CN204529784U - A kind of liquid fuel extraction system - Google Patents
A kind of liquid fuel extraction system Download PDFInfo
- Publication number
- CN204529784U CN204529784U CN201520208940.XU CN201520208940U CN204529784U CN 204529784 U CN204529784 U CN 204529784U CN 201520208940 U CN201520208940 U CN 201520208940U CN 204529784 U CN204529784 U CN 204529784U
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- Prior art keywords
- seawater
- liquid fuel
- reverse osmosis
- osmosis membrane
- extraction system
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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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model provides a kind of liquid fuel extraction system, for extracting the liquid fuel containing deuterium ion from seawater, it comprises: extraction element and seawater bin, described extraction element comprises reverse osmosis membrane apparatus and strainer, by pipeline, seawater is derived from seawater bin, filter out impurity in seawater and fresh water through filter and reverse osmosis membrane apparatus successively, collect the liquid fuel containing deuterium ion.In the utility model, make use of reverse osmosis technology, the fresh water in seawater is separated, extract the seawater enriched material containing deuterium ion, it is oppositely utilized, proposes brand-new developing direction in the exploitation field of seawater, convert seawater to liquid fuel.
Description
Technical field
The utility model relates to extraction system, particularly the extraction system of liquid fuel.
Background technology
The exploitation of the energy and innovation are global problems, at present, there are oil, coal, ore, sun power, waterpower, wind-force etc. by the energy that people develop, main widespread use or oil and coal etc. hide resource deeply, when these energy are always used up, and the burning of centuries uses, and brings the pollution of a lot of waste gas and wastes also to entirely ball, while utilizing natural resource, bring more environmental pollution to nature.
Scientific discovery, the sun is a fixed star constantly carrying out thermonuclear reaction, it relies on the continual generation fusion nucleus reaction of D atom, create a large amount of light and heats, send to each fixed star solar, simultaneously, also carry a large amount of D atoms with the form of solar wind form cosmic dust and distribute to universe, D atom is a kind of isotropic substance of high energy particle hydrogen, the best fuel of nucleosynthesis, the D atom major part that solar wind takes the earth to is all scattered in sea, through the accumulation of For hundreds of millions of years, the storage of the D atom/ion in ocean is very huge, how to utilizing oceanic resources, find the large problem that eco-friendly power source is various countries' scientists.
Utility model content
In order to extract the liquid fuel containing high density deuterium ion from seawater, the utility model provides a kind of liquid fuel extraction system, being separated, extracting required liquid fuel from seawater by filtering with reverse osmosis process to fresh water.
In order to realize above-mentioned utility model object, the utility model provides a kind of liquid fuel extraction system, for extracting the liquid fuel containing deuterium ion from seawater, it comprises: extraction element and seawater bin, described extraction element comprises reverse osmosis membrane apparatus, derived from seawater bin by seawater by pipeline, filter out the fresh water in seawater through reverse osmosis membrane apparatus, the seawater concentrated solution of collection containing deuterium ion is as liquid fuel.
Preferably, the dissolvability solid amount of described liquid fuel is equal to or greater than 30,000 mg/litre, and the pH value of described liquid fuel is equal to or greater than 50.
Preferably, described extraction element comprises the strainer be connected with reverse osmosis membrane apparatus further, after seawater is filtered impurity, import reverse osmosis membrane apparatus and leach fresh water, described strainer is multistage filter, described strainer at different levels is connected mutually, draws seawater filter out impurities through multistage filter by pipeline from seawater bin.
Preferably, described extraction element comprises power transmission pump further, and it is installed on the feed-water end of strainer, by power transmission pump extracting seawater transferring in strainer from seawater bin.Described power transmission pump comprises low-pressure pump and high-pressure pump, and described high-pressure pump is arranged at the feed-water end of strainer at different levels respectively, draws seawater by pipeline from seawater bin, imports in strainer successively carry out sea water filter through low-pressure pump and high-pressure pump.
