|Publication number||US2388009 A|
|Publication date||Oct 30, 1945|
|Filing date||Oct 19, 1943|
|Priority date||Oct 19, 1943|
|Publication number||US 2388009 A, US 2388009A, US-A-2388009, US2388009 A, US2388009A|
|Inventors||Pike Robert D|
|Original Assignee||Pike Robert D|
|Export Citation||BiBTeX, EndNote, RefMan|
|Referenced by (41), Classifications (12)|
|External Links: USPTO, USPTO Assignment, Espacenet|
OCt. 30, 1945. R D PIKE SOLUTION MINING OF TRON?.
Filed OC'L. 19, 1943 2V Sheets-Sheet 1 Naz co5- am: P5@ /oo ams. H20
INVENTOR. A905527' D. PIKE.
BY fad-ovh, VU@
Oct. 30, 1945. R D PlKE SOLUTION MINING OF TRONA Filed Oct. 19, 1943 2 Sheets-Sheet 2 UWT @Q05 INVENTOR. @05597 D. 10J/(Lf: BY @am Patented Oct. 30, 1945 l UNITED STATES PATENT OFFICE SOLUTION MINING OF TRDNA- nobm D. Pike, Pittsburgh, rs. Application October 19, 1943, Serial No. 506,841
Claims. '(lCl. 23-38) 'I'his invention relates to the mining of trona,
especially by solution methods, and a maior object of the invention is to provide a method of recovering trona from underground solid deposits which ls simple, easily performed and efdcient, and which results in a trona that is easily and cheaply converted into soda ash of acceptable commercial purity.
The invention will be described with reference to the accompanvng drawings in which the graphs of Fig. 1 represent solubility relationships which are applied in the practice of the invention, and Fig. 2 is a flow sheet illustrating the preferred practice of the invention.
There has been discovered by core drilling in the Green River formation near Green River, Wyoming, a vast deposit of the mineral trona which in its pure state has the empirical formula NazCO:.NaHCO3.2HzO. The soluble portion of this deposit, which averages `at least about 95 per cent ofthe formation, is almost pure trona. although typical analyses indicate that its content of the normal carbonate is slightly greater than corresponds to the empirical formula. Chlo-- rides and sulfates occur only in traces, and the iron content is extremely low but is present, at least to a considerable extent, in the remains of organisms such as Artemia salina. The purity of this trona deposit would thus render it an ideal source of soda ash but the bed, which averages about 12 feet in thickness, occurs at a depth of about 1500 feet and is overlaid by well compacted sedimentary deposits. Mining of that formation by usual methods would, therefore, involve the sinking of deep shafts with the expense attendant upon it and upon manual mining methods.
In accordance with' the the present invention a well is driven into the trona formation for the purpose of passing into it a brine of such composi- V tion and at such a temperature as to be capable of dissolving the trona in the bed. 'I'he resultant without metathetical or other alteration of the trona constituents. Most suitably the brine contains sodium carbonate and bicarbonate, and preferably it contains substantially more of the normal carbonate than o! the bicarbonate.
The solubility relationships that are made use ofv in practicing this invention with such a brine are as explained in my copending application Serial No. 385,092-, illed March 25, 1941, now Patent No. 2,346,140, granted April 11, 1944, of which the present application is a continuation-impart. Fig. 1 is a duplicate of Fig. 1 of that application. In that drawing the lower graph represents the composition of brines of sodium carbonate and bicarbonate at about 30 C., and the upper graph represents the relationships at about 100 C., and both graphs show compositions which are saturated with reference to sodium sesquicarbonate (trona). A brine saturated with sequicarbonate as shown by the lower graph is brought into contact with a body of `natural trona which is to be recovered from the formation. By increasing the temperature the brine will dissolve the soluble matter from the trona, and upon cooling the resultant solution trona, or sodium sesquicarbonate, will be crystallized from it. Thus, a brine corresponding to the point A of the lower graph will contain, per hundred grams of water, approximately 5.4 grams of sodium bicarbonate and 23.4 grams of sodium carbonate. Upon heating this brine above 30 C. and contacting it with trona the composition of the solution will change alongthe line AB, and upon cooling the resultant solution to 30 C. sodium sesquicarbonate will be crystallized out with progressive impoverishment of the solution with respect to sodium carbonate and bicarbonate. This action occurs along line A-B until the point A is reached, when the brine is reheated and used for further treatment of the4 trona bed. a
The process may beV described in greater detail with reference to Fig. 2, which is illustrative of its preferred embodiment. As shown there, the trona formation I is penetrated by a well which comprises an outer casing 2` that reaches at least to the upper level of the bed, and a tube 3 which is disposed concentrically within the casing 2 and which extends substantially to the bottom of the deposit. The portion of tubing 3 which is within the trona formation is provided with a plurality of perforations I. Brine of appropriate composition, as indicated above, is passed by a pump 5 through a heater 6 and thence is forced, under the action of pump 5, into the trona deposit through the annular space provided between casing 2 and tubing 3. The brine supplied to the formation may advantageously be one which is in equilibrium with trona as the solid phase from about 20 to 40 C., and in passing through heater 6 it is brought to a temperature such that when it comes into contact with the trona I it'Wi'll be at a temperature substantially above the equilibrium temperature of the brine with respect to solid trona, which in this case is about 20 to 40 C., so that when it reaches the trona formation the brine will be capable of readily dissolving the trona congruently to form a pregnant brine which passes through the periorations 4 and is withdrawn through tube 3 for treatment to recover trona from it. The pump 5 is of suillcient capacity to maintain a suitable ilow through the Vwell in this manner, for example, at least 100 gallons per minute which, operating in accordance with Fig. 1, should result in production equivalent t about 50 tons of soda ash per day using brine that enters the well at a temperature of at least about 100 C.
