Movatterモバイル変換


[0]ホーム

URL:


SE126674C1 - - Google Patents

Info

Publication number
SE126674C1
SE126674C1SE126674DASE126674C1SE 126674 C1SE126674 C1SE 126674C1SE 126674D ASE126674D ASE 126674DASE 126674 C1SE126674 C1SE 126674C1
Authority
SE
Sweden
Prior art keywords
rock
pyrolysis
heating
slate
zone
Prior art date
Application number
Other languages
Swedish (sv)
Publication date
Publication of SE126674C1publicationCriticalpatent/SE126674C1/sv

Links

Landscapes

Description

Translated fromSwedish

Uppfinnare: F. Ljungstrom. Inventor: F. Ljungstrom.

I patenten 121 737 och 123 136 har det 16- reslagits, att medelst i kanaler i ett skifferberg nedstuckna elektriska varmeelement, uppvarma detsamma, sâ att pyrolys framkallas. De darvid bildade oljegaserna avensom andra gaser uttagas genom sarskilda avloppskanaler i berget i och for uppsamling och nyttiggOrande genom kondensation och andra processer. Uppfinningen avser bl. a. att genornfOra denna uppvarmningsprocess, sa att den for densamma erforderliga energien erhalles till lagre kostnad an hittills och sa att alltsâ framstallningsmetoden fOr oljan nedbringas. Ett annat andamal ãr att a.stadkomma en uppvarmningsprocess, i vilket skifferberget tjanstg5r sa att saga som en ackumulator for billig ,elektrisk energi, soin alltst tillvaratages i form av varme och ,darmed kommer en vid senare tillfalle genomfortl pyrolys tillgodo. Ytterligare ett andamal är att astadkomma en forpreparering av skifferberget, sh att lackage av de yid pyrolysen utvunna produkterna verksamt f8rhindras.In patents 121,737 and 123,136 it has been proposed that by means of electric heating elements embedded in channels in a slate rock, it be heated so that pyrolysis is induced. The resulting oil gases, like other gases, are extracted through special drainage channels in the rock for collection and recovery through condensation and other processes. The invention relates, inter alia, to a. to carry out this heating process, so that the energy required for it is obtained at a lower cost than hitherto, and so that the production method for the oil is thus reduced. Another purpose is to bring about a heating process, in which the slate mountain serves as a sawmill as an accumulator for cheap, electrical energy, which is always utilized in the form of heat and, thus, in a later case, complete pyrolysis will benefit. Another aim is to achieve a pre-preparation of the slate rock, so that the lacquering of the products recovered from the pyrolysis is effectively prevented.

Dessa aven som andra andamal och i ovrigt uppfinningen kannetecknande egenskaper skola nannare beskrivas i det foljande, varvid a bilagda ritning schematiskt askadliggjorts ett utforingsexempel av uppfinningen. Harvid visa: Fig. 1 en vertikalsektion genom ett skifferberg och fig. 2 och 3 tvenne diagram. A ritningen betecknar 10 ett olj eforande skiff erlager, a vilket kan vara Overlagrat ett kalkbergsskikt 12 och eventuellt ett jordskikt 14. I vertikalt borrade kanaler aro nedstuckna ett start antal elektriska varmeelement 16, anordnade att avgiva sitt varme till skifferlagret 10. For en narmare beskrivning av dessa varmeelements avensom avloppskanalernas utformning och anbringande hanvisas till ovannamnda patent. Varmeelementen 16 sta medelst grenledningar 18 i forbindelse med ett elektriskt kraftledningssystem 20, varigenom lagspand strom inmatas i varmeelementen. &Isom avenledes framgar av dessa patent genomfores uppvarmningen av skifferberget ph sa salt, att en horisontellt vandrande varmefront skapas, vars riktning i fig. 1 betecknas med 22. I enlighet med uppfinningen delas uppvarmningen av skifferberget i Iva steg, en forvarmning och en efterfoljande uppvarmning till slut-hg temperatur, nedan benamnd pyrolysuppvarmningen. Vid uppvarmning av skiff ern intraffar en oljebildande pyrolys vid en temperatur, som overstiger 250° C, och Hirst i n.arheten av 300° b5rja oljegaserna och andra kolvategaser att i namnvard grad bildas. Mellan t. ex. 300° och 400° pa& den livligaste pyrolysen, d. v. s. mom detta omrade bildas i huvudsak all den olje- och gasmangd, som under den elektrotermiska olj eframstallningen frambringas. FOrvarmningen bedrives nu vid det Li ritningen askadliggjorda utforingsexemplet mom ett omrade av skifferberget begransat av de streckprickade linjerna 24, 26, varvid de mom detta omrade befintliga varmeelementen aro kopplade till kraftledningen 20. Temperaturen stiger darvid gradvis genom successiv inkoppling av nya rader av varmeelement 16, enligt kurvan 30 i fig. 2, vars abskissa angiver skifferfaltets enligt fig. 1 ytutstrackning i varmefrontens riktning, medan dess ordinata angiver temperaturen i skifferberget. Under forvarmningen upphettas skifferberget till en temperatur svarande mot linjen 32 i fig. 2, dar nagon vasentlig pyrolys dnnu ej uppkommit, t. ex. 240° a 280°. Pyrolysuppvarmningen bedrives mom ett parti av berget begransat av linjern.a 34, 36, vilket parti ãr skilt Iran forvarmningspartiet. Under pyrolysuppvarmningen stegras bergets temperatur stegvis enligt kurvan 38 till den slutliga temperaturemi enligt linjen 40, som kan uppga. till 360° a 420°. Efter en viss tids fOrlopp ken forvarmningen have natt fram till kurvan 30° och pyrolysuppvarmnin.gen till kurvan 38°. I skifferberget finnas alltsa tva skilda uppvarmningszoner, som. -vandra framat i samma riktning.These, like other objects and other features of the invention, may be described in more detail below, in which the accompanying drawing schematically illustrates an exemplary embodiment of the invention. In this case: Fig. 1 shows a vertical section through a slate mountain and Figs. 2 and 3 two diagrams. In the drawing, 10 denotes an oil-bearing slate bearing, which may be superimposed on a limestone rock layer 12 and possibly an earth layer 14. In vertically drilled channels a starting number of electric heating elements 16 are arranged, arranged to give off their heat to the slate layer 10. For a more detailed description of these heating elements as well as the design and application of the drainage channels are referred to the above-mentioned patent. The heating elements 16 are connected by means of branch lines 18 in connection with an electric power line system 20, whereby layered current is fed into the heating elements. As is clear from these patents, the heating of the slate rock ph so salt is carried out, that a horizontally traveling heating front is created, the direction of which in Fig. 1 is denoted by 22. In accordance with the invention, the heating of the slate rock is divided into Iva steps, a preheating and a subsequent heating to final-hg temperature, hereinafter referred to as the pyrolysis heating. When the shale is heated, an oil-forming pyrolysis occurs at a temperature exceeding 250 ° C, and near 300 ° Hirst the oil gases and other piston gases begin to form to a nominal degree. Between e.g. 300 ° and 400 ° pa & the liveliest pyrolysis, i.e. in this area, essentially all the amount of oil and gas formed during the electrothermal oil production is formed. The preheating is now carried out in the embodiment of the slate which is damaged in the drawing, in one area of the slate mountain bounded by the dashed lines 24, 26, the existing heating elements in this area being connected to the power line 20. The temperature rises gradually by successive connection of new rows of heating elements according to curve 30 in Fig. 2, the abscissa of which indicates the surface extent of the slate field according to Fig. 1 in the direction of the heat front, while its ordinate indicates the temperature in the slate rock. During the preheating, the slate rock is heated to a temperature corresponding to line 32 in Fig. 2, where no essential pyrolysis has yet arisen, e.g. 240 ° and 280 °. The pyrolysis heating is carried out with a portion of the rock bounded by lines 34, 36, which section is separate from the Iran preheating section. During the pyrolysis heating, the temperature of the rock rises stepwise according to curve 38 to the final temperature chemistry along line 40, which may indicate. to 360 ° and 420 °. After a certain period of time, the preheating has reached the 30 ° curve and the pyrolysis heating to the 38 ° curve. In the slate mountain there are thus two different heating zones, which. -wander forward in the same direction.

