纺织学报 ›› 2023, Vol. 44 ›› Issue (12): 216-224.doi: 10.13475/j.fzxb.20230402602

• 综合述评 • 上一篇    下一篇

废弃纤维素纺织品水热降解技术的研究进展

张永芳(), 费鹏飞, 阎智锋, 王淑花, 郭红   

  1. 太原理工大学 轻纺工程学院, 山西 太原 030024
  • 收稿日期:2023-04-18 修回日期:2023-08-02 出版日期:2023-12-15 发布日期:2024-01-22
  • 作者简介:张永芳(1970—),女,讲师,博士。主要研究方向为废弃纺织品再资源化。E-mail:zyfzyflyf@163.com
  • 基金资助:
    国家自然科学基金项目(21802101);山西省自然科学基金项目(20210302124492)

Research progress of hydrothermal degradation of waste cellulose textiles

ZHANG Yongfang(), FEI Pengfei, YAN Zhifeng, WANG Shuhua, GUO Hong   

  1. College of Textile Engineering, Taiyuan University of Technology, Taiyuan, Shanxi 030024, China
  • Received:2023-04-18 Revised:2023-08-02 Published:2023-12-15 Online:2024-01-22

摘要:

为提高废弃纤维素纺织品的循环利用率,解决其引起的严重污染及浪费问题,介绍了水热降解法循环利用废弃纤维素纺织品的新途径。纤维素水热降解技术是一种利用亚(超)临界水进行热化学转化的新技术,综述了废弃纤维素纺织品水热降解技术的研究现状,分析了纤维素纤维亚(超)临界水热降解的机制、反应历程及产物种类,归纳了纤维素水热降解过程及降解产物的影响因素,对纤维素水热降解技术存在的问题及研究方向进行了总结与展望。分析认为:利用亚(超)临界水体系中水既是溶剂又是反应物和催化剂的特性,可以对纤维素类纺织品进行有效降解及分离回收,通过水解糖化、水热炭化等反应历程,得到水溶糖、水热炭、生物原油等多种水热产品;温度、时间、催化剂及纤维素结构对纤维素纤维水热降解有重要影响;目前该技术还存在部分反应机制不明确及目标产品产率较低等问题。基于这些问题对今后该领域的主要研究方向提出了建议。该技术绿色环保、成本低、产物可控、产品附加值高,具有很好的开发前景。

关键词: 废弃纤维素纺织品, 循环再利用, 水热降解, 降解机制, 亚(超)临界水热体系

Abstract:

Significance Large amount of waste textiles are heaped up, landfilled or incinerated as solid waste year by year, leading to heavy pollution of the environment and waste of the resources. In the face of the worsening energy crisis and environment troubles, the recycling of waste textiles has become a pressing social problem to be tackled. Various ways have been used physically or chemically in the study of the recycling of waste textiles. Among others, hydrothermal degradation is a highly noticeable thermochemical conversion technology featuring environmental friendliness, productive richness, and economy, which can effectively degrade and recycle cellulose textiles, and obtain high value-added hydrothermal products. The green and high-valued recycling of waste textiles are of great economic and social importance for the development of circular economy and reduction of pollution and carbon emission.
Progress New technologies are introduced for hydrothermal degradation of waste cellulose textiles in subcritical (supercritical) environments. With the special properties of subcritical (supercritical) water, cellulose fibers can be degraded hydrothermally into high value-added chemical products such as water-soluble sugar, hydrothermal carbon, and bio-oil. After step-by-step separation, the hydrothermal products can be effectively recovered without pollutant emission. The strong hydrogen bond and stable structure of high crystallinity of cellulose makes it hard to degrade at room temperature, which is the biggest problem in natural cellulose utilization. This paper analyzed the mechanism and reaction process of cellulose fiber hydrothermal degradation, summarized different processes of the hydrothermal degradation and corresponding target products, and concluded the influencing factors of the process and products. In the subcritical (supercritical) water system, acting as a reactant, a catalyst and an organic solvent concurrently, water can effectively break the hydrogen bond and crystal structure, and promote the break of glycosidic bond of cellulose. Under certain hydrothermal conditions, cellulose materials are degraded into substances such as glucose, fructose, 5-HMF (5-hydroxymethylfurfural), and organic acids. The soluble oligomers obtained through hydrolysis will form various carbon containing materials, bio-oils, and a small amount of gases after dehydration, polymerization, condensation, and aromatization. The hydrothermal degradation can be divided into processes of hydrolytic saccharification, hydrothermal carbonization, hydrothermal liquefaction and hydrothermal gasification, with respective products of water-soluble sugar, hydrothermal carbon, bio-oil and gas products. Temperature, time, catalyst, and cellulose structure are important factors affecting the hydrothermal degradation process and degradation products of cellulose. Different reaction conditions result in different degradation rates, products, yields, and properties of the hydrothermal degradation. By adjusting the temperature, catalyst and other parameters, the hydrolysis process can be regulated and the selectivity of target products can be adjusted to achieve different target products.
Conclusion and Prospect Hydrothermal treatment of cellulose fibers can yield high value-added chemical products such as glucose, 5-HMF, lactic acid, and carbon microspheres, while selective degradation of cellulose fibers can achieve effective separation and recycling of cellulose based blended fabrics, demonstrating that hydrothermal degradation technology of cellulose fibers is an effective way for high-valued recycling of waste textiles. However, researches in the area are still in the phase of laboratory exploration, at certain distance from large-scale production, due to the complex process relating to cellulose hydrothermal degradation. Still, the complexity of the hydrothermal degradation process and uncertainty of the decomposition mechanism and pathway of intermediate products, and the catalytic mechanism and regulatory mechanism of catalysts led to low yield of target products. Consequently, additional research should be conducted on the existing issues. With the evolution of the research, the industrial application of hydrothermal degradation technology in waste textiles treatment in the future will achieve significant social and economic benefits.

