CN1039830A - The method and apparatus of preparation gelatin corpuscle jelly - Google Patents
The method and apparatus of preparation gelatin corpuscle jelly Download PDFInfo
- Publication number
- CN1039830A CN1039830A CN 88104639 CN88104639A CN1039830A CN 1039830 A CN1039830 A CN 1039830A CN 88104639 CN88104639 CN 88104639 CN 88104639 A CN88104639 A CN 88104639A CN 1039830 A CN1039830 A CN 1039830A
- Authority
- CN
- China
- Prior art keywords
- gelatin
- jelly
- nozzle
- pressurized air
- corpuscle
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Images
Landscapes
- Jellies, Jams, And Syrups (AREA)
Abstract
The present invention relates to a kind of method and apparatus for preparing gelatin corpuscle jelly, described method is characterised in that with pressurized air to be power, and the gelatin liquid that contracts is deeply from bottom to top blown out a certain size granule type jelly.Described equipment mainly comprises the nozzle that at least one can make the ejection of gelatin concentrated solution, is arranged at the pressurized air ingress pipe of nozzle below and surrounds described nozzle and the pressurized air importing mouth of pipe and upwardly extending collection air channel.Method and apparatus provided by the invention can directly utilize pressurized air that gelatin is blow molded into usually the jelly of required 2.0-2.5mm particle diameter, can directly be dried into commercial gelatin, need not pulverize and sieve.
Description
The present invention relates to prepare the method and apparatus of gelatin corpuscle jelly.
As everyone knows, using more general gelatin jelly forming method at present is that the gelatin concentrated solution is cooled to below the condensing temperature, make strong solution form certain exsiccant jelly shape that helps simultaneously, gelatin after the moulding freezes and is generally strip, rectangular etc. as short beggar's bar or irregular circle, resulting like this jelly bar must be pulverized and be sieved after drying, brought technologic inconvenience, in addition, owing to can produce a part of fine powder when pulverizing, this fine powder can bond agglomerating in use, often needs to granulate again, has caused certain waste.
Disclosed a kind of granules preparation technology that can be used for manufacturing of gelatin among the Chinese patent application GK86106504, its specific practice is in granulation zone liquid ingredient to be distributed on the solids, then will become undersized particle from the particle separation of granulation zone, the particle of less qualified size, the particle logistics of the particle of bigger qualified size and oversized dimensions, and improperly sized particle is recycled to granulation zone, this method technology is complicated, and solid-liquid two-phase blended process is arranged, the oven dry rear surface is bigger and rough, also must sieve again.
United States Patent (USP) the 3rd, 886 has disclosed a kind of production method and equipment of gelatin spherolite No. 086, whole granulating process is carried out in a post, and the top of post is gas-phase reagents, and the bottom is then filled with liquid phase reagent, be generally oil, the gelatin drop from post from top to bottom, the cooling curing balling-up.But the prepared gelatin grain of this method surface contamination oil is so general anorexia is used.
The purpose of this invention is to provide a kind of method for preparing gelatin corpuscle jelly convenient and simplely.Another object of the present invention provides a kind of equipment of implementing the method for gelatin corpuscle jelly moulding.
The objective of the invention is to be accomplished: a kind of method for preparing gelatin corpuscle jelly by following design, comprise that gelatin solution concentrates and the preparation of corpuscle jelly, the preparation method of described corpuscle jelly mainly comprises with pressurized air being power, the gelatin concentrated solution is from bottom to top blown out a certain size granule type jelly.
Above-mentioned compressed-air actuated pressure is generally 1-10kg/cm
2, be preferably 2-5kg/cm
2, temperature is generally 2-30 ℃, is preferably 5-15 ℃, and humidity is generally 20-50%, is preferably 30-40%.
A kind of equipment of implementing above-mentioned method that is exclusively used in mainly comprises the nozzle that at least one can make the ejection of gelatin concentrated solution, is arranged at the pressurized air ingress pipe of nozzle below, and surrounds described nozzle and the pressurized air importing mouth of pipe and upwardly extending collection air channel.
Described nozzle is other can be provided with a lever regulating mechanism.Described collection air channel by spraying plating the steel plate of tetrafluoroethylene or trifluorochloroethylene film form.
Advantage of the present invention and effect are tangible, the method for preparing gelatin corpuscle jelly that it provided, can directly utilize pressurized air gelatin to be blow molded into the jelly of required usually 2.0-2.5mm particle diameter, can in general dryer, dry commercial gelatin, so just remove pulverizing required usually in the prior art and the operation of sieving from, simultaneously, also avoided the generation fine powder, resulting gelatin dissolves convenient in water, can satisfy edible and industrial needs.And the specific equipment of preparation gelatin corpuscle jelly provided by the present invention, it is simple in structure, and is easy to operate, can produce gratifying gelatin corpuscle jelly.
