CARBONATED DRINKING WATER GENERATOR USING CYCLIC COMPRESSION SYSTEM

31-03-2016 дата публикации
Номер:
KR1020160035155A
Принадлежит:
Контакты:
Номер заявки: 01-14-102025947
Дата заявки: 22-09-2014

[1]

Integer such as refrigerator the present invention refers to the frames are arranged in carbonated water by contact of water with carbon dioxide and consequently for producing drinking carbonated water prevents the loss, in particular carbon dioxide is dissolved in water to circulation is repeatedly set by means of compression system for the composed of metals such as Cu, in a short time the carbonated water by one so that a work process is formed inside the tie..

[2]

Carbonated water carbonate refers to water containing gas to, and believed unique bag before drinking the tea, carbonated water in addition to the in the stimulating mucosal membranes mouth carbon dioxide is to generate needle first and the field of force help digestion promotion is applied to an, the expansion field to help market motion a starting switch enables the diet or diet constipation such as several advantages are obtained due to user for drinking carbonated water the interior of wet liquid to flow down is diffused.

[3]

In particular, direct at home, the for producing carbonated water carbonated water drinking by adding water integer such as refrigerator manufacturing machine provided line discharges the following steps using the dispenser a drink, it is proposed.

[4]

Such a device for manufacturing carbonated water, raw water (water filter via water is integer) which is supplied with a stored on the essence tank is fitted to the prepared, carbonic acid gas for storing the gas barrel having gas for storage tank and gas infusion line is characterized by connecting a raw water having storage tank immersed in a gas ionizing support spring for video tape cassette from the state that an injected through the infusion line is forming a carbonated water.

[5]

The, gas infusion line immersed in storage tank end of a water-immersion be structure to sufficiently fill the carbon dioxide and water of the invention is to be well to water and carbon dioxide, a carbon dioxide not being available for absorption while a storage tank and moved in a longitudinal over time while dissolving in water concentration of carbonated water is higher in the recording operation..

[6]

I.e., device of the existing method for producing carbonated water Figure 1 as shown in storage tank (100) to an integer supplied raw water having won (200) for supplying a raw water is connected to the raw water line (20) disposed on the raw water inflow the installing a fuel injection valve to be closed and opened to control the, carbonic acid gas is stored a gas (300) is stored tank (100) and the gas infusion line (30) is produced by storage tank are made and another new gas injection carbonate, storage tank (100) has a dispenser (D) exhaust line direction (50) the discharge carbonated water by forming a, storage tank (100) the exhaust means (60) mounting remaining carbonate. constructed which performs simultaneous venting of gases.

[7]

Such pluralities structure for operating device for manufacturing carbonated water performance to the surface of glass raw water through a constant-temperature storage tank, supply water to fifth silicon nitride layer, for the injection of an carbon dioxide carbon dioxide filled storage tank the pressure within the reactor housing is a sudden rise, time eight stipendiary son to raw water carbon dioxide c language so as to penetrate through while is higher in concentration carbonate is produced is carbonated water.

[8]

The, within the storage tank as a temporarily such that a higher pressure carbonate the gas to the gas injection device are sequentially scanned using explosion generates if the carbonic acid gas followed by producing a, thus high concentration carbonated water in order to produce ( nativity acid) periodically injected into carbonic acid gas which is thin, thus introducing a carbonic acid gas about interval of the interval nativity carbonated or non-carbonated which the number of steps can be density control acid..

[9]

And the thus produced planar metallised textile structure is discharged through a dispenser carbonated water, until level etection is carbonated water is ejected been exhausted exhaust means (60) making open a to allow gas to exit remaining carbonate water while after desalination back to storage tank, said is perform a making method of the recording operation..

[10]

However, carbonic acid gas problems device for manufacturing carbonated water drinking such water that occurs naturally in absorbable time pending carbonated water is be obtained, creating a carbon dioxide is of the wafer is not stably dissolved in water as well as, dissolution time is too positioned a problem that the recording operation..

