TECHNICAL FIELD OF THE INVENTION This invention relates generally to refrigerant reclamation and purification systems, and more particularly to a self-contained refrigerant reclamation and purification apparatus and method for removing moisture, oil, solid particulates, non-condensables, acid and other impurities and contaminants from CFCs, HCFCs, HFC's and refrigerant blends and reclaiming the refrigerant.

BACKGROUND ART

In the past, venting of refrigerants from refrigeration systems to the atmosphere was an expedient and economical method of removing contaminated refrigerants to permit repairs and allow the equipment to be returned to full production as quickly as possible. Scientific research has concluded that venting of chloroflourocarbon (CFC) and related refrigerants to the atmosphere has led to the depletion of the stratospheric ozone layer. In view of these findings, various taxes and legislative restrictions have been imposed to limit the production, use, and discourage discharging of such refrigerants. Alternative refrigerants, such as hydroflourocarbon (HFC) and hydrochloro-flourocarbon (HCFC) may be used in place of CFC, but they are more costly and their usage in present equipment is not compatible in all cases. The above noted problems have necessitated the recovery, recycling, and reuse of CFC and HCFC types of refrigerants.

My previous patents, U.S. Patent 5,022,230 issued June 11, 1991 and U.S. Patent 5,363,662 issued November 15, 1994 disclose apparatus and methods for reclaiming a refrigerant which utilize a flooded distillation chamber to maintain the refrigerant at a low temperature during the distillation process. Although effectively cleaning the refrigerant by separating the contaminants from the

refrigerant using a low temperature distillation process, which essentially freezes the moisture entrained in the refrigerant, the two systems of the previous patents require a reservoir of liquid refrigerant to be maintained in the distiller sump to achieve the desired temperature to effectuate the systems reclamation processing ability. The method taught in these previous patents is self limiting because, working with the lower temperature range causes the volume rate of distillation vapors to decrease, therefore slowing down total volume output of the system.

The present invention is a significant improvement over the prior art in general and these patents in particular, in that in the present invention, all refrigerant is vaporized in the separation chamber, prior to reaching the contaminate sump, except for a residual amount which is entrained in the contaminates and there is no low temperature maintenance requirement to effectuate the distillation/reclamation process.

The present invention is distinguished over the prior art in general, and these patents in particular by a portable refrigerant reclamation and purification apparatus and method which removes moisture, oil, solid particulates, non- condensables, acid and other impurities and contaminants from CFCs, HCFCs, HFCs and refrigerant blends and reclaims the refrigerant using cross heat exchange abd velocity change. Contaminated refrigerant is introduced through a spray nozzle into a separation chamber and vaporized as it passes over a series of heat exchanger coils. During vaporization the bulk of contaminants are separated from the refrigerant and fall into a sump and the vapors are redirected 180° to an upward flow separating the contaminants from the refrigerant vapors. The vapors are drawn out of the chamber through de-misting screens which strip remaining contaminants from the vapors and are passed through a suction accumulator to either a compressor or a vacuum pump where the gases are compressed. The compressed gases are passed through an oil separator to remove oil and then passed either through the heat exchangers

in the separation chamber where their heat is used to vaporize incoming liquid refrigerant and residual refrigerant from waste contaminants in the sump, or to a condenser coil where they are condensed to liquid and passed through a sub- cooling coil in the chamber over which the vapors being drawn from the chamber pass to lower the temperature of the refrigerant in the sub-cooling coil. The sub-cooled liquid refrigerant passes through a receiver where non-condensables are purged from the system and the condensed liquid is then passed through a series of filters rendering it suitable for reuse.

DISCLOSURE OF THE INVENTION

It is therefore an object of the present invention to provide a highly efficient self-contained portable refrigerant reclamation and purification apparatus and method for removing moisture, oil, solid particulates, non- condensables, acid and other impurities and contaminants from CFCs, HCFCs, HFCs and refrigerant blends and reclaiming the refrigerant.

It is another object of this invention to provide an apparatus for reclaiming and purifying refrigerants which may be easily transported from one location to another, and may be connected to either a container containing contaminated refrigerant or to an operating industrial-sized refrigeration system for reclaiming the refrigerant without requiring the customer to shut down the operating refrigeration system.

Another object of this invention is to provide a method and apparatus for reclaiming and purifying refrigerants which utilizes a novel separation chamber in cross heat exchange with a condenser whereby the flow of the refrigerant vapors are used to assist in the separation of certain contaminants.

Another object of this invention is to provide a method and apparatus for reclaiming and purifying refrigerants which produces a valuable ecological function by

purifying large volumes of used or contaminated refrigerants and CFCs and allows them to be reused in lieu of venting them to the atmosphere.

