Dichlorethan

Guichon fertigt Sonderarmaturen zur Herstellung von Dichlorethan

Monokeilscheiber

FAQ
Monokeilschieber
Typ : 202N

DN 300 PN 16
– Hydraulischer Antrieb
Monokeilschieber 
Typ : 202N
Schieber mit parallelen Sitzen
Typ : 706

DN 25 bis 400 PN 16 bis 100
– geschweisste Ausführung
Edelstahl, Duplexstahl, Nickellegierungen und Sonderlegierungen
Schieber mit parallelen Sitzen  
Typ : 706

Herstellung

  • Materialen C-Stahl (CS), Edelstahl (SS), Duplex & Super Duplex, Titan (Ti), Zirkonium (Zr), Uranus® B6, Tantal (Ta), Nickel (Ni), Hastelloy®, Monel
  • Konstruktion Schweisstechnik, Gusstechnik, Aus dem Vollen (Monoblock)

Verwendung

  • Betriebsbedingungen Hochdruck, Hochtemperatur, Tieftemperatur, Abrasion, Korrosion, Hochviskosität, Vakuum, Langlebigkeit, Geräuscharmut, Totraumfreiheit
  • Medien Flüssigkeiten, Flüssigkeiten mit festen Bestandteilen, Gas, Pulver und pulverartige Medien, Viskose und hochviskose Medien

FAQ - Dichloroethan (Äthylendichlorid)

Dichloroethan (Äthylendichlorid) – Anwendungen von Dichloroethan :

– manufacture of ethylenediamine, ethylene glycol, polyvinyl chloride, nylon, rayon, various plastics
– solvent for fats, oils, waxes, resins, rubber, and for the extraction of spices
– fumigation of grains (cereals), orchards, …
– manufacture of paints, varnishes, cleaning, soap, cleaners, …

Posted in: FAQ - Dichloroethan (Äthylendichlorid)

Dichloroethan (Äthylendichlorid) – Herstellungsprozess von Dichlorethan :

1,2-dichloroethane,commonly known by its old name of ethylene dichloride (EDC), is
mainly used to produce vinyl chloride monomer (VCM) the major precursor for PVC production

EDC is made by the direct chlorination or oxychlorination of ethylene. Most EDC plants are integrated with VCM plants. The VCM process generates considerable quantities of hydrogen chloride (HCl), which is then recycled in the oxychlorination process to generate more EDC. By operating both the oxychlorination and the direct chlorination pathway at the same time, the overall process eliminates the problem of hydrogen chloride disposal. This technology (often known as «balanced process») is employed in the majority of the developed regions (see figure 1 for this process).

Figure 1. Illustration of the «balanced process» of an EDC plant, using both an
oxychlorination reactor and a direct chlorination reactor.

Direct chlorination is performed in the liquid phase where liquid chlorine and pure ethylene are reacted in the presence of ferric chloride. The reaction can be carried out at either low (20-70°C) or high (100-150°C) temperatures.

The low temperature process has the advantage of low by-product formation but requires more energy to recover the EDC. The high temperature process utilises the heat of reaction in the distillation of the EDC , leading to considerable energy savings.

In the oxychlorination process, pure ethylene and hydrogen chloride, mixed with
oxygen, are reacted at 200-300°C and 4-6 bar in the presence of a catalyst, usually cupric chloride. The reaction takes place in either a fixed bed or fluid bed reactor, the latter being preferred as it is easier to control the temperature.
Some recent development in the choice of  the catalyst have been reported to produce EDC of high quality which eliminates the need for distillation.

Posted in: FAQ - Dichloroethan (Äthylendichlorid)

Dichloroethan (Äthylendichlorid) – Empfohlene Ventile :

The valves present in this process must resist corrosion.

Posted in: FAQ - Dichloroethan (Äthylendichlorid)