WO2013063747A1 - Appareil de traitement de liquide et système de génération d'énergie l'utilisant - Google Patents

Appareil de traitement de liquide et système de génération d'énergie l'utilisant Download PDF

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Publication number
WO2013063747A1
WO2013063747A1 PCT/CN2011/081576 CN2011081576W WO2013063747A1 WO 2013063747 A1 WO2013063747 A1 WO 2013063747A1 CN 2011081576 W CN2011081576 W CN 2011081576W WO 2013063747 A1 WO2013063747 A1 WO 2013063747A1
Authority
WO
WIPO (PCT)
Prior art keywords
liquid
chamber
water
processing apparatus
conduit
Prior art date
Application number
PCT/CN2011/081576
Other languages
English (en)
Chinese (zh)
Inventor
关大俊
Original Assignee
琦胜科技有限公司
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 琦胜科技有限公司 filed Critical 琦胜科技有限公司
Priority to PCT/CN2011/081576 priority Critical patent/WO2013063747A1/fr
Publication of WO2013063747A1 publication Critical patent/WO2013063747A1/fr

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Classifications

    • 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
    • C02F1/10—Treatment of water, waste water, or sewage by heating by distillation or evaporation by direct contact with a particulate solid or with a fluid, as a heat transfer medium
    • C02F1/12—Spray evaporation
    • 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
    • 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

