KR100387008B1 - A process for preparing a tea drawn by distilled water and its apparatus - Google Patents
A process for preparing a tea drawn by distilled water and its apparatus Download PDFInfo
- Publication number
- KR100387008B1 KR100387008B1 KR10-2000-0061216A KR20000061216A KR100387008B1 KR 100387008 B1 KR100387008 B1 KR 100387008B1 KR 20000061216 A KR20000061216 A KR 20000061216A KR 100387008 B1 KR100387008 B1 KR 100387008B1
- Authority
- KR
- South Korea
- Prior art keywords
- water
- distillation
- distilled water
- tea
- condenser
- Prior art date
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 91
- 239000012153 distilled water Substances 0.000 title claims abstract description 31
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 17
- 241001122767 Theaceae Species 0.000 title claims abstract 9
- 238000004821 distillation Methods 0.000 claims abstract description 31
- 230000004075 alteration Effects 0.000 claims abstract description 28
- 238000000605 extraction Methods 0.000 claims abstract description 17
- 238000001816 cooling Methods 0.000 claims abstract description 16
- 239000000463 material Substances 0.000 claims abstract description 10
- 239000000284 extract Substances 0.000 claims abstract description 8
- 238000000034 method Methods 0.000 claims abstract description 4
- 230000001105 regulatory effect Effects 0.000 claims description 4
- 239000002184 metal Substances 0.000 claims 2
- 238000005507 spraying Methods 0.000 claims 2
- 238000010438 heat treatment Methods 0.000 claims 1
- 239000004615 ingredient Substances 0.000 abstract description 5
- 238000009833 condensation Methods 0.000 abstract description 4
- 230000005494 condensation Effects 0.000 abstract description 4
- 238000001914 filtration Methods 0.000 abstract description 2
- 239000008236 heating water Substances 0.000 abstract description 2
- 244000269722 Thea sinensis Species 0.000 description 26
- 235000013616 tea Nutrition 0.000 description 23
- 235000003261 Artemisia vulgaris Nutrition 0.000 description 5
- 240000006891 Artemisia vulgaris Species 0.000 description 5
- 239000002994 raw material Substances 0.000 description 5
- 240000008397 Ganoderma lucidum Species 0.000 description 4
- 235000001637 Ganoderma lucidum Nutrition 0.000 description 4
- 244000241838 Lycium barbarum Species 0.000 description 4
- 235000015459 Lycium barbarum Nutrition 0.000 description 4
- 241000234314 Zingiber Species 0.000 description 4
- 235000006886 Zingiber officinale Nutrition 0.000 description 4
- 235000008397 ginger Nutrition 0.000 description 4
- 235000009569 green tea Nutrition 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 235000015468 Lycium chinense Nutrition 0.000 description 3
- 239000012141 concentrate Substances 0.000 description 3
- 235000019986 distilled beverage Nutrition 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 239000008399 tap water Substances 0.000 description 2
- 235000020679 tap water Nutrition 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 239000002075 main ingredient Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- -1 water vapor Chemical compound 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23F—COFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
- A23F3/00—Tea; Tea substitutes; Preparations thereof
- A23F3/16—Tea extraction; Tea extracts; Treating tea extract; Making instant tea
- A23F3/18—Extraction of water soluble tea constituents
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
- A23V2250/00—Food ingredients
- A23V2250/20—Natural extracts
- A23V2250/21—Plant extracts
- A23V2250/214—Tea
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Tea And Coffee (AREA)
Abstract
본 발명은 증류수차의 제조방법 및 그 장치에 관한 것임.The present invention relates to a method for producing distillation aberration and an apparatus thereof.
본 발명은 물을 가열하여 수증기로 만드는 수증기 발생단계와, 수증기를 60 ∼ 80℃The present invention is a steam generating step of heating water to make water vapor, water vapor 60 ~ 80 ℃
정도의 증류수로 만드는 응축단계 또는 수증기를 80℃를 초과하는 증류수와 100℃ 정도의 수증기로 만드는 응축단계와, 차원료가 장입된 차성분추출탱크에 증류수 또는 증류수를 포함하고 있는 수증기를 통과시키는 차성분추출단계와, 차성분이 추출된 증류수차를 상온으로 냉각, 여과 및 저장하는 단계로 증류수차를 제조하는 방법과 장치임.A condensation step to make distilled water of about 50 ° C, and a condensation step to make water vapor of more than 80 ° C. and steam of about 100 ° C., and a tea that passes distilled water or steam containing distilled water to a tea ingredient extraction tank loaded with a pulp material A method and apparatus for preparing a distillation aberration by the step of extracting the components and cooling, filtering and storing the distillation aberration from which the tea components are extracted at room temperature.
