Patent US4083941A successfully refreshed from Google Patents.
← Back to Patent Explorer
US4083941A Expired / Lapsed US ⏱️ 0.0 years remaining

Purification of anhydrous hydrogen fluoride

Assignee: EIDP Inc
•
Filing: 1977-04-18
•
Granted: 1978-04-11
•
Expires: 1997-04-18
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract A process for preparing very high purity anhydrous hydrogen fluoride by contacting anhydrous hydrogen fluoride with at least 2.3% by weight of persulfuric acid based on the anhydrous hydrogen fluoride or at least 0.7% by weight of hydrogen peroxide based on the anhydrous hydrogen fluoride at ambient temperature and either at least 0.6% by weight of methanol based on the anhydrous hydrogen fluoride or at least one mole of sulfuric acid per mole of hydrogen peroxide at a temperature of from 0 DEG to 75 DEG C and distilling the resulting mixture to recover very high purity anhydrous hydrogen fluoride.

Inventors

  • 👤 Madhusudan Dattatraya Jayawant
  • 👤 Geoffrey Walsh Meadows

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 18:46
CPC Classifications
C; C01; C01B; C01B7/00; C01B7/19; C01B7/191

Claims Analysis

Total Claims: 17
Claim 1
Independent Claim 134 words
A process for the preparation of pure anhydrous hydrogen fluoride with reduced arsenic and sulfite impurities consisting essentially of (1) contacting in equipment inert thereto anhydrous hydrogen fluoride having arsenic and sulfite impurities with (a) at least 2.3% by weight of H 2 SO 5 based on the anhydrous hydrogen fluoride or (b) at least 0.7% by weight based on the anhydrous hydrogen fluoride of hydrogen peroxide and either at least 0.6% by weight of methanol based on the anhydrous hydrogen fluoride or at least 1 mole of sulfuric acid per mole of hydrogen peroxide, at a temperature of from 0° to 75° C, (2) distilling the resulting mixture and (3) recovering a high purity anhydrous hydrogen fluoride with arsenic and sulfite impurities of 0.03 ppm or less and 3 ppm or less respectively.
Claim 2
Dependent Claim 134 words
A process for the preparation of pure anhydrous hydrogen fluoride with reduced arsenic and sulfite impurities consisting essentially of (1) contacting in equipment inert thereto anhydrous hydrogen fluoride having arsenic and sulfite impurities with (a) at least 2.3% by weight of H 2 SO 5 based on the anhydrous hydrogen fluoride or (b) at least 0.7% by weight based on the anhydrous hydrogen fluoride of hydrogen peroxide and either at least 0.6% by weight of methanol based on the anhydrous hydrogen fluoride or at least 1 mole of sulfuric acid per mole of hydrogen peroxide, at a temperature of from 0° to 75° C, (2) distilling the resulting mixture and (3) recovering a high purity anhydrous hydrogen fluoride with arsenic and sulfite impurities of 0.03 ppm or less and 3 ppm or less respectively.
Claim 3
Dependent Claim 13 words
The process of claim 1 wherein the temperature is 0° to 20° C.
Claim 4
Dependent Claim 14 words
The process of claim 1 wherein 0.7 to 1.5% of hydrogen peroxide is used.
Claim 5
Dependent Claim 13 words
The process of claim 1 wherein 0.6 to 2% of methanol is used.
Claim 6
Dependent Claim 15 words
The process of claim 1 wherein 1 to 5 moles of sulfuric acid is used.
Claim 7
Dependent Claim 10 words
The process of claim 1 wherein sulfuric acid is used.
Claim 8
Dependent Claim 15 words
The process of claim 6 wherein 1.5 to 5 moles of sulfuric acid is used.
Claim 9
Dependent Claim 12 words
The process of claim 1 wherein hydrogen peroxide and methanol are used.
Claim 10
Dependent Claim 20 words
The process of claim 8 wherein 0.7% to 1.5% of hydrogen peroxide and 0.6% to 2.0% of methanol is used.
Claim 11
Dependent Claim 14 words
The process of claim 9 wherein the temperature is from 0° to 20° C.
Claim 12
Dependent Claim 12 words
The process of claim 1 wherein H 2 SO 5 is used.
Claim 13
Dependent Claim 17 words
The process of claim 11 wherein 2.3% to to 5% of H 2 SO 5 is used.
Claim 14
Dependent Claim 14 words
The process of claim 12 wherein the temperature is from 0° to 20° C.
Claim 15
Dependent Claim 13 words
The process of claim 1 wherein hydrogen peroxide and sulfuric acid are used.
Claim 16
Dependent Claim 22 words
The process of claim 14 wherein 0.7% to 1.5% of hydrogen peroxide and 1 to 5 moles of sulfuric acid are used.
Claim 17
Dependent Claim 14 words
The process of claim 15 wherein the temperature is from 0° to 20° C.

References Cited (Backward Citations)

SU342831A1 Cited
US3166379A Cited
GB1174382A Cited
US3689370A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-04-10 1981-10-10 1982-04-11 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-04-10 1985-10-10 1986-04-11 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-04-10 1989-10-10 1990-04-11 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag