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    专

    一种大马士革玫瑰特征花香香精

    1772000003876A
    发明人
    席辉, 付英杰, 孙世豪, 史清照, 李鹏, 王丁众, 张文娟, 范武, 刘珊, 曾世通, 姬凌波, 宗永立
    受让人
    ZHENGZHOU TOBACCO RES INST CHINA TOBACCO (CNTA-C)
    申请人
    新智认知数据服务有限公司
    申请号
    15761327
    申请日
    2001-08-22
    公开(公告)号
    1772000003876A
    公开(公告)日
    2020-10-06
    IPC分类号
    G06N020/00G06N020/20G06T007/11G06T007/90
    CPC分类号
    -
    优先权号
    019013
    优先权日
    1990-08-30
    摘要

    NOVELTY - The cover (1) has a planar main structure (5) with flat upper walking surface. A warning light such as LED is provided on the walking surface, in the form of a lighting stud (6) to emit the flashing light whose flashing rate equals or exceeds two per second. The warning light is powered by a solar cell.

    USE - Temporary ground cover such as trench cover, temporary ramp, and simple cover for covering uneven ground, open hole, and trench in footpath and other areas with pedestrian traffic, and path for entry/exit of people into/from building during emergency situations such as fire accident.

    ADVANTAGE - The adequate warning of hazard to pedestrians and wheelchair operator can be provided since the warning light to emit the flashing light is provided on the walking surface. The cover can be adequately secured to preset position in ground so that accident occurrence can be suppressed.

    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the temporary ground cover.

    Temporary ground cover (1)

    Peripheral edge (3)

    Fixing hole (4)

    Planar main structure (5)

    Lighting stud (6)