Another object of this invention is to provide a method and apparatus for bulk reclamation and purification of contaminated CFCs, HCFCs, HFCs and refrigerant blends which will meet ARI 700 purification standards.

Another object of this invention is to provide a method and apparatus for reclaiming and purifying refrigerants which does not require maintaining a liquid refrigerant at a low temperature in the sump of the separation chamber to effectuate reclamation processing ability.

Another object of this invention is to provide a method and apparatus for reclaiming and purifying refrigerants wherein the liquid refrigerant is substantially vaporized in the separation chamber before reaching the reservoir sump, thereby increasing the volume rate of distillation vapors and increasing the processing speed and total volume output.

Another object of this invention is to provide a method and apparatus for reclaiming and purifying refrigerants wherein the bulk of contaminants are separated from liquid refrigerant during vaporization and changing the direction of the vapors to increase the efficiency of separating high-boiling contaminants from the refrigerant vapors.

Another object of this invention is to provide a method and apparatus for reclaiming and purifying refrigerants which will strip residual refrigerant from accumulated waste contaminants by introducing hot discharge gas into the contaminants to effectively vaporize the residual entrained refrigerant.

Another object of this invention is to provide a method and apparatus for reclaiming and purifying refrigerants which also allows the filtration media used in the filtering units to be evacuated, dehydrated and re¬ generated.

A further object of this invention is to provide a method and apparatus for reclaiming and purifying refrigerants which can process either high-pressure or low- pressure refrigerants without modification of the apparatus.

A still further object of this invention is to provide an apparatus for reclaiming and purifying refrigerants which is simple in construction, economical to manufacture, and reliable in operation.

Other objects of the invention will become apparent from time to time throughout the specification and claims as hereinafter related.

The above noted objects and other objects of the invention are accomplished by a portable refrigerant reclamation and purification apparatus and method which removes moisture, oil, solid particulates, non-condensables, acid and other impurities and contaminants from CFCs, HCFCs, HFCs and refrigerant blends and reclaims the refrigerant. Contaminated refrigerant is introduced through a spray nozzle into a separation chamber and vaporized as it passes over a series of heat exchanger coils. During vaporization the bulk of contaminants are separated from the refrigerant and fall into a sump and the vapors are redirected 180° to an upward flow separating the contaminants from the refrigerant vapors. The vapors are drawn out of the chamber through de-misting screens which strip remaining contaminants from the vapors and are passed through a suction accumulator to either a compressor or a vacuum pump where the gases are compressed. The compressed gases are passed through an oil separator to remove oil and then passed either through the heat exchangers in the separation chamber where their heat is used to vaporize incoming liquid refrigerant and residual refrigerant from waste contaminants in the sump.

or to a condenser coil where they are condensed to liquid and passed through a sub-cooling coil in the chamber over which the vapors being drawn from the chamber pass to lower the temperature of the refrigerant in the sub-cooling coil. The sub-cooled liquid refrigerant passes through a receiver where non-condensables are purged from the system and the condensed liquid is then passed through a series of filters rendering it suitable for reuse.

BRIEF DESCRIPTION OF THE DRAWINGS

Fig. 1 is a schematic diagram of a refrigerant reclamation and purification system in accordance with a preferred embodiment of the invention.

Fig. 2 is a schematic diagram of the interior of the separation chamber which utilizes target baffling and cross heat exchange to produce vaporization of liquid refrigerant droplets, and showing apparatus connected at the lower portion of the chamber for removing waste contaminates and removing residual refrigerant from the contaminate waste product.

Fig. 3 is a cross section of the receiver/purge apparatus depicting schematically a flow control float means in the receiver section and a non-condensable separation means utilizing a refrigerated coil in the purge section to separate non-condensables from the refrigerant vapors.

Fig. 4 is a schematic diagram illustrating a system of apparatus for dehydrating and re-generating the molecular sieve filtration media used in the filter units of the system.

BEST MODE FOR CARRYING OUT THE INVENTION

Referring to the drawings by numerals of reference, there is shown schematically in Fig. 1, the refrigerant reclamation and purification apparatus 5 in accordance with a preferred embodiment of the present invention. The apparatus of the present invention may be assembled on a skid or trailer that may be easily transported from one refrigeration system to another. In operation, the apparatuε may be connected to a container "A" containing contaminated

refrigerant or, as described hereinafter, to an operating industrial-sized refrigeration system, such as a centrifugal chiller (not shown) for reclaiming the refrigerant. In the latter arrangement, the present reclamation process strips the refrigerant of moisture, acid, solid particles as well as excessive oil entrained in the liquid refrigerant and returns the refurbished refrigerant back to the operating chiller, thus eliminating the requirement for the customer to shut down the chiller when refrigerant cleaning is desired.