Key words: waste cellulose textile, recycling, hydrothermal degradation, degradation mechanism, subcritical (supercritical) hydrothermal system

中图分类号: 

  • TS102.9

表1

废弃纤维素织物再利用方法比较"

回收
方法
过程复
杂性
原料
体量

产品附
加值

综合
优势
机械法 较简单 一般
化学法 较复杂 较高 较高 一般
溶解法 较复杂
但成熟
较少 较大 较优
水热法 简单

图1

纤维素纤维水热降解反应历程"

[1] ASHJARAN A, AZARMI R. Survey on common bio fibers and polymers in recyclable textiles[J]. Journal of Chemical & Pharmaceutical Research, 2015, 7:202-208.
[2] SHEN F, XIAO W X, LIN L L, et al. Enzymatic saccharification coupling with polyester recovery from cottonebased waste textiles by phosphoric acid pretreatment[J]. Bioresource Technology, 2013, 130:248-255.
[3] WANG J, LI Y, WANG Z, et al. Influence of pretreatment on properties of cotton fiber in aqueous NaOH/urea solution[J]. Cellulose, 2016, 23(3):2173-2183.
[4] ASAADI S, HUMMEL M, HELLSTEN S, et al. Renewable high-performance fibers from the chemical recycling of cotton waste utilizing an ionic liquid[J]. Chemsuschem, 2016, 22(9):3250-3258.
[5] MUSSANA H, YANG X, TESSIMA M, et al. Preparation of lignocellulose aerogels from cotton stalks in the ionic liquid-based co-solvent system[J]. Industrial Crops and Products, 2018, 113: 225-233.
[6] HONG F, GUO X, ZHANG S, et al. Bacterial cellulose production from cotton-based waste textiles: enzymatic saccharification enhanced by ionic liquid pretreatment[J]. Bioresource Technology, 2012, 104: 503-508.
[7] SILVA R D, WANG X, BYRNE N. Recycling textiles: the use of ionic liquids in the separation of cotton polyester blends[J]. RSC Advances, 2014, 55(4):29094-29098.
[8] 陈亚宁, 陈昀. 稀盐酸水解棉纤维反应过程的综合研究[J]. 北京服装学院学报(自然科学版), 2010, 30(2): 24-28.
CHEN Yaning, CHEN Yun. Comprehensive study on the process of cotton fiber hydrolysis by dilute hydrochloric acid[J]. Journal of Beijing Institute of Fashion Technology(Natural Science Edition), 2010, 30(2):24-28.
[9] CHU C Y, WU S Y, TSAI C Y, et al. Kinetics of cotton cellulose hydrolysis using concentrated acid and fermentative hydrogen production from hydrolysate[J]. International Journal of Hydrogen Energy, 2011, 36(14): 8743-8750.
[10] JEIHANIPOUR A, KARIMI K, NIKLASSON C, et al. A novel process for ethanol or biogas production from cellulose in blended-fibers waste textiles[J]. Waste Management, 2010, 30(12):2504-2509.
[11] LIN N, HUANG J, CHANG P R, et al. Surface acetylation of cellulose nanocrystal and its reinforcing function in poly(lactic acid)[J]. Carbohydrate Polymers, 2011, 83:1834-1842.
[12] CERQUEIRA D A, FILHO G R, MEIRELES C D S. Optimization of sugarcane bagasse cellulose acetyla-tion[J]. Carbohydrate Polymers, 2007, 69(3):579-582.
[13] FILHO G R, MONTEIRO D S, MEIRELES C D S, et al. Synthesis and characterization of cellulose acetate produced from recycled newspaper[J]. Carbohydrate Polymers, 2008, 73:74-82.
[14] 刘红茹, 陈韵. 醇解法分离废弃涤棉混纺织物工艺研究[J]. 合成纤维工业, 2015, 38(6):22-24.
LIU Hongru, CHEN Yun. Separation of waste polyester-cotton blended fabrics by glycolysis method[J]. China Synthetic Fiber Industry, 2015, 38(6):22-24.
[15] MA M Y, WANG S, LIU Y, et al. Insights into the depolymerization of polyethylene terephthalate in methanol[J]. Journal of Applied Polymer Science, 2022.DOI:10.1002/app.52814.