Preferably; over-pressure safety device and electromagnetic valve device is provided with between described high-pressure pump and low-pressure pump; the hydraulic pressure entering high-pressure pump is controlled by over-pressure safety device; when the hydraulic pressure of deriving from low-pressure pump exceedes setup pressure value; over-pressure safety device sends electrical signal and drives electromagnetic valve device control high-pressure pump out of service; to carry out overvoltage protection to the work of high-pressure pump, avoid that hydraulic pressure is excessive causes greater impact to it.
Preferably, described extraction system comprises byproduct collection box further, and it is connected with reverse osmosis membrane apparatus by byproduct output channel, for collecting the fresh water byproduct filtered out through reverse osmosis membrane apparatus.
Preferably, be communicated with by liquid fuel output channel between reverse osmosis membrane apparatus and seawater bin, by liquid fuel output channel, the liquid fuel containing deuterium ion extracted through reverse osmosis membrane apparatus is transmitted back in seawater bin, with the liquid fuel repeatedly needed for concentrated seawater concentrated solution to acquisition, through circulation reverse osmosis, the dissolvability solid amount in seawater can be promoted exponentially, detect its dissolvability solid amount when reaching set(ting)value, required liquid fuel can be obtained.
Wherein, in described reverse osmosis membrane apparatus, reverse osmosis membrane is cellulose acetate membrane, aromatic polyhydrazide film or aromatic polyamide film.
Compared with prior art, the utility model liquid fuel extraction system, make use of seawater resources fully, find deuterium ion content abundant in seawater, make use of reverse osmosis technology, the fresh water in seawater is separated, extract the seawater enriched material containing deuterium ion, in seawater enriched material, deuterium ion is the optimum feed stock of nuclear reaction, and when its soluble solid content reaches certain value, deuterium ion concentration reaches the standard of liquid fuel.Reverse osmosis process extensively utilizes in fresh water extracts, but the seawater enriched material after people also do not utilize fresh water to extract, and process as waste water, in the utility model, it is oppositely utilized, brand-new developing direction is proposed in the exploitation field of seawater, convert seawater to liquid fuel, instead of traditional oil, coal, the various energy such as firepower, the liquid fuel that seawater conversion obtains, not only draw materials extensively, cheap, refine simple and easy, and, have pollution-free without discharge, energy transformation ratio advantages of higher, generating can be widely used in, automobile, aircraft, on the power such as steamer, it is a quantum jump of energy development.
Accompanying drawing explanation
Fig. 1 is the structural representation of a kind of liquid fuel extraction system of the utility model.
Embodiment
In order to effectively utilize deuterium element in seawater, the seawater isolate containing deuterium ion is gone out by multi-filtering and reverse osmosis process concentration extraction, it can be used as efficient liquid fuel, huge energy is discharged by nuclear fusion reaction, instead of the traditional energy such as oil, coal, obtain a kind of brand-new eco-friendly power source.
In order to obtain described liquid fuel, the utility model provides a kind of liquid fuel extraction system, for extracting the liquid fuel containing deuterium ion from seawater, it comprises: extraction element 1 and seawater bin 2, described extraction element 1 comprises reverse osmosis membrane apparatus 10, derived from seawater bin 2 by seawater by pipeline, filter out the fresh water in seawater through reverse osmosis membrane apparatus 10, the seawater concentrated solution of collection containing deuterium ion is as liquid fuel.
Preferably, described extraction element 1 comprises the strainer 11 be connected with reverse osmosis membrane apparatus 10 further, and seawater, after filter 11 impurity screening, imports reverse osmosis membrane apparatus 10 and leaches fresh water.