The apparatus 5 of the present invention comprises a refrigerant inlet isolation valve 6 connected by conduit 7 to a filter 8 containing filtering media and having a strainer 9 at the outlet thereof. The strainer 9 is connected by conduit 10 to a distributor nozzle 15 at the top of the inner chamber 20 of a separation chamber 16 (described in detail below) for conducting liquid thereto. A check valve 11 a sight glass 12, a solenoid valve 13, and a flow control valve 14 are connected in the conduit 10 between the strainer 9 and the distributor nozzle 15.

Referring additionally to Fig. 2, the separation chamber 16 is shown in greater detail. An outer housing 17 surrounds an inner housing 18 defining an annular outer chamber 19 surrounding an inner chamber 20. A tubular perforated screen 21 extends from the bottom end of the inner housing 18. The rounded bottom end of the outer chamber 19 serves as a contaminate waste product sump 22. A plurality of oil-mist eliminators or de-mister screen pads 23A, 23B, and 23C, are disposed in the annular outer chamber 19 between the exterior of the side wall of the inner housing 18 and the interior of the side wall of the outer housing 17 in vertically spaced relation. A suction conduit 24 is connected at the upper portion of the outer housing 17 in fluid communication with the annular outer chamber 19. The outer housing 17 is provided with a drain outlet 25 in its rounded bottom end.

A conduit 26 extends inwardly through the side wall of the outer housing and passes horizontally through the waste product sump 22 and then curves to form an internal sump stripper coil 27 and has a vertical riser 28 which extends upwardly through the inner chamber 20 adjacent the interior of the side wall of the inner housing 18. A safety relief valve 29 is connected at the upper end of the vertical riser 28. The outer end of the conduit 26 is connected to a conduit 30 through a two-way hand operated flow diverter valve 31. The conduit 30 is connected in fluid communication to the inlet of a condensing coil 32 (Fig. 1) which may be either air cooled 32A or water cooled 32B.

A plurality of horizontal heat exchanger coils 33A, 33B, and 33C having their ends connected in fluid communication to the vertical riser 28 are disposed within the inner chamber 20 in vertically spaced relation beneath the distributor nozzle 15. The horizontal portions of the heat exchanger coils 33A, 33B, and 33C each have a perforated screen or baffle plate 34A, 34B, 34C, 34D, 34E, and 34F attached to their upward facing exterior surfaces which break up the refrigerant and distribute it as droplets onto the heat exchangers below the upper screens. A conduit 35 is connected to the lower leg of each tube or coil 33A, 33B and 33C and extends vertically downward to the lower portion of the inner chamber 20 and outwardly through the side walls of the inner and outer housings 18 and 17 and is joined after passing through a check valve 36 in fluid communication with the conduit 30 above the flow diverter valve 31. As explained hereinafter, the flow diverter valve 31 will direct hot discharged gas either into conduit 26 or 30 depending upon whether an internal or external condenser is selected.

A horizontal liquid refrigerant sub-cooling coil 37 is disposed in the annular outer chamber 19 between the side walls of the inner and outer housings 18 and 17 above the sump 22 and its ends extend outwardly through the side wall of the outer chamber housing 17. A check valve 39 is connected to the outlet of the condensing coil 32 and conduit

38 is connected at one end to the check valve 39 and its other end is connected to the inlet end of the liquid refrigerant sub-cooling coil 37. The outlet end of the liquid refrigerant sub-cooling coil 37 is joined by conduit 40 to a receiver 41 (Figs. 1 and 3, described hereinafter).

A suction accumulator 63 is connected to the outer end of the suction conduit 24 of the separation chamber 16. As shown in Fig. 2, a tubular guide cylinder 64 is disposed in the interior of the accumulator 63 and the interior of the accumulator is filled with coalescing filter material 65. The guide cylinder 64 directs gases downward to the rounded bottom portion of the accumulator 63. The bottom of the accumulator 63 is joined through a check valve 66, sight glass 67, and conduit 68 to the interior of the outer chamber 19 just below the lowermost de-mister screen pad 23C. A high pressure outlet 69 and a low pressure outlet 70 are provided at the upper portion of the accumulator 63.

Referring again to Fig. 1, the high pressure outlet 69 of accumulator 63 is connected through isolation valve 71 and conduit 72 to a high pressure reciprocating open-drive type compressor 73. The low pressure outlet 70 of accumulator 63 is connected through isolation valve 74 and conduit 75 to a vacuum pump 76. A check valve 77 and isolation valve 78 are connected to the discharge of the compressor 73. A check valve 79 and isolation valve 80 are connected to the discharge of the vacuum pump 76 and the isolation valves 78 and 80 are joined by a common header 81.