[16] SARTOVA K, OMURZAK E, KAMBAROVA G, et al. Activated carbon obtained from the cotton processing wastes[J]. Diamond and Related Materials, 2019, 91:90-97.
[17] OZSEL B K, NIS B, MERYEMOGLU B, et al. Utilization of waste cotton linter for preparation of activated carbon to be used as catalyst support in aqueous-phase reforming process[J]. Environmental Progress & Sustainable Energy, 2019, 38(2):445-450.
[18] KIM S H, LEE C M, KAFLE K. Characterization of crystalline cellulose in biomass: basic principles, applications, and limitations of XRD, NMR, IR, Raman, and SFG[J]. Korean Journal of Chemical Engineering, 2013, 30(12):2127-2141.
[19] ONDA A, OCHI T, YANAGISAWA K. Hydrolysis of cellulose selectively into glucose over sulfonated activated-carbon catalyst under hydrothermal condi-tions[J]. Topics In Catalysis, 2009, 52(6/7):801-807.
[20] TALLARICO S, COSTANZO P, BONACCI S, et al. Combined ultrasound/microwave chemocatalytic method for selective conversion of cellulose into lactic acid[J]. Scientific Reports, 2019. DOI:10.1038/s41598-019-55487-y.
[21] 汪利平. 纤维素水热降解制备5-羧甲基糠醛的实验研究[D]. 天津: 天津大学, 2006:14-26.
WANG Liping. Experimental study on the preparation of 5-carboxymethylfurfural by hydrothermal degradation of cellulose[D]. Tianjin: Tianjin University, 2006:14-26.
[22] CUI L P, SHI S, HOU W S, et al. Hydrolysis and carbonization mechanism of cotton fibers in subcritical water[J]. New Carbon Materials, 2018, 33(3):245-250.
[23] BEDIAKO J K, WEI W, YUN Y S. Conversion of waste textile cellulose fibers into heavy metal adsorbents[J]. Journal of Industrial and Engineering Chemistry 2016, 43:61-68.
[24] CHENG X X, FU A P, LI H L, et al. Sustainable preparation of copper particles decorated carbon microspheres and studies on their bactericidal activity and catalytic properties[J]. ACS Sustainable Chemistry & Engineering, 2015, 3(10):2414-2422.
[25] MÖLLER M, HARNISCH F, SCHRÖDER U. Hydrothermal liquefaction of cellulose in subcritical water-the role of crystallinity on the cellulose reactivi-ty[J]. RSC Advances, 2013, 3(27):11035-11044.
[26] SASAKI M, FANG Z, FUKUSHIMA Y, et al. Dissolution and hydrolysis of cellulose in subcritical and supercritical water[J]. Industrial and Engineering Chemistry Research, 2000, 39(8):2883-2890.
[27] ABEL S, PETERS A, TRINKS S, et al. Impact of biochar and hydrochar addition on water retention and water repellency of sandy soil[J]. Geoderma, 2013, 202/203:183-191.
[28] REICHE S, KOWALEW N, SCHLOGL R. Influence of synthesis pH and oxidative strength of the catalyzing acid on the morphology and chemical structure of hydrothermal carbon[J]. Chemphyschem, 2015, 16(3): 579-587.
[29] DU Z, HU B, SHI A, et al. Cultivation of a microalga chlorella vulgaris using recycled aqueous phase nutrients from hydrothermal carbonization process[J]. Bioresource Technology, 2012, 126:354-357.
[30] PETERSON A A, VOGEL F, LACHANCE R P, et al. Thermochemical biofuel production in hydrothermal media: a review of sub- and supercritical water technologies[J]. Energy & Environmental Science, 2008, 1:32-65.
[31] SAVAGE P E. Organic chemical reactions in supercritical water[J]. Chemical Reviews, 1999, 99(2): 603-622.