    权利要求
    1、一种拜访位置寄存器VLR获取用户数据的方法,其特征在于,判断VLR与归属位置寄存器HLR之间的D接口流量是否超负荷,如果超负荷,则在注册时对注册消息进行优先级排序,然后VLR根据所述优先级排序的结果先向HLR发送优先级高的注册消息。
    2、根据权利要求1所述的方法,其特征在于,所述方法是在VLR复位之后执行的。
    3、根据权利要求1所述的方法,其特征在于,所述对注册消息进行优先级排序是VLR对注册消息进行优先级排序。
    4、根据权利要求1所述的方法,其特征在于,如果判断出VLR与HLR之间的D接口流量不超负荷,则不在注册过程中对注册消息进行优先级排序。
    5、根据权利要求1所述的方法,其特征在于,所述对注册消息进行优先级排序为:根据用户注册消息中的注册参数,对注册消息进行优先级排序。
    6、根据权利要求5所述的方法,其特征在于,所述注册参数包括注册类型;所述根据注册参数对注册消息进行优先级排序为:根据注册类型,将进行业务时,注册类型为隐含注册的注册消息设为优先级最高。
    7、根据权利要求5所述的方法,其特征在于,所述注册参数包括前位置区参数;所述根据注册参数对注册消息进行优先级排序为:根据前位置区参数确定新上网用户,将新上网用户的注册消息设为优先级最高。
    8、根据权利要求7所述的方法,其特征在于,所述根据前位置区参数确定新上网用户为:将前位置区参数所标识的位置区不属于所述VLR覆盖的位置区范围内的用户,确定为新上网用户。
    9、根据权利要求2所述的方法,其特征在于,该方法进一步包括:在VLR复位之后,VLR接收到对拜访该VLR用户的呼叫,VLR向所述拜访该VLR用户下发寻呼。
    10、根据权利要求9所述的方法,其特征在于,该方法进一步包括:在VLR复位之前对用户数据进行备份。
    11、根据权利要求10所述的方法,其特征在于,所备份的用户数据包括用户位置信息;所述VLR向所述拜访该VLR用户下发寻呼为:VLR读取备份的所述拜访该VLR用户的位置信息,根据所读取的位置信息向所述拜访该VLR用户下发寻呼。
    12、根据权利要求10所述的方法,其特征在于,该方法进一步包括:VLR收到所述拜访该VLR用户的寻呼响应之后,根据备份的用户数据恢复该用户的数据。
    13、根据权利要求12所述的方法,其特征在于,所述对用户数据进行备份为:将用户数据备份在交换设备中;则所述根据备份的用户数据恢复用户数据为根据备份在交换设备中的用户数据恢复用户数据;或者,所述对用户数据进行备份为将用户数据备份在硬盘上;所述根据备份的用户数据恢复用户数据为根据备份在硬盘上的用户数据恢复用户数据。
    14、根据权利要求2或12所述的方法,其特征在于,该方法进一步包括:在VLR复位之后,VLR主动恢复用户的数据。
    15、根据权利要求11所述的方法,其特征在于,所述VLR接收到对拜访VLR用户的寻呼之后,并在向所述拜访该VLR用户下发寻呼之前,进一步包括:VLR根据备份的用户数据恢复全部用户数据;所述VLR向所述拜访该VLR用户下发寻呼为:所述VLR根据所恢复的用户数据中的位置信息向所述拜访该VLR用户下发寻呼。
    16、根据权利要求11所述的方法,其特征在于,该方法进一步包括:在VLR复位之后,VLR先根据备份的数据恢复用户的位置信息;所述VLR向所述拜访该VLR用户下发寻呼包括:VLR根据恢复的位置信息向所述拜访该VLR用户下发寻呼;在收到该被叫用户的寻呼响应之后,进一步包括:VLR根据备份的数据恢复该用户的其他数据。
    17、一种VLR,其特征在于,该VLR包括:业务处理模块和排序模块;业务处理模块,用于接收拜访VLR的用户发来的注册请求,将注册请求发送给排序模块,并根据排序模块的排序结果,先向HLR发送优先级高的注册消息;排序模块,用于对接收到的注册消息进行优先级排序,将优先级排序结果通知业务处理模块。
    18、根据权利要求17所述的VLR,其特征在于,所述业务处理模块,进一步用于判断与HLR之间的D接口流量是否超负荷,在确定超负荷后,执行所述的将注册请求发送给排序模块,在确定未超负荷后,直接将注册请求发送给HLR。
    19、根据权利要求17所述的VLR,其特征在于,该VLR进一步包括备份模块和VLR数据库;备份模块,用于将用户数据备份在外部存储设备上,或者读取备份在外部存储设备上的用户数据,将所读取的用户数据发送给业务处理模块;业务处理模块,根据接收到的用户数据恢复拜访VLR的被叫用户的用户数据,将所恢复的用户数据保存在VLR数据库中。
    说明书
    [0001]This application claims the benefit of U.S. Provisional Application Ser. No. 60/349,262, filed on Jan. 18, 2002, which is expressly incorporated by reference. In addition, this application is a continuation-in-part of U.S. application Ser. No. 10/019,857, filed Nov. 9, 2001, now U.S. Pat. No. 6,616,832, which claims the benefit of PCT International Application No. PCT/US00/12615, filed May 9, 2000, and which is a continuation-in-part of U.S. application Ser. No. 09/309,047, filed May 10, 1999, now U.S. Pat. No. 6,132,599, all of which are expressly incorporated by reference herein.
    [0002]BACKGROUND AND SUMMARY OF THE INVENTION The present invention relates to wastewater treatment systems and improvements thereto. More particularly, this invention relates to an apparatus for treatment of primary effluent from residential and commercial establishments to allow subsurface or surface disposable of wastewater therefrom. Many areas in this country are experiencing an increase in population accompanied by a larger demand for housing and commercial establishments in rural areas and around major municipalities with no access to a public sewer system. Conventional onsite wastewater systems provide a viable option for managing the wastewater generated by development, however, not all soils are suitable for these systems. Conventional onsite wastewater systems also require a large land area, putting a premium cost on real estate in many locations. In order to maintain a non-hazardous environment, residential and commercial establishments must treat wastewater that they produce. Since public utility wastewater treatment systems and conventional onsite systems are not always available or are not desirable, alternative wastewater treatment methods are often necessary. Due to the premium price on real estate and the high density of residential and commercial building, it is desirable to reduce and minimize the space required for wastewater treatment systems to treat the wastewater to acceptable standards. According to an illustrated embodiment of the present invention, a wastewater treatment apparatus comprising a recirculation chamber, a dosing chamber having no direct fluid connection to the recirculation chamber, and a filter layer containing a filter media and being located above the recirculation and dosing chambers. The recirculation chamber, the dosing chamber, and the filter layer are located in a single tank. The apparatus also comprises an influent pipe that directs wastewater entering the wastewater treatment apparatus into the recirculation chamber, and a recirculation pump located in the recirculation chamber. The recirculation pump pumps the wastewater from the recirculation chamber onto the filter layer. The apparatus further comprises a septic tank return pipe connected to the dosing chamber, a portion of the wastewater being discharged from the wastewater