US2007738A - Method of fumigation - Google Patents
Method of fumigation Download PDFInfo
- Publication number
- US2007738A US2007738A US707810A US70781034A US2007738A US 2007738 A US2007738 A US 2007738A US 707810 A US707810 A US 707810A US 70781034 A US70781034 A US 70781034A US 2007738 A US2007738 A US 2007738A
- Authority
- US
- United States
- Prior art keywords
- vapors
- liquid
- proportions
- fumigation
- pressure
- 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
- 238000003958 fumigation Methods 0.000 title description 9
- 238000000034 method Methods 0.000 title description 9
- 239000007788 liquid Substances 0.000 description 24
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 18
- 229910002092 carbon dioxide Inorganic materials 0.000 description 9
- 239000001569 carbon dioxide Substances 0.000 description 9
- 239000007789 gas Substances 0.000 description 8
- 239000000203 mixture Substances 0.000 description 7
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 description 5
- TZIHFWKZFHZASV-UHFFFAOYSA-N methyl formate Chemical compound COC=O TZIHFWKZFHZASV-UHFFFAOYSA-N 0.000 description 4
- 239000002316 fumigant Substances 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 3
- 229910052753 mercury Inorganic materials 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 2
- 241000238631 Hexapoda Species 0.000 description 2
- 241000607479 Yersinia pestis Species 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- 235000013311 vegetables Nutrition 0.000 description 2
- 239000005977 Ethylene Substances 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000002341 toxic gas Substances 0.000 description 1
Images
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23B—PRESERVATION OF FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES; CHEMICAL RIPENING OF FRUIT OR VEGETABLES
- A23B2/00—Preservation of foods or foodstuffs, in general
- A23B2/70—Preservation of foods or foodstuffs, in general by treatment with chemicals
- A23B2/704—Preservation of foods or foodstuffs, in general by treatment with chemicals in the form of gases, e.g. fumigation; Compositions or apparatus therefor
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23B—PRESERVATION OF FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES; CHEMICAL RIPENING OF FRUIT OR VEGETABLES
- A23B7/00—Preservation of fruit or vegetables; Chemical ripening of fruit or vegetables
- A23B7/14—Preserving or ripening with chemicals not covered by group A23B7/08 or A23B7/10
- A23B7/144—Preserving or ripening with chemicals not covered by group A23B7/08 or A23B7/10 in the form of gases, e.g. fumigation; Compositions or apparatus therefor
Definitions
- This invention relates to an improved method means for heating the vapors, as for example of fumigation, and particularly to the fumigaa steam coil I. tion of vegetable products with a mixture of va- In carrying out the process the tank 2, conpors from volatile liquids. taining the liquids, the vapors of which are to In carrying out fumigation of ,food or other he used as fumigants, is connected to the ac- 5 vegetable and animal products, a mixture of vacumuleter- If mmi q i W not mix pors i customarily supplied. The vapors are within the tank; but the lighter will float upon taken from the liquids, which are supplied in the heavier.
- the fumigant stantially the entire contents of the liquid tank 2 comprises carbon dioxide or other inert gas such are then evap rated in h ul r 3, 01 10 as nitrogen or the like, together with a minor until the pressure in the two are substantially proportion of toxic gas such as ethylene oxide, equal, and are mixed within the accumulator to methyl formate or the like.
- the fumigating mateof 120 F. they may be admitted to the fumigator.
- rials are supplied in liquid form, the liquids be- In the pr f d method f fu ati n. t ing placed in the desiredproportion under high products to be fumigat'ed are placed within the pressure in a steel tank.
- the liquids commonly fumigator 5, which is evacuated to a pressure of 2 used may not be miscible in the proportions used. A1" of mercury absoluteor less, and the fumigat- On this account removal of vapors in the proing gases are then admitted and the total gas portions in which the liquids are present is not pressure brought up thereby to 15-20" of mercury possible under present methods.
- vapors are If desired, more than one tank fullof liquid may supplied in exactly the predetermined and desired be vaporized into the accumulator. In each case proportions, and in perfectly homogeneous form. it is important to evacuate the entire container,
- the invention is illustrated diagrammatically however. in the drawing, wherein is shown a liquid con-
- the vapors within the accumulator are pref- "30 tainer 2 from which the vapors may be removed erably heated to a temperature of 120 F. It has to the accumulator I.
