US1447954A - pelham manor - Google Patents
pelham manor Download PDFInfo
- Publication number
- US1447954A US1447954A US1447954DA US1447954A US 1447954 A US1447954 A US 1447954A US 1447954D A US1447954D A US 1447954DA US 1447954 A US1447954 A US 1447954A
- Authority
- US
- United States
- Prior art keywords
- oil
- distillate
- air
- fumes
- oxidizable
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 239000003921 oil Substances 0.000 description 34
- 235000019198 oils Nutrition 0.000 description 34
- 239000003517 fume Substances 0.000 description 12
- 238000001035 drying Methods 0.000 description 6
- 238000005188 flotation Methods 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 6
- 235000021388 linseed oil Nutrition 0.000 description 6
- 239000000944 linseed oil Substances 0.000 description 6
- 239000007788 liquid Substances 0.000 description 6
- 239000000463 material Substances 0.000 description 6
- 238000007605 air drying Methods 0.000 description 4
- 238000009835 boiling Methods 0.000 description 4
- 229910052500 inorganic mineral Inorganic materials 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 150000002739 metals Chemical class 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000011707 mineral Substances 0.000 description 4
- 239000003973 paint Substances 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 150000003568 thioethers Chemical class 0.000 description 4
- 239000002966 varnish Substances 0.000 description 4
- 235000015112 vegetable and seed oil Nutrition 0.000 description 4
- 239000008158 vegetable oil Substances 0.000 description 4
- 240000007842 Glycine max Species 0.000 description 2
- 235000010469 Glycine max Nutrition 0.000 description 2
- 235000010678 Paulownia tomentosa Nutrition 0.000 description 2
- 240000002834 Paulownia tomentosa Species 0.000 description 2
- 240000008042 Zea mays Species 0.000 description 2
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 235000005822 corn Nutrition 0.000 description 2
- 235000005824 corn Nutrition 0.000 description 2
- 239000010685 fatty oil Substances 0.000 description 2
- 239000006260 foam Substances 0.000 description 2
- -1 gums Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000001473 noxious Effects 0.000 description 2
- 239000007800 oxidant agent Substances 0.000 description 2
- 235000020030 perry Nutrition 0.000 description 2
- 239000000049 pigment Substances 0.000 description 2
- 238000005057 refrigeration Methods 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000002383 tung oil Substances 0.000 description 2
- 239000000341 volatile oil Substances 0.000 description 2
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09F—NATURAL RESINS; FRENCH POLISH; DRYING-OILS; DRIERS (SICCATIVES); TURPENTINE
- C09F7/00—Chemical modification of drying oils
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L91/00—Compositions of oils, fats or waxes; Compositions of derivatives thereof
- C08L91/005—Drying oils
Definitions
- This distillate is an oxidizable oil which is well adapted for use in the flotation process of recovering metals and for other purposes.
- the fumes being driven off from. the heating kettles are collected in fume-collectors and passed. through a series of condensers. densers may consist of tubes which are cooled by means of air, cooling liquids, refrigeration materials, or a combination of two or more of these.
- the distillate from the drying oils is oxidizable'and air maybe led into thecondensing tubesto oxidize the fumes while they are in the hot state so that the distillate will be oxidized to a grea er or less extent whenit is condensing.
- a greater or smaller amount of the distillate will be completely oxidized when it is recovered from the corn
- the con-' o xIDIzABLE om The con-' o xIDIzABLE om.
- the improved oil distillate will condense at temperatures below 75 F., and a relatively larger proportion of the fume will be condensed as the temperatures are carried down to 0 F. and lower.
- the distillate which has been condensed at temperatures below 75 F. down to 32 F. is a comparatively stable liquid and below temperatures of 32 F. the distillate isa semi-solidv- The maximum boiling point of the distillate is not materially above 75 F.
- the stable liquid distillateat tempera tures between 35 and F. is an oxidizable vegetable oil which may be used with oer-- tain kinds of minerals in the flotation separation process to produce a light foam or froth for carrying the metallic particles and sulfides in the minerals.
- the agitation of the oil distillate particularly by means of air as well as by mechanical agitation, serves to break up the oil-to form a comparatively light and thick froth which is particularly adapted for carrying certain types of metallic and. sulfide particles.
- the oil distillate' which is called linorienated oil, may be oxidized "by means of air or other oxidizing agents so that it can be converted into a semi-solid or solid condition int? been thHSJlQSCIllOQ a What is Claimed as i new is: v
- An oxidizable oil comprising a dis-, tillate of an air-drying fatty oil which has a condensing point below 75 F. and congeals to a semisolid condition at a temperature below 32 F.
- An oxidizable oil comprising a dis tillate of linseed oil which has a condensing point below 7 5 F,
- A21 miidizable comprising a partially axidimd di "r'llate of am air drying fatizy oil.
