US2277342A - Process for the preparation of tung oil - Google Patents
Process for the preparation of tung oil Download PDFInfo
- Publication number
- US2277342A US2277342A US291564A US29156439A US2277342A US 2277342 A US2277342 A US 2277342A US 291564 A US291564 A US 291564A US 29156439 A US29156439 A US 29156439A US 2277342 A US2277342 A US 2277342A
- Authority
- US
- United States
- Prior art keywords
- oil
- solvent
- tung
- tung oil
- extracted
- 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
- 239000002383 tung oil Substances 0.000 title description 58
- 238000000034 method Methods 0.000 title description 16
- 238000002360 preparation method Methods 0.000 title description 4
- 239000003921 oil Substances 0.000 description 46
- 239000002904 solvent Substances 0.000 description 30
- 235000010678 Paulownia tomentosa Nutrition 0.000 description 24
- 240000002834 Paulownia tomentosa Species 0.000 description 24
- 235000012970 cakes Nutrition 0.000 description 22
- 239000007788 liquid Substances 0.000 description 20
- RTZKZFJDLAIYFH-UHFFFAOYSA-N diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 12
- 238000000605 extraction Methods 0.000 description 8
- PNDPGZBMCMUPRI-UHFFFAOYSA-N iodine Chemical compound II PNDPGZBMCMUPRI-UHFFFAOYSA-N 0.000 description 8
- 229910052740 iodine Inorganic materials 0.000 description 8
- 239000011630 iodine Substances 0.000 description 8
- 239000003208 petroleum Substances 0.000 description 8
- 239000012071 phase Substances 0.000 description 8
- 239000007787 solid Substances 0.000 description 8
- 238000009835 boiling Methods 0.000 description 6
- 239000000463 material Substances 0.000 description 6
- 238000007711 solidification Methods 0.000 description 6
- 238000003825 pressing Methods 0.000 description 4
- 239000003337 fertilizer Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000005325 percolation Methods 0.000 description 2
- 239000007790 solid phase Substances 0.000 description 2
- 238000000638 solvent extraction Methods 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 239000002966 varnish Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B1/00—Production of fats or fatty oils from raw materials
- C11B1/10—Production of fats or fatty oils from raw materials by extracting
Description
Patented Mar. 24, 1942 PROCESS FOR THE PREPARATION OF TUNG OIL Robert S. McKinney, Chevy Chase, and William Gordon Rose, College Park, lVId., and Andrew F. Freeman, Washington, D. C.
No Drawing. Application August 23, 1939, Serial No. 291,564
(Granted under the act of March 3, 1883, as amended April 30, 1928; 3700. G. 757) 1 Claim.
This application is made under the act of March 3, 1883, as amended by the act of April 30, 1928, and the invention herein described and claimed, if patented, may be manufactured and used by or for the Government of the United States of America for governmental purposes without the payment to use of any royalty there- We hereby dedicate the invention herein described to the free use of the People in the territory of the United States to take effect on the granting of a patent to us.
Our invention relates. to a new process for the production of a clear, liquid, solvent-extracted tung oil from tung kernels and from tung oil press cake.
The principal object of our invention is to produce a solvent-extracted tung oil, which will not change to the solid phase after it has been prepared. The solvent extraction of tung oil from the tung kernels and tung oil press cake, because of the economies which are clearly evident from the almost complete removal of the oil, has been considered a great improvement over the pressing methods. However, attempts to prepare a commercially usable, solvent-extracted tung oil have been unsuccessful because the solvent-extracted tung oil, while initially clear, soon forms a solid. Upon standing, this solid becomes insoluble and infusible and this material is no longer usable in the Varnish kettle. This solidified tung oil is, therefore, not acceptable to the tung oil trade.
We have invented a process by which solventextracted tung oil is prepared from tung oil press cake, and from tung kernels, the resulting oils being liquid at ordinary temperatures. These liquid extracted oils, therefore, are acceptable to the tung oil trade and our process, because of its greater yield of oil, in comparison to the present pressing process, and because it yields a valuable oil and a superior fertilizer from the tung oil press cake, is of value to the industry.
We have found that when the oil is extracted from tung kernels, and from tung oil press cake, by a suitable solvent, such as we describe hereinafter, and the solvent-extracted oil is freed from solvent and subjected to a suitable heat treatment, the resulting oil is liquid and remains so. These oils are much superior to other solventextracted tung oils, in that they are liquid and, therefore, acceptable to the tung oil trade.
