WO2016000520A1 - 利用船舶发动机排气余热的间接低温多效海水淡化系统 - Google Patents
利用船舶发动机排气余热的间接低温多效海水淡化系统 Download PDFInfo
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- WO2016000520A1 WO2016000520A1 PCT/CN2015/081335 CN2015081335W WO2016000520A1 WO 2016000520 A1 WO2016000520 A1 WO 2016000520A1 CN 2015081335 W CN2015081335 W CN 2015081335W WO 2016000520 A1 WO2016000520 A1 WO 2016000520A1
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- seawater desalination
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/26—Multiple-effect evaporating
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- 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
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- 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
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- 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
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- 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
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- 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
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- 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
Definitions
- the invention relates to a seawater desalination technology for marine vessels, in particular to an indirect low-temperature multi-effect seawater desalination system utilizing exhaust heat of a ship engine exhaust.
- seawater desalination technology is an important technical measure to ensure the supply and replenishment of freshwater water.
- the application of seawater desalination technology is in its infancy in China.
- the “thermal method” low-temperature multi-effect (ie LT-MED) seawater desalination technology is designed to use fresh low-temperature and low-pressure steam to prepare fresh water under certain vacuum conditions, thus solving the main equipment. The problem of scaling at high temperatures.
- Low-temperature multi-effect distillation seawater desalination technology refers to the desalination technology that the maximum evaporation temperature of seawater is generally lower than 70 °C.
- the low-temperature multi-effect distillation seawater desalination system is a series of evaporators connected in series, when working, the low-temperature multi-effect seawater desalination system
- the first effect evaporator absorbs external heat, vaporizes the circulating seawater of the first effect evaporator, generates higher pressure water vapor, and the water vapor is sent to the second effect, as the heat source of the second effect evaporator,
- the condensation in the effect evaporator is fresh water, and at the same time, the circulating seawater of the effect is vaporized, and new steam is sent to the third effect.
- the low-temperature multi-effect distillation seawater desalination system uses a certain amount of steam input to evaporate the seawater several times, and condenses the evaporated gas into water through seawater, thereby obtaining a desalination process of distilled water having a multiple of steam amount, along the flow direction of the steam.
- the evaporation temperature and pressure of the latter effect are lower than the previous one.
- the low-temperature multi-effect seawater desalination technology develops rapidly due to its long service life, simple operation, reliable operation and high product water purity.
- the exhaust gas of the diesel engine contains acid gases such as SO3. When the temperature is high, they will exist in a gaseous form. When the temperature is lower than a certain temperature, they will combine with the water vapor in the exhaust gas to form sulfuric acid and corrode the heat exchange equipment.
- the acid dew point of diesel oil is as high as 120 °C-130 °C. In order to avoid the acid dew corrosion of the heating surface of the tail, the diesel engine exhaust temperature is usually designed to be higher, and the actual operation will be higher.
- an object of the present invention is to provide an indirect low-temperature multi-effect seawater desalination system utilizing exhaust heat of a ship engine for solving the problem that the exhaust heat of a ship engine in the prior art cannot be directly used for low temperature.
- the problem of multi-effect seawater desalination systems is to provide an indirect low-temperature multi-effect seawater desalination system utilizing exhaust heat of a ship engine for solving the problem that the exhaust heat of a ship engine in the prior art cannot be directly used for low temperature.
- the present invention provides an indirect low-temperature multi-effect seawater desalination system utilizing exhaust heat of a ship engine, comprising a low-temperature multi-effect seawater desalination device, a low-temperature steam generating device, and an exhaust pipe disposed in the engine
- the seawater is pretreated and preheated into the low-temperature multi-effect seawater desalination device for desalination treatment, wherein the first-effect air inlet and condensate outlet in the low-temperature multi-effect seawater desalination device
- the low temperature steam generating device is connected to the low temperature steam generating device, and the low temperature steam generating device is connected to the waste heat recovery device through the rising pipe and the descending pipe.
- the first effect condensate outlet is connected to the low temperature steam generating device, and a first preheater is disposed on the pipeline connected to the low temperature steam generating device, and the first preheater is further disposed in the seawater entering the first effect. On the water pipe.
- the seawater is divided into two paths after being pretreated, and respectively passed through a preheater to enter the low-temperature multi-effect seawater desalination device, wherein one preheater is disposed in the product of the low-temperature multi-effect seawater desalination device On the water outlet pipe, another preheater is disposed on the concentrated brine collection pipe of the low temperature multi-effect seawater desalination device.
- the waste heat recovery device is provided with a temperature sensor.
- the conduit of the first effect fresh water outlet connected to the cryogenic steam generating device is also in communication with a fresh water supply pipe.
