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10024-97-2

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10024-97-2 Usage

Description

dinitrogen monoxide’s (N2O) common name is nitrous oxide.Nitrous oxide is a colorless, nonfl ammable, nontoxic gas with a slightly sweet odor and taste. Nitrous oxide is produced by the thermal decomposition of ammonium nitrate at approximately 240°C: NH4NO3(g) → N2O(g) + 2H2O(g).Nitrous oxide is an important greenhouse gas. Its atmospheric residence time is 120 years. A molecule of N2O has 310 times the potential for absorbing heat compared to a molecule of CO2. Nitrous oxide is stable and unreactive on the earth’s surface, but it can be transported to the stratosphere where it absorbs energy and is converted into reactive forms of nitrogen such as nitric oxide and the nitrate radical contributing to ozone destruction.

Chemical Properties

Different sources of media describe the Chemical Properties of 10024-97-2 differently. You can refer to the following data:
1. A colorless gas without appreciable odor or a slightly sweetish odor and taste. One L at 0°C and at a pressure of 760 mm of mercury weighs about 1.97 g. One volume dissolves in about 1.4 volumes of water at 20°C and at a pressure of 760 mm of mercury. It is freely soluble in alcohol and soluble in ether and in oils. It is prepared by thermal decomposition of ammonium nitrate.
2. Colourless gas with sweetish odour
3. Nitrous oxide is a colorless gas. Slightly sweet odor. Shipped as a liquefied compressed gas.
4. Nitrous oxide is a nonflammable, colorless and odorless, sweettasting gas. It is usually handled as a compressed gas, stored in metal cylinders.
5. Nitrous oxide has a slight sweetish, odor and taste. This gas is also reported as without appreciable odor. At 0°C and a pressure of 760 mm of mercury, 1 L weighs about 1.97 g.

Physical properties

Colorless gas with faint sweet odor and taste; heavier than air, density in air 1.53 (air=1); gas density 1.977 g/L at 0°C; noncombustible gas; supports combustion; liquefies to a colorless liquid at -88.5°C; liquid density 1.226 g/mL at -89°C; freezes to a cubic crystalline solid at -90.8°C; dipole moment 0.166 ; critical temperature 36.5°C; critical pressure 71.7 atm; solubility in water: 130 mL gas dissolves in 100mL water at 0°C and 56.7 mL in 100 mL water at 25°C; soluble in alcohol, ether and sulfuric acid.

History

nitrous oxide was prepared in 1772 by Joseph Priestley (1733 1804) . Priestley called nitric oxide nitrous air, nitrogen dioxide nitrous acid vapor, and nitrous oxide phlogisticated nitrous air, but also referred to the dioxide. Priestley prepared nitric oxide by reacting nitric acid with a metal such as copper: 3Cu(s) + 8HNO3(aq) 2NO(g) + 3Cu(NO3)2(aq) + 4H2O(l).He prepared nitrous oxide by reducing nitric oxide using iron: 2NO(g) + H2O(l) + Fe(s) N2O(g) + Fe(OH)2(aq).For example, the year of discovery for nitrous oxide ranges between 1772 and 1793. Humphrey Davy (1778 1829) examined the physiological effects of nitrous oxide and in 1799 wrote Researches Chemical and Philosophical, Chiefly Concerning Nitrous Oxide.

Uses

Different sources of media describe the Uses of 10024-97-2 differently. You can refer to the following data:
1. Nitrous oxide is called laughing gas and has been used as a recreational inhalant, anesthetic, oxidizer, and propellant. Nitrous oxide is widely used as an anesthetic in dental surgery, which accounts for approximately 90% of its use. It is used by the dairy industry as a foaming agent for canned whipping creams. The gas is used as an anesthetic, especially in dentistry and minor surgery. It produces mild hysteria and laughter preceding the anesthetic effect, for which reason it also is called “laughing gas.” It is used as an aerosol propellant, an aerating agent for whipped cream, and an oxidizing agent at high temperatures. Nitrous oxide also is used in the preparation of nitrites and as a flame gas in flame atomic absorption spectrometry of metals.
2. Nitrous oxide is used in the productionof nitrites, in rocket fuel, as an inhalationanesthesia and analgesic agent.
3. Nitrous Oxide is a noncombustible gas used as a propellant in certain dairy and vegetable fat whipped toppings contained in pressurized containers.
4. Nitrous oxide was discovered by Priestley. It is found in the atmosphere in trace concentrations. The gas is used as an anesthetic, especially in dentistry and minor surgery. It produces mild hysteria and laughter preceding the anesthetic effect, for which reason it also is called “laughing gas.” It is used as an aerosol propellant, an aerating agent for whipped cream, and an oxidizing agent at high temperatures. Nitrous oxide also is used in the preparation of nitrites and as a flame gas in flame atomic absorption spectrometry of metals.
5. Nitrous oxide is still commonly used in combination with a volatile agent to maintain anaesthesia. However, there is growing concern regarding its toxic effects and cost. Consequently, medical air in combination with oxygen is now being used increasingly during anaesthesia.

Preparation

Prepared by thermal decomposition of ammonium nitrate NH4NO3 → N2O↑ + 2H2O

Definition

Different sources of media describe the Definition of 10024-97-2 differently. You can refer to the following data:
1. ChEBI: A nitrogen oxide consisting of linear unsymmetrical molecules with formula N2O. While it is the most used gaseous anaesthetic in the world, its major commercial use, due to its solubility under pressure in vegetable fats combined with ts non-toxicity in low concentrations, is as an aerosol spray propellant and aerating agent for canisters of 'whipped' cream.
2. A colorless gas with a faintly sweet odor and taste. It is appreciably soluble in water (1.3 volumes in 1 volume of water at 0°C) but more soluble in ethanol. It is prepared commercially by the careful heating of ammonium nitrate: NH4NO3(s) = N2O(g) + 2H2O(g) Dinitrogen oxide is fairly easily decomposed on heating to temperatures above 520°C, giving nitrogen and oxygen. The gas is used as a mild anesthetic in medicine and dentistry, being marketed in small steel cylinders. It is sometimes called laughing gas because it induces a feeling of elation when inhaled.

Production Methods

Different sources of media describe the Production Methods of 10024-97-2 differently. You can refer to the following data:
1. Prepared (1) by reaction of silver hyponitrite Ag2N2O2 and hydrogen chloride in anhydrous ether, an evaporation of the resulting solution, (2) by reaction of hydroxylamine H2NOH plus nitrous acid HONO.
2. Nitrous oxide is prepared by heating ammonium nitrate to about 170°C. This reaction also forms water.

Biological Functions

N2O (commonly called laughing gas) produces its anesthetic effect without decreasing blood pressure or cardiac output. Although it directly depresses the myocardium, cardiac depression is offset by an N2O– mediated sympathetic stimulation. Likewise, respiration is maintained.Tidal volume falls, but minute ventilation is supported by a centrally mediated increase in respiratory rate. However, since the respiratory depressant effect of N2O are synergistic with drugs such as the opioids opioids and benzodiazepines, N2O should not be considered benign. Deep levels of anesthesia are unattainable, even when using the highest practical concentrations of N2O (N2O 60–80% with oxygen 40–20%). Although unconsciousness occurs at these inspired levels, patients exhibit signs of CNS excitation, such as physical struggling and vomiting. If the airway is unprotected, vomiting may lead to aspiration pneumonitis, since the protective reflexes of the airway are depressed. On the other hand, lower inspired concentrations (25–40%) of N2O produce CNS depression without excitatory phenomena and are more safely used clinically. CNS properties of low inspired tension of N2O include periods of waxing and waning consciousness, amnesia, and extraordinarily effective analgesia. N2O 25% produces the gas’s maximum analgesic effect.With this concentration, responses to painful surgical manipulations are blocked as effectively as they would be with a therapeutic dose of morphine. Such low inspired concentrations of N2O are used in dentistry and occasionally for selected painful surgical procedures (i.e., to relieve the pain of labor). Since the tissue solubility of N2O is low, the CNS effects are rapid in onset, and recovery is prompt when the patient is returned to room air or oxygen. The most common use of N2O is in combination with the more potent volatile anesthetics. It decreases the dosage requirement for the other anesthetics, thus lowering their cardiovascular and respiratory toxicities. For example, an appropriate anesthetic maintenance tension for N2O and halothane would be N2O 40% and halothane 0.5%.With this combination in a healthy patient, anesthesia is adequate for major surgery, and the dose-dependent cardiac effects of halothane are reduced.

