NO153128B - PLASTIC PACKAGING consisting of a container and a lid - Google Patents
PLASTIC PACKAGING consisting of a container and a lid Download PDFInfo
- Publication number
- NO153128B NO153128B NO810891A NO810891A NO153128B NO 153128 B NO153128 B NO 153128B NO 810891 A NO810891 A NO 810891A NO 810891 A NO810891 A NO 810891A NO 153128 B NO153128 B NO 153128B
- Authority
- NO
- Norway
- Prior art keywords
- gas
- lid
- container
- waste heat
- heat boiler
- Prior art date
Links
- 238000004806 packaging method and process Methods 0.000 title abstract 2
- 239000007789 gas Substances 0.000 claims description 56
- 239000002918 waste heat Substances 0.000 claims description 15
- 239000003054 catalyst Substances 0.000 claims description 9
- 229930195733 hydrocarbon Natural products 0.000 claims description 7
- 150000002430 hydrocarbons Chemical class 0.000 claims description 7
- 238000004519 manufacturing process Methods 0.000 claims description 7
- 238000000034 method Methods 0.000 claims description 7
- 239000002994 raw material Substances 0.000 claims description 6
- 239000004215 Carbon black (E152) Substances 0.000 claims description 5
- 238000006243 chemical reaction Methods 0.000 claims description 5
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 4
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 4
- 230000001105 regulatory effect Effects 0.000 claims description 2
- 238000009434 installation Methods 0.000 claims 2
- 238000007789 sealing Methods 0.000 abstract 6
- 239000012267 brine Substances 0.000 abstract 2
- 150000003839 salts Chemical class 0.000 abstract 2
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 abstract 2
- 239000011324 bead Substances 0.000 abstract 1
- 238000010438 heat treatment Methods 0.000 description 4
- 239000002912 waste gas Substances 0.000 description 3
- 238000005406 washing Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D43/00—Lids or covers for rigid or semi-rigid containers
- B65D43/02—Removable lids or covers
- B65D43/0202—Removable lids or covers without integral tamper element
- B65D43/0204—Removable lids or covers without integral tamper element secured by snapping over beads or projections
- B65D43/0212—Removable lids or covers without integral tamper element secured by snapping over beads or projections only on the outside, or a part turned to the outside, of the mouth
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D2543/00—Lids or covers essentially for box-like containers
- B65D2543/00009—Details of lids or covers for rigid or semi-rigid containers
- B65D2543/00018—Overall construction of the lid
- B65D2543/00027—Stackable lids or covers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D2543/00—Lids or covers essentially for box-like containers
- B65D2543/00009—Details of lids or covers for rigid or semi-rigid containers
- B65D2543/00018—Overall construction of the lid
- B65D2543/00259—Materials used
- B65D2543/00296—Plastic
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D2543/00—Lids or covers essentially for box-like containers
- B65D2543/00009—Details of lids or covers for rigid or semi-rigid containers
- B65D2543/00444—Contact between the container and the lid
- B65D2543/00481—Contact between the container and the lid on the inside or the outside of the container
- B65D2543/0049—Contact between the container and the lid on the inside or the outside of the container on the inside, or a part turned to the inside of the mouth of the container
- B65D2543/00509—Cup
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D2543/00—Lids or covers essentially for box-like containers
- B65D2543/00009—Details of lids or covers for rigid or semi-rigid containers
- B65D2543/00444—Contact between the container and the lid
- B65D2543/00481—Contact between the container and the lid on the inside or the outside of the container
- B65D2543/00537—Contact between the container and the lid on the inside or the outside of the container on the outside, or a part turned to the outside of the mouth of the container
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D2543/00—Lids or covers essentially for box-like containers
- B65D2543/00009—Details of lids or covers for rigid or semi-rigid containers
- B65D2543/00444—Contact between the container and the lid
- B65D2543/00481—Contact between the container and the lid on the inside or the outside of the container
- B65D2543/00555—Contact between the container and the lid on the inside or the outside of the container on both the inside and the outside
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D2543/00—Lids or covers essentially for box-like containers
