CA1262330A - Apparatus for cleaning an oil contaminated vessel - Google Patents
Apparatus for cleaning an oil contaminated vesselInfo
- Publication number
- CA1262330A CA1262330A CA000458145A CA458145A CA1262330A CA 1262330 A CA1262330 A CA 1262330A CA 000458145 A CA000458145 A CA 000458145A CA 458145 A CA458145 A CA 458145A CA 1262330 A CA1262330 A CA 1262330A
- Authority
- CA
- Canada
- Prior art keywords
- tank
- fluidized
- sludge
- compartment
- pump
- 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
Links
- 238000004140 cleaning Methods 0.000 title description 17
- 239000010802 sludge Substances 0.000 claims abstract description 65
- 239000007921 spray Substances 0.000 claims abstract description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 20
- 239000007787 solid Substances 0.000 claims description 14
- 239000007764 o/w emulsion Substances 0.000 claims description 4
- 238000000034 method Methods 0.000 abstract description 16
- 239000003995 emulsifying agent Substances 0.000 abstract description 4
- 239000003921 oil Substances 0.000 description 35
- 239000000839 emulsion Substances 0.000 description 19
- 239000003795 chemical substances by application Substances 0.000 description 7
- 239000010779 crude oil Substances 0.000 description 4
- 239000004215 Carbon black (E152) Substances 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000003209 petroleum derivative Substances 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- VEUMANXWQDHAJV-UHFFFAOYSA-N 2-[2-[(2-hydroxyphenyl)methylideneamino]ethyliminomethyl]phenol Chemical compound OC1=CC=CC=C1C=NCCN=CC1=CC=CC=C1O VEUMANXWQDHAJV-UHFFFAOYSA-N 0.000 description 1
- 208000034723 Amelia Diseases 0.000 description 1
- 208000006586 Ectromelia Diseases 0.000 description 1
- 206010024503 Limb reduction defect Diseases 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 239000013529 heat transfer fluid Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000008161 low-grade oil Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 230000000750 progressive effect Effects 0.000 description 1
- BALXUFOVQVENIU-KXNXZCPBSA-N pseudoephedrine hydrochloride Chemical compound [H+].[Cl-].CN[C@@H](C)[C@@H](O)C1=CC=CC=C1 BALXUFOVQVENIU-KXNXZCPBSA-N 0.000 description 1
- 230000003134 recirculating effect Effects 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000007762 w/o emulsion Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002569 water oil cream Substances 0.000 description 1
Classifications
-
- 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
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Ocean & Marine Engineering (AREA)
- Cleaning In General (AREA)
- Cleaning By Liquid Or Steam (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
A B S T R A C T
An apparatus and process adapted to clean oil contaminated vessels which uses a closed fluidized system through which fluidized sludge is recirculated to be sprayed under pressure on interior walls of the vessel. Emulsifying agents are added to the vessel to initially form a pool of fluidized sludge in the vessel which is then conveyed to a tank and from the tank conveyed to a high pressure spray where it is sprayed onto the walls to fluidize more sludge.
An apparatus and process adapted to clean oil contaminated vessels which uses a closed fluidized system through which fluidized sludge is recirculated to be sprayed under pressure on interior walls of the vessel. Emulsifying agents are added to the vessel to initially form a pool of fluidized sludge in the vessel which is then conveyed to a tank and from the tank conveyed to a high pressure spray where it is sprayed onto the walls to fluidize more sludge.
Description
~ 23~
~`~, ~eE~S~ APPARATUS FOR CLEANING AN OIL CONTAMINATED
VESSEL
~ ,~
FIELD OF THE INVENTION
-This invention relates to an apparatus and process for cleaning an oil contaminated vessel having one or more cargo compartments each containing sludge utilizing a closed fluidized circuit.
BACKGROUND OF THE INVENTIC)N
Vessels containing oil, such as storage tanks, tank cars, oceangoing tankers, barges, pipelines or other structures for storlng or transporting crud~ oil or petroleum products will over a period of time aceumulate large amounts of sludge made up of chemical or hydrocarbon deposits which ~5 deposits occur particularly in crude oils or heavy oils.
Build up of such sludge over a period of time subtracts from the load carrying or s~orage capacity of the vessel.
Further build up of sludge in oil conveying vessels such as tank cars or trucks results in carrying excess dead weight when the vessel is returned empty from a delivery point to a shipping point thus increasing cost of operations.
Consequently the interiors of such vessels must be cleaned from time to time of accumulation of sludge.
Further vessels carrying or s~oring crude oil or other petroleum products, particularly barges and oceangoing tankers, are often used to carry other products besides oils or carry other grades of oils. It thus becomes necessary to cleanse the interior of such vessels prior to being lo~dQd with other products or higher grades of oil Vessels of this type must be cleansed to a gas free state from time to time so that they may be entered for periodic inspection - or for repair in the event of damage.
Existing techniques for ~leaning oil carrying vessels has involved the use of steam and water applied in large volumes through spray nozzles agains~ interior side walls of the vessels under high pressure. Occasionally ,, . _ ~2~i233~
chemicals are used in the cleaning but generally such cleaning systems involve the use of large volumes of water.
This techique of cleaning has proved to be labor intensive, energy intensi~e, and generally results in the Eormation of large volumes of oil contaminated waste water. Vessels cleaned utilizing this technique are often not completely free of hydrocarbon deposits and are not suitable for upgrading and carrying or storing other products without further hand cleaning of the interior of the vessel.
It is ther~fore an object of our invention to provide for an apparatus and process for cleaning an oil contaminated vessel which will utilize a minimum of water and which will substantially completely clean an oil contaminated vessel of oil and any sludge in a comparatively short time and at minimal expense.
It is a still further object of the invention to provide for an apparatus and method of cleaning oil contaminated vessels of oil and sludge by which usable oil may be conveniently recovered for further use.
~0 GENERAL DESCRIPTION OF THE INVENTION
Broadly a process for cleaning an oil contaminated vessel according to our invention involves use of a closed recirculating fluidized system or circuit where the system has a tank, a discharge means extending from the interior of a compartment within the vessel to the tank and a pressurized spray means extending from the tank to the interior of the compartment by which the contents of the tank may be sprayed onto the interior walls of the compartment.
The process involves the steps of treating the sludge with a fluidizing agent to form a pool of fluidized sludge which is then circulated through ~he system and sprayed under pressure onto the interior walls of the compartment. When the fluidized sludge spray contacts the walls it cleans oil from the walls and also fluidizes any sludge thereon to increase the size of the pool in the bottom of the compartment ~26Z33~
containing fluidized sludge. This fluidized sludge i8 then discharged from the vessel to the tank where it is recir-culated again through the pressurized spray means back to the compartment. This recirculation is continued until the compartment is substantially cleansed of sludge leaving onl~
a film of self emulsifiable oil.
The fluidizing agent may be initially added directly to the compartment to form an initial pool of fluidized sludge which is then conveyed to the tank or the agent may be added directly to the tank after which it is circulated ~hrough the pressurized spray means onto the interior side walls of the compartment so as to form a pool of fluidized sludge.
Preferably the fluidized sludge is heated conven-iently by a heat exchanger in the tank to further enhancethe cleaning action. The tank itself may act as a settling tank to capture any large solids such as rust or sand particles to prevent their being recirculated in the closed system through the pressurized spray means.
Sufficient fluidizing agent is periodically added to the system, ei~her directly to the tank or to the com-partment being cleaned, to maintain fluidity of the sludge.
The process may include the further step of periodically removing excess oil from the closed system and trans~erring it to a holding tank.
The remaining film of self emulsifiable oil left in the compartment after being sprayed with the fluidized sludge may then be completely removed by rinsing with a small amount of hot or cold water using a standard spray type Butterworth wash system. The rinse water is then stripped from the compartment and transferred to a separating tank where oil is allowed to separate from the water. The recovered oil may then be used as a fuel or reclaimed for refining and the rinse water may be drawn off and used in subsequent rinsing. By this procedure use of rinse water is minimized while at the same time oil is recovered.
~iZ~3~
The process described above may use water as a component of a wash solution when the vessel being cleaned contains low grade oil or crude oil sludge. In this case the sludge itself may contain from 0 to 40% water as a water in oil emulsion. The fluidizing agent serves to invert the emulsion to orm an oil in water emulsion having much better flow characteristics. #6 oil normally does not contain any water such that the fluidized oil recovered will be water free when vessels containing such oil are cleaned.
The process described above is also applicable for use in cleaning vessels having a plurality of compartments each containing sludge. In this instance fluidized sludge from the first compartment cleansed is sprayed into a second or further compartment to form an initial pool of fluidized sludge in the second compartment which is then recirculated through the closed fluidized system until the second compartment is substantially cleansed of sludge.
An apparatus constructed according to our invention comprises broadly a tank adapted to hold the fluidized sludge or emulsion, a pressurized spray means extending from the tank and adapted to extend into the interior of a compartment containing sludge and a discharge means having one end connected to the tank and an opposite end adapted to be connected to the compartment to remove fluidized sludge or emulsion therefrom to the tank.
The pressurized spray means preferably includes a first pump and the discharge means a second pump with both pumps being of equal capacity and driven by a common drive means to assure that both operate with equal throughput.
The pumps, drive means and tank are mounted on a common base such as a skid to form a unit which can be conveniently lifted into position, as for example onto the deck of a bargeO in order to clean cargo compartments.
The tank preferably has a ver~ical baffle therein dividing the tank into a solids settling portion and into a substantially solids free portion connected to the pressurized . _ _ ~2~ 3~
spray means.
