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497-19-8 Usage

Chemical Description

Sodium carbonate is a common chemical used in various industries, including glassmaking and water treatment.

Chemical Description

Sodium carbonate, also known as washing soda, is a white, odorless powder used in the production of glass, detergents, and other chemicals.

Chemical Description

Sodium carbonate is a salt that is used to neutralize acidic solutions.

Chemical Description

Sodium carbonate is a basic compound used in the washing of organic compounds.

Chemical Description

Sodium carbonate is used to neutralize the reaction mixture.

Chemical Description

Sodium carbonate is a basic salt used as a neutralizing agent.

Chemical Description

Sodium carbonate is a salt that is commonly used as a base in organic reactions.

Chemical Description

Sodium carbonate is a salt that contains sodium and carbonate ions.

Check Digit Verification of cas no

The CAS Registry Mumber 497-19-8 includes 6 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 3 digits, 4,9 and 7 respectively; the second part has 2 digits, 1 and 9 respectively.
Calculate Digit Verification of CAS Registry Number 497-19:
(5*4)+(4*9)+(3*7)+(2*1)+(1*9)=88
88 % 10 = 8
So 497-19-8 is a valid CAS Registry Number.
InChI:InChI=1/CH2O3.2Na/c2-1(3)4;;/h(H2,2,3,4);;/q;2*+1/p-2

497-19-8 Well-known Company Product Price

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  • CAS number
  • Packaging
  • Price
  • Detail
  • Alfa Aesar

  • (10861)  Sodium carbonate, anhydrous, Puratronic?, 99.997% (metals basis)   

  • 497-19-8

  • 5g

  • 441.0CNY

  • Detail
  • Alfa Aesar

  • (10861)  Sodium carbonate, anhydrous, Puratronic?, 99.997% (metals basis)   

  • 497-19-8

  • 25g

  • 1391.0CNY

  • Detail
  • Alfa Aesar

  • (10861)  Sodium carbonate, anhydrous, Puratronic?, 99.997% (metals basis)   

  • 497-19-8

  • 100g

  • 5033.0CNY

  • Detail
  • Alfa Aesar

  • (10861)  Sodium carbonate, anhydrous, Puratronic?, 99.997% (metals basis)   

  • 497-19-8

  • 500g

  • 22656.0CNY

  • Detail
  • Alfa Aesar

  • (33377)  Sodium carbonate, ACS primary standard, 99.95-100.05% (dried basis)   

  • 497-19-8

  • 100g

  • 307.0CNY

  • Detail
  • Alfa Aesar

  • (33377)  Sodium carbonate, ACS primary standard, 99.95-100.05% (dried basis)   

  • 497-19-8

  • 500g

  • 1163.0CNY

  • Detail
  • Alfa Aesar

  • (11552)  Sodium carbonate, anhydrous, ACS, 99.5% min   

  • 497-19-8

  • 50g

  • 347.0CNY

  • Detail
  • Alfa Aesar

  • (11552)  Sodium carbonate, anhydrous, ACS, 99.5% min   

  • 497-19-8

  • 500g

  • 464.0CNY

  • Detail
  • Alfa Aesar

  • (11552)  Sodium carbonate, anhydrous, ACS, 99.5% min   

  • 497-19-8

  • 2kg

  • 797.0CNY

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  • Alfa Aesar

  • (88617)  Sodium carbonate, Acculute Standard Volumetric Solution, Final Concentration 0.1N   

  • 497-19-8

  • 1unit

  • 466.0CNY

  • Detail
  • Alfa Aesar

  • (88617)  Sodium carbonate, Acculute Standard Volumetric Solution, Final Concentration 0.1N   

  • 497-19-8

  • 6units

  • 2619.0CNY

  • Detail
  • Alfa Aesar

  • (35609)  Sodium carbonate, 0.05N Standardized Solution   

  • 497-19-8

  • 1L

  • 252.0CNY

  • Detail

497-19-8Synthetic route

ammonium carbonate

ammonium carbonate

ammonia
7664-41-7

ammonia

sodium chloride
7647-14-5

sodium chloride

sodium carbonate
497-19-8

sodium carbonate

Conditions
ConditionsYield
In water NH3 passed into a soln. of (NH4)2CO3-NaCl until satn.; product free of Cl and NH3;100%
In water NH3 passed into a soln. of (NH4)2CO3-NaCl until satn.; product free of Cl and NH3;100%
Na2[B(CN)3]

