WO2011005129A2 - Installation and procedure for the treatment of waste resulting from activities on a ship - Google Patents

Installation and procedure for the treatment of waste resulting from activities on a ship Download PDF

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Publication number
WO2011005129A2
WO2011005129A2 PCT/RO2009/000019 RO2009000019W WO2011005129A2 WO 2011005129 A2 WO2011005129 A2 WO 2011005129A2 RO 2009000019 W RO2009000019 W RO 2009000019W WO 2011005129 A2 WO2011005129 A2 WO 2011005129A2
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WO
WIPO (PCT)
Prior art keywords
pipe
water
pipeline
steam
installation
Prior art date
Application number
PCT/RO2009/000019
Other languages
French (fr)
Other versions
WO2011005129A3 (en
Inventor
Vasile Muscalu
Original Assignee
S.C. Hellenic Tiler Invest Srl
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by S.C. Hellenic Tiler Invest Srl filed Critical S.C. Hellenic Tiler Invest Srl
Publication of WO2011005129A2 publication Critical patent/WO2011005129A2/en
Publication of WO2011005129A3 publication Critical patent/WO2011005129A3/en

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B63SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
    • B63JAUXILIARIES ON VESSELS
    • B63J4/00Arrangements of installations for treating ballast water, waste water, sewage, sludge, or refuse, or for preventing environmental pollution not otherwise provided for
    • B63J4/006Arrangements of installations for treating ballast water, waste water, sewage, sludge, or refuse, or for preventing environmental pollution not otherwise provided for for treating waste water or sewage
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B63SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
    • B63JAUXILIARIES ON VESSELS
    • B63J1/00Arrangements of installations for producing fresh water, e.g. by evaporation and condensation of sea water
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/02Treatment of water, waste water, or sewage by heating
    • C02F1/04Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/16Treatment of water, waste water, or sewage by heating by distillation or evaporation using waste heat from other processes
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/008Originating from marine vessels, ships and boats, e.g. bilge water or ballast water
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination

