| Dokumentenidentifikation |
EP1857171 03.01.2008 |
| EP-Veröffentlichungsnummer |
0001857171 |
| Titel |
System zur Entsalzung von Meerwasser mittels eines Düsenverfahrens |
| Anmelder |
Xu, Xiaoning, Hai Dian District, Beijing, CN |
| Erfinder |
Xu, Xiaoning, Hai Dian District, Beijing 100089, CN; Ji, Ming, Hai Dian District, Beijing 100089, CN |
| Vertreter |
derzeit kein Vertreter bestellt |
| Vertragsstaaten |
AT, BE, BG, CH, CY, CZ, DE, DK, EE, ES, FI, FR, GB, GR, HU, IE, IS, IT, LI, LT, LU, LV, MC, MT, NL, PL, PT, RO, SE, SI, SK, TR |
| Sprache des Dokument |
EN |
| EP-Anmeldetag |
15.05.2007 |
| EP-Aktenzeichen |
072519903 |
| EP-Offenlegungsdatum |
21.11.2007 |
| Veröffentlichungstag im Patentblatt |
03.01.2008 |
| IPC-Hauptklasse |
B01D 61/04(2006.01)A, F, I, 20071023, B, H, EP
|
| IPC-Nebenklasse |
C02F 1/44(2006.01)A, L, I, 20071023, B, H, EP
B01J 19/10(2006.01)A, L, I, 20071023, B, H, EP
B06B 1/02(2006.01)A, L, I, 20071023, B, H, EP
C02F 1/04(2006.01)A, L, I, 20071023, B, H, EP
C02F 1/36(2006.01)A, L, I, 20071023, B, H, EP
C02F 1/00(2006.01)A, L, I, 20071023, B, H, EP
|
| IPC additional class |
C02F 103/08 (2006.01) A, L, N, 20071023, B, H, EP
|
| Beschreibung[en] |
|
The present invention relates to a seawater desalination
apparatus. More particularly, the present invention relates to a seawater desalination
apparatus by using a jet technique, which falls in a technical field of the International
Patent Classification C02F1/00 "water, wastewater, sewage treatment."
Description of the Prior Art
Currently, various methods for seawater desalination have
been applied at home and abroad, including phase-changing, evaporation, distillation,
cooling, membrane separation, reverse osmosis, electro-dialysis, chemical equilibrium,
ionexchange, hydration, solvent extraction, and so on. Recently, flash-evaporation
takes the leading role, which occupies about 70% of the total production of the
desalinated seawater. However, flash-evaporation has the disadvantages of a high
investment in apparatuses, a large seawater circulation, a small water production,
a low concentration ratio, and a high operation cost.
Summary of the Invention
Accordingly, the present invention is directed to a novel
seawater desalination system using a jet technique, to overcome the disadvantages
of the prior art.
The object of the present invention is achieved by the
following technical solutions.
The present invention provides a seawater desalination
system using the jet technique, which comprises a filter apparatus, a sonic energy
treatment apparatus, and a desalination apparatus. The filter apparatus includes:
a seawater collecting port, connected to a seawater bump; a seawater bump connected
to a coarse filter apparatus; and a fine filter apparatus connected to the coarse
filter apparatus. After the fine filtering process, the seawater enters into the
sonic energy treatment apparatus. According to actual requirements, the sonic energy
treatment apparatus can include two to multiple stages. After being treated by the
sonic energy treatment apparatus, the seawater exists in the form of small molecular
clusters and stored in a water storage tank, and then bumped to a reverse osmosis
membrane. Then, after osmosis, the water becomes freshwater and stored in a freshwater
tank.
In another solution of the present invention, the reverse
osmosis membrane of the above solution is replaced by a distillatory, and the freshwater
distilled from the distillatory is stored in a freshwater tank.