Under forvarmningen tillf5res vid ovansthende exempel omkring tvd tredjedelar av den erforderliga varmemangden till skiffer- 2— — berget och under pyrolysuppvarmningen endast omkring en tredjedel darav. Medan forvarmningen kan bedrivas periodiskt, sker pyrolysuppvarmningen mojligast kontinuerligt, vilket har en fordelaktig inverkan pa produktionen. Som exempel ma antagas det fallet, att forvarmningen endast ager rum under hal-va aret. Det ma antagas, att samma energimangd alltid tillfores, ett varmeelement per tidsenhet. Eftersom tva tredjedelar .av den totala varmemangden tillf0- res under forvarmningen, skall tydligen tinder denna fyra ganger sa manga varmeelement som under pyrolysuppvarmningen vara inkopplade, vilket innebar, att dubbla Tarmemangden 'Mores pa halva tiden. Vandringshastigheten hos den av linjerna 24, '26, begransade forvarmningsfronten blir samtidigt dubbelt sa stor som vandringshastigheten for pyrolysfronten mellan linjerna 34, 36. Det inses hara-v, att mellan de hada uppvarmningsfronterna kommer att forefinnas ett parti av skifferberget av varierande langd. Detta parti har nâtt temperaturnivan enligt linjen 32, d. v. s. bringats upp till den ternperatur, vid vilken pyrolysen kan paborj as. Da forvarmningen är avbruten minskas avstandet mellan linjerna 26 och 34; nar aterigen forvarmningen igangsattes Ras detta avstand.During the preheating, in the above example, about two thirds of the required amount of heat is supplied to the slate rock, and during the pyrolysis heating only about one third of it is supplied. While the preheating can be carried out periodically, the pyrolysis heating takes place as continuously as possible, which has a beneficial effect on production. An example is the case where the preheating only takes place during half the year. It must be assumed that the same amount of energy is always supplied, one heating element per unit of time. Since two thirds of the total heating amount is supplied during the preheating, it must apparently be four times as many heating elements as during the pyrolysis heating must be connected, which meant doubling the intestinal amount 'Mores in half the time. The migration speed of the preheating front delimited by lines 24, '26 will at the same time be twice as fast as the migration speed of the pyrolysis front between lines 34, 36. It will be appreciated that between the hot heating fronts there will be a portion of the slate rock of varying length. This portion has reached the temperature level along line 32, i.e. has been brought up to the temperature at which the pyrolysis can be started. When preheating is interrupted, the distance between lines 26 and 34 is reduced; when again the preheating was initiated Ras this distance.

Detta avbrott i varmetillforseln till ,skifferberget, sedan detsamma natt temperaturnivan 32, medfor ett flertal mycket betydelsefulla fOrdelar. Under det att varme tillfores ett varmeelement 16 far skifferberget omkring detsamma aka temperatur, i det att denna faller i riktning fran elemenet enligt kurvan 42 i fig. 3. I denna figur är den mot kurvan 42 svarande abskissan betecknad med 44. Sedan den elektriska energien frankopplats, utj amnas temperaturen enligt kurvan 46. Skiff erberget kommer alltsâ pa grund air intervallet Indian de bada uppvarmningsperioderna att uppvisa en mera fullbordad utjamning av temperaturen inom det uppvirmda bergpartiet. Ett .skifferberg har en yarmeutvidgningskoefficient air omkring 0,c000l. Pa de distanser om 2-3 in, som forekomma mellan de olika varmeelementen 16, bliva darvid med de ternperaturskillnader, som framga av kurvan 42 i fig, 3 (t. ex. 2000) de av uppvarmningen framkallade utvidgningarna av olika partier hiigst variabla mom skifferberget, varvid mycket ojamna varmespanningar framkallas inom desamma. I allmanhet forefinnes emellertid en tendens till varmeansvallning i horisontell riktning, framkallad av bergets generella uppvarmning. Denna varineansvallning tenderar till att sammanpressa alla vertikalsprickor, som finnas mom skifferberget, och verkar därfOr tatande pa dessa sprickor. Emellertid uppstd under forvarmningsperioden a ena sidan mom berget partiella zoner, som vilja sammantrycka de ovannamnda sprickorna och a andra sidan andra zoner dar en sadan sammantryckning forhindras. Vid utjamningen av temperaturen under intervallet mellan de bada uppvarmningsperiodema blir sammantryckningen air forekommande sprickor mera generell och darigenom mera effektiv. Genom avbrott i varmetillforseln motverkas salunda i mycket langtgaende grad, att de vid pyrolysuppvarmningen alstrade gaserna taga lake onskade vagar. Vidare medfor uppfinningen f8rdelar i det ekonomiska slutresultatet vid elektrotermisk utvinning a-v olj a. Forvarmningsperioden kan med fordel verkstallas under sadana ti-der, da billig vattenkraft i relativt overfl8d finnes tillganglig. Uppfinningen erbjuder darvid ett formanligt alternativ till de elektriska angpannor, dar som bekant elektrisk energi anvandes for angframstallning Pyrolysuppvarmningen verkstalles under relativt jamn tillforsel air elektrisk energi. Den harlot' erforderliga varmetillforseln kan lampligen ut0- b Ora en mindre del av hela den tillforda varmemangden enligt ovanstaende.This interruption in the supply of heat to, the slate mountain, since the same night the temperature level 32, entails a number of very significant advantages. While heat is supplied to a heating element 16, the slate rock rises around the same aka temperature, in that it falls in the direction of the element according to the curve 42 in Fig. 3. In this figure, the abscissa corresponding to the curve 42 is denoted by 44. Then the electrical energy disconnected, the temperature is equalized according to curve 46. The skiff rock will thus, due to the air interval Indian the two warming periods, show a more complete equalization of the temperature within the heated rock section. A slate mountain has a coefficient of thermal expansion air around 0, c000l. At the distances of 2-3 in, which occur between the different heating elements 16, the expansions of different parts caused by the heating of the most variable conditions are produced with the temperature differences, which appear from the curve 42 in Fig. 3 (eg 2000). the slate rock, whereby very uneven heat stresses are produced within them. In general, however, there is a tendency for heat to swell in the horizontal direction, caused by the general heating of the rock. This swelling of the veins tends to compress all the vertical cracks that are present in the slate rock, and therefore acts on these cracks. However, during the preheating period, partial zones arise on the one hand, which want to compress the above-mentioned cracks, and on the other hand, other zones where such compression is prevented. When the temperature is equalized during the interval between the two heating periods, the compression of the cracks occurring becomes more general and thereby more effective. By interrupting the heat supply, it is thus counteracted to a very far-reaching degree, that the gases generated during the pyrolysis heating take lake desired scales. Furthermore, the invention has advantages in the economic end result of electrothermal recovery of oil. The preheating period can advantageously be effected during such times, when cheap hydropower in relative abundance is available. The invention thereby offers a formable alternative to the electric steam boilers, where as is known electrical energy is used for steam production. The pyrolysis heating is carried out under a relatively even supply of electric energy. The required heat supply can suitably account for a small part of the entire supplied heat amount according to the above.

