CN1669636A - Composition of keeping ice house and horticulture production fresh and its manufacturing technics - Google Patents
Composition of keeping ice house and horticulture production fresh and its manufacturing technics Download PDFInfo
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- CN1669636A CN1669636A CNA2004100079715A CN200410007971A CN1669636A CN 1669636 A CN1669636 A CN 1669636A CN A2004100079715 A CNA2004100079715 A CN A2004100079715A CN 200410007971 A CN200410007971 A CN 200410007971A CN 1669636 A CN1669636 A CN 1669636A
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L9/00—Disinfection, sterilisation or deodorisation of air
- A61L9/01—Deodorant compositions
- A61L9/014—Deodorant compositions containing sorbent material, e.g. activated carbon
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L9/00—Disinfection, sterilisation or deodorisation of air
- A61L9/01—Deodorant compositions
- A61L9/012—Deodorant compositions characterised by being in a special form, e.g. gels, emulsions
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- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B33/00—Clay-wares
- C04B33/02—Preparing or treating the raw materials individually or as batches
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- C04B33/131—Inorganic additives
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L2209/00—Aspects relating to disinfection, sterilisation or deodorisation of air
- A61L2209/20—Method-related aspects
- A61L2209/22—Treatment by sorption, e.g. absorption, adsorption, chemisorption, scrubbing, wet cleaning
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Abstract
The invention relates to a composition for ice house deodorizing and keeping horticulture product and food fresh by adsorbing ethene gas and its manufacturing technique. Particularly, the byproduct red mud generated by extracting bauxite from laterite is mixed with activated carbon, extruded and molded by an extruder, dried under 70-120 DEG C and calcined under 800-950 DEG C. The calcined product is washed by inorganic acid solution and added with 10-20wt% active metal salt immediately. The product can adsorb the plant hormone ethene which can rot the horticulture product to keep the product fresh.
Description
Technical field
The invention relates to ethylene adsorption gas and keep the composition of the freshness of gardening product and food and relevant freezer deodorant and manufacturing process.In more detail mixture cooperation, shaping, the drying of the red soil of various forms and activated carbon, anoxic is calcined and is immersed in and removes the impurity after washing in the hydrochloric acid solution under 950 ℃ of conditions, injects 15~20% frerrous chloride isoreactivity slaines in the composition of washing.The product of Zhi Zaoing has very excellent in performance to removing the foul gas in the freezer and the gas of absorption corrosion gardening product like this, and has increased adsorbance it can be used for a long time.Simultaneously in the application of field of food because of having the advantages that to keep freshness, so the invention relates to the stench that produces on removal freezer, the gardening product treatment facility and invention to the composition of the very effective deodorization medicament that purifies air and relevant manufacturing process.
Background technology
For the freshness that keeps gardening product and food uses the ethene remover to be because the more and more stronger result of desire more fresh, the better product of taste is sought in the raising of consumer's the consumption consciousness recently, therefore be not only large-scale circulation company, agricultural product whole seller at present, the epoch of fresh produce are also sold in the supermarket.Again the producer and the producing region between keen competition caused the long distanceization in consumption place and the competition of quality.Here require because long preservation is adjusted outbound and keep the highly preservation technology of freshness in the process of circulation.Because the gardening product major part all contains very high moisture content, and perishable, thereby occurred after the harvesting reducing the situation that freshness brings the commodity performance obviously to descend or completely lose because of inappropriate storage and circulation.After the harvesting store and the process of circulation in influence the factor of crops freshness many, but the tissue of accelerating because of physiological reason (ethylene gas) aging be the sale time limit of shortening product, the major reason of reduction product quality.Can remove activated carbon, the potassium permanganate (KMnO of ethene
4) wait in the material, activated carbon has the removal efficient of pair low-concentration ethane low, and the ethene that not only is adsorbed on the activated carbon may be emitted, and the too moist shortcoming that can reduce its removal ability.Potassium permanganate effect on the ability that continues removal ethene is very good, but because of containing the heavy metal of strong toxicity, because of carelessness at remover with after agricultural product contact, because disaster can take place strong oxidizing property, and can not utilize again after using, so need when handling to note especially.Therefore the present invention is the problem that exists when solving above-mentioned removal ethene, and keeps the freshness of gardening product and the freshness of food to develop.
