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7697-37-2

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7697-37-2 Usage

Check Digit Verification of cas no

The CAS Registry Mumber 7697-37-2 includes 7 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 4 digits, 7,6,9 and 7 respectively; the second part has 2 digits, 3 and 7 respectively.
Calculate Digit Verification of CAS Registry Number 7697-37:
(6*7)+(5*6)+(4*9)+(3*7)+(2*3)+(1*7)=142
142 % 10 = 2
So 7697-37-2 is a valid CAS Registry Number.
InChI:InChI=1S/HNO3/c2-1(3)4/h(H,2,3,4)

7697-37-2SDS

SAFETY DATA SHEETS

According to Globally Harmonized System of Classification and Labelling of Chemicals (GHS) - Sixth revised edition

Version: 1.0

Creation Date: Aug 16, 2017

Revision Date: Aug 16, 2017

1.Identification

1.1 GHS Product identifier

Product name nitric acid

1.2 Other means of identification

Product number -
Other names Rfna

1.3 Recommended use of the chemical and restrictions on use

Identified uses For industry use only. Processing Aids and Additives
Uses advised against no data available

1.4 Supplier's details

1.5 Emergency phone number

Emergency phone number -
Service hours Monday to Friday, 9am-5pm (Standard time zone: UTC/GMT +8 hours).

More Details:7697-37-2 SDS

7697-37-2Synthetic route

silver nitrate

silver nitrate

A

nitric acid
7697-37-2

nitric acid

B

silver
7440-22-4

silver

Conditions
ConditionsYield
With H nitrate, in dild. soln., is completely reacting with Pd, satd. with H, at 16 °C in 24 hours to Ag and HNO3;;A 100%
B 100%
With H
ceric ammonium nitrate

ceric ammonium nitrate

2-(salicylideneamino)thiophenol
3449-05-6

2-(salicylideneamino)thiophenol

A

ammonium nitrate

ammonium nitrate

B

(OC6H4CHNC6H4S)Ce(NO3)2(H2O)
240814-62-4

(OC6H4CHNC6H4S)Ce(NO3)2(H2O)

C

nitric acid
7697-37-2

nitric acid

Conditions
ConditionsYield
With ammonium hydroxide In ethanol; water addn. of hot soln. of Schiff base in EtOH to soln. of Ce salt in EtOH (ratio 1 : 1), addn. of H2O and EtOH (to 85% EtOH), pH adjusting to 5.0 - 6.0 (NH4OH), refluxing (2 h), concn. (vac.), crystn. on cooling (over night); filtration, washing (EtOH), recrystn. (hot DMF/EtOH), washing (EtOH, Et2O), drying (vac.); elem. anal.;A n/a
B 90%
C n/a
aluminum trihydroxide

aluminum trihydroxide

aluminum oxide
1333-84-2, 1344-28-1

aluminum oxide

sodium nitrate
7631-99-4

sodium nitrate

A

sodium aluminate
1302-42-7

sodium aluminate

B

nitric acid
7697-37-2

nitric acid

Conditions
ConditionsYield
heating; it attacks vessel of iron or platinum and glass or china;A n/a
B 89%
isoquinoline
119-65-3

isoquinoline

uranyl nirate hexahydrate

uranyl nirate hexahydrate

malonic acid
141-82-2

malonic acid

dihydrogen peroxide
7722-84-1

dihydrogen peroxide

A

UO(O2)(CH2(COO)2)(C9H7N)2
187455-26-1

UO(O2)(CH2(COO)2)(C9H7N)2

B

nitric acid
7697-37-2

nitric acid

Conditions
ConditionsYield
In ethanol; water addn. of org. acid in EtOH to aq. soln. of metal salt, cooling, addn. ofsoln. of isoquinoline in EtOH, addn. of aq. H2O2 (30 %), stirring (30 m in; pptn.); filtration, washing (water, EtOH), purification by TLC, drying (vac., over silica gel); elem. anal.;A 79%
B n/a
quinoline
91-22-5

quinoline

uranyl nirate hexahydrate

uranyl nirate hexahydrate

homophthalic acid

homophthalic acid

dihydrogen peroxide
7722-84-1

dihydrogen peroxide

A

UO(4+)*O2(2-)*C8H4O4(2-)*2C9H7N=UO(O2)(C6H4(COO)2)(C9H7N)2

UO(4+)*O2(2-)*C8H4O4(2-)*2C9H7N=UO(O2)(C6H4(COO)2)(C9H7N)2

B

nitric acid
7697-37-2

nitric acid

Conditions
ConditionsYield
In ethanol; water addn. of org. acid in EtOH to aq. soln. of metal salt, cooling, addn. ofsoln. of quinoline in EtOH, addn. of aq. H2O2 (30 %), stirring (30 min; pptn.); filtration, washing (water, EtOH), purification by TLC, drying (vac., over silica gel); elem. anal.;A 76%
B n/a
isoquinoline
119-65-3

isoquinoline

uranyl nirate hexahydrate

uranyl nirate hexahydrate

homophthalic acid

homophthalic acid

dihydrogen peroxide
7722-84-1

dihydrogen peroxide

A

UO(4+)*O2(2-)*C8H4O4(2-)*2C9H7N=UO(O2)(C6H4(COO)2)(C9H7N)2

UO(4+)*O2(2-)*C8H4O4(2-)*2C9H7N=UO(O2)(C6H4(COO)2)(C9H7N)2

B

nitric acid
7697-37-2

nitric acid

Conditions
ConditionsYield
In ethanol; water addn. of org. acid in EtOH to aq. soln. of metal salt, cooling, addn. ofsoln. of isoquinoline in EtOH, addn. of aq. H2O2 (30 %), stirring (30 m in; pptn.); filtration, washing (water, EtOH), purification by TLC, drying (vac., over silica gel); elem. anal.;A 72%
B n/a
quinoline
91-22-5