Definitions

  • the invention refers to an installation and a procedure for the treatment of waste resulting from activities on a ship, when sea water can also be desalinated.
  • the problem that the invention solves consists in the treatment of waste so that it is no more stored and discharged during the stay on the shore.
  • the installation removes the disadvantages shown before by having a pipe connected to a general admission in which there are assembled some electric valves, with water containing waste of the reactor chambers from the basin and the pushing pipes of the water by the pumps of the recirculating water absorbed by the pipes from the coolers being connected to the upstream of the electric valves to the general admission, the pipe of the recirculating water from the work-chamber of the second reactor being connected to a pipe down the cooler, so that the water circulating through it and also through the pipe connected to a heat exchanger or to a water desalination installation to pass the cooler and then to be introduced into the general pipe, the chamber of the second reactor being connected to a pipe which contains a mounted electric valve through which the steam joining the steam from a pipe which contains a mounted electric valve is introduced into the blade turbine which drags along an electricity generator and from which the steam passes through the heat exchanger or is directed to the water desalination installation, the water evacuated from the reactors' work-chambers being collected into a pipe which
  • the procedure applied, according to the invention removes the disadvantages shown before by the fact that the steam is collected at a 300-400 degrees C from the reactors' chambers and directed for transforming the thermal energy into mechanical energy in a turbine and then into an electricity generator, the steam recovered from the turbine having a 280..300 degrees C temperature being passed through a saver from which the domestic water results at a temperature of 80..100 degrees C, the water from the saver being directed through any of the coolers and being reintroduced after cooling at a 50...60 degrees C temperature into the general admission pipe, and the water evacuated from the room after retaining the coal particles from it is collected into a pipe from which is aspired and pushed away with a pump into the basin.
  • the installation has a high reliability.
  • the installation according to the invention has as a component some A reactors straight positioned , having each a mantle 1 which delimitates an A work - chamber in which electrodes 2,3 and 4 are centrally placed and front and back at the sides, having their axis placed in a horizontal plan and in relationship with the mantle 1 there are mounted some sensors 5, 6, and 7 of level, temperature and pressure.
  • the hot water evacuated on the inferior side of chamber a of the other reactor A is circulated through a pipe 34 passed through a filter 35 for retaining the carbon particles and transferred through a pipe 36 having mounted an electro-valve 37 in it into the pipe 29 of aspiration of the pump 31.
  • the steam from the chamber a of the second reactor A is evacuated through a pipe 38 having mounted in it an electric valve 39 and passed together with the evacuated steam from the from the chamber a of the first reactor A, through a pipe 40, having mounted an electric valve 41 in it connected to the pipe 38 upstream the electric valve 39 and downstream a turbine 42 with palettes which involves an electricity generator 43. From the turbine 42 the steam is passed through a heat exchanger 44 to obtain hot water or is supplied to a known desalination water installation which is not represented in the figures.
  • the hot water from the exchanger 44 can be introduced into the pipe 20 through some pipes 44 and 46, into the pipe 20 upstream the cooler 22, or through a pipe 47 having mounted an electric valve 48 in it into a cooler 49 from which through a pipe 50 is aspired by a 51 pump and pushed through a pipe 52 having mounted an electric valve 53 in the pipe 17 upstream the electric valve 19.
  • a pipe 54 is connected to the pipe 47 upstream the electric valve 48 having mounted an electric valve 55 in it through which the water circulation from the work chamber of the second reactor A is accomplished.
