PRODUCE FUMIGATION METHOD AND APPARATUS

Abstract: A method is described for fumigating produce using a shorter fumigation time and higher concentration of fumigant than with conventional fumigation. It has been found that kills achieved are as good, damage to produce is no greater and residues of fumigant are no higher than with conventional fumi­ gation. An apparatus as described incorporating a fumigation chamber. There are described four modes of effecting fumiga­ tion with the apparatus.

Description: TITLE: Produce Fumigation Method and Apparatus BACKGROUND OF THE INVENTION 1. Field of the Invention This invention relates to a produce fumigation process and apparatus. More particularly it relates to the fumigation of apples with methyl bromide although it is not limited thereto. 2. Description of the Prior Art It is conventional practice in the produce packing art to fumigate produce which is thought to be contaminated by insects. The practice is to subject the produce to dosages of low concentrations of a fumigant for periods of two to three hours which is sufficient to kill the infesting insect species. Generally fumigation is carried out in a specially constructed sealable vessel built to withstand a vacuum. Alternatively, produce is enclosed within a plastic cover to retain a fumigant for a sufficient length of time to allow it to kill the infesting species. Common fumigants include methyl bromide, ethylene dibromide, hydrogen cyanide or mixtures of these. The fumigants may be employed with or without an inert atmosphere and may include the addition of gases such as carbon dioxide, carbon monoxide or nitrogen. Each fumigant has its particular advantages and disadvantages but of paramount concern in relation to produce are the chemical residues deposited in the produce as a result of the fumigation. Modern practice is to endeavour to strike a fine balance aiming to minimise residues while still giving complete mortalities. In the apple packing industry it is accepted practice to fumigate packed graded fruit immediately prior to storage or transport. Where transport to another country or state is involved fumigation is often carried out upon arrival. Methyl bromide and ethylene dibromide are the most commonly 3 used fumigants added at dosages of 10 to 60 g/m for the 2 former and 2 to 20 g/m for the latter, depending on the temperature, for two to two and a half hours. Fruit damage often results following such fumigation, the severity of the damage varying between the type of apple and sometimes between sources for the same type of apple. In addition damage may vary with fruit maturity and length of time in storage prior to fumigation. Such damage may be mitigated by the use of a dip with an anti-scald agent such as diphenylamine (DPA) or by using a wrap impregnated with a compound such as DPA. It is an object of this invention to go some way towards overcoming this disadvantage or to at least offer the public a useful choice. SUMMARY OF THE INVENTION Accordingly the invention may be said broadly to consist in a process for the fumigation of produce which comprises treating said produce with gaseous fumigant at a concentration sufficiently high to be fatal to the target pest for frdm 5 to 30 minutes. Preferably the invention may be said broadly to consist in a process for fumigation of produce which comprises treating said produce with gaseous methyl bromide in a 3 concentration of from 40 to 600 g/m for from 5 to 30 minutes with the proviso that the product of concentration (expressed in g/m ) x time (expressed in hours) is within 3 the range of 20 to 150 ghr/m Preferably said treatment is conducted from 8 to 15 minutes. Alternatively said fumigant is gaseous ethylene dibromide held at a concentration of from 10 to 200 3 g/m with the proviso that the ct product is from 5 to 50 ghr/m Preferably said treatment is conducted in a sealed fumigation chamber under a partial vacuum. Preferably said concentration x time product (ct) is 3 from 40 to 80 ghr4m for fumigating light brown apple moth or any other leaf roller species with methyl bromide. 