General Description

Different sources of media describe the General Description of 10024-97-2 differently. You can refer to the following data:
1. Nitrous oxide is a gas at room temperature and is supplied asa liquid under pressure in metal cylinders. Nitrous oxide is a“dissociative anesthetic” and causes slight euphoria and hallucinations.
2. NITROUS OXIDE is a colorless, sweet-tasting gas. NITROUS OXIDE is also known as "laughing gas". Continued breathing of the vapors may impair the decision making process. NITROUS OXIDE is noncombustible but NITROUS OXIDE will accelerate the burning of combustible material in a fire. NITROUS OXIDE is soluble in water. Its vapors are heavier than air. Exposure of the container to prolonged heat or fire can cause NITROUS OXIDE to rupture violently and rocket. NITROUS OXIDE is used as an anesthetic, in pressure packaging, and to manufacture other chemicals.

Reactivity Profile

NITROUS OXIDE is an oxidizing agent. Nonflammable but supports combustion. Can explode at high temperature (after vaporization). Vapors can undergo a violent reaction with aluminum, boron, hydrazine, lithium hydride, phenyllithium, phosphine, sodium, tungsten carbide [Bretherick, 5th ed., 1995, p. 1686]. Contact of the cold liquefied gas with water may result in vigorous or violent boiling. If the water is hot, a liquid "superheat" explosion may occur. Pressures may build to dangerous levels if liquefied gas contacts water in a closed container [Handling Chemicals Safely 1980].

Hazard

Supports combustion, can form explosive mixture with air. Narcotic in high concentration. Central nervous system impairment, hematologic effects, and embryo/fetal damage. Questionable carcinogen.

Health Hazard

Different sources of media describe the Health Hazard of 10024-97-2 differently. You can refer to the following data:
1. Inhalation causes intense analgesia; concentrations of over 40-60% cause loss of consciousness preceded by hysteria. Contact of liquid with eyes or skin causes frostbite burn.
2. Toxicity and irritant effects of nitrous oxidein humans are very low. It is an anesthetic.Inhalation of this gas at high concentrationscan produce depression of the central nervous system, decrease in body temperature,and fall in blood pressure. The LC50 valueof a 4-hour exposure in mice is in the rangeof 600 ppm.

Fire Hazard

Behavior in Fire: Will support combustion, and may increase intensity of fire. Containers may explode when heated.

Pharmaceutical Applications

Nitrous oxide and other compressed gases such as carbon dioxide and nitrogen are used as propellants for topical pharmaceutical aerosols. They are also used in other aerosol products that work satisfactorily with the coarse aerosol spray that is produced with compressed gases, e.g. furniture polish and window cleaner. The advantages of compressed gases as aerosol propellants are that they are less expensive, of low toxicity, and practically odorless and tasteless. In contrast to liquefied gases, their pressures change relatively little with temperature. However, there is no reservoir of propellant in the aerosol, and as a result the pressure decreases as the product is used, changing the spray characteristics. Misuse of a product by the consumer, such as using a product inverted, results in the discharge of the vapor phase instead of the liquid phase. Since most of the propellant is contained in the vapor phase, some of the propellant will be lost and the spray characteristics will be altered. Additionally, the sprays produced using compressed gases are very wet. However, recent developments in valve technology have reduced the risk of misuse by making available valves which will spray only the product (not propellant) regardless of the position of the container. Additionally, barrier systems will also prevent loss of propellant, and have found increased use with this propellant. Therapeutically, nitrous oxide is best known as an anesthetic administered by inhalation. When used as an anesthetic it has strong analgesic properties but produces little muscle relaxation. Nitrous oxide is always administered in conjunction with oxygen since on its own it is hypoxic.

Materials Uses

Nitrous oxide is noncorrosive and may therefore be used with any of the common, commercially available metals. Because of its oxidizing action, however, all equipment being prepared to handle nitrous oxide, particularly at high pressures, must be free of oil, grease, and other readily combustible materials. Nitrous oxide may cause swelling ofsome elastomers.

Clinical Use

The low potency of nitrous oxide (MAC= 104%) precludes it from being used alone for surgical anesthesia.To use it as the sole anesthetic agent the patient wouldhave to breathe in pure N2Oto the exclusion of oxygen. Thissituation would obviously cause hypoxia and potentially leadto death. Nitrous oxide can inactivate methionine synthase, aB12-dependent enzyme necessary for the synthesis of DNAand therefore should be used with caution in pregnant andB12-deficient patients. Nitrous oxide is also soluble in closedgas containing body spaces and can cause these spaces toenlarge when administered possibly leading to adverse occurrences(occluded middle ear, bowel distension, pneumothorax).Nitrous oxide is a popular anesthetic in dentistrywere it is commonly referred to as “laughing gas.” It is usedin combination with more potent anesthetics for surgicalanesthesia and remains a drug of recreational abuse.Nitrous oxide undergoes little or no metabolism.

Safety Profile

Moderately toxic by inhalation. Human systemic effects by inhalation: general anesthetic, decreased pulse rate without blood pressure fall, and body temperature decrease. An experimental teratogen. Experimental reproductive effects. Mutation data reported. An asphyxiant. Does not burn but is flammable by chemical reaction and supports combustion. Moderate explosion hazard; it can form an explosive mixture with air. Violent reaction with Al, B, hydrazine, LiH, LiC6H5, PH3, Na, tungsten carbide. Also self-explodes at high temperatures.

Safety

Nitrous oxide is most commonly used therapeutically as an anesthetic and analgesic. Reports of adverse reactions to nitrous oxide therefore generally concern its therapeutic use, where relatively large quantities of the gas may be inhaled, rather than its use as an excipient. The main complications associated with nitrous oxide inhalation occur as a result of hypoxia. Prolonged administration may also be harmful. Nitrous oxide is rapidly absorbed on inhalation.

Potential Exposure

Used as an anesthetic in dentistry and surgery; used as a gas in food aerosols, such as whipped cream; used in manufacture of nitrites; used in rocket fuels; in firefighting; diesel emissions. Large amounts of nitrous oxide will decrease the amount of available oxygen. Nitrous Oxide 2231 Oxygen should be routinely tested to ensure that it is at least 19% by volume.

Physiological effects

Nitrous oxide's primary physiological effect is central nervous system (CNS) depression. At high concentrations, anesthetic levels can be obtained, but the low potency of nitrous oxide necessitates concomitant administration of other depressant drugs. Nitrous oxide has been associated with several side effects from longterm exposure. The most strongly substantiated effect is neuropathy. Epidemiological studies also suggest feto-toxic effects and higher incidents of spontaneous abortion in exposed personnel.Although no cause-and-effect relationship has been firmly established, exposure to the gas should be minimized. Inhalation of nitrous oxide without the provision of a sufficient oxygen supply may be fatal or cause brain damage. Due to the concern over longterm exposure effects, release of the product into general work areas should be minimized. NIOSH has recommended a maximum exposure on an 8-hour Time-Weighted Average (TWA) of 25 parts per million for anesthetic and analgesic administration. ACGIH recommends a Threshold Limit Value-Time-Weighted Average (TLV-TWA) of 50 ppm (90 mglm3) for nitrous oxide. The TLV- TWA is the time-weighted average concentration for a normal 8-hour workday and a 40-hour workweek, to which nearly all workers may be repeatedly exposed, day after day, without adverse effect. Warning: The misuse of nitrous oxide can cause death by reducing the oxygen necessary to support life. Nitrous oxide abuse can impair an individual's ability to make and implement lifesustaining decisions.

Carcinogenicity

The possible carcinogenicity of nitrous oxide has been studied in dentists and chairside assistants with occupational exposures. No effect was observed in male dentists, but a 2.4- fold increase in cancer of the cervix in heavily exposed female assistants was reported.7 Other epidemiological reports of workers exposed to waste anesthetic gases have been negative.1 Carcinogenic bioassays in animals have yielded negative results. Nitrous oxide was not genotoxic in a variety of assays.

storage

Nitrous oxide is essentially nonreactive and stable except at high temperatures; at a temperature greater than 500°C nitrous oxide decomposes to nitrogen and oxygen. Explosive mixtures may be formed with other gases such as ammonia, hydrogen, and other fuels. Nitrous oxide should be stored in a tightly sealed metal cylinder in a cool, dry place.

Shipping

UN1070 Nitrous oxide, compressed, Hazard Class: 2.2; Labels: 2.2-Nonflammable compressed gas; 5.1-Oxidizer; UN2201 Nitrous oxide, refrigerated liquid, Hazard Class: 2.2; Labels: 2.2-Nonflammable compressed gas; 5.1-Oxidizer. Cylinders must be transported in a secure upright position, in a well-ventilated truck. Protect cylinder and labels from physical damage. The owner of the compressed gas cylinder is the only entity allowed by federal law (49CFR) to transport and refill them. It is a violation of transportation regulations to refill compressed gas cylinders without the express written permission of the owner.