- the mixed vapors from been discovered that by supplying the gases at this the accumulator are passed through the line 4 temperature the fumigation is considerably into the fumigator I.
- a vacuum pump 6 is proassisted. vided in order to evacuate the fumigator if de- The product to be fumigated, for instance to- 56 sired.
- the accumulator 3 is also provided with bacco, food products or the like, is then placed within the fumigator, which is closed and evacuated. Atter the desired degree of vacuum has beensecuredthemixedandheatedvaporsare thenadmittedtothetanhthepressurebeing raised thereby, and are held within the fumigator for the desired period, for example two or three hours.
- liquid denotes materiais of approximately liquid density, whether actually above or below the critical point.
- immiscible denotes materials which are not completely miscible in the proportions in which they are used as fumi-.v
- steps of completely volatilizing said liquids thoroughly admixing the vapors therefrom heating said vapors to a temperature of the order of 120 F. under a' pressure of 75 lbs., and introducing said heated vapors into a vacuum zone containingthe material to be fumigated.
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Wood Science & Technology (AREA)
- Zoology (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
Patented July 9, 935 2 07 73 UNITED STATES PATENT OFFICE John Baer, Chicago, 11]., asslgnor to The Gllardite Corporation, a corporation of Illinois Application January 22, 1934, Serial No. 707,810
' B CIaims. (Cl. 99-9) This invention relates to an improved method means for heating the vapors, as for example of fumigation, and particularly to the fumigaa steam coil I. tion of vegetable products with a mixture of va- In carrying out the process the tank 2, conpors from volatile liquids. taining the liquids, the vapors of which are to In carrying out fumigation of ,food or other he used as fumigants, is connected to the ac- 5 vegetable and animal products, a mixture of vacumuleter- If mmi q i W not mix pors i customarily supplied. The vapors are within the tank; but the lighter will float upon taken from the liquids, which are supplied in the heavier. In carrying out the invention, subtanks under pressure. Generally the fumigant stantially the entire contents of the liquid tank 2 comprises carbon dioxide or other inert gas such are then evap rated in h ul r 3, 01 10 as nitrogen or the like, together with a minor until the pressure in the two are substantially proportion of toxic gas such as ethylene oxide, equal, and are mixed within the accumulator to methyl formate or the like. For example, a form a. homogeneos mixture before admission to preferred fumigant'comprises 9 parts by weight the fumigator. After thoroughly mixing in the of carbon dioxide and 1 part by weight of ethylene accumulator, du g w h time the gases are 15 oxide. preferably heated to a temperature of the order In commercial practice, the fumigating mateof 120 F., they may be admitted to the fumigator. rials are supplied in liquid form, the liquids be- In the pr f d method f fu ati n. t ing placed in the desiredproportion under high products to be fumigat'ed are placed within the pressure in a steel tank. The liquids commonly fumigator 5, which is evacuated to a pressure of 2 used may not be miscible in the proportions used. A1" of mercury absoluteor less, and the fumigat- On this account removal of vapors in the proing gases are then admitted and the total gas portions in which the liquids are present is not pressure brought up thereby to 15-20" of mercury possible under present methods. If the outlet absolute. The gases are maintained at a conis from the bottom of the tank the heavier siderable pressure in the accumulator 3, for ex- 25 liquid comes oil first, whereas if vapors are reample, 75 lbs., and it is found that there is no moved from the top, the more volatile comes ofi separation of the gases upon their subsequent in-excessive amounts in the beginningv and the rarefication in the fumigator. Therefore, being less volatile in excessive amounts at the end. mixed in the proper proportions in the accumu- Attempts have been made to remedy this situalater, the drop in pressure therein has no effect '30 1 .tion by the use of multiple hole inductor tubes, upon the proportions and the fumigator is always and while these have helped considerably, they supplied with precisely the desired ratio of vapors. by no means overcome the diiiiculty. The As an example of the invention, 6 lbs. of ethylchanges from the desired proportions will cause ene oxide and 54 lbs. of liquid carbon dioxide are very considerable variations in the efliciency of provided in a pressure tank, under a pressure of 35 the fumigation, and many fumigation failures are roughly 800 lbs. per square inch. These madirectly traceable to variations in the proportions terials are then vaporized into an accumulator of the constituents. having a capacity of in the neighborhood of 100 v Also in the case of liquids which may be more cubic feet. This will involve a reduction of pres- 40 or less completely miscible, removal of vapors in sure to about 75 lbs. The vapors are admitted to 40 the proportions in which the liquids are present the accumulator under afairly high pressure drop may be impossible or difficult, under present so that mixing is promptly and completely semethods, because the evaporation rates may not cured. When the entire quantity of liquid has correspond to the desired mixture. vaporized, the liquid tank may be disconnected.
