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Patent US7038701 - Method for zooming - Google PatentsSearch Images Maps Play YouTube News Gmail Drive More »Sign inPatentsAn image is being presented on a display device connected to a storage unit, wherein said presentation image is loaded to the display device from said storage unit and said presentation image comprises at least one preselected, zoomable area. A method for zooming in the image comprises the steps of continuously...http://www.google.com/patents/US7038701?utm_source=gb-gplus-sharePatent US7038701 - Method for zoomingAdvanced Patent SearchTry the new Google Patents, with machine-classified Google Scholar results, and Japanese and South Korean patents.Publication numberUS7038701 B2Publication typeGrantApplication numberUS 09/853,602Publication dateMay 2, 2006Filing dateMay 14, 2001Priority dateFeb 2, 2001Fee statusPaidAlso published asCN1265319C, CN1489750A, CN1489751A, EP1364339A1, EP1366465A1, US20020105531, US20020141655, WO2002061681A1, WO2002061681A8, WO2002061682A1, WO2002061682A8Publication number09853602, 853602, US 7038701 B2, US 7038701B2, US-B2-7038701, US7038701 B2, US7038701B2InventorsSami NiemiOriginal AssigneeScalado AbExport CitationBiBTeX, EndNote, RefManPatent Citations (11), Non-Patent Citations (2), Referenced by (32), Classifications (16), Legal Events (4) External Links: USPTO, USPTO Assignment, EspacenetMethod for zooming
Patent CitationsCited PatentFiling datePublication dateApplicantTitleUS5341466May 9, 1991Aug 23, 1994New York UniversityFractal computer user centerface with zooming capabilityUS5880856Nov 19, 1996Mar 9, 1999Microsoft CorporationProgressive image transmission using discrete wavelet transformsUS5907640Mar 25, 1994May 25, 1999Live Picture, Inc.Functional interpolating transformation system for image processingUS6049342Oct 27, 1997Apr 11, 2000International Business Machines CorporationSystem and method for controlling the downloading and display of an animated sequence from a networkUS6147709 *Apr 7, 1997Nov 14, 2000Interactive Pictures CorporationMethod and apparatus for inserting a high resolution image into a low resolution interactive image to produce a realistic immersive experienceUS6281874 *Aug 27, 1998Aug 28, 2001International Business Machines CorporationMethod and system for downloading graphic images on the internetUS6526234 *Jul 17, 2001Feb 25, 2003Eastman Kodak CompanyRevision suggestion camera and methodUS6600840 *Jul 21, 1997Jul 29, 2003International Business Machines CorporationImage format conversion such as photometric, rotation, cropping, padding, scaling, dithering, bit padding, grayscale and color transformation, encoding and decoding using a plurality of filtersUS20030033402 *Apr 7, 2000Feb 13, 2003Reuven BattatMethod and apparatus for intuitively administering networked computer systemsEP0878956A1May 11, 1998Nov 18, 1998Canon Kabushiki KaishaMethod of and system for editing imagesGB2343807A Title not available* Cited by examinerNon-Patent CitationsReference1Nisha Talagala et al., "The Art of Massive Storage: A Web Image Archive", Computer, pp. 22-28 (Nov. 11, 2000).2Nisha Talagala et al., "Usage Patterns of a Web-Based Image Collection," IEEE Symposium on Mass Storage Systems 1999: 203-214.Referenced byCiting PatentFiling datePublication dateApplicantTitleUS7451405 *Sep 15, 2004Nov 11, 2008Research In Motion LimitedMethod for requesting and viewing a zoomed area of detail from an image attachment on a mobile communication deviceUS7733356 *Feb 13, 2009Jun 8, 2010Research In Motion LimitedMethod for requesting and viewing an attachment image on a portable electronic deviceUS7812852Oct 31, 2006Oct 12, 2010Research In Motion LimitedMethod and system for zoomable attachment handling on a portable electronic deviceUS7843472Apr 26, 2010Nov 30, 2010Research In Motion LimitedMethod for requesting and viewing an attachment image on a portable electronic deviceUS7986465Feb 28, 2008Jul 26, 2011Rhevision Technology, Inc.Systems and methods for effecting zoom and focus using fluidic adaptive lensesUS7991837Nov 24, 2010Aug 2, 2011Cme Advantage, Inc.Systems and methods for networked, in-context, high resolution image viewingUS8018473Aug 30, 2010Sep 13, 2011Research In Motion LimitedMethod and system for zoomable attachment handling on a portable electronic deviceUS8082512Aug 3, 2007Dec 20, 2011Microsoft CorporationFractal display advertising on computer-driven screensUS8196062 *Aug 27, 2008Jun 5, 2012Research In Motion LimitedMethod for requesting and viewing a zoomed area of detail from an image attachment on a mobile communication deviceUS8254034Mar 27, 2009Aug 28, 2012Rhevision Technology, Inc.Fluidic adaptive lens with a lens membrane having suppressed fluid permeabilityUS8584037May 9, 2012Nov 12, 2013Blackberry LimitedMethod for requesting and viewing a zoomed area of detail from an image attachment on a mobile communication deviceUS8923650Jan 7, 2013Dec 30, 2014Wexenergy Innovations LlcSystem and method of measuring distances related to an objectUS8957920Jun 25, 2010Feb 17, 2015Microsoft CorporationAlternative semantics for zoom operations in a zoomable sceneUS9098170Feb 16, 2007Aug 4, 2015Blackberry LimitedSystem, method, and user interface for controlling the display of images on a mobile deviceUS9208581Dec 23, 2014Dec 8, 2015WexEbergy Innovations LLCMethod of determining measurements for designing a part utilizing a reference object and end user provided metadataUS9230339Jul 1, 2014Jan 5, 2016Wexenergy Innovations LlcSystem and method of measuring distances related to an objectUS9342864Jan 7, 2015May 17, 2016Microsoft Technology Licensing, LlcAlternative semantics for zoom operations in a zoomable sceneUS9691163Sep 25, 2015Jun 27, 2017Wexenergy Innovations LlcSystem and method of measuring distances related to an object utilizing ancillary objectsUS20060055693 *Sep 15, 2004Mar 16, 2006Arizan CorporationMethod for requesting and viewing a zoomed area of detail from an image attachment on a mobile communication deviceUS20060056604 *Sep 15, 2004Mar 16, 2006Research In Motion LimitedMethod for scaling images for usage on a mobile communication deviceUS20060072820 *Oct 5, 2004Apr 6, 2006Nokia CorporationSystem and method for checking framing and sharpness of a digital imageUS20070234232 *May 29, 2007Oct 4, 2007Gheorghe Adrian CituDynamic image displayUS20080102887 *Oct 31, 2006May 1, 2008Sylthe Olav AMethod and System for Zoomable Attachment Handling on a Portable Electronic DeviceUS20080102900 *Feb 16, 2007May 1, 2008Research In Motion LimitedSystem, method, and user interface for controlling the display of images on a mobile deviceUS20080316225 *Aug 27, 2008Dec 25, 2008Sylthe Olav AMethod for requesting and viewing a zoomed area of detail from an image attachment on a mobile communication deviceUS20090037838 *Aug 3, 2007Feb 5, 2009Microsoft CorporationFractal display advertising on computer-driven screensUS20090128581 *Nov 20, 2007May 21, 2009Microsoft CorporationCustom transition framework for application state transitionsUS20090177538 *Jan 8, 2008Jul 9, 2009Microsoft CorporationZoomable advertisements with targeted contentUS20090207190 *Feb 13, 2009Aug 20, 2009Sylthe Olav AMethod for requesting and viewing an attachment image on a portable electronic deviceUS20100235753 *Apr 26, 2010Sep 16, 2010Sylthe Olav AMethod for Requesting and Viewing an Attachment Image on a Portable Electronic DeviceUS20110050704 *Aug 30, 2010Mar 3, 2011Sylthe Olav AMethod and System For Zoomable Attachment Handling on a Portable Electronic DeviceUS20110118834 *Sep 1, 2010May 19, 2011Yuhwa LoFluidic intraocular lens systems and methods* Cited by examinerClassifications U.S. Classification345/660International ClassificationG06T3/40, G09G5/36, H04N1/393, G06T1/00, G06F3/048, G06T15/20, G09G5/00, G06F3/14Cooperative ClassificationG09G2340/0407, G09G2370/027, G06F3/14, G06T3/403, G09G2340/045European ClassificationG06T3/40E, G06F3/14Legal EventsDateCodeEventDescriptionSep 4, 2001ASAssignmentOwner name: SCALADO AB, SWEDENFree format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:NIEMI, SAMI;REEL/FRAME:012135/0583Effective date: 20010822Oct 9, 2009FPAYFee paymentYear of fee payment: 4Jul 6, 2012ASAssignmentOwner name: MOBILE IMAGING IN SWEDEN AB, SWEDENFree format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:SCALADO AB;REEL/FRAME:028499/0047Effective date: 20120629Oct 2, 2013FPAYFee paymentYear of fee payment: 8RotateOriginal ImageGoogle Home - Sitemap - USPTO Bulk Downloads - Privacy Policy - Terms of Service - About Google Patents - Send FeedbackData provided by IFI CLAIMS Patent Services