Vid elektrotermisk skifferolj eframstallning alstras dels oljebildande gaser, vilka genom kondensation tillvaratagas i flytande form, och dels Liven andra gasformiga kolvaten jamte vatgas, som endast med star svarighet under laga temperaturer kunna kondenseras och som darfor ham nedan kallas icke kondenserbara gaser. Dessa gaser utgora i allmanhet balm a mangden av samtliga utvunna kolvaten och hava ungefar samma effektiva forbranningsvarde, som de flytande kolvatena. For varje liter producerad olja erhalles salunda samtidigt omkring 1 in' gas. Denna gas dr ett utmarkt bransle och har, anvant pa ratt satt, ett stort kommersiellt varde, likvardigt med oljans, men densamma ãr med hansyn till distributionen och ftirsaljningsmojligheterna lake lika latthanterlig som oljan. Eli omfattande gasledningsnat och stora anlaggningskostnader komma saledes att folja en distribution av gasen, och skulle all gas distribueras fran ett stalle ddr t. ex. 200000 In' olja arligen framstalles, uppsta betydande svarigheter. I den man som i gasen befintliga bestandsdelar icke pa platsen kunna tillvaratagas (svavel m. m.) anvandes densamma i stallet lampligen sasom bransle i en kraftcentral som alstrar elektrisk energi, vii-ken enligt uppfinningen eventuellt alternativt med annan t. ex. Iran vattenkraft tillford energi appliceras f Or pyrolysuppvarnmingen av skifferberget. Uppvarmes nu skifferberget enligt uppfinningen pa ovan beskrivna satt, erhalles a ena sidan en periodisk forvarmning ay skifferberget, under det att a andra sidan en jamnt eller nara jamnt fortskridande pyrolysuppvarmning genom tillforande air elektrisk energi kan ordnas fran den gaseldade kraftcentralen. Pyrolysuppvarmningen kan alltsa genom lampligt avvagande av den — —3 temperatur, till vilken berget under fOruppvarmningen upphettas, bedrivas utan yttre energitillskott i form av vattenkraft. Pyrolysuppvarmningen fortgar darunder kontinuerligt oberoende av forvarmningen, som kan periodiskt ordnas, anpassad t. ex. efter tillgangen pa overflodeskraft fran vattenkrafteentralerna. Angcentralen far tydligen pa detta satt en kontinuerlig och darest sa onskas jamn belastning och vad som är av sarskild vikt, pyrolysen pagar i ett jamnt och ()start forlopp, oberoende av vattenkraftens konjunkturforhallanden. Emellertid kan pyrolysuppvarmningen bedrivas med olika intensitet under olika perioder resp. arstider, genom att olika antal -varmeelement aro samtidigt inkopplade i stromnatet. I land, t. ex. av Sveriges storlek och naturforhallanden mojliggar uppfinningen, alt under alla forhallanden overskottsenergi eller sa kallad sekundarkraft fran vattenkraftverken kan ekonomiskt formanligt finna anvandning for framstallning av flytande bransle. Skiff erberget utgor ddrvid genom farvarmningen en ackumulator, som i form ay varme tar vara pa vattenkraftsenergi, som sedan vid, om sa onskas, en langt senare tidpunkt kan utnyttjas for den slutliga. oljeutvinningen.In electrothermal shale oil production, oil-forming gases are generated, which are recovered in liquid form by condensation, and Liven other gaseous hydrocarbons as well as hydrogen gas, which can only be condensed at low temperatures under low temperatures and which is therefore called non-condensable gases below. These gases generally account for the amount of all recovered hydrocarbons and have approximately the same effective calorific value as the liquid hydrocarbons. For every liter of oil produced, about 1 in 'gas is thus obtained at the same time. This gas is an excellent industry and, used in the right way, has a large commercial value, equivalent to that of oil, but the same is true with regard to distribution and sales opportunities, as easy to handle as oil. Eli extensive gas pipeline night and large construction costs will thus follow a distribution of the gas, and would all gas be distributed from a stable ddr e.g. 200000 In 'oil annually produced, arise significant responsibilities. In the case where the constituents present in the gas cannot be recovered on site (sulfur, etc.), the same was used instead as a branch in a power plant which generates electrical energy, which according to the invention may alternatively with another e.g. Iran hydropower supply energy is applied f Or the pyrolysis warming of the slate rock. If the shale rock according to the invention is now heated in the manner described above, on the one hand a periodic preheating of the shale rock is obtained, while on the other hand an even or near evenly progressing pyrolysis heating by supplying electrical energy can be arranged from the gas-fired power plant. The pyrolysis heating can thus be carried out without suitable external energy in the form of hydropower by suitable balancing of the temperature at which the rock is heated during the preheating. The pyrolysis heating continues continuously independently of the preheating, which can be arranged periodically, adapted e.g. after the supply of abundant power from the hydropower plants. The steam center apparently has a continuous and, if desired, even load in this way, and what is of particular importance, the pyrolysis proceeds in a smooth and () start-up process, regardless of the economic conditions of hydropower. However, the pyrolysis heating can be carried out with different intensities during different periods resp. times, in that different numbers of heating elements are simultaneously connected in the current. On land, e.g. of Sweden's size and natural conditions, the invention is possible, or under all conditions surplus energy or so-called secondary power from hydropower plants can be used economically for the production of liquid fuel. The skiff erberg then forms an accumulator through the heating, which in the form of heat takes advantage of hydropower energy, which can then, if desired, be used for the final one at a much later time. oil recovery.

Enligt uppfinningen kan angkraftcentralen eldas antingen enbart med gas frail pyrolysprocessen eller kan densamma eldas med andra brdnslen, beroende pa konjunkturforhallandena vid vane .sarskilt tillfalle. Salunda kan gasen under vissa perioder Tara kilt att avyttra, som t. ex. under vin-tern for stadernas fOrseende med gag. Under sommaren, da dylik gaskonsumtion är mindre, kan angcentralen eldas enbart riled gasen .eller med lamMig kombination av gas °eh andra branslen. Enligt uppfinningen kan saledes aven den icke kondenserbara gasen nyttiggoras pa sarskilt gynnsaint satt, varvid kombinationen av d ena sidan .ett periodvis uppvarmt skifferberg, dar forvarmningen pagar, ackumulerar och utnyttjar tillganglig billig vattenfallsenergi, samtidigt som a andra sidan pyrolysuppvarnmingen kan verkstallas enbart med den genom pyrolysen framkommande icke kondenserbara gasen, varvid denna anvandning av gasen avenledes kan ske periodiskt i vaxelverkan med gasens anvandning far andra andamal. liven i dylikt fall an det tankbart att variera pyrolysuppvarmningens intensitet genom andring av antalet .strOmforande varmeelement 16 f8r att avpassa den per tidsenhet framstallda olje- resp. gasmangden och at*igen av elenergi efter prisforhallandena. En periodisk drift av foryarmningen kan i allmanhet tankas genomf8rd synkront med arstiderna. Pa sommaren finnes t. ex. i re-gel overskott av elektrisk energi tillganglig samtidigt som under denna arstid t. ex. gaskonsumtionen i staderna nedgar till mindre an halften mot under vintertiden. Genom den under sommaren uppackumulerade forvarmningsenergien kan darfOr enligt uppfinningen angkraftverken pa vintern bidraga till den elektriska energiforsorjningen genom eldning med andra branslen an gasen, samtidigt som den under samma tid tillverkade pyrolysgasen anvandes i stadernas gasdistribution och dar betingar ett hogre varde an i form av angpannebransle. Enligt uppfinningen majliggores en framstallning av t. ex. skifferraolja pa elektrotermisk vag ur de relativt oljefattiga svenska skiffrarna med sa god ekonom!, att denna olja kan i kostnadsayseende konkurrera med utifran importerade oljor.According to the invention, the steam power plant can be fired either only with gas from the pyrolysis process or it can be fired with other fuels, depending on the economic conditions in the usual case. Salunda can the gas during certain periods Tara kilt to sell, such as. during the winter for the provision of the cities with gag. During the summer, when such gas consumption is lower, the steam plant can be fired only on the riled gas .or with lamMig combination of gas ° eh other industries. According to the invention, the non-condensable gas can thus also be utilized in a particularly favorable manner, the combination of on the one hand being a periodically heated slate rock, where the preheating paves, accumulates and utilizes available cheap waterfall energy, while on the other hand the pyrolysis heating can be effected only by pyrolysis resulting in the non-condensable gas, whereby this use of the gas can, by contrast, take place periodically in interaction with the use of the gas for other purposes. In such a case, it is conceivable to vary the intensity of the pyrolysis heating by changing the number of flowing heating elements 16 in order to adapt the oil produced per unit time. the amount of gas and at * again of electricity according to the price conditions. A periodic operation of the forearm can generally be carried out synchronously with the seasons. In the summer there are e.g. as a rule surplus of electrical energy available at the same time as during this season e.g. gas consumption in the cities decreases to less than half compared to during the winter. Due to the pre-accumulated preheating energy during the summer, the steam power plants in the winter can therefore contribute to the electrical energy supply by firing with other industries than the gas, while the pyrolysis gas produced during the same time is used in urban gas distribution. According to the invention, a preparation of e.g. shale crude oil on electrothermal vapor from the relatively oil-poor Swedish shales with such good economics that this oil can compete in terms of cost with imported oils.

Den gaseldade kraftcentralen kan givetvis vara forsedd med angturbiner eller gasturbiner eller andra moderna varmekraftmotorer.The gas-fired power plant can of course be equipped with ang turbines or gas turbines or other modern thermal power engines.

Storleken has Sveriges skifferforekomster tillata att enligt uppfinningen mycket stora varmekraftcentraler (100 MW och mera) komma till anvandning. Enligt uppfinningen kun.na dessa krafteentraler samtidigt las disponibla sasom reserv fOr vattenkraften inorn landet saint for upptagandet av spetsbelastningar a statens kraftnat. Under spetsbelastningarna kan en krafteentral saledes alternativt anvandas, antingen for skiff eroljeframstallning eller som statens reservkraftverk under torra dr, da oljeframstallningen eventuellt kan avstallas.The size of Sweden's shale deposits allows, according to the invention, very large thermal power plants (100 MW and more) to be used. According to the invention, these power plants could at the same time be made available as a reserve for hydropower within the country for the absorption of peak loads by the state. During peak times, a power plant can thus alternatively be used, either for shale oil production or as the state's reserve power plant during dry dr, as the oil production can possibly be stored.

