← Back to Patent Explorer
US3336104A Expired / Lapsed US ⏱️ 0.0 years remaining

Continuous recycle heating process for the production of soda ash and alkali metal phosphates

Assignee: Intermountain Research and Development Corp
•
Filing: 1963-12-13
•
Granted: 1967-08-15
•
Expires: 1983-12-13
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

No abstract record available.

Inventors

  • 👤 Miller Warren Standish

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-25 05:07
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/02; B; B01; B01J; B01J6/00; B01J6/001; C01; C01B; C01B25/00; C01B25/16; C01B25/26; C01B25/30; C01B25/308; C01B25/38; C01B25/39; C01B25/395; C01D; C01D7/00; C01D7/12; C01D7/123; C01D7/35

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 135 words
A CONTINUOUS HEAT TRANSFER PROCESS WHICH COMPRISES CONTACTING RECYCLE SODA ASH WITH A HEATING GAS HEATED ABOVE THE TEMPERATURE NECESSARY TO HEAT THE FEED MATERIAL TO THE DESIRED PRODUCT TEMPERATURE IN A CONCURRENT FLOW WHEREBY THE RECYCLE SODA ASH IS SUPERHEADTED AND THE HEATING GAS IS TEMPERED, CONTACTING THE FEED MATERIAL SELECTED FROM THE GROUP CONSISTING OF SODIUM SESQUICARBONATE, SODIUM CARBONATE MONOHYDRATE AND MOIST ANHYDROUS SODAT ASH TO BE HEATED WITH THE TEMPERED HEATING GAS IN A CONCURRENT FLOW AND MIXING THE SUPERHEATED RECYCLE SODA ASH WITH THE FEED MATERIAL, WHEREBY THE FEED MATERIAL IS HEATED BY TRANSFER OF HEAT FROM THE HEATING GAS AND THE SUPERHEATED RECYCLE SODA ASH TO THE DESIRED SODA ASH TEMPERATURE, RECOVERING PART OF THE HEAT MATERIAL AND RECYCLING THE REMAINDER OF THE MATERIAL TO CONTACT WITH THE HEATING GAS.
Claim 2
Dependent Claim 135 words
A CONTINUOUS HEAT TRANSFER PROCESS WHICH COMPRISES CONTACTING RECYCLE SODA ASH WITH A HEATING GAS HEATED ABOVE THE TEMPERATURE NECESSARY TO HEAT THE FEED MATERIAL TO THE DESIRED PRODUCT TEMPERATURE IN A CONCURRENT FLOW WHEREBY THE RECYCLE SODA ASH IS SUPERHEADTED AND THE HEATING GAS IS TEMPERED, CONTACTING THE FEED MATERIAL SELECTED FROM THE GROUP CONSISTING OF SODIUM SESQUICARBONATE, SODIUM CARBONATE MONOHYDRATE AND MOIST ANHYDROUS SODAT ASH TO BE HEATED WITH THE TEMPERED HEATING GAS IN A CONCURRENT FLOW AND MIXING THE SUPERHEATED RECYCLE SODA ASH WITH THE FEED MATERIAL, WHEREBY THE FEED MATERIAL IS HEATED BY TRANSFER OF HEAT FROM THE HEATING GAS AND THE SUPERHEATED RECYCLE SODA ASH TO THE DESIRED SODA ASH TEMPERATURE, RECOVERING PART OF THE HEAT MATERIAL AND RECYCLING THE REMAINDER OF THE MATERIAL TO CONTACT WITH THE HEATING GAS.
Claim 3
Independent Claim 114 words
THE METHOD OF PRODUCING ALKALI METAL PHOSPHATE SALTS FROM ALKALI METAL PHOSPHATE SOLUTIONS, WHICH COMPRISES CONTACTING RECYCLE ALKALI METAL PHOSPHATE SALT WITH A HOT GAS, HEATED ABOVE THE TEMPERATURE REQUIRED TO CONVERT ALKALI METAL PHOSPHATE SOLUTIONS INTO SOLID SALTS WHEREBY THE RECYCLE ALKALI METAL PHOSPHATE SALT IS SUPERHEATED, CONTACTING THE ALKALI METAL PHOSPHATE SALT IS SUPERHEATED, CONTACTING THE ALKALI METAL PHOSPAHTE SOLUTION WITH THE SUPERHEATED RECYCLE CALT TO CONVERT THE ALKALI METAL PHOSPHATE SOLUTION INTO CRYSTALLINE SALT, CONTACTING THE CRYSTALLINE SALT WITH TEMPERED HEATING GAS TO DEHYDRATE THE SAID SALT, RECOVERING A PORTION OF THE CRYSTALLIZED SALT AND RECYCLING THE REMAINDER OF THE CRYSTALLINE ALKALI METAL SALT TO CONTACT WITH THE HOT HEATING GAS.
Claim 4
Independent Claim 114 words
THE METHOD OF PRODUCING ALKALI METAL PHOSPHATE SALTS FROM ALKALI METAL PHOSPHATE SOLUTIONS, WHICH COMPRISES CONTACTING RECYCLE ALKALI METAL PHOSPHATE SALT WITH A HOT GAS, HEATED ABOVE THE TEMPERATURE REQUIRED TO CONVERT ALKALI METAL PHOSPHATE SOLUTIONS INTO SOLID SALTS WHEREBY THE RECYCLE ALKALI METAL PHOSPHATE SALT IS SUPERHEATED, CONTACTING THE ALKALI METAL PHOSPHATE SALT IS SUPERHEATED, CONTACTING THE ALKALI METAL PHOSPAHTE SOLUTION WITH THE SUPERHEATED RECYCLE CALT TO CONVERT THE ALKALI METAL PHOSPHATE SOLUTION INTO CRYSTALLINE SALT, CONTACTING THE CRYSTALLINE SALT WITH TEMPERED HEATING GAS TO DEHYDRATE THE SAID SALT, RECOVERING A PORTION OF THE CRYSTALLIZED SALT AND RECYCLING THE REMAINDER OF THE CRYSTALLINE ALKALI METAL SALT TO CONTACT WITH THE HOT HEATING GAS.

References Cited (Backward Citations)

US1602819A Cited
US2034599A Cited
US2459414A Cited
US2582712A Cited
GB883202A Cited
US3049419A Cited
US3030180A Cited
US3057680A Cited
US3028215A Cited
US3189408A Cited
US3167494A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1970-08-14 1971-02-13 1971-08-15 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1974-08-14 1975-02-13 1975-08-15 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1978-08-14 1979-02-13 1979-08-15 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag