CN101678881A - Be used to handle the method for the ballast water in the ship of packing into - Google Patents
Be used to handle the method for the ballast water in the ship of packing into Download PDFInfo
- Publication number
- CN101678881A CN101678881A CN200880014901A CN200880014901A CN101678881A CN 101678881 A CN101678881 A CN 101678881A CN 200880014901 A CN200880014901 A CN 200880014901A CN 200880014901 A CN200880014901 A CN 200880014901A CN 101678881 A CN101678881 A CN 101678881A
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- China
- Prior art keywords
- seawater
- oil
- disconnector
- ship
- 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.)
- Pending
Links
- 238000000034 method Methods 0.000 title claims abstract description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims description 38
- 238000012856 packing Methods 0.000 title claims description 11
- 239000013535 sea water Substances 0.000 claims abstract description 83
- 239000012266 salt solution Substances 0.000 claims abstract description 18
- 238000010612 desalination reaction Methods 0.000 claims description 16
- 238000004140 cleaning Methods 0.000 claims description 8
- 238000005086 pumping Methods 0.000 claims description 8
- 238000003672 processing method Methods 0.000 claims 2
- 239000013505 freshwater Substances 0.000 abstract description 28
- 238000004519 manufacturing process Methods 0.000 abstract description 11
- 238000012545 processing Methods 0.000 abstract description 2
- 238000011084 recovery Methods 0.000 description 6
- 239000012855 volatile organic compound Substances 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 3
- 238000011068 loading method Methods 0.000 description 3
- 239000002918 waste heat Substances 0.000 description 3
- 241000283074 Equus asinus Species 0.000 description 1
- 241001503485 Mammuthus Species 0.000 description 1
- 239000012267 brine Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B63—SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
- B63J—AUXILIARIES ON VESSELS
- B63J4/00—Arrangements of installations for treating ballast water, waste water, sewage, sludge, or refuse, or for preventing environmental pollution not otherwise provided for
- B63J4/002—Arrangements of installations for treating ballast water, waste water, sewage, sludge, or refuse, or for preventing environmental pollution not otherwise provided for for treating ballast water
-
- 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
- B63—SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
- B63B—SHIPS OR OTHER WATERBORNE VESSELS; EQUIPMENT FOR SHIPPING
- B63B13/00—Conduits for emptying or ballasting; Self-bailing equipment; Scuppers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B63—SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
- B63B—SHIPS OR OTHER WATERBORNE VESSELS; EQUIPMENT FOR SHIPPING
- B63B17/00—Vessels parts, details, or accessories, not otherwise provided for
- B63B17/06—Refuse discharge, e.g. for ash
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/26—Treatment of water, waste water, or sewage by extraction
- C02F1/265—Desalination
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/008—Originating from marine vessels, ships and boats, e.g. bilge water or ballast water
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/08—Seawater, e.g. for desalination
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/001—Build in apparatus for autonomous on board water supply and wastewater treatment (e.g. for aircrafts, cruiseships, oil drilling platforms, railway trains, space stations)
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- Ocean & Marine Engineering (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Hydrology & Water Resources (AREA)
- Life Sciences & Earth Sciences (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Public Health (AREA)
- Toxicology (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
- Physical Water Treatments (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The invention discloses pack into the method for the seawater in the ship of a kind of processing.This method comprises to fresh water production equipment (30) provides seawater, seawater being separated into fresh water and salt solution, and fresh water is offered the ballast tank (6) of ship.
Description
Technical field
The present invention relates to a kind ofly be used to handle the method for the ballast water in the ship of packing into, and concrete but and not exclusively relate to a kind of method of the ballast seawater in the oil tanker of packing into that is used to handle.The invention still further relates to a kind of device that is used to realize this method.
Background technology
At present, surpassing 50% in the global carriage of goods by sea amount is oil.Usually, oil is to transport in the oil cargo tank of oil tanker, and oil tanker arrives its destination from the produce oil zone, and is not with goods just to return the produce oil zone after unloading, is loaded into seawater in its ballast tank to keep the stable of oil tanker.Ballast water will occupy 30% to 40% of tanker cargo capacity usually during return.