Claims (5)

Translated fromSwedish
Patentansprak:Patent claim:1. Satt att framstalla skifferolja genom elektrotermisk pyrolys dtrekt i ett skiff en-berg, kannetecknat darav, att tva uppvarmningszoner skapas i skifferberget, i en av vilka detta foruppyarmes, medan redan farvarmt skifferberg underkastas pyrolysuppvarmning i den andra zonen, och att till bada tillfores elvarme dock under skilda betingelser i avseende pa tiden pa sa salt, att melIan foruppyarnmingszonen och pyrolysuppvarmningszonen befinner sig ett foruppvarmt bergparti av i horisontell led varierande bredd.1. Set to produce shale oil by electrothermal pyrolysis in a slate-rock, characterized in that two heating zones are created in the shale rock, in one of which this is preheated, while already heated shale rock is subjected to pyrolysis heating in the other zone, and to both electric heating, however, under different conditions with respect to the time at such a salt, that between the preheating zone and the pyrolysis heating zone there is a preheated rock section of horizontally varying width.2. Satt enligt patentanspraket 1, kannetecknat darav, att en zon av skifferberget forst forvarmes medelst diskontinuerligt tillfort elvarme, under det att en annan zon av skifferberget, som yid en tidigare tidpunkt blivit forvarmd, uppyarmes till hogre temperatur, -vid vilken pyrolys ager ruin, av tillfort elvarme aven under perioder, da tillforseln av elvarme till den forstnamnda zonen av skifferberget är avbruten.2. Put according to claim 1, characterized in that a zone of the slate rock is first preheated by discontinuous supply of electric heat, while another zone of the slate rock, which has been preheated at a previous time, is heated to a higher temperature, at which pyrolysis is ruined. , of supplied electric heat even during periods, when the supply of electric heat to the first-mentioned zone of the slate rock is interrupted.3. Satt enligt patentanspraket 1 eller 2,, kannetecknat darav, att det for pyrolysuppvarmningen av skifferberget erforderliga elvarmet tages fran ett kraftverk, eldat atminstone delvis med pyrolysgaser, framkomna genom pyrolysprocessen i berget. — —3. A set according to claim 1 or 2, characterized in that the electric heat required for the pyrolysis heating of the shale rock is taken from a power plant, fired at least in part with pyrolysis gases, produced by the pyrolysis process in the rock. - -4. Satt enligt nagot av de foregaende patentanspraken, kanneteeknat darav, att skifferberget uppvarmes under forvarmningen over ett storre temperaturintervall an under pyrolysuppvarmningen.4. According to some of the preceding patent claims, it may be characterized in that the slate rock is heated during the preheating over a larger temperature range than during the pyrolysis heating.5. Solt enligt nagot av de foregaende patentanspraken, kanneteeknat darav, att Mrvarmningen bedrives under tillforsel av storre elmangder per tidsenhet an pyrolysuppvarmningen. Stockholm 1949. Kungl. Boktr. P. A. Norsteclt & Miner 1900395. Solt according to any of the preceding patent claims, may be characterized by the fact that the heating is carried out with a supply of larger amounts of electricity per unit of time than the pyrolysis heating. Stockholm 1949. Kungl. Boktr. P. A. Norsteclt & Miner 190039
SE126674DSE126674C1 (en)

Applications Claiming Priority (1)

Application NumberPriority DateFiling DateTitle
SE126674T

Publications (1)

Publication NumberPublication Date
SE126674C1true SE126674C1 (en)1949-01-01

Family

ID=41925090

Family Applications (1)

Application NumberTitlePriority DateFiling Date
SE126674DSE126674C1 (en)

Country Status (1)

CountryLink
SE (1)SE126674C1 (en)

Cited By (30)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US4886118A (en)1983-03-211989-12-12Shell Oil CompanyConductively heating a subterranean oil shale to create permeability and subsequently produce oil
US6581684B2 (en)2000-04-242003-06-24Shell Oil CompanyIn Situ thermal processing of a hydrocarbon containing formation to produce sulfur containing formation fluids
US6588504B2 (en)2000-04-242003-07-08Shell Oil CompanyIn situ thermal processing of a coal formation to produce nitrogen and/or sulfur containing formation fluids
US6698515B2 (en)2000-04-242004-03-02Shell Oil CompanyIn situ thermal processing of a coal formation using a relatively slow heating rate
US6715546B2 (en)2000-04-242004-04-06Shell Oil CompanyIn situ production of synthesis gas from a hydrocarbon containing formation through a heat source wellbore
US6715548B2 (en)2000-04-242004-04-06Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation to produce nitrogen containing formation fluids
US6782947B2 (en)2001-04-242004-08-31Shell Oil CompanyIn situ thermal processing of a relatively impermeable formation to increase permeability of the formation
US6877555B2 (en)2001-04-242005-04-12Shell Oil CompanyIn situ thermal processing of an oil shale formation while inhibiting coking
US6932155B2 (en)2001-10-242005-08-23Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation via backproducing through a heater well
US6948562B2 (en)2001-04-242005-09-27Shell Oil CompanyProduction of a blending agent using an in situ thermal process in a relatively permeable formation
US6969123B2 (en)2001-10-242005-11-29Shell Oil CompanyUpgrading and mining of coal
US7011154B2 (en)2000-04-242006-03-14Shell Oil CompanyIn situ recovery from a kerogen and liquid hydrocarbon containing formation
US7066254B2 (en)2001-04-242006-06-27Shell Oil CompanyIn situ thermal processing of a tar sands formation
US7073578B2 (en)2002-10-242006-07-11Shell Oil CompanyStaged and/or patterned heating during in situ thermal processing of a hydrocarbon containing formation
US7090013B2 (en)2001-10-242006-08-15Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation to produce heated fluids
US7096953B2 (en)2000-04-242006-08-29Shell Oil CompanyIn situ thermal processing of a coal formation using a movable heating element
US7104319B2 (en)2001-10-242006-09-12Shell Oil CompanyIn situ thermal processing of a heavy oil diatomite formation
US7121342B2 (en)2003-04-242006-10-17Shell Oil CompanyThermal processes for subsurface formations
US7165615B2 (en)2001-10-242007-01-23Shell Oil CompanyIn situ recovery from a hydrocarbon containing formation using conductor-in-conduit heat sources with an electrically conductive material in the overburden
US7320364B2 (en)2004-04-232008-01-22Shell Oil CompanyInhibiting reflux in a heated well of an in situ conversion system
US7435037B2 (en)2005-04-222008-10-14Shell Oil CompanyLow temperature barriers with heat interceptor wells for in situ processes
US7533719B2 (en)2006-04-212009-05-19Shell Oil CompanyWellhead with non-ferromagnetic materials
US7540324B2 (en)2006-10-202009-06-02Shell Oil CompanyHeating hydrocarbon containing formations in a checkerboard pattern staged process
US7549470B2 (en)2005-10-242009-06-23Shell Oil CompanySolution mining and heating by oxidation for treating hydrocarbon containing formations
US7798220B2 (en)2007-04-202010-09-21Shell Oil CompanyIn situ heat treatment of a tar sands formation after drive process treatment
US7831133B2 (en)2005-04-222010-11-09Shell Oil CompanyInsulated conductor temperature limited heater for subsurface heating coupled in a three-phase WYE configuration
US7866388B2 (en)2007-10-192011-01-11Shell Oil CompanyHigh temperature methods for forming oxidizer fuel
US8151907B2 (en)2008-04-182012-04-10Shell Oil CompanyDual motor systems and non-rotating sensors for use in developing wellbores in subsurface formations
US8220539B2 (en)2008-10-132012-07-17Shell Oil CompanyControlling hydrogen pressure in self-regulating nuclear reactors used to treat a subsurface formation
US8327932B2 (en)2009-04-102012-12-11Shell Oil CompanyRecovering energy from a subsurface formation