- the ship engine may also be a furnace containing sulfur fuel, and correspondingly, the engine exhaust pipe is a flue of the heating furnace.
- the indirect low-temperature multi-effect seawater desalination system utilizing the exhaust heat of a ship engine of the present invention has It has the following beneficial effects: the low temperature steam generating device is used as a heat transfer point, which absorbs the heat absorbed by the waste heat recovery device in the exhaust pipe of the engine to generate low temperature steam, and ensures that the temperature of the steam entering the low temperature multi-effect seawater desalination device is lower than 70 °, and the wall temperature of the waste heat recovery device is not lower than the acid dew point temperature, ensuring that the waste heat recovery device does not cause acid dew corrosion due to the low wall temperature. Therefore, the present invention ensures that the waste heat recovery device is free from acid dew corrosion. In the case of the engine exhaust heat, it can provide a heat source for the low-temperature multi-effect seawater desalination device, and generate steam or hot water at the temperature required for the low-temperature multi-effect seawater desalination device.
- FIG. 1 is a schematic view showing a low-temperature multi-effect seawater desalination system using the exhaust heat of a ship engine according to the present invention.
- the present invention provides an indirect low-temperature multi-effect seawater desalination system utilizing exhaust heat of a ship engine, comprising a low-temperature multi-effect seawater desalination device 4, a low-temperature steam generating device 2, and an exhaust gas disposed in the engine 3.
- the waste heat recovery device 1 in the pipeline 9 is subjected to pre-treatment and pre-heating into the low-temperature multi-effect seawater desalination device 4 for desalination treatment, wherein the first-effect air inlet and condensate in the low-temperature multi-effect seawater desalination device 4
- the outlet is connected to the low temperature steam generating device through a pipe (i.e., steam pipe 2-1, condensate pipe 2-2), and the low temperature steam generating device 2 is connected to the waste heat recovery device 1 through the riser pipe 1-1 and the down pipe 1-2.
- the invention adopts a low temperature steam generating device as an intermediate heat transfer point, which absorbs the heat absorbed by the waste heat recovery device in the exhaust pipe of the engine to generate low temperature steam, and ensures that the temperature of the steam entering the low temperature multi-effect seawater desalination device is lower than 70°, At the same time, the wall temperature of the waste heat recovery device will not be lower than the acid dew point temperature, ensuring that the waste heat recovery device will not cause acid dew corrosion due to low temperature.
- the invention adopts the double-loop heat exchange method to realize the low-temperature steam required for converting the exhaust heat of the engine into the low-temperature multi-effect seawater desalination device, and the waste heat recovery device 1 passes the riser 1-1 and the down pipe 1-2 and the low-temperature steam generating device 2 connected to form a first circuit, which mainly ensures that the wall temperature of the waste heat recovery device is higher than the acid dew point temperature, so as to prevent the waste heat recovery device from being corroded by acid dew in the engine exhaust pipe; the low temperature steam generating device 2 passes through the steam pipe 2-1,
- the first connection of the condensed water pipe 2-2 to the low-temperature multi-effect seawater desalination device 4 forms a second circuit, It is mainly used to produce low-temperature steam required for low-temperature multi-effect seawater desalination, that is, to ensure that the steam temperature generated is lower than 70°, so that the steam can be used as a heat source for the low-temperature multi-effect sea
- the condensed water pipe 2-2 connected to the low-temperature steam generating device 2 of the first-effect condensed water outlet is further connected to a fresh water supply pipe 14, and the fresh-water supply pipe 14 is provided with an on-off valve 15 so that the low-temperature multi-effect When the condensed water produced by the first effect of the seawater desalination device cannot satisfy the second circuit cycle, it can be externally replenished.
- the condensed water pipe 2-2 connected to the low-temperature steam generating device 2 of the first effective condensate outlet is provided with a first preheater 16, which is also disposed on the seawater inlet pipe entering the first effect.
- the condensed water generated by the first effect flows out from the condensate outlet and is preheated into the first effect seawater by the first preheater 16 and then flows back to the low temperature steam generating device 2, so that the first effect condensed water can enter the first effect
- the seawater is preheated to ensure maximum heat utilization.
- the seawater is processed by the pre-processor 8 and divided into two paths, which are respectively passed through a preheater and then enter the low-temperature multi-effect desalination device 4, wherein one preheater (ie, the second preheater) 12) It is disposed on the product water outlet pipe 7 of the low-temperature multi-effect seawater desalination device 4, and the other preheater (i.e., the third preheater 5) is disposed on the brine collection pipe 6 of the low-temperature multi-effect seawater desalination device 4.