quinoline

zirconium(IV) nitrate hexahydrate

zirconium(IV) nitrate hexahydrate

malonic acid
141-82-2

malonic acid

dihydrogen peroxide
7722-84-1

dihydrogen peroxide

A

Zr(O2)(CH2(COO)2)(C9H7N)2
187455-21-6

Zr(O2)(CH2(COO)2)(C9H7N)2

B

nitric acid
7697-37-2

nitric acid

Conditions
ConditionsYield
In ethanol; water addn. of org. acid in EtOH to aq. soln. of metal salt, cooling, addn. ofsoln. of quinoline in EtOH, addn. of aq. H2O2 (30 %), stirring (30 min; pptn.); filtration, washing (water, EtOH), purification by TLC, drying (vac., over silica gel); elem. anal.;A 72%
B n/a
quinoline
91-22-5

quinoline

uranyl nirate hexahydrate

uranyl nirate hexahydrate

malonic acid
141-82-2

malonic acid

dihydrogen peroxide
7722-84-1

dihydrogen peroxide

A

UO(O2)(CH2(COO)2)(C9H7N)2
187455-25-0

UO(O2)(CH2(COO)2)(C9H7N)2

B

nitric acid
7697-37-2

nitric acid

Conditions
ConditionsYield
In ethanol; water addn. of org. acid in EtOH to aq. soln. of metal salt, cooling, addn. ofsoln. of quinoline in EtOH, addn. of aq. H2O2 (30 %), stirring (30 min; pptn.); filtration, washing (water, EtOH), purification by TLC, drying (vac., over silica gel); elem. anal.;A 70%
B n/a
isoquinoline
119-65-3

isoquinoline

zirconium(IV) nitrate hexahydrate

zirconium(IV) nitrate hexahydrate

malonic acid
141-82-2

malonic acid

dihydrogen peroxide
7722-84-1

dihydrogen peroxide

A

Zr(O2)(CH2(COO)2)(C9H7N)2
187455-22-7

Zr(O2)(CH2(COO)2)(C9H7N)2

B

nitric acid
7697-37-2

nitric acid

Conditions
ConditionsYield
In ethanol; water addn. of org. acid in EtOH to aq. soln. of metal salt, cooling, addn. ofsoln. of isoquinoline in EtOH, addn. of aq. H2O2 (30 %), stirring (30 m in; pptn.); filtration, washing (water, EtOH), purification by TLC, drying (vac., over silica gel); elem. anal.;A 70%
B n/a
isoquinoline
119-65-3

isoquinoline

zirconium(IV) nitrate hexahydrate

zirconium(IV) nitrate hexahydrate

homophthalic acid

homophthalic acid

dihydrogen peroxide
7722-84-1

dihydrogen peroxide

A

Zr(4+)*O2(2-)*C8H4O4(2-)*2C9H7N=Zr(O2)(C6H4(COO)2)(C9H7N)2

Zr(4+)*O2(2-)*C8H4O4(2-)*2C9H7N=Zr(O2)(C6H4(COO)2)(C9H7N)2

B

nitric acid
7697-37-2

nitric acid

Conditions
ConditionsYield
In ethanol; water addn. of org. acid in EtOH to aq. soln. of metal salt, cooling, addn. ofsoln. of isoquinoline in EtOH, addn. of aq. H2O2 (30 %), stirring (30 m in; pptn.); filtration, washing (water, EtOH), purification by TLC, drying (vac., over silica gel); elem. anal.;A 68%
B n/a
quinoline
91-22-5

quinoline

zirconium(IV) nitrate hexahydrate

zirconium(IV) nitrate hexahydrate

homophthalic acid

homophthalic acid

dihydrogen peroxide
7722-84-1

dihydrogen peroxide

A

Zr(4+)*O2(2-)*C8H4O4(2-)*2C9H7N=Zr(O2)(C8H4O4)(C9H7N)2

Zr(4+)*O2(2-)*C8H4O4(2-)*2C9H7N=Zr(O2)(C8H4O4)(C9H7N)2

B

nitric acid
7697-37-2

nitric acid

Conditions
ConditionsYield
In ethanol; water addn. of org. acid in EtOH to aq. soln. of metal salt, cooling, addn. ofsoln. of quinoline in EtOH, addn. of aq. H2O2 (30 %), stirring (30 min; pptn.); filtration, washing (water, EtOH), purification by TLC, drying (vac., over silica gel); elem. anal.;A 67%
B n/a
1,1,1-trifluoro-4-(2-thienyl)butane-2,4-dione
326-91-0

1,1,1-trifluoro-4-(2-thienyl)butane-2,4-dione

europium(III) nitrate

europium(III) nitrate

1,4,10,13-tetraoxa-7,16-diazacyclooctadecane
23978-55-4

1,4,10,13-tetraoxa-7,16-diazacyclooctadecane

A

2H(1+)*2Eu(CF3C(O)CHC(O)C4H3S)4(1-)*C12H26N2O4=H2[Eu(CF3C(O)CHC(O)C4H3S)4]2*C12H26N2O4

2H(1+)*2Eu(CF3C(O)CHC(O)C4H3S)4(1-)*C12H26N2O4=H2[Eu(CF3C(O)CHC(O)C4H3S)4]2*C12H26N2O4

B

nitric acid
7697-37-2

nitric acid

Conditions
ConditionsYield
In water; toluene dropwise addn. of soln. of Eu-salt in H2O to soln. of macrocycle and diketone (stirring), sepd. of org. phase after 30 min, pptn. on addn. of cyclohexane to org. phase; collection, recrystn. (toluene/cyclohexane 1/1), drying (over P2O5, vac., 5 h); elem. anal.;A 62%
B n/a
ammonia
7664-41-7

ammonia

nitric acid
7697-37-2

nitric acid

Conditions
ConditionsYield
With oxygen NH3-air mixture,at gently red heat;60%
With oxygen; Sr(2+)*PbO3(2-)*Sr(2+)*MnO4(2-)=SrPbO3*SrMnO4 byproducts: nitrogen oxides; above 500 °C,NH3-air mixture,overall yield:from 90%;
With oxygen; Ba(2+)*PbO3(2-)*Ba(2+)*MnO4(2-)=BaPbO3*BaMnO4 byproducts: nitrogen oxides; above 500 °C,NH3-air mixture,overall yield:from 90%;
[Fe3O(CH3COO)6(H2O)3]·(NO3)·4H2O