Purification Methods

Wash the gas with concentrated alkaline pyrogallol solution, to remove O2, CO2, and NO2, then dry it by passing it through columns of P2O5 or Drierite, and collecting in a dry trap cooled in liquid N2. It is further purified by freeze-pump-thaw and distillation cycles under vacuum [Ryan & Freeman J Phys Chem 81 1455 1977, Schenk in Handbook of Preparative Inorganic Chemistry (Ed. Brauer) Academic Press Vol I pp 484-485 1963].

Toxicity evaluation

Large amounts of released nitrous oxide can decrease the amount of available oxygen. Medical complications of nitrous oxide inhalation are due to varying degrees of hypoxia affecting primarily the heart and brain. By inactivating vitamin B12, a critical cofactor in hematopoiesis and lipid membrane formation, nitrous oxide can cause anemia and neuropathy via selective inhibition of methionine synthase, a key enzyme in methionine and folate metabolism.

Incompatibilities

Different sources of media describe the Incompatibilities of 10024-97-2 differently. You can refer to the following data:
1. Nitrous oxide is generally compatible with most materials encountered in pharmaceutical formulations, although it may react as a mild oxidizing agent.
2. Nitrous oxide is a weak oxidizer. Incompatible with oxidizers (chlorates, nitrates, peroxides, permanganates, perchlorates, chlorine, bromine, fluorine, etc.); contact may cause fires or explosions. Keep away from alkaline materials, strong bases, strong acids, oxoacids, epoxides. Violent reactions with organic peroxides, hydrazine, hydrogen, hydrogen sulfide; lithium, boron, lithium hydride, sodium, aluminum, phosphine. This chemical is a strong oxidizer @ .300C and self-explodes at high temperature. May form explosive mixtures with ammonia, carbon monoxide; hydrogen sulfide; oil, grease and fuels.

Waste Disposal

Disperse in atmosphere or spray on dry soda ash/lime with great care; then flush to sewer.

Regulatory Status

GRAS listed. Accepted for use as a food additive in Europe. Included in nonparenteral medicines licensed in the UK and USA. Included in the Canadian List of Acceptable Non-medicinal Ingredients.

GRADES AVAILABLE

Nitrous oxide is available in medical, commercial, and high-purity grades. The medical (USP) grade is the most widely used. Manufacturers typically produce nitrous oxide for this use to the specification published in the United States Pharmacopeia/National Formulary. CGA G-8.2, Commodity Specification for Nitrous Oxide, describes the requirements for particular grades of nitrous oxide. Other specifications to meet particular requirements are available from suppliers. The absence of a value in a listed quality verification level does not mean to imply that the limiting characteristic is or is not present, but merely indicates that the test is not required for compliance with the specification.

Check Digit Verification of cas no

The CAS Registry Mumber 10024-97-2 includes 8 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 5 digits, 1,0,0,2 and 4 respectively; the second part has 2 digits, 9 and 7 respectively.
Calculate Digit Verification of CAS Registry Number 10024-97:
(7*1)+(6*0)+(5*0)+(4*2)+(3*4)+(2*9)+(1*7)=52
52 % 10 = 2
So 10024-97-2 is a valid CAS Registry Number.
InChI:InChI=1/N2O/c1-2-3

10024-97-2SDS

SAFETY DATA SHEETS

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

Version: 1.0

Creation Date: Aug 12, 2017

Revision Date: Aug 12, 2017

1.Identification

1.1 GHS Product identifier

Product name Dinitrogen monoxide

1.2 Other means of identification

Product number -
Other names dinitrogen oxide

1.3 Recommended use of the chemical and restrictions on use

Identified uses For industry use only. Food 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:10024-97-2 SDS

10024-97-2Synthetic route

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%
[Fe2(2,6-bis[[bis(2-pyridylmethyl)amino]methyl]-4-methylphenolato)(propionato)(NO)2](triflate)2

[Fe2(2,6-bis[[bis(2-pyridylmethyl)amino]methyl]-4-methylphenolato)(propionato)(NO)2](triflate)2

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

Conditions
ConditionsYield
With cobaltocene In dichloromethane at 20℃; for 0.0166667h; Kinetics; Time; Temperature; Concentration;100%
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
[CuI(tris(2-pyridylmethyl)amine)(CH3CN)]2+
114581-86-1

[CuI(tris(2-pyridylmethyl)amine)(CH3CN)]2+

nitrogen(II) oxide
10102-43-9

nitrogen(II) oxide

A

[Cu(tris(2-pyridylmethyl)amine)(H2O)](2+)
133578-96-8

[Cu(tris(2-pyridylmethyl)amine)(H2O)](2+)

B

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

Conditions
ConditionsYield
In water room temp., pH = 7.0; reaction followed by gas chromy.;A 99%
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%
trifluoromethyldifluorophosphine
1112-04-5

trifluoromethyldifluorophosphine

nitrogen(II) oxide
10102-43-9

nitrogen(II) oxide

A

Trifluormethylphosphonsaeuredifluorid
19162-94-8

Trifluormethylphosphonsaeuredifluorid

B

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

Conditions
ConditionsYield
20°C (7 d); oxydation;A 98%
B n/a
[(copper(II)(tris(2-pyridylmethyl)amine))2(μ-hyponitrite)](2+)

[(copper(II)(tris(2-pyridylmethyl)amine))2(μ-hyponitrite)](2+)

nitrogen(II) oxide
10102-43-9

nitrogen(II) oxide

A

[copper(I)(tris(2-pyridylmethyl)amine)](1+)
188637-84-5

[copper(I)(tris(2-pyridylmethyl)amine)](1+)

B

[copper(II)(tris(2-pyridylmethyl)amine)(nitrito)](1+)

[copper(II)(tris(2-pyridylmethyl)amine)(nitrito)](1+)

C

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

Conditions
ConditionsYield
In tetrahydrofuran; methanol for 8h; Solvent; Inert atmosphere; Schlenk technique;A 96%
B 85%
C 98%
{Cu2(NO)N6OC36H39}(2+)

{Cu2(NO)N6OC36H39}(2+)

tetrabutylammonium nitrite

tetrabutylammonium nitrite

A

{Cu2(O)N6OC36H39}(1+)*PF6(1-)={Cu2(O)N6OC36H39}PF6

{Cu2(O)N6OC36H39}(1+)*PF6(1-)={Cu2(O)N6OC36H39}PF6

B

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

Conditions
ConditionsYield
With P(C6H5)3 In not given byproducts: OP(C6H5)3; react. of 1 equiv. N(C4H9)4(NO2) with (Cu2(NO)N6OC36H39)(2+) in presence of P(C6H5)3 (1 equiv.);; elem. anal.;A 60%
B 97%
In not given byproducts: O2; react. of 1 equiv. N(C4H9)4(NO2) with (Cu2(NO)N6OC36H39)(2+);; elem. anal.;A 60%
B 79%
Cu2(I)(C6H3(O)(CH2N(C2H4-2-pyridyl)2)2)(1+)
90065-16-0

Cu2(I)(C6H3(O)(CH2N(C2H4-2-pyridyl)2)2)(1+)

nitrogen(II) oxide
10102-43-9

nitrogen(II) oxide

A

{Cu2(O)N6OC36H39}(1+)*PF6(1-)={Cu2(O)N6OC36H39}PF6

{Cu2(O)N6OC36H39}(1+)*PF6(1-)={Cu2(O)N6OC36H39}PF6

B

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

Conditions
ConditionsYield
In dichloromethane exposure of (Cu2N6OC36H39)(1+) to NO(g) in CH2Cl2 at -80 °C, warming;;A 55%
B 96%
trans-hydroxotetraamminenitrosoruthenium(II)

trans-hydroxotetraamminenitrosoruthenium(II)

nitric acid
7697-37-2

nitric acid

trans-tetraamminenitratonitrosoruthenium(III) nitrate

trans-tetraamminenitratonitrosoruthenium(III) nitrate

B

water
7732-18-5

water

C

Nitrogen dioxide
10102-44-0

Nitrogen dioxide

D

nitrosylchloride
2696-92-6

nitrosylchloride

E

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

Conditions
ConditionsYield
In nitric acid byproducts: Cl2; to Ru complex was added concd. HNO3; mixt. heated under reflux for 5 min; cooled to room temp.; ppt. filtered off; washed (water, alc., ether); dried (vac.); recrystd. (aq. HNO3); elem. anal.;A 95%
B n/a
C n/a
D n/a
E n/a
4-nitrosotetrahydro-2H-pyran-4-yl 2,2,2-trichloroacetate
1194657-31-2