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Patent US20040152304 - Insitu post atomic layer deposition destruction of active species - Google PatentsSearch Images Maps Play YouTube News Gmail Drive More »Sign inAdvanced Patent SearchPatentsSystems and methods for insitu post atomic layer deposition (ALD) destruction of active species are provided. ALD processes deposit multiple atomic layers on a substrate. Pre-cursor gases typically enter a reactor and react with the substrate resulting in a monolayer of atoms. After the remaining gas...http://www.google.com/patents/US20040152304?utm_source=gb-gplus-sharePatent US20040152304 - Insitu post atomic layer deposition destruction of active speciesAdvanced Patent SearchPublication numberUS20040152304 A1Publication typeApplicationApplication numberUS 10/356,981Publication dateAug 5, 2004Filing dateJan 30, 2003Priority dateJan 30, 2003Also published asUS6844260, US8257497, US20050150460Publication number10356981, 356981, US 2004/0152304 A1, US 2004/152304 A1, US 20040152304 A1, US 20040152304A1, US 2004152304 A1, US 2004152304A1, US-A1-20040152304, US-A1-2004152304, US2004/0152304A1, US2004/152304A1, US20040152304 A1, US20040152304A1, US2004152304 A1, US2004152304A1InventorsDemetrius Sarigiannis, Shuang Meng, Garo DerderianOriginal AssigneeMicron Technology, Inc.Export CitationBiBTeX, EndNote, RefManReferenced by (6), Classifications (26), Legal Events (3) External Links: USPTO, USPTO Assignment, EspacenetInsitu post atomic layer deposition destruction of active speciesUS 20040152304 A1Abstract Systems and methods for insitu post atomic layer deposition (ALD) destruction of active species are provided. ALD processes deposit multiple atomic layers on a substrate. Pre-cursor gases typically enter a reactor and react with the substrate resulting in a monolayer of atoms. After the remaining gas is purged from the reactor, a second pre-cursor gas enters the reactor and the process is repeated. The active species of some pre-cursor gases do not readily purge from the reactor, thus increasing purge time and decreasing throughput. A high-temperature surface placed in the reactor downstream from the substrate substantially destroys the active species insitu. Substantially destroying the active species allows the reactor to be readily purged, increasing throughput. Images(8) Claims(37)
We claim: 1. A method of atomic layer deposition, the method comprising: heating at least one workpiece in a reactor to a temperature suitable for atomic layer deposition; introducing a gas into the reactor; heating a surface in the reactor to a temperature high enough to substantially destroy the portion of the gas that does not react with the workpiece; subjecting the non-reacted portion to the heated surface; and purging the gas from the reactor. 2. The method of claim 1 wherein the workpiece is a semiconductor substrate. 3. The method of claim 1 wherein the heating comprises heating the surface to a temperature high enough to cause the portion of the gas that does not react with the workpiece to substantially decay into a non-active species. 4. The method of claim 1 wherein the surface comprises MnO, MnO2, or CuO. 5. The method of claim 1 wherein the surface comprises a catalyst that destroys at least a portion of the gas that does not react with the workpiece. 6. The method of claim 1 wherein the surface is heated to a temperature greater than about 200� C. and less than about 300� C. 7. The method of claim 1 wherein the surface is heated to a temperature greater than about 300� C. and less than about 400� C. 8. The method of claim 1 wherein the surface is heated to a temperature greater than about 400� C. 9. The method of claim 1 wherein the subjecting comprises forcing gases to flow from the heating of the workpiece to the heated surface. 10. The method of claim 1 wherein the surface is selected from the group consisting of a ring, a mesh, a perforated plate, a fin, and any combination thereof. 11. The method of claim 10 wherein the ring includes passageways through which gas can pass. 12. The method of claim 11 wherein vacuum is pulled through at least one of the passageways. 13. A method of atomic layer deposition, the method comprising: heating a workpiece to a first temperature inside a reactor; introducing a gas into the reactor for atomic layer deposition; heating a structure inside the reactor to a second temperature; creating a gas flow from the substrate to the structure; and purging the gas from the reactor. 14. The method of claim 13 wherein the first temperature causes at least a portion of the gas to react with the workpiece. 15. The method of claim 13 wherein the second temperature is high enough to substantially destroy that portion of the gas that does not react with the workpiece. 16. The method of claim 13 wherein the first temperature is lower than the second temperature. 17. The method of claim 13 wherein the first temperature is higher than the second temperature. 18. A reactor for use in atomic layer deposition, the reactor comprising: at least one gas input through which gas enters the reactor; a heater operative to heat a workpiece inside the reactor to a temperature suitable for atomic layer deposition; at least one surface operative to be heated to a temperature high enough to substantially destroy that portion of a gas that does not react with the workpiece; and at least one gas output through which gas exits the reactor. 19. The reactor of claim 18 wherein the surface comprises MnO, MnO2, or CuO. 20. The reactor of claim 18 wherein the surface comprises a catalyst that destroys at least a portion of a gas that does not react with the workpiece. 21. The reactor of claim 18 wherein the surface is operative to be heated to a temperature greater than about 200� C. and less than about 300� C. 22. The reactor of claim 18 wherein the surface is operative to be heated to a temperature greater than about 300� C. and less than about 400� C. 23. The reactor of claim 18 wherein the surface is operative to be heated to a temperature greater than about 400� C. 24. The reactor of claim 18 wherein the surface is selected from the group consisting of a ring, a mesh, a perforated plate, a fin, and any combination thereof. 25. The reactor of claim 24 wherein the ring includes ducts through which gas can flow. 26. The reactor of claim 25 wherein vacuum is pulled through at least one duct. 27. A reactor for use in atomic layer deposition, the reactor comprising: at least one gas input through which a gas enters the reactor; at least one gas output through which gas exits the reactor; at least one heater operative to heat a semiconductor substrate inside the reactor to a first temperature; and at least one structure operative to be heated to a second temperature, the structure positioned inside the reactor between the heater and the gas output. 28. The reactor of claim 27 wherein the first temperature is high enough such that a portion of the pre-cursor gas reacts with the substrate. 29. The reactor of claim 27 wherein the second temperature is high enough to destroy a portion of the pre-cursor gas that does not react with the substrate. 30. The reactor of claim 27 wherein the first temperature is lower than the second temperature. 31. Apparatus for use in atomic layer deposition, the apparatus comprising: means for entering a gas into an enclosure; means for causing a portion of the gas to react with a material in the enclosure; means for heating the gas in the enclosure after it reacts with the material; and means for purging the gas from the enclosure. 32. A method of atomic layer deposition, the method comprising: heating a first area inside an enclosure to about 200� C.; heating a second area inside the enclosure concurrently to about 400� C.; and creating a gas flow from the first area to the second area. 33. The method of claim 32 further comprising: providing a gas to the first area; and purging gas from the second area. 34. The method of claim 33 wherein the gas comprises ozone. 35. The method of claim 32 further comprising placing a semiconductor substrate in the first area. 36. A method of atomic layer deposition, the method comprising: heating a first area inside an enclosure to a first temperature; heating a structure in a second area inside the enclosure concurrently to heating the first area to a second temperature; placing a workpiece in the first area; providing a gas to the first area; creating a gas flow from the first area to the second area; and purging gas from the second area. 37. A reactor for use in atomic layer deposition, the reactor comprising: at least one gas input through which a gas enters the reactor; at least one gas output through which gas exits the reactor; a heater operative to heat a workpiece to at least 200� C.; and at least one structure operative to be heated to a temperature greater than 200� C., the structure positioned inside the reactor between the heater and the gas output. Description