- one preheater ie, the second preheater 12
- the other preheater i.e., the third preheater 5
- the two preheaters respectively absorb the heat of the product water and the agricultural brine flowing out of the low-temperature multi-effect seawater desalination device to preheat the seawater entering the low-temperature multi-effect seawater desalination device, thereby improving the heat utilization rate inside the entire system.
- the seawater is pretreated by the pretreatment unit 8 and then enters the third preheater 5 and the second preheater 12 in two ways, absorbing the heat of the product water and the concentrated brine, and then entering the condenser of the low temperature multi-effect desalination device 4
- the heat of the vapor evaporated by the final effect evaporator is further absorbed, preheated, degassed, and then divided into two, most of which enter the front multi-effect seawater evaporator, and the excess seawater serves as cooling water from the cooling seawater pipe. 13 discharge.
- a condensate recovery pump 10 is disposed on the condensate water pipe 2-2.
- the waste heat recovery device 1 is provided with a temperature sensor 11, which can detect the wall temperature of the waste heat recovery device in real time, and ensure that the wall surface temperature of the waste heat recovery device is higher than the acid dew point temperature.
- the on-off valve 15 When the system is started, the on-off valve 15 is opened, and the system is replenished by the fresh water supply pipe 14 to allow the fresh water to enter the waste heat recovery device to heat the fresh water and start the water circulation.
- the steam tube 2-1 If low temperature and low pressure steam is used as the heat source, the steam tube 2-1 is also required to be evacuated when the system is started, so that the generated steam temperature is the temperature required for the first effect. If hot water is used directly as a heat source, the water temperature can be heated to the desired temperature.
- the seawater enters the low-temperature multi-effect sea after passing through the pre-processor 8, the third preheater 5 and the second preheater 12
- the water desalination device 4, the saturated steam or the hot water in the first effect of the low-temperature multi-effect seawater desalination device 4 completes the heat exchange with the raw material seawater, and the raw seawater generates almost the same amount of fresh steam outside the heat exchange tube and is introduced to the next.
- the evaporation and condensation process is repeated to generate product water, and the condensed water is circulated through the condensed water pipe 2-2 through the condensed water pipe 2-2 into the low temperature steam generating device 2 by the condensed water recovery pump 10.
- the evaporation temperature is controlled by controlling the pressure in the waste heat recovery device 1, so that the control wall temperature is maintained above the acid dew point temperature, thereby fundamentally avoiding the occurrence of acid dew corrosion.
- the dual-loop can also generate the low-temperature heat source required for the low-temperature multi-effect seawater desalination while maintaining the wall temperature higher than the acid dew point, and does not cause the scaling problem of the seawater desalination equipment.
- the invention is equally applicable to other furnaces containing sulfur fuel, and correspondingly, the engine exhaust duct 9 is a flue of the furnace.
- the indirect low-temperature multi-effect seawater desalination system utilizing the exhaust heat of the marine engine of the present invention uses a low-temperature steam generating device as an intermediate heat transfer point, which absorbs heat absorbed by the waste heat recovery device in the exhaust pipe of the engine.
- the low-temperature steam is generated to ensure that the temperature of the steam entering the low-temperature multi-effect seawater desalination device is lower than 70°, and the wall temperature of the waste heat recovery device is not lower than the acid dew point temperature, ensuring that the waste heat recovery device does not cause acid dew corrosion. Therefore, the present invention effectively overcomes various shortcomings in the prior art and has high industrial utilization value.