  • the gas which contains hydrogen, oxygen and carbon generated in the a chambers is evacuated from these through some pipes 59 and 60 and passed through some filters 61 and 62 from which are passed through some pipes 63 and 64 having mounted some electric valves 65 and 66 mounted in them is aspired by some air pumps 67 and 68 and pushed trough some pipes 69 and 70 having mounted some electric valves 71 and 72 in them in some tanks 73 and 74.
  • the gas in tanks 73 and 74 supplies a collector 91 by means of pipes 92 and 93, which include electric vales 94 and 95 which lead gas by means of pipes 96 and 97 including electric valves 98 and 99 to electricity generators 100 and 101.
  • Commands are transmitted to reactors A from panela 81, 82, 83 and 84 by means of power lines 102, 103, 104 and 104 and the supply of panels 81 and 82 is performed from generators 79 and 80 by means of power lines 106.
  • the electrode 2 is attached to a shaft 107, preferably made of stainless steel, powered by brushes 108.
  • the shaft 107 crosses mantle 1 by means of a tightening gland 109 and a worm wheel 110 is attached to shaft 107 at the outer part of mantle 1, which connects with a worm 111 rotated by an electrical motor 85 attached by means of screws 103 to a mobile plate 104.
  • a vertical plate 105 is attached to mantle 1 and provided with two guidances 106 and 107, along which plate 104 may be moved by means of ball guidance joints 108.
  • a nut 109 is attached to shaft 107, which in turn operates a coarse thread screw 110, rotated by an electrical motor 86, supported by a horizontal plate 111 attached to plate 105.
  • the nut 109 is guided by a ball couple 112 at the lower part, mounted in connection with two bars 113 attached by plate 111 at the ends.
  • Electrodes 3 and 4 are mounted on each of the axes 114 and 115 which connect to a source of electricity and cross the mantle 1 by means of glands 116 and 117 and which may be horizontally moved by means of one of the nuts 118 and 119 which operate with one of the coarse thread screws 120 and 121, rotated in turn by one of the electrical motors 87 and 88.
  • the latter are supported by one of the vertical plates 122 and 123 fixed to mantle 1.
  • Some pairs of horizontal bars 124 and 125 are attached to the ends of plates 122 and 123, and nuts 118 and 119 shall come into contact with them.
  • the procedure applied for the installation consists in that waste water is simultaneously introduced into chambers a of reactors A, through pipe 17, through which cold recirculation water proceeding from hot water in chambers a is also introduced after cold water was cooled to a temperature of 50...60 0 C, in order to create conditions for the electrical discharges between electrodes 2, 3 and 4, supplied with a voltage of 40 V and a current intensity of 2,000 A, to produce a maximum amount of gas from water.
  • Gas is separated from steam through filtration, compressed at a pressure of 150...200 Ban * and stored for the supply of power generators, both for internal consumption andTf ⁇ r delivery to other consumers.
  • Water exhausted at the lower part of chambers a is filtered for retaining carbon particles in filters 28 and 35 and aspired through a common pipe 29 by pump 31 and pushed into basin 8, from where it re-enters the supply circuit of chambers a through pipe 17.
  • Steam at a temperature of 300..400 0 C is exhausted from the upper parts of chambers a of reactors A and crosses turbine 42 which operates the generator 43 which produces electricity, after which steam at a temperature of 180..280 0 C crosses heat exchanger 44, from where hot water is recovered at a temperature of 50...60 0 C.
  • Steam proceeding from turbine 42 may be directly transferred to a water desalination installation, known in itself, but not represented in figures, and hot water proceeding from the desalination installation may be cooled together with the circulation water in chamber a of the second reactor A up to a temperature of 40...50 0 C and reintroduced into chamber a.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Ocean & Marine Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Combustion & Propulsion (AREA)
  • Public Health (AREA)
  • Toxicology (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

