US1806740A - A cobfoba - Google Patents
A cobfoba Download PDFInfo
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- US1806740A US1806740A US1806740DA US1806740A US 1806740 A US1806740 A US 1806740A US 1806740D A US1806740D A US 1806740DA US 1806740 A US1806740 A US 1806740A
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- Prior art keywords
- tank
- cleaning
- tanks
- liquid
- interior
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- 238000004140 cleaning Methods 0.000 description 45
- 239000007788 liquid Substances 0.000 description 35
- 238000000034 method Methods 0.000 description 21
- 239000013049 sediment Substances 0.000 description 16
- 239000003921 oil Substances 0.000 description 11
- 239000012530 fluid Substances 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 238000010438 heat treatment Methods 0.000 description 6
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 6
- 238000010025 steaming Methods 0.000 description 6
- 239000003350 kerosene Substances 0.000 description 5
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 238000005086 pumping Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 239000010779 crude oil Substances 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 1
- 244000080575 Oxalis tetraphylla Species 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 230000035508 accumulation Effects 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 238000012550 audit Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000002845 discoloration Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000007747 plating Methods 0.000 description 1
- 238000009877 rendering Methods 0.000 description 1
- 238000012857 repacking Methods 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B08—CLEANING
- B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
- B08B9/00—Cleaning hollow articles by methods or apparatus specially adapted thereto
- B08B9/08—Cleaning containers, e.g. tanks
- B08B9/093—Cleaning containers, e.g. tanks by the force of jets or sprays
- B08B9/0936—Cleaning containers, e.g. tanks by the force of jets or sprays using rotating jets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B63—SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
- B63B—SHIPS OR OTHER WATERBORNE VESSELS; EQUIPMENT FOR SHIPPING
- B63B57/00—Tank or cargo hold cleaning specially adapted for vessels
- B63B57/02—Tank or cargo hold cleaning specially adapted for vessels by washing
Definitions
- Patented May 26, 1931 3 mean ⁇ STATESMPATENT OFFICE 'ARTHUR'B. BUTTERWORTH, OF HOB-T ARTHUR, TEXAS, ASSIGNOR, BY ASSIGN- MENTS, TO BUTTERWORTH SYSTEM, ING, OF WILmGTON, DELAWARE, A. CORPORA- TION Oh DELAWARE 1 METHOD or CLEANING. SCALINQAND ens FREEING BULK CARGO TANKS 01 mm a 1 vEssELs I Application filed October 11, 1927. Serial No. 225,592.
- My invention relates to a method of clean-. ing the interior of tanks of tank vessels employed in transporting crude oil and its derivatives.
- the tanks of vessels employed in transporting petroleum and its distillates may be em.- ployed in the carrying of the heavy crude or any of the distillates obtained'therefrom, andit sometimes becomes necessary after a tanker has been employed in the transportation of heavy crude to carry in this same vessel a cargo of the lighter.
- distillates such as gasoline or benzine.
- the first operation is usually to steam out the tanks by forcing into the tanks a supply of steam which is intended to make the residue oil within the tank more fluid and to "remove from the rust and scale so on the interior of the tank, gas-forming residue which accumulates along. the sides and among the numerous plates and'the framework of the vessel.
- the steaming' is carried out for a desired period I and then the tanks are opened up to cool and arethen washed down' with a hose first from the deck and then from the bottom of the tank. After this all the shelves, frame work, plating and sides of the tank are scraped down by hand to get the bulk of the sediment and rust from thetank; The bottom sediment is then hauled out on deck.
- the first operation is usually to steam out the tanks by forcing into the tanks a supply of steam which is intended to make the residue oil within the tank more fluid and to "remove from the rust and scale so on the interior of the tank, gas-forming residue which accumulates along. the sides and among the numerous plates and'the framework of
- caustic soda is then sprinkled on the frames, shelves, gussets, etc., or this may be done previous to the first steaming, the steam dissolving the soda and tending to can ⁇ ? the deposit with it to the bottom of the tan 1
- the tanks are-then ready to receive the liquid for soaking and the cleaning liquid is then forced into the tank.
- kerosene is preferred, although a distillate or other similar mixture may be employed. It is the usual practice to fill one or more tanks well up in the expansion trunk and then allow it to soak for from six to twenty-four hours.