5 By means of the present invention, vapors are If desired, more than one tank fullof liquid may supplied in exactly the predetermined and desired be vaporized into the accumulator. In each case proportions, and in perfectly homogeneous form. it is important to evacuate the entire container,
The invention is illustrated diagrammatically however. in the drawing, wherein is shown a liquid con- The vapors within the accumulator are pref- "30 tainer 2 from which the vapors may be removed erably heated to a temperature of 120 F. It has to the accumulator I. The mixed vapors from been discovered that by supplying the gases at this the accumulator are passed through the line 4 temperature the fumigation is considerably into the fumigator I. A vacuum pump 6 is proassisted. vided in order to evacuate the fumigator if de- The product to be fumigated, for instance to- 56 sired. The accumulator 3 is also provided with bacco, food products or the like, is then placed within the fumigator, which is closed and evacuated. Atter the desired degree of vacuum has beensecuredthemixedandheatedvaporsare thenadmittedtothetanhthepressurebeing raised thereby, and are held within the fumigator for the desired period, for example two or three hours.
The term "liquid", as used herein, denotes materiais of approximately liquid density, whether actually above or below the critical point.
The term immiscible", as used herein, denotes materials which are not completely miscible in the proportions in which they are used as fumi-.v
there is a division between the fumigating with said mixed vapors.
2. The method as set forth in claim 1, in which the liquids are present in the proportions of the order of 9 parts carbon dioxide to one part of ethylene oxide. v
3. The method of fumigating with mixtures of ethylene oxide and'carbon dioxide, which comprises expanding a liquid charge containing said ingredients in the desired proportions to completely gasiiy the same, retaining the completely gasifled charge in gasifled form until it becomes homogeneous, and subsequently. applying gas from the charge to the articles to be fumigated.
.4.-'ihemethcdotmmigatingwithmixtmesof ethylene oxide and'carbon dioxide, which comprises'chargingacontainerwiththeliquidingredients'in the proportions desired for fumi-' gating, expanding substantially the entire container charge into gaseous form. and retaining the expanded gaseous charge before application to the articles to be fumigated until it becomes entirely homogeneous in the gaseous form.
5'. The method of fumigating with mixtures of methyl formate and carbon dioxide, which comprises expanding a liquid charge containing said ingredients in the demred proportions to completely gasify the same, retaining the completely gasiiled charge in gasified form until it becomes homogeneous, and subsequently applying gas from the charge to the. articles to be i'umigated.
6. In'the fumigation of insect pests with a mixed vapor from a charge of liquid ethylene" oxide and carbon dioxide, the steps of completely volatilizing said liquids, thoroughly admixing the v vapors therefrom, heating said vapors to a tem perature of the order of 120 it, and introducing said heated vapors into a vacuum zone containing the material to be fumigated.
7. In the fumigation of insect pests with a liquid charge of ethylene oxide and carbon dioxide, the
steps of completely volatilizing said liquids thoroughly admixing the vapors therefrom, heating said vapors to a temperature of the order of 120 F. under a' pressure of 75 lbs., and introducing said heated vapors into a vacuum zone containingthe material to be fumigated.
8. The method'as set forth in claim 7, in which the vapors are collected under a pressure of the order 0M5 lbs. superatmospheric, and said fumigation is carried out under an air pressure of the order of inch of mercury.