" deodorant " is meant to removing Korea S's atmospheric environment and saves hydrogen sulfide, methyl mercaptan, ammonia, amino class and other gaseous matters excitatory that is defined as stench in the method from damage in the present invention, and causing unplessantness displeasure after the stimulation sense of smell and detesting the smell of feeling is the material that purpose is used.Stench is caused by the mixing of several compounds that generally these materials not only cause offending taste, and human body is also had bad influence.
Popular deodour method has the method for using stabilized chlorine dioxide at present, utilize additive and deodorant that the masking agent method that strong fragrance is covered odorant is sprayed in the deodorization source, nertralizer by certain concentration in big gas jet and the method for taste composition, use activated carbon, charcoal, the molecular sieve of silica-gel desiccant and zeolite etc. is to methods such as deodorization source absorption.
Masking agent method in the above-mentioned deodour method is difficult to the basic effect of removing stench of expectation because of strong fragrance, and existence combines the worry that the 3rd kind of harmful material caused in the back with odorant.The method of spraying neutralization is because nertralizer band flavor itself can disappear with the concentration of object gas is irrelevant, and the additional simultaneously gas that generates is also harmful to the person.Therefore traditional deodour method of extensive use is the suction type that utilizes molecular sieve.Because molecular sieve is strong to the absorption affinity of moisture content,, when moisture content is too high, have the characteristics that absorption affinity too reduces so can reduce its freshness by dry gardening product.
On the one hand, use coconut meat, the coal class during material charings such as timber, is made activated carbon after the activate under reducing condition, and its form has granular, broken shape and Powdered etc., and pore diameter is about 1~100nm, and major part is made up of the tiny pore below the 2nm.Activated carbon is the lipophile adsorbent, and is strong to the absorption of nonpolar molecule, though specific area is without limits, and general 1000~1400m
2/ g is for more suitable.Such activated carbon has general absorption removal effect as traditional adsorbent to stench widely, is divided into alkalescence, neutrality, acid activated carbon according to the gas of adsorption treatment.Though non-polar hydrocarbon such as activated carbon Pyrogentisinic Acid, toluene have tangible adsorption effect, low-boiling compounds such as ethene, ammonia and polar molecule foul gas had the shortcoming that can not fully absorb.
Therefore recently in order to replenish the adsorption capacity of hydrophily adsorbent zeolite and lipophile adsorption activity carbon, reported much about zeolite and activated carbon and mixed the manufacturing process of the adsorbent that complex function is arranged and material that can active carbide, and the bond of zeolite and analog or silicate compound and the activated carbon manufacturing process of mixing.
Ri Ben patent for example, Japanese publication communique clear and 54-53669 number on published and added bentonite in zeolite and the activated carbon mixture and gentle method of decomposing with product is made in white sugar postforming, drying, calcining.In above-mentioned manufacturing process, used the bentonite of natural red soil class, so be mingled with impurity in the product as inorganic bonding agent.
On the flat city 4-4039 of Japanese publication communique number, published and added the method that the blast furnace ash powder is made the oil absorption water treatment agent in the zeolite, but present technique has caused the ecological safety issue of blast furnace ash, and forming property is bad, spheroidizing engineering difficulty, the problem low to the lipophile adsorptivity.
At Japanese publication communique clear and 59-69146 number on published and added the method that the shape adsorbent is filtered in the manufacturing of silicic acid chloride in the activated carbon, but present technique exists activated carbon to be stopped up pore by the silicic acid chloride again and reduces the problem of absorption property because of the molecular sieve effect.
Published the technology of in zeolite and activated carbon mixture, adding inorganic bonding agent-alkaline soil metal silicate and organic bond honey on the patent 94-18327 of Korea S.There is the calcining engineering in present technique on manufacturing process, so there is above-mentioned problem too.Simultaneously on the ability of improving energy of adsorption and specific area, there is limit.On Korean Patent 97-0031732 number about also having the calcining engineering in zeolite and lipophile, non-polar compound and the manufacturing technology that activated carbon combines, there are the problems referred to above too through calcining with after injecting metal, and owing to dust problem occurs after forming property and the wearing and tearing, so also have limit on energy of adsorption and the specific area improving.