The sonic energy treatment apparatus is mainly a hydrodynamic
sonic energy generator, which is a metal chamber composed of a middle chamber, and
an upper and a lower axial chamber; an upper and a lower end surface of the upper
and lower chambers have two coaxial outlets disposed on the axel center, and the
middle chamber has inlets uniformly distributed thereon. The middle chamber has
4-40 inlets distributed thereon, which are inclined holes in the moving direction
of the fluid, and the angle between an axis of the inlets and a tangent line of
the excircle is 30°-90°. The aperture ratio of the inlets to the outlets
is in the range of 100:1 - 100:20. The ratio of the root diameter of the upper axial
chamber for the hydrodynamic sonic energy generator to the diameter of the middle
chamber is in the range of 1:1 - 1:5.
The present invention has the advantages of a simple structure,
less investment on the apparatuses, low cost, and stable performance. The seawater
is not only desalinated, but also chain-shortened into water of small molecular
clusters, which is easily absorbed and utilized by human body.
Brief description of the drawings
- FIG. 1 is a schematic view of a combination of apparatuses for a seawater desalination
system according to the present invention; and
- Figs. 2 and 3 are schematic structural views of an inner chamber of a sonic
energy generator in the sonic energy treatment apparatus.
List of Reference Numerals
- 1
- Seawater collecting port
- 2
- Seawater bump
- 3
- Coarse filter apparatus
- 4
- Fine filter apparatus
- 5
- Air compressor
- 6
- Sonic energy treatment apparatus
- 7
- Small molecular seawater storage tank
- 8
- Pump
- 9
- Reverse osmosis membrane
- 10
- Freshwater tank
- 11
- Hydrodynamic sonic energy generator
Detailed Description
As shown in FIG 1, seawater to be desalinated is sent to
a coarse filter apparatus 3 from a seawater collecting port 1 by a seawater pump
2. After a preliminary filtering process, various impurities are filtered off. After
passing the coarse filter, the seawater enters a fine filter apparatus 4 for performing
germicidal treatment and so on, and then enters a sonic energy treatment apparatus
6. Then, air is sent into a hydrodynamic sonic energy generator 11 by an air compressor
5. Then, after two-stage (or multi-stage) oscillating and jetting treatment, the
seawater was processed into refined small molecular seawater, and stored in a small
molecular seawater storage tank 7, and then sent to a reverse osmosis membrane 9
by a pump 8. After the reverse osmosis treatment, the salt is removed, and the small
molecular seawater becomes freshwater and stored in a freshwater tank 10 for being
used. (The coarse filter apparatus and the fine filter apparatus are apparatus applied
in the conventional art).
As shown in FIG. 2, the hydrodynamic sonic energy generator
11 is a metal chamber, which includes a middle chamber, and an upper and a lower
axial chamber; an upper and a lower end surface of the upper and lower chambers
have two coaxial outlets disposed in the axis, and the middle chamber has inlets
uniformly distributed thereon. The middle chamber has 4-40 inlets distributed thereon,
which are inclined holes in the moving direction of the fluid, and the angle between
an axis of the inlets and a tangent line of the excircle is 30°-90°. The
aperture ratio of the inlets to the outlets is in the range of 100:1 - 100:20. The
ratio of the root diameter of the upper axial chamber for the hydrodynamic sonic
energy generator 11 to the diameter of the middle chamber is in the range of 1:1
- 1:5. The frequency of the generator is 100 Hz-300,000 Hz, and the sound intensity
is greater than 100 dB. The pressure of the hydraulic pump is 0.2 MPa-80 MPa, and
the power of the hydraulic pump is 2 KW-500 KW.
The jet technique of the present invention is a hydrodynamic
sonic energy processing technique, and the principle is described as follows. The
procedure of the hydrodynamic sonic energy processing can be briefly described as:
according to various solid, liquid, and gas materials to be processed and various
processing purposes, a specific hydrodynamic medium, specific sound frequency, specific
sound intensity, specific sound field distribution, and other processing conditions
are selected. The material to be processed is processed under these conditions,
so that corresponding mechanical effect, thermal effect, chemical effect, biological
effect, or changes caused by the above effects occur in the material, so as to achieve
the purpose of sonic energy processing.