3 Preferably said ct product is from 60-120 ghr/m for fumigating codling moth with methyl bromide. Preferably said produce is apples. Preferably said process includes a preliminary step of treating apples in a DPA solution with a concentration of up to 2000 pp, for a time of up to 2 minutes and fumigating said treated apples within one half hour after said treating. Preferably said process includes the additional step of rinsing said produce after said fumigation. Preferably said treatment with said fumigant is carried o o out at a temperature of from 5 C to 40 C. Preferably there is a controlled atmosphere containing inert gases such as carbon dioxide or nitrogen together with said fumigant. Preferably said fumigant is recovered by adsorbing fumigant exhausted from said fumigation chamber on activated carbon. Alternatively said fumigation is effected by desorbing adsorbed fumigant. In one embodiment said fumigant is dissolved in a liquid and fumigation effected by treating fruit with said solution of fumigant. Alternatively said fumigant is stored in a vessel and reused in a fumigation cycle. In another alternative the invention may be said broadly to consist in an apparatus for fumigating produce comprising a fumigation chamber capable of withstanding elevated and reduced pressures, means for opening and closing said chamber, means for injecting a metered amount of fumigant into said chamber, means for flushing fumigant from said chamber, sequencing means for sequencing the operation of said opening and closing means, said injecting means and said flushing means, the arrangement being such that in use said sequencing means activates said injecting means when said chamber is closed, activates said flushing means after fumigant has been in said chamber a predetermined length of time and opens said chamber after a predetermined flushing time. Preferably said apparatus includes means for pressurising or evacuating said chamber and the arrangement is such that said sequencing means activates said injecting means when a predetermined pressure is reached in said chamber. Preferably said apparatus includes means for detecting the presence of fumigant in said chamber and the arrangement is such that said sequencing means opens said doors only after said detecting means has detected that the concentration of fumigant has fallen below a predetermined level Preferably said door opening and closing means comprises an hydraulically operated ram and locking mechanism activated by said sequencing means. Preferably said chamber is provided with an evacuating means comprising a vacuum pump. Preferably said means for injecting comprises a single dose piston injector. In another alternative said means for injecting fumigant comprises a fumigant adsorber/desorber. Preferably there are a pair of said fumigant adsorber/desorbers and said sequencing means is programmed to allow for one to be desorbing while the other is adsorbing and vice versa. Preferably there is provided conveying means for conveying produce into and out of said fumigation chamber. Preferably said sequencing means comprises a microprocessor. Preferably there is provided means for heating and/or cooling said fumigant. Preferably there is provided liquid spraying means within said chamber to assist in removal of said fumigant. The invention consists in the foregoing and also envisages constructions of which the following gives examples. BRIEF DESCRIPTION OF THE DRAWINGS The invention may be more fully understood by having reference to the accompanying drawings, wherein: Figure 1 is a schematic diagram of a preferred embodiment of the invention, Figure 2 is a flow diagram of the control functions of a preferred embodiment of the invention. DESCRIPTION OF THE PREFERRED EMBODIMENTS CONSTRUCTION Fumigation chamber 10 is pressure tight and can withstand pressures up to 2 to 3 atmospheres or a high vacuum. Chamber 10 is provided with doors 11 and 13 at either end thereof. A portion of the chamber is illustrated as broken away to show a sprayer 15 which is connected to a mains source of water through valve 43. In the embodiment illustrated, the fumigant to be employed is stored under pressure in a gas cylinder 12. A vapouriser 21 in the form of a heater is provided to vapourise any fumigant not in a gaseous form after passing control valve 38. Valve 38 is a three-way valve connected with an apparatus known as a single dose piston injector. The injection is precalibrated to withdraw a metered amount of fumigant from cylinder 12 in a first configuration. In a second configuration valve 38 is closed and the dose of fumigant is stored in the injector. In the third configuration valve 38 is opened to the circuit which circulates the gas through chamber 10. A blower 14 is provided in series with a fumigant heater 16 and