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JOURNAL OF RESEARCH of the National Bureau of Standards Volume 82, No. 3, November-December 1977 Investigation of Calcium Aluminate Cement Phases Under High Gaseous Pressure* J. L. Waring, R. S. Roth, W. S. Brower, and C. A. Harding Institute for Materials Research, National Bureau of Standards, Washington, D.C. 20234 (AUgUlt 2, 1977) The che mi ca l deg radat ion of refractory ce me nt castable li ners is impo rt ant in the coal gas ifi ca ti on process . Th e system CaO-AI20,,- H20 has bee n inv es ti gated at high temp era ture an d pr ess ur e. A pse udobi nary rea c ti on diagram wa s constructed for the syste nl CaO-A I20 ,,- H20 in st ea m at 1000 psig. Seve ral experiments were co ndu c ted in th e CaO-A l20,,- H20 sys tem in CO2, CH4, and CO . Key wo rd s: Alumina ce me nt s; CaO· AI 20,, ' H2 0; coa l gas ifi ca ti on; re fr ac tory ce ments. 1. Introduction The process of coa l gasification re quires the handling and containment of cOlTosive gases at high temperature and press ur e. Although the chemical composition of the gaseous environment found to occur in coal gas ifi cation reac tors varies d epe nding on the processes employed, they generally contain CO, CO2, H2, H2 0, and CH4 as major constituents and C2H6, H2S, and N2 as minor const itu en ts. Thi s inv est i- gation wa s conce rned with the che mi cal degradation pro- duced by the inte ra ction of high pressu re H20 , CO, and CO2 with some of the pha ses forming th e hot cas table high purity calc iu m aluminat e liner material found in ma ny operating coal gasifiers. The principal constituents of this castable liner material ar e calcium aluminates and alumina. 2. Specimen Preparation and Test Methods For most of the hydration experiments, pure, well-charac- terize d, starting materials were emp loyed. The compositions 3CaO . A1 20 3, CaO' A120 3, CaO' 2A120 3, and CaO' 6Al20 3 were prepared from high purity CaC03 and A120 3. These admixtures were ground and calcined at 700°C for 60 hours, 1000 °C for 16 hours, and 1500 °C for 60 hours. The three compositions highest in Al20 3 content were reheated for an additional 60 hours at 1550 0c. All of these materials, synthesized in air, were characterized by x-ray powd,er diffraction techniques and found to be single phase. These single phase mate rial s we re placed in small plati- num tubes , with calculated, weighed amounts of H20 and sealed. The tubes were heat ed by co nv entional hydrothermal tec hniques, que nch ed, opened, and dried. The reaction products were identified by x-ray powder diffraction. Mate- rials reacted in other environme nt s were tr eated similarly except that they were heated in open platinum tub es in the absence of introdu ced H2 0. • This work was supported in pari by ERDA:FE Contract No. 14-32-0001-1749 and shorter versions of this paper have been included liS parts of ERDA Quarterly Reports. 3. Results and Discussion 3.1. System CaO-AI 20 3 in Steam Considerable information on the CaO-AI203-H20 system has bee n reported in th e lit erature. The work of Pe pp ler and We ll s [1 r and Majumdar and Roy [2] summarize mo st of our present knowledge of this syste m. Nurse et a1. [3] found that 12CaO' 7 Ab03 melts congru e ntl y at 1392 °C in a tm osphe ri c air. In dry air, preformed 12CaO' 7 A1 20 3 melts in congruently to CaO' Al20 3 and a liquid at 1374 °C. He furth er c onclud ed that the 12CaO' 7Al20 3 co mpound did not have a field of stability in the stric tl y anh ydrous CaO-A1203 system. For the purpose of studyin g the solid state reactions encountered with stea m in a coal gasifier th e solubility data of Peppler and We ll s were reinterpreted with th e vi ew of integrating the data with tho se of Ma jumdar and Roy. This wa s acco mplished by cons tructing the diagram, figure 1, from th e data given by Peppler and Wells and Majumdar and Roy and from th e data in table I. From these l ow temperature data, it wa s possible to predict th e behavior at 1000 0c. Therefor e, it was necessa ry only to verify th at portion of the system which co uld directly affect the operation of a coal gasifier at 1000 °C and 1000 psig 2 of steam. To verify the reactions whi ch occur in the CaO-AI20 3- H20 system at high temperatures and press ures a se ri es of experiments were conducted and th e results are given in table II. A pseudobinary reaction diagram, figure 2, wa s constructed from the data in table II. In constructing figure 2, it was necessa ry to neglect the starting pha ses and assume the various starting materials would approach the same equilibrium product s in any given temp era ture, pres- s ur e, time sequence. From figure 2 it can be see n that the first hydrat e forme d, 3CaO' A1 20 3' 6H2 0, is unstable and dissociates, above room temperature, to form Ca(OHh and 4CaO' 3A120 3' 3H2 0. 1 Figures in brackets indicate the literature references I.It the e nd of this paper. 2 The use of psi, psig, bar, and kbar follows Ihe current common practi ce of workers in the field. Not e that 1 bar = 1(1' N/ m2 (or pascal) = 0.9869 aim = 14. 504 ps i. The accepted inte rn utionul standard ( 51) unit of press ure is the pascal or newton per S(luare meier. 167