Wherein, extraction element 1 is for filtering and reverse-osmosis treated seawater, it is packaged in cylindricality casing, comprises reverse osmosis membrane apparatus 10, strainer 11, inlet channel 12, liquid fuel output channel 13, byproduct output channel 14 and the various control instruments be attached thereto.Seawater bin 2 can be positioned over the outside of extraction element 1, be connected with the strainer 11 of extraction element by inlet channel 12, so that the seawater in seawater bin 2 is extracted, reverse osmosis membrane apparatus 10 is connected with seawater bin 2 by liquid fuel output channel 13, be connected with a byproduct collection box 3 by byproduct output channel 14, by liquid fuel output channel 13, the seawater concentrated solution gone out through reverse osmosis isolation is extracted back in seawater bin 2, the liquid fuel of set(ting)value is reached through the concentrated acquisition deuterium ion concentration that repeatedly circulates, and the byproduct such as fresh water gone out through reverse osmosis isolation transfers in byproduct collection box 3 through byproduct output channel 14.Be separated seawater concentrated solution and byproduct by twin flue, and circulating filtration, infiltration are carried out repeatedly to seawater concentrated solution, improve the deuterium ion TDS value (dissolvability solid amount) in seawater concentrated solution exponentially, to obtain required liquid fuel.
Wherein, described strainer 11 is multistage filter, and described strainer 11 at different levels is connected mutually, draws seawater filter out impurities through multistage filter 11 by inlet channel 12 from seawater bin 2.In the present embodiment, described strainer 11 comprises the two-stage filter of series connection mutually, twice filtration is carried out through two-stage filter, effectively can filter out a large amount of impurity in seawater, as muriate, metal-salt etc., described extraction element 1 comprises power transmission pump 15 further, and it is installed on the feed-water end of strainer 11, by power transmission pump 15 extracting seawater transferring in strainer 11 from seawater bin 2.Described power transmission pump 15 comprises low-pressure pump 150 and high-pressure pump 151, described high-pressure pump 151 is arranged at the feed-water end of strainer 11 at different levels respectively, from seawater bin 2, draw seawater by pipeline, import in strainer 11 through low-pressure pump 150 and high-pressure pump 151 successively and carry out sea water filter.Low-pressure pump 150 provides power, carries out primary filter by seawater suction strainer 11.High-pressure pump 110 is provided with in described strainer 11, over-pressure safety device 111 and electromagnetic valve device 112, described over-pressure safety device 111 and electromagnetic valve device 112 are arranged between low-pressure pump 150 and high-pressure pump 151, the hydraulic pressure entering high-pressure pump 151 is controlled by over-pressure safety device 111, setting hydraulic pressure higher limit, when the seawater hydraulic pressure of deriving from low-pressure pump 150 is greater than setup pressure value, when the hydraulic pressure of deriving from low-pressure pump 150 exceedes setup pressure value, over-pressure safety device 111 sends electrical signal and drives electromagnetic valve device 112 to control high-pressure pump 151 out of service, to carry out overvoltage protection to strainer.In over-pressure safety device 111, arrange 3-5Mpa is normally-pressured neighbor.In described reverse osmosis membrane apparatus 10, reverse osmosis membrane is cellulose acetate membrane, aromatic polyhydrazide film or aromatic polyamide film.
Liquid fuel within output channel 13 is provided with first throttle valve, to regulate seawater water flow; Byproduct output channel 14 is also provided with second throttle, to regulate the water flow of the by products such as fresh water.
The utility model additionally provides a kind of extraction process of liquid fuel, it comprises the step by reverse osmosis membrane apparatus filtering fresh water from seawater, when the dissolvability solid amount of the seawater concentrated solution after filtering fresh water is equal to or greater than 30,000 mg/litre, obtain described liquid fuel.By detecting the TDS value in seawater concentrated solution, to judge whether it reaches the standard of fuel.
Preferably, in described extraction process, comprise the step of seawater being carried out to cascade filtration further, the impurity in filtering sea.Described filtration step before or after fresh water reverse-osmosis treated, can be preferably before reverse-osmosis treated.