This arrangement has a lot of significant disadvantages.Surplus usually in oil cargo tank during the oil tanker return have 2 percent to three Cargo Oil, and this may cause the steam of volatile organic compound (VOC), and this may bring safety and environmental threat.Brine disposal in oil tanker when unloading ballast tank is a difficult task very, and seawater has strong corrosive property.Accretion in the ballast chamber also may bring serious problem, and the exchange of ballast water may cause safety problem to oil tanker.Transporting mammoth tanker and not carrying any useful goods shortcoming economically also is clearly.In addition, between the ballast water commutation period, may be difficult to keep the stability and the structure integrity of oil tanker.
Summary of the invention
Preferred implementation of the present invention attempts to overcome one or more in the above-mentioned shortcoming of prior art.
According to an aspect of the present invention, the method that provides a kind of processing to pack the interior seawater of ship into, this method comprises:
Seawater is provided at least one first disconnector;
By means of at least one described first disconnector at least in part to seawater desalination so that the water of basic desalination to be provided; With
The water of described basic desalination is offered at least one ballast tank of described ship.
Be converted into fresh water by at least a portion that will be used as the seawater of ballast in the ship return, doing like this provides a lot of significantly advantages.Useful goods is provided during the ship return.Consider that a lot of in the world produce oil zones have the fact of heavy demand for fresh water, this is particularly advantageous under the situation that is oil tanker.
This method may further include the salt solution that will be produced by at least one described first disconnector and enters marine.
This method may further include the step that the heat that produces by means of at least one driving engine by ship comes the water of pumping seawater and/or salt solution and/or basic desalination.
The step of the water of pumping seawater and/or salt solution and/or basic desalination can comprise that the heat by at least one driving engine generation of ship produces steam.
Ship can be that oil tanker and this method may further include:
Before described first disconnector separates seawater by at least one, provide seawater at least one second disconnector from least one oil cargo tank of oil tanker; With
From described seawater, remove Cargo Oil with described sea water mixing at least in part by means of at least one described second disconnector.
In at least one oil cargo tank by the oil tanker of before handling, seawater being packed into, and at least one ballast tank of after handling, fresh water being packed into, it is the appearance that has reduced VOC steam dangerous in oil cargo tank that the advantage that provides is provided like this, and makes the appearance of marine corrosion ballast tank situation minimize.Seawater packed into can also discharge remaining at least a portion Cargo Oil in the oil cargo tank in the oil cargo tank, so again can the remaining Cargo Oil of recovery section.
This method may further include in that described oil cargo tank cleaned the step of the wall portion of at least one described oil cargo tank before at least one described second disconnector provides seawater from least one.
It is to make Cargo Oil recovery maximization and the threat of VOC is minimized that the advantage that provides is provided like this.
Described cleaning can be carried out with seawater.
This method may further include and will offer at least one described oil cargo tank of oil tanker by means of the isolated Cargo Oil of at least one described second disconnector.
This method may further include the step of the heat pumping Cargo Oil that produces by means of at least one driving engine by oil tanker.
It is to have utilized the unnecessary heat of a part that is produced by marine engine usually that the advantage that provides is provided like this.
The step of pumping Cargo Oil can comprise that the heat that produces by means of at least one driving engine by oil tanker produces steam.
This method may further include and before at least one described second disconnector provides seawater seawater received at least one described oil cargo tank.
According to another aspect of the present invention, provide a kind of ballast water treatment plant of the seawater in the ship of packing into that is used to handle, this device comprises:
At least one first disconnector, its be used to receive seawater and at least in part to described seawater desalination so that the water of basic desalination to be provided; With
At least one first pump, it is used for the water of basic desalination is pumped to from least one described first disconnector at least one ballast tank of ship.
This device may further include and is used for salt solution is entered at least one marine second pump from least one described first disconnector.
This device can be to be used to handle the device of the seawater in the oil tanker of packing into, and may further include at least one second disconnector, described at least one second disconnector is used for receiving before described first disconnector is handled seawater by at least one from the seawater of at least one oil cargo tank of oil tanker and from described seawater to be removed and the Cargo Oil of described sea water mixing at least in part.
