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Nitrogen is a colorless, odorless, and tasteless chemical element represented by the symbol 'N' on the periodic table. It is the seventh element with an atomic number of 7 and primarily exists as a diatomic gas (N2) in its natural state. Nitrogen is an essential building block of amino acids and thus, life, making up around 3% by weight of the human body and about 78% of the earth's atmosphere by volume. It has a unique ability to form stable multiple bonds with carbon, leading to a wide range of known nitrogenous compounds. Nitrogen also shows different oxidation states ranging from +5 to -3 and can exist in several different forms (allotropes), but the diatomic form is most common.

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  • 7727-37-9 Structure
  • Basic information

    1. Product Name: Nitrogen
    2. Synonyms: Diatomicnitrogen;Dinitrogen;Molecular nitrogen;Nitrogen (N2);Nitrogen gas;Nitrogennutrition (plant);Nitrogen-14;CHEBI:17997;HSDB 5060;
    3. CAS NO:7727-37-9
    4. Molecular Formula: N2
    5. Molecular Weight: 28.0134
    6. EINECS: 231-783-9
    7. Product Categories: N/A
    8. Mol File: 7727-37-9.mol
    9. Article Data: 805
  • Chemical Properties

    1. Melting Point: -210℃
    2. Boiling Point: 77.36 K, -195.79 °C, -320.33 °F
    3. Flash Point: N/A
    4. Appearance: Colorless odorless gas
    5. Density: 0.875 g/cm3
    6. Refractive Index: N/A
    7. Storage Temp.: N/A
    8. Solubility: N/A
    9. CAS DataBase Reference: Nitrogen(CAS DataBase Reference)
    10. NIST Chemistry Reference: Nitrogen(7727-37-9)
    11. EPA Substance Registry System: Nitrogen(7727-37-9)
  • Safety Data

    1. Hazard Codes: N/A
    2. Statements: N/A
    3. Safety Statements: S38:;
    4. WGK Germany:
    5. RTECS:
    6. HazardClass: N/A
    7. PackingGroup: N/A
    8. Hazardous Substances Data: 7727-37-9(Hazardous Substances Data)

7727-37-9 Usage

Uses

Used in Industrial Production:
Nitrogen is used as a raw material for the production of ammonia, nitric acid, TNT, and fertilizers. Its ability to form stable multiple bonds with carbon makes it an essential component in these industrial processes.
Used in Food Industry:
Nitrogen is used as a food preservative to displace oxygen and prevent oxidation, which can lead to spoilage and the growth of aerobic bacteria. This helps to extend the shelf life of packaged foods.
Used in Medical Applications:
Nitrogen is used in medical applications, such as cryotherapy, where it is used to freeze and remove skin lesions. It is also used in the production of medical-grade oxygen, where nitrogen is removed from air to obtain a higher concentration of oxygen for patients.
Used in Electronics Industry:
Nitrogen is used in the electronics industry as a protective gas during the manufacturing of semiconductors and other electronic components. It helps to prevent oxidation and contamination of the materials during the production process.
Used in Cryogenic Applications:
Nitrogen is used in cryogenic applications, such as cryopreservation, where it is used to freeze and store biological samples, such as stem cells, at extremely low temperatures. This allows for the long-term storage and preservation of these samples for future use.
Used in Environmental Applications:
Nitrogen is used in environmental applications, such as soil remediation, where it is used to promote the growth of nitrogen-fixing bacteria that can help to reduce the levels of harmful contaminants in the soil. This can aid in the restoration of polluted environments and improve soil quality.

Check Digit Verification of cas no

The CAS Registry Mumber 7727-37-9 includes 7 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 4 digits, 7,7,2 and 7 respectively; the second part has 2 digits, 3 and 7 respectively.
Calculate Digit Verification of CAS Registry Number 7727-37:
(6*7)+(5*7)+(4*2)+(3*7)+(2*3)+(1*7)=119
119 % 10 = 9
So 7727-37-9 is a valid CAS Registry Number.
InChI:InChI=1/N2/c1-2

7727-37-9 Well-known Company Product Price

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  • Sigma-Aldrich

  • (00474)  Nitrogen  ≥99.999%

  • 7727-37-9

  • 00474-1EA

  • 962.91CNY

  • Detail
  • Sigma-Aldrich

  • (00474)  Nitrogen  ≥99.999%

  • 7727-37-9

  • 00474-1L

  • 501.93CNY

  • Detail
  • Aldrich

  • (769061)  Nitrogen  Messer® CANGas, 99.999%

  • 7727-37-9

  • 769061-1L

  • 947.70CNY

  • Detail

7727-37-9SDS

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 dinitrogen

1.2 Other means of identification

Product number -
Other names Nitrogen

1.3 Recommended use of the chemical and restrictions on use

Identified uses For industry use only. Uncategorized
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:7727-37-9 SDS

7727-37-9Synthetic route

nitrogen(II) oxide
10102-43-9

nitrogen(II) oxide

nitrogen
7727-37-9

nitrogen

Conditions
ConditionsYield
With Pd supported ZrO2-CeO2 catalyst at 175 - 400℃; for 1h; Reagent/catalyst; Temperature; Inert atmosphere;100%
With H2; O2; catalyst: 0.1 wtpercent Pt/La0.7Sr0.2Ce0.1FeO3 In neat (no solvent, gas phase) Kinetics; NO:H2:O2 = 1:0.25:5% gas mixt. with 5% H2O added in feed stream; at 140°C for 20 h; H2O as reagent; detd. by mass spectrometry, gas chromy.;93%
With (Y0.90Pr0.10)2O(3+x) at 900℃; Temperature; Inert atmosphere;79%
ammonia
7664-41-7

