CN105257980B - A kind of technical method of low pressure gas storage methane or natural gas - Google Patents
A kind of technical method of low pressure gas storage methane or natural gas Download PDFInfo
- Publication number
- CN105257980B CN105257980B CN201510709502.6A CN201510709502A CN105257980B CN 105257980 B CN105257980 B CN 105257980B CN 201510709502 A CN201510709502 A CN 201510709502A CN 105257980 B CN105257980 B CN 105257980B
- Authority
- CN
- China
- Prior art keywords
- natural gas
- methane
- adsorbent
- activated carbon
- adsorption
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
The present invention provides a kind of new improved method, this method is based on active carbon adsorption memory technology, activated carbon adsorbent is improved by aperture adjustment technology, and combine the optimal design-aside that adsorption element is set, to reach the adsorption storage capability for improving methane or natural gas, the purpose of the heat endurance of storing process is improved.Its technical characteristics includes:(1) it is more sorbent used than same type technology that there is stronger absorption property using 1.1~1.5nm scope micropore distributed numbers in aperture adjustment technology increase activated carbon, so as to improve its adsorption capacity to methane or natural gas;(2) Soaking treatment is carried out to adsorbent, adsorbent surface is formed water membrane, further increase adsorbance of the adsorbent to methane or natural gas, while enhance the heat endurance of storage system;(3) adsorbent is filled in adsorption column, and set using boundling, reached the purpose of increase amount of storage.
Description
Technical field
The invention belongs to gas storing technology field, its technology contents is related to a kind of storage method of methane or natural gas, profit
The low pressure gas storage to light gas such as methane can be realized with this method.
Background technology
Natural gas or methane have many advantages as oil replacement fuel.First, natural gas resource rich reserves, China
It is accumulative at present to verify gas reserves up to 2.16 × 10,400,000,000 m 3, and the stock number available of surrounding countries' natural gas is also suitable
Greatly, calculated with existing depletion rate, World reserves of natural gas can also at least use 60 years, and petroleum resources are then about 30
Will be depleted after year;Secondly, pollution is light, and environment friendly is strong.Air pollution is increasingly tight as caused by vehicle fuel at present
Weight, and sulfur content is less in natural gas, easily removing, combustibility is strong, and combustion process is complete, granular material discharged few.From administer it is big,
Middle urban atmospheric pollution angle is seen, compared with fuel-engined vehicle, CO2 discharge capacity reduces 25%, CO in natural gas and auto tail gas
Discharge capacity reduce 89.7%, SO2 discharge capacity and reduce 70%, NO discharge capacitys and reduce 40%, hydrocarbons discharge capacity drop
It is low
70%, discharge quantity of particulate matter reduces 80%.It was predicted that 2010~2020 years natural gases are in China's energy knot
Ratio in structure is up to 35% ~ 40%, and natural gas will progressively turn into the preferred fuels for substituting oil in 21st century.However, natural gas
Or the storage and transport of methane are the key technical problems that it is solved as oil replacement fuel requirement.
At present, known methane or natural gas storage technology mainly have liquefaction technology (LNG), compress technique (CNG) and water
Conjunction technology (NGH).These technical methods both have it is respective the advantages of, but there is also it is respective the shortcomings that.For example, liquefied storage technology
Memory capacity it is maximum, storage directly as motor vehicle fuel than that up to more than 600 times, can supply, but the technology is in the presence of being liquefied as
This height, gas station technical difficulty is big, and investment is high, requires high to the heat-insulating property of storage bottle material, automobile needs to install additional using liquefied gas
A series of defects such as auxiliary equipment;Although the memory capacity for compressing storing technology is also larger, it is too high to there is pressure store
The problems such as (25Mpa), compression device investment is big, and the resistance to pressure request of holding bottle is high, and potential safety hazard is more;Although it is hydrated storing technology tool
Have, store the advantages that pressure is low, and storage condition is gentle, safe, but there is also induction period length is hydrated, decomposition of hydrate to be delayed
Slowly, the problems such as inconvenient for use.Therefore, in order to reduce methane or natural gas storage and use cost, solve existing memory technology and deposit
Storage pressure it is high, equipment investment is big, potential safety hazard is more, inconvenient for use the problems such as, it is necessary to develop a kind of new
Substitute technology method solves the storage problem of methane or natural gas.
