METHOD FOR DRYING SLURRY, RINSE WATER AND INDUSTRIAL EFFLUENT AND/OR RESIDUES

Abstract: Method for drying slurry, comprising the steps of: providing an air-permeable drying bed with a suitable carrier material, arranging, for instance spraying, on the drying bed the (semi-liquid) slurry, drawing in and/or blowing drying air and guiding this air through the drying bed; removing thus dried (semi-liquid) slurry, shuffling the carrier material at chosen times, measuring quantities of the drying air; measuring quantities of air guided through the drying bed; and arranging the (semi-liquid) slurry, shuffling the carrier material and removing dried (semi-liquid) slurry on the basis of the measured quantities.

Description: METHOD FOR DRYING SLURRY, RINSE WATER AND INDUSTRIAL EFFLUENT AND/OR RESIDUES The invention relates to a method for drying 1 slurry, which in a living quarters for animals such as agricultural livestock is produced by these animals, or rinse water or industrial effluent and/or residues, which method comprises the steps of: - providing an air-permeable drying bed with suitable carrier material; - arranging, for instance spraying, the slurry on the drying bed; - drawing in and/or blowing drying air and guiding this air through the drying bed; - removing thus dried manure; and - shuffling the carrier material at chosen times, for instance periodically, in order to ensure a predetermined air-permeability of the drying bed. According to known methods for drying slurry the slurry is first of all separated into a thin and a thick fraction, whereafter the thick fraction is dried while the thin fraction is disposed of. A drawback hereof is that a large part of precisely those minerals which can serve as nutrients for plants are dissolved in the thin fraction. US-A-5 666 905 describes a method wherein slurry drops through a slatted floor into a basement and there has the water removed with drains. Air from the living quarters is blown through and over the drained thick fraction in order to dry the manure. A drawback of this method is that the manure is drained, whereby the manure is separated into a watery and a thick fraction. Only the thick fraction is dried and the thin fraction is disposed of. Since the manure accumulates in the basement, the air permeability is very w to t H H in o in o LΠ O LΠ 3 ft> rr Φ K H- ft ) l— 1 fw ø & Hi Φ 3 0 <! H- 0 Q a. μ H- Φ Ωi 3 ft> ø ø HJ Φ . — . 0 H rt tr Φ p. r-i H- Φ industrial residual product or waste flow) on the basis of the measured quantities. Measuring of the different quantities and performing the different steps on the basis thereof enables precise control of the process, whereby a minimal amount of energy is used to obtain a maximum result. These quantities are for instance the flow rate, temperature and air humidity of the air flow. Use can be made in advantageous manner of the ventilation air of the living quarters. This air has an air humidity of around 80%. This stall air is usually preheated. Another advantage of using stall air is that it is ventilated in very large quantities. In addition, the dust is filtered out of the stall air by the device, so that it can be disposed of with the dried manure. According to a further embodiment of the method according to the invention the method comprises the step prior to