An oil separator 82 is connected by conduit 83 to the common header 81 between the isolation valves 78 and 80. An oil return conduit 84 extends from the outlet of the oil separator 82 and is connected between two solenoid valves 85 and 86. The solenoid valve 85 is connected by conduit 87 to the oil sump of the vacuum pump 76 and the solenoid valve 86 is connected by conduit 88 to the oil sump of compressor 73. A gas discharge conduit 89 extends from the oil separator 82 and has an auxiliary discharge valve 90 at its outer end. A conduit 89A having one end connected with the conduit 89

between the oil separator 82 and discharge valve 90 joins the oil separator 82 to the two-way hand operated flow diverter valve 31 (described above) .

Referring now additionally to Fig. 3, the receiver 41 is shown in greater detail. The receiver has a lower housing 42 defining a lower chamber 43 and an upper housing 44 defining a purge chamber 45. A target baffle plate 46 is disposed on the interior side wall of the lower chamber 43 of the receiver 41 adjacent the end of inlet conduit 40. The receiver 41 has an outlet 47 at its bottom end.

A commercially available float level reed switch valve control mechanism 48 is disposed in the interior of the lower chamber 43 and controls the liquid feed through the outlet 47. The control mechanism 48 has an upper reed switch float 49A and a lower reed switch float 49B slidably mounted on a rod 50 secured at the bottom of the chamber. When the switches of both floats are closed, an electrical circuit is completed to open the solenoid valve 102 and liquid leaves the chamber and continues until both switches open. The lower chamber 43 and purge chamber 45 are separated by a plate 51 and connected in fluid communication by a pair of check valves 52 and 53.

A cooling coil 54 is disposed in the purge chamber 45 and receives liquid refrigerant at one end through expansion valve 55 and conduit 58 joined to conduit 99 between isolation valve 100 and solenoid valve 102. The outlet of the coil 54 is connected by conduit 56 to the interior of the outer chamber 19 of the separation chamber 16 through sight glass 67 and conduit 68. The coil 54 is surrounded by a hollow cylindrical guide chamber 57 having a closed top end and vent holes 57A at its lower end. An exhaust valve 60 is connected to the top end of the purge chamber 45 in fluid communication with the interior of the purge chamber. The expansion valve 55 meters liquid refrigerant as it passes into the coil 54 creating a refrigerated condenser and conduit 56 returns the vapors from the coil 54 to the interior of the outer chamber 19 of the separation chamber 16

for re-processing. Check valve 52 allowε non-condensable gases to pass into purge chamber 45 where they are directed across the coil 54. Non-condensables and refrigerant pass upward contacting the coil 54 where the refrigerant is condensed to a liquid and the remaining non-condensables pass through the collect in the chamber 75 for future venting through exhaust valve 60.

A weir 61 is disposed over the check valve 53 such that liquid refrigerant in the lower portion of the purge chamber 45 must exit through the weir. The weir 61 prevents water, which has been condensed from the refrigerant, from reentering the lower chamber 43 and check valve 53 prevents reverse flow of liquid back into the purge chamber 45. A sight glass 62 and drain valve 63 are disposed on the exterior of the purge chamber on fluid communication with the interior of the chamber. The drain valve 63 is used to remove any free water accumulation in purge chamber 45 that may be observed through sight glass 62.

A commercially available electronic refractory liquid level switch 59 is secured in the purge chamber 45. When the liquid level in the purge chamber 45 drops below a designated level, the switch 59 closes and completes an electrical circuit to actuate the solenoid vent valve 60.

Referring again to Fig. 1, the outlet 47 of the receiver 41 is connected by a conduit 91 to the inlet of a first filter unit 92 through an isolation valve 93 and to a second filter unit 94 through an isolation valve 95. The filter units 92 and 94 are filled with molecular sieve filtration media. An isolation valve 96 is disposed in the conduit 91 between the valves 93 and 95. A conduit 97 is connected at one end into the conduit 91 between the valves 95 and 96 and is connected at its other end to the upper portion of the first filter unit 92 through an isolation valve 98. One end of a conduit 99 is connected to the upper portion of the second filter 94 through an isolation valve 100 and its other end is connected to a third filter 101 through a solenoid valve 102 and sight glass 103. The end of

the conduit 91 iε joined into the conduit 99 between the isolation valve 100 and the solenoid valve 102 through an isolation valve 104. The outlet of the third filter unit 101 is connected through an outlet valve 105 and conduit 106 to a second container "B". As explained hereinafter, an arrangement is provided for dehydrating and re-generating the filtration medium used in the filter units 92 and 94.

