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CHP

Smith, R., and Jones, P. S., The Optimal Design of Integrated Evaporation Systems, Heat Recovery Systems and CHP, 10 341, 1990. [Pg.93]

The functions of the bulb in the inlet tube C are to reduce the danger of spurting and also the sucking back of the liquid in A the latter can be prevented by the timely opening of the screw chp on E. [Pg.1106]

C—H bonds are polarized by attached unsaturated carbon substituents. Such groups "activate" the neighbouring CHj, CHp or CH groups in the following order CR=NR > COR > CN > COOR > CR = NR > Ph > CR=CRj. Two activating substituents reinforce each other. [Pg.9]

Fig. 10. Dow diaphragm ceU (a) Six-ceU series, (b) Internal ceU parts a, cathode elements b, cathode pocket elements c, copper spring cHps d, perforated steel backplate e, brine inlet f, chlorine oudet g, copper backplate h, titanium backplate i, anode element. Fig. 10. Dow diaphragm ceU (a) Six-ceU series, (b) Internal ceU parts a, cathode elements b, cathode pocket elements c, copper spring cHps d, perforated steel backplate e, brine inlet f, chlorine oudet g, copper backplate h, titanium backplate i, anode element.
The primary sources of contamination in ion implantation come from metal atoms that may be etched off reactor fixtures, such as reactor wads, wafer holder, cHps, and so on. The pump oils used by the vacuum pumps may be a source of hydrocarbon contamination. The dopant sources themselves are not a significant source of contamination because unwanted ions are separated out from the beam during beam analysis. [Pg.350]

An expandable anode involves compression of the anode stmcture using cHps during cell assembly so as not to damage the diaphragm already deposited on the cathode (Eig. 3a). When the cathode is in position on the anode base, 3-mm diameter spacers are placed over the cathode and the cHps removed from the anode. The spring-actuated anode surfaces then move outward to bear on the spacers, creating a controlled 3-mm gap between anode and cathode (Eig. 3b). This design has also been appHed to cells for the production of sodium chlorate (22). [Pg.122]

A typical phenol plant based on the cumene hydroperoxide process can be divided into two principal areas. In the reaction area, cumene, formed by alkylation of benzene and propylene, is oxidized to form cumene hydroperoxide (CHP). The cumene hydroperoxide is concentrated and cleaved to produce phenol and acetone. By-products of the oxidation reaction are acetophenone and dimethyl benzyl alcohol (DMBA). DMBA is dehydrated in the cleavage reaction to produce alpha-methylstyrene (AMS). [Pg.288]

Safety is a critical aspect in the design of phenol plants. Oxidation of cumene to CHP occurs at conditions close to the flammable limits. Furthermore, the CHP is a potentially unstable material which can violendy decompose under certain conditions. Thus, phenol plants must be carefully designed and provided with weU-designed control and safety systems. [Pg.289]

Phenol quahty tests and analyses can be divided into two categories wet lab and Hquid and gas chromatography. In the wet lab, phenol is tested for pH, sohdification point, solubiUty in water, bromine index, color, and distillation ranges. Phenol concentration, impurities, and CHP contents are analy2ed using highly automated Hquid and gas chromatography. [Pg.290]

The most widely used process for the production of phenol is the cumene process developed and Hcensed in the United States by AHiedSignal (formerly AHied Chemical Corp.). Benzene is alkylated with propylene to produce cumene (isopropylbenzene), which is oxidized by air over a catalyst to produce cumene hydroperoxide (CHP). With acid catalysis, CHP undergoes controUed decomposition to produce phenol and acetone a-methylstyrene and acetophenone are the by-products (12) (see Cumene Phenol). Other commercial processes for making phenol include the Raschig process, using chlorobenzene as the starting material, and the toluene process, via a benzoic acid intermediate. In the United States, 35-40% of the phenol produced is used for phenoHc resins. [Pg.292]

The crystallinity of poly(lactide- (9-glycoHde) samples has been studied (36). These copolymers are amorphous between the compositional range of 25—70 mol % glycoHde. Pure polyglycoHde was found to be about 50% crystalline whereas pure poly-L-lactide was about 37% crystalline. An amorphous poly(L-lactide-i (9-glycoHde) copolymer is used in surgical cHps and staples (37). The preferred composition chosen for manufacture of cHps and staples is the 70/30 L-lactide/glycoHde copolymer. [Pg.191]

Siace a large part of the beer market is take-home beer, brewers must provide retailers with packs that are easily handled and stored. Clear shrink wrappiag has become a dominant feature because it permits the content of the pack to be seen. Other packagiag methods are Shrink Wrapped 2 dozea Tray Pack, Cardboard Sleeve, Hi Coae 3 Pack, Hi Coae 6 Pack ia Tray, and Top CHp Bottle Pack (see Packaging materials). [Pg.27]


See other pages where CHP is mentioned: [Pg.362]    [Pg.403]    [Pg.471]    [Pg.472]    [Pg.920]    [Pg.921]    [Pg.922]    [Pg.259]    [Pg.31]    [Pg.58]    [Pg.588]    [Pg.591]    [Pg.489]    [Pg.492]    [Pg.381]    [Pg.255]    [Pg.535]    [Pg.416]    [Pg.516]    [Pg.67]    [Pg.56]    [Pg.419]    [Pg.513]    [Pg.289]    [Pg.74]    [Pg.7]    [Pg.8]    [Pg.465]    [Pg.477]    [Pg.233]    [Pg.245]    [Pg.245]    [Pg.271]    [Pg.330]    [Pg.344]   
See also in sourсe #XX -- [ Pg.21 ]

See also in sourсe #XX -- [ Pg.178 ]

See also in sourсe #XX -- [ Pg.19 , Pg.39 , Pg.42 , Pg.109 ]




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