performing step (B) of adding an additive, such as a bacteria culture, to the slurry. The addition of an additive, for instance a bacteria culture, makes it possible to accelerate the decomposition of (harmful) substances, whereby the emission of for instance dust, ammonia and odour can be reduced. A chemical substance can also be envisaged as additive, whereby for instance the acidity of the slurry can be increased or decreased, or a vegetable substance which for instance dispels odour . The invention further comprises a device for performing the method according to the invention, which device comprises: - a housing; - an air-permeable drying bed with suitable carrier material arranged in the housing; - application means arranged in the housing and placed above the drying bed for distributing slurry over the drying bed; - ventilation means for drawing in air from the living quarters and guiding the air through the drying bed; and - removing means for removing a layer of thus dried manure (or other dried product) . In a preferred embodiment of a device according to the invention, this device comprises a shuffler device for shuffling the dried slurry on the drying bed in order to ensure a predetermined air-permeability. The thickness of the drying bed is preferably kept as small as possible, for instance a thickness of 3-10 cm. The pressure losses over the drying bed are kept minimal by the shuffling, whereby operation can usually take place with the existing ventilators of the living quarters (or, in the case of industrial applications, the factory) . No additional energy, or only a minimal amount, is then necessary to guide the air through the drying bed. At start-up a carrier material other than the product for drying is usually used temporarily (for instance a compost-like product) . The shuffler device can be embodied such that it also forms the removing means for removal of a layer of manure . In yet another preferred embodiment of the device according to the invention, the device comprises a reservoir for storing the slurry; and means for mixing the manure in the reservoir in order to obtain a substantially homogeneous mixture. When the slurry is pumped out of the manure pit, it is then not completely homogenous . So as to allow spraying and/or distribution of the slurry to take place optimally and to prevent fouling or blockage of the sprayers, the slurry is stored temporarily in a reservoir and there homogenized by means of homogenizing means such that an improved homogeneity results . The housing of the device is preferably formed by a container of standardized dimensions. It is hereby possible to construct the system in the container and to transport the whole container, including the device, to L U) to to H H LΠ o in o in o in Ω ft ) 0 TJ 3 rt ft ) 0 tr 3 Hi Hi Hj rt TJ μ- * ft ) TJ TJ ft ) P. tr -> <! ft ) CQ μ- ft ) ft ) O Hi Hi ft ) tr Hi TJ 0 μ- ø Φ Φ tr μ- CQ μ- 0 Ω Hi Φ μ- μ- φ μ- Φ rt μ- ø 0 Hi 0 rt Φ Hi £ 3 <! Hi CQ CQ Hi TJ tr Hf 3 ft ) Ω ft ) < < ø tr TJ Hi rt Φ ft ) Ω Φ Q ft ) ft ) 0 μ- rt Φ Φ o Φ Hi •<! TJ Ω 0 ≤ Hi μ- μ- rr Φ μ- ft ) μ- Φ μ- ft> Φ Hi Φ 0 Hi LQ ø tr Pi Φ LQ φ 2 2 0 0 μ- φ Φ Hi μ- 0 ø ø μ- ft> ø Hi CQ φ X ø P. Ω CQ μ- LQ LQ μ- Hi 3 CQ Pi Ωi Pi ø Hi LQ LQ rt LQ ft ) ><! μ- ø •<: O CQ ft> CQ Φ 0 Hi o 0 tr ø 3 φ μ- LQ rt ft ) rt Hi rt Q 0 3 • T) Pi 0 Φ rt μ- μ- φ φ ft ) Hi ft ) ø • tr Λ Λ rt Φ Λ Φ Φ Hi rt ø TJ TJ H{ 0 μ- tr TJ Hf H{ ft> P. ø 0 μ- Ωi LQ Φ 0 ø μ- :*! ø ft ) ft ) μ- CQ Hi 0 •-3 H ft ) μ- rt rt φ 0 ) CQ H{ ftl (_1. Hi ft ) ft ) 0 Ω ft ) CQ Pi Ω ø Φ CQ tr t • ; ø < ^ CQ Ω co CQ tr σ rt ft ) rt H ι-3 Hi Hi 0 tr H Hi TJ μ- rt LQ >< CQ rt μ- φ O μ- • CQ CQ ft ) . μ- rt • ; Φ 0 tr ft ) Ω tr 0 tr Φ tr rt rt ft> 0 rr ft ) μ- φ 1 CQ μ- H rt Hi ft ) μ- 0 Pi tr < Hi Φ Φ Φ Φ Φ Φ Φ 3 ø Φ Ω ; o O 0 CQ CQ tr W 0 tr ] φ Hi ft ) μ- Hi TJ 0 rt 0 Q Hi Hi φ LQ ft ) H φ 0 μ- Hi rt μ- Ω Φ Hi ft ) ft ) Hi tr 0 Ω ft ) μ- rt P. tr Hi Ω Φ CQ CQ ft" φ Q μ- • <! . ? ft ) ft ) H Φ Ω Hi φ Φ 0 £ ø Ω φ tr TJ Φ Φ μ- μ- • ø Hi Hi μ- ø μ- TJ φ Hi Hi O rt CQ CQ rt ^ Ω ft ) LQ 0 Hi Φ ^ <; LQ ft ) Ω CQ ø Ω ø CQ H{ H{ O S ø Φ Φ 0 Φ • rt Ω rt tr ø H ft ) o μ- μ- ø ft ) ø ft ) μ- Hi ft ) 0 LQ Hi 3 μ- ft ) μ- TJ Hi Ω H{ 0 o ø rt 0 ≤ μ- 0 Ω ø Hi rt Pi 0 s- CQ rt 0 ft ) 0 μ- ft ) φ 0 CQ <: r μ- ) -3 3 ft ) $, ft ) Ω 0 ø Hi φ < Φ Φ μ- tr ft ) rt Λ o rt Hi LQ TJ 0 μ- ft ) tr ft ) TJ rt 0 tr μ- O in Φ φ P. 0 tr rt Ω Φ Hi rt tr ø Pi ft ) Φ Φ ft ) ft ) μ- 0 Φ H φ μ- Hi μ- ø 3 o ft ) H ø CQ rt φ tr 0 H o μ- Φ Φ ft ) μ- 0 H{ 3 Pi Hi Hi 0 Ω Hi 0 0 Ω Φ TJ ft ) 0 LO rt tr ≤ tr 0 Hi <! P. Hi Hi Ω rt μ- ft ) Pi rt ft ) CQ ft ) CQ ø tr tr Hi H{ 0 rt M ft ) μ- 0 μ- Φ tr $ 0 TJ μ- rt ft ) μ- ft> rt ft ) H{ ∞ TJ ø 0 ft ) CQ 0 μ- ft ) μ- Ω 0 rt Hi φ tr φ Hi μ- ø ft> Φ M rt Φ rt ^ 0 μ- 0 LQ rt 0 rt 0 CQ 0 ø < Ω 0 CQ tr ft ) μ- Ω φ ø LQ ϊ- Pi Hi H ^ Hi μ- Hi rr J ft ) H( Φ Φ μ- CQ tr Hi Φ ft ) Hi μ- 0 Hi rt Ω rt Hi CQ tr CQ ; 0 μ- rt ø 0 Φ Hi P. ø μ- Φ CQ 0 ø Hi ft ) Hi Φ Φ tr Φ φ rt Φ ft ) 0 H{ ft ) tr LQ tr Q * • < 3 ø CQ ft ) LQ Ωi Φ ft ) i Pi Hi ft ) « Hi ø ft ) 0 Hi Φ 0 CQ vo 0 Φ tr rt LQ CQ rt ft ) ft ) μ- μ- TJ Hi rt Hi H ø ft ) Φ rt 0 ø 0 tr 0 TJ tr ft ) ; tr ft ) μ- <! TJ Λ ø φ φ ø z Hi 0 Φ Ω Hi tr ft ) i rt CQ Hi Ω CQ Φ CQ Hi rt tr φ ø Φ • -J ø ø tr Hi μ- ø 0 LQ Hi n Hi μ- Φ rt ^ LQ t ) rt Pi μ- ft ) tr Φ Hi CQ rt ø Pi Φ 0 f Hi Ωi 0 ø 3 ft ) CQ φ Φ rt CQ rt Φ Φ rt 0 Ωi ø ft ) ø • ; Φ Φ tr Ωi ft ) Hi ft ) ø Ωi LQ TJ Hi rt TJ 0 CQ tr tr 0 Φ ft ) Hi tr rt Hi Hi Hi 1 LQ Φ ft ) tr μ- μ- μ- 0 ■ ; H{ CQ ø rt 0 Φ Ω CQ μ- 0 Φ tr Hi μ- Hi rt H Hi CQ Pi •<; ø Q CQ Pi Pi μ- Ω Λ n^ Φ Ω φ 0 rt ft ) rt Q rt Hi Hi μ- ^ φ O -j CQ P- Ω μ- μ- ø rt ø Hi rt rt Hi tr μ- tr 0 0 0 rt Φ CQ Pi Hi 0 0 • ø Φ ft ) rt Hi tr Pi CQ N LQ ft ) μ- CQ tr μ- rt Φ Hi Φ Pi Hi ft ) μ- Hi 0 H Hi Pi Ω tr φ ft ) φ φ Hi ø Φ < O rt μ- CQ Φ Ω Ω CQ CQ μ- > O H{ Λ Φ CQ Hi tr CQ P. 1 . rt rt to Φ tr 0 Ω 0 3 Φ μ- Ω 0 ft ) ø rt Hi •<: rt 0 Φ LQ 0 0 • Φ 0 • μ- rt Φ CQ ft ) 0 Φ Hi ø tr 0 0 Hi CQ 0 CQ tr tr Hi £ O μ- Hi H{ Φ 0 TJ P. H{ ø < tr Φ H{ rt ø < Φ 0 0 Hi TJ Hi riΦ μ- ft ) tr μ- Hi Φ <! Ω TJ μ- CQ Pi CΩ μ- Φ μ- Pi Hi rt Φ ft ) ft ) rt φ μ- Hi Hi ft ) Ω 0 μ- CQ rt φ CQ 0 Hi tr 3 tr Φ φ Φ ø μ- Φ ø rt ft ) Ω φ ft ) ^ 0 P. tr LQ Ω tr CQ Φ μ- Hi Φ μ- Φ μ- t <! 