- B65D2543/00009—Details of lids or covers for rigid or semi-rigid containers
- B65D2543/00444—Contact between the container and the lid
- B65D2543/00592—Snapping means
- B65D2543/00601—Snapping means on the container
- B65D2543/00611—Profiles
- B65D2543/00657—U-shaped or inverted U
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D2543/00—Lids or covers essentially for box-like containers
- B65D2543/00009—Details of lids or covers for rigid or semi-rigid containers
- B65D2543/00444—Contact between the container and the lid
- B65D2543/00592—Snapping means
- B65D2543/00601—Snapping means on the container
- B65D2543/00675—Periphery concerned
- B65D2543/00685—Totality
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D2543/00—Lids or covers essentially for box-like containers
- B65D2543/00009—Details of lids or covers for rigid or semi-rigid containers
- B65D2543/00444—Contact between the container and the lid
- B65D2543/00592—Snapping means
- B65D2543/00712—Snapping means on the lid
- B65D2543/00722—Profiles
- B65D2543/0074—Massive bead
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D2543/00—Lids or covers essentially for box-like containers
- B65D2543/00009—Details of lids or covers for rigid or semi-rigid containers
- B65D2543/00444—Contact between the container and the lid
- B65D2543/00592—Snapping means
- B65D2543/00712—Snapping means on the lid
- B65D2543/00787—Periphery concerned
- B65D2543/00796—Totality
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Closures For Containers (AREA)
- Packages (AREA)
- Stackable Containers (AREA)
Abstract
Emballasjen består av en beholder med lokk (3) som inngriper innbyrdes langs tre rundtgående, henholdsvis ytre, øvre og indre tetningsflater (6, 8, 16), som innbyrdes er adskilt ved hulrom (11, 17) hvorav det beholderens indre, nærmeste (17) har en form som avbryter hårrrsvirkningen stammende fra spesielt saltlakeinnhold, mens det annet ytre (11) er utformet til å oppta salt ut-skilt ved osmose. Den innvendig glatte beholdervegg (1) går oventil via den øvre tetningsflate (8) over i et kjegleformet, nedad forløpende flensavsnitt (4), som nedentil går over i et sylindrisk flensavsnitt (5), som inngriper med en sylindrisk lokkdels (1) innerflate og undergripes av vulsten (12) Lokkflensen (19) er forsenket via veggdelen (15), hvis tykkelse gradvis vokser nedad, og sam ut for tetningsflaten (16) har et større tverrmoå enn beholderen. Ut over å medføre tettende inngrep ved tetningsflaten (16) presses herved veggen (3) og dermed flensavsnittet (5) utad mot lokkdelen (10) for tetning ved tet-ningsf laten (6). For lokkstabling er lokkdelen (10) via en skrå, utad forløpende del (13) forbundet med en sylindrisk fotdel (14), og veggdelen (15) via en skrått, innad forløpende veggdel forbundet med lokkflaten (19). Utformningen av lokk og beholder hind-rer at salt fra et saltlakeinnhold avsettes utenpå emballasjen og medfører at lokk og beholder kan stables enkeltvis for magasinering, og at beholder med påsatt lokk likeledes kan stables, idet lokkets form ytterligere sikrer at det under påfringen styres korrekt inn over beholdermunningen (2).The package consists of a container with a lid (3) which engages with each other along three circumferential, outer, upper and inner sealing surfaces (6, 8, 16), respectively, which are mutually separated by cavities (11, 17) of which the inner, nearest (container) of the container 17) has a shape which interrupts the hairy effect originating from a special brine content, while the other outer (11) is designed to receive salt secreted by osmosis. The internally smooth container wall (1) merges upwards via the upper sealing surface (8) into a conical, downwardly extending flange section (4), which at the bottom merges into a cylindrical flange section (5), which engages with an inner surface of a cylindrical lid part (1). and is gripped by the bead (12). In addition to causing sealing engagement at the sealing surface (16), the wall (3) and thus the flange section (5) is thereby pressed outwards against the lid part (10) for sealing at the sealing surface (6). For lid stacking, the lid part (10) is connected via an inclined, outwardly extending part (13) to a cylindrical foot part (14), and the wall part (15) via an inclined, inwardly extending wall part to the lid surface (19). The design of the lid and container prevents salt from a brine content from being deposited on the outside of the packaging and means that the lid and container can be stacked individually for storage, and that the container with the lid attached can also be stacked, further ensuring that the lid is controlled correctly during application. over the container mouth (2).