ammonia

oxygen
80937-33-3

oxygen

A

nitrogen
7727-37-9

nitrogen

B

nitrogen(II) oxide
10102-43-9

nitrogen(II) oxide

C

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

Conditions
ConditionsYield
With oxygen In neat (no solvent) Fe-ZSM-5 catalyst prepared by ion exchange and heat-treated at 400, 425or 450 °C, 100 % NH3 conversion, 100 % N2 selectivity, 1000 ppm NH3 in 2 % O2-contg. He;A 100%
B 0%
C 0%
With catalyst:Fe-mordenite In neat (no solvent) Fe-mordenite catalyst prepared by ion exchange and heat-treated at 425 °C, 92 % NH3 conversion, 99 % N2 selectivity, 1000 ppm NH3 in 2 %O2-contg. He;A 92%
B n/a
C 0%
With catalyst:Fe-ZSM-5 In neat (no solvent) Fe-ZSM-5 catalyst prepared by ion exchange and heat-treated at 375 °C, 90 % NH3 conversion, 99 % N2 selectivity, 1000 ppm NH3 in 2 % O2-contg. He;A 90%
B n/a
C 0%
mercury(II) fulminate

mercury(II) fulminate

phenylhydrazine
100-63-0

phenylhydrazine

A

nitrogen
7727-37-9

nitrogen

B

mercury

mercury

Conditions
ConditionsYield
at room temperature;A n/a
B 100%
at room temperature;A n/a
B 100%
hydroxylamine
7803-49-8

hydroxylamine

nitrogen
7727-37-9

nitrogen

Conditions
ConditionsYield
silver (I) ion In water catalytic oxydation in presence of AgCl at pH=7.2;;100%
silver (I) ion In water catalytic oxydation in presence of AgI at pH=12.7;;91%
silver (I) ion In water catalytic oxydation in presence of (Ag(S2O3)2)(3-) at pH=12.7;;89%
barium hydrazine disulfinate

barium hydrazine disulfinate

A

barium sulfite

barium sulfite

B

nitrogen
7727-37-9

nitrogen

Conditions
ConditionsYield
5 d;A 100%
B n/a
5 d;A 100%
B n/a
(dinitrogen)bis(1,2-bis(diehylphosphino)ethane)iron(0)

(dinitrogen)bis(1,2-bis(diehylphosphino)ethane)iron(0)

A

nitrogen
7727-37-9

nitrogen

B

oxygen
80937-33-3

oxygen

Conditions
ConditionsYield
With HCl In tetrahydrofuran acidolysis (excess of HCl);A 100%
B 96%
In sulfuric acid aq. H2SO4;A 77%
B 90%
poly(sulfur nitride)
12033-56-6

poly(sulfur nitride)

A

(S3N3)
79796-30-8

(S3N3)

B

nitrogen
7727-37-9

nitrogen

Conditions
ConditionsYield
In neat (no solvent, gas phase) by heating to 130-150°C at low pressure; at temp. > 450°CS2, N2, S2N2 are produced; at temp. < 130°C S4N2, S4N4, S2N2 areproduced; various product ratio for various conditions; further products; detected by He I photoelectron spectroscopy and quadrupole mass specrometry;A 100%
B <1
(PPh3)3CoH(N2)
21373-88-6, 16920-54-0

(PPh3)3CoH(N2)

2,2,2-trifluoroethyl benzoate
1579-72-2

2,2,2-trifluoroethyl benzoate

A

(trifluoroethoxo)tris(triphenylphosphine)cobalt(I)
99668-73-2

(trifluoroethoxo)tris(triphenylphosphine)cobalt(I)

B

benzoic acid benzyl ester
120-51-4

benzoic acid benzyl ester

C

nitrogen
7727-37-9

nitrogen

D

hydrogen
1333-74-0

hydrogen

E

benzene
71-43-2

benzene

Conditions
ConditionsYield
In toluene PhCOOCH2CF3 added to toluene soln. of CoH(N2)(PPh3)3, evacuated, stirred at 20°C for 2 days;A n/a
B 28%
C 100%
D 17%
E 32%
strontium nitride diazenide

strontium nitride diazenide

A

strontium nitride diazenide

strontium nitride diazenide

B

nitrogen
7727-37-9

nitrogen

Conditions
ConditionsYield
In neat (no solvent) loading and unloading carried out in inert gas; heated at 920 K and pressure of 9 bar; elem. anal.;A 100%
B n/a
strontium diazenide

strontium diazenide

A

strontium nitride diazenide

strontium nitride diazenide

B

nitrogen
7727-37-9

nitrogen

Conditions
ConditionsYield
In neat (no solvent) High Pressure; loading and unloading carried out in inert gas; heated at 920 K and pressure of 400 bar; elem. anal.;A 100%
B n/a
strontium diazenide

strontium diazenide

A

strontium nitride

strontium nitride

B

nitrogen
7727-37-9

nitrogen

Conditions
ConditionsYield
In neat (no solvent) loading and unloading carried out in inert gas; heated at 618 K and pressure of 1E-5 bar; elem. anal.;A 100%
B n/a
ferrocenium trifluoromethanesulfonate

ferrocenium trifluoromethanesulfonate

Na(1+)*[Mo(N(C((2)H3C)2CH3)((CH3)2C6H3))3(N2)](1-)*99C4H8O=Na[Mo(N(C((2)H3C)2H3C)((CH3)2C6H3))3N2]*99C4H8O

Na(1+)*[Mo(N(C((2)H3C)2CH3)((CH3)2C6H3))3(N2)](1-)*99C4H8O=Na[Mo(N(C((2)H3C)2H3C)((CH3)2C6H3))3N2]*99C4H8O

A

Mo(N(C(CD3)2CH3)-3,5-C6H3Me2)3

Mo(N(C(CD3)2CH3)-3,5-C6H3Me2)3

B

nitrogen
7727-37-9

nitrogen

Conditions
ConditionsYield
In tetrahydrofuran -35°C or 25°C; followed by IR and NMR spectroscopy;A 100%
B n/a
ammonia
7664-41-7

