Conditions | Yield |
---|---|
In water stirring Ca(OH)2-milk with Na2CO3-lye at 35°C with a turbo-mixer;; | A n/a B 96% |
In water byproducts: Na2CO3*10H2O; caustification of concd. Na2CO3 lye with Ca(OH)2; cooling down to 0 to -15°C by pptn. of Na2CO3*10H2O;; lye containing 15 - 25% NaOH and not more than 1% Na2CO3;; | |
In water PARNELL process;; |
Conditions | Yield |
---|---|
With clay; sodium carbonate In water byproducts: NaAlO2; reaction of bricks of NaCl and clay with hot gases and overheated vapor in a shaft furnace; melting residue (acidic sodium silicon aluminate) with Na2CO3; product leached with water;; NaOH contains some Na2CO3 and NaAlO2;; | 90% |
With clay; sodium carbonate In water byproducts: NaAlO2; reaction of bricks of NaCl and clay with hot gases and overheated vapor in a shaft furnace; melting residue (acidic sodium silicon aluminate) with Na2CO3; product leached with water;; NaOH contains some Na2CO3 and NaAlO2;; | 90% |
With water byproducts: HCl; H2O steam; 1000°C; |
Conditions | Yield |
---|---|
In neat (no solvent) reaction with steam gives 6% conversion in 1.5 h and 12.6% in 12 h;; | |
silica gel In neat (no solvent) byproducts: HCl; at 810°C;; | |
Electrolysis; electrolysis of moist NaCl;; |
water
potassium carbonate
B
sodium carbonate
C
sodium hydroxide
Conditions | Yield |
---|---|
With tetrahydrofuran | A 100% B n/a C n/a |
Conditions | Yield |
---|---|
With lead(II) oxide In water byproducts: basic lead chlorides; repeated grinding NaCl with PbO, Ca(OH)2 and a small amount of H2O;; evapn. of lye and sucking off pptd. NaCl; recycling basic lead chlorides (by heating to 170°C with boiling Ca(OH)2 soln. to form PbO);; | 50% |
In water at ambient temp., equilibrium;; | 3% |
With Ca-aluminate or bauxite In water byproducts: Ca-chloroaluminate; autoclave or 100°C, increase of yield with bauxite or Ca-aluminate;; |
Conditions | Yield |
---|---|
With H2O In water hydrolysis equilibrium investigated;; |
Conditions | Yield |
---|---|
With hydroxide In neat (no solvent) redn. with C or P and a hydroxide of the second-row elements by heating;; | |
With H2 or H2/N2; nickel In neat (no solvent) byproducts: NH3; treatment with H2 or H2/N2-mixture at 100-800°C in presence of a catalyst; increase of yield with increase of H2-pressure;; | |
With H2 or H2/N2; copper In neat (no solvent) byproducts: NH3; treatment with H2 or H2/N2-mixture at 100-800°C in presence of a catalyst; increase of yield with increase of H2-pressure;; |
Conditions | Yield |
---|---|
With barium carbonate at 100℃; for 5h; |
Conditions | Yield |
---|---|
In water Electrolysis; electrolysis of a Na2CO3 soln. in the cold with Hg cathode; decompn. of formed amalgam in paraffined tube in presence of CO2-free air and Pt with dest. H2O;; | |
at 800°C; equiv. content 97.5% Na2CO3, 2.5% NaOH; | |
In water Electrolysis; electrolysis of a concd. Na2CO3-soln., Hg-cathode, react. of the generated Na-amalgame with H2O, evapn. in vac. over H2SO4 at ambinet temp., dehydration of NaOH*H2o in vac. or in a dry N2-stream at 200-300°C;; pure NaOH; Na2CO3-content: 0.015-0.04%, H2O-content <0.1%;; | |
In neat (no solvent) reaction of Na2CO3 with H2O-vapor;; | |
at 800°C; equiv. content 97.5% Na2CO3, 2.5% NaOH; |
Conditions | Yield |
---|---|
In neat (no solvent) adding at 175°C powdered NaNO3 to cautiously heated pure NaNH2 in Ni crucible;; | A 65.7% B n/a C n/a |