[Fe3O(CH3COO)6(H2O)3]·(NO3)·4H2O

D-(-)-quinic acid
77-95-2

D-(-)-quinic acid

water
7732-18-5

water

A

[Fe7O3(OH)3(C7H10O6)6]·20.5H2O

[Fe7O3(OH)3(C7H10O6)6]·20.5H2O

B

nitric acid
7697-37-2

nitric acid

C

acetic acid
64-19-7

acetic acid

Conditions
ConditionsYield
at 4 - 20℃; pH=2.5;A 56%
B n/a
C n/a
hydrogenchloride
7647-01-0

hydrogenchloride

dinitrogen pentoxide
10102-03-1

dinitrogen pentoxide

A

nitric acid
7697-37-2

nitric acid

B

chlorine
7782-50-5

chlorine

C

Nitryl chloride

Nitryl chloride

Conditions
ConditionsYield
In neat (no solvent) at 213 K; purified from N2O5 and nitric acid by distillation at 213 K;A n/a
B 2%
C n/a
2-nitroamino-1,3-diazacyclopent-2-ene
5465-96-3

2-nitroamino-1,3-diazacyclopent-2-ene

nitric acid
7697-37-2

nitric acid

Conditions
ConditionsYield
at 0℃; Rate constant; in festen und fluessigen H2SO4-H2O-Gemischen <84.5-86.4%ig>.Hydrolysis;
nitro-tetrahydropyrimidin-2-ylidene-amine
53360-90-0

nitro-tetrahydropyrimidin-2-ylidene-amine

sulfuric acid
7664-93-9

sulfuric acid

acetic acid
64-19-7

acetic acid

nitric acid
7697-37-2

nitric acid

Conditions
ConditionsYield
at 25℃; Rate constant;
nitro-tetrahydropyrimidin-2-ylidene-amine
53360-90-0

nitro-tetrahydropyrimidin-2-ylidene-amine

water
7732-18-5

water

H2SO4 <68-78.6% >

H2SO4 <68-78.6% >

nitric acid
7697-37-2

nitric acid

Conditions
ConditionsYield
at 25℃; Rate constant;
water
7732-18-5

water

(4-methyl-4,5-dihydro-1(3)H-imidazol-2-yl)-nitro-amine
100130-44-7

(4-methyl-4,5-dihydro-1(3)H-imidazol-2-yl)-nitro-amine

H2SO4 <76.1-87.5 % >

H2SO4 <76.1-87.5 % >

nitric acid
7697-37-2

nitric acid

Conditions
ConditionsYield
at 25℃; Rate constant; Hydrolysis;
2-nitroamino-1,3-diazacyclopent-2-ene
5465-96-3

2-nitroamino-1,3-diazacyclopent-2-ene

water
7732-18-5

water

H2SO4 <76-93% >

H2SO4 <76-93% >

nitric acid
7697-37-2

nitric acid

Conditions
ConditionsYield
at 25℃; Rate constant; Hydrolysis;
water
7732-18-5

water

(4-methyl-4,5-dihydro-1(3)H-imidazol-2-yl)-nitro-amine
100130-44-7

(4-methyl-4,5-dihydro-1(3)H-imidazol-2-yl)-nitro-amine

H2SO

H2SO

nitric acid
7697-37-2

nitric acid

Conditions
ConditionsYield
at 0℃; Rate constant; in festen und fluessigen Gemischen <84.5%ig>.Hydrolysis;
nitro-tetrahydropyrimidin-2-ylidene-amine
53360-90-0

nitro-tetrahydropyrimidin-2-ylidene-amine

water
7732-18-5

water

HClO4 <59.6-67% >

HClO4 <59.6-67% >

nitric acid
7697-37-2

nitric acid

Conditions
ConditionsYield
at 25℃; Rate constant;
creatinine
60-27-5

creatinine

A

methyl-imidazolidinetrione-5-oxime
151201-39-7

methyl-imidazolidinetrione-5-oxime

B

nitric acid
7697-37-2

nitric acid

Conditions
ConditionsYield
With sodium nitrite
5-isonitroso-creatinine

5-isonitroso-creatinine

A

methyl-imidazolidinetrione-5-oxime
151201-39-7

methyl-imidazolidinetrione-5-oxime

B

nitric acid
7697-37-2

nitric acid

Conditions
ConditionsYield
With sodium nitrite
2,4,6-Trinitrophenol
88-89-1

2,4,6-Trinitrophenol

persulfate

persulfate

A

hydrogen cyanide
74-90-8

hydrogen cyanide

B

nitric acid
7697-37-2

nitric acid

water
7732-18-5

water

2,4,6-Trinitrophenol
88-89-1

2,4,6-Trinitrophenol

ammonium persulfate

ammonium persulfate

A

hydrogen cyanide
74-90-8

hydrogen cyanide

B

carbon dioxide
124-38-9

carbon dioxide

C

nitric acid
7697-37-2

nitric acid

pyridine
110-86-1

pyridine

sodium persulfate

sodium persulfate

acid

acid

A

carbon dioxide
124-38-9

carbon dioxide

B

ammonia
7664-41-7

ammonia

C

nitric acid
7697-37-2

nitric acid

Conditions
ConditionsYield
at 70 - 80℃; es erfolgt Oxidation;
5-chloro-4-[cyclohexyl-(2,2,2-trifluoroacetyl)amino]-2-methoxybenzoic acid methyl ester
871932-89-7

5-chloro-4-[cyclohexyl-(2,2,2-trifluoroacetyl)amino]-2-methoxybenzoic acid methyl ester

nitric acid
7697-37-2

nitric acid

5-chloro-4-[cyclohexyl-(2,2,2-trifluoroacetyl)amino]-2-methoxy-3-nitrobenzoic acid methyl ester
871932-90-0

5-chloro-4-[cyclohexyl-(2,2,2-trifluoroacetyl)amino]-2-methoxy-3-nitrobenzoic acid methyl ester