Absorbing and storing technology is a kind of new gas memory technology method occurred in recent years.The technology refers in storage tank
Load the natural gas Special adsorbent of high-specific surface area, using its huge internal surface area and abundant microcellular structure in 4Mpa
The technical method for storing methane or Adsorption Natural Gas under~5Mpa mesolow.Because the technology has, pressure is low, aerating
The advantages that station equipment small investment, gas bomb are from heavy and light, material requirements is low, high safety, therefore received significant attention.However,
The problems such as existing absorbing and storing technology is relatively low there is also memory capacity, and stability is easily affected by temperature.To solve existing absorption
The problem of memory technology is present, the present invention provide a kind of new improved method, this method can greatly increase adsorbent to methane or
The adsorption capacity of natural gas, storage pressure is reduced, the heat endurance of storing process is improved, so that absorbing and storing technology can be more
It is applied to the storage of methane or natural gas well.
The content of the invention
In order to overcome, storage pressure existing for current methane or natural gas storage technology is high, equipment investment is big, material requirement
High, the defects of security is low, inconvenient for use, the present invention provides a kind of new memory technology method, and this method is deposited in novel adsorption
It is improved on the basis of storage technology, adsorption capacity of the adsorbent to methane or natural gas can be greatly increased, reduces storage pressure,
The heat endurance of storing process is improved, the storage of methane or natural gas can be preferably applied for.
The technical solution adopted for the present invention to solve the technical problems is:(1) novel adsorption memory technology is selected as storage first
The basic technology of alkane or natural gas;(2) 1.1~1.5nm in activated carbon adsorbent is improved using adsorbent aperture regulation technology
Micropore quantity, result of study show that the micropore quantity increase of this pore diameter range is highly beneficial to adsorbed methane, so as to improve
Adsorption capacity of the carbon adsorbent to methane or natural gas;(3) activated carbon adsorbent is soaked in water, the activity after water soaks
Carbon adsorbent will be greatly increased to the adsorbance of methane or natural gas, and after its reason is soaking, activated carbon hole surface can be formed
Water membrane, when methane contacts moisture film, hydrate is easily formed, so as to promote absorption of the adsorbent to methane and stably,
Simultaneously because activated carbon specific surface area is big, water film thickness is small, and the induction period of gas hydrate synthesis is short, and the self-shield effect of water is weak, passes
Matter resistance is low, and desorption rate is also than very fast.On the other hand, due to there is the presence of water, the increase of system thermal capacitance, it is not easy by environment temperature
The influence of change, stability are enhanced.
The technical characteristics that the present invention has are:(1)Compared with traditional methane or natural gas storage technology, the present invention carries
The memory technology method based on absorption supplied can store methane or natural gas under 4~5Mpa low pressure, well below compression
The storage pressure of 25Mpa needed for memory technology, and store ratio and can reach more than 180, reach the requirement of national regulation.(2)
1.1~1.5nm scope micropore distributed numbers in activated carbon are increased using aperture adjustment technology, so as to improve it to methane
Or the adsorption capacity of natural gas, it is more sorbent used than same type technology that there is stronger absorption property.(3)Water-filling is entered to adsorbent
Leaching is handled, and adsorbent surface is formed water membrane, is further increased adsorbance of the adsorbent to methane or natural gas, simultaneously
Enhance the heat endurance of storage system.