Na2[B(CN)3]

water
7732-18-5

water

potassium carbonate
584-08-7

potassium carbonate

A

K[HB(CN)3]

K[HB(CN)3]

B

sodium carbonate
497-19-8

sodium carbonate

C

sodium hydroxide
1310-73-2

sodium hydroxide

Conditions
ConditionsYield
With tetrahydrofuranA 100%
B n/a
C n/a
Glauber's salt

Glauber's salt

carbon monoxide
201230-82-2

carbon monoxide

hydrogen
1333-74-0

hydrogen

A

hydrogen sulfide
7783-06-4

hydrogen sulfide

B

water
7732-18-5

water

C

sodium carbonate
497-19-8

sodium carbonate

Conditions
ConditionsYield
with molten Na2SO4*10H2O; heating at 927 to 983°C for 2 h; ratio of CO and H2 1:3;A 98%
B n/a
C n/a
carbon monoxide
201230-82-2

carbon monoxide

water
7732-18-5

water

sodium sulfate
7757-82-6

sodium sulfate

sodium carbonate
497-19-8

sodium carbonate

Conditions
ConditionsYield
iron(III) oxide In neat (no solvent) passing a mixture of CO/H2O-vapor over powdered Na2SO4 at 660°C; partial pressure of H2O: 0.3 at, catalyst: Fe2O3 in form of a Fe(NO3)2-soln.;; 85-92% Na2CO3;;97%
With catalyst: Fe2O3 and Sb2O5 or Fe2O3 and Sb2O4 or; Fe2O3 and As2O5 In neat (no solvent) passing a mixture of CO/H2O-vapor (CO from passing air through hot charcoal) over Na2SO4; partial pressure of H2O: 0.4 at, gas, containing 14.6% CO, is applied in 1.5-fold excess; catalyst: mixture of Fe2O3 and Sb2O5, Sb2O4 or As2O5;; 88.5% Na2CO3;;93.8%
With catalyst: Fe2O3 and Sb2O5 or Fe2O3 and Sb2O4 or; Fe2O3 and As2O5 In neat (no solvent) passing a mixture of CO/H2O-vapor (CO from passing air through hot charcoal) over Na2SO4, partial pressure of H2O: 0.4 at, catalyst :mixture of Fe2O3 and Sb2O5, Sb2O4 or As2O5;; 91.3-95.6% Na2CO3;;94-97.6
N-Cyanoguanidine
127099-85-8, 780722-26-1

N-Cyanoguanidine

sodium hydroxide
1310-73-2

sodium hydroxide

A

disodium cyanamide

disodium cyanamide

B

sodium carbonate
497-19-8

sodium carbonate

Conditions
ConditionsYield
after V. A. Shushunov and A. M. Pavlov, Dokl. Akad. Nauk SSSR, 89, 1033(1953);A 95%
B 5%
disodium tetracarbonylferrate

disodium tetracarbonylferrate

carbon dioxide
124-38-9

carbon dioxide

iron pentacarbonyl
13463-40-6

iron pentacarbonyl

B

sodium carbonate
497-19-8

sodium carbonate

Conditions
ConditionsYield
In tetrahydrofuran reductive disproportionation, mechanism discussed;; IR; iron carbonyl not isolated;;A 82%
B 94%
sodium formate
141-53-7

sodium formate

A

sodium oxalate
62-76-0

sodium oxalate

B

sodium carbonate
497-19-8

sodium carbonate

Conditions
ConditionsYield
sodium hydroxide In solid byproducts: H2; with NaOH (1:0.05) in N2 atmosphere, the heating rate 6 deg/min;A 92%
B n/a
In solid thermal decomposition of sodium formate in H2 atmosphere (TG at 435 :degree.C, the heating rate 6 deg/min;A 35%
B n/a
In solid thermal decomposition of sodium formate in CO atmosphere (TG at438 °C), the heating rate 6 deg/min;A 34%
B n/a
disodium tetracarbonylosmate

disodium tetracarbonylosmate

carbon dioxide
124-38-9

carbon dioxide

iodine
7553-56-2

iodine

cis-Os(CO)4(I)2
17632-05-2

cis-Os(CO)4(I)2

B

sodium carbonate
497-19-8

sodium carbonate

Conditions
ConditionsYield
In tetrahydrofuran addn. of CO2 to suspension of Na2(Os(CO)4) in THF, filtn. onto I2 at 4°C;; pptg. of carbonate; soln.: removal of solvent (IR), sublimation off excess I2, extn. into toluene and concg. under vacuum;;A 61%
B 92%
(R)-phenylglycine
875-74-1

