Vacuum drying kiln

• US 4,194,296 A
• Filed: 05/04/1978
• Issued: 03/25/1980
• Est. Priority Date: 05/17/1977
• Status: Expired due to Term

• Current Assignee: Ernesto G. Pagnozzi, Vincenzo Pagnozzi
• Original Assignee: Ernesto G. Pagnozzi, Vincenzo Pagnozzi
• Inventors: Pagnozzi, Vincenzo, Pagnozzi, Ernesto G.
• Primary Examiner(s): Camby, John J.
• Application Number:
  US05/902,632
• Time in Patent Office: 691 Days
• Field of Search: 34/15, 34/16.5, 34/76, 34/77, 34/78, 34/92
• US Class Current: 34/410
• CPC Class Codes: F26B 2210/16 Wood, e.g. lumber, timber
• 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 23/10 using tubes or passages containing heated fluids , e.g. acting as radiative elements; Closed-loop systems for combustion gases F26B3/305
• CPC Class Codes: F26B 5/04 by evaporation or sublimation of moisture under reduced pressure, e.g. in a vacuum F26B11/049 and F26B17/128 take precedence
• 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

A vacuum drying kiln has a drying chamber in which, in use, is placed timber to be dried and around which is a surrounding water jacket through which is circulated a heat exchange fluid which derives its heat by flowing through the secondary circuit of a heat exchanger through the primary circuit of which is pumped a mixture of air and water vapor drawn by a vacuum pump from the interior of the drying chamber. The kiln is operated cyclically through successive heating and evacuation phases and the vacuum pump is one utilizing a secondary fluid to effect pumping, the characteristics of this secondary fluid being that it is immiscible with water and has a low specific heat so that it encourages the condensation of the water vapor in the primary circuit of the heat exchanger by undergoing large temperature variations for small changes in heat content.

Claims

1. In a vacuum drying kiln suitable for drying timber, comprising:

at least one drying chamber,

heating means including a primary fluid operable to transfer heat to the interior of said chamber,

a vacuum pump containing a secondary fluid and having an inlet and an outlet,

means selectively connected the inlet of said vacuum pump to said chamber whereby to produce in said chamber a pressure reduction for the purpose of evaporating water contained in the timber, and

heat pump means including condenser means connected to the outlet of said vacuum pump for receiving said water vapour and said secondary fluid, said condenser means being operable to extract from the water vapour drawn from the wood at the operating temperature in said chamber a quantity of the heat conveyed thereby from the chamber, and also to extract from the water vapour a quantity of heat corresponding to the thermal equivalent of the work done on the water vapour by the vacuum pump, and thereby raise the temperature of this extracted heat above the said operating temperature in the chamber and transfer means for transferring said heat back to the interior of the said chamber via the said heating means.

2. The vacuum drying kiln of claim 1, wherein said condenser means is of the mixing kind, operating to mix the water vapour extracted from the wood with said secondary fluid.

3. The vacuum drying kiln of claim 2, wherein said secondary fluid is a liquid which is immiscible and nonemulsionable with water, and the specific heat of which is less than unity.

4. The vacuum drying kiln of claim 3, wherein the secondary fluid has a specific heat less then 0.5.

5. The vacuum drying kiln of claim 3, wherein the boiling point temperature of the secondary fluid is greater than that of water.

6. The vacuum drying kiln of claim 3, wherein the secondary fluid is a diathermic oil.

7. The vacuum drying kiln of claim 3, wherein the secondary fluid is a diathermic oil having the following characteristics:

--specific gravity 0.750-0.9 at 15°

C.

--flash point;

greater than 200°

C.

--viscosity index 95

--viscosity;

2.8 Engler at 50°

C.

1.45 Engler at 100°

C.

1.34 Engler at 114°

C., and

--specific heat 0.4 Cal/°

C.

8. The vacuum drying kiln of claim 1, wherein said transfer means comprises a heat exchanger having:

a primary circuit through which flows, in use, the mixture of secondary fluid and water vapour,

a secondary circuit isolated from the primary circuit, apart from thermal contact therewith, through which flows said primary fluid, and

means for directing said primary fluid from the heat exchanger, in which it absorbs heat by cooling the mixture of secondary fluid and water vapour in the primary, to the heating means where it loses heat to the interior of the drying chamber.

9. The vacuum drying kiln of claim 8, wherein:

there are at least two drying chambers,

means for selectively connecting the interior of each of said two chambers with said vacuum pump,

valve means for closing off these connections when required so that the vacuum pump can be connected selectively to create a vacuum in either of said two chambers for a period of time during which water is evaporated from wood placed in this chamber,

means for maintaining the interior of the other chamber at a greater pressure during this time in an atmosphere including water vapour, and

means for circulating said primary fluid through the secondary circuit of the heat exchanger whereby to receive heat therefrom, and the heating means of the said other chamber whereby to effect heating of timber therein.

10. The vacuum drying kiln of claim 9, wherein there are further provided:

means for connecting the two chambers together, including valve means, so that the pressures in the two chambers can be equalised by putting them in communication with each other.

11. The vacuum drying kiln of claim 1, wherein the condenser means is provided with means for inducing therein a pressure higher than that at which the water vapour is extracted from the drying chamber, whereby to increase the condensation temperature in the condenser.

12. A method of drying timber using a vacuum drying kiln having first and second drying chambers, heating means including a primary fluid operable to transfer heat to the interior of said chambers, a vacuum pump containing a secondary fluid and having an inlet and an outlet, means for selectively connecting the inlet to one of said chambers, a heat exchanger having a primary and secondary circuit and conduit means for selectively connecting said chambers directly to each other, comprising the steps of:

(a)--heating the interior of at least the second drying chamber to raise the temperature of timber placed therein;

(b)--evacuating said second chamber with said vacuum pump and extracting the heat from the air and water vapour drawn therefrom by means of said heat exchanger and transferring this heat into said first chamber;

(c)--placing said first and second chambers into communication with one another through said conduit means and isolated from the atmosphere so that the pressures therein are equalised at a subatmospheric pressure;

(d)--evacuating said first chamber with said vacuum pump, extracting the heat contained in the air and water vapour drawn therefrom by means of said heat exchanger and transferring this heat into the second chamber; and

(e)--repeating steps (b), (c), and (d) cyclically in this sequence until the moisture content of the timber in the two chambers has fallen to the required level.

13. The method of drying timber as in claim 12, wherein the output from the vacuum pump is a mixture of said secondary fluid and air and water vapour drawn from whichever of the two chambers to which it is connected, and the secondary fluid being one which has a low specific heat thereby encouraging condensation of the water vapour in the primary circuit of the heat exchanger through which it flows.

14. The method of drying timber as in claim 13, wherein the heat from the water vapour and air drawn from the two chambers is transferred at the heat exchanger to said primary fluid which is circulated through the secondary circuit of the heat exchanger, and through said heating means in thermal contact with the interior of one of the first and second chambers.

15. The method of drying timber as in claim 14, wherein the temperature of said primary fluid at the outlet of the said heating means in thermal contact with the interior of said first and second chambers is not greater than the condensation temperature of water vapour at the pressure existing in the primary circuit of the heat exchanger.