The invention refers to a plant and a procedure for the treatment of waste resulting from the activities on a ship, leading to sea water desalination. The problem solved by the invention consists in waste treatment so that it should not be stored and discharged while stopping on shore. Installation for the treatment of waste resulting from the activities on a ship, including two vertically arranged reactors, within which some electric valves are mounted, water contains waste from the tank of reactors' chambers, to the general supply pipeline there are connected, to the upstream of electric valves, the pipelines for pushing recirculated water by pumps, sucked through the pipelines from coolers, the recirculation water pipeline from the working chamber of the second reactor is connected to a pipeline to the downstream of the cooler, so that water circulated through it and respectively through the pipeline connected to a heat exchanger or to a water desalination plant shall be passed through cooler and then introduced inserted into the general pipeline, the working chamber of the second reactor is in connection with a pipeline with an electric valve mounted on the inside, through-which the steam together with steam from a pipeline with an electric valve mounted is introduced into the blade turbine, which operates an electricity generator and from which steam passes through the heat exchanger or is conducted into the water desalination plant, the water discharged from the working chambers of the reactor is collected in a pipeline from where it is pushed by a pump through a pipeline into the tank.

Description

Installation and procedure for the treatment of waste resulting from activities on a ship
The invention refers to an installation and a procedure for the treatment of waste resulting from activities on a ship, when sea water can also be desalinated.
There are known installations for storing the waste resulting from the activities on the ship which contain some tight containers in which the waste is stored and which are discharged in set up areas in harbours.
The disadvantages of these installations consist in that the waste is kept in these containers during the whole period of navigation which demands the setting up of an area for such storage.
There are known procedures for storing the waste resulting from the activities on the ship which consist of collecting the waste by pumping in some tight containers and stored in a set up area.
The disadvantages_of. these procedures consist in that their storage for- a-relatively- long period of time can cause the outdoor environment pollution by the accidental damage of these containers.
The problem that the invention solves consists in the treatment of waste so that it is no more stored and discharged during the stay on the shore.
According to the invention, the installation removes the disadvantages shown before by having a pipe connected to a general admission in which there are assembled some electric valves, with water containing waste of the reactor chambers from the basin and the pushing pipes of the water by the pumps of the recirculating water absorbed by the pipes from the coolers being connected to the upstream of the electric valves to the general admission, the pipe of the recirculating water from the work-chamber of the second reactor being connected to a pipe down the cooler, so that the water circulating through it and also through the pipe connected to a heat exchanger or to a water desalination installation to pass the cooler and then to be introduced into the general pipe, the chamber of the second reactor being connected to a pipe which contains a mounted electric valve through which the steam joining the steam from a pipe which contains a mounted electric valve is introduced into the blade turbine which drags along an electricity generator and from which the steam passes through the heat exchanger or is directed to the water desalination installation, the water evacuated from the reactors' work-chambers being collected into a pipe which is pushed in the basin through a pump.
The procedure applied, according to the invention, in the case of the installation removes the disadvantages shown before by the fact that the steam is collected at a 300-400 degrees C from the reactors' chambers and directed for transforming the thermal energy into mechanical energy in a turbine and then into an electricity generator, the steam recovered from the turbine having a 280..300 degrees C temperature being passed through a saver from which the domestic water results at a temperature of 80..100 degrees C, the water from the saver being directed through any of the coolers and being reintroduced after cooling at a 50...60 degrees C temperature into the general admission pipe, and the water evacuated from the room after retaining the coal particles from it is collected into a pipe from which is aspired and pushed away with a pump into the basin.
The installation and the procedure according to the invention from the group of inventions offers the following advantages: removes waste storage and its safe shipping to the shore;
- the products obtained as a consequence of waste treatment are consumable as they are, as happens with gas and hot water and these can be the resources for generating electricity;
- it doesn't produce noxes pollution of the environment;
- the installation needs a relatively diminished area for mounting and functioning;
- the installation has a high reliability.
In the following there are given some examples of accomplishment of the installation and the procedure according to the inventions from the group of inventions in relationship with figure 1, which represents:
- fig.1, global view of the installation according to the invention;
- fig.2, vertical section through an installation reactor; - fig.3, view of a central electrode of a reactor.
The installation according to the invention has as a component some A reactors straight positioned , having each a mantle 1 which delimitates an A work - chamber in which electrodes 2,3 and 4 are centrally placed and front and back at the sides, having their axis placed in a horizontal plan and in relationship with the mantle 1 there are mounted some sensors 5, 6, and 7 of level, temperature and pressure. In the chambers A water from a closed collecting basin 8, in which a pump 9 pushes through a pipe 10 having an electric valve 11 in it the waste aspirated with or without the salted water through a pipe 12 is pushed by a pump 13 which aspires water through a pipe 14 and pushes it through a pipe 15 having a an electro-valve 16 mounted in it into a general admission pipe 17 having mounted some electro-valves 18 and 19 in it connected to the mantle l.The water from the chamber a of the first reactor A is recirculated through a pipe 20 having mounted an electric valve 21 in it, through a cooler 22 from which through a pipe 23 it is aspired by a pump 24 and pushed through a pipe 25 having mounted an electric valve 26 in it into the pipe 17 upstream the electro- valve 18. From the chamber a from the first reactor A through its inferior side, hot water is evacuated through a pipe 27 and passed through a filter 28 in which are retained the carbon particles and next the water is aspired through a pipe 29, having an electro- valve 30 mounted in it by a pump 31 and pushed trough a pipe 32 having mounted an electric valve 33 in it in the basin 8.