(R)-phenylglycine

methyl chloroformate
79-22-1

methyl chloroformate

sodium carbonate
497-19-8

sodium carbonate

Conditions
ConditionsYield
With sodium hydroxide In water at 0℃; for 1h;91%
carbon dioxide
124-38-9

carbon dioxide

sodium carbonate
497-19-8

sodium carbonate

Conditions
ConditionsYield
With [(1,1,4,7,10,10-hexamethyltriethylenetetramine)(Fe(NO)2)2]; sodium In tetrahydrofuran at 20℃; under 760.051 Torr; for 72h; Glovebox; Inert atmosphere; Sealed tube;90%
With Na-silicate In water introduction of CO2 into the aq. soln.;;
With Na-aryl sulfonate In further solvent(s) byproducts: aryl sulfonic acid ester; dissolving Na-aryl sulfonate (from aryl sulfonic acid and NaCl) in an alcohol, introduction of CO2-gas;;
sodium sulfate
7757-82-6

sodium sulfate

barium carbonate

barium carbonate

sodium carbonate
497-19-8

sodium carbonate

Conditions
ConditionsYield
In water byproducts: BaSO4; wt.-ratio Na2SO4:BaCO3=5:11, 7h. at 33.+-.1°C;;88.97%
With Ba(HCO3)2 In not given reaction of a soln. of BaCO3 with Na2SO4; complete reaction by addition of a small amount of Ba(HCO3)2;;
sodium tetrahydroborate
16940-66-2

sodium tetrahydroborate

sodium formate
141-53-7

sodium formate

A

sodium oxalate
62-76-0

sodium oxalate

B

sodium carbonate
497-19-8

sodium carbonate

Conditions
ConditionsYield
In solid reaction of sodium formate with NaBH4 (1:0.05) in N2 atmosphere, the heating rate 6 deg/min;A 88%
B n/a
In solid reaction of sodium formate with NaBH4 (1:1) in N2 atmosphere, the heating rate 6 deg/min;A 0%
B n/a
sodium sulfate
7757-82-6

sodium sulfate

calcium carbonate

calcium carbonate

sodium carbonate
497-19-8

sodium carbonate

Conditions
ConditionsYield
With pyrographite In neat (no solvent) Leblanc process: heating; Na2SO4:CaCO3:C=100:100:75;;88%
In melt0%
In water Electrolysis; electrolysis of Na2SO4 soln. with an inert anode covered with a layer of insoluble CaCO3; reaction of CaCO3 with formed H2SO4 forming CO2; reaction of CO2 with NaOH formed in the cathod region;;
In melt0%
In water
2Na(1+)*W(CO)5(2-) = Na2[W(CO)5]
54099-82-0

2Na(1+)*W(CO)5(2-) = Na2[W(CO)5]

carbon dioxide
124-38-9

carbon dioxide

A

tungsten hexacarbonyl
14040-11-0

tungsten hexacarbonyl

B

sodium carbonate
497-19-8

sodium carbonate

Conditions
ConditionsYield
In tetrahydrofuran reductive disproportionation; mechanism discussed;; IR;;A 83%
B n/a
In tetrahydrofuran soln. of the W-compound was treated with gasous CO2 at -78°C, warmed to 25°C; solvent removed (vac.), extd. (diethyl ether), ether removed (vac.); IR, MAS;A 83%
B n/a
sodium tetracarbonylruthenate(II)

sodium tetracarbonylruthenate(II)

carbon dioxide
124-38-9

carbon dioxide

iodine
7553-56-2

iodine

B

sodium carbonate
497-19-8

sodium carbonate

Conditions
ConditionsYield
In tetrahydrofuran bubbling of excess CO2 through a suspension of Na2(Ru(CO)4) in THF (stirred 20min, 4°C), filtration of soln. onto I2 at 4°C;; pptg. of carbonate; soln.: removal of solvent (IR), sublimation off of excess iodine, extn. with THF;;A 73%
B 61%
2Na(1+)*{V(C5H5)(CO)3}(2-)*C4H8O=Na2{V(C5H5)(CO)3}*C4H8O

