NUMERICAL SIMULATIONS OF HEAT AND MASS TRANSFER IN CONDENSING HEAT EXCHANGERS...ssuser7dcef0
Power plants release a large amount of water vapor into the
atmosphere through the stack. The flue gas can be a potential
source for obtaining much needed cooling water for a power
plant. If a power plant could recover and reuse a portion of this
moisture, it could reduce its total cooling water intake
requirement. One of the most practical way to recover water
from flue gas is to use a condensing heat exchanger. The power
plant could also recover latent heat due to condensation as well
as sensible heat due to lowering the flue gas exit temperature.
Additionally, harmful acids released from the stack can be
reduced in a condensing heat exchanger by acid condensation. reduced in a condensing heat exchanger by acid condensation.
Condensation of vapors in flue gas is a complicated
phenomenon since heat and mass transfer of water vapor and
various acids simultaneously occur in the presence of noncondensable
gases such as nitrogen and oxygen. Design of a
condenser depends on the knowledge and understanding of the
heat and mass transfer processes. A computer program for
numerical simulations of water (H2O) and sulfuric acid (H2SO4)
condensation in a flue gas condensing heat exchanger was
developed using MATLAB. Governing equations based on
mass and energy balances for the system were derived to
predict variables such as flue gas exit temperature, cooling
water outlet temperature, mole fraction and condensation rates
of water and sulfuric acid vapors. The equations were solved
using an iterative solution technique with calculations of heat
and mass transfer coefficients and physical properties.
NUMERICAL SIMULATIONS OF HEAT AND MASS TRANSFER IN CONDENSING HEAT EXCHANGERS...ssuser7dcef0
Power plants release a large amount of water vapor into the
atmosphere through the stack. The flue gas can be a potential
source for obtaining much needed cooling water for a power
plant. If a power plant could recover and reuse a portion of this
moisture, it could reduce its total cooling water intake
requirement. One of the most practical way to recover water
from flue gas is to use a condensing heat exchanger. The power
plant could also recover latent heat due to condensation as well
as sensible heat due to lowering the flue gas exit temperature.
Additionally, harmful acids released from the stack can be
reduced in a condensing heat exchanger by acid condensation. reduced in a condensing heat exchanger by acid condensation.
Condensation of vapors in flue gas is a complicated
phenomenon since heat and mass transfer of water vapor and
various acids simultaneously occur in the presence of noncondensable
gases such as nitrogen and oxygen. Design of a
condenser depends on the knowledge and understanding of the
heat and mass transfer processes. A computer program for
numerical simulations of water (H2O) and sulfuric acid (H2SO4)
condensation in a flue gas condensing heat exchanger was
developed using MATLAB. Governing equations based on
mass and energy balances for the system were derived to
predict variables such as flue gas exit temperature, cooling
water outlet temperature, mole fraction and condensation rates
of water and sulfuric acid vapors. The equations were solved
using an iterative solution technique with calculations of heat
and mass transfer coefficients and physical properties.
Harnessing WebAssembly for Real-time Stateless Streaming PipelinesChristina Lin
Traditionally, dealing with real-time data pipelines has involved significant overhead, even for straightforward tasks like data transformation or masking. However, in this talk, we’ll venture into the dynamic realm of WebAssembly (WASM) and discover how it can revolutionize the creation of stateless streaming pipelines within a Kafka (Redpanda) broker. These pipelines are adept at managing low-latency, high-data-volume scenarios.
HEAP SORT ILLUSTRATED WITH HEAPIFY, BUILD HEAP FOR DYNAMIC ARRAYS.
Heap sort is a comparison-based sorting technique based on Binary Heap data structure. It is similar to the selection sort where we first find the minimum element and place the minimum element at the beginning. Repeat the same process for the remaining elements.
Literature Review Basics and Understanding Reference Management.pptxDr Ramhari Poudyal
Three-day training on academic research focuses on analytical tools at United Technical College, supported by the University Grant Commission, Nepal. 24-26 May 2024
2. 2
Connection Establishment and
Termination
• required by connection-oriented transport
protocols like TCP
• need connection establishment and
termination procedures to allow:
– each end to know the other exists
– negotiation of optional parameters
– triggers allocation of transport entity resources
2
5. 5
Connection Termination
• either or both sides by mutual agreement
• graceful or abrupt termination
• if graceful, initiator must:
– send FIN to other end, requesting termination
– place connection in FIN WAIT state
– when FIN received, inform user and close connection
• other end must:
– when receives FIN must inform TS user and place
connection in CLOSE WAIT state
– when TS user issues CLOSE primitive, send FIN & close
connection
5
6. 6
Connection Establishment
• two way handshake
– A send SYN, B replies with SYN
– lost SYN handled by re-transmission
– ignore duplicate SYNs once connected
• lost or delayed data segments can cause
connection problems
– eg. segment from old connection
6
11. 11
TCP Connection Establishment:
Summary
• three way handshake
– SYN, SYN-ACK, ACK
• connection determined by source and
destination sockets (host, port)
• can only have a single connection between
any unique pairs of ports
• but one port can connect to multiple ports
12. 12
Connection Termination (2)
• also need 3-way handshake
• misordered segments could cause:
– entity in CLOSE WAIT state sends last data segment,
followed by FIN
– FIN arrives before last data segment
– receiver accepts FIN, closes connection, loses data
• need to associate sequence number with FIN
• receiver waits for all segments before FIN sequence
number
12
13. 13
Connection Termination:
Graceful Close
• also have problems with loss of segments and
obsolete segments
• need graceful close which will:
• send FIN i and receive AN i+1
• receive FIN j and send AN j+1
• wait twice maximum expected segment
lifetime
13