US2017137763A1PendingUtilityA1

Mass-cultivation system for microalgae

Assignee: KOREA IND TECH INSTPriority: Jun 30, 2014Filed: Feb 10, 2015Published: May 18, 2017
Est. expiryJun 30, 2034(~7.9 yrs left)· nominal 20-yr term from priority
C12M 31/10C12M 23/58C12M 47/20C12M 33/00C12M 35/04C12M 21/02C12M 47/02C12M 29/18
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Claims

Abstract

Disclosed is a mass-cultivation system for microalgae, including a reactor that contains a cultivation liquid in the interior thereof, wherein the liquid includes functional particles. According to the mass-cultivation system for microalgae according to the present invention, because various functions that are necessary for cultivation of microalgae may be uniformly distributed in a cultivation liquid by allowing functional particles having various functions to flow in the cultivation liquid, a suitable environment may be created based on the cultivation of a large amount of microalgae and the growth of microalgae so that a high efficiency cultivation system may be realized while the problems of mass-cultivation of an existing cultivation system may be solved.

Claims

exact text as granted — not AI-modified
1 . A mass-cultivation system for microalgae, comprising:
 a reactor that contains a cultivation liquid in the interior thereof,   wherein the liquid comprises functional particles.   
     
     
         2 . The mass-cultivation system for microalgae of  claim 1 , further comprising:
 a recycling unit and a recover unit that are fluid-communicated with the reactor,   wherein the functional particles are introduced into the recycling unit such that functions thereof are recycled.   
     
     
         3 . The mass-cultivation system for microalgae of  claim 2 , wherein the functional particles comprises one or more of light supply particles, nutrient supply particles, harmful substance adsorption particles, CO 2  supply particles, and microalgae recovery particles. 
     
     
         4 . The mass-cultivation system for microalgae of  claim 3 , wherein each of the light supply particles, the nutrient supply particles, the harmful substance adsorption particles, and the CO 2  supply particles comprises a hollow capsule that defines an outer side of the particle. 
     
     
         5 . The mass-cultivation system for microalgae of  claim 4 , wherein the interiors of the capsules of the light supply particles are filled with a light emitting material. 
     
     
         6 . The mass-cultivation system for microalgae of  claim 4 , wherein the interiors of the capsules of the nutrient supply particles are filled with a nutrient supply material. 
     
     
         7 . The mass-cultivation system for microalgae of  claim 4 , wherein the interiors of the capsules of the CO 2  supply particles are filled with CO 2 . 
     
     
         8 . The mass-cultivation system for microalgae of  claim 4 , wherein the interiors of the capsules of the harmful substance adsorption particles are filled with a harmful substance adsorption material. 
     
     
         9 . The mass-cultivation system for microalgae of  claim 4 , wherein a plurality of bosses are formed on surfaces of the microalgae recovery particles to capture cultivated microalgae. 
     
     
         10 . The mass-cultivation system for microalgae of  claim 4 , wherein one or more of the light supply particles, the nutrient supply particles, the harmful substance adsorption particles, the CO 2  supply particles, and the microalgae recovery particles have a magnetism, and
 wherein the recycling unit or the recovery unit has a magnetism so that the particles having a magnetism are separated to flow to the recycling unit or the recovery unit.   
     
     
         11 . The mass-cultivation system for microalgae of  claim 4 , wherein the light supply particles, the nutrient supply particles, the harmful substance adsorption particles, the CO 2  supply particles, and the microalgae recovery particles have a specific gravity in a predetermined range. 
     
     
         12 . The mass-cultivation system for microalgae of  claim 11 , wherein the light supply particles, the nutrient supply particles, the harmful substance adsorption particles, the CO 2  supply particles, and the microalgae recovery particles have different specific gravities in the predetermined range so that the particles are separated to flow to the recycling unit or the recovery unit. 
     
     
         13 . The mass-cultivation system for microalgae of  claim 4 , wherein two or more of the light supply particles, the nutrient supply particles, the harmful substance adsorption particles, the CO 2  supply particles, and the microalgae recovery particles are connected to each other by a connection line. 
     
     
         14 . The mass-cultivation system for microalgae of  claim 5 , wherein the recycling unit comprises a light source or a power supply unit, and
 wherein the light supply particles flow to the recycling unit such that the light emitting material filled in the light supply particles is recycled by the light source or the power supply unit and is reintroduced into the reactor.   
     
     
         15 . The mass-cultivation system for microalgae of  claim 4 , wherein the recycling unit contains a nutrient supply material, a light emitting material, a harmful substance adsorption material, or CO 2 , and
 wherein the nutrient supply particles, the harmful substance adsorption particles, or the CO 2  supply particles flow to the recycling unit such that the nutrient supply material, the harmful substance adsorption material, or CO 2  contained in the recycling unit are refilled and are reintroduced into the reactor.   
     
     
         16 . The mass-cultivation system for microalgae of  claim 9 , wherein the microalgae recovery particles flow to the recovery unit and are reintroduced into the reactor, and
 wherein the recovery unit comprises a freezer unit or a drying unit that freezes or dries the microalgae captured by the microalgae recovery particles.   
     
     
         17 . The mass-cultivation system for microalgae of  claim 16 , wherein the recovery unit separates the captured microalgae from the microalgae recovery particles by rotating the frozen or dried microalgae recovery particles or applying ultrasonic waves or vibration to the microalgae recovery particles. 
     
