the compounds that inhibit ethylene responses in plants are disclosed in the following references , all of which are incorporated by reference . u . s . pat . no . 5 , 100 , 462 discloses that diazocyclopentadiene and its derivatives are effective blocking agents that inhibit the ethylene response in plants . sisler et al ., plant growth reg . 9 , 157 - 164 , 1990 , discloses that cyclopentadiene was an effective blocking agent for inhibiting the ethylene response in plants . u . s . pat . no . 5 , 518 , 988 discloses that cyclopropene and its derivatives , including methylcyclopropene , are effective blocking agents for inhibiting the ethylene response in plants . rather than repeat the disclosure of those references in this specification , they are incorporated by reference in their entireties . the derivatives of cyclopropene , cyclopentadiene and diazocyclopentadiene may contain from 1 to 4 r groups . the number of such r groups is more preferably 2 and most preferably 1 . as previously mentioned , suitable r groups include hydrogen , saturated or unsaturated c1 to c10 alkyl , hydroxy , halogen , c1 to c10 alkoxy , amino and carboxy . the term “ alkyl ” is defined herein to refer to linear or branched , saturated or unsaturated alkyl groups . examples include but are not limited to methyl , ethyl , propyl , isopropyl and butyl . alkyl groups of the present invention are most preferably single carbon or linear . pursuant to the present invention , cyclopropene and its derivatives are made by reacting , in an inert environment , a metal amide salt , such as lithium amide salt , sodium amide salt , potassium amide salt , lithium diisopropylamide salt , sodium diisopropylamide salt or other metal amide salts , and a halogenated carbene , such as 3 - chloro - 3 - methyl - 2 - methylpropene , 3 - bromo - 3 - methyl - 2 - methylpropene , 3 - chloro - 2 - methylpropene , 3 - bromo - 2 - methylpropene or some other halogenated carbene . the specific compounds named above are preferred . methylcyclopropene is made under the same conditions with the same metal amide salts discussed above by reacting them with a halogenated methylpropene . the preferred halogenated methyl propenes are 3 - chloro - 2 - methylpropene and 3 - bomo - 2 - methylpropene . these halogenated methyl propenes lead to a high purity product for the intended use and are readily available . suitable methods for making cyclopropene and its derivatives , including methylcyclopropene , are covered in the examples below . while a variety of different volatile and non - volatile non - reactive solvents can be utilized , preferred suitable solvents include glycerine , mineral oil , polyethylene glycol , diglyme and tetraglyme . the use of a non - reactive solvent is optional . the inert environment can be created by any known method including purging the reaction vessel with nitrogen or any other inert gas . the concentration ratio of the metal amide salt to the halogenated carbene or halogenated methyl propene is a molar ratio of about 1 : 1 to about 4 : 1 . the reaction temperature can range from about 20 ° to about 60 ° c . and the reaction pressure can range from about 1 to about 100 psi . the resulting exothermic solution from this reaction is allowed to react until no further heat is given off . after the reaction is complete , a polar solvent is added to the reaction solution . while a variety of polar solvents can be used , suitable examples of such polar solvents include water , acetone and alcohol . after the polar solvent has been added , the head space of the reaction solution is displaced , cooled and placed into a second vessel containing a molecular encapsulation agent , such as cyclodextrin , and buffered water to form the desired molecular encapsulation agent complex . when the gas is released into the original vessel using sodium amide , a non - polar solvent is used to release the gas when a lithium salt is employed as the metal amide salt . although it is not necessary to achieve the objectives of this invention , fractional distillation can be used on the final product . in one preferred embodiment , the headspace of the reaction solution is cooled through a condenser and cold trap . the water used with the molecular encapsulation agent is buffered to approximately a ph of 4 to 6 , and the reaction product and molecular encapsulation agent is stirred for 1 to 24 hours at temperatures ranging from room temperature to 40 ° c . after the complex is formed , the excess water is filtered off and the resulting slurry dried to form a powder . the examples below describe a method of preparing a molecular encapsulation agent from methylcyclopropene and alpha - cyclodextrin . as previously explained , forming a complex from the molecular encapsulation agent and the gaseous compound capable of inhibiting the ethylene response in plants is important for two reasons . first , strained carbenes such as methylcyclopropene are quite unstable to reaction with oxygen , self polymerization and reaction with other organic compounds . the complexes of the present invention overcome those instability problems . second , it is preferable to use a product