Conditions
ConditionsYield
Stage #1: 5-chloro-4-[cyclohexyl-(2,2,2-trifluoroacetyl)amino]-2-methoxybenzoic acid methyl ester; nitric acid at -40 - -20℃; for 2h;
Stage #2: With sodium hydroxide In water
100%
dysprosium((III) oxide

dysprosium((III) oxide

water
7732-18-5

water

nitric acid
7697-37-2

nitric acid

dysprosium(III) nitrate hydrate

dysprosium(III) nitrate hydrate

Conditions
ConditionsYield
at 80℃;100%
In nitric acid aq. HNO3; dissolving metal oxide in concd. HNO3, heating; evapn. on water bath, dissolving in water;
In nitric acid aq. HNO3; by treating the metal oxide with dil. HNO3; the soln. was evapd. on a steam bath; the residue was dissolved in water, conced. to a viscous mass, cooled and kept in a desiccator after breaking up any lumps;
europium(III) oxide

europium(III) oxide

water
7732-18-5

water

nitric acid
7697-37-2

nitric acid

europium(III) nitrate hydrate

europium(III) nitrate hydrate

Conditions
ConditionsYield
at 80℃;100%
In nitric acid aq. HNO3; Eu2O3 treated with concd. HNO3; excess HNO3 evapd.;
In nitric acid aq. HNO3; dissolving metal oxide in concd. HNO3, heating; evapn. on water bath, dissolving in water;
yttrium(III) oxide

yttrium(III) oxide

water
7732-18-5

water

nitric acid
7697-37-2

nitric acid

yttrium(III) nitrate hydrate

yttrium(III) nitrate hydrate

Conditions
ConditionsYield
at 80℃;100%
In water react. metal oxide with 6N HNO3; evapn. at 100°C;
In nitric acid aq. HNO3; by treating the metal oxide with dil. HNO3; the soln. was evapd. on a steam bath; the residue was dissolved in water, conced. to a viscous mass, cooled and kept in a desiccator after breaking up any lumps;
In nitric acid aq. HNO3; dissolving of Y2O3 in excess amt. of aq. nitric acid;
nitric acid
7697-37-2

nitric acid

ammonia
7664-41-7

ammonia

Conditions
ConditionsYield
In water Electrolysis; Cu-cathode, in presence of H2SO4;;100%
With aluminium In water at elevated pressure;;0%
With aluminium In water only small amounts of NH3 in dild. HNO3 (5%-20%) at atmospheric pressure;;
nitric acid
7697-37-2

nitric acid

palladium
7440-05-3

palladium

palladium (II) nitrate

palladium (II) nitrate

Conditions
ConditionsYield
With sulfur trioxide pyridine complex at 25 - 100℃; for 180h; Sealed tube;100%
In nitric acid in presence of air;
In nitric acid byproducts: N-oxide; by heating; in presence of air;
terbium(III) oxide

terbium(III) oxide

water
7732-18-5

water

nitric acid
7697-37-2

nitric acid

H6N3O12Tb

H6N3O12Tb

Conditions
ConditionsYield
at 80℃;100%
lead(II) tungstate

lead(II) tungstate

ammonium hydroxide

ammonium hydroxide

nitric acid
7697-37-2

nitric acid

A

tungsten(VI) oxide

tungsten(VI) oxide

B

lead(II) oxide

lead(II) oxide

Conditions
ConditionsYield
In nitric acid aq. HNO3; PbWO4 dissolved in aq. HNO3 (10 wt %) at 75°C; isothermal holdingtime was 2 h; ppt. filtered off; washed (aq. HNO3); calcined at 700°C (WO3 was obtained); to filtrate contg. Pb(NO3)2 added aq. NH4OH with stirring; final pH was 8.9; ppt. diltered off; dried; calcined at 800°C;A 99.9%
B 93.6%
antimony
7440-36-0

antimony

nitric acid
7697-37-2

nitric acid

antimony pentoxide

antimony pentoxide

Conditions
ConditionsYield
In water byproducts: NO2; Sb powder was covered with concd. nitric acid, heated under an open hood and over a bunsen burner flame, solid was filtered, washed with water,left to dry, heated in open beaker over a bunsen burner flame;99.729%
nitric acid
7697-37-2

nitric acid

sodium oxalate
62-76-0

sodium oxalate

sodium nitrate
7631-99-4

sodium nitrate

Conditions
ConditionsYield
In water byproducts: oxalic acid; between 15 and 65°C;; pure NaNO3;;99%
(CH3)3SiCHCH2(SFe(CO)3)2

(CH3)3SiCHCH2(SFe(CO)3)2

nitric acid
7697-37-2

nitric acid

A

ferric nitrate
7782-61-8

ferric nitrate

B

ethenyltrimethylsilane
754-05-2

ethenyltrimethylsilane

Conditions
ConditionsYield
In nitric acid byproducts: H2SO4, NO, CO; stirring for 0.5 h at 25°C; condensing silane in a trap cooled with solid CO2, treating aq. layer with NaOH, evapn. to dryness, IR;A n/a
B 99%
sodium bismuthate

sodium bismuthate

americium(3+)

americium(3+)

nitric acid
7697-37-2

nitric acid

americyl

americyl

Conditions
ConditionsYield
In further solvent(s) the mixt. of NaBiO3 and Am(3+) in 0.1 M nitric acid was agitated at roomtemp.; detected by UV spectra and γ-ray spectroscopy;99%
sodium bismuthate

sodium bismuthate

americium(3+)

americium(3+)

nitric acid
7697-37-2

nitric acid

(243)AmO2(1+)

(243)AmO2(1+)

Conditions
ConditionsYield
In further solvent(s) the mixt. of NaBiO3 and Am(3+) in 0.1 M nitric acid was heated at 80°C; detected by UV spectra and γ-ray spectroscopy;99%
bismuth (III) nitrate pentahydrate

bismuth (III) nitrate pentahydrate

nitric acid
7697-37-2

nitric acid

iodic acid
7782-68-5

iodic acid

Bismuth oxide iodate
1316858-53-3

Bismuth oxide iodate

Conditions
ConditionsYield
In water High Pressure; Bi(NO3)3, HIO3, HNO3 were heated in autoclave to 200°C, held for 1 week, cooled slowly, 6°C/h, to room temp.; filtered, washed with distilled water;99%
bismuth
7440-69-9