본 발명은 수증기로 부터 응축되는 증류수 또는 증류수를 포함하고 있는 수증기로 각종 차원료의 차성분을 연속적으로 유효하게 추출할 수 있고, 차종류에 따라서 운전모드를 선택하면서 다양한 증류수차를 단일설비에서 경제적으로 제조할 수 있는 장점이 있다.The present invention can continuously and effectively extract the tea components of various dimension materials with distilled water condensed from steam or water containing distilled water. There is an advantage that can be manufactured.
Description
본 발명은 각종 차의 원료 성분이 포함된 증류수차의 제조방법 및 그 장치에 관한 것으로서 보다 구체적으로는 수증기로 부터 응축되는 증류수 또는 증류수를 포함하고 있는 수증기로 차성분을 연속적으로 추출하는 증류수차의 제조방법 및 그 장치에 관한 것이다.The present invention relates to a method for producing a distillation aberration containing the raw material components of various teas, and more particularly, to a distillation aberration that continuously extracts tea components with distilled water condensed from water vapor or steam containing distilled water. A manufacturing method and apparatus therefor.
종래에 대한민국 특허 공개번호 제 2000-0024959 호로 알려진바 있는 인진쑥을 주원료로 한 증류수 무균음료의 제조방법은 인진쑥에서 엑기스를 추출, 농축하는 것으로서, 마른 인진쑥을 마대자루에 담아 추출기에 넣은 후 정제수를 투입하고Conventionally known as Republic of Korea Patent Publication No. 2000-0024959 The method of producing a sterile distilled beverage with the main ingredients of Injin mugwort is to extract and concentrate the extract from Injin mugwort, put the dried Injin mugwort into the sack and put purified water and
, 추출기 뚜껑을 닫은 다음 스팀을 공급하여 추출기의 내부온도가 90℃ 로 올라간 상태에서 22시간 동안 추출액을 추출시키고, 추출된 추출액을 여과기에서 여과시킨 후 농축기에서 60℃로 10시간 농축시키며, 추출액에서 발생된 수증기를 진공펌프로흡입시키고, 흡입된 수증기를 냉각수로 냉각시켜서 인진쑥 증류수를 제조하는 것이었다.Close the extractor lid and supply steam to extract the extract for 22 hours while the extractor's internal temperature rose to 90 ℃, filter the extracted extract in a filter, and concentrate it at 60 ℃ in a concentrator. Phosphorus mugwort distilled water was prepared by suctioning the generated steam with a vacuum pump and cooling the sucked steam with cooling water.
이와 같은 종래의 증류수 음료의 제조방법은 비교적 제조공정이 복잡하고, 증류수 음료를 연속적으로 생산할 수 없었을 뿐 아니라 인진쑥에서 엑기스를 추출, 농축하는데 32시간 정도가 소요되는 것이어서 산업화하기에 적합하지 못한 등의 문제점이 있었다.Such a conventional method of preparing a distilled beverage has a relatively complicated manufacturing process, is unable to continuously produce a distilled beverage, and takes about 32 hours to extract and concentrate extracts from jinjin mugwort, which is not suitable for industrialization. There was a problem.
본 발명은 수증기로 부터 응축되는 증류수 또는 증류수를 포함하고 있는 수증기로 차원료의 차성분을 연속적으로 추출함으로서 산업화하기에 적합한 증류수차의 제조방법 및 그 장치를 제공하는데 기술적 과제를 둔 것이다.The present invention has been made to provide a method and apparatus for producing a distillation aberration suitable for industrialization by continuously extracting the tea components of the pulp material with distilled water condensed from steam or steam containing distilled water.
도 1은 본 발명에 의한 증류수차 제조방법의 블록다이어그램.1 is a block diagram of a method for producing distillation aberration according to the present invention.
도 2는 본 발명에 의한 증류수차 제조장치의 계통도.Figure 2 is a system diagram of a distillation aberration manufacturing apparatus according to the present invention.