0 ø Ξ ft ) <! ft ) Φ rt 0 ft ) μ- rt Hi ^ Ω Hi Φ tr TJ φ Hi Hj 0 CQ Φ ø CQ μ- Hi rt ø φ μ- P- Hi CQ ft ) μ- ø φ £ Φ ^ ft ) P. 0 ft ) <! • 3 P. CQ μ- Ω Hi μ- 0 ø ø Hi 0 Hi CQ Φ μ- 3 P. tr μ- ft> 3 Hi 0 μ- μ- tr ø Φ ^ 0 Hi Φ rt μ- Hi rt tr φ Hi rt ft ) μ- Ω ø Ω 0 Hf TJ φ tr μ- rt ø TJ 0 0 rt 0 X μ- Hi ø tr 0 ft ) rt Ω 0 LQ ft ) 0 φ Φ CQ Φ H{ rt tr rr ft ) 0 0 0 H μ- ft ) φ 0 Hi rt rr Φ 0 0 μ- rt Φ tr 0 Hi P. P. φ rr Φ O CQ CQ CQ . Q μ- P. ø 0 0 tr CQ 0 CQ Q 0 Hi CQ Hi φ 3 rt Hi μ- CQ • μ- i CQ Ωi 3 φ p. μ- Hi rt μ- μ- μ- μ- Hi Φ 0 CQ ft ) φ ø Φ n Φ ≤ rt Φ ø • rt rt ft ) CQ CQ φ 0 Hi Hi CQ LQ < rt μ- rt tr <! LQ ft ) tr tr rt Hi μ- μ- ft> μ- tr Φ μ- > ft> φ Hi ^1 Ω Ω φ Ω rt φ Φ Φ 12 from sprayers 10. Via fan 5 and air duct 6 air from the living quarters is further blown and/or sucked into housing 7 and this air is forced through drying bed 11. The air can also be extracted from the container. Here the stall air is extracted via a discharge pipe 13 and a fan 14. Because the relatively dry stall air is drawn through the carrier material and the drying bed the slurry will dry. This results in a layer 15 of dried manure on carrier material 12. In order to ensure the air-permeability of drying bed 11, carrier material 12 and the dried manure 15, a (travelling) shuffler device 16 is arranged above drying bed 11. Shuffler device 16 comprises for instance a number of blades 17 which can reach to drying bed 11. It is hereby possible by rotating the blades to shuffle and mix carrier material 12 and dried manure 15 , thereby creating a mass with a relatively high air-permeability. When the mass of carrier material 12 and dried manure 15 rises above a certain predetermined height, it is then necessary to discharge a part of this mass. This can take place by causing shuffler device 16 to scrape over the top of the mass of carrier material 12 and dried manure 15 and to discharge the mass via a hatch 18 or for instance a screw conveyor to the outside. After prolonged use the carrier element is therefore formed by dried manure . Device 1 further preferably comprises a control device (not shown) which measures quantities of the air flow in air duct 6 and the air flow in discharge pipe 13. These quantities are flow rate, temperature and relative humidity and optionally the pressure loss over the drying bed. On the basis of this measured data the control calculates how much water there is in the ingoing air and how much water there is in the outgoing air. When the discharged quantity of water corresponds roughly with the quantity of water from the slurry which has been arranged on the bed, a fresh quantity of slurry will then be arranged on the drying bed. ) lo to to H H LΠ o in o in o in TJ ft ) P. P. Hf 0 3 μ- μ- φ 0 0 Hi Hi CQ LQ ø Hi Hi CQ Φ 0 Φ φ 0 Hf rt Hf Hi Hi Q φ Φ Φ Ω 0 0 0 rt Ω Ω P- 3 0 φ Φ s! μ- TJ H tr Hi ft ) 0 0 rt φ Hi μ- tr < < ø Φ Φ o Φ Φ μ- Hf CQ ø Hf Hf CQ ft ) Φ rt 0 ≤ ft ) rt ft ) >Q Ω μ- ιo tr ø Φ rt o TJ Φ CQ ft ) tr 1 Hi 0 0 s- in 0 Ωi rt μ- ft ) o TJ Hi TJ μ- μ- φ *< o rt μ. TJ Hi μ- CQ ^ 1 ft ) ø CQ rt TJ CQ * LQ μ- 0 tr Φ Ω tr Hi Φ H ft ) ft ) tr 0 3 h- 1 μ- Φ Φ Pi Φ . Hi p. K μ- ft ) rt μ- ø tr s: TJ 0 φ Ω μ- tr Φ > Pi HJ Φ hf 3 Φ μ- ø g ø Φ 3 ft ) rt Φ 0 ft ) ft ) CQ < rt ft ) Hf CQ rt Φ tr tr 3 0 Φ Hf Φ h- 1 ft ) Hf Hf rt Φ φ h- 1 Φ μ- 0 tQ Pi ft ) ø Hf Ωi TJ rt H μ- • : hi Hf tr o Hf μ- *<; φ Φ μ- o φ ø μ- CQ CQ 1 3 LQ ø CQ TJ to Φ LQ 0 Hf Hf o ø tr Hf φ Φ o rt φ tr Φ CQ 3 CQ P. Φ CQ 0 TJ «. p. 0 < ft ) 0 Hf Φ C Q rt o Φ Ω tr ft ) Φ It is possible, depending on the capacity required, to place one or more containers parallel to each other. In the drying of industrial effluent or industrial residues the process is per se identical. From a cost viewpoint use is preferably then made of a drying air flow which is already available on site.