In neat (no solvent) adding at 175°C powdered NaNO3 to cautiously heated pure NaNH2 in Ni crucible;; | A 65.7% B n/a C n/a |
Conditions | Yield |
---|---|
With oxygen In not given byproducts: NH3; | |
With O2 In not given byproducts: NH3; |
Conditions | Yield |
---|---|
In water byproducts: BaSO4; cyclic process: reduction of BaSO4 to BaS, regeneration of Ba(OH)2 on boiling with H2O; 30% Na2SO4-soln., 3% excess Ba(OH)2;; 18% NaOH-soln.;; | 75% |
In water byproducts: BaSO4; cyclic process: reduction of BaSO4 to BaS, regeneration of Ba(OH)2 on boiling with H2O; 40% Na2SO4-soln., 3% excess Ba(OH)2;; 27% NaOH-soln.;; | 70% |
In water byproducts: BaSO4; |
Conditions | Yield |
---|---|
With H2 In neat (no solvent) quantitative react. at 700-900°C;; | |
With H2 In neat (no solvent) quantitative react. at 700-900°C;; |
Conditions | Yield |
---|---|
With ammonia In not given ammonolysis of Na2O;; | |
With NH3 In not given ammonolysis of Na2O;; |
Conditions | Yield |
---|---|
With oxygen In ammonia in presence of NH4Br;; | |
With O2 In ammonia NH3 (liquid); in presence of NH4Br;; |
Conditions | Yield |
---|---|
With air In neat (no solvent) in moist air after a longer period of time;; | |
With air In neat (no solvent) in moist air after a longer period of time;; |
Conditions | Yield |
---|---|
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 |
Conditions | Yield |
---|---|
With water In water decompn.;; | |
With H2O In water decompn.;; |
Conditions | Yield |
---|---|
With H2 or H2/N2; iron In neat (no solvent) byproducts: NH3; treatment with H2 or H2/N2-mixture at 100-800°C in presence of a catalyst; increase of yield with increase of H2-pressure;; | |
With H2 or H2/N2; nickel In neat (no solvent) byproducts: NH3; treatment with H2 or H2/N2-mixture at 100-800°C in presence of a catalyst; increase of yield with increase of H2-pressure;; | |
With H2 or H2/N2; copper In neat (no solvent) byproducts: NH3; treatment with H2 or H2/N2-mixture at 100-800°C in presence of a catalyst; increase of yield with increase of H2-pressure;; |
Conditions | Yield |
---|---|
In water Electrolysis; formation of PbSO4 on Pb-anode; electrolysis of PbSO4; | A 91% B 91% |
With H2O Electrolysis; | |
In water Electrolysis; |
Conditions | Yield |
---|---|
In not given react. of Ba(OH)2 lye with Na2SO4;; reprocessing of BaSO4;; | |
In not given dissolving recrystallized Na2SO4; addition of the soln. to a soln. of recrystallizaed Ba(OH)2;; filtration of fromed BaSO4; crystn. of NaOH on evaporating;; |
Conditions | Yield |
---|---|
In neat (no solvent) exothermic react., react. enthalpy given;; | |
In neat (no solvent) exothermic react., react. enthalpy given;; |
Conditions | Yield |
---|---|
With sodium nitrate absent of air; NaOH-melt; | |
With H2O(gas) In melt byproducts: HI(gas); hydrolytic equilibrium (1100 and 1200 K); emf control of cell with gaseous electrodes and molten salt mixt.; |
Conditions | Yield |
---|---|
With water; oxygen In melt Electrochem. Process; molten Na is used as anode on a layer of molten NaOH, the cathode is a metal covered with a layer of oxide by influence of oxygen, or which is covered by higher Mn-Oxides. Introduction of H2O vapor causes electrochemical formation of NaOH;; molten NaOH is continuously separated from the reaction mixture;; | |