[11]

I.e., recorded in the machining program manufacturing a constant-temperature storage tank, to an event that both a carbonated water is exhausted after the long time (drinking for producing carbonated water device with 30 minute or more generally in the case of refrigerator) are allocated, at multiple channels/levels ready to use in a one since, during exhaust stream, such as internal low of sound boil a carbonated water thus had carbonated water is inserted into at least one additional mold foaming die equipment in use, nail or otherwise (of food in within job removing applications or add adhesive to fluids until the carbonated water is used, which) to rapid to be used when needed if so, a..

[12]

In particular, high concentration of carbonated water produce a carbonic acid gas as described above for periodically injecting the time information is is is carbonated water the longer the length becomes has a risk is more the compressed spring increases and accepts the..

[13]

As well as, for producing carbonated water thus the manner in which the carbonic acid gas signal power is out of the range catalytic compounds is therefore, its solubility with residual not medium and a time shift is performed to water and the carbonic acid gas, herein, the tooth profile has an thus significant amount of carbonic acid gas followed by producing a used gas quantity carbonate with adjacent to the Bulletin window is a problem of the n is the fixed number more than..

[14]

In particular, in producing a repeatedly carbonated water to carbonated water is exhausted in order supply raw water through storage tank within the storage tank as a pressure with reduced fed raw water through in which, during this process carbonated water for preparing and a constant-temperature storage tank, inflows through the of carbon dioxide exhaust means through the two time data are into the air which are carbonic acid gas thereby, since key input gas is main.

[15]

Thus the present invention refers to carbon dioxide and water using carbonated water during the of carbon dioxide dissolved mounted between a bottom of the first the same concentration reference carbonated water used in fabricating carbon dioxide usage, reducing the risk of carbon dioxide after finishing the state, in the circulation gas and water carbonate repeated multiple times by compression system for re-compression the upper plates for producing carbonated water forwardly is formed inside the tie. can be.

[16]

To this end the present invention refers to a storage tank for storing carbonated water line supplied to integer source line supplied immersion liquid is connected to the gas line and gas injection line is branched into integer integer source gas are each coupled to the storage tank and to integer water carbonate gas is supplied to storage tank while dissolving in water carbon dioxide comprises is for producing carbonated water, storage tank water and carbonic acid gas housing includes a suck-in while forming a circulation line that re-supplies a the circular line circulation pressure pump and suction line circulated as the mounted orifice the water-and carbon dioxide storage tank than the orifice in the relatively high pressures, the valve member is dissolved in water to carbon dioxide is while passing through the connector the to material supply storage tank, such compression action performed iteratively efficiency dissolution of the carbonic acid gas by height in a short time that can be carbonated water is formed inside the tie..

[17]

Furthermore, said water circulates through the storage tank mounted porous block the circulation line via a line in the circulation water process comprises dispersion of particles, comes into contact with carbon dioxide and water surface or a dissection pattern carbonic acid gas dissolver a state of horizontally being laid down more efficiency.

[18]

Thus the present invention refers to water with carbon dioxide and consequently after the supply a constant-temperature storage tank, repeatedly set by means of circulating system to be recycled to a high carbonic acid gas is provided to circulate by the pressure in can be dissolved in raw water forcefully and re-compression by applying very group consisting of carbonated water can be shortened and, the carbonated water stored in the storage tank-HEMT having inverted both a maximum gray scale to reuse after the carbonated water stored in a hard disk drive or memories in case of a non the system is very is enabled.

[19]

Furthermore, high concentration of carbonated water ( nativity acid) even when the compression by pumping repeatedly brings about shortening in the production time carbonated water since the, manufacturing in a short time regardless concentration thereby, the water the recording operation. may.

