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China Plastics ›› 2021, Vol. 35 ›› Issue (8): 64-76.DOI: 10.19491/j.issn.1001-9278.2021.08.009
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LI Mingfeng1(), CAI Zhiqiang2, ZOU Liang1, WEI Xiaoli1, XI Yuanbing1, WANG Guoqing3, CAI Lile1, ZHANG Zhemin1, XIA Guofu1, JIANG Haibin3
Received:
2021-04-07
Online:
2021-08-26
Published:
2021-08-27
CLC Number:
LI Mingfeng, CAI Zhiqiang, ZOU Liang, WEI Xiaoli, XI Yuanbing, WANG Guoqing, CAI Lile, ZHANG Zhemin, XIA Guofu, JIANG Haibin. Exploration on Chemical Recovery Technology of Plastic Wastes in Sinopec[J]. China Plastics, 2021, 35(8): 64-76.
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URL: https://www.plaschina.com.cn/EN/10.19491/j.issn.1001-9278.2021.08.009
来源 | 位置 | 主体种类 | Cl含量/μg·g-1 |
---|---|---|---|
矿泉水瓶 | 瓶体 | PET | 247 |
瓶贴标签 | PP | 2 738 | |
塑料购物袋 | 白色部分 | PE | 194 |
标签部分 | PE | 2 195 | |
编织袋 | 无字部分 | PP | 397 |
黑色快递 包装袋 | 黑色主体 | PE | 392 |
黑色主体+胶带 | PE、PP | 554 | |
黑色主体+快递单 | PE、纸 | 1 088 | |
软质热塑膜 | 主体部分 | PVC | 38 % |
来源 | 位置 | 主体种类 | Cl含量/μg·g-1 |
---|---|---|---|
矿泉水瓶 | 瓶体 | PET | 247 |
瓶贴标签 | PP | 2 738 | |
塑料购物袋 | 白色部分 | PE | 194 |
标签部分 | PE | 2 195 | |
编织袋 | 无字部分 | PP | 397 |
黑色快递 包装袋 | 黑色主体 | PE | 392 |
黑色主体+胶带 | PE、PP | 554 | |
黑色主体+快递单 | PE、纸 | 1 088 | |
软质热塑膜 | 主体部分 | PVC | 38 % |
项目 | 数值 |
---|---|
20 ℃密度/kg·m-3 | 837 |
C/% | 86.3 |
H/% | 13.7 |
馏程/% | 数值 |
汽油馏分段(IBP~180 ℃) | 20.8 |
柴油馏分段(180~350 ℃) | 69.2 |
馏分油段(350~500 ℃) | 8.5 |
重油馏分段(>500 ℃) | 1.5 |
杂质含量/μg·g-1 | 数值 |
Cl | 8.7 |
Si | <1 |
项目 | 数值 |
---|---|
20 ℃密度/kg·m-3 | 837 |
C/% | 86.3 |
H/% | 13.7 |
馏程/% | 数值 |
汽油馏分段(IBP~180 ℃) | 20.8 |
柴油馏分段(180~350 ℃) | 69.2 |
馏分油段(350~500 ℃) | 8.5 |
重油馏分段(>500 ℃) | 1.5 |
杂质含量/μg·g-1 | 数值 |
Cl | 8.7 |
Si | <1 |
项目 | 废旧塑料热解油A柴油馏分 | 柴油馏分加氢产品 |
---|---|---|
质量收率/% | 60.1 | - |
密度(20 ℃)/ kg·m-3 | 811.9 | 797.2 |
馏程/℃ | 180~346 | 173~345 |
S/μg·g-1 | 356 | 7.1 |
Si/μg·g-1 | 1078 | <1 |
Cl/μg·g-1 | 25 | <0.5 |
质量族组成/% | 废旧塑料热解油A柴油馏分 | 柴油馏分加氢产品 |
链烷烃 | 36.1 | 68.6 |
总环烷烃/总烯烃 | 47.7 | 24.9 |
总芳烃 | 16.2 | 6.5 |
多环芳烃 | 4.5 | 0.6 |
合计 | 100 | 100 |
十六烷值 | 50.3 | 61.2 |
项目 | 废旧塑料热解油A柴油馏分 | 柴油馏分加氢产品 |
---|---|---|
质量收率/% | 60.1 | - |
