CN203112541U - Seawater desalter for flue gas waste heat recovery of marine turbine - Google Patents
Seawater desalter for flue gas waste heat recovery of marine turbine Download PDFInfo
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- CN203112541U CN203112541U CN2013201228745U CN201320122874U CN203112541U CN 203112541 U CN203112541 U CN 203112541U CN 2013201228745 U CN2013201228745 U CN 2013201228745U CN 201320122874 U CN201320122874 U CN 201320122874U CN 203112541 U CN203112541 U CN 203112541U
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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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Abstract
The utility model discloses a seawater desalter for flue gas waste heat recovery of a marine turbine. The seawater desalter comprises a steam generator, a first condensing heat exchanger, a second condensing heat exchanger, a pollution discharge heat exchanger, a fresh water container, delivery pipelines and a PID (Proportion-Integration-Differentiation) controller, wherein the steam generator is in a shape of a pot, a flue gas heater is arranged on the lower part in the steam generator, a water collector is arranged on the upper part in the steam generator, and a water level controller and a temperature inductor are arranged in the steam generator; the temperature inductor is connected with a data collector arranged outside the steam generator, and the data collector is used for inputting data into the PID controller; and the delivery pipelines are a seawater pipeline, a steam pipeline and a pollution discharge pipeline. According to the seawater desalter for the flue gas waste heat recovery of the marine turbine, which is provided by the utility model, firstly, flue gas generated by the marine turbine is utilized to heat seawater, so that the seawater is boiled, and then two-stage heating of steam latent heat and quantitative pollution discharging heat is performed on fresh seawater, so as to increase the temperature of the fresh seawater which enters the steam generator, thereby improving effective utilization of waste heat.
Description
Technical field
The utility model relates to a kind of fresh-water generator, particularly, relates to a kind of marine turbine fume waste heat and reclaims fresh-water generator.
Background technology
The fresh water of boats and ships can take the space of ship and increase load by deposit mainly from land at present, and utilizing seawater to produce fresh water is a kind of comparatively desirable water mode processed, and sea water desaltination mainly contains reverse osmosis method, flash method, distillation method etc.
Semi-permeable membranes reverse osmosis method device complexity peculiar to vessel, cost is higher, and seawater needs pre-treatment, and it is bigger that fresh water producing water ratio and fresh water quality are subjected to the influent quality influence.
The flash distillation ratio juris is the seawater after the heating to be input to negative-pressure container evaporate, at present the marine sea water desalting device is to send into vacuum chamber after utilizing the diesel cylinder sleeve cooling water heat with the seawater heating to carry out vacuum-evaporation and be condensed into fresh water, because the jacket-cooling water temperature is about 80 ℃, so heated seawater only could evaporate under negative pressure state, need power and negative pressure device and produce negative pressure, complex structure and cost height, be restricted in application, general small-sized civilian ship is seldom used.Because the cylinder sleeve quantity of circulating water is limited, this fresh-water generator only is used for high-power seagoing vessel or war vessels simultaneously.
Distillation method is the simple method of a kind of traditional principle, and its method is that seawater is heated to boiling, will obtain fresh water behind the vapor condensation that produce.Distillation method is the main method that present many boats and ships prepare fresh water, the equipment that distillation method prepares fresh water comparatively simply need not to make the power-equipment of negative pressure, quality requirements to seawater is not high, need not to carry out sea water preprocessing, because producing process is with condensation behind the evaporation of seawater, the water outlet quality of its preparation fresh water is higher.The main drawback of distillation method is that equipment scaling is serious, and energy consumption is very high.
The utility model content
The purpose of this utility model provides a kind ofly efficiently utilizes the marine turbine using waste heat from tail gas to carry out the device of sea water desaltination for the sea water desaltination field according to the thermal conduction study relative theory.
In order to achieve the above object, the utility model provides a kind of marine turbine fume waste heat to reclaim fresh-water generator, wherein, described this fresh-water generator comprises vapour generator, first condensing heat exchanger, second condensing heat exchanger, blowdown interchanger, fresh water holder, transport pipe and PID controller (Proportion Integration Differentiation, proportional-integral derivative controller).
