KR830000847B1 - Method for manufacturing dried fish soluble - Google Patents

Method for manufacturing dried fish soluble Download PDF

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Publication number
KR830000847B1
KR830000847B1 KR7903979A KR790003979A KR830000847B1 KR 830000847 B1 KR830000847 B1 KR 830000847B1 KR 7903979 A KR7903979 A KR 7903979A KR 790003979 A KR790003979 A KR 790003979A KR 830000847 B1 KR830000847 B1 KR 830000847B1
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South Korea
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drum
dried
product
thickness
circumferential speed
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KR7903979A
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Korean (ko)
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요시노리 구리하라
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요시노리 구리하라
가부시기가이샤 비분
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    • AHUMAN NECESSITIES
    • A22BUTCHERING; MEAT TREATMENT; PROCESSING POULTRY OR FISH
    • A22CPROCESSING MEAT, POULTRY, OR FISH
    • A22C25/00Processing fish ; Curing of fish; Stunning of fish by electric current; Investigating fish by optical means

Abstract

Drum (dia.; 100-200 cm, thickness; 15-35 mm) was heated to obtain a surface temp. of 52-70≰C and circumferential speed was kept at 2-5 m/min. Softened fish on th surface of a roller was gelled, continuously transferred and dried to produce dried fish soluble. In fig. I, raw materials were dried at (10) and seasoning operation was carried out at 13 (17) represents a light heating apparatus.

Description

건조연제품의 제조법Manufacturing method of dry leaded product

첨부한 도면은 본 발명방법을 실시하는 장치의 1예를 표시하는 정면도.The accompanying drawings are front views which show an example of the apparatus which implements the method of this invention.

본 발명은 생산성이 좋고, 또한 높은 품질의 건조 연제품을 제조하는 방법을 제공하려고 하는 것이다.It is an object of the present invention to provide a method for producing a product having good productivity and high quality dry soft products.

종래 수산연제품원료를 갈아뭉게서(

Figure kpo00001
)연성하여 건조 연제품을 제조하는 방법으로서는 예컨대 특허공보 소화 50년 제39139호가 알려져 있으나 본 발명자에 의한 수많은 실험에 따르면 그 방법에 의한 제조는 생산성이 그다지 좋지않으며, 또한 높은 품질의 것이 얻어지기 어려운 결점이 있었다.By grinding the raw fish seafood products
Figure kpo00001
As a method for producing a dry soft product by ductility, for example, Patent Publication No. 5039 No. 39139 is known, but according to a number of experiments by the inventors, the production by the method is not very productive, and high quality is difficult to obtain. There was a flaw.

본 발명은 이러한 결점을 개량하도록 예의 검토한 결과 생산성을 수배로 향상시킴과 아울러 두께가 두꺼운 것이나 또는 얇은 것이라도 품질이 높은 건조연제품으로 만들수가 있는 본발명에 도달하였다.As a result of earnestly examining the above-mentioned drawbacks, the present invention has improved the productivity by several times and has reached the present invention which can be made into a high quality dry soft product even if it is thick or thin.

이하 본 발명실시의 1예를 첨부한 도면에 따라 설명한다.Hereinafter, one example of an embodiment of the present invention will be described with reference to the accompanying drawings.

(1)은 재질이 SS 41 혹은 SUS 304 등인 회전드럼이며, 지름은 대략 100cm-200cm로서 두께는 15mm-35mm이다. 여기에서 드럼의 지름이 대략 100cm-200cmm이며, 또한 두께를 15mm-35mm로 하도록 하는 것은 생산성의 향상과 뒤에서 설명하는 가열온도 및 원주속도의 관계로서 드럼표면온도를 안정적으로 보전시키기 위한 것이다.(1) is a rotating drum made of SS 41 or SUS 304. The diameter is approximately 100cm-200cm and the thickness is 15mm-35mm. Here, the diameter of the drum is approximately 100cm-200cmm and the thickness of 15mm-35mm is to improve the productivity and to stably maintain the drum surface temperature in relation to the heating temperature and the circumferential speed described later.

