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2、ulsion polymerization. And the effects of different polymerization technological parameters, such as initiator, crosslinker, emulsifier, on the oil absorbency of high oil-absorption resins were discussed in detail. The result indicatedthat the absorption of the resin was about 9.2(g/g) for toluene a

3、nd 16.2(g/g) for chloroform.Key words: concentrated inverse emulsion polymerization；oilabsorption resin；oil absorption rate摘要、16.2倍的三氯甲烷。关键字：超浓反相乳液聚合；吸油性树脂；吸油速率ContentsAbstractAbstract in Chinese1 Introduction12 Experiment32.1Materials32.2Polymerization32.3 Measurements3 Oil absorption test32.3.2 R

4、egeneration test42.3.3 Oil retention42.3.4 Characterization43 Results and Discussion53.1 The effect of cross-linking amount on the oil absorbency53.2 Effect of the amount of the emulsifier on the oil absorbency53.3 The effect of initiator amount on the oil absorbency63.4 Oil absorption rate of the r

5、esins73.5 Relation of oil retention ratio with time83.6 Oil absorption repetitive characteristic of resins84 Conclusions10Bibliography1112 / 161 IntroductionOil pollution of marine environments is being a serious issue. With the growth of the off-shore petroleum industry and the necessity of marine

6、oil transportation. Various methods for the treatment of spilled oil have been tried15. One of the methods to solve this problem is by using oil absorptive resins, which can collect and remove the oil spilled on water, and some have proved to be highly efficient6-7. High oil-absorption resin, being

7、different from traditional oil-absorbing materials, is a new kind of self-swelling oil-absorbing material with many virtues of absorbing large quantity and variety of oils, only absorbing oil from oil/water mixture and high capacity for oil retention, and has a promising future. Synthesis and applic

8、ations of high oil-absorption resins have very important practical significance for environment protection.Acrylic has been widely used as monomers to prepare high oil-absorbing resins. Copolymerization of acrylic can be approached by various methods such as emulsion polymerization and suspension po

9、lymerization. However, the resins obtained by the above methods universally have some defects of pact structure810. It is important to select asuitable technique and optimize the conditions of polymerization for synthesis of workable acrylic copolymer.Concentrated emulsions are gel-like emulsions in

10、 which the volume fraction of the dispersed phase is greater than 0.74. The dispersed phase is in the form of spherical or polyhedral cells separated by a continuous-phase network of thin films. Concentrated emulsions have three important characteristics:11-12 (1) the reduced monomer mobility betwee

11、n cells, because of the presence of a reinforced surfactant layer, can generate an earlier gel effect, which leads to a delay in the bimolecular termination reaction and, therefore, a higher molecular weight; (2) the particle size can be controlled easily by the selection of a suitable surfactant ty

12、pe and concentration; and (3) a polymer containing little water, from which powdery resins are easily formed, can be obtained through concentrated emulsion polymerization. In parison with the four methods of free-radical polymerization (bulk, solvent,suspension, and emulsion), concentrated emulsions

13、 have not only a paste like appearance and a high solid content but also a nucleation mechanism for the latex particle; the morphology of latex products is different from that of conventional emulsion polymerization. For these reasons, concentrated emulsion polymerization deserves to be studied deep

14、ly and widely.In this essay, the influences of emulsifiers，the amount of cross-link agent, the amount of initiator on the absorption properties of the resin were investigated2 ExperimentMaterialsButyl methacrylate(BMA) analytical reagent grade, Tianjin KediReagent,was used as monomer ; Ammonium pers

15、ulfate(APS) and sodium hydrogensulfite(SHS) analytical reagent grade, Tianjin Fuchen Reagents, were used as redox initiator; Span80 analytical reagent grade,Tianjin kemio Reagent,was used as emulsifier; Divinyl benzene(DVB) chemically pure,ShanghaReagent , was used as cross-link agent.2.2 Polymeriza

16、tionBMA was carried out in 150-ml roundbottom flask. A typical procedure was as follows: the required amounts of Span80 and DVB were put into the reaction system. The system was charged with N2 for 20 mins and was sealed under N2. Then 32-ml deionized water was injected into the reaction system. Aft

17、er that, ammonium persulfate(APS)/sodium hydrogensulfite(SHS) were injected into the reaction system. The flask was wholly immersed in a water bath held at 40 by a thermostat to start the polymerization. The reaction was carried out under stirring. The reaction time was 3h. The polymer was dried in

