CN100580352C - Method for producing fluidified fuel of marsh gas, and dedicated fluidified jar capable of measuring marsh gas - Google Patents
Method for producing fluidified fuel of marsh gas, and dedicated fluidified jar capable of measuring marsh gas Download PDFInfo
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- CN100580352C CN100580352C CN200610115111A CN200610115111A CN100580352C CN 100580352 C CN100580352 C CN 100580352C CN 200610115111 A CN200610115111 A CN 200610115111A CN 200610115111 A CN200610115111 A CN 200610115111A CN 100580352 C CN100580352 C CN 100580352C
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- biogas
- micropore
- methane
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Abstract
A method for preparing methane liquefied fuel includes sending methane to low pressure gas cabin through pipeline then sending methane into accountable methane liquefaction tank packed with solutizer by gas compressor being automatically controlled, sending compressed methane to micro-hole gas-jet pipe unit connected with safety check valve, jetting methane through solutizer liquid layer to generate micro-hole energy focusing effect to liquefy methane to be liquefied methane.
Description
Technical field:
The present invention relates to a kind of processing method and special equipment thereof of liquefied gas as fuel, particularly produce the method and the special equipment thereof of biogas liquefied fuel for the primary raw material deep processing with biogas.The present invention is former female case: patent application day: on April 29th, 2005, and number of patent application: 200510070344.0, denomination of invention is: the dividing an application of " non-failure biogas fermentation tank and biogas liquefied fuel and bio-compound fertilizer producing method ".
Background technology:
As female case: number of patent application: 200510070344.0 denominations of invention are: described in " non-failure biogas fermentation tank and biogas liquefied fuel and bio-compound fertilizer producing method ", current " typing " marsh gas fermentation pool that is widely current and has built up or built in town and country, especially big-and-middle-sized marsh gas fermentation pool, it is the pig farm recovery of three wastess(waste gas,waste water and industrial residue), one of the main large-scale production facility that must possess of developing a circular economy, if with every day " three wastes " all full dose " innoxious " dispose, then have a large amount of biogas to produce; Through measuring and calculating: the dirts such as ight soil that medium-sized pig farm full dose every day " innoxious " that scale is 3000 boars disposes the same day, more than 2,000 cubic metre of biogas of energy output every day, and pig farm itself is used for illumination, life fuel etc., only can consume sub-fraction (a few hectostere), all the other a large amount of biogas need to handle, inconvenient again remote the transmission have to seen its bubbling race Heaven in vain, caused the huge wasting of resources.
Summary of the invention:
The technical problem to be solved in the present invention is: provide a kind of production method and special equipment thereof of biogas liquefied fuel, to solve a large amount of biogas resource utilization issues that produce of big-and-middle-sized marsh gas fermentation pool.
The technical scheme that solves the problems of the technologies described above is: a kind of production method of biogas liquefied fuel, its technical process is as follows: biogas is delivered to the low pressure gas storehouse through appendix, powerful compression is sent into special-purpose measurable biogas liquefied jar that cosolvent is housed in advance through the special gas compressor of control automatically, biogas by compression ends the micropore air jet pipe group device that valve is connected via returning with air inlet safety, from countless micropore ejections, pass through the cosolvent liquid layer, the prominent big phenomenon-be the micropore Mohaupt effect of discharging of biogas delivery pressure energy appears with cosolvent liquid junctional area, obtain a species transformation energy and the metamorphosis of liquefying changes into LMG, described cosolvent is the mixed liquor of a certain amount of combination partner of carbon five following liquid phase low molecular hydrocarbons classes.
The described cosolvent that is made of the mixed liquor of a certain amount of combination partner of carbon five following liquid phase low molecular hydrocarbons classes mainly can contain a certain amount of component mixed liquors such as liquid ethane, special propane, special butane; Can also contain a certain amount of component mixed liquors such as propylene, butylene, propane propylene, butane butylene and their isomers, senior liquefied gas.
