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發酵學概論
Biochemical engineering is no longer an academic
challenge
•US: most new professorships are biomolecularly oriented
•Europe: moving in same direction
–Long searches to find new professors of biochemical
engineering
–Most comes from industry (Patents, few publications)
–Solution: move towards biomolecular focus
•
Metabolic engineering
•
Complex control systems to re-engineer eucaryotic cells
•
Tissue engineering
Biotechnology –
major sectors
New pharma compounds
and materials, devices,

Agro-efficiency

Control systems, gene
therapy

Food quality
Agrochemicals

Biodegradation
End-of-pipe solution
Integrated processes

Biomass
Biofuels
Bioelectricity

•
Pharma
•
Agriculture
•
Environment
•
Chemistry
•
Energy

New materials
New compounds
New processes

Green Chemistry
經濟部篩選國內具潛力之生化產品
•原料藥與製劑
•血液製品
•檢驗試劑與檢驗儀器
•生物晶片
•人用疫苗
•生物農藥
•特用化學品
•科學化中藥
•食用色素

•菇類保健食品
•益生菌保健食品
•食品用酵素
•免疫食品
•傳統發酵食品
•保健食品
•酒類製品
•香料及化妝品
•機能性素材及食品
什麼是發酵?
發酵(fermentation)
一詞來自於拉丁語“ (fervere) 意為煮沸
發”
描述酵母菌將糖轉變成二氧化碳造成如沸騰之現象。
巴斯德認為發酵是酵母在無氧狀態下的呼吸過程。
生物化學上之定義為微生物在無氧時的代謝過程。
現在:人們把利用微生物在有氧與無氧條件下的生命活
動來製備微生物菌體或其代謝產物的過程通稱發酵
Industrial Microbiology and
Fermentation Technology
•Industrial Microbiology is the discipline
that uses microorganisms, usually grown on
a large scale, to produce valuable
commercial products or carry out
important chemical transformations.
•Fermentation Technology is the technology
to grow cells in a large scale with high
efficiency, it also includes product recovery
processes.
Microbial Products: Microbial Cells, Enzymes, Pharmaceutical
Products, Specialty Chemicals and Food Additives
發酵的演化與歷史
階段

第一階段
1900年以前

第二階段
1900-1945

第三階段
1945-1960

第四階段
1960-70

第五階段
1970-

產品

酒精、醋
(龍山文化、
埃及)

麵包酵母、丙
酮、丁醇、檸檬
酸

盤尼西林、
維他命B12、
纖維分解酵
素

蛋白質分解
酵素、單細
胞蛋白質、
抗生素

抗生素、必
須胺機酸、
胰島素

設備

木桶、銅器

鋼製儲桶、通氣

機械攪拌、
無菌操作

細胞固定化
連續式離心
機

流動化床與
氣舉式醱酵
槽

製程控制 憑經驗

溫度控制、pH
控制

可滅菌pH及
溶氧探針

電腦控制

回饋控制、
人工智慧控
制控制

使用菌種 使用代代相
傳之麴

使用純種生產菌
種

利用突變及
篩選改進菌
種

基因工程萌
芽

基因改質菌
種篩選較佳
生產菌種
發酵的分類
•
•
•
•
•

微生物菌體發酵:益生菌、藥用真菌
微生物產物發酵(一級代謝物):氨基酸、核酸、醣類
微生物代謝產物發酵(二級代謝物):抗生素、維生素
微生物轉化發酵:抗生素轉化、中草藥發酵
細胞培養:動、植物細胞培養
發酵特點
•1
•2
•3
•4
•5
•6
•7