In carrying out our invention, the tung oil press cake, or the tung kernels, which have been separated from tung hulls and shells, are ground and rolled, to rupture the oil cells, allowing the subsequent removal of the tung oil, by the solvent. The ground and rolled tung kernels, or ground tung oil press cake, is subjected to the action of a petroleum solvent of a short boiling range, between room temperature and the boiling point of water. The extraction process is conducted, using the counter-current system, the fresh solvent first coming into contact with the partly extracted ground material. When the extraction process is completed, the oil-bearing solvent is filtered and then run to a still, where most of the solvent is removed by steam heat. The solventbearing oil is filtered and freed of remaining solvent by spraying it into a vacuum evaporator onto steam heated coils. Here the solvent-free oil is removed from. the bottom of the evaporator, while the solvent vapors are removed from the top of the evaporator. The. solvent-free tung oil is heated to 200 C., or higher, for a sufiicient time to yield a clear liquid oil.
Various apparatus may be used. to carry out our process of producing a clear, solvent-extracted, tung oil from tung kernels and from tung oil press cake. The following example is illustrative of the preferred manner in which our invention may be practiced:
Erample.A quantity of ground tung oil press cake, or tung kernels which have been separated from tung hulls and shells and ground and rolled, is subjected to the action of petroleum ether (boiling range to 138 F.) This extraction process is of the continuous percolation type, the fresh solvent running upon the bed of ground material. Upon completion of the extraction process, the oil-bearing solvent is filtered and run into a still, where the solution is heated preferably by a closed steam coil, thereby removing the bulk of the solvent. This concentrated solvent-bearing oil is filtered and then sprayed onto steam heated coils in a vacuum evaporator. Here the oil is freed of the remaining solvent and falls over the heated pipes to the bottom of the evaporator, while the solvent vapors are removed from the top of the evaporator and recovered by any suitable means. The solvent-free oil is heated to at least 200 C. for substantially 30 minutes, yielding an oil which remains clear and liquid at room temperature.
The solvent-extracted oil from the tung oil press cake when obtained by the first phase of the above method had the following characteristics: iodine value (Wijs) 160.0; time for Browne heat test, 15.5 minutes; solid at room temperature. The remainingv solvent-extracted oil from the tung oil press cake after it was heat-treated by the second phase had the following characteristics: iodine value (Wijs) 145.7; time of solidification with Browne heat test, 13 minutes; refractive index at 25, 1.5097; viscosity by Gardner standards=U=6.5 poises; liquid at room temperature.
When the solvent-extracted oil was obtained from tung kernels by the first phase of the foregoing method it had the following characteristics: iodine value (Wijs) 165.0; time of solidification with Browne heat test, 11% minutes; solid at room temperature. The remaining solventextracted oil from the tung kernels after it was heat-treated by the second phase had the following characteristics: iodine (Wijs) 152.5; time of solidification with Browne heat test, 11% minutes; liquid at room temperature.
Having thus described our invention, what we claim for Letters Patent is:
A process for producing a clear liquid petroleum ether solvent-extracted tung oil, which comprises subjecting petroleum ether solvent-extracted tung oil to a temperature of at least 200 C. for substantially 30 minutes.
ROBERT S. MCKINNEY. WILLIAM GORDON ROSE. ANDREW F. FREEMAN.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US291564A US2277342A (en) | 1939-08-23 | 1939-08-23 | Process for the preparation of tung oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US291564A US2277342A (en) | 1939-08-23 | 1939-08-23 | Process for the preparation of tung oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2277342A true US2277342A (en) | 1942-03-24 |
Family
ID=23120816
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US291564A Expired - Lifetime US2277342A (en) | 1939-08-23 | 1939-08-23 | Process for the preparation of tung oil |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2277342A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106867653A (en) * | 2017-02-23 | 2017-06-20 | 郴州国盛生物能源股份有限公司 | A kind of energy-efficient tung nut processing method |
-
1939
- 1939-08-23 US US291564A patent/US2277342A/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106867653A (en) * | 2017-02-23 | 2017-06-20 | 郴州国盛生物能源股份有限公司 | A kind of energy-efficient tung nut processing method |
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