The hot water evacuated on the inferior side of chamber a of the other reactor A is circulated through a pipe 34 passed through a filter 35 for retaining the carbon particles and transferred through a pipe 36 having mounted an electro-valve 37 in it into the pipe 29 of aspiration of the pump 31.
The steam from the chamber a of the second reactor A is evacuated through a pipe 38 having mounted in it an electric valve 39 and passed together with the evacuated steam from the from the chamber a of the first reactor A, through a pipe 40, having mounted an electric valve 41 in it connected to the pipe 38 upstream the electric valve 39 and downstream a turbine 42 with palettes which involves an electricity generator 43. From the turbine 42 the steam is passed through a heat exchanger 44 to obtain hot water or is supplied to a known desalination water installation which is not represented in the figures.
The hot water from the exchanger 44 can be introduced into the pipe 20 through some pipes 44 and 46, into the pipe 20 upstream the cooler 22, or through a pipe 47 having mounted an electric valve 48 in it into a cooler 49 from which through a pipe 50 is aspired by a 51 pump and pushed through a pipe 52 having mounted an electric valve 53 in the pipe 17 upstream the electric valve 19.
A pipe 54 is connected to the pipe 47 upstream the electric valve 48 having mounted an electric valve 55 in it through which the water circulation from the work chamber of the second reactor A is accomplished.
In the basin 8 through a pipe 56 having mounted an electric valve 57 in it the dejections are pushed by a pump 58.
The gas which contains hydrogen, oxygen and carbon generated in the a chambers is evacuated from these through some pipes 59 and 60 and passed through some filters 61 and 62 from which are passed through some pipes 63 and 64 having mounted some electric valves 65 and 66 mounted in them is aspired by some air pumps 67 and 68 and pushed trough some pipes 69 and 70 having mounted some electric valves 71 and 72 in them in some tanks 73 and 74.
The latter are connected by means of pipes 75 and 76, which contain electric valves 77 and 78 and electricity generators 79 and 80 with supply some general control panels 81 and 82 as well as secondary control panela 83 and 94 for motors 85, 86, 87 and 88 which operate electrodes 2, 3 and 4 and, respectively, accumulators 89 and 90.
The gas in tanks 73 and 74 supplies a collector 91 by means of pipes 92 and 93, which include electric vales 94 and 95 which lead gas by means of pipes 96 and 97 including electric valves 98 and 99 to electricity generators 100 and 101.
Commands are transmitted to reactors A from panela 81, 82, 83 and 84 by means of power lines 102, 103, 104 and 104 and the supply of panels 81 and 82 is performed from generators 79 and 80 by means of power lines 106.
The electrode 2 is attached to a shaft 107, preferably made of stainless steel, powered by brushes 108. The shaft 107 crosses mantle 1 by means of a tightening gland 109 and a worm wheel 110 is attached to shaft 107 at the outer part of mantle 1, which connects with a worm 111 rotated by an electrical motor 85 attached by means of screws 103 to a mobile plate 104. A vertical plate 105 is attached to mantle 1 and provided with two guidances 106 and 107, along which plate 104 may be moved by means of ball guidance joints 108. A nut 109 is attached to shaft 107, which in turn operates a coarse thread screw 110, rotated by an electrical motor 86, supported by a horizontal plate 111 attached to plate 105. The nut 109 is guided by a ball couple 112 at the lower part, mounted in connection with two bars 113 attached by plate 111 at the ends.
Electrodes 3 and 4 are mounted on each of the axes 114 and 115 which connect to a source of electricity and cross the mantle 1 by means of glands 116 and 117 and which may be horizontally moved by means of one of the nuts 118 and 119 which operate with one of the coarse thread screws 120 and 121, rotated in turn by one of the electrical motors 87 and 88. The latter are supported by one of the vertical plates 122 and 123 fixed to mantle 1. Some pairs of horizontal bars 124 and 125 are attached to the ends of plates 122 and 123, and nuts 118 and 119 shall come into contact with them.
According to the invention, the procedure applied for the installation consists in that waste water is simultaneously introduced into chambers a of reactors A, through pipe 17, through which cold recirculation water proceeding from hot water in chambers a is also introduced after cold water was cooled to a temperature of 50...600C, in order to create conditions for the electrical discharges between electrodes 2, 3 and 4, supplied with a voltage of 40 V and a current intensity of 2,000 A, to produce a maximum amount of gas from water.
Gas is separated from steam through filtration, compressed at a pressure of 150...200 Ban* and stored for the supply of power generators, both for internal consumption andTfόr delivery to other consumers.
Water exhausted at the lower part of chambers a is filtered for retaining carbon particles in filters 28 and 35 and aspired through a common pipe 29 by pump 31 and pushed into basin 8, from where it re-enters the supply circuit of chambers a through pipe 17.
Steam at a temperature of 300..4000C is exhausted from the upper parts of chambers a of reactors A and crosses turbine 42 which operates the generator 43 which produces electricity, after which steam at a temperature of 180..2800C crosses heat exchanger 44, from where hot water is recovered at a temperature of 50...600C. Steam proceeding from turbine 42 may be directly transferred to a water desalination installation, known in itself, but not represented in figures, and hot water proceeding from the desalination installation may be cooled together with the circulation water in chamber a of the second reactor A up to a temperature of 40...500C and reintroduced into chamber a.