Described vapour generator is a jar shape, and its inner below is provided with flue gas heater, and inner and upper is provided with water-recovering device, also is provided with water monitor and temperature inductor in the described vapour generator; Described temperature inductor links to each other with the data collecting instrument that is located at the vapour generator outside, and described data collecting instrument is to PID controller input data; Described transport pipe comprises seawater pipeline, steam-pipe and blow-off line; Described seawater pipeline is connected with second condensing heat exchanger with first condensing heat exchanger respectively, the other end of first condensing heat exchanger is connected with blowdown interchanger and vapour generator successively by seawater pipeline, and the other end of second condensing heat exchanger is the seawater discharge line; Also be provided with PID control valve and altitude valve on the seawater pipeline between described blowdown interchanger and the vapour generator successively; Described PID control valve links to each other with the PID controller, and described altitude valve links to each other with water monitor; Described steam-pipe is arranged on the top of described vapour generator, and passes from the inside of first condensing heat exchanger and the inside of second condensing heat exchanger successively, and the end of described steam-pipe is connected with the fresh water holder; Described blow-off line is arranged on the bottom of described vapour generator, and passes from the inside of described blowdown interchanger, and the end of described blow-off line is sewage draining exit.
The seawater of described this fresh-water generator heats up to twin-stage heats up, and is undertaken by condensing heat exchanger and blowdown interchanger respectively.First condensing heat exchanger is that the steam latent heat in the steam-pipe that utilizes realizes that the fresh seawater first step heats up; The blowdown interchanger is that the sensible heat of the vapour generator that the utilizes waste water of discharging realizes that the fresh seawater second stage heats up.Be that the first step is that fresh seawater and condensing heat exchanger heat exchange heat up, this one-level heat exchange is the latent heat of vaporization of Absorption by Sea Water vapor evaporated from vapour generator; The second stage is the high density salt solution heat exchange that fresh seawater and blowdown go out, and what this one-level fresh seawater absorbed is the sensible heat heat of sewer.
The vapor condensation of described this fresh-water generator is two-stage condensation, and steam by at first condensation, all is condensed into liquid water for guaranteeing steam in first condensing heat exchanger, is stored in the fresh water holder again by second condensing heat exchanger, and then with the fresh water that makes.Namely, fresh seawater is heated and makes its temperature raise during first step condensation, this first step mainly is the rising that requirement guarantees the fresh seawater temperature, second stage condensation is by a large amount of seawater condensed steam, the second stage is can both be condensed into liquid water for the water vapour that guarantees to evaporate, namely make by uncooled water vapor enforcing condensation still behind first condensing heat exchanger, thereby improve producing water ratio.
Above-mentioned marine turbine fume waste heat reclaims fresh-water generator, wherein, be provided with filtering net, make-up pump, sea water preprocessing device and first flow variable valve successively from an initial end on the described seawater pipeline, the seawater pipeline of the first flow variable valve the other end links to each other with second condensing heat exchanger with first condensing heat exchanger respectively.Seawater enters the sea water preprocessing device through make-up pump after boosting and carries out preliminary treatment, prevents that silt from bringing vapour generator into.
Above-mentioned marine turbine fume waste heat reclaims fresh-water generator, wherein, also is provided with second flow control valve on the seawater pipeline between described first condensing heat exchanger and the first flow variable valve.Second flow control valve and first flow variable valve are used for distributing seawater to enter the discharge of first condensing heat exchanger, second condensing heat exchanger.
Above-mentioned marine turbine fume waste heat reclaims fresh-water generator, and wherein, the blow-off line in described sewage draining exit the place ahead is provided with the blowdown control valve.This fresh-water generator adopts the supply of residual quantity water level, and the vapour generator evaporated water is the water yield difference that enters altitude valve and blowdown control valve.
Above-mentioned marine turbine fume waste heat reclaims fresh-water generator, wherein, described vapour generator is forced continuous blowdown by described blowdown control valve, blowdown flow rate is to enter 5 ~ 15% of vapour generator fresh seawater amount, avoid in the producer salt concentration to raise, thereby slow down and prevent scale formation.
Above-mentioned marine turbine fume waste heat reclaims fresh-water generator, and wherein, described PID controller is also controlled the flue gas inlet of described flue gas heater, and described flue gas is ship engine tail gas, and its temperature is higher than 200 ℃ all can satisfy the heat transfer requirement.