Definitions

  • the present invention relates to a liquid processing apparatus, and more particularly to a liquid processing apparatus which can be applied to seawater desalination and a power generating system using the same.
  • the above seawater desalination system mainly heats and vaporizes seawater by incinerator combustion to produce fresh water.
  • the incinerator used in this desalination system needs to burn heavy oil fuel, which not only causes an increase in seawater desalination costs, but also causes air pollution problems.
  • Another object of the present invention is to provide a liquid processing apparatus which reduces liquid handling costs and reduces air pollution. Another object of the present invention is to provide a power generation system to reduce power generation costs.
  • Embodiments of the present invention provide a liquid processing apparatus including a chamber, a sprinkler, and a chamber heating device.
  • the chamber has an opening and an air inlet, and the opening is located above the air inlet.
  • the sprinkler includes a liquid conduit, a pressure pump, and an atomizer spray.
  • the liquid conduit extends from outside the chamber to the chamber.
  • the pressurizing pump is disposed on a liquid transport path in the liquid conduit to pressurize the liquid.
  • An atomizing sprayer is coupled to one end of the liquid conduit within the chamber, the atomizing sprayer being adapted to convert the liquid into a mist and provide the mist into the chamber.
  • a chamber heating device is disposed around the chamber and is configured to heat the chamber to convert water in the mist into water vapor, the water vapor exiting the chamber through the opening of the chamber.
  • the liquid processing apparatus further includes a water collecting device connected to the opening of the chamber to collect liquid water formed by condensation of water vapor.
  • the liquid processing apparatus further includes a cooling device coupled between the opening of the chamber and the water collecting device.
  • the sprinkler device further includes a liquid filter disposed in the liquid transport path within the liquid conduit.
  • the liquid processing apparatus further includes a gas supply device.
  • the gas supply device includes a gas conduit and a blower.
  • the gas conduit is connected to the tuyere.
  • the blower is disposed in the gas transport path within the gas conduit.
  • the gas supply device further includes an air filter disposed on a gas transport path in the gas conduit.
  • the liquid processing apparatus further includes a gas conduit heating device disposed around the gas conduit.
  • At least one of the chamber heating device and the gas conduit heating device is a solar heating device.
  • the solar heating device comprises a collector and a concentrating unit.
  • the collector is coupled to the outer surface of the chamber or the outer surface of the gas conduit, and the collector has at least one fin that extends into the chamber or within the gas conduit.
  • the concentrating unit is adapted to concentrate sunlight onto the collector.
  • the gas conduit heating device includes a solar heating device and an auxiliary heating device.
  • the liquid processing apparatus further includes a steam power generating device that connects to the opening of the chamber.
  • the mist liquid comprises a plurality of liquid beads each having a diameter of between 5 micrometers and 20 micrometers.
  • the liquid processing apparatus includes a first chamber, a first sprinkler, a first chamber heating device, and a water collecting device.
  • the first chamber has an opening and an air inlet, and the opening is located above the air inlet.
  • the first sprinkler device includes a first liquid conduit, a first pressurizing pump, and a first atomizing sprayer.
  • the first liquid conduit extends from outside the first chamber to the first chamber.
  • the first pressure pump is disposed on the first liquid guide The liquid is transported through the tube to pressurize the liquid.
  • the first atomizing sprayer is coupled to one end of the first liquid conduit within the first chamber, the first atomizing sprayer being adapted to convert the liquid into a mist and to provide the mist into the first chamber.
  • a first chamber heating device disposed around the first chamber and configured to heat the first chamber to convert water in the mist into water vapor, the water vapor leaving the first chamber through the opening of the first chamber room.
  • the water collecting device is connected to the opening of the first chamber to collect the liquid water formed by condensation of the water vapor.
  • the power generating device is connected to a water collecting device of the liquid processing device, and the power generating device includes a second chamber, a second sprinkling device, a second chamber heating device, and a steam power generating device.
  • the second sprinkler device includes a second liquid conduit, a second pressurizing pump, and a second atomizing sprayer.
  • a second liquid conduit is coupled to the water collection device and extends from outside the second chamber to the second chamber to transport liquid water within the water collection device.
  • the second pressurizing pump is disposed on the transport path of the liquid water in the second liquid conduit to pressurize the liquid water.
  • a second atomizing sprayer is coupled to one end of the second liquid conduit within the second chamber, the second atomizing sprayer being adapted to convert liquid water to misty water and to provide the misty water to the second chamber.
  • the second chamber heating device is disposed around the second chamber and is configured to heat the second chamber to convert the misty water into water vapor.
  • the steam power generating device is connected to the second chamber to generate electricity by using water vapor in the second chamber.
  • the second sprinkling device further includes a liquid filter disposed in the liquid water transport path in the second liquid conduit.
  • the power generating apparatus further includes a second liquid conduit heating device disposed around the second liquid conduit.