본 발명에 의한 증류수차 제조방법은 도 1에 예시한 바와 같이 물을 가열하여 수증기로 만드는 수증기 발생단계에서 얻어진 수증기를 대기압을 초과하는 압력으로 가압시키는 단계와, 가압된 수증기를 60 ∼ 80℃정도의 온도를 갖는 증류수로 응축시켜 주는 응축단계(A) 또는 가압된 수증기를 80℃를 초과하는 온도의 증류수와 100℃ 정도의 수증기 상태로 응축시켜주는 응축단계(B)를 선택적으로 거친 증류수 또는 증류수를 포함한 수증기를 분말입자 크기가 100 ∼ 400메쉬 정도인 차원료가 장입된 차성분 추출탱크에 공급하여 차성분을 추출하는 차성분 추출단계 및 고온의 증류수차를 상온으로 냉각시켜주는 냉각단계와, 증류수차를 여과시키면서 저장탱크에 저장하는 단계로 증류수차를 제조하는 것이다.Distillation aberration manufacturing method according to the present invention is a step of pressurizing the water vapor obtained in the steam generation step of heating water to make water vapor as illustrated in Figure 1 to a pressure exceeding atmospheric pressure, and pressurized water vapor about 60 ~ 80 ℃ Distilled water or distilled water optionally subjected to condensation step (A) for condensing into distilled water having a temperature of 100 ° C. or condensation step (B) for condensing the pressurized water vapor to a temperature of about 100 ° C. A tea component extraction step of extracting tea components by supplying water vapor, including water vapor, into a tea ingredient extraction tank loaded with a dimensional material having a particle size of about 100 to 400 mesh, and a cooling step of cooling the high temperature distillation aberration to room temperature; The distillation aberration is to prepare a distillation aberration by storing in a storage tank while filtering.
본 발명에 의한 증류수차 제조장치는 도 2에 예시한 바와 같이 담겨지는 물(10)을 침수전열기(12)로 가열시켜서 수증기(14)로 만들어주는 수증기 발생탱크(16)와 냉각관(18) 사이에는 제 1 응축기(20), 제 2 응축기(22) 및 차성분 추출탱크(24)를 연결하고, 냉각관(18)에는 증류수차 저장탱크(26)를 연결하여서 된 것이다.Distillation aberration manufacturing apparatus according to the present invention is a steam generating tank 16 and the cooling tube 18 to heat the water 10 contained in the immersion heater 12 to make water vapor 14 as illustrated in FIG. The first condenser 20, the second condenser 22, and the tea ingredient extraction tank 24 are connected therebetween, and the cooling pipe 18 is connected to the distillation wheel storage tank 26.
수증기발생탱크(16)의 수증기배출도관(28)에는 수증기발생탱크(16)에서 생산되는 수증기중 초기에 생산된 수증기에 포함된 각종 불순물을 제거시켜주기 위한 초기 수증기 배출밸브(30)와, 수증기발생탱크(16)에서 생산되는 수증기의 압력이 대기압 보다 높은 압력으로 가압되었을 때에만 개방되는 압력조절밸브(32)가 달려있다.The steam discharge conduit 28 of the steam generating tank 16 includes an initial steam discharge valve 30 for removing various impurities included in the steam produced initially among the steam produced in the steam generating tank 16, and steam. There is a pressure control valve 32 which opens only when the pressure of the steam produced in the generating tank 16 is pressurized to a pressure higher than atmospheric pressure.
상기 수증기배출도관(28)의 끝에는 제 1 응축기(20)의 입구(20')와 연결된 제 1 수증기공급도관(34)과, 제 2 응축기(22)의 입구(22')와 연결된 제 2 수증기공급도관(36)이 3방향밸브(38)로 연결되어 있어서 상기 압력조절밸브(32)를 통해서 공급되는 가압된 수증기를 제 1 응축기(20)와 제 2 응축기(22)에 선택적으로 공급해 줄 수 있도록 되어 있다.At the end of the steam discharge conduit 28, a first steam supply conduit 34 connected to the inlet 20 ′ of the first condenser 20 and a second steam connected to the inlet 22 ′ of the second condenser 22. A supply conduit 36 is connected to the three-way valve 38 to selectively supply pressurized water vapor supplied through the pressure regulating valve 32 to the first condenser 20 and the second condenser 22. It is supposed to be.