- A21 omdizabie oil comprising pma tbimlly @zidized disiifiat/a 01 linseed oil.
Description
' soya bean oil are bo led and heated with Patented Mar. 6, ldfid.
entrain snares earanr FAUL WENTWORTH WEB$TER, 0F PELHAM MANOR, NEW YORK, it WEBSTER INCORPORATED, 011 ELIZABETH, NEW JERSEY,
' NEW JERSEY.
No Drawing.
a vegetable oil which is particularly adapted as a'froth-producing material in the flota tion process of recovering metals.
In the manufacture of paints and varnishes, various types of drying oils such as linseed oil, tung 011, china wood oil and resins, gums, pigments and other materials to form the finished products. In these heating operations, the fumes are driven oil from the boiling and heating kettles which'consist of vapors and volatile oils and some com paratively permanent gases- These fumes heretofore have been exhausted through stacks and were a great source of annoyance to the community around the paint and varnish factory because they were very noxious and gave a disagreeable deposit. Examiner tion of these fumes has'shown that they contain an oil distillate formed-from the drying oils which may be se arated from the other constituents of the umes by condensation. This distillate is an oxidizable oil which is well adapted for use in the flotation process of recovering metals and for other purposes. To recover the oxidizableoil, the fumes being driven off from. the heating kettles are collected in fume-collectors and passed. through a series of condensers. densers may consist of tubes which are cooled by means of air, cooling liquids, refrigeration materials, or a combination of two or more of these. The distillate from the drying oils is oxidizable'and air maybe led into thecondensing tubesto oxidize the fumes while they are in the hot state so that the distillate will be oxidized to a grea er or less extent whenit is condensing. In accordance with the amount of airadmitted to the condensing tubes, a greater or smaller amount of the distillate. will be completely oxidized when it is recovered from the corn The con-' o xIDIzABLE om.
Application filed October 3, 1918. Serial Ti le. 258,738.
tail description of the method of and apparatus for recovering the improved distillate; The improved oil distillate will condense at temperatures below 75 F., and a relatively larger proportion of the fume will be condensed as the temperatures are carried down to 0 F. and lower. The distillate which has been condensed at temperatures below 75 F. down to 32 F. is a comparatively stable liquid and below temperatures of 32 F. the distillate isa semi-solidv- The maximum boiling point of the distillate is not materially above 75 F.
The stable liquid distillateat tempera tures between 35 and F. is an oxidizable vegetable oil which may be used with oer-- tain kinds of minerals in the flotation separation process to produce a light foam or froth for carrying the metallic particles and sulfides in the minerals. The agitation of the oil distillate particularly by means of air as well as by mechanical agitation, serves to break up the oil-to form a comparatively light and thick froth which is particularly adapted for carrying certain types of metallic and. sulfide particles.
The oil distillate'which is called linorienated oil, may be oxidized "by means of air or other oxidizing agents so that it can be converted into a semi-solid or solid condition int? been thHSJlQSCIllOQ a What is Claimed as i new is: v
1. An oxidizable oil comprisinga dis-, tillate of an air-drying fatty oil which has a condensing point below 75 F. and congeals to a semisolid condition at a temperature below 32 F.
2. An oxidizable oil comprising a dis tillate of linseed oil which has a condensing point below 7 5 F,
3. A21 miidizable comprising a partially axidimd di "r'llate of am air drying fatizy oil. A21 omdizabie oil comprising pma tbimlly @zidized disiifiat/a 01 linseed oil.
5.- An ozzidimbie oil comprisin a mixfiure 50;? oxidized and mon-axidized dlsfiiliams of Kins sad oil. 1
". An oxidimbfie 0H inflame of an mil whic'l cnmpxising dishave hereunto set my hand.
PAUL WTVVQRTH WEB Witnesses S. PERRY, V. A, BAYNTON.
