纺织学报 ›› 2026, Vol. 47 ›› Issue (07): 261-269.doi: 10.13475/j.fzxb.20260100302

• 综合述评 • 上一篇    下一篇

纤维素纤维用活性染料低给液染色研究进展

宋金洋1,2, 房宽峻1,2()   

  1. 1 青岛大学 纺织服装学院, 山东 青岛 266071
    2 青岛大学 生态纺织省部共建协同创新中心, 山东 青岛 266071
  • 收稿日期:2026-01-04 修回日期:2026-05-11 出版日期:2026-07-15 发布日期:2026-07-29
  • 通讯作者: 房宽峻(1963—),男,教授,博士。主要研究方向为绿色低碳染整技术。E-mail:13808980221@163.com
  • 作者简介:宋金洋(1998—),男,博士生。主要研究方向为绿色低碳染整技术。
  • 基金资助:
    山东省重大科技创新工程项目(2023CXGC010504);山东省重点研发计划项目(2023CXPT022);山东省重大科技创新工程项目(2023CXGC010612)

Research progress in low wet pick-up dyeing of cellulosic fibers with reactive dyes

SONG Jinyang1,2, FANG Kuanjun1,2()   

  1. 1 College of Textiles & Clothing, Qingdao University, Qingdao, Shandong 266071, China
    2 Collaborative Innovation Center for Eco-textiles of Shandong Province and the Ministry of Education, Qingdao University, Qingdao, Shandong 266071, China
  • Received:2026-01-04 Revised:2026-05-11 Published:2026-07-15 Online:2026-07-29

摘要:

针对传统纤维素纤维活性染料染色工艺中存在的水资源消耗量大与染料利用率低的问题,系统综述了低给液染色技术领域的最新研究进展。通过精确调控织物带液率并优化织物内水分分布状态,可从源头有效抑制活性染料水解动力学过程,进而显著提升染料固着效率。分析并比较了2类主要技术路径:其一为减量式给液途径,借助真空抽吸、高压气流冲击、低温预烘等脱水手段移除多余液体,该路径优势在于初始染液渗透充分、染色均匀性优良,然而其亦面临水资源消耗总量未获实质性削减与脱水单元能耗偏高的技术悖论;其二为计量式给液途径,涵盖泡沫施加、液体转移、喷雾沉积、喷墨打印以及非水介质辅助施液等工艺方式,此类技术展现出极高的资源利用效率,但由于缺乏机械挤压作用,常面临染液渗透性不足与匀染性欠佳的问题。最后指出,未来研究应着重关注染整工艺与装备系统的协同创新,借助数字化手段构建基于织物特征参数的自适应智能给液体系,以驱动印染行业迈向高质量可持续发展之路。

关键词: 活性染料, 低给液染色, 清洁染色, 少水技术, 带液率, 绿色低碳, 节能减排

Abstract:

Significance Reactive dyes dominate the dyeing market for cellulosic fibers owing to their wide color gamut, brilliant shades, broad applicability, and favorable color fastness. However, in conventional dyeing processes, reactive dyes are prone to hydrolysis, resulting in the discharge of substantial amounts of unfixed dyes into wastewater, which leads to considerable resource waste and environmental pollution. Low wet pick-up dyeing technology, because of its potential to reduce the input of water and chemical agents at the source, has become one of the key research directions for promoting the green and low-carbon transformation of the textile dyeing industry.