cooler 17. A vacuum pump 18 is connected through valve 42 with chamber 10. A variable volume fumigant holding chamber 20 is provided in which is stored the fumigating medium. An upper tank 22 and lower tank 28 to are provided for storage of a working liquid, generally water. A pump 24 provides pumping for liquid from lower tank 28 to upper tank 22. A mixer 26 is also provided in tank 28. Tank 22 has a capacity to at least fill chamber 10 and tank 28 has a slightly greater capacity than the combined capacities of chamber 10 and tank 22. A combination spray/dip booth 32 is provided adjacent door 13 of chamber 10. A second identical booth may be provided adjacent door 11. A conveyor, not illustrated, runs at either end from chamber 10 into tank 32 when present. A pump 30 recirculates liquid sprayed in tank 32. A pair of fumigant adsorber/generator vessels 34 and 36 are provided. Each vessel contains a bed of activated carbon and a means for heating the carbon such as superheated steam or hot oil. A compressor 66 is provided and when superatmospheric pressures are to be employed pressurises chamber 10. Control valves 40, 41, 42, 43, 44, 46, 48, 50, 52, 54, 56, 58, 59, 60, 62, 64, and 65 are provided in the circuit and their operation is described below. OPERATION In operation bins of fruit or produce preferably brought directly from the orchard or field were transferred into chamber 10 by means of a suitable conveyor after opening of door 11. For some varieties of apples it was desirable to dip them in a solution of DPA prior to fumigation. This could be done in a tank or in a booth such as booth 32 prior to entry into chamber 10. Alternatively, the DPA solution was stored in tank 22 and the dipping was done in fumigation chamber 10. The dip solution employed had a concentration of up to 2000 ppm DPA. Dipping was maintained for up to two minutes, usually for from 1 to 2 minutes. We generally fumigated wet fruit as soon as possible after dipping. Fumigation could be delayed for half to three hours after dipping or even until the fruit was dry. There are four distinct modes of fumigation that can be employed with the apparatus described. MODE 1. Direct Injection from Pressure Cylinder Vacuum pump 18 evacuates chamber 10 to a predetermined low pressure, for example 86 kPa abs which automatically activates and closes valve 42. A metered amount of methyl bromide gas from cylinder 12 is injected via valve 38 into the system through vapouriser 21 and is circulated by blower 14 through heater 16 and cooler 17. Valves 40, 41 and 44 are open while valves 42, 43, 46, 48, 50, 52, 54, 56, 58, 59, 60 and 65 are closed during this phase of the operation. In the preferred embodiment according to this invention 3 methyl bromide concentrations of 200 g/m for twelve minutes 3 or 300 g/m for ten minutes have been found to be adequate to give complete kills of the larvae stage of the light brown apple moth (Epiplyas Postvittana) which is the most resistent to fumigation. These equate to ct values of 40 to 50. It will be seen that there are at the lower end of the range which is used in conventional fumigation. It has been observed that at these levels it has been possible to fumigate apples with little or no fruit damage and at very low levels of residual bromide. It has been found that times of from 5 to 30 minutes with concentrations up to 600 3 g/m have achieved the desired results. We have observed 3 that concentrations of 40 to 600 g/m for times between five and thirty minutes give desired kills without high residual bromide levels with the proviso that the ct product remains 3 in the range of 20 to 150 ghr/m With ethylene dibromide as fumigant the concentration required for kills equivalent to those achieved with methyl bromide was between one half and one tenth, preferably one third and one quarter of that of methyl bromide. Fumigation times remained the same and thus ct values were proportionally smaller. When the predetermined fumigation time has elapsed methyl bromide is vented by opening of valves 48 and 50 and closing valve 40. Atmospheric air entering through valve 48 displaces the methyl bromide. When venting is substantially complete valve 43 may be opened and fresh water sprayed via sprayer 15 to remove most of the residual methyl bromide. Detectors within chamber 10 detect a level of methyl bromide concentration down to 20 parts per million. When this minimum level is reached the doors 11 and 13 are opened and