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JOURNAL OF RESEARCH of the National Bureau of Standards Volume 82, No. 3, November-December 1977

Investigation of Calcium Aluminate Cement Phases Under High Gaseous Pressure*

J. L. Waring, R. S. Roth, W. S. Brower, and C. A. Harding

Institute for Materials Research, National Bureau of Standards, Washington, D.C. 20234

(AUgUlt 2, 1977)

The che mi ca l degradat ion of refra ctory ce me nt castabl e li ne rs is import a nt in the coal gas ifi cati on process . The system CaO-A I20,,- H20 has been investi gated a t hi gh te mperature and pressure. A pseudobi nary reacti on diagram was constru cted for the systenl CaO-A I20 ,,- H20 in stea m at 1000 ps ig. Several ex periment s we re conduc ted in th e CaO-A l20,,- H20 system in CO2, CH4 , and CO .

Key words : Alumina ceme nt s; CaO· AI20,, ' H20; coa l gasifi ca ti on; refractory ceme nt s .

1. Introduction

The process of coal gasification requires the handling and containment of cOlTosive gases at high temperature and pressure . Alt hough the chemical composition of the gaseous environment found to occur in coal gasifi cation reactors varies depending on the processes employed , th ey generally contain CO, CO2, H2, H20, and CH4 as major constituents and C2H6 , H2S, and N2 as minor constituen ts. This investi­gation was concerned with th e chemi cal degradation pro­duced by th e interaction of hi gh pressu re H20 , CO , and CO2 with some of th e phases forming th e hot castable high purity calc iu m aluminate liner material found in many operating coal gasifiers. The principal constituents of this castable liner material are calcium aluminates and alumina.

2. Specimen Preparation and Test Methods

For most of the hydration experiments, pure, well-charac­terized, starting materials were employed. The compositions 3CaO . A120 3 , CaO' A120 3, CaO' 2A120 3, and CaO' 6Al20 3

were prepared from high purity CaC03 and A120 3 . These admixtures were ground and calcined at 700°C for 60 hours, 1000 °C for 16 hours, and 1500 °C for 60 hours. The three compositions highest in Al20 3 content were reheated for an additional 60 hours at 1550 0c. All of these materials, synthesized in air, were characterized by x-ray powd,er diffraction techniques and found to be single phase.