4-nitrosotetrahydro-2H-pyran-4-yl 2,2,2-trichloroacetate

A

Tetrahydro-4H-pyran-4-one
29943-42-8

Tetrahydro-4H-pyran-4-one

B

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

C

trichloroacetic acid
76-03-9

trichloroacetic acid

Conditions
ConditionsYield
With water In methanol; aq. phosphate buffer at 20℃; for 24h; pH=7.4; Kinetics; Reagent/catalyst; Sealed tube;A n/a
B 95%
C 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%
trifluorormethanesulfonic acid
1493-13-6

trifluorormethanesulfonic acid

[Fe2(NO)4(μ-1,3-bis(dimethylamino)-2-propanolate)]2(κ4-N2O2)

[Fe2(NO)4(μ-1,3-bis(dimethylamino)-2-propanolate)]2(κ4-N2O2)

A

[Fe2(NO)4(μ-1,3-bis(dimethylamino)-2-propanolate)(μ-OSO2CF3)]

[Fe2(NO)4(μ-1,3-bis(dimethylamino)-2-propanolate)(μ-OSO2CF3)]

B

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

Conditions
ConditionsYield
In tetrahydrofuran at 0℃; for 1h; Schlenk technique; Inert atmosphere;A n/a
B 93%
4-nitrosotetrahydro-2H-pyran-4-yl 2,2-dichloropropanoate

4-nitrosotetrahydro-2H-pyran-4-yl 2,2-dichloropropanoate

A

Tetrahydro-4H-pyran-4-one
29943-42-8

Tetrahydro-4H-pyran-4-one

B

2,2-Dichloropropionic acid
75-99-0

2,2-Dichloropropionic acid

C

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

Conditions
ConditionsYield
With water In methanol; aq. phosphate buffer at 20℃; for 24h; pH=7.4; Kinetics; Reagent/catalyst; Sealed tube;A n/a
B n/a
C 92%
C46H57Fe2N13O4S(2+)*2BF4(1-)

C46H57Fe2N13O4S(2+)*2BF4(1-)

A

C43H49Fe2N10O2(2+)

C43H49Fe2N10O2(2+)

B

2C39H41N10O(1-)*2Fe(2+)*2Fe(3+)*4HO(1-)

2C39H41N10O(1-)*2Fe(2+)*2Fe(3+)*4HO(1-)

C

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

Conditions
ConditionsYield
With cobaltocene In dichloromethane for 0.0833333h; Sealed tube; Inert atmosphere;A n/a
B n/a
C 91%
nitrogen(II) oxide
10102-43-9

nitrogen(II) oxide

A

nitrogen
7727-37-9

nitrogen

B

oxygen
80937-33-3

oxygen

C

Nitrogen dioxide
10102-44-0

Nitrogen dioxide

D

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

Conditions
ConditionsYield
Irradiation (UV/VIS); irradn. with Al-glitter (wave length:1860,1930 and 1990 A);A 90%
B 90%
C 10%
D 10%
Irradiation (UV/VIS); irradn. with Al-glitter (wave length:1860,1930 and 1990 A);A 90%
B 90%
C 10%
D 10%
La0.7Ba0.3Mn0.8In0.1Cu0.1O3 In neat (no solvent) decomposition over catalyst at 1073 K;A 69.4%
B 42.3%
C 27.1%
D 0%
ammonia
7664-41-7

ammonia

oxygen
80937-33-3

oxygen

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

Conditions
ConditionsYield
manganese(II) oxide In neat (no solvent) catalytic oxidn. of NH3 (300 °C, O2-excess);;90%
byproducts: N2, NO; excess of O2; at 300 °C; catalyst MnO2/Fe2O3/(eventually) Bi2O3; yield depending on mole ratio O2:NH3 and flow rate;;90%
cobalt(II) oxide In neat (no solvent) oxidation at 300°C;;
ammonia
7664-41-7

ammonia

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

Conditions
ConditionsYield
With oxygen 300 °C,with air;90%
Electrolysis; NH3 soln. contg. CO2;anod contains Pt,Pd or Fe;14.6%
Electrolysis;
Nitrite

Nitrite

tin(ll) chloride

tin(ll) chloride

A

hydroxylamine
7803-49-8

hydroxylamine

B

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

C

trans-hyponitrous acid
19467-31-3, 173728-04-6

trans-hyponitrous acid

Conditions
ConditionsYield
In waterA n/a
B 90%
C n/a
cis-nitrous acid
7782-77-6

cis-nitrous acid

tin(ll) chloride

tin(ll) chloride

A

hydroxylamine
7803-49-8

hydroxylamine

B

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

C

trans-hyponitrous acid
19467-31-3, 173728-04-6

trans-hyponitrous acid

Conditions
ConditionsYield
In waterA n/a
B 90%
C n/a
copper(II)-hyponitrite

copper(II)-hyponitrite

A

nitrogen
7727-37-9

nitrogen

B

nitrogen(II) oxide
10102-43-9

nitrogen(II) oxide

C

copper(II) oxide

copper(II) oxide

D

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

Conditions
ConditionsYield
In neat (no solvent) decompn. at 225-230°C;;A 2-6
B 3-5
C n/a
D 90%
In neat (no solvent) decompn. at 225-230°C;;A 2-6
B 3-5
C n/a
D 90%
hydroxylamine
7803-49-8

hydroxylamine

A

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

B

nitrosyl hydride

nitrosyl hydride

Conditions
ConditionsYield
With hypochloric acid In aq. phosphate buffer at 37℃; pH=7.4;A n/a
B 90%
potassium nitrite
7758-09-0

potassium nitrite

hydrazin sulfate

hydrazin sulfate

A

nitrogen
7727-37-9

nitrogen

B

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

C

trans-hyponitrous acid
19467-31-3, 173728-04-6

trans-hyponitrous acid

Conditions
ConditionsYield
In not given at room temp. or upon boiling from equimolar amounts in 3% solns.; no formation of H2N2O2 even in concd. solns. at low temps.; mole ratio of N2O:N2 depends on the mole ratio nitrite:hydrazonium salt;;A 11%
B 89%
C 0%
C52H70Fe2N14O5(3+)*3BF4(1-)

C52H70Fe2N14O5(3+)*3BF4(1-)

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

Conditions
ConditionsYield
With cobaltocene In dichloromethane for 0.0833333h; Inert atmosphere;89%
With silver; N,N,N,N-tetraethylammonium tetrafluoroborate In dichloromethane Inert atmosphere; Electrochemical reaction;89%
hydroxylamine
7803-49-8

hydroxylamine

A

nitrogen
7727-37-9

nitrogen

B

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

Conditions
ConditionsYield
With Hg2(NO3)2 In not given byproducts: Hg; addn. of 0.04 M NH2OH to 0.005 M Hg2(NO3)2 soln. buffered with acetate at 20°C, autocatalysis of reaction by Hg;;A 13%
B 87%
With Hg2(NO3)2; silver In not given byproducts: Hg; addn. of 0.04 M NH2OH to 0.005 M Hg2(NO3)2 soln. buffered with acetate at 20°C, autocatalysis of reaction by Hg, further catalysis by addn. of collodial Ag soln.;;A 63%
B 34%
With oxygen In not given byproducts: water; Electrolysis; N2O formed on cathode, N2 formed on anode;
[(copper(II)(tris(2-pyridylmethyl)amine))2(μ-hyponitrite)](2+)

[(copper(II)(tris(2-pyridylmethyl)amine))2(μ-hyponitrite)](2+)

nitrogen(II) oxide
10102-43-9

nitrogen(II) oxide

A

[copper(II)(tris(2-pyridylmethyl)amine)(nitrito)](1+)

[copper(II)(tris(2-pyridylmethyl)amine)(nitrito)](1+)

B

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

Conditions
ConditionsYield
In methanol Inert atmosphere; Schlenk technique;A 85%
B n/a
Ketene
463-51-4

Ketene

nitrogen(II) oxide
10102-43-9

nitrogen(II) oxide

A

fulminic acid
51060-05-0

fulminic acid

B

hydrogen cyanide
74-90-8

hydrogen cyanide

C

carbon monoxide
201230-82-2

carbon monoxide

D

water
7732-18-5

water

E

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

Conditions
ConditionsYield
byproducts: H2CO; Irradiation (UV/VIS); photolysis of CH2CO/NO/Ar mixt. with 200 W high pressure Hg lamp (photolysis of CH2CO generates CH2 radicals) in Duran glass tube (20 cm long, 4cm i.d.) at room temp. and ambient pressure;A 84%
B 15%
C n/a
D n/a
E n/a
bis(η5.-pentamethylcyclopentadienyl)(η2-phenyltrimethylsilylacetylene)zirconium

bis(η5.-pentamethylcyclopentadienyl)(η2-phenyltrimethylsilylacetylene)zirconium

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

(η(5)-C5Me5)2Zr(OCPh=CSiMe3)
205107-24-0

(η(5)-C5Me5)2Zr(OCPh=CSiMe3)

