Manganese slag thermal insulation material combined type paving mechanism
A thermal insulation material, combined technology, applied in transportation and packaging, loading/unloading, etc., can solve problems such as low leveling efficiency, high local accumulation, and failure to meet design requirements.
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0090] Prepare the base pipe shell 4-2-2-1 of the present invention according to the following steps, and count in parts by weight:
[0091] S1: In the stirring type biomass thermal energy reactor, add 337.4 parts of demineralized pure water and 129.0 parts of 13-methylpentadecaepoxyhetero-10-en-2-one, start the stirrer in the stirring type biomass thermal energy reactor , set the rotation speed to 130rpm, start the steam extraction heating evaporator in the stirred biomass thermal energy reactor, and raise the temperature to 145.4°C;
[0092] S2: Add 2-[4-[[1-[[(2-methoxy-5-methyl-4-sulfonic acid phenyl)amino]carbonyl]-2-oxopropyl]azo]benzene Base]-6-methyl-7-benzothiazole sulfonic acid disodium salt 132.6 parts, stir evenly, add 3-(methylthio) propanal 128.9 parts;
[0093] S3: The flow rate is 121.7m 3 Argon gas per min for 122.0 minutes; then add 131.8 parts of Jinguanghong into the stirred biomass thermal energy reactor, and start the steam extraction heating evaporator...
Embodiment 2
[0100] Prepare the base pipe shell 4-2-2-1 of the present invention according to the following steps, and count in parts by weight:
[0101] S1: In the stirred type biomass thermal energy reactor, add 562.3 parts of demineralized pure water and 171.9 parts of 13-methylpentadecaepoxyhetero-10-en-2-one, start the stirrer in the stirred type biomass thermal energy reactor , set the rotation speed at 176rpm, start the steam extraction heating evaporator in the stirred biomass thermal energy reactor, and raise the temperature to 146.3°C;
[0102] S2: Add 2-[4-[[1-[[(2-methoxy-5-methyl-4-sulfonic acid phenyl)amino]carbonyl]-2-oxopropyl]azo]benzene Base]-6-methyl-7-benzothiazole sulfonic acid disodium salt 241.6 parts, stir evenly, add 3-(methylthio) propanal 145.4 parts;
[0103] S3: The inflow flow rate is 162.4m 3 / min of argon for 133.9 minutes; then add 188.6 parts of Jinguanghong into the stirred biomass thermal energy reactor, and start the steam extraction heating evaporato...
Embodiment 3
[0110] Prepare the base pipe shell 4-2-2-1 of the present invention according to the following steps, and count in parts by weight:
[0111] S1: In the stirred type biomass thermal energy reactor, add 380.5 parts of demineralized pure water and 150.0 parts of 13-methylpentadecaepoxyhetero-10-en-2-one, start the stirrer in the stirred type biomass thermal energy reactor , set the rotation speed to 150rpm, start the steam extraction heating evaporator in the stirred biomass thermal energy reactor, and raise the temperature to 146.0°C;
[0112] S2: Add 2-[4-[[1-[[(2-methoxy-5-methyl-4-sulfonic acid phenyl)amino]carbonyl]-2-oxopropyl]azo]benzene Base]-6-methyl-7-benzothiazole sulfonic acid disodium salt 166.0 parts, stir evenly, add 3-(methylthio) propanal 135.0 parts;
[0113] S3: The incoming flow rate is 150.0m 3 Argon gas per min for 126.0 minutes; then add 170.0 parts of Jinguanghong into the stirred biomass thermal energy reactor, and start the steam extraction heating eva...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 