[32] RUIZ H A, RODRÍGUEZ-JASSO R M, FERNANDES B D, et al. Hydrothermal processing, as an alternative for upgrading agriculture residues and marine biomass according to the biorefinery concept: a review[J]. Renewable & Sustainable Energy Reviews, 2013, 21: 35-51.
[33] LING C, SHI C, HOU W S, et al. Separation of waste polyester/cotton blended fabrics by phosphotungstic acid and preparation of terephthalic acid[J]. Polymer Degradation and Stability, 2019, 161:157-165.
[34] ZHANG Y F, HOU W S, GUO H, et al. Preparation and characterization of carbon microspheres from waste cotton textiles by hydrothermal carbonization[J]. Journal of Renewable Materials, 2019, 7(12): 1309-1319.
[35] LU X W, PELLECHIA P J, FLORA J R V, et al. Inflfluence of reaction time and temperature on product formation and characteristics associated with the hydrothermal carbonization of cellulose[J]. Bioresource Technology, 2013, 138:180-190.
[36] WANG S H, WEI M X, XU Q L, et al. Functional porous carbons from waste cotton fabrics for dyeing wastewater purification[J]. Fibers and Polymers, 2016, 17(2):212-219.
[37] AKHTAR J, AMIN N A S. A review on process conditions for optimum bio-oil yield in hydrothermal liquefaction of biomass[J]. Renewable and Sustainable Energy Reviews, 2011, 15(3):1615-1624.
[38] ZHANG L, LI C J, ZHOU D, et al. Hydrothermal liquefaction of water hyacinth: product distribution and identification[J]. Energy Sources Part A: Recovery, Utilization and Environmental Effects, 2013, 35(14): 1349-1357.
[39] MOHAN D, PITTMAN C U, STEELE P H. Pyrolysis of wood/biomass for bio-oil: a critical review[J]. Energy & Fuels, 2006, 20 (3):848-889.
[40] KRUSE A. Supercritical water gasification[J]. Biofuels Bioproducts & Biorefining-Biofpr, 2008, 2(5): 415-437.
[41] KRUSE A, HENNINGSEN T, SINAG A, et al. Biomass gasification in supercritical water: influence of the dry matter content and the formation of phenols[J]. Industrial & Engineering Chemistry Research, 2003, 42(16): 3711-3717.
[42] SINAG A, GULBAY S, USKAN B, et al. Comparative studies of intermediates produced from hydrothermal treatments of sawdust and cellulose[J]. Supercrit Fluids, 2009, 50:121-127.
[43] INOUE S, UNO S, MINOWA T. Carbonization of cellulose using the hydrothermal method[J]. Journal of Chemical Engineering of Japan, 2008, 41(3):210-215.
[44] SAKAKI T, SHIBATA M, MIKI T, et al. Decomposition of cellulose in near critical[J]. Energy Fuels, 1996, 10:684-688.
[45] XIAO L, SHI Z, XU F, et al. Hydrothermal carbonization of lignocellulosic biomass[J]. Bioresource Technology, 2012, 118:619-623.
[46] SEVILLA M, FUERTES A B. The production of carbon materials by hydrothermal carbonization of cellulose[J]. Carbon, 2009, 47(9):2281-2289.
[47] QI Y J, ZHANG M, QI L, et al. Mechanism for the formation and growth of carbonaceous spheres from sucrose by hydrothermal carbonization[J]. RSC Advances, 2016, 6(25):20814-20823.
[48] FUNKE A, ZIEGLER F. Hydrothermal carbonization of biomass: a summary and discussion of chemical mechanisms for process engineering[J]. Biofuels Bioproducts & Biorefining, 2010, 4:160-177.
[49] GAGIC T, PERVA-UZUNALIC A, KNEZ Z, et al. Hydrothermal degradation of cellulose at temperature from 200 to 300℃[J]. American Chemical Society, 2018, 57: 6576-6584.