bismuth

nitric acid
7697-37-2

nitric acid

bismuth (III) nitrate pentahydrate

bismuth (III) nitrate pentahydrate

Conditions
ConditionsYield
With water; ammonium carbonate In nitric acid solution of Bi in HNO3 (36 Be); vigorous reaction, repeated addition of H2O;; filtration through an asbestos filter and evaporation of the filtrate; crystallisation and washing with H2O (containing a small amount of HNO3); drying at 25°C; addition of (NH4)2CO3 to the end liquors and formation of Bi nitrate with HNO3;;98%
With H2O; (NH4)2CO3 In nitric acid solution of Bi in HNO3 (36 Be); vigorous reaction, repeated addition of H2O;; filtration through an asbestos filter and evaporation of the filtrate; crystallisation and washing with H2O (containing a small amount of HNO3); drying at 25°C; addition of (NH4)2CO3 to the end liquors and formation of Bi nitrate with HNO3;;98%
With water; oxygen In nitric acid byproducts: N oxides; addition of warm Bi grains under reflux to HNO3 and O2; absorption of the formed N oxides after oxidation in H2O and returning back to the reaction mixture;;
sulfolane
126-33-0

sulfolane

1,2,3,5-tetrafluoro-4-nitrobenzene
314-41-0

1,2,3,5-tetrafluoro-4-nitrobenzene

nitric acid
7697-37-2

nitric acid

2,4,5,6-Tetrafluoro-1,3-dinitrobenzene
20002-14-6

2,4,5,6-Tetrafluoro-1,3-dinitrobenzene

Conditions
ConditionsYield
With boron trifluoride at 65-70°C 7 d;98%
With BF3 at 65-70°C 7 d;98%
barium(II) nitrate

barium(II) nitrate

4C12H28N(1+)*4H2O*V4O12(4-)

4C12H28N(1+)*4H2O*V4O12(4-)

nitric acid
7697-37-2

nitric acid

dimethyl sulfoxide
67-68-5

dimethyl sulfoxide

4Ba(2+)*14C2H6OS*NO3(1-)*V14O38(7-)

4Ba(2+)*14C2H6OS*NO3(1-)*V14O38(7-)

Conditions
ConditionsYield
Stage #1: barium(II) nitrate; 4C12H28N(1+)*4H2O*V4O12(4-); dimethyl sulfoxide at 70℃; for 4h;
Stage #2: nitric acid at 20℃; for 2h;
98%
N,N’-trans-cyclohexane-1,4-diylbis(pyrrolidin-2-one)

N,N’-trans-cyclohexane-1,4-diylbis(pyrrolidin-2-one)

nitric acid
7697-37-2

nitric acid

uranium(4+)

uranium(4+)

N6O18U*2C14H23N2O2(1-)*2H(1+)

N6O18U*2C14H23N2O2(1-)*2H(1+)

Conditions
ConditionsYield
With hydrazine In water98%
rac-N,N’-trans-cyclohexane-1,2-diylbis(pyrrolidin-2-one)

rac-N,N’-trans-cyclohexane-1,2-diylbis(pyrrolidin-2-one)

nitric acid
7697-37-2

nitric acid

uranium(4+)

uranium(4+)

N6O18U*2C14H23N2O2(1-)*2H(1+)

N6O18U*2C14H23N2O2(1-)*2H(1+)

Conditions
ConditionsYield
With hydrazine In water98%
Au(N,N'-bis(2,6-diisopropyl)imidazol-2-ylidene)(Bpin)

Au(N,N'-bis(2,6-diisopropyl)imidazol-2-ylidene)(Bpin)

nitric acid
7697-37-2

nitric acid

Au(IPr)(ONO2)

Au(IPr)(ONO2)

Conditions
ConditionsYield
In benzene-d6 at 20℃; for 0.0833333h; Glovebox;98%
thallium(I) nitrate

thallium(I) nitrate

Nd(W5O18)2(9-)

Nd(W5O18)2(9-)

water
7732-18-5

water

nitric acid
7697-37-2

nitric acid

6Tl(1+)*3H(1+)*Nd(W5O18)2(9-)*7.5H2O=Tl6H3[Nd(W5O18)2]*7.5H2O

6Tl(1+)*3H(1+)*Nd(W5O18)2(9-)*7.5H2O=Tl6H3[Nd(W5O18)2]*7.5H2O

Conditions
ConditionsYield
In water HNO3 added to Nd/H(+)=2, Tl salt added dropwise at 25°C with vigorous stirring, kept for 24 h; ppt. filtered, washed (cold water), dried air; elem. anal.;97.78%

7697-37-2Relevant articles and documents

Hart, E.

, p. 580 (1895)

Formation and Decay of Peroxynitrous Acid: A Pulse Radiolysis Study

Loegager, T.,Sehested, K.

, p. 6664 - 6669 (1993)

Peroxynitrous acid and peroxynitrite anion have been studied using pulse radiolysis of nitrite and nitrate solutions.The formation rate constant determined to be k(OH + NO2) = (4.5 +/- 1.0) * 109 M-1 s-1, and the rate constant for the OH radical reaction with nitrite is determined to be k(OH +NO2-) = (6.0 +/- 1.0) * 109 M-1 s-1.In nitrate solutions, the competing reaction between OH and NO32- is found to have a rate constant of k(OH + NO32- = (3.0 +/- 1.0) * 109 M-1 s-1.The intermediate species in the nitrate system, NO32-, HNO3-, and H2NO3, decay into NO2 according to the first-order rate constants: (5.6 +/ - 0.5) * 104, (2.0 +/- 0.5) * 105, and (7.0 +/- 2.0) * 105 s-1, respectively.The rate constants k(H + NO3-) = (1.0 +/- 0.3) * 107 M-1 s-1 and k(H + NO2) = (1.0 +/- 0.2) * 1010 M-1 s-1 were also determined.The pKa of NOOH is found to be 6.5 +/- 0.1 by absorption measurements, and the maximum extinction coefficient at 240 nm is ε240(ONOOH) = 770 +/- 50 M-1 cm-1.The decay of peroxynitrous acid is detrmined to proceed through the first-order isomerization of ONOOH to HNO3 according to the rate equation kobs = kiso/(1 + Ka/+>) with rate constants kiso = 1.0 +/- 0.2 s-1 and Ka = (1.0 +/- 0.3) * 10-7.A comparison of all available literature values for the pKa and the decay rate is reported.