- the hull of a ship is designated by the numeral 1, the cross section showingthe two tanks, one on each side of the interior of the vessel, separated by a central partition 4.
- the bottom of the vessel is ordinarily somewhat flattened, as shown at 2, the deck being indicated at 3.
- wing tanks are used to contain the cleaning liquid, although it is to be understood that this liquid may be contained in a separate container or tank on the deck or in an adjacent vessel.
- the liquid employed in the cleaning is placed in this tank and may be heated through a heating coil 26 connected by means of the pipe to a source of supply of steam or other heating fluid.
- the cleaning fluid is circulated from the wing tank by means of a pump 9 having a suction line 10 directed into the wing tank, and an outlet line 11 through which the liquid from the pump may be directed into the pipe 12 and downwardly to the nozzles 15 through which the liquid is discharged in a solid stream against the sides of the tank.
- a pump 9 having a suction line 10 directed into the wing tank, and an outlet line 11 through which the liquid from the pump may be directed into the pipe 12 and downwardly to the nozzles 15 through which the liquid is discharged in a solid stream against the sides of the tank.
- the two nozzles 15, one at each side of the main carrying line 13 are directed in opposite directions.
- This type of cleaning device is shown in my previous Patent No. 1,557,240, issued October 13th, 1925, and the exact construction thereof is not apart of the present invention.
- the connecting T 1 1 is secured rigidly upon the pipe 13, the pipe 13 being rotated through a shaft 18 at the upper end thereof and the pipe 12, through which the fluid flows from the pipe 11, is held sta tionary.
- the lower end of the pipe 12 is formed with a stationary gear 17 thereon which is engaged by a gear16 upon one of the nozzles.
- the rotation of the shaft 18 and the tube 13 leading therefrom rotates the T 14 and the nozzles and the engagement between the gear 16 and the stationary gear 17, while the tube 13 is rotated, will cause the nozzles to be rotated in planes parallel with the pipe 12.
- the gears 16 and 17 are not of exactly the same size so that the courses of the streams issuing from the nozzles 15 will take a different path on each revolution which they make about the central shaft 13.
- the shaft 18 is rotated by means of a gear 19 thereon connected with a gear 20 engaged therewith and said gear 20 may be rotated by any desired means, such as the crank 21, or
- the cleaning appara- I tus is supported upon the upper end of the hatch way 5 but it is to be understood that it may be mounted in any desired manner, the object being to locate the nozzles 15 in such position within the tank that the streams of cleaning fluid may be directed under high pressure against the whole interior of the tank, it being found that in apparatus of this kind the whole inner side of the tank will be engaged by the streams of liquid during the rotation of the nozzles so that all sediment scale and dirt will be removed.
- This pump may be placed in any convenient position. I have shown the same as seated within the bottom of the tank adjacent the one being cleaned.
- This pump 23 has an inlet or suction line 24 directed through the wall between the two tanks and acting, to withdraw the cleaning liquid together with the sediment and this liquid is pumped out through the line 22 to the wing tank 7, where the sediment will settle out therefrom and the same cleaning liquid used over again.
- the interior of the tank may be Washed first with hot water.
- the Water after being heated in the wing tank through the heating coils, or through any other suitable means, is pumped under heavy pressure against the interior of the tank, removing the-sediment and the rust and washing the same to the bottom of the tank where it is at once removed.
- the removal of the cleaning liquid allows the streams of cleaningliquid which are directed against the bottom: to have a full cleaning effect thereon in the same manner as it has against the side and top walls.
- the cleaning liquid proper is usually kerosene or some similar distillate which is heated and directed against the sides of the tank and the pumping of the same against the wall with force removes the rust and sediment from all the corners and crevices between the plates and the framework and washes it down to the bottom where it is at once removed. This process may be 'continued until the interior is entirely free of foreign material. This may take from four to eight hours, depending upon the state of the interior of the tank before the cleaning is begun.
- the pressure employed be sufiicient to erode or cut the scale and other sediment from the surface to be cleaned, and the initial pressure of the jets or streams as delivered into the tanks by the nozzles should not be substantially less than forty pounds to the square inch or 'even in those cases where the splashing reaction of the 'e'ts is 4 or even higher, is employed.
