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Analyzing the Energy Consumption, GHG Emission, and Cost of Seawater Desalination in China

The result's identifiers

  • Result code in IS VaVaI

    <a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F00216305%3A26210%2F19%3APU133763" target="_blank" >RIV/00216305:26210/19:PU133763 - isvavai.cz</a>

  • Result on the web

    <a href="https://www.mdpi.com/1996-1073/12/3/463" target="_blank" >https://www.mdpi.com/1996-1073/12/3/463</a>

  • DOI - Digital Object Identifier

    <a href="http://dx.doi.org/10.3390/en12030463" target="_blank" >10.3390/en12030463</a>

Alternative languages

  • Result language

    angličtina

  • Original language name

    Analyzing the Energy Consumption, GHG Emission, and Cost of Seawater Desalination in China

  • Original language description

    Seawater desalination is considered a technique with high water supply potential and has become an emerging alternative for freshwater supply in China. The increase of the capacity also increases energy consumption and greenhouse gases (GHG) emissions, which has not been well investigated in studies. This study has analyzed the current development of seawater desalination in China, including the capacity, distribution, processes, as well as the desalted water use. Energy consumption and GHG emissions of overall desalination in China, as well as for the provinces, are calculated covering the period of 2006–2016. The unit product cost of seawater desalination plants specifying processes is also estimated. The results showed that 1) The installed capacity maintained increased from 2006 to 2016, and reverse osmosis is the major process used for seawater desalination in China. 2) The energy consumption increased from 81 MWh/y to 1,561 MWh/y during the 11 years. The overall GHG emission increase from 85 Mt CO 2eq /y to 1,628 Mt CO 2eq /y. Tianjin had the largest GHG emissions, following are Hebei and Shandong, with emissions of 4.1 Mt CO 2eq /y, 2.2 Mt CO 2eq /y. and 1.0 Mt CO 2eq /y. 3) The unit product cost of seawater desalination is higher than other water supply alternatives, and it differentiates the desalination processes. The average unit product cost of the reverse osmosis process is 0.96 USD and 2.5 USD for the multiple-effect distillation process. The potential for future works should specify different energy forms, e.g. heat and power. Alternatives of process integration should be investigated—e.g. efficiency of using the energy, heat integration, and renewables in water desalination, as well as the utilization of total site heat integration.

  • Czech name

  • Czech description

Classification

  • Type

    J<sub>imp</sub> - Article in a specialist periodical, which is included in the Web of Science database

  • CEP classification

  • OECD FORD branch

    20402 - Chemical process engineering

Result continuities

  • Project

    <a href="/en/project/EF15_003%2F0000456" target="_blank" >EF15_003/0000456: Sustainable Process Integration Laboratory (SPIL)</a><br>

  • Continuities

    P - Projekt vyzkumu a vyvoje financovany z verejnych zdroju (s odkazem do CEP)

Others

  • Publication year

    2019

  • Confidentiality

    S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů

Data specific for result type

  • Name of the periodical

    ENERGIES

  • ISSN

    1996-1073

  • e-ISSN

  • Volume of the periodical

    3

  • Issue of the periodical within the volume

    12

  • Country of publishing house

    CH - SWITZERLAND

  • Number of pages

    2

  • Pages from-to

    463-464

  • UT code for WoS article

    000460666200131

  • EID of the result in the Scopus database

    2-s2.0-85060912601