The special-purpose measurable biogas liquefied jar that the production method of described a kind of biogas liquefied fuel is used, mainly claim two big combined integratedization of parts to form by tank body and special electronic, the tank body part main member has two safety relief valves, tank shell, two suspension ring, the liquid in-out safety valve, Pressure gauge, air inlet safety is returned and is ended valve and micropore air jet pipe group, described micropore air jet pipe group is mounted in one group of high-voltage tube group of jar inner bottom part, be equipped with numerous micropore on the pipe perisporium, one termination blind plugging of pipe, other end parallel connection communicates and returns only with air inlet safety that valve is connected, described special electronic claims parts mainly by supporting plate, the two groups of guide pillar guide pin bushings in front and back, the two groups of gravity sensors in front and back, the electronic signal acquisition process shows computer, base plate and base are formed, the two groups of guide pillars in front and back are weldingly fixed on the tank body, and corresponding guide pin bushing is weldingly fixed on the sole plate base.
The invention has the beneficial effects as follows: the present invention is raw material with biogas, its deep processing is liquefied, producing bottled is the alkane liquid gas alternative fuel of Main Ingredients and Appearance with biogas, solve biogas inconvenience long distance and gone out the difficult problem that use in the other places, enlarged the social function of biogas utilization of new energy resources, for big-and-middle-sized pig farm, town and country makes full use of a large amount of associated resources (biogas) in " three wastes " innoxious downstream, prolong industrial chain, develop a circular economy, both thoroughly solve " three wastes " problem of environment pollution caused, significantly promoted economic benefit of enterprises again.
The present invention implements on big-and-middle-sized pig farm, and extraordinary economic benefit and social benefit are arranged.Through measuring and calculating, biogas as one 3000 livestock on hand kind pig farms, except that personal, the residual gas deep processing is liquefied, annual output at least is the alkane liquid gas fuel of Main Ingredients and Appearance with biogas for 40,000 bottles, and the benefit contribution portion of fuel is equivalent to nearly about half of enterprise's normal profit that whole pig products are created.
Below, its special-purpose measurable biogas liquefied jar technical characterictic of production method to a kind of biogas liquefied fuel of the present invention is described further in conjunction with the accompanying drawings and embodiments.
Description of drawings:
Fig. 1: the technological process of the production method of a kind of biogas liquefied fuel of the present invention and technical equipment block diagram;
Fig. 2: measurable biogas liquefied jar of cross section structure schematic diagram.
Among the figure:
1-low pressure gas storehouse, 2-special gas compressor assembly, special-purpose measurable biogas liquefied jar of 3-, 4-product can packing machine, 5-cosolvent can packing machine, 6-product library, 7-cosolvent storehouse, 8, the 25-safety relief valve, the 9-tank shell, 10,20-suspension ring, two guide pillar guide pin bushings before the 11-liquid in-out safety valve, 12-, dual power sensor before the 13-, the 14-Pressure gauge, 15-cosolvent liquid level, the 16-supporting plate, the 17-signal acquisition process shows computer, the 18-base, 19-micropore air jet pipe group, 21-base plate, dual power sensor behind the 22-, two guide pillar guide pin bushings behind the 23-, 24-air inlet safety is returned only valve.
The specific embodiment:
A kind of production method of biogas liquefied fuel.The technological process of production of this method and technical equipment block diagram be as shown in Figure 1: biogas is delivered to the low pressure gas storehouse through appendix, powerful compression is sent into measurable biogas liquefied jar that cosolvent is housed in advance through the special gas compressor of control automatically, biogas by compression ends the micropore air jet pipe group device that valve is connected via returning with air inlet safety, from countless micropore ejections, pass through the cosolvent liquid layer, by the prominent big phenomenon-promptly call the micropore Mohaupt effect of discharging of biogas delivery pressure energy occurring, obtain enough abnormal energy and the metamorphosis of liquefying changes into LMG with cosolvent liquid junctional area; Described cosolvent is the mixed liquor of a certain amount of combination partner of carbon five following liquid phase low molecular hydrocarbons classes; It mainly is the mixed liquor that contains a certain amount of ethane, special propane, special butane combination partner; It also can be the mixed liquor that contains combination partner such as a certain amount of propylene, butylene, propane propylene, butane butylene and their isomers, senior liquefied gas.
