Dynamic forces on a horizontal slat immersed in a fluidized bed of fine particles

2017 ◽  
Vol 117 ◽  
pp. 604-613 ◽  
Author(s):  
Duiping Liu ◽  
Shuhao Zhang ◽  
Ruoyi Wang ◽  
Yongmin Zhang
Author(s):  
Steven L McDougall ◽  
Mohammad Saberian ◽  
Cedric Briens ◽  
Franco Berruti ◽  
Edward W Chan

Monitoring the fluidization quality represents an operating challenge for many processes in which a liquid is sprayed into a gas-fluidized bed, such as fluid coking, fluid catalytic cracking, gas-phase polymerization, agglomeration and drying. Although the presence of liquid will generally have an adverse effect on fluidization, there are often strong incentives in operating with high liquid loadings. For the fluid coking process, for example, operating at lower reactor temperature increases yield and reduces emissions but increases the bed wetness, which may lead to local zones of poor mixing, local defluidization and a reduction in fluidization quality, compromising the reactor performance and stability. The objective of this study is to develop reliable methods to quantify the effects of liquids on fluidized beds.This study examined several methods to evaluate the fluidization quality. Each method was tested in a 3 m tall column, 0.3 m in diameter. Bed wetness was achieved with an atomized spray of various liquids, spanning a wide range of liquid properties.The introduction of liquid in a fluidized bed may result in the formation of wet agglomerates that settle at the bottom of the bed. The liquid may also spread on the particles, increasing their cohesivity and reducing the bed fluidity.Several experimental methods were developed to characterize the effect of liquids on fluidization. Some methods such as the falling ball velocity or the detection of micro-agglomeration from the entrainment of fine particles, are unaffected by agglomerates and detect only the change in bed fluidity. Other methods, such as deaeration or the determination of bubble size from the TDH, are affected by agglomerate formation and changes in bed fluidity.


1998 ◽  
Vol 24 (1) ◽  
pp. 69-74 ◽  
Author(s):  
DAISUKE TANEDA ◽  
HITOSHI TAKAHAGI ◽  
SYOUICHI AOSHIKA ◽  
NOBUYOSHI NAKAGAWA ◽  
KUNIO KATO

2019 ◽  
Vol 19 (3) ◽  
pp. 227-234
Author(s):  
N. A. Yazykov ◽  
A. D. Simonov ◽  
Yu. V. Dubinin ◽  
O. O. Zaikina

Results of the studies of catalytic combustion of peat, anthracite, as well as the mixture at the peat to anthracite weight percent ratio 40/60 are discussed. The degree of the mixture burning-off was shown to increase when peat evolving large quantity of volatile substances is added to anthracite. The burn-up degrees of the solid fuel particles less than 1.25 mm in size were 98.2 % of peat, 50.9 % of anthracite, 74.2 % of the peat and anthracite mixture at 700–750 °C and 1 m height bed of the industrial aluminum-copper-chromium oxide catalyst IC-12-70. In combusting coarse particles (equivalent diameter 11.6–18.6 mm) of molded peat and anthracite mixture, the burn-up degree was 80.5 % at the top of the fluidized catalyst bed. The burn-up degree of the coarse particles fed to the bottom of the fluidized bed was estimated with allowance for the burn-up degree of fine particles moving through the bed. With the coarse molded particles of the peat and anthracite mixture fed to 1 m height catalyst bed, the burn-up degree was shown to reach no less than 95 %. When the catalyst used is 2 mm in size, the peat and anthracite particles comprised in the molded fuel must be no more than 1–1.5 mm in size in order to prevent from ash accumulation in the fluidized catalyst bed.


2015 ◽  
Vol 35 (3) ◽  
pp. 2801-2809 ◽  
Author(s):  
M. Alfe ◽  
P. Ammendola ◽  
V. Gargiulo ◽  
F. Raganati ◽  
R. Chirone

Sign in / Sign up

Export Citation Format

Share Document