that has a long shelf life , is simple to handle and comparatively non - reactive . the complexes of the present invention meet those objectives as well . methylcyclopropene is reactive and explosive at concentrations over one percent . additionally , it is difficult to handle as a gas , requires compression into metal containers or the use of a non - oxygen permeable container . since for most applications , less than 1 ppm ( part per million ) and preferably less than 1 ppb ( parts per billion ) of methyloyclopropene in the atmosphere are required , the amount of methylcyclopropene required to treat a normal room is about one gram or less . the recommended dosage is around 500 - 700 ppb for 4 - 6 hours at room temperature for a few crops . a molecular encapsulation agent is a compound that has a lock and key structure similar to an enzyme whereby a substrate selectively fits into the encapsulation site . the most preferred molecular encapsulation agent found to date is alpha - cyclodextrin . other molecular encapsulation agents , such as crown ethers , polyoxyalkylenes , prophorines , polysiloxanes , phophazenes and zeolites , were also found to work . most of these molecular encapsulation agents can be obtained from the aldrich chemical company . methylcyclopropene can be complexed with cyclodextrin in water . for example , when the water is removed after methylcyclopropene is bubbled through an aqueous solution of alpha - cyclodextrin , it was discovered that the methylcyclopropene was firmly locked into the cyclodextrin cage structure . in addition , the cyclodextrin cake after drying can be milled into a powder and blended to a uniform concentration . it has been surprisingly discovered that this particular complex ( methylcyclopropene and alpha - cyclodextrin ) was stable for over one year as judged by accelerated shelf life studies . moreover , a powdered complex can be easily measured and packaged into appropriately - sized doses for treatment of plants . the method of delivery of the present invention provides a user - friendly application . it also promotes a lower initial dose of active compound and a decrease in the need for repeated applications as compared with previously proposed solid carrier systems . a variety of molecular encapsulation agents may be utilized in the present invention provided they have the correct cage structure to form a molecular trap for the compound capable of inhibiting the ethylene response in plants . thus , as one skilled in the art would recognize , the use of other molecular encapsulation agents falls within the spirit and scope of the present invention . cyclodextrins , also known as “ schardinger dextrins ”, are cyclic oligosaccharides composed of glucose units bonded together by alpha 1 , 4 bonds . the six - membered ring structure is named alpha - cyclodextrin , the seven membered ring is beta - cyclodextrin and the eight membered ring is gamma - cyclodextrin . generally , compounds that are encapsulated fit inside of the oligosaccharide ring . as is well known , cyclodextrins are produced from starch of any selected plant variety such as corn , potato , waxy maize and the like . the starch may be modified or unmodified starch derived from cereal or tuber origin and the amylose or amylopectin fractions thereof . the selected starch in aqueous slurry at selected concentration up to about 35 % by weight solids is usually liquefied as by gelatinization or treatment with liquefying enzyme such as bacterial alpha - amylase enzymes and then subjected to treatment with a cyclodextrin glucosyl transferase enzyme to form the cyclodextrin . the amount of the individual alpha , beta and gamma cyclodextrins produced by treating the starch with the glucosyl transferase enzyme will vary depending on the selected starch , selected glucosyl transferace enzyme and processing conditions . the parameters to select for glucosyl transferase enzyme conversion for the desired result in the amount of each individual cyclodextrin to be produced is conventional and well described in the literature . separation and purification of the cyclodextrin thus obtained is also conventional and well known to those of skill in the art . in one embodiment , the cyclodextrin utilized in the complex of the present invention is alpha - cyclodextrin . however , as one skilled in the art will appreciate , any cyclodextrin or mixture of cyclodextrins , cyclodextrin polymers as well as modified cyclodextrins can also be utilized pursuant to the present invention . cyclodextrins are available from american maize products company , hammond , ind ., as well as other vendors . in order to form a molecular encapsulation agent complex , the active compound and the molecular encapsulation agent molecules are mixed together in a solution for a period of time sufficient to form the complex . the complex is then removed from the solution and dried . the dried complex is then ready for use . as noted previously , the resulting complex of the present invention provides a number of advantages to manufacturers as well as ultimate consumers . due to the ability of the cyclodextrin to entrap a large amount of