2Na(1+)*{V(C5H5)(CO)3}(2-)*C4H8O=Na2{V(C5H5)(CO)3}*C4H8O

carbon dioxide
124-38-9

carbon dioxide

A

tetracarbonyl(η(5)-cyclopentadienyl)vanadium(I)

tetracarbonyl(η(5)-cyclopentadienyl)vanadium(I)

B

sodium carbonate
497-19-8

sodium carbonate

Conditions
ConditionsYield
In tetrahydrofuran bubbling of gaseous CO2 through suspension of corresponding carbonyl complex in THF for 5min at room temp.;; IR; removal of excess CO2 under vacuum, concg., extraction with pentane, concg. under reduced pressure; pentane insol. ppt.: carbonate;;A 67%
B 57%
sodium hexaflorophosphate

sodium hexaflorophosphate

[Fe(η5-cyclopentadienyl)(η-benzene)]

[Fe(η5-cyclopentadienyl)(η-benzene)]

carbon dioxide
124-38-9

carbon dioxide

trimethylphosphane
594-09-2

trimethylphosphane

A

{Fe(cp)(PMe3)3}(PF6)

{Fe(cp)(PMe3)3}(PF6)

B

{Fe(cp)(PMe3)2CO}(PF6)

{Fe(cp)(PMe3)2CO}(PF6)

C

sodium carbonate
497-19-8

sodium carbonate

Conditions
ConditionsYield
CO2 reacts with (Fe(cp)(C6H6)) (1 atm, 0°C) in presence of PMe3 and NaPF6 to (Fe(cp)(PMe3)3)PF6;A 66%
B 33%
C n/a
selenium
7782-49-2

selenium

A

sodium selenate

sodium selenate

B

sodium carbonate
497-19-8

sodium carbonate

C

sodium hydroxide
1310-73-2

sodium hydroxide

Conditions
ConditionsYield
With sodium peroxide In neat (no solvent) byproducts: Na2SO4; oxidation of Se on melting with Na2O2in a Ni crucible;; the formed melt contains NaOH and Na2CO3; isolation as mixture of Na2SeO4 and Na2SO4;;A 58%
B n/a
C n/a
With Na2O2 In neat (no solvent) byproducts: Na2SO4; oxidation of Se on melting with Na2O2in a Ni crucible;; the formed melt contains NaOH and Na2CO3; isolation as mixture of Na2SeO4 and Na2SO4;;A 58%
B n/a
C n/a
sodium acetate
127-09-3

sodium acetate

A

sodium carbonate
497-19-8

sodium carbonate

B

pyrographite
7440-44-0

pyrographite

C

acetone
67-64-1

acetone

Conditions
ConditionsYield
In neat (no solvent) decomposition at 390°C, formation of acetone, Na2CO3 and traces of C between 410 and 450°C while distilling;;A n/a
B <1
C 53%
In neat (no solvent) decomposition at 390°C, formation of acetone, Na2CO3 and traces of C between 410 and 450°C while distilling;;A n/a
B <1
C 53%
sodium formate
141-53-7

sodium formate

lithium hydroxide
1310-65-2

lithium hydroxide

A

sodium oxalate
62-76-0

sodium oxalate

B

sodium carbonate
497-19-8

sodium carbonate

Conditions
ConditionsYield
In solid byproducts: H2; reaction of sodium formate with LiOH (1:0.05) in N2 atmosphere, the heating rate 6 deg/min;A 49%
B n/a
dinatriumdecacarbonylwolframate