BACKGROUND OF THE INVENTION [0001] This invention relates to systems and methods that destroy active species of pre-cursor gases used in atomic layer deposition (ALD). More particularly, this invention relates to systems and methods that destroy active species of pre-cursor gases inside the reactor in which the ALD occurs. [0002] ALD is a process in which atoms are deposited on a substrate, monolayer at a time, to grow a multi-layered thin film. In typical ALD processes, a first pre-cursor gas enters a reactor in which a substrate is placed. The first pre-cursor gas saturates the surface of the substrate forming a first monolayer. The reactor is then typically purged with an inert gas. Purging is required to prevent parasitic chemical vapor deposition (CVD) reactions from occurring between the first pre-cursor gas and a second pre-cursor gas that enters the chamber after purging. If most of the pre-cursor gas is not purged from the chamber, these reactions can form particles that will either ruin the thin film being grown, result in an undesired CVD-type deposition, or both. Problems associated with CVD-type deposition include poor step coverage and poor uniformity. [0003] After the first pre-cursor gas is purged, a second pre-cursor gas enters the reactor and reacts with the adsorbed monolayer or partial monolayer (i.e., the first monolayer) to form a monolayer of the desired film. The reactor is again purged with an inert gas. This process is repeated until the thin film is grown to a desired thickness. [0004] In some ALD reactions, one of the pre-cursors may include an active species. An active species is a molecule that is not in its most stable state. Active species will readily react to either accept or donate electrons in a reaction (e.g., O3, O*, or N* (where * denotes an excited state with excess energy)). Because most active species readily decay or recombine into a more stable state as temperature increases, they have a relatively short half-life in an ALD chamber operating at temperatures in excess of 400� C. However, in some cases, it may be advantageous to grow a film via ALD at lower temperatures such as 200� C. In this situation, the half-life of the active species is increased, and for a given purge time, there is a higher initial concentration of active species present to be purged from the reactor. This directly reduces the throughput of the reactor. [0005] Variables that can affect the half-life of active species of gases include temperature and pressure. As temperature and pressure increase, the half-life of the active species decreases because of simple kinetics. Destruction of the active species is necessary because of their high reactivity. For [0006] the eyes and lungs, and so should be completely converted into O2 before being discharged to the atmosphere. ALD processes that require the use of an active species typically run at temperatures high enough to destroy (e.g., consume or decompose) most of the active species before they leave the chamber. This reduces the concentration level of the active species significantly. [0007] However, current experience with ALD processes indicates that it may be advantageous to operate at temperatures lower than the high temperatures of many known ALD processes. For example, many of the metal-organic pre-cursors that may be used in the ALD of hafnium (Hf) oxide decompose at temperatures higher than 200� C. Therefore, in order to obtain a film with acceptable properties (e.g., step coverage, low carbon content) the reactor must be operated at a temperature close to or lower than 200� C. When ozone is used as an oxidizer in this process, these lower temperatures are not sufficient to decompose all of the ozone before it leaves the reactor. [0008] For example, in the ALD of hafnium oxide, if ozone is supplied to a reactor and the chamber is running at 400� C., a certain percentage of the ozone, X, will be consumed by the reaction with the Hf pre-cursor and another percentage, Y, will be consumed by kinetic recombination of the O3 and O* to form O2. This kinetic recombination reaction is driven by temperature. The overall percentage of ozone remaining in the chamber will be Z. However, if the chamber is running at 200� C., the percentage of ozone that recombines will be far less than Y. Thus, the amount remaining to be purged will be greater than Z. This requires a longer purge time. [0009] In view of the foregoing, it would be desirable to decrease the purge time of active species of pre-cursor gases from reactors used in ALD to improve throughput. SUMMARY OF THE INVENTION [0010] It is an object of this invention to decrease the purge time of active species of pre-cursor gases from reactors used in ALD to improve throughput. [0011] Some active species of pre-cursor gases that do not readily decay at typical ALD reaction temperatures are known to readily decay at temperatures higher than the ALD reaction temperatures. For example, when aluminum oxide is deposited using trimethylaluminum (TMA) and ozone (ozone includes O3, O2, and O*), the active species of the ozone (i.e., O3 and O*) do not readily decay at the typical reaction temperature of about 300� C. That is, a large percentage of the active species remains active. In other words, a large concentration of the active species remains in the reactor. This hinders the throughput of the reactor. However, at higher temperatures (e.g., at temperatures equal to or greater than 400� C.) the active species of the ozone readily break down. [0012] There are three ways to decrease the concentration of an active species in the reactor: [0013] i) consume more O3 in the surface reaction to grow film (in ALD this is limited because only one monolayer is grown at a time); ii) increase the temperature to destroy more active species via a kinetic recombination reaction; iii) purge for a longer time. The addition of a high temperature surface beyond the wafer but before the outlet will destroy more active species. This will drop the concentration of the active species to one that can be reduced more readily with a shorter purge time. [0014] In accordance with this invention, a high-temperature surface is placed inside the reactor to significantly speed the decay of the active species and thus increase the throughput of the reactor. The high-temperature surface preferably has a high surface area. The high-temperature surface is preferably a metal, other material, or combination thereof that can be heated to a temperature high enough to induce the rapid decay of the active species of a pre-cursor gas used in ALD. The high-temperature surface may also include a material that catalyzes the active species to further increase the rate of decay. Alternatively, the surface may be coated with a catalyst. In the case of ozone as an active species, the high-temperature surface is preferably heatable to about 400� C. or higher. [0015] The high-temperature surface is preferably placed inside the reactor downstream (with respect to the flow of gas) from the gas input and the substrate and upstream from the gas output. The high-temperature surface is preferably placed inside the reactor such that the temperature of the substrate is not substantially affected by the high-temperature surface. As the active species of a pre-cursor gas are purged, they are �de-activated� (i.e., destroyed) as they pass over the high-temperature surface. [0016] Advantageously, more than one high-temperature surface may be placed inside the reactor according to the invention. In addition, the high-temperature surface or surfaces can be of various shapes. For example, the surface or surfaces may be a group of fins, a ring, a perforated plate, an ordered mesh of metal or other material, or a random mesh of metal or other material. The high-temperature surface is preferably shaped and situated inside the reactor such that the flow of gas through the reactor is not substantially impeded. [0017] Advantageously, thin films may be grown on multiple substrates simultaneously according to the invention.