제 1 응축기(20)와 제 2 응축기(22)의 내부에는 수많은 구멍(40)을 가진 여러개의 냉각판(42)이 경사지게 지그재그 형태로 고정되어 있어서 각각의 입구(20'), (22')쪽으로 유입되는 수증기를 냉각 시켜주면서 각각의 출구(20"), (22")쪽으로 유출시켜 줄 수 있도록 되어 있다.Inside the first condenser 20 and the second condenser 22, a plurality of cooling plates 42 having numerous holes 40 are inclined and zigzag fixed to each inlet 20 ', 22'. It cools the water vapor flowing in to the outlet, and can flow out to the respective outlets 20 " and " 22 ".
그중 제 1 응축기(20)의 주위에는 물 재킷(jacket)(44)이 형성되어 있고, 물재킷(44)의 입수구(44')쪽에는 수도관(46)이 연결되어 있으며, 물 재킷(44)의 출수구(44")쪽에는 상기 수증기발생탱크(16)의 급수관(48)과 연결되는 급수도관(50)이 연결되어 있어서 제 1 응축기(20)는 유입되는 수증기와 물 재킷(44)으로 유입되는 수도물과의 열교환이 이루어지도록 하여 수증기를 약 60 ∼ 80℃ 정도의 온도를 갖는 증류수로 만들어 출구(20") 쪽으로 유출시켜 줌과 아울러 수증기발생탱크(16)로 공급되는 물을 예열시켜 줌으로서 수증기발생탱크(16)의 소비전력을 절약시켜 줄 수 있도록 되어 있다.Among them, a water jacket 44 is formed around the first condenser 20, a water pipe 46 is connected to the inlet 44 ′ of the water jacket 44, and the water jacket 44 is provided. A water supply conduit 50 connected to the water supply pipe 48 of the steam generating tank 16 is connected to the outlet port 44 ″ of the first condenser 20 so that the first condenser 20 flows into the water vapor and the water jacket 44. By making the heat exchange with the tap water to be made into distilled water having a temperature of about 60 ~ 80 ℃ to flow out to the outlet (20 ") and by preheating the water supplied to the steam generating tank 16 The power consumption of the steam generating tank 16 is to be saved.
제 2 응축기(22)는 유입되는 수증기를 내장된 냉각판(42)으로만 자연 냉각시켜서 80℃를 초과하는 온도의 증류수와 100℃정도의 수증기를 출구(22") 쪽으로 유출시켜 준다.The second condenser 22 naturally cools the incoming steam only to the built-in cooling plate 42 to allow distilled water at a temperature exceeding 80 ° C. and water vapor at about 100 ° C. toward the outlet 22 ″.
제 1 응축기(20)의 출구(20")와 제 2 응축기(22)의 출구(22")는 차성분추출탱크(24)의 입구(24')와 각각 연결관(52), (54)으로 연결되어 있다.The outlet 20 " of the first condenser 20 and the outlet 22 " of the second condenser 22 are connected to the inlet 24 ' Is connected.
차성분추출탱크(24)의 상부에는 확대노즐형 증류수분사기(56)가 고정되어 있고, 차성분추출탱크(24)의 하부에는 100 ∼ 400메쉬 정도의 입자크기를 가진 차원료(58)가 금속망(60) 위에 담겨지는 차원료카트리지(62)가 장입되어 있다.An enlarged nozzle type distilled water injector 56 is fixed to the upper portion of the tea component extraction tank 24, and the dimension material 58 having a particle size of about 100 to 400 mesh is formed on the lower portion of the tea component extraction tank 24. A pulp cartridge 62 contained on the net 60 is charged.
차성분추출탱크(24)의 출구(24")는 냉각관(18)의 입구(18')와 연결되어 있고, 증류수차저장탱크(26)와 연결된 냉각관(18)의 출구(18") 쪽에는 필터(64)가 마련되어 있다.The outlet 24 ″ of the tea ingredient extraction tank 24 is connected to the inlet 18 ′ of the cooling tube 18 and the outlet 18 ″ of the cooling tube 18 connected to the distillation aberration storage tank 26. The filter 64 is provided in the side.
본 발명에 있어서, 제 1 응축기(20)의 출구(20")쪽 연결관(52)에는 제 2 응축기(22)로 부터 유출되는 고온의 증류수와 수증기가 제 1 응축기(20) 쪽으로 유입되는 것을 차단시켜 주는 체크밸브(66)가 달려있다.In the present invention, the high temperature distilled water and water vapor flowing out from the second condenser 22 flows into the first condenser 20 in the connection pipe 52 toward the outlet 20 ″ of the first condenser 20. There is a check valve 66 to shut off.