發酵過程為全生命反應,數十個生化反應可串聯發生
常溫、常壓、耗能少
原料需求簡單,成本低
微生物種類繁多,具特異功能
生產條件標準化,可cGMP化
培養時間短,量產化簡單
可調控代謝途徑,產品多樣化
傳統發酵技術應用
發酵應用範圍包括:
食品工業—
• 製造麵包,澱粉分解為較小的片段,同時放出二氧化
碳
• 釀酒過程,使糖類分解成酒精同時放出二氧化碳
• 茶製工藝,使茶葉中的沒食子茶素分解再合成為茶黃
素,使茶葉成為紅茶
• 醬油、豆腐乳、乳酪、酸奶、紅麴、味增等都需要發
酵過程。
製藥工業—
• 藉由大型生物反應器-醱酵槽,來進行抗生素、氨基酸
等生產。
近代發酵技術應用〔一〕
•製藥界:基因工程蛋白質藥物(胰島素)、新一
代的抗生素及非抗生素(降血脂)產品。
•保健食品:益生菌產品、乳酸菌產品、發酵乳
品、食用藥用菇菌類產品、新式發
酵飲料、機能性飲料
•環保領域:環境微生物製劑、農漁牧業用的處理
微生物、廢棄物、污染源處理、廢水
處理、水質淨化、廚餘有機堆肥
近代發酵技術應用〔二〕
•農業產業:動物疫苗、動物用生長荷爾蒙、生
物農藥及土地改質的生物製劑
•化妝品領域:保濕產品如:透明質酸
細胞活性因子如:SKⅡ的pitera
醱酵技術之目標
•沒有雜菌
•最佳生長狀態

–培養菌快速生長
–代謝產物快速累積

•有效率之回收純化
•最有效率之生產程序
(單位時間、單位成本生產最大產量)
影響發酵之參數
生物參數
菌種特性
菌種年齡
繼代次數
接菌體積

化學參數
培養基組成
發酵條件

物理參數
發酵槽體設計
環境刺激
代謝調控
Flowsheet for developing an industrial
microbial fermentation process
•Strain selection
•Laboratory process development
•Pilot Scale up
•Industrial Scale up
•Downstream process development
•Product packaging techniques
•Other commercial consideration
•Examples
Fermentation Process
Typical Fermentation Train
Total time 3-20 days

Frozen
Seed

Seed
Flask

Pre-Seed
Fermenter

Seed
Fermemter

Production
Fermenter
Strain Selection
–
Purchase from Culture Collections
–
Screening of nature circumstances
–
Genetic engineering
–
Mutations
–
Cell biology techniques
International Culture Collections

Domestically, strains can be purchased from: CGMCC or
China General Microbiological Culture Collection Center
Screening of nature circumstances
Genetic
Engineering
Incorporation into
artificial plasmids of
genes from a wide
variety of sources has
made possible the
transfer of genetic
material across
virtually any species
barrier
Various high value
added products have
been produced from
Genetic engineering
methods
Mutation
Via chemical
or physical,
and biological
means
Cell Biology Techniques
•
Protoplast fusion (promote high frequencies
of genetic recombinants)
–removing the cell wall with lytic enzymes in the
presence of osmotic stabilizers.
–In the presence of fusogenic agent such as
polyethylene glycol (PEG), protoplasts are
induced to fuse and form transient hybrids or
diploids.
–Regeneration of viable cells from the fused
protoplasts.
Laboratory Process Development
Shake Flask Experiments
Optimization of conditions
for cell growth and product
formation using shake flask
experiments:
1. pH
2. Temperature
3. Dissolved oxygen (DO)
4. Substrate choice
5. Maximal and optimal
substrate concentration
6. Others
Laboratory
Process
Development
Fermentor
Experiments
• Agitation
• Cooling and heating
• Air inlet and outlet
• pH control
• Nutrient addition
• Inoculation
• Viewing port
Laboratory Process Development
Lab scale fermentor experiments
•
Batch process
•
Fed-batch process
•
Continuous process
•
Semi-continuous
process
Process control and monitoring
•Process parameters to be monitors
Agitation
pH
Cell Dry Weight

Product
Sugar consumption
Temperature

Fermentation time (h)
Computer softwares have been developed to monitor and change the process on line
Pilot Scale Up
•Scale up: The transfer of a process from smallscale laboratory equipment to large-scale
commercial equipment

