G04563844

IOSR Journal of Engineering (IOSRJEN) www.iosrjen.org
ISSN (e): 2250-3021, ISSN (p): 2278-8719
Vol. 04, Issue 05 (May. 2014), ||V6|| PP 38-44
International organization of Scientific Research 38 | P a g e
Thermodynamic Analysis of Kapitza Cycle based on Nitrogen
Liquefaction
Vijay Singh Bisht
Assistant Professor Department of Mechanical Engineering, Uttaranchal University,
Dehradun ,Uttarakhand, India
Abstract: - Cryogenic technology is used for liquefaction of many gases and it has several applications in food
process engineering. The thermodynamic analysis of various cryogenic systems for liquefaction of different
gases has been done by many researchers. Thermodynamic analysis of a nitrogen liquefaction system based on
Kapitza cycle which is a modified Claude cycle has been carried out to evaluate various vital parameters of the
system.
Parametric evaluation using EES Commercial helps to identify the effects of expander flow fraction,
isentropic efficiency of expander on the FOM (figure of merit) of the liquefaction cycle.
The study computes helps in selecting expander flow fraction, operating temperature levels of expanders, and
approach temperature of the heat exchangers through them. Results from the analysis may help evolving
guidelines for designing appropriate thermodynamic cycles for practical nitrogen liquefaction systems.
I. INTRODUCTION
The word cryogenics stems from Greek and means "the production of freezing cold". The science and
technology of producing a low-temperature environment is generally referred to as cryogenics. It is perhaps
appropriate to start with some definitions. The word cryogenics has its origin in the Greek language where
"cryos" means frost or cold and "gen" is a common root for the English verb to generate. However, the term is
used today as a synonym for the low-temperature state. It is not well-defined at what point on the temperature
scale refrigeration ends and cryogenics begins, but most scientists assume it starts at or below -150 °C or 123 K
(about -240 °F). The National Institute of Standards and Technology at Boulder, Colorado has chosen to
consider the field of cryogenics as that involving temperatures below −180 °C (-292 °F or 93.15 K). This is a
logical dividing line, since the normal boiling points of the so-called permanent gases (such as helium,
hydrogen, neon, nitrogen, oxygen, and normal air) lie below −180 °C while the Freon refrigerants, hydrogen
sulfide, and other common refrigerants have boiling points above −180 °C.
The cryogenic mean literally, the production of ice cold, however the term is used today as a for low
temperatures. Cryogenics is defined as that branch of physics which deals with the production of very low
temperatures and their effect on matter a formulation which addresses both aspects of attaining low temperatures
which do not naturally occur on Earth, and of using them for the study of nature or the human industry. In a
more operational way it is also defined as the science and technology of temperatures below 123 K.
1). 0.01-.1k = Dilution refrigerator
2). 1-10 k = Magnetic refrigerator
3). 10-50 k = Liquid helium
4). 50-123 k = Air liquefies
APPLICATION OF LIQUID NITROGEN IN FOOD PROCESSING [4][5][7][8][9]
1.Freezing of baked goods, shrimp, meats, soups, and so on requires a process known as CRYO-QUICK in the
food processing industry.
2.Liquid nitrogen is widely used in food processing and food transportation because of minimum production
costs.
3. Cryogenic (i.e., very low-temperature) freezing results in smaller weight losses from dehydration than
traditional mechanical freezing. Frozen food processors can thus preserve the quality of. Their products with a
freezing system that uses environmentally friendly liquid nitrogen.
4. Due to its own extremely cold temperature, liquid nitrogen can enable a cryogenic system to freeze food
within minutes instead of the hours traditionally required with other systems The faster freezing causes the
formation of small ice crystals, which then help ensure product moisture and quality are maintained longer.
5.In freezing on microbial flora of ground beef patties. It was observed that LN2 freezing produced significantly
greater reduction in microbial activity than the mechanical air blast freezer. Patties containing 30% fat provided
greater.