"The hydrodynamic sonic energy generator generates audible
sounds and ultrasounds by adjusting the liquid or high-speed gas with fluids as
the power source, which has the unique advantages of a simple structure, low cost,
large handling capacity, convenient operation, and desirable durability 7", and
more importantly, it still has the advantages of "a low energy consumption, and
a convenient power source, so that it is suitable for being used in industrial applications
8". Though the hydrodynamic sonic energy generator theoretically has the above seven
advantages, in order to develop a system for preparing water-coal slurry through
a hydrodynamic sonic energy technique as the present invention, it is necessary
to shorten the distance from the theoretical possibility to the technical reality.
Currently, the hydrodynamic sonic energy generator has
shown unique advantages in industrial applications, and has exhibited its powerful
vitality. However, due to various factors, relevant mathematical treatments are
very difficult, so that the sound production mechanism has not yet been explained
satisfactorily till now, and thus, most of the study is merely limited at the analysis
of relevant experimental phenomena. In series of applications, the problem is considered
merely based upon the experimental formula and the results and characteristic trends
given by the experimental curves under specific and different conditions. As for
actual requirements, the accurate predictions in terms of theory and sound wave
features relevant to the calculation, such as frequency, intensity, sound field
distribution, will be undoubtedly beneficial for the applications and control. Therefore,
further study on the generation and features of the sound of the hydrodynamic sonic
energy generator is the research direction deserving to be studied in depth. 9"
A part of the notes about "sonic energy" is cited from
"ultrasonics" by Chongfu Ying; 7 is cited from Page 495, Chapter 7, Section
7.3; 8 is cited from Page 506, Chapter 7, Section 7.3.6; and 9 is cited from Page
506, Chapter 7, Section 7.3.6. "Ultrasonics" is published by China Science
Press, [Beijing] Copyright Registration Number 092, First Edition: December, 1990;
Second Printing: December, 1993.
|
| Anspruch[en] |
|
A seawater desalination system using a jet technique, comprising a filter
apparatus, a sonic energy treatment apparatus, and a desalination apparatus, wherein
the filter apparatus comprises: a seawater collecting port (1), connected to a seawater
pump (2); the seawater bump (2), connected to a coarse filter apparatus (3); the
coarse filter apparatus (3), with an outlet connected to an inlet of a fine filter
apparatus (4); the fine filter apparatus (4), with an outlet connected to an sonic
energy treatment apparatus (6); the last stage sonic energy treatment apparatus,
connected to a small molecular cluster seawater storage tank (7); the water storage
tank (7), connected to a reverse osmosis membrane (9) through a pump (8), and connected
to a freshwater tank (10) by a pipeline.
The seawater desalination system using the jet technique as claimed
in Claim 1, wherein the reverse osmosis membrane (9) is replaced by a distillatory.
The seawater desalination system using the jet technique as claimed
in Claim 1, wherein the sonic energy treatment apparatus (6) is a combination of
one-stage to multi-stage hydrodynamic sonic energy generator (11); a hydrodynamic
sonic energy generator (11) is a metal chamber, comprising a middle chamber, and
an upper and a lower axial chamber, wherein an upper and a lower end surface of
the upper and the lower axial chambers have two coaxial outlets disposed at an axle
center, and the middle chamber has inlets uniformly distributed thereon.
The seawater desalination system using the jet technique as claimed
in Claim 1, wherein the middle chamber has 4-40 inlets distributed thereon.
The seawater desalination system using the jet technique as claimed
in Claim I, wherein the inlets are inclined holes in the moving direction of the
fluid, and an angle between an axis of the inlets and a tangent line of an excircle
is 30°-90°.
The seawater desalination system using the jet technique as claimed
in Claim 1, wherein an aperture ratio of the inlets to the outlets is in the range
of 100:1 - 100:20.
The seawater desalination system using the jet technique as claimed
in Claim 1, wherein the ratio of the root diameter of the upper axial chamber for
the hydrodynamic sonic energy generator (11) to the diameter of the middle chamber
is in the range of 1:1-1:5.
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