cyclopropene , the present invention should lower the initial dosage of cyclopropene needed for treatment as compared with previously proposed solid carriers . likewise , it should decease the need for repeated treatments of cyclopropene compared with previously proposed solid carriers . the potential of these advantages is demonstrated in the examples below which show the unexpected ability of the complex of the present invention to entrap large quantities of cyclopropene . a still further advantage of the present invention is the increased stability of the resulting methylcyclopropene / alpha - cyclodextrin complex as compared to compressed gas . based on heat stability testing , it was determined that when concentrated methylcyclopropene gas was exposed to heat of about 50 ° c ., a 75 % to 100 % reduction in concentration was observed . when left at room temperature , the concentrated gas lost 30 % to 42 % of its concentration . on the other hand , when the methylcyclopropene / alpha - cyclodexrin complex of the present invention was exposed to 50 ° c ., only a 38 % reduction in the concentration of methylcyclopropene was observed . when left at room temperature , there was no reduction in the concentration of methylcyclopropene from the methylcyclopropene / alpha - cyclodextrin complex . the present invention also provides a convenient product for commercial use . for example , select quantities of the complex of the present invention can be sealed into a package for retail and wholesale use . in one embodiment , the preferable package is made of polyvinyl alcohol . the inventors have discovered that polyvinyl alcohol increases the efficiency of release , reduces any exposure , and insures proper dosage . when the consumer is ready to use the complex , the consumer may either dissolve the powder in an aqueous solution ( e . g ., water ) and expose the resulting solution to the plant . understandably , various changes and modifications to the presently preferred embodiments described herein will be apparent to those skilled in the art . such changes and modifications can be made without departing from the spirit and scope of the present invention and without diminishing its intended advantages . therefore , the claims are intended to cover such changes and modifications . the controlled release of compounds capable of inhibiting the ethylene response in plants controlled release of methylcyclopropene as well as other compounds capable of inhibiting the ethylene response in plants from a molecular encapsulation agent complex such as cyclodextrin is facilitated by the addition of an excess of water . addition of an acid or alkaline substance to the water also facilitates a faster release of the active compound . heating the water also facilitates a faster release of the active compound . because methylcyclopropene has a high vapor pressure at normal working temperatures from 4 to 25 ° c ., it quickly escapes into the atmosphere . by releasing methylcyclopropene from a complex in water in a closed container or room , the methylcyclopropene diffuses onto the ethylene receptor sites of all the plants within the room . use of fans or other means to move the air for more suitable equilibration in the chamber is also often useful . depending on the plant , generally a dose of less than 1 ppm ( part per million ) or preferably less than 500 ppb ( parts per billion ) of methylcyclopropene or some other active compound in the atmosphere of the sealed container or room for about 2 - 6 hours is sufficient to protect the plant or plant product from further ethylene damage . the term “ plant ” is used generically in the present invention to also include woody - stemmed plants in addition to field crops , potted plants , cut flowers , harvested fruits and vegetables and ornamentals . some of the plants that can be treated by the methods of the present invention are listed below . plants treated by the compounds of the present invention that inhibit the ethylene response need to be treated at levels that are below phytotoxic levels . this phytotoxic level varies not only by plant but also by cultivar . when correctly used , the compounds of the present invention prevent numerous ethylene effects , many of which have been disclosed in u . s . pat . nos . 5 , 518 , 988 and 3 , 879 , 188 , both of which are incorporated herein by reference in their entirety . the present invention can be employed to combat numerous plant ethylene responses . ethylene responses may be initiated by either exogenous or endogenous sources of ethylene . ethylene responses include , for example , ( i ) the ripening and / or senescence of flowers , fruits and vegetables , ( ii ) the abscission of foliage , flowers and fruit , ( iii ) the prolongation of the life of ornamentals , such as potted plants , cut flowers , shrubbery and dormant seedlings , ( iv ) the inhibition of growth in some plants such as the pea plant , and ( v ) the stimulation of plant growth in some plants such as the rice plant . vegetables which may be treated by the methods of the present invention to inhibit senescence include leafy green vegetables such as lettuce ( e . g ., lactuea