These single phase mate rial s were placed in small plati­num tubes , with calculated, weighed amounts of H20 and sealed. The tubes were heated by conventional hydrothermal techniques, quenched, opened, and dried. The reaction products were identifi ed by x-ray powder diffraction. Mate­rials reacted in other environments were treated similarly except that they were heated in open platinum tubes in the absence of introduced H20.

• This work was supported in pari by ERDA:FE Contract No. 14-32-0001- 1749 and short er versions of thi s paper have been included liS parts of ERDA Quarterly Report s.

3. Results and Discussion

3.1. System CaO-AI20 3 in Steam

Considerable information on the CaO-AI203-H20 system has been reported in the literature. The work of Peppler and Wells [1 r and Majumdar and Roy [2] summarize most of our present knowl edge of thi s sys tem. Nurse et a1. [3] found that 12CaO' 7 Ab03 melts congruentl y at 1392 °C in a tmosphe ri c air. In dry air, preform ed 12CaO' 7 A120 3 melts incongruently to CaO' Al20 3 and a liquid at 1374 °C. He further concluded that the 12CaO' 7 Al20 3 compound did not have a field of stability in th e s tri ctl y anh ydrous CaO-A1203 system.

For the purpose of s tudying the solid state reac tions encountered with steam in a coal gasifi er th e solubilit y data of Peppler and Well s were reinte rpreted with th e vi ew of integrating th e data with those of Majumdar and Roy. This was accompli shed by constru cting th e diagram, figure 1, from the data given by P eppler and Wells and Majumdar and Roy and from the data in table I. From these low temperature data, it was possible to predi ct th e behavior at 1000 0c. Therefore, it was necessary only to verify that portion of the system which could directly affect the operation of a coal gasifier at 1000 °C and 1000 psig2 of steam.

To verify the reac tions whi ch occur in the CaO-AI20 3-H20 system at high temperatures and pressures a seri es of experiments were conduc ted and the results are given in table II. A pseudobinary reaction diagram, figure 2, was constructed from the data in tabl e II. In construc ting figure 2 , it was necessa ry to neglect th e starting phases and assume th e various s tarting material s would approach the same equi librium products in any given temperature, pres­sure, time sequence.

From figure 2 it can be seen that the first hydrate formed, 3CaO' A120 3 ' 6H20, is unstable and dissociates, above room temperature, to form Ca(OHh and 4CaO' 3A120 3 ' 3H20.

1 Figures in brackets indicate the lit erature references I.It the end of thi s paper. 2 The use of psi, psig, bar, and kbar follows Ihe current common practi ce of workers in the field.

Note that 1 bar = 1(1' N/m2 (or pasca l) = 0.9869 aim = 14. 504 ps i. The accepted intern utionul standard (51) unit of pressure is the pasca l or newton per S(luare meier.

167

':' ~

"

5600 -

4800 -

4000 -

5 3200 -

::

I I

I I P I I

I I 1 1 I

o CO

+ 1<1 + t2 + I BOEH+MITE \ BOEHMITE I

12,1 CIIOH)2 I BOEHMITE I + I

I CI(OH)2 I I H6 I I /

I / cb CI(OH)2 ~ BOEHMITE + 4,],3 + CI(OH)2 # //0

I

-

-

-

GIBB+SITE I / / / 2400 - 3,106 I / / / 1<1 + 102 + 1207 +

I / / / CIO

-

CI(OH)2

1600 -

100 -

I U / I II I I f~ I I + / I I + / + / 1/1

+

I ® _J~---/ Ill> I Iili ® F'80EHMnE + 31~ + CI(OH)]2 cb I

Starting flaterial l1

1: 2

1: 2

1:1

1 :2

1 :2

1:1

1:1

1I1:2 = CaO·2A1 203

1: 1 = CaO .A1 203

100 200 300 400 500 600 100

TEMPERATURE · C

FIGURE 1. Proposed constitution diagram. ® Peppler and Wells o Majumdar and Roy + Waring et 01. (this work)

Table 1. Experimenta l Data Used to Construct the Pressure­Temperature Diagram for the System CaO-A 1203-H 20.