Below liquid fuel leaching process is briefly described:
Step 1) first plug in, close the water valve entering seawater bin 2 and byproduct collection box 3,
Step 2) starting outfit, carries out back flushing, is rinsed well by the impurity that machine is residual;
Step 3) then, open the water valve of seawater bin 2 and byproduct collection box 3, close tap water water discharge valve, formally enter the operation of fuel extraction procedure;
Step 4) seawater is first through low-pressure pump 150, by low-pressure pump extracting seawater from seawater bin 2, be transported in double filter, through twice filtration, leach the impurity such as the most of metal-salt in seawater, seawater after filtration enters one-level high-pressure pump, enter secondary high-pressure pump again, pipeline has tensimeter to detect, and controlling ducted pressure range is 3-5MPA, exceed described pressure, then over-pressure safety device transmission electrical signal drives electromagnetic valve device control high-pressure pump out of service;
Step 5) last, enter reverse osmosis membrane apparatus 10, through reverse osmosis membrane apparatus 10, fresh water separation is disengaged, fresh water after separation transfers in byproduct collection box 3 by byproduct output channel 14, by liquid fuel output channel 13, the liquid fuel containing deuterium ion extracted through reverse osmosis membrane apparatus 10 is transmitted back in seawater bin 2, with the liquid fuel repeatedly needed for concentrated seawater to acquisition, so circulate, constantly increase the concentration of deuterium ion.
Seawater iterative cycles containing deuterium ion is concentrated, improve the dissolvability solid amount of the deuterium ion in seawater exponentially, the dissolvability solid amount of described liquid fuel is equal to or greater than 30,000 mg/litre, when being preferably greater than 40,000 mg/litre, the pH value of described liquid fuel is equal to or greater than 50, reaches the TDS value of required liquid fuel and the standard of pH value.
The utility model liquid fuel extraction system, make use of seawater resources fully, find deuterium ion content abundant in seawater, make use of reverse osmosis technology, be separated by fresh water in seawater, extract the seawater enriched material containing deuterium ion, in seawater enriched material, deuterium ion is the optimum feed stock of nuclear reaction, when its soluble solid content reaches certain value, deuterium ion concentration reaches the standard of liquid fuel.Reverse osmosis process extensively utilizes in fresh water extracts, but the seawater enriched material after people also do not utilize fresh water to extract, and process as waste water, in the utility model, it is oppositely utilized, brand-new developing direction is proposed in the exploitation field of seawater, convert seawater to liquid fuel, instead of traditional oil, coal, the various energy such as firepower, the liquid fuel that seawater conversion obtains, not only draw materials extensively, cheap, refine simple and easy, and, have pollution-free without discharge, energy transformation ratio advantages of higher, generating can be widely used in, automobile, aircraft, on the power such as steamer, it is a quantum jump of energy development.
Claims (10)
1. a liquid fuel extraction system, for extracting the liquid fuel containing deuterium ion from seawater, it is characterized in that comprising: extraction element and seawater bin, described extraction element comprises reverse osmosis membrane apparatus, by pipeline, seawater is derived from seawater bin, filter out the fresh water in seawater through reverse osmosis membrane apparatus, the seawater concentrated solution of collection containing deuterium ion is as liquid fuel.
2. liquid fuel extraction system according to claim 1, is characterized in that: the dissolvability solid amount of described liquid fuel is equal to or greater than 30,000 mg/litre.
3. liquid fuel extraction system according to claim 1, is characterized in that: the pH value of described liquid fuel is equal to or greater than 50.
4. liquid fuel extraction system according to claim 1, it is characterized in that: described extraction element comprises the strainer be connected with reverse osmosis membrane apparatus further, after seawater is filtered impurity, import reverse osmosis membrane apparatus and leach fresh water, described strainer is multistage filter, described strainer at different levels is connected mutually, draws seawater filter out impurities through multistage filter by pipeline from seawater bin.