Below, with in conjunction with the accompanying drawings and by to the description of specific embodiment and further illustrate advantage of the present invention and effect.
Fig. 1 is the synoptic diagram of equipment of the present invention.
Fig. 2 is the synoptic diagram of the another form of equipment of the present invention.
With reference to Fig. 1, equipment of the present invention mainly comprises the jar 1 that holds the gelatin concentrated solution, divide the nozzle 2 that is arranged, connect the pipeline 3 between jar 1 and the nozzle 2, the valve 4 that is provided with in the pipeline 3, be arranged at the pressurized air ingress pipe 5 of nozzle 2 belows, valve 6 that is provided with in the pressurized air ingress pipe 5 and pressurized air import the mouth of pipe 7, surround the collection air channel 8 that described nozzle 2 and pressurized air import the mouth of pipe 7.
With reference to Fig. 2, equipment of the present invention mainly comprises the jar 1 that holds the gelatin concentrated solution, the liquid level visor 9 of tank skin arranged outside and thermometer 10, the insulation jacket layer 11 that tank wall is provided with, divide the nozzle 2 that is arranged, the nozzle 2 other tapered rods 12 that are provided with, the lever 13 that joins with tapered rod 12, but and the lever shaft 14 of adjustment (adjusting) lever 13, connect jar 1 and nozzle 2 between pipeline 3, the valve 4 that is provided with in the pipeline 3 is arranged at the pressurized air ingress pipe 5 of nozzle 2 belows, valve 6 that is provided with in the pressurized air ingress pipe 5 and pressurized air import the mouth of pipe 7, the spur rack 15 that is connected with pressurized air ingress pipe 5 with the pinion(gear) 16 that spur rack matches, surrounds the collection air channel 8 that described nozzle 2 and pressurized air import the mouth of pipe 7, the small fan 17 that collection 8 belows, air channel are provided with connects the flanged plate 19 that collects air channel 8 and small fan 17.
Described jar 1 with respect to nozzle 2, generally adopts the form of high level tank, otherwise, need add a pump in addition so that the gelatin concentrated solution is extruded from nozzle 2, jar 1 volume is generally 1.5-2M
3; The quantity of nozzle 2 is at least one, but but tens of as many as, its bore is generally 2-2.5mm; The caliber of pipeline 3 is generally φ 30-50mm, the caliber of pressurized air 5 is generally φ 20-40mm, the material in collection air channel 8 has generally adopted to the indifferent spraying plating of gelatin glue the steel plate of tetrafluoroethylene or voltalef film, and its shape can be upwards expansion (tubaeform).The specification of small fan 17 is generally 12 inches, and the specification of all the other component and material all can adopt known in the art.
The effect of small fan 17 is upwards to rouse cold and the exsiccant air, assistance jelly moves upward, and become para-curve from collection air channel 8, to dish out, because of with spraying plating do not have avidity between the made collection air channel 8 of the steel plate behind tetrafluoroethylene or the voltalef film and the gelatin, wind path wall also is difficult for bonding thereon even pellet shapes jelly is run into collection.
Concrete working method is such: the gelatin solution after will concentrating imports jar 1 by pipeline 20, can observe the amount that it enters jar 1 by the set liquid level visor 9 of tank wall, the temperature of gelatin solution can be by the thermometer measure of tank wall setting, and can regulate water temperature in the insulation jacket layer, make the gelatin in jar 1 can the condensation caking.Open valve 4, then concentrating gelatin solution can flow out from nozzle 2, open valve 6 simultaneously, then pressurized air blows out from the pressurized air importing mouth of pipe 7, and 2 effusive gelatin concentrated solutions of nozzle are blown be broken into erose drop, the quantity of nozzle 2 is consistent with the quantity that pressurized air imports the mouth of pipe 7, and each pressurized air imports the mouth of pipe 7 and aims at a nozzle 2, and the pressure of the air that is sprayed is generally 1-10kg/cm
2, be preferably 2-5kg/cm
2Temperature is generally 2-30 ℃, be preferably 5-15 ℃, humidity is generally 20-50%, be preferably 30-40%, the upper-lower position that pressurized air imports the mouth of pipe can be regulated spur racks 15 liftings by rotation pinion 16 and determine, and pressurized air just in time can in time be blown nozzle 2 effusive gelatin concentrated solutions be broken into irregular drop, utilize the bigger surface tension of gelatin concentrated solution that the instantaneous pellet that is punctured into diameter 2-2.5mm of irregular drop is cooled into simultaneously and be jelly.
The size of jelly can obtain needed by the caliber size of direct change nozzle 2, also can regulate the position that tapered rods 12 enter nozzle 2 by lever 13 and regulate, and certainly, compressed-air actuated pressure size also can be regulated the jelly particle diameter.
