EP2802385A2 - Verfahren zum löschen von bränden in kohlebergwerken und einheit zur durchführung dieses verfahrens - Google Patents

Verfahren zum löschen von bränden in kohlebergwerken und einheit zur durchführung dieses verfahrens

Info

Publication number
EP2802385A2
EP2802385A2 EP12704516.9A EP12704516A EP2802385A2 EP 2802385 A2 EP2802385 A2 EP 2802385A2 EP 12704516 A EP12704516 A EP 12704516A EP 2802385 A2 EP2802385 A2 EP 2802385A2
Authority
EP
European Patent Office
Prior art keywords
polymer
superabsorbent
partially
water
totally
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.)
Withdrawn
Application number
EP12704516.9A
Other languages
English (en)
French (fr)
Inventor
René Pich
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SPCM SA
Original Assignee
SPCM SA
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by SPCM SA filed Critical SPCM SA
Publication of EP2802385A2 publication Critical patent/EP2802385A2/de
Withdrawn legal-status Critical Current

Links

Classifications

    • A—HUMAN NECESSITIES
    • A62—LIFE-SAVING; FIRE-FIGHTING
    • A62D—CHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS
    • A62D1/00—Fire-extinguishing compositions; Use of chemical substances in extinguishing fires
    • A—HUMAN NECESSITIES
    • A62—LIFE-SAVING; FIRE-FIGHTING
    • A62C—FIRE-FIGHTING
    • A62C3/00—Fire prevention, containment or extinguishing specially adapted for particular objects or places
    • A—HUMAN NECESSITIES
    • A62—LIFE-SAVING; FIRE-FIGHTING
    • A62D—CHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS
    • A62D1/00—Fire-extinguishing compositions; Use of chemical substances in extinguishing fires
    • A62D1/0028—Liquid extinguishing substances
    • A62D1/005—Dispersions; Emulsions
    • E—FIXED CONSTRUCTIONS
    • E21—EARTH OR ROCK DRILLING; MINING
    • E21F—SAFETY DEVICES, TRANSPORT, FILLING-UP, RESCUE, VENTILATION, OR DRAINING IN OR OF MINES OR TUNNELS
    • E21F15/00—Methods or devices for placing filling-up materials in underground workings
    • E21F15/005—Methods or devices for placing filling-up materials in underground workings characterised by the kind or composition of the backfilling material

