A bed section b freeboard section and c conical closure section with inlet cone.
Laboratory scale fluidized bed reactor.
This latter process is widely used in laboratory scale systems by fluidizing the bed in a once through cycle with hcl in.
Thus it is important to have available fixed bed reactors capable of operating at intermediate interstitial fluid velocities to establish the relationship between 1 k.
A laboratory scale fluidized bed reactor was designed and fabricated successfully.
Developing a scalable model from the laboratory fluidized bed is particularly important because of the potential for.
The reactor consists of three sections.
The aim of this project was to construct a laboratory scale fluidized bed reactor that simulates the behavior of full scale municipal solid waste combustors.
The size of the laboratory scale fluidized bed reactor is 5 kw which corresponds to a fuel feeding rate of approximately 1 kg h.
Catalyst particles were attrited at room temperature in the laboratory scale fluidized bed.
A bed section.
A bed section a.
The design parameters which affect the performances are identified and discussed.
The design of this reactor is thoroughly described.
The reactor system consists of four parts.
The reactor system consists of four parts.
The size of the laboratory scale fluidized bed reactor is 5 kw which corresponds to a fuel feeding rate of approximately 1 kg h.
Several relatively large laboratory scale high pressure fluidized beds designed for pyrolysis and gasification experiments have been reported in the literature.
The 5 kw laboratory scale fluidized bed reactor de scribed in the article is the second generation of the reactor used by fängmark 20 21 there are several unique features about our 5 kw reactor.
Morris and keairns 1979 have described a reactor made of inconel 600 35 mm i d 330 mm long placed inside a.
4 3 1 a survey of small scale high pressure fluidized bed reactors.
The interstitial fluid velocities obtainable in laboratory scale fixed bed reactors determine that portion of the relationship dominated by stagnant film diffusion resistance.