produce removed. It has been found that a first detector for larger concentrations and a second detector for micro concentrations give appropriate detection results. MODE 2. Circulation from Storage Tank Fruit is placed in chamber 10 as before. Valves 48 and 59 are opened and all other valves into or out of chamber 10 are closed. Water from tank 22 floods chamber 10 expelling air present past valve 48 to atmosphere. Valves 59 and 48 are then closed and valves 46 and 60 opened. The water in chamber 10 is dumped into tank 28 and the fumigating medium in tank 20 is drawn into chamber 10. Valves 46 and 60 are closed, valves 40, 41 and 44 are opened and blower 14 is started. Vacuum pump 18 is also started and valve 42 opened. Valve 42 is set to close at a preset pressure, in this case 86 kPa abs, although the level is not critical. The fumigating medium is allowed to circulate in chamber 10 for a predetermined fumigation period. During fumigation pump 24 pumps water from lower tank 28 to upper tank 22. At the end of the fumigation period valves 40 and 44 are closed valves 59 and 46 are opened and water in tank 22 displaces the fumigating medium in chamber 10 and returns it to storage tank 20. Water in chamber 10 is again dumped into tank 28 by opening valves 48 and 60 and chamber 10 opened and the fruit removed. Fumigant lost by absorption in water and through vacuum pump 18 may be made up by injection of fumigant from tank 12 at the beginning of fumigation in the manner described above. MODE 3. Fumigant Adsorption/Desorption Fruit is placed into the chamber 10 as before. For the first fumigation using this circuit the method described under part 1 above is repeated up to the point where venting of the fumigant is to commence. At the same time one of the vessels 34 or 36 is set for adsorption of fumigant being circulated through chamber 10 by closing valve 41 and by opening valves 52 and 54 or alternatively valves 58 and 56. When 90-95% of the circulating methyl bromide has been adsorbed valves 40, 44, 52, 54, 56 and 58 are closed and valves 48 and 50 are opened to vent the remaining methyl bromide. Fruit is removed as before. This cycle is repeated once so that the other of vessels 34 and 26 is loaded with adsorbed gas. Alternatively, the activated carbon in vessels 34 and 26 can both be loaded with methyl bromide at the same time by closing valve 41 as before and opening valves 52, 54, 56 and 58 and injecting 2 to 4 doses of methyl bromide through valve 38 from cylinder 12 instead of a single dose as before. While one vessel 34 is adsorbing fumigant the activated o carbon in the other vessel 36 is being heated to 150 C for desorption of fumigant in the next fumigation cycle. After fruit is placed in the vessel under reduced pressure, as in mode 1 above, valves 40, 44, 56 and 58 are opened, valves 41, 50, 52, 54 and the remaining valves into chamber 10 are closed and desorbed fumigant from vessel 36 circulated into chamber 10. When the desired concentration of fumigant has been desorbed valve 41 is opened and valves 56 and 58 are closed for the balance cf the fumigation period. Any shortfall of fumigant is made up by injection of the balance of fumigant required by injector 38 as described in relation to mode 1. At the completion of fumigation valve 41 is again closed and either the pair of valves 52 and 54 or the pair of valves 56 and 58 is opened to the depleted vessel 34 or 36 and the circulating fumigant adscrbed onto the activated carbon. The loaded activated carbon in the other of vessels o 34 and 36 is at this time being heated to 150 to begin the next cycle. MODE 4. Fumigation with Aqueous Methyl Bromide Solution An aqueous solution containing dissolved methyl bromide is stored in upper tank 22. As before fruit is placed in chamber 10. Valves 59 and 48 are opened and the fumigating solution fills chamber 10 at the completion of fumigation valve 60 is opened and the fumigating solution is then pumped by pump 24 up to tank 22 for the next fumigation cycle. The solution of methyl bromide may be made up by filling chamber 10 with methyl bromide and dumping water in from tank 22. When fresh fumigant solution is required and the spent solution is no longer desired valves 62 and 64 may be opened and the water in tanks 22 and 28 allowed to drain away. ELEVATED PRESSURE OPERATION With any one of the four modes of operation just described fumigation can be conducted in conjunction with compressor 66 and valve 