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Abstract
Description
Claims (6)
- 一种利用船舶发动机排气余热的间接低温多效海水淡化系统,其特征在于,包括低温多效海水淡化装置(4),低温蒸汽发生装置(2),以及设于发动机排气管道(9)内的余热回收装置(1),海水经预处理和预加热后进入所述低温多效海水淡化装置(4)内进行淡化处理,其中,所述低温多效海水淡化装置(4)中第一效的进气口、凝结水出口与低温蒸汽发生装置(2)通过管道相连,低温蒸汽发生装置(2)通过上升管(1-1)、下降管(1-2)与所述余热回收装置(1)相连。
- 根据权利要求1所述的利用船舶发动机排气余热的间接低温多效海水淡化系统,其特征在于:所述第一效的凝结水出口与所述低温蒸汽发生装置(2)相连的管道上设有第一预热器(16),所述第一预热器(16)还设置在进入第一效的海水进水管上。
- 根据权利要求1所述的利用船舶发动机排气余热的间接低温多效海水淡化系统,其特征在于:所述海水经预处理后分为两路,分别经过一个预热器后进入所述低温多效海水淡化装置中,其中一个预热器设在所述低温多效海水淡化装置(4)的产品水出水管道(7)上,另一个预热器设在所述低温多效海水淡化装置(4)的浓盐水收集管道(6)上。
- 根据权利要求1所述的利用船舶发动机排气余热的间接低温多效海水淡化系统,其特征在于:所述余热回收装置(1)上设有温度传感器(11)。
- 根据权利要求1所述的利用船舶发动机排气余热的间接低温多效海水淡化系统,其特征在于:所述第一效的淡水出口与所述低温蒸汽发生装置(2)相连的管道还与一淡水补给管(14)相连通。
- 根据权利要求1所述的利用船舶发动机排气余热的间接低温多效海水淡化系统,其特征在于:所述船舶发动机(3)替换为含硫燃料的加热炉,相应的,所述发动机排气管道(9)为加热炉的烟道。
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
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JP2016575428A JP6404955B2 (ja) | 2014-06-30 | 2015-06-12 | 船舶エンジンの排気余熱を利用する間接低温マルチエフェクト海水淡水化システム |
DE112015002615.0T DE112015002615T5 (de) | 2014-06-30 | 2015-06-12 | Ein die Abgaswärme von Schiffsmotoren verwendendes indirektes Niedertemperatur-Multieffekt-Entsalzungssystem |
KR1020177000885A KR20170008888A (ko) | 2014-06-30 | 2015-06-12 | 선박 엔진 배기 여열을 이용한 간접 저온 다면 효과 해수 담수화 시스템 |
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CN201410307193.5 | 2014-06-30 | ||
CN201410307193.5A CN104030385B (zh) | 2014-06-30 | 2014-06-30 | 利用船舶发动机排气余热的间接低温多效海水淡化系统 |
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JP (1) | JP6404955B2 (zh) |
KR (1) | KR20170008888A (zh) |
CN (1) | CN104030385B (zh) |
DE (1) | DE112015002615T5 (zh) |
WO (1) | WO2016000520A1 (zh) |
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CN107010684A (zh) * | 2017-04-22 | 2017-08-04 | 祝长宇 | 一种低温多效海水淡化系统 |
CN107720861A (zh) * | 2017-11-16 | 2018-02-23 | 哈尔滨工程大学 | 小型化正压蒸馏海水淡化系统 |
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CN108751311A (zh) * | 2018-07-18 | 2018-11-06 | 中国海洋大学 | 一种利用船舶发动机余热的蒸发式海水淡化系统及方法 |
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- 2015-06-12 KR KR1020177000885A patent/KR20170008888A/ko not_active Application Discontinuation
- 2015-06-12 JP JP2016575428A patent/JP6404955B2/ja not_active Expired - Fee Related
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CN107010684A (zh) * | 2017-04-22 | 2017-08-04 | 祝长宇 | 一种低温多效海水淡化系统 |
CN107720861A (zh) * | 2017-11-16 | 2018-02-23 | 哈尔滨工程大学 | 小型化正压蒸馏海水淡化系统 |
CN107720862A (zh) * | 2017-11-16 | 2018-02-23 | 哈尔滨工程大学 | 一种紧凑型蒸馏法海水淡化装置 |
CN108751311A (zh) * | 2018-07-18 | 2018-11-06 | 中国海洋大学 | 一种利用船舶发动机余热的蒸发式海水淡化系统及方法 |
CN110526318A (zh) * | 2019-09-17 | 2019-12-03 | 南京龙源环保有限公司 | 一种烟气消白耦合海水淡化的能量综合利用方法及系统 |
CN110526318B (zh) * | 2019-09-17 | 2023-10-24 | 国能龙源环保南京有限公司 | 一种烟气消白耦合海水淡化的能量综合利用方法及系统 |
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CN114149045A (zh) * | 2020-11-13 | 2022-03-08 | 山东大学 | 一种换热器及船舶废气余热的海水淡化装置 |
CN114526621A (zh) * | 2021-03-26 | 2022-05-24 | 山东大学 | 一种烟气温控音乐预警的热管换热装置 |
CN113072114A (zh) * | 2021-05-08 | 2021-07-06 | 西安热工研究院有限公司 | 一种浓盐水余热回收用于加热生活用水的系统及方法 |
CN114715968A (zh) * | 2022-04-20 | 2022-07-08 | 中国人民解放军32181部队 | 一种海水淡化处理系统及方法 |
Also Published As
Publication number | Publication date |
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JP6404955B2 (ja) | 2018-10-17 |
DE112015002615T5 (de) | 2017-03-02 |
KR20170008888A (ko) | 2017-01-24 |
CN104030385B (zh) | 2016-10-19 |
CN104030385A (zh) | 2014-09-10 |
JP2017523027A (ja) | 2017-08-17 |
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