Summary of the invention
So the present invention is in order to improve the problems referred to above, and constantly make great efforts the result that exploitation can keep gardening product and food freshness and have the deodorant of freezer deodorizing performance.Finished and injected metal ingredient after hydrophily and the activated carbon that outstanding absorption property arranged to the red soil composition that has layer structure of the very strong adsorption capacity of polar molecule with to lipophile and nonpolar molecule suitably removed foreign body in conjunction with postforming, drying, calcining and by pickling, the adsorbance of specific composition has been had the invention of the deodorant compositions of the increase of epoch-making significance and that imparts selective.The red soil (Red Mud) that has flourishing layer structure is the accessory substance that generates behind the extraction alumina from red bauxite, very active influence is arranged utilizing of expense of saving material and accessory substance aspect close environment such as effect and the economy.So the invention provides have hydrophilic and lipophile simultaneously, to the adsorption capacity of polarity and nonpolar molecule, and deodorant compositions and its manufacturing process that can keep the outstanding characterization of adsorption of having of freshness to freezer and gardening product and food.
[description of drawings]
Fig. 1 manufacturing process flow diagram
The time dependent deodorant product of Fig. 2 is to the clearance experimental result of hydrogen sulfide, wherein,
■ represents the experimental result of charcoal; represents the experimental result of our company's product;
The experimental result of representing 0 company's product.
The time dependent deodorant product of Fig. 3 is to the clearance experimental result of ammonia, wherein,
The experimental result of expression charcoal; ■ represents the experimental result of our company's product; represents the experimental result of 0 company's product.
The time dependent deodorant product of Fig. 4 is to the clearance experimental result of front three ammonia, wherein,
The experimental result of expression charcoal; ■ represents the experimental result of our company's product; represents the experimental result of 0 company's product.
The clearance of Fig. 5 various deodorant products after 15 minutes compares, wherein,
Expression hydrogen sulfide; ■ represents ammonia; represents front three ammonia.
Fig. 6 deodorization material maximum material removal rate compares, the removal efficient of deodorization material after promptly 15 minutes, wherein,
The experimental result of expression charcoal; ■ represents the experimental result of our company's product; represents the experimental result of 0 company's product.
Fig. 7 a, Fig. 7 b, Fig. 7 c represent the symptom of being destroyed by ethene that occurs in the pears of east ' new ancient ', and wherein, Fig. 7 a represents that inside hinders; Fig. 7 b represents pericarp spot (severity); Fig. 7 c represents pericarp spot (bluring).
Effect in the new ancient pears that store in each freezer of Fig. 8 behind the use ethene treatment facility relatively
Fig. 9 a, the peach fruit surface appearance that Fig. 9 b handles with the ethene remover, wherein Fig. 9 a peach fruit surface appearance of representing to be untreated; Fig. 9 b represents the surface appearance with the peach fruit after our company's development product bag processing.
Figure 10 medium photo
The specific embodiment
The present invention is shaped the accessory substance red soil (Red Mud) and the mixture of activated carbon that generate behind the extraction alumina in the red bauxite with extruder, and under 70~120 ℃ of temperature conditions with continuous method drying, active metal salt is injected at last with the inorganic acid solution removal foreign body of 5~10 weight % in calcining back under 800~950 ℃ of reducing conditions.In Pickling Engineering, remove a large amount of impurity be positioned at flourishing red soil layer structure and open the pore of layer structure, and excessive iron ion is penetrated into makes it have firm pore structure in the pore, the specific area of red soil is increased considerably.Because active metal salt disperseed with the form of molecule or plated film at the pore of the red soil that has layer structure and the pore of activated carbon, physical absorption and chemisorbed are taken place simultaneously.Such composition not only is not subjected to the influence of moisture content, and has embodied adsorption efficiency and the adsorbance very high to polar molecule, nonpolar molecule, non-saturated fatty acid.Improve the invention of removing foul gas efficient and keeping the composition of gardening product freshness so the invention relates to.
Explain the manufacturing process of keeping gardening product freshness and freezer deodorant compositions again according to the present invention as follows:
Process 1: be moisture accessory substance red soil and activated carbon powder weight ratio, adjust the process of mixing with kneading type mixer behind water content 35~45 weight % with 60: 40.