Embodiment
The 1st, activated carbon adsorbent is carried out to Fractional Heat-treatment regulation activated carbon pore-size distribution under the conditions of 600 DEG C and 800 DEG C,
Wherein, 600 DEG C are handled 1.5 hours, and 800 DEG C are handled 0.5 hour, its 1.1~1.5nm of the activated carbon after heat treatment obtained
The distributed quantity in aperture will add more than 20% than before processing, and the absorption affinity of methane or natural gas is enhanced.
2nd, the activated carbon adsorbent after via hole diameter is adjusted is soaked 24 hours in deionized water, logical in cool place after filtering
Dried in the air at wind to semi-wet state, its moisture is controlled 8~10%.
3rd, obtained activated carbon adsorbent is filled in circular metal adsorption column, and the gold for being filled with adsorbent by more
Belong in storage container of the adsorption column insertion with pipe support and be provided with filling interface and valve into collection pencil, memory upper end, methane or
When natural gas is filling, gas pours into through compressor under 4~5Mpa low pressure from interface.
Claims (1)
1. a kind of be used to increase methane or the technical method of Adsorption Natural Gas amount of storage, including following content:
(1) activated carbon adsorbent is carried out to Fractional Heat-treatment regulation activated carbon pore-size distribution under the conditions of 600 DEG C and 800 DEG C, its
In, 600 DEG C are handled 1.5 hours, and 800 DEG C are handled 0.5 hour, its 1.1~1.5nm aperture of the activated carbon after heat treatment obtained
Distributed quantity will add more than 20% than before processing, and the absorption affinity of methane or natural gas is enhanced;
(2) activated carbon adsorbent after via hole diameter is adjusted is soaked 24 hours in deionized water, after filtering at shady and cool ventilation
Dry in the air to semi-wet state, its moisture is controlled 8~10%;
(3) obtained activated carbon adsorbent is filled in circular metal adsorption column, and the metal for being filled with adsorbent by more
Be provided with filling interface and valve into collection pencil, storage container upper end in storage container of the adsorption column insertion with pipe support, methane or
When natural gas is filling, gas pours into through compressor under 4~5Mpa low pressure from interface.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510709502.6A CN105257980B (en) | 2015-10-28 | 2015-10-28 | A kind of technical method of low pressure gas storage methane or natural gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510709502.6A CN105257980B (en) | 2015-10-28 | 2015-10-28 | A kind of technical method of low pressure gas storage methane or natural gas |
Publications (2)
Publication Number | Publication Date |
---|---|
CN105257980A CN105257980A (en) | 2016-01-20 |
CN105257980B true CN105257980B (en) | 2018-04-03 |
Family
ID=55097805
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201510709502.6A Expired - Fee Related CN105257980B (en) | 2015-10-28 | 2015-10-28 | A kind of technical method of low pressure gas storage methane or natural gas |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN105257980B (en) |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5626637A (en) * | 1993-10-25 | 1997-05-06 | Westvaco Corporation | Low pressure methane storage with highly microporous carbons |
CN2265850Y (en) * | 1996-05-21 | 1997-10-29 | 成晓迪 | High wind rate waste gas handling adsorption tower |
CN1258638A (en) * | 1998-12-25 | 2000-07-05 | 中国科学院山西煤炭化学研究所 | Preparation of active carbon adsorbing and storing methane |
CN1342863A (en) * | 2001-09-26 | 2002-04-03 | 天津大学 | Water enhancing method for storing low-carbon hydrocarbon (natural gas or coal-seam gas) in activated carbon |
CN1952468A (en) * | 2006-11-16 | 2007-04-25 | 中山大学 | Hydration-adsorption combined natural gas storage method |
CN1959179A (en) * | 2006-09-30 | 2007-05-09 | 哈尔滨工业大学 | Method for forming hydrate of natural gas in active carbon |