Temperature Pressure °C psig

300 100O

700 100O

700 1000

400 1000

500 100O

400 1000

500 100O

Time days

11

11

11

11

X-ray Diffraction Analysis

1:2 + 4:3:3 + boehmite

1: 2

1 : 1 + trace 1: 2

1:2 + boehmite + 4:3:3

1: 2

1: 1

1:1 may have faint trace of 1:2

4:3:3 = 4CaO·3A1 203·3H 2O

A 1203 -1120 = boermite

-

1

800 900 1000

Conclusion

1:2 ~ boehmite + 4 :3: 3

1:1 ~ 1:1

1:2 ~ boehmite + 4:3:3

1: 1 (?)

1:1 ~ 1:1

Preformed 3CaO' Al20 3 was found to have a minimum dissociation temperature in excess of 1000 °C and 1000 psig steam. The 1000 °C and 1000 psig data were obtained using a TZM (titanium-zirconiu m-molybdenum alloy)3 apparatus.

3 Certain commerciall y available materials or instruments are identified in this publication for the purpose of providing a complete description of the work performed. The experiments reported do not constitute a complete evaluation of the performance characteristics of the products so identified. In no case does such identification imply recommendation or endorsement by the Nationa l Bureau of Standards nor does it imply that the items identified are necessarily the best available for the purpose.

The maximum and mlOimum dissociation temperatures for the 12CaO' 7 Al20 3 have not been established . However, the minimum dissociation temperature is probably in excess of 400°C and the compound should be stable up to the melting point of 1392 °C. The hydrate 4CaO' 3A120 3 ' 3H20 forms in a wet atmosphere at about 20°C and is stable up to about 600°C in 1000 psig steam. The compounds CaO ' Al20 3 and CaO' 2AI20 3 were found to exist at temperatures in excess

168

" ,

1400 -

1300 -

3 :1 1200 - I

1 12 :7

1100 - ___________ i ____ _ ~ 1000 - •

900 -

800 -CaD + 12 :7

700 - • 1 1

600 - • 1 -- ______________ 1

1:1 1:2 1:6

12:7 + 1:1 1:1 + 1:2

1:2 + 1 :6

• •

500 - Ca (OH ) + 127. 112?7i4:'3~ , 4 1:6 + boehmite

, • I + .• ~+ ... ';;.,: '+~~"",.""" .... '="",."",.""""""~"",."",."""~ 400 - 1----------- - - - - - - 4:3 :3-.. a.c.::",,:. ;.;.;. ~.:;.;.;:::"":: ;.;.;:::c.;.:: ;';';:::';':':: :"":: ;';';: •• "1"",,,;.;.;c.;.:.:;.;.;.;c.;.;.;.;c.;.;.;.;.;.:.c.;.;.;.;c.;.;.;.;.;.:.c.;.;.;.;""4

Ca IOH ), + 4:3:3 • ~ 300 - 1

• • • 200 - 1----------- ______ ....J

3:1:6 + 4:3:3 I 4:3:3 + boehmite --------------------------------100 - Ca (OH )2 + 3:1:6

3:1:6 + boehmite

I 10

I I I I I I I I I I 80

I 90 20 30 40 50 60 70

3:1 :6 12:7 4:3:3 Ca(OH)2

1 :2

F IGU RE 2. Tentative pseu.dobinary reaction diagram of the syst.em CaO-AI 20: .. H20 at 1000 psig_ 3: 1:6 = 3CaO- A I2 O,' 6H2 0 4 :3:3 = 4CaO· 3A 12 0a ' 3H20