차성분추출탱크(24)의 입구(24') 쪽에는 온도감지기(68)가 달려있고, 이 온도감지기(68)는 제 1 수증기공급도관(34)에 있는 솔레노이드밸브(70)와 연결되어 있어서 제 1 응축기(20)로 부터 차성분추출탱크(24) 쪽으로 유입되는 증류수의 온도가 80℃를 초과할 경우 수증기발생탱크(16)로 부터 제 1 응축기(20) 쪽으로의 수증기공급을 차단시켜 줄 수 있도록 되어 있다.A temperature sensor 68 is attached to the inlet 24 'of the tea ingredient extraction tank 24, which is connected to the solenoid valve 70 in the first water vapor supply conduit 34. When the temperature of the distilled water flowing from the first condenser 20 toward the secondary component extraction tank 24 exceeds 80 ° C., the water vapor supply from the steam generating tank 16 to the first condenser 20 is blocked. It is supposed to be.
그리고 수증기발생탱크(16)의 급수관(48)에 있는 솔레노이드밸브(72)는 수위감지기(74)와 연결되어 있어서 수증기발생탱크(16) 내의 수위를 조절할 수 있도록 되어 있고, 상기 솔레노이드밸브(72)와 수증기발생탱크(16)의 침수전열기(12)는 증류수차저장탱크(26)에 있는 수위감지기(76)와도 연결되어 있어서 수증기의 생산량을 증류수차 저장량과 연동하여 자동적으로 조절할 수 있도록 되어 있다.And the solenoid valve 72 in the water supply pipe 48 of the steam generating tank 16 is connected to the water level detector 74 to adjust the water level in the steam generating tank 16, the solenoid valve 72 And the submerged heater 12 of the steam generating tank 16 is also connected to the water level sensor 76 in the distillation aberration storage tank 26, so that the production of water vapor can be automatically adjusted in conjunction with the distillation aberration storage amount.
도면중 미설명 부호 78은 드레인밸브, 80은 오우버플로우관, 82는 수위계, 84는 증류수차배출밸브, 86은 냉각팬, 88은 안전밸브이다.In the drawings, reference numeral 78 denotes a drain valve, 80 an overflow tube, 82 a water gauge, 84 a distillation aberration discharge valve, 86 a cooling fan, and 88 a safety valve.
이와 같이 구성된 본 발명은 녹차나 둥글레차와 같이 60 ∼ 80℃ 정도의 온수에서 추출하는 것이 바람직한 차를 제조할 경우에는 차원료카트리지(62)에 분말입자가 100 ∼ 400메쉬 정도로 가공된 녹차나 둥글레차 원료를 담아서 차성분추출탱크(24)에 장입하고, 수증기발생탱크(16)에서 생산되는 수증기중 초기에 생산되어 불순물이 포함된 수증기를 초기 수증기 배출밸브(30)를 개방시켜 제거한 후 초기 수증기 배출밸브(30)를 다시 폐쇄시킨 다음 3방향밸브(38)를 제 1 수증기공급도관In the present invention configured as described above, when manufacturing a tea, which is preferably extracted from hot water at about 60 to 80 ° C., such as green tea or round tea, green tea or round processed powder particles in the pulp material cartridge 62 is about 100 to 400 mesh. After filling the tea raw material into the tea component extraction tank 24, and the initial production of the water vapor produced in the steam generating tank 16 to remove the impurities containing water by opening the initial steam discharge valve 30, the initial steam Close the discharge valve 30 again and then connect the three-way valve 38 to the first steam supply conduit.
(34) 쪽으로 개방시키면 압력조절밸브(32)에 의해서 대기압 보다 높은 압력으로 가압된 수증기가 제 1 응축기(20) 내로 유입되고, 유입된 수증기는 경사지게 지그재그형태로 고정된 냉각판(42)을 따라서 상승하면서 냉각되고 제 1 응축기(20)의 주위에 있는 물 재킷(44)으로 유입된 수도물과도 열교환이 이루어지면서 약 60 ∼ 80℃정도의 증류수로 응축되어 차성분추출탱크(24)의 확대노즐형증류수분사기(56)를 통해서 차원료카트리지(62)에 담겨진 녹차나 둥글레차 원료를 통과하므로 녹차나 둥글레차 성분이 추출된 증류수차가 제조된다.Opening toward (34), water vapor pressurized by the pressure regulating valve 32 to a pressure higher than atmospheric pressure is introduced into the first condenser 20, and the introduced water vapor is inclined along the cooling plate 42 fixed in a zigzag form. The nozzle of the primary component extraction tank 24 is condensed with distilled water of about 60 to 80 ° C. while being heat-exchanged with the tap water introduced into the water jacket 44 around the first condenser 20. Since the green tea or round tea raw material contained in the pulp material cartridge 62 is passed through the mold distillation sprayer 56, the green tea or round tea component is extracted.