Resulting jelly particle can directly place general dryer commonly used oven dry to form required gelatin corpuscle, can dailyly eat and industrial application, and need not pulverize or sieve. This shows that advantage of the present invention and effect are obvious.
Claims (7)
1, a kind of method for preparing gelatin corpuscle jelly, comprise that gelatin solution concentrates and the preparation of corpuscle jelly, the preparation method who it is characterized in that described corpuscle jelly mainly comprises with pressurized air being power, the gelatin concentrated solution is from bottom to top blown out a certain size granule type jelly.
2, the method for claim 1 is characterized in that described compressed-air actuated pressure is 1-10kg/cm
2, be preferably 2-5kg/cm
2
3, the method for claim 1 is characterized in that described compressed-air actuated temperature is 2-30 ℃, is preferably 5-15 ℃.
4, the method for claim 1 is characterized in that described compressed-air actuated humidity is 20-50%, is preferably 30-40%.
5, a kind of equipment of implementing the described method of claim 1 that is exclusively used in, it is characterized in that it mainly comprises the nozzle that at least one can make the ejection of gelatin concentrated solution, be arranged at the pressurized air ingress pipe of nozzle below and surround described nozzle and the pressurized air importing mouth of pipe and upwardly extending collection air channel.
6, equipment as claimed in claim 5 is characterized in that the other lever regulating mechanism that is provided with of described nozzle.
7, equipment as claimed in claim 5, it is characterized in that described collection air channel by spraying plating the steel plate of tetrafluoroethylene or voltalef film formed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 88104639 CN1039830A (en) | 1988-07-25 | 1988-07-25 | The method and apparatus of preparation gelatin corpuscle jelly |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 88104639 CN1039830A (en) | 1988-07-25 | 1988-07-25 | The method and apparatus of preparation gelatin corpuscle jelly |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN1039830A true CN1039830A (en) | 1990-02-21 |
Family
ID=4833086
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 88104639 Pending CN1039830A (en) | 1988-07-25 | 1988-07-25 | The method and apparatus of preparation gelatin corpuscle jelly |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1039830A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110403057A (en) * | 2019-08-14 | 2019-11-05 | 陈蜀乔 | A kind of novel edible manufacturing of gelatin technique and process units |
-
1988
- 1988-07-25 CN CN 88104639 patent/CN1039830A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110403057A (en) * | 2019-08-14 | 2019-11-05 | 陈蜀乔 | A kind of novel edible manufacturing of gelatin technique and process units |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US3408169A (en) | Pan granulation | |
| US3619293A (en) | Granular sucrose products and process for producing same | |
| JPH06254382A (en) | Production of microcapsule and its apparatus for production | |
| CN1039830A (en) | The method and apparatus of preparation gelatin corpuscle jelly | |
| CN100500634C (en) | Sodium butyrate-containing chemical product production technology | |
| CN101709010A (en) | Control system for viscosity of compound fertilizer slurry | |
| CN1087727C (en) | Method for producing crystalline D-sorbitol | |
| CN203855523U (en) | Preparation device of calcium ammonium nitrate | |
| US4263012A (en) | Method of granulation of sulfur | |
| CN109608509B (en) | Continuous preparation method of granular isomalt | |
| CN2683240Y (en) | Spray column-fluidized bed pelletizer | |
| CN209865974U (en) | Top-spraying granulation fluidized bed of collapse-proof bed | |
| JP3322766B2 (en) | Method for producing granulated brown sugar | |
| CN208349890U (en) | Underwater pelletizer pelletizing water heat-exchange system | |
| CN207324730U (en) | Calcium nitrate granulation tower | |
| CN112811964A (en) | Method for preparing secondary element fertilizer by using mother liquor without drying | |
| CN101433814A (en) | Spray cooling and granulating technique for geoceric acid or hydrogenatedoil | |
| CN1067673C (en) | Process for preparing crystalline sorbitol powder | |
| JPH1192424A (en) | Production of neopentylglycol hydroxypivalate granule, neopentylglycol hydroxypivalate granule, and use of apparatus for granulation of the same | |
| CN110734320A (en) | Urea magnesium sulfate fertilizer and preparation method thereof | |
| CN1204621A (en) | Production process technology and device of granular lithium chloride | |
| CN212417867U (en) | Fluidized bed workbin and horizontal or spraying fluidized bed | |
| CN211273594U (en) | Extraction drying device for preparing amino acid trace element mineral substance by biological enzyme method | |
| US20090197085A1 (en) | Organic nanoparticles and method of preparation thereof | |
| CN220238486U (en) | Granulating device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C01 | Deemed withdrawal of patent application (patent law 1993) | ||
| WD01 | Invention patent application deemed withdrawn after publication |