Description
Fremgangsmåte samt anlegg til fremstilling av lysgass. Process and plant for the production of light gas.
Denne oppfinnelse vedrører en fremgangsmåte og et apparat for fremstilling av lysgass ved. omdannelse av gassformige eller flytende hydrocarboner, hvor råstoffet behandles med damp i nærvær av en katalysator, og den behandlede gass føres gjennom en utvekslingskonverter for å redusere dens innhold av carbonmonoksyd. This invention relates to a method and an apparatus for the production of light gas by. conversion of gaseous or liquid hydrocarbons, where the feedstock is treated with steam in the presence of a catalyst, and the treated gas is passed through an exchange converter to reduce its carbon monoxide content.
Formålet med oppfinnelsen er å kunne kontrollere temperaturen hos den gass som The purpose of the invention is to be able to control the temperature of the gas which
trer inn i utvekslingskonverter en, så at gassen som forlater reaktoren ved 800— 850°C, kjøles ned til 350—400°C innen den trer inn i utvekslingskonverter en. enters exchange converter one, so that the gas leaving the reactor at 800-850°C is cooled to 350-400°C before it enters exchange converter one.
Ifølge oppfinnelsen blir en del av den omdanne te gass ført gjennom en spill var - mekjel og derved nedkjølt, og tilføres deretter til resten av den omdannete gass innen denne trer inn i utvekslingskonyerte-ren, idet temperaturen reguleres ved å styre den gassmengde som føres gjennom spill - varmekjelen. According to the invention, a part of the converted gas is passed through a waste heating boiler and thereby cooled, and is then added to the rest of the converted gas before it enters the exchange reactor, the temperature being regulated by controlling the amount of gas that is passed through game - the hot pot.
I en egnet utførelsesform for et anlegg for gjennomføring av oppfinnelsen blir kontrollerte mengder av hydrocarbonråstoff og luft forbrent i en reaktor; dette oppvarmer katalysatorsengen i reaktoren. De varme spillgasser føres deretter gjennom en seksjon i en spillvarmekjel som er delt i to deler. En ventil som fører inn til en skorstein er åpen, og spillgassene, som nå er kalde, føres hen til atmosfæren gjennom skorsteinen. Når katalysatorsengen i reaktoren har nådd den ønskete tempe-ratur, blir lufttilførselen utkoblet, og etter en kort utspyling med damp, lukkes skorsteinsventilen. Hydrocarbonråstoff og damp føres nå gjennom reaktorens katalysatorseng og omdannes til gass som inneholder carbonmonoksyd. In a suitable embodiment of a plant for carrying out the invention, controlled amounts of hydrocarbon raw material and air are burned in a reactor; this heats the catalyst bed in the reactor. The hot waste gases are then passed through a section in a waste heat boiler which is divided into two parts. A valve leading into a chimney is open, and the waste gases, now cold, are led to the atmosphere through the chimney. When the catalyst bed in the reactor has reached the desired temperature, the air supply is switched off, and after a short purge with steam, the chimney valve is closed. Hydrocarbon feedstock and steam are now passed through the reactor's catalyst bed and converted into gas containing carbon monoxide.