- the suction pump emp oyed for the removal of the liquid from the bottomof the tank should be positioned aft as in any empty vessel the draught will be this aft ,end will be the low point of the vessel, and therefor the suction pump should be so positioned that it will be in the aft. end or Whatever other osition is substantially the lowest point of t lie vesselso that the sur faces to be cleaned are substantially kept clear of a butler layer of cleaning liquid which is being recirculated through the vessel to be cleaned.
- M improved process not only enables me to e ect the cleaning of cargo tanks at from 50% to 75% less cost than other processes now in use, but it accomplishes the cleaning of the ships pipe lines, pumps and valves simultaneously with the cleaning operation,
- I preferably include as part of my system the ships pump and pipe lines, and it thereby becomes unnecessary to renew the packing in the pipe system or open the'valves or customarily now the case when the cleaning of the ship is undertaken.
- I In order to prevent the cleaning fluid, particularly when kerosene is employed for this purpose, from being too rapi ly volatilized, I cause a solid jet of the same tobe propelled through the nozzles which deliver into the vessel being cleaned instead of effecting the introduction of the liquid in the form of an atomized spray.
- the ejector nozzles are, positively driven through gearing instead of reliance being placed upon the reaction obtainable frpm the high pressure of the liquid circulating therethrough to revolve the same since, owing to the unevenness of the surface upon which the high pressure jets im inge due to obstructions on the inside of tan ers, such as iron cross beams, there is a counter reaction transmitted back to the nozzles from the uneven surface of the tank and, due to the fact that they are arranged in pairs so as to counterbalance each other, they would if the reaction of the jets were the sole motive power cease to rotate entirely under certain conditions.
- light :oil such as gas oil or kerosene for example
- it will dissolve the otherwisevirtually useless bottom oil sediments or residues that can be run through the crack ing stills of a refinery, thus greatly reducing the cost of the cleaning, since the cleaning oil will be increased in bulk proportionate to the amount of residues dissolved therein.
- a recess of cleaning the interiors of tanks cargo-vessels and the like comprising heating a cleaning liquid, directing the said liquid in streams with force against the sides and the bottom walls of said tanks, and
- a recess of cleaning the interior of oil tanks 0 the character described comprising fiushing the interior thereof with a jet'of hotwater, removing the used water and sediment, then directing a solid jet of hot kerosene with force against the bottom and other walls of said tanks, and maintaining said bottom walls approximately free of liquid and sediment to permit direct contact of said jets therewith.
- the step which comprises the repeated circulation of jets of hot water through said tank under high pressure while removing the introduced water at a rate sutficient to maintain the bottom substantially bare of an interposed bufier layer of cleansing water.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Ocean & Marine Engineering (AREA)
- Cleaning In General (AREA)
Description
. M y 26. 1931,. A. a. BUTTERWORTH Y 1, 06
METHOD OF CLEANING, SCALING, AND GAS FREEZING BULK CARGO TANKS 0F TANK VESSELS Filed Oct. 11. 1927 mamam. 3
Patented May 26, 1931 3 mean \STATESMPATENT OFFICE 'ARTHUR'B. BUTTERWORTH, OF HOB-T ARTHUR, TEXAS, ASSIGNOR, BY ASSIGN- MENTS, TO BUTTERWORTH SYSTEM, ING, OF WILmGTON, DELAWARE, A. CORPORA- TION Oh DELAWARE 1 METHOD or CLEANING. SCALINQAND ens FREEING BULK CARGO TANKS 01 mm a 1 vEssELs I Application filed October 11, 1927. Serial No. 225,592.