The apparatus also preferably may include a separating tank in which excess oil or emulsion may be transferred from the closed fluidized circuit. Oil is allowed to separate from the emulsion in the separating tank where it is then removed for further use while the remaining water is available for furthex use.
BRIEF DESCRIPTION OF THE DRAWINGS
Figure l is a diagrammatic view of an apparatus constructed according to the invention mounted in part on an oil tanker having a plurality of compartments to be cleaned;
and, Figure 2 is an enlarged sectional view of a portion of the apparatus disclosed in Figure l.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
Referring to Figure l, there is illustrated a vessel in the form of an oil tanker l having a plurality of-cargo compartments 2, 3, 4 and S accessible by hatches 6.
An apparatus l0 adapted to clean the compartments is lifted into place onto the deck of the tanker where it is available for operation. As shown in Figure 2, the apparatus comprises a tank 20, a discharge means 21 having one end 22 connected to the tank 20 and an opposite end 23, shown in Figure l, adapted to extend into a pool 24 of fluidized sludge in a compartment in order to discharge fluidized sludge or an emulsion from the compartment into the tank 20.
The apparatus l0 also includes a pressurized spray means 25 terminating in a spray head or nozzle 26 adapted to extend into a compartment in order that fluidized sludge or emulsion contained in ~he tank 20 may be sprayed under pressure onto the interior side walls and bottom of a compartment to clean the same of sludge.
The pressurized spray means 25 includes a first pump 30 to convey emulsion under pressure to the nozzle 25.
- If desired, filter means 31 may be included in the pressurized spray means to catch and fiiter any debris that might 510g the nozzle 26.
The discharge means 21 includes a second pump 32 the intake of which is adapted to communicate with a compartment and the outlet of which extends to the,tank 20.
Pumps 30 and 32 are of equal capacity and are preferably driven by a common drive means 36 in the form of an internal combustion engine or electric motor. The pumps are coupled through independent transmissions so that they may be operated independently or at the same speed and through put.
The tank 20, pumps 30 and 32 as well as the common drive means 36 are mounted on a base or skid 38 so that the several parts making up the apparatus may be considered as a unit which may be easily lifted onto the deck or other portion of a vessel to be cleaned.
The tank 20 besides acting as a,holding tank also acts as a settling tank to entrap large solids, such as sand or rust particles, that may be circulated within the tank.
To assist in this function ,a vertically extending baffle 40 extends upwardly from the bottom of the tank about three quarters of the height of the tank to divide the tank into a solids settling portion 41 and a solids free portion 42. The end 22 of the discharge means 21 discharges into the top of the solids settling portion 41 while the intake of the pump 30 draws from the bottom of the solids free portion 42 which further minimizes likelihood of solids being drawn into the pump 30.
Preferably a heat transfer means in the form of coils 45 are contained in the tank 20 to heat the circulated emulsion to further enhar.ce cleaning action. The coils may be connected by piping to a boiler, not shown, contained at a convenient location, as for example an on-shore site, which heats a heat transfer fluid, for example steam, which is circulated through the coils. While the coils are shown in the solids settling portion of ~he tank, they could be _= _ ~Z623~
located in any portion of the closed fluidized system defined by ~h~ discharge means 21, the ~ank 20 and the pressurized spray mea~s 25.
The apparatus preferably also has a separating tank 50 sited on shore to which excess oil or e~ulsion is drawn by a pump 51 through a discharge conduit 52 which as shown e~tenas into the pool of fluidized sludge 24. The conduit 52 could just as conve~ie~tly~extend to the tank 20 or other por~ion of the closed fluidized syst~m to withdraw excess oi~ or e.~ulsion therefrom. Oil is separated out of the emulsion in ~he separating ~ank 50 where i~ may be removed ~or further use, as for example, a'fuel. The remaining water is then available to be returned by conduit 53 to a holding tank not shown, where it is available for subse~uent rinsing o~ a compar~ment cleaned of sludge.
The spray head or nozzle 26 preferably comprises a jet nozzle and may be of the portable type such as a Gunclean 270 A manufactured by Salen and Wicander Marin AB, Gothenburg, Sweden. The nozzle is further preferably programmable and driven by air so as to move through pre-detenmined arcs both in ver~ical planes and in horizontal planes to assure that a jet of fluidized sludge or emulsion will contact those areas of a compartment to be cleaned. We have found that in many vessels, it is not necessary to cle-n the top of the interior of the vessel since this area does not come in~o contact with a cargo or a stored material 50 in suc~ ins.ances the nozzle is programmed such that the jet of emulsion will not contac~ top interior surfaces of the vessel.
We have found that an appara~us as desc~ibed operates successfully where the tank 20 has a capacity of approxim2tely 2~0 gallons ~nd pump pressure is on t~e orce-of 100-150 psig. The pumps the~sel~es may be of a progressive cavity type as manufac~ured by Moyno Products, Robbins &
Mye_s, Inc., Springfield, Ohio.
