Example files from Absorption Chillers and Heat Pumps
by K.E. Herold,
R. Radermacher and S.A. Klein, CRC 1996
List of EES Files
File names marked with asterisk can also be downloaded from the CRC Press World Wide Web server by accessing the CRC Press home page. Follow the prompts to the section for Absorption Chillers and Heat Pumps.
If you have EES installed on your PC, you should be able to run any of the hotlinked files on this page by clicking on the highlighted example name. Your browser must be set so that it recognizes files with extension EES as MIME type 'application/ees' and so that it knows to start EES when it encounters such a file. In Navigator, this can be easily setup by going to Options|General Preferences|Create New Type. Then just follow the prompts. Note that the EES files are stored with upper case extension (for some reason). In Explorer, a similar setup is required.
| Chapter 2 | Example 2.2 |
| Chapter 3 | Example [3.1], [3.2], [3.3] |
| Chapter 4 |
Example [4.1], [4.2], [4.3], [4.4], [4.5], [4.6], [4.7], [4.8], [4.9], [4.10], [4.11] |
| Chapter 6 |
Table [6.1], [6.3], [6.6] Figure [6.3], [6.13], [6.9], [6.10], [6.11], [6.12], [6.13], [6.14], [6.15], [6.16], [6.17], [6.18], [6.19], [6.20], [6.21], [6.25] |
| Chapter 7 |
Table 7.4, Table 7.5, Series flow, solution to low desorber first |
|
Table [8.1]
, [8.3]
, [8.5] |
|
| Chapter 9 |
Example [9.1]
, [9.2]
, [9.3]
, [9.4]
, [9.5]
, [9.6] |
| Chapter 10 |
Example [10.1]
, [10.2] |
|
Example [11.1]
, [11.2]
, [11.3] |
If you have comments or suggestions, email me at herold@eng.umd.edu
|
CHAPTER 2
|
Example 2.2 Absorption Cycle Optimization
|
CHAPTER 3 |
Example
3.1 Relationship Between Partial
Molal and Partial Mass Properties
Example 3.2 Thermodynamics Consistency
Example 3.3 Total Evaporation of
Ammonia/Water Mixture
|
CHAPTER 4 |
Example
4.1 Adiabatic Mixing with
Water/Lithium Bromide
Example 4.2 Desorption
Example 4.3 Desorption of Water from
Aqueous Lithium Bromide
Example 4.4 Absorber
Example 4.5 Absorption of Water Vapor
into Aqueous Lithium Bromide
Example 4.6 Condensation and Evaporation
of Water
Example 4.7 Throttling Process with Pure
Fluid
Example 4.8 Throttling Aqueous Lithium Bromide
Example 4.9 Throttling of Liquid Ammonia/Water
Example 4.10 Reflux Cooler
Example 4.11 Rectifier
|
CHAPTER 6 |
Table
6.1 Operating conditions for
single-effect water/lithium bromide machine
Table 6.3 Operating conditions for a
single-effect water/lithium bromide cycle with heat exchangers
Table 6.6 Single-effect Type II
operating conditions
Figure 6.3 Cooling COP versus
solution heat exchanger effectiveness for a single-effect chiller
Figure 6.13 Effect of cooling water
inlet temperature on COP and capacity for a single-effect
water/lithium bromide absorption chiller
Figure 6.9 Effect of desorber inlet
temperature on COP and capacity for a single-effect water/lithium
bromide absorption chiller
Figure 6.10 Effect of desorber inlet
temperature on heat transfer for a single-effect water/lithium bromide
absorption chiller
Figure 6.11 Effect of desorber inlet
temperature on temperatures for a single-effect water/lithium bromide
absorption chiller
Figure 6.12 Effect of chilled water
inlet temperature on COP and capacity for a single-effect
water/lithium bromide absorption chiller
Figure 6.13 Effect of cooling water
inlet temperature on COP and capacity for a single-effect
water/lithium bromide absorption chiller
Figure 6.14 Effect of solution pump
flow rate on COP, capacity and solution heat exchanger heat transfer
rate for a single-effect water/lithium bromide absorption chiller
Figure 6.15 Effect of desorber heat
transfer fluid flow rate on COP and capacity for a single-effect
water/lithium bromide absorption chiller
Figure 6.16 Effect of pressure drop
between evaporator and absorber on COP and capacity for a
single-effect water/lithium bromide absorption chiller
Figure 6.17 Effect of desorber heat
exchanger on COP and capacity for a single-effect water/lithium
bromide absorption chiller
Figure 6.18 Effect of absorber heat
exchanger on COP and capacity for a single-effect water/lithium
bromide absorption chiller
Figure 6.19 Effect of condenser heat
exchanger on COP and capacity for a single-effect water/lithium
bromide absorption chiller
Figure 6.20 Effect of evaporator
heat exchanger on COP and capacity for a single-effect water/lithium
bromide absorption chiller
Figure 6.21 Effect of solution heat
exchanger on COP and capacity for a single-effect water/lithium
bromide absorption chiller
Figure 6.25 Effect of solution heat
exchanger effectiveness of COP and capacity of the Type II cycle
|
CHAPTER 7 |
Table
7.4 Baseline operating conditions
for a parallel flow double-effect water/lithium bromide machine
Table 7.5 Operating conditions for a
series flow double-effect water/lithium bromide machine
Series flow, solution to low desorber
first
|
CHAPTER 8 |
Table 8.1
Operating conditions for the
half-effect cycle
Table 8.3 Operating conditions for the
triple-effect cycle
Table 8.5 Operating conditions for the
resorption cycle
|
CHAPTER 9 |
Example
9.1 Evaporator Temperature Glide
Example 9.2 Single-Stage Ammonia/Water System
Example 9.3 Subcooler
Example 9.4 Subcooler with Liquid Evaporation
Example 9.5 Rectifier Heat Integration
Example 9.6 Solution Recirculation in
the Absorber
|
CHAPTER 10 |
Example
10.1 Two-Stage Double-Effect
Ammonia/Water System with Separate Rectifiers
Example 10.2 Two-Stage Triple-Effect
Ammonia/Water System
Example
11.1 GAX Cycle
Example 11.2 Effect of Approach
Temperature
Example 11.3 Branched GAX