[20]

Furthermore, water is fed with carbon dioxide and consequently SnO 1 in the process where the oil is dissolved in water to carbon dioxide after time for producing carbonated water supplied to a can be shortened further more, by surface area of particle in porous block solubilized height by improving the efficiency circulation line endless from by means of, a re-compression in the process where the oil nearly any raw water of carbon dioxide to carbonic acid gas residual the stipendiary son the rotation central and a loss thereof is small is carbonic acid gas as well as the support spring for video tape cassette replacement parallel reduction of the construction cost, resource be able to reduce exhaustion is.

[21]

Figure 1 shows a device for manufacturing carbonated water drinking of the existing method also coarse indicative of the structure of Figure 2 shows a coarse indicative of the structure compression system circulation of the present invention also Also 3 and another of the present invention also in the embodiment according to Figure 4 shows a circulation compression system coarse indicative of the structure

[22]

Hereinafter accompanying drawing the present invention based on detail the. off at the first and the second.

[23]

Also 2 as shown in the present invention refers to purified water is stored integer won (200) a gas is stored gas carbonate (300) a supply line (10) stored tank (100) and connecting the axial fan to an, supplied immersion liquid line (10) a the the essence (20) and gas injection line (30) comprising the [...] integer to won (200) and gas (300) are each coupled to storage tank by (100) carbon dioxide and the integer register water to the carbonated water that can be to, said storage tank (100) gas recovering section (40a) and a liquid recovering section (40b) by the withdrawal of a treatment fluid and carbonic acid gas and water stored tank (100) is supplied back into a circulation line (40) is formed, the circular line (40) the circulation pressure pump (41) the to, and recovering water with carbon dioxide and consequently, a cover (40), so the apparatus controls the flow the an orifice (42) mounting suction by fixing an the water-and carbon dioxide storage tank (100) than the orifice in the relatively high pressures, the valve member (42) while passing through the connector compression induction-in is done, in the process carbon dioxide by pressure on the water is formed inside the tie. dissolve in.

[24]

Thus integer won (200) supplied from an purified water storage tank (100) supplied to water to fifth silicon nitride layer, for the injection of an carbon dioxide carbon dioxide filled storage tank (100) is a sudden rise the pressure within the reactor housing eight time stipendiary son to raw water carbon dioxide where it is heated, a cover state (40) of pressure pump (41) operated when gas recovering section (40a) and a liquid recovering section (40b) carbonic acid gas through orifice and the water is drawn (42) after the, storage tank (100) which is supplied back into, said circulation compression action are performed to iteratively to produce carbonated water storage tank (100) remaining in the residual carbonic acid gas which forces includes a plurality of domes like of un-dissolved carbonic acid gas is dissolved in water to [...] efficiency height in a short time that can be carbonated water is formed inside the tie..

[25]

Furthermore, carbonic acid gas and the water orifice (42) after the high pressure on the circulation line is located at a predetermined position in vibrated while injection, the water particles and carbonic acid gas, contacting area among waste to dissolve efficiency can be which is used, thus a cover (40) through the a carbonic acid gas and the water storage tank as they are formed foam the foamed extrudate is conducted within further gas mixing carbonate is formed inside the tie. to derive.

[26]

The, said circulation line (40) the supply line (10) connected to be one line to share a as possibly, storage tank (100) in such a manner that the end connected to storage tank (100) positioned at the lower end of the when the circulation line (40) via a carbonic acid gas and the water storage tank (100) while they are being fed material on both sides of produces a large foam can make forming, and then the foam by carbonic acid gas dissolver can be increased by efficiency is.

[27]

Furthermore, said circulation line (40) a gas recovering section (40a) and a liquid recovering section (40b) into separate line patterns are formed by developing, gas recovering section (40a) to the storage tank (100) while configured on the upper end of liquid recovering section (40b) a storage tank (100) carbonate portion in the direction of lower end of each gas and water which can be recovered in, the, said gas recovering section (40a)-recovered orifice (43) suction by fixing an mounting a carbonic acid gas by regulating the flow rate of total circulation line (40) in flow rate of recovering section (40a) and a liquid recovering section (40b), and is then drawn into a a flow proportion of side polymers may be adjusted which comprises, the recovery orifice (88 80000393888) the flow rate of circulation line (40) a piece (42) flow rate of 50% contrast 1:1 gas and water carbonate when formed at rates of compression is recovering, and formed at one end of is it can.

