United Nations Industrial Development Organization: Recent submissions

  • Unknown author (United Nations Industrial Development Organization, 1979-01)
    DDVP, with the common name dichlorvos, has an active ingredient, 2,2-dicWorovinyl dimethyl phosphate, which was flrst introduced by Ciba Geigy AG under the trademark "Nuvan" and by Shell Chemical Co. under the trademark ...
  • Unknown author (United Nations Industrial Development Organization, 1979-01)
    Carboxymethyl cellulose (CMC), a kind of cellulose ether, is a white powdery sizing agent made from pulp cellulose. Since its discovery by Jansen of Germany in 1918, it has rapidly expanded in advanced western countries. In ...
  • Unknown author (United Nations Industrial Development Organization, 1979-01)
    Caustic soda is one of the basic chemical products produced in the largest quantity along with sulfuric acid, ammonia and ethylene. Moreover, because of its large production scale, caustic soda is generally classified ...
  • Unknown author (United Nations Industrial Development Organization, 1979-01)
    Limestone is one of the most abundantly available natural resources on earth. Composed mainly of calcium carbonate, limestones are divided into the weathered marine shell, white soft earthy limestone, sugar calcite and ...
  • Unknown author (United Nations Industrial Development Organization, 1979-01)
    Generally, foaming agents are the substances forming pores or cells in the material. Among them, chemical foaming agents are the compounds which decopose with the generation of gases when heated within a fixed range ...
  • Unknown author (United Nations Industrial Development Organization, 1979-01)
    Naphtha boils in the gasoline boiling range ie C5-220oC. A steam to hydrocarbon weight ratio used for cracking naphtha is about 0.5:1. Reaction is performed at a coil outlet temperature of 850'C. Furnace design varies ...
  • Unknown author (United Nations Industrial Development Organization, 1979-01)
    A stream containing 0.3:1 ratio of steam to hydrocarbon is heated to 9000C in a vertical tubular furnace Optimum yield pattern is obtained in less than 0.5 seconds. The reaction is halted by lowering the temperature in ...
  • Unknown author (United Nations Industrial Development Organization, 1979-01)
    Atmospheric gas oil boils in the range of 200-4000C. A dilution steam to hydrocarbon weight ratio of 0.8-1.0 is employed to give the appropriate hydrocarbon partial pressure at furnace cracking conditions. Gas oil ...
  • Unknown author (United Nations Industrial Development Organization, 1979-01)
    Ethane vapour brought from outside battery limits is heated in stages and mixed with dilution steam, it therefore enters the convection section of the cracking furnaces where it is further heated. On leaving the ...
  • Unknown author (United Nations Industrial Development Organization, 1979-01)
    Dry benzene, a catalyst slurry (of fresh aluminum chloride and ethyl benzene) , and ethylene are charged to the alkylation reactor together with recycle polyethyl benzenes an a small quantity of ethyl chloride (catalyst ...
  • Ethanol 
    Unknown author (United Nations Industrial Development Organization, 1979-01)
    The direct hydration process involves the catalytic addition of water to ethylene. Phosphoric acid is commonly used as the catalyst. The reaction is exothermic operating at about 3000C and 69 bar. Unconverted gases ...
  • Unknown author (United Nations Industrial Development Organization, 1979-01)
    This process also called Dynamit-Witten-Nobel process involves the oxidation of para-xylene in an oxidation reactor maintained at 15 bar and 190oC. The oxidation catalyst used may be a 0.1-0.5 percent cobaltous-manganese salt ...
  • Unknown author (United Nations Industrial Development Organization, 1979-01)
    Benzene and hydrogen-rich gas are fed to a liquid-phase reactor in which raney nickel catalyst is maintained in uniform dispersion at a temperature below 2500C and a pressure above 3 bar. Overheads are sent to a ...
  • Cumene 
    Unknown author (United Nations Industrial Development Organization, 1979-01)
    Fresh chemical grade propylene is combined with benzene which is maintained at a high recycle rate to prevent formation of dealkylated and polymer products. Solid phosphoric acid catalyst is non-corrosive and the ...
  • Unknown author (United Nations Industrial Development Organization, 1979-01)
    Salt is dissolved in fresh and recycled water and sent to brine treatment for calcium and magnesium removal. The brine enters the electrolytic cells for electrolysis by low voltage direct current, produced by transforming ...
  • Unknown author (United Nations Industrial Development Organization, 1979-01)
    Cyclohexanone (ONE) is first produced via oxidation of cyclohexane by air at 16S'C and 10.7 bar. Yield of ONE is 81 mole percent. A hydroxylamine solution is then contacted with the ONE to produce the cyclohexanone ...
  • Unknown author (United Nations Industrial Development Organization, 1979-01)
    Reformate, consisting of chiefly benzene, toluene and xylenes (BTX) is prefractionated and fed to the extractor, where it is contacted against a falling stream of sulfolane solvent. Undissolved hydrocarbons pass out ...
  • Aniline 
    Unknown author (United Nations Industrial Development Organization, 1979-01)
    This process consists of separate nitrobenzene and aniline production sections. Primarily 96 and 98 percent sulphuric and nitric acids respectively are blended and charged to the last of three nitrators operating at ...
  • Unknown author (United Nations Industrial Development Organization, 1979-01)
    The capital cost of a given plant is divided into that of the production unit proper (battery limits capital cost - BLCC) and that of the off-unit facilities (offsites capital cost) required to support the production ...
  • Unknown author (United Nations Industrial Development Organization, 1979-01)
    Long-chain alcohols are valuable raw materials in the detergent, textile and leather industries. Total synthesis from olefins is highly capital intensive, and feasible only when undertaken Ln large petrochemical ...

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