  • At least one of the second chamber heating device and the second liquid conduit heating device is a solar heating device.
  • the second liquid conduit heating device comprises a solar heating device and an auxiliary heating device.
  • the misty liquid and the misty water respectively comprise a plurality of liquid beads, each of which has a diameter of between 5 and 20 meters.
  • the power generation system of the present invention adopts the above The liquid handling equipment can reduce the cost of liquid handling.
  • the second atomizing atomizer of the power generating device can convert the liquid water into the mist water first, the mist water can be easily converted into water vapor to generate electricity. Therefore, the power generation system of the present invention can reduce the power generation cost.
  • FIG. 1 is a schematic illustration of a liquid processing apparatus in accordance with one embodiment of the present invention.
  • FIG. 2 is a schematic view of a solar heating apparatus according to an embodiment of the present invention.
  • FIG. 3 is a schematic illustration of a power generation system in accordance with one embodiment of the present invention.
  • FIG. 4 is a schematic diagram of a power generating apparatus of a power generation system according to another embodiment of the present invention. Preferred embodiment of the invention
  • the liquid processing apparatus 10 of the present embodiment includes a chamber 110, a sprinkler 120, and a chamber heating device 130.
  • the chamber 110 has an opening 111 and an air inlet 112.
  • the opening 111 is located above the air inlet 112.
  • the gas outside the chamber 110 can enter the chamber 110 via the air inlet 112.
  • the sprinkler device 120 includes a liquid conduit 121, a pressure pump 122, and an atomizing sprayer 124.
  • the liquid conduit 121 extends from the outside of the chamber 110 to the inside of the chamber 110.
  • the pressurizing pump 122 is disposed on the transport path of the liquid 50 in the liquid conduit 121 to perform a pressurizing operation on the liquid 50.
  • the atomizing atomizer 124 is coupled to one end of the liquid conduit 121 located within the chamber 110, and the atomizing atomizer 124 is adapted to convert the liquid 50 into a mist 51 and supply the mist 51 into the chamber 110.
  • the mist 51 includes a plurality of liquid droplets, each of which has a diameter of, for example, between several micrometers and several tens of micrometers. In a preferred embodiment, each of the liquid beads is, for example, between 5 meters and 20 degrees. Between meters.
  • the sprinkler 120 can also include a liquid
  • the body filter 123 is disposed on the transport path of the liquid 50 in the liquid conduit 121 to filter impurities in the liquid 50.
  • the chamber heating device 130 is disposed around the chamber 110 and is used to heat the chamber 110 to convert water in the mist 51 into water vapor 52. Water vapor 52 exits chamber 110 via opening 111 of chamber 110.
  • the chamber heating device 130 of the present embodiment can be selected from the solar heating device shown in Fig. 2, which includes a heat collector 210 and a concentrating unit 220.
  • the collector 210 can be connected to the side wall of the chamber 110, and the concentrating unit 220 is used to concentrate the sunlight 80 to the collector 210, so that the collector 210 can heat the chamber 110.
  • the collector 210 may have at least one fin 14 and FIG. 2 is exemplified by a plurality of fins 212. These heat sink fins 212 extend through the sidewalls of the chamber 110 into the chamber 110 to dissipate thermal energy into the chamber 110.
  • the chamber heating device 130 described above may be other types of heating devices, such as electric heating devices.
  • the chamber heating device 130 can also include both solar heating devices and other types of heating devices. In this way, when the sun is not enough, it can be heated with other types of heating devices.
  • the liquid processing apparatus 10 of the present embodiment may further include a water collecting means 140 which is connected to the opening 111 of the chamber 110 to collect the liquid water 53 formed by condensation of the water vapor 52. Further, in order to increase the cooling efficiency of the water vapor 52, the liquid processing apparatus 10 may further include a cooling device 150 connected between the opening 111 of the chamber 110 and the water collecting device 140.
  • the cooling device 150 has, for example, a plurality of fins 152 adapted to exchange heat with the water vapor 52 to cause the water vapor 52 to condense more quickly into the liquid water 53.
  • the structure of the above-described cooling device 150 is for illustrative purposes only, and the present invention is not limited to the specific structure of the cooling device.
  • the cooling device can also include an active heat dissipating component, such as a fan.
  • the liquid processing apparatus 10 may further include a gas supply device 160.
  • This gas supply device 160 includes a gas conduit 161 and a blower 162.
  • the gas conduit 161 is connected to the air inlet 112 of the chamber 110.
  • the blower 162 is disposed on the transport path of the gas 60 within the gas conduit 161 and is used to supply the gas 60 into the chamber 110.
  • the gas supply device 160 may further include an air filter 163 disposed on a transmission path of the gas 60 in the gas conduit 161 to filter impurities in the gas 60.
  • the liquid processing apparatus 10 may further include a gas conduit heating device 170 disposed around the gas conduit 161 to heat the gas 60 in the gas conduit 161.
  • the gas conduit heating device 170 can be selected from the solar heating device shown in FIG. 2, but is not limited thereto.
  • the heat collector 210 of the solar heating device can contact the gas conduit 161, and the heat dissipation fins 212 of the heat collector 210 can extend into the gas conduit 161 to dissipate thermal energy into the gas conduit 161.
  • the gas conduit heating device 170 may further include an auxiliary heating device in addition to the solar heating device described above. This auxiliary heating device is different from the solar heating device, so that the gas 60 in the gas conduit 161 can still be heated by the auxiliary heating device when the sunlight is insufficient.