Conditions
ConditionsYield
In neat (no solvent) byproducts: N2; absence of air and moisture; 500 Torr N2O, room temp., 24 h; removal of gases; elem. anal.;100%
In toluene byproducts: N2; absence of air and moisture; N2O-atmosphere, warming from -78°C to room temp., stirring for 30 min; rsolvent removal, recrystn. (hexane/O(SiMe3)2);65%
In benzene absence of air and moisture;
(η(5)-C5Me5)2Zr(Me3SiC.tplbond.C(c-C5H9))

(η(5)-C5Me5)2Zr(Me3SiC.tplbond.C(c-C5H9))

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

(η(5)-C5Me5)2Zr(OC(c-C5H9)=CSiMe3)
205107-25-1

(η(5)-C5Me5)2Zr(OC(c-C5H9)=CSiMe3)

Conditions
ConditionsYield
In neat (no solvent) byproducts: N2; absence of air and moisture; 500 Torr N2O, room temp., 24 h; removal of gases; elem. anal.;100%
In benzene absence of air and moisture;
(((p-tolyl)B(pyrazolyl)2)2Py)ScH

(((p-tolyl)B(pyrazolyl)2)2Py)ScH

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

(((p-tolyl)B(pyrazolyl)2)2Py)Sc-O-Sc(((p-tolyl)B(pyrazolyl)2)2Py)

(((p-tolyl)B(pyrazolyl)2)2Py)Sc-O-Sc(((p-tolyl)B(pyrazolyl)2)2Py)

Conditions
ConditionsYield
In benzene-d6 at 80℃; under 760.051 Torr; for 18h; Inert atmosphere; Schlenk technique;100%
methane
34557-54-5

methane

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

A

methanol
67-56-1

methanol

B

formaldehyd
50-00-0

formaldehyd

C

carbon dioxide
124-38-9

carbon dioxide

D

carbon monoxide
201230-82-2

carbon monoxide

E

nitrogen
7727-37-9

nitrogen

Conditions
ConditionsYield
In neat (no solvent) Kinetics; Oxidation of CH4 by N2O in presence of catalyst (773 K): deposited Cu(2+) on carbon;;A 0.2%
B 0.3%
C 99.5%
D 0%
E n/a
In neat (no solvent) Kinetics; byproducts: C2H5OH (small quantity); oxidation of CH4 by N2O in presence of catalyst (773 K): deposited Ti(4+) on carbon;;A 13.8%
B 0%
C 86.2%
D 0%
E n/a
In neat (no solvent) Kinetics; Oxidation of CH4 by N2O in presence of catalyst (773 K): deposited Co(2+) on carbon;;A 0%
B 0%
C 75%
D 25%
E n/a
potassium amide

potassium amide

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

potassium azide
20762-60-1

potassium azide

Conditions
ConditionsYield
byproducts: KOH, NH3; 270-280 °C in rotating furnace; the white layer of KOH and KN3 dissolved in water, the soln. evaporated, KN3 crystd.;99%
byproducts: KOH, NH3; 270-280 °C in rotating furnace; the white layer of KOH and KN3 dissolved in water, the soln. evaporated, KN3 crystd.;99%
In ammonia byproducts: KOH, NH3; -70°C;
In ammonia byproducts: KOH, NH3; NH3 (liquid); -70°C;
nitrogen trifluoride
7783-54-2

nitrogen trifluoride

antimony pentafluoride
7783-70-2

antimony pentafluoride

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

NF2O(1+)*Sb2F11(1-) =(NF2O)(Sb2F11)
12528-55-1

NF2O(1+)*Sb2F11(1-) =(NF2O)(Sb2F11)

Conditions
ConditionsYield
byproducts: N2; 150°C;99%
100°C;0%
N[2-P(CHMe3)2-4-methylphenyl]2V(CH2tBu)2
1039748-93-0

N[2-P(CHMe3)2-4-methylphenyl]2V(CH2tBu)2

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

V(N[4-Me-2-(PiPr2)C6H3]2)(CHtBu)O*0.5C5H10

V(N[4-Me-2-(PiPr2)C6H3]2)(CHtBu)O*0.5C5H10

Conditions
ConditionsYield
In benzene V-complex reacted with N2O in benzene at 90°C;99%
(η5-C5Me5)*W{N(iPr)C(Me)N(iPr)}(NSiMe3)

(η5-C5Me5)*W{N(iPr)C(Me)N(iPr)}(NSiMe3)

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

(η5-C5Me5)W[N(iPr)C(Me)N(iPr)](nitrido)(OSiMe3)

(η5-C5Me5)W[N(iPr)C(Me)N(iPr)](nitrido)(OSiMe3)

Conditions
ConditionsYield
at 25℃; for 216h;99%
bis[2,6-bis(1-naphthyl)phenyl]germylene
328396-60-7

bis[2,6-bis(1-naphthyl)phenyl]germylene

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

bis[2,6-bis(1-naphthyl)phenyl]germanone
327179-04-4

bis[2,6-bis(1-naphthyl)phenyl]germanone

Conditions
ConditionsYield
In toluene left standing under N2 for 2 d; solvent evpd. in vacuo;98%
potassium diphenylphosphanylborohydride

potassium diphenylphosphanylborohydride

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

KOPPh2BH3

KOPPh2BH3

Conditions
ConditionsYield
In tetrahydrofuran soln. of B compd. stirred at room temp. under N2O atm. until gas evolution stopped (ca. 5 min); evapd., elem. anal.;98%
K[P((t)Bu)2BH3]

K[P((t)Bu)2BH3]

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

K(1+)*OP(C(CH3)3)2BH3(1-)=K[(C(CH3)3)2OPBH3]

K(1+)*OP(C(CH3)3)2BH3(1-)=K[(C(CH3)3)2OPBH3]

Conditions
ConditionsYield
In tetrahydrofuran soln. of B compd. stirred at room temp. under N2O atm. until gas evolution stopped (ca. 5 min); evapd., elem. anal.;98%
[{(i-Bu)2(aminotroponiminate)Ge(i-Pr)(ZnCl2)}2]

[{(i-Bu)2(aminotroponiminate)Ge(i-Pr)(ZnCl2)}2]

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

[{(i-Bu)2ATIGe(O)(i-Pr)(ZnCl2)}2]

[{(i-Bu)2ATIGe(O)(i-Pr)(ZnCl2)}2]

Conditions
ConditionsYield
In tetrahydrofuran at 20℃; for 0.5h; Inert atmosphere; Schlenk technique;98%
[(C(C6H4P(CH(CH3)2)2)2)IrCl]

[(C(C6H4P(CH(CH3)2)2)2)IrCl]

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

C25H36ClIrOP2

C25H36ClIrOP2

Conditions
ConditionsYield
In benzene-d6 at 20℃; under 760.051 Torr; for 24h;98%
ethylenebis(1,3-di-tert-butylcyclopentadienyl)titanium
1033858-47-7

ethylenebis(1,3-di-tert-butylcyclopentadienyl)titanium

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

A

μ-oxotetrakis(1,3-di-tert-butylcyclopentadienyl)dititanium
827030-28-4

μ-oxotetrakis(1,3-di-tert-butylcyclopentadienyl)dititanium

B

di-μ-oxotetrakis(1,3-di-tert-butylcyclopentadienyl)dititanium
1033858-56-8

di-μ-oxotetrakis(1,3-di-tert-butylcyclopentadienyl)dititanium

Conditions
ConditionsYield
In pentane Ti complex dissolved in pentane; exposed to N2O (1 atm); solvent removed under vac.; extd. into hot toluene; cooled to room temp.and then to -20°C; crystals isolated; elem. anal.;A 0%
B 97%
(HC(CMeNC-2,6-i-Pr2C6H3)2)-germanium(II) hydride
382150-90-5

(HC(CMeNC-2,6-i-Pr2C6H3)2)-germanium(II) hydride

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

(HC(CMeNC-2,6-i-Pr2C6H3)2)-germanium(II) hydroxide
692776-46-8

(HC(CMeNC-2,6-i-Pr2C6H3)2)-germanium(II) hydroxide

Conditions
ConditionsYield
In toluene under N2 or Ar; dry N2O bubbled into soln. of Ge compd. in toluene at room temp. for 30 min; volatiles removed in vac.; treated with n-hexane; filtered; dried in vac.;95%
C20H46BN2P

