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(+-)-2-Butanol → Bis(2-butyl) ether

HRID 1263372
Notizen
Druckvorschau

Reaktionsgleichung

Reaktionsgleichung von HRID 1263372
[CH3:1][CH2:2][CH2:3][CH3:4].C=CCC.[CH:9]([OH:13])([CH2:11][CH3:12])[CH3:10]>O>[CH:2]([O:13][CH:9]([CH2:11][CH3:12])[CH3:10])([CH2:3][CH3:4])[CH3:1]
KomponentenVersuchsvorschriftAufarbeitungQuellen und NachweiseNotizen zur Reaktion

Komponenten

4

Edukt 2

HCID 6568(+-)-2-ButanolHCID 53438526Butane--but-1-ene (1/1)

Produkt 1

HCID 23294Bis(2-butyl) ether

Reagenzien, Katalysatoren, Lösungsmittel 1

HCID 962WaterLösungsmittel

Versuchsvorschrift

The procedure described in comparison Example 1 was altered so that by use of an additional dosing pump 54 kgs of the process water (total amount 204 kgs) were charged to the n-butane/n-butene mixture (feedgas and recycle gas=3,000 kgs/h) and transferred to the evaporator. Employing the same conditions as in comparison Example 1 (155° C. to 160° C., 70 bar) a temperature of 155° C. to 162° C. could be maintained in the reactor without additional heating or cooling. In the sump of a column, average amounts of 201.3 kgs (2,720 moles) of sec. butyl alcohol and 2.1 kgs (16.2 moles) of di-sec. butyl ether were obtained per hour as an approx. 99% purity crude alcohol. 101.5 kgs of n-butene and 46.4 kgs of n-butane were obtained as an approx. 59% mixture.

Aufarbeitung

  1. customtransferred to the evaporator
  2. customas in comparison Example 1 (155° C. to 160° C., 70 bar)
  3. customa temperature of 155° C. to 162° C.
  4. temperaturecould be maintained in the reactor
  5. temperaturewithout additional heating
  6. temperaturecooling

Quellen und Nachweise

ORD-Eintrag
ord-d869dcf705a5440ba4c1877936079b88
Quelldatensatz
uspto-grants-1984_06
DOI
10.6084/m9.figshare.5104873.v1
Patentnummer
US04456776

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