BRIEF DESCRIPTION OF THE DRAWINGS [0018] The above and other objects and advantages of the invention will be apparent upon consideration of the following detailed description, taken in conjunction with the accompanying drawings, in which like reference characters refer to like parts throughout, and in which: [0019]FIG. 1 illustrates a cross-section of a known reactor used in atomic layer deposition; [0020]FIG. 1A illustrates a plan view of a heater support used in the reactor of FIG. 1 taken through line 1A-1A of FIG. 1; [0021]FIG. 2 illustrates a cross-section of a reactor with a first embodiment of a high-temperature surface therein according to the invention; [0022]FIG. 2A illustrates a plan view of the high-temperature surface of FIG. 2 taken through line 2A-2A of FIG. 2; [0023]FIG. 3 illustrates a cross-section of a reactor with a second embodiment of a high-temperature surface therein according to the invention; [0024]FIG. 3A illustrates a plan view of the high-temperature surface of FIG. 3 taken through line 3A-3A of FIG. 3; [0025]FIG. 4 illustrates a cross-section of a reactor with a third embodiment of a high-temperature surface therein according to the invention; [0026]FIG. 4A illustrates a plan view of the high-temperature surface of FIG. 4 taken through line 4A-4A of FIG. 4; [0027]FIG. 5 illustrates a cross-section of a reactor with a fourth embodiment of a high-temperature surface therein according to the invention; [0028]FIG. 5A illustrates a plan view of the high-temperature surface of FIG. 5 taken through line 5A-5A of FIG. 5; [0029]FIG. 6 illustrates a cross-section of a reactor with a fifth embodiment of a high-temperature surface therein according to the invention; [0030]FIG. 6A illustrates a plan view of the high-temperature surface of FIG. 6 taken through line 6A-6A of FIG. 6; [0031]FIG. 7 illustrates a cross-section of a reactor with a sixth embodiment of a high-temperature surface therein according to the invention; [0032]FIG. 7A illustrates a plan view of the high-temperature surface of FIG. 7 taken through line 7A-7A of FIG. 7; [0033]FIG. 8 illustrates a reactor with more than one gas input and gas output according to the invention; [0034]FIG. 9 illustrates a reactor with multiple substrates therein according to the invention; [0035]FIG. 10 illustrates another reactor with multiple substrates therein according to the invention; [0036]FIG. 11 illustrates a reactor in which the flow of gas is horizontal according to the invention; [0037]FIG. 12 illustrates another reactor in which the flow of gas is horizontal according to the invention; and [0038]FIG. 13 is a flow chart of a process for growing thin films according to the invention.
DETAILED DESCRIPTION OF THE INVENTION [0039] Atomic layer deposition (ALD) processes are used to grow multi-layered thin films for use in a variety of semiconductor fabrication applications. Such applications include DRAMs, SiO2 dielectrics, and gate dielectrics. In typical ALD processes, pre-cursor gases enter a reactor one at a time via one or more gas inputs. Pre-cursor gases used in ALD are often chosen for their self-regulation properties with respect to growth. In some ALD systems, one of the pre-cursors is or includes an active species. For example, in a system to grow aluminum oxide, pre-cursors of trimethylaluminum (TMA) and ozone (ozone includes O3, O2, and O*) are alternately entered into a chamber. Ozone includes the active species O3 and O*. [0040] When a pre-cursor gas reacts with a substrate inside the reactor, a portion of the pre-cursor gas saturates the substrate forming a monolayer of atoms on the substrate. After the pre-cursor gas reacts with the substrate, the pre-cursor and active species (if any) are purged out of the reactor. This is done by either pulling a vacuum on one or more gas outputs of the reactor, forcing an inert gas (e.g., argon) through the reactor, or both. [0041] After the first monolayer is deposited and the first pre-cursor purged, a second pre-cursor gas enters the reactor. This second pre-cursor reacts with the deposited portion of the first pre-cursor gas (i.e., grows on top of the deposited portion of the first pre-cursor gas). The remaining pre-cursor gas and active species (if any) of the second pre-cursor gas are then purged from the reactor. This process is repeated until the film is grown to the desired thickness. [0042]FIG. 1 illustrates a cross-section of a typical reactor for ALD. Gases enter reactor 100 via a gas input 120, which is coupled to a gas line 110. Gas line 110 may be connected to one or more gas sources (not shown). Gas selectively enters reactor 100 by opening or closing valves (not shown) in gas line 110. Gases exit reactor 100 via gas output 190. [0043] Inside reactor 100 is one or more [0044] heaters 140. Heater 140 is supported by heater column 144 and heater support 146. Substrate 130 rests on and is substantially flush with surface 142 of heater 140. Surface 142 should be heated to a temperature suitable for the ALD of the film being grown. That is, surface 142 should be at a temperature that causes a pre-cursor gas to react with the substrate. Substrate 130 may rest on surface 142 simply due to gravity or be held under a vacuum or by mechanical means, or any combination thereof. The surface of substrate 130 with which the pre-cursor gases react does not have to face upward or towards the gas input (however, it should not face down on surface 142). Alternatively, substrate 130 can be placed near heater 140, instead of on it. [0045] Surface 142 is preferably larger in both length and width than the largest substrate to be placed on surface 142. Surface 142 and heater [0046] column 144 are preferably cylindrical. This allows gas to pass over substrate 130 and through reactor 100 more rapidly as compared to surfaces and columns of other shapes. However, surface 142 and heater column 144 can still be of other shapes such as square, hexagonal, or octagonal. [0047]FIG. 1A illustrates a plan view of heater support 146. At the center of support 146 is a [0048] base 150 on which column 144 rests. Extending radially outward from base 150 are several arms 152 that extend to ring 154. As shown, heater support 146 has several openings 156 to allow gas to pass through. Only one arm may be required to support base 150. Ring 154 may be connected to, or be a part of, reactor wall 102. [0049] When growing ALD films, pre-cursor gases and their active species should be purged from the reactor as quickly as possible after the pre-cursor gases react with the substrate. When mass producing ALD films, purge time becomes an important factor in the number of films that can be produced in a given time. [0050] Purging of active species may be difficult when they do not quickly decay into non-active species. This decreases the throughput of the reactor and the overall ALD process time. Non-active species are more readily purgeable because they are more stable and less reactive than active species. [0051] To decrease the purge time of active species used in ALD, which are often temperature sensitive, a high-temperature surface is placed in the reactor in accordance with the invention. The high-temperature surface decreases the half-life of the active species and thus decreases purge time. For ALD reactions using, for example, trimethylaluminum (TMA) and ozone as the pre-cursor gases, the active species of ozone (O3 and O*) usually limit how fast the