With potassium hydroxide In neat (no solvent) byproducts: K; equilibrium;; | |
In not given |
Conditions | Yield |
---|---|
With methyllithium In water equilibrium of causticizing react. investigated;; | |
With iron(III) oxide In water byproducts: Fe(OH)3, CO2; heating of soda with metal oxide, especially Fe2O3; formation of CO2 and residue NaOH;; | |
With iron(III) oxide In water byproducts: Fe(OH)3; evaporation of Na2CO3 soln. with Fe2O3 to dryness; mixture heating to red heat (in revolving furnace); formation of CO2 and Na-ferrite, which is leached with cold and then with hot water; use of pptd. Fe(OH)3 as educt;; concd. NaOH (d=1.32 - 1.38);; |
Conditions | Yield |
---|---|
With iron oxide In water reaction with iron oxide in water;; | |
With water byproducts: H2S, O2; between 300 and 1400°C; | |
With sodium sulfide; silica gel In melt leaching out of melt;; |
Conditions | Yield |
---|---|
With manganese(IV) oxide; oxygen In water oxidation of aq. Na2S with MnO2 forming Na2S2O3, NaOH and Mn(OH)2; oxidation of Mn(OH)2 by O2 reprocessing MnO2;; | |
With oxygen In water oxidation of aq. Na2S on air forming Na2S2O3;; | |
With MnO2; O2 In water oxidation of aq. Na2S with MnO2 forming Na2S2O3, NaOH and Mn(OH)2; oxidation of Mn(OH)2 by O2 reprocessing MnO2;; | |
With O2 In water oxidation of aq. Na2S on air forming Na2S2O3;; |
sodium hydroxide
Conditions | Yield |
---|---|
With ZnO or Zn In potassium hydroxide byproducts: ZnS; Na2S was treated with alkaline soln. of ZnO or Zn, filtration of the hot soln., crystn. of NaOH from the filtrate;; | |
With Cu oxides | |
With Zn- or Sn- or Pb- or Ni- or Mn- or Cu- or; Fe-metallate In water treatment of Na2S with a Na-metallate;; thermal decompn. of the metal-sulfide in oxide and SO2;; |
sodium hydroxide
Conditions | Yield |
---|---|
With ammonia In neat (no solvent) byproducts: H2O, Na, N; careful heating, formation of NaNH2 and H2O, further heating to 200 - 300°C formation of NaOH and Na, N and H;; | |
With carbon monoxide; water In neat (no solvent) heating glass in a reductive flame: redn. of Na2O by CO, react. of Na with H2O;; | |
With water In water dissolving in H2O;; not isolated;; | |
With H2O In water dissolving in H2O;; not isolated;; | |
With NH3 In neat (no solvent) byproducts: H2O, Na, N; careful heating, formation of NaNH2 and H2O, further heating to 200 - 300°C formation of NaOH and Na, N and H;; |
Conditions | Yield |
---|---|
In water N2H4*H2O (80%) added to aq. soln. of NiCl2*6H2O (temp. increased to 65°C) under vigorous stirring, cooling to 50°C, aq. NaOH (50%)added (temp. increased to 54°C), 1 h; ppt. washed with water and dried at room temp. for 16 h; | 100% |
In water; ethylene glycol byproducts: N2, H2O; other Radiation; soln. of Ni compd. in ethylene glycol treated with hydrazine hydrate andNaOH under external magnetic field (0.13-0.35 T) with vigorous stirring , react at 60°C; pptd., septd., washed (ethanol), dried (vac., 40°C, 24 h), SEM, XRD; |
Conditions | Yield |
---|---|
In water pure SO2 is introduced into alkaline Na2S soln.; | A n/a B 100% |
Conditions | Yield |
---|---|
In water; isopropyl alcohol soln. of Ni salt added to hot soln. of NaOH at a rate of 100 drops/min at stirring within 1.5-2.0 h; i-PrOH added; mixt. stirred for 30 min at 80°C; ppt. washed (H2O); dried at 50°C; ground in agate mortar; | 100% |