' My invention relates to a method of clean-. ing the interior of tanks of tank vessels employed in transporting crude oil and its derivatives. i
I The tanks of vessels employed in transporting petroleum and its distillates may be em.- ployed in the carrying of the heavy crude or any of the distillates obtained'therefrom, andit sometimes becomes necessary after a tanker has been employed in the transportation of heavy crude to carry in this same vessel a cargo of the lighter. distillates, such as gasoline or benzine. In changing from transortation of the heavyv oil to that of the ighter distillates, it becomes necessary to thoroughly clean the interior of the cargo tanks so that the distillate will not be discolored during transportation, 'due to the residue left in the tank from the crude oil. 4 an The present system of cleaning the tanks of a vessel of this character involves a long and laborious process which is also expensive in its operation and which may also result in a deterioration of the hull of the vessel. 26 the old method, the first operation is usually to steam out the tanks by forcing into the tanks a supply of steam which is intended to make the residue oil within the tank more fluid and to "remove from the rust and scale so on the interior of the tank, gas-forming residue which accumulates along. the sides and among the numerous plates and'the framework of the vessel. In this method, the steaming'is carried out for a desired period I and then the tanks are opened up to cool and arethen washed down' with a hose first from the deck and then from the bottom of the tank. After this all the shelves, frame work, plating and sides of the tank are scraped down by hand to get the bulk of the sediment and rust from thetank; The bottom sediment is then hauled out on deck. In
some cases caustic soda is then sprinkled on the frames, shelves, gussets, etc., or this may be done previous to the first steaming, the steam dissolving the soda and tending to can}? the deposit with it to the bottom of the tan 1 The tanks are-then ready to receive the liquid for soaking and the cleaning liquid is then forced into the tank. Usually kerosene is preferred, although a distillate or other similar mixture may be employed. It is the usual practice to fill one or more tanks well up in the expansion trunk and then allow it to soak for from six to twenty-four hours. After this the liquid is pumped out of the tank and the steam turned on through the steam smothering line for several hours after which the sides are washed down with water and the parts again scraped and scaled and the sediment removed from the bottom. 'This operation is repeated with a new batch of cleaning liquid and then all the packing is renewed about the hatch covers, expansion 'joints, ullage plates, valves, etc.. This repacking of the parts becomes necessary from the straining of the parts due to the unequal heating involved in the cleaning operation, audit is found that by this method of cleaning'the li uid accumulates in the bottom of the ta so that the lower part of the tank is kept comparatively cool, while a the upper part is heated, and furthermore, the gathering of liquid in the bottom portion of the tank prevents this area from being cleaned when the hose is used against the tops and sides. 5 It'is an object of myinvention to provide a process of cleaning the interiorof tanks of this character in which the interior of the tank is thoroughly cleaned at all points and in which unequal heating of the tank is entirely avoided. v
It is also an object to dispensewith the necessity of scraping and the hand work in volved in the old method of cleaning.
It is another object to simplify the labor and cheapen the cost of cleaning the interior of tanks of the character stated.
It is desired to clean the interior of the tank by, force of streams of liquid directed against the sides under high pressure and in which the liquid thus usedin cleaning is simultaneously removed from the tank together with the sediment obtained in the cleaning operation. w 7 Referring to the drawings herewith, I have shown somewhat diagrammatically a cross section of the hull of a tanker showing the ap-.
paratus by means of which my process maybe carried into execution.
In the drawing the hull of a ship is designated by the numeral 1, the cross section showingthe two tanks, one on each side of the interior of the vessel, separated by a central partition 4. The bottom of the vessel is ordinarily somewhat flattened, as shown at 2, the deck being indicated at 3.
It is a'common feature in the usual tanker to provide wing tanks on the upper outer portions of the main tanks, and such a tank is shown in the drawings on each of the main I tank sections 27. These tanks have a bottom 8 and an inner side wall 7 the outer wall corresponding with that of the main tank. In carrying out my invention, the wing tanks are used to contain the cleaning liquid, although it is to be understood that this liquid may be contained in a separate container or tank on the deck or in an adjacent vessel. The liquid employed in the cleaning is placed in this tank and may be heated through a heating coil 26 connected by means of the pipe to a source of supply of steam or other heating fluid. The cleaning fluid is circulated from the wing tank by means of a pump 9 having a suction line 10 directed into the wing tank, and an outlet line 11 through which the liquid from the pump may be directed into the pipe 12 and downwardly to the nozzles 15 through which the liquid is discharged in a solid stream against the sides of the tank. It will be noted that the two nozzles 15, one at each side of the main carrying line 13, are directed in opposite directions. This type of cleaning device is shown in my previous Patent No. 1,557,240, issued October 13th, 1925, and the exact construction thereof is not apart of the present invention. The connecting T 1 1 is secured rigidly upon the pipe 13, the pipe 13 being rotated through a shaft 18 at the upper end thereof and the pipe 12, through which the fluid flows from the pipe 11, is held sta tionary. The lower end of the pipe 12 is formed with a stationary gear 17 thereon which is engaged by a gear16 upon one of the nozzles. The rotation of the shaft 18 and the tube 13 leading therefrom rotates the T 14 and the nozzles and the engagement between the gear 16 and the stationary gear 17, while the tube 13 is rotated, will cause the nozzles to be rotated in planes parallel with the pipe 12. It is to be understood that the gears 16 and 17 are not of exactly the same size so that the courses of the streams issuing from the nozzles 15 will take a different path on each revolution which they make about the central shaft 13.