.i~
-8~ 3~
The process for cleaning a vessel of contaminated sludge utilizing the apparatus as described above is as follows:
Approximately one fifty-five gallon drum of an emulsifying agent is added to an end compartment of a vessel having a plurality of compartments each having a capacity of approximately two thousand barrels, for example, compartmen~
~`~, ~eE~S~ APPARATUS FOR CLEANING AN OIL CONTAMINATED
VESSEL
~ ,~
FIELD OF THE INVENTION
-This invention relates to an apparatus and process for cleaning an oil contaminated vessel having one or more cargo compartments each containing sludge utilizing a closed fluidized circuit.
BACKGROUND OF THE INVENTIC)N
Vessels containing oil, such as storage tanks, tank cars, oceangoing tankers, barges, pipelines or other structures for storlng or transporting crud~ oil or petroleum products will over a period of time aceumulate large amounts of sludge made up of chemical or hydrocarbon deposits which ~5 deposits occur particularly in crude oils or heavy oils.
Build up of such sludge over a period of time subtracts from the load carrying or s~orage capacity of the vessel.
Further build up of sludge in oil conveying vessels such as tank cars or trucks results in carrying excess dead weight when the vessel is returned empty from a delivery point to a shipping point thus increasing cost of operations.
Consequently the interiors of such vessels must be cleaned from time to time of accumulation of sludge.
Further vessels carrying or s~oring crude oil or other petroleum products, particularly barges and oceangoing tankers, are often used to carry other products besides oils or carry other grades of oils. It thus becomes necessary to cleanse the interior of such vessels prior to being lo~dQd with other products or higher grades of oil Vessels of this type must be cleansed to a gas free state from time to time so that they may be entered for periodic inspection - or for repair in the event of damage.
Existing techniques for ~leaning oil carrying vessels has involved the use of steam and water applied in large volumes through spray nozzles agains~ interior side walls of the vessels under high pressure. Occasionally ,, . _ ~2~i233~
chemicals are used in the cleaning but generally such cleaning systems involve the use of large volumes of water.
This techique of cleaning has proved to be labor intensive, energy intensi~e, and generally results in the Eormation of large volumes of oil contaminated waste water. Vessels cleaned utilizing this technique are often not completely free of hydrocarbon deposits and are not suitable for upgrading and carrying or storing other products without further hand cleaning of the interior of the vessel.
It is ther~fore an object of our invention to provide for an apparatus and process for cleaning an oil contaminated vessel which will utilize a minimum of water and which will substantially completely clean an oil contaminated vessel of oil and any sludge in a comparatively short time and at minimal expense.
It is a still further object of the invention to provide for an apparatus and method of cleaning oil contaminated vessels of oil and sludge by which usable oil may be conveniently recovered for further use.
~0 GENERAL DESCRIPTION OF THE INVENTION
Broadly a process for cleaning an oil contaminated vessel according to our invention involves use of a closed recirculating fluidized system or circuit where the system has a tank, a discharge means extending from the interior of a compartment within the vessel to the tank and a pressurized spray means extending from the tank to the interior of the compartment by which the contents of the tank may be sprayed onto the interior walls of the compartment.
The process involves the steps of treating the sludge with a fluidizing agent to form a pool of fluidized sludge which is then circulated through ~he system and sprayed under pressure onto the interior walls of the compartment. When the fluidized sludge spray contacts the walls it cleans oil from the walls and also fluidizes any sludge thereon to increase the size of the pool in the bottom of the compartment ~26Z33~
containing fluidized sludge. This fluidized sludge i8 then discharged from the vessel to the tank where it is recir-culated again through the pressurized spray means back to the compartment. This recirculation is continued until the compartment is substantially cleansed of sludge leaving onl~
a film of self emulsifiable oil.
The fluidizing agent may be initially added directly to the compartment to form an initial pool of fluidized sludge which is then conveyed to the tank or the agent may be added directly to the tank after which it is circulated ~hrough the pressurized spray means onto the interior side walls of the compartment so as to form a pool of fluidized sludge.
Preferably the fluidized sludge is heated conven-iently by a heat exchanger in the tank to further enhancethe cleaning action. The tank itself may act as a settling tank to capture any large solids such as rust or sand particles to prevent their being recirculated in the closed system through the pressurized spray means.
Sufficient fluidizing agent is periodically added to the system, ei~her directly to the tank or to the com-partment being cleaned, to maintain fluidity of the sludge.
The process may include the further step of periodically removing excess oil from the closed system and trans~erring it to a holding tank.
The remaining film of self emulsifiable oil left in the compartment after being sprayed with the fluidized sludge may then be completely removed by rinsing with a small amount of hot or cold water using a standard spray type Butterworth wash system. The rinse water is then stripped from the compartment and transferred to a separating tank where oil is allowed to separate from the water. The recovered oil may then be used as a fuel or reclaimed for refining and the rinse water may be drawn off and used in subsequent rinsing. By this procedure use of rinse water is minimized while at the same time oil is recovered.