密度(20 ℃)/ kg·m-3 | 811.9 | 797.2 |
馏程/℃ | 180~346 | 173~345 |
S/μg·g-1 | 356 | 7.1 |
Si/μg·g-1 | 1078 | <1 |
Cl/μg·g-1 | 25 | <0.5 |
质量族组成/% | 废旧塑料热解油A柴油馏分 | 柴油馏分加氢产品 |
链烷烃 | 36.1 | 68.6 |
总环烷烃/总烯烃 | 47.7 | 24.9 |
总芳烃 | 16.2 | 6.5 |
多环芳烃 | 4.5 | 0.6 |
合计 | 100 | 100 |
十六烷值 | 50.3 | 61.2 |
项目 | 数值 |
---|---|
密度(20 ℃)/ kg·m-3 | 800.3 |
折光(20 ℃) | 1.45 |
溴价/g·(Br100 mL)-1 | 43.5 |
碳含量/% | 86.1 |
氢含量/% | 13.9 |
氮含量/μg·g-1 | 154 |
硫含量/μg·g-1 | 363 |
硅含量/μg·g-1 | 730 |
氯含量/μg·g-1 | 96 |
馏程/℃ | 数值 |
汽油馏分 (初馏点~200 ℃) | 27.9 |
柴油馏分 (200~350 ℃) | 52.2 |
蜡油馏分 (350~500℃) | 19.9 |
烃质量组成/% | 数值 |
链烷烃 | 36.5 |
环烷烃+烯烃 | 50.4 |
芳烃 | 13.1 |
项目 | 数值 |
---|---|
密度(20 ℃)/ kg·m-3 | 800.3 |
折光(20 ℃) | 1.45 |
溴价/g·(Br100 mL)-1 | 43.5 |
碳含量/% | 86.1 |
氢含量/% | 13.9 |
氮含量/μg·g-1 | 154 |
硫含量/μg·g-1 | 363 |
硅含量/μg·g-1 | 730 |
氯含量/μg·g-1 | 96 |
馏程/℃ | 数值 |
汽油馏分 (初馏点~200 ℃) | 27.9 |
柴油馏分 (200~350 ℃) | 52.2 |
蜡油馏分 (350~500℃) | 19.9 |
烃质量组成/% | 数值 |
链烷烃 | 36.5 |
环烷烃+烯烃 | 50.4 |
芳烃 | 13.1 |
产物产率 | 汽油 | 汽油和低碳烯烃 |
---|---|---|
裂化气 | 25.9 | 50.0 |
其中乙烯 | 0.7 | 3.90 |
其中丙烯 | 8.7 | 15.5 |
汽油 | 50.2 | 30.5 |
汽油烃质量组成 | 汽油 | 汽油和低碳烯烃 |
饱和烃 | 43.0 | 21.4 |
烯烃 | 19.9 | 10.8 |
其中二烯烃 | 0.1 | 0.3 |
芳烃 | 37.2 | 67.8 |
产物产率 | 汽油 | 汽油和低碳烯烃 |
---|---|---|
裂化气 | 25.9 | 50.0 |
其中乙烯 | 0.7 | 3.90 |
其中丙烯 | 8.7 | 15.5 |
汽油 | 50.2 | 30.5 |
汽油烃质量组成 | 汽油 | 汽油和低碳烯烃 |
饱和烃 | 43.0 | 21.4 |
烯烃 | 19.9 | 10.8 |
其中二烯烃 | 0.1 | 0.3 |
芳烃 | 37.2 | 67.8 |
项目 | 废旧塑料热解油D | 废旧塑料热解油D加氢产品 |
---|---|---|
密度(20 ℃)/kg·m-3 | 830.9 | 826.0 |
馏程/℃ | 153~516 | 94~556 |
S/μg·g-1 | 336 | 111 |
N/μg·g-1 | 629 | 207 |
Si/μg·g-1 | 46 | <1 |
Cl/μg·g-1 | 84 | <0.5 |
金属含量/μg·g-1 | 废旧塑料热解油D | 废旧塑料热解油D加氢产品 |
Fe | 1.1 | <1 |
Ca | 1.1 | <1 |
质量组成 | 废旧塑料热解油D | 废旧塑料热解油D加氢产品 |
链烷烃% | 25.4 | 59.8 |
总环烷烃或烯烃% | 52.3 | 20.9 |
总芳烃% | 22.3 | 19.3 |
项目 | 废旧塑料热解油D | 废旧塑料热解油D加氢产品 |
---|---|---|
密度(20 ℃)/kg·m-3 | 830.9 | 826.0 |
馏程/℃ | 153~516 | 94~556 |
S/μg·g-1 | 336 | 111 |
N/μg·g-1 | 629 | 207 |
Si/μg·g-1 | 46 | <1 |
Cl/μg·g-1 | 84 | <0.5 |
金属含量/μg·g-1 | 废旧塑料热解油D | 废旧塑料热解油D加氢产品 |
Fe | 1.1 | <1 |
Ca | 1.1 | <1 |
质量组成 | 废旧塑料热解油D | 废旧塑料热解油D加氢产品 |
链烷烃% | 25.4 | 59.8 |
总环烷烃或烯烃% | 52.3 | 20.9 |
总芳烃% | 22.3 | 19.3 |
项目 | WP | WP IBP~180 ℃ | WP 180~350 ℃ | WH1 | WH2 |
