US4443620A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Production of epoxy compounds from olefinic compounds
Assignee: Lummus Technology LLC
•
Filing: 1979-05-03
•
Granted: 1984-04-17
•
Expires: 1999-05-03
Abstract
Abstract Chlorine and tertiary alkanol dissolved in an inert organic solvent are reacted with calcium oxide in aqueous calcium chloride to produce tertiary alkyl hypochlorite which is recovered in the organic solvent and reacted with water and olefinically unsaturated compound to produce chlorohydrin and tertiary alkanol. Chlorohydrin and tertiary alkanol recovered in the organic solvent are contacted with calcium oxide in aqueous calcium chloride to produce the epoxy compound, and tertiary alkanol recovered in the organic solvent is recycled to hypochlorite production. Calcium chloride produced as by-product in the hypochlorite production and saponification is recovered as an aqueous solution having a calcium chloride concentration of at least 25 wt. % to provide calcium chloride in a usable form.
Inventors
- 👤 Abraham P. Gelbein
- 👤 Arthur S. Nislick
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-02 07:08
CPC Classifications
C; C07; C07D; C07D301/00; C07D301/02; C07D301/24; C07D301/26
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
242 words
A process for converting an olefinically unsaturated compound to the corresponding epoxy compound, comprising: contacting a tertiary alkanol in an inert organic solvent, chlorine and calcium oxide in aqueous calcium chloride having a combined concentration of calcium oxide and calcium chloride equivalent to at least 25 weight percent expressed as calcium chloride to produce tertiary alkyl hypochlorite and aqueous calcium chloride; recovering tertiary alkyl hypochlorite in the inert organic solvent; contacting tertiary alkyl hypochlorite in the inert organic solvent, water and an olefinically unsaturated compound to produce the corresponding chlorohydrin and a tertiary alkanol; recovering tertiary alkanol and chlorohydrin in the inert organic solvent; contacting chlorohydrin and tertiary alkanol in the inert organic solvent and calcium oxide in an aqueous solution of calcium chloride having a combined concentration of calcium oxide and calcium chloride equivalent to at least 25 weight percent expressed as calcium chloride to convert the chlorohydrin to the corresponding epoxy compound and produce aqueous calcium chloride; recovering said epoxy compound; recovering tertiary alkanol in the inert organic solvent; passing tertiary alkanol in the inert organic solvent to the hypochlorite production; recovering from said hypochlorite production and said epoxy compound production an aqueous solution of calcium chloride having a calcium chloride concentration of at least 25 weight percent; and combining calcium oxide with a portion of said recovered aqueous solution of calcium chloride for providing said calcium oxide in aqueous calcium chloride for the producing of hypochlorite and epoxy compound.
Claim 2
Dependent Claim
242 words
A process for converting an olefinically unsaturated compound to the corresponding epoxy compound, comprising: contacting a tertiary alkanol in an inert organic solvent, chlorine and calcium oxide in aqueous calcium chloride having a combined concentration of calcium oxide and calcium chloride equivalent to at least 25 weight percent expressed as calcium chloride to produce tertiary alkyl hypochlorite and aqueous calcium chloride; recovering tertiary alkyl hypochlorite in the inert organic solvent; contacting tertiary alkyl hypochlorite in the inert organic solvent, water and an olefinically unsaturated compound to produce the corresponding chlorohydrin and a tertiary alkanol; recovering tertiary alkanol and chlorohydrin in the inert organic solvent; contacting chlorohydrin and tertiary alkanol in the inert organic solvent and calcium oxide in an aqueous solution of calcium chloride having a combined concentration of calcium oxide and calcium chloride equivalent to at least 25 weight percent expressed as calcium chloride to convert the chlorohydrin to the corresponding epoxy compound and produce aqueous calcium chloride; recovering said epoxy compound; recovering tertiary alkanol in the inert organic solvent; passing tertiary alkanol in the inert organic solvent to the hypochlorite production; recovering from said hypochlorite production and said epoxy compound production an aqueous solution of calcium chloride having a calcium chloride concentration of at least 25 weight percent; and combining calcium oxide with a portion of said recovered aqueous solution of calcium chloride for providing said calcium oxide in aqueous calcium chloride for the producing of hypochlorite and epoxy compound.
Claim 3
Dependent Claim
38 words
The process of claim 1 wherein aqueous calcium chloride from the saponification includes some tertiary alkanol, said aqueous calcium chloride including tertiary alkanol being introduced into the hypochlorite production to convert the tertiary alkanol to tertiary alkyl hypochlorite.
Claim 4
Dependent Claim
12 words
The process of claim 2 wherein the tertiary alkanol is tertiary butanol.
Claim 5
Dependent Claim
21 words
The process of claim 3 wherein the olefinically unsaturated compound is selected from the group consisting of propylene and allyl chloride.
Claim 6
Dependent Claim
30 words
The process of claim 1 wherein the combined calcium oxide and calcium chloride concentration produces aqueous calcium chloride from the hypochlorite and epoxy compound production saturated as to calcium chloride.
Claim 7
Dependent Claim
26 words
The process of claim 1 wherein the combined concentration of calcium oxide and calcium chloride is from 30% to 45%, by weight, expressed as calcium chloride.
Claim 8
Dependent Claim
34 words
The process of claim 2 wherein a portion of the aqueous solution of calcium chloride recovered from the hypochlorite production is combined with calcium oxide for providing said calcium oxide in aqueous calcium chloride.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-04-17 | 1987-10-17 | 1988-04-17 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-04-17 | 1991-10-17 | 1992-04-17 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-04-17 | 1995-10-17 | 1996-04-17 | $7700.00 | Window Closed / Lapsed |