dinatriumdecacarbonylwolframate

A

triphenylphosphine tungsten pentacarbonyl
15444-65-2

triphenylphosphine tungsten pentacarbonyl

B

sodium formate
141-53-7

sodium formate

C

sodium hydrogencarbonate
144-55-8

sodium hydrogencarbonate

D

sodium carbonate
497-19-8

sodium carbonate

Conditions
ConditionsYield
With carbon dioxide; triphenylphosphine In acetonitrile Irradiation (UV/VIS); (Ar or N2); UV irradn. (>420 nm) of soln. of W compd. and PPh3 with stirring at ca. 20°C for ca. 12 h under CO2 pressure, formed ppt. was sepd.; W(CO)5PPh3 was detected IR spect. in filtrate, not isolated; NaHCOO detected 1HNMR spect. in D2O soln. of ppt.; Na2CO3 and NaHCO3 detd. in aq. soln. of ppt. by titrn.;A 70-90
B 20%
C 18%
D 39%
Na(1+)*H(1+)*W2(CO)10(2-)=NaHW2(CO)10

Na(1+)*H(1+)*W2(CO)10(2-)=NaHW2(CO)10

A

triphenylphosphine tungsten pentacarbonyl
15444-65-2

triphenylphosphine tungsten pentacarbonyl

trans-triphenylphosphane tetracarbonyltungsten
16743-03-6, 38800-77-0, 68738-00-1

trans-triphenylphosphane tetracarbonyltungsten

C

sodium formate
141-53-7

sodium formate

D

sodium hydrogencarbonate
144-55-8

sodium hydrogencarbonate

E

sodium carbonate
497-19-8

sodium carbonate

Conditions
ConditionsYield
With carbon dioxide; triphenylphosphine In acetonitrile Irradiation (UV/VIS); (Ar or N2); UV irradn. (>420 nm) of soln. of W compd. and PPh3 with stirring at ca. 20°C for ca. 12 h under CO2 pressure, formed ppt. was sepd.; W compds. were detected IR spect. in filtrate, not isolated; NaHCOO detected 1HNMR spect. in D2O soln. of ppt.; Na2CO3 and NaHCO3 detd. in aq. soln. of ppt. by titrn.;A n/a
B n/a
C 30%
D 29%
E 27%
ammonia
7664-41-7

ammonia

amino-guanidine; compound with copper (II)-nitrate

amino-guanidine; compound with copper (II)-nitrate

sodium carbonate
497-19-8

sodium carbonate

water
7732-18-5

water

copper(II) methylsalicylate dihydrate

copper(II) methylsalicylate dihydrate

A

sodium carbonate
497-19-8

sodium carbonate

B

methyl salicylate
119-36-8

methyl salicylate

C

copper hydroxide

copper hydroxide

Conditions
ConditionsYield
Hydrolysis;
edetate disodium
139-33-3

edetate disodium

A

carbon dioxide
124-38-9

carbon dioxide

B

sodium carbonate
497-19-8

sodium carbonate

C

NaNO3

NaNO3

Conditions
ConditionsYield
With ozone at 20℃; Mechanism; Rate constant; Thermodynamic data; variation in pH, acidity of solution, and temperature; activation energy;
alpha-D-glucopyranose
492-62-6

alpha-D-glucopyranose

A

ethanol
64-17-5

ethanol

C

sodium carbonate
497-19-8

sodium carbonate

D

sodium lactate
312-85-6

sodium lactate

Conditions
ConditionsYield
With sodium hydroxide at 145℃; for 1h; Product distribution;
sodium L-(+)-lactate

sodium L-(+)-lactate

A

ethanol
64-17-5

ethanol

B

sodium carbonate
497-19-8

sodium carbonate

C

sodium lactate
312-85-6

sodium lactate

Conditions
ConditionsYield
With sodium hydroxide at 145℃; for 1h; Product distribution;
1-13C-sodium-L-lactate

1-13C-sodium-L-lactate

A

ethanol
64-17-5

ethanol

B

sodium carbonate
497-19-8

sodium carbonate

C

sodium lactate
312-85-6

sodium lactate

Conditions
ConditionsYield
With sodium hydroxide at 145℃; for 1h; Product distribution;

497-19-8Relevant articles and documents

Deshpande, D. A.,Ghormare, K. R.,Jawadekar, V. L.,Deshpande, N. D.

, p. 295 - 302 (1983)

Thermal decomposition of NaHCO3 powders and single crystals. A study by DSC and optical microscopy

Guarini, G. G. T.,Dei, L.,Sarti, G.