Denne varme gass deles nå i to strøm-mer, hvorav en passerer gjennom den samme seksjon i spillvarmekjelen og avkjøles i denne. En gj ennomstrømningsventil åp-nes og tillater den nedkjølte gass å strøm-me inn i en hovedledning for kald gass. Gassen bringes til å strømme gj ennom denne hovedledning av damp som trenges for utvekslingsreaksjonen med carbonmonoksyd, og brukes i form av en injektor. En alternativ måte til å fremme gasstrømning gjennom hovedledningen .for kaldgass er ved hjelp av en vifte eller ved å tildanne en venturistrupeåpning i hovedledningen for varmgass ved utløpet fra reaktoren. This hot gas is now divided into two streams, one of which passes through the same section in the waste heat boiler and is cooled in it. A bypass valve opens and allows the cooled gas to flow into a main cold gas line. The gas is made to flow through this main line of steam which is needed for the exchange reaction with carbon monoxide, and is used in the form of an injector. An alternative way to promote gas flow through the cold gas main is by means of a fan or by forming a venturi throat opening in the hot gas main at the outlet from the reactor.
Den kalde gass blandes med strøm-men av varm gass fra reaktoren og temperaturen for den blandete gass styres ved å variere mengden av gass som nedkjøles og blandes med yarmgassen. Styrepunktet er en klaffventil som er innskutt mellom gjennomstrømningsventilen og dampinjek-toren. Styringen kan foregå automatisk fra et avfølingspyrometer i den blandete gassstrøm eller ved katalysatorsengen for CO-utveksling. The cold gas is mixed with the flow of hot gas from the reactor and the temperature of the mixed gas is controlled by varying the amount of gas that is cooled and mixed with the yarm gas. The control point is a flap valve that is inserted between the flow valve and the steam injector. The control can take place automatically from a sensing pyrometer in the mixed gas stream or at the catalyst bed for CO exchange.
CO-innholdet i den blandete gass senkes ved føring gjennom CO-utvekslings-katalysatoren, og den varme, behandlete gass passerer gjennom den annen seksjon i spillvarmekjelen og gjennom en automatisk vanntetning i et vaskeapparat, og etter The CO content of the mixed gas is lowered by passing it through the CO exchange catalyst, and the hot, treated gas passes through the second section of the waste heat boiler and through an automatic water seal in a scrubber, and after
å ha passert gjennom vannstråler, forlater having passed through jets of water, leaves
den nedkjølte og vaskete gass anlegget. the cooled and washed gas plant.
I et annet egnet arrangement anvendes en spillvarmekjel med enkelte gjennomløp for å nedkjøle en viss andel av den omdan- In another suitable arrangement, a waste heat boiler with individual passages is used to cool down a certain proportion of the converted
nete gass, og en damoverheter brukes til å nete gas, and a dam overheter is used to
nedkjøle gassen som forlater utvekslingskonverteren. cool the gas leaving the exchange converter.
Det henvises nå til de medfølgende Reference is now made to the accompanying documents
tegninger, hvor: drawings, where:
Fig. 1 viser en utførelsesform for et apparat ifølge oppfinnelsen, under oppvarmingsfasen. Fig. 2 viser den samme utførelse under fremstillingsfasen. Fig. 1 shows an embodiment of a device according to the invention, during the heating phase. Fig. 2 shows the same design during the manufacturing phase.
Fig. 3 viser et modifisert arrangement. Fig. 3 shows a modified arrangement.
