Biogenic porous carbon silicon dioxide compositions and methods of making and using same
US-2021220801-A1 · Jul 22, 2021 · US
US11427775B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11427775-B2 |
| Application number | US-202017074808-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 20, 2020 |
| Priority date | Oct 21, 2019 |
| Publication date | Aug 30, 2022 |
| Grant date | Aug 30, 2022 |
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Disclosed herein are integrated preparation and detection devices for studying biomass-burning aerosols, where the devices include a micro-fluidized bed reactor (MFBR), a transmission line, and an on-line detection unit that are connected in sequence. The MFBR may include a pyrolysis reactor and a pyrolysis furnace; the pyrolysis reactor may include a thermocouple, an introduction tube, and quartz sands; the on-line detection unit may be an on-line photoionization mass spectrometer; and the photoionization mass spectrometer may include a laser desorption system, a laser ionizer and a light energy ionizer. Devices of the present disclosure are beneficial to retain the original state of aerosol particles, and the fixed MFBR can realize rapid pyrolysis of a biomass due to its high and stable heat conduction efficiency, which is beneficial to studying the formation mechanism of aerosol particles.
Opening claim text (preview).
What is claimed is: 1. A method for preparing an aerosol, the method comprising: placing a biomass sample in an upper half of a pyrolysis reactor contained in a micro-fluidized bed reactor, wherein the micro-fluidized bed reactor is made of quartz glass, the pyrolysis reactor contains quartz sand, and the quartz sand is located at a position 3 cm above the bottom of the pyrolysis reactor with a thickness of 3 mm; sealing the micro-fluidized bed reactor and introducing nitrogen in order to remove oxygen from the micro-fluidized bed reactor; and introducing the biomass sample into the quartz sand and subjecting the biomass sample to pyrolysis due to a uniform temperature range of the quartz sand to form the aerosol with a carrier gas introduced into the pyrolysis reactor during the pyrolysis, wherein a flow rate of the carrier gas is controlled so as to avoid a secondary reaction of the aerosol. 2. The method according to claim 1 , wherein the micro-fluidized bed reactor adopts a fixed design. 3. The method according to claim 1 , wherein the micro-fluidized bed reactor further contains a pyrolysis furnace. 4. The method according to claim 1 , wherein the pyrolysis reactor further contains a thermocouple and an introduction tube.
using wave or particle radiation to ionise a gas, e.g. in an ionisation chamber · CPC title
with means for pyrolysis · CPC title
with means for introducing as a spray, a jet or an aerosol (electrospray ion sources H01J49/165) · CPC title
Details of feeding means · CPC title
Inert particles, e.g. as heat exchange medium in a fluidized or moving bed, heat carriers, sand · CPC title
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