제조된 증류수차는 냉각관(18)을 거치면서 상온정도로 냉각되면서 필터(64)를 지나 증류수차저장탱크(26)에 저장된다.The manufactured distillation aberration is stored in the distillation aberration storage tank 26 through the filter 64 while being cooled to room temperature while passing through the cooling tube 18.
그리고 영지, 구기자 및 생강 등과 같이 100℃ 정도의 온수에서 추출하는 것이 바람직한 차를 제조할 경우에는 차원료카트리지(62)에 분말입자가 100 ∼ 400메쉬 정도로 가공된 영지, 구기자 및 생강차 원료를 담아서 차성분추출탱크(24)에 장입하고, 3방향밸브(38)를 제 2 수증기 공급도관(36) 쪽으로 개방시키면 압력조절밸브(32)에 의해서 대기압 보다 높은 압력으로 가압된 수증기가 제 2 응축기(22) 내로 유입되고, 유입된 수증기는 경사지게 지그재그 형태로 고정된 냉각판(42)을 따라서 상승하면서 냉각되어 80℃를 초과하는 증류수와 100℃ 정도의 수증기가 섞인 상태로 차성분추출탱크(24)의 확대노즐형증류수분사기(56)를 통해서 차원료카트리지(62)에 담겨진 영지, 구기자 및 생강차 원료를 통과하므로 영지, 구기자 및 생강차 성분이 추출된 증류수차가 제조된다.In addition, when manufacturing tea, which is preferably extracted from hot water at about 100 ° C., such as ganoderma lucidum, goji berries and ginger, the raw material of ganoderma lucidum, wolfberry and ginger tea with powder particles processed to 100 to 400 mesh in the pulp cartridge 62 Charged into the component extraction tank 24 and opening the three-way valve 38 toward the second steam supply conduit 36, the steam condensed at a pressure higher than atmospheric pressure by the pressure regulating valve 32, the second condenser 22 ), The introduced steam is cooled while rising along the cooling plate 42 fixed in a zigzag form obliquely, distilled water of more than 80 ℃ and water vapor of about 100 ℃ mixed of the primary component extraction tank 24 The distillation aberration from which ganoderma lucidum, wolfberry and ginger tea components are extracted is passed through the expansion nozzle-type distilled water injector (56) through raw materials of ganoderma lucidum, wolfberry and ginger tea contained in the pulp material cartridge (62). The.
제조된 증류수차는 냉각관(18)을 거치면서 상온정도로 냉각되면서 필터(64)를 지나 증류수차저장탱크(26)에 저장된다.The manufactured distillation aberration is stored in the distillation aberration storage tank 26 through the filter 64 while being cooled to room temperature while passing through the cooling tube 18.
본 발명은 수증기로 부터 응축되는 증류수 또는 증류수를 포함한 수증기로 각종 차원료의 차성분을 연속적으로 유효하게 추출할 수 있고, 차종류에 따라서 운전모드를 선택할 수 도 있는 것이어서 다양한 증류수차를 단일설비에서 경제적으로 제조 할 수 있는 등의 장점이 있다.The present invention can continuously and effectively extract the tea components of various dimension materials with distilled water condensed from steam or water containing distilled water, and the operation mode can be selected according to the type of tea so that various distillation aberrations can be obtained in a single facility. It can be manufactured economically.