Above-mentioned marine turbine fume waste heat reclaims fresh-water generator, and wherein, described temperature inductor is the temperature inductor of pt100 or armouring T type thermopair, is located at described flue gas heater top.
Above-mentioned marine turbine fume waste heat reclaims fresh-water generator, and wherein, when the temperature that described temperature inductor records was lower than 105 ℃, described PID controller reduced the seawater flooding quantity by the PID control valve; When the described temperature that records is higher than 120 ℃, by described PID controller, strengthens the seawater flooding quantity or reduce the flue gas inlet.Thereby at the nucleate boiling state, avoid excessive boiling to influence heat exchange the control of the boiling state in the vapour generator, perhaps temperature is lower than nucleate boiling and causes that the steam output capacity is low.That is, when temperature during less than 105 ℃, belong to convective heat exchange in the vapour generator this moment, and the steam quantum of output is little, should reduce the infeed of seawater, when temperature reaches 105 ~ 115 ℃, enters nucleate boiling, and this moment, the steam generation was bigger, belonged to steady state.When temperature surpasses 120 ℃, reach excessive boiling in the vapour generator, boiling crisis appears, and rapidly strengthen flooding quantity or reduce flue gas throughput by the PID controller this moment.
Above-mentioned marine turbine fume waste heat reclaims fresh-water generator, and wherein, described water-recovering device is provided with wavy channel, and passage width is 2 ~ 10mm.The seawater steam that this water-recovering device can be taken the vapour generator bumping out of is captured and is only allowed water vapour pass through, thereby improves purity and the quality that distills out water vapour.
Above-mentioned marine turbine fume waste heat reclaims fresh-water generator, and wherein, described water monitor is positioned at described water-recovering device below, and water surface top.This water monitor can be controlled the seawater flooding quantity by altitude valve, avoids the vapour generator median water level too high.
Above-mentioned marine turbine fume waste heat reclaims fresh-water generator, and wherein, the seawater flow of described second condensing heat exchanger is 3 ~ 10 times of the first condensing heat exchanger seawater flow.
The marine turbine fume waste heat that the utility model provides reclaims fresh-water generator and has the following advantages:
The utility model is exactly the shortcoming at prior art, employing be the blowdown interlock method of forcing continuously, namely force continuous blowdown according to certain seawater ratio that enters, avoid that salt concentration raises in the producer, thereby slow down and prevent scale formation.Simultaneously at the high characteristics of distillation method energy consumption, utilize be the tail gas used heat of engine emission as thermal source, the heat of marine diesel engine tail gas accounts for more than 30% of total energy at present, its temperature is about 400 ℃, utilize this part energy to produce fresh water, have good prospect and effect.What adopt simultaneously is that the fresh seawater two-stage heats up, and namely one-level is that fresh seawater and condensing heat exchanger heat exchange heat up, and this one-level heat exchange is the latent heat of vaporization of Absorption by Sea Water vapor evaporated from vapour generator; The second stage is the high density salt solution heat exchange that goes out with blowdown, and what this one-level fresh seawater absorbed is the sensible heat heat of sewer.Thereby improve the afterheat utilization rate.
Description of drawings
Fig. 1 is the synoptic diagram that marine turbine fume waste heat of the present utility model reclaims fresh-water generator.
Embodiment
Below in conjunction with accompanying drawing embodiment of the present utility model is further described.
As shown in Figure 1, the marine turbine fume waste heat that the utility model provides reclaims fresh-water generator, comprises vapour generator 1, first condensing heat exchanger 2, second condensing heat exchanger 3, blowdown interchanger 4, fresh water holder 5, transport pipe 6 and PID controller 7.
Vapour generator 1 is a jar shape, and its inner below is provided with flue gas heater 8, and inner and upper is provided with water-recovering device 9, also is provided with water monitor 10 and temperature inductor 11 in the vapour generator 1.
Transport pipe 6 comprises seawater pipeline 61, steam-pipe 62 and blow-off line 63.