This device may further include at least one the 3rd pump that is used for seawater is pumped to from least one described oil cargo tank at least one described second disconnector.
This device may further include at least one the 4th pump that is used for seawater is pumped to from least one described second disconnector at least one described first disconnector.
This device may further include the Cargo Oil that is used for removing is pumped at least one described oil cargo tank from least one described second disconnector at least one the 5th pump.
At least one described first pump and/or second pump and/or the 3rd pump and/or the 4th pump and/or the 5th pump can be suitable for providing power by the heat that at least one driving engine by means of described ship produces.
According to a further aspect in the invention, provide a kind of ship, it comprises at least one ballast tank and aforesaid ballast water treatment plant.
This ship can be Tanker-Transport and may further include at least one oil cargo tank.
Description of drawings
Now with reference to accompanying drawing, introduce preferred implementation of the present invention, in the accompanying drawings by the mode that does not only have any restricted intention as example:
Fig. 1 is mounted in the scheme drawing of the ballast water treatment plant of the first embodiment of the invention in the oil tanker;
Fig. 2 shows pipeline and the valve bonded assembly scheme drawing in the ballast water treatment plant among Fig. 1;
Fig. 3 is mounted in the scheme drawing of the Waste Heat Recovery System (WHRS) in the ballast water treatment plant among Fig. 1; And
Fig. 4 is mounted in the scheme drawing of the ballast water treatment plant of the second embodiment of the invention in the common ship.
The specific embodiment
With reference to Fig. 1, oil tanker 2 has oil cargo tank 4 and ballast tank 6.Seawater inlet 8 is provided with and is used to remove sedimentary filter (not shown), and is connected to each oil cargo tank 4 by first sea water pump 10, seawater pipeline 12 and triple valve 14.Triple valve 14 is connected to Cargo Oil pipeline 20 with oily to oil cargo tank 4 loadings and oily from oil cargo tank 4 unloadings by cargo oil pump 16 and another triple valve 18, and is connected to the oil water separator 22 that is used for from the seawater separating oil that is received by oil cargo tank 4.
Isolated oil is sent to dirty oil tank 26 by pipeline 24 from oil water separator 22, is sent to by second sea water pump 28 through the seawater (seawater of by disconnector 22 oil therefrom having been separated just) that cleans to be used for being separated into the fresh water production equipment 30 of fresh water and salt solution through the seawater of cleaning.Fresh water production equipment is connected to by pipeline 32 and is used for salt solution is entered marine salt solution discharge orifice 34, and the ballast pump 38 that is connected to ballast tank 6 (only showing one of them in Fig. 1) and is used for fresh water is discharged by fresh water discharge orifice 40 by triple valve 36.
With reference to Fig. 2, can find out that triple valve 14 is connected to the suction point 46 of each oil cargo tank 4 by Cargo Oil pipeline 42 and cooresponding two-port valve 44.Similarly, triple valve 36 sucks point 52 by the correspondence that ballast water pipeline 48 and cooresponding two-port valve 50 are connected to each ballast tank 6.
With reference to Fig. 3, show and be used for the Waste Heat Recovery System (WHRS) 54 that the ballast water treatment plant with Fig. 1 and Fig. 2 uses together.By means of energy being provided for energy saver/donkey boiler 56, in pipeline 58, produce the high pressure steam that is used for driving pump 10,16,28,38 thus from the unnecessary heat of oil tanker sustainer, main engine (not shown).In addition, cabin heating pipeline 60 provides low pressure steam with the seawater in the heating oil cargo tank 4.
Operation to ballast water treatment plant of the present invention now is introduced.
In order to transport Cargo Oil, oil tanker 2 moves in a usual manner, that is to say that ballast tank 6 is empty, and oil cargo tank 4 is filled oil, in the destination of oil tanker oil is unloaded subsequently.