Major technique is equipped with: appendix, low pressure gas storehouse 1, special gas compressor and automatic control system 2, special-purpose measurable biogas liquefied jar 3, fuel tank installation 4, cosolvent can packing machine 5, product library 6, cosolvent storehouse 7.Described special use is the indispensable equipment specials of biogas liquefied deep processing for measurable biogas liquefied jar 3, its structure is as accompanying drawing 2: claimed integratedly to constitute by tank body and special electronic, the tank body parts have: safety relief valve 8,25, tank shell 9, suspension ring 10,20, liquid in-out material safety valve 11, Pressure gauge 14, air inlet safety is returned and is ended valve 24 and micropore air jet pipe group 19; Micropore air jet pipe group 19 is mounted in one group of high-voltage tube group of jar inner bottom part, be equipped with numerous micropore on the pipe perisporium, one termination blind plugging, in addition in parallel the communicating of end returned the ad hoc device that valve 24 only is connected with air inlet safety, its effect is to make biogas have increased access to a kind of physical energy under special environment condition, promptly calls the micropore Mohaupt effect.
Special electronic claims parts by supporting plate 16, the two groups of guide pillar guide pin bushings 12,23 in front and back, before and after two groups of dual power sensors 13,22, the electronic signal acquisition process shows that computer 17, base plate 21 and base 18 constitute, it is used to aim at production process metering, demonstration, printout production factors, bill.
The technological process of production of the method for a kind of biogas liquefied deep processing production alkane liquid gas fuel of the present invention is as follows:
(1) produces preparation: by the cosolvent can packing machine of specially joining on the production line, it is standby that a certain amount of cosolvent is injected equipment special " measurable biogas liquefied jar ", and the hydrotropy dosage of injection will flood the ad hoc micropore air jet pipe group 19 of equipment special at least and reach certain degree of depth;
(2) production line production starts: from the marsh gas fermentation pool output, by conflux a large amount of biogas bodies in input low pressure gas storehouse 1 of appendix, by special gas compressor assembly 2 powerful force feeds, end micropore air jet pipe group 19 devices that valve 24 is connected via returning with air inlet safety, from countless micropore ejections, pass through the cosolvent liquid layer, entering equipment special---measurable biogas liquefied gas tank 3 sprays moment at micropore mouth place, the big phenomenon of the prominent release of biogas delivery pressure energy appears with cosolvent liquid junctional area, promptly call the micropore Mohaupt effect, acceleration forces by brute force and presses next biogas, be subjected to the intimate contact of cosolvent similar dielectric object large tracts of land of the same clan, the intimate fusion, dissolving and high pressure, the acting in conjunction and the influence of chemistry such as micropore effect and physical energy, the biogas molecule obtains enough abnormal energy and the liquefaction conversion takes place.During production, can observe directly on the measurable biogas liquefied jar of display screen of equipment special, the pressure indication is being risen, and the indication that calculates the weight also value added variation is taking place slowly synchronously.When reaching certain high pressure, the compressor automatic system is controlled by setting program, and engine cuts off power supply automatically, stops to be pressed into biogas.For a moment, the indication of pressure on the display screen is falling after rise, and variation is not sent out in the weight indication any, shows that the biogas density in the jar is being shunk, and biogas is in the presentation that continues liquefaction.When pressure dropped to certain value, the compressor assembly 2 on the production line started power again automatically, and again with the biogas in the low pressure gas storehouse 1, the powerful said process that repeats is finished next production trifle and clapped cyclic process.Several production trifles are clapped cyclic program and are finished, and have obtained " is the alkane liquefaction mixed liquor of Main Ingredients and Appearance with biogas " of designed productive capacity in the measurable biogas liquefied jar, through fuel tank installation bottling, promptly get commodity " alkane liquefied fuel " product; Finish product canned after, the another production cyclic program of taking turns has begun.
Special suggestion: product (fuel) production process, raw materials for production, production auxiliary materials that the technology of the present invention is related, all are inflammable and explosive production projects, all participate in to be produced, management, cooperate buying, transportation, storage personnel outward, must carry out strict vocational training, take appointment with certificate; All produced on-site technical equipments, production environment, storage environment, means of transport all must meet the safety in production standard of national regulation fully; Sign is expressed in the safety precaution that must be provided with standard, guarantees long-term safety production and environmental protection.