Be provided with filtering net 15, make-up pump 16, sea water preprocessing device 17 and first flow variable valve 18 successively from an initial end on the seawater pipeline 61, the seawater pipeline 61 of first flow variable valve 18 the other ends links to each other with second condensing heat exchanger 3 with first condensing heat exchanger 2 respectively.Seawater enters sea water preprocessing device 17 through make-up pump 16 after boosting and carries out preliminary treatment, prevents that silt from bringing vapour generator 1 into.Also be provided with second flow control valve 19 on the seawater pipeline 61 between first condensing heat exchanger 2 and the first flow variable valve 18.Second flow control valve 19 and first flow variable valve 18 are used for distributing seawater to enter the discharge of first condensing heat exchanger 2, second condensing heat exchanger 3.The seawater flow of second condensing heat exchanger 3 is 3 ~ 10 times of first condensing heat exchanger, 2 seawater flows.
Steam-pipe 62 is arranged on the top of vapour generator 1, and passes from the inside of first condensing heat exchanger 2 and the inside of second condensing heat exchanger 3 successively, and the end of steam-pipe 62 is connected with fresh water holder 5.
Blow-off line 63 is arranged on the bottom of vapour generator 1, and passes from the inside of blowdown interchanger 4, and the end of blow-off line 63 is sewage draining exit 631.The blow-off line 63 in sewage draining exit 631 the place aheads is provided with blowdown control valve 20.Vapour generator 1 is forced continuous blowdown by blowdown control valve 10, and blowdown flow rate is to enter 5 ~ 15% of vapour generator 1 fresh seawater amount, avoids in the producer salt concentration to raise, thereby slows down and prevent scale formation.
PID controller 7 is also controlled the flue gas inlet of flue gas heater 8, and flue gas is ship engine tail gas, and its temperature is higher than 200 ℃ all can satisfy the heat transfer requirement.
Water-recovering device 9 is provided with wavy channel, and passage width is 2 ~ 10mm.The seawater steam that this water-recovering device 9 can be taken vapour generator 1 bumping out of is captured and is only allowed water vapour pass through, thereby improves purity and the quality that distills out water vapour.
The workflow that the marine turbine fume waste heat that the utility model provides reclaims fresh-water generator is as follows.
Vapor generation and heat exchange process: fresh seawater is squeezed into by make-up pump 16, enters first condensing heat exchanger 2, and with the steam heat-exchanging that vapour generator 1 produces, fresh seawater enters blowdown interchanger 4 thereupon, and the dirty wastewater heat exchange with forcing to discharge realizes the two-stage heat exchange.Heat exchange heats up seawater and enters vapour generator 1 afterwards through two-stage.Fresh seawater is heated to explosive evaporatoin by turbine tail gas in vapour generator 1, steam is by being installed in the water-recovering device 9 on vapour generator 1 top, this water-recovering device 9 adopts wavy channel, passage width 2 ~ 10mm, the seawater steam that this water-recovering device 9 can be taken vapour generator 1 bumping out of is captured and is only allowed water vapour pass through, thereby improves purity and the quality that distills out water vapour; Water vapor enters 2 condensations of first condensing heat exchanger and heats fresh seawater afterwards, water vapor condensation may be also insufficient, so it is fed second condensing heat exchanger 3 again, this step only is to utilize cooled with seawater, can both be condensed into liquid water in order to ensure the water vapour that evaporates, the seawater flow that enters second condensing heat exchanger 3 is 3 ~ 10 times of first condensing heat exchanger, 2 seawater flows, distributes by second flow control valve 19 and first flow variable valve 20.
Control flow in the vapour generator 1: the temperature inductor 11 that water monitor 10, pt100 or armouring T type thermopair are installed in vapour generator 1, and by the boiling state in altitude valve 14 and PID control valve 13 control flooding quantity, flue gas inlet and the vapour generators 1, make its temperature guarantee nucleate boiling state between 105 ℃ ~ 115 ℃, avoid excessive boiling or temperature too low and evaporation is slower.When temperature during less than 105 ℃, belong to convective heat exchange in the vapour generator 1 this moment, and the steam quantum of output is little, should reduce the infeed of seawater, when temperature reaches 105 ℃ ~ 115 ℃, enters nucleate boiling, and this moment, the steam generation was bigger, belonged to steady state.When temperature surpasses 120 ℃, reach excessive boiling in the vapour generator 1, boiling crisis appears, and rapidly strengthen flooding quantity or reduce flue gas throughput by PID controller 7 this moment.