ALD reactions can be completed. At 250� C. (and 1 Torr) the half-life of ozone is about 76 seconds. The half-life drops to about 0.75 seconds at 400� C. (and 1 Torr), and to about 0.02 seconds at 600� C. (and 1 Torr). [0052] The high-temperature surface is preferably positioned inside the reactor such that the pre-cursor gases react with the substrate before coming in the vicinity of, or in contact with, the high-temperature surface. In other words, the high-temperature surface is preferably downstream from the heater surface and substrate and upstream from the gas output. As the active species of a pre-cursor gas are purged, they are de-activated or �destroyed� (i.e., their reactivity is destroyed) as they pass over the high-temperature surface. [0053]FIG. 2 illustrates a cross-section of a reactor 200 with several high-temperature surfaces 280 therein according to the invention. High-temperature surfaces 280 are �fins� that protrude from inner [0054] wall 202 of reactor 200. Fins 280 may be made of any suitable material or materials that can be heated to a temperature high enough to destroy (i.e., induce the rapid decay of) the active species of pre-cursor gases used in ALD processes. Fins 280 also may include (e.g., be coated with) a material that catalyzes the destruction of the active species. For example, in the case of ozone, fins 280 may include MnO, MnO2, or CuO. Arrows 201 illustrate the flow of gas through [0055] reactor 200. [0056]FIG. 2A illustrates fins 280 extending radially outward from inner wall 202. Fins 280 are preferably not in contact with heater column 244 and may be any suitable shape that does not substantially impede gas flow. For example, the width (along the surface of wall 202) of fins 280 may be substantially smaller than their length (i.e., the portion that extends outward from wall 202). Fins 280 may also be arranged in any suitable way that does not substantially impede gas flow. For example, fins 280 may be pitched. In other words, fins 280 may be situated at angles similar to fan blades. [0057]FIG. 3 illustrates a cross-section of a reactor 300 in accordance with the invention. Closely surrounding heater 340 and preferably slightly below heater surface 342 is heat ring 380. Ring 380 is made of a material or materials that can be heated to a temperature high enough to destroy the active species of pre-cursor gases used in ALD processes. Ring 380 can be, for example, ceramic or Inconel. Heat ring 380 preferably has a flat circular surface and may be supported and connected to reactor wall 302 by [0058] support 382. [0059]FIG. 4 shows another embodiment of a high-temperature surface inside a reactor according to the invention. High-temperature surface 480 is a heated pumping ring with pumping ports (e.g., passageways or ducts). Pumping ring 480 is heated to a temperature high enough to destroy the active species of a pre-cursor gas used in ALD processes. Gases are pulled through openings 486 of pumping ports 484 located on top surface 488 of pumping ring 480. Top surface 488 is preferably even with or below surface 442 of [0060] heater 440. Pumping ring 480 may be similar to pumping rings available from Applied Materials, of Santa Clara, Calif. Barrier 490 preferably prevents gas from flowing past surface 442 to the output of reactor 400 without passing through openings 486 of pumping [0061] ring 480. [0062]FIG. 4A shows openings 486 on top surface 488 of ring 480 to pumping ports 484 (not shown in [0063]FIG. 4A). Some of the gas entering reactor 400 is pulled through pumping ports 484 by a pressure differential. This pressure differential may be created by a vacuum or other type of pump (not shown) connected to pumping ports 484. Pumping ring 480 may be connected to reactor wall 402 or supported by a support (not shown). [0064]FIG. 5 illustrates a reactor 500 with a high-temperature surface 580 according to the invention. Surface 580 is a perforated plate and preferably has a substantially circular opening in the middle of the plate with a diameter slightly larger than the diameter of heater column 544. Surface 580 is preferably placed inside reactor 500 such that surface 580 and heater column 544 are not in contact. Surface 580 is heated to a temperature high enough to destroy the active species of a pre-cursor gas used in ALD processes. [0065]FIG. 5A shows several openings 582 in [0066] surface 580. Openings 582 may be small or large depending on the number of openings 582. The size and number of openings 582 should be such that they do not substantially hinder gases from passing through reactor 500, yet provide enough surface area of surface 580 to ensure that active species are destroyed. The outer diameter of surface 580 may be the same as the inner diameter of reactor wall 502. Alternatively, the outer diameter of surface 580 may be less than the diameter of reactor wall 502 and may be supported by a support extending from wall 502 (not shown). [0067]FIG. 6 illustrates another high-temperature surface inside a reactor 600 in accordance with the invention. Surface 680 includes a preferably ordered mesh (better seen in FIG. 6A) of material or materials that can be heated to a temperature high enough to destroy the active species of pre-cursor gases used in ALD processes. Such materials may be, for example, ceramics or Inconel. [0068]FIG. 7 illustrates a high-temperature surface 780 similar to surface 680. Surface 780 is also a mesh of a material or materials that can be heated to a temperature high enough to destroy the active species of pre-cursor gases used in ALD processes. However, as shown in FIG. 7A, mesh 780 is a random arrangement of metal, other material, or combination thereof. [0069] The reactors of FIGS. 1-7 are shown with one gas input and one gas output for illustrative purposes only. Other numbers of gas inputs and gas outputs may be used. Reactor 800 of FIG. 8, for example, has two gas inputs 820 and two gas outputs 890. Gas may be selectively input into reactor 800 via gas inputs 820 by operating valves (not shown) that control the flow of gas through gas lines connected to gas inputs 820. Gas exits reactor 800 via gas outputs 890. Similarly, gas outputs 890 may be coupled to valves (not shown) that control the flow of gas through gas lines connected to gas outputs 890. Preferably, gas lines connected to the gas outputs are connected to pumps (not shown) to increase the throughput of gas through reactor 800. Inside reactor 800 is surface 880. Surface 880 is heated to a temperature high enough to destroy the active species of pre-cursor gases used in ALD processes. [0070] Furthermore, although the embodiments of FIGS. 1-7 are shown with one heating surface and one substrate, again for illustrative purposes only, other numbers of heating surfaces and substrates may be used in accordance with the invention. [0071] For example, FIG. 9 illustrates a cross-section of reactor 900. Reactor 900 has multiple heaters 940 that have multiple heating surfaces 942. Heaters 940 may be supported by heater supports 946, which are fixed to reactor wall 902. Alternatively, heaters 940 may be supported in other suitable ways such that substrates 930 placed on respective heating surfaces 942 may have thin films grown on them. In addition, a vacuum may be used to hold substrates 930 to respective heating surfaces 942 during the ALD. The surface of a substrate 930 on which a film is to be grown does not have to be