But when the return of oil tanker began, the unloaded oil cargo tank 4 that still has about 2% to 3% original Cargo Oil in its wall portion was loaded into quantity and is approximately 20% to 30% seawater above ballast tank 6 capacity.During voyage, utilize by Waste Heat Recovery System (WHRS) 54 generations and along the low pressure steam that low pressure cabin heating pipeline 60 provides oil cargo tank 4 interior seawater are heated to 40 to 50 ℃.It will be understood by those skilled in the art that the work efficiency that has just improved oil water separator 22 and fresh water production equipment 30 like this.
Oil is removed from the side of oil cargo tank 4 with help with the wall portion of seawater spraying oil cargo tank 4 subsequently.Make cargo oil pump 16 subsequently and be connected to oil water separator 22 triple valve 18 work so that from the seawater of oil cargo tank 4 through oil water separator 22 and be separated into the oil of recovery and through the seawater of cleaning, the oil that reclaims is sent to dirty oil tank 26, and is sent to fresh water production equipment 30 through the seawater of cleaning by sea water pump 28.
Fresh water production equipment 30 will be separated into salt solution and fresh water through the seawater of cleaning, and salt solution is discharged to marine by salt solution discharge orifice 34, and fresh water is sent to triple valve 36, and triple valve 36 is sent into fresh water in the ballast tank 6 subsequently.Because fresh water production equipment 30 can reclaim about 70% fresh water from seawater, so oil cargo tank 4 can produce 20% to 30% useful loading seawater above ballast tank 6 capacity.The fresh water of gained is exactly vendible commodity subsequently, and it can be discharged by ballast pump 36 and fresh water discharge orifice 40 in the destination of oil tanker.Can utilize suitable controller (not shown) to control the loading and unloading order of cabin 4,6 to keep structure integrity, safety and the stability of oil tanker.
Fig. 4 shows the ship 102 (that is to say and be not oil tanker) of general type, and ship 102 has the water treatment plant of second embodiment of the invention, with parts identical in the embodiment of Fig. 1 to Fig. 3 by similarly but having increased by 100 Reference numeral represents.Ship 102 has cargo hold 104 and ballast tank 106.Seawater inlet 108 is connected to the rough filter of flushing certainly 121 that is used for removing from seawater accretion and bigger suspended material by first sea water pump 110 and seawater pipeline 112.
Delivered to the fresh water production equipment 130 that is used for the seawater through cleaning is separated into fresh water and salt solution through the seawater that filters by second sea water pump 128 from filter 121.Fresh water production equipment 130 is connected to by pipeline 132 and is used for salt solution is discharged to marine salt solution discharge orifice 134, and is connected to ballast tank 106 and the ballast pump 138 that is used for fresh water is discharged by fresh water discharge orifice 140 by triple valve 136.
It will be understood by those skilled in the art that above-mentioned embodiment only is not have any restrictive, sense as the example introduction, and have various modifications and distortion and do not deviate from the protection domain that the present invention is indicated in the appended claims.For example, can use gravity well known to those of ordinary skill in the art/coalescent design-calculated oil water separator 22, perhaps also can use the oil water separator 22 of other types.Similarly, can use the fresh water production equipment 30 of reverse osmosis design, but also can use the fresh water production equipment of other types.
Claims (22)
1, a kind of processing method of the seawater in the ship of packing into, this method comprises:
Seawater is provided at least one first disconnector;
By means of at least one described first disconnector at least in part to seawater desalination so that the water of basic desalination to be provided; With
The water of described basic desalination is offered at least one ballast tank of described ship.
2, the method for claim 1 comprises that further the salt solution that will be produced by at least one described first disconnector enters marine.
3, method as claimed in claim 1 or 2 comprises that further the heat that produces by means of at least one driving engine by described ship comes the step of the water of pumping seawater and/or salt solution and/or basic desalination.
4, method as claimed in claim 3, wherein the step of the water of pumping seawater and/or salt solution and/or basic desalination comprises that the heat that produces by means of at least one driving engine by described ship produces steam.
5, any as described above described method of claim, wherein said ship is that oil tanker and this method further comprise:
Before described first disconnector separates seawater by at least one, provide seawater at least one second disconnector from least one oil cargo tank of described oil tanker; With
From described seawater, remove Cargo Oil with described sea water mixing at least in part by means of at least one described second disconnector.