---|---|---|---|---|---|
合计 | — | 100.0 | — | 100.0 | 100.0 |
20 ℃密度/g·cm-3 | 0.769 | 0.760 | 0.826 | 0.786 | 0.808 |
S/μg·g-1 | 131 | 58 | 466 | — | — |
N/μg·g-1 | 95 | 66 | 265 | — | — |
Si/μg·g-1 | 773.7 | 779.0 | 786.4 | — | — |
Cl/μg·g-1 | 1315.8 | 1313.7 | 938.4 | — | — |
馏程/℃ | WP | WP IBP~180 ℃ | WP 180~350 ℃ | WH1 | WH2 |
IBP | 75 | 72 | 180 | 29 | 49 |
10 % | 98 | 93 | 193 | 64 | 126 |
30 % | 123 | 120 | 207 | 132 | 207 |
50 % | 137 | 135 | 237 | 156 | 282 |
70 % | 147 | 136 | 285 | 209 | 362 |
EBP | 274 | 201 | 436 | 536 | 562 |
烃类组成/% | WP | WP IBP~180 ℃ | WP 180~350 ℃ | WH1 | WH2 |
链烷烃 | — | 16.3 | — | 27.4 | 47.0 |
环烷烃 | — | 10.6 | — | 46.9 | 39.2 |
烯烃 | — | 38.6 | — | 0 | 0 |
芳烃 | — | 34..5 | — | 25.7 | 13.8 |
胶质 | — | 0 | — | 0 | 0 |
项目 | WP | WP IBP~180 ℃ | WP 180~350 ℃ | WH1 | WH2 |
---|---|---|---|---|---|
合计 | — | 100.0 | — | 100.0 | 100.0 |
20 ℃密度/g·cm-3 | 0.769 | 0.760 | 0.826 | 0.786 | 0.808 |
S/μg·g-1 | 131 | 58 | 466 | — | — |
N/μg·g-1 | 95 | 66 | 265 | — | — |
Si/μg·g-1 | 773.7 | 779.0 | 786.4 | — | — |
Cl/μg·g-1 | 1315.8 | 1313.7 | 938.4 | — | — |
馏程/℃ | WP | WP IBP~180 ℃ | WP 180~350 ℃ | WH1 | WH2 |
IBP | 75 | 72 | 180 | 29 | 49 |
10 % | 98 | 93 | 193 | 64 | 126 |
30 % | 123 | 120 | 207 | 132 | 207 |
50 % | 137 | 135 | 237 | 156 | 282 |
70 % | 147 | 136 | 285 | 209 | 362 |
EBP | 274 | 201 | 436 | 536 | 562 |
烃类组成/% | WP | WP IBP~180 ℃ | WP 180~350 ℃ | WH1 | WH2 |
链烷烃 | — | 16.3 | — | 27.4 | 47.0 |
环烷烃 | — | 10.6 | — | 46.9 | 39.2 |
烯烃 | — | 38.6 | — | 0 | 0 |
芳烃 | — | 34..5 | — | 25.7 | 13.8 |
胶质 | — | 0 | — | 0 | 0 |
装置 | 预加氢 | 催化裂化 | 催化汽油加氢 | 柴油加氢 | 热解 | 油品燃烧 | 燃料气燃烧 |
---|---|---|---|---|---|---|---|
装置小计/t CO2 | 21 033.67 | 22 363.88 | 1 064.84 | 2 441.90 | 15 000 | 212 337.2 | 7 444.3 |
总计/t CO2 | 281 685.70 | ||||||
单位碳排放/t CO2·(t废旧塑料)-1 | 2.82 |
装置 | 预加氢 | 催化裂化 | 催化汽油加氢 | 柴油加氢 | 热解 | 油品燃烧 | 燃料气燃烧 |
---|---|---|---|---|---|---|---|
装置小计/t CO2 | 21 033.67 | 22 363.88 | 1 064.84 | 2 441.90 | 15 000 | 212 337.2 | 7 444.3 |
总计/t CO2 | 281 685.70 | ||||||
单位碳排放/t CO2·(t废旧塑料)-1 | 2.82 |
装置 | 预加氢 | SC?N | SC?D | SC?H | 汽油加氢 | PP | PE | 热解 | 油品燃烧 |
---|---|---|---|---|---|---|---|---|---|
