CN1387001A - Solid-phase gas hydrate and its preparing process - Google Patents
Solid-phase gas hydrate and its preparing process Download PDFInfo
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- CN1387001A CN1387001A CN 01118175 CN01118175A CN1387001A CN 1387001 A CN1387001 A CN 1387001A CN 01118175 CN01118175 CN 01118175 CN 01118175 A CN01118175 A CN 01118175A CN 1387001 A CN1387001 A CN 1387001A
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- gas
- hydrate
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Abstract
A solid-phase gas hydrate is prepared through mixing porous medium with purified water, introducing the compressed gas into it for quickly generating hydrate in porous medium, and freezing at -10 deg.c. Said hydrate has relatively high stability in a certain condition.
Description
The present invention relates to a kind of solid-phase gas hydrate and preparation method thereof, it be a kind of in porous medium the form high density storage micro-molecular gas (N with hydrate
2, CO
2, CH
4, C
2H
6, C
3H
8Deng) method.
Hydrate is meant micro-molecular gas (N
2, CO
2, CH
4, C
2H
6, C
3H
8Deng) a kind of crystalline solid of under uniform temperature and pressure, generating with water.Generally between 0 ℃ and 15 ℃, difference is very big with the difference of the gas that generates hydrate to generate pressure for the generation temperature of hydrate.Gas hydrates are subjected to the attention of international energy circle day by day over surplus in the of nearly ten year, since 93 years, held three large-scale international conferences, gas hydrates have been discussed specially as potential new energy and the new technology development development prospect of (solid-state conveying, storage, environmental protection, mixture separate etc.).Developed countries such as English, U.S., day have dropped into lot of manpower and material resources and have carried out relevant basic and applied research.Domestic research to relevant gas hydrates does not at present also cause enough attention, and relevant gas hydrate basis and application study of (solid-state conveying, storage, environmental protection, mixture separation etc.) aspect new technology development carried out very few.
After hydrate was found, people just attempted coming natural gas-storing in the mode of hydrate always, because 1 cubic metre hydrate can be stored the rock gas of about 180 standard cubic meters.Gas hydrates are freezing under normal pressure can to have good thermostability during to-15 ℃.Come the accumulating gas cost than LNG Liquefied natural gas about low about 25% with Hydrate Technology.This technology has safely simultaneously, and environmentally safe advantage such as can use under any scale, so the gas hydrates technology has broad application prospects.But this technological development is also very immature.
The object of the present invention is to provide a kind of solid-phase gas hydrate that utilizes porous medium to form, it is the hydrate of the high gas storage energy storage density of a kind of tool, has very high thermostability, can realize storing under normal pressure and transportation.
The present invention also provides the making method of this solid-phase gas hydrate.
This solid-phase gas hydrate provided by the invention is meant the hydrate that gas generates in the porous medium carrier, it is at 0～-15 ℃, and under low pressure is stable.Wherein, described porous medium comprises natural materials such as silicious marl, asbestos, bentonite clay etc., artificial synthesis material such as active carbon, molecular sieve, silica gel, carclazyte, activated alumina, alumina silicate, pottery etc.
Described gas is rock gas, coal-seam gas or refinery's cracking gas.
The present invention also provides the preparation method of this solid-phase gas hydrate, it comprises in the mixed system of porous medium and pure water and feeds virgin gas, and regulate pressure to more than the balance pressure of this gas hydrate, make this gas in porous medium, generate hydrate, be refrigerated to-5～-15 ℃ process then.
The technology of the present invention is characterised in that: the characteristics of utilizing porous medium (for example active carbon) to provide sufficient gas-liquid to contact for gas and water generate the gas hydrate of high gas storage energy storage density fast.The porous medium and the pure water mixing of proper ratio are placed under the certain operation condition, feed and regulate and control generation pressure (being higher than balance pressure), make it in porous medium, generate hydrate fast, be refrigerated to 0～-15 ℃ then, preferably-10 ℃, promptly get required solid phase hydration thing.
When keeping suitable temperature conditions and storing mode, for example control temperature-15～0 and ℃ keep adiabatic down, and pilot pressure at normal pressure to 10MPa, then gained solid phase hydration thing has quite high stability, can store under normal pressure and transport.
Method of the present invention is based on characteristic and the porous medium that gas hydrate has higher gas storage and energy storage density and good mass transfer channel can be provided and self can adsorbs the advantage of a certain amount of gas as carrier, by utilizing the method that in porous medium, generates gas hydrate, improve formation speed, gas storage density and the thermostability of hydrate, and then realize storing and transporting such as rock gas, coal-seam gas or refinery's cracking gas.
