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Solvent extraction 
 | 
Elimination of endotoxin/high purity 
 | 
Break PHA granules morphology 
 | 
  
 | 
No polymer degradation 
 | 
Hazards connected with halogenated solvents 
 | 
  
 | 
  
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High price/Low recovery 
 | 
Digestion by surfactants 
 | 
Treatment of high cell densities 
 | 
Low purity/Water waste 
 | 
  
 | 
No polymer degradation 
 | 
treatment needed 
 | 
Digestion by NaOCl 
 | 
High purity 
 | 
Degradation of the polymer 
 | 
Digestion by NaOCl and chloroform 
 | 
Low polymer degradation/ high purity 
 | 
High quantity of solvent needed 
 | 
Digestion by NaOCl and surfactants 
 | 
Limited degradation/low operating cost 
 | 
  
 | 
Digestion by chelate and surfactants 
 | 
High purity/low environmental pollution 
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Large volume of wastewater 
 | 
  
 | 
  
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Low degradation of the polymer 
 | 
Selective dissolution of NPCM 
 | 
High recovery and purity, low operating costs 
 | 
  
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Enzymatic digestion 
 | 
Good recovery 
 | 
High costs of enzymes 
 | 
Bead mill disruption 
 | 
No chemicals used 
 | 
Require several passes 
 | 
High pressure homogenization 
 | 
No chemicals used 
 | 
Poor disruption rate for low biomass levels 
 | 
  
 | 
  
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Low micronization 
 | 
Supercritical CO2 
 | 
Low cost and toxicity 
 | 
Low recovery 
 | 
Using cell fragility 
 | 
Use of weak extracting conditions 
 | 
  
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Air classification 
 | 
High purity 
 | 
Low recovery 
 | 
Dissolved air flotation 
 | 
No chemicals used 
 | 
Require several consecutive flotation steps 
 | 
| Spontaneous liberation | 
No extracting chemicals needed | 
Low recovery |