Idet det henvises til figurene 1 og 2 With reference to figures 1 and 2
finnes det deri en reaktor 1 med katalysa- there is a reactor 1 with catalysis
torseng 2, innløp 3, 4, 5 for luft, hydrocar-bonråstof f og damp, et utløp 6 til den nedre seksjon 7 i en spillvarmekjel, samt et rør 8 hen til en CO-utvekslingskonverter 9 som inneholder en katalysatorseng 10. Konver- bed 2, inlets 3, 4, 5 for air, hydrocarbon feedstock f and steam, an outlet 6 to the lower section 7 of a waste heat boiler, as well as a pipe 8 to a CO exchange converter 9 containing a catalyst bed 10. Convert-
teren 9 har et utløp 11 til den øvre seksjon 12 i spillvarmekjelen, hvorfra det forløper et rør 13 til en gassvasker 14. Fra den nedre seksjon 7 i kjelen fører et rør 15 gjennom en skorsteinsventil 16 til en skorstein 17, The tank 9 has an outlet 11 to the upper section 12 of the waste heat boiler, from which a pipe 13 runs to a gas scrubber 14. From the lower section 7 of the boiler, a pipe 15 leads through a chimney valve 16 to a chimney 17,
mens et forgreningsrør 18 med ventil 19 og dampinjektor 20 fører hen til røret 8. En klaffventil 21 er anbragt i røret 18. while a branch pipe 18 with valve 19 and steam injector 20 leads to pipe 8. A flap valve 21 is placed in pipe 18.
Under oppvarmingsfasen blir luft og During the heating phase, air and
råstoff tilført ved 3 og 4 og forbrennes i re- raw material added at 3 and 4 and burned in re-
aktoren 1 for å oppvarme katalysatorsen- the actuator 1 to heat the catalytic converter
gen 2, idet spillgassene passerer gjennom kjelseksjonen 7 hen til skorsteinen 17. Et- gen 2, as the waste gases pass through the boiler section 7 to the chimney 17. A
ter at oppvarmingsfasen er fullført, veksles anlegget over til fremstilling ved å lukke skorsteinsventilen 17 og å åpne ventilen 19, idet råstoff og damp tilføres ved 4 og 5. Once the heating phase has been completed, the plant is switched over to production by closing the chimney valve 17 and opening the valve 19, as raw material and steam are supplied at 4 and 5.
Gass fremstilt i katalysatorsengen 2 strøm- Gas produced in the catalyst bed 2 current-
mer gjennom utvekslingskonverteren 9 og kjelseksjonen 12 til vaskeapparatet 14. En del av gassen avledes gjennom utløpet 9 more through the exchange converter 9 and the boiler section 12 to the washer 14. Part of the gas is diverted through the outlet 9
til kjelseksjonen 7 og røret 18 for atter å to the boiler section 7 and the pipe 18 again
slutte seg til hovedgasstrømmen i røret 8. join the main gas stream in pipe 8.
Denne del av gassen, hvis mengde kan sty- This part of the gas, the amount of which can be
res med klaffventilen 21, nedkjøles i kjelseksjonen 7 og tjener til å styre tempera- res with the flap valve 21, is cooled in the boiler section 7 and serves to control the temperature
turen for gassen som trer inn i konverte- the trip for the gas entering the converter
ren 9. Den fremstilte gass passerer fra vaskeapparatet 14 hen til forbruksstedet. clean 9. The produced gas passes from the washing device 14 to the point of consumption.
