US1373720A - Process of treating hydrocarbons - Google Patents
Process of treating hydrocarbons Download PDFInfo
- Publication number
- US1373720A US1373720A US1373720DA US1373720A US 1373720 A US1373720 A US 1373720A US 1373720D A US1373720D A US 1373720DA US 1373720 A US1373720 A US 1373720A
- Authority
- US
- United States
- Prior art keywords
- water
- hydrocarbon
- tank
- suspension
- engine
- 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
- 229930195733 hydrocarbon Natural products 0.000 title description 34
- 150000002430 hydrocarbons Chemical class 0.000 title description 34
- 238000000034 method Methods 0.000 title description 11
- 239000004215 Carbon black (E152) Substances 0.000 description 30
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 29
- 239000000725 suspension Substances 0.000 description 11
- 239000007788 liquid Substances 0.000 description 7
- 239000003350 kerosene Substances 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 239000002360 explosive Substances 0.000 description 4
- 239000000203 mixture Substances 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 230000000717 retained effect Effects 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 230000005587 bubbling Effects 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D35/00—Filtering devices having features not specifically covered by groups B01D24/00 - B01D33/00, or for applications not specifically covered by groups B01D24/00 - B01D33/00; Auxiliary devices for filtration; Filter housing constructions
- B01D35/005—Filters specially adapted for use in internal-combustion engine lubrication or fuel systems
Definitions
- the invention relates to new and useful improvements in processes for treating hydrocarbons for explosive engmes and more particularly to the process for treating the hydrocarbon on its way from a storage tank to the carburetor.
- An object of the invention is to provide a process of supplying an explosive engine with a volatile liquid hydrocarbon whereby the hydrocarbon is washed on its way to. the engine and all foreign substances 1n suspension separated from the hydrocarbon and retained by the washing liquid, and
- the figure of the drawing is a view partly in side elevation and partly in section showing such apparatus.
- the process consists broadly in causing a liquid hydrocarbon on its way from a storage receptacle to the engine to pass through a body of water, coming directly in contact with the water so that the liquid hydrocarbon will be thoroughly washed and all foreign substances in suspension separated from the hydrocarbon and re tained by the washing water, and whereby the liquid hydrocarbon will also take up in suspension a certain amount of the water and carry the same into the engine.
- the hydrocarbon is caused to bubble in a finely divided state up through the water which brings about the above results.
- the hydrocarbon used may be gasolene, kerosene or a mixture of gasolene and kerosene, or in fact any other of the well-known similar distillates.
- 1 indicates a tank or supply for the hydrocarbon
- 2 indicates a carbureter where the hydrocarbon is carbureted before it is delivered to the engine.
- a pipe 4 connects with the pipe 5 which is tapped into the tank 3 near the bottom thereof. This pipe 4 is also tapped into the tank at 6 near the top of the tank.
- a three-way valve 7 directs the flow of hydrocarbon to the tank 3 and as the valve is set the hydrocarbon will pass into the bottom of the tank.
- a pipe 8 leads frointhe top of the tank 3 to the carbureter 2.
- the tank 3 is provided with a short pipe 9 which extends below the bottom of the tank and this pipe 9 is controlled by a valve 10.
- the valve 10 is attached to the lever 11 which is provided with a small weight 12.
- a rod 13 connected to the lever 11 carries a float 14.
- This rod is guided in a suitable bracket 15.
- the tank is provided with a suitable filling opening indicated at 16.
- the hydrocarbon whatever it may be, whether gasolene, kerosene, or gasolene and kerosene mixed or any other volatile distillate is placed in the supply tank 1.
- This tank is also placed a quantity of water.
- the amount of water may be varied. For example, five gallons of gasolene and five gallons of kerosene may be put in the supply tank and to this amount of mixture should be added two quarts of water or thereabout. From time to time a little Water should be added to the hydrocarbon mixture.
- the mixed hydrocarbon and water passing down into the tank 3 enters the tank near the bottom thereof and the water settles by gravity at the bottom of the tank 3.
- the water will accumulate in the tank until a water level indicated by the line w-m is reached.
- the float 14 and weight 12 are so proportioned that the float will rest on the surface of the water partly submerged therein but will sink in gasolene.
- any increase in water above this line will raise the valve and allow some of the water to drain off through the pipe 9.
- the water column recedes to the line w-w the valve will close and thus a water-well is maintained, the level of which is at the line m00.
- the hydrocarbon entering through the pipe 5 will bubble up through the water-well.