In water pptn. by dropwise addn. of 0.5 M NaOH to aq. soln. of Ni salt; washed, dried at 130°C overnight; | |
In water soln. of Ni(NO3)2 in water was added to soln. of NaOH in water, stirring, pptn. of apple-green solid, stirring for 5 min.; filtration, washing with water, dried for 12 h at 80 ° C; |
Conditions | Yield |
---|---|
In sodium hydroxide High Pressure; 2 M Zn(NO3)2 neutralized with 2 M NaOH to pH 11; heated with microwave treatment (100°C, 15 psi, 2 min); solid sepd. (centrifugation), washed (deionized H2O, EtOH), dried; XRD; | 100% |
In sodium hydroxide Sonication; 2 M Zn(NO3)2 neutralized with 2 M NaOH to pH 12; heated with microwave treatment (100°C, 15 or 30 min); solid sepd. (centrifugation), washed (deionized H2O, EtOH), dried; XRD; | 99.7% |
In sodium hydroxide High Pressure; 2 M Zn(NO3)2 neutralized with 2 M NaOH to pH 12; heated with microwave treatment (100°C, 15 psi, 2 min); solid sepd. (centrifugation), washed (deionized H2O, EtOH), dried; XRD; | 98.3% |
Conditions | Yield |
---|---|
In water at ratio OH(1-):Cd(2+)=1.56; | 100% |
In water pptn.; | |
In water pptn.; |
Conditions | Yield |
---|---|
In sodium hydroxide heating in 8% NaOH solution; precipitate contents NaOH; a small amount of Zr phosphate remains in filtrate;; | 100% |
Conditions | Yield |
---|---|
In water filtration, titration (pH 5.5), crystn.; IR spectroscopy; | 100% |
dihydrogen peroxide
chlorine
sodium hydroxide
oxygen
B
sodium chloride
Conditions | Yield |
---|---|
In water H2O2 soln. poured onto porous glass plate within the singlet O2 generator (closed glass system, under Ar), spent liquid discarded into the lower flask, Cl2 (1-2 kPa) admitted, alkali soln. poured in, evolution of singlet O2 over a period of 12-16 min.; luminiscence spectroscopy, calorimetry; | A 100% B n/a |
Conditions | Yield |
---|---|
In sodium hydroxide aq. NaOH; dissolving 0.01mol Na4P4O12 in 85ml hot H2O, addn. of 0.02mol NaOH in a small amount of H2O after cooling, standing in vac. over H2SO4 at 40°C for 100h;; | 100% |
Conditions | Yield |
---|---|
In water High Pressure; soln. of NaOH added to soln. of HfOCl2*8H2O; heated in autoclave at 120°C for 792 h at pH 7 or for 24 h at pH 13; washed twice with water; dried at 60°C for 24 h; | 100% |
In water High Pressure; soln. of NaOH added to soln. of HfOCl2*8H2O; heated in autoclave at 90°C, 336 h, pH 9.5; washed twice with water; dried at 60°C for 24 h; | 78% |
sodium hydroxide
Conditions | Yield |
---|---|
In acetone byproducts: Mg(OH)2; addn. of an aq. soln. of NaOH to a soln. of ((Os(PhNNC(NO)CH3)3)2Mg) inacetone, stirring at 298 K for 0.5 h, color turns green; filtered from pptd. Mg(OH)2, evapn. (vac.), recrystn. from acetonitrile/water; | 100% |
Conditions | Yield |
---|---|
In sodium hydroxide aq. NaOH; High Pressure; mixt. of V2O3 and GeO2 in 1.05 M aq. NaOH in sealed OD silver tubes heated at 580°C in a Tuttle "cold sealed" autoclave for 3 d; | 100% |
sodium hydroxide
Conditions | Yield |
---|---|
In water Ar atm.; 1 N NaOH, 60°C, 1 h; | 100% |
sodium hydroxide
Conditions | Yield |
---|---|
In water stirring (48 h, pptn.), centrifugation; washing (water, centrifugation), drying in vacuum; elem. anal.; | 100% |
Triisopropyl borate
sodium hydroxide
N-(n-butyl)-2-(2-bromophenyl)-benzimidazole
Conditions | Yield |
---|---|