6, method as claimed in claim 5 further is included in the step of cleaning the wall portion of at least one described oil cargo tank from least one described oil cargo tank before at least one described second disconnector provides seawater.
7, method as claimed in claim 6, wherein said cleaning is carried out with seawater.
8,, further comprise and to offer at least one described oil cargo tank of described oil tanker by means of the isolated Cargo Oil of at least one described second disconnector as any described method in the claim 5 to 7.
9,, further comprise the step of the heat pumping Cargo Oil that produces by means of at least one driving engine by described oil tanker as any described method in the claim 7 to 8.
10, method as claimed in claim 9, wherein the step of pumping Cargo Oil comprises that the heat that produces by means of at least one driving engine by described oil tanker produces steam.
11, as any described method in the claim 5 to 10, further being included in at least one described second disconnector provides seawater before seawater to be received at least one described oil cargo tank.
12, a kind of processing method of the seawater in the ship of packing into, this method are described with reference to accompanying drawing in as mentioned basically.
13, a kind ofly be used to handle the ballast water treatment plant of the seawater in the ship of packing into, this device comprises:
At least one first disconnector, its be used to receive seawater and at least in part to described seawater desalination so that the water of basic desalination to be provided; With
At least one first pump, it is used for the water of basic desalination is pumped to from least one described first disconnector at least one ballast tank of described ship.
14, device as claimed in claim 13 further comprises being used for salt solution is entered at least one marine second pump from least one described first disconnector.
15, as claim 13 or 14 described devices, be used to handle the interior seawater of oil tanker of packing into, further comprise at least one second disconnector, described at least one second disconnector is used for receiving before described first disconnector is handled seawater by at least one from the seawater of at least one oil cargo tank of described oil tanker and from described seawater to be removed and the Cargo Oil of described sea water mixing at least in part.
16, device as claimed in claim 15 further comprises at least one the 3rd pump that is used for seawater is pumped to from least one described oil cargo tank at least one described second disconnector.
17,, further comprise at least one the 4th pump that is used for seawater is pumped to from least one described second disconnector at least one described first disconnector as claim 15 or 16 described devices.
18,, comprise that further the Cargo Oil that is used for removing is pumped at least one the 5th pump of at least one described oil cargo tank from least one described second disconnector as any described device in the claim 13 to 17.
19, as any described device in the claim 13 to 18, wherein at least one described first pump and/or second pump and/or the 3rd pump and/or the 4th pump and/or the 5th pump are fit to provide power by the heat that at least one driving engine by means of described ship produces.
20, a kind ofly be used to handle the ballast water treatment plant of the seawater in the ship of packing into, this device is described with reference to accompanying drawing in as mentioned basically.
21, a kind of ship comprises at least one oil cargo tank, at least one ballast tank and as any described ballast water treatment plant in the claim 13 to 20.
22, ship as claimed in claim 21, wherein this ship is oil tanker and further comprises at least one oil cargo tank.
