A lubricating device for welding slide rail of dust removal pipe
A technology of lubricating device and dust removal pipe, which is used in lubricating oil containers, lubricating parts, engine lubrication, etc., can solve the problems of not being able to supply different types of lubricating oil, affecting the service life of sliding rails and sliding seats, etc.
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Embodiment 1
[0056] Prepare the collection container 8-6-2-2-1-6 of the present invention according to the following steps, and in parts by weight:
[0057] Step 1: In the mechanically stirred UASB reactor, add 326.2 parts of iron-free manganese water and 118.0 parts of 16-methylheptadecanic acid, start the mixer in the mechanically stirred UASB reactor, set the speed at 119rpm, and start the mechanically stirred UASB The light oil heater in the reactor raised the temperature to 134.2°C, added 121.4 parts of 2-methoxy-3-(2-methylpropyl)pyrazine and stirred evenly, and reacted for 111.0 minutes, then added methyl ionone 117.2 parts, the flow rate is 110.8 m 3 The xenon gas per min was 111.0 minutes; after that, 120.3 parts of yeast extract were added to the mechanically stirred UASB reactor, and the light oil heater in the mechanically stirred UASB reactor was started again to raise the temperature to 151.4°C, kept for 111.2 minutes, and added 4, 4'-(1-methylethylene)bisphenol and (chlorom...
Embodiment 2
[0064] Prepare the collection container 8-6-2-2-1-6 of the present invention according to the following steps, and in parts by weight:
[0065] Step 1: In the mechanically stirred UASB reactor, add 551.4 parts of iron-free manganese water and 160.4 parts of 16-methylheptadecanic acid, start the mixer in the mechanically stirred UASB reactor, set the speed at 165rpm, and start the mechanically stirred UASB The light oil heater in the reactor raised the temperature to 135.4°C, added 230.1 parts of 2-methoxy-3-(2-methylpropyl)pyrazine and stirred evenly, and reacted for 122.4 minutes, then added methyl ionone 134.6 parts, the flow rate is 151.6 m 3 The xenon gas per min was 122.4 minutes; after that, 177.3 parts of yeast extract were added to the mechanically stirred UASB reactor, and the light oil heater in the mechanically stirred UASB reactor was started again to raise the temperature to 184.1°C, kept for 122.6 minutes, and added 4, 4'-(1-methylethylene)bisphenol and (chlorom...
Embodiment 3
[0072] Prepare the collection container 8-6-2-2-1-6 of the present invention according to the following steps, and in parts by weight:
[0073] Step 1: In the mechanically stirred UASB reactor, add 326.9 parts of iron-free manganese water and 118.9 parts of 16-methylheptadecanic acid, start the stirrer in the mechanically stirred UASB reactor, set the rotating speed to be 119rpm, start the mechanical Stir the light oil heater in the UASB reactor to raise the temperature to 134.9°C, add 121.9 parts of 2-methoxy-3-(2-methylpropyl)pyrazine and stir evenly, carry out the reaction for 111.9 minutes, add methyl 117.9 parts of ionone, the flow rate is 110.9 m 3 The xenon gas per min was 111.9 minutes; after that, 120.9 parts of yeast extract were added to the mechanically stirred UASB reactor, and the light oil heater in the mechanically stirred UASB reactor was started again to raise the temperature to 151.9°C, kept for 111.9 minutes, and added 4, 4'-(1-methylethylene)bisphenol and...
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