- the hydrocarbon As the hydrocarbon passes through this water-well it will be thoroughly washed and all foreign substances in suspension such as silica, alumina and free carbon will be removed and trapped by the water; Furthermore the hydrocarbon, bubbling up through the water, takes up a certain amount of the water in suspension and carries the same through into the engine. This water in suspension greatly increases. the efficiency of the explosive charge and thereby greatly increases the mileage which may be obtained on a measured amount of hydrocarbon. It is obvious that from certain aspects of the in vention, the water well may be otherwise formed. The essential feature consists in the causing of the hydrocarbon to bubble up from the water well where the hydrocarbon is thoroughly washed and all foreign substances in suspension, such as silica,
Description
D. B. GISH.
PROCESS OF TREATING HYDROCARBONS.
APPLlCATlON man JUNE 12. 19W. RENEWED APR. 22.1920.
1 $373,720 Patented Apr. 5 192K.
CHRBUEETOT? 21 UNITED STATES PATENT OFFIQE.
PROCESS OF TREATING IIYDROCARBONS.
Specification of Letters Patent.
' Patented Apr. 5, 15121.
Application filed June 12, 1917, Serial No. 174,334. Renewed April 22, 1920. Serial No. 375,899.
To all whom it may concern:
Be it known that I, DANIEL BRA1LEY GIsH, a citizen of the United States, residing at l Vashington, in the District of (lolumbla, have invented certain new and useful Improvements in Processes of Treating Hydro carbons for Explosive-Engines, of which the following is a description, reference being had to the accompanylng drawing, and to the figures of reference marked thereon.
The invention relates to new and useful improvements in processes for treating hydrocarbons for explosive engmes and more particularly to the process for treating the hydrocarbon on its way from a storage tank to the carburetor. I
An object of the invention is to provide a process of supplying an explosive engine with a volatile liquid hydrocarbon whereby the hydrocarbon is washed on its way to. the engine and all foreign substances 1n suspension separated from the hydrocarbon and retained by the washing liquid, and
wherebv the hydrocarbon is caused to take up in suspension certain of the washing liquid and carry the same into the englne.
In order to aid in the disclosure of the invention I have illustrated in the drawing an apparatus which may be used in carrying out the process.
The figure of the drawing is a view partly in side elevation and partly in section showing such apparatus.
The process consists broadly in causing a liquid hydrocarbon on its way from a storage receptacle to the engine to pass through a body of water, coming directly in contact with the water so that the liquid hydrocarbon will be thoroughly washed and all foreign substances in suspension separated from the hydrocarbon and re tained by the washing water, and whereby the liquid hydrocarbon will also take up in suspension a certain amount of the water and carry the same into the engine. In carrying out the invention, the hydrocarbon is caused to bubble in a finely divided state up through the water which brings about the above results. The hydrocarbon used may be gasolene, kerosene or a mixture of gasolene and kerosene, or in fact any other of the well-known similar distillates.
Referring to the apparatus which I have shown as one embodiment of a device for carrying out my process, 1 indicates a tank or supply for the hydrocarbon, and 2 indicates a carbureter where the hydrocarbon is carbureted before it is delivered to the engine. Located between the supply tank 1 which may be of any character, either a gravity feed, pressure feed, or a vacuum feed is a small tank 3. A pipe 4 connects with the pipe 5 which is tapped into the tank 3 near the bottom thereof. This pipe 4 is also tapped into the tank at 6 near the top of the tank. A three-way valve 7 directs the flow of hydrocarbon to the tank 3 and as the valve is set the hydrocarbon will pass into the bottom of the tank. A pipe 8 leads frointhe top of the tank 3 to the carbureter 2. The tank 3 is provided with a short pipe 9 which extends below the bottom of the tank and this pipe 9 is controlled by a valve 10. The valve 10 is attached to the lever 11 which is provided with a small weight 12. A rod 13 connected to the lever 11 carries a float 14.
This rod is guided in a suitable bracket 15.