With tert.-butyl lithium In diethyl ether; pentane a soln. of benzimidazole-compound in ether at -78°C under Ar was treated with t-BuLi in pentane over 15 min, stirred at -78.degre.C for 1h, treated with B(Oi-Pr)3, stirred for 48 h, allowed to warm to room te mp., NaOH was added, stirred for 1 h; ppt. was filtered, washed with ether, dried; | 100% |
sodium hydroxide
Conditions | Yield |
---|---|
In water Ar atm.; 1 N NaOH, 60°C, 1 h; | 100% |
gadolinium(III) chloride
sodium hydroxide
Conditions | Yield |
---|---|
In water equimolar ratio Gd:ligand, pH 7, stirring; evapn. (vac.), drying (3 h, 200°C), ; elem. anal.; | 100% |
Conditions | Yield |
---|---|
In ethanol soln. of ZnCl2 (0.19 mmol) in EtOH added to soln. of ligand (0.08 mmol) and 0.3 ml 1M NaOH in EtOH; stirred for 75 min; ppt. filtered off; washed (EtOH); dried (vac., 56°C); elem. anal.; | 100% |
Conditions | Yield |
---|---|
In water at 100℃; for 72h; Autoclave; High pressure; | 100% |
Conditions | Yield |
---|---|
In methanol at 20℃; Darkness; | 100% |
uracil
sodium hydroxide
sodium pyrimidin-1-ide-2,4-dione
Conditions | Yield |
---|---|
In ethanol; water at 20℃; for 0.25h; | 100% |
Conditions | Yield |
---|---|
With polyethylene glycol 20,000 In water at 160℃; for 12h; Autoclave; Sealed tube; | 100% |
Conditions | Yield |
---|---|
at 80℃; for 18h; pH=8; | 100% |
sodium hydroxide
Na[Mn(N-tosyl-N',N",N"-diethylenetriaminetriacetate)]
Conditions | Yield |
---|---|
In water pH=6.4 - 6.6; | 100% |
4-vinyl(pyridine-2,6-diyl)bis(methyleneamino)-N,N,N',N'-tetrakis(acetic acid)
sodium hydroxide
Conditions | Yield |
---|---|
In water pH=7.2; | 100% |
sodium hydroxide
Conditions | Yield |
---|---|
Stage #1: gadolinium(III) chloride hexahydrate; C75H77N15O24Ru(2+)*2C2F3O2(1-) In water at 20℃; for 1h; Stage #2: sodium hydroxide In water at 20℃; for 18h; pH=5 - 6; | 100% |
sodium hydroxide
Conditions | Yield |
---|---|
Stage #1: europium(III) chloride hexahydrate; C75H77N15O24Ru(2+)*2C2F3O2(1-) In water at 20℃; for 1h; Stage #2: sodium hydroxide In water at 20℃; for 18h; pH=5 - 6; | 100% |
sodium hydroxide
Conditions | Yield |
---|---|
Stage #1: neodymium(III) chloride hexahydrate; C75H77N15O24Ru(2+)*2C2F3O2(1-) In water at 20℃; for 1h; Stage #2: sodium hydroxide In water at 20℃; for 18h; pH=5 - 6; | 100% |
sodium hydroxide
Conditions | Yield |
---|---|
Stage #1: ytterbium(III) chloride hexahydrate; C75H77N15O24Ru(2+)*2C2F3O2(1-) In water at 20℃; for 1h; Stage #2: sodium hydroxide In water at 20℃; for 18h; pH=5 - 6; | 100% |
Sodium hydroxide, with the CAS register number 1310-73-2, is also called as Lye and Caustic soda. The substance is white opaque crystals. It should be stored in a tightly closed container, and in a cool, dry, well-ventilated area away from incompatible substances. In addition,Sodium hydroxide should be kept away from metals, acids and moisture. Its containers must be tightly closed to prevent the conversion of NaOH to sodium carbonate by the CO2 in air. Sodium hydroxide is insoluble in ether and other non-polar solvents. It is very soluble in water with liberation of heat. Sodium hydroxide also can dissolve in ethanol and methanol, though it exhibits lower solubility in these solvents than does potassium hydroxide. It is hygroscopic which readily absorbs water from the air, so it should be stored in an airtight container.