sativa ), spinach ( spinaca oleracea ) and cabbage ( brassica oleracea ; various roots such as potatoes ( solanum tuberosum ), carrots ( daucus ); bulbs such as onions ( allium sp . ); herbs such as basil ( ocimum basilicum ), oregano ( origanum vulgare ) and dill ( anethum graveolens ); as well as soybean ( glycine max ), lima beans ( phaseolus limensis ), peas ( lathyrus sp . ), corn ( zea mays ), broccoli ( brassica oleracea italica ), cauliflower ( brassica oleracea botrytis ) and asparagus ( asparagus officinalis ). fruits which may be treated by the methods of the present invention to inhibit ripening include tomatoes ( lycopersicon esculentum ), apples ( malus domes tica ), bananas ( musa sapientum ), pears ( pyrus communis ), papaya ( carica papya ), mangoes ( mangifera indica ), peaches ( prunus persica ), apricots ( prunus armeniaca ), nectarines ( prunus persica nectarina ), oranges ( citrus sp . ), lemons ( citrus limonia ), limes ( citrus aurantifolia ), grapefruit ( citrus paradisi ), tangerines ( citrus nobilis deliciosa ), kiwi ( actinidia . chinenus ), melons such as cantaloupes ( c . cantalupensis ) and musk melons ( c . melo ), pineapples ( aranae comosus ), persimmon ( diospyros sp .) and raspberries ( e . g ., fragaria or rubus ursinus ), blueberries ( vaccinium sp . ), green beans ( phaseolus vulgaris ), members of the genus cucumis such as cucumber ( c . sativus ) and avocados ( persea americana ). ornamental plants which may be treated by the methods of the present invention to inhibit senescence and / or to prolong flower life and appearance ( such as the delay of wilting ), include potted ornamentals and cut flowers . potted ornamentals and cut flowers which may be treated with the methods of the present invention include azalea ( rhododendron spp . ), hydrangea ( macrophylla hydrangea ), hibiscus ( hibiscus rosasanensis ), snapdragons ( antirrhinum sp . ), poinsettia ( euphorbia pulcherima ), cactus ( e . g ., cactaceae schlumbergera truncata ), begonias ( begonia sp . ), roses ( rosa sp . ), tulips ( tulipa sp . ), daffodils ( narcissus sp . ), petunias ( petunia hybrida ), carnation ( dianthus caryophyllus ), lily ( e . g ., lilium sp . ), gladiolus ( gladiolus sp . ), alstroemeria ( alstroemaria brasiliensis ), anemone ( e . g ., anemone bland ), columbine ( aquilegia sp . ), aralia ( e . g ., aralia chinesis ), aster ( e . g ., aster carolinianus ), bougainvillea ( bougainvillea sp . ), camellia ( camellia sp . ), bellflower ( campanula sp . ), cockscomb ( celosia sp . ), falsecypress ( chamaecyparis sp . ), chrysanthemum ( chrysanthemum sp . ), clematis ( clematis sp . ), cyclamen ( cyclamen sp . ), freesia ( e . g ., freesia refracta ), and orchids of the family orchidaceae . plants which may be treated by the methods of the present invention to inhibit abscission of foliage , flowers and fruit include cotton ( gossypium spp . ), apples , pears , cherries ( prunus avium ), pecans ( carva illinoensis ), grapes ( vitis vinifera ), olives ( e . g ., olea europaea ), coffee ( cofffea arabica ), snapbeans ( phaseolus vulgaris ), and weeping fig ( ficus benjamina ), as well as dormant seedlings such as various fruit trees including apple , ornamental plants , shrubbery , and tree seedlings . in addition , shrubbery which may be treated according to the present invention to inhibit abscission of foliage include privet ( ligustrum sp . ), photinea ( photina sp . ), holly ( ilex sp . ), ferns of the family polypodiaceae , schefflera ( schefflera sp . ), aglaonema ( aglaonema sp . ), cotoneaster ( cotoneastersp . ), barberry ( berberris sp . ), waxmyrtle ( myrica sp . ), abelia ( abelia sp . ), acacia ( acacia sp . ), and bromeliades of the family bromeliaceae . while many of the examples described below are related to the synthesis molecular encapsulation agent compexing and delivery or application of methylcyclopropene to plants , the same synthesis methods have also been found effective for cyclopropene and other cyclopropene derivatives and the same molecular encapsulation agent compexing and delivery or application methods have also been found effective for cyclopropene , cyclopentadiene , diazocyclopentadiene and their derivatives . methylcyclopropene was used in the examples because it is one of the most active derivatives of cyclopropene that binds to the ethylene receptor site of plants . at room temperature , nitrogen gas ( 99 . 