즉, 특허공보 소화 50년 제39138호로서 제안되어있는 것같이 드럼(1)의 표면온도를 30℃-50℃로 보전시키는 경우의 원주속도는 대략 0.5-1.5m/분이며, 원주속도를 이정도의 범위로 하지 않으면 겔화가 불가능하게 되든가 혹은 반대로 로울러표면에 눌어붙어서 떼어내기가 곤란하게 된다.That is, the circumferential speed at which the surface temperature of the drum 1 is maintained at 30 ° C.-50 ° C., as proposed in Korean Patent Publication No. 39138, is approximately 0.5-1.5 m / min, and the circumferential speed is about this degree. If it is not in the range of, gelation becomes impossible or, on the contrary, it is difficult to detach by pressing on the roller surface.

따라서 생산성이 매우 떨어지는(후술될 비교자료에서 나타난바와같이)것이었으나 본 발명에서는 드럼의 표면온도를 52℃-70℃(바람직하게는 55℃-65℃)로 되도록 함과 아울러 그 원주속도는 대략 2-5m/으로 하도록 하는 것이다.Therefore, although the productivity was very low (as shown in the comparative data to be described later), in the present invention, the surface temperature of the drum was set to 52 ° C.-70 ° C. (preferably 55 ° C.-65 ° C.) and the circumferential speed thereof was approximately. 2-5m /.

본 발명에서는 드럼의 원주속도를 종래의 4배 내지 10배로 하며, 이것에 수반하여 표면온도도 종래의 30℃-50℃를 초과한 범위로 설정하는 것이다.In the present invention, the circumferential speed of the drum is set to 4 to 10 times that of the conventional one, and with this, the surface temperature is set to a range exceeding the conventional 30 ° C to 50 ° C.

본 발명에서 표면온도를 52℃ 이하로 하는 경우는 겔화가 불충분하게 되며 또 70℃이상의 경우는 떼어내기가 곤란하므로 지장을 초래한다.In the present invention, when the surface temperature is set to 52 ° C or less, gelation becomes insufficient, and when the surface temperature is 70 ° C or more, it is difficult to remove, which causes trouble.

(2)는 원료공급 흡퍼,(2) the raw material supply absorber,

(3)은 두께 조정판으로서 종래의 것과 변함이 없으며,(3) is a thickness adjusting plate and does not change from the conventional one,

(4)는 드럼(1)의 외주면에 배설되어서 이루어진 가스등의 가열장치로서 드럼표면의 조사열처리(照射熱處理)가 행하여진다. 이때에 원료공급호퍼(2)에는 드럼(1)에서의 열기를 차단하도록 하는 냉각수단을 설치할 수 있으며 드럼표온면도는 내부에서 미묘한 온도조절이 행하여지도록 되어있다.Numeral 4 denotes a heating device such as a gas provided on the outer circumferential surface of the drum 1 to perform irradiation heat treatment on the surface of the drum. At this time, the raw material supply hopper (2) can be provided with a cooling means to block the heat from the drum (1), the surface temperature of the drum is to be subjected to subtle temperature control inside.

즉, 드럼(1)내는 중공으로 형성되어 있으며, 그 내부에는 파이프(5)가 배설되어있다.That is, the drum 1 is formed hollow, and the pipe 5 is arrange | positioned inside.

그리고, 그 파이프에는 도면에 표시하지않은 장치에서 냉수, 온수나 스팀이 순환하도록 공급되는 것이며 전기한 온도범위의 미묘한 온도제어가 행하여 지도록 되는것이며, 예컨대 여름철의 제품의 두께가 얇을 경우에는 냉수가 공급되도록 하게된다.In addition, the pipe is supplied to circulate cold water, hot water or steam in a device not shown in the drawing, and subtle temperature control of the aforementioned temperature range is performed. For example, in the case of thin summer products, cold water is supplied. To be possible.

또 겨울철용으로 제품의 두께가 두꺼운 경우에는 온수가 송급되도록 한다.In addition, if the product is thick for winter, hot water should be supplied.

종래의 드럼의 지름은 고작해야 60cm-80cm정도의 것에 불과하였으나 이것을 본 발명에서는 100cm-200cm로 하고, 또한 원주속도를 2-5m/분으로 하도록 하는것에 의하여 생산성이 종래의 것의 여러배로 비약적인 향상을 도모할수 있는 것이다.The diameter of the conventional drum is only about 60 cm-80 cm at best, but in the present invention, the diameter is 100 cm-200 cm, and the circumferential speed is 2-5 m / min. It can be planned.