ammonia

nitrogen
7727-37-9

nitrogen

Conditions
ConditionsYield
With oxygen In gaseous matrix 450°C; (NH3) = 1000 ppm; (O2) = 2%; He = balance; total flow rate = 500 ml/min; space velocity = 2.3 10**5 1/h;99%
With oxygen In gaseous matrix 450°C; (NH3) = 1000 ppm; (O2) = 2%; He = balance; total flow rate = 500 ml/min; space velocity = 2.3 10**5 1/h;97%
With oxygen In gaseous matrix byproducts: N2O, NO; 400°C; (NH3) = 1000 ppm; (O2) = 2%; He = balance; total flow rate = 500 ml/min; space velocity = 2.3 10**5 1/h;93%
ammonia
7664-41-7

ammonia

A

nitrogen
7727-37-9

nitrogen

B

nitrogen(II) oxide
10102-43-9

nitrogen(II) oxide

C

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

Conditions
ConditionsYield
With oxygen In neat (no solvent) Fe-mordenite catalyst prepared by ion exchange and heat-treated at 450 °C, 99 % NH3 conversion, 100 % N2 selectivity, 1000 ppm NH3 in 2 % O2-contg. He;A 99%
B 0%
C 0%
With oxygen; platinum high excess O2,500 °C;A <1
B n/a
C n/a
With oxygen; platinum at 300 °C;A n/a
B <9
C n/a
ammonia
7664-41-7

ammonia

oxygen
80937-33-3

oxygen

A

nitrogen
7727-37-9

nitrogen

B

nitrogen(II) oxide
10102-43-9

nitrogen(II) oxide

Conditions
ConditionsYield
Sr0.22La0.78CoO2.843 In neat (no solvent) byproducts: H2O; 800°C;A n/a
B 98.6%
Sr0.42La0.68CoO2.80 In neat (no solvent) byproducts: H2O; 800°C;A n/a
B 98.1%
Sr0.46La0.54CoO2.79 In neat (no solvent) byproducts: H2O; 800°C;A n/a
B 98%
tetrabutylammonium dimethylaurate(I)
228118-52-3

tetrabutylammonium dimethylaurate(I)

A

nitrogen
7727-37-9

nitrogen

Conditions
ConditionsYield
With ClC6H4N2(1+) In tetrahydrofuran byproducts: ClC6H5, CH4, C2H6; -78°C;A 98%
B n/a
With 2,4,6-trichlorobenzenediazonium PF6 In acetonitrile byproducts: 2,4,6-trichlorobenzene, CH4, C2H6; -78°C;A 96%
B n/a
With CH3OC6H4N2(1+) In tetrahydrofuran byproducts: CH3OC6H5, C2H6; -78°C;A 96%
B n/a
ammonium nitrate

ammonium nitrate

A

nitrogen
7727-37-9

nitrogen

B

nitrogen(II) oxide
10102-43-9

nitrogen(II) oxide

C

Nitrogen dioxide
10102-44-0

Nitrogen dioxide

D

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

Conditions
ConditionsYield
at 220-260°C, nearly 98% N2O, 2% N2; troces of NO and NO2 (0.001%);A 2%
B n/a
C n/a
D 98%
potassium cyanide

potassium cyanide

nitrogen
7727-37-9

nitrogen

Conditions
ConditionsYield
With copper(II) oxide In neat (no solvent) heating in a stream of CO2, ratio KCN:CuO=2:10, gegin of react. at 115°C, formation of 98% N2 at 420°C;;98%
With CuO In neat (no solvent) heating in a stream of CO2, ratio KCN:CuO=2:10, gegin of react. at 115°C, formation of 98% N2 at 420°C;;98%
heating; exclusion of air; anhydrous KCN;
(PPh3)3CoH(N2)
21373-88-6, 16920-54-0

(PPh3)3CoH(N2)

2,2,2-trifluoroethyl acetate
406-95-1

2,2,2-trifluoroethyl acetate

A

methane
34557-54-5

methane

B

(trifluoroethoxo)tris(triphenylphosphine)cobalt(I)
99668-73-2

(trifluoroethoxo)tris(triphenylphosphine)cobalt(I)

C

nitrogen
7727-37-9

nitrogen

D

hydrogen
1333-74-0

hydrogen

E

ethyl acetate
141-78-6

ethyl acetate

Conditions
ConditionsYield
In toluene CH3COOCH2CF3 added to toluene soln. of CoH(N2)(PPh3)3, evacuated, stirred at room temp. for 2 days; hexane added, solid recrystd. from toluene-hexane; elem. anal.;A 1%
B 40%
C 98%
D 23%
E 30%
hydrogen
1333-74-0

hydrogen

nitrogen(II) oxide
10102-43-9

nitrogen(II) oxide

Nitrogen dioxide
10102-44-0

Nitrogen dioxide

A

nitrogen
7727-37-9

nitrogen

B

ammonia
7664-41-7

ammonia

Conditions
ConditionsYield
With catalyst: industrial nickel methanation catalyst In neat (no solvent) reduction of mixt. of NO/NO2 in gas mixt. of N2/H2 on zeolite catalyst (pretreated in H2 at 550°C, 200°C reaction temp.); gas chromy. (dimethylsulfolane coated diatomite);A 96%
B 0%
With catalyst: industrial nickel methanation catalyst In neat (no solvent) reduction of mixt. of NO/NO2 in gas mixt. of N2/H2 on zeolite catalyst (pretreated in H2 at 300°C, 200°C reaction temp.); gas chromy. (dimethylsulfolane coated diatomite);A 92.5%
B 7.5%
With catalyst: industrial nickel methanation catalyst In neat (no solvent) reduction of mixt. of NO/NO2 in gas mixt. of N2/H2 on zeolite catalyst (pretreated in H2 at 300°C, 150°C reaction temp.); gas chromy. (dimethylsulfolane coated diatomite);A 91%
B 0%
1,3-di-tert-butyl-2,2-dimethyl-1,3,2,4-diazasilagermaetidine
84806-15-5

