High pressure steam pipe cutting device for treating carbon tetrachloride
A high-pressure steam and cutting device technology, applied in welding equipment, gas flame welding equipment, metal processing equipment, etc., can solve the problems of slow delivery time, high cost, and low cutting efficiency.
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Embodiment 1
[0072] Prepare the acetylene connecting pipe 8-5-4 of the present invention according to the following steps, and in parts by weight:
[0073] Step 1: In the continuous stirred tank reactor, add 323.7 parts of ultrapure water and 115.1 parts of 2-methyldodecylaldehyde, start the mixer in the continuous stirred tank reactor, set the speed at 116rpm, start The heat conduction oil heater in the continuous stirred tank reactor raised the temperature to 131.7°C, added 118.4 parts of 2-methoxy-3-methylpyrazine and stirred evenly, and reacted for 108.1 minutes, then added 2-[(methylpyrazine Esteramino)-[2-nitro-5-(n-thiopropyl)-phenylimino] methylamino] 114.1 parts of ethyl sulfuric acid, the flow rate is 107.6m 3 The xenon gas per min was 108.1 minutes; after that, 117.0 parts of yeast ribonucleic acid were added to the continuous stirred tank reactor, and the heat conduction oil heater in the continuous stirred tank reactor was started again to raise the temperature to 148.4°C, kep...
Embodiment 2
[0080] Prepare the acetylene connecting pipe 8-5-4 of the present invention according to the following steps, and in parts by weight:
[0081] Step 1: In the continuous stirred tank reactor, add 548.0 parts of ultrapure water and 157.8 parts of 2-methyldodecylaldehyde, start the mixer in the continuous stirred tank reactor, set the speed at 162rpm, start The heat conduction oil heater in the continuous stirred tank reactor raised the temperature to 132.0°C, added 227.9 parts of 2-methoxy-3-methylpyrazine and stirred evenly, and reacted for 119.8 minutes, then added 2-[(methylpyrazine Esteramino)-[2-nitro-5-(n-thiopropyl)-phenylimino] methylamino] 131.6 parts of ethyl sulfuric acid, the flow rate is 148.6m 3 The xenon gas per min was 119.8 minutes; after that, 174.5 parts of yeast ribonucleic acid were added to the continuous stirred tank reactor, and the heat conduction oil heater in the continuous stirred tank reactor was started again to raise the temperature to 181.9°C, and...
Embodiment 3
[0088] Prepare the acetylene connecting pipe 8-5-4 of the present invention according to the following steps, and in parts by weight:
[0089] Step 1: In the continuous stirred tank reactor, add 323.9 parts of ultrapure water and 115.9 parts of 2-methyldodecylaldehyde, start the mixer in the continuous stirred tank reactor, set the speed at 116rpm, start The heat conduction oil heater in the continuous stirred tank reactor raised the temperature to 131.9°C, added 118.9 parts of 2-methoxy-3-methylpyrazine and stirred evenly, and reacted for 108.9 minutes, then added 2-[(methylpyrazine Esteramino)-[2-nitro-5-(n-thiopropyl)-phenylimino] methylamino] 114.9 parts of ethyl sulfuric acid, the flow rate is 107.9m 3 xenon gas per min for 108.9 minutes; then add 117.9 parts of yeast ribonucleic acid into the continuous stirred tank reactor, start the heat conduction oil heater in the continuous stirred tank reactor again, make the temperature rise to 148.9°C, keep it warm for 108.9 minu...
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