또 종래의 드럼의 두께는 대략 10mm 전후일뿐이었으나 본발명에서는 이것을 15mm 내지 35mm로 하는 것이며, 이와같이 두께를 증대시키는 것은 겔화온도를 안정시켜 높은 품질의 제품이 얻어지도록 하는 것이다.In addition, although the thickness of the conventional drum was only about 10 mm, in the present invention, the thickness is set to 15 mm to 35 mm. In this way, the thickness is increased to stabilize the gelation temperature so that a high quality product can be obtained.

다음에 목적으로 하는 최종제품이 얻어지도록 하기위하여서는 이하의 공정을 거쳐서 행하여진다.Next, in order to obtain the desired final product, the following steps are carried out.

(6)은 드럼(1)의 회동이 반대쪽에서 앞에서 설명한 건조기와의 사이에 상승하는 경사상태로 설치되는 콘베이어이며, 드럼(1)과 콘베이어(6)와의 사이에는 드럼(1)쪽에 근접하여 박리판(7)이 설치되고 또 콘베이어(6)의 길이방향에는 회동하는 네트(NET)(8)을 협지하여 그 상하사이에 조사수단(照射手段)(9a)(9b)이 설치되어 있다.(6) is a conveyor installed in an inclined state in which the rotation of the drum (1) rises between the dryers described above on the opposite side, and peels close to the drum (1) side between the drum (1) and the conveyor (6). The board 7 is provided, and the net (8) which rotates is clamped in the longitudinal direction of the conveyor 6, and the irradiation means 9a and 9b are provided between the upper and lower sides.

(10)은 건조기로서 여러층의 콘베이어(11a)(11b)(11c)가 수평으로 된 선반의 층모양으로 배치되며 또한 회동방향이 교대로 달라지도록하여 회동하게 되어있고, 또 아래쪽에는 열풍을 송급하도록 하기위한 송풍기(12)가 설치되어 있다.(10) is a dryer, in which a plurality of conveyors (11a) (11b) (11c) are arranged in a layered shape of a shelf which is horizontal, and rotated so that the rotation direction is alternately changed, and the hot air is supplied to the lower side. A blower 12 is installed to make it possible.

(13)은 조미액조로서 간장 기타의 조미료에 의해 조미된 조미액이 저장되면, 앞뒤에는 유도로울러(14)및 견인회수용 로울러(15)가 설치되어 있다.(13) is a seasoning liquid tank, when seasoning liquid seasoned by soy sauce and other seasonings is stored, the induction roller 14 and the towing recovery roller 15 are provided in front and back.

(16)은 발포기로서 상하로 대향시켜서 1쌍의 망으로된 밸브(17a1)(17b1)를 회동시킴과 아울러 그 안쪽의 길이 방향으로는 조사가열수단(17a2)(17b2)를 설치하고 있다.(16) rotates a pair of meshed valves (17a 1 ) (17b 1 ) by facing up and down as a foaming machine, and irradiating heating means (17a 2 ) (17b 2 ) in the longitudinal direction therein. I install it.

상기한 공정에 있어서 건조기(10)실내는 송풍기(12)의 운전에 의하여 열풍이 송급되어 실내온도 70℃-100℃의 범위로 가온되어 있어서 띠모양으로된 원료는 선반의 층모양의 콘베이어(11a)(11b)(11c)가 교대로 그 방향이 달라지도록 하여 회동하는것에 의하여 위쪽에서 순차로 아래쪽으로 향하여 이동통과시켜지며 수본비물이 40%이하로 되도록 건조된다. 그리고 목적으로 하는 수분비율 이하로된 띠모양의 원료는 출구에서 유도로울러(14)를 거쳐서 조미액조(13)내로 송급되어서 조미가 행하여진후 견인회수로울러(15)에 의하여 순차회수되어서 발포기(16)내로 송급된다.In the above-described process, the dryer 10 is supplied with hot air by the operation of the blower 12 and is heated in a range of 70 ° C.-100 ° C., so that the strip-shaped raw material is a shelf conveyor 11a. ) 11b and 11c are alternately rotated in a different direction so that they are passed from the top to the bottom and dried so that the effluent is less than 40%. And the band-shaped raw material which is below the desired moisture ratio is fed into the seasoning liquid tank 13 through the induction roller 14 at the exit, and seasoning is performed, and it is collect | recovered sequentially by the towing recovery roller 15, and the foaming machine 16 Will be remitted.