1,3-di-tert-butyl-2,2-dimethyl-1,3,2,4-diazasilagermaetidine

Phenyl azide
622-37-7

Phenyl azide

A

1,3,7,9-tetra-tert-butyl-2,2,8,8-tetramethyl-5,10-diphenyl-1,3,5,7,9,10-hexaaza-2,8-disila-4,6-digermadispiro{3.1.3.1}decane
138174-58-0

1,3,7,9-tetra-tert-butyl-2,2,8,8-tetramethyl-5,10-diphenyl-1,3,5,7,9,10-hexaaza-2,8-disila-4,6-digermadispiro{3.1.3.1}decane

B

nitrogen
7727-37-9

nitrogen

Conditions
ConditionsYield
In tetrahydrofuran under Ar, dropwise addn. of THF soln. of diaminogermylene to THF soln. of phenyl azide at -25.degreeC, 3h; pptn., recrystn. (THF), elem. anal.;A 64%
B 96%
In tetrahydrofuran under Ar, dropwise addn. of THF soln. of diaminogermylene to THF soln. of phenyl azide at 25.degreeC, 3h; pptn., recrystn. (THF), elem. anal.;A 64%
B 83%
tetra-n-butylammonium tetramethylaurate(III)

tetra-n-butylammonium tetramethylaurate(III)

trimethyl(triphenylphosphine)gold(III)

trimethyl(triphenylphosphine)gold(III)

B

nitrogen
7727-37-9

nitrogen

Conditions
ConditionsYield
With 4-chlorobenzenediazonium hexafluorophosphate byproducts: CH4, ClC6H5;A 91%
B 96%
tetra-n-butylammonium tetramethylaurate(III)

tetra-n-butylammonium tetramethylaurate(III)

A

nitrogen
7727-37-9

nitrogen

Conditions
ConditionsYield
With CH3OC6H4N2(1+) In tetrahydrofuran byproducts: CH3OC6H5, C2H6, CH4; -78°C;A 95%
B n/a
With 2,4,6-trichlorobenzenediazonium PF6 In tetrahydrofuran byproducts: 2,4,6-trichlorobenzene, CH4, C2H6; -78°C;A 94%
B n/a
With 2,4,6-trichlorobenzenediazonium PF6 In acetonitrile byproducts: 2,4,6-trichlorobenzene, CH4, C2H6; -78°C;A 94%
B n/a
(NaCl(C9H5CH(CH3)2CH3)2Zr)2N2

(NaCl(C9H5CH(CH3)2CH3)2Zr)2N2

iodine
7553-56-2

iodine

A

(C9H5CH(CH3)2CH3)2ZrI2
1072431-21-0, 1072431-11-8

(C9H5CH(CH3)2CH3)2ZrI2

B

nitrogen
7727-37-9

nitrogen

Conditions
ConditionsYield
A 95%
B n/a
ammonia
7664-41-7

ammonia

A

nitrogen
7727-37-9

nitrogen

B

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

Conditions
ConditionsYield
With oxygen In gaseous matrix byproducts: NO; 0.2 g of catalyst, 1000 ppm NH3, 2% O2, He as balance, GHSV=2.0E+5 h**-1, at 450°C; mass spect.;A 94%
B 0%
With oxygen In gaseous matrix byproducts: NO; 0.2 g of catalyst, 1000 ppm NH3, 2% O2, He as balance, GHSV=2.0E+5 h**-1, at 400°C; mass spect.;A 93%
B 0%
With oxygen In gaseous matrix byproducts: NO; 0.2 g of catalyst, 1000 ppm NH3, 2% O2, He as balance, GHSV=2.0E+5 h**-1, at 400°C; mass spect.;A 92%
B 0%
ammonia
7664-41-7

ammonia

chlorine
7782-50-5

chlorine

A

chloroamine
12190-75-9

chloroamine

B

nitrogen
7727-37-9

nitrogen

C

ammonium chloride

ammonium chloride

Conditions
ConditionsYield
In neat (no solvent) NH3:Cl2 = 39; at ambient temp.;;A 94%
B n/a
C n/a
In neat (no solvent) NH3:Cl2 = 9; at ambient temp.;;A 5%
B n/a
C n/a
In neat (no solvent) Cl2:NH3 = 1:10-50; reaction of Cl2 and NH3 dild. with N2 below 180°C under pressure;;
In neat (no solvent) Cl2:NH3:N2 = 1:20:8; at 100°C;;
(dinitrogen)bis(1,2-bis(diehylphosphino)ethane)iron(0)

(dinitrogen)bis(1,2-bis(diehylphosphino)ethane)iron(0)

nitrogen
7727-37-9

nitrogen

Conditions
ConditionsYield
In neat (no solvent, solid phase) thermolysis (150°C, 3 h);94%
nitrogen
7727-37-9

nitrogen

magnesium
7439-95-4

magnesium

magnesium nitride

magnesium nitride

Conditions
ConditionsYield
In neat (no solvent) Mg (purity: 99.5%) was heated in N2 (free of O2) at 800-850 °C for 4-5 h;;100%
In neat (no solvent) Mg was heated in a stream of N2 at 900 °C;;95%
nitrogen
7727-37-9

nitrogen

barium
7440-39-3

barium

barium nitride

barium nitride

Conditions
ConditionsYield
260-560°C, then 0.5h at 600°C;100%
In neat (no solvent) exothermic formation out of the elements at temperatures under the melting point of Ba; after heating cooling to keeping the necessary temperature;;
above 190°C; 96.15% Ba3N2;
nitrogen
7727-37-9