Thermodynamic analysis of Kapitza cycle based on nitrogen liquefaction
6.LN2 freezing of prawns over. It was reported that the beneficial effect of LN2 freezing over conventional plate
freezing can exist even after 59 days at a commercial storage temperature of 255 K.
7.The use of LN2 as a secondary refrigerant along with ice for transportation of wet fish. It is found that the ice
melting rate can be reduced by about 50%.
8. The freezing point and freezing rate of tilapia meat in LN2 freezers at186 and 145K. It is found that the
freezing rate in LN2 freezing is independent of thickness of the product to be frozen.
9. Liquid nitrogen used in polar stream system for refrigerated transportation of frozen fish.
II. KAPITZA LIQUEFACTION SYSTEM[2]
Kapitza (1939) modified the basic Claude system by eliminating the third heat exchanger or low
temperature heat exchanger. Several notable practical modifications were also introduced in this system a rotary
expansion engine was instead of reciprocating expander. The first or high temperature heat exchanger in the
kapitza system was actually a set of valved regenerators, which combined the cooling process with the
purification process. The incoming warm gas was cooled in one unit and impurities were deposited there, while
the outgoing stream warmed up in the other unit and flushed out the frozen impurities deposited in it. Kapitza
did a careful analysis of turbo-refrigeration and developed radial flow turbines for air refrigeration.
2.1 Components Used[2]
1. COMPRESSOR: - It is a device used to reduce the volume of gaseous air and increase the pressure.
Generally for cryogenic application compressor with high compression ratio are used. To achieve high stage
compression ratio a number of compressor are used in series rather using a single compressor. It also reduces
work consumption. For present work isothermal compression process is used.
2. Expander: - A rotary expansion engine was used have high efficiency than reciprocating engine and the loss
also less in rotary expender.
3. HEAT EXCHANGER: - Heat exchangers are devices which transfer heat from hot fluid stream to cold fluid
stream. In heat exchanger hot fluid temperature decreases and there is increase in temperature of cold fluid. By
losing heat hot fluid is prepared for throttling process and similarly by gaining heat cold fluid heated up for
compression process.
4. VALVE: - A throttling valve is used to reduce the pressure of the compressed air so that liquid air can be
produced and stored. The process is assumed to be isenthalpic expansion.
5.SEPARATOR/DISTILLATION COLUMN: - In this chamber air is separated into desired components like
liquid N2, liquid O2 etc. and the gaseous part is again recirculated.
6. MIXER: - It is a device helps to maintain a constant flow rate of air into the compressor. The extra amount of
air is added into incoming stream from separator. The process is assumed to be isobaric.
2.2 Advantages [3]
1. A rotary expansion engine of high isentropic efficiency is used instead of reciprocating engine as in
Claude cycle.
2.First heat exchanger replaced by a set of valved regenerators which combined the cooling process with
purification process.
3.Kapitza cycle can be operate at relatively low pressure is lower than critical pressure of nitogen gas.
III. MATHEMATICAL MODEL
A computer program has been developed depending upon the requirements of engineering equation solver
(EES). The equations are written in the equation window of EES in the FORTRAN LANGUAGE. EES solves
these equations itself on giving „calculate‟ command [10].
Assumptions:
1. The system is at steady state condition. All processes are steady flow processes.
2. Neglecting the effects of kinetic and potential energy in analysis of all the components of system
3.There is no heat in-leak to the system.
Mass balance
Let m = mass flow rate of N2 compressed = 0.1kg/s
m e = mass flow rate of N2 bypassed to the expander = 0.06m kg/s
m 4 = mass flow rate of N2 passing through the second heat exchanger = 0.04m kg/s

m = m e+ m 4 (1)
xe =
me
m
= fraction of nitrogen gas going to expander
m 6 = mass flow rate of liquid N2 produced
y =
m6
m
= liquid yield
Applying First Law for steady flow to the heat exchangers, the expansion valve and the liquid receiver as a unit
excluding compressor, for no external heat transfer to the control volume then
m − m6 h10 + m6h6 + m11h11 − mh2 − meh3 = 0 (2)
On arranging terms and putting value of xeand y we get
y =
m6
m
=
h10−h2
h10−h6
− xe ×
h3−h11
h10−h6
(3)
In case of actual system we consider isentropic efficiency of turbine
Ƞ 𝐞
=
𝐡 𝟑−𝐡` 𝟏𝟏
𝐡 𝟑−𝐡 𝟏𝟏
Then yield becomes
y =
m6
m
=
h10−h2
h10−h6
− xe ×
h3−h11
h10−h6
(4)
Theoretical minimum work requirement or the system [1]
wi = T1 s1 − s6 − h1 − h6 (5)
work requirement for the system
𝐰 =
𝟏
𝐲
𝐓𝟏 𝐬 𝟏 − 𝐬 𝟐 − (𝐡 𝟏 − 𝐡 𝟐) − 𝐱 𝐞(𝐡 𝟑 − 𝐡 𝟏𝟏) (6)
Considering isentropic efficiency of turbine, the actual work requirement
w=
1
y
T1 s1 − s2 − (h1 − h2) − Ƞe
xe(h3 − h11) (7)
3.1 Figure of merit (FOM) [1]
It is defined as the ratio of theoretical work requirement and actual work requirement for the system.
The figure of merit is a number between 0 and 1.It gives measure of how closely the actual system approaches
the ideal system performance .If the figure of merit greater than unity, it would be in violation of the second law
of thermodynamics. The above equation is of FOM is for liquefaction system.
𝐅𝐎𝐌 =
𝐖𝐈
𝐖
Kapitza system
Fig. 1 Kapitza system

z
Fig.2 Kapitza cycle on T-s plane
Fig.3 Plot Variation of for with efficiency of expander and FOM
0.00
0.10
0.20
0.30
0.40
0.50
0.60
0.70
0.80
0.90
0.5 0.6 0.7 0.8
FOM
expanderisentropic efficiency
FOM
atDTHX_1=5K,D
THX_2=10K
FOM
atDTHX_1=10K,
DTHX_2=15K
FOM
atDTHX_1=15K,
DTHX_2=20K
FOM
atDTHX_1=20K,
DTHX_2=25K

Fig. 4 Plot of Yield and FOM with different fraction of nitrogen going to expander.
Fig. 5 Plot of Yield and FOM at different expander tempretures.