treatment apparatus through the septic tank return pipe back to a septic tank for additional treatment, and an effluent discharge pipe connected to the dosing chamber. Wastewater is discharged from the wastewater treatment apparatus through the effluent discharge pipe for final disposal. In the illustrated embodiment, the apparatus further comprising a porous underdrain for the filter layer. Wastewater flowing through the filter media of the filter layer is directed through the underdrain and into the recirculation chamber or the dosing chamber. Illustratively, a chamber wall divides the recirculation chamber and the dosing chamber so that wastewater passing through the underdrain proportionally enters the recirculation chamber and dosing chamber as determined by the placement of the chamber wall. Also in the illustrated embodiment, the apparatus further comprising a filter distribution pipe and a spray nozzle for the filter layer. The recirculation pump pumps the wastewater onto the filter media of the filter layer through the filter distribution pipe and the spray nozzle. The illustrated embodiment further includes a treated effluent discharge control system having first and second electric valves on the effluent discharge pipe and the septic tank return pipe, respectively. The first and second electric valves are controlled by the control system selectively to discharge treated effluent to the effluent discharge pipe and the septic tank return pipe. Additional features of the invention will become apparent to those skilled in the art upon consideration of the following detailed description of the best mode of carrying out the invention as presently perceived.
    [0003]BRIEF DESCRIPTION OF THE DRAWINGS The detailed description particularly refers to the accompanying figures in which: FIG. 1 is a sectional view taken through a waste treatment apparatus of the present invention illustrating that the filter section located above a recirculation chamber and illustrating a recirculation pump located within a recirculation pump basin; FIG. 2 is a sectional view taken through the apparatus of FIG. 1 illustrating a recirculation basin and a dosing basin below the filter section; FIG. 3 is a top view of the apparatus with a cover removed illustrating the filter section, a recirculation pump basin, and a dosing pump basin; FIG. 4 is a sectional view illustrating further details of a recirculation pump located within the recirculation pump basin and a dosing pump located within the dosing pump basin; and FIG. 5 is an inlet in view of the waste treatment apparatus of the present invention.
    [0004]DETAILED DESCRIPTION OF THE DRAWINGS Referring now to the drawings, FIG. 1 illustrates an embodiment of a wastewater treatment apparatus 10 which includes a tank 12 . The tank 12 is illustratively made of a suitable material, such as concrete, polyethylene or steel. A tank-lifting notch 14 is provided on the tank 12 . The tank 12 is divided into a pump section 18 and a filter section 20 by a pump wall 22 that is substantially the height of the tank 12 . The pump section 18 contains at least one pump which circulates the wastewater through the treatment apparatus 10 . In the embodiment shown in FIG. 1 , filter section 20 includes a single filter layer 26 . In other embodiments, multiple filter layers may be used. FIG. 2 illustrates a bottom layer 24 of the wastewater treatment apparatus 10 which is divided into a recirculation chamber 28 and a dosing chamber 30 by a chamber wall 32 and a pump chamber wall 34 . The chamber wall 32 extends to the bottom of filter layer 26 and the pump chamber wall 34 is substantially the height of the tank 12 . The recirculation chamber 28 and the dosing chamber 30 are not in direct fluid communication. The recirculation chamber 28 is divided into a recirculation basin 36 and a recirculation pump basin 38 by the pump wall 22 . Settled and screened wastewater from a septic tank or other primary treatment device enters the apparatus through influent pipe 48 shown in FIG. 5 . The influent mixes with treated water falling from filter underdrain 50 and is stored in the recirculation chamber 28 . The mixture of influent wastewater and treated effluent flows through the recirculation conduit 44 in the pump wall 22 into the recirculation pump chamber 38 shown in FIG. 3 . The recirculation pump 68 pumps the wastewater through a filter distribution pipe 58 to a spray nozzle 62 , which sprays and distributes the wastewater over the filter layer 26 . Filter distribution pipe 58 includes a plurality of pipe unions 56 which join adjacent pipe segments. A support pipe 64 supports the spray nozzle 62 . A slotted plastic pipe or other similar screen 54 surrounds pump 68 preventing the pump from ingesting debris and plugging spray nozzle 62 . For larger systems, a larger tank 12 is used