Cited By (257)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US4886118A (en)1983-03-211989-12-12Shell Oil CompanyConductively heating a subterranean oil shale to create permeability and subsequently produce oil
US6745837B2 (en)2000-04-242004-06-08Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation using a controlled heating rate
US6749021B2 (en)2000-04-242004-06-15Shell Oil CompanyIn situ thermal processing of a coal formation using a controlled heating rate
US6591906B2 (en)2000-04-242003-07-15Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation with a selected oxygen content
US6591907B2 (en)2000-04-242003-07-15Shell Oil CompanyIn situ thermal processing of a coal formation with a selected vitrinite reflectance
US6607033B2 (en)2000-04-242003-08-19Shell Oil CompanyIn Situ thermal processing of a coal formation to produce a condensate
US6609570B2 (en)2000-04-242003-08-26Shell Oil CompanyIn situ thermal processing of a coal formation and ammonia production
US6688387B1 (en)2000-04-242004-02-10Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation to produce a hydrocarbon condensate
US6698515B2 (en)2000-04-242004-03-02Shell Oil CompanyIn situ thermal processing of a coal formation using a relatively slow heating rate
US6702016B2 (en)2000-04-242004-03-09Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation with heat sources located at an edge of a formation layer
US6708758B2 (en)2000-04-242004-03-23Shell Oil CompanyIn situ thermal processing of a coal formation leaving one or more selected unprocessed areas
US6712135B2 (en)2000-04-242004-03-30Shell Oil CompanyIn situ thermal processing of a coal formation in reducing environment
US6712137B2 (en)2000-04-242004-03-30Shell Oil CompanyIn situ thermal processing of a coal formation to pyrolyze a selected percentage of hydrocarbon material
US6712136B2 (en)2000-04-242004-03-30Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation using a selected production well spacing
US6715546B2 (en)2000-04-242004-04-06Shell Oil CompanyIn situ production of synthesis gas from a hydrocarbon containing formation through a heat source wellbore
US6715547B2 (en)2000-04-242004-04-06Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation to form a substantially uniform, high permeability formation
US6715549B2 (en)2000-04-242004-04-06Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation with a selected atomic oxygen to carbon ratio
US6745832B2 (en)2000-04-242004-06-08Shell Oil CompanySitu thermal processing of a hydrocarbon containing formation to control product composition
US6719047B2 (en)2000-04-242004-04-13Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation in a hydrogen-rich environment
US6722429B2 (en)2000-04-242004-04-20Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation leaving one or more selected unprocessed areas
US6722431B2 (en)2000-04-242004-04-20Shell Oil CompanyIn situ thermal processing of hydrocarbons within a relatively permeable formation
US6722430B2 (en)2000-04-242004-04-20Shell Oil CompanyIn situ thermal processing of a coal formation with a selected oxygen content and/or selected O/C ratio
US6725921B2 (en)2000-04-242004-04-27Shell Oil CompanyIn situ thermal processing of a coal formation by controlling a pressure of the formation
US6725920B2 (en)2000-04-242004-04-27Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation to convert a selected amount of total organic carbon into hydrocarbon products
US6725928B2 (en)2000-04-242004-04-27Shell Oil CompanyIn situ thermal processing of a coal formation using a distributed combustor
US6745831B2 (en)2000-04-242004-06-08Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation by controlling a pressure of the formation
US6729396B2 (en)2000-04-242004-05-04Shell Oil CompanyIn situ thermal processing of a coal formation to produce hydrocarbons having a selected carbon number range
US6729395B2 (en)2000-04-242004-05-04Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation with a selected ratio of heat sources to production wells
US6729397B2 (en)2000-04-242004-05-04Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation with a selected vitrinite reflectance
US6732796B2 (en)2000-04-242004-05-11Shell Oil CompanyIn situ production of synthesis gas from a hydrocarbon containing formation, the synthesis gas having a selected H2 to CO ratio
US6732794B2 (en)2000-04-242004-05-11Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation to produce a mixture with a selected hydrogen content
US6732795B2 (en)2000-04-242004-05-11Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation to pyrolyze a selected percentage of hydrocarbon material
US6736215B2 (en)2000-04-242004-05-18Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation, in situ production of synthesis gas, and carbon dioxide sequestration
US6739393B2 (en)2000-04-242004-05-25Shell Oil CompanyIn situ thermal processing of a coal formation and tuning production
US6739394B2 (en)2000-04-242004-05-25Shell Oil CompanyProduction of synthesis gas from a hydrocarbon containing formation
US6742589B2 (en)2000-04-242004-06-01Shell Oil CompanyIn situ thermal processing of a coal formation using repeating triangular patterns of heat sources
US6742587B2 (en)2000-04-242004-06-01Shell Oil CompanyIn situ thermal processing of a coal formation to form a substantially uniform, relatively high permeable formation
US6742593B2 (en)2000-04-242004-06-01Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation using heat transfer from a heat transfer fluid to heat the formation
US6742588B2 (en)2000-04-242004-06-01Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation to produce formation fluids having a relatively low olefin content
US6715548B2 (en)2000-04-242004-04-06Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation to produce nitrogen containing formation fluids
US6588504B2 (en)2000-04-242003-07-08Shell Oil CompanyIn situ thermal processing of a coal formation to produce nitrogen and/or sulfur containing formation fluids
US6729401B2 (en)2000-04-242004-05-04Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation and ammonia production
US6991031B2 (en)2000-04-242006-01-31Shell Oil CompanyIn situ thermal processing of a coal formation to convert a selected total organic carbon content into hydrocarbon products
US6752210B2 (en)2000-04-242004-06-22Shell Oil CompanyIn situ thermal processing of a coal formation using heat sources positioned within open wellbores
US6758268B2 (en)2000-04-242004-07-06Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation using a relatively slow heating rate
US6761216B2 (en)2000-04-242004-07-13Shell Oil CompanyIn situ thermal processing of a coal formation to produce hydrocarbon fluids and synthesis gas
US6763886B2 (en)2000-04-242004-07-20Shell Oil CompanyIn situ thermal processing of a coal formation with carbon dioxide sequestration
US6769483B2 (en)2000-04-242004-08-03Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation using conductor in conduit heat sources
US6769485B2 (en)2000-04-242004-08-03Shell Oil CompanyIn situ production of synthesis gas from a coal formation through a heat source wellbore
US7798221B2 (en)2000-04-242010-09-21Shell Oil CompanyIn situ recovery from a hydrocarbon containing formation
US6789625B2 (en)2000-04-242004-09-14Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation using exposed metal heat sources
US6805195B2 (en)2000-04-242004-10-19Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation to produce hydrocarbon fluids and synthesis gas
US6820688B2 (en)2000-04-242004-11-23Shell Oil CompanyIn situ thermal processing of coal formation with a selected hydrogen content and/or selected H/C ratio
US6866097B2 (en)2000-04-242005-03-15Shell Oil CompanyIn situ thermal processing of a coal formation to increase a permeability/porosity of the formation
US6871707B2 (en)2000-04-242005-03-29Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation with carbon dioxide sequestration
US8225866B2 (en)2000-04-242012-07-24Shell Oil CompanyIn situ recovery from a hydrocarbon containing formation
US6877554B2 (en)2000-04-242005-04-12Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation using pressure and/or temperature control
US6880635B2 (en)2000-04-242005-04-19Shell Oil CompanyIn situ production of synthesis gas from a coal formation, the synthesis gas having a selected H2 to CO ratio
US8485252B2 (en)2000-04-242013-07-16Shell Oil CompanyIn situ recovery from a hydrocarbon containing formation
US6889769B2 (en)2000-04-242005-05-10Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation with a selected moisture content
US6896053B2 (en)2000-04-242005-05-24Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation using repeating triangular patterns of heat sources
US6902003B2 (en)2000-04-242005-06-07Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation having a selected total organic carbon content
US6902004B2 (en)2000-04-242005-06-07Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation using a movable heating element
US6910536B2 (en)2000-04-242005-06-28Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation using a natural distributed combustor
US6913078B2 (en)2000-04-242005-07-05Shell Oil CompanyIn Situ thermal processing of hydrocarbons within a relatively impermeable formation
US6581684B2 (en)2000-04-242003-06-24Shell Oil CompanyIn Situ thermal processing of a hydrocarbon containing formation to produce sulfur containing formation fluids
US7096953B2 (en)2000-04-242006-08-29Shell Oil CompanyIn situ thermal processing of a coal formation using a movable heating element
US7096941B2 (en)2000-04-242006-08-29Shell Oil CompanyIn situ thermal processing of a coal formation with heat sources located at an edge of a coal layer
US7086468B2 (en)2000-04-242006-08-08Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation using heat sources positioned within open wellbores
US7036583B2 (en)2000-04-242006-05-02Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation to increase a porosity of the formation
US7017661B2 (en)2000-04-242006-03-28Shell Oil CompanyProduction of synthesis gas from a coal formation
US7011154B2 (en)2000-04-242006-03-14Shell Oil CompanyIn situ recovery from a kerogen and liquid hydrocarbon containing formation
US6948563B2 (en)2000-04-242005-09-27Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation with a selected hydrogen content
US6997255B2 (en)2000-04-242006-02-14Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation in a reducing environment
US6953087B2 (en)2000-04-242005-10-11Shell Oil CompanyThermal processing of a hydrocarbon containing formation to increase a permeability of the formation
US6959761B2 (en)2000-04-242005-11-01Shell Oil CompanyIn situ thermal processing of a coal formation with a selected ratio of heat sources to production wells
US6994161B2 (en)2000-04-242006-02-07Kevin Albert MaherIn situ thermal processing of a coal formation with a selected moisture content
US6966372B2 (en)2000-04-242005-11-22Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation to produce oxygen containing formation fluids