95 % pure ) is pumped into a nitrogen vessel ( 35½ ″× 28 ″× 32 ″) containing either sodium amide powder ( 90 %- nanh 2 ) or lithium diisopropylamide powder ( 97 %-[( ch 3 ) 2 ch ] 2 nli ). a separate powder addition vessel is also purged with the same nitrogen gas . purging with nitrogen is necessary because of the reactivity of the above - mentioned lewis bases with air , and to eliminate any contamination before conducting the synthesis reaction . in the powder addition vessel containing the inert atmosphere , the sodium amide ( or an equivalent molar concentration of lithium diisopropylamide ) is added in an amount ranging from 365 - 1100 grams , with the larger amount being preferred . to weigh the proper amount of the lewis base , all weighing is performed in a nitrogen box with nitrogen purging to eliminate oxygen and the threat of spontaneous ignition of the base . special care is important when working with such bases for proper safety . once the lewis base in powder form is completely added , the openings in the powder addition vessel that were used for purging are sealed off to exclude air . the powder addition vessel is attached to the main system . the reaction vessel , which already has been purged with nitrogen and has been partially evacuated , is opened to the powder addition vessel to allow the powder to fall into the reaction vessel with the aid of nitrogen flow . nitrogen enters the powder addition vessel during transfer of the lewis base . after the powder is transferred into the reaction vessel , the ball valve is closed . after the powder is added , a light mineral oil ( dried with molecular sieves ) or another equivalent solvent is added by opening the connecting ball valve and allowing it to pour into the reaction vessel with the aid of nitrogen flow . the amount of oil added during the reaction can vary from 1 - 47 liters , with the higher amount 47 liters being preferred . the reaction vessel is then purged and closed . the reaction vessel temperature is adjusted to a temperature anywhere from 0 ° c . to 75 ° c ., and preferably about 20 ° c . to start the reaction . the temperature can be raised or lowered by heating or chilling the jacket using a circulating pump . should the holding capacity of the vessel be exceeded , the procedure is repeated . during the addition of ingredients , the contents of the reaction vessel are stirred with a propeller mixer , but splashing of the contents should be avoided . after mixing for 1 - 60 minutes , and preferably for about 20 minutes , 3 - chloro - 2 - methylpropene is added to the reaction vessel in an amount ranging from 0 . 15 - 1 . 0 liters . during the addition of the 3 - chloro - 2 - methylpropene , there is continuous purging with nitrogen gas . the liquid reactant 3 - chloro - 2 - methylpropene is added slowly over a period of 20 minutes . during this addition , the temperature of the reaction vessel is monitored and kept at less than 40 ° c . once the 3 - chloro - 2 - methylpropene is completely added , the vessel should be agitated for an additional 1 - 30 minutes , and preferably for 15 minutes , using the propeller mixer discussed above . a reaction vessel pressure of about two atmospheres is used in this example . after all the 3 - chloro - 2 - methylpropene has been reacted , the desired end - product , methylcyclopropene , exists as a sodium salt . to react the remainder of the lewis base and facilitate liberation of the methylcyclopropene product , the nitrogen purge is stopped and water is added ranging from 0 . 00 - 1 . 47 liters by adding the water under positive pressure over a period of 1 hour . once all the water has been added , a ball valve connecting the vessel with the condenser is opened . any pressure is then released by bubbling the gaseous methylcyclopropene product through a mixture of cyclodextrin dissolved in water ( as explained later in this example ). once the reactive ingredients have been mixed , the headspace gas in the reaction vessel is transferred to a 5 gallon mixing vessel , already lined with a bag filter ( 5 - 25 micron mesh plastic ) and containing 0 . 9 - 2 . 8 kg of alpha - cyclodextrin , 0 . 575 liters of a buffer solution . the alpha - cyclodextrin is weighed out on an electronic scale and transferred to the mixing vessel by pouring it through the opening of the mixing vessel . the buffer solution is prepared by combining a 0 . 2 m sodium acetate solution with a 0 . 2 m acetic acid solution which gives a ph in the range of 3 to 5 . the headspace gas in the reaction vessel is transferred by pulling a vacuum on the mixing vessel to 15 psi , closing the condenser / reaction vessel ball valve and opening the ball valve linking the condenser ( 15 coils , ⅜ ′) to the mixing vessel , allowing the gas in the condenser , which has been chilled at a temperature of 0 - 10 ° c . by a chilling circulating pump , to pass through to the mixing vessel . the reason for chilling the gas in the condenser is to significantly reduce any 3 - chloro - 2 - methylpropene from entering the mixing vessel . the lower boiling point of methylcyclopropene ( which is approximately 12 ° c .) compared to the higher boiling point of the 3 - chloro - 2 - methylpropene ( which is 70 ° c .) prevents the later from entering the mixing vessel . the condenser is also positioned in such a way that the 3 - chloro - 2 - methylpropene will return to the reaction flask . once the gas passes from the condenser , the condenser / mixing vessel ball valve is closed , and the condenser / reaction vessel ball valve is opened allowing the headspace gas from the reaction vessel to flow into the condenser . the condenser / reaction vessel ball valve is then closed , the condenser / mixing vessel ball valve is reopened , and the gas flows to the mixing vessel . once the initial head space is transferred over to the mixing vessel , a vacuum will begin to be created in the reaction vessel which can be detected by reading the mounted pressure gauge . when this occurs , the reaction vessel is filled with nitrogen gas ( 99 . 