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1447954A true US1447954A (en) | 1923-03-06 |
Family
ID=3403744
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US1447954D Expired - Lifetime US1447954A (en) | pelham manor |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1447954A (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20020121328A1 (en) * | 1998-09-17 | 2002-09-05 | Kurth Thomas M. | Method of producing a bio-based carpet material |
| US6465569B1 (en) | 1998-09-17 | 2002-10-15 | Urethane Soy Systems Co. | Plastic material |
| US20040209971A1 (en) * | 1998-09-17 | 2004-10-21 | Urethane Soy Systems Company | Oxylated vegetable-based polyol having increased functionality and urethane materials formed using the polyol |
| US20050131092A1 (en) * | 1998-09-17 | 2005-06-16 | Urethane Soy Systems Company | Vegetable oil-based coating and method for application |
| US6979477B2 (en) | 2000-09-06 | 2005-12-27 | Urethane Soy Systems Company | Vegetable oil-based coating and method for application |
| US7063877B2 (en) | 1998-09-17 | 2006-06-20 | Urethane Soy Systems Company, Inc. | Bio-based carpet material |
| US7989647B2 (en) | 2005-03-03 | 2011-08-02 | South Dakota Soybean Processors, Llc | Polyols derived from a vegetable oil using an oxidation process |
| US8333905B1 (en) | 2000-09-06 | 2012-12-18 | Tandem Polymers, Inc. | Transesterified polyol having selectable and increased functionality and urethane material products formed using the polyol |
-
0
- US US1447954D patent/US1447954A/en not_active Expired - Lifetime
Cited By (27)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20050182228A1 (en) * | 1998-09-17 | 2005-08-18 | Kurth Thomas M. | Plastic material |
| US7595094B2 (en) | 1998-09-17 | 2009-09-29 | Urethane Soy Systems, Co. | Vegetable oil-based coating and method for application |
| US20020121328A1 (en) * | 1998-09-17 | 2002-09-05 | Kurth Thomas M. | Method of producing a bio-based carpet material |
| US20040034163A1 (en) * | 1998-09-17 | 2004-02-19 | Kurth Thomas M. | Plastic material |
| US20040102596A1 (en) * | 1998-09-17 | 2004-05-27 | Kurth Thomas M. | Plastic material |
| US20040209971A1 (en) * | 1998-09-17 | 2004-10-21 | Urethane Soy Systems Company | Oxylated vegetable-based polyol having increased functionality and urethane materials formed using the polyol |
| US6864296B2 (en) | 1998-09-17 | 2005-03-08 | Urethane Soy Systems Company | Plastic material |
| US6867239B2 (en) | 1998-09-17 | 2005-03-15 | Urethane Soy Systems Company | Plastic material |
| US6881763B2 (en) | 1998-09-17 | 2005-04-19 | Urethane Soy Systems Company | Plastic material |
| US20050121134A9 (en) * | 1998-09-17 | 2005-06-09 | Kurth Thomas M. | Method of producing a bio-based carpet material |
| US20050131092A1 (en) * | 1998-09-17 | 2005-06-16 | Urethane Soy Systems Company | Vegetable oil-based coating and method for application |
| US20050131093A1 (en) * | 1998-09-17 | 2005-06-16 | Urethane Soy Systems Company | Vegetable oil-based coating and method for application |
| US6624244B2 (en) | 1998-09-17 | 2003-09-23 | Urethane Soy Systems Company | Plastic material |
| US6962636B2 (en) | 1998-09-17 | 2005-11-08 | Urethane Soy Systems Company, Inc. | Method of producing a bio-based carpet material |
| US8575226B2 (en) | 1998-09-17 | 2013-11-05 | Rhino Linings Corporation | Vegetable oil-based coating and method for application |
| US8449946B2 (en) | 1998-09-17 | 2013-05-28 | Tandem Polymers, Inc. | Vegetable oil-based coating and method for application |
| US7063877B2 (en) | 1998-09-17 | 2006-06-20 | Urethane Soy Systems Company, Inc. | Bio-based carpet material |
| US7084230B2 (en) | 1998-09-17 | 2006-08-01 | Urethane Soy Systems Company, Inc. | Oxylated vegetable-based polyol having increased functionality and urethane materials formed using the polyol |
| US7537665B2 (en) | 1998-09-17 | 2009-05-26 | Urethane Soy Systems Company, Inc. | Method for producing a bio-based carpet material |
| US6465569B1 (en) | 1998-09-17 | 2002-10-15 | Urethane Soy Systems Co. | Plastic material |
| US20100022675A1 (en) * | 1998-09-17 | 2010-01-28 | Kurth Thomas M | Vegetable oil-based coating and method for application |
| US20050260351A1 (en) * | 1998-09-17 | 2005-11-24 | Urethane Soy Systems Company, Inc. | Method for producing a bio-based carpet material |
| US8062710B2 (en) | 1998-09-17 | 2011-11-22 | Urethane Soy Systems Company | Vegetable oil-based coating and method for application |
| US8333905B1 (en) | 2000-09-06 | 2012-12-18 | Tandem Polymers, Inc. | Transesterified polyol having selectable and increased functionality and urethane material products formed using the polyol |
| US6979477B2 (en) | 2000-09-06 | 2005-12-27 | Urethane Soy Systems Company | Vegetable oil-based coating and method for application |
| US7989647B2 (en) | 2005-03-03 | 2011-08-02 | South Dakota Soybean Processors, Llc | Polyols derived from a vegetable oil using an oxidation process |
| US9045581B2 (en) | 2005-03-03 | 2015-06-02 | Rhino Linings Corporation | Polyols derived from a vegetable oil using an oxidation process |
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