Dismiss
InnovationQ will be updated on Sunday, Oct. 22, from 10am ET - noon. You may experience brief service interruptions during that time.
Browse Prior Art Database

Circulation Multistage Fuidized Bed Combustor Design Concept

IP.com Disclosure Number: IPCOM000219909D
Publication Date: 2012-Jul-17

Publishing Venue

The IP.com Prior Art Database

This text was extracted from a PDF file.
This is the abbreviated version, containing approximately 15% of the total text.

Page 01 of 16

CTWCIILATTNG ~I].TT~TACE FT.ITTDTVVD BED COMBUSTOR DESIGN CONCEPT

Lowell D. Fra]ey Keh-Hsien Hsiao

            Aage Solbakken
/a~u~aLi <:as) Sadhukhan lung-Y1 L1n

INTRODUCTION

In a previous s[udy for DOE, M. W. Kellogg performed a design analysis for the Kellogg CFBC. The analysis conclusively showed that the Kellogg CFBC met or exceeded perfor- mance criteria for advanced atmospheric FBC's. The Kellogg
CFBC is described in prior publications (i-6).

This paper presents the results of a further study made for DOE to reduce capital and operating costs of the Kellogg CFBC, configured into an industriai" boiler system of 150,000 pounds per hour steaming capacity. The results show the Kellogg CFBC to be a very economical concept.

When compared to the lowest cost bubbling-bed system of the same capacity, the Kellogg CFBC is 24% less costly. The basic equip-
ment cost has a greater difference~ $40.6/1000 ib steamfor the CFBC
and $59.3/1000 ib steam for the bubbl~ng-bed, i.e., 32% less costly.

The cost of steam from the opti- mized Kellogg CFBC is 18.8% less

1

] /M. W. Kellogg Company, Technology |Industrial Park Ten, Houston, TX 77084

  _ /M. W. Kellogg Company ~ . /M. W. Kellogg Company ~ ~ /M. W. Kellogg Company i D /M. W. Kello Com an ~ve[

than from a bubbling-bed system. During the earlier DOE study and subsequent scale-up studies, areas of over-conservatism in Kellogg's design were identified. Of particular concern was the basic kinetic model wherein only sulfur dioxide reactions with lime had been considered and which had not adequately accounted for coal devolatilization. The first effort was to remedy these deficiencies and take into account reactions occurring under reducing conditions (primary air less than stoichi- ometric), mainly H2S-CaO
reactions and nitrogen compounds degrading to nitrogen. The computerized kinetic model has proven to be a powerful tool. It presents a better understanding of the complex reactions that occur in the CFBC's simple geometry and allows designers to develop a feel for the interactions of parameters of importance. The targets of reduced combustor height, diameter and pressure drop were readily achieved. Additionally, the nuances of ~igher temperatures and very fine particles were easily developed. A one T~ pilot plant has been constructed at the MWK Technical Development Center to verify the kinetic model.

)pment Center, 16200 Park Row,


Page 02 of 16

~h~!~a~l~'~'scale~up studies made by Kellogg identified several system areas whic~ needed intensive review since thel~ contributions to capital cost appeared excessive: structures, piping, and instrumen- tation/control. It appeared that some additional c~st savings could be achieved in th~ coal/llmestone feed system, cyclones, and boiler by more innovative design. Accord- ingly, a full design review by

Kellogg's commercial engineering staff was made.

The following sections describe MWK CFBC concepts, the kinetic model, a description of the pilot plant, plant design f...