Here moisture accessory substance red soil and activated carbon powder are put into kneading type mixer continuously, the last fully stirring with 80~120rpm speed mixing again for 2~3 times.At this moment water content 35~40 weight % are for the most suitable.
The diameter of the accessory substance red soil that uses in invention is preferably less than 1,60~50 weight % with whole compositions are fit to for the use amount of forming accessory substance red soil, its use amount can reduce adhesion during less than 50 weight %, reduce hydrophilic characterization of adsorption, can reduce the oleophylic characterization of adsorption when surpassing 60 weight %.
The specific area of activated carbon should be greater than 1000~1200m in addition
2/ g preferably uses surface area greater than 1200m
2The powdered activated carbon with the coconut meat manufacturing of/g also can have been used cigarette carbon system, charcoal system, activated carbon etc.Activated carbon use amount in the present invention is 50~40 weight % preferably, can reduce the oleophylic characterization of adsorption during its use amount less than 40 weight %, can reduce hydrophilic absorption property when surpassing 50 weight %, and be difficult to obtain wear-resisting granular composition.
Process 2: this process is the process that the composition that has mixed is shaped with extruder, and the size of formed body is to adjust according to purposes control nozzle, and extrusion temperature generally is controlled between 40~60 ℃.
Process 3: the composition that is shaped is placed on continuous drying in the fluidized bed drying machine, and temperature is to be fit to 70~120 ℃, and best temperature range is 80~100 ℃.The too high meeting of temperature makes formed body occur evenly splitting reduction intensity, and the time of drying can be long in the time of below 70 ℃.The water content that is fit to of dry postforming body is 5~10 weight %.
Process 4: as the process that dry formed body is calcined in the environment of reduction, suitable calcination time is under 800~950 ℃ of conditions 1~2 hour.Accessory substance red soil is sintered in calcination process, and the intensity of formed body reduces when the intensity of this process decision formed body, 800 ℃ of less thaies, exists when surpassing 950 ℃ because of destroying the shortcoming that pore structure reduces specific area.
Process 5: remove the silica gel that generates in the calcining and the process of impurity as pickling, composition is extracted under 40~80 ℃ of conditions with the inorganic acid solution of 5~10 weight % and pickling 2~6 hours.The inorganic acid that is fit in this process is hydrochloric acid, sulfuric acid, nitric acid etc.Inorganic acid and divalent and 3 valency molysite that the iron reaction that is contained in the calcined composition generates at absorption of the surface of formed body and plated film, improve adsorption capacity, strengthen stratiform mechanism skeleton.
Process 6: as the process of injecting active metal salt in the formed body after pickling, disperse plated film to have the pore of red soil of layer structure and the pore surface of activated carbon with molecular state, metal salt concentrations used herein is 20~18 weight %, and the most suitable is 10~15 weight %.The solution temperature that is fit to is 40~60 ℃, is separated into body and solution later in lasting 2~4 hours approximately, and is dry under 60~80 ℃ of conditions.Here so-called slaine is meant silver, lead, copper and molysite etc., wherein optional a kind or 2~3 kinds of slaines uses.
Composition by such manufacturing process manufacturing is as the criterion with solid, and accessory substance red soil accounts for 50~60 weight %, and activated carbon accounts for 50~40 weight %, and active metal salt is to be as the criterion 2~10 weight % for suitable with binder, and being more suitable for is 2~5 weight %.The injection rate of active metal salt can reduce absorption affinity during less than 2 weight %, and there is the worry of the pore that stops up activated carbon pore and red soil layer structure during greater than 10 weight % in injection rate.
Say that according to above-mentioned institute composition of the present invention reacts the back in many ways with the gas that becomes the stench reason to be removed, and removes ethene, ammonia, gases such as amino, hydrogen sulfide with this principle absorption and reaction.
The specific area of the composition among the present invention is greater than 500m
2/ g, greater than 50mg/g, greater than 50mg/g, greater than 320mg/g, abrasion resistance is more than 99% to the iodine energy of adsorption to the energy of adsorption of hydrogen sulfide to the energy of adsorption of ammonia.
Following the above-mentioned invention of saying is described in detail with example, but the present invention not only is confined to example.