C20H46BN2P

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

C20H46BN2OP

C20H46BN2OP

Conditions
ConditionsYield
In toluene at 20℃; under 760.051 Torr; for 24h; Cooling with liquid nitrogen; Inert atmosphere;94%
[(2,6-(2,4,6-Me3C6H2)2C6H3)Ge-(1,3,4,5-tetramethylimidazol-2-ylidene)2][(3,5-(CF3)2C6H3)4B]

[(2,6-(2,4,6-Me3C6H2)2C6H3)Ge-(1,3,4,5-tetramethylimidazol-2-ylidene)2][(3,5-(CF3)2C6H3)4B]

dinitrogen monoxide
10024-97-2

dinitrogen monoxide

[(2,6-(2,4,6-Me3C6H2)2C6H3)Ge(O)(1,3,4,5-tetramethylimidazol-2-ylidene)2][(3,5-(CF3)2C6H3)4B]

[(2,6-(2,4,6-Me3C6H2)2C6H3)Ge(O)(1,3,4,5-tetramethylimidazol-2-ylidene)2][(3,5-(CF3)2C6H3)4B]

Conditions
ConditionsYield
In acetonitrile Inert atmosphere;94%

10024-97-2Relevant articles and documents

Kinetics and mechanism of the iron phthalocyanine catalyzed reduction of nitrite by dithionite and sulfoxylate in aqueous solution

Kudrik, Evgeny V.,Makarov, Sergei V.,Zahl, Achim,Van Eldik, Rudi

, p. 6470 - 6475 (2005)

The reactions of sodium nitrite with sodium dithionite and sulfoxylate ion were studied in the presence of iron(III) tetrasulfophthalocyanine, Fe III(TSPc)3-, in aqueous alkaline solution. Kinetic parameters for the different reaction steps in the catalytic reduction by dithionite were determined. The final product of the reaction was found to be nitrous oxide. Contrary to this, the product of the catalytic reduction of nitrite by sulfoxylate was found to be ammonia. The striking difference in the reaction products is accounted for in terms of different structures of the intermediate complexes formed during the reduction by dithionite and sulfoxylate, in which nitrite is suggested to coordinate to the iron complex via nitrogen and oxygen, respectively. Sulfoxylate is shown to be a convenient reductant for the synthesis of the highly reduced iron phthalocyanine species FeI(TSPc?)6- in aqueous solution. The kinetics of the reduction of FeI(TSPc)5- to Fe I(TSPc?)6-, as well as the oxidation of the latter species by nitrite, was studied in detail.

Investigation of N2O production from 266 and 532 nm laser flash photolysis of O3/N2/O2 mixtures

Estupinan,Nicovich,Li,Cunnold,Wine

, p. 5880 - 5890 (2002)

Tunable diode laser absorption spectroscopy has been employed to measure the amount of N2O produced from laser flash photolysis of O3/N2/O2 mixtures at 266 and 532 nm. In the 532 nm photolysis experiments very little N2O is observed, thus allowing an upper limit yield of 7 × 10-8 to be established for the process O3? + N2 → N2O + O2, where O3? is nascent O3 that is newly formed via O(3PJ) + O2 recombination (with vibrational excitation near the dissociation energy of O3). The measured upper limit yield is a factor of ~600 smaller than a previous literature value and is approximately a factor of 10 below the threshold for atmospheric importance. In the 266 nm photolysis experiments, significant N2O production is observed and the N2O quantum yield is found to increase linearly with pressure over the range 100-900 Torr in air bath gas. The source of N2O in the 266 nm photolysis experiments is believed to be the addition reaction O(1D2) + N2 + M k6 → N2O + M, although reaction of (very short-lived) electronically excited O3 with N2 cannot be ruled out by the available data. Assuming that all observed N2O comes from the O(1D2) + N2 + M reaction, the following expression describes the temperature dependence of k6 (in its third-order low-pressure limit) that is consistent with the N2O yield data: k6 = (2.8 ± 0.1) × 10-36(T/300)-(0.88±0.36) cm6 molecule-2s-1, where the uncertainties are 2σ and represent precision only. The accuracy of the reported rate coefficients at the 95% confidence level is estimated to be 30-40% depending on the temperature. Model calculations suggest that gas phase processes initiated by ozone absorption of a UV photon represent about 1.4% of the currently estimated global source strength of atmospheric N2O. However, these processes could account for a significant fraction of the oxygen mass-independent enrichment observed in atmospheric N2O, and they appear to be the first suggested photochemical mechanism that is capable of explaining the altitude dependence of the observed mass-independent isotopic signature.

Reactivity of Rh+(CO)2 during the NO-CO and CO-O2 Reactions over Rh/Al2O3

Almusaiteer, Khalid A.,Chuang, Steven S. C.,Tan, Cher-Dip

, p. 247 - 247 (2000)

Exposure of Rh+(CO)2 on Rh/Al2O3 to NO causes CO desorption and adsorption of NO as Rh-NO+; exposure of Rh+(CO)2 to NO/H2 produced N2O at 573 K. The presenc

Pd/NaY-zeolite and Pd-W/NaY-zeolite catalysts: Preparation, characterization and NO decomposition activity

Pergher, Sibele B.C.,Dallago, Rogerio M.,Veses, Renato Cataluna,Gigola, Carlos E.,Baibich, Ione M.

, p. 107 - 115 (2004)

Pd/NaY-zeolite and Pd-W/NaY-zeolite catalysts were prepared from the compounds Pd(NO3)2 and [W(CO)6]. Tungsten was added by photochemical activation of [W(CO)6] to obtain a Pd-W interaction. The prepared catalysts were active for NO decomposition at 573 K leading mainly to N2 and N2O. NO conversion and the selectivity to N2O were studied as a function of time and the reduction temperature. The Pd/NaY-zeolite and the Pd-W/NaY-zeolite samples showed an initial period of high and constant activity followed by deactivation. Tungsten prevented the sintering of small Pd particles. Bimetallic sample deactivated faster, indicating that the Pd-W interaction decreased the fraction of exposed Pd atoms. The onset of N2O formation was in accord with the initiation of the deactivation.

Rate constants for formation of NO in vibrational levels v=2 through 7 from the reaction N(4S) + O2 -> NO* + O

Rahbee, A.,Gibson, J. J.

, p. 5143 - 5148 (1981)

Vibration-rotation spectra of the Δv=2 sequence of the nitric oxide formed by the chemiluminescent reaction N(4S) + O2 -> NO(X2Π) + O have been obtained with a spectral resolution of 15 cm-1.Emission bands due to N2O were observed to occur in the same spectral region as the first overtone of NO.These were experimentally eliminated and the resulting NO spectra were used to derive rate constants for formation of NO in vibrational levels v=2 through v=7.In units of 10-19 cm3/sec, these room temperature rate constants are, respectively, 55 +/- 14, 57 +/- 9, 33 +/- 3, 24 +/- 4, 7 +/- 2, and 5 +/- 2.Of all the nitric oxide molecules formed in the reaction, only 18percent are formed in levels v > 2.In terms of energy, of the 1.39 eV exothermicity of the reaction, about 10 percent goes into vibrational energy in levels v > 2.

Stabilization of ammonium dinitramide in the liquid phase

Andreev,Anikin,Ivanov,Krylov,Pak

, p. 1974 - 1976 (2000)

The kinetics of accumulation of the main products of thermal decomposition of ammonium dinitramide in the melt was investigated. The isotope composition of nitrogen-containing gases evolved by the decomposition of 15NH4N(NO2/su

The catalytic chemistry of HCN + NO2 over Na- and Ba-Y,FAU: An in situ FTIR and TPD/TPR study

Szanyi, János,Kwak, Ja Hun,Peden, Charles H. F.

, p. 1481 - 1490 (2005)

The adsorption of HCN and the reaction of HCN with NO2 over Na-, and Ba-Y,FAU zeolite catalysts were investigated using in situ FTIR and TPD/ TPR spectroscopies. Both catalysts adsorb HCN molecularly at room temperature, and the strength of ads

Baiker, A.,Dollenmaier, P.,Reller, A.

, p. 394 - 398 (1987)

Wilkins, C. J.,Soper, F. G.