~iZ~3~
The process described above may use water as a component of a wash solution when the vessel being cleaned contains low grade oil or crude oil sludge. In this case the sludge itself may contain from 0 to 40% water as a water in oil emulsion. The fluidizing agent serves to invert the emulsion to orm an oil in water emulsion having much better flow characteristics. #6 oil normally does not contain any water such that the fluidized oil recovered will be water free when vessels containing such oil are cleaned.
The process described above is also applicable for use in cleaning vessels having a plurality of compartments each containing sludge. In this instance fluidized sludge from the first compartment cleansed is sprayed into a second or further compartment to form an initial pool of fluidized sludge in the second compartment which is then recirculated through the closed fluidized system until the second compartment is substantially cleansed of sludge.
An apparatus constructed according to our invention comprises broadly a tank adapted to hold the fluidized sludge or emulsion, a pressurized spray means extending from the tank and adapted to extend into the interior of a compartment containing sludge and a discharge means having one end connected to the tank and an opposite end adapted to be connected to the compartment to remove fluidized sludge or emulsion therefrom to the tank.
The pressurized spray means preferably includes a first pump and the discharge means a second pump with both pumps being of equal capacity and driven by a common drive means to assure that both operate with equal throughput.
The pumps, drive means and tank are mounted on a common base such as a skid to form a unit which can be conveniently lifted into position, as for example onto the deck of a bargeO in order to clean cargo compartments.
The tank preferably has a ver~ical baffle therein dividing the tank into a solids settling portion and into a substantially solids free portion connected to the pressurized . _ _ ~2~ 3~
spray means.
The apparatus also preferably may include a separating tank in which excess oil or emulsion may be transferred from the closed fluidized circuit. Oil is allowed to separate from the emulsion in the separating tank where it is then removed for further use while the remaining water is available for furthex use.
BRIEF DESCRIPTION OF THE DRAWINGS
Figure l is a diagrammatic view of an apparatus constructed according to the invention mounted in part on an oil tanker having a plurality of compartments to be cleaned;
and, Figure 2 is an enlarged sectional view of a portion of the apparatus disclosed in Figure l.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
Referring to Figure l, there is illustrated a vessel in the form of an oil tanker l having a plurality of-cargo compartments 2, 3, 4 and S accessible by hatches 6.
An apparatus l0 adapted to clean the compartments is lifted into place onto the deck of the tanker where it is available for operation. As shown in Figure 2, the apparatus comprises a tank 20, a discharge means 21 having one end 22 connected to the tank 20 and an opposite end 23, shown in Figure l, adapted to extend into a pool 24 of fluidized sludge in a compartment in order to discharge fluidized sludge or an emulsion from the compartment into the tank 20.
The apparatus l0 also includes a pressurized spray means 25 terminating in a spray head or nozzle 26 adapted to extend into a compartment in order that fluidized sludge or emulsion contained in ~he tank 20 may be sprayed under pressure onto the interior side walls and bottom of a compartment to clean the same of sludge.
The pressurized spray means 25 includes a first pump 30 to convey emulsion under pressure to the nozzle 25.
- If desired, filter means 31 may be included in the pressurized spray means to catch and fiiter any debris that might 510g the nozzle 26.
The discharge means 21 includes a second pump 32 the intake of which is adapted to communicate with a compartment and the outlet of which extends to the,tank 20.
Pumps 30 and 32 are of equal capacity and are preferably driven by a common drive means 36 in the form of an internal combustion engine or electric motor. The pumps are coupled through independent transmissions so that they may be operated independently or at the same speed and through put.
The tank 20, pumps 30 and 32 as well as the common drive means 36 are mounted on a base or skid 38 so that the several parts making up the apparatus may be considered as a unit which may be easily lifted onto the deck or other portion of a vessel to be cleaned.
The tank 20 besides acting as a,holding tank also acts as a settling tank to entrap large solids, such as sand or rust particles, that may be circulated within the tank.
To assist in this function ,a vertically extending baffle 40 extends upwardly from the bottom of the tank about three quarters of the height of the tank to divide the tank into a solids settling portion 41 and a solids free portion 42. The end 22 of the discharge means 21 discharges into the top of the solids settling portion 41 while the intake of the pump 30 draws from the bottom of the solids free portion 42 which further minimizes likelihood of solids being drawn into the pump 30.
Preferably a heat transfer means in the form of coils 45 are contained in the tank 20 to heat the circulated emulsion to further enhar.ce cleaning action. The coils may be connected by piping to a boiler, not shown, contained at a convenient location, as for example an on-shore site, which heats a heat transfer fluid, for example steam, which is circulated through the coils. While the coils are shown in the solids settling portion of ~he tank, they could be _= _ ~Z623~
located in any portion of the closed fluidized system defined by ~h~ discharge means 21, the ~ank 20 and the pressurized spray mea~s 25.