Claims

Claims
1. Installation for the treatment of waste resulting from the activities on a ship, composed by two vertical reactors, each with a mantle delimitating a work room, with level, temperature and pressure sensors mounted in connection with the mantle, with central, front and back lateral electrodes mounted in connection with the mantle, placed in a horizontal plane, supplied with electricity by means of a secondary control panel from electricity generators, and the power supply of generators is made by means of a general control panel from the same power generators connected to tanks of gas proceeding from work rooms, compressed by means of compressors, as well as a closed basin for the collection of dejections and other waste water, from which a pump aspires through a pipe and pushes through another pipe the mixture in the basin, with the hot water in each work chamber being recirculated by means of pipes which include electric valves through coolers from which it is apires by means of pipes and pushed through another pipes by pumps, and the mentioned pipe (15) is connected to a general admission pipe (17), which includes electric valves (18 and 19) with water containing waste from the mentioned basin (8) of chambers (a) of the mentioned reactors (A), the general admission pipe (17) is connected to the upstream of the electric valves (18 and 19) to the mentioned pipes (25 and 49) for pushing by pumps (24 and 51) of the recirculation water aspired by pipes (20 and _ 54.)_ .from. the. mentioned_coolers (22. arid 49) and pipe (54) for water recirculation from the working room (a) of the second reactor (A) is connected to a pipe (47) to the upstream of the cooler (49), so that water circulated through it and respectively through pipe (45) connected to a heat exchanger (44) or a water desalination installation crosses the cooler (49) and is then introduced into the general admission pipe (17), the work room (a) of the second reactor (A) is connected to a pipe (38) including an electric valve (39) through which steam, together with the steam in a pipe (40) including an electric valve (41) is introduced into the bladed turbine (42) which operates a power generator (43) and from where steam passes through the heat exchanger (44) or is directed into the water desalination installation, water discharged from work chambers (a) of the reactors (A) is collected into a pipe (29) from which, by means of a pump (31), it is pushed through a pipe (32) into the basin (8).
2. Procedure for the treatment of waste resulting from activities on a ship applied within an installation, according to claim 1, the steam is collected at a temperature of 300-400 degrees C from the chambers (a) of reactors (A) and directed for transforming the thermal energy into mechanical energy in a turbine (42) and then into an electricity generator (42), the steam recovered from the turbine" (42) having a 280..300 degrees C temperature being passed through a heat recovery device (44) from which the domestic water results at a temperature of 80..100 degrees C, the water from the recovery device (44) being directed through any of the coolers (49 and 22) and being reintroduced after cooling at a 50...60 degrees C temperature into the general admission pipe (17), and the water evacuated from chamber (a) after retaining the coal particles from it is collected into a pipe (29) from which it is aspired and pushed away with a pump (31) into the basin (8).
PCT/RO2009/000019 2009-06-18 2009-11-30 Installation and procedure for the treatment of waste resulting from activities on a ship WO2011005129A2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
ROA200900458A RO126017A2 (en) 2009-06-18 2009-06-18 Installation and process for treating waste resulting from activities on a ship
ROA200900458 2009-06-18

Publications (2)

Publication Number Publication Date
WO2011005129A2 true WO2011005129A2 (en) 2011-01-13
WO2011005129A3 WO2011005129A3 (en) 2011-11-17

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2016044100A1 (en) * 2014-09-16 2016-03-24 Deepwater Desal Llc Systems and methods for applying power generation units in water desalination
CN106516020A (en) * 2016-10-28 2017-03-22 中国船舶科学研究中心(中国船舶重工集团公司第七0二研究所) Water pressure balance flushing type toilet storage container device for great depth manned submersible
CN107728661A (en) * 2017-10-26 2018-02-23 北京金控数据技术股份有限公司 A kind of control method of sea-water-desalination water producing, system, terminal device and medium

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5248394A (en) * 1992-03-23 1993-09-28 Fsr Patented Technologies, Ltd. Liquid purifying/distillation device
EP1908733A1 (en) * 2006-10-02 2008-04-09 L'AIR LIQUIDE, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Method and plant for joint production of electricity, steam and desalinated water

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5248394A (en) * 1992-03-23 1993-09-28 Fsr Patented Technologies, Ltd. Liquid purifying/distillation device
EP1908733A1 (en) * 2006-10-02 2008-04-09 L'AIR LIQUIDE, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Method and plant for joint production of electricity, steam and desalinated water

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2016044100A1 (en) * 2014-09-16 2016-03-24 Deepwater Desal Llc Systems and methods for applying power generation units in water desalination
US10934181B2 (en) 2014-09-16 2021-03-02 Deepwater Desal Llc Systems and methods for applying power generation units in water desalination
CN106516020A (en) * 2016-10-28 2017-03-22 中国船舶科学研究中心(中国船舶重工集团公司第七0二研究所) Water pressure balance flushing type toilet storage container device for great depth manned submersible
CN107728661A (en) * 2017-10-26 2018-02-23 北京金控数据技术股份有限公司 A kind of control method of sea-water-desalination water producing, system, terminal device and medium

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RO126017A2 (en) 2011-02-28
WO2011005129A3 (en) 2011-11-17

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