3: 1 = 3CaO' AI20a 12:7 = 12CaO' 7A I2 0a

' :1 = CaO' AI2 0a 1:2 = C.O· 2A I2 0a 1:6 = CaO' 6A I2 0a

A I2 0 a' H2 0 = boehrnile ill = region of und ete rm ined equilibria • = expe rim e nta l poin ts

of 1000 °C and to hydrate below 400 °C. The compounds CaO' A120 3, CaO' 2Al20 3 and CaO' 6A120 3 , expe rimentally, appear to have th e same minimum tempera ture of stabilit y since a t these relatively low temperatures the reactions occur very slowl y. It has not been poss ible to delin eate these boundaries; therefore , the region of uncert aint y is shaded in the diagra m, fi gure 2. At a temperature below approximately 400-450 °C, these phases di ssoc iate into boehmite (AI20 3 ' H 2 0) and 4CaO ' 3A120 3 ' 3H20. The phase transition between boehmite and Ab03 in th e pressure range of 1000 psig was not dete rmined.

In a cement whi ch in itiall y consists of CaO' Ab03 and CaO ' 2Al20 3 with Ab03 grog, the 3CaO ' A120 3' 6H20 ori gi­nall y formed after th e additi on of H20 will transform rapidly upon the increase of pressure and temperature to fOt-m 4CaO' 3A120 3 ' 3 H20. Th is phase will then react at slowly inc reas ing tempera tures to form , first, 12CaO ' 7 Al20 3 plus CaO . Al20 3 and the n, eventu al! y, CaO' 6Al20 3 plus AI20 a, if the whole product atta ins equilibrium.

Several ex pe riments were conduc ted at high temperature in CO2 (860 psig) and the results are given in table III.

The data given in table III indi ca te that th e reac tions whi ch occur in a CO2 e nvironment are simila r to those occulTing in s team. The re a re seve ral exceptions. The 4CaO' 3A120 3 ' 3H20 phase at 500 °C is s tab le in s tea m but in CO2 partially decomposes to CaC0 3 + A120 3. At 600 °C( 860 psig CO2 , that portion of the 4CaO' 3AI20 ;J' 3H20, which has not reacted with the CO2, dehydrates to form a cubic phase with a == 8.9 A, whi ch is appa rentl y th e aluminate analog of sodalite (Ca4AI60 13, analogous to Na4A13Si3012Cl) . The occurrence of th e calcium aluminate analog of sodalite was reported by Ponomarev, Khe ibe r, and Belov [4] to form by dehyd ra tion in air from hydrothe rmall y grown single crystals. Several experiments ind ica te that other CaO-A1203 phases may also be s table with respect to the CaC03-A120 3 system under th ese conditi ons .

169

Table II. Experimental Data for Compositions in the Systen CaO-AI 203-H 20 at 1000 PSi9 Steam Pressu re .

~!~;~~~jll Temp . Pressure Time X-ray Diffraction Conclusions ·C PS i 9 hrs Analysis

3: 1:6 350 1000 720 4:3:3 + Ca(OH)2 + hydrate 3:1:6 ~ 4:3:3 + hydrate

3: 1 :6 450 1000 720 4:3:3 + Ca(OH)2 + 3:1:6 + hydrate 3:1:6 ~ 4:3:3 + hydrate

3: 1 350 1000 720 3:1 + Ca(OH)2 + 12:7 3:1 ~ 12:7 + Ca(OH)2

3 : 1 450 1000 720 3:1 + Ca(OH)2 + 12:7 3:1 ~ 12:7 + Ca(OH)2

3: 1 500 1000 168 3:1 + 12:7 + Ca(OH)2 3:1 ~ 12:7 + Ca(OH)2

3: 1 600 1000 168 12:7 + 3:1 + CaO 3:1 ~ 12:7 + CaO

3: 1 700 1000 168 3:1 + 12:7 + CaO 3:1 ~ 12:7 + CaO

3: 1 1000 945 120 12:7 + CaO 3: 1 ~ 12: 7 + CaO

4:3 :3 350 1000 720 4:3:3 + boehmite ~~~~~)~ ;:~~nh~~~~a~3 +

4:3:3 + amorphous Ca(OH)~ + 4:3: 3 400 1000 86 4:3:3 + Ca(OH)2 amorphous A1 203 ' 4:3:3