65. The modes of operation are in each case as described above except that reference to the opening and closing of valve 42 should be read as opening and closing of valve 65 and the operation of vacuum pump 18 should be read as operation of compressor 66. Compressor 66 is adjusted to provide a temperature in excess of atmospheric, preferably 2 to 3 atmospheres. POST FUMIGATION TREATMENT After fumigation according to any one of the methods described above is completed door 13 is opened and the bins containing the apples transferred on a suitable conveyor into a spray and/or dip booth 32. In the present instance the booth consists of a stainless steel chamber having rollers to allow the bins of fruit to be passed therethrough. At the bottom of the chamber is a catching and holding reservoir and the water can be recirculated by means of pump 30. In some instances it is desirable to employ a solution of sodium chloride in finally washing the apples. AUTOMATIC SEQUENCING The operation of the microprocessor which can be used to automatically control the apparatus may be more fully understood by having reference to figure 2. Because the fumigant gases are toxic to humans there may be detectors at critical points throughout the overall plant for the protection of the operators. The main detectors may be within chamber 10. There will be a general detector which detects the higher concentrations and a micro-detector for detecting the quantities near the minimum. Referring to the flow sheet, when the cycle start/restart circuit, which is the gas level detector, has detected that the level has fallen below the maximum safe level then it will engage the door open and close circuit to activate hydraulic rams which open the doors of chamber 10, thus completing an operation and leaving the apparatus ready to begin a new operation. Other types of cycle start/restart cycles such as a timer may be employed alternatively. When the doors are open the bin loading and unloading circuit positions rollers up to both ends of chamber 10 and a conveyor conveys bins of fruit into chamber 10 at the same time pushing the bins already in the chamber out of it. Once bins of fruit have been placed into the chamber 10 an automatic cycle is started and the door open/close circuit ensures that both doors 11 and 13 are closed. Then when operating in either of modes 1 or 3 the pressurising/depressurising circuit commences its cycle by closing valves 43, 46, 48, 50, 52, 54, 56, 58, 59, 60, and 65 and opening valves 40, 41, 42 and 44 and coiiunencing vacuum pump 18. When the pressure has fallen to a predetermined low level valve 42 is closed and the fumigation injection cycle is commenced in mode 1. When operating in mode 1 the fumigation injection circuit valves 40, 41 and 44 remain open while the remaining relevant valves listed above are closed and the single dose piston injector 38 injects the appropriate charge of fumigant into the system. Fan 14 will be in operation to circulate the fumigant and heater 16 or cooler 17 will be set to keep the fumigating gas at a predetermined o o temperature between 5 C and 40 C. The upper level fumigant detector within chamber 10 allows for venting if excess fumigant above a predetermined level is detected. However, in normal operation the dose injected will have the correct predetermined level. The microprocessor is programmed to fumigate for a predetermined time depending on the concentration of the fumigant so as to achieve the ct product which is sought. Once the preset fumigation time has elapsed the microprocessor commences venting by opening valve 48 and 50 and closing valve 40 to complete fumigation in mode 1. When operating in mode 2 the water dumping cycle is instituted by opening the valves as described above in sequence. The pressurising/depressurising circuit is engaged after the fumigating medium is present in chamber 10. The fumigant injection circuit is also engaged at this point to inject a "make up" amount of fumigant to replace that lost through the vacuum pump and water absorption. When the mode 3 fumigant circuit is employed, valves 41 and 48 are closed and the appropriate pair of valves 52 and 54 or 56 and 58 opened to pass the fumigant flushed from chamber 10 over the activated charcoal after the pressurising circuit has been engaged to bring the pressure to the desired level of vacuum. The mode then continues in the same sequencing as mode 1. With the mode 4 fumigation circuit