US6994160B2 (en)2000-04-242006-02-07Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation to produce hydrocarbons having a selected carbon number range
US6994168B2 (en)2000-04-242006-02-07Scott Lee WellingtonIn situ thermal processing of a hydrocarbon containing formation with a selected hydrogen to carbon ratio
US6973967B2 (en)2000-04-242005-12-13Shell Oil CompanySitu thermal processing of a coal formation using pressure and/or temperature control
US6948562B2 (en)2001-04-242005-09-27Shell Oil CompanyProduction of a blending agent using an in situ thermal process in a relatively permeable formation
US6915850B2 (en)2001-04-242005-07-12Shell Oil CompanyIn situ thermal processing of an oil shale formation having permeable and impermeable sections
US6991032B2 (en)2001-04-242006-01-31Shell Oil CompanyIn situ thermal processing of an oil shale formation using a pattern of heat sources
US7735935B2 (en)2001-04-242010-06-15Shell Oil CompanyIn situ thermal processing of an oil shale formation containing carbonate minerals
US6991036B2 (en)2001-04-242006-01-31Shell Oil CompanyThermal processing of a relatively permeable formation
US6991033B2 (en)2001-04-242006-01-31Shell Oil CompanyIn situ thermal processing while controlling pressure in an oil shale formation
US6782947B2 (en)2001-04-242004-08-31Shell Oil CompanyIn situ thermal processing of a relatively impermeable formation to increase permeability of the formation
US6966374B2 (en)2001-04-242005-11-22Shell Oil CompanyIn situ thermal recovery from a relatively permeable formation using gas to increase mobility
US6964300B2 (en)2001-04-242005-11-15Shell Oil CompanyIn situ thermal recovery from a relatively permeable formation with backproduction through a heater wellbore
US6994169B2 (en)2001-04-242006-02-07Shell Oil CompanyIn situ thermal processing of an oil shale formation with a selected property
US6951247B2 (en)2001-04-242005-10-04Shell Oil CompanyIn situ thermal processing of an oil shale formation using horizontal heat sources
US6997518B2 (en)2001-04-242006-02-14Shell Oil CompanyIn situ thermal processing and solution mining of an oil shale formation
US7004247B2 (en)2001-04-242006-02-28Shell Oil CompanyConductor-in-conduit heat sources for in situ thermal processing of an oil shale formation
US7004251B2 (en)2001-04-242006-02-28Shell Oil CompanyIn situ thermal processing and remediation of an oil shale formation
US6877555B2 (en)2001-04-242005-04-12Shell Oil CompanyIn situ thermal processing of an oil shale formation while inhibiting coking
US7013972B2 (en)2001-04-242006-03-21Shell Oil CompanyIn situ thermal processing of an oil shale formation using a natural distributed combustor
US6880633B2 (en)2001-04-242005-04-19Shell Oil CompanyIn situ thermal processing of an oil shale formation to produce a desired product
US7032660B2 (en)2001-04-242006-04-25Shell Oil CompanyIn situ thermal processing and inhibiting migration of fluids into or out of an in situ oil shale formation
US6929067B2 (en)2001-04-242005-08-16Shell Oil CompanyHeat sources with conductive material for in situ thermal processing of an oil shale formation
US7040398B2 (en)2001-04-242006-05-09Shell Oil CompanyIn situ thermal processing of a relatively permeable formation in a reducing environment
US7040397B2 (en)2001-04-242006-05-09Shell Oil CompanyThermal processing of an oil shale formation to increase permeability of the formation
US7040399B2 (en)2001-04-242006-05-09Shell Oil CompanyIn situ thermal processing of an oil shale formation using a controlled heating rate
US7051807B2 (en)2001-04-242006-05-30Shell Oil CompanyIn situ thermal recovery from a relatively permeable formation with quality control
US8608249B2 (en)2001-04-242013-12-17Shell Oil CompanyIn situ thermal processing of an oil shale formation
US7051811B2 (en)2001-04-242006-05-30Shell Oil CompanyIn situ thermal processing through an open wellbore in an oil shale formation
US7055600B2 (en)2001-04-242006-06-06Shell Oil CompanyIn situ thermal recovery from a relatively permeable formation with controlled production rate
US6981548B2 (en)2001-04-242006-01-03Shell Oil CompanyIn situ thermal recovery from a relatively permeable formation
US7225866B2 (en)2001-04-242007-06-05Shell Oil CompanyIn situ thermal processing of an oil shale formation using a pattern of heat sources
US7066254B2 (en)2001-04-242006-06-27Shell Oil CompanyIn situ thermal processing of a tar sands formation
US6918443B2 (en)2001-04-242005-07-19Shell Oil CompanyIn situ thermal processing of an oil shale formation to produce hydrocarbons having a selected carbon number range
US7096942B1 (en)2001-04-242006-08-29Shell Oil CompanyIn situ thermal processing of a relatively permeable formation while controlling pressure
US6923257B2 (en)2001-04-242005-08-02Shell Oil CompanyIn situ thermal processing of an oil shale formation to produce a condensate
US6918442B2 (en)2001-04-242005-07-19Shell Oil CompanyIn situ thermal processing of an oil shale formation in a reducing environment
US6969123B2 (en)2001-10-242005-11-29Shell Oil CompanyUpgrading and mining of coal
US7128153B2 (en)2001-10-242006-10-31Shell Oil CompanyTreatment of a hydrocarbon containing formation after heating
US7077198B2 (en)2001-10-242006-07-18Shell Oil CompanyIn situ recovery from a hydrocarbon containing formation using barriers
US6991045B2 (en)2001-10-242006-01-31Shell Oil CompanyForming openings in a hydrocarbon containing formation using magnetic tracking
US7100994B2 (en)2001-10-242006-09-05Shell Oil CompanyProducing hydrocarbons and non-hydrocarbon containing materials when treating a hydrocarbon containing formation
US7104319B2 (en)2001-10-242006-09-12Shell Oil CompanyIn situ thermal processing of a heavy oil diatomite formation
US7114566B2 (en)2001-10-242006-10-03Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation using a natural distributed combustor
US7090013B2 (en)2001-10-242006-08-15Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation to produce heated fluids
US7086465B2 (en)2001-10-242006-08-08Shell Oil CompanyIn situ production of a blending agent from a hydrocarbon containing formation
US7156176B2 (en)2001-10-242007-01-02Shell Oil CompanyInstallation and use of removable heaters in a hydrocarbon containing formation
US6932155B2 (en)2001-10-242005-08-23Shell Oil CompanyIn situ thermal processing of a hydrocarbon containing formation via backproducing through a heater well
US7165615B2 (en)2001-10-242007-01-23Shell Oil CompanyIn situ recovery from a hydrocarbon containing formation using conductor-in-conduit heat sources with an electrically conductive material in the overburden
US7461691B2 (en)2001-10-242008-12-09Shell Oil CompanyIn situ recovery from a hydrocarbon containing formation
US7066257B2 (en)2001-10-242006-06-27Shell Oil CompanyIn situ recovery from lean and rich zones in a hydrocarbon containing formation
US7063145B2 (en)2001-10-242006-06-20Shell Oil CompanyMethods and systems for heating a hydrocarbon containing formation in situ with an opening contacting the earth's surface at two locations
US8627887B2 (en)2001-10-242014-01-14Shell Oil CompanyIn situ recovery from a hydrocarbon containing formation
US7051808B1 (en)2001-10-242006-05-30Shell Oil CompanySeismic monitoring of in situ conversion in a hydrocarbon containing formation
US7121341B2 (en)2002-10-242006-10-17Shell Oil CompanyConductor-in-conduit temperature limited heaters
US8238730B2 (en)2002-10-242012-08-07Shell Oil CompanyHigh voltage temperature limited heaters
US8224164B2 (en)2002-10-242012-07-17Shell Oil CompanyInsulated conductor temperature limited heaters
US7219734B2 (en)2002-10-242007-05-22Shell Oil CompanyInhibiting wellbore deformation during in situ thermal processing of a hydrocarbon containing formation
US8224163B2 (en)2002-10-242012-07-17Shell Oil CompanyVariable frequency temperature limited heaters
US7073578B2 (en)2002-10-242006-07-11Shell Oil CompanyStaged and/or patterned heating during in situ thermal processing of a hydrocarbon containing formation
US8579031B2 (en)2003-04-242013-11-12Shell Oil CompanyThermal processes for subsurface formations
US7360588B2 (en)2003-04-242008-04-22Shell Oil CompanyThermal processes for subsurface formations
US7640980B2 (en)2003-04-242010-01-05Shell Oil CompanyThermal processes for subsurface formations
US7942203B2 (en)2003-04-242011-05-17Shell Oil CompanyThermal processes for subsurface formations
US7121342B2 (en)2003-04-242006-10-17Shell Oil CompanyThermal processes for subsurface formations
US7320364B2 (en)2004-04-232008-01-22Shell Oil CompanyInhibiting reflux in a heated well of an in situ conversion system
US7490665B2 (en)2004-04-232009-02-17Shell Oil CompanyVariable frequency temperature limited heaters
US7353872B2 (en)2004-04-232008-04-08Shell Oil CompanyStart-up of temperature limited heaters using direct current (DC)
US8355623B2 (en)2004-04-232013-01-15Shell Oil CompanyTemperature limited heaters with high power factors
US7383877B2 (en)2004-04-232008-06-10Shell Oil CompanyTemperature limited heaters with thermally conductive fluid used to heat subsurface formations
US7510000B2 (en)2004-04-232009-03-31Shell Oil CompanyReducing viscosity of oil for production from a hydrocarbon containing formation
US7481274B2 (en)2004-04-232009-01-27Shell Oil CompanyTemperature limited heaters with relatively constant current
US7424915B2 (en)2004-04-232008-09-16Shell Oil CompanyVacuum pumping of conductor-in-conduit heaters
US7370704B2 (en)2004-04-232008-05-13Shell Oil CompanyTriaxial temperature limited heater
US7431076B2 (en)2004-04-232008-10-07Shell Oil CompanyTemperature limited heaters using modulated DC power
US7357180B2 (en)2004-04-232008-04-15Shell Oil CompanyInhibiting effects of sloughing in wellbores
US8233782B2 (en)2005-04-222012-07-31Shell Oil CompanyGrouped exposed metal heaters
US7575052B2 (en)2005-04-222009-08-18Shell Oil CompanyIn situ conversion process utilizing a closed loop heating system
US8070840B2 (en)2005-04-222011-12-06Shell Oil CompanyTreatment of gas from an in situ conversion process
US8230927B2 (en)2005-04-222012-07-31Shell Oil CompanyMethods and systems for producing fluid from an in situ conversion process
US7831134B2 (en)2005-04-222010-11-09Shell Oil CompanyGrouped exposed metal heaters
US7942197B2 (en)2005-04-222011-05-17Shell Oil CompanyMethods and systems for producing fluid from an in situ conversion process
US7860377B2 (en)2005-04-222010-12-28Shell Oil CompanySubsurface connection methods for subsurface heaters
US7575053B2 (en)2005-04-222009-08-18Shell Oil CompanyLow temperature monitoring system for subsurface barriers
US7500528B2 (en)2005-04-222009-03-10Shell Oil CompanyLow temperature barrier wellbores formed using water flushing
US7986869B2 (en)2005-04-222011-07-26Shell Oil CompanyVarying properties along lengths of temperature limited heaters
US8027571B2 (en)2005-04-222011-09-27Shell Oil CompanyIn situ conversion process systems utilizing wellbores in at least two regions of a formation