Ca(OH)2

4: 3: 3 450 1000 720 4:3:3 4:3:3 + amorphous Ca(OH)2 + amorphous A1 203 • 4:3:3

4:3:3 + amorphous Ca(OH)~ + 4: 3: 3 500 1000 86 4:3:3 + Ca(OH)2 amorphous A1 20 3 ' 4:3:3

cryst Ca(OH)2

4: 3: 3 500 1000 168 4 :3: 3 4:3:3 + amorphous A1203 + amorphous Ca(OH)2 ~ 4:3:3

4:3: 3 600 1000 168 4:3:3 + 12:7 + CaO 4:3:3 ~ 12:7 + CaO

4:3: 3 700 1000 168 (leaked) 12:7 + 1:1

1:1 300 1000 168 4 :3:3 + 1: 1 + boehmite 1:1 ~ boehmite + 4:3:3

1: 1 400 1000 240 1:1 1: 1 (?)

1:1 450 1000 240 1 : 1 + 4 :3:3 1: 1 ~ 4:3:3

1:1 500 1000 264 1 :1 1:1 ~ 1:1

1:1 700 1000 168 1:1 + 1:2 1:1 ~ 1:1

1:1 1000 945 120 1:1 1:1 ~ 1:1

1 :2 300 1000 168 1:2 + 4 :3:3 + boehmite 1:2 -+ boetTnite + 4:3:3

1 :2 400 1000 264 1:2 + boehmite + 4:3:3 1:2 ~ boehmite + 4:3:3

1 :2 450 1000 240 1 :2 1:2 ~ 1:2

1 :2 500 1000 264 1 :2 1:2 ~ 1:2

1 :2 700 1000 168 1 :2 1: 2 ~ 1:2

1 :2 1000 945 120 1: 2 1: 2 ~ 1:2

1 :6 350 1000 945 1:6 + 4:3:3 + A1 203 1:6 .4 :3:3 + A1 203 (+ boehmHe-?)

1 :6 450 1000 945 1:6 + A1 203 1 : 6 • 1 : 6 + A 12°3

1I 3:1:6 = 3CaO.AI 203·6H 2O AI 203 ·H 20 = boehmite

1:2 = CaO·2A1 203 3:1 = 3CaO.AI 203

4:3:3 = 4CaO·3AI 203 ·3H 2O

12:7 = 12CaO·7A1 203 1:1 = CaO.AI 203 1:6 = CaO·6AI 203

hydrate = hydrated calcium allJl1inate of unknown composition

Two specimens consIsting of CA-25, a commercially available calcium aluminate cement, and 4CaO . 3Al20 3 • 3H20 were heated in a methane environment at 800°C for two weeks at 1000 psig. The x-ray powder pattern of the CA-25 specimen showed the CaO' A120 3 , CaO' 2Al20 3 and Al20 3

which were present in the original CA-25 plus an unknown phase with a line at about 24° 28 (CuKa radiation). This

unknown phase did not appear to be calcium formate. The 4CaO . 3Al20 3 • 3H20 contains 12CaO' 7 Ah03 and CaO . A120 3• These are the same reaction products as those occurring under 1000 psig steam at the same composition and temperature. Table IV summarizes the results.