95 % pure ) by closing any connections to the rest of the system , and allowing the nitrogen gas to enter through the nitrogen inlet valve when a slight vacuum occurs . once the reaction vessel has been filled with nitrogen gas , which will be identifiable by reading the mounted pressure gauge , the head space gas from the reaction vessel is once again transferred to the mixing vessel . the process is repeated until the mixing vessel is filled with gas as indicated by the pressure gauge . a minimum concentration of 80 , 000 ppm of methylcyclopropene is preferred in the mixing vessel at this step . this concentration can be calculated the same way as previously mentioned . after the mixing vessel is filled , all the connections are closed , and the vessel is removed from the system and placed on a shaker , which is allowed to shake so that the mixture is completely agitated for 1 - 5 hours at less than 70 ° c . the methylcyclopropene is trapped in the alpha - cyclodextrin during this unit operation . after the contents are agitated , the mixing vessel is allowed to equilibrate for 0 - 72 hours , and preferably for at least 24 hours at a temperature of 0 - 30 ° c . ( preferably about 4 ° c .). next , the contents in the mixing vessel , if containing the buffer solution , are filtered out by vacuum filtration , by connecting a vacuum pump at the bottom outlet of the mixing vessel , which will remove the buffer solution from the mixture while the powder remains in the confines of the filtering bag . once all the buffer solution has been removed , the wet powder containing the entrapped methylcyclopropene is transferred onto a plastic tray and allowed to air dry for 24 - 48 hr . once it has been dried , the filtered material is ground in a powder grinder , creating a fine powder ( approximately 100 mm mesh ). if the material in the mixing vessel did not contain the buffer solution , no filtering or grinding is needed . after the powder is ground , it is placed in a powder mill and allowed to mix for 5 - 10 minutes at approximately 100 rpm . once the powder is mixed , it is analyzed and mixed with dextrose or dextrin to the desired concentration of methylcyclopropene entrapment . if the amount of entrapped methylcyclopropene is lower than the desired concentration , it is bulked and milled with other samples . in both cases , after the newly formed powders are mixed , they are analyzed again to insure that they meet specifications . per every reaction vessel made , 2 - 7 mixing vessels can be filled , depending on the amount of methylcyclopropene remaining in the reaction vessel after the head space has been transferred . however , depending on the amount of methylcyclopropene gas remaining in the reaction vessel , a waiting period of 0 - 3 hours may be necessary for the reaction vessel to produce more methylcyclopropene gas . once the mixing vessels are filled , and there is not enough methylcyclopropene gas to fill more vessels , the reaction vessel is removed from the system , but kept inside a hood . cleaning : water is slowly added to the reaction vessel to begin the cleaning process . water is added slowly due to its reactivity with excess sodium amide . when the sodium amide is mixed with water , ammonia and sodium salts are formed . once the reaction vessel has been washed completely , it is allowed to air dry completely before it is reused . the three addition vessels are cleaned once a week with water . they are thoroughly rinsed with water until no reactants are found . all the piping / tubing and condenser are also cleaned thoroughly once a week with water . the mixing vessels and inner filter linings are thoroughly washed with water after every use . all waste water is disposed of according to governmental regulations . cleanliness , in addition to purging of the vessels with nitrogen gas and the cooling of gas in the condenser are safety steps that also prevent any contamination of the methylcyclopropene . under a nitrogen atmosphere , approximately 0 . 1 to 0 . 5 moles of lithium dilsopropylamide are placed into a two liter container . 100 ml of a non - volatile organic solvent , such as dried mineral oil , is then added to the container . approximately 0 . 1 to 0 . 5 moles of 3 - bromo - 2 - methyl propene is then added to the container . a 1 : 1 molar ratio of the lithium amide and the halogenated methyl propene is utilized . the exothermic solution is then allowed to react until no heat was given off . then , approximately 0 . 1 to 0 . 5 moles of a polar solvent , such as water , is added to the container . the head space of the reaction is displaced with a syringe or by sweeping with nitrogen through a condenser and cold trap , connected to a vacuum system into a flask containing approximately 50 to 200 grams of alpha - cyclodextrin and 50 to 200 ml of water buffered at a ph of approximately 4 to 6 . the cold trap is kept at a temperature of approximately 0 - 10 ° c ., whereas the condenser is at a temperature ranging from approximately 10 - 20 ° c . this solution is then stirred for about 1 to 24 hours at a temperature ranging from room temperature to 45 ° c . lastly , after the solution has reacted , the excess water is filtered out . then the slurry is dried to a powder form . in this manner , a complex is formed in accordance with the present invention . plants are preferably exposed to a non - phytotoxic amount of the active compound . in one embodiment , approximately 0 . 