The shaft 18 is rotated by means of a gear 19 thereon connected with a gear 20 engaged therewith and said gear 20 may be rotated by any desired means, such as the crank 21, or
through connection with some source of power such as an air engine or similar apparatus.
Itwill be noted that the cleaning appara- I tus is supported upon the upper end of the hatch way 5 but it is to be understood that it may be mounted in any desired manner, the object being to locate the nozzles 15 in such position within the tank that the streams of cleaning fluid may be directed under high pressure against the whole interior of the tank, it being found that in apparatus of this kind the whole inner side of the tank will be engaged by the streams of liquid during the rotation of the nozzles so that all sediment scale and dirt will be removed.
Simultaneously with the cleaning of the interior of the tank, I remove the cleaning liquid at once'from the bottom of said tank. This is done by means of a pump, the inlet port of which is connected with a pipe closely adjacent the bottom of the tank. This pump may be placed in any convenient position. I have shown the same as seated within the bottom of the tank adjacent the one being cleaned. This pump 23 has an inlet or suction line 24 directed through the wall between the two tanks and acting, to withdraw the cleaning liquid together with the sediment and this liquid is pumped out through the line 22 to the wing tank 7, where the sediment will settle out therefrom and the same cleaning liquid used over again.
In carrying out this process, the interior of the tank may be Washed first with hot water. The Water, after being heated in the wing tank through the heating coils, or through any other suitable means, is pumped under heavy pressure against the interior of the tank, removing the-sediment and the rust and washing the same to the bottom of the tank where it is at once removed. The removal of the cleaning liquid allows the streams of cleaningliquid which are directed against the bottom: to have a full cleaning effect thereon in the same manner as it has against the side and top walls.
The cleaning liquid proper is usually kerosene or some similar distillate which is heated and directed against the sides of the tank and the pumping of the same against the wall with force removes the rust and sediment from all the corners and crevices between the plates and the framework and washes it down to the bottom where it is at once removed. This process may be 'continued until the interior is entirely free of foreign material. This may take from four to eight hours, depending upon the state of the interior of the tank before the cleaning is begun.
In carrying out my improved method, it is essential that the pressure employed be sufiicient to erode or cut the scale and other sediment from the surface to be cleaned, and the initial pressure of the jets or streams as delivered into the tanks by the nozzles should not be substantially less than forty pounds to the square inch or 'even in those cases where the splashing reaction of the 'e'ts is 4 or even higher, is employed. F urthermoref the surfaces to be cleaned and particularly the bottom of the tank, wherein the greater f part of the sediment tends to collect, should be maintained substantially bare, that is, a large volume of liquid should not be allowed to collect thereon during the cleaning operation, in order that the high pressure jets may directly impinge against the sediment, rust, scale and like material to be eroded and to be removed, and accordin ly, for this purpose, the suction pump emp oyed for the removal of the liquid from the bottomof the tank should be positioned aft as in any empty vessel the draught will be this aft ,end will be the low point of the vessel, and therefor the suction pump should be so positioned that it will be in the aft. end or Whatever other osition is substantially the lowest point of t lie vesselso that the sur faces to be cleaned are substantially kept clear of a butler layer of cleaning liquid which is being recirculated through the vessel to be cleaned.
M improved process not only enables me to e ect the cleaning of cargo tanks at from 50% to 75% less cost than other processes now in use, but it accomplishes the cleaning of the ships pipe lines, pumps and valves simultaneously with the cleaning operation,
as I preferably include as part of my system the ships pump and pipe lines, and it thereby becomes unnecessary to renew the packing in the pipe system or open the'valves or customarily now the case when the cleaning of the ship is undertaken. i In order to prevent the cleaning fluid, particularly when kerosene is employed for this purpose, from being too rapi ly volatilized, I cause a solid jet of the same tobe propelled through the nozzles which deliver into the vessel being cleaned instead of effecting the introduction of the liquid in the form of an atomized spray.