The apparatus preferably also has a separating tank 50 sited on shore to which excess oil or e~ulsion is drawn by a pump 51 through a discharge conduit 52 which as shown e~tenas into the pool of fluidized sludge 24. The conduit 52 could just as conve~ie~tly~extend to the tank 20 or other por~ion of the closed fluidized syst~m to withdraw excess oi~ or e.~ulsion therefrom. Oil is separated out of the emulsion in ~he separating ~ank 50 where i~ may be removed ~or further use, as for example, a'fuel. The remaining water is then available to be returned by conduit 53 to a holding tank not shown, where it is available for subse~uent rinsing o~ a compar~ment cleaned of sludge.
The spray head or nozzle 26 preferably comprises a jet nozzle and may be of the portable type such as a Gunclean 270 A manufactured by Salen and Wicander Marin AB, Gothenburg, Sweden. The nozzle is further preferably programmable and driven by air so as to move through pre-detenmined arcs both in ver~ical planes and in horizontal planes to assure that a jet of fluidized sludge or emulsion will contact those areas of a compartment to be cleaned. We have found that in many vessels, it is not necessary to cle-n the top of the interior of the vessel since this area does not come in~o contact with a cargo or a stored material 50 in suc~ ins.ances the nozzle is programmed such that the jet of emulsion will not contac~ top interior surfaces of the vessel.
We have found that an appara~us as desc~ibed operates successfully where the tank 20 has a capacity of approxim2tely 2~0 gallons ~nd pump pressure is on t~e orce-of 100-150 psig. The pumps the~sel~es may be of a progressive cavity type as manufac~ured by Moyno Products, Robbins &
Mye_s, Inc., Springfield, Ohio.
.i~
-8~ 3~
The process for cleaning a vessel of contaminated sludge utilizing the apparatus as described above is as follows:
Approximately one fifty-five gallon drum of an emulsifying agent is added to an end compartment of a vessel having a plurality of compartments each having a capacity of approximately two thousand barrels, for example, compartmen~
2 of the tanker shown in Figure 1. A hose is attached to the suction side of the pump 32 and lowered to a pickup point at the lowest part of the compartment, which may be conveniently formed by ballasting to impart a list to the tanker to lower one end.
The emulsifying agent will fluidize some of the sludge in the tank so as to form a pool of fluidized sludge.
As the sludge becomes fluidized, it is conveyed to the tank 20 by the pump 32 where it can be heated and the fluidized sludge or emulsion (in the case of crude oil) is then circulated through the tank 20 into the pressurized spray means and onto the walls of the compartment. This recirculation of fluidized sludge or emulsion is continued until the compartment walls have been cleansed of sludge and all of the sludge in the bottom of the compartment has been fluidized. During this time it may become necessary to add further fluidizing agent to the recirculated fluidized sludge 2 or emulsion to maintain fluidity of the sludge which can be determined by checking the fluidity in the tank 20.
When all of the sludge in the tank has been fluidized, it is pumped into the separating tank 50 and the nozzle 26 is moved to the next adjacent compartment 3. A
small amount of the fluidized sludge or emulsion from compartment 2 may be used as a beginning pool of fluidized sludge for the next adjacent compartment 3 to be cleaned.
This is accomplished by leaving the end 23 of the discharge means in the pool 24 of compartment 2 until the nozzle 26 has sprayed sufficient fluidized sludge or emulsion Qnto the walls of compartment 3 to form a pool o~ fluidized sludge in that ~L26~33~
compartment after which the end 23 is moved to the pool in compartment 3 such that fluidized sludge or emulsion from that ~ompaxtment is then recirculated through the closed fluidizing system. This procedure is repeated for cleaning the remaining compartments.
Portions of the walls of a compartment may be masked or shaded by interior structure from impingement by the spray from the nozzle 26. These untouched portions may be cleaned by a hand~held spray from the deck or by someone entering the compartment to spray the fluidizing agent directly onto the untouched areas followed by washing with a hand-held water hose.
The compartment after cleaning is then rinsed with cold water using Butterworth nozzles for approximately fifteen to thirty minutes to form an oil water emulsion.
This emulsion is continuously removed from the compartment during rinsing and txasferred to a holding tank, not shown.
An oil layer will form on the surface within the holding tank after a few hours and the rinse water may be decanted from the bottom of the tank and recycled for future rinsing.
Emulsifying agents suitable for use in the described process are of the types disclosed in United States Patent No.4,276,094 and those sold by Petroferm U.S.A., Amelia Island, Florida No.'s PFC-2209, PFC-0247 or We have found that the process and apparatus asdescribed above results in much faster cleaning of oil contaminated vessels than when compared to conventional hot water or steam systems. Further because we utilize a closed fluidized system through which fluidized sludge is re-circulated, production of large amounts of waste water and attendant disposal problems are minimized.
The emulsifying agent will fluidize some of the sludge in the tank so as to form a pool of fluidized sludge.