Definitions

  • Coal mines have always been a security problem. Some unexploited mines have burned for centuries. However, the number of fires has risen sharply since coal mining for steel or energy production.
  • coal fires are also common on the surface: heaps of fines or silos, especially in the presence of high sulfur coal.
  • the third country is India where fires began in the 18th century.
  • the Jharia mine is the world's largest mine fire where the fire began in 1916.
  • Water in the bottom of the mine can also vaporize and create explosions due to pressure.
  • the dense foam filled with inert gas has a relatively high flow slope and allows by injection, to plug horizontal galleries reducing horizontal transfers of oxygen. But the foam has no extinguishing effect because it does not contain enough water to cool the walls. The foam actually disappears at relatively low temperatures (50 to 80 ° C). In the case of sludge injection, for example bentonites, the sludge tends to flow like water and to separate at the bottom of the wells. In addition, their flow slope, very low, does not allow the closure of horizontal galleries.
  • the polymers have been used as binders and water maintainers for the production of gels or mineral pastes containing silica, kaolin, bentonite, fly ash, various sludge, ... which serve to seal the air in the burning coal mines.
  • the objective of the invention is therefore to develop a method of extinguishing coal mine fires combining the following characteristics:
  • Injection fluid flow slope to obstruct horizontal galleries
  • the Applicant has developed a method to solve all of these problems by using superabsorbent (SAP) or (co) polymers with a high rate of swelling in water.
  • SAP superabsorbent
  • these polymers are crosslinked.
  • the polymers according to the invention are injected in the form of partially or totally swollen superabsorbents, contrary to the prior art.
  • water-soluble, cross-linked, or cross-linked, natural or synthetic polymers polyvinyl alcohol, guar, alginates, carboxymethyl cellulose, dextran, xanthan, polyethylene oxide, etc.
  • Superabsorbents are polymers well known in specialty chemistry. They are usually in the form of powder. Their structure based on a three-dimensional network assimilable to a multitude of small cavities each having the ability to deform and absorb water gives them the property of absorbing very large quantities of water and thus inflating .
  • Such polymers are described, for example, in patent FR 2 559 158 in which crosslinked polymers of acrylic or methacrylic acid, crosslinked graft copolymers of polysaccharide type / acrylic or methacrylic acid, crosslinked terpolymers of the acrylic or methacrylic acid / acrylamide / sulfonated acrylamide type and their alkaline earth or alkaline metal salts.
  • these polymers have for their main characteristic a high capacity to swell in an aqueous medium. They can absorb and retain large amounts of water up to 100 times or more their mass. They are used especially in agriculture to retain water in the soil, in baby hygiene products intended to contain urine and similar applications.
  • the subject of the invention is therefore a method for extinguishing fires of coal mine wells consisting of:
  • the polymers are chosen from the group comprising:
  • crosslinked copolymers obtained by polymerization of acrylamide and partially or totally salified acrylic acid, preferably in the form of a sodium salt,
  • crosslinked polyacrylic acids partially or totally salified, preferably in the form of a sodium salt, which is more sensitive to the salinity of water and in particular to Ca 2+ and Mg 2+ .
  • the polymers are crosslinked copolymers of acrylamide and partially or totally salified acrylic acid and contain between 40 and 90 mol% of acrylamide and between 10 and 60 mol% of acrylic acid partially or totally salified.
  • the SAP is a crosslinked terpolymer obtained by polymerization of acrylamide and / or partially or totally salified acrylic acid and / or partially or completely salified ATBS (acrylamido tert-butylsufonate) and / or NVP. (N vinylpyrrolidone).
  • SAP is partially or fully inflated.
  • a fully inflated SAP is characterized by the fact that all the small cavities of the three-dimensional network are filled with saturation water, ie at a level such that by adding additional water, the SAP no longer absorbs water additional.
  • the polymers are crosslinked with 100 to 6000 ppm of at least one crosslinking agent chosen from the group comprising acrylic compounds, for example methylenebisacrylamide, allylic compounds such as, for example, tertraalylammonium chloride, vinylic compounds, for example divinylbenzene, diepoxy, metal salts ...
  • a crosslinking agent chosen from the group comprising acrylic compounds, for example methylenebisacrylamide, allylic compounds such as, for example, tertraalylammonium chloride, vinylic compounds, for example divinylbenzene, diepoxy, metal salts ...
  • Polyacrylamides have the ability to produce swollen SAPs that are stiffer and less sensitive to divalent metals than polyacrylates.
  • the water used to swell the polymer is the least saline possible, and this, to obtain the maximum swelling of the SAP for a given amount.
  • the water preferably contains less than 200 g / l, very preferably less than 100 g / l of salts, for example NaCl, CaCl 2 or MgCl 2. For this purpose, it can be treated by reverse osmosis.
  • SAPs When SAPs are inflated, the SAP flow slope varies depending on the initial particle size of the SAP. With a particle size less than 1 mm (less than about 5 mm inflated), the flow slope is of the order of 10 °. With a particle size less than 4 mm (less than 1.5 cm inflated), the slope can reach 15-20 °. It is therefore possible to plug galleries simply by injection.
  • the stored water evaporates and the polymer is burned. But for 1 gr of polymer, 100 g of water were evaporated, ie an energy absorption of 226 KJ to which it is necessary to add the temperature rise heat of the water vapor generated at 400-600 ° C. For example, with a flow rate of 1000 1 / minute, 4000 MJ / min can be eliminated compared to the heat of combustion of 1 liter of gas oil of 36 MJ.
  • the inflated superabsorbent therefore has both a mechanical effect like a rigid foam, and a thermal effect such as water which has a formation of water vapor of 1.7 m 3 per liter of evaporated water, and whose vapor does not dissociate in oxygen and dihydrogen, explosively, not before 1600 ° C. In addition, it can deform according to the movements of ground maintaining their shutter function.
  • the inflated SAP is prepared in a fire-free zone thus avoiding any dangerous handling near the flames.
  • the inflated SAP is then transported and then injected by pressure or pipeline truck.
  • the partially or fully inflated SAP can be formed continuously or batchwise.
  • SAP is injected at the wellhead, horizontal or vertical vertical or surface cracks.
  • the invention also relates to an installation implementing the method described above and comprising:
  • the means for mixing the water and the superabsorbent (co) polymer is in the form of two successive tanks allowing continuous and homogeneous swelling of the superabsorbent.
  • Figure 1 is a representation of an installation implementing the method of the invention according to a first embodiment.
  • FIG. 2 is a representation of an installation implementing the method of the invention according to a second embodiment.
  • the superabsorbent is delivered in big bags of 750 to 1000 kg, in containers of 2 to 5 tons (1) (see figure 1) or in tanker truck (1) (see figure 2) then stored in a hopper or a silo ( 2). It is dosed by a screw feeder (3) in a continuous system with 2 tanks (4, 5) equipped with a powerful agitator (6, 7) propeller or spiral.
  • the superabsorbent (1) and the water (8) are dosed in the first swelling chamber (4), the water being in excess of the swelling of the (co) polymer (eg 1200 liters per hour for 10 kg swelling 100 times), which allows more efficient agitation.
  • the required residence time depends on the particle size and is between 1 hour (less than 1 mm) and 3 hours (less than 4 mm).
  • the second tank (5) works with a high level low level stopping the screw feeder (3) and the water inlet (8) high point.
  • the inflated SAP is pumped either by means of a Moineau type pump (9) up to pressures of about 10 bar and by means of a piston pump up to 200 bar.
  • the inflated SAP is then injected by means of an injection nozzle (10) at the wellhead or in horizontal or vertical vertical or surface fissures.