When the cleaning operation is finished, it is preferred to remove the small residual body of liquid which may collect in the low point of the vessel when the operation of the apparatus is stopped by means of a vacuum pump or manually, as desired.
This method of cleaning the interior of tanks is not only quicker in its operation and more economical to carry out than is the old process, but itis much less harmful to the interior of the tank. All of the'sides of the tank areequally heated through the oil so such that thatthereis no unequal strain on the rivets.
Also all portions of the interior of the tank L are equally clean. All of the rust and'scalc can be thus removed so that no gas forming sediment can be left upon the walls of the tank. The vbottom of the tank is cleaned the tank may be used for the lighter distillates with practically no discoloration whatever to the liquid being carried. It also eliminates danger and discomfort to men who. under the old method, are compelled to enter the tanks to scrape and brush the surfaces, and eliminates exposure of these men togas and the heat. The further advantages thereof will be obvious to those skilled in the art.
"The ejector nozzles are, positively driven through gearing instead of reliance being placed upon the reaction obtainable frpm the high pressure of the liquid circulating therethrough to revolve the same since, owing to the unevenness of the surface upon which the high pressure jets im inge due to obstructions on the inside of tan ers, such as iron cross beams, there is a counter reaction transmitted back to the nozzles from the uneven surface of the tank and, due to the fact that they are arranged in pairs so as to counterbalance each other, they would if the reaction of the jets were the sole motive power cease to rotate entirely under certain conditions.
One of the principal advantages of my improved system resides in the fact that no preliminary steaming whatsoever of the tanks to be cleaned is-required either for the purpose of gas-freeing the same or for rendering the heavy oil residuum susceptible to removal 't't.,Asaconremove the pump heads or p p fittings as is by the high pressure lmpac e s sequence the deterioration of tankers and others vessels due to the expansion'and contraction strains under steaming with the consequent loosening of rivets and the acceleration of corrosion resulting from steaming operations is avoided while at the same time owing to the terrific direct erosion and melting action and secondary reflecting, splashing or rebounding action of the hot high pressure impact jets, it.is possible to completely gas-free and otherwise clean every crevice cleaningas well as the complete gas-freeing,
without the necessity for resorting to steaming with its attendant direct and indirect expense, are startling.
Where light :oil, such as gas oil or kerosene for example, is employed as the circulatory cleansing liquid, it will dissolve the otherwisevirtually useless bottom oil sediments or residues that can be run through the crack ing stills of a refinery, thus greatly reducing the cost of the cleaning, since the cleaning oil will be increased in bulk proportionate to the amount of residues dissolved therein.
Furthermore the residues, which are stripped or eroded as minute or small particles or droplets from the tank bottom and sides and the ships pipe lines as well, will float upon or be carried oif with the draw lating liquid. As a consequence, neither the pump lines nor the pump will be clogged up during the pumping operation with the gobs or snake-like strings of residuum from the tank, so that the cleaning is accomplished continuously without any halts or shut downs being required to blow out the accumulated masses or gobs of residue from the hose, the pump lines or the pump itself, and in this respect my process differs materially from other pumping operations now resorted to for p removing bottom residues from tanks and tankers.
What I claim as new is:
1. A recess of cleaning the interiors of tanks cargo-vessels and the like comprising heating a cleaning liquid, directing the said liquid in streams with force against the sides and the bottom walls of said tanks, and
simultaneously removing the used liquid at a rate to maintain the bottom walls free of liquid and in condition to be cleaned by the same operation.
2. A recess of cleaning the interior of oil tanks 0 the character described comprising fiushing the interior thereof with a jet'of hotwater, removing the used water and sediment, then directing a solid jet of hot kerosene with force against the bottom and other walls of said tanks, and maintaining said bottom walls approximately free of liquid and sediment to permit direct contact of said jets therewith.