Referring now to Fig. 2, the lower portion of the separation chamber 16 is shown connected with a system of apparatus which is used to carry out the distillation process when required. As described above, the outer end of the conduit 26 is joined with a conduit 30 through a two-way hand operated flow diverter valve 31. When distillation is required, the hot discharge gases are directed via flow diverter valve 31 through conduit 26 into internal sump stripper coil 27, where the initial heat of compression is used to heat the waste product that will be separated from the initial inlet refrigerant stream. A tee fitting 107 is connected to the drain outlet 25 of the separation chamber waste sump 22. One end of the tee fitting 107 is connected by a conduit 108 and drain valve 109. The conduit 108 serves as a manual drain line which is used when the sump 22 requires complete draining.

The other end of the tee fitting 107 is connected through conduit 110 and isolation valve 111 to the εuction end of a solution pump 112. The discharge end of the pump 112 is connected by conduit 113 to a two-way valve 114. The two-way valve 114 is connected to a waste container (not shown) by conduit 115 and is connected by conduit 116 to the internal coil 117 of a heat exchanger 118. The outlet of the coil 117 is connected by conduit 119 to a two-way valve 120. Conduit 121 is connected at one end to the two-way valve 120 and extends through the side wall of the outer chamber 19 and into the waste sump 22 at the lower end of the separation chamber 16. The coil 117 is submerged in a heated oil bath and assists sump heat exchanger stripper coil 27 in adding additional heat to the waste product in the sump 22.

Conduit 122 is connected at one end to the two-way valve 120 and its other end is joined back into the refrigerant inlet valve 6 (Fig. 1) .

A conduit 123 is connected through an isolation valve 124 into the conduit 110 between the isolation valve 111 and the pump 112. The valve 124 and conduit 123 is uεed to connect the present system to an operating industrial sized refrigeration system such as a centrifugal chiller (not shown) to reclaim the refrigerant without the necesεity of shutting down the chiller when refrigerant cleaning is desired (described hereinafter) . Solution pump 112 adds additional suction pressure to the suction of the operating refrigeration syεtem, thuε enhancing the on-line refrigerant cleaning process.

Referring now to Fig 4, there iε shown schematically, a system of apparatus for dehydrating and re-generating the molecular sieve filtration media used in the filter units 92 and 94. Thermostatically controlled electrical heating units

125, such as strap-on electrical heaters, are installed on the housings of the filter units 92 and 94 and connected to an electrical source (not shown) by electrical connectorε

126. Each heater 125 iε controlled by a thermoεtat 127. A tee fitting 128 is installed between the check valve 66 and sight glaεs 67 in the conduit 68 which connects the bottom of the suction accumulator 63 to the interior of the outer chamber 19 of the separator chamber 16. A conduit 129 is connected at one end to the tee fitting 128 and connected to the lower end of the first filter unit 92 through an isolation valve 130. A conduit 131 is connected at one end into the conduit 129 and at its other end to the lower portion of the second filter unit 94 through an isolation valve 132. An isolation valve 133 and check valve 134 are installed in the conduit 129 between the tee fitting 128 and the isolation valve 132.

The inlet of a vacuum pump 135 is connected to the conduit 129 between the isolation valve 130 and conduit 131 by conduit 136 and isolation valve 137. An iεolation valve

138 and check valve 139 are connected to the diεcharge outlet of the vacuum pump 135 through a tee fitting 140. A conduit 141 is connected at one end to the tee fitting 140 at the pump discharge and its other end is joined through an isolation valve 142 and check valve 143 back into the conduit 129 between the isolation valve 133 and check valve 134.

OPERATION

Referring again to Fig. 1, contaminated refrigerant in container • ^■ A" enters through inlet isolation valve 6, pasεing through conduit 7, paεεing through filter 8, where the large εolid particles are prevented from entering the remaining procesε piping. When the refrigerant leaveε the filter 8 it will pass through strainer 9, check valve 11, through conduit 10 into sight glaεε 12, εolenoid valve 13 and to the flow control valve 14. The flow control valve 14 meters the flow of liquid refrigerant through conduit 10 to the distributor nozzle 15 located at the top of the inner chamber 20 of the separation chamber 16. The annular outer chamber 19 of the separation chamber 16 surroundε the inner chamber and iε in fluid communication with the εuction portε of the compreεεor 73 and vacuum pump 76.

Aε the liquid refrigerant paεεeε through the diεtributor nozzle 15 the liquid undergoeε a reduction in preεεure while being εprayed downward in an even pattern over the heat exchanger coilε 33A-33C and baffle plateε 34A-34F which are encloεed in the inner chamber 20. The perforated screens or baffle plates 34A-34F break up the refrigerant and distribute it as droplets onto the succeεεive lower heat exchanger coilε 33A-33C and baffle plateε 34A-34F and provide a large heat tranεfer εurface area and cauεe complete vaporization of the liquid refrigerant droplets, thuε effectively separating the high boiling residueε and other contaminateε from the refrigerant vapors.