Visible light photocatalytic degradation of nitric oxides on PtOx-modified TiO2 via sol-gel and impregnation method

Huang, Chun-Hung,Wang, I-Kai,Lin, Yu-Ming,Tseng, Yao-Hsuan,Lu, Chun-Mei

, p. 163 - 170 (2010)

The visible light active catalysts, PtOx-doped TiO2 (PtOx-TiO2) and PtOx-loaded TiO2 (PtOx/TiO2), were successfully synthesized by the acid-catalyzed sol-gel process and the impregnation method. Pt(NH3)4(NO3)2 or H2Pt(OH)6 was employed as the PtOx precursor. By comparing the results of De-NOx, the modified photocatalysts exhibited a higher visible-light-responsive activity, and a lower NO2 selectivity than the unmodified ones. The FE-SEM images suggested that the particle size was unchanged after modification. The XRD patterns showed that the crystal structure still remained as anatase phase. Nitrogen adsorption revealed no significant change in surface areas for all samples. The UV-vis spectra indicated that PtOx promoted the absorption of visible light. Furthermore, the XPS spectra evidenced that the mixed valence states of PtO-PtO2 coexisted on the surface of TiO2. The adding of PtOx on TiO2 not only promoted the visible-light-responsive activity of converting NO to NO2 but also increased the consecutive reaction rate of NO2 to NO3-.

The inhibition of N2O5 hydrolysis in sulfuric acid by 1-butanol and 1-hexanol surfactant coatings

Park, Seong-Chan,Burden, Daniel K.,Nathanson, Gilbert M.

, p. 2921 - 2929 (2007)

Gas - liquid scattering experiments are used to measure the fraction of N2O5 molecules that are converted to HNO3 after colliding with 72 wt % H2SO4 containing 1-hexanol or 1-butanol at 216 K. These alcohols segregate to the surface of the acid, with saturation coverages estimated to be 60% of a close-packed monolayer for 1-hexanol and 44% of a close-packed monolayer for 1-butanol. We find that the alkyl films reduce the conversion of N2O5 to HNO 3 from 0.15 on bare acid to 0.06 on the hexyl-coated acid and to 0.10 on the butyl-coated acid. The entry of HC1 and HBr, however, is enhanced by the hexanol and butanol films. The hydrolysis of N2O5 may be inhibited because the alkyl chains restrict the transport of this large molecule and because the alcohol OH groups dilute the surface region, suppressing reaction between N2O5 and near-interfacial H 3O+ or H2O. In contrast, the interfacial alcohol OH groups provide additional binding sites for HC1 and HBr and help initiate ionization. These and previous scattering experiments indicate that short-chain alcohol surfactants impede or enhance sulfuric acid-mediated reactions in ways that depend on the chain length, liquid phase acidity, and nature of the gas molecule.

Hart, E.

, p. 576 - 580 (1895)

Fairlie et al.

, p. 3786 (1953)

Wilfarth, H.

, p. 587 (1884)

Water vapor effect on the HNO3 yield in the HO2 + NO reaction: Experimental and theoretical evidence

Butkovskaya, Nadezhda,Rayez, Marie-Therese,Rayez, Jean-Claude,Kukui, Alexandre,Le Bras, Georges

, p. 11327 - 11342 (2009)

The influence of water vapor on the production of nitric acid in the gas-phase HO2 + NO reaction was determined at 298 K and 200 Torr using a high-pressure turbulent flow reactor coupled with a chemical ionization mass spectrometer. The yield o

Ferric microperoxidase-11 catalyzes peroxynitrite isomerization

Ascenzi, Paolo,Leboffe, Loris,Santucci, Roberto,Coletta, Massimo

, p. 56 - 61 (2015)

Microperoxidase-11 (MP11) is an undecapeptide derived from horse heart cytochrome c offering the possibility to study the reactivity of the heme group relatively unshielded by the protein. Here, the peroxynitrite isomerization to NO3-/sup

The hydrolysis of chlorine nitrate and its possible atmospheric significance

Rowland,Sato,Khwaja,Elliott

, p. 1985 - 1988 (1986)

The hydrolysis of CIONO2 takes place very readily on a variety of laboratory surfaces and may also occur catalytically on particulate surfaces in the stratosphere. The reaction can be considered as an oxide exchange between two X-O-Y molecules with X and Y = H, C1, or NO2. Two other reactions in this class which might occur in the stratosphere are HOCl plus HOCl, and HOCl plus ClONO2. Each of these three is approximately thermoneutral and should be accompanied by the reverse reaction with a comparable reaction rate constant. Current atmospheric models have not explained the very large ozone depletions which have taken place during Antarctic spring in the past decade. The chemical reactions included in these models may need to include heterogeneous catalysis of one or more of these oxide exchange reactions.

The Heterogeneous Reaction of N2O5 with HBr on Ice Comparison with N2O5+HCl

Seisel, Sabine,Miche, Beno?t Flilckiger,Rossi

, p. 811 - 820 (1998)

The heterogeneous reactions of N2O5 with HC1 and HBr on ice have been studied in the temperature range 180 to 200 K using a Knudsen flow reactor. The uptake of N2O5 on ice in the presence of HBr was found to be strongly dependent on :he HBr concentration. For the highest HBr concentrations used a maximum uptake coefficient of N2O5 of 7 = 0.11 has been determined. We observed Br2 and MONO in 80% yield as products with respect to N2O5 taken up. The uptake coefficient of N2O5 on ice in the presence of HC1 was found to be 3.2-10-2 and increased with increasing HCl concentration. C1NO2 was detected as the sole reaction product with a maximum yield of 63% with respect to N2O5 consumed. Hydrolysis of N2O5 resulting in HNO3 was found to be competitive with the title reaction. For the case of the HBr reaction the branching ratio between Br2 and HONO formation, on the one hand, and hydrolysis of N2O5, on the other hand, has been determined. Mechanistic aspects of the heterogeneous reaction of N2O5 with HX have been discussed. WILEY-VCH Verlag GmbH, 1998.

Evaluation of Activation Volumes for the Conversion of Peroxynitrous to Nitric Acid

Kissner, Reinhard,Thomas, Chris,Hamsa, Mohamed S.A.,Van Eldik, Rudi,Koppenol, Willem H.