US8224165B2 (en)2005-04-222012-07-17Shell Oil CompanyTemperature limited heater utilizing non-ferromagnetic conductor
US7435037B2 (en)2005-04-222008-10-14Shell Oil CompanyLow temperature barriers with heat interceptor wells for in situ processes
US7527094B2 (en)2005-04-222009-05-05Shell Oil CompanyDouble barrier system for an in situ conversion process
US7831133B2 (en)2005-04-222010-11-09Shell Oil CompanyInsulated conductor temperature limited heater for subsurface heating coupled in a three-phase WYE configuration
US7546873B2 (en)2005-04-222009-06-16Shell Oil CompanyLow temperature barriers for use with in situ processes
US8606091B2 (en)2005-10-242013-12-10Shell Oil CompanySubsurface heaters with low sulfidation rates
US8151880B2 (en)2005-10-242012-04-10Shell Oil CompanyMethods of making transportation fuel
US7635025B2 (en)2005-10-242009-12-22Shell Oil CompanyCogeneration systems and processes for treating hydrocarbon containing formations
US7591310B2 (en)2005-10-242009-09-22Shell Oil CompanyMethods of hydrotreating a liquid stream to remove clogging compounds
US7584789B2 (en)2005-10-242009-09-08Shell Oil CompanyMethods of cracking a crude product to produce additional crude products
US7581589B2 (en)2005-10-242009-09-01Shell Oil CompanyMethods of producing alkylated hydrocarbons from an in situ heat treatment process liquid
US7562706B2 (en)2005-10-242009-07-21Shell Oil CompanySystems and methods for producing hydrocarbons from tar sands formations
US7559367B2 (en)2005-10-242009-07-14Shell Oil CompanyTemperature limited heater with a conduit substantially electrically isolated from the formation
US7559368B2 (en)2005-10-242009-07-14Shell Oil CompanySolution mining systems and methods for treating hydrocarbon containing formations
US7556095B2 (en)2005-10-242009-07-07Shell Oil CompanySolution mining dawsonite from hydrocarbon containing formations with a chelating agent
US7556096B2 (en)2005-10-242009-07-07Shell Oil CompanyVarying heating in dawsonite zones in hydrocarbon containing formations
US7549470B2 (en)2005-10-242009-06-23Shell Oil CompanySolution mining and heating by oxidation for treating hydrocarbon containing formations
US7673786B2 (en)2006-04-212010-03-09Shell Oil CompanyWelding shield for coupling heaters
US7793722B2 (en)2006-04-212010-09-14Shell Oil CompanyNon-ferromagnetic overburden casing
US8192682B2 (en)2006-04-212012-06-05Shell Oil CompanyHigh strength alloys
US7785427B2 (en)2006-04-212010-08-31Shell Oil CompanyHigh strength alloys
US7683296B2 (en)2006-04-212010-03-23Shell Oil CompanyAdjusting alloy compositions for selected properties in temperature limited heaters
US7533719B2 (en)2006-04-212009-05-19Shell Oil CompanyWellhead with non-ferromagnetic materials
US8083813B2 (en)2006-04-212011-12-27Shell Oil CompanyMethods of producing transportation fuel
US7912358B2 (en)2006-04-212011-03-22Shell Oil CompanyAlternate energy source usage for in situ heat treatment processes
US7635023B2 (en)2006-04-212009-12-22Shell Oil CompanyTime sequenced heating of multiple layers in a hydrocarbon containing formation
US7631689B2 (en)2006-04-212009-12-15Shell Oil CompanySulfur barrier for use with in situ processes for treating formations
US7610962B2 (en)2006-04-212009-11-03Shell Oil CompanySour gas injection for use with in situ heat treatment
US7604052B2 (en)2006-04-212009-10-20Shell Oil CompanyCompositions produced using an in situ heat treatment process
US7866385B2 (en)2006-04-212011-01-11Shell Oil CompanyPower systems utilizing the heat of produced formation fluid
US7597147B2 (en)2006-04-212009-10-06Shell Oil CompanyTemperature limited heaters using phase transformation of ferromagnetic material
US7677314B2 (en)2006-10-202010-03-16Shell Oil CompanyMethod of condensing vaporized water in situ to treat tar sands formations
US7677310B2 (en)2006-10-202010-03-16Shell Oil CompanyCreating and maintaining a gas cap in tar sands formations
US7673681B2 (en)2006-10-202010-03-09Shell Oil CompanyTreating tar sands formations with karsted zones
US7644765B2 (en)2006-10-202010-01-12Shell Oil CompanyHeating tar sands formations while controlling pressure
US8555971B2 (en)2006-10-202013-10-15Shell Oil CompanyTreating tar sands formations with dolomite
US7635024B2 (en)2006-10-202009-12-22Shell Oil CompanyHeating tar sands formations to visbreaking temperatures
US7845411B2 (en)2006-10-202010-12-07Shell Oil CompanyIn situ heat treatment process utilizing a closed loop heating system
US7631690B2 (en)2006-10-202009-12-15Shell Oil CompanyHeating hydrocarbon containing formations in a spiral startup staged sequence
US7841401B2 (en)2006-10-202010-11-30Shell Oil CompanyGas injection to inhibit migration during an in situ heat treatment process
US7681647B2 (en)2006-10-202010-03-23Shell Oil CompanyMethod of producing drive fluid in situ in tar sands formations
US7703513B2 (en)2006-10-202010-04-27Shell Oil CompanyWax barrier for use with in situ processes for treating formations
US7717171B2 (en)2006-10-202010-05-18Shell Oil CompanyMoving hydrocarbons through portions of tar sands formations with a fluid
US7730946B2 (en)2006-10-202010-06-08Shell Oil CompanyTreating tar sands formations with dolomite
US7730945B2 (en)2006-10-202010-06-08Shell Oil CompanyUsing geothermal energy to heat a portion of a formation for an in situ heat treatment process
US7730947B2 (en)2006-10-202010-06-08Shell Oil CompanyCreating fluid injectivity in tar sands formations
US7562707B2 (en)2006-10-202009-07-21Shell Oil CompanyHeating hydrocarbon containing formations in a line drive staged process
US8191630B2 (en)2006-10-202012-06-05Shell Oil CompanyCreating fluid injectivity in tar sands formations
US7540324B2 (en)2006-10-202009-06-02Shell Oil CompanyHeating hydrocarbon containing formations in a checkerboard pattern staged process
US8459359B2 (en)2007-04-202013-06-11Shell Oil CompanyTreating nahcolite containing formations and saline zones
US8662175B2 (en)2007-04-202014-03-04Shell Oil CompanyVarying properties of in situ heat treatment of a tar sands formation based on assessed viscosities
US8791396B2 (en)2007-04-202014-07-29Shell Oil CompanyFloating insulated conductors for heating subsurface formations
US7832484B2 (en)2007-04-202010-11-16Shell Oil CompanyMolten salt as a heat transfer fluid for heating a subsurface formation
US7798220B2 (en)2007-04-202010-09-21Shell Oil CompanyIn situ heat treatment of a tar sands formation after drive process treatment
US7931086B2 (en)2007-04-202011-04-26Shell Oil CompanyHeating systems for heating subsurface formations
US8381815B2 (en)2007-04-202013-02-26Shell Oil CompanyProduction from multiple zones of a tar sands formation
US8327681B2 (en)2007-04-202012-12-11Shell Oil CompanyWellbore manufacturing processes for in situ heat treatment processes
US7849922B2 (en)2007-04-202010-12-14Shell Oil CompanyIn situ recovery from residually heated sections in a hydrocarbon containing formation
US7950453B2 (en)2007-04-202011-05-31Shell Oil CompanyDownhole burner systems and methods for heating subsurface formations
US7841425B2 (en)2007-04-202010-11-30Shell Oil CompanyDrilling subsurface wellbores with cutting structures
US7841408B2 (en)2007-04-202010-11-30Shell Oil CompanyIn situ heat treatment from multiple layers of a tar sands formation
US8042610B2 (en)2007-04-202011-10-25Shell Oil CompanyParallel heater system for subsurface formations
US7866386B2 (en)2007-10-192011-01-11Shell Oil CompanyIn situ oxidation of subsurface formations
US8240774B2 (en)2007-10-192012-08-14Shell Oil CompanySolution mining and in situ treatment of nahcolite beds
US8011451B2 (en)2007-10-192011-09-06Shell Oil CompanyRanging methods for developing wellbores in subsurface formations
US8113272B2 (en)2007-10-192012-02-14Shell Oil CompanyThree-phase heaters with common overburden sections for heating subsurface formations
US8146661B2 (en)2007-10-192012-04-03Shell Oil CompanyCryogenic treatment of gas
US8536497B2 (en)2007-10-192013-09-17Shell Oil CompanyMethods for forming long subsurface heaters
US8272455B2 (en)2007-10-192012-09-25Shell Oil CompanyMethods for forming wellbores in heated formations
US8276661B2 (en)2007-10-192012-10-02Shell Oil CompanyHeating subsurface formations by oxidizing fuel on a fuel carrier
US7866388B2 (en)2007-10-192011-01-11Shell Oil CompanyHigh temperature methods for forming oxidizer fuel
US8146669B2 (en)2007-10-192012-04-03Shell Oil CompanyMulti-step heater deployment in a subsurface formation
US8162059B2 (en)2007-10-192012-04-24Shell Oil CompanyInduction heaters used to heat subsurface formations
US8196658B2 (en)2007-10-192012-06-12Shell Oil CompanyIrregular spacing of heat sources for treating hydrocarbon containing formations
US8151907B2 (en)2008-04-182012-04-10Shell Oil CompanyDual motor systems and non-rotating sensors for use in developing wellbores in subsurface formations
US8562078B2 (en)2008-04-182013-10-22Shell Oil CompanyHydrocarbon production from mines and tunnels used in treating subsurface hydrocarbon containing formations
US8162405B2 (en)2008-04-182012-04-24Shell Oil CompanyUsing tunnels for treating subsurface hydrocarbon containing formations
US8752904B2 (en)2008-04-182014-06-17Shell Oil CompanyHeated fluid flow in mines and tunnels used in heating subsurface hydrocarbon containing formations
US8172335B2 (en)2008-04-182012-05-08Shell Oil CompanyElectrical current flow between tunnels for use in heating subsurface hydrocarbon containing formations
US8636323B2 (en)2008-04-182014-01-28Shell Oil CompanyMines and tunnels for use in treating subsurface hydrocarbon containing formations
US8177305B2 (en)2008-04-182012-05-15Shell Oil CompanyHeater connections in mines and tunnels for use in treating subsurface hydrocarbon containing formations
US8281861B2 (en)2008-10-132012-10-09Shell Oil CompanyCirculated heated transfer fluid heating of subsurface hydrocarbon formations
US8267185B2 (en)2008-10-132012-09-18Shell Oil CompanyCirculated heated transfer fluid systems used to treat a subsurface formation
US8261832B2 (en)2008-10-132012-09-11Shell Oil CompanyHeating subsurface formations with fluids
US8256512B2 (en)2008-10-132012-09-04Shell Oil CompanyMovable heaters for treating subsurface hydrocarbon containing formations
US8220539B2 (en)2008-10-132012-07-17Shell Oil CompanyControlling hydrogen pressure in self-regulating nuclear reactors used to treat a subsurface formation
US8267170B2 (en)2008-10-132012-09-18Shell Oil CompanyOffset barrier wells in subsurface formations
US8353347B2 (en)2008-10-132013-01-15Shell Oil CompanyDeployment of insulated conductors for treating subsurface formations
US8881806B2 (en)2008-10-132014-11-11Shell Oil CompanySystems and methods for treating a subsurface formation with electrical conductors
US9022118B2 (en)2008-10-132015-05-05Shell Oil CompanyDouble insulated heaters for treating subsurface formations
US8327932B2 (en)2009-04-102012-12-11Shell Oil CompanyRecovering energy from a subsurface formation
US8448707B2 (en)2009-04-102013-05-28Shell Oil CompanyNon-conducting heater casings
US8434555B2 (en)2009-04-102013-05-07Shell Oil CompanyIrregular pattern treatment of a subsurface formation