As the now vaporized gaseε reach the perforated screen 21 at the lower portion of the inner chamber 20, the vaporized gases pasε through the εcreen and are abruptly re¬ directed 180° from a downward motion to an upward motion, and

thereby causing εubstantially all of the non-volatile contaminates, such aε oil, acid, free-water, and solid particles, to drop to the waste product sump 22 at the lower end of the separation chamber 16.

Continuing to follow the path of the now vaporized refrigerant gases, the vaporized refrigerant gases are now drawn upward through the annular outer chamber 19 between the side walls of the inner and outer housings 18 and 17. As these gases are drawn in the direction of the suction conduit 24 by the compreεεor 73 or vacuum pump 76, they will pass through the oil mist eliminators or de-mister screen pads 23A-23C, and across the refrigerant sub-cooling coil 37. The de-mister pads 23A-23C interrupt the gas path, causing any residue non-volatile mist to be stripped from the gas stream, thus substantially removing all the contaminates from the vapors leaving the separation chamber 16.

The liquid refrigerant sub-cooling coil 37 disposed in the path of the vaporized refrigerant gases contains the liquid refrigerant which is leaving the condenser coil 32 and the cold refrigerant gaεeε being drawn through the de-miεter padε and across the coil 37 reduces the temperature of the liquid refrigerant in the coil after it leaves condenser coil 32. The refrigerant vaporε pass through suction conduit 24 and enter the chamber of the suction accumulator chamber 63. The vaporε pass through coalescing filter material 65 and the guide cylinder 64 directs the gases downward to the rounded lower portion of the accumulator chamber. The gases then change direction 180° from a downward direction to an upward direction and rise to the upper portion of the suction accumulator 63 where two potential exitε outlets 69 and 70 are available, depending upon whether the type of refrigerant that iε being proceεεed iε high-pressure or low-presεure. Any accumulation of liquid refrigerant in the chamber of the suction accumulator 63 is drawn back into the εeparation chamber 16 through check valve 66, εight glaεε 67, and conduit 68 which are in fluid communication with the outer chamber 19 juεt below the lowermost de-miεter εcreen pad 23C.

The high-presεure outlet 69 of the suction accumulator 63 is connected to the high-presεure reciprocating open drive type compressor 73 through conduit 72. The low-presεure outlet 70 iε connected to the vacuum pump 76 through conduit 75. The iεolation valves, 71, 74, 78, and 80 and check valves 77 and 79 prevent refrigerant gaseε from entering the compreεεing means (73 or 76) that is not being utilized.

At this point in time a selection of the type of refrigerant to be proceεεed must be determined. If low- pressure refrigerant procesεing iε deεired, isolation valves 71 and 78 are closed and isolation valves 74 and 80 are opened, and the vacuum pump 76 will be in service and low- pressure refrigerant may be procesεed. If high-preεεure refrigerant proceεεing iε deεired, iεolation valve 71 and 78 are opened and iεolation valveε 74 and 80 are cloεed and the high-preεsure reciprocating compreεεor 73, iε opened to the refrigerant circuit to permit processing of high-presεure refrigerant.

Aε the high-preεεure or low-preεεure refrigerant gaε iε discharged from either the vacuum pump 76 through check valve 79 and isolation valve 80 or from compressor 73 through check valve 77 and isolation valve 78, the refrigerant gas enters into the common header 81. The hot discharged refrigerant gas pasεeε through conduit 83 into the oil εeparator 82 where the oil, picked up during the compreεεion cycle, iε removed from the refrigerant gaε εtream. This oil is returned either to the oil εump of the vacuum pump 76 through solenoid valve 85 or the oil sump of the compresεor through solenoid valve 86.

The hot refrigerant gas which was separated from the oil is discharged from the oil separator 82 via conduit 89 and to the auxiliary discharge valve 90 though conduit 89 and to the two way hand operated flow diverter valve 31 via conduit 89A. At this point, a selection of either internal or external condenser processing is determined, thuε directing the hot diεcharge gaε either into conduit 26 or 30

via the two-way valve 31. When diεtillation iε required, the hot discharge gaseε are directed through conduit 26 into the sump stripper coil 27, where the initial heat of compression is used to heat the waste product that will be εeparated from the initial inlet refrigerant εtream. Thiε diεcharge gaε heat will cauεe the remaining refrigerant to be vaporized from the waste product, prior to it being removed from the waste product sump 22 of the separation chamber 16.

The discharge gas, paεεeε through the sump heating coil 27. The refrigerant waste product in the sump 22 becomes heated, causing the refrigerant which iε entrained in the waεte to vaporize. To aεεiεt in thiε vaporization εtripping process, the solution pump 112 and heat exchanger 118 are utilized. The εolution pump 112 draws waste product from the waεte εump drain 25 through conduit 110 and diεcharges the heated waste product through conduit 113 to the two-way valve 114. The two-way valve 114 directε the waste product either to a waste container (not εhown) through conduit 115 or to the heat exchanger 118 through the conduit 116.

