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Liquid sulfur terminal

There is a continuing trend towards the use of liquid sulfur tank ships in international trade and the installation of liquid sulfur terminal facilities at points of consumption. This was being brought about because of environmental problems associated with the storage and shipment of dry bulk elemental sulfur with its associated dust problems, and the preference of consumers for the dehvery of hquid sulfur... [Pg.131]

Siarkopol Gdansk - opened a liquid sulfur terminal at Gdansk in 1971 -storage and transfer of sulfur from land to ships. [Pg.137]

In the earliest days of the industry, liquid sulfur was allowed to solidify into blocks and was then dug out by hand or mechanical shovel, or blown apart by dynamite. The sulfur chimks are friable, forming dust easily. The dust from broken sulfur was more than just a nuisance, as it posed a dust-explosion hazard. Broken sulfur shipments largely disappeared after liquid shipments took over after World War II. However, Alberta was too far from oeean ports to justify liqirid sirl-fur movements overseas. While Canada ships over one million tonnes of liquid sulfur by rail car into the U.S. every year, it has never shipped liquid sulfur by vessel. A major project was undertaken to develop such a mode of transportation in the late 1990 s. The Sulfur Corporation of Canada began construction of a liquid sulfur terminal at Prince Rupert, BC, in 1999, but the company ran out of cash in July 2002, and was forced to abandon its project. In 2010, the project was looked into again by ICEC Terminals. [Pg.154]

Liquid sulfur terminals were opened across Western Europe Rotterdam (Sulexco, SNPA Siarkopol), Botlek, Antwerp (APSA Sulexco), Rouen (SNPA), Immingham (SNPA, APSA), Teeside, Runcorn, and Workington in the U.K., and Seaport Brake (NEAG) in Germany. [Pg.163]

A number of examples have been studied in recent years, including liquid sulfur [1-3,8] and selenium [4], poly(o -methylstyrene) [5-7], polymer-like micelles [9,11], and protein filaments [12]. Besides their importance for applications, EP pose a number of basic questions concerning phase transformations, conformational and relaxational properties, dynamics, etc. which distinguish them from conventional dead polymers in which the reaction of polymerization has been terminated. EP motivate intensive research activity in this field at present. [Pg.510]

Mexican sulfur was e5q)orted from the port of Coatzocoalcos, near Vera Cmz. APSA had set up sulfur terminals in Tampa (1960) and Immingham, in England. In 1961, the liquid sulfur vessel Etude (ex. Antelope Hills), later replaced by H.H. Jaquet (to U.S. named after Harold Jaquet, the vice-president of operations for APSA), entered the fleet. Other early vessels were the Pochteca (ex. Atlantic Refiner) and the Harry C. Webb, which was later rechristened the Otapan (to Europe). Mexican shipments to Europe started in 1965. In October 1989, Pemex launched the Teoatl. These vessels are now out of service, and Pemex is chartering vessels from Polsteam. [Pg.135]

All acetylenes with a terminal triple bond are instantaneously converted into the alkali acetylides by alkali amides in liquid ammonia. For many alkylations with primary alkyl halides liquid ammonia is the solvent of choice and the functionalization with oxirane can also be carried out in it with good results. Reactions of ROOM with sulfenyladng agents (R SSR1, R SON, R SSC R ) or elemental sulfur, selenium or tellurium are mostly very successful in ammonia, the same holds for the preparation of ROC1 from RC=CM and iodine. The results of couplings with carbonyl compounds are very variable. [Pg.20]

Two of the more recently developed polysulfide polymers are the mercaptan-terminated polyoxypropylene urethane polymer and the polythioether polymer. The urethane-backbone-based polymer is used in many sealant formulations for insulating glass applications. The thioether backbone contains sulfur, but no S—S bonds, which are the weakest part of the conventional polysulfide polymer. This polymer improves the thermal stability and reduces the gas—liquid permeability. [Pg.312]

The principal features of elemental sulfur in the displayed T, P range are the usual liquid and vapor phases and two solid forms, a-sulfur ( red sulfur, of orthorhombic crystalline form) and /3-sulfur ( yellow sulfur, monoclinic needle-like crystals), both of which are available as common stockroom species. The stable phase ranges for each elemental form are shown by the solid lines in Fig. 7.5. The liquid-vapor coexistence line terminates in a critical point at 1041°C, and will not be discussed further. [Pg.229]

Sulfur and Chlorine Pipelines. Underground sulfur is melted by superheated water and then piped as liquid to the surface with compressed air. At the surface, molten sulfur is transported by heated pipeline to a storage or shipping terminal. One such pipeline, located under 15 m of water in the Gulf of Mexico, is insulated and surrounded by steel casing to which are strapped two 130-mm dia pipelines that carry return water from the deposit. The superheated water is carried from shore to the deposit in a 63.5-mm dia pipe inside the pipeline that carries the molten sulfur (21). [Pg.47]

Material Fabrication and Manufacturing Processes The lead-add battery is comprised of three primary components the element, the container, and the electrolyte. The element consists of positive and negative plates connected in parallel and electrically insulating separators between them. The container is the package which holds the clcctrochcmically active ingredients and houses the external connections or terminals of the batteiv. The electrolyte, which is the liquid active material and ionic conductor, is an aqueous solution of sulfuric acid (see Fig. 1). [Pg.182]

Amocat 1A was tested in an aging run for the hydroprocessing of 50% W. Kentucky SCT SRC. The run was made at constant conditions (2000 psig, 775°F, 0.5 LHSV) and was smoothly operated for 15 days. The run was then terminated due to incipient plugging in the reactor. The results are shown in Figure 10, where sulfur content in the liquid products has been plotted vs. days-on-stream. During this first four days the temperature was varied to obtain an activation energy estimation, and these data have been omitted. [Pg.189]

Poly sulfide compounds that are compatible with epoxy resins are liquid elastomers at room temperature. The most significant commercial resin of this type is LP-3 from Toray. The predominant product is a mercaptan-terminated liquid polymer (LP) that contains approximately 37% bound sulfur (see Fig. 7.2). It is the high concentration of sulfur linkages that provides these products with their unique chemical properties. A sulfur odor is noticeable during processing, making ventilation important. [Pg.130]

Carefully pour or spoon the mixture, in a single pile, on the incendiary. Prepare the mixture for ignition with eitiier l usc Cord (0101) or Improvised String Fuse (0102) in the normal manner. The fuse cord should terminate near the center of the igniter mixture. Concentrated Sulfuric Acid (0103) and Water (0104) can be used as initiators but are generally less convenient. Ignition takes place almost immediately on contact with the acid or water. These liquid initiators are convenient for use Mith specific delay mechanisms found in chapter 5. [Pg.287]


See other pages where Liquid sulfur terminal is mentioned: [Pg.5]    [Pg.130]    [Pg.166]    [Pg.5]    [Pg.130]    [Pg.166]    [Pg.15]    [Pg.1158]    [Pg.176]    [Pg.143]    [Pg.8]    [Pg.39]    [Pg.130]    [Pg.167]    [Pg.88]    [Pg.2373]    [Pg.84]    [Pg.17]    [Pg.110]    [Pg.221]    [Pg.25]    [Pg.337]    [Pg.299]    [Pg.541]    [Pg.223]    [Pg.392]    [Pg.2128]    [Pg.832]    [Pg.166]    [Pg.421]    [Pg.260]    [Pg.107]    [Pg.147]    [Pg.2377]   
See also in sourсe #XX -- [ Pg.154 ]




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