'I'he pregnant brine leaving the well will carry with it insoluble matter in suspension which should, of course, be removed to avoid contamination of the crystallized trona. To this end the pregnant brine is passed to a settling tank 1 provided with a blowdown valve 8 through which the insoluble sludge may be passed to waste. The iron contained in this trona is' in a form which becomes colloidally dispersed-'and which is didicult to remove by ordinary methods. It may be removed readily, however, in accordance with the procedure described and claimed in my aforesaid copending application, in accordance with which the solution is intimately contacted with an adsorbent, most suitably activated carbon. Thereby the iron content of the pregnant brine is virtually eliminated. As applied to the present process, the partiyclariied brine passes from settling tank 'I to a clariiler tank 9 where itis agitated with a charge of activated carbon that is subsequently removed in a suitable illter I0. To avoid premature deposition of trona in an impure state, the operations just described are prei'- erably carried on in a. closed system with the well, i. e., without reducing the vpressure and without substantial cooling of the brine as it leaves the well.
The fully clarified Abrine is then ready for the crystallization step. In the embodiment shown it passes from filter I0 to one or more vacuum cryscycled brine but this may be corrected by the cc.
casional addition to tank I3 of soda ash from caleiner I4. y
It will be understood from Fig. 1 that brines in equilibrium with trona at a temperature of about 30 C. (average'ot 20 to 40 C.) may be used, and that the brine is preferably heated so that when it meets the trona it will be at about 85 C. The longer the line A--B in Fig. 1, the greater the proportion of rened trona produced per cycle, and for this reason it is preferred to work with brines in the vicinity of point A, although any of the brines of the lower graph saturated with sesquicarbonate may be used. Thus, the brines used for treating trona and for recycling in accordance with the invention may contain per hundred grams of water from about 22 to 38 grams oi sodium carbonate and from about 1 to 5.8 grams of sodium bicarbonate. The closer the point B comes to coinciding with the upper graph, the greater will be the amount of reilned sesquicarbonate produced per cycle. However, as the point B approaches the upper curve the likelihood of loss of carbon dioxide, by decomposition o! trona, in-
creases. For this reason it is preferred to operate in a closed system and with the pregnant brine at a maximum temperature not much over about 100 C. The process may be carriedl out satisfactorily at about 85 to 100 C., which is my preferred practice, or even higher. Of course, with adequate maintenance of CO2l pressure higher tallizers II which, in effect, act as evaporators by utilizing the sensible heat of the liquid to eiIect evaporation by application or reduced pressure, which also results in a marked reduction of the temperature of the liquid. In short, the sensible heat of the liquid is converted into the latent heat of evaporation. Thus the brine becomes supersaturated with respect to trona and causes it to be crystallized congruently. The crystallized trona and mother liquor then pass to a, illter I2. The mother liquor from the lterpasses to a tank I3 and thence is recycled to the well by pump 5 as described above. 'I'he trona cake from filter I2 may be used as desired, e. g., by passing it Ito a calciner I4 ywhere it is converted to soda as The trona recovered in this manner is of high temperatures may be used. Likewise, thevbrine passed to the well may be of such composition as to be in equilibrium with trona at temperatures higher or lower than 30 C.
Other modifications are equally permissible without departing from the spirit of the invention. Thus, the pregnant brine may be merely cooled to obtain a. crop oitrona crystals, or it may be subjected to evaporation in other than vacuum crystallizers, the primary requisite being to alter the condition of the brine to effect crys'- v tallization oi.' the trona which it hasdissolved from the formation, which is accompanied by evaporation and cooling. either or both. Likewise, instead of using the single well shown in Fig. 2 the brine might be pumped into one or more input wells and caused to pass through the formation to a separate output'well. The type of well shown in Fig. 2 is preferred, however, because the ingoing brine keeps the outcoming pregnant brine hot and thus presents premature trona crystallization.