18、vacuum for 24h at a 35.All of theingredients used are summarized in Table 1.Table 1. Standard recipe for the concentrated inverse emulsion polymerization of BMAIngredientDosageBMA7mlDVB Span80H2O32mlNH4)2S4O8NaHSO32.3 Measurements2.3.1 Oil absorption test (g oil/g sample)0.2 g of dried sample weight

19、ed beforehand was put into a filter bag and immersed in toluene at room temperature. After given time periods (24h is needed for full oil absorbency), the filter bag with the sample was lifted from the oil and drained for 1 min. Then the sample was immediately taken out and weighed. The oil absorben

20、cy was calculated by the following formula:W1=( G2- G1)G1where G1 is the weight of resins before oil absorption and G2 is the weight of resins after oil absorption.For the study of oil absorption rate of the resins, the above measurementsare repeated from time to time.2.3.2 Regeneration testOil-abso

21、rbed samples were dried invacuum for 24 h. Using the abovemeasurements tests oil absorbency at five times.2.3.3 Oil retentionThe resins after oil absorption were put in drying oven for 5h at 50, and then weighted. 2.3.4 CharacterizationThe particle morphology of the BMA polymer was observed with sca

22、nningelectronmicroscopy (SEM; JSM-5610LV). The samples were sputter-coated withAu film before the examination and the voltage is 20 kV.3 Results and DiscussionThe effect of cross-linking amount on the oil absorbencyThe oil-absorbing process of high oil-absorption resins, as low degree of polymer, wa

23、s swelling process. As evidence, not only the sorts of crosslinker can affect the interstitial space structures of the resins, but also the amount of crosslinker can directly influence the particle morphology and the degree of crosslinking of the resins. Figure 1 illustrated the relationship between

24、 oil absorbency and the amount of DVB. As shown in Fig.1, there was a maximum point. When the amount of DVB was smaller than that at the maximum point, the oil absorbency increased with increasing DVB. However, the oil absorbency decreased with increasing DVB when the mount of DVB was larger than th

25、at at the maximum point.Fig.1 The effect of cross-linking amount on the oil absorbency It is well known that an increase in the amount of a crosslinker causes the denser network of the polymer. Adding less amount of DVB, the degree of crosslinking of the resins was lower, the tridimensional network

26、was not satisfying. The resins were soluble in oil and the viscosity of the product increased. The resins which have absorbed oil cannot recover. If the amount of crosslinker was too great, the crosslinker degree increased and the network space in the resins decreased. As a result, the oil absorbenc

27、y reduced. The resins had the best oil absorptivity when the interstitial space is at its optimum value. Figure. 1 shows that this occurs at 8.8.3.2 Effect of the amount of the emulsifier on the oil absorbencyIn concentrated inverse emulsion polymerization, although emulsifiers do not directly take

28、part in the reaction, they have reducing interface tension, emulsification, and dispersing effects. The main difference with a conventional emulsion polymerization is that a part of emulsifier is present at the monomer/water interface and not only at the polymer particle/water interface. Another poi

29、nt is that, in most cases, the amount of the emulsifier is very low, so that the particles formed by the emulsion process are not stable enough and easily coalesce to give much larger primary particles.Fig.2 The effect of Span80 concentration on the oil absorbency The effect of the amount of the emu

30、lsifier based on the oil absorbency was shown in Fig.2.When concentration emulsifier is low, the oil absorbency increased. Because the primary particles formed with agglomerates of latex particles were more stable because of the colloid protection behavior of the emulsifier, the oil absorbency incre

31、ased. With increasing Span80 concentration, the colloid protection behavior was more prominent, and the polymerization proceeded stably; then, the primary particles existed more stably, and more large particles were formed. As a result, the oil absorbency decreased.3.3 The effect of initiator amount

32、 on the oil absorbencyBMA polymer as short-chain high oil-absorption resins were prepared by concentrated inverse emulsion polymerization, with the formation of radicals in water phase, and the radicals were captured by the existing particles inside the water phase. The effects of variousAPS and SHS

33、 concentrations based on the weight of BMA on the oil absorbency were shown in Fig. 3With increasing initiator concentration, the oil absorbency increased, and then decreased. The concentration of APS and SHS needed to be in a certain range to ensure that the reaction proceeds smoothly.Fig.3 The eff

34、ect of initiator amount on the oil absorbencyIn the reaction system, the concentration of the initiator will cause effects on the reaction rate, the molecular weight of the resins, and the crosslinking degree. Moreover, it is known that the more initiator will generate more active centers in order t