nitrogen

barium
7440-39-3

barium

barium subnitride

barium subnitride

Conditions
ConditionsYield
In neat (no solvent) loading and unloading carried out in inert gas; Ba metal loaded in tungsten crucible, which palced in a steel tube before loaded in quartz glasstube; evacuated (p<1E-6 bar); heated in stream of nitrogen at 1120 K fo r 24 h; evacuated again (p<1E-6 bar) for 24 h at 900 K; elem. anal.;100%
In further solvent(s) absence of air and moisture; passing N2 through soln. of Ba in liquid Naat 573 K (pptn.); filtration; reaction followed by resistivity measurements;
In further solvent(s) under inert atmosphere; Ba submerged in molten Na in stainless steel crucible; sealed; evacuated; filled with N2; heated at 973 K for 48 h; cooled under vac.; heated at 723 K for 24 h; cooled to room temp.; opened in Ar filled glovebox; detd. by X-ray powder diffraction;
bismuth
7440-69-9

bismuth

nitrogen
7727-37-9

nitrogen

bismuth nitride

bismuth nitride

Conditions
ConditionsYield
In neat (no solvent) Electrochem. Process; cothodic pulverization within 10 hours of Bi under pure N2 (0.1 - 0.3 Torr), glow-discharge at 1000-1500 V; anode Fe; description of the aparatus given;; 359.8 mg BiN; deposition of 12.1 weight % on cathode, of 45.4 weight % on anode, 25.2 weight % on glass parts of the aparatus, 17.3 weight % on Fe- (or Al-) protecting ring of the aparatus;;100%
In further solvent(s) Electric Arc; between Bi-cathode and Cu-anode in a liquid mixture of argon and nitrogen;;
In further solvent(s) Electric Arc; between Bi-cathode and Cu-anode in a liquid mixture of argon and nitrogen;;
In neat (no solvent) cathodic pulverization of Bi during glow discharge under N2 (0.1 - 0.3 torr);;
nitrogen
7727-37-9

nitrogen

strontium

strontium

strontium nitride

strontium nitride

Conditions
ConditionsYield
In neat (no solvent) loading and unloading carried out in inert gas; Sr metal loaded in tungsten crucible, which palced in a steel tube before loaded in quartz glasstube; evacuated (p<1E-6 bar); heated in stream of nitrogen at 1120 K fo r 24 h; evacuated again (p<1E-6 bar); for 24 h at 900 K; elem. anal.;100%
In gas other Radiation; strontium deposited on MgO substrate at temp. 673 K under irradn. of nitrogen radicals (RF power 350 W, N2 feed 3.0 cm**+3(STP)min**-1); annealed in vac. at 673 K or continuous nitrogen radical irradn. for 30 min; cooled;
In neat (no solvent) Fresh Sr filings are loaded into a Al2O3 jacket which is itself placed in a quartz tube. The assembly is evacuated to E-5 Torr. N2 is introduced into the vacuum line to a total pressure of 100 Torr. The temp. is slowly increased to 750°C.;
nitrogen
7727-37-9

nitrogen

ammonia
7664-41-7

ammonia

benzene
71-43-2

benzene

hydrogen cyanide
74-90-8

hydrogen cyanide

Conditions
ConditionsYield
With catalyst: Pt-oxide at 1000°C;100%
platinum at 1000°C;100%
platinum at 800°C;62.8%
With catalyst: Pt-oxide at 800°C;62.8%
Mo(N(C(CD3)2CH3)-3,5-C6H3Me2)3

Mo(N(C(CD3)2CH3)-3,5-C6H3Me2)3

nitrogen
7727-37-9

nitrogen

sodium triethylborohydride

sodium triethylborohydride

[Mo(N(C((2)H3C)2CH3)((CH3)2C6H3))3N]
163929-87-1

[Mo(N(C((2)H3C)2CH3)((CH3)2C6H3))3N]

Conditions
ConditionsYield
In tetrahydrofuran; toluene stirring (25°C, N2 atmosphere, 24 h); evapn. (vac.);100%
strontium nitride diazenide

strontium nitride diazenide

nitrogen
7727-37-9

nitrogen

strontium diazenide

strontium diazenide

Conditions
ConditionsYield
In neat (no solvent) High Pressure; loading and unloading carried out in inet gas; SrN loaded in a Mo boat, which placed in an autoclave; evacuated; filled up with N2; heated at 920 K for 24 h at 5500 bar; elem. anal.;100%
Mo(N(C(CD3)2CH3)-3,5-C6H3Me2)3

Mo(N(C(CD3)2CH3)-3,5-C6H3Me2)3

nitrogen
7727-37-9

nitrogen

[Mo(N(C((2)H3C)2CH3)((CH3)2C6H3))3N]
163929-87-1

[Mo(N(C((2)H3C)2CH3)((CH3)2C6H3))3N]

Conditions
ConditionsYield
With sodium amalgam In tetrahydrofuran stirring (28°C, 1 atm. N2);100%
With 1-methyl-1H-imidazole In diethyl ether 25°C, ether, 1 atm. of N2, 1 equiv of 1-methylimidazole, 6 h; evapd., extd. with pentane, filtered, evapd., recrystd. from pentane at -35°C;91%
With dmap In diethyl ether 25°C, ether, 1 atm. of N2, 4-dimethylaminopyridine, 24 h; evapd., extd. with pentane, filtered, evapd., recrystd. from pentane at -35°C;85%
Mo(N[((t)Bu)(3,5-C6H3Me2)])3

