A NEW METHOD FOR MANUFACTURING POPPING CANDY

Abstract: This invention is related to a new method used in the production of hard candy by employing a treatment with neutral carbon dioxide gas and thus having gas bubbles, which effervesces in the mouth.

Description: A NEW METHOD FOR MANUFACTURING POPPING CANDY This invention is related to a new production method that treats the material with neutral carbon dioxide gas and forms a hard candy that contains gas bubbles in it creating small popping effect in the mouth. PRIOR ART Technically, popping candy production is attained with methods that resembles much or less to each other. Some of these are explained below. In British Patent 1 540 515, a system containing two pressurized tanks that are connected to each other is used. In this method, gas is applied to the hot sugar concentrate from the first pressured tank that is under super atmospheric pressure and later this mixture is transferred to the second tank through a pipe and valve system. While it is being transferred from the second tank to the first tank, the mixture is cooled in this tank under pressure and by decreasing the pressure, it is then possible to crumble the solid mixture. The disadvantage of this method is that because of using two pressurized reactors, the cost of the system is increased and the processing time prolongs. In British Patents 1 521 150 and 1 521 179 similar methods are used. During the application of the method described in British patent application No. 2 200 830, a new gas adding method is mentioned for the production of popping candy. In this method, gas is supplied to the hot candy concentrate in a pressurized tank, at a place close to the bottom of the tank in the form of a gas curtain. In British Patent application No. 2 048 643 wherein a reactor having the capacity of 500 litre carbon dioxide gas is used to provide the distribution of the gas bubbles within the sugar concentrate homogenously, gas is fed from the bottom part of the reactor and the distribution of the gas bubbles is provided by means of a vertical mixing system. However, using a reactor having a volume of 500 liters in this known method to produce already expensive popping candy is resulting in a more expensive manufacturing process. Furthermore, another disadvantage of this method is that too much time is spent during the cooling of the hot sugar mass of 500 liters. In addition, unloading the cooled sugar mass also causes loss of time and labor. Another disadvantage is that in case of a breakdown or a mistake during the course of the process, a great loss can be expected. DESCRIPTION OF THE INVENTION This invention is related to the production of candy by mixing the hot candy mass with neutral carbon dioxide gas homogenously under high pressure and solidifying the mass with bubbles wherein the gas bubbles entrapped in the candy during the manufacturing causes small popping in the mouth. Instead of using expensive and complex units, in the method of this invention a reactor in which candy mass is mixed with gas homogenously and cooling can be conducted as well before being charged out. The invention will be described herebelow with reference to the enclosed drawings. In the drawings; Figure 1 is the cross-section of the reactor used in the present method; Figure 2 is side cross section view of the reactor with the internal shafts; Figure 3 is the side cross section of the reactor; Figure 4 is the view taken from top of the reactor with the internal shafts; Figure 5 is the front view of the reactor with the internal shafts. According to this method, the sugar syrup composed of sugar, glucose, lactose and water are boiled in the cooking unit until the temperature of the mass reaches up to 155°C and thus the amount of water in the sugar mass decreases to 1-1.5%. High moisture level results in soft sticky matrix and it causes the release of the gas in the bubbles without being entrapped within the candy. This boiled highly concentrated syrup is poured from the charge inlet (4) into a pressure reactor wherein the outer surface is double walled. Right after pouring the mass, carbon dioxide gas with high atmospheric pressure is supplied and the mixing operation is started. Mixing is provided by means of blades (1) having the form of flat plates located intermittently and in an angle the shaft horizontally shaft within the reactor having two shafts (12, 13) placed within each other at the centre of the reactor and by means of reactor wall stripper (2) in the form of a flat plate having the same thickness and width of the blades and connecting the blades, the ends of which are folded parallel to the internal side surface, located parallel and a few millimetres away from the internal side of the reactor. Mixing is conducted by rotating the stirring mechanism with 120 rpm within the prescribed time along with the candy mass and neutral gas within the reactor. Although the stirring speed is proportional to the volume and amount of the mass, higher stirring speed will destroy the chemical structure of the candy and the resultant product cannot be used. With higher stirring rates, it will not be possible to have a candy with desired properties and this will lead to the increase of the friction that leads to the increase of the heat. In the end, the candy will start crystallise quite early. Lower stirring speed will also cause the crystallisation. Stirring is provided by rotating the reactor that is placed horizontally to the direction of the fingers of a hand when the thumb is placed to the centre of the outer side of the reactor. Stirring direction will be the direction of the blade (1) plates that are located in an angle. (Figure 3) As the blades (1) rotate, the soft candy having high viscosity and neutral gas mixed with it create a turbulence. This increases the movement of the candy and gas within the reactor and also provides the replacement on the screw threads formed by the location, angles and rotation of the blades. As a result a homogenous mixture is provided. The movement of the blades (1) also causes the fracturing of the gas bubbles entrapped in the candy because the rotating blades causes the entrapping of the gas into the candy and fractures of the bubbles. In the result bubbles having various sizes and amount are attained. The reactor used in the present method, wherein the candy is mixed with carbon dioxide gas under high pressure and then cooled, is made of stainless steel having a volume of 70 litres with double walls. The reactor is resistant to high atmospheric pressures having a stirring system consisting of a reactor wall stripper (2) attached to the blades, located in an angle to the shaft horizontally, onto the double shafts (12, 13) which are placed horizontally within one another in the middle of the reactor. The reactor is assembled on a mobile platform the height of which can be adjusted. As the platform is mobile, the reactor can be transported to any place needed during manufacturing. The hot candy mass is poured into the reactor from its outlet (4) and following the addition of the flavouring, the outlet is closed. The carbon dioxide gas having 45 atmospheric pressure is injected into the space at the upper part of the reactor from gas inlet (5). At this phase, the mixture is stirred by means of horizontal stirrer rotating at 120 rpm having mixing blades (1) placed onto the horizontal stirring shaft (13). The mixing blades (1) in the mixer are placed at one side of the shaft (13) and have 30°C angle to the axes of the shaft. Hot sugar mass can move from one end to the other horizontally and at each cycle of the blades (1), the carbon dioxide gas mixing with the hot sugar mass is distributed to the entire reactor equally and thus a homogeneous gas distribution is attained. Mixing time and the position of the blades (1) on the mixing rod must be carefully observed to size the carbon dioxide bubbles in the hot sugar mass. The blades must be capable of having the carbon dioxide bubbles that are mixed into the hot sugar mass at each rotation, to reach the desired size. In case the aim is to have a popping candy in effervescent type, by increasing the mixing time the carbon dioxide bubbles can be reduced to a rather small size. In case it is aimed to have a more stronger small popping effect, the mixing time is reduced and thus larger bubbles can be formed in the hot candy mass. The mixing process takes 3 to 8 minutes according to the product preferred. After stirring process is completed, the inside pressure of the reactor is decreased to 30 atmosphere from 45 atmosphere in order to attend bubbles at desired diameter. Also large bubbles entrapped in the mass start to move towards the upper surface of the hot candy mass. Other bubbles at desired size stay hanged in the hot sugar mass which acquired the required degree of consistency. The reactor is connected to the cooling fluid unit and the fast cooling process by means of the cold water circulating in the double wall of the reactor from outside to inside and from the centre towards each side from centre towards each side is started. Hot candy syrup at high concentration is cooled with water at 15° C charged from cooling fluid inlet valves (6,8,10) and circulating in the double walls and two shafts (12, 13) and moving from the centre towards the sides cooling is continued until the temperature of the candy mass mixed with carbon dioxide gas reaches to 15°C. Thanks to the double walls and cooling of the hot candy mass is attained from the centre towards sides but the thickness of the hot candy mass prevents an efficient and fast cooling. Therefore, cooling fluid circulating within the shafts (12, 13) provides heat exchange. Thus, with the present method, cooling period is shortened and manufacturing capacity is increased. At the end of the cooling period, carbon dioxide gas with high atmospheric pressure in the reactor is released suddenly by opening the gas discharge valve. As a result of this sudden pressure change, the sugar mass is broken into pieces and crumbled. The product is discharged out of the reactor by opening the front lid (3). The pieces vary in size. The sugar pieces that are smaller than the desired size is sieved and the large ones are taken to the breaking unit for crumbling. According to this method, carbon dioxide gas is homogeneously distributed into the reactor and therefore the product sizes are very close to each other and the rate of loss is rather low. Following sieving, the percentage of usable sugar pieces changes between 74% and 82%. Thus, the rate of waste is 18% 23 % and the sizes of the sugar crumbles which are considered as waste is 0.01 mm or lower and because of having rather low popping effect, these can not be included into end product. According to this method, in case the stirring time exceeds 3 to 8 minutes, the increase of powder and pieces having unacceptable size in the end product, can not be prevented.