Claims: CLAIMS 1. Method for drying slurry, which in a living quarters for animals such as agricultural livestock is produced by these animals, or rinse water or industrial effluent and/or industrial residues, which method comprises the steps of: - providing an air-permeable drying bed with suitable carrier material; - arranging, for instance spraying, the slurry on the drying bed; - drawing in and/or blowing drying air and guiding this air through the drying bed; - removing thus dried manure; and - shuffling the carrier material at chosen times, for instance periodically or continuously, in order to ensure a predetermined air-permeability of the drying bed, characterized by - measuring quantities of the drying air; - measuring quantities of air guided through the drying bed; and - arranging the slurry, shuffling the carrier material and removing dried manure on the basis of the measured quantities. 2. Method as claimed in claim 1, wherein the quantities are flow rate, temperature and/or relative humidity. 3. Method as claimed in either of the foregoing claims, wherein the air is air from the living quarters. 4. Method as claimed in claim 1, comprising the step of: adding an additive, such as a bacteria culture, to the slurry prior to performing. 5. Device for performing the method as claimed in claim 1, which device comprises: - a housing; - an air-permeable drying bed with suitable carrier material arranged in the housing; - application means arranged in the housing and placed above the drying bed for substantially homogeneous distribution of slurry over the drying bed; - ventilation means for drawing and/or blowing air as homogeneously as possible from the living quarters and guiding this air through the drying bed; and - removing means for removing a layer of thus dried manure . 6. Device as claimed in claim 5, comprising a shuffler device for shuffling the carrier material on the drying bed in order to ensure a predetermined air- permeability. 7. Device as claimed in claim 5, comprising - a reservoir for storing the slurry; and - means for homogenizing the slurry in the reservoir. 8. Device as claimed in claim 5, wherein the housing is a container of standardized dimensions. 9. Device as claimed in claim 5, wherein a heat exchanger with two circuits is connected to the outlet of the ventilation means, wherein air guided through the drying bed flows through the first circuit and fresh, clean air flows through the second circuit such that heat is exchanged between the two flows. 10. Device as claimed in any of the claims 5-9, comprising: - measuring means for measuring quantities of air from the living quarters and of the air guided through the drying bed; and - control means for controlling the application means, the removing means and/or the shuffler device on the basis of the measured quantities.

Inventors: ROELOFS SEINE, WAANDERS MARCELLINUS BERNARDUS, ROELOFS, SEINE, WAANDERS, MARCELLINUS, BERNARDUS, EDUARDES
Applicants: DELTA BIO MESTBEWERKING B V, ROELOFS SEINE, WAANDERS BEHEER B V, WAANDERS MARCELLINUS BERNARDUS, DELTA BIO MESTBEWERKING B.V., ROELOFS, SEINE, WAANDERS BEHEER B.V., WAANDERS, MARCELLINUS, BERNARDUS, EDUARDES
Application year: 2000
Main classification: F26B9
IPC codes: A01C3, B01D1, C02F1, C02F11, F26B3, F26B9, F26B25