Claims (5)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR10-2000-0061216A KR100387008B1 (en) | 2000-10-18 | 2000-10-18 | A process for preparing a tea drawn by distilled water and its apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR10-2000-0061216A KR100387008B1 (en) | 2000-10-18 | 2000-10-18 | A process for preparing a tea drawn by distilled water and its apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| KR20020030883A KR20020030883A (en) | 2002-04-26 |
| KR100387008B1 true KR100387008B1 (en) | 2003-06-12 |
Family
ID=19694059
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| KR10-2000-0061216A KR100387008B1 (en) | 2000-10-18 | 2000-10-18 | A process for preparing a tea drawn by distilled water and its apparatus |
Country Status (1)
| Country | Link |
|---|---|
| KR (1) | KR100387008B1 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100781806B1 (en) * | 2005-08-31 | 2007-12-04 | 녹차원(주) | Equipment for being flavoured of green tea |
| KR100707498B1 (en) * | 2005-08-31 | 2007-04-13 | 녹차원(주) | Equipment for being flavoured of flour green tea |
| CN114680202B (en) * | 2022-03-04 | 2024-02-09 | 南阳和佳农林科技有限公司 | Tea extracting solution extracting system and method |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5568254A (en) * | 1978-11-17 | 1980-05-22 | Kawamura Yuji | Method and apparatus for intermittent extraction for preparation of soluble coffee |
| JPS59125843A (en) * | 1982-12-30 | 1984-07-20 | Morishita Yasuhiro | Preparation of instant green tea |
| KR880002028A (en) * | 1986-07-22 | 1988-04-28 | 김중길 | Stereoscopic lens |
| JPH10304822A (en) * | 1997-05-08 | 1998-11-17 | Harada Seichiya Kk | Instant green tea and its production |
-
2000
- 2000-10-18 KR KR10-2000-0061216A patent/KR100387008B1/en not_active IP Right Cessation
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5568254A (en) * | 1978-11-17 | 1980-05-22 | Kawamura Yuji | Method and apparatus for intermittent extraction for preparation of soluble coffee |
| JPS59125843A (en) * | 1982-12-30 | 1984-07-20 | Morishita Yasuhiro | Preparation of instant green tea |
| KR880002028A (en) * | 1986-07-22 | 1988-04-28 | 김중길 | Stereoscopic lens |
| JPH10304822A (en) * | 1997-05-08 | 1998-11-17 | Harada Seichiya Kk | Instant green tea and its production |
Also Published As
| Publication number | Publication date |
|---|---|
| KR20020030883A (en) | 2002-04-26 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN1679729A (en) | Chinese medicine preparation and set of apparatuses thereof | |
| CN104707349B (en) | Plate evaporator type MVR heat pump evaporation system | |
| CN105013199A (en) | Single-effect external-cycle concentrator and application thereof | |
| US10092855B2 (en) | CO2 extraction and filtration system | |
| CN1679730A (en) | Material of Chinese medicine extracting process and apparatus thereof | |
| CN100571836C (en) | Alcohol-soluble plant component extraction device | |
| CN110358631A (en) | A kind of Rosa Damascana extraction system and its extracting method | |
| CN105194903B (en) | Herbal concentrated solution production process | |
| CN113080280A (en) | Tea extraction equipment and method | |
| KR100387008B1 (en) | A process for preparing a tea drawn by distilled water and its apparatus | |
| CN206089622U (en) | High accuracy flower bud of lily magnolia flower extraction of essential oil device | |
| KR20130080421A (en) | Pure liquid production device | |
| CN105417609B (en) | A kind of regulation and control method of dissolved gas in boiler feedwater | |
| CN103695181B (en) | Preparation method of elsholtziae extract | |
| CN204767486U (en) | Single -action extrinsic cycle concentrator | |
| CN207418323U (en) | A kind of split type condensing unit | |
| CN102258882A (en) | Device for dynamic extraction by utilizing subcritical fluid | |
| CN211133067U (en) | Percolation extraction system | |
| CN105199833B (en) | A kind of method for comprehensive processing of dried ginger slice and ginger oil | |
| CN105289040B (en) | A kind of natural vegetable powder production technology | |
| CN206872471U (en) | Plug-in heat pressing type distilled water preparation system | |
| CN214571786U (en) | Plant essential oil refining equipment | |
| EP2384770B1 (en) | Method and device for cooling a sterilizer | |
| KR101916319B1 (en) | High efficiently coffee extracting system and method of extracting coffee using the same | |
| CN105733815B (en) | Natural spice preparation method and equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A201 | Request for examination | ||
| E902 | Notification of reason for refusal | ||
| E701 | Decision to grant or registration of patent right | ||
| GRNT | Written decision to grant | ||
| FPAY | Annual fee payment |
Payment date: 20090528 Year of fee payment: 7 |
|
| LAPS | Lapse due to unpaid annual fee |