GB2106800A - Apparatus and a process for injecting steam directly into a product in a processing vessel - Google Patents
Apparatus and a process for injecting steam directly into a product in a processing vessel Download PDFInfo
- Publication number
- GB2106800A GB2106800A GB08129403A GB8129403A GB2106800A GB 2106800 A GB2106800 A GB 2106800A GB 08129403 A GB08129403 A GB 08129403A GB 8129403 A GB8129403 A GB 8129403A GB 2106800 A GB2106800 A GB 2106800A
- Authority
- GB
- United Kingdom
- Prior art keywords
- steam
- product
- air
- processing vessel
- pressure
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
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Classifications
-
- A—HUMAN NECESSITIES
- A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
- A47J—KITCHEN EQUIPMENT; COFFEE MILLS; SPICE MILLS; APPARATUS FOR MAKING BEVERAGES
- A47J27/00—Cooking-vessels
- A47J27/14—Cooking-vessels for use in hotels, restaurants, or canteens
- A47J27/16—Cooking-vessels for use in hotels, restaurants, or canteens heated by steam
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- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Commercial Cooking Devices (AREA)
Abstract
Apparatus and a process for injecting steam directly into a product e.g. a food product, in a processing vessel are described. The apparatus comprises a steam inlet valve (12, 13) operable under steam pressure to inject steam fed through the valve into a product in a processing vessel. Air inlet means (9) are provided for bleeding air at a predetermined pressure into the steam being fed to the steam inlet valve means, the pressure of the air bled into the steam being such that hammering of the steam in the processing vessel is prevented. <IMAGE>
Description
SPECIFICATION
Apparatus and a process for injecting steam directly into a product in a processing vessel
This invention relates to apparatus and a process for injecting steam directly into a product.
A common problem in the processing of products, particularly food products, is the total time required.
Avariety of methods may be employed for reducing the times of either the heating or cooling cycles of the processing but the problems of speeding heat exchange from the heating medium to the product and preventing the product cooking-on to the walls of the vessel in which the product is being processed are difficult to solve.
Accordingly, where water is used as a phase in the product, it has been proposed to inject steam directly into the product so as to drastically reduce the heating time required and at the same time prevent the product cooking-on to the walls of the vessel because the processing vessel walls and product are at the same temperature.
However, such direct injection of steam into a cold product causes excessive steam hammering which may damage the processing vessel and which in any case makes operation of the process undesirably noisy. In an attempt to obviate this problem, venturi arrangements have been provided to recirculate the product into the injector. However, in such an arrangement, the product must pass through an extremely small orifice, thereby preventing use of the arrangement with any product containing solid particles and making the apparatus difficult to clean.
It is an object of the invention to provide apparatus and a process for injecting steam directly into a product in a processing vessel, while avoiding the difficulties of the previously proposed arrangements.
According to one aspect of the invention there is provided apparatus for injecting steam directly into a product in a processing vessel, comprising steam inlet valve means operable under steam pressure to inject steam fed thereto into a product in a processing vessel and air inlet means for bleeding air at a predetermined pressure into the steam being fed to the steam inlet valve means, the pressure of the air bled into the steam being such that hammering of the steam in the processing vessel is prevented.
According to a second aspect of the invention there is provided a process for injecting steam directly into a product in a processing vessel, comprising injecting steam under pressure into the product via steam inlet valve means operable under the steam pressure and bleeding air at a predetermined pressure into the steam prior to injection of the steam into the product, the pressure of air bled into the steam being such that steam hammering in the processing vessel is prevented.
In order that the invention may be more readily understood, an embodiment thereof will now be described, by way of example, with reference to the accompanying drawing, in which:
Figure 1 is a part-sectional view of apparatus embodying the invention connected to an inlet of a steam jacketted processing vessel;and
Figure 2 is a plan view from above of the apparatus of Figure 1.
Referring now to the drawing and in particlar
Figure 1, steam injection apparatus embodying the invention is attached to a steam jacketted processing vessel by means of a tubular pipe or branch 4 sealingly welded in an opening formed through inner and outer walls 21 and 22 of the processing vessel and an annular flange 1 welded to the free end of the branch 4.
A main body 2 of the steam injecting apparatus is formed with a longitudinally extending bore 23, the ends of the bore 23 being flared outwardly such that the bore has upper and lower frustoconical portions with respect to the processing vessel. The main body 2 is sealed in the branch 4 by means of an O-ring carried by the main body.