According to the provisions of the patent statutes, I have explained the principle and mode of practicing my invention, and have illustrated and described what I now consider to represent its best embodiment. However, I desire to have it understood that, within the scope oi the appended claims, the invention may be practiced otherwise than as speciiically illustrated andk described.
1. That method of producing soda ash from an underground deposit of Wyoming trona carrying' organic matter -and contained iron which comprises forcing into the trona formation under a pressure greater than atmospheric a heated cycling brine of sodium carbonate and sodium bicarbonate containing substantially more normal carbonate than bicarbonate,-and which is unsaturated with respect to trona and from which the dissolved trona may be crystallized congruently.
mation. contacting the pregnant solution with au adsorbent and thereby removing said organic iied solution from said adsorbent, crystallizing and recovering from the clarified brine renned sodium sesquicarbonate, calcining the crystallized sesquicarbonate to produce soda ash, and'cycling the mother liquor from said crystallizing step to thefiormation.
2. A method according to claim 1 in -which a portion of said soda ash is cycled to said mother liquor to maintain the ratio of normal carbonate to bicarbonatein the cycling brine.
3. A method according to claim 1 in which the cycling brine contains about 22 to 28 grams of sodium`carbonate and 1 to 5.8 grams of sodium bicarbonate per 100 grams of water and is heated to at least about 85 C. as it is passed to the formation.
4. 'Ihat method of producing soda ash from an underground deposit of Wyoming trona carrying organic matter and contained iron which comprises forcing into the trona formation under a pressure greater than atmospheric a heated cycling brine of sodium carbonate and sodium bicarbonate containing' substantially more normal carbonate than bicarbonate and which is unsaturated with respect to trona and from which 'the dissolved trona may be crystallized cogruently, withdrawing the pregnant solution from the formation, contacting the pregnant solution with an adsorbent and thereby removing said the clarlned solution from said adsorbent, crystallizing and recovering from the clarined brine refined sodium sesquicarbonate with some' of said brine adhering to the crystals, calcining said crystais with the adherentbrine to produce soda ash, and cycling the mother liquor from said crystallizing step to the formation. l
5. 'I'hat method of producing soda ash from an underground deposit of Wyoming trona carrying organic matter and -contained iron which comprises forcing into the trona formation under a pressure greater than atmospheric a heated cycling brine of sodium carbonate and sodium bicarbonate containing substantially more normal carbonate than bicarbonate and which is unsaturated with respect to trona and from which the dissolved trona may be crystallized congruent-Jy, withdrawing the pregnant solution from the formation, contacting the pregnant solution with an adsorbent and thereby removing said organic matter and contained iron; separating the clarified solution from said adsorbent, subjecting the clarified solution to vacuum crystallization and recovering refined sodium sesquicarbonate with some of the brine adhering to the crystals, calcining said crystals with adherent brine to produce soda ash, cycling the mother liquor from said crystallizing step to the formation. and cycling to said mother liquor a portion of said soda ash to maintain the ratio of normal carbonate to bicarbonate in the cycling brine.
ROBERT D. PIKE.
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US2625384 *||Jul 1, 1949||Jan 13, 1953||Fmc Corp||Mining operation|
|US2639217 *||Jul 29, 1949||May 19, 1953||Pike Robert D||Production of sodium sesquicarbonate from crude trona|
|US2685438 *||Jun 30, 1948||Aug 3, 1954||Kansas City Testing Lab||Process for the solution mining of potassium compounds|
|US2704239 *||Jun 1, 1951||Mar 15, 1955||Pike Robert D||Production of sodium bicarbonate and soda ash from trona|
|US2896930 *||Jun 10, 1954||Jul 28, 1959||Nuclear Dev Corp Of America||Method of recovering uranium from underground deposit|
|US2979317 *||Aug 12, 1959||Apr 11, 1961||Fmc Corp||Solution mining of trona|
|US3050290 *||Oct 30, 1959||Aug 21, 1962||Fmc Corp||Method of recovering sodium values by solution mining of trona|
|US3058729 *||Jan 8, 1960||Oct 16, 1962||Pittsburgh Plate Glass Co||Solution mining method|
