Preparation of organometallic compounds
A compound and metal technology, applied in 3/13 organic compounds without C-metal bonds, 4/14 organic compounds without C-metal bonds, organic chemistry, etc., can solve the problem of low yield of TMG
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0056] The table below shows various organometallic compounds prepared according to this method. Suitable organic solvents are listed where such solvents are required or optionally used.
[0057] compound
[0058] Abbreviations have the following meanings: LAB = linear alkylbenzene; TDMA = tetrakis(dimethylamine) or [(CH 3 ) 2 N] 4 ; and TEMA=tetrakis(methylethylamine) or [(CH 3 )(CH 3 CH 2 )N] 4 .
Embodiment 2
[0060] In a reactor (which comprises a contact zone containing a first inlet and a second inlet, a plurality of heat transfer zones, a plurality of mixing zones with different radii of curvature and a reaction zone after each mixing zone), at 200- 300KPa, 10-30°C temperature, add a large amount at a flow rate of 10-20 units / h as the first reactant TMA liquid flow and at 200-300KPa, 10-30°C temperature, add a large amount at a flow rate of 20-40 units / h as the second reaction A liquid stream of tripropylamine ("TPA") was passed through the reactor inlet into a laminar flow environment. The flow rate was set to control the molar ratio of TPA to TMA slightly greater than 1 / 1. The two reactant streams are fed into the mixing zone of the reactor with concentric and substantially laminar flow. Each reactant stream entering the mixing zone has a Reynolds number 20 seconds. Upon leaving the reactor, the product (TMA-TPA adduct) stream is passed to a separation unit to remove impurit...
Embodiment 3
[0062] Into a reactor similar to the reactor used in Example 2, a large amount of the TMA-TPA liquid from Example 2 was added as the first reactant at a temperature of 200-300KPa, 40-60°C at a flow rate of 20-40 units / h Flow and add a large amount of gallium chloride in aromatic hydrocarbon solvent as the second reactant at a flow rate of 20-40 units / h at a temperature of 200-300KPa, 2-10°C to maintain the molar ratio of aluminum to gallium metal greater than 1 / 1 . The heat transfer zone of the reactor maintains the temperature at the outlet of the reactor at 85-100°C. The reactor was operated continuously for more than 24 hours, during which time the product (trimethylgallium or "TMG") was continuously purified in the separation unit to produce over 100 kg of high purity TMG in an overall yield of >85%.
PUM
| Property | Measurement | Unit |
|---|---|---|
| length | aaaaa | aaaaa |
| diameter | aaaaa | aaaaa |
| melting point | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More 