  • the liquid processing apparatus 10 of the present embodiment can be applied to seawater desalination, that is, the liquid 50 described above can be seawater.
  • the invention does not limit the use of the liquid processing apparatus 10.
  • the liquid processing apparatus 10 of the present embodiment since the liquid 50 is converted into the mist liquid 51 by the atomizing atomizer 124, the water in the mist liquid 51 can be easily converted into water without using too much heat energy. Steam 52, which reduces the cost of liquid handling.
  • air pollution can be reduced.
  • both the chamber heating device 130 and the gas conduit heating device 170 can be equipped with a solar heating device, the liquid handling cost and air pollution can be further reduced.
  • the liquid processing apparatus may not include the above-mentioned water collecting device 140 and the cooling device 150, and the opening 111 of the chamber 110 may be connected to a steam power generating device (not shown) to utilize Water vapor 52 is used to generate electricity.
  • FIG. 3 is a schematic illustration of a power generation system in accordance with one embodiment of the present invention.
  • the power generation system 30 of the present embodiment includes the liquid processing apparatus 10 and the power generating apparatus 31 described above, and the power generating apparatus 31 is connected to the water collecting apparatus 140 of the liquid processing apparatus 10.
  • the power generating device 31 includes a chamber 310, a sprinkling device 320, a chamber heating device 330, and a steam power generating device 340.
  • the sprinkler device 320 includes a liquid conduit 321, a pressure pump 322, and an atomizing spray 324.
  • the liquid conduit 321 is connected to the water collecting device 140 and extends from the outside of the chamber 310 to the inside of the chamber 310 to transfer the liquid water 53 in the water collecting device 140.
  • the pressurizing pump 322 is disposed on the transport path of the liquid water 53 in the liquid conduit 321 to pressurize the liquid water 53.
  • An atomizing sprayer 324 is coupled to one end of the liquid conduit 321 located within the chamber 310, and the atomizing sprayer 324 is adapted to transfer liquid water 53
  • the water is changed to the misty water 54, and the misty water 54 is supplied into the chamber 310.
  • the misty water 54 includes a plurality of liquid droplets, each of which has a diameter of, for example, between several micrometers and several tens of micrometers.
  • each of the liquid beads is, for example, between 5 meters and 20 degrees. Between meters.
  • the sprinkling device 320 may further include a liquid filter 323 disposed on a transport path of the liquid water 53 in the liquid conduit 321 to filter impurities in the liquid water 53.
  • the chamber heating device 330 is disposed around the chamber 310 and is used to heat the chamber 310 to convert the misty water 54 into water vapor 55.
  • the steam power plant 340 communicates with the chamber 310 to generate electricity using water vapor 55 within the chamber 310.
  • the chamber heating device 330 of this embodiment may use the solar heating device shown in Fig. 2, but is not limited thereto.
  • the heat collector 210 of the solar heating device can contact the sidewall of the chamber 310, and the heat dissipation fins 212 of the heat collector 210 can extend into the chamber 310 through the sidewall of the chamber 310 to dissipate heat energy to the chamber.
  • the chamber heating device 330 can also include both solar heating devices and other types of heating devices. In this way, when there is insufficient sunlight, it can be heated with other types of heating devices.
  • the power generating apparatus 31 may further include a liquid conduit heating device 370 disposed around the liquid conduit 321 to heat the liquid water 53 in the liquid conduit 321 .
  • the liquid conduit heating device 370 can be selected from the solar heating device shown in Fig. 2, but is not limited thereto.
  • the collector 210 of the solar heating device can contact the liquid conduit 321, and the heat sink fins 212 of the collector 210 can extend into the liquid conduit 321 to dissipate thermal energy into the liquid conduit 321 .
  • the liquid conduit heating device may further include an auxiliary heating device in addition to the solar heating device described above.
  • This auxiliary heating device is different from the solar heating device, so that the liquid water 53 in the liquid conduit 321 can still be heated by the auxiliary heating device when the sunlight is insufficient. Moreover, since the atomizing atomizer 324 of the power generating device 31 can first convert the liquid water 53 into the misty water 54, the misty water 53 can be easily converted into water vapor 54 without requiring much heat energy for power generation. Therefore, the power generation system 30 of the present embodiment can reduce the power generation cost.
  • the power generating device 41 of the present embodiment includes a plurality of the above-described chambers 310, a water sprinkling device 320, and a chamber heating device 330. Further, the steam power generating device 440 of the power generating device 41 is connected to the chambers 310, and a pressure valve 420 is provided between each of the chambers 310 and the steam power generating device 440.
  • the pressure valve 420 is opened, and the power generating device 41 can use water vapor to generate electricity.
  • the pressure valve 420 is closed. Therefore, the power generating apparatus 41 of the present embodiment can take turns to generate electricity using water vapor in different chambers 310 in turn.
  • the power generation system of the present invention can reduce the cost of liquid processing by employing the liquid processing apparatus described above.
  • the second atomizing atomizer of the power generating device can convert the liquid water into the mist water first, the mist water can be easily converted into water vapor for power generation. Therefore, the power generation system of the present invention can reduce the power generation cost.