Properties of Sodium hydroxide: Sodium hydroxide is predominantly ionic, containing sodium cations and hydroxide anions. The hydroxide anion makes Sodium hydroxide a strong base which reacts with acids, both organic and inorganic, to form water and the corresponding salts. Heating with a mixture of methyl alcohol and trichlorobenzene during an attempted synthesis, it will led to a sudden increase in pressure and an explosion. Sodium hydroxide will readily absorb moisture from the air to give caustic semi-solids that attacks aluminum and zinc with the evolution of flammable hydrogen gas.
Catalyzes the polymerization of acetaldehyde and other polymerizable compounds these reactions can occur violently, for example, acrolein polymerizes with extreme violence when put in contact with alkaline materials such as sodium hydroxide. Hot and concentrated NaOH can cause hydroquinone to decompose exothermically at elevated temperature.
Preparation of Sodium hydroxide: Of historic interest is the Leblanc process, which produced sodium carbonate, followed by roasting to create carbon dioxide and sodium oxide, which readily absorbs water to create Sodium hydroxide. Sodium hydroxide is produced along with chlorine and hydrogen via the chloralkali process. This involves the electrolysis of an aqueous solution of sodium chloride. The Sodium hydroxide builds up at the cathode, where water is reduced to hydrogen gas and hydroxide ion. The Cl– ions are oxidized to chlorine gas at the anode.
2 Na+Cl- + 2 H2O + 2 e- → H2 + 2 Cl- + 2 NaOH
Sodium hydroxide is industrially produced as a 50 % solution by variations of the electrolytic chloralkali process. Solid sodium hydroxide is obtained from this solution by the evaporation of water. Sodium hydroxide may be formed by the metathesis reaction between calcium hydroxide and sodium carbonate:
Ca(OH)2 + Na2CO3 → CaCO3 + 2 NaOH
Uses of Sodium hydroxide: 56 % of Sodium hydroxide produced is used by the chemical industry, with 25 % of the same total used by the paper industry. Sodium hydroxide is the principal strong base used in the chemical industry. It is used in many industries, mostly as a strong chemical base in the manufacture of pulp and paper, textiles, drinking water, soaps and detergents and as a drain cleaner, sodium salts and detergents, for pH regulation, and for organic synthesis. Sodium hydroxide is used in the Bayer process of aluminium production.
Food uses of Sodium hydroxide include washing or chemical peeling of fruits and vegetables, chocolate and cocoa processing, caramel coloring production, poultry scalding, soft drink processing, and thickening ice cream. Sodium hydroxide is frequently used as an industrial cleaning agent where it is often called "caustic". It is added to water, heated, and then used to clean the process equipment, storage tanks, etc. It can dissolve grease, oils, fats and protein based deposits. Sodium hydroxide is traditionally used in soap making. Sodium hydroxide is used in all sorts of scenarios where it is desirable to increase the alkalinity of a mixture, or to neutralize acids.
When you are using Sodium hydroxide please be cautious about it as the following: The substance may cause severe burns. It is also irritating to eyes and skin. In case of contact with eyes, you should rinse immediately with plenty of water and seek medical advice. And when you use it, you should wear suitable protective clothing, gloves and eye/face protection to avoid contact with skin and eyes. Moreover, in case of accident or if you feel unwell, you can seek medical advice immediately.
You can still convert the following datas into molecular structure:
(1)Canonical SMILES: [OH-].[Na+]
(2)InChI: InChI=1S/Na.H2O/h;1H2/q+1;/p-1
(3)InChIKey: HEMHJVSKTPXQMS-UHFFFAOYSA-M
The toxicity data of Sodium hydroxide is as follows:
Organism | Test Type | Route | Reported Dose (Normalized Dose) | Effect | Source |
---|---|---|---|---|---|
mouse | LD50 | intraperitoneal | 40mg/kg (40mg/kg) | Comptes Rendus Hebdomadaires des Seances, Academie des Sciences. Vol. 257, Pg. 791, 1963. | |
rabbit | LDLo | oral | 500mg/kg (500mg/kg) | Naunyn-Schmiedeberg's Archiv fuer Experimentelle Pathologie und Pharmakologie. Vol. 184, Pg. 587, 1937. |
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