Adopting method of the present invention to generate in the solid phase hydration thing process, require porous medium and pure water to form mixed system in the proper ratio, this ratio is relevant with hole structure, surface properties and the granularity of porous medium, the ratio of preferably adjusting pure water and porous medium reach or be not higher than this medium saturated extent of adsorption, for example when using 20-40 purpose ature of coal granular active carbon, the mass ratio of water and active carbon generally is controlled at about 1-1.8.For a person skilled in the art, the ratio of finding out different medium and water by test is easily.
Balance pressure when gas with various generates hydrate is different, usually requiring generation pressure to be higher than this balance pressure gets final product, in order to satisfy the requirement of production technology, the control that the invention provides generating pressure has proposed qualification, and this generation pressure is normally controlled by the control air inflow.
The optimized technical scheme according to the present invention, being controlled at the temperature that generates gas hydrate in the porous medium is 2-10 ℃, pressure is higher than balance pressure, generally at 0.1-20MPa.
The present invention compares with present like product, has following advantage: same LNG Liquefied natural gas, compressed natural gas and liquid fuel are compared, and energy consumption of the present invention is low, technology is simple, equipment investment is few, and product has antiknock preferably and shock proof ability simultaneously, and is safe; Compare with adsorption method, energy storage density of the present invention can significantly surpass the energy storage density of sorbent, and the composition to rock gas does not have specific (special) requirements simultaneously, has reduced the pretreated cost of rock gas; Generate hydrate with pure water and compare, the present invention need not to stir and formation speed fast, the hydrate thermostability height that is generated.Particularly the present invention has improved formation speed, gas storage density and the thermostability of gas hydrates, has simplified production technology, save operation cost and equipment investment simultaneously, with the tangible economic benefit of tool.
Below describe the realization and the characteristics of the present invention of the object of the invention in detail by specific embodiment, but practical range of the present invention is not constituted any qualification.
Embodiment 1: a certain amount of pure water is packed in the hydrator, control then that temperature feeds methane and makes the hydrator internal pressure reach required pressure in the hydrator between 2 ℃～8 ℃.Begin to stir, along with the generation of methane hydrate, the hydrator internal pressure begins to reduce, and after pressure stopped to descend, reaction was finished.Regulate the interior temperature of hydrator to about-10 ℃, promptly get required methane hydrate.
Gas-storing capacity representation unit volume hydrate (V in the following table
H) in standard state under the storage volume (Vm) of methane.
Operational condition: 2.6 ℃ of temperature
Initial pressure (MPa) water (g) gas-storing capacity (V
m/ V
H)
4.54??????????????????6.6???????????????????60
5.52??????????????????7.6???????????????????80
6.56??????????????????8.1???????????????????86
9.20??????????????????10.1??????????????????90
Embodiment 2: the mixture of getting 20-40 purpose active carbon and pure water is packed in the hydrator, and (mass ratio of pure water and active carbon is 1-1.8: 1), control then that temperature feeds methane and makes the hydrator internal pressure reach required pressure in the hydrator between 2 ℃～8 ℃.Keep static condition, along with the generation of methane hydrate, the hydrator internal pressure begins to reduce, and after pressure stopped to descend, reaction was finished.Regulate the interior temperature of hydrator to about-10 ℃, promptly get required methane hydrate.
(V in the gas-storing capacity representation unit volume system in the following table
H+C, active carbon adds hydrate) in standard state under the storage volume (V of methane
m).
Operational condition: 2.6 ℃ of temperature, initial pressure 9.3～9.2MPa
Water (g) active carbon (g) active carbon/water (g/g) gas-storing capacity (V
m/ V
H+C)
2.54????????2???????????????1.27????????????132
3.38????????2???????????????1.69????????????171
3.73????????1.63????????????2.29????????????170
4.70????????1.63????????????2.88????????????178
Embodiment 3: stability test
At the hydrate of embodiment 1 and 2, in locking system, carry out decomposition run, initial pressure is 0.1MPa, the results are shown in following table:
| Temperature (℃) | Methane/pure aquatic system | Methane/pure water+active carbon system | ||
| ????-5 ????-8 | Time (min) | Residual capacity (V%) | Time (min) | Residual capacity (V%) |
| ????10 ????20 | ????＜10 ????＜10 | ????300 ????600 | ????50 ????70 | |
Can find out that from last table result hydrate formation of the present invention is compared with the hydrate formation of pure water, stability obviously improves.
Claims (10)
1, a kind of solid-phase gas hydrate is the hydrate that gas generates in the porous medium carrier, and it is stable under low pressure at 0～-15 ℃.
2, the solid-phase gas hydrate of claim 1, wherein, this porous medium comprises silicious marl, asbestos, bentonite clay, active carbon, molecular sieve, silica gel, carclazyte, activated alumina, alumina silicate, pottery.
3, claim 1 or 2 described solid-phase gas hydrates, wherein, described gas is rock gas, coal-seam gas or refinery's cracking gas.
