PL423020A1 - Associated desalted water production system - Google Patents

Associated desalted water production system

Info

Publication number
PL423020A1
PL423020A1 PL423020A PL42302017A PL423020A1 PL 423020 A1 PL423020 A1 PL 423020A1 PL 423020 A PL423020 A PL 423020A PL 42302017 A PL42302017 A PL 42302017A PL 423020 A1 PL423020 A1 PL 423020A1
Authority
PL
Poland
Prior art keywords
pipeline
effect
distillate production
absorption chiller
absorption
Prior art date
Application number
PL423020A
Other languages
Polish (pl)
Other versions
PL234746B1 (en
Inventor
Marcin Malicki
Filip Mariusz Herman
Yousef Muhammed AL YOUSEF
Fahad Saleh AL KASMOUL
Original Assignee
New Energy Transfer Spółka Z Ograniczoną Odpowiedzialnością
King Abdulaziz City For Science And Technology
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 New Energy Transfer Spółka Z Ograniczoną Odpowiedzialnością, King Abdulaziz City For Science And Technology filed Critical New Energy Transfer Spółka Z Ograniczoną Odpowiedzialnością
Priority to PL423020A priority Critical patent/PL234746B1/en
Priority to PCT/SA2018/050025 priority patent/WO2019066687A1/en
Publication of PL423020A1 publication Critical patent/PL423020A1/en
Publication of PL234746B1 publication Critical patent/PL234746B1/en

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D1/00—Evaporating
    • B01D1/26—Multiple-effect evaporating
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D1/00—Evaporating
    • B01D1/0011—Heating features
    • B01D1/0058—Use of waste energy from other processes or sources, e.g. combustion gas
    • 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
    • C02F1/02—Treatment of water, waste water, or sewage by heating
    • C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/16—Treatment of water, waste water, or sewage by heating by distillation or evaporation using waste heat from other processes
    • 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
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B15/00—Sorption machines, plants or systems, operating continuously, e.g. absorption type
    • F25B15/02—Sorption machines, plants or systems, operating continuously, e.g. absorption type without inert gas
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00—Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124—Water desalination
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00—Combustion technologies with mitigation potential
    • Y02E20/14—Combined heat and power generation [CHP]
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Organic Chemistry (AREA)
  • Sorption Type Refrigeration Machines (AREA)
  • Other Air-Conditioning Systems (AREA)

Abstract

Skojarzony układ produkcji wody odsolonej składający się ze źródła ciepła (1), chłodziarki absorpcyjnej (2), bloku efektów do produkcji destylatu (3), wieży chłodniczej (4), charakteryzujący się tym, że chłodziarka absorpcyjna (2) jest zasilana ciepłem odzyskanym ze źródła ciepła (1) za pośrednictwem rurociągu czynnika grzewczego (5) łączącego chłodziarkę absorpcyjną (2) z układem kogeneracyjnym (1); pierwszy efekt produkcji destylatu (3a) bloku MED (3) jest zasilany ciepłem odebranym z układu chłodzenia chłodziarki absorpcyjnej (2) za pośrednictwem rurociągu (6) łączącego chłodziarkę absorpcyjną (2) z pierwszym efektem produkcji destylatu (3a) gdzie rurociąg (6) składa się rurociągu zasilającego (6a) i rurociągu powrotnego (6b); skraplacz ostatniego efektu produkcji destylatu (3n) jest chłodzony za pomocą wody lodowej produkowanej przez chłodziarkę absorpcyjną (2), gdzie woda lodowa dostarczana jest rurociągiem wody zimnej (7) łączącym ostatni efekt produkcji destylatu (3n) z chłodziarką absorpcyjną (2), gdzie rurociąg (7) składa się rurociągu zasilającego (7a) i rurociągu powrotnego (7b); solanka doprowadzana jest do pierwszego efektu produkcji destylatu (3a) za pośrednictwem rurociągu solanki (11) a zagęszczona solanka wyprowadzana jest z ostatniego efektu produkcji destylatu (3n) za pośrednictwem rurociągu (12) a odsolona woda za pośrednictwem rurociągu (14).Associated desalinated water production system consisting of a heat source (1), absorption chiller (2), distillate production block (3), cooling tower (4), characterized by that the absorption chiller (2) is fed with heat recovered from heat sources (1) via the heating medium pipeline (5) connecting the absorption chiller (2) to the cogeneration system (1); the first effect of distillate production (3a) of the MED block (3) is fed by heat taken from the absorption cooling system (2) via a pipeline (6) connecting the absorption cooler (2) with the first effect of distillate production (3a) where the pipeline (6) consists the supply pipeline (6a) and return pipeline (6b); the condenser of the last distillate production effect (3n) is cooled by means of ice water produced by the absorption chiller (2), where the chilled water is supplied by a cold water pipeline (7) connecting the last effect of distillate production (3n) with the absorption chiller (2), where the pipeline (7) consists of the supply pipeline (7a) and return pipeline (7b); brine is fed to the first distillate production effect (3a) via the brine pipeline (11) and concentrated brine is extracted from the last distillate production effect (3n) via the pipeline (12) and desalinated water via the pipeline (14).