CN102338278A (en) * | 2011-09-02 | 2012-02-01 | 中国石油大学(北京) | Method for increasing natural gas adsorption storage capability |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3021412B2 (en) * | 1997-02-17 | 2000-03-15 | 高千穂化学工業株式会社 | Gas storage / delivery method and gas storage / delivery device |
-
2015
- 2015-10-28 CN CN201510709502.6A patent/CN105257980B/en not_active Expired - Fee Related
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5626637A (en) * | 1993-10-25 | 1997-05-06 | Westvaco Corporation | Low pressure methane storage with highly microporous carbons |
CN2265850Y (en) * | 1996-05-21 | 1997-10-29 | 成晓迪 | High wind rate waste gas handling adsorption tower |
CN1258638A (en) * | 1998-12-25 | 2000-07-05 | 中国科学院山西煤炭化学研究所 | Preparation of active carbon adsorbing and storing methane |
CN1342863A (en) * | 2001-09-26 | 2002-04-03 | 天津大学 | Water enhancing method for storing low-carbon hydrocarbon (natural gas or coal-seam gas) in activated carbon |
CN1959179A (en) * | 2006-09-30 | 2007-05-09 | 哈尔滨工业大学 | Method for forming hydrate of natural gas in active carbon |
CN1952468A (en) * | 2006-11-16 | 2007-04-25 | 中山大学 | Hydration-adsorption combined natural gas storage method |
CN102338278A (en) * | 2011-09-02 | 2012-02-01 | 中国石油大学(北京) | Method for increasing natural gas adsorption storage capability |
Also Published As
Publication number | Publication date |
---|---|
CN105257980A (en) | 2016-01-20 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Li et al. | Pine cone shell-based activated carbon used for CO 2 adsorption | |
Zhang et al. | Grain-based activated carbons for natural gas storage | |
CN102302925B (en) | Natural gas adsorbent, absorption tank utilizing natural gas adsorbent for storing and transporting natural gas, and method for absorbing, storing and transporting natural gas | |
CN101614318A (en) | Heat accumulating type storage tank for absorbing natural gas | |
Zhang et al. | Multicomponent adsorptive separation of CO2, CH4, N2, and H2 over M-MOF-74 and AX-21@ M-MOF-74 composite adsorbents | |
CN102585953A (en) | Efficient variable-frequency and variable-pressure adsorptive separation and purification method for methane and carbon dioxide | |
CN102536519A (en) | Liquefied natural gas automobile fuel system with adsorption tank | |
CN101699126B (en) | Production method of steel cylinder for adsorbing natural gas at low and middle pressure and natural gas charging and using method | |
CN103712413B (en) | A kind of natural gas liquefaction device | |
CN105257980B (en) | A kind of technical method of low pressure gas storage methane or natural gas | |
US20150001101A1 (en) | Adsorbed natural gas storage | |
CN104548879B (en) | A kind of oil plant sour water tank method for treating release gas and device | |
WO2021067661A1 (en) | Mobile natural gas storage and transportation unit based on adsorption | |
Hamza et al. | Natural gas adsorption on biomass derived activated carbons: A mini review | |
CN106310697A (en) | Novel integrated oil and gas deep recovery and emission control device | |
CN104130814A (en) | High-yield recovery method of light hydrocarbon of high-pressure natural gas | |
CN103712414B (en) | A kind of natural gas liquefaction device and its liquefaction process | |
CN213668552U (en) | Compression condensation film adsorption combined type oil gas recovery device | |
CN204429057U (en) | A kind of device for recovering oil and gas | |
Mota | Adsorbed natural gas technology | |
CN201844195U (en) | Energy-saving, environmental-friendly and safe device for recovering and reusing methane for liquefied natural gas vehicles (LNGV) | |
CN100486686C (en) | High molecular derivatives composite material used for absorbing and storing methane, and its preparing method | |
CN109748242B (en) | Adsorbent for efficient purification of hydrogen | |
CN201192637Y (en) | Molecular sieves special for compression of natural gas | |
CN101255945B (en) | Method for storing methyl hydride using active carbon microsphere adsorption agent and for removing carbon dioxide |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180403 Termination date: 20191028 |
|
CF01 | Termination of patent right due to non-payment of annual fee |