Mo(N[((t)Bu)(3,5-C6H3Me2)])3

nitrogen
7727-37-9

nitrogen

A

Na(1+)*[Mo(N(C(CH3)3)((CH3)2C6H3))3(N2)](1-)*99C4H8O=Na[Mo(N(C(CH3)3)((CH3)2C6H3))3(N2)]*99C4H8O

Na(1+)*[Mo(N(C(CH3)3)((CH3)2C6H3))3(N2)](1-)*99C4H8O=Na[Mo(N(C(CH3)3)((CH3)2C6H3))3(N2)]*99C4H8O

B

[Mo(N(C((2)H3C)2CH3)((CH3)2C6H3))3N]
163929-87-1

[Mo(N(C((2)H3C)2CH3)((CH3)2C6H3))3N]

Conditions
ConditionsYield
With sodium amalgam In tetrahydrofuran addn. of soln. of Mo-complex to stirred suspn. of amalgam (syringe pump,10 h); decantation, filtration (Celite), evapn. (vac.), dissoln. (pentane), filtration (Celite), evapn. (vac.);A 100%
B 1%
strontium nitride diazenide

strontium nitride diazenide

nitrogen
7727-37-9

nitrogen

strontium nitride diazenide

strontium nitride diazenide

Conditions
ConditionsYield
In neat (no solvent) High Pressure; loading and unloading carried out in inet gas; Sr4N3 loaded in a Mo boat, which placed in an autoclave; evacuated; filled up with N2; heated at 920 K for 24 h at 400 bar; elem. anal.;100%
strontium nitride

strontium nitride

nitrogen
7727-37-9

nitrogen

strontium diazenide

strontium diazenide

Conditions
ConditionsYield
In neat (no solvent) High Pressure; loading and unloading carried out in inet gas; Sr2N loaded in a Mo boat,which placed in an autoclave; evacuated; filled up with N2; heated at 9 20 K for 24 h at 5500 bar; elem. anal.;100%
High Pressure; under N2 pressure of 5500 bar; heated at 920 K in Mo-boat for 72 h; initial pressure about 2720 bar; X-ray and neutron diffraction; TG/DTA; elem. anal.;
lithium nitride

lithium nitride

nitrogen
7727-37-9

nitrogen

Li2.7Fe0.3N

Li2.7Fe0.3N

Conditions
ConditionsYield
In neat (no solvent) Li3N fused in pure iron vessel; sealed under 300 kPa of N2; heated at 850-1050°C for 12 h; thermally quenched; detd. by X-ray powder diffraction;100%
(RuH(μ-Cl)(triisopropylphosphine)2
262359-17-1

(RuH(μ-Cl)(triisopropylphosphine)2

nitrogen
7727-37-9

nitrogen

RuHCl(triisopropylphosphine)2(N2)
262359-18-2

RuHCl(triisopropylphosphine)2(N2)

Conditions
ConditionsYield
In benzene-d6 (Ar); soln. of Ru-complex in benzene-d6 added to NMR tube, sample degassed, benzene frozen in ice, tube filled with N2 to ca. 1 atm., tube agitated for 5 min;100%
Sr0992Eu0.008(Al0.5Si0.5)2

Sr0992Eu0.008(Al0.5Si0.5)2

nitrogen
7727-37-9

nitrogen

SrAlSiN3#dotEu(2+)

SrAlSiN3#dotEu(2+)

Conditions
ConditionsYield
In neat (no solvent) alloy powder transferred into boron nitride crucible, loaded into hot isostatic pressing with graphite heater, N2 pressure raised to 190 MPa at room temp., heated to 2173 K, held for 2 h, temp. reduced to ca. 473 K, pressure to 70 MPa; cooled to room temp.; detd. by XRD;100%
Ca(0.2-x)Sr0.8Eu(x)(Al0.5Si0.5)2

Ca(0.2-x)Sr0.8Eu(x)(Al0.5Si0.5)2

nitrogen
7727-37-9

nitrogen

Sr0.8Ca0.2AlSiN3#dotEu(2+)

Sr0.8Ca0.2AlSiN3#dotEu(2+)

Conditions
ConditionsYield
In neat (no solvent) alloy powder transferred into boron nitride crucible, loaded into hot isostatic pressing with graphite heater, N2 pressure raised to 50 MPa at room temp., heated to 2173 K, held for 2 h, temp. reduced to ca. 473 K, pressure to 70 MPa; cooled to room temp.; detd. by XRD;100%
Ca(0.5-x)Sr0.5Eu(x)(Al0.5Si0.5)2

Ca(0.5-x)Sr0.5Eu(x)(Al0.5Si0.5)2

nitrogen
7727-37-9

nitrogen

Sr0.5Ca0.5AlSiN3#dotEu(2+)

Sr0.5Ca0.5AlSiN3#dotEu(2+)

Conditions
ConditionsYield
In neat (no solvent) alloy powder transferred into boron nitride crucible, loaded into hot isostatic pressing with graphite heater, N2 pressure raised to 50 MPa at room temp., heated to 2173 K, held for 2 h, temp. reduced to ca. 473 K, pressure to 70 MPa; cooled to room temp.; detd. by XRD;100%

7727-37-9Relevant articles and documents

Can TiO2 promote the reduction of nitrates in water?

Sa, Jacinto,Berger, Thomas,Foettinger, Karin,Riss, Alexander,Anderson, James A.,Vinek, Hannelore

, p. 282 - 291 (2005)

Monometallic palladium catalysts were synthesized using different titanium supports and tested for the reduction of nitrates from aqueous solutions using hydrogen as a reductant. The Pd/TiO2 catalysts were characterized by electron paramagnetic resonance (EPR), low-temperature Fourier transform infrared (FTIR) spectroscopy of adsorbed CO, and X-ray diffraction (XRD). The catalysts studied exhibited a high activity for nitrate removal with a lower tendency for nitrite formation than the conventional bimetallic Pd catalysts. Although ammonium formation was greater than desired, the use of a monometallic catalyst for this two-step reduction process is significant and suggests that a single site may be responsible for both reduction stages. The titanium support (particularly the Ti3+ centers generated during prereduction in the presence of Pd) appear to play an important role in the nitrate degradation process. The potential role of Pd β-hydride in generating these Ti 3+ centers is discussed.