35、o increase the conversion and the gel fraction and decrease the length of the basic chain in polymer systems. As a result, the chain length between crosslinking points of the network decreased and the crosslink density increased with the increase of the initiator concentration. Therefore, the final

36、result was a decrease of the oil absorbency.3.4 Oil absorption rate of the resinsTheSEMmicrophotographs of particles prepared by concentrated inverse emulsion polymerization was displayed in Fig. 4. It was apparent that there were many small random pores in the crosslinked resins prepared by concent

37、rated inverse emulsion polymerization. These pores will support large surfaces in the polymeric network. The morphology of a crosslinked resins will influence the rate of oil absorption. The oil absorption rate of the resins is shown in Fig.5. At first, the speed rate of the oil absorption was very

38、fast at first 30mins. Obviously, it only need 2h to the highest oil absorbency.Fig.4 SEM microphotographs of particles prepared byconcentrated inverse emulsion polymerizationFig.5 Oil absorption rate of the resin 3.5 Relation of oil retention ratio with timeThe resins after oil absorption were put i

39、n drying oven for 5h at 50, and then weighted. The result of oil retention was in Table 2.Tab.2Relation of oil retention ratio with timeTime(h)12345Prue oil (%)Oil retention rate of resin (%)3.6 Oil absorption repetitive characteristic of resinsThe result of oil absorption repetitive characteristic

40、of resins was in Fig. 6.Fig.6 Oil absorption repetitive characteristic of resins4 Conclusions BMA polymer as short-chain high oil-absorption resin was synthesized by concentrated inverse emulsion polymerization. The effects of the concentration of the crosslinker, the concentration of the initiator,

41、 and the amount of the emulsifier on the oil absorbency were discussed. The optimum polymerization conditions were obtained as follows:mDVB/mmonomer=8.8wt%, m(APS/SHS)/mmonomer =3.75 wt%, mSpan80/mmonomer =8wt%; The highest oil absorbency was 9.2 g/g for toluene and 16.2 g/g for chloroform.The speed

42、 rate of the oil absorption was very fast at first 30mins,and it only need 2h to the highest oil absorbency.Bibliography1 B. Wu, M. H. Zhou. Recycling ofwastetyre rubber into oil absorbent.Waste Manage. 2009, 29, 355359.2 A. M. Atta, K. F. Arndt.Swelling and network parameters of high oil-absorptive

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44、4920.4 T. Shimizu, S. Koshiro, Y. Yamada. Effect of cell structure on oil absorption of highly oil absorptive polyurethane foam for on-site use. J. Appl. Polym. Sci. 1997, 65,179186.5 S. Suni, A. L. Kosunen, M. Hautala, Mar.Useof a by-product of peat excavation, cotton grass fibre, as a sorbent for

45、oil-spills. Pollut. Bull. 2004, 49, 916921.6 C. Teas, S. Kalligeros, F. Zanikos. Investigation of the effectivenessof absorbent materials in oil spills clean up. Desalination 2001, 140, 259264.7M. H. Zhou, W. J. Cho. High oil-absorptive posites based on 4-tert-butylstyrene-EPDM-divinylbenzene graftp

46、olymer. Polym. Int. 2001, 50, 11931200.8 M. J. Zhang, X. Zhi. New Chem. Mater. 2007, 35(1), 5960.9 K. J. Yao, W. J. Zhou. Synthesis and water absorbency of the copolymer of acrylamide with anionic monomers. J. Appl. Polym. Sci. 1994, 53(11), 15331538.10 G. R. Shan, P. Y. Xu, Z. X. Weng, Z. M. Huang.

47、Synthesis and properties of oil absorption resins filled with polybutadiene.J. Appl. Polym. Sci. 2003,89(12), 33093314.11 G. R. Shan, P. Y. Xu, Z. X. Weng, Z. M. Huang.Oil-Absorption Function of Physical Crosslinking in theHigh-Oil-Absorption Resins. J. Appl. Polym. Sci. 2003,90(14), 39453950.12 X. W. Li, J. Q. Liu, Chem. World. 2007, (1), 5659.13 C. L. Du, R. M. Zhao, Liaoning Chem. Ind. 2007, 36(4), 235236, 239.14 J. Z. Huang, Q. X. Zheng, J. Su, Chem. Bioeng. 2007, 24(8), 6365.15 Y. Y. Li,W. B. Shu, L. N. Zan., Chem. Ind. Eng.

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