The tank is provided with a suitable filling opening indicated at 16. The hydrocarbon, whatever it may be, whether gasolene, kerosene, or gasolene and kerosene mixed or any other volatile distillate is placed in the supply tank 1. In this tank is also placed a quantity of water. The amount of water may be varied. For example, five gallons of gasolene and five gallons of kerosene may be put in the supply tank and to this amount of mixture should be added two quarts of water or thereabout. From time to time a little Water should be added to the hydrocarbon mixture. The mixed hydrocarbon and water passing down into the tank 3 enters the tank near the bottom thereof and the water settles by gravity at the bottom of the tank 3. The water will accumulate in the tank until a water level indicated by the line w-m is reached. The float 14 and weight 12 are so proportioned that the float will rest on the surface of the water partly submerged therein but will sink in gasolene. When the water level reaches the line w-m any increase in water above this line will raise the valve and allow some of the water to drain off through the pipe 9. When however, the water column recedes to the line w-w the valve will close and thus a water-well is maintained, the level of which is at the line m00. The hydrocarbon entering through the pipe 5 will bubble up through the water-well. As the hydrocarbon passes through this water-well it will be thoroughly washed and all foreign substances in suspension such as silica, alumina and free carbon will be removed and trapped by the water; Furthermore the hydrocarbon, bubbling up through the water, takes up a certain amount of the water in suspension and carries the same through into the engine. This water in suspension greatly increases. the efficiency of the explosive charge and thereby greatly increases the mileage which may be obtained on a measured amount of hydrocarbon. It is obvious that from certain aspects of the in vention, the water well may be otherwise formed. The essential feature consists in the causing of the hydrocarbon to bubble up from the water well where the hydrocarbon is thoroughly washed and all foreign substances in suspension, such as silica,
alumina, and tree carbon removed therefrom and trapped by the water, and where the hydrocarbon is also caused to take up in suspension water vapor.
Having thus described my invention what I claim as new is The process of supplying an explosive engine with a volatile liquid hydrocarbon consisting in providing a body of 'ater between the supply tank and the engine and. passingthe hydrocarbon through said water on the way to the engine, whereby the hydrocarbon is washed and all foreign substances in suspension separated from the hydrocarbon and retained by the water and whereby said hydrocarbon is caused to take up in suspension a certain amount oi? water and carry the same into the engine.
In testimony whereof I aiiix my signature.
DANIEL BRAILEY ersn.
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1373720A true US1373720A (en) | 1921-04-05 |
Family
ID=3398237
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US1373720D Expired - Lifetime US1373720A (en) | Process of treating hydrocarbons |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1373720A (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2790560A (en) * | 1951-11-27 | 1957-04-30 | Robert W Beyland | Liquid separator |
| US3260572A (en) * | 1961-05-19 | 1966-07-12 | Commissariat Energie Atomique | Countercurrent liquid-liquid extraction apparatus |
| US3273716A (en) * | 1966-09-20 | Liquid petroleum fuel cleaner | ||
| US3724429A (en) * | 1970-11-16 | 1973-04-03 | N Tomlinson | Pollution-reducing fuel filter |
| US4443385A (en) * | 1981-01-30 | 1984-04-17 | Herman Laub | Fuel system for vehicles |
| US5080781A (en) * | 1989-05-18 | 1992-01-14 | Evins Iv Alexander A | Down-hole hydrocarbon collector |
| US7185707B1 (en) | 2005-12-02 | 2007-03-06 | Graham Robert R | Hydrostatic separator apparatus and method |
| US20120186557A1 (en) * | 2011-01-24 | 2012-07-26 | Jenkins Walter P | Apparatus, system, and method for vaporizing fuel mixture |
-
0
- US US1373720D patent/US1373720A/en not_active Expired - Lifetime
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3273716A (en) * | 1966-09-20 | Liquid petroleum fuel cleaner | ||
| US2790560A (en) * | 1951-11-27 | 1957-04-30 | Robert W Beyland | Liquid separator |
| US3260572A (en) * | 1961-05-19 | 1966-07-12 | Commissariat Energie Atomique | Countercurrent liquid-liquid extraction apparatus |
| US3724429A (en) * | 1970-11-16 | 1973-04-03 | N Tomlinson | Pollution-reducing fuel filter |
| US4443385A (en) * | 1981-01-30 | 1984-04-17 | Herman Laub | Fuel system for vehicles |
| US5080781A (en) * | 1989-05-18 | 1992-01-14 | Evins Iv Alexander A | Down-hole hydrocarbon collector |
| US7185707B1 (en) | 2005-12-02 | 2007-03-06 | Graham Robert R | Hydrostatic separator apparatus and method |
| US20120186557A1 (en) * | 2011-01-24 | 2012-07-26 | Jenkins Walter P | Apparatus, system, and method for vaporizing fuel mixture |
| US10648430B2 (en) * | 2011-01-24 | 2020-05-12 | Walter P. Jenkins | Apparatus, system, and method for vaporizing fuel mixture |
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