Four compositions were heated in CO (Table V) at 1000 psig and 700°C for llO hours. The x-ray pattern of the

170

"

Table III. Exper imen t a l Data for Compositions in the System CaO-A1 203-H 2O i n 860 psig of CO2 ,

Star ting Temp. Pressure Time ResultsW Material~ °C ps i g hrs X-ray Diffraction Analysis Conclus i ons

3: 1 600 860 72 3: 1 3: 1 + 3 : 1

3: 1 700 860 72 3: 1 + 12: 7 + CaC03 3: 1 + 12:7 + CaC03 3: 1 700 860 144 3: 1 + 12: 7 + CaC03 3: 1 + 12:7 + CaC03

3: 1 : 6 500 860 336 CaC03 + 4: 3: 3 3:1:6 + CaC0 3 + 4 : 3 : 3

3: 1: 6 600 860 384 CaC03 + 12: 7 + 1 :2 3: 1 : 6 + CaC03 + 12: 7 + 1: 2

3: 1: 6 800 860 144 CaC03 + un know~ + 1 :2 3:1:6 + CaC03 + unknow~ + 1: 2

4:3: 3 500 860 288 4:3:3 + Al 03 + CaC03 4:3:3 + CaC03 + A1 503 4:3:3 600 860 384 "sodalite"~ + CaC03 4:3:3 + "sodal ite"--' + CaC03 4:3:3 700 860 144 1: 1 + CaC03 + unknown( s)~ 4 :3 :3 + 1: 1 + CaC03 + unknown( s}~

1: 1 + 1:2 + CaC03 + unknow~ 4:3:3 800 860 144 4: 3:3 + 1: 1 unknownV

+ 1: 2 + CaC03 +

1:1 500 860 288 1:1 + A1 203 + CaC03 1:1 + A1 203 + CaC0 3

1:1 600 860 72 1:1 1:1 + 1:1

1:1 700 860 72 1:2 + CaC03 1:1 + 1: 2 + CaC03

1 : 1 800 860 144 1:1 1:1 + 1:1

1: 2 500 860 720 1 :2 1 :2 + 1 :2

1: 2 700 860 192 1 :2 1:2 + 1: 2

1: 6 500 860 720 1: 6 + tr Cl-A1 203 1:6 + 1 :6

~ All bulk starting materials, which were spectrographically pure, were mixed and calcined for sufficient time and at a temperature to obtain single phase materials . These specimens were heated in a conventional hydro­thermal bOOlb in open Pt tube and were quenched by water i mmersion from the temperatures indi cated.

£( The phases identified are given in order of the amount present (greatest amount first) at room temperature. These phases are not necessarily those present at the temperature to which the specimen was heated.

Y The following short notations were used for clarity:

3:1 = 3CaO·A1 203 3:1:6 = 3CaO ·A1 203·6H20

12 :7 = 12CaO . 7A1 20 3 4:3:3 = 4CaO . 3A1 203 ·3H20

1 :1 = CaO·A1 203 1:2 = CaO.2A1 203 1:6 = CaO.6A1 203

if The "sodal ite" dehydration product (major peak, d = 3.642)

Y Unknown dehydration product (major peak, = 3.697)

V Unknown dehydration product (major peak, = 3.620)

sample which was initially CaO' Ab03 showed a mixture of CaO ' Al20 3 and CaO' 2A120 3 . The 4CaO' 3A1 20 3 ' 3H20 showed the same decomposition products as those heated in CO2• The CA-25 x-ray pattern showed mixtures of CaC03 ,

A120 3 , CaO· 2AI20:J and CaO' AJ 20 3 • The CaO' 2Al20 3

showed no reaction.

4. Summary

Many questions ,-emain unanswered which could not be investigated in thi s study. However, th e following observa­tions should be noted:

171

1. At 1000 psig steam pressure, th e phase boundaries are essenti all y those which can be predicted from a combination of th e published data of Peppler and Wells [1] and Majumdar and Roy [2J.

2. The cementitious phases 3CaO' A1 20:l . 6H20 and 4CaO ' 3A120 3 • 3H20 are not stable at any hi gher temperature in 1000 psig steam than they are at atmospheric pressure.

3 . The compound 4CaO' 3Al20 3 • 3H20 decomposes to metastable phases in dry atmospheres such as CO2 or CO and di!"ectly to the stable phases in steam.