装置小计/t CO2 | 15 185.00 | 9 360.48 | 34 918.66 | 16 786.53 | 444.73 | 5 154 | 21 068.5 | 15 000 | 119 006.1 |
总计/t CO2 | 237815.1 | ||||||||
单位碳排放/t CO2·(t废旧塑料)-1 | 2.4 |
装置 | 预加氢 | SC?N | SC?D | SC?H | 汽油加氢 | PP | PE | 热解 | 油品燃烧 |
---|---|---|---|---|---|---|---|---|---|
装置小计/t CO2 | 15 185.00 | 9 360.48 | 34 918.66 | 16 786.53 | 444.73 | 5 154 | 21 068.5 | 15 000 | 119 006.1 |
总计/t CO2 | 237815.1 | ||||||||
单位碳排放/t CO2·(t废旧塑料)-1 | 2.4 |
装置 | 加氢精制 | DCC | 加氢抽提 | 柴油加氢 | 气体分离 | PP | 热解 | 燃烧 |
---|---|---|---|---|---|---|---|---|
装置小计/t CO2 | 21 033.6 | 32 281.5 | 2 871.6 | 2 276.9 | 3 844.4 | 5 856.4 | 15 000 | 169 064.6 |
总计/t CO2 | 252 228.9 | |||||||
单位碳排放/CO2·(t废旧塑料)-1 | 2.5 |
装置 | 加氢精制 | DCC | 加氢抽提 | 柴油加氢 | 气体分离 | PP | 热解 | 燃烧 |
---|---|---|---|---|---|---|---|---|
装置小计/t CO2 | 21 033.6 | 32 281.5 | 2 871.6 | 2 276.9 | 3 844.4 | 5 856.4 | 15 000 | 169 064.6 |
总计/t CO2 | 252 228.9 | |||||||
单位碳排放/CO2·(t废旧塑料)-1 | 2.5 |
物料 | 原油 | 氢气 | 汽油 | 航煤 | 柴油 | 苯 |
---|---|---|---|---|---|---|
合计 | 10 103 | |||||
产量/kt | -10 000 | -103 | 2 406 | 1 446 | 2 937 | 215 |
物料 | 二甲苯 | 聚乙烯 | 聚丙烯 | 异丁烯 | 丙烷 | 抽余油 |
产量/kt | 342 | 379 | 419 | 202 | 86 | 246 |
物料 | C4/C5 | 干气 | 烧焦 | 油浆 | ||
产量/kt | 291 | 704 | 249 | 155 |
物料 | 原油 | 氢气 | 汽油 | 航煤 | 柴油 | 苯 |
---|---|---|---|---|---|---|
合计 | 10 103 | |||||
产量/kt | -10 000 | -103 | 2 406 | 1 446 | 2 937 | 215 |
物料 | 二甲苯 | 聚乙烯 | 聚丙烯 | 异丁烯 | 丙烷 | 抽余油 |
产量/kt | 342 | 379 | 419 | 202 | 86 | 246 |
物料 | C4/C5 | 干气 | 烧焦 | 油浆 | ||
产量/kt | 291 | 704 | 249 | 155 |
装置 | 开采 | 常减压 | 预加氢与重整 | 渣油加氢 | 航煤加氢 | 柴油加氢 | 加氢裂化 | 液化气脱硫 | ||||
---|---|---|---|---|---|---|---|---|---|---|---|---|
加工量/kt | 10 000 | 10 000 | 2 017 | 3 184 | 957 | 2856 | 2 295 | 676 | ||||
碳排放/kt | 3320 | 390 | 439 | 629 | 16 | 399 | 562 | 704 | ||||
装置 | 气体分离 | 催化裂化 | 汽油加氢 | 蒸汽裂解 | PE | PP | 油品燃烧 6 969 22 171 | |||||
加工量/kt | 664 | 2 832 | 1 432 | 1 182 | 388 | 406 | ||||||
碳排放/kt | 99 | 743 | 54 | 1 051 | 330 | 159 |
装置 | 开采 | 常减压 | 预加氢与重整 | 渣油加氢 | 航煤加氢 | 柴油加氢 | 加氢裂化 | 液化气脱硫 | ||||
---|---|---|---|---|---|---|---|---|---|---|---|---|
加工量/kt | 10 000 | 10 000 | 2 017 | 3 184 | 957 | 2856 | 2 295 | 676 | ||||
碳排放/kt | 3320 | 390 | 439 | 629 | 16 | 399 | 562 | 704 | ||||