[28]

Furthermore, said gas injection lines (30) orifice (42) from the flow rate higher than a transition temperature of the auxiliary orifice (70) when a gas infusion line (30) carbonic acid gas high pressure lower flowrates through c language so as to penetrate through injected raw water line (20) of mixing raw water having comprises supply [...] is made, in the process carbon dioxide while material permeated raw water 1 is occurs predominantly in the difference.

[29]

I.e., carbonic acid gas auxiliary orifice (70) via a carbonic acid gas is injected immediately after see you particles and water with an mixing finished product is carbonate surface area of contact extends the gas and water grains is promoted under carbonic acid gas dissolver while the recording operation..

[30]

Thus thus dissolved difference 1 after the storage tank (100) and is energized gas and water carbonate to forming a carbonated water is carbonated water for producing of shortening the time is it can.

[31]

On the other hand, a constant-temperature storage tank, carbonic acid gas followed by producing a temporary such that a higher pressure carbonate the gas to the gas injection device are sequentially scanned using explosion generates carbonic acid gas followed by producing a periodically repeated of carbon dioxide rather than by implanting ( nativity acid) is to produce a high concentration carbonated water to preferably, the storage tank and circulation by compression system (100) and an effluent discharge port formed therein rapidly connected carbonic acid gas introducing a nativity carbonated or non-carbonated about reducing the distance interval acid density control in a short time. which the number of steps can be.

[32]

Water thus produced and a storage tank (100) (D) dispenser to exhaust line direction (50) by forming a (D) dispenser user through a simple manner by means of the opening/closing valve is may be used in, carbonated water is storage tank (100) until level etection in capacity is been exhausted exhaust means (60) making open a remaining carbonate to allow gas to exit after desalination back to storage tank raw water through while, said is perform a making method of the recording operation..

[33]

The, said exhaust line (50) the water regulator (51) the storage tank and mounting (100) relatively in the low pressure end to discharge the carbonated water to, same line (50) open/close valves 102a, 102b (52) the-atmospheric pressure to controlling the discharge of carbonated water is formed inside the tie..

[34]

Furthermore, also 3 said, such as a cover (40) to porous block (44) holding water circulation line (40) via pixel block having a predetermined size in water dispersion of particles purpose: it is, water dispersed comes into contact with carbon dioxide and by particles such as impurities, fillers water surface or a dissection pattern carbonic acid gas dissolver can be efficiency the recording operation..

[35]

I.e., porous block (44) a charge of water m micro 5 particles (microns) small particles of water into this cable, the hereinafter, the second foam so as to be decentralized in the end to, water particles and carbonic acid gas structure to sufficiently fill the with carbon dioxide and consequently better mixing and achieve high thermal destruction of. be taken.

[36]

The, said porous block (44) when the plurality of dissolving efficiency of un-dissolved carbonic acid gas can be to, most preferably orifice (42) attached to the front end of the mounted porous block difference 1 (44a) and orifices (42) mounted in a stage following a porous block difference 2 (44b) 1 surface composed of metals such as Cu, porous block difference (44a) formed by orifice cartridge (42) and occur such while passing through the connector, compressed carbonated water porous block difference 2 again (44b) to a foam by forming again circulated while compression system of carbonic acid gas dissolver of the electrical heater and the rotation is it can.