, p. 11261 - 11263 (2003)

Peroxynitrous acid, an inorganic toxin of biological importance, acts both as an oxidizing and a nitrating agent during its conversion to nitric acid. In discussions of the mechanism of this conversion, activation volumes have been invoked to distinguish between possible mechanisms, viz., homolysis of the O-O bond versus rotation via the N-O bond of peroxynitrous acid. A reinvestigation of the activation volume for the conversion of peroxynitrous acid to nitric acid by high-pressure stopped-flow spectrophotometry yielded an average value of 6.9 ± 0.9 cm3 mol-1 at 25 °C. Activation volumes currently cited in the literature for this process range from 6 to 10 cm3 mol-1 in the temperature range 18-25 °C. Such moderately positive values do not support a definite conclusion regarding the mechanism of the conversion.

Heterogeneous Reactions on Model Polar Stratospheric Cloud Surfaces: Reaction of N2O5 on Ice and Nitric Acid Trihydrate

Quinlan, Michael A.,Reihs, Christa M.,Golden, David M.,Tolbert, Margaret A.

, p. 3255 - 3260 (1990)

A Knudsen cell flow reactor was used to study the heterogeneous reaction of N2O5 on laboratory ice surfaces and nitric acid trihydrate (NAT) surfaces representative of polar stratospheric clouds (PSCs).N2O5 was quantitatively converted to HNO3 on ice surfaces at 188 K.On initially pure ice surfaces, a gradual increase in the N2O5 uptake efficiency was observed up to a maximum value near 0.03.The slow rise in reactivity with time is consistent with an acid-catalyzed surface reaction.With increasing initial nitric acid concentrations, the maximum reactivity occurred more rapidly although the overall reactivity was depressed.The uptake efficiency for N2O5 on NAT at 188 K was found to be 0.015 +/- 0.006.

Infrared matrix isolation and theoretical studies of SO2-HNO3 and SO2-HONO systems

Wierzejewska, Maria,Mielke, Zofia,Wieczorek, Robert,Latajka, Zdzislaw

, p. 17 - 29 (1998)

Argon matrix infrared spectra of sulphur dioxide complexes with nitric or nitrous acid indicate formation of hydrogen-bonded structures. The red shifts of the OH stretching modes are equal to ca. 179, 51 and 40 cm-1 in SO2-HNO3

UV Resonance Raman Investigation of Pentaerythritol Tetranitrate Solution Photochemistry and Photoproduct Hydrolysis

Gares, Katie L.,Bykov, Sergei V.,Asher, Sanford A.

, p. 7889 - 7894 (2017)

Ultraviolet resonance Raman spectroscopy (UVRR) is being developed for standoff trace explosives detection. To accomplish this, it is important to develop a deep understanding of the accompanying UV excited photochemistry of explosives, as well as the impact of reactions on the resulting photoproducts. In the work here we used 229 nm excited UVRR spectroscopy to monitor the photochemistry of pentaerythritol tetranitrate (PETN) in acetonitrile. We find that solutions of PETN in CD3CN photodegrade with a quantum yield of 0.08 ± 0.02, as measured by high performance liquid chromatography (HPLC). The initial step in the 229 nm UV photolysis of PETN in CD3CN is cleavage of an O-NO2 bond to form NO2. The accompanying photoproduct is pentaerythritol trinitrate (PETriN), (CH2ONO2)3CCH2OH formed by photolysis of a single O-NO2. The resulting UVRR spectra show a dominant photoproduct band at ~1308 cm-1, which derives from the symmetric stretch of dissolved NO2. This photoproduct NO2 is hydrolyzed by trace amounts of water, which downshifts this 1308 cm-1 NO2 Raman band due to the formation of molecular HNO3. The dissociation of HNO3 to NO3- in the presence of additional water results in an intense NO3- symmetric stretching UVRR band at 1044 cm-1.

The oxidation product (NO3-) of NO pollutant in flue gas used as a nitrogen source to improve microalgal biomass production and CO2fixation

Cheng, Jun,Huang, Yun,Lu, Hongxiang,Huang, Rui,Zhou, Junhu,Cen, Kefa

, p. 42147 - 42154 (2014)

In order to eliminate the inhibition effect of the toxic nitric oxide (NO) in flue gas on microalgal growth and CO2fixation, NO was converted by a wet UV/H2O2method to produce nitrate (NO3-), which then be used as a nitrogen source for microalgae to improve its growth. The growth ability and biomass compositions of the microalgae cultivated with the produced NO3-from NO gas were similar to those of the microalgae cultivated with equivalent moles of commercial NaNO3. The NO3-concentration produced from NO increased with UV lamp power, H2O2, and NO concentrations, resulting in an improved microalgal growth. The concentration of NO3-from 500 ppm NO wet-oxidized by 6% (v/v) H2O2and 55 W UV light was up to 8.8 mM. When the produced nitrate was used as supplementary nitrogen source, the maximum growth productivity of Chlorella PY-ZU1 at 15% (v/v) CO2reached 1.18 g L-1per day (0.97 times higher than that cultivated with the standard medium). The peak fixation efficiency of 15% (v/v) CO2was 69.6% (1.13 times higher than that cultivated with the standard medium). This journal is

Removal of low concentration nitrogen oxides through photoassisted heterogeneous catalysis

Ibusuki,Takeuchi

, p. 93 - 102 (1994)

Titanium dioxide (Tio2) oxidized nitric oxide (NO) to nitric acid (HNO3) very rapidly under ultraviolet light illumination, but some NO was oxidized to nitrogen dioxide (NO2), while activated carbon (AC) adsorbed NO2 well. A mixture of TiO2 and AC was thus confirmed to be an excellent photoassisted catalyst for removal of low concentration (sub-ppm) NOx from air. Addition of 1-3 wt % of ferric oxide to the mixture could markedly increase the catalytic activity. Even though the catalytic activity gradually declined with the reaction time, it could be completely recovery only by washing the catalyst was removed.

