一种中低阶煤温和加氢液化制备化学品和燃料油的方法 |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5650991A (en) * | 1979-10-03 | 1981-05-08 | Shoichi Yoshikawa | Production of fuel oil from coal and coal-like material |
JPS6254791A (ja) * | 1985-09-04 | 1987-03-10 | Sumitomo Metal Ind Ltd | コ−ルタ−ルの処理方法 |
JPH04122789A (ja) * | 1990-09-14 | 1992-04-23 | Osaka Gas Co Ltd | 重質油の接触水素化分解方法 |
CN1082083C (zh) * | 1999-07-22 | 2002-04-03 | 中国石油化工集团公司 | 一种溶剂油的生产方法 |
CN1670127A (zh) * | 2004-03-19 | 2005-09-21 | 张宪 | 一种煤焦油加氢转化方法及其催化剂 |
CN1276059C (zh) * | 2004-07-30 | 2006-09-20 | 山西东辉煤焦化集团有限公司 | 从煤焦油生产化工品及燃料油的方法 |
CN1311058C (zh) * | 2005-03-09 | 2007-04-18 | 内蒙古远兴天然碱股份有限公司 | 煤焦油制燃料油的工艺 |
-
2005
- 2005-10-28 CN CNB2005100484547A patent/CN100348702C/zh not_active Expired - Fee Related
Cited By (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100532509C (zh) * | 2006-08-03 | 2009-08-26 | 湖南长岭石化科技开发有限公司 | 一种煤焦油加氢改质生产燃料油的方法 |
CN101250433B (zh) * | 2008-03-28 | 2012-02-15 | 湖南长岭石化科技开发有限公司 | 一种煤焦油加氢工艺 |
CN101633851B (zh) * | 2008-10-14 | 2014-01-01 | 何巨堂 | 一种不同沸程煤焦油馏份的联合加氢转化方法 |
CN101760238B (zh) * | 2008-10-16 | 2013-12-04 | 何巨堂 | 一种不同沸程煤焦油馏份的联合加氢转化方法 |
CN101760238A (zh) * | 2008-10-16 | 2010-06-30 | 何巨堂 | 一种不同沸程煤焦油馏份的联合加氢转化方法 |
CN101724461B (zh) * | 2009-12-07 | 2012-10-03 | 中国科学院山西煤炭化学研究所 | 一种多产轻质清洁燃料油的煤焦油催化加氢处理方法 |
CN102477310B (zh) * | 2010-11-25 | 2014-06-18 | 邵素英 | 一种煤焦油制燃料油的方法 |
CN102476055B (zh) * | 2010-11-25 | 2013-10-09 | 邵素英 | 一种煤焦油制燃料油催化剂及生产工艺 |
CN102476055A (zh) * | 2010-11-25 | 2012-05-30 | 邵素英 | 一种煤焦油制燃料油催化剂及生产工艺 |
CN102477310A (zh) * | 2010-11-25 | 2012-05-30 | 邵素英 | 一种煤焦油制燃料油的方法 |
CN103122260A (zh) * | 2013-01-29 | 2013-05-29 | 沈阳三聚凯特催化剂有限公司 | 重质苯与洗油混合物的加氢精制工艺 |
CN103122260B (zh) * | 2013-01-29 | 2015-06-03 | 沈阳三聚凯特催化剂有限公司 | 重质苯与洗油混合物的加氢精制工艺 |
CN104927914A (zh) * | 2014-03-23 | 2015-09-23 | 何巨堂 | 包含使用供氢烃的低氢油比预加氢过程的高芳烃加氢方法 |
CN106687565A (zh) * | 2014-09-16 | 2017-05-17 | 托普索公司 | 从高沸点芳香性碳质材料生产高品质柴油燃料和润滑剂 |
CN106687565B (zh) * | 2014-09-16 | 2020-07-03 | 托普索公司 | 从高沸点芳香性碳质材料生产高品质柴油燃料和润滑剂 |
CN108300510A (zh) * | 2017-01-12 | 2018-07-20 | 中国石油化工股份有限公司 | 一种煤焦油加氢生产燃料油的方法 |
CN108300510B (zh) * | 2017-01-12 | 2020-09-22 | 中国石油化工股份有限公司 | 一种煤焦油加氢生产燃料油的方法 |
CN113528184A (zh) * | 2020-04-20 | 2021-10-22 | 广元市天森煤化有限公司 | 一种煤焦油制燃料油的方法 |
CN113583756A (zh) * | 2021-08-13 | 2021-11-02 | 北京化工大学 | 一种中低阶煤温和加氢液化制备化学品和燃料油的方法 |
CN113583756B (zh) * | 2021-08-13 | 2024-02-06 | 北京化工大学 | 一种中低阶煤温和加氢液化制备化学品和燃料油的方法 |
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Address after: 100029 Beijing City, Chaoyang District Hui Street No. 6 Co-patentee after: Luoyang Petrochemical Engineering Corporation /SINOPEC Patentee after: China Petrochemical Group Corp. Address before: 100029 Beijing City, Chaoyang District Hui Street No. 6 Co-patentee before: Luoyang Petrochemical Engineering Co., China Petrochemical Group Patentee before: China Petrochemical Group Corp. |
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