level and can be oriented in any direction (however, the surface of substrate 930 on which a film is to be grown should not face down on heater surface 942). [0072] Inside reactor 900 is high temperature surface 980, which is a perforated plate with openings 982. Surface 980 is heated to a temperature high enough to destroy the active species of pre-cursor gases used in ALD processes. [0073]FIG. 10 illustrates a cross-section of reactor 1000. As shown, thin films may be grown on multiple substrates 1030, which are each on or near a heater (not shown). After gas passes substrates 1030, the gas passes over and through high-temperature surface 1080, which can be any one of surfaces 280, 380, 480, 580, 680, 780, 880, or 980. The gas exits reactor 1000 on the same side as it enters [0074] reactor 1000. [0075]FIG. 11 shows a cross-section of [0076] reactor 1100, which is arranged such that the flow of gas from gas input 1120 to gas output 1190 is horizontal. The direction of gas flow is not important provided that the number of atoms deposited on a substrate is substantially uniform across the substrate and that the amount of atoms deposited on each subsequent monolayer is also substantially uniform. [0077] Inside reactor 1100 are two substrates 1130 fixed to two respective heating surfaces 1140. Substrates 1130 may be held to heaters 1140 by, for example, vacuum. The surface of each substrate 1130 on which a film is to be grown preferably faces the center of reactor 1100. This ensures that substantially uniform monolayers of atoms are deposited on the substrate. A high-temperature surface 1180 is downstream (with respect to the flow of gas) from substrates 1130 and heaters 1140. Surface 1180 is heated to a temperature high enough to destroy the active species of pre-cursor gases used in ALD processes. [0078]FIG. 12 illustrates a cross-section of reactor 1200 in which the flow of gas over [0079] substrate 1230 is again horizontal. High-temperature surfaces 1280 are downstream (with respect to the flow of gas) from substrate 1230. Surfaces 1280 are heated to a temperature high enough to destroy the active species of pre-cursor gases used in ALD processes. [0080] The reactors of the invention can be of any type suitable for ALD including depression reactors and barrel reactors. [0081] High-temperature surfaces such as [0082] surfaces 280, 380, 480, 580, 680, 780, 980, 1080, 1180, and 1280 may be heated by, for example, an electrical power source external to the reactor in which the surface is located. High-temperature surfaces may also be heated by, for example, heat convection. [0083]FIG. 13 shows an ALD process in accordance with the invention. At 1302, a pre-cursor gas enters a reactor. At 1304, the active species of the pre-cursor gas react with a substrate resulting in a monolayer of atoms on the substrate. The active species are substantially de-activated at 1306 when they come in the vicinity of, or into contact with, one or more high-temperature surfaces, such as surface 280, 380, 480, 580, 680, 780, 980, 1080, 1180, or 1280, inside the reactor. The remaining gases are purged from the reactor at 1308. If the desired thin film thickness has not yet been grown, then at 1310, the process returns to 1302. [0084] The above embodiments destroy active species of pre-cursor gases insitu by subjecting them to a high-temperature surface in the same reactor in which the ALD process occurs. In those ALD processes in which active species of pre-cursor gases can be destroyed by subjecting them to a cold-temperature surface, a cold-temperature surface may be alternatively placed inside the reactor. The cold-temperature surface may be the same shape as any of high-temperature surfaces 280, 380, 480, 580, 680, 780, 980, 1080, 1180, or 1280. The cold-temperature surface can be at any temperature below the reaction temperature of the ALD process that induces rapid decay of active species. For example, the cold-temperature surface can be about 100� C., room temperature, freezing, or below freezing, depending on the active species to be destroyed. [0085] Note that although semiconductor substrates have been described herein with respect to ALD, the invention is not limited to them. Other workpieces appropriate for ALD are also within the scope of the invention. [0086] In addition, although the ALD processes described herein have been described using only two pre-cursor gases, the invention is not limited to two pre-cursor gases. For example, three or four pre-cursor gases may be used. [0087] Thus it is seen that systems and methods of insitu post atomic layer deposition destruction of active species are provided. One skilled in the art will appreciate that the invention can be practiced by other than the described embodiments, which are presented for purposes of illustration and not of limitation, and the invention is limited only by the claims which follow. Referenced byCiting PatentFiling datePublication dateApplicantTitleUS7303996 *Oct 1, 2003Dec 4, 2007Taiwan Semiconductor Manufacturing Co., Ltd.High-K gate dielectric stack plasma treatment to adjust threshold voltage characteristicsUS7329615 *Aug 9, 2005Feb 12, 2008Micron Technology, Inc.Atomic layer deposition method of forming an oxide comprising layer on a substrateUS7407892May 11, 2005Aug 5, 2008Micron Technology, Inc.Deposition methodsUS8257497 *Dec 10, 2004Sep 4, 2012Micron Technology, Inc.Insitu post atomic layer deposition destruction of active speciesUS20050150460 *Dec 10, 2004Jul 14, 2005Micron Technology, Inc.Insitu post atomic layer deposition destruction of active speciesWO2006130298A2 *May 2, 2006Dec 7, 2006Micron Technology IncDeposition methods, and deposition apparatuses* Cited by examinerClassifications U.S. Classification438/680, 257/E21.17, 257/E21.171, 438/681, 257/E21.28, 438/785International ClassificationC23C16/44, H01L21/285, H01L21/316, C23C16/46, C23C16/455Cooperative ClassificationY10S438/905, Y10S438/913, Y10S438/935, Y10S438/903, C23C16/45544, H01L21/31616, H01L21/28556, C23C16/46, H01L21/28562, C23C16/4407European ClassificationC23C16/46, H01L21/285B4H2, H01L21/285B4H, C23C16/44A8, C23C16/455F2DLegal EventsDateCodeEventDescriptionJun 20, 2012FPAYFee paymentYear of fee payment: 8Jul 3, 2008FPAYFee paymentYear of fee payment: 4Jan 30, 2003ASAssignmentOwner name: MICRON TECHNOLOGY, INC., IDAHOFree format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:SARIGIANNIS, DEMETRIUS;MENG, SHUANG;DERDERIAN, GARO J.;REEL/FRAME:013726/0956Effective date: 20030121Owner name: MICRON TECHNOLOGY, INC. 8000 SOUTH FEDERAL WAYBOISFree format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:SARIGIANNIS, DEMETRIUS /AR;REEL/FRAME:013726/0956RotateOriginal ImageGoogle Home - Sitemap - USPTO Bulk Downloads - Privacy Policy - Terms of Service - About Google Patents - Send FeedbackData provided by IFI CLAIMS Patent Services©2012 Google

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text:
Dennis J Griffin DDS - Schaumburg, IL | Groupon
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Four Seasons of Top-Bar Beekeeping by Stephen Garriga | NOOK Book (eBook) | Barnes & Noble® Books by Author Books by Series Collectible Editions Coming Soon by Date Coming Soon by Subject New Releases NY Times Bestsellers Signed Books Top Books of the Month
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When Liu Yu, an impressionable Chinese girl, witnesses the venomous public trial of her mother’s ...