, (1939)

Efficient conversion of NO2 into N2 and O2 in N2 or into N2O5 in Air by 172-nm Xe 2 excimer lamp at atmospheric pressure

Tsuji, Masaharu,Kawahara, Masashi,Senda, Makoto,Noda, Kenji

, p. 376 - 377 (2007)

Decomposition of NO2 (200 ppm) in N2 or air by 172-nm Xe2 excimer lamp was studied at 1 atm. The NO2 conversion in N2 was 99%, and the formation ratios of N2, O 2, NO, and N2O were 47, 98, 0, and 2%, respectively, after 30 min irradiation. The NO2 in air (5-20% O2) could be completely converted to N2O5 and HNO3 due to reactions by O3 and H2O after only 1.0-1.5 min irradiation. The present results give a new simple photochemical aftertreatment technique of NO2 in air without using any catalysts. Copyright

Mesostructured CeO2 and Pd/CeO2 nanophases: Templated synthesis, crystalline structure and catalytic properties

Zhang,Yang,Shen,Wang

, p. 182 - 190 (2005)

This work reports a ceria solid and Pd/ceria catalyst prepared through a surfactant-templated synthesis route used for simultaneous abasement of NO and CO emissions. The surface features, textural properties and crystalline structure of ceria and Pd/ceria catalyst were studied by means of thermogravimetric analysis (TGA), N2 physisorption isotherms and in situ Fourier transform infrared (FT-IR) spectroscopy, high resolution electron transmission microscopy (TEM) and X-ray diffraction (XRD) techniques. In the calcination procedure, part of the adsorbed water on the surface of the solid was derived into unidentate and bidentate hydroxyls associated with surface cationic ions of ceria. The surfactant cations were strongly interacted with the solid during the preparation, which induces defects formation in the crystalline structure of the annealed ceria. The retained surfactant in the solid could be combusted to yield CO2, water and organic molecules with a small amount of coke-like deposits. The resultant ceria showed mesoporous texture and cubic phase containing lattice defects in the crystalline structure. The Pd/CeO2 catalyst was very active for NO reduction via CO with a high selectivity to N2. A 100% NO conversion with a selectivity to 100% N2 was achieved over the Pd/ceria catalyst at a reaction temperature of 300 °C. The catalytic activity and selectivity of this catalyst are much superior to the catalysts of Pt or Rh supported on TiO2, Al2O3, TiO 2-Al2O3 and ZrO2-Al 2O3 prepared by a sol-gel method. A possible reaction mechanism of NO reduction by CO over the Pd/CeO2 catalyst was discussed.

Effects of O2 on the reduction of NO over prereduced CaO surfaces: A mechanistic understanding

Acke, Filip,Panas, Itai

, p. 2195 - 2201 (1999)

The effect of O2 on the reduction of NO over prereduced CaO surfaces is investigated. The experimental results suggest the existence of at least three different reaction channels, of which two are related to the high-temperature reduction of the CaO surfaces and involve the use of extra electrons in breaking the NO bond. The third reaction channel does not employ extra electrons for bond breaking, but the activity is affected by the amount of adsorbed surface oxygens. The difference between the former two reaction channels is found in the temperature needed for an observable activity. The reaction channel which is already active at low temperatures is described by a model based on F-centers, whereas the one which needs elevated temperatures involves a hole transport through the bulk. The activation energy for this transport is determined experimentally using a temperature-programmed reaction technique as well as theoretically by means of ab initio quantum chemistry calculations. Room-temperature exposure to O2 is suggested to result in a poisoning of the F-centers, but has only a minor effect on the reaction channel proposed for high temperatures. Effects on the reduction of NO of time as well as temperature for the O2 exposure step are also investigated and found to be consistent with an understanding based on the coexistence of different reaction channels. ? 1999 American Chemical Society.

Modified Electronic Structure and Enhanched Catalytic Activity of Cobalt Tetraphenylporphirin Supported by Titanium Dioxide

Mochida, Isao,Tsuji, Kazuhiko,Suetsugu, Katsuya,Fujitsu, Hiroshi,Takeshita, Kenjiro

, p. 3159 - 3162 (1980)

The electronic structure and the catalytic activity of cobalt tetraphenylporphirin supported on titanium dioxide (CoTPP/TiO2) were studied in order to reveal the electronic interaction between the oxide and the planar complex, which can modify the nature of the latter substance.CoTPP/TiO2 showed a sharp isotropic ESR signal at a g value of 2.003 and a UV band around 590 nm, values which were completely different from those of the unsupported CoTTP.The formation of an anionic radical, which has an odd electron in the porphyrin ring, is suggested.CoTTP?TiO2 showed remarkable catalytic activity for the reduction of nitric oxide to nitrous oxide and molecular nitrogen even at 50 deg C with hydrogen, which was found to be adsorbed on CoTTP/TiO2.The activity was much accelerated at 150 deg C, where a successive reduction of nitric oxide in the sequence NO --> N2O --> N2 was clearly indicated.

Catalytic activity of Ir for NO-CO reaction in the presence of SO2 and excess oxygen

Ogura, Masaru,Kawamura, Aya,Matsukata, Masahiko,Kikuchi, Eiichi

, p. 146 - 147 (2000)

Catalytic performance of Ir catalysts for reduction of nitric oxide with carbon monoxide in the presence of SO2 and excess oxygen was investigated. NO was selectively reduced with CO on Ir/silicalite in an oxidizing atmosphere containing 1% to

Selective Reduction of NO by NH3 over Chromia on Titania Catalyst: Investigation and Modeling of the Kinetic Behavior

Willi,Maciejewski,Goebel,Koeppel,Baiker

, p. 356 - 367 (1997)

The kinetics and the parametric sensitivity of the selective catalytic reduction (SCR) of NO by NH3 were investigated over a chromia on titania catalyst. The chromium oxide phase was made up predominantly of X-ray amorphous Cr2O3. High SCR activity and selectivity to N2 was attained at low temperatures. The high selectivity is attributed to the absence of significant amounts of CrO2 and crystalline α-Cr2O3 which favor N2O formation. The selectivity to N2O increased with higher temperature. Addition of up to 6% H2O to the dry feed reduced the rate of NO conversion and decreased the undesired formation of N2O. The effect of water on the catalytic behavior was reversible. In the absence of oxygen, the reaction between NO and NH3 became marginal independently whether H2O was present or not. Small amounts of oxygen were sufficient to restore SCR activity. Admission of SO2 to the SCR feed resulted in a severe loss of activity. The poisoning of the catalyst by SO2 was already notable for low SO2 concentrations (30 ppm) and for temperatures up to 573 K. X-ray photoelectron and FTIR spectroscopy revealed the presence of sulfate species on the catalyst surface. Analysis of the kinetic data indicated that the SCR reaction is first order in NO and zeroth order in NH3 for temperatures in the range 400-520 K. The estimated activation energies for dry and wet feed amounted to 60.0 ± 1.6 kJ/mol (95% confidence limits). For temperatures in the range 400-520 K, and for a SO2 free feed, the steady-state kinetic data could be well described with a model based on an Eley-Rideal type reaction between activated ammonia surface species and gaseous or weakly adsorbed NO.

Reaction of trans-[RuNO(NH3)4(OH)]Cl2 with nitric acid and synthesis of ammine(nitrato)nitrosoruthenium complexes

Kabin,Emel'yanov,Vorob'yev,Alferova,Tkachev,Baidina

, p. 1146 - 1153 (2012)

The reaction of trans-[RuNO(NH3)4(OH)]Cl2 with nitric acid has been studied. Reaction prod- ucts have been identified by IR spectroscopy, NMR, mass spectrometry, powder and single-crystal X-ray dif- fraction, and chemical

TG-FTIR, DSC and ESCA characterization of histamine complexes with transition metal ions

Materazzi,Curini,Gentili,D'Ascenzo

, p. 45 - 50 (1997)

The thermoanalytical study of some MeHmx complexes (Hm = histamine; x = 1, 2) and MeHmx(NO3)2 (x = 2, 4) with Co(II), Ni(II) and Cu(II) is reported. By TG-FTIR coupled analysis,

On the surface steps of a heterogeneous catalytic reaction

Matyshak

, p. 812 - 817 (2007)

Based on a study of the properties of intermediate complexes in the reactions of low-temperature ammonia oxidation and nitrogen oxide reduction in the presence and absence of oxygen on various catalysts, it was hypothesized that the sequence of steps in the formation of reaction products on chemically different catalysts can be the same if the initial adsorption forms of reactants are identical. In this case, variations in catalysts or reaction conditions affect the ratio between reaction rates.

A novel mechanism for poisoning of metal oxide SCR catalysts: Base-acid explanation correlated with redox properties

Chang, Huazhen,Li, Junhua,Su, Wenkang,Shao, Yuankai,Hao, Jiming

, p. 10031 - 10034 (2014)

A novel mechanism is proposed for the poisoning effect of acid gases and N2O formation on SCR catalysts involving base-acid properties correlated with redox ability of M-O or M-OH (M = Ce or V) of metal oxides and the strength of their basicity responsible for resistance to HCl and SO 2 at medium and low temperatures. This journal is the Partner Organisations 2014.

