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14515-52-7

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14515-52-7 Usage

Check Digit Verification of cas no

The CAS Registry Mumber 14515-52-7 includes 8 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 5 digits, 1,4,5,1 and 5 respectively; the second part has 2 digits, 5 and 2 respectively.
Calculate Digit Verification of CAS Registry Number 14515-52:
(7*1)+(6*4)+(5*5)+(4*1)+(3*5)+(2*5)+(1*2)=87
87 % 10 = 7
So 14515-52-7 is a valid CAS Registry Number.

14515-52-7SDS

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 Dichlorotetrakis(pyridyl) platinum

1.2 Other means of identification

Product number -
Other names p-sulfobenzoic acid potassium salt

1.3 Recommended use of the chemical and restrictions on use

Identified uses For industry use only.
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:14515-52-7 SDS

14515-52-7Downstream Products

14515-52-7Relevant articles and documents

Sol-gel synthesis of Pt/Al2O3 catalysts: Effect of Pt precursor and calcination procedure on Pt dispersion

Hu, Linjie,Boateng, Kenneth A.,Hill, Josephine M.

, p. 51 - 60 (2006)

Pt/Al2O3 catalysts are used in a wide variety of reactions. Tailoring the catalyst structure is important in order to efficiently and effectively utilize the noble metal. In this work, the effects of Pt precursor (Pt(NH3)4Cl2, Pt(C5H5N)4Cl2, Pt(CH3NH2)4Cl2, or Pt(C4H9NH2)4Cl2) and calcination procedure (heating rates of 2 °C/min or 10 °C/min in different atmospheres) have been investigated for 1.5 wt% Pt/Al2O3 catalysts prepared by sol-gel synthesis. After drying, calcination, and reduction, the Pt dispersion was measured by H2 chemisorption. The catalyst structures were characterized using X-ray diffraction, N2 adsorption, and transmission electron microscopy. The Pt precursors as well as the calcination procedures influenced the Pt dispersion. Higher dispersions were obtained using a lower heating rate (2 °C/min), an ammonia precursor, and a flowing gas stream (as opposed to static). Monitoring the emissions during calcination with time resolved mass spectrometry indicated that decomposition of the precursors could be achieved in helium and that subsequent treatment in oxygen was not required. Differential thermal analysis indicated that larger heat flows resulted at the higher heating rate (10 °C/min) and with the pyridine precursor, compared to the ammonia precursor. The larger heat flows may have caused more sintering and, thus, a lower dispersion. Toluene hydrogenation was used as a model reaction to demonstrate that the catalysts with higher dispersions had higher activities and better catalyst stability.

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