Pyrometallurgical reactor cooling element and its manufacture

Details Pyrometallurgical reactor cooling element and its manufacture Pyrometallurgical reactor cooling element and its manufacture

2001-06-15

2003-09-09

Bennett, Henry (Department: 3743)

Heat exchange

With coated, roughened or polished surface

C165S905000, C165S179000, C029S890030, C029S890053, C164S098000, C164S132000, C428S137000

Reexamination Certificate

active

06615913

ABSTRACT:

FIELD OF THE INVENTION
The present invention relates to a method of manufacturing a cooling element with flow channels for pyrometallurgical reactors. In order to enhance the heat transfer capability of the element, the surface area of the flow channel wall, which is traditionally round in cross-section, is increased without increasing the diameter or length of the flow channel. The invention also relates to the element manufactured by this method.
BACKGROUND OF THE INVENTION
The refractory of reactors in pyrometallurgical processes is protected by water-cooled cooling elements so that, as a result of cooling, the heat coming to the refractory surface is transferred via the cooling element to water, whereby the wear on the lining is significantly reduced compared with a reactor which is not cooled. Reduced wear is caused by the effect of cooling, which brings about forming of so called autogenic lining, which fixes to the surface of the heat resistant lining and which is formed from slag and other substances precipitated from the molten phases.
Conventionally cooling elements are manufactured in two ways: primarily, elements can be manufactured by sand casting, where cooling pipes made of a highly thermal conductive material such as copper are set in a sand-formed mould, and are cooled with air or water during the casting around the pipes. The element cast around the pipes is also of highly thermal conductive material, preferably copper. This kind of manufacturing method is described in e.g. GB patent no. 1386645. One problem with this method is the uneven attachment of the piping acting as cooling channel to the cast material surrounding it. Some of the pipes may be completely free of the element cast around it and part of the pipe may be completely melted and thus fused with the element. If no metallic bond is formed between the cooling pipe and the rest of the cast element around it, heat transfer will not be efficient. Again if the piping melts completely, that will prevent the flow of cooling water. The casting properties of the cast material can be improved, for example, by mixing phosphorus with the copper to improve the metallic bond formed between the piping and the cast material, but in that case, the heat transfer properties (thermal conductivity) of the copper are significantly weakened by even a small addition. One advantage of this method worth mentioning is the comparatively low manufacturing cost and independence from dimensions.
Another method of manufacture is used, whereby glass tubing in the shape of a channel is set into the cooling element mould, which is broken after casting to form a channel inside the element.
U.S. Pat. No. 4,382,585 describes another much used method of manufacturing cooling elements, according to which the element is manufactured for example from rolled or forged copper plate by machining the necessary channels into it. The advantage of an element manufactured this way, is its dense, strong structure and good heat transfer from the element to a cooling medium such as water. Its disadvantages are dimensional limitations (size) and high cost.
The ability of a cooling element to receive heat can be presented by means of the following formula:
Q=&agr;×A×&Dgr;T, where
Q=amount of heat being transferred [W]
&agr;=heat transfer coefficient between flow channel wall and water [W/Km
2
]
A=heat transfer surface area [m
2
]
&Dgr;T=difference in temperature between flow channel wall and water [K]
Heat transfer coefficient a can be determined theoretically from the formula
 
Nu=&agr;D/&lgr;
&lgr;=thermal conductivity of water [W/mK]
D =hydraulic diameter [m]
Or
Nu
=0.023
×Re
{circumflex over ( )}0.8
Pr
{circumflex over ( )}0.4,
where
Re=wD&rgr;l&eegr;
w=speed [m/s]
D=hydraulic diameter of channel [m]
&rgr;=density of water [kg/m
3
]
&eegr;=dynamic viscosity
Pr=Prandtl number [ ]
Thus, according to the above, it is possible to influence the amount of heat transferred in a cooling element by influencing the difference in temperature, the heat transfer coefficient or the heat transfer surface area.
The difference in temperature between the wall and the tube is limited by the fact that water boils at 100° C., when the heat transfer properties at normal pressure become significantly worse due to boiling. In practice, it is more advantageous to operate at the lowest possible flow channel wall temperature.
The heat transfer coefficient can be influenced largely by changing the flow speed, i.e. by affecting the Reynolds number. This is limited however by the increased loss in pressure in the tubing as the flow rate increases, which raises the costs of pumping the cooling water and pump investment costs also grow considerably after a certain limit is exceeded.
In a conventional solution, the heat transfer surface area can be influenced either by increasing the diameter of the cooling channel and/or its length.
The cooling channel diameter cannot be increased unrestrictedly in such a way as to be still economically viable, since an increase in channel diameter increases the amount of water required to achieve a certain flow rate and furthermore, the energy requirement for pumping. On the, other hand, the channel diameter is limited by the physical size of the cooling element, which for reasons of minimizing investment costs, is preferably made as small and light as possible. Another limitation on length is the physical size of the cooling element itself, i.e. the quantity of cooling channel that will fit in a given area.
SUMMARY OF THE INVENTION
The present invention relates to a method of manufacturing a cooling element for a pyrometallurgical reactor from a highly thermal conductive metal such as copper, in which the heat transfer capability of said cooling element is enhanced significantly by increasing heat transfer surface area so that it is economically feasible to manufacture a thinner cooling element. This is done so that the wall surface area of the flow channel is increased without increasing the diameter of the cooling channel or adding length. The surface of the flow channel in the cooling element, which is essentially round in cross-section, is enlarged by forming grooves or threads on the inner surface of the channel, by means of subsequent machining. As a result, a smaller temperature difference is required between the water and the cooling channel wall with the same amount of heat, and furthermore, a lower cooling element temperature. The invention also relates to the cooling element manufactured by this method. The essential features will become apparent in the attached patent claims.
In the cooling element described in the present invention, the heat transfer surface area is increased so that, although the cooling element flow channel is basically round in cross-section, its wall is not smooth, but by changing the contour of the wall very slightly, a greater heat transfer surface area can be achieved with the same flow cross-sectional area (the same rate can be achieved with the same amount of water) compared with the unit of length of the cooling channel. This increase in surface area can be achieved in the following ways:
A cooling element, manufactured by working, e.g. by rolling or forging, into which at least one flow channel which is round in cross-section is machined for example by drilling, threads are machined afterwards on the inner surface of the flow channel. The cross-section of the channel remains essentially round.
A cooling element, manufactured by working, into which at least one flow channel, which is round in cross-section is machined, rifle-like grooves are machined afterwards on the inner surface of the flow channel. The cross-section of the channel remains essentially round.
Rifle-like grooves can be obtained advantageously by using a so-called expanding mandrel, which is drawn through the

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