The upperfrustoconical portion of the bore 23 forms a seat for a frustoconical head 12 of a steam inlet poppet valve which normally closes the end of the box 23 opening into the processing vessel. The valve head 12 is welded to a valve stem 13 in the form of a solid pipe which extends axially through the bore 23. The valve stem 23 passes with clearance through an aperture formed in a member 6 extending across the lower end of the bore 23 and engaging in recesses formed in the inner walls of the main body 2. The member 6 partially blocks the lower end of the bore 23 and is preferably, as shown, elliptical in cross-section, the major axis of the elipse extending across the lower end of the bore 23.
The end of the valve stem 13 passing through the member 6 extends into a tubular member 5 and is provided with an annular flange or abutting surface 16 retained in place on the valve stem by two lock nuts 15. A compression spring 14 extends between the abuting surface 16 and a recess formed in the member 6 and is arranged to bias the valve head 12 towards the normally closed position of the poppet valve.
The end of the tubular member 5 adjacent the member 6 is welded to a further flange 3 and the main body 2 and tubular member 5 are held in place with respect to the processing vessel by means of bolts 11 extending through aligned apertures formed in the flanges 1 and 3 and in a radially enlarged end of the main body 2. Gaskets 7 and 8 respectively ensure sealing contact between the flange 1 and the main body 2 and between the flange 3 and the main body 2.
The free end of the tubular member 5 is welded to a 1"(2.5cm) BSPsteam inlet pipe 10 for connection to a steam supply via an adjustable steam pressure reducing valve (not shown) with a preferred range of from 5 to 20 psig (3.44 to 13.8 x 104 Pa) and an on/off valve (not shown).
An air inlet nozzle 9 extends through the wall of the tubular member 5 and is welded in place. The air inlet nozzle 9 is connected by a nut 18 to a non-return valve 19 and a 1/4" (0.6cm) BSP air inlet pipe for connection to a pressurized air supply via an adjustable air pressure reducing valve with a preferred range of from 5 to 20 psig (3.44 to 13.8 x 104 Pa) (not shown) and an on/off valve (not shown).
Normally, the apparatus is fitted to the processing vessel during manufacture. However, the apparatus may be supplied separately and fitted to a processing vessel provided with an inlet having a branch 4 welded therein and a flange 1 connected to the free end of the branch.
Once the apparatus attached to a processing vessel has been connected to both the steam and pressurised air supply, the steam injecting apparatus should be adjusted as follows.
First, the pressure vessel is filled with cold water. It should be noted that initial setting up of the apparatus cannot be carried out at temperatures over 80"C. Ideally water at ambient temperature should be used.
The steam supply to the injecting apparatus is then turned on and the pressure of the steam supply to the reducing valve is adjusted to approximately 10 psig (6.88 x 104 pa) allowing steam to be injected into the water in the processing vessel and causing severe steam hammering in the vessel. Next, ensuring that the air pressure reducing valve is initially turned to the minimum pressure, the air supply is turned on. The pressure of the air bled into the steam being fed into the processing vessel via the poppet valve is then adjusted until the hammering stops and a clear hiss is heard which will usually occur when the air pressure is 1 or2 psig (6.9or13.8 x 103 Pa) above the steam pressure.
The processing vessel incorporating the steam injecting apparatus is now ready for use and the above described adjustments need not be made again.
The steam injecting apparatus may be used in conjunction with the steam jacket of the processing vessel or may be used separately not only for heating the product but also for simmering or maintaining the product at a particular temperature.
Preferably, if the steam injecting apparatus is to be used for controlled temperature processing, the air supply and steam supply to the processing vessel are controlled automatically by means of a remote on/off valve or valves controlled by a signal produced by a temperature probe provided in the processing vessel and by a temperature controller, for example a thermostat, associated with the vessel. If the air and steam supply are to be operated manually, it is recommended that the steam injecting apparatus be used only to attain the required maximum temperature and that the steam jacket be used if it is desired to maintain the product at a given temperature.
Of course, where the steam heated vessel is to be operated under pressure, the necessary vent valve provided on the vessel must of course be open during heating up times to 100"C. Overthistemperature range final heating to the required level may be achieved by using the steam jacket only, the steam injecting apparatus or both. Preferably, these operations are undertaken automatically.