Table IV. Exrerir:1ental Data for Coopositions in the System CaO-A1 203-HZO in CII 4 ,

Start~ng I Temp. Pressure Time Resul ts~1 l iat(-r1a l s~ °C ps i9 hr s X- ray Diffraction Ana lysis

Conclusions

CA - 25 000 1000 JI6 1:2 + 1:1 + a-A '2°3 + unknow$

4: J: J 800 1000 JI6 12: 7 + I: I 4:J:J -·12:7 + 1:1

i}j All bu l k starting materi a ls . \'.'hich .... 'cre spectrograrhically pure , were nixed and calcined for suffic ient time and at a tmperature to ob tai n single phase materials. These specimens were heated in an open platinum t ube in a conventional hydrothemal bomb.

Y The phases identified are given in orde r of the amount present (greatest amount first) at room tefTIpef'ature . TI,ese phases are not necessarily those present at the tef:".perature to which thE> spec in en ~Ia shea ted.

5J ":3 : '" 4CaC . 3A1 203 . 3H 20

:2 " C,0.2foI 203 : 1 " CaO.AI 20J

12 "12CaO.7P.120J (fI· 2S = f.. corn ercia1 cement containing 1:1 . 1:2 and u-fl l ,03

'1.1 Srcc ir,' cr co ntains an unknO\-Jn r hasc with the najor x · ray ciffracti on powder 1 ine occurring {i t abou t J. 70A.

Terr,p. Pressure Ti r.: e ResultsQl Conc1u s ior$ \~ ~ ~ ~; ~:~ s2.1 °C ps i 9 hr s X- ray Diffraction Analysis

:1 700 lOOn 110 :1 + 1: 2

J : J 70C 1000 110 : 1 + "sodal ite "'S.l + CaC03 J:J -. :1 + CaCOJ

1: 2 700 ICOO 110 : £: : 2 -. I: 2

CA - 2S 700 1000 110 CaCOJ + Q-A 12°3 + 1: 2 + 1:1

~I All bulk startinq materials, which were srectrographically pure , were mixec ard calcined for sufficient ti me and at a t€fTlperature to ohtain sinq1e phas e materials. These specimens were heated i n an oren platinum tube in a conventional hydrothemal borr h.

Y ThE rhases identified are giver. in order of the amount present (greatest amount first) at room tCli r-erature. These phases are not necessarily t hose presen t at the temperature to what the s peci l'len \~as I~ eated ,

~/ This nateria l is a dehydration product which appears to be the ca1cit;m aluminate i'lna10g c f soea 1 ite.

t: 3 3 = 4CaO . JA1203 · 3H,O

I : ? " CaO -2fo I 20J 1 '1 " CoO -AI 20)

C l\ -: ~; = A cor.rerci c 1 c€'!rent contair.ing 1:1.1:2 ar.d a -A'2C3

4 . Most of th e phases in the CaO-AI20 :r H20 system are not s table in CO2 (860 psig) with respect to the system CaC 0 3-AI20 3 ·

In order to dete rmine th e possible deleterious effects of the combined gaseous atmospheres present in a coal gas ifi er, a conside rably more detai led study must be made of the CaO-AI20 3-H20 system, especially in CH4 and in various gaseous combinations.

172

S. References

[11 Peppler, R_ B., and Well s, L 5_, J. Res. Nat. Bur. Stand . (U.S.), 50, No.2, 75-92 (1954) RP2476_

[2] Majumda r, A. J., and Roy, R.]., J. Am. Ceram. Soc. 38, 568 (1956). [3] Nurse, R_ W., Welch, J. H., and Majumdar, A. J., Trans . Bri t.

Ceram. Soc. 64, r9] 409 (1965). [4] Ponomarev, Y. I. , Kheiber, D. M., and Belov, N. V., Soviet Physics

15 [5] 799, (1971).

l