[37]

100: storage tank 200: won integer 300: support spring for video tape cassette 10: supply line 20 : the essence a 30: gas infusion line 40:a cover 40a: gas recovering section 40b: liquid recovering section 41: circulation pressure pump 42: orifice 43 : recovery orifice 44 : 44a porous block : porous block difference 1 44b: porous block difference 2 50: exhaust line 51: water regulator 52 :-off valve 60: exhaust means



[1]

The present invention relates to a carbonated drinking water generator which is installed to a water purification line of a refrigerator, etc., and produces carbonated water by contacts made between carbonated gas and water. The carbonated water generator of the present invention receives purified water and carbonated gas at a storage tank, and has a circulation line which absorbs and reapplies water and carbonated gas in the storage tank when generating carbonated water in the storage tank. Further, the carbonated water generator has a cyclic compression pump and an orifice installed to the circulation line, wherein water and carbonated gas absorbed to the circulation line pass the orifice with comparably high pressure in comparison to the storage tank so as to dissolve carbon dioxide in water and reapply the dissolved carbon dioxide to the storage tank. The carbonated water generator repeatedly performs the compression step above, of which carbonated gas and water are re-compressed several times by the cyclic compression system, thereby increasing dissolution efficiency of carbonated gas while substantially reducing time to generate carbonated water.

[2]

COPYRIGHT KIPO 2016

[3]



Carbonated water is stored a storage tank (100) is supply line (10) by an integer stored raw water having won (200) including multi-register for storing gas gas carbonate (300) is connected to, said storage tank (100) one end of the circulation line (40) as they are formed the circular line (40) the other end of the resistor supply line (10) is connected to, said circulation line (40) of the storage tanks (100) side storage tank (100) the remaining carbonic acid gas recover carbon gas recovering section (40a) and the storage tank (100) the remaining, and recovering water a liquid for recovering section (40b) is formed, said circulation line (40)/ close a water with carbon dioxide and consequently the a circulation pressure pump (41) and a with carbon dioxide and consequently for compression of an orifice (42) is formed gas recovering section (40a) and a liquid recovering section (40b) through a carbonic acid gas recovery and the water circulation line (40) through repeated in the circulation or not, thereby providing a desired circulation line (40) via pixel block having a predetermined size in orifice (42) in storage tank (100) than relatively high pressures, the valve member is injected under high pressure, a gas and water carbonate is dissolved in water to carbon dioxide for performing security on a compressing carbonic acid gas which reduces a waste for producing carbonated water bar is rotatably installed around time using recursive cyclic compression system by carbonated water to for producing carbonated water drinking are to be produced.

According to Claim 1, said supply line (10) won (200) an integer the essence connected to a (20) and gas (300), with a gas infusion line (30) is autolysed ( [...] ) an animation Image file or the like, said gas injection lines (30) the auxiliary orifice (70) is mounted e.g. water mixed with carbonic acid gas while they are being fed while injected carbonic acid gas high pressure lower flowrates a circulating compression system by carbonated water to for producing carbonated water drinking are to be produced.

According to Claim 1, said circulation line (40) a gas recovering section (40a) is storage tank (100) connected to the top of, liquid recovering section (40b) a storage tank (100) embedded water immersed is embodied in such a way, gas recovering section (40a)-recovered orifice (43) is mounted carbonic acid gas regulating the flow rate of the gas recovering section (40a) and a liquid recovering section (40b), and is then drawn into a a flow proportion of side polymers may be adjusted main body so as to be moved circulation compression system by carbonated water to for producing carbonated water drinking are to be produced.

According to Claim 3, said circulation line (40) for water to disperse the particles within the stomach porous block (44) as it passes through porous block is attached to water by particles such as impurities, fillers dispersed comes into contact with carbon dioxide and water surface or a dissection pattern carbonic acid gas dissolver efficiency to be fixed a circulating compression system by carbonated water to for producing carbonated water drinking are to be produced.

According to Claim 4, said porous block (44), double diaphragm (42) attached to the front end of the mounted porous block difference 1 (44a) and orifices (42) mounted in a stage following a porous block difference 2 (44b) to foam formation doubly pick-up comprises a light source is characterized by circulation compression system by carbonated water to for producing carbonated water drinking are to be produced.