JP6529132B2 - 膜濃縮法及び凍結濃縮法による濃縮製品の製造方法 - Google Patents
膜濃縮法及び凍結濃縮法による濃縮製品の製造方法 Download PDFInfo
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- 238000000926 separation method Methods 0.000 claims description 110
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
- A23C1/00—Concentration, evaporation or drying
- A23C1/06—Concentration by freezing out the water
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
- A23C9/00—Milk preparations; Milk powder or milk powder preparations
- A23C9/14—Milk preparations; Milk powder or milk powder preparations in which the chemical composition of the milk is modified by non-chemical treatment
- A23C9/142—Milk preparations; Milk powder or milk powder preparations in which the chemical composition of the milk is modified by non-chemical treatment by dialysis, reverse osmosis or ultrafiltration
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
- A23C9/00—Milk preparations; Milk powder or milk powder preparations
- A23C9/14—Milk preparations; Milk powder or milk powder preparations in which the chemical composition of the milk is modified by non-chemical treatment
- A23C9/142—Milk preparations; Milk powder or milk powder preparations in which the chemical composition of the milk is modified by non-chemical treatment by dialysis, reverse osmosis or ultrafiltration
- A23C9/1427—Milk preparations; Milk powder or milk powder preparations in which the chemical composition of the milk is modified by non-chemical treatment by dialysis, reverse osmosis or ultrafiltration by dialysis, reverse osmosis or hyperfiltration, e.g. for concentrating or desalting
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
- B01D61/04—Feed pretreatment
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/14—Ultrafiltration; Microfiltration
- B01D61/16—Feed pretreatment
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/0004—Crystallisation cooling by heat exchange
- B01D9/0013—Crystallisation cooling by heat exchange by indirect heat exchange
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/0036—Crystallisation on to a bed of product crystals; Seeding
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/02—Crystallisation from solutions
- B01D9/04—Crystallisation from solutions concentrating solutions by removing frozen solvent therefrom
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Water Supply & Treatment (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Crystallography & Structural Chemistry (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Life Sciences & Earth Sciences (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Nanotechnology (AREA)
- Dairy Products (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Description
被処理流体を冷却し、逆浸透膜、ナノ濾過膜、限外濾過膜、精密濾過膜のいずれかを用いて、固形分濃度を1.5倍以上に膜濃縮して、膜濃縮被処理流体を調製(製造)する膜濃縮工程と、
膜濃縮被処理流体を冷却し、前記膜濃縮被処理流体に前記膜濃縮被処理流体の氷結晶を生成させ、前記氷結晶が生成されたことによって前記膜濃縮被処理流体が更に濃縮された濃縮被処理流体と、前記氷結晶との混合流体にする氷結晶生成工程と、
前記混合流体を前記濃縮被処理流体と前記氷結晶とに分離して、前記濃縮被処理流体を取り出す氷結晶分離工程と
を備えている膜濃縮法及び凍結濃縮法による濃縮製品の製造方法
である。
前記膜濃縮被処理流体を調製する処理と、前記膜濃縮被処理流体が更に濃縮された濃縮被処理流体と、前記氷結晶との混合流体にする処理と、前記混合流体を前記濃縮被処理流体と前記氷結晶とに分離して、前記濃縮被処理流体を取り出す処理とを回分式で行うことを特徴とする請求項1記載の凍結濃縮法による濃縮製品の製造方法
である。
前記氷結晶分離工程で取り出した前記濃縮被処理流体について、前記氷結晶生成工程と、これに引き続く前記氷結晶分離工程とを1回で乃至複数回で繰り返して行うことを特徴とする請求項1又は2記載の膜濃縮法及び凍結濃縮法による濃縮製品の製造方法