It should be noted that the use of steam injection will cause the steam to condense in the product being processed and that the amount of water condensed into theiproduct is easily calculable being a function of the steam pressure, the rate of heating, and the starting and finishing temperatures. Of course, where flash evaporation by vacuum of the product is available for increasing the speed of the cooling cycle, the amount of water added by the steam injecting apparatus will be equal to the amount of water vapour removed under vacuum, provided of course that the process starting and finishing temperatures are similar.
A typical heating up time of 17 minutes is obtained using steam injecting apparatus embodying the invention on a 250 litre batch of product containing a total of 30% by volume of water in the final mixture with a starting temperature of approximately 2"C and heating through to 100 C. The amount of water condensed in the product is 53 litres. Thus, it will be seen that by adjusting the initial raw material batch to accept less water the difference can easily be catered for.
It should be noted that, for the steam injecting apparatus to operate successfully, the steam should be clean (having preferably been cleaned by filters etc), the boiler producing the steam should be able to work on a "no condensate return" system and most importantly non carcinogenic boiler water inhibitors should be used.
The steam injecting apparatus embodying the invention is normally fully self-cleaning. However, it is advisable that during each cleaning cycle of the processing vessel, a short, for example five minute, burst of steam be passed through the injecting apparatus to ensure sterility. It will of course be understood that, if necessary, the steam injecting apparatus may be dismantled and removed the processing vessel by undoing the bolts 11.
Extensive research have shown that hammering is generally caused by the collapse of bubbles of steam rapidly when injected into the colder projects and that the mixing of air with the steam before injection into the colder product ensures that, when the bubble of steam collapses and condenses it is still contained within a bubble of air. At the correct pressure therefore the air prevents steam hammering in the processing vessel and any damage to the material from which the vessel is constructed caused by hammering is also avoided. Thus, the constant flexing of the material of the processing vessel caused by steam hammering and the rapid workhardening associated therewith are obviated by using apparatus embodying the invention.
Steam injecting apparatus embodying the invention may be used in the food industry in particular and also widely in the pharmaceutical and cosmetic industries.
Claims (14)
1. Apparatus for injecting steam directly into a product in a processing vessel, comprising steam inlet valve means operable under steam pressure to inject steam fed thereto into a product in a processing vessel and air inlet means for bleeding air at a predetermined pressure into the steam being fed to the steam inlet valve means, the pressure of the air bled into the steam being such that hammering of the steam in the processing vessel is prevented.
2. Apparatus according to claim 1, wherein the steam inlet valve of the steam inlet valve means is biased toward a closed position by spring biasing means.
3. Apparatus according to claim 2, wherein the steam inlet valve is a poppet valve.
4. Apparatus according to claim 1, 2 or 3, wherein the air inlet means comprises a nozzle connectable to a pressurised air supply.
5. Apparatus according to claim 4, wherein the nozzle is connected to the pressurised air supply via a one way valve.
6. Apparatus according to any preceding claim, wherein air is supplied to the air inlet means via a pressure reducing valve.
7. Apparatus according to any preceding claim, wherein steam is supplied to the steam inlet valve means via a pressure reducing valve.
8. Apparatus accoding to any preceding claim, wherein means are provided for switching the air supply and/or the steam supply on or off.
9. Apparatus according to claim 8, wherein the switching means are operable in response to the required operating conditions.
10. Apparatus for injecting steam directly into a product substantially as hereinbefore described with reference to and as illustrated in the accompanying drawing.
11. A processing vessel whenever incorporating the apparatus of any one of claims 1 to 10.
12. A process for injecting steam directly into a product in a processing vessel, comprising injecting steam under pressure into the product via steam inlet valve means operable under the steam pressure and bleeding air at a predetermined pressure into the steam prior to injection of the steam into the product, the pressure of air bled into the steam being such that steam hammering in the processing vessel is prevented.
13. A process according to claim 12, wherein the steam inlet valve of the steam inlet valve means is biased toward a closed position by spring biasing means.
14. A processing vessel whenever incorporating the apparatus of claim 12 or 13.
14. A processing according to claim 13, wherein the steam inlet valve is a poppet valve.
15. A process according claim 12, 13 or 14, wherein the air inlet means comprises a nozzle connectable to a pressurised air supply.
16. A process according to claim 15, wherein the nozzle is connected to the pressurised air supply via a one way valve.
17. A process according to any one of claims 12 to 16, wherein air is supplied to the air inlet means via a pressure reducing valve.
18. A process according to any one of claims 12 to 17, wherein steam is supplied to the steam inlet valve means via a pressure reducing valve.
19. A process according to any one of claims 12 to 18, wherein means are provided for switching the air supply and/or the steam supply on or off.