Monitoring of the evolved gases in apatite-ammonium sulfate thermal reactions

Tonsuaadu, Kaia,Pelt,Borissova, Maria

, p. 655 - 658 (2005)

Thermal reactions in natural fluorapatite or fluorcarbonate apatite and ammonium sulfate mixtures with mole ratio 1:4 at calcination up to 500°C were studied by simultaneous thermogravimetry and FTIR analysis of the evolved gases. The composition of natur

Evidence for Homolytic Decomposition of Ammonium Nitrate at High Temperature

Brower, K. R.,Oxley, Jimmie C.,Tewari, Mohan

, p. 4029 - 4033 (1989)

Rates of decomposition of ammonium nitrate in the liquid and vapor state have been measured at temperatures up to 400 deg C.The evidence indicates that an ionic mechanism operating at temperatures below 290 deg C is overtaken by a homolytic mechanism at higher temperatures.The activation energy increases to 193 kJ/mol, which is nearly equal to the N-O bond energy in HNO3.Water and NH3 strogly inhibit the ionic reaction at low temperature, but the effect fades away at high temperature.There is no primary H/D kinetic isotope effect.The reaction rates of liquid and vapor are nearly the same at high temperature.The rate at high temperature is given by (kT/h)e4.06e-23300/T.

Carbon-Nitrogen and Nitrogen-Nitrogen Bond Formation from Nucleophilic Attack at Coordinated Nitrosyls in Fe and Ru Heme Models

Abucayon, Erwin G.,Powell, Douglas R.,Richter-Addo, George B.

, p. 9495 - 9498 (2017)

The conversion of inorganic NOx species to organo-N compounds is an important component of the global N-cycle. Reaction of a C-based nucleophile, namely the phenyl anion, with the ferric heme nitrosyl [(OEP)Fe(NO)(5-MeIm)]+ generates a mixture of the C-nitroso derivative (OEP)Fe(PhNO)(5-MeIm) and (OEP)Fe(Ph). The related reaction with [(OEP)Ru(NO)(5-MeIm)]+ generates the (OEP)Ru(PhNO)(5-MeIm) product. Reactions with the N-based nucleophile diethylamide results in the formation of free diethylnitrosamine, whereas the reaction with azide results in N2O formation; these products derive from attack of the nucleophiles on the bound NO groups. These results provide the first demonstrations of C-N and N-N bond formation from attack of C-based and N-based nucleophiles on synthetic ferric-NO hemes.

Thermal behaviour of ammonium nitrate prills coated with limestone and dolomite powder

Rudjak,Kaljuvee,Trikkel,Mikli

, p. 749 - 754 (2010)

The thermal behaviour of ammonium nitrate (AN) and its prills coated with limestone and dolomite powder was studied on the basis of commercial fertilizer-grade AN and six Estonian limestone and dolomite samples. Coating of AN prills was carried out on a plate granulator and a saturated solution of AN was used as a binding agent. The mass of AN prills and coating material was calculated based on the mole ratio of AN/(CaO + MgO) = 2:1. Thermal behaviour of AN and its coated prills was studied using combined TG-DTA-FTIR equipment. The experiments were carried out under dynamic heating conditions up to 900 °C at the heating rate of 10 °C min-1 and for calculation of kinetic parameters, additionally, at 2, 5 and 20 °C min-1 in a stream of dry air. A model-free kinetic analysis approach based on the differential isoconversional method of Friedman was used to calculate the kinetic parameters. The results of TG-DTA-FTIR analyses and the variation of the value of activation energy E along the reaction progress α indicate the complex character of the decomposition of neat AN as well as of the interactions occurring at thermal treatment of AN prills coated with limestone and dolomite powder.

Characterization and catalytic activity for the NO decomposition and reduction by CO of nanosized Co3O4

Zhang, Zhaoliang,Geng, Haoran,Zheng, Lisheng,Du, Bin

, p. 317 - 321 (2005)

Nanosized Co3O4 prepared by a precipitation method was characterized by TEM, XRD, BET and TPD techniques, and studied for NO decomposition and reduction by CO. It is found that Co3O4 thus obtained has a specific surface area of 23.4 m2/g and an average particle size of 26 nm. Catalytic tests showed that full NO conversion to N2 was obtained above 300 °C. A redox mechanism between Co 3+ and Co2+ ions based on NO decomposition is proposed.

SURFACE STATES OF MoO3 ON ZrO2 AND CATALYTIC PROPERTIES FOR THE REACTION OF NO WITH H2

Iizuka, Tokio,Itoh, Masahumi,Hattori, Hideshi,Tanabe, Kozo

, p. 501 - 508 (1982)

The adsorption and reaction of nitric oxide on reduced molybdena-zirconia were studied by means of e.s.r., i.r. and u.v. spectroscopies.On the surface, at least two types of nitrosyl complex exist.At an early stage of reduction, a diamagnetic dinitrosyl complex with i.r. bands at ca. 1790 and 1690 cm-1 formed on NO adsorption and was ascribed to Mo(4+)(NO)2.After reduction at a higher temperature, a paramagnetic dinitrosyl species appeared upon NO adsorption and was tentatively assigned to Mo(5+)(NO)2.Nitric oxide can adsorb on Mo(5+) in tetrahedral coordination, but not on Mo(5+) in octahedral coordination.This can be explained by the coordination being limited.For the reaction of NO with H2, the species of Mo(5+)(NO)2 was concluded to be a main active complex in the catalytic cycle.

Solid-gas reactions for nitroxyl (HNO) generation in the gas phase

Carrone, Guillermo,Mazzeo, Agostina,Marceca, Ernesto,Pellegrino, Juan,Suárez, Sebastián,Zarenkiewicz, Jessica,Toscano, John P.,Doctorovich, Fabio

, (2021/07/25)

We present a novel nitroxyl (HNO) generation method, which avoids the need of using a liquid system or extreme experimental conditions. This method consists of the reaction between a gaseous base and an HNO donor (Piloty's acid) in the solid phase, allowi

The influence of Ba addition on thermal stability and catalytic activity of Cu-based mixed oxide

Rachele, Karen Gon?alves,Palacio, Luz Amparo,Zotin, Fatima Maria Zanon

, p. 234 - 242 (2020/07/15)

Catalytic reduction of NO by CO was studied over La2-xBaxCuO4 (x = 0.0 or 0.4) mixed oxides prepared by coprecipitation method. The catalysts were characterized by X ray diffraction (XRD), O2 temperature-programmed desorption (O2-TPD), H2 temperature-programmed reduction (H2-TPR) and X-ray absorption near edge structure (XANES). NO + CO reaction was carried out in a fixed-bed flow reactor, from room temperature to 500 °C, at atmospheric pressure. Both fresh catalysts were active for the NO + CO reaction but when were submitted to thermal aging, the barium free catalyst significantly lost its activity. The partial substitution of La by Ba enhanced the thermal stability and although the activity of the catalyst has decreased, it remains high, approaching 100 % at 500 °C. These results can be associated with reducible copper species observed by XANES in the thermal aged catalyst containing Ba.

The Effects of Platinum Dispersion and Pt State on Catalytic Properties of Pt/Al2O3 in NH3 Oxidation

Slavinskaya, Elena M.,Kibis, Lidiya S.,Stonkus, Olga A.,Svintsitskiy, Dmitry A.,Stadnichenko, Andrei I.,Fedorova, Elizaveta A.,Romanenko, Anatolii V.,Marchuk, Vasyl,Doronkin, Dmitry E.,Boronin, Andrei I.

, p. 313 - 327 (2020/10/30)

Dependence of NH3 oxidation on the state and dispersion of Pt species in Pt/γ-Al2O3 catalysts was investigated. Prereduced Pt/γ-Al2O3 catalysts containing Pt0 nanoparticles exhibited significantly higher activity than preoxidized ones with the same Pt dispersion. The most significant improvement of the catalytic activity (TOF increased by 30 times) was observed when the size of Pt0 particles increased from ~1 to ~8 nm. N2 selectivity was found to be mainly determined by the reaction temperature, with a minor influence of Pt particle size. Preoxidized catalysts containing ionic Pt were activated by the reaction medium, while partial deactivation was observed for the prereduced ones. The activity improvement was associated with the presence of Pt4+/Pt2+ species on the surface of preoxidized catalysts. The activity decrease of the prereduced catalysts was due to the partial oxidation and subsequent redispersion of Pt particles. Introduction of H2O and CO2 to the reaction mixture only moderately influenced NH3 oxidation activity shifting NH3 conversion curves by about +15 °C.