Landscapes

  • Emergency Management (AREA)
  • Business, Economics & Management (AREA)
  • Chemical & Material Sciences (AREA)
  • Mining & Mineral Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Dispersion Chemistry (AREA)
  • Geology (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Public Health (AREA)
  • Fire-Extinguishing Compositions (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Fireproofing Substances (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
EP12704516.9A 2012-01-09 2012-01-09 Verfahren zum löschen von bränden in kohlebergwerken und einheit zur durchführung dieses verfahrens Withdrawn EP2802385A2 (de)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/FR2012/050050 WO2012063009A2 (fr) 2012-01-09 2012-01-09 Procede d'extinction de feux de mines de charbon et installation pour la mise en oeuvre du procede

Publications (1)

Publication Number Publication Date
EP2802385A2 true EP2802385A2 (de) 2014-11-19

Family

ID=45688171

Family Applications (1)

Application Number Title Priority Date Filing Date
EP12704516.9A Withdrawn EP2802385A2 (de) 2012-01-09 2012-01-09 Verfahren zum löschen von bränden in kohlebergwerken und einheit zur durchführung dieses verfahrens

Country Status (6)

Country Link
EP (1) EP2802385A2 (de)
CN (1) CN104428038A (de)
AU (1) AU2012202891A1 (de)
CA (1) CA2858655A1 (de)
RU (1) RU2014125244A (de)
WO (1) WO2012063009A2 (de)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2763214C1 (ru) * 2021-01-11 2021-12-28 Федеральное государственное автономное образовательное учреждение высшего образования "Сибирский федеральный университет" Способ тушения скважинных возгораний порошковым огнетушащим веществом

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104989444A (zh) * 2015-06-05 2015-10-21 安徽理工大学 一种防治煤炭自燃的胶体泡沫材料及制备方法
CN106237563B (zh) * 2016-08-16 2021-08-31 华电电力科学研究院有限公司 一种基于煤质的智能阻燃剂喷淋系统及方法
CN108498998B (zh) * 2018-03-30 2021-07-20 中煤科工集团重庆研究院有限公司 煤矿用复合灭火材料及其制备方法
CN110496343B (zh) * 2018-05-18 2021-02-23 山东昊月新材料股份有限公司 一种多用途灭火器
CN114200043B (zh) * 2021-12-01 2023-09-05 中煤科工集团沈阳研究院有限公司 一种煤自然发火标志气体检测系统、方法及其储气装置

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JPS60163956A (ja) 1984-02-04 1985-08-26 Arakawa Chem Ind Co Ltd 吸水性樹脂の製法
CN2721877Y (zh) * 2004-06-29 2005-08-31 杨海 矿用移动式固化泡沫充填装置
US8096622B2 (en) * 2007-09-25 2012-01-17 Micon Method of controlling mine fires with polymeric gel
CN101392657A (zh) * 2008-10-22 2009-03-25 河北金牛能源股份有限公司葛泉矿 一种防治煤炭自燃的制浆系统

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO2012063009A2 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2763214C1 (ru) * 2021-01-11 2021-12-28 Федеральное государственное автономное образовательное учреждение высшего образования "Сибирский федеральный университет" Способ тушения скважинных возгораний порошковым огнетушащим веществом

Also Published As

Publication number Publication date
WO2012063009A2 (fr) 2012-05-18
WO2012063009A3 (fr) 2013-10-24
CA2858655A1 (en) 2012-05-18
AU2012202891A1 (en) 2014-07-10
RU2014125244A (ru) 2016-01-20
CN104428038A (zh) 2015-03-18

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