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Polymerization flow chart

C to give the expected 2-methyl-1-butene in high selectivites (24). The AI2O2 catalyzed process can be optimized to give di- -pentyl ether as the exclusive product (23). Dehydration of 1-pentanol over an alkah metal promoted AI2O2 catalyst at 300—350°C provides 1-pentene at selectivities of 92% (29,30). Purification produces polymerization grade (99.9% purity) 1-pentene. A flow chart has been shown for a pilot-plant process (29). [Pg.372]

Seven of the tools of quahty have been summarized (43). The first tool is a flow chart, used to help understand the organizational flow of a procedure or process. A flow chart should be constmcted with the fiiU participation of the people who do the work. Its principal benefit is to enable teams, such as problem-solving or productivity improvement teams, to reach a common vision of the work flow. Its use enables the improvement effort to begin with this common understanding. Figure 3 contains an example for manufacture of a polymeric material. [Pg.369]

A schematic flow chart of this process is shown in Fig. 6. The feed is composed of 25-35 wt% purified isobutene and the required amount of isoprene (0.4-1.25 wt%), dissolved in cooled liquid methyl chloride. Purity of supplied isobutene is variable and preliminary drying and fractionation in a two-tower system remove water, n-alkenes, f-butanol, and diisobutenes. The polymerization grade (>99.5%) fresh isobutene is then mixed in a feed blend drum with isoprene (purity >98%) and a recycle stream of diluent and unreacted monomers. A concentrated catalyst solu-... [Pg.694]

Figure 3 shows a flow chart of the polymerization plant with the injection system, on-line registration of the polymerization rate, temperature course and pressure, and the stirrer tachometer. The injection system allows the immediate in situ start of the reaction, and the flow meters enable measurement of the true initial rates (monomer consumption in dependence on time). With this very rapid technique it is also possible to pursue strong unsteady polymerizations versus time courses. [Pg.8]

A flow chart of this general process is illustrated in Figure 5.11. Surfactant and alkaline coupler solutions are combined to form a solution wherein surfactant and coupler form mixed micelles. This solution is then acidified and the coupler is reprotonated to create metastable coupler (nano)particles. Excess salt is then removed by washing (ultrafiltration or dialysis). Steric stabilization may be imparted by adding polymeric stabilizers or nonionic surfactants at the initial or final process stages. [Pg.100]

Figure 5.9 Flow chart for the production process of core-shell nanoparticles (CSN) via miniemulsion polymerization. Figure 5.9 Flow chart for the production process of core-shell nanoparticles (CSN) via miniemulsion polymerization.
Figure 7.1. Flow chart for a typical semibatch emulsion polymerization process. Figure 7.1. Flow chart for a typical semibatch emulsion polymerization process.
If polymers are examined spectroscopically without removing additives such as fillers, plasticisers, stabilisers, lubricants, etc. then their infrared spectra may be affected drastically by the presence of these substances. Also, if care has not been taken during the preparation of a sample, bands due to contaminants such as water, silicate, phthalates, polypropylene (from laboratory ware), etc, may appear in the spectra and so result in some confusion. Hence, the flowcharts given below should be used with some degree of caution. In order to confirm an assignment made by use of the flow chart, it is important finally to make use of known infrared reference spectra. However, it should be borne in mind that stereoregular polymers may have spectra which differ from their atactic form and that sample preparative techniques may also affect the spectrum obtained for a particular polymeric sample. [Pg.279]

Draw a schematic flow chart for chemical and electrochemical polymerization for 3-methyl thiophene, clearly noting the commonalities and differences in the mechanistics of the two. [Pg.23]

The poly aniline nanospheres (PANI-NS) were synthesized by oxidative polymerization of aniline monomer at 0 °C in an ice bath using ammonium persulfate as the oxidant in the presence of surfactant. Aniline, ammonium persulfate, Polyvinylpyrrolidone, cetyl ammonium bromide, and camphorsulfonic acid are used as received from Sigma-Aldrich. Camphorsulfonic acid surfactant as the dopant and ammonium persulfate as the oxidant were used in the present synthesis of polyaniline nanospheres (see flow chart in Fig. 8.11). Calculated quantities of aniline monomer (0.005 mol) were mixed with 50 mL of distilled water and stirred using magnetic stirrer for 10 min. Meanwhile, calculated quantities of surfactant (0.75 mol) and oxidant (0.005 mol) were dissolved separately in distilled water and stirred for 10 min in an ice bath. The surfactant solution was first added to the aniline monomer aqueous solution, and then the previously cooled oxidant solution was added drop wise after which the mixture was allowed to react for 10 h in an ice bath. The precipitate was filtered and washed several times with distilled water and... [Pg.196]

Ethylene mass-flow meter is an important part in the design of a polymerization reactor. The meter provides instant feedback on the polymerization rate and is connected to a strip chart recorder. In addition, the meter may be used to develop a process model for a particular reactor design. [Pg.374]


See other pages where Polymerization flow chart is mentioned: [Pg.426]    [Pg.443]    [Pg.372]    [Pg.417]    [Pg.9]    [Pg.690]    [Pg.90]    [Pg.208]    [Pg.321]    [Pg.172]    [Pg.94]   
See also in sourсe #XX -- [ Pg.66 ]




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