the pressurising and depressuring circuit is by-passed. The sequence of valve openings is as described above in relation to mode 4 above. The fumigant injection circuit may be activated to make up fumigant lost during either of the fumigating cycles. The water spray circuit is activated either by a time sequence signal or by a fumigant detector to open valve 43 and allow flow of mains water into chamber 10. With any one of the fumigant modes 1-4 it is possible to omit the water spray circuit. When the microdetector of the fumigation detection circuit detects that a safe level of fumigant has been reached it engages the door open/close circuit once more. However, in the prefered embodiment to speed up the fumigation process the water spray circuit involving feeding water by opening valve 43 from mains is engaged to speed up the removal of fumigant. It will be appreciated that many variations of the process and apparatus described within the scope of this invention will be apparent to those who are skilled in the art. PILOT PLANT ASSESSMENT A pilot plant assessment of High Concentration - Short Time (HCST) fumigation included large scale insect mortality studies on light brown apple moth and brownheaded leafroller, and the evaluation of the susceptibility of freshly picked Granny Smith apples to fumigation damage and for bromine residues. The results showed that complete mortality of light brown apple moth (LBAM) and brownheaded leafroller (BHLR) 3 larvae could be achieved with fumigations at 300-350 g/m of o methyl bromide for 10 minutes at 15 C and 86 kPa abs pressure. At higher vacuums (31 kPa abs) complete mortality could be achieved at lower dosages. The fruit damage experiments have shown that freshly picked fruit can be treated at the above fumigation conditions without sustaining commercially significant levels of damage. Fruit that had been stored at ambient for up to three days could also be fumigated without damage levels becoming unacceptably high. Bromine residues were below 5.0 mg/kg, the maximum permissible level in the U.S.A. For fumigation treatment sufficient to achieve complete 3 mortality of LBAM and BHLR ie 300-350 g/m for 10 minutes there is no significant fruit damage on fruit fumigated the day after picking and coolstored for 2 months before assessment. On the more severe treatments there was a small amount of damage which was mainly calyx-end breakdown. This damage was of academic interest only. A comparison between the fruit damage results for conventional (i.e. two hour) fumigation and fumigation according to the present invention shows that there was no difference in damage levels for the majority of treatment and fruit handling options. on the late season fruit that had been held at ambient before fumigation, however, the internal damage levels on conventionally fumigated fruit were consistently higher than for fruit fumigated according to the present invention for all five orchards. Apart from assessing comparative damage levels between fumigation according to the present invention and traditional fumigation, the pilot plant trials were designed to determine the treatment and handling limits beyond which fruit quality was affected. This was clearly demonstrated in the experiments in which the treatment was delayed and the fruit held at ambient for up to 5 days before being fumigated. The fruit fumigated after 5 days showed some considerable incidence of minor treatment - induced internal damage, particularly the late season fruit. The latter fruit also showed a slight susceptibility to external damage. For the other treatment options investigated there was no significant alteration in the fruit quality after 2 months coolstorage (except for the high vacuum treatments at high concentrations). On the small quantity of fruit kept for 3 months however there was a small increase in the incidence of external damage. This demonstrates that ,ome forms of damage require long periods of coolstorage to become apparent. Fruit from some trials, particularly the use of DPA to reduce damage should perhaps be left for longer periods before assessment. The experimental programme has confirmed the feasibility of a rapid fumigation process for apples. Apples in bulk, either freshly picked (up to 3 days old) or temporarily coolstored can be fumigated under conditions sufficient to ensure total leafroller mortality without sustaining undesired fruit damage or unacceptable residual bromine levels.