Embodiment
Example 1
Accessory substance red soil (water content 40 weight % (weight), solids basis 6.0kg) and activated carbon powder (below 200 orders, 4.0kg) moisture content put into kneading type mixer after adjusting to 35 weight %, mix manufacturing body with the 5mm die extruder after 30 minutes with the speed of 80rpm.
The formed body of extruding is put into drying machine, drying is 2 hours under 105 ℃ condition, and after calcining 2 hours under 950 ℃ of reducing conditions, calcined material (9.5kg) was put into 5 weight % hydrochloric acid solutions (45 liters) 2 hours, temperature is 60 ℃, then be separated into body and solution,, then keep injecting 10 weight % ferric chloride solutions 4 hours with 1: 1 solids basis under 40 ℃ of conditions with 100 premium on currency washing formed body.Solid separates the water washing of back with discharging with solution, obtained the 18.5kg formed body in dry 4 hours at 90 ℃ of fluidized bed drying machines at last.
Example 2
Accessory substance red soil (water content 40 weight % (weight), solids basis 6.2kg) and activated carbon powder (below 200 orders, 4.3kg) moisture content put into kneading type mixer after adjusting to 35 weight %, mix manufacturing body with the 5mm die extruder after 30 minutes with the speed of 80rpm.
The formed body of extruding is put into drying machine, drying is 2 hours under 105 ℃ condition, and after calcining 2 hours under 950 ℃ of reducing conditions, calcined material (9.9kg) was put into 5 weight % sulfuric acid solutions (45 liters) 2 hours, temperature is 60 ℃, then be separated into body and solution,, then keep injecting 10 weight % copper-baths 4 hours with 1: 1 solids basis under 40 ℃ of conditions with 100 premium on currency washing formed body.Solid separates the water washing of back with discharging with solution, obtained the 18.8kg formed body in dry 4 hours at 90 ℃ of fluidized bed drying machines at last.
Example 3
Accessory substance red soil (water content 40 weight % (weight), solids basis 6.0kg) and activated carbon powder (below 200 orders, 4.0kg) moisture content put into kneading type mixer after adjusting to 35 weight %, mix manufacturing body with the 5mm die extruder after 30 minutes with the speed of 80rpm.
After the formed body of extruding put into drying machine, drying is 2 hours under 105 ℃ condition, and under 950 ℃ of reducing conditions the calcining 2 hours with, calcined material (9.45kg) was put into 5 weight % sulfuric acid solutions (45 liters) 2 hours, temperature is 60 ℃, then be separated into body and solution,, then keep injecting 10 weight % lead sulfate solution 4 hours with 1: 1 solids basis under 40 ℃ of conditions with 100 premium on currency washing formed body.Solid separates the water washing of back with discharging with solution, obtained the 18.4kg formed body in dry 4 hours at 90 ℃ of fluidized bed drying machines at last.
The characteristic of the formed body composition that obtains in (table 1) example
Distinguish | Example 1 | Example 2 | Example 3 | |
Form (weight %) | Red soil | ????45.87 | ????48.16 | ????46.64 |
Activated carbon | ????48.5 | ????46.3 | ????48.3 | |
Effective metal content | ????Fe?5.63 | ????Cu?5.14 | ????Zn?5.06 | |
Hardness (%) | ????99 | ????99 | ????99 | |
Specific area | ????520 | ????525 | ????523 |
Example 4
We have carried out hydrogen sulfide, ammonia, the sweetening power comparative experiments of trimethylamine to his company's deodorant of just selling on the market with my company's development product.Comparison other is the freezer deodorant of 0 company, and charcoal and my company's development product have been transformed 5L Tetrabag according to Batch-Test sweetening power experimental technique, and deodorization object and deodorant are inserted, and mixes, and stirs, and tests time dependent concentration.Test analysis has used the gas of Japanese gastack to detect machine and detector tube.