, p. 31 - 44 (1995)

The thermal decomposition of four commercial powders and of differently stored single crystals of sodium hydrogen carbonate is studied by power compensation DSC and by optical and FT-IR microscopy. Independently of manufacturer, specified purity and price, the thermal curves of all the commercial powders show a more or less pronounced low temperature peak preceding the one due to the main decomposition. Such small peak is not observed when samples of laboratory recrystallized material are used. However the thermal behaviour of the latter preparation differs remarkably depending on storage conditions: the material kept in closed glass containers decomposes at temperatures higher than those of the material stored in a desiccator in the presence of concentrated H2SO4. The observation by optical microscopy of the behaviour of the surfaces of single crystals coming from different storage conditions when the temperature is raised in a Kofler heater helps the interpretation of the data collected. The mechanism of the decomposition is discussed and the relevant kinetic parameters reported.

Waldbauer, L.,McCann, D. C.,Tuleen, L. F.

, p. 336 - 337 (1934)

Interaction of graphite with hydroxide-salt melts

Zarubitskii,Dmitruk,Zakharchenko

, p. 525 - 528 (2006)

The mechanism and kinetics of graphite dissolution in melts based on sodium hydroxide were studied. The effect of various salt additives on the intensity of the occurring reactions is considered. A method recommended for removal of graphite in the form of remainders of molds and mold cores from titanium casts is described. Pleiades Publishing, Inc., 2006.

Smith, G. F.,Croad, F.

, p. 141 - 142 (1937)

Kinetic studies on the thermal decomposition of aluminium doped sodium oxalate under isothermal conditions

Jose John,Muraleedharan,Kannan,Abdul Mujeeb,Ganga Devi

, p. 64 - 70 (2012)

The kinetics of thermal decomposition of sodium oxalate (Na 2C2O4) has been studied as a function of concentration of dopant, aluminium, at five different temperatures in the range 783-803 K under isothermal conditions by thermogravimetry (TG). The TG data were subjected to both model fitting and model free kinetic methods of analysis. The model fitting analysis of the TG data shows that no single kinetic model describes the whole α versus t curve with a single rate constant throughout the decomposition reaction. Separate kinetic analysis shows that Prout-Tompkins model best describes the acceleratory stage of the decomposition while the decay region is best fitted with the contracting cylinder model. Activation energy values were evaluated by model fitting and model free kinetic methods for both stages of decomposition. As proposed earlier the results favours a diffusion controlled mechanism for the isothermal decomposition of sodium oxalate.

Quantitative kinetic and structural analysis of geopolymers. Part 1. the activation of metakaolin with sodium hydroxide

Zhang, Zuhua,Wang, Hao,Provis, John L.,Bullen, Frank,Reid, Andrew,Zhu, Yingcan

, p. 23 - 33 (2012)

Isothermal conduction calorimetry (ICC) is used here to measure the kinetics of geopolymerisation of metakaolin by reaction with NaOH solution under a variety of conditions. Three exothermic peaks are observed in the calorimetric curve, and are assigned to the dissolution of metakaolin, the formation of geopolymer with disordered or locally ordered structure, and finally the reorganization and partial crystallization of this inorganic polymer gels. For the purpose of further quantifying the ICC data, the geopolymeric reaction products are assumed to have an analcime-like local structure, and their standard formation enthalpies are estimated from the available data for this structure. This assumption enables ICC to be used for the first time in a quantitative manner to determine the real reaction kinetics of geopolymerization. Increasing the NaOH concentration up to a molar overall Na/Al ratio of 1.1 is seen to enhance the reaction extent observed at 3 days, up to a maximum of around 40% in the high liquid/solid ratio systems studied here, and accelerates the crystallization process. However, further addition of NaOH does not give any additional reaction within this period, or any further acceleration. Raising the reaction temperature from 25 °C to 40°C increases the initial reaction rate but has little effect on the final reaction extent, particularly when Na/Al > 1.

Thermal Decomposition of Solid Sodium Bicarbonate

Ball, Matthew C.,Snelling, Christine M.,Strachan, Alec N.,Strachan, Rebecca M.