Progress In order to improve the utilization efficiency of reactive dyes, a series of low wet pick-up dyeing technologies have been developed. According to the underlying technical principles and liquor-application modes, such systems can be broadly classified into two main categories, i.e.,the expression-type and topical-type. The expression-type approaches include vacuum dewatering wet steaming, low-moisture pad-bake steaming, and high-pressure air dewatering, and the topical-type techniques include foam dyeing, transfer-application-based dyeing, spray dyeing, and inkjet-based coloration. Among these, foam dyeing has completed the transition from laboratory research to industrial application and is currently in the stage of industrial promotion. Low wet pick-up technologies, such as spray dyeing and inkjet-based coloration, which enable precise control of dye-liquor application, have developed rapidly,and are regarded as important technologies for the green transformation of the textile dyeing and printing industry. It can be learnt from the review that the expression-type low wet pick-up dyeing benefits from an initially high wet pick-up, which facilitates adequate liquor penetration into the cellulosic fiber's assembly and subsequent diffusion of dye molecules into the cellulosic fiber's interior, thereby providing the basis for level dyeing. However, this route presents two major dilemmas. First, although the dewatering stage effectively controls the final wet pick-up, it does not reduce the overall water consumption of the process. Second, the energy consumed during dewatering counteracts the energy savings achieved during fixation. Owing to its inherent high-to-low wet-pick-up profile, the reduction in fixation energy is often offset by the substantial energy demand of the dewatering unit, making net energy savings across the whole process difficult to realize. By contrast, metered-application-type low wet pick-up dyeing is characterized by the precise application of dye liquor at the initial stage. However, unlike conventional pad dyeing, it lacks the full-bath impregnation and nip pressure that promote uniform liquor penetration, thereby limiting subsequent dye transport into the cellulosic fiber's interior. This directly leads to two challenges: insufficient penetration and non-uniform surface distribution. In addition, much of the existing research remains limited to comparisons of macroscopic dyeing performance, such as K/S values, whereas understanding of the underlying transport and distribution mechanisms remains insufficient, which has become a key constraint on the transition from laboratory research to industrial application.

Conclusion and Prospect This paper systematically scrutinized two principal technical routes for low wet pick-up reactive dyeing, namely, the expression-type and the metered application-type route. Future research should focus on synergistic process-equipment innovation, strengthening theoretical research and evaluation systems, and advancing technology integration. The development of low-energy dewatering units, penetration-enhanced metered-application systems, standardized evaluation methods, and digitally controlled adaptive application technologies will be essential for further progress

Key words: reactive dye, low wet pick-up dyeing, cleaner dyeing, water-saving technology, wet pick-up, green and low-carbon, energy conservation and emission reduction

中图分类号: 

  • TS190.8

图1

不同带液率的棉纤维模型"

图2

纤维素纤维用活性染料低给液染色技术时间脉络图"

图3

密封装置示意图"

表1

减量式低给液染色方法"

染色工艺 脱水
设备
染料
类型
浸轧染液质量
浓度/(g·L-1)
织物面密度/
(g·m-2)
起始织物
带液率/%
脱水后织物
带液率/%
固色
环境
固色率
提高率/%
K/S
提升率/%
参考
文献
真空脱水辅助
湿蒸染色工艺
真空
干燥箱
活性
黑5
10、30 140 75±2 30±2 常压饱和
汽蒸,100 ℃
11、22 [15]
浸轧—真空脱水—
湿蒸染色工艺
真空
干燥箱
活性金
黄SER
25 176 75±2 25±2 常压饱和
汽蒸,100 ℃
10 16 [16]
低含水率湿蒸
染色工艺
真空
干燥箱
应用活
性蓝19
10 140 75±3 30 常压饱和
汽蒸,100 ℃
10 8 [17]
低含水率焙蒸
固色工艺
连续式
织物定
形机
活性红198 30 115 75±2 30 焙蒸
固色,140 ℃
25 [19]

表2

计量式低给液染色方法"

染色
工艺
工作液的
施加方式
染料
类型
织物面密度/
(g·m-2)
染液
浓度
计量式低给液
技术的织物
带液率/%
对比工艺及其
带液率/%
固色
环境
K/S
对比
参考
文献
泡沫
染色
化学起泡
给液
活性红120 176 20 g/L 两相法
轧染,80
常压饱和
汽蒸,102 ℃
7.34, 7.2 [30]
喷液
染色
喷墨打印
给液
活性黑5 115 7.07% (o.w.f) 40 一浴法轧染
工艺,80
过热汽蒸,130 ℃,
相对湿度60%
20.37,
19.99
[32]
喷雾
染色
压力雾化
给液
雷马素系列
RGB拼混染料
60 g/L 52 两相法
轧染,100
常压饱和
汽蒸,100 ℃
基本
相同
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