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| | HYDROXYLAMINE PHOSPHATE Basic information |
| | HYDROXYLAMINE PHOSPHATE Chemical Properties |
| Melting point | 169-171 °C(lit.) | | storage temp. | -70°C | | form | frozen liquid | | color | clear colorless | | biological source | human | | Stability: | Stable. Incompatible with bases, oxidizing agents. | | InChI | 1S/3H3NO.H3O4P/c3*1-2;1-5(2,3)4/h3*2H,1H2;(H3,1,2,3,4) | | InChIKey | XBUFCZMOAHHGMX-UHFFFAOYSA-N | | SMILES | NO.NO.NO.OP(O)(O)=O |
| Hazard Codes | C,N | | Risk Statements | 22-34-43-48/22-50 | | Safety Statements | 26-36/37/39-45-61 | | RIDADR | UN 3262 8/PG 2 | | WGK Germany | 3 | | F | 21 | | Storage Class | 1 - Explosive hazardous materials | | Hazard Classifications | Acute Tox. 4 Dermal
Acute Tox. 4 Oral
Aquatic Acute 1
Carc. 2
Expl. 1.1
Eye Irrit. 2
Skin Irrit. 2
Skin Sens. 1
STOT RE 2 |
| | HYDROXYLAMINE PHOSPHATE Usage And Synthesis |
| Chemical Properties | white crystalline powder | | Uses | Reactant for:
- Aqueous preparation of rhenium diphosphate
- Gas and solid state reactions with acetone
- Hydroxylamine formation via photolysis
| | Biochem/physiol Actions | MAO inhibitor; inhibits platelet aggregation | | Synthesis | Before feeding the inorganic liquid in the hydroxylamine reactor, by continuously replenishing 30-99% (wt%) nitric acid (of which the nitrite content was less than 0.3% wt%, and the content of the scorch residue was less than 0.4% wt%), so that the hydroxylamine reactor inorganic liquid feeding volume was 80 m3/h, and the inorganic liquid feeding concentration of hydrogen ions (H+) was 2.65 mol/kg, the hydroxylamine root ions ( NH3OH+) concentration of 0.06 mol/kg, free nitric acid concentration of 0.66 mol/kg, when the reaction temperature is 60 ??, the pressure is 2450 KPa (gauge pressure), the hydrogen concentration of 32.07% (% by volume), in the platinum / palladium / charcoal (Pt / Pd / C, containing Pt8%, Pd2%, activated carbon as a carrier, the United States JM company production) catalyst role Under the catalyst of Pt/Pd/C (Pt/Pd/C, containing Pt8%, Pd2%, activated carbon as carrier, produced by JM Company, USA), the hydroxylamine reactor effluent inorganic liquid hydrogen ion concentration (H+) was 0.40 mol/kg, and the hydroxylamine root ion (NH3OH+) concentration was 0.89 mol/kg (the net generation of hydroxylamine phosphate was 0.83 mol/kg). |
| | HYDROXYLAMINE PHOSPHATE Preparation Products And Raw materials |
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