1 gram of an encapsulated cyclopropene or derivative thereof per 50 to 500 cubic feet of atmosphere to be treated is dissolved in an aqueous solution and exposed to plants to prolong their life or inhibit their ethylene response . the methods of the present invention involve initially the step of providing the complex of the present invention . then the complex is dissolved to release the gaseous form of the complex . a variety of solutions may be utilized and generally encompass polar solvents , such as water , dmso , ethanol and methanol . to expose the plant to the gaseous cyclopropene or derivative thereof , the aqueous solution is preferably positioned near the plant . alternatively , the powder may be placed in an aerosol can containing sufficient water and 40 - 50 psi of compressed gas . then , the gaseous cyclopropene may be sprayed onto the plant . to release methylcyclopropene from the cyclodextrin molecular encapsulation agent and treat plants , the first thing that should be done is to place the plants into a closed environment , preferably at elevated temperatures , preferably from 13 ° to 24 ° c . the amount of methylcyclopropene should preferably be from 100 to 500 ppb ( parts per billion of methylcyclopropene in the atmosphere after release ) for crops like carnations . the amount of molecular encapsulating agent complex needed to release the proper amount of methylcyclopropene or any other compound capable of inhibiting the ethylene response in plants will depend upon the plant being treated and the specific complex formulation used . before the active compound is released , the treating chamber is closed and the air flow arranged so that all the plants in the closed chamber will be treated . the methylcyclopropene / alpha - cyclodextrin complex is then added to water . the amount of water used should be at least 10 times the weight of the cyclodextrin and preferably 100 times the weight of the cyclodextrin . other factors that facilitate a more complete release of the active compound capable of inhibiting the ethylene response in plants are the addition of an acidic or alkaline agent to the water so as to buffer the water to an acidic or basic ph . additionally , the water containing the cyclodextrin complex can be heated up to 45 ° c . to facilitate a better release of the methylcyclopropene . the release of methylcyclopropene is faster with heating or changing ph , but in lieu of these treatments , use of a greater amount of water is sufficient to obtain a full release of the methylcyclopropene from the cyclodextrin complex . the plant treatment time is usually at least one hour , but preferably at least 6 hours unless the plants are being held at a temperature less than 15 ° c . in which case more time is preferred ( sometimes as much as 10 hours ). once the plants are treated , the sealed chamber may be opened if desired . the methylcyclopropene is now protecting the plants because it has blocked all the available ethylene receptor sites . this treatment will protect the plants from the action of ethylene until the plant grows new unblocked ethylene receptor sites . the following comparative examples demonstrate the effectiveness of the molecular encapsulation agent complexes of the present invention . the comparative examples demonstrate the benefits of the present invention ( utilizing an alpha - cyclodextrin / methylcyclopropene complex ) as compared to traditional solid inert carriers , such as wood flour and molecular sieves . specifically , these comparative examples demonstrate the amount of methylcyclopropene absorbed by traditional solid carriers as compared to that entrapped by utilizing a molecular encapsulation agent , alpha - cyclodextrin , of the present invention . this experiment evaluates the differences between utilizing the complex of the present invention with a solid carrier , as proposed in u . s . pat . no . 5 , 518 , 988 . specifically , the inventors tested the absorption amount , if any , of methylcyclopropene onto wood flour . the wood flour used was obtained from american wood fibers and was identified as # 10010 hardwood . to evaluate the amount of absorption of methylcyclopropene , 0 . 01 grams of wood flour ( previously exposed to methylcyclopropene in a buffered water solution as described below for the molecular sieve comparative example ) was weighed out in a 25 ml vial , and dissolved with 5 ml of deionized water . then , 1 ml of the headspace from the vial was injected into a gas chromatograph ( a total of 20 ml of headspace was tested ). in addition to testing with 0 . 01 grams of wood flour , 0 . 