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  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)

Abstract

L'invention porte sur un appareil de traitement de liquide, lequel appareil comprend une chambre (110), un dispositif de pulvérisation d'eau (120) et un dispositif de chauffage de chambre (130), dans lequel appareil la chambre a une ouverture (111) et une entrée d'air (112) ; le dispositif de pulvérisation d'eau comprend un conduit de liquide (121), une pompe de pression (122) et un pulvérisateur de pulvérisation (124), le conduit de liquide (121) s'étendant à partir de l'extérieur jusqu'à l'intérieur de la chambre et le pulvérisateur de pulvérisation (124) étant relié à l'extrémité du conduit de liquide à l'intérieur de la chambre et étant apte à changer le liquide en un liquide pulvérisé ; le dispositif de chauffage de chambre (130) est disposé autour de la chambre pour le chauffage de celle-ci, de façon à changer l'eau dans le liquide pulvérisé en vapeur, et la vapeur quitte la chambre à travers l'ouverture (111) de celle-ci. L'appareil de traitement de liquide peut être utilisé comme appareil de désalinisation de l'eau de mer. La présente invention porte également sur un système de génération d'énergie utilisant l'appareil de traitement de liquide. L'appareil de traitement de liquide et le système de génération d'énergie l'utilisant peuvent réduire les coûts.
PCT/CN2011/081576 2011-10-31 2011-10-31 Appareil de traitement de liquide et système de génération d'énergie l'utilisant WO2013063747A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PCT/CN2011/081576 WO2013063747A1 (fr) 2011-10-31 2011-10-31 Appareil de traitement de liquide et système de génération d'énergie l'utilisant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/CN2011/081576 WO2013063747A1 (fr) 2011-10-31 2011-10-31 Appareil de traitement de liquide et système de génération d'énergie l'utilisant

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WO2013063747A1 true WO2013063747A1 (fr) 2013-05-10

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104418397A (zh) * 2013-08-21 2015-03-18 莫少民 一种太阳能双效海水淡化装置及其海水淡化方法

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2412888Y (zh) * 2000-03-28 2001-01-03 孙建岐 喷洒式海水淡化装置
KR100659375B1 (ko) * 2005-08-30 2006-12-19 (주)동양화학 무화증기를 이용한 해수 담수화 장치
CN2868996Y (zh) * 2005-12-01 2007-02-14 张五毛 一种废液蒸发机
CN201309841Y (zh) * 2008-11-28 2009-09-16 王鑫 一种太阳能海水淡化装置
US20110017583A1 (en) * 2009-07-26 2011-01-27 Michael John Lord Method and Apparatus for Effluent Free Sea Water Desalination
US20110056822A1 (en) * 2009-09-04 2011-03-10 Massachusetts Institute Of Technology Water Separation Under Reduced Pressure

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2412888Y (zh) * 2000-03-28 2001-01-03 孙建岐 喷洒式海水淡化装置
KR100659375B1 (ko) * 2005-08-30 2006-12-19 (주)동양화학 무화증기를 이용한 해수 담수화 장치
CN2868996Y (zh) * 2005-12-01 2007-02-14 张五毛 一种废液蒸发机
CN201309841Y (zh) * 2008-11-28 2009-09-16 王鑫 一种太阳能海水淡化装置
US20110017583A1 (en) * 2009-07-26 2011-01-27 Michael John Lord Method and Apparatus for Effluent Free Sea Water Desalination
US20110056822A1 (en) * 2009-09-04 2011-03-10 Massachusetts Institute Of Technology Water Separation Under Reduced Pressure

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104418397A (zh) * 2013-08-21 2015-03-18 莫少民 一种太阳能双效海水淡化装置及其海水淡化方法
CN104418397B (zh) * 2013-08-21 2017-02-08 莫少民 一种太阳能双效海水淡化装置及其海水淡化方法

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