JOHN in. mm
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US707810A US2007738A (en) | 1934-01-22 | 1934-01-22 | Method of fumigation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US707810A US2007738A (en) | 1934-01-22 | 1934-01-22 | Method of fumigation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2007738A true US2007738A (en) | 1935-07-09 |
Family
ID=24843243
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US707810A Expired - Lifetime US2007738A (en) | 1934-01-22 | 1934-01-22 | Method of fumigation |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2007738A (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2965936A (en) * | 1957-06-25 | 1960-12-27 | Ben Venne Lab Inc | Sterilizing apparatus employing gas |
| US3054270A (en) * | 1960-08-19 | 1962-09-18 | American Sterilizer Co | Gas sterilizing system |
| US3489505A (en) * | 1967-08-28 | 1970-01-13 | Hugo Sonnenschein | Sterilizing apparatus |
| US4374087A (en) * | 1981-06-17 | 1983-02-15 | Hallstroem Bengt O | Method of sterilizing mattresses, laundry sacks and similar articles in a sterilizing apparatus |
| US4435194A (en) | 1980-02-12 | 1984-03-06 | La Calhene | Circuit for ventilating and filtering the medium contained in a confinement enclosure |
| US4889708A (en) * | 1985-06-27 | 1989-12-26 | The Boc Group, Inc. | Fumigant system |
| US5340538A (en) * | 1993-09-27 | 1994-08-23 | Liquid Carbonic Corporation | Sterilizing gas delivery method |
| US5527507A (en) * | 1992-10-01 | 1996-06-18 | American Sterilizer Company | Accumulator based liquid metering system and method |
-
1934
- 1934-01-22 US US707810A patent/US2007738A/en not_active Expired - Lifetime
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2965936A (en) * | 1957-06-25 | 1960-12-27 | Ben Venne Lab Inc | Sterilizing apparatus employing gas |
| US3054270A (en) * | 1960-08-19 | 1962-09-18 | American Sterilizer Co | Gas sterilizing system |
| US3489505A (en) * | 1967-08-28 | 1970-01-13 | Hugo Sonnenschein | Sterilizing apparatus |
| US4435194A (en) | 1980-02-12 | 1984-03-06 | La Calhene | Circuit for ventilating and filtering the medium contained in a confinement enclosure |
| US4374087A (en) * | 1981-06-17 | 1983-02-15 | Hallstroem Bengt O | Method of sterilizing mattresses, laundry sacks and similar articles in a sterilizing apparatus |
| US4889708A (en) * | 1985-06-27 | 1989-12-26 | The Boc Group, Inc. | Fumigant system |
| US5527507A (en) * | 1992-10-01 | 1996-06-18 | American Sterilizer Company | Accumulator based liquid metering system and method |
| US5340538A (en) * | 1993-09-27 | 1994-08-23 | Liquid Carbonic Corporation | Sterilizing gas delivery method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US2779680A (en) | Fumigation with fluorocyclobutenes | |
| US2007738A (en) | Method of fumigation | |
| EP0616821B1 (en) | Fragrance extraction | |
| US2719129A (en) | Pressurized liquid room and air deodorant compositions | |
| US2785984A (en) | Fumigation with chlorofluoropropenes | |
| Cotton et al. | Ethylene Oxide as a Fumigant1 | |
| US4295581A (en) | Insecticidal aerosol formulation having a liquified petroleum gas propellant | |
| Jones et al. | Extinction of Ethylene Oxide Flames with Carbon Dioxide1 | |
| US5085849A (en) | d-Limonene containing space or room aerosol deodorant | |
| US3371460A (en) | Method of filling aerosol containers and the like | |
| Wilson | Triethanolamine Emulsions1 | |
| US2101587A (en) | Insecticidal product and process | |
| US2223724A (en) | Shortening and process of producing the same | |
| US7015367B2 (en) | Stabilization and use of propargyl bromide | |
| US3038816A (en) | Method for producing sprayable composition | |
| US1874258A (en) | Stabilized heating fluid and method of stabilizing same | |
| US2550196A (en) | Composite solid carbon dioxide | |
| US2463363A (en) | Milk treatment with oxidation inhibiting gases | |
| US2803581A (en) | Noninflammable fumigant mixture | |
| US2091935A (en) | Insecticides and fungicides | |
| US2129275A (en) | Fumigation | |
| US1029737A (en) | Fusible phenol resin and method of forming same. | |
| US1877875A (en) | Process for the extraction of valuable ingredients from heat sensitive raw materials | |
| US1223153A (en) | Method or process of treating liquids. | |
| US1400484A (en) | Process of treating substances |