Conduit 116 directε the waεte product into the coil 117 of the heat exchanger 118 which iε εubmerged in a heated oil bath. The heat exchanger coil 117 pickε up additional heat in the heat exchanger 118 and aεεists the sump heat exchanger stripper coil 27 by adding additional heat to the waste passing through the coil 117.

After the waste product has been heated by the heat exchanger coil 117, it flows through conduit 119 to the two- way valve 120 where it is directed either through conduit 121 or conduit 122 (conduit 122 will be discuεsed hereinafter) .

Conduit 121 directs the heated waste product back into the waεte sump 22 where it is exposed to the suction pressure in the separation chamber 16. The heat, in combination with the suction presεure inεide the chamber 16 εubεtantially vaporizes all the remaining refrigerant. The remaining waste material can be drained through conduit 110

by pump 112 when the two-way valve 114 iε poεitioned to dump through conduit 115. Conduit 108 and valve 109 are uεed when the sump 22 requires complete draining.

As an additional feature to the reclamation procesε, the preεent system may be used to reclaim refrigerant from an operating induεtrial εized refrigeration system such aε a centrifugal chiller. The reclamation process stripε the refrigerant of moiεture, acid, solid particles aε well aε excessive oil entrained in the liquid refrigerant and returns the refurbished refrigerant back to the operating chiller, thus eliminating the requirement for the customer to shut down the chiller when refrigerant cleaning is desired.

Thiε process is accompliεhed by directing the incoming contaminated refrigerant from the cuεtomer'ε refrigeration εyεtem (which would normally enter through inlet valve 6) , through conduit 123 and iεolation valve 124 into conduit 110. Iεolation valve 111 iε cloεed to prevent any refrigerant waεte from entering thiε liquid refrigerant εtream. The liquid refrigerant enterε the εolution pump 112 through conduit 110 and is discharged through conduit 113 to the two-way valve 114. The two-way valve 114 iε poεitioned to direct the flow of refrigerant to the heat exchanger 118 through conduit 116. Aε the liquid refrigerant paεεeε through heat exchanger coil 117, the preεεure and the temperature of the refrigerant iε increaεed. The refrigerant then flows through conduit 119 to the two-way valve 120. The two-way valve 120 iε poεitioned to direct the flow of refrigerant through conduit 122 to the conduit 7 at the inlet of the refrigerant inlet valve 6. Inlet valve 6 then introduceε the refrigerant from the other εyεtem to the reclamation proceεε aε deεcribed above. The solution pump 112 adds additional εuction preεεure to the suction presεure of the other operating refrigeration εystem, thus enhancing the efficiency of the on-line refrigerant cleaning procesε.

Referring now to Fig. 2, the hot diεcharge gaε leaving the heat exchange εtripper coil 27 in the εump 22 flowε upwardly through vertical riεer 28 and iε diεtributed

through the heat exchanger coilε 33A-33C having baffle plateε 34A-34F on their upper εurfaces. The relief valve 29 at the top of the riser 28 serveε aε a safety release to prevent over-presεurization.

The contaminate liquid refrigerant εtream entering the separation chamber 16 through the distributor nozzle 15 vaporizes as it strikes the heated coils and baffle plates, thus diεtilling the liquid refrigerant while the hot discharge gas, pasεing through interior of the coils 33A-33C becomes εub-cooled, thuε condenεing theεe vaporε into a liquid phaεe. The now condenεed liquid fallε downwardly through conduit 35 and paεεeε through check valve 36 and into conduit 30, which iε in fluid communication with the either air cooled 32A or water cooled 32B condenεing coil 32 (Fig. 1) . At this point the refrigerant gases will complete the condensing cycle and the liquid refrigerant will pass from the condensing coil 32 through conduit 38 and check valve 39 into the sub-cooler coil 37.

The sub-cooler coil 37 is poεitioned in the path of the cool refrigerant vaporε exiting the εeparation chamber 16. The cooled refrigerant vapors leaving the chamber 16 extract heat from the liquid refrigerant pasεing through the sub-cooler 37, thuε εignificantly reducing the temperature of the liquid refrigerant and enhancing the efficiency of the system by increasing filter media performance due to the ability of the filter media to absorb larger quantitieε of moisture when the temperature of the entering liquid passing through filters 92 and 94 is lowered.