with increased filter section 20 , single or multiple recirculation pumps 68 , single or multiple pump screens 54 , multiple spray nozzles 62 , and single or multiple dosing pumps 72 based on the flow capacity of the system. A recirculation basin level control 70 , located in the recirculation pump chamber 38 measures the water level in the recirculation chamber 28 . A preferred recirculation basin level control is a pressure transducer. A typical pressure transducer is a submersible, stainless steel 4–20 mA output model available from Measurement Specialties, Inc. located in Hampton, Va. When the water level in the recirculation chamber 28 reaches a programmed minimum level above the floor of recirculation chamber 28 as measured by recirculation basin level control 70 , control panel 16 activates recirculation pump 68 to begin pumping to filter section 20 on a programmable time interval. The timed doses will repeat on a programmed schedule as long as the water level in the recirculation chamber 28 remains above the programmed minimum level above the floor of recirculation chamber 28 . If the water level in the recirculation chamber 28 rises above a programmed maximum level above the floor of the recirculation chamber 28 as measured by recirculation basin level control 70 , control panel 16 activates recirculation pump 68 to pump until a programmed drop in water level in recirculation chamber 28 is achieved. If the water level in recirculation chamber 28 does not drop after a programmed time or the level continues to rise, control panel 16 will signal a high recirculation chamber alarm by activating an alarm light, audio alarm and a telephone dialer within control panel 16 to call and alert a service representative. The sprayed wastewater is aerated in the air space 66 and flows through the filter layer 26 by gravity. As the wastewater flows through the filter media 52 , it is treated by a combination of physical, chemical and aerobic biological processes. A preferred media is textile chips. Illustratively, the filter media 52 is a non-woven textile fabric composed of polyethylene filaments such as Type 4-17PE textile chips available from Texel, Inc. located in Quebec, Canada. The treated effluent flows through a filter underdrain 50 which illustratively comprises a fiberglass grating, perforated precast concrete or materials of a similar design and falls back into the recirculation basin 36 or the dosing basin 40 . The location of chamber wall 32 determines the percentage of effluent entering the recirculation basin 36 or the dosing basin 40 and determines the recirculation ratio for the treatment process. The treated filter effluent in the recirculation basin 36 is mixed with the influent wastewater from pipe 48 . A dosing basin level control 74 located in the dosing pump basin 42 measures the water level in the dosing chamber 30 . A preferred dosing basin level control is a pressure transducer. A typical pressure transducer is a submersible, stainless steel 4–20 mA output model available from Measurement Specialties, Inc. located in Hampton, Va. When the water level in the dosing chamber 30 reaches a programmed minimum level above the floor of the dosing chamber 30 , the dosing basin level control 74 signals the control panel 16 to begin pumping to the effluent discharge pipe 76 on a programmable timed basis until a programmed level of water has been removed from the dosing chamber 30 . The doses will repeat on a programmed schedule as long as the water level in the dosing chamber 30 remains above the programmed minimum level above the floor of the dosing chamber 30 . If the water level in the dosing chamber 30 rises above a programmed maximum level above the floor of the dosing chamber 30 , the dosing basin level control 74 signals the control panel 16 to start dosing pump 72 and pump until a programmed drop in level is achieved. If the level in the dosing basin does not drop after a programmed time or the level continues to rise, the control panel 16 will signal a high dosing chamber alarm by activating an alarm light, audio alarm and a telephone dialer within control panel 16 to call and alert a service representative. The treated filter effluent falling into the dosing basin 40 flows through the dosing conduit 46 in the pump wall 22 into the dosing pump basin 42 . The dosing pump 72 pumps the treated effluent through the effluent discharge pipe 76 into a treated effluent filter 78 , a typical filter being a Spin-Clean filter available from Agricultural Products, Inc. located in Ontario, Calif. The treated effluent filter 78 is equipped with an orifice plate or modulating valve to allow a portion of the treated effluent entering the filter to flush any screenings through the filter flush outlet pipe 79 back to the recirculation pump chamber 38 . The treated effluent passing through the