4, the making method of the described solid-phase gas hydrate of claim 1, it comprises in the mixed system of porous medium and pure water and feeds virgin gas, and regulate pressure to more than the balance pressure of this gas hydrate, and make this gas in porous medium, generate hydrate, be refrigerated to-5～-15 ℃ then.
5, the described making method of claim 4, wherein, this porous medium comprises the porous mass of natural porous mass and artificial synthesis.
6, the described making method of claim 5, wherein, this porous medium comprises silicious marl, asbestos, bentonite clay, active carbon, molecular sieve, silica gel, carclazyte, activated alumina, alumina silicate, pottery.
7, the described making method of claim 4, wherein, the temperature that generates gas hydrate in porous medium is 2-10 ℃, pressure is higher than balance pressure.
8, the described solid-phase gas hydrate of claim 1 is in the application that stores and transport in the gas.
9, the described application of claim 8, the condition of wherein said storage comprise that control temperature-15-0 ℃ keeps adiabatic, and pilot pressure at normal pressure to 10MPa.
10, claim 8 or 9 described application, wherein, described gas is rock gas, coal-seam gas or refinery's cracking gas.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01118175 CN1261715C (en) | 2001-05-18 | 2001-05-18 | Solid-phase gas hydrate and its preparing process |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01118175 CN1261715C (en) | 2001-05-18 | 2001-05-18 | Solid-phase gas hydrate and its preparing process |
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| Publication Number | Publication Date |
|---|---|
| CN1387001A true CN1387001A (en) | 2002-12-25 |
| CN1261715C CN1261715C (en) | 2006-06-28 |
Family
ID=4663016
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|---|---|---|---|
| CN 01118175 Expired - Fee Related CN1261715C (en) | 2001-05-18 | 2001-05-18 | Solid-phase gas hydrate and its preparing process |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100404946C (en) * | 2004-10-09 | 2008-07-23 | 石油大学(北京) | Dynamic control method for hydrate in oil-gas-water mixed system |
| CN100430459C (en) * | 2005-11-10 | 2008-11-05 | 中国石油大学(北京) | Method for storing and/or transporting fluid fuel |
| CN101376854A (en) * | 2008-09-09 | 2009-03-04 | 中国石油大学(北京) | Method and apparatus for simulating gas hydrate accumulation process under three-dimensional condition |
| CN101537321B (en) * | 2009-04-16 | 2011-06-01 | 中国石油大学(北京) | Vertical-type gas-liquid two-phase fluid mixing flow stabilizer |
| CN103861529A (en) * | 2014-04-09 | 2014-06-18 | 中能天地（北京）节能科技股份有限公司 | Combustible ice self-organizing production device |
| CN105757450A (en) * | 2016-05-10 | 2016-07-13 | 西南石油大学 | Adsorption-hydration coupled new gas storage and transportation method |
| CN106381125A (en) * | 2016-08-26 | 2017-02-08 | 华南理工大学 | Chinese herb extract and application thereof in preparing gas hydrate of high gas storage density |
-
2001
- 2001-05-18 CN CN 01118175 patent/CN1261715C/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100404946C (en) * | 2004-10-09 | 2008-07-23 | 石油大学(北京) | Dynamic control method for hydrate in oil-gas-water mixed system |
| CN100430459C (en) * | 2005-11-10 | 2008-11-05 | 中国石油大学(北京) | Method for storing and/or transporting fluid fuel |
| CN101376854A (en) * | 2008-09-09 | 2009-03-04 | 中国石油大学(北京) | Method and apparatus for simulating gas hydrate accumulation process under three-dimensional condition |
| CN101376854B (en) * | 2008-09-09 | 2013-06-05 | 中国石油大学(北京) | Method and apparatus for simulating gas hydrate accumulation process under three-dimensional condition |
| CN101537321B (en) * | 2009-04-16 | 2011-06-01 | 中国石油大学(北京) | Vertical-type gas-liquid two-phase fluid mixing flow stabilizer |
| CN103861529A (en) * | 2014-04-09 | 2014-06-18 | 中能天地（北京）节能科技股份有限公司 | Combustible ice self-organizing production device |
| CN103861529B (en) * | 2014-04-09 | 2016-04-06 | 中能天地（北京）节能科技股份有限公司 | A kind of combustible ice self-organizing process units |
| CN105757450A (en) * | 2016-05-10 | 2016-07-13 | 西南石油大学 | Adsorption-hydration coupled new gas storage and transportation method |
| CN106381125A (en) * | 2016-08-26 | 2017-02-08 | 华南理工大学 | Chinese herb extract and application thereof in preparing gas hydrate of high gas storage density |
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| Publication number | Publication date |
|---|---|
| CN1261715C (en) | 2006-06-28 |
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