共查询到20条相似文献,搜索用时 62 毫秒
1.
2.
介绍了电石法PVC生产中降低电石单耗的措施,包括加强电石生产和运输过程管理、新建电石大料仓、回收电石灰、回收蒸发冷凝系统和洗涤系统水中夹带的乙炔等. 相似文献
3.
4.
电石路线氯乙烯生产技术新进展 总被引:1,自引:0,他引:1
探讨了在电石法PVC生产中从电石生产、乙炔发生、乙炔清净、电石渣浆清液循环、电石渣浆中乙炔回收、乙炔脱水、氯乙烯合成一直到氯乙烯脱水干燥这一系列生产过程中的技术新进展情况,指出我国电石法PVC已不再是“低水平建设”。探讨了生产工艺中还须改进之处。 相似文献
5.
通过加强电石库管理并改进乙炔发生工艺,将生产PVC的电石单耗从1.42 t降低到1.36 t,降低了生产成本,增强了产品的市场竞争力。 相似文献
6.
7.
8.
9.
介绍了齐化集团聚氯乙烯分厂采用电石法生产PVC树脂的成本控制措施:①加强电石管理,严格控制电石单耗指标;②加强对原辅材料气的控制;③技术改造对成本的控制;④产量及其他因素对成本的控制。这些措施实施后生产1t PVC树脂的电石单耗达到了1.38t、VCM单耗达到了1.067t。 相似文献
10.
通过采取加强电石库管理、改进发生器加料方式、增加乙炔回收装置、严格控制原料气配比、回收聚合工序废水及废气中的氯乙烯等措施,使PVC生产的电石单耗从1.42 t降至1.36 t,有效降低了生产成本。 相似文献
11.
乙烯酮(双乙烯酮)是十分重要的化工中间体,其下游产品较多。江苏某化工厂开发生产乙烯酮(双乙烯酮)下游产品三十多个,年生产规模三万多吨,是国内以乙烯酮(双乙烯酮)为中间体生产精细化学品的综合骨干企业。针对乙烯酮(双乙烯酮)下游产品废水特点,该厂结合企业实际,开展了产品优化,结构调整,清洁生产,资源循环利用,节水降耗等工作,从源头削减了污染物的生产。同时投资二千多万元新建预处理装置三套,6000m3/d废水生化处理装置一套,使全厂乙烯酮(双乙烯酮)下游产品的废水得到了有效的治理。 相似文献
12.
13.
14.
15.
我厂3号回转窑(Φ4m×60m)生产线在1996年年底由SP窑(产量912t/d)改为NSP窑(产量1320t/d),预分解系统为四级旋风预热器带离线式分解炉 相似文献
16.
Conclusions It is significant that the purification on a single passage of viscose through porous ceramic corresponds to the result of a two-stage filtration of it in industrial filter-presses with standard fillings.Kiev Combine. Kiev Technological Institute of Light Industry. Translated from Khimicheskie Volokna, No. 3, pp. 20–22, May–June, 1969. 相似文献
17.
The objective of the study was to explore the effect of the degree of deacetylation (DD) of the chitosan used on the degradation rate and rate constant during ultrasonic degradation. Chitin was extracted from red shrimp process waste. Four different DD chitosans were prepared from chitin by alkali deacetylation. Those chitosans were degraded by ultrasonic radiation to different molecular weights. Changes of the molecular weight were determined by light scattering, and data of molecular weight changes were used to calculate the degradation rate and rate constant. The results were as follows: The molecular weight of chitosans decreased with an increasing ultrasonication time. The curves of the molecular weight versus the ultrasonication time were broken at 1‐h treatment. The degradation rate and rate constant of sonolysis decreased with an increasing ultrasonication time. This may be because the chances of being attacked by the cavitation energy increased with an increasing molecular weight species and may be because smaller molecular weight species have shorter relaxation times and, thus, can alleviate the sonication stress easier. However, the degradation rate and rate constant of sonolysis increased with an increasing DD of the chitosan used. This may be because the flexibilitier molecules of higher DD chitosans are more susceptible to the shear force of elongation flow generated by the cavitation field or due to the bond energy difference of acetamido and β‐1,4‐glucoside linkage or hydrogen bonds. Breakage of the β‐1,4‐glucoside linkage will result in lower molecular weight and an increasing reaction rate and rate constant. © 2003 Wiley Periodicals, Inc. J Appl Polym Sci 90: 3526–3531, 2003 相似文献
18.
19.
20.
A refined nonlinear value of the main parameter of a material, i.e., the elongation modulus versus the instant temperature value, was suggested for introduction into the computational algorithm of tempering stresses. 相似文献