The blowdown flow process: blowdown control valve 10 is installed, adopt force continuously blowdown method, blowdown flow rate be set at flooding quantity 5 ~ 15% between, avoid salt concentration rising in the vapour generator 1, thereby slow down and prevent scale formation, and make it that secondary adds hot sea water in blowdown interchanger 4, enter the sea subsequently.
The marine turbine fume waste heat that the utility model provides reclaims fresh-water generator, the fume waste heat that at first utilizes marine turbine to produce adds hot sea water makes it boiling, thereby thereby then by utilizing water vapour latent heat and forcing the heat two-stage heating fresh seawater of blowdown to improve effective utilization that fresh seawater enters the temperature raising used heat of vapour generator 1 continuously.
Although content of the present utility model has been done detailed introduction by above preferred embodiment, will be appreciated that above-mentioned description should not be considered to restriction of the present utility model.After those skilled in the art have read foregoing, for multiple modification of the present utility model with to substitute all will be apparent.Therefore, protection domain of the present utility model should be limited to the appended claims.
Claims (10)
1. a marine turbine fume waste heat reclaims fresh-water generator, it is characterized in that this fresh-water generator comprises vapour generator (1), first condensing heat exchanger (2), second condensing heat exchanger (3), blowdown interchanger (4), fresh water holder (5), transport pipe (6) and PID controller (7);
Described vapour generator (1) is a jar shape, and its inner below is provided with flue gas heater (8), and inner and upper is provided with water-recovering device (9), also is provided with water monitor (10) and temperature inductor (11) in the described vapour generator (1); Described temperature inductor (11) data collecting instrument (12) outside with being located at vapour generator (1) links to each other, and described data collecting instrument (12) is to PID controller (7) input data;
Described transport pipe (6) comprises seawater pipeline (61), steam-pipe (62) and blow-off line (63);
Described seawater pipeline (61) is connected with second condensing heat exchanger (3) with first condensing heat exchanger (2) respectively, the other end of first condensing heat exchanger (2) is connected with blowdown interchanger (4) and vapour generator (1) successively by seawater pipeline (61), and the other end of second condensing heat exchanger (3) is seawater discharge line (611);
Also be provided with PID control valve (13) and altitude valve (14) on the seawater pipeline (61) between described blowdown interchanger (4) and the vapour generator (1) successively; Described PID control valve (13) links to each other with PID controller (7), and described altitude valve (14) links to each other with water monitor (10);
Described steam-pipe (62) is arranged on the top of described vapour generator (1), and pass from the inside of first condensing heat exchanger (2) and the inside of second condensing heat exchanger (3) successively, the end of described steam-pipe (62) is connected with fresh water holder (5);
Described blow-off line (63) is arranged on the bottom of described vapour generator (1), and passes from the inside of described blowdown interchanger (4), and the end of described blow-off line (63) is sewage draining exit (631).
2. marine turbine fume waste heat as claimed in claim 1 reclaims fresh-water generator, it is characterized in that, described seawater pipeline (61) is gone up and is provided with filtering net (15), make-up pump (16), sea water preprocessing device (17) and first flow variable valve (18) successively from an initial end, and the seawater pipeline (61) of first flow variable valve (18) the other end links to each other with second condensing heat exchanger (3) with first condensing heat exchanger (2) respectively.
3. marine turbine fume waste heat as claimed in claim 2 reclaims fresh-water generator, it is characterized in that, also is provided with second flow control valve (19) on the seawater pipeline (61) between described first condensing heat exchanger (1) and the first flow variable valve (2).
4. marine turbine fume waste heat as claimed in claim 1 reclaims fresh-water generator, it is characterized in that the blow-off line (63) in described sewage draining exit (631) the place ahead is provided with blowdown control valve (20).
5. marine turbine fume waste heat as claimed in claim 4 reclaims fresh-water generator, it is characterized in that, described vapour generator (1) is forced continuous blowdown by described blowdown control valve (20), and blowdown flow rate is for entering 5 ~ 15% of vapour generator (1) fresh seawater amount.