[50] YAN L F, QI X Y. Degradation of cellulose to organic acids in its homogeneous alkaline aqueous solution[J]. American Chemical Society, 2014, 2(4):897-901.
[51] EHARA K, SAKA S. Decomposition behavior of cellulose in supercritical water, subcritical water, and their combined treatments[J]. Journal of Wood Science, 2005, 51(2):148-153.
[52] KIM D, YOSHIKAWA K, PARK K. Characteristics of biochar obtained by hydrothermal carbonization of cellulose for renewable energy[J]. Energies, 2015, 8(12): 14040-14048.
[53] KIM D, LEE K, PARK K Y. Upgrading the characteristics of biochar from cellulose, lignin, and xylan for solid biofuel production from biomass by hydrothermal carbonization[J]. Journal Of Industrial And Engineering Chemistry, 2016, 42:95-100.
[54] SAHA N, SABA A, REZA M T. Effect of hydrothermal carbonization temperature on pH, dissociation constants, and acidic functional groups on hydrochar from cellulose and wood[J]. Journal of Analytical & Applied Pyrolysis, 2019, 137:138-145.
[55] YANG F, LI G, GAO P, et al. Mild hydrothermal degradation of cotton cellulose by using a mixed-metal-oxide ZnO-ZrO2 catalyst[J]. Energy Technology, 2013, 1:581-586.
[56] ZHAO Y, LI W, ZHAO X, et al. Carbon spheres obtained via citric acid catalysed hydrothermal carbonisation of cellulose[J]. Materials Research Innovations, 2013, 17(7):546-551.
[57] DEGUCHI S, TSUJII K, HORIKOSHI K. Effect of acid catalyst on structural transformation and hydrolysis of cellulose in hydrothermal conditions[J]. Green Chemistry, 2008, 10(6):623-626.
[58] ZHANG C, LIN S, PENG J, et al. Preparation of highly porous carbon through activation of NH4Cl induced hydrothermal microsphere derivation of glucose[J]. RSC Advances, 2017, 7(11): 6486-6491.
[59] ZHAO H Y, LU X A, WANG Y, et al. Effects of additives on sucrose-derived activated carbon microspheres synthesized by hydrothermal carbonization[J]. Journal of Materials Science, 2017, 52(18):10787-10799.
[60] GARCÍA-BORDEJÉ E, PIRES E, FRAILE J M. Parametric study of the hydrothermal carbonization of cellulose and effect of acidic conditions[J]. Carbon, 2017, 123:421-432.
[61] MOLLER M, NILGES P, HARNISCH F, et al. Subcritical water as reaction environment: fundamentals of hydrothermal biomass transformation[J]. Chemsuschem, 2011, 4(5):566-579.
[62] SAKA S, UENO T. Chemical conversion of various celluloses to glucose and its derivatives in supercritical water[J]. Cellulose, 1999, 6(3):177-191.
[63] ZHANG Y F, DAI J M, GUO H, et al. A comparative study of carbon microsphere preparation by the hydrothermal carbonization of waste cotton fibers, viscose fibers and Avicel[J]. New Carbon Materials, 2020, 35(3):286-294.
[1] 李红颖, 徐毅, 杨帆, 任瑞鹏, 周全, 吴丽杰, 吕永康. 三维乒乓菊状CdS/BiOBr催化剂的制备及其光催化降解罗丹明B[J]. 纺织学报, 2023, 44(09): 124-133.
[2] 周小桔, 胡正龙, 任一鸣, 谢兰东. Bi2MoO6修饰TiO2复合纳米棒阵列光催化剂的制备及其光催化性能[J]. 纺织学报, 2022, 43(10): 97-105.
[3] 施敏慧, 李冰蕊, 王挺, 吴礼光. 高含盐废水中TiO2复合光催化剂光降解甲基橙机制及性能[J]. 纺织学报, 2021, 42(12): 103-110.
[4] 龙晓静 高翠丽 王兵兵 赵卫 潘若才 夏延致. 碳材料对海藻酸钠纺丝液降解性的影响[J]. 纺织学报, 2014, 35(2): 138-0.
Viewed
Full text


Abstract

Cited

  Shared   
  Discussed   
No Suggested Reading articles found!