Method and device for hydrolyzing pulping
A hydrolysis reaction and reactor technology, which is applied in the field of papermaking and pulping, can solve problems such as environmental pollution and waste of plant resources, and achieve the effects of improving thermal power efficiency, improving utilization rate, and reducing thermal power conversion process
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Embodiment 1
[0038] like Figure 1 to Figure 4 As shown, the device for hydrolysis pulping includes: a preprocessor 1 , a reactor 2 , an expander 3 , a turbocompressor 4 , a gas-liquid separator 5 , and a blower 6 .
[0039] The discharge port of the preprocessor 1 is connected with the feed port of the reactor 2, and the preprocessor 1 is used for heating and pretreating the raw materials required for production. The reactor 2 is cylindrical. The upper part of the reactor is provided with a feed inlet 21 and a gas outlet 22, and the bottom is provided with a feed outlet 23. The reactor 2 includes a heating pipe 24, which is a heating coil, which is located inside the reactor. a gas distributor 25, which includes an air inlet 251 and a plurality of nozzles 252 for exhaust; the expander 3 is connected to the gas outlet of the reactor 2. The turbocompressor 4 is connected to the expander 3 , and the turbocompressor 4 is driven to work by the expander 3 , and the gas outlet of the turbocompr...
Embodiment 2
[0048] The reaction unit that uses is identical with embodiment 1, a kind of method for hydrolysis pulping, comprises the following steps:
[0049] (1) Prepare the raw materials, mix water and bagasse in a mass ratio of 200:1, and then preheat;
[0050] (2) Hydrolysis reaction, put the mixture prepared in step (1) into the reactor, heat up to 300°C, and fill the reactor with CO 2 , the temperature in the reactor is 300°C, and the pressure is 15MPa;
[0051] (3) Take out the mixed gas after reaction in the reactor, the mixed gas contains CO 2 , water vapor, furfural and acetic acid, the flow rate of the mixed gas taken out from the reactor is 0~10000m 3 / h, when the gas flow rate is 0, no gas flows out. Pass the gas through the expander, expand and reduce the pressure to 0~1.0MPa, cool down to 20℃~30℃, enter the gas-liquid separator for separation, the temperature of the gas-liquid separator is 10~20℃, and the pressure is 0.0~ 1.0MPa, the liquid flow rate of the gas-liquid ...
Embodiment 3
[0054] The reaction unit that uses is identical with embodiment 1, a kind of method for hydrolysis pulping, comprises the following steps:
[0055] (1) Prepare the raw materials, mix water and bagasse in a mass ratio of 70:1, and then preheat;
[0056] (2) Hydrolysis reaction, put the mixture prepared in step (1) into the reactor, heat up to 500°C, and fill the reactor with CO 2 , the temperature in the reactor is 500°C, and the pressure is 30MPa;
[0057] (3) Take out the mixed gas after reaction in the reactor, the mixed gas contains CO 2 , water vapor, furfural and acetic acid, the flow rate of the mixed gas taken out from the reactor is 0~10000m 3 / h, when the gas flow rate is 0, no gas flows out. Pass the gas through the expander, expand and reduce the pressure to 0~1.0MPa, cool down to 20℃~30℃, enter the gas-liquid separator for separation, the temperature of the gas-liquid separator is 10~20℃, and the pressure is 0.0~ 1.0MPa, the liquid flow rate of the gas-liquid s...
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