6. marine turbine fume waste heat as claimed in claim 1 reclaims fresh-water generator, it is characterized in that, described PID controller (7) is also controlled the flue gas inlet of described flue gas heater (8), and described flue gas is ship engine tail gas, and its temperature is higher than 200 ℃.
7. marine turbine fume waste heat as claimed in claim 1 reclaims fresh-water generator, it is characterized in that described temperature inductor (11) is the temperature inductor (11) of pt100 or armouring T type thermopair, is located at described flue gas heater (8) top.
8. marine turbine fume waste heat as claimed in claim 7 reclaims fresh-water generator, it is characterized in that, when the temperature that described temperature inductor (11) records was lower than 105 ℃, described PID controller (7) reduced the seawater flooding quantity by PID control valve (13); When the described temperature that records is higher than 120 ℃, by described PID controller (7), strengthens the seawater flooding quantity or reduce the flue gas inlet.
9. marine turbine fume waste heat as claimed in claim 1 reclaims fresh-water generator, it is characterized in that described water-recovering device (9) is provided with wavy channel, and passage width is 2 ~ 10mm.
10. marine turbine fume waste heat as claimed in claim 1 reclaims fresh-water generator, it is characterized in that the seawater flow of described second condensing heat exchanger (3) is 3 ~ 10 times of first condensing heat exchanger (2) seawater flow.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013201228745U CN203112541U (en) | 2013-03-19 | 2013-03-19 | Seawater desalter for flue gas waste heat recovery of marine turbine |
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| Application Number | Priority Date | Filing Date | Title |
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| CN2013201228745U CN203112541U (en) | 2013-03-19 | 2013-03-19 | Seawater desalter for flue gas waste heat recovery of marine turbine |
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| CN203112541U true CN203112541U (en) | 2013-08-07 |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103145207A (en) * | 2013-03-19 | 2013-06-12 | 上海海事大学 | Sea water desalting device for twin-stage recovery of flue gas waste heat of marine steam turbine |
| RU2562660C2 (en) * | 2013-11-13 | 2015-09-10 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Оренбургский государственный университет" | Desalination installation generating cold and electric power (versions) |
| CN109049485A (en) * | 2018-09-18 | 2018-12-21 | 咸阳陶瓷研究设计院有限公司 | A kind of inorganic sponge water-storage material foamable is set with drying integrated makeup |
| RU2678065C1 (en) * | 2017-12-01 | 2019-01-22 | федеральное государственное автономное образовательное учреждение высшего образования "Самарский национальный исследовательский университет имени академика С.П. Королёва" | Combined installation of marine water decomposition and electricity development |
| RU2797936C1 (en) * | 2022-04-12 | 2023-06-13 | федеральное государственное автономное образовательное учреждение высшего образования "Самарский национальный исследовательский университет имени академика С.П. Королева" | Sea water desalination plant |
-
2013
- 2013-03-19 CN CN2013201228745U patent/CN203112541U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103145207A (en) * | 2013-03-19 | 2013-06-12 | 上海海事大学 | Sea water desalting device for twin-stage recovery of flue gas waste heat of marine steam turbine |
| CN103145207B (en) * | 2013-03-19 | 2014-04-09 | 上海海事大学 | Sea water desalting device for twin-stage recovery of flue gas waste heat of marine steam turbine |
| RU2562660C2 (en) * | 2013-11-13 | 2015-09-10 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Оренбургский государственный университет" | Desalination installation generating cold and electric power (versions) |
| RU2678065C1 (en) * | 2017-12-01 | 2019-01-22 | федеральное государственное автономное образовательное учреждение высшего образования "Самарский национальный исследовательский университет имени академика С.П. Королёва" | Combined installation of marine water decomposition and electricity development |
| CN109049485A (en) * | 2018-09-18 | 2018-12-21 | 咸阳陶瓷研究设计院有限公司 | A kind of inorganic sponge water-storage material foamable is set with drying integrated makeup |
| RU2797936C1 (en) * | 2022-04-12 | 2023-06-13 | федеральное государственное автономное образовательное учреждение высшего образования "Самарский национальный исследовательский университет имени академика С.П. Королева" | Sea water desalination plant |
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