Similar Documents

PublicationPublication DateTitle
SE126674C1 (en)
Kamate et al.Exergy analysis of cogeneration power plants in sugar industries
CA2574830C (en)Electric power plant with thermal storage medium
CN1575373B (en)Method for in situ thermal treatment of hydrocarbon containing formations by reverse production through heater wells
Birdsell et al.Minimum transmissivity and optimal well spacing and flow rate for high-temperature aquifer thermal energy storage
CN107525055A (en)For selectively being used to include the system and method for improving oil recovery process from solar thermal collector and heater production steam
JP6298072B2 (en) Centralized thermodynamic solar power plant or conventional thermal power plant
AU633246B2 (en)Power generation plant
CN102359365B (en)Oil extraction method for injecting high-temperature steam into oil layer to initiate hydrothermal exothermic reaction
Serpen et al.Turkey-A geothermal success story: A retrospective and prospective assessment
Parri et al.Larderello: 100 years of geothermal power plant evolution in Italy
CN207122890U (en)A kind of combustion engine waste heat boiler device with fused salt heat accumulation
CN114021324A (en)Method for determining later-period transfer flooding time of superheated steam SAGD (steam assisted gravity drainage) by using heat efficiency
Labib et al.Waste heat of a brick kiln–an opportunity of power generation
ZA202203785B (en)New combined thermodynamic cycle with high energy recovery
CN103644673A (en)Exploitation method for geothermal energy in salt mineral deposit
Reyna et al.Applications of small scale renewable energy
Biryuk et al.Unitized power and heat generating steam–gas plant
Buchta et al.Economical and ecological aspects of renewable energy generation in coal fired power plant supported with geothermal heat
US1759718A (en)Power installation
CN114001339B (en) A zero-carbon electric-driven heat pump steam production device and method
ENERGYCHAPTER FIVE AN ASSESSMENT OF RENEWABLE ENERGY GENERATION IN A CONVENTIONAL STEAM POWER PLANT JANUSZ BUCHTA1
SchumacherEnergy and Man—the Development of Demand
BuchtaAn assessment of renewable energy generation in a conventional steam power plant with geothermal feedwater preheating
Parri et al.Larderello, Italy: The Oldest Geothermal Field in Operation in the World

[8]ページ先頭

©2009-2025 Movatter.jp