|US3184287 *||Oct 5, 1961||May 18, 1965||Fmc Corp||Process for the production of soda ash from underground trona deposits|
|US3211519 *||Sep 13, 1961||Oct 12, 1965||Intermountain Res & Dev Corp||Method of controlling sulfide concentration to prevent iron contamination in the processing of trona|
|US3779602 *||Aug 7, 1972||Dec 18, 1973||Shell Oil Co||Process for solution mining nahcolite|
|US3966541 *||Feb 20, 1975||Jun 29, 1976||Abraham Sadan||Concentration of underground brines in situ by solar evaporation|
|US4178233 *||Jul 31, 1978||Dec 11, 1979||Otisca Industries, Ltd.||Fluorinated hydrocarbons in coal mining and beneficiation|
|US4244351 *||Nov 6, 1978||Jan 13, 1981||Intertechnology/Solar Corporation||Solar collection system|
|US4557910 *||Mar 29, 1982||Dec 10, 1985||Intermountain Research & Development Corporation||Production of soda ash from nahcolite|
|US4815790 *||May 13, 1988||Mar 28, 1989||Natec, Ltd.||Nahcolite solution mining process|
|US5262134 *||Feb 21, 1992||Nov 16, 1993||Fmc Corporation||Process for producing sodium salts from brines of sodium ores|
|US5283054 *||Mar 30, 1993||Feb 1, 1994||Fmc Corporation||Process for producing sodium salts from brines of sodium ores|
|US5609838 *||Jun 9, 1995||Mar 11, 1997||Tg Soda Ash, Inc.||Equilibrium production of sodium carbonate from sodium bicarbonate|
|US5690390 *||Apr 19, 1996||Nov 25, 1997||Fmc Corporation||Process for solution mining underground evaporite ore formations such as trona|
|US5766270 *||May 21, 1996||Jun 16, 1998||Tg Soda Ash, Inc.||Solution mining of carbonate/bicarbonate deposits to produce soda ash|
|US5955043 *||Aug 29, 1996||Sep 21, 1999||Tg Soda Ash, Inc.||Production of sodium carbonate from solution mine brine|
|US5989505 *||Mar 18, 1996||Nov 23, 1999||Solvay Minerals, Inc.||Method for recovery of alkali values from trona using air stripping|
|US6228335||Dec 10, 1997||May 8, 2001||Fmc Wyoming Corporation||Process for the production of sodium carbonate crystals|
|US6251346||Aug 20, 1997||Jun 26, 2001||Tg Soda Ash, Inc.||Solution mining of carbonate/bicarbonate deposits to produce soda ash|
|US6322767||May 19, 2000||Nov 27, 2001||Fmc Corporation||Process for making sodium carbonate decahydrate from sodium carbonate/bicarbonate liquors|
|US6428759||May 2, 2000||Aug 6, 2002||Fmc Wyoming Corporation||Production of feed liquors for sodium carbonate crystallization processes|
|US7611208||Aug 17, 2005||Nov 3, 2009||Sesqui Mining, Llc||Methods for constructing underground borehole configurations and related solution mining methods|
|US7638109||Dec 18, 2006||Dec 29, 2009||Fmc Corporation||Production of sodium sesquicarbonate and sodium carbonate monohydrate|
|US8057765||Sep 24, 2009||Nov 15, 2011||Sesqui Mining, Llc||Methods for constructing underground borehole configurations and related solution mining methods|
|US8899691||Jul 29, 2011||Dec 2, 2014||Sesqui Mining, Llc||Methods for constructing underground borehole configurations and related solution mining methods|
|US9010869||Dec 21, 2012||Apr 21, 2015||Solvay Sa||Solution mining of ore containing sodium carbonate and bicarbonate|
|US9260918||Oct 28, 2014||Feb 16, 2016||Sesqui Mining LLC.||Methods for constructing underground borehole configurations and related solution mining methods|
|US9433894||Apr 25, 2014||Sep 6, 2016||Tronox Alkali Wyoming Corporation||Removal of hydrogen sulfide from gas streams|
|US20060039842 *||Aug 17, 2005||Feb 23, 2006||Sesqui Mining, Llc||Methods for constructing underground borehole configurations and related solution mining methods|
|US20070140945 *||Dec 18, 2006||Jun 21, 2007||Copenhafer William C||Production of sodium sesquicarbonate and sodium carbonate monohydrate|
|US20100066153 *||Sep 24, 2009||Mar 18, 2010||Sesqui Mining, Llc||Methods for constructing underground borehole configurations and related solution mining methods|
|US20150315893 *||Dec 12, 2013||Nov 5, 2015||Solvay Sa||Process for recovering soda values from underground soda deposits|
|EP2607313A1||Dec 21, 2012||Jun 26, 2013||Solvay SA||Solution mining of ore containing sodium carbonate and bicarbonate|
|EP2607314A1||Dec 21, 2012||Jun 26, 2013||Solvay SA||Solution mining of ore containing sodium carbonate and bicarbonate|
|EP2924233A1||Mar 13, 2015||Sep 30, 2015||Solvay SA||Multi-well solution mining exploitation of an evaporite mineral stratum|
|U.S. Classification||423/206.1, 23/302.00T, 299/5, 299/7|
|International Classification||C01D7/14, C01D7/00, E21B43/28, E21B43/00|
|Cooperative Classification||C01D7/14, E21B43/281|
|European Classification||E21B43/28B, C01D7/14|