Referring now to Fig. 3, the sub-cooled liquid refrigerant from the coil 37 is directed through conduit 40 into the chamber 43 of receiver 41. A portion of the refrigerant and non-condensable gaseε pass through check valve 52 into the purge chamber 45 and acrosε the cooling coil 54 where the refrigerant condenεes into a liquid phase and drops to the lower portion of the chamber. The non- condensable gases fill the guide cylinder, stopping the refrigerant from condenεing and forcing the liquid level in

the purge chamber to drop sufficient to activate the electronic float valve εwitch 59 to open the vent valve 60. Thus, the non-condensable gases are separated from the liquid refrigerant in the purge chamber 45 of the receiver 41. The liquid refrigerant in the lower portion of the purge chamber 45 pasεes through the check valve 53 into the lower chamber 43 and water which has been separated from the refrigerant iε prevented from reentering the lower chamber by the weir 61. Drain valve 63 is used to remove any free water accumulation that may be observed through sight glaεε 62 from the purge chamber 45.

Expanεion valve 55 is used to meter liquid refrigerant aε it passeε into the coil 54 to create a refrigerated condenεer. Conduit 56 connected between the sight glass 66 and check valve 67 returns the vapors passing through the cooling coil 54 to chamber 13 through check valve 67 and conduit 68 for re-procesεing.

Referring again to Fig. 1, the liquid refrigerant which accumulateε in receiver 41 now paεεeε through the outlet 47 and conduit 91 to the inlet of filter units 92 and 94. When filtration is required the liquid refrigerant may be passed through filter units 92 and 94 by opening iεolation valve 93 and closing isolation valve 96. The liquid refrigerant then enters filter unit 92 and exits through isolation valve 98 and conduit 97 back into conduit 91. With isolation valve 104 closed, the filtered refrigerant pasεeε through open iεolation valve 95 into filter unit 94. With isolation valve 100 open, the now twice filtered refrigerant passes through solenoid valve 102 and sight glass 103 and enters the filter unit 101. Filter unit 101 captures the filter media residues from the filter units 92 and 94. Exit valve 105 is opened to discharge the filtered and purified refrigerant through conduit 106 into container "B".

Another feature of the present apparatus and method is the re-generation of the molecular εieve filtration media uεed in the filter units 92 and 94. Referring now to Fig. 4, process for evacuation, dehydration and re-generating the

molecular sieve filtration media in the filter units 92 and 94 will be described. The molecular sieve material reduces the moisture content of the liquid refrigerant to reclamation specification standardε (moisture content of 10 ppm or lesε) .

The regeneration proceεε can be accompliεhed by isolating either one or both filter units 92 and 94. Liquid refrigerant flowing through the conduit 91 from the receiver 41 is redirected around the filter units 92 and 94 by opening isolation valves 96 and 104 and closing iεolation valves 93, 98, 95, and 100, thus isolating the filter units 92 and 94. By opening iεolation valves 130 and 132 and closing isolation valve 137, the liquid refrigerant contained in the filter unitε 92 and 94 will be drawn through the conduitε 129 and 131, the check valve 134, the iεolation valve 133, into the tee fitting 128, and through the εight glaεε 67 and conduit 68, into the outer chamber 19 of the εeparation chamber 16. Due to the lowered pressure in the separation chamber 16, when the reclamation procesε is in operation, substantially all the liquid and gas refrigerant in filter units 92 and 94 is drawn from the units and into the separation chamber 16 where it iε reprocessed.

Upon evacuation of the filter units 92 and 94, isolation valves 137 and 142 are opened and vacuum pump 135 is turned on. The pump 135 preferably drawε a vacuum in the range of about 7mm to about 10mm Hg. The remaining vapors in the filter units 92 and 94 are drawn through isolation valve 137 and into the εuction εide of the vacuum pump 135. The gases are discharged through the diεcharge εide of the pump 135, through the now open iεolation valve 142, through check valve 143, and reenterε the conduit 129, and then passeε through isolation valve 133, into the tee fitting 128, and through the sight glass 67 and conduit 68, into the outer chamber 19 of the separation chamber 16.

At a vacuum of approximately 25 inches Hg. , the electric heating units 125 are manually activated to increaεe the temperature of the filter unitε 92 and 94 to

approximately 200° F. This increase in temperature heatε εubstantially all the molecular sieve media contained within the filter units 92 and 94.

The combination of the heat generated by the heating units 125 and the vacuum in the range of from about 7mm to about 10mm Hg. generated by the vacuum pump 135 will cause the moisture which has been absorbed within the molecular sieve media to vaporize and it can then be extracted as a gas. Thiε iε accomplished by closing isolation valves 142 and 133, thus venting the gaεeε from the εystem through the now open isolation valve 138 and check valve 139.

The evacuation, dehydration, and re-generation proceεs takes about 4 hours to accomplish the desired result, after which the filter units 92 and 94 may be returned to their intended function in the reclamation process.

While this invention has been deεcribed fully and completely with εpecial emphaεiε upon a preferred embodiment, it should be understood that within the scope of the appended claimε the invention may be practiced otherwise than as specifically deεcribed herein.