I det modifiserte arrangement som er In the modified arrangement that is
vist i fig. 3 har spillvarmekjelen bare en seksjon 7, hvorigjennom gasser fra reakto- shown in fig. 3, the waste heat boiler has only one section 7, through which gases from the reactor
ren 1 strømmer hen til skorsteinen 17 eller røret 18 slik som tidligere. Gassen som strømmer gjennom røret 18 under fremstillingsfasen trer inn i utløpsrøret 8 fra reaktoren 1, og trer deretter inn i en damp- clean 1 flows to the chimney 17 or pipe 18 as before. The gas flowing through the pipe 18 during the production phase enters the outlet pipe 8 from the reactor 1, and then enters a steam
□verheter 22, hvor temperaturen for hele gasstrømmen senkes til det som, trenges i konverteren 9. Fra konverteren 9 strøm- □verheter 22, where the temperature of the entire gas flow is lowered to what is needed in the converter 9. From the converter 9 current
mer gassen gjennom en super heter 23 til vaskeapparatet 14, idet denne superheter eller overheter 23 erstatter den øvre kjelsek- more the gas through a super heater 23 to the washing device 14, as this super heater or super heater 23 replaces the upper boiler
sjon 12 i figurene 1 og 2. Temperaturen for gassen som trer inn i overheter en 22 sty- tion 12 in Figures 1 and 2. The temperature of the gas entering the superheater en 22 sty-
res ved å variere mengdeforholdet med hensyn på gass frembragt i reaktoren, som kjøles ved å passere gjennom kjelen 7. res by varying the quantity ratio with regard to gas produced in the reactor, which is cooled by passing through the boiler 7.
Dampen som frembringes i spillvarme- The steam produced in waste heat-
kjelen og overheterne (når disse anvendes) the boiler and superheaters (when these are used)
kan brukes til å gjennomføre prosessen, can be used to carry out the process,
og til å fremføre gassen i røret 18 ved hjelp av injektoren 20, hvorved man skaf- and to advance the gas in the pipe 18 by means of the injector 20, whereby one obtains
fer den damp som trenges for CO-utveks-lingsreaksj onen. provides the steam needed for the CO exchange reaction.
Claims (4)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DK114280A DK148416C (en) | 1980-03-17 | 1980-03-17 | PLASTIC PACKAGING CONTAINING A CONTAINER AND A COVER |
Publications (3)
Publication Number | Publication Date |
---|---|
NO810891L NO810891L (en) | 1981-09-18 |
NO153128B true NO153128B (en) | 1985-10-14 |
NO153128C NO153128C (en) | 1986-01-22 |
Family
ID=8101484
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
NO810891A NO153128C (en) | 1980-03-17 | 1981-03-16 | PLASTIC PACKAGING consisting of a container and a lid. |
Country Status (5)
Country | Link |
---|---|
JP (1) | JPS571055A (en) |
DE (1) | DE3110057A1 (en) |
DK (1) | DK148416C (en) |
NO (1) | NO153128C (en) |
SE (1) | SE449847B (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB9516562D0 (en) * | 1995-08-12 | 1995-10-11 | Penlea Plastics Ltd | Sealed pack |
DE19628934C2 (en) * | 1996-07-18 | 1999-03-04 | Rolf Kimmich | Transport packaging |
JP2001240091A (en) * | 2000-03-01 | 2001-09-04 | Shikoku Kakoki Co Ltd | Bottle hermetic sealer |
JP4610318B2 (en) * | 2004-12-10 | 2011-01-12 | 株式会社エフピコ | Packaging container lid, packaging container and food packaging |
US8210391B2 (en) * | 2005-10-14 | 2012-07-03 | Ropak Corporation | Performance oriented pail |
-
1980
- 1980-03-17 DK DK114280A patent/DK148416C/en not_active IP Right Cessation
-
1981
- 1981-03-12 SE SE8101581A patent/SE449847B/en not_active IP Right Cessation
- 1981-03-16 NO NO810891A patent/NO153128C/en unknown
- 1981-03-16 DE DE19813110057 patent/DE3110057A1/en not_active Withdrawn
- 1981-03-17 JP JP3734181A patent/JPS571055A/en active Pending
Also Published As
Publication number | Publication date |
---|---|
DK148416C (en) | 1985-11-25 |
DE3110057A1 (en) | 1982-01-07 |
NO810891L (en) | 1981-09-18 |
SE449847B (en) | 1987-05-25 |
JPS571055A (en) | 1982-01-06 |
NO153128C (en) | 1986-01-22 |
SE8101581L (en) | 1981-09-18 |
DK148416B (en) | 1985-07-01 |
DK114280A (en) | 1981-09-18 |
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