3. In the process of cleaning oil tanks to remove residual deposits and gases therefrom, the step which comprises the repeated circulation of jets of hot water through said tank under high pressure while removing the introduced water at a rate sutficient to maintain the bottom substantially bare of an interposed bufier layer of cleansing water.
4. In the process of cleaning oil tanks to remove oil residuum therefrom, the steps which comprise delivering an impact jet of cleaning fluidinto the tank to be cleaned -n an arcuate path under a high initial pressure and in excess of -75 lbs. and during bottom of said tank substantially bare of charged into the tank as high pressure splash-- ing impact jets under a pressure of not less than 7 lbs. per square inch and portions of the liquid being withdrawn from the tank at a rate sufficient to substantially maintain the tank in a stripped condition and thereby avoid the interposition of a substantial buffer layer of liquid in the bottom of the tank and to thereby insure the direct impingement of the jets on the accumulations of dislodged residues, and,without substantially changing the zone of delivery of such jets into said tank, causing said jets to travel in predetermined but constantly changing aths.
In testimony whereof I hereunto afiix fii signature this th day of September, A. D.
ARTHUR B. BUTTERWORTH.
the delivery of such cleaning fluid maintaining the
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1806740A true US1806740A (en) | 1931-05-26 |
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|---|---|---|---|
| US1806740D Expired - Lifetime US1806740A (en) | A cobfoba |
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Cited By (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2542041A (en) * | 1943-10-22 | 1951-02-20 | Stearns Roger Mfg Company | Fluid treatment apparatus |
| US2550997A (en) * | 1949-02-14 | 1951-05-01 | Shell Dev | Inhibition of corrosion |
| US2714080A (en) * | 1952-12-31 | 1955-07-26 | Pyrate Sales Inc | Tank cleaning device and method |
| US2925223A (en) * | 1954-04-14 | 1960-02-16 | Producers Creamery Company Inc | Spray cleaning |
| US2933093A (en) * | 1954-08-18 | 1960-04-19 | British Miller Hydro Company L | Apparatus for cleansing liquid containing tanks or vessels |
| US2991203A (en) * | 1957-10-31 | 1961-07-04 | Cornelis In T Veld | Method and apparatus for cleaning the interior of a tank |
| US3022792A (en) * | 1959-05-25 | 1962-02-27 | Warren K Price | Apparatus for gas-freeing and cleaning tankers |
| US3052574A (en) * | 1958-05-14 | 1962-09-04 | Pyrate Sales Inc | Tank cleaning device and method |
| US3074078A (en) * | 1959-07-06 | 1963-01-22 | Sigurd F Varian | Swimming pool cleaning method and apparatus |
| US3090393A (en) * | 1959-07-06 | 1963-05-21 | Edward L Valentine | Method and apparatus for cleaning tanks |
| US3113046A (en) * | 1954-04-14 | 1963-12-03 | Producers Creamery Company Inc | Spray cleaning |
| US3120237A (en) * | 1961-03-15 | 1964-02-04 | Pure Oil Co | Crankcase spray device |
| US3140828A (en) * | 1963-02-26 | 1964-07-14 | Theodore E Ferris & Sons | Tank washing system |
| US3730193A (en) * | 1971-04-12 | 1973-05-01 | Texaco Development Corp | Method and apparatus for preventing electrostatic fields in large tanks |
| US3746023A (en) * | 1972-03-22 | 1973-07-17 | Gulf Oil Corp | Method for cleaning oil tanker holds |
| JPS4925511A (en) * | 1972-07-03 | 1974-03-07 | ||
| US4153553A (en) * | 1977-09-29 | 1979-05-08 | Davis Larry R | Apparatus for and method of reclaiming and cleaning oil from bottom settlings of tanks |
| EP0032813B1 (en) * | 1980-01-19 | 1984-04-11 | Emultec Limited | Recovery of heavy hydrocarbons from oil sludge |