Complexation of nitrous oxide by frustrated lewis pairs

Otten, Edwin,Neu, Rebecca C.,Stephan, Douglas W.

, p. 9918 - 9919 (2009)

(Figure Presented) Frustrated Lewis pairs comprised of a basic yet sterically encumbered phosphine with boron Lewis acids bind nitrous oxide to give intact PNNOB linkages. The synthesis, structure, and bonding of these species are described.

Reaction between NOx and NH3 on Iron Oxide-Titanium Oxide Catalyst

Kato, Akira,Matsuda, Shimpei,Kamo, Tomoichi,Nakajima, Fumito,Kuroda, Hiroshi,Narita, Tsuneo

, p. 4099 - 4102 (1981)

The reduction of NOx (NO2 alone or mixture of NO and NO2) with NH3 on iron oxide-titanium oxide catalyst was studied using a flow reactor.The reaction between NO2 and NH3 proceeds at 3:4 mole ratio in the presence or absence of oxygen.When the reaction gas mixture contain equal amounts of NO and NO2, the reaction consuming equimolal NO and NO2 proceeds preferentially at a NH3/NOx ratio of unity.The rate of the reaction is faster than either the NO-NH3 or NO2-NH3 reaction.The overall reactions between NOx (NO2, NO+NO2) and NH3 are given as 6NO2+8NH3->7N2+12H2O and NO+NO2+2NH3->2N2+3H2O.Reaction mechanisms are proposed to explain the experimental results.

Characterization of vanadium and titanium oxide supported SBA-15

Segura,Cool,Kustrowski,Chmielarz,Dziembaj,Vansant

, p. 12071 - 12079 (2005)

Supported vanadium and titanium oxide catalysts were prepared by adsorption and subsequent calcination of the vanadyl and titanyl acetylacetonate complexes, respectively, on mesoporous SB A-15 by the molecular designed dispersion (MDD) method. Liquid and gas phase depositions at different temperatures were carried out with vanadyl acetylacetonate, and the different results together with those of titanyl acetylacetonate in the liquid phase deposition were discussed. The bonding mechanism, the influence of the metal interaction with the support material, and differences due to the way of deposition and the temperature were investigated by TGA, chemical analysis, FTIR, and Raman spectroscopy. Elevated dissolving temperatures in the liquid phase led to higher final loadings on the SBA-15 without the formation of clusters, even at high loadings. The decomposition of the anchored vanadium and titanium complexes, their thermal stability, and the conversion to the covalently bound VOX and TiOx species on SBA-15 were studied and investigated by in situ transmission IR spectroscopy. In general, the titanium complex is more reactive than the vanadium complex toward the surface of SBA-15 and has a higher thermal stability. The MDD method of the VO(acac)2 and TiO(acac)2 enables to create a dispersed surface of supported VOx and TiOx, respectively. The structure configurations of VOx and TiOx oxide catalysts obtained at different metal loadings were studied by Raman spectroscopy. Pore size distributions, XRD, and N2 sorption confirmed the structural stability of these materials after grafting. VOx/SBA-15 and TiO x/SBA-15 samples, with different metal loadings, were also catalytically tested for the selective catalytic reduction (SCR) of NO with ammonia. ? 2005 American Chemical Society.

The 193 (and 248) nm photolysis of HN3: Formation and internal energy distributions of the NH (a1Δ, b1Σ+, A3Π, and c1Π) states

Rohrer, F.,Stuhl, F.

, p. 4788 - 4799 (1988)

The UV photolysis of HN3 at 193 nm was investigated in detail in the bulk phase at 300 K.NH radicals in the X, a, b, A, and c states were found to be formed with quantum yields 0.0019 , 0.4, 0.017, 0.00015, and 0.000 61, respectively.Relative rotational and vibrational populations were measured for all states except for NH(X).Average translational energies were estimated for NH(a,ν = 0 and 1 ) and NH(b,ν = 0).The 248 nm photolysis of HN3 was reinvestigated with respect to processes forming NH radicals other than NH(a).The observed energy distributions differ for both laser wavelengths and for high and low lying NH states.The distribution can be better described by a simple impulsive than by a statistical model.Some conclusions are drawn concerning the upper HN3 potential surfaces involved.

Photocatalytic reduction of nitrate over chalcopyrite CuFe0.7Cr0.3S2 with high N2 selectivity

Wang, Rong,Yue, Mufei,Cong, Rihong,Gao, Wenliang,Yang, Tao

, p. 731 - 736 (2015)

Photocatalytic reduction of nitrate (NO3-) is a green and potentially inexpensive technique for reducing NO3- pollution in ground water. TiO2-based photocatalysts have been studied extensively for this purpose. In the present study, the semiconducting catalyst CuFe0.7Cr0.3S2 was applied to NO3- reduction. Loading this catalyst with metal co-catalysts (Ru, Au, Cu, Ag, Pt, and Pd) greatly increased the rate of NO3- reduction and the N2 selectivity. In addition, there was a synergistic enhancement of the photocatalytic performance when the catalyst was loaded two co-catalysts. For example, the catalyst loaded with Pd and Au at mass fractions of 0.75% and 3%, respectively, could photocatalyze the complete reduction of NO3- in a 100 ppm N aqueous solution with 100% N2 selectivity in less than 5 h with UV irradiation. However, with an inner irradiation from a full-arc Xe lamp, the NO3- conversion rate reduced to 0.065 mg N/h, probably because of the low density of the photoexcited electrons. The results show the potential of metal sulfides for photocatalytic reduction of NO3-, and the possibility of use of visible light.