     
         18 . The mass-cultivation system for microalgae of  claim 3 , wherein the reactor comprises:
 a primary reactor, a secondary reactor that is fluid-communicated with the primary reactor, and a tertiary reactor that is fluid-communicated with the secondary reactor,   wherein the recycling unit comprises:   a first recycling unit that is fluid-communicated with the primary reactor, a second recycling unit that is fluid-communicated with the secondary reactor, and a third recycling unit that is fluid-communicated with the tertiary reactor, and   wherein the recovery unit is fluid-communicated with the tertiary recycling unit.   
     
     
         19 . The mass-cultivation system for microalgae of  claim 18 , wherein each of the light supply particles, the nutrient supply particles, the harmful substance adsorption particles, and the CO 2  supply particles comprises a hollow capsule that defines an outer side of the particle. 
     
     
         20 . The mass-cultivation system for microalgae of  claim 19 , wherein the interiors of the capsules of the light supply particles are filled with a light emitting material. 
     
     
         21 . The mass-cultivation system for microalgae of  claim 19 , wherein the interiors of the capsules of the nutrient supply particles are filled with a nutrient supply material. 
     
     
         22 . The mass-cultivation system for microalgae of  claim 19 , wherein the interiors of the capsules of the CO 2  supply particles are filled with CO 2 . 
     
     
         23 . The mass-cultivation system for microalgae of  claim 19 , wherein the interiors of the capsules of the harmful substance adsorption particles are filled with a harmful substance adsorption material. 
     
     
         24 . The mass-cultivation system for microalgae of  claim 19 , wherein a plurality of bosses or cilia are formed on surfaces of the microalgae recovery particles to capture cultivated microalgae. 
     
     
         25 . The mass-cultivation system for microalgae of  claim 19 , wherein one or more of the light supply particles, the nutrient supply particles, the harmful substance adsorption particles, the CO 2  supply particles, and the microalgae recovery particles have a magnetism, and
 wherein the recycling units or the recovery unit has a magnetism so that the particles having a magnetism are separated to flow to the recycling units or the recovery unit.   
     
     
         26 . The mass-cultivation system for microalgae of  claim 19 , wherein the light supply particles, the nutrient supply particles, the harmful substance adsorption particles, the CO 2  supply particles, and the microalgae recovery particles have a specific gravity in a predetermined range. 
     
     
         27 . The mass-cultivation system for microalgae of  claim 26 , wherein the light supply particles, the nutrient supply particles, the harmful substance adsorption particles, the CO 2  supply particles, and the microalgae recovery particles have different specific gravities in the predetermined range so that the particles are separated to flow to the recycling units or the recovery unit. 
     
     
         28 . The mass-cultivation system for microalgae of  claim 19 , wherein two or more of the light supply particles, the nutrient supply particles, the harmful substance adsorption particles, the CO 2  supply particles, and the microalgae recovery particles are connected to each other by a connection line. 
     
     
         29 . The mass-cultivation system for microalgae of  claim 20 , wherein the light supply particles, the nutrient supply particles, the CO 2  supply particles, and the harmful substance adsorption particles circulate between the primary reactor and the first recycling unit, and between the secondary reactor and the second recycling unit, and
 wherein the microalgae recovery particles circulate between the tertiary reactor and the third recycling unit.   
     
     
         30 . The mass-cultivation system for microalgae of  claim 29 , wherein the amounts of the light emitting material, the nutrient supply material, CO 2 , and the harmful substance adsorption material that are respectively filled in the light supply particles, the nutrient supply particles, the CO 2  supply particles, and the harmful substance adsorption material that circulate the secondary reactor and the second recycling unit may be larger than the amounts of the light emitting material, the nutrient supply material, CO 2 , and the harmful substance adsorption material that are respectively filled in the light supply particles, the nutrient supply particles, the CO 2  supply particles, and the harmful substance adsorption material that circulate the primary reactor and the first recycling unit. 
     
     
         31 . The mass-cultivation system for microalgae of  claim 29 , wherein each of the first and second recycling units comprises a light source or a power supply unit, and
 wherein the light supply particles flow to the first and second recycling units such that the light emitting material filled in the light supply particles is recycled by the light source or the power supply unit and is reintroduced into the primary reactor and the secondary reactor.   
     
     
         32 . The mass-cultivation system for microalgae of  claim 21 , wherein the first and second recycling units contain a nutrient supply material, a light emitting material, a harmful substance adsorption material, or CO 2 , and
 wherein the nutrient supply particles, the harmful substance adsorption particles, or the CO 2  supply particles flow to the first and second recycling units such that the nutrient supply material the light emitting material, the harmful substance adsorption material or CO 2  contained in the first and second recycling units is refilled and is reintroduced into the primary reactor  110  and the secondary reactor.   
     
     
         33 . The mass-cultivation system for microalgae of  claim 24 , wherein the microalgae recovery particles flow to the recovery unit and are reintroduced into the tertiary reactor, and
 wherein the recovery unit comprises a freezer unit or a drying unit that freezes or dries the microalgae captured by the microalgae recovery particles.   
     
     
         34 . The mass-cultivation system for microalgae of  claim 33 , wherein the recovery unit separates the captured microalgae from the microalgae recovery particles by rotating the frozen or dried microalgae recovery particles or applying vibration to the microalgae recovery particles. 
     
     
         35 . The mass-cultivation system for microalgae of  claim 3 , wherein two or more of light supply particles, nutrient supply particles, harmful substance adsorption particles, CO 2  supply particles, and microalgae recovery particles are integrally formed.

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