である。
2回目以降の前記氷結晶生成工程において、直前の前記氷結晶分離工程において取り出された前記濃縮被処理流体に、直前の氷結晶分離工程で分離された前記氷結晶に相当する容積の前記膜濃縮被処理流体を添加して新たに濃縮処理される被処理流体とし、2回目以降の前記氷結晶生成工程を行うことを特徴とする請求項3記載の膜濃縮法及び凍結濃縮法による濃縮製品の製造方法
である。
前記被処理流体が生乳、脱脂乳、発酵乳(液状発酵乳、ドリンクヨーグルト等)、乳酸菌飲料、ホエイ、バターミルクのいずれかであることを特徴とする請求項1〜4のいずれか一項記載の膜濃縮法及び凍結濃縮法による濃縮製品の製造方法
である。
未処理の製品に比べて、香気成分が0.7倍以上で保持されることを特徴とする、請求項1〜5のいずれか一項記載の膜濃縮法及び凍結濃縮法による濃縮製品の製造方法
である。
未処理の製品に比べて、有用微生物の生菌数が0.7倍以上で保持されることを特徴とする、請求項1〜6のいずれか一項記載の膜濃縮法及び凍結濃縮法による濃縮製品の製造方法
である。
被処理流体として、生乳(原料乳、固形分濃度:12.3重量%)を100kgで用いた。この生乳を約10℃に保持し、逆浸透膜(RO膜)を用いて膜濃縮処理することで、膜濃縮被処理流体(原料乳の約1.8倍濃縮、固形分濃度:約22重量%)を得た。この膜濃縮被処理流体を、結晶生成タンク(ジャケット付きタンク)(内径:20cm、高さ:100cm、攪拌羽根の形状:門型、容量:140kg)に投入した。
被処理流体として、バターミルク(原料乳、固形分濃度:10.6重量%)を100kgで用いた。このバターミルクを約10℃に保持し、逆浸透膜(RO膜)を用いて膜濃縮処理することで、膜濃縮被処理流体(原料乳の約1.7倍濃縮、固形分濃度:約18重量%)を得た。この膜濃縮被処理流体を、結晶生成タンク(ジャケット付きタンク)(内径:20cm、高さ:100cm、攪拌羽根の形状:門型、容量:140kg)に投入した。
被処理流体として、脱脂乳(原料乳、固形分濃度:9.0重量%)を100kgで用いた。この脱脂乳を約10℃に保持し、逆浸透膜(RO膜)を用いて膜濃縮処理することで、膜濃縮被処理流体(原料乳の約1.8倍濃縮、固形分濃度:約16重量%)を得た。この膜濃縮被処理流体を、結晶生成タンク(ジャケット付きタンク)(内径:20cm、高さ:100cm、攪拌羽根の形状:門型、容量:140kg)に投入した。
図2に示す工程に沿って、回分的に処理を行う場合を説明する。
被処理流体として、生乳(原料乳、固形分濃度:12.3重量%)を100kgで用いた。この生乳を、結晶生成タンク(ジャケット付きタンク)(内径:20cm、高さ:100cm、攪拌羽根の形状:門型、容量:140kg)に投入した。
Claims (7)
- 乳成分を含む被処理流体を冷却し、逆浸透膜、ナノ濾過膜、限外濾過膜、精密濾過膜のいずれかを用いて、固形分濃度を1.5倍以上に膜濃縮して、膜濃縮被処理流体を調製する膜濃縮工程と、
膜濃縮被処理流体を冷却し、前記膜濃縮被処理流体に前記膜濃縮被処理流体の氷結晶を生成させ、前記氷結晶が生成されたことによって前記膜濃縮被処理流体が更に濃縮された濃縮被処理流体と、前記氷結晶との混合流体にする氷結晶生成工程と、
結晶分離カラムにより前記混合流体を前記濃縮被処理流体と前記氷結晶とに分離して、前記濃縮被処理流体を取り出す氷結晶分離工程と
を備えている膜濃縮法及び凍結濃縮法による濃縮製品の製造方法。 - 前記膜濃縮被処理流体を調製する処理と、前記膜濃縮被処理流体が更に濃縮された濃縮被処理流体と、前記氷結晶との混合流体にする処理と、前記混合流体を前記濃縮被処理流体と前記氷結晶とに分離して、前記濃縮被処理流体を取り出す処理とを回分式で行うことを特徴とする請求項1記載の凍結濃縮法による濃縮製品の製造方法。
- 前記氷結晶分離工程で取り出した前記濃縮被処理流体について、前記氷結晶生成工程と、これに引き続く前記氷結晶分離工程とを1回で乃至複数回で繰り返して行うことを特徴とする請求項1又は2記載の膜濃縮法及び凍結濃縮法による濃縮製品の製造方法。
- 2回目以降の前記氷結晶生成工程において、直前の前記氷結晶分離工程において取り出された前記濃縮被処理流体に、直前の氷結晶分離工程で分離された前記氷結晶に相当する容積の前記膜濃縮被処理流体を添加して新たに濃縮処理される被処理流体とし、2回目以降の前記氷結晶生成工程を行うことを特徴とする請求項3記載の膜濃縮法及び凍結濃縮法による濃縮製品の製造方法。
- 前記被処理流体が原料乳、生乳、発酵乳、ホエイ、バターミルクのいずれかであることを特徴とする請求項1〜4のいずれか一項記載の膜濃縮法及び凍結濃縮法による濃縮製品の製造方法。
- 未処理の製品に比べて、香気成分が0.7倍以上で保持されることを特徴とする、請求項1〜5のいずれか一項記載の膜濃縮法及び凍結濃縮法による濃縮製品の製造方法。
- 未処理の製品に比べて、有用微生物の生菌数が0.7倍以上で保持されることを特徴とする、請求項1〜6のいずれか一項記載の膜濃縮法及び凍結濃縮法による濃縮製品の製造方法。
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US10139317B2 (en) * | 2015-10-30 | 2018-11-27 | South Dakota Board Of Regents | Methods and apparatuses for trace and ultratrace analysis |
JP6238254B2 (ja) | 2016-05-12 | 2017-11-29 | 株式会社明治 | 固液分離装置の固液分離カラム内における固液分布検出方法及び検出装置 |
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PL3040108T3 (pl) | 2021-06-14 |
US20160205959A1 (en) | 2016-07-21 |
JP6797952B2 (ja) | 2020-12-09 |
EP3040108A1 (en) | 2016-07-06 |
DK3040108T3 (da) | 2021-04-06 |
HK1226019B (zh) | 2017-09-22 |
JPWO2015030162A1 (ja) | 2017-03-02 |
CA2922831C (en) | 2021-11-09 |
AU2014312814A1 (en) | 2016-03-17 |
WO2015030162A1 (ja) | 2015-03-05 |
SG11201601448RA (en) | 2016-03-30 |
AU2014312814B2 (en) | 2018-01-25 |
CN105682762A (zh) | 2016-06-15 |
US9913484B2 (en) | 2018-03-13 |
CA2922831A1 (en) | 2016-03-05 |
NZ717499A (en) | 2021-08-27 |
EP3040108B1 (en) | 2021-02-17 |
EP3040108A4 (en) | 2017-05-03 |
CN105682762B (zh) | 2018-09-04 |
JP2019069447A (ja) | 2019-05-09 |
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