Claims: CLAIMS 1. A process for the fumigation of produce which comprises treating said produce with gaseous fumigant at a concentration sufficiently high to be fatal to the target pest for from 5 to 30 minutes. 2. A process according to claim 1 wherein said produce is treated with gaseous methyl bromide in a concentration of from 40 to 600 g/m for from 5 to 30 minutes with the proviso that the product of concentration (expressed in 3 g/m ) x time (expressed in hours) is within the range of 20 to 150 gbr/m 3. A process according to claim 1 wherein said produce is treated with gaseous ethylene dibromide held at a 3 concentration of from 10 to 200 g/m with the proviso that 3 the ct product is from 5 to 50 ghr/m 4. A process according to claim 2 or 3 wherein said treatment is conducted for from 8 to 15 minutes. 5. A process according to claim 1 wherein said treatment is conducted in a sealed fumigation chamber under a partial vacuum. 6. A process according to claim 5 wherein said concentration x time product (ct) is from 40 to 80 3 ghr/m for fumigating light brown apple moth or any other leaf roller species with methyl bromide. 7. A process according to claim 5 wherein said ct product 3 is from 60-120 ghr/m for fumigating codling moth with methyl bromide. 8. A process according to claim 6 wherein said produce is apples. 9. A process according to claim 8 wherein said process includes a preliminary step of treating apples in a DPA solution with a concentration of up to 2000 ppm,for a time of up to 2 minutes and fumigating said treated apples within one half hour after said treating. 10. A process according to claim 9 which includes the additional step of rinsing said produce after said fumigation. 11. A process according to any of claims 2 or 6 to 10 wherein said fumigant is recovered by adsorbing methyl bromide exhausted from said fumigation chamber on activated carbon. 12. A process according to claim 11 wherein said fumigation is effected by desorbing adsorbed fumigant. 13. A process according to any of claims 1 to 11 wherein said treatment with said fumigant is carried out at a temperature of from 50C to 40 C. 14. An apparatus for fumigating product comprising a fumigation chamber capable of withstanding elevated and reduced pressures, means for opening and closing said chamber, means for injecting a metered amount of fumigant into said chamber, means for flushing fumigant from said chamber, sequencing means for sequencing the operation of said opening and closing means, said injecting means and said flushing means, the arrangement being such that in use said sequencing means activates said injecting means when said chamber is closed, activates said flushing means after fumigant has been in said chamber a predetermined length of time and opens said chamber after a predetermined flushing time. 15. Apparatus according to claim 14 including means for pressurising or evacuating said chamber, the arrangement being such that said sequencing means activates said injecting means when a predetermined pressure is reached in said chamber. 16. Apparatus according to claim 15 which includes means for detecting the presence of fumigant in said chamber and in which the arrangement is such that said sequencing means opens said doors only after said detecting means has detected that the concentration of fumigant has fallen below a predetermined level. 17. Apparatus according to claim 16 in which said chamber is provided with an evacuating means comprising a vacuum pump. 18. Apparatus according to any of claims 14 to 17 in which said door opening and closing means comprises an hydraulically operated ram and locking mechanism activated by said sequencing means. 19. Apparatus according to any of claims 14 to 18 wherein said means for injecting comprises a single dose piston injector. 20. Apparatus according to any of claims 14 to 19 in which said means for injecting fumigant includes a fumigant adsorber/desorber. 21. Apparatus according to claim 20 in which there are a pair of said fumigant adsorber/desorbers and said sequencing means is programmed to allow for one to be desorbing while the other is adsorbing and vice versa. 22. Apparatus according to claim 21 in which said sequencing means comprises a micro-processor. 23. Apparatus according to any of claims 14 to 22 wherein there is provided means for heating and/or cooling said fumigant. 24. Apparatus according to any of claims 14 to 23 wherein there is provided liquid spraying means within said chamber to assist in removal of said fumigant.

Inventors: COLLIE, NAYLOR, FIELDES, ROBERT BLAKE, MCLACHLAN, CORRAN NORMAN STUART, NICOL, ROSS STUART, SMITH, DONALD KENNETH WELDON
Applicants: THE NEW ZEALAND APPLE AND PEAR MARKETING BOARD
Application year: 1982
Main classification: A23L3
IPC codes: A23B7, A01M17, A23L3, A01M13, A01N25