20. A process according to claim 19, wherein the switching means are operable in response to the required operating conditions.
21. A process for injecting steam directly into a product in a processing vessel substantially as
hereinbefore described with reference to the accom
panying drawings.
22. A product whenever produced by the process
of any one of claims 12 to 21.
23. Any novel feature or combination of features
disclosed herein.
New claims or amendments to claims filed on 2 Dec
82
Superseded claims 1 - 23
New or amended claims:- 1 - 14
1. A process for injecting steam directly into a product in a processing vessel, comprising injecting steam under pressure into the product via steam
inlet valve means operable under the steam press
ure and bleeding air at a predetermined pressure
into the steam prior to injection of the steam into the
product, the pressure of air bled into the steam being such that steam hammering in the processing vessel
is prevented.
2. A process according to claim 1, wherein the steam inlet valve of the steam inlet valve means is biased toward a closed position by spring biasing means.
3. A process according to claim 2, wherein the steam inlet valve is a poppet valve.
4. A process according claim 1,2 or 3, wherein the air inlet means comprises a nozzle connectable to a pressurised air supply.
5. A process according to claim 4, wherein the nozzle is connected to the pressurised air supply via a one way valve.
6. A process according to any one of claims 1 to 4, wherein air is supplied to the air inlet means via a pressure reducing valve.
7. A process according to any one of claims 1 to 5, wherein steam is supplied to the steam inlet valve means via a pressure reducing valve.
8. A process according to any one of claims 1 to 7, wherein means are provided for switching the air supply and/or the steam supply on or off.
9. A process according to claim 8, wherein the switching means are operable in response to the required operating conditions.
10. A process for injecting steam directly into a product in a processing vessel substantially as herein before described with reference to the accompanying drawings.
11. A product whenever produced by the process of any one of claims 1 to 10.
12. Apparatus for carrying out the method of any one of claims 1 to 10, comprising steam inlet valve means operable under steam pressure to inject steam fed thereto into a product in a processing vessel and air inlet means for bleeding air at a predetermined pressure into the steam being fed to the steam inlet valve means, the pressure of the air bled into the steam being such that hammering of the steam in the processing vessel is prevented.
13. Apparatus for carrying outthe method of any one of claims 1 to 10, substantially as hereinbefore described with reference to and as illustrated in the accompanying drawing.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB08129403A GB2106800B (en) | 1981-09-29 | 1981-09-29 | Apparatus and a process for injecting steam directly into a product in a processing vessel |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB08129403A GB2106800B (en) | 1981-09-29 | 1981-09-29 | Apparatus and a process for injecting steam directly into a product in a processing vessel |
Publications (2)
Publication Number | Publication Date |
---|---|
GB2106800A true GB2106800A (en) | 1983-04-20 |
GB2106800B GB2106800B (en) | 1984-08-08 |
Family
ID=10524816
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB08129403A Expired GB2106800B (en) | 1981-09-29 | 1981-09-29 | Apparatus and a process for injecting steam directly into a product in a processing vessel |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB2106800B (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102010002444A1 (en) * | 2010-02-26 | 2011-09-01 | BSH Bosch und Siemens Hausgeräte GmbH | Nozzle device with exhaust valve |
DE102010002442A1 (en) * | 2010-02-26 | 2011-09-01 | BSH Bosch und Siemens Hausgeräte GmbH | Nozzle device for a household appliance |
RU2573807C2 (en) * | 2010-11-11 | 2016-01-27 | Конинклейке Филипс Электроникс Н.В. | Steam cooker |
-
1981
- 1981-09-29 GB GB08129403A patent/GB2106800B/en not_active Expired
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102010002444A1 (en) * | 2010-02-26 | 2011-09-01 | BSH Bosch und Siemens Hausgeräte GmbH | Nozzle device with exhaust valve |
DE102010002442A1 (en) * | 2010-02-26 | 2011-09-01 | BSH Bosch und Siemens Hausgeräte GmbH | Nozzle device for a household appliance |
RU2573807C2 (en) * | 2010-11-11 | 2016-01-27 | Конинклейке Филипс Электроникс Н.В. | Steam cooker |
EP2637530B1 (en) * | 2010-11-11 | 2020-02-19 | Koninklijke Philips N.V. | A food steamer |
Also Published As
Publication number | Publication date |
---|---|
GB2106800B (en) | 1984-08-08 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PE20 | Patent expired after termination of 20 years |
Effective date: 20010928 |