GB2029948A - Refrigeration apparatus with improved oil separation - Google Patents
Refrigeration apparatus with improved oil separation Download PDFInfo
- Publication number
- GB2029948A GB2029948A GB7832387A GB7832387A GB2029948A GB 2029948 A GB2029948 A GB 2029948A GB 7832387 A GB7832387 A GB 7832387A GB 7832387 A GB7832387 A GB 7832387A GB 2029948 A GB2029948 A GB 2029948A
- Authority
- GB
- United Kingdom
- Prior art keywords
- oil
- compressor
- condenser
- refrigerant
- separator
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B1/00—Compression machines, plants or systems with non-reversible cycle
- F25B1/04—Compression machines, plants or systems with non-reversible cycle with compressor of rotary type
- F25B1/047—Compression machines, plants or systems with non-reversible cycle with compressor of rotary type of screw type
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Applications Or Details Of Rotary Compressors (AREA)
Abstract
To improve the efficiency of oil separation in refrigeration apparatus having a compressor (1), a condenser (2,4), an evaporator (6) and an oil separator (3), the oil separator (3) is disposed downstream of a first condenser stage (2) and before a second condenser stage (4). <IMAGE>
Description
SPECIFICATION
Refrigeration apparatus with improved oil
separation
The invention relates to a method of improving the
efficiency of oil separation in refrigeration plants.
The invention is particularly applicable to refriger
ation plants incorporating screw compressors which
have quantities of oil injected to them in order to
improve the efficiency of the sealing against vapour
leakage within the compressor. A disadvantage
associated with the injection of oil for sealing
purposes is that very efficient oil separation
methods are required in the discharge of the com
pressor in order to prevent the carry over of
unacceptable quantities of oil into the rest of the
refrigeration system where it would impair the
efficiency of heat transfer. The refrigerant evapor
ator is particularly vulnerable to impairment of heat
transfer because of unacceptable quantities of oil.
In conventional screw compressor refrigerating
systems there is usualy provided a large and effi
cient oil separator in the compressor discharge. The
separated oil is returned to the compressor through
an oil cooler which may be water cooled or cooled
directly by refrigerant. Significant quantities of heat
relative to the refrigerating capacity may be re
moved from the oil at this stage. In other screw
compressor designs liquid refrigerant is injected at
high pressure into the compressor discharge, thus
cooling the oil by direct contact between evaporat
ing refrigerant and hot oil.
It is an object of the present invention to provide a
refrigeration apparatus with improved oil separation
means.
The present invention provides a refrigeration
apparatus having a compressor, a condenser, an
evaporator and an oil separator characterised in that
the oil separator is disposed downstream of a first
condenser stage and before a second condenser
stage.
Further, preferred, details of the invention will
appear from the following description of one embo
diment of a refrigeration apparatus according to the
present invention illustrated with reference to the
accompanying schematic drawing.
The apparatus comprises a screw compressor 1
which is followed in the downstream direction of
refrigerant fluid circulation by a first condenser stage
2, an oil separator 3, a second condenser stage 4, an
expansion valve 5 and an evaporator 6.
Some specific and latent heat is removed from the
mixture of oil and refrigerant in the first condenser
stage condenser 2. Within this stage, there is
considerable condensation of oil vapour on the cold
condensing surfaces. The resulting mixture of re
frigerant vapour and oil is then passed from the first
stage condenser 2 to an oil separator 3 whose I efficiency is considerably increased compared to the
efficiency of a separator place immediately down
stream of the compressor discharge before the
condenser, for various reasons. Firstly the specific
volume of the refrigerant oil mixture is considerably reduced due to the lowering of the temperature of the mixture and some condensation of refrigant.
Secondly, the oil will be more readily separated because a significant proportion of it will have coalesced on the cold surfaces within the first stage condenser. As a result of this the oil separator can be made significantly smallerthan one used in conventional refrigeration apparatus in which the separator is placed immediately downstrean at the compressor discharge.
The oil collected in the separator 3 is normally returned to the screw compressor 1 through an oil return line 7. Any small quantities of condensed refrigerant which are returned with the oil to the compresor 1 do not affect the pumping capacity of the compressor 1 because they are returned to the compression space after compression has begun.
These small quantities of refrigerant may evaporate within the compressor 1 and the oil to some extent and provide additional cooling to the compressor 1.
The substantially oil-free refrigerant issuing from the oil separator 3 is fed into a second stage condenser 4 where it is substantially condensed to high pressure liquid refrigerant which may then be fed to the evaporator 6 through the expansion valve 5 in conventional manner. Within the evaporator 6 the refrigerant extracts heat by vaporisation thereof providing cooling in conventional manner and is then returned to the inlet side of the compressor 1.
1. A refrigeration apparatus having a compressor, a condenser, an evaporator and an oil separator characterised in that the oil separator is disposed downstream of a first condenser stage and before a second condenser stage.
2. A refrigeration apparatus as claimed in claim 1 wherein is provided an oil return line extending from the separator to the compressor.
3. A refrigeration apparatus according to claim 1 substantially as described hereinbefore with particular reference to the accompanying drawing.
**WARNING** end of DESC field may overlap start of CLMS **.
Claims (3)
1. A refrigeration apparatus having a compressor, a condenser, an evaporator and an oil separator characterised in that the oil separator is disposed downstream of a first condenser stage and before a second condenser stage.
2. A refrigeration apparatus as claimed in claim 1 wherein is provided an oil return line extending from the separator to the compressor.
3. A refrigeration apparatus according to claim 1 substantially as described hereinbefore with particular reference to the accompanying drawing.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB7832387A GB2029948A (en) | 1978-08-05 | 1978-08-05 | Refrigeration apparatus with improved oil separation |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB7832387A GB2029948A (en) | 1978-08-05 | 1978-08-05 | Refrigeration apparatus with improved oil separation |
Publications (1)
Publication Number | Publication Date |
---|---|
GB2029948A true GB2029948A (en) | 1980-03-26 |
Family
ID=10498885
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB7832387A Withdrawn GB2029948A (en) | 1978-08-05 | 1978-08-05 | Refrigeration apparatus with improved oil separation |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB2029948A (en) |
-
1978
- 1978-08-05 GB GB7832387A patent/GB2029948A/en not_active Withdrawn
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
WAP | Application withdrawn, taken to be withdrawn or refused ** after publication under section 16(1) |