As the sludge becomes fluidized, it is conveyed to the tank 20 by the pump 32 where it can be heated and the fluidized sludge or emulsion (in the case of crude oil) is then circulated through the tank 20 into the pressurized spray means and onto the walls of the compartment. This recirculation of fluidized sludge or emulsion is continued until the compartment walls have been cleansed of sludge and all of the sludge in the bottom of the compartment has been fluidized. During this time it may become necessary to add further fluidizing agent to the recirculated fluidized sludge 2 or emulsion to maintain fluidity of the sludge which can be determined by checking the fluidity in the tank 20.
When all of the sludge in the tank has been fluidized, it is pumped into the separating tank 50 and the nozzle 26 is moved to the next adjacent compartment 3. A
small amount of the fluidized sludge or emulsion from compartment 2 may be used as a beginning pool of fluidized sludge for the next adjacent compartment 3 to be cleaned.
This is accomplished by leaving the end 23 of the discharge means in the pool 24 of compartment 2 until the nozzle 26 has sprayed sufficient fluidized sludge or emulsion Qnto the walls of compartment 3 to form a pool o~ fluidized sludge in that ~L26~33~
compartment after which the end 23 is moved to the pool in compartment 3 such that fluidized sludge or emulsion from that ~ompaxtment is then recirculated through the closed fluidizing system. This procedure is repeated for cleaning the remaining compartments.
Portions of the walls of a compartment may be masked or shaded by interior structure from impingement by the spray from the nozzle 26. These untouched portions may be cleaned by a hand~held spray from the deck or by someone entering the compartment to spray the fluidizing agent directly onto the untouched areas followed by washing with a hand-held water hose.
The compartment after cleaning is then rinsed with cold water using Butterworth nozzles for approximately fifteen to thirty minutes to form an oil water emulsion.
This emulsion is continuously removed from the compartment during rinsing and txasferred to a holding tank, not shown.
An oil layer will form on the surface within the holding tank after a few hours and the rinse water may be decanted from the bottom of the tank and recycled for future rinsing.
Emulsifying agents suitable for use in the described process are of the types disclosed in United States Patent No.4,276,094 and those sold by Petroferm U.S.A., Amelia Island, Florida No.'s PFC-2209, PFC-0247 or We have found that the process and apparatus asdescribed above results in much faster cleaning of oil contaminated vessels than when compared to conventional hot water or steam systems. Further because we utilize a closed fluidized system through which fluidized sludge is re-circulated, production of large amounts of waste water and attendant disposal problems are minimized.
Claims (9)
1. Apparatus adapted to clean an oil contaminated vessel having at least one compartment containing sludge comprising a tank adapted to hold fluidized sludge, pressurized spray means extending from said tank and adapted to extend into the interior of a compartment by which said fluidized sludge may be sprayed onto the interior sides of the compartment to fluidize further sludge therein to form a pool of fluidized sludge in the bottom of said compartment, discharge means having one end connected to said tank and an opposite end adapted to extend into said pool by which said fluidized sludge may be conveyed to said tank; said tank, discharge means and pressurized spray means forming a closed fluidized circuit when in operation through which fluidized sludge may be continuously circulated from said compartment, through said discharge means to said tank, and from said tank through said pressurized spray means back to the compartment.
2. Apparatus according to Claim 1 wherein said pressurized spray means includes a first pump to convey fluidized sludge under pressure from said tank to a compartment.
3. Apparatus according to Claim 2 wherein said discharge means includes a second pump for conveying fluidized sludge from a compartment to said tank.
4. Apparatus according to Claim 3 wherein said first pump and said second pump are of equal capacity.
5. Apparatus according to Claim 4 having in addition a common drive means coupled to said first pump and to said second pump.
6. Apparatus according to Claim 5 wherein said tank, first pump, second pump and said drive means are mounted on a common base to form a portable unit.
7. Apparatus according to Claim 1 wherein said tank has a vertically extending baffle therein to separate the tank into a solids settling portion and into a substantially solids free portion with said solids settling portion being connected to said discharge means and said substantially solids free portion being connected to said pressurized spray means.
8. Apparatus according to Claim 1 wherein the tank is adapted to hold a fluidized sludge comprising an oil in water emulsion, including in addition a separating tank, withdrawal means extending between said closed fluidized circuit and said separating tank by which excess oil in water emulsion may be removed from said closed fluidized circuit and water recycle means by which water separated in said separating tank from the oil in water emulsion may be stored for further use as a rinse.