, p. 3709 - 3716 (1986)

The thermal decomposition of solid sodium bicarbonate has been studied in the temperature range 360-500 K over a range of partial pressures of carbon dioxide.The effect of water vapour has also been studied.Above 440 K the reaction follows contracting-cube kinetics with an activation energy of 32 kJ mol-1 and a frequency factor of 101 s-1.In this temperature range the presence of water or carbon dioxide has little effect on the kinetics.Below 390 K the reaction follows first-order kinetics.In nitrogen, the activation energy is ca. 64 kJ mol-1, the frequency factor is 105 s-1 and water vapour has little effect.High partial pressures of carbon dioxide increase the activation energy to ca. 130 kJ mol-1 and the frequency factor to 1013.5 s-1.The results of microscopic examination generally confirm the kinetics but show that at low temperatures in nitrogen and carbon dioxide the process are different in detail.

Synthesis, spectroscopy, single crystal XRD and biological studies of multinuclear organotin dicarboxylates

Hussain, Shabbir,Ali, Saqib,Shahzadi, Saira,Tahir, Muhammad Nawaz,Shahid, Muhammad,Munawar, Khurram Shahzad,Abbas, Syed Mustansar

, p. 64 - 72 (2016)

Multinuclear organotin(IV) dicarboxylates of the general formula (Me3Sn)2L·H2O (1), (Ph3Sn)2L (2) and Me2SnL[Sn(Cl)2Me2]2 (3) were synthesized by refluxing disodium iminodiacetate hydrate (Na2L·H2O) with Me3SnCl/Ph3SnCl/Me2SnCl2 in methanol. The elemental analysis (C, H and N) data agreed well with the chemical compositions of the products. IR spectroscopy demonstrated a bridging coordination mode of the carboxylate group. 1H NMR spectroscopy suggested a penta-coordinated environment around the tin(IV) center in complexes 1 and 3. The title complex 3 represents one of the very few examples of organotin(IV) carboxylates showing simultaneously coordination with dimethyltin(IV) as well as dichlorodimethyltin(IV) moieties, by substitution and addition reactions, respectively. The 13C NMR spectroscopy demonstrated the carboxylate-metal linkages. EIMS and ESI spectra verified the molecular skeletons of the products 1-3. Thermogravimetric analysis revealed the bimetallic nature of 2. A single crystal XRD study of 3 has shown a predominantly square pyramidal geometry with some trigonal bipyramidal characteristics around each metal center. The novel products exhibited antibacterial/antifungal potential and their minimal inhibitory concentrations (MIC) were also evaluated. In vitro hemolytic studies on human red blood cells indicated a slightly toxic nature of the synthesized complexes.

Fry, H. S.,Schulze, E. L.

, p. 1131 - 1138 (1928)

Easterbrook, W. C.

, p. 383 - 390 (1957)

Tanaka, H.

, p. 521 - 526 (1987)

PbTe nanostructures: Microwave-assisted synthesis by using lead Schiff-base precursor, characterization and formation mechanism

Ahmadian-Fard-Fini, Shahla,Salavati-Niasari, Masoud,Monfared, Azam,Mohandes, Fatemeh

, p. 778 - 788 (2013)

Pure cubic phase lead telluride (PbTe) nanostructures have been produced by using a Schiff-base complex as a precursor in the presence of microwave irradiation. The Schiff base used as ligand was derived from salicylaldehyde and ethylenediamine. The Schiff-base complex was marked as [Pb(salen)]. In addition, the effect of the irradiation time and the type of reducing agent on the morphology and purity of the final products was investigated. The as-synthesized PbTe nanostructures were characterized extensively by techniques like X-ray powder diffraction (XRD), transmission electron microscopy (TEM), and scanning electron microscopy (SEM). The microwave formation mechanism of the PbTe nanostructures was studied by XRD patterns of the products. Although it was found that both ionic and atomic mechanisms could take place for the preparation of PbTe, the main steps were according to the atomic reaction process, which could occur between elemental Pb and Te.

Gorski, A.,Krasnicka, A. D.

, p. 1895 - 1904 (1987)

Worm

, p. 688 - 688 (1897)

Duval, C.,Wadier, C.,Servigne, Y.