装置 | 气体分离 | 催化裂化 | 汽油加氢 | 蒸汽裂解 | PE | PP | 油品燃烧 6 969 22 171 | |||||
加工量/kt | 664 | 2 832 | 1 432 | 1 182 | 388 | 406 | ||||||
碳排放/kt | 99 | 743 | 54 | 1 051 | 330 | 159 |
1 | JAMBECK J R, GEYER R, WILCOX C, et al. Plastic Waste Inputs from Land into the Ocean [J]. Science, 2015, 347(6223): 768⁃771. |
2 | GEYER R, JAMBECK J R, LAW K L. Production, Use, and Fate of all Plastics Ever Made [J]. Science Advances, 2017, 3(7): e1700782. |
3 | AMOBONYE A, BHAGWAT P K, SINGH S, et al. Plastic Biodegradation: Frontline Microbes and Their Enzymes [J]. Science of the Total Environment, 2021, 759: 143536. |
4 | GEWERT B, PLASSMANN M M, MACLEOD M. Pathways for Degradation of Plastic Polymers Floating in the Marine Environment [J]. Environmental Science Processes & Impacts, 2015, 17(9): 1 513⁃1 521. |
5 | DANSO D, CHOW J, STREIT W R. Plastics: Environmental and Biotechnological Perspectives on Microbial Degradation [J]. Applied and Environmental Microbiology, 2019, 85(19): e01095⁃19. |
6 | FOUNDATION M A. Growth within: A Circular Economy Vision for a Competitive Europe [J]. Sb Business Weekly, 2017: 18. |
7 | AL⁃SALEM S M, LETTIERI P, BAEYENS J. Recycling and Recovery Routes of Plastic Solid Waste (PSW): A Review [J]. Waste Management, 2009, 29(10): 2 625⁃2 643. |
8 | VELDEN M V D, BAEYENS J, BOUKIS L. Modeling CFB Biomass Pyrolysis Reactors [J]. Biomass & Bioenergy, 2008, 32(2): 128⁃139. |
9 | A. G, BUEKENS. Resource Recovery and Waste Treatment in Japan [J]. Resource Recovery & Conservation, 1978, 3(3): 275⁃306. |
10 | MICHAELI W, LACKNER V. Degradative Extrusion as a Pretreating Process for Chemical Recycling of Plastics Waste [J]. Die Angewandte Makromolekulare Chemie, 1995, 232(1): 167⁃185. |
11 | ZIA K M, BHATTI H N, BHATTI I A. Methods for Polyurethane and Polyurethane Composites, Recycling and Recovery: A Review [J]. Reactive and Functional Polymers, 2007, 67(8): 675⁃692. |
12 | HUANG J, HUANG K, QI W, et al. Process Analysis of Depolymerization Polybutylene Terephthalate in Supercritical Methanol [J]. Polymer Degradation & Stability, 2006, 91(10): 2 527⁃2 531. |
13 | SHUKLA S R, HARAD A M. Aminolysis of Polyethylene Terephthalate Waste [J]. Polymer Degradation & Stability, 2006, 91(8): 1 850⁃1 854. |