9. Apparatus according to Claim 1 including in addition a holding tank, withdrawal means extending between said fluidized circuit and said holding tank by which excess oil may be removed from said closed fluidized circuit and stored for later use.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA000458145A CA1262330A (en) | 1983-07-11 | 1984-07-04 | Apparatus for cleaning an oil contaminated vessel |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US51248983A | 1983-07-11 | 1983-07-11 | |
| US512,489 | 1983-07-11 | ||
| CA000458145A CA1262330A (en) | 1983-07-11 | 1984-07-04 | Apparatus for cleaning an oil contaminated vessel |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA1262330C CA1262330C (en) | 1989-10-17 |
| CA1262330A true CA1262330A (en) | 1989-10-17 |
Family
ID=24039320
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA000458145A Expired CA1262330A (en) | 1983-07-11 | 1984-07-04 | Apparatus for cleaning an oil contaminated vessel |
Country Status (13)
| Country | Link |
|---|---|
| EP (1) | EP0132197A3 (en) |
| JP (1) | JPS6084193A (en) |
| KR (1) | KR890000090B1 (en) |
| AU (1) | AU3031484A (en) |
| BR (1) | BR8403430A (en) |
| CA (1) | CA1262330A (en) |
| DK (1) | DK337984A (en) |
| ES (1) | ES534169A0 (en) |
| GR (1) | GR82396B (en) |
| IL (1) | IL72366A0 (en) |
| NO (1) | NO842792L (en) |
| PT (1) | PT78880B (en) |
| ZA (1) | ZA845272B (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DK35792D0 (en) * | 1992-03-17 | 1992-03-17 | Jan Stampe Hummer | PROCEDURE AND PLANT FOR CLEANING ISAAS 'GREAT TANK SPACES |
| FR2690857B1 (en) * | 1992-05-06 | 1995-03-31 | Marcel Claude | Device for cleaning oil and diesel tanks. |
| KR20000063242A (en) * | 2000-06-01 | 2000-11-06 | 조래웅 | a fabrication method of block |
| CN104928698B (en) * | 2015-05-11 | 2017-08-25 | 青岛亿民九洲清洗有限公司 | A kind of marine piping atomization cleaning equipment and cleaning |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB350850A (en) * | 1930-09-22 | 1931-06-18 | Butterworth System Inc | An improved method of and apparatus for cleaning tanks such as the cargo tanks of oil transporting vessels |
| GB951618A (en) * | 1960-05-06 | 1964-03-11 | Polycell Prod Ltd | Improvements relating to the cleaning of the surfaces of oil tanks and other oil contaminated surfaces |
| GB915533A (en) * | 1960-05-13 | 1963-01-16 | John Alexander Christensen | A method and apparatus for cleaning oil containing tanks |
| NL290674A (en) * | 1962-03-27 | |||
| JPS5314770B2 (en) * | 1972-07-03 | 1978-05-19 | ||
| JPS4939270A (en) * | 1972-08-23 | 1974-04-12 | ||
| JPS5491863A (en) * | 1977-12-28 | 1979-07-20 | Ebara Corp | Method and device for crude oil sludge removal |
-
1984
- 1984-07-04 CA CA000458145A patent/CA1262330A/en not_active Expired
- 1984-07-05 AU AU30314/84A patent/AU3031484A/en not_active Abandoned
- 1984-07-09 ZA ZA845272A patent/ZA845272B/en unknown
- 1984-07-09 NO NO842792A patent/NO842792L/en unknown
- 1984-07-09 GR GR75241A patent/GR82396B/el unknown
- 1984-07-10 DK DK337984A patent/DK337984A/en not_active Application Discontinuation
- 1984-07-10 EP EP84401462A patent/EP0132197A3/en not_active Withdrawn
- 1984-07-10 BR BR8403430A patent/BR8403430A/en unknown
- 1984-07-10 ES ES534169A patent/ES534169A0/en active Granted
- 1984-07-10 IL IL72366A patent/IL72366A0/en unknown
- 1984-07-10 PT PT78880A patent/PT78880B/en unknown
- 1984-07-11 JP JP59142502A patent/JPS6084193A/en active Pending
- 1984-07-11 KR KR1019840004061A patent/KR890000090B1/en active IP Right Grant
Also Published As
| Publication number | Publication date |
|---|---|
| EP0132197A3 (en) | 1985-07-10 |
| AU3031484A (en) | 1985-01-17 |
| CA1262330C (en) | 1989-10-17 |
| ZA845272B (en) | 1985-02-27 |
| IL72366A0 (en) | 1984-11-30 |
| DK337984D0 (en) | 1984-07-10 |
| DK337984A (en) | 1985-01-12 |
| KR850001106A (en) | 1985-03-16 |
| JPS6084193A (en) | 1985-05-13 |
| PT78880B (en) | 1986-07-14 |
| ES8602452A1 (en) | 1985-12-01 |
| BR8403430A (en) | 1985-06-25 |
| ES534169A0 (en) | 1985-12-01 |
| GR82396B (en) | 1984-12-13 |
| KR890000090B1 (en) | 1989-03-07 |
| EP0132197A2 (en) | 1985-01-23 |
| PT78880A (en) | 1984-08-01 |
| NO842792L (en) | 1985-01-14 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| MKLA | Lapsed | ||
| MKLA | Lapsed |
Effective date: 19920419 |