Oscillations in the N2O-H2 reaction over Ir(1 1 0). Route to chaos

Carabineiro, Sónia A.C.,Van Noort, Wibo D.,Nieuwenhuys, Bernard E.

, p. 96 - 102 (2003)

The study described in the present paper is focused on the N2O-H2 reaction on the Ir(1 1 0) surface and, in particular, on different kinds of oscillatory behaviour, including the route to chaos. Oscillations in rate were observed in the temperature range between 460 and 464 K, at a N2O pressure of 1 × 10-6 mbar with H2/N2O ratios close to 1. Upon minor changes in the H2/N2O ratio, a series of period doublings is observed, resulting finally in aperiodic behaviour.

Nature and catalytic role of active silver species in the lean NO x reduction with C3H6 in the presence of water

Iglesias-Juez,Hungria,Martinez-Arias,Fuerte,Fernandez-Garcia,Anderson,Conesa,Soria

, p. 310 - 323 (2003)

A study of the lean NOx reduction activity with propene in the presence of water over Ag/Al2O3 catalysts with different silver loadings (1.5-6 wt%) has been done using X-ray diffraction, ultraviolet-visible spectroscopy, transmission electron microscopy, and in situ diffuse reflectance infrared and X-ray absorption spectroscopies under reaction conditions. The catalysts were prepared by an impregnation method employing EDTA complexes that allow highly dispersed silver phases to be obtained, which are stabilized under reaction conditions by strong interactions with the support. It is shown that the active species corresponds to silver aluminate-like phases with tetrahedral local symmetry. The role of silver in the reaction mechanism is shown to be mainly in the activation of NO x and propene species. In particular, the silver entities have been found to offer a new reaction path for propene activation which involves generation of acrylate species as a partially oxidized active intermediate. Differences between two active catalysts containing 1.5 and 4.5 wt% of Ag suggest that optimization of the SCR activity can be related to the oxygen lability of the tetrahedral silver aluminate-like phase present in the catalyst. As postulated previously, the high nonselective propene oxidation activity of the highest loaded sample (with 6 wt% Ag) appears to be related to formation of metallic silver surface states at low reaction temperatures which are active for NO dissociation.

Nano-spatially confined Pd-Cu bimetals in porous N-doped carbon as an electrocatalyst for selective denitrification

Bai, Nan,Chen, Zehan,Fan, Jianwei,Gu, Tianhang,Teng, Wei,Zhang, Wei-Xian,Zhao, Dongyuan

, p. 9545 - 9553 (2020)

Bimetals have attracted considerable attention as electrocatalysts towards selective reduction of nitrate to benign dinitrogen. Design of highly efficient and stable bimetallic catalysts by taking the effects of both active sites increasing and synergistic composition into account is of paramount importance but still a grand challenge. Herein we report novel bimetallic Pd-Cu nanoparticles (NPs) incorporated in porous N-doped carbon octahedra prepared by a spatial confinement strategy ofin situpyrolysis of metal-organic frameworks with the assistance of polyvinyl pyrrolidone (PVP) as electrocatalysts achieving targeted denitrification. Pd-Cu NPs exhibit superior dispersity with a N-doped matrix and are strongly dependent on the variation of PVP, Pd precursor and pyrolysis temperature. The material shows high efficiency (~97.1%) for the reduction of nitrate from 100 to 2.9 mg NO3--N L-1(well below drinking water standards of 10 mg NO3--N L-1), and especially the selectivity over 83% for benign N2at neutral pH within 24 h. Encapsulated and well-dispersed Pd-Cu NPs and doped N in the carbonaceous matrix synergistically enhance the interfacial electron transfer for transformation of NO3--N(v). Porous structures endow the catalyst with outstanding stability after eight cycles and over a wide pH of 4-10. More importantly, the nanocatalyst performs well with real contaminated water (selectivity of 91% for nitrogen) in laboratory batch reactors. This nanocatalyst shows promise in wastewater treatment and environmental remediation due to the spatial confinement strategy and introduction of heterogeneous atoms.

Promotional effects of Zr on K+-poisoning resistance of CeTiOx catalyst for selective catalytic reductionof NOx with NH3

Xu, Baoqiang,Xu, Haidi,Lin, Tao,Cao, Yi,Lan, Li,Li, Yuanshan,Feng, Xi,Gong, Maochu,Chen, Yaoqiang

, p. 1354 - 1361 (2016)

CeTiOx and CeZrTiOx catalysts were prepared by a coprecipitation method and used for selective catalytic reduction of NOx by NH3 (NH3-SCR). Various amounts of KNO3 were impregnated on the catalyst surface to investigate the effects of Zr addition on the K+-poisoning resistance of the CeTiOx catalyst. The NH3-SCR performance of the catalysts showed that the NOx removal activity of the Zr-modified catalyst after poisoning was better than that of the CeTiOx catalyst. Brunauer-Emmett-Teller data indicated that the Zr-containing catalyst had a larger specific surface area and pore volume both before and after K+ poisoning. X-ray diffraction, Raman spectroscopy, and transmission electron microscopy showed that Zr doping inhibited anatase TiO2 crystal grain growth, i.e., the molten salt flux effect caused by the loaded KNO3 was inhibited. The Ce 3d X-ray photoelectron spectra showed that the Ce3+/Ce4+ ratio of CeZrTiOx decreased more slowly than that of CeTiOx with increasing K+ loading, indicating that Zr addition preserved more crystal defects and oxygen vacancies; this improved the catalytic performance. The acidity was a key factor in the NH3-SCR performance; the temperature-programmed desorption of NH3 results showed that Zr doping inhibited the decrease in the surface acidity. The results suggest that Zr improved the K+-poisoning resistance of the CeTiOx catalyst.

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