Complete, reversible H+/Li+ ion exchange reaction between rhombohedral LiMO3 and perovskite-type HMO3 (M = Nb, Ta)

Thangadurai,Weppner

, p. 2417 - 2425 (2002)

We demonstrate for the first time the complete, reversible H+/Li+ ion exchange reaction between HMO3 and LiMO3 (M=Nb, Ta) using molten LiNO3 at 320°C for 5 days. HMO3 were prepared from LiMO3 by ion exchange reactions using dilute HNO3. The results reveal that both LiMO3 prepared by normal solid state reaction between Li2CO3 and M2O5, and by ion exchanged from HMO3 using molten LiNO3 are isostructural. LiMO3 prepared using HMO3 yields nearly uniformly sized crystallites in contrast to those prepared by conventional solid state synthesis. The present method is simple and inexpensive compared to other methods of preparation of high purity LiMO3 powders.

Absolute Rate Constants for the Reaction of OH with NO2 in N2 and He from 225 to 389 K

Anderson, Larry G.

, p. 2152 - 2155 (1980)

The temperature dependence of the rate of the reaction OH + NO2 + N2 --> HNO3 + N2 was investigated by using a discharge flow system for OH production and resonance fluorescence for its detection.The reaction was investigated at room temperature in He, and between 225 and 389 K in N2.The temperature dependence could be fit by the Arrhenius expression (1.6 +/- 0.4)E-31 exp cm6 molecule-2 s-1 or preferably by (2.3 +/- 0.6)E-30(T/298)-2.9 cm6 molecule-2 s-1.Earlier data have been used to determine the temperature dependence of the high-pressure limiting rate constant for this reaction.Troe's simplified expression for calculating rate constants in the falloff region was used to compare the appropriateness of different limiting values for the description of the experimentally observed pressure dependence of the rate constant.This reevaluation of the rate data suggests more appropriate values for k0 and k for use in atmospheric modeling: k0 = 2.3E-30(T/298)-2.9 cm6 molecule-2 s-1 and k = 1.2E-11(T/298)-1.6 cm3 molecule-1 s-1.

Detection of autocatalytic decomposition behavior of energetic materials using APTAC

Wei,Rogers,Mannan

, p. 125 - 130 (2006)

Characterization of autocatalytic decomposition reactions is important for the safe handling and storage of energetic materials. Isothermal differential scanning calorimetry (DSC) has been widely used to detect autocatalytic decomposition of energetic materials. However, isothermal DSC tests are time consuming and the choice of experimental temperature is crucial. This paper shows that an automatic pressure tracking calorimeter (APTAC) can be a reliable and efficient screening tool for the identification of autocatalytic decomposition behavior of energetic materials. Hydroxylamine nitrate (HAN) is an important member of the hydroxylamine family. High concentrations of HAN are used as liquid propellants, and low concentrations of HAN are used primarily in the nuclear industry for decontamination of equipment. Because of its instability and autocatalytic decomposition behavior, HAN has been involved in several incidents. This paper presents calorimetric measurements for the thermal decomposition of 24 mass% HAN/water. APTAC heat-wait-search and heat-soak-search modes are used to characterize the thermal decomposition of HAN. By comparing the kinetic analysis for the two modes, it is concluded that HAN shows strong autocatalytic decomposition behavior. The most likely decomposition pathway of HAN is proposed to explain the observed autocatalytic behavior.

Facile synthesis of double cone-shaped Ag4V2O7/BiVO4 nanocomposites with enhanced visible light photocatalytic activity for environmental purification

Hu, Yang,Fan, Jun,Pu, Chenchen,Li, Hua,Liu, Enzhou,Hu, Xiaoyun

, p. 172 - 183 (2017)

Ag4V2O7/BiVO4 photocatalysts with double cone-shaped nanostructure were successfully synthesized by a facile sodium polyphosphate-assisted hydrothermal method. The results demonstrate that coupling Ag4V2O7 with BiVO4 can promote the separation of photoinduced charge carriers and enhance the photon absorption efficiency. Experimental results indicate that Ag4V2O7/BiVO4 composites exhibit the enhanced photocatalystic activity for degradation of methylene blue (MB) and oxidation of NO in high concentrate (1600?ppb) compared to the pure BiVO4 under visible light irradiation (λ?>?420?nm). The composite with 0.08 mol% Ag4V2O7 has the highest photocatalytic activity. MB degradation rate can reach 98.48% in 1?h and NO oxidation rate can reach 52.83% in 0.5?h on 0.08-Ag4V2O7/BiVO4, which are about 2.90 and 3.11 times higher than that of pure BiVO4 respectively. The excellent activity can be attributed to the efficient charge transfer between Ag4V2O7 and BiVO4, and active species h+ and [rad]O2? play important roles during MB degradation and NO oxidation. In addition, this composite exhibits favorable stability during the cycling experiment, suggesting it may be a promising visible light active photocatalyst for environmental applications.

PLATINUM-ACRIDINE COMPOUNDS AND METHODS OF TREATING CANCERS

-

, (2021/10/30)

Platinum-acridines and analogs thereof as cytotoxic agents for cancer treatment. Also provided methods of using hMATE1 (SLC47A1) as a biomarker to identify tumors that are likely to respond to the agents, and epigenetically sensitizing tumor tissue to anticancer drugs targeting this membrane transporter.

Capture of nitrogen dioxide and conversion to nitric acid in a porous metal–organic framework

Li, Jiangnan,Han, Xue,Zhang, Xinran,Sheveleva, Alena M.,Cheng, Yongqiang,Tuna, Floriana,McInnes, Eric J. L.,McCormick McPherson, Laura J.,Teat, Simon J.,Daemen, Luke L.,Ramirez-Cuesta, Anibal J.,Schr?der, Martin,Yang, Sihai

, p. 1085 - 1090 (2019/11/29)

Air pollution by nitrogen oxides, NOx, is a major problem, and new capture and abatement technologies are urgently required. Here, we report a metal–organic framework (Manchester Framework Material 520 (MFM-520)) that can efficiently confine dimers of NO2, which results in a high adsorption capacity of 4.2 mmol g–1 (298 K, 0.01 bar) with full reversibility and no loss of capacity over 125 cycles. Treatment of NO2?MFM-520 with water in air leads to a quantitative conversion of the captured NO2 into HNO3, an important feedstock for fertilizer production, and fully regenerates MFM-520. The confinement of N2O4 inside nanopores was established at a molecular level, and the dynamic breakthrough experiments using both dry and humid NO2 gas streams verify the excellent stability and selectivity of MFM-520 and confirm its potential for precious-metal-free deNOx technologies.