1 grams was also tested . alpha - cyclodextrin was also tested under the same conditions . it was experimentally found that no methylcyclopropene attachment to the wood flour was detectable . this shows that use of a dry absorbent , such as wood flour , was not effective in absorbing methylcyclopropene . to evaluate the differences between utilizing a molecular encapsulation agent complex of the present invention and molecular sieves , another comparative experiment was also conducted . molecular sieves were selected for these comparison tests because they are one of the most common carriers of chemicals in the chemical industry . two types of molecular sieves were utilized in this comparative example , 13x and 5a . both were obtained from the aldrich chemical company in milwaukee , wis . each molecular sieve was first dried at 50 ° c . for 30 minutes before being used . 25 grams of each were then placed in separate 250 ml erlenmeyer flasks and cooled to − 80 ° c . by placing then in a dry ice / acetone bath . 20 ml of methylcyclopropene ( approximately 60 , 000 ppm ) was injected into the flask and allowed to sit for 24 hours either at room temperature or at 4 ° c . 1 gram of molecular sieve was then weighed in a 20 ml vial , and 5 ml of deionized water was added to release the methylcyclopropene . 1 ml of the headspace from the vial was injected into a gas chromatograph to determine the concentration of methylcyclopropene adsorbed onto the molecular sieves . the following methylcyclopropene release data was obtained . the alpha - cyclodextrin / methylcyclopropene complex used in this example was made by trapping 80 , 000 ppm of methylcyclopropene in a 5 gallon mixing vessel with 1 . 3 kg of alpha - cyclodextrin in 0 . 575 liters of buffer solution having a ph of 4 . the buffer solution was made with 0 . 2 m sodium acetate and 0 . 2 m acetic acid solutions . this is referred to as the “ wet ” cyclodextrin loading in the results discussed below . a “ dry ” cyclodextrin loading was also run . in the dry experiment , the methylcyclopropene was contacted with dry alpha - cyclodextrin , i . e ., cyclodextrin that was not in an aqueous solution . in both experiments , the vessel was chilled to 4 ° c . and the contents mixed for 24 hours . once the methylcyclopropene is trapped onto the cyclodextrin , the pressure fell from about 2 atmospheres to a vacuum . nitrogen gas was then added to atmospheric pressure . the buffer solution was removed by filtering through a filtering bag within the vessel and the cyclodextrin cake was transferred to a plastic tray and allowed to air dry for 48 hours . the dry cyclodextrin with entrapped methylcyclopropene was ground with a powder grinder to a 100 mm mesh size . the complex was stored for two weeks before analysis . to evaluate the amount of methylcyclopropene complexed or trapped by alpha - cyclodextrin , 0 . 01 grams of cyclodextrin ( previously exposed to methylcyclopropene as described above ) was weighed out in a 25 ml vial , and dissolved with 5 ml of deionized water . then 1 ml of the headspace from the vial was injected into a gas chromatograph to determine the concentration of methylcyclopropene in the complex . the results are shown below . the methylcyclopropene was absorbed either wet or dry onto the cyclodextrin and then evaluated as described above . these results demonstrate that the 13x molecular sieve was only capable of taking up 15 ppm of methylcyclopropene . the heat of adsorption may have caused the decay of some methylcyclopropene according to the chromatographic results , but it is estimated that no more than 15 ppm could have been lost . in contrast , the results from the molecular encapsulation agent complex of the present invention demonstrate a substantially complete entrapment of the methylcyclopropene . these dramatic differences in release amounts of methylcyclopropene could not have been expected from the literature . clearly , the molecular encapsulation agent complex of the present invention is far superior to the passive absorption to solids taught in u . s . pat . no . 5 , 518 , 988 .
the present invention generally relates to the regulation of plant physiology , in particular to methods for inhibiting the ethylene response in plants or plant products , and has three embodiments . the first embodiment relates to methods of minimizing impurities capable of reversibly binding to plant ethylene receptor sites during the synthesis of cyclopropene and its derivatives such as methylcyclopropene , thereby avoiding the negative effects these impurities have on plants treated with cyclopropene and its derivatives . the second embodiment relates to complexes formed from molecular encapsulation agents such as cyclodextrin , and cyclopropene and its derivatives such as methylcyclopropene , in addition to cyclopentadiene and diazocyclopentadiene and their derivatives , thereby providing a convenient means for storing and transporting these compounds capable of inhibiting the ethylene response in plants , which are reactive gases and highly unstable because of oxidation and other potential reactions . the third embodiment relates to convenient methods of delivering to plants these compounds capable of inhibiting the ethylene response in the plants in order to extend their shelf life .