, p. 263 - 267 (1959)

Thermal decomposition of copper(II) and zinc carbonate hydroxides by means of TG-MS: Quantitative analyses of evolved gases

Koga,Tanaka

, p. 725 - 729 (2005)

For the quantitative analyses of evolved CO2and H2O during the thermal decomposition of solids, calibration curves, i.e. the amounts of evolved gases vs. the corresponding peak areas of mass chromatograms measured by TG-MS, were plot

The hidden equilibrium in aqueous sodium carbonate solutions - Evidence for the formation of the dicarbonate anion

Zeller, Klaus-Peter,Schuler, Paul,Haiss, Peter

, p. 168 - 172 (2005)

Crossover 13C NMR experiments between [13C]carbonate and [18O]carbonate in aqueous solution confirm the combined action of two oxygen-exchange modes. The isotopomeric carbon dioxides formed in the hydrolysis equilibrium of

Marotta, A.,Saiello, S.,Buri, A.

, p. 193 - 198 (1982)

Thermal Decomposition of Solid Sodium Sesquicarbonate, Na2CO3*NaHCO3*2H2O

Ball, Matthew C.,Snelling, Christine M.,Strachan, Alec N.,Strachan, Rebecca M.

, p. 631 - 636 (1992)

The thermal decomposition of solid sodium sesquicarbonate has been studied at temperatures between 350 and 487 K in nitrogen and carbon dioxide atmospheres.In nitrogen, a single-stage decomposition to sodium carbonate occurs, following Avrami-Erofeyev kinetics (n = 2), with an inflexion at ca. 390 K.The activation energies are 24 kJ mol-1 for the high-temperature region and 58 kJ mol-1 for the low-temperature region.In carbon dioxide above 435 K, the single-stage reaction follows contracting disc kinetics with an activation energy of 29 kJ mol-1.In carbon dioxide at low temperatures, wegscheiderite (Na2CO3*3NaHCO3) and sodium carbonate monohydrate (Na2CO3*H2O) are formed, and this reaction follows first-order kinetics, withb an activation energy of 67 kJ mol-1.Microscopic evidence is also presented.Relationships between the decomposition of sesquicarbonate and other related compounds are discussed.

Galwey, Andrew Knox,Hood, William John

, p. 1810 - 1816 (1979)

Fire retardancy impact of sodium bicarbonate on ligno-cellulosic materials

Bakirtzis,Delichatsios,Liodakis,Ahmed

, p. 11 - 19 (2009)

In this paper, the effect of NaHCO3 as fire retardant additive during pyrolysis and combustion has been investigated. Four different contents (5%, 10%, 15%, and 20% w/w) of NaHCO3 have been tested on Pinus brutia, Laurus nobilis and

Features of the Thermolysis of Li, Na, and Cd Maleates

Avdin, V. V.,Merzlov, S. V.,Nayfert, S. A.,Polozov, M. A.,Polozova, V. V.,Sakthi Dharan, C. P.,Taskaev, S. V.,Zherebtsov, D. A.

, p. 1311 - 1318 (2020/07/21)

Abstract: Processes of the multi-stage decomposition of maleic acid and Li, Na, and Cd maleates in an inert atmosphere are studied via thermal analysis with synchronous analysis of the composition of the released gases. Reaction mechanisms are proposed according to the data on the mass loss stages determined via thermal analysis, gaseous products, and the final solid decomposition products. It is shown that when heated to 700°C, Li and Na carbonates incorporated into the porous carbon matrix are the final products. Above 350°C, cadmium is reduced from oxide to metal and evaporates to form a porous carbon residue as the only product of thermolysis. All carbon products are X-ray amorphous. Maleic acid decomposes completely into gaseous products in the range of 133–239°C. The maleate ion is more stable in the structure of lithium maleate than in free maleic acid, and Na and Cd cations reduce its stability.

METHOD FOR PRODUCING METAL CARBONATE AND CATALYST FOR PRODUCING THE SAME

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Paragraph 0023; 0024, (2017/08/26)

A method for producing metal carbonate is disclosed. The method includes the following steps of providing a first mixture of metal and a catalyst containing iron, NO groups, and N-containing ligands first; then introducing carbon dioxide to the first mixture to form a second mixture and obtaining a product. The method described here can improve the yield and decrease the cost of metal carbonate production.

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