5. liquid fuel extraction system according to claim 4, it is characterized in that: described extraction element comprises power transmission pump further, it is installed on the feed-water end of strainer, by power transmission pump extracting seawater transferring in strainer from seawater bin.
6. liquid fuel extraction system according to claim 5, it is characterized in that: described power transmission pump comprises low-pressure pump and high-pressure pump, described high-pressure pump is arranged at the feed-water end of strainer at different levels respectively, from seawater bin, draw seawater by pipeline, import in strainer through low-pressure pump and high-pressure pump successively and carry out sea water filter.
7. liquid fuel extraction system according to claim 6; it is characterized in that: between described high-pressure pump and low-pressure pump, be provided with over-pressure safety device and electromagnetic valve device; the hydraulic pressure entering high-pressure pump is controlled by over-pressure safety device; when the hydraulic pressure of deriving from low-pressure pump exceedes setup pressure value, over-pressure safety device sends electrical signal and drives electromagnetic valve device control high-pressure pump out of service.
8. liquid fuel extraction system according to claim 1, it is characterized in that: described extraction system comprises byproduct collection box further, it is connected with reverse osmosis membrane apparatus by byproduct output channel, for collecting the fresh water byproduct filtered out through reverse osmosis membrane apparatus.
9. liquid fuel extraction system according to claim 1, it is characterized in that: be communicated with by liquid fuel output channel between reverse osmosis membrane apparatus and seawater bin, by liquid fuel output channel, the seawater concentrated solution containing deuterium ion extracted through reverse osmosis membrane apparatus is transmitted back in seawater bin, with the liquid fuel repeatedly needed for concentrated seawater to acquisition.
10. liquid fuel extraction system according to claim 1, is characterized in that: in described reverse osmosis membrane apparatus, and reverse osmosis membrane is cellulose acetate membrane, aromatic polyhydrazide film or aromatic polyamide film.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520208940.XU CN204529784U (en) | 2015-04-08 | 2015-04-08 | A kind of liquid fuel extraction system |
| PCT/CN2016/078620 WO2016161939A1 (en) | 2015-04-08 | 2016-04-07 | Liquid fuel extraction system and extraction process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520208940.XU CN204529784U (en) | 2015-04-08 | 2015-04-08 | A kind of liquid fuel extraction system |
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| CN204529784U true CN204529784U (en) | 2015-08-05 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201520208940.XU Expired - Fee Related CN204529784U (en) | 2015-04-08 | 2015-04-08 | A kind of liquid fuel extraction system |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104726142A (en) * | 2015-04-08 | 2015-06-24 | 广州同合能源科技有限公司 | Liquid fuel extraction system and process |
| CN105502718A (en) * | 2016-01-06 | 2016-04-20 | 广州同合能源科技有限公司 | Multi-stage concentrate seawater fuel extracting system |
| WO2016161939A1 (en) * | 2015-04-08 | 2016-10-13 | 林溪石 | Liquid fuel extraction system and extraction process |
-
2015
- 2015-04-08 CN CN201520208940.XU patent/CN204529784U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104726142A (en) * | 2015-04-08 | 2015-06-24 | 广州同合能源科技有限公司 | Liquid fuel extraction system and process |
| WO2016161939A1 (en) * | 2015-04-08 | 2016-10-13 | 林溪石 | Liquid fuel extraction system and extraction process |
| CN105502718A (en) * | 2016-01-06 | 2016-04-20 | 广州同合能源科技有限公司 | Multi-stage concentrate seawater fuel extracting system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190704 Address after: 510000 Luogang Industrial Park (Office Building) No. 9, Licheng Street, Zengcheng District, Guangzhou City, Guangdong Province Patentee after: Guangzhou Cold Fusion Power Technology Co., Ltd. Address before: 510515 No. 298 Xinsha Taibei Road, Taihe Town, Baiyun District, Guangzhou City, Guangdong Province Patentee before: Guangzhou is with closing Energy Science Co., Ltd |
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| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150805 Termination date: 20210408 |