Applications Claiming Priority (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GBGB0704979.4A GB0704979D0 (en) | 2007-03-15 | 2007-03-15 | Process for treatment of ballast water aboard cargo transport tankers |
| GB0704979.4 | 2007-03-15 | ||
| GB0709591.2 | 2007-05-18 | ||
| GBGB0709591.2A GB0709591D0 (en) | 2007-03-15 | 2007-05-18 | Process for treatment of ballast water aboard ships |
| PCT/GB2008/000788 WO2008110762A1 (en) | 2007-03-15 | 2008-03-06 | Process for treatment of ballast water aboard ships |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN101678881A true CN101678881A (en) | 2010-03-24 |
Family
ID=38008473
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200880014901A Pending CN101678881A (en) | 2007-03-15 | 2008-03-06 | Be used to handle the method for the ballast water in the ship of packing into |
Country Status (4)
| Country | Link |
|---|---|
| KR (1) | KR20100015566A (en) |
| CN (1) | CN101678881A (en) |
| GB (3) | GB0704979D0 (en) |
| WO (1) | WO2008110762A1 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103459246A (en) * | 2012-04-13 | 2013-12-18 | 株式会社商船三井 | Ship and ballast water processing device |
| CN105585182A (en) * | 2016-03-03 | 2016-05-18 | 金晨光 | Ballast water treatment equipment |
| CN108996581A (en) * | 2017-06-07 | 2018-12-14 | 吕坤土 | Distilled water use, ship, ballast water generation system, facility and operation method |
Families Citing this family (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9010261B2 (en) | 2010-02-11 | 2015-04-21 | Allen Szydlowski | Method and system for a towed vessel suitable for transporting liquids |
| US8007845B2 (en) | 2005-10-21 | 2011-08-30 | Waters of Patagonia | Method and system for recovering and preparing glacial water |
| US20120216875A1 (en) * | 2010-08-31 | 2012-08-30 | Allen Szydlowski | Methods and systems for producing, trading and transporting water |
| US8403718B2 (en) | 2010-02-11 | 2013-03-26 | Allen Szydlowski | Method and system for a towed vessel suitable for transporting liquids |
| US9521858B2 (en) | 2005-10-21 | 2016-12-20 | Allen Szydlowski | Method and system for recovering and preparing glacial water |
| US9017123B2 (en) | 2009-10-15 | 2015-04-28 | Allen Szydlowski | Method and system for a towed vessel suitable for transporting liquids |
| US9371114B2 (en) | 2009-10-15 | 2016-06-21 | Allen Szydlowski | Method and system for a towed vessel suitable for transporting liquids |
| WO2011047275A1 (en) | 2009-10-15 | 2011-04-21 | World's Fresh Waters Pte. Ltd | Method and system for processing glacial water |
| US11584483B2 (en) | 2010-02-11 | 2023-02-21 | Allen Szydlowski | System for a very large bag (VLB) for transporting liquids powered by solar arrays |
| KR101291353B1 (en) * | 2011-03-23 | 2013-07-30 | 삼성중공업 주식회사 | Water treatment system for ship |
| WO2014058556A1 (en) * | 2012-10-08 | 2014-04-17 | Allen Szydlowski | Methods and systems for producing, trading, and transporting water |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3182669A (en) * | 1963-03-30 | 1965-05-11 | Algonquin Shipping & Trading | Combined tanker service unit |
| JPS52123095A (en) * | 1976-04-07 | 1977-10-15 | Hitachi Ltd | Water preparing vessel |
| US5908040A (en) * | 1995-10-25 | 1999-06-01 | Defraites, Jr.; Arthur A. | Method of cleaning boats that have been contaminated with oil and gas well drilling fluids and hazardous waste |
| CN100436251C (en) * | 2002-09-20 | 2008-11-26 | 梁富泉 | Multiple driving gliding submarine |
-
2007
- 2007-03-15 GB GBGB0704979.4A patent/GB0704979D0/en not_active Ceased
- 2007-05-18 GB GBGB0709591.2A patent/GB0709591D0/en not_active Ceased
-
2008
- 2008-03-06 CN CN200880014901A patent/CN101678881A/en active Pending
- 2008-03-06 KR KR1020097021437A patent/KR20100015566A/en not_active Application Discontinuation
- 2008-03-06 WO PCT/GB2008/000788 patent/WO2008110762A1/en active Application Filing
-
2009
- 2009-11-16 GB GB0919993A patent/GB2461484A/en not_active Withdrawn
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103459246A (en) * | 2012-04-13 | 2013-12-18 | 株式会社商船三井 | Ship and ballast water processing device |
| CN105585182A (en) * | 2016-03-03 | 2016-05-18 | 金晨光 | Ballast water treatment equipment |
| CN108996581A (en) * | 2017-06-07 | 2018-12-14 | 吕坤土 | Distilled water use, ship, ballast water generation system, facility and operation method |
Also Published As
| Publication number | Publication date |
|---|---|
| GB2461484A (en) | 2010-01-06 |
| KR20100015566A (en) | 2010-02-12 |
| GB0704979D0 (en) | 2007-04-25 |
| GB0919993D0 (en) | 2009-12-30 |
| GB0709591D0 (en) | 2007-06-27 |
| WO2008110762A1 (en) | 2008-09-18 |
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