PL423020A 2017-09-29 2017-09-29 Associated desalted water production system PL234746B1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
PL423020A PL234746B1 (en) 2017-09-29 2017-09-29 Associated desalted water production system
PCT/SA2018/050025 WO2019066687A1 (en) 2017-09-29 2018-09-26 Combined desalinated water production system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PL423020A PL234746B1 (en) 2017-09-29 2017-09-29 Associated desalted water production system

Publications (2)

Publication Number Publication Date
PL423020A1 true PL423020A1 (en) 2019-04-08
PL234746B1 PL234746B1 (en) 2020-03-31

Family

ID=64402241

Family Applications (1)

Application Number Title Priority Date Filing Date
PL423020A PL234746B1 (en) 2017-09-29 2017-09-29 Associated desalted water production system

Country Status (2)

Country Link
PL (1) PL234746B1 (en)
WO (1) WO2019066687A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
PL452177A1 (en) * 2024-10-18 2026-04-20 Green Hac Spółka Z Ograniczoną Odpowiedzialnością Method of using the output heat of the working medium of the condenser

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109802793B (en) 2017-11-17 2021-04-02 电信科学技术研究院 Method, device, terminal, and device for processing partial bandwidth deactivation timer
CN110332727B (en) * 2019-06-27 2020-05-19 山东大学 An adsorption water purification refrigeration system driven by industrial waste heat and its application

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
PL138858B1 (en) * 1980-08-22 1986-11-29 Energiagazdalkodasi Intezet Apparatus for carrying out thermodynamical processes comprising mutual phase opposition of working medium transitions
CN204675851U (en) * 2015-05-29 2015-09-30 湖南铁道职业技术学院 A kind of open type heat pump low-temperature multi-effect evaporation seawater desalinization device of water-electricity cogeneration

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DE3004197A1 (en) * 1980-02-06 1981-08-27 GST Gesellschaft für Systemtechnik mbH, 4300 Essen METHOD FOR RECOVERY OF THE HEAT ENERGY CONTAINED IN THE MULTI-STAGE EVAPORATORS USED IN THE BROTHS OF THERMAL FUEL SEPARATION PROCESSES, AND DEVICE FOR CARRYING OUT THE PROCESS
US6010599A (en) * 1995-09-20 2000-01-04 American Technologies Group, Inc. Compact vacuum distillation device
DE19903781A1 (en) * 1999-02-01 2000-08-10 Jakob Hois Multi-stage continually-operated water distillation process uses poorer quality raw water without loss of output water quality
WO2017066534A1 (en) 2015-10-14 2017-04-20 Qatar Foundation For Education, Science And Community Development Hybrid cooling and desalination system
US10246345B2 (en) 2015-12-30 2019-04-02 General Electric Company Water desalination system and method for fast cooling saline water using turbines
CN105841395B (en) 2016-04-01 2018-04-20 集美大学 Light six co-generation system of thermoelectric cold steam heating of cryogenic energy utilization
CN105923676B (en) 2016-04-27 2018-10-23 武汉凯迪工程技术研究总院有限公司 High-efficiency solar sea water desalination and air conditioner refrigerating cooperation method and system
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CN205653194U (en) 2016-05-24 2016-10-19 天津大学 Utilize absorption formula sea water desalination of solar energy and geothermal energy combined drive
CN106698563A (en) 2017-01-25 2017-05-24 国家海洋局天津海水淡化与综合利用研究所 Multi-effect membrane distillation seawater desalination system based on mechanical compression

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
PL138858B1 (en) * 1980-08-22 1986-11-29 Energiagazdalkodasi Intezet Apparatus for carrying out thermodynamical processes comprising mutual phase opposition of working medium transitions
CN204675851U (en) * 2015-05-29 2015-09-30 湖南铁道职业技术学院 A kind of open type heat pump low-temperature multi-effect evaporation seawater desalinization device of water-electricity cogeneration

Non-Patent Citations (1)

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Title
DIEGO-CESAR ALARCON-PADILLA, LOURDES GARCIA-RODRIGUEZ, APPLICATION OF ABSORPTION HEAT PUMPS TO MULTI-EFFECT DISTILLATION: A CASE STUDY OF SOLAR DESALINATION, 25 June 2007 (2007-06-25) *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
PL452177A1 (en) * 2024-10-18 2026-04-20 Green Hac Spółka Z Ograniczoną Odpowiedzialnością Method of using the output heat of the working medium of the condenser

Also Published As

Publication number Publication date
PL234746B1 (en) 2020-03-31
WO2019066687A1 (en) 2019-04-04

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