treated effluent filter 78 is directed to either the disposal discharge pipe 86 or the septic tank return pipe 82 . Treated effluent is returned to the septic tank for denitrification to reduce the nitrates in the aerobically treated effluent. Denitrification occurs in the septic tank due to the lack of oxygen in the tank and the availability of organic carbon in the raw wastewater entering the tank. An electrically actuated disposal discharge pipe valve 80 and an electrically actuated septic tank return pipe valve 81 are installed on the disposal discharge pipe 86 and the septic tank return pipe 82 to direct flow based on control inputs from control panel 16 , to either outlet based on the level of treated effluent in the dosing chamber 30 as measured by the dosing basin level control 74 . If water level in the dosing chamber 30 is low, the septic tank return pipe valve 81 on the septic tank return pipe 82 is opened while the disposal discharge pipe valve 80 on the disposal discharge pipe 86 remains closed so that all pumped effluent is returned to the septic tank during the pump dosing cycle. During normal water levels in the dosing chamber 30 , the disposal discharge pipe valve 80 and the septic tank return pipe valve 81 are alternatively opened and closed on each pump cycle to evenly distribute the treated effluent to the disposal discharge pipe 86 and the septic return pipe 82 . During periods of high water level in the dosing chamber 30 , the disposal discharge pipe valve 80 on the disposal discharge pipe 86 is opened while the septic tank return pipe valve 81 on the septic tank return pipe 82 remains closed for the pump cycle so that all effluent is discharged from the treatment system. Alternatively, a single electrically actuated three-way valve could be used in place of disposal discharge pipe valve 80 and septic tank return pipe valve 81 . Treated effluent being discharged from the system through disposal discharge pipe 86 passes through a treated effluent flow sensor 60 prior to discharge from the system. A typical treated effluent flow sensor 60 being a RFO/RFA-2500 Series RotorFlow Sensor available from Gems Sensors located in Plainville, Conn. The treated effluent flow sensor 60 sends a signal proportional to the fluid velocity to control panel 16 which converts the signal to a flow rate and totalizes the flow volume over a programmable time period. An optional tablet chlorinator 84 consisting of a polyvinyl chloride pipe with slots located in the bottom of the pipe below the low water elevation may be located in the dosing pump basin 42 . The tablet chlorinator 84 is filled with chlorine disinfectant tablets and capped at the top. The water flowing through the dosing conduit 46 when dosing pump 72 is operating moves through the slotted pipe containing the chlorine tablets and slowly dissolves the tablets while imparting a chlorine residual in the treated effluent. The chlorine residual acts to disinfect the treated effluent by killing the pathogenic organisms in the effluent. The hardness and percentage of chlorine in the tablets can be regulated to produce the proper chlorine residual in the treated effluent to provide the necessary disinfection level. Alternately, other forms of treated effluent disinfection can be used such as ultraviolet light disinfection or ozonation. Pump section riser 94 located over the pump section 18 provides access to the pumps and mechanical equipment for maintenance. The pump section riser 94 is covered with pump section hatch 98 and is removed using pump section hatch handles 104 . The pump section hatch 98 includes pump section vent 99 which allows air to enter pump section 18 to replace the water removed during the pumping cycles. The filter section riser 96 is located over the filter section 20 and provides access to the spray nozzle support pipe 64 , spray nozzle 62 , air space 66 , and filter media 52 for maintenance. The filter section riser 96 is covered with filter section hatch 100 and is removed using filter section hatch handles 106 . Filter section hatch 98 includes filter section vent 102 which allows air to enter and mix with the sprayed wastewater in air space 66 . As the wastewater falls by gravity through filter layer 26 , air is pulled in through filter section vent 102 to displace the water, thereby passively aerating the filter media 52 . A filter level switch 108 is installed within the air space 66 to provide a signal to control panel 16 if the filter media 52 should become plugged and water begins ponding on top of the filter layer 26 . Although the invention has been described in detail with reference to certain illustrated embodiments, variations and modifications exist within the scope and spirit of the present invention as described and defined in the following claims.
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