| US20030137895A1 (en) * | 2000-09-22 | 2003-07-24 | Hummer Jan Stumpe | Method and a process plant for treating a batch of liquids |
| WO2005009876A3 (en) * | 2003-07-17 | 2005-08-04 | Saudi Arabian Oil Co | Gas expansion trunk for marine vessels |
-
0
- US US1806740D patent/US1806740A/en not_active Expired - Lifetime
Cited By (29)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2542041A (en) * | 1943-10-22 | 1951-02-20 | Stearns Roger Mfg Company | Fluid treatment apparatus |
| US2550997A (en) * | 1949-02-14 | 1951-05-01 | Shell Dev | Inhibition of corrosion |
| US2714080A (en) * | 1952-12-31 | 1955-07-26 | Pyrate Sales Inc | Tank cleaning device and method |
| US3113046A (en) * | 1954-04-14 | 1963-12-03 | Producers Creamery Company Inc | Spray cleaning |
| US2925223A (en) * | 1954-04-14 | 1960-02-16 | Producers Creamery Company Inc | Spray cleaning |
| US2933093A (en) * | 1954-08-18 | 1960-04-19 | British Miller Hydro Company L | Apparatus for cleansing liquid containing tanks or vessels |
| US2991203A (en) * | 1957-10-31 | 1961-07-04 | Cornelis In T Veld | Method and apparatus for cleaning the interior of a tank |
| US3052574A (en) * | 1958-05-14 | 1962-09-04 | Pyrate Sales Inc | Tank cleaning device and method |
| US3022792A (en) * | 1959-05-25 | 1962-02-27 | Warren K Price | Apparatus for gas-freeing and cleaning tankers |
| US3090393A (en) * | 1959-07-06 | 1963-05-21 | Edward L Valentine | Method and apparatus for cleaning tanks |
| US3074078A (en) * | 1959-07-06 | 1963-01-22 | Sigurd F Varian | Swimming pool cleaning method and apparatus |
| US3120237A (en) * | 1961-03-15 | 1964-02-04 | Pure Oil Co | Crankcase spray device |
| US3140828A (en) * | 1963-02-26 | 1964-07-14 | Theodore E Ferris & Sons | Tank washing system |
| US3730193A (en) * | 1971-04-12 | 1973-05-01 | Texaco Development Corp | Method and apparatus for preventing electrostatic fields in large tanks |
| US3746023A (en) * | 1972-03-22 | 1973-07-17 | Gulf Oil Corp | Method for cleaning oil tanker holds |
| JPS4925511A (en) * | 1972-07-03 | 1974-03-07 | ||
| US3874399A (en) * | 1972-07-03 | 1975-04-01 | Fuji Oil Co Ltd | Delivery system for high melting point oils in a tank |
| US4153553A (en) * | 1977-09-29 | 1979-05-08 | Davis Larry R | Apparatus for and method of reclaiming and cleaning oil from bottom settlings of tanks |
| EP0032813B1 (en) * | 1980-01-19 | 1984-04-11 | Emultec Limited | Recovery of heavy hydrocarbons from oil sludge |
| US20050207268A1 (en) * | 2000-09-22 | 2005-09-22 | Hummer Jan Stumpe | Method and a process plant for treating a batch of liquids |
| US20030137895A1 (en) * | 2000-09-22 | 2003-07-24 | Hummer Jan Stumpe | Method and a process plant for treating a batch of liquids |
| US7059759B2 (en) * | 2000-09-22 | 2006-06-13 | Iso-Mix A/S | Method and a process plant for treating a batch of liquids |
| WO2005009876A3 (en) * | 2003-07-17 | 2005-08-04 | Saudi Arabian Oil Co | Gas expansion trunk for marine vessels |
| US20070034131A1 (en) * | 2003-07-17 | 2007-02-15 | Saudi Arabian Oil Company | Gas expansion trunk for marine vessels |
| JP2007537907A (en) * | 2003-07-17 | 2007-12-27 | サウジ アラビアン オイル カンパニー | Gas expansion trunk for marine vessels |
| KR100971895B1 (en) | 2003-07-17 | 2010-07-23 | 사우디 아라비안 오일 컴퍼니 | Gas expansion trunks for marine vessels and marine vessels |
| US7905191B2 (en) | 2003-07-17 | 2011-03-15 | Saudi Arabian Oil Company | Gas expansion trunk for marine vessels |
| CN1849242B (en) * | 2003-07-17 | 2011-04-20 | 沙特阿拉伯石油公司 | Marine vessel with gas expansion trunk |
| EP1648759A4 (en) * | 2003-07-17 | 2012-01-04 | Saudi Arabian Oil Co | Gas expansion trunk for marine vessels |
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