METHOD FOR EFFICIENT AND EFFECTIVE DRYING

• US 20200132372A1
• Filed: 06/12/2018
• Published: 04/30/2020
• Est. Priority Date: 07/18/2017
• Status: Active Grant

• Current Assignee: Jorge Alonso Diaz
• Original Assignee: Jorge Alonso Diaz
• Inventors: Diaz, Jorge Alonso
• Granted Patent: US 11,125,500 B2
• Time in Patent Office: Days
• CPC Class Codes: F26B 11/049 with provisions for working under increased or reduced pressure, with or without heating
• CPC Class Codes: F26B 21/10 Temperature; Pressure F26B23/026 takes precedence
• CPC Class Codes: F26B 21/12 Velocity of flow; Quantity of flow , e.g. by varying fan speed, by modifying cross flow area F26B21/004 takes precedence; changing air flow pattern F26B21/022
• CPC Class Codes: F26B 2200/06 Grains, e.g. cereals, wheat, rice, corn
• CPC Class Codes: F26B 23/004 by compressing and condensing vapour in exhaust gases, i.e. using an open cycle heat pump system
• CPC Class Codes: F26B 3/06 the gas or vapour flowing through the materials or objects to be dried F26B3/14 takes precedence
• CPC Class Codes: F26B 9/06 in stationary drums or chambers
• CPC Class Codes: Y02B 30/52 Heat recovery pumps, i.e. heat pump based systems or units able to transfer the thermal energy from one area of the premises or part of the facilities to a different one, improving the overall efficiency
• CPC Class Codes: Y02P 70/10 Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

Abstract

Hot air drying is an intensive energy consuming process, 5000-8000 kJ per kg of water. More efficient processes produce low drying rates or cannot totally dry the product because they do not integrate the four drying phases, warm up, constant drying, falling drying and aeration and do not handle dripping. To reduce the energy consumption, the exhausted mix of air and vapor is used as working fluid to drive each phase, and the dripping is collected before it goes back to the product. This fluid is compressed inside of a heat-exchanger to heat the product; however, the mix proportion, vapor and air, changes on each phase. For warm up phase, the working fluid is either hot air or condensed water; in constant phase, it is mostly vapor; in falling phase, it changes from vapor to air; and for aeration, it is air. Inlet and outlet valves control these proportions.

Claims

1. A method for totally or partially drying a product in a drying equipment, wherein the method is driven by one or more compressors acting on an air/vapor mix released by the product, integrates the drying phases of (i) Warming up, (ii) Constant drying, (iii) Falling drying, and (iv) Aeration, and controls a dripping formed in the drying equipment, comprising the steps of:

a. reducing the pressure inside the drying equipment by the action of the compressor.

b. sucking up ambient air into the drying equipment through an air inlet;

c. warming up said air and the product with a heat exchanger which evaporates the moisture in the product, releasing the air/vapor mix;

d. compressing the air/vapor mix released by the product by means of the compressor which increases its temperature and its thermal energy;

e. transferring the thermal energy from the compressed mix inside the heat exchanger to the product and air on the other side of the heat exchanger, which reduces the mix temperature, condensates most of its vapor and warms up the product and the air on the other side of the heat exchanger;

generating an air/vapor/condensate mix inside the heat exchanger; and

f. discharging all the air/vapor/condensate mix.

2. The method according to claim 1, wherein ambient air comes into the process through an air inlet regulated by a valve which controls an amount of incoming air and the pressure inside the drying equipment for each drying phase:

(i) Warming up, (ii) Constant drying, (iii) Falling drying, and (iv) Aeration

3. The method according to claim 1 wherein all the air/vapor/condensate mix leaves the process through an outlet regulated by a valve.

4. The method according to claim 1, wherein the amount of vapor in the air/vapor mix to be compressed changes according to each drying phase:

warm up;

constant;

falling; and

aeration.

5. The method according to claim 1, wherein the method is adapted for a batch drying process.

6. The method according to claim 1, wherein the method is adapted for a continuous drying process.

7. The method according to claim 1, wherein the drying equipment has an inside maximum temperature above the boiling point of water at atmospheric pressure.

8. The method according to claim 1, wherein the drying equipment has an inside maximum temperature below the boiling point of water at atmospheric pressure.

9. The method according to claim 1, wherein the dripping that occurs on the drying equipment surfaces is collected and enhanced by cooling down said surfaces.

10. The method according to claim 9, wherein the drying equipment has a double wall having an inner wall and an outer wall, the inner wall is a barrier that allows the free flow of the air/vapor mix but the product;

and the vapor is condensed on the surface of the outer wall.

11. The method according to claim 9, wherein the drying equipment has a double walled pipe having an inner pipe and an outer pipe;

the external pipe is a barrier that allows the free flow of the air/vapor mix but the product; and

the vapor is condensed on the external surface of the inner pipe.

12. The method according to claim 1, wherein the method is used for drying a laminar product such as paper and paperboard;

and the heat exchanger is heated rotating cylinders.

13. The method according to claim 1, wherein the method is applied until the falling phase when the product moisture is higher than the equilibrium moisture (Meq).