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Drying Technology
An International Journal
Volume 40, 2022 - Issue 14
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Articles

System design and thermo-economic analysis of municipal solid waste power system integrated with steam dryer

, , , &
Pages 2904-2919 | Received 28 Apr 2021, Accepted 28 Aug 2021, Published online: 26 Sep 2021
 

Abstract

High moisture content of municipal solid waste (MSW) decreases the efficiency of power plant firing MSW directly. The MSW power system integrated with an external steam dryer and waste heat recovery system (WHRS) is proposed to enhance the MSW power plant (MSWP) efficiency. A reference case study with a 12 MW MSWP is carried out. The efficiency of MSWP integrated with a steam dryer can be enhanced by 1.07 percentage points (%-pts) and 0.36%-pts with 0.21 and 1.13 MPa steam extraction, respectively, as dryer heating source at a dryness degree of 0.25. Furthermore, when the WHRS is integrated, the power plant efficiency is enhanced by 1.79%-pts and 1.08%-pts. Then, economic analysis is carried out, and results show that the MSWP can bring profits with the integration of a steam dryer with steam 1.13 MPa steam as heat source at rated degree of dryness.

Nomenclature

Abbreviation

AAP=

additional air preheater

COND=

condenser

CP=

condensate pump

DE=

deaerator

ECO=

economizer

EVA=

evaporator

FP=

feedwater pump

Gen=

generator

HTAP=

high temperature air preheater

HPH=

high pressure heater

LPH=

Low pressure heater

LTAP=

low temperature air preheater

LTE=

low temperature economizer

MSW=

municipal solid waste

MSWP=

conventional MSW power plant

MSWPD=

MSW power plant integrated dryer

MSWPDR=

MSW power plant integrated dryer and waste heat recovery system

NPV=

net present value

SC=

shaft seal cooler

SH=

superheater

WHRS=

waste heat recovery system

pts=

points

%-pts=

percentage points

Symbol

h =

enthalpy, kJ·kg−1

H =

hydrogen

I =

discount rate

m =

mass, kg

P =

pressure, MPa

s =

entropy, kJ·kg−1·K−1

T =

temperature, K

Subscript

ar=

as received basis

b=

boiler

ex=

exergy

d=

dried

ph=

physical

sat=

saturated

sur=

surrounding

t=

turbine

w=

water

Disclosure statement

The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.

Additional information

Funding

Authors’ work was supported the National Natural Science Foundation of China (Grant Number 52022079).

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