•
Pilot experiment
– test the feasibility of the lab scale
To
fermentation process in a semi-industrial
scale
–
Pilot fermentors normally have a size ranging
from 100 L to 10,000 L, depending on the
products to be mass produced later.
Problems emerging during the scale up
•As the size of the equipment is increased, the surfacevolume ratio changes
•Large fermentor has much more volume for a given
surface area, it is obviously more difficult to mix the big
tank than the small flask
•In scale up studies on aerobic fermentations, oxygen
rate in the fermentor is best kept constant as the size of
the fermentor is increased.
–How to keep DO constant?
•
Increase stirring rate
•
Increase air pressure
•
Use pure oxygen
•
Increase air inlet
桌上型5L發酵槽
100L發酵槽
1噸發酵槽
1噸發酵槽
抗生素生產工廠
Product Recovery
•What purity is necessary?
–acetic acid or alcohol little purification
–industrial enzymes: moderate purity
–food additives have high purity
–pharmaceuticals super purity

•What is the concentration of the product?
Product Recovery
•Is the product in the cell or secreted?
–enzymes and other proteins in cell require cell
harvest and extraction
–secreted products allow for continuous
fermentation
–secreted products reduce costs of purification.
Why?

•Can we improve secretion?
Downstream Process
Development
Filter (press filter)

Chromatography
Downstream
Process
Development

Continuous
centrifuges
Unit Operations in Downstream Separation
• Microfilters
• Ultrafiltration
Size
• Gel chromatography
• Reverse osmosis
Diffusivity
• Dialysis
• Electrodialysis
Ion exchange
• Ion exchange
• Distillation/freeze dry
Vapour temperature, pressure
Solubility
• Solvent extraction
Surface activity
• Foam and bubble fractionation
• Ultracentrifugation
• Centrifugation
Density
• Liquid cyclones
• Gravity sedimentation
Processing fermentation broth
Fermentation
Dilute slurry

Centrifugation
Filtration
Sedimentation
Clarified liquor

Concentrated slurry

Filtration

Dewatering
Drying

Bright liquor

Dry Biomass
Centrifugation: Continuous
centrifugation
Disc-Centrifuges

Solids-retaining
centrifuge

Periodically
solids-ejecting
centrifuge

Nozzle with pressurized
discharge of concentrate

Nozzle with peripheral
nozzles

Periodically
solids-ejecting
centrifuge with
axial channels
Product Packaging
Techniques
•Steril Packaging Techniques for Medical
Applications and Food Preservation
•Pyrogen Free and Steril Packaging for Injection
Purpose
•Freeze Dry Packaging for Foods or Medicines
•Dewatered Packaging (such as Dry Yeast)
•Normal Food Packaging (such as Na-glutamate)
•Salty Packaging
•Preservation Chemicals
•Ordinary Packaging
Other Commercial Consideration
Strengths and weaknesses of biotechnological processes

•Strengths
– Reliance on renewable
feedstocks
– Versatility with different
feedstocks
– Food, feed and drug
applications
– Fine chemicals to bulk
chemical applications
– Low temperature
– Operation in aqueous media
– Several reactions achieved in
a single fermentation step
– High level of automation
– Stereospecificity
– Complex molecules
converted and/or produced
–“
Benign”
effluents produced

•Weaknesses
– Feedstocks are oxidized and
unsuitable for many applications
– Feedstock costs fluctuate
– Sterilization is a major cost
– Product often in dilute aqueous
solutions
– Product recovery costly
– Equipment costs high
– Reactions slow leading to poor
volumetric productivity
– Complicated reaction conditions
– Mainly batch operation
– High cell (catalyst) regeneration
costs
– High BOD wastes
Other Commercial Consideration
Cost Evaluation

•Outline of total capital investment
•Fixed capital
–Direct costs (Land, site development, buildings,
processing, services)
–Indirect costs (Engineering, construction,
Contingency, Fees)
–Start-up costs

•Working capital
–Inventory, accounts receivable, account payable

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