Continuous Flow Reactor for Conversion of Wastewater to Biohydrogen Using Activated Sludge and Microalgae

Patent metadata

Field	Value
Publication number	US-2025109414-A1
Application number	US-202318374407-A
Country	US
Kind code	A1
Filing date	Sep 28, 2023
Priority date	Sep 28, 2023
Publication date	Apr 3, 2025
Grant date	—

Abstract

Apparatus 101 for producing a continuous stream of biohydrogen includes a continuous flow stirred tank reactor (CSTR) 12, lighting arrangement 13; ports 14; peristaltic pumps 16; and gas chromatograph (GC) 18. The CSTR 12 includes internal bioreactor chamber 20; a photosynthesizing microorganism inlet stream 22.1 for delivering Chlorella vulgaris; an organic waste inlet stream 22.2 for delivering wastewater activated sludge (WWAS); and a nutrient inlet stream 22.3 for delivering nutrients into the chamber 20; an outlet stream 24; and stirrers for stirring the contents of the chamber. The lighting 13 is provided by lamps 26 for transmitting light through a transparent sidewall of the chamber 20. The ports 14 and CG 18 are for taking measurements from the chamber 20. The pumps 16 control flowrate of the streams 22.1, 22.2, 22.3 and 24 for regulating biohydrogen production from fermentation while Chlorella vulgaris consumes oxygen to avoid biohydrogen conversion into methane.

First claim

1 . An apparatus for producing a stream of biohydrogen, the apparatus including:
a bioreactor without any gas-permeable porous material with open pore structure, the bioreactor having: (a) an internal bioreactor chamber; (b) three separate inlet streams, each inlet stream leading into the bioreactor chamber; and (c) an outlet stream leading out of the bioreactor chamber and through which the contents of the bioreactor chamber can flow out of the bioreactor chamber; fluid flow controlling means for independently controlling a fluid flow through the associated inlet stream for controlling fluid flow via the associated inlet stream into the bioreactor chamber; wherein the inlet streams comprise: (i) a photosynthesizing microorganism inlet stream; (ii) an organic waste inlet stream; and (iii) a nutrient inlet stream; and lighting means for exposing the photosynthesizing microorganism to light, thereby to enable photosynthesis.

2 . The apparatus as claimed in claim 1 , wherein the stream of biohydrogen is a continuous stream of biohydrogen.

3 . The apparatus as claimed in claim 1 , wherein the bioreactor has a stirring means for stirring the contents of the bioreactor chamber.

4 . The apparatus as claimed in claim 1 , wherein the bioreactor is in the form of a continuous flow stirred tank reactor (CSTR).

5 . The apparatus as claimed in claim 1 , wherein the photosynthesizing microorganisms is in the form of microalgae.

6 . The apparatus as claimed in claim 1 , wherein the microalgae is Chlorella vulgaris.

7 . The apparatus as claimed in claim 1 , wherein the organic waste sludge is in the form of wastewater activated sludge (WWAS).

8 . The apparatus as claimed in claim 1 , wherein the apparatus includes one or more ports in flow communication with the bioreactor chamber, wherein said one or more ports are selected from the group consisting of: a pH control port, a hydrogen sensor port, an oxygen sensor port, a gas collection port, a gas sensor port; and combinations thereof.

9 . The apparatus as claimed in claim 1 , wherein the fluid flow controlling means is further configured for controlling a fluid flow through the outlet stream for controlling fluid flow via the outlet stream out of the bioreactor chamber.

10 . The apparatus as claimed in claim 9 , wherein the fluid flow controlling means includes one or more of a photosynthesizing microorganism inlet stream controller; an organic waste inlet stream controller; a nutrient inlet stream controller; and an outlet stream controller; for controlling, respectively, a fluid flow through the photosynthesizing microorganism inlet stream; the organic waste inlet stream; the nutrient inlet stream; the outlet stream.