Claims: CLAIMS 1. A method for the production of popping candy wherein the water amounts in the candy mass is decreased to 1 to 1.5%. by weight and said mass is mixed with neutral carbon dioxide gas homogeneously under high pressure and cooling and solidifying of the said mass along with the gas bubbles entrapped therein is conducted in a horizontally placed reactor of preferably 70 litre volume resistant to high pressures having double walls and stirring the candy mass by means of a stirring mechanism is consisting of two rotating shafts placed in one another in the centre of the reactor horizontally having blades (1) in the form of flat plates placed in an angle of 30° to the axes of the horizontal shaft and a stripper (2) in the form of a flat plate having the same thickness and width as the blades placed on top of them connecting the blades without changing their angle and which is parallel to the internal side of the reactor and the ends of which are folded in parallel to the internal side, and then cooling the candy mass in a short time by means of a cooling fluid circulating from outer surface to the centre within the two horizontal shafts placed into one another in the centre of the reactor. 2. Method as claimed in Claim 1 wherein the stirring process continues preferably 3 to 8 minutes. 3. Method as claimed in Claim 1 and 2 wherein in the said stirring process, the carbon dioxide gas is supplied at 45 atmospheric pressure and then it is decreased to 30 atmospheric pressure. 4. Method as claimed in Claim 1 wherein the said reactor is placed horizontally on a mobile platform. 5. Method as claimed in Claim 1 wherein stirring blades are provided at one side and preferably to the top of the said stirring shaft. 6. Method as claimed in Claim 1 wherein the said blades are placed with approximately 30° angle to the axes. 7. Method as claimed in claims 1 to 6 wherein the said shaft is comprised of two hollow shafts placed in one another and cooling fluid is entered into the inner shaft and circulated within the space between the outer shaft and the inner shaft. 8. Method as claimed in Claims 1 to 7 wherein the stirring is continued for 7 to 8 minutes for effervescing effect of the candy and 4,5 to 6 minutes for small poppings. 9. Method as claimed in Claims 1 to 8 wherein the blades are concave. 10. Method as claimed in claim 1 wherein the said shaft rotates with 120 rpm.

Inventors: ERDEN IBRAHIM SEMIH, ERDEN, IBRAHIM, SEMIH
Applicants: ERDEN IBRAHIM SEMIH, HLEKS GIDA SANAYI VE TICARET A, ERDEN, IBRAHIM, SEMIH, HLEKS GIDA SANAYI VE TICARET ANONIM &SCEDIL
Application year: 1998
Main classification: A23G3
IPC codes: A23G3