When Liu Yu, an impressionable Chinese girl, witnesses the venomous public trial of her mother’s co-worker and friend during the Cultural Revolution, her life is changed forever. The incident silences her voice but not her desire to escape from poverty ...
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From hive to home!From the satisfying taste of fresh honey butter to the blissful aroma ...
From hive to home!From the satisfying taste of fresh honey butter to the blissful aroma of a beeswax candle, Honey Crafting celebrates everything the hive has to offer. Inside, you'll find a variety of sweet crafts for around the home, ...

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> A-1 Construction Company
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Principal: Ms. Wanda Franklin, Owner
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This company offers gutters/carports/patios/siding/roof.
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Now, city’s heritage furniture to go under hammer in Paris | chandigarh | Hindustan Times
Now, city’s heritage furniture to go under hammer in Paris
HT Correspondent, Hindustan Times, Chandigarh | Updated: May 19, 2014 12:19 IST
With not many steps being taken by the Chandigarh administration to preserve its heritage furniture, different houses across the world are earning good amount of money by auctioning articles designed by Le Corbusier’s cousin Pierre Jeanneret.
After auctions by Chicago-based Wright Auction house, Paris-based Artcurial auction house has scheduled an auction for Monday. The house is set to earn thousands of Euros by selling 14 heritage items at the auction, as per their website.
Wright Auction house had started auctioning Chandigarh’s furniture from 2008 onwards. Till last year, it had held 234 auctions where it had sold 204 items earning over Rs 10 crore.
While these foreign auction houses knowing the worth of such fur niture have ear ned a colossal wealth, the UT had dumped the furniture and later auctioned it as part of junk. Now, the same administration is busy for ming policies to save whatever little heritage furniture has been left in the city.
Talking to HT, city- based architect Surender Bagha said, “We have reached this stage where heritage furniture from our city is being auctioned all across the world, all because of steps not being taken by the administration in time.”

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READING, Pa., July 21, 2015 /PRNewswire/ -- EnerSys (NYSE: ENS), the global leader in stored energy solutions for industrial applications, will host a conference call to discuss the Company's first quarter fiscal 2016 financial results and to provide an overview of the business. The call will conclude with a question and answer session.
The call, scheduled for Thursday, August 6 beginning at 9:00 am Eastern Time, will be hosted by John D. Craig, Chairman & Chief Executive Officer, David M. Shaffer, President & Chief Operating Officer and Michael J. Schmidtlein, Senior Vice President – Finance & Chief Financial Officer.
78555290
A replay of the conference call will be available from 12:30 p.m. on August 6, 2015 through midnight on September 5, 2015.


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ClassificationG01D21/00, G06F11/34, G06F11/30, G06F13/36Cooperative ClassificationG06F11/3485, G06F11/3058, G06F11/3041European ClassificationG06F11/30Legal EventsDateCodeEventDescriptionApr 6, 1992ASAssignmentOwner name: TANDEM COMPUTERS INCORPORATED, CALIFORNIAFree format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNORS:LUI, ALBERT;FULLER, WILLIAM T.;REEL/FRAME:006078/0629Effective date: 19920331Feb 2, 1998FPAYFee paymentYear of fee payment: 4Jan 17, 2002FPAYFee paymentYear of fee payment: 8Mar 16, 2004ASAssignmentOwner name: COMPAQ COMPUTER CORPORATION, A DELAWARE CORPORATIOFree format text: MERGER;ASSIGNOR:TANDEM COMPUTERS INCORPORATED;REEL/FRAME:014506/0598Effective date: 19981231Owner name: COMPAQ INFORMATION TECHNOLOGIES GROUP, L.P., A TEXFree format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:COMPAQ COMPUTER CORPORATION;REEL/FRAME:014506/0133Effective date: 20010531Owner name: HEWLETT-PACKARD DEVELOPMENT COMPANY, L.P., TEXASFree format text: CHANGE OF NAME;ASSIGNOR:COMPAQ INFORMATION TECHNOLOGIES GROUP, L.P.;REEL/FRAME:014428/0584Effective date: 20021001Feb 22, 2006REMIMaintenance fee reminder mailedAug 9, 2006LAPSLapse for failure to pay maintenance feesOct 3, 2006FPExpired due to failure to pay maintenance feeEffective date: 20060809RotateOriginal ImageGoogle Home - Sitemap - USPTO Bulk Downloads - Privacy Policy - Terms of Service - About Google Patents - Send FeedbackData provided by IFI CLAIMS Patent Services


text:
Model Trains - the Collectors Guide by Chris Ellis - Alibris
ISBN-13: 9780785802211
ISBN: 0785802215
Alibris ID: 15585970661
Fine. 0785802215.
Alibris ID: 15846344147
Alibris ID: 15817660658
Alibris ID: 15799957007
1994, Magna Book Publisher
Publisher: Magna Book Publisher
Alibris ID: 11996485856
Fine. No Jacket as Expected. 4to-over 9¾"-12" Tall. A fine copy with no wear or markings. Still looks about new in spite of its age.
Alibris ID: 11427524400
Fine in Fine dust jacket. 0785802215. Quarto; Photographs-mostly color; 0.7 x 12.2 x 9.2 Inches; 80 pages.
Alibris ID: 13965318408
Alibris ID: 15827264929
Alibris ID: 14521603530
Alibris ID: 14521604155
1995, Book Sales Inc, Edison

value: This website is is an online store that sells new books, used books, out-of-print books, rare books, and other media through an online network of independent booksellers.


text:
Hotell Newspaper Rock State Historical Monument, USA – från SEK 507 | Booking.com
Hotell och boenden nära Newspaper Rock State Historical Monument i Monticello (USA)
Letar du efter boende i närheten av Newspaper Rock State Historical Monument?