11 . The apparatus as claimed in 10 , wherein the fluid flow controlling means is operable for controlling one or more of the hydraulic retention time; and the flow rates through the bioreactor.

12 . The apparatus as claimed in 11 , wherein the photosynthesizing microorganism inlet stream controller; the organic waste inlet stream controller; the nutrient inlet stream controller; and the outlet stream controller is in the form of a photosynthesizing microorganism inlet pump; an organic waste inlet pump; a nutrient inlet stream pump; an outlet stream pump.

13 . The apparatus as claimed in 1 , wherein the lighting means is provided by a light transmittable sidewall defining the bioreactor chamber, and through which light may enter the bioreactor chamber.

14 . The apparatus as claimed in 13 , wherein the lighting means further includes one or more light source arranged for transmitting light via the light transmittable sidewall into the interior of the bioreactor chamber.

15 . The apparatus as claimed in 14 , wherein said one or more light source is in the form of a lamp.

16 . The apparatus as claimed in claim 1 , including the inlet streams.

17 . A method for producing a stream of biohydrogen, the method including:
providing a bioreactor including an internal bioreactor chamber; providing and controlling three separate inlet streams leading into the bioreactor chamber, wherein each separate inlet stream includes:
(i) a photosynthesizing microorganism inlet stream;
(ii) an organic waste inlet stream; and
(iii) a nutrient inlet stream;
providing and controlling an outlet stream leading out of the bioreactor chamber, exposing the photosynthesizing microorganism to light, thereby to enable photosynthesis.

18 . The method as claimed in claim 17 , wherein the stream of biohydrogen is a continuous stream of biohydrogen.

19 . The method as claimed in claim 17 , wherein providing a bioreactor comprises providing a stirring means for stirring the contents of the bioreactor chamber.

20 . The method as claimed in claim 17 , wherein providing a bioreactor comprises providing a continuous flow stirred tank reactor (CSTR).

21 . The method as claimed in claim 17 , wherein the photosynthesizing microorganisms is provided in the form of microalgae, preferably Chlorella vulgaris.

22 . The method as claimed in claim 17 , wherein the organic waste sludge is provided in the form of wastewater activated sludge (WWAS).

23 . The method as claimed in claim 17 , wherein the method includes providing one or more ports in flow communication with the bioreactor chamber.

24 . The method as claimed in claim 23 , wherein said one or more ports provided are selected from the group consisting of: a pH control port, a hydrogen sensor port, an oxygen sensor port, a gas collection port, a gas sensor port; and combinations thereof.

25 . The method as claimed in claim 17 , wherein the method includes controlling a hydraulic retention time.

26 . The method as claimed in claim 17 , wherein the method further includes controlling a flow rate through the bioreactor.

27 . The method as claimed in claim 17 , wherein the photosynthesizing microorganisms is provided in the form of Chlorella vulgaris and wherein the organic waste sludge is provided in the form of wastewater activated sludge (WWAS); and wherein the method includes controlling a ratio of Chlorella vulgaris to WWAS such that the ratio is 1:1.5.

28 . The apparatus as claimed in claim 1 , wherein the three separate inlet streams are for continuous inflow of influent.

29 . The apparatus as claimed in claim 1 , wherein the outlet stream is for continuous outflow of effluent.

Assignees

• Univ United Arab Emirates

Inventors

• Aly Hassan Ashraf
• Javed Muhammad Asad

Classifications

• C12M21/04

  for producing gas, e.g. biogas (digesters for manure with production of biogas A01C3/028, biological treatment of water, waste water or sewage C02F3/00, C02F11/02, preparation of natural gas or syngas C10L3/06, C10L3/10) · CPC title

• C12N1/12

  Unicellular algae; Culture media therefor (as new plants A01H13/00) · CPC title

• C02F2209/40

  Liquid flow rate · CPC title

• C12M31/02

  located outside the reactor · CPC title

• C02F2209/06

  pH · CPC title