Time dependent deodorant product is to the clearance (unit: ppm) of hydrogen sulfide in (table 2) example 2
Distinguish | Charcoal | Our company's product | 0 company | |
Initial stage concentration | ????180 | ????180 | ????180 | |
After 15 minutes | Concentration | ????164 | ????49 | ????67 |
Efficient (%) | ????8.9 | ????72.8 | ????62.8 | |
After 60 minutes | Concentration | ????120 | ????10 | ????27.5 |
Efficient (%) | ????33.3 | ????94.4 | ????84.7 |
In time deodorant product is to the clearance (unit: ppm) of ammonia in (table 3) example 2
Distinguish | Charcoal | Our company's product | 0 company | |
Initial stage concentration | ????60 | ????70 | ????56 | |
After 15 minutes | Concentration | ????46 | ????4 | ????36 |
Efficient (%) | ????23.3 | ????94.3 | ????35.7 | |
After 60 minutes | Concentration | ????40 | ????2 | ????28 |
Efficient (%) | ????33.3 | ????97.1 | ????50 |
(table 4) deodorant product class trimethylamine clearance in time
(unit: ppm)
Distinguish | Charcoal | Our company's product | 0 company | |
Initial stage concentration | ????192 | ????160 | ????200 | |
After 15 minutes | Concentration | ????141 | ????10 | ????88 |
Efficient (%) | ????26.56 | ????93.7 | ????56.0 | |
After 60 minutes | Concentration | ????122 | ????4 | ????73 |
Efficient (%) | ????36.5 | ????97.5 | ????63.5 |
(table 5) removal efficient of deodorant product after 15 minutes
(unit: ppm)
Distinguish | Charcoal | Our company's product | 0 company | |
Hydrogen sulfide | Efficient (%) | ????9 | ????73 | ????63 |
The maximal efficiency contrast ratio | ????0.12 | ????1.00 | ????0.86 | |
Ammonia | Efficient (%) | ????23 | ????94 | ????36 |
The maximal efficiency contrast ratio | ????0.24 | ????1.00 | ????0.37 | |
Front three ammonia | Efficient (%) | ????36 | ????98 | ????64 |
The maximal efficiency contrast ratio | ????0.37 | ????1.00 | ????0.65 |
Example 5
For removing the ethylene gas that gardening product produces, check is installed in the performance of our company's product on the machine, loyal Nanjing University learns department of horticulture and utilizes the ethene removal device new ancient pears to be carried out removing the experiment of ethene, the result has reduced the pericarp spot and the inside of certain degree and has hindered, and can keep freshness for a long time.Be to be experimental subjects with ' new ancient ' pears below, remove the result who obtains behind the ethene, this paper is published in the U.S. gardening association journal.
Remain at ethylene concentration that the investigation result after 2 months shows that the pericarp spot has all appearred in most of fruit and reaction is hindered in inside under the condition of 10ppm.After the mutually anticaustic machine that our company's product is installed is removed ethene, occurred having only the inside of 5% pericarp spot and 10% to hinder, so let us remove the important factors that ethene is the preservation fruit as can be seen.
[table 6] removes the influence of ethene to the physiology generation of new ancient pears
Distinguish | The pericarp spot | Inside is hindered |
Remove ethene (ethene treatment region) | ????5% | ????10% |
Ethene disaster (8.8-10.2ppm) | ????90% | ????100% |
The A freezer of not removing ethene shows that with the investigation result of the B freezer of having removed ethene in the same time period murder degree of A freezer approximately is 3 times of B freezer.And the pears of producing in same farmers' are increased to 58.2% along with spot that the variation of time occurs in freezer, and the spot that occurs in the pilot freezer of removing ethene is about 7.2%.
Example 6
Remove effect in order to examine ethene, after the Bai Taoyong PVC plastics vacuolar membrane of harvesting just packing, placed 5 days, compared the fruit hardness in the ethene removal and the district of being untreated at normal temperature.The hardness of ethene treatment region is 0.56kg, and is high more about 12% than the hardness 0.5kg that is untreated, so be the treatment effect that object has been examined development with Huang Tao.
In experiment, the yellow peach in the good garden of the length of harvesting just is divided into two groups according to the look state.Uncoloured crude fruit and painted mellow fruit were object at storage in 4 ℃ after 15 days, and normal temperature condition exposes down, gives selling term, by each phase analysis quality.