여기에서 발포기(16)는 1쌍의 망으로된 밸브(17a1)(17b1)가 화살표(ㄷ)방향으로 회동되도록 설치되고, 띠모양원료는 그 망으로된 밸트(17a1)(17b1)사이에 협지되어서 이동되며, 그 상하양면을 조사가열수단에 의하여 가열처리가 실시된다. 발포기는 제품을 그 질이 팽창되도록 함과 아울러 반점모양의 눌어붙은 자리가 형성되도록 만들어진것으로서 발포기내의 조사가열수단(17a2)(17b2)은 대략 400℃-700℃의 높은 온도로 보전되고 있다.Here, to give (16) is a valve to the network of the pair (17a 1) (17b 1) an arrow (c) is provided to be rotated in the direction of band-shaped material is a belt in the network (17a 1) (17b 1 ) It is sandwiched and moved between, and heat-treatment is performed on the upper and lower surfaces by irradiation heating means. Foam product groups that should be such that the expansion and irradiation as well as heating means of the expanded cabin as designed to form a seat attached to please press the spot shape (17a 2) (17b 2) is being held at a high temperature of approximately 400 ℃ -700 ℃ have.

따라서 이에관한 종래의 제품(일특공소 53-39139호)에 비하여 본 발명의 생산성이 수배로 향상하였다는 결과를 입증해주는 자료를 보면.Therefore, if you look at the data demonstrating the result that the productivity of the present invention has been improved several times compared to the conventional product (Japanese Patent Application No. 53-39139).

Figure kpo00002
Figure kpo00002

이상에서 나타난 바와같이 회전드럼의 크기를 종래의 배이상(종래는 600-800mm)으로하고, 또 드럼의 표면온도를 배정도로 하는것에 의하여 동일한 어육두께의 연제품원료를 겔화하여서 꺼내는데 3배정도 효율이 증가되도록 한것이며, 그후 드럼의 표면온도가 높아지면 콘베이어 조사기간도 짧아지게 되고, 또한 건조시간을 포함하여 후 처리공정에서 종래의 것보다도

Figure kpo00003
정도 단축되도록 한 효과를 얻을수 있게 한것이다.As shown above, the size of the rotating drum should be more than twice the size of the conventional drum (600-800 mm), and the surface temperature of the drum should be about twice the efficiency of gelling out the soft fish raw material of the same fish thickness. After that, if the drum surface temperature increases, the conveyor irradiation period will be shorter, and the drying time will be shorter than the conventional one.
Figure kpo00003
The effect is to reduce the degree.

그러므로 본발명은 이상과같이 실시하는 것에 의하여 종래 제품과 비교하여 그 생산성을 몇배로 향상시킴과 아울러 5-6mm의 두께의 것이라도, 또는 2mm전후의 얇은 것이라도 안정되어 높은 품질의 건조연제품으로 만들수가 있는 것이다.Therefore, the present invention improves the productivity several times compared to the conventional products by performing as described above, and is stable even if it is 5-6 mm thick or thin around 2 mm and is a high quality dry leaded product. You can make it.

Claims (1)

지름이 100cm-200cm이며 두께가 15mm-35mm인 드럼을 표면온도가 52℃-70℃로 되도록 가열시킴과 아울러 원주속도를 대략 2m-5m/분으로 되도록 하여서 회동하고, 그 로울러표면에 점조(粘稠)한 상태로 연성(練成)한 어육을 띠 모양으로 공급하면서 겔(GEL)화 한후에 박리하고, 이어서 연속적으로 이송하면서 건조처리를 시행하여 건조연제품을 제조하도록 하는것을 특징으로 하는 건조연제품의 제조법.Heat the drum with diameter of 100cm-200cm and thickness of 15mm-35mm to the surface temperature of 52 ℃ -70 ℃, and rotate it with the circumferential speed to be about 2m-5m / min. (I) gelling (GEL) while feeding soft fish meat in a stripped state in a stripped state, and then peeling it, and then performing drying treatment while continuously transferring the dried lead to produce a dried leaded product. The recipe of the product.
KR7903979A 1979-11-14 1979-11-14 Method for manufacturing dried fish soluble KR830000847B1 (en)

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