Hotell nära Newspaper Rock State Historical Monument
Inn at the Canyons 2-stjärnigt hotell
Monticello (19,5 km från Newspaper Rock State Historical Monument)
Beskrivning This Monticello hotel, just 48 miles from Canyonlands National Park, offers an expansive indoor pool and hot tub. A daily continental breakfast and free Wi-Fi are provided for guests.
"Bra frukost, trevligt med pool. Nära till den enda bra restaurangen i området."
AndreB91. Sverige
Monticello (20,5 km från Newspaper Rock State Historical Monument)
Beskrivning Offering daily breakfast options, The Grist Mill Inn is 50 miles from Canyonlands National Park. Each room includes a flat-screen TV with satellite channels. Free parking is provided for all guests.
Blue Mountain Horsehead Inn 2 stjärnor
Monticello (19,9 km från Newspaper Rock State Historical Monument)
Beskrivning Located 48 miles from Canyonlands National Park, this motel is 4 minutes’ drive from Monticello Golf Course. Each room has a TV with free movie channels. Free parking is provided on site.
"Super friendly staff! Had ice on site which was great. Liked that we could park right in front of the room."
Rodeway Inn & Suites Monticello 2-stjärnigt hotell
Monticello (19,4 km från Newspaper Rock State Historical Monument)
Beskrivning On highway 191, this Monticello hotel is 48 miles from Canyonlands National Park. The hotel offers an indoor pool, free Wi-Fi and a daily continental breakfast.
Canyonlands Motor Inn 2 stjärnor
7,4 Bra 419 recensioner
Beskrivning This Monticello motel is within 48 miles of Canyonlands National Park. The motel offers guest rooms with free Wi-Fi, cable TV, microwave and refrigerator.
"very comfortable king size bed, room was nice and clean"
Wayside Motor Inn 2-stjärnigt hotell
Monticello (20,1 km från Newspaper Rock State Historical Monument)
Beskrivning Free Wi-Fi and a daily expanded continental breakfast are provided at this Monticello hotel, just 48 miles from Canyonlands National Park. An outdoor pool and spa are available for guest use.
Visa fler boenden nära Newspaper Rock State Historical Monument
Andra sevärdheter nära Newspaper Rock State Historical Monument
597207|6,550517,591517,578107,595967,588597|1,597207|9,588337,568227,587067|1,576247,587067|2,275824,581897,597207|3,556487,597207,588597,580227,598117,581907,533337,587067,597207|8

value: This website is a Dutch online travel agency for lodging reservations & other travel products, and a subsidiary of Booking Holdings. It is headquartered in Amsterdam.The website has over 28 million listings.


text: Concierge services Free newspapers in lobby Babysitting or childcare (surcharge) Children's club (free) Supervised childcare/activities (surcharge) Bar/lounge Total number of rooms - 198 24-hour front desk Safe-deposit box at front desk Hair salon Laundry facilities Dry cleaning/laundry service Elevator/lift Number of floors - 4 Year Built 1899 Wedding services Free breakfast Fireplace in lobby Fitness facilities Full-service spa Designated smoking areas Pool umbrellas Number of outdoor pools - 2 Tours/ticket assistance Free WiFi Free wired Internet Garden Gift shops or newsstand Business center Luggage storage Spa treatment room(s) Meeting rooms 7 Multilingual staff Free valet parking Terrace Picnic area Poolside bar Porter/bellhop Area shuttle (surcharge) Number of restaurants - 4 Number of meeting rooms - 7 Outdoor tennis courts - 2 Free self parking Pool sun loungers Sauna Shopping on site Airport transportation (surcharge) Spa services on site Steam room Show all hotel amenities

value: This website is an online travel agency owned by Expedia Group, an American online travel shopping company based in Seattle.


text:
Junk Dealers in Jamestown, Pennsylvania with Reviews & Ratings - YP.comFind People•Advertise With UsBrowseFind PeopleFeatured CollectionsRestaurantsAutomotiveHome ImprovementHealth & WellnessAttorneysPeople Searched For...RestaurantsHotelsGarbage CollectionInsuranceFloristsBoat Rental CharterTaxidermistBarsPet Boarding KennelsHorseback RidingBars With Live MusicHeavy Equipment RentalPizzaFoundation ContractorsStorage UnitMeat PackersBar And GrillUsed Major AppliancesCity, Village & Township GovernmentChiropracticWeb Site Design And ServicesCabinsAmusement Places ArcadesAre you alocal business owner?Advertise with YPor call 888-367-2194What do you want to find?Search by business name, or keywordnearWhere? 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Junior's Core and Reycling(1)7015 State Route 7Kinsman, OH 44428(330) 876-2673Recycling CentersScrap MetalsMetalsFrom Business: We pay top dollar for all your scrap Aluminum, Cans, Copper, Brass, Catalatic Converters, Radiators, Starters, Alternators, Transmissions, Batteries, Electric Motor…Add to mybookRemove from mybookAdded to your car collection!Error when adding to car collectionThis business was removed from the car collection11. Deforest Used Parts(1)1534 Deforest Rd SEWarren, OH 44484(330) 652-0378Junk DealersUsed & Rebuilt Auto PartsWebsiteDirectionsMore InfoPurchased a door handle for a Pontiac Vibe. Employees where very helpful and quick to get me the part I needed and at a very reasonable price! Will …Add to mybookRemove from mybookAdded to your car collection!Error when adding to car collectionThis business was removed from the car collection12. 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of 29resultsAdd a New CollectionOops! There was a problem saving the new custom collection.Please try again.Collection Name cannot be emptyUpload a Photo(optional)Remaining Characters: 100Remaining Characters: 500CancelSaveMap ViewFeatured Junk Dealersin Jamestown, PennsylvaniaDonate Car - Breast Cancer GIV Foundation(4)Serving the Jamestown area.(888) 556-5324Help A Friend, Donate Your Car Today!More InfoFeatured Junk Dealersin Jamestown, PennsylvaniaPay Max Cash For CarsServing the Jamestown area.(888) 493-1899Get An INSTANT OFFER on ANY Car or Truck! CALL NOWWebsiteMore InfoCar Buyer(1)Serving the Jamestown area.(800) 454-7498Sell Your Car Today with NO Hassle!WebsiteMore InfoCash For CarsServing the Jamestown area.(888) 695-5344We'll Buy Cars or Trucks, Running or Not!WebsiteContact UsMore Info1800CashforJunkCarsServing the Jamestown area.(800) 385-9619WebsiteMore Info1-800 Donate CarsServing the Jamestown area.(866) 259-8166Feel Great Helping OthersMore InfoCash For Junk Cars Today Free RemovalServing the Jamestown area.(800) 757-5211More InfoDidn't find what you were looking for?magnifying glassPlease help others by helping us do better.Suggest a BusinessAboutAbout UsSite FeedbackContact UsAdvertise with UsCareers - We're HiringCorporate BlogEngineering BlogLegal

value: This website is a United States-based web site operated by YP Holdings that provides listings for local businesses. In 2013 it was re-branded as YP.com or simply "YP".