14 | SHUKLA S R, HARAD A M, JAWALE L S. Chemical Recycling of PET Waste into Hydrophobic Textile Dyestuffs [J]. Polymer Degradation & Stability, 2009, 94(4): 604⁃609. |
15 | ONWUDILI J A, INSURA N, WILLIAMS P T. Composition of Products from the Pyrolysis of Polyethylene and Polystyrene in a Closed Batch Reactor: Effects of Temperature and Residence Time [J]. Journal of Analytical and Applied Pyrolysis, 2009, 86(2): 293⁃303. |
16 | 陈俊武,许友好. 催化裂化工艺与工程 [M]. 北京: 中国石化出版社, 2015: 38. |
17 | SAMIR S, KOUTRA E, KORNAROS M, et al. Degradation of Conventional Plastic Wastes in the Environment: A Review on Current Status of Knowledge and Future Perspectives of Disposal [J]. Science of the Total Environment, 2021, 771: 144719. |
18 | RINALDINI C A, MATTARELLI E, SAVIOLI T, et al. Performance, Emission and Combustion Characteristics of a IDI Engine Running on Waste Plastic Oil [J]. Fuel, 2016, 183: 292⁃303. |
19 | 王松汉. 乙烯装置技术与运行 [M]. 北京: 中国石化出版社, 2009:162. |
20 | JUNG S H, CHO M H, KANG B S, et al. Pyrolysis of a Fraction of Waste Polypropylene and Polyethylene for the Recovery of BTX Aromatics Using a Fluidized Bed Reactor [J]. Fuel Processing Technology, 2010, 91(3): 277⁃284. |
21 | LIU Y, QIAN J, WANG J. Pyrolysis of Polystyrene Waste in a Fluidized⁃bed Reactor to Obtain Styrene Monomer and Gasoline Fraction [J]. Fuel Processing Technology, 2000, 63(1): 45⁃55. |
22 | ZHANG Y G, NAN X Q, SHI Y, et al. Study on Steam Cracking of Naphtha with Trace Chlorides [J]. Petrochemical Technology, 2018, 047(7): 671⁃675. |
23 | WU M, JIANG G Q, JIA F R, et al. Carbon Emissions from the Petroleum Industry Based on the Analysis of Material Flow and Life Cycle [J]. Resources Science, 2018, 040(6): 1 287⁃1 296. |
24 | LAN J J, CHEN H P, ZHONG Y J, et al. Benchmarking Analysis Based on the Standard Supply Coal Consumption Rate of Thermal Power Enterprises [J]. Energy Conservation, 2012, 31(10): 34⁃36. |
[1] | ZHOU Yingxin, WENG Yunxuan, ZHANG Caili, DIAO Xiaoqian, SONG Xinyu. Review of Recovery Technology and Standard Status of Poly(ethylene terephthalate) [J]. China Plastics, 2021, 35(8): 162-171. |
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