Fig. 6 Plot of Yield against expander efficiency.
Fig. 7 Plot of pressure ratio at different heat capacity ratio of heat exchangers.
IV. RESULTS AND DISCUSSION
A mathematical model has been developed for theestimation of yield of liquid nitrogen produced and FOM
(figure of merit) of Kapitza system for varying compressor exit pressure,expander flow rate ratio, and isentropic
efficiency of expander, approach temperature of regenerator and heat exchanger and inlet temperature of
expander
1. From figure 3 the plot between expander efficiency and FOM at different approach temperatures of
regenerator and heat exchanger, we conclude at given expander efficiency that the best FOM is achieved at 5
K and 10K approach temperature of regenerator and heat exchanger respectively.As shown in graph by
considering various approach tempratures for regenerator and heat exchanger the curve of 5 K and 10K
approach temperature of regenerator and heat exchanger have highest value of FOM obtained is approximately
.78.
.
0.6 0.65 0.7 0.75 0.8 0.85 0.9
0.09
0.1
0.11
0.12
0.13
0.14
0.15
0.16
ne [-]
y[-]
yy
5 10 15 20 25 30 35
0.1
1
10
Pr [-]
CR,2,CR,1

2 From fig. 4 Plot of Yield and FOM with different fraction of nitrogen going to expander, shows that both yield
and FOM increases. It appears that to maximize the y(yield) x(expander flow rate ratio) should take on its
maximum value, however conservation of mass flow requires that y+x≤1 , because some gas also returned
from lower pressure side for cooling of heat exchangers.
3. plot between expander inlet temperature as input parameter or independent parameter,yield and FOM are
dependent parameters both yield and FOM increases with increase in expander inlet temperature. The liquid
yield rise is more sensitive than the fom,we here take care the range of expander inlet temperature from 260 to
280 k because we also have taken care of cooling done by regenerator at given approach temperature.
4. As from figure 6 to study the impact of expander efficiency on the performance of Kapitza liquefaction cycle,
isentropic efficiency of the expanders is varied in a practically possible range 55–85%. When varying the
isentropic efficiency of expander observed from the Fig. 6 that the relationships between the liquid production
and the isentropic efficiency of expanders are almost linear and the trends are very similar to each other.
5.It is been found that for HX1 Heat Capacity Ratio CR1 is less than 1 which is resulting from the reduced
return stream flow due to withdrawal of liquid from the cycle. For HX2 that are connected in parallel to the
expander, the return stream flow is higher, and therefore, they always have CR greater than 1. This is due to the
reason that a part of the high pressure stream (forward stream) before HX2 is diverted through EXP1 and the
expander stream finally join the return flow after these two heat exchangers.
V. CONCLUSIONS
1 The best FOM is achieved at 5 K and 10K approach temperature of regenerator and heat exchanger
respectively. The highest value of FOM obtained is approximately .78.
2. The relationships between the liquid production and the isentropic efficiency of expanders are almost linear .
3. Both yield and FOM increases with increase in expander inlet temperature. The liquid yield rise is more
sensitive than the fom,
REFERENCES
[1] Barron R F “Cryogenic Systems‟, second edition, New York, Oxford University Press,1985.
[2] S.Prasad “Study Cryogenics Cycles with ASPEN - HYSYS simulation” N.I.T Rourkela 2009.
[3] SciverS.W.V.“Heliumcryogenics”,Timmerhaus K.D.,RizzutoC.“International cryogenics monograph
series Pentium publishing corporationNew York, 1986.
[4] Ventura G,RisegariL.“The art of cryogenics low-temperature experimental techniques” published in
Elsevier Ltd, 2008.
[5] Kraft AA et al. Effect of composition and method of freezing on microbial flora of ground beef patties. J
Food Sci 1979; 44:350–5.
[6] Chakrabarti R, Chaudhary DR. Advantages of liquid nitrogen freezing of penaeusmonodon over
conventional plate freezing Fishery Techno 1987;24:44–7.
[7] Chattopadhyay P, Roy AK, Lala S. Studies on Transportation of wet fish IV. Use of liquid nitrogen as a
secondary refrigerant. J Food SciTechnol 1987;24:178–80.
[8] Chen YL, Bonnie SP. Freezing tilapia by airblast and liquid nitrogen––freezing point and freezing ate. Int
J Food Sci Technol1995;30:159–66.
[9] Goswami TK, Das H, Bose AN. A system design for transportation of frozen fish using liquid nitrogen.
In: Proceedings of INCONCRYO‟85. 1985, p. 332–41.
[10] Klein, S.A. 2012. Engineering Equation Solver.VersionV9.205 3-D. F Chart Software.

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