Claims (1)
1, a kind of special-purpose measurable biogas liquefied jar of production method of biogas liquefied fuel, the technical process of the production method of described biogas liquefied fuel is as follows: biogas is delivered to the low pressure gas storehouse through appendix, powerful compression is sent into measurable biogas liquefied jar that cosolvent is housed in advance through the special gas compressor of control automatically, biogas by compression ends the micropore air jet pipe group device that valve is connected via returning with air inlet safety, from countless micropore ejections, pass through the cosolvent liquid layer, by the prominent big phenomenon-be the micropore Mohaupt effect of discharging of biogas delivery pressure energy occurring, obtain enough abnormal energy and the metamorphosis of liquefying changes into LMG with cosolvent liquid junctional area; Described cosolvent is the mixed liquor of a certain amount of combination partner of carbon five following liquid phase low molecular hydrocarbons classes, it is characterized in that: described special use mainly claims two big combined integratedization of parts to form by tank body and special electronic for measurable biogas liquefied jar, the tank body part main member has safety relief valve (8,25), tank shell (9), suspension ring (10,20), liquid in-out safety valve (11), Pressure gauge (14), air inlet safety is returned and is ended valve (24) and micropore air jet pipe group (19), described micropore air jet pipe group (19) is mounted in one group of high-voltage tube group of jar inner bottom part, be equipped with numerous micropore on the pipe perisporium, one termination blind plugging of pipe, other end parallel connection communicates and returns only with air inlet safety that valve (24) is connected, described special electronic claims parts mainly by supporting plate (16), the two groups of guide pillar guide pin bushings (12 in front and back, 23), the two groups of gravity sensors (13 in front and back, 22), the electronic signal acquisition process shows computer (17), base plate (21) and base (18) are formed, the two groups of guide pillars in front and back are weldingly fixed on the tank body, and corresponding guide pin bushing is weldingly fixed on the sole plate base.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200610115111A CN100580352C (en) | 2005-04-29 | 2005-04-29 | Method for producing fluidified fuel of marsh gas, and dedicated fluidified jar capable of measuring marsh gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200610115111A CN100580352C (en) | 2005-04-29 | 2005-04-29 | Method for producing fluidified fuel of marsh gas, and dedicated fluidified jar capable of measuring marsh gas |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2005100703440A Division CN100489082C (en) | 2005-04-29 | 2005-04-29 | Non-failure biogas fermentation tank |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101004318A CN101004318A (en) | 2007-07-25 |
| CN100580352C true CN100580352C (en) | 2010-01-13 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200610115111A Expired - Fee Related CN100580352C (en) | 2005-04-29 | 2005-04-29 | Method for producing fluidified fuel of marsh gas, and dedicated fluidified jar capable of measuring marsh gas |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100580352C (en) |
-
2005
- 2005-04-29 CN CN200610115111A patent/CN100580352C/en not_active Expired - Fee Related
Non-Patent Citations (2)
| Title |
|---|
| 沼气压缩贮存技术. 刘必琥.太阳能，第4期. 1985 |
| 沼气压缩贮存技术. 刘必琥.太阳能，第4期. 1985 * |
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| Publication number | Publication date |
|---|---|
| CN101004318A (en) | 2007-07-25 |
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Assignee: GUANGXI HONGHUA BIOLOGICAL INDUSTRIAL CO., LTD. Assignor: Guo Yiqiang Contract record no.: 2011450000018 Denomination of invention: Method for producing fluidified fuel of marsh gas, and dedicated fluidified jar capable of measuring marsh gas Granted publication date: 20100113 License type: Exclusive License Open date: 20070725 Record date: 20110530 |
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Owner name: GUANGXI HONGHUA BIOLOGICAL INDUSTRY CO., LTD. Free format text: FORMER OWNER: GUO YIQIANG Effective date: 20111220 |
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Free format text: CORRECT: ADDRESS; FROM: 545005 LIUZHOU, GUANGXI ZHUANG AUTONOMOUS REGION TO: 545007 LIUZHOU, GUANGXI ZHUANG AUTONOMOUS REGION |
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Effective date of registration: 20111220 Address after: 545007 No. 7 middle west road, Liuzhou, Guangxi Patentee after: GUANGXI HONGHUA BIOLOGICAL INDUSTRIAL CO., LTD. Address before: Take 545005 Liuzhou Road, the Guangxi Zhuang Autonomous Region No. 85-3 Patentee before: Guo Yiqiang |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100113 Termination date: 20160429 |