Just the immature friut and pericarp color of harvesting is deep green, but after normal temperature exposed 3 days, the leaf green minimizing had appearred in each stage, and yellow thickens, and has red phasic Chang a little.Thereupon the HUE value also from bottle-green 100.91 change to untreated 89.17 and treatment region 93.12.What can relax change in color because of our company's development product has proved its effect.But hardness does not have too big difference, and the deviation ratio of the fruit that usefulness our company development product is handled is bigger.The effect that generally speaking stores back removal ethene is apparent in view, but the result that hardness is kept effect has appearred reducing in the normal temperature exposure after 3 days.Inconsistent about the difference of the influence of pol being managed throughout the district, but acid content is kept than higher in treatment region, and the taste of fruit and quality seem fine.
Though the ethene generation rate of fruit is inconsistent, the ethylene concentration of treatment region is lower on the whole, and the respiratory rate of treatment region significantly is not inclined to.Significantly characteristics are when normal temperature exposes under untreated situation, often take place because of rotting or the rotten phenomenon that reduces commodity of pulp.Such phenomenon is rare in the ethene treatment region, can produce effect very much to keeping the fruit freshness by determination processing ethene from such phenomenon.That is, be that object carries out ethene when suppress handling with immature yellow peach, can keep very high hardness, proved that our company's product can delay the effect that pericarp variable color etc. keeps freshness.
Composition among the present invention has very flourishing tiny pore, physical absorption and chemisorbed can take place simultaneously, because adsorption capacity and removal efficient height, for organic solvent class, toxic gas (ammonia, hydrogen sulfide, trimethylamine) and very outstanding, and at freezer to the adsorption capacity that makes the aging hormone ethylene gas of plant with also very useful in the application of deodorant, freshness retention agent and air cleaning deodorization filter material.
Claims (6)
1. the manufacturing process that keeps the composition of freezer and gardening product freshness, it comprises, after red bauxite accessory substance red soil and activated carbon mixed with water content 30~45 weight %, be shaped with extruder, and it is dry under 70~120 ℃ of temperature conditions, calcining back obtains the composition of deodorant and maintenance gardening product freshness thus with the inorganic acid pickling and inject 2~10 weight % active metal salts under 800~950 ℃ of conditions.
2. manufacturing process as claimed in claim 1, the specific area of wherein said composition are 500m
2More than/the g, the ammonia energy of adsorption is more than the 50mg/g, and the hydrogen sulfide energy of adsorption is more than the 50mg/g, and the iodine energy of adsorption is more than the 320mg/g, and abrasion resistance is more than 99%.
3. manufacturing process as claimed in claim 1 is characterized in that, the composition of described composition is 40~60 weight % red soil, 30~50 weight % activated carbon, 2~10 weight % active metal salts.
4. manufacturing process as claimed in claim 1, wherein said inorganic acid are sulfuric acid, hydrochloric acid or nitric acid, and solution concentration is 5~10 weight %.
5. manufacturing process as claimed in claim 1, wherein said active metal salt are silver, lead, zinc, copper or molysite.
6. by the composition that freezer and gardening product are carried out deodorization and keep freshness and can use on air purifier of the manufacturing process manufacturing of claim 1.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR18262/2004 | 2004-03-18 | ||
KR1020040018262A KR100566777B1 (en) | 2004-03-18 | 2004-03-18 | Formation for deodorizing and maintaining freshness of a garden plant |
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CN1669636A true CN1669636A (en) | 2005-09-21 |
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Application Number | Title | Priority Date | Filing Date |
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CNA2004100079715A Pending CN1669636A (en) | 2004-03-18 | 2004-03-23 | Composition of keeping ice house and horticulture production fresh and its manufacturing technics |
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KR (1) | KR100566777B1 (en) |
CN (1) | CN1669636A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103068682A (en) * | 2010-06-01 | 2013-04-24 | 佩福知识有限责任公司 | Package for preserving respiring produce and apparatus for making the same |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101258092B1 (en) * | 2012-11-23 | 2013-04-25 | 태성건설 주식회사 | Deodorant agent |
-
2004
- 2004-03-18 KR KR1020040018262A patent/KR100566777B1/en not_active IP Right Cessation
- 2004-03-23 CN CNA2004100079715A patent/CN1669636A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103068682A (en) * | 2010-06-01 | 2013-04-24 | 佩福知识有限责任公司 | Package for preserving respiring produce and apparatus for making the same |
Also Published As
Publication number | Publication date |
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KR20050093044A (en) | 2005-09-23 |
KR100566777B1 (en) | 2006-04-03 |
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