text:
|Publication number
|Publication type
|Application number
|Publication date
|Oct 20, 1992
|Filing date
|Aug 24, 1990
|Priority date
|Jul 8, 1987
|Fee status
|Publication number
|Kaj Henricson, Mika Makela, Toivo Niskanen, Olavi Pikka, Vesa Vikman
|Original Assignee
|A. Ahlstrom Corporation
|Export Citation
|BiBTeX, EndNote, RefMan
|Patent Citations (37), Non-Patent Citations (2), Referenced by (5), Classifications (12), Legal Events (7)
|External Links: USPTO, USPTO Assignment, Espacenet
This is a continuation-in-part of copending U.S. patent application Ser. No. 216,842, filed Jul. 8, 1988, now U.S. Pat. No. 4,975,204.
The present invention relates to a method and apparatus for the continuous discharge of water from a suspension, especially from fibrous pulp, whereby pulp is thickened without the water being filtered through a thick, uncontrollably gathered fiber mat and so that fine particles are removed therefrom.
In the pulp and paper industry there are various processes which are carried out with a low consistency of pulp, even under 1%. Such processes include, for example, normal and reverse vortex cleaning. Subsequent to vortex cleaning the pulp is directed to a processing stage, as for example a thickener, or to the head box of a paper or drying machine. In any event, thickening always follows vortex cleaning in the paper making process.
The treatment of fibrous material, especially cellulose and wood fiber material, often takes place, as mentioned above, in low consistency suspension. For example, screening with perforated or slotted screens is carried out with a consistency of 1 to 3%. Subsequent to such screening the fibrous material is, for various reasons, thickened to a higher consistency. Often the consistency is thereby raised to the range of 10 to 15%, by way of example, for storage or bleaching.
Thickening is carried out in accordance with modern techniques by means of different types of disk or drum thickeners and curved filters. In conventional drum and disk thickeners the discharge of liquid, i.e. thickening, is based on so-called "gravity deckers", vacuum filters or pressure filters.
In gravity deckers the thickening is carried out by means of a horizontally mounted drum formed of perforated plate and covered with wire cloth. The pressure difference required for the thickening results from the level difference between pulp in the trough and filtrate in the filtrate chamber. Pulp may be filtered either from the inside of the drum to the outside or from the outside to the inside, which latter direction is the most common. In practice the diameter of the drum may be 4 m of which, for example, 60% is underwater. The maximum pressure difference is thus about 20 kPa. The pressure difference at the bottom dead center is zero, which difference increases to its maximum value toward the surface of the pulp in the trough. As a consequence substantially no thickening takes place on either side close to the bottom dead center. The situation is also similar in that part of the drum which is not underwater. Thus, a considerable part of the drum surfaces of the gravity deckers is inefficiently utilized. The capacity of that part or parts of the drum in efficient use also varies according to the prevailing pressure difference relative to the filtering surface. The specific thickening capacity of gravity deckers varies in accordance with the pulp and the running or operating conditions, but is typically in the range of 400 to 700 l/m2 /min. These types of thickeners are typically used to prethicken low consistency pulp as, for example, from 0.5% to 1.5-5%.
The filtering surface of the drum is kept clean or open to the flow by moving the surface against the filtrate or by using air to clean it. For example, a paper mill producing 500 tons of 90% consistency pulp requires a filter with a diameter of 4 m and a length of 7 m, the surface area being about 88 m2 of wire surface, to thicken the pulp from 0.5% to 1.5%.
The thickening method using a curved filter is also based on gravity decker filtering. The suspension to be thickened is pumped onto an inclined filtering surface. The thickening capacity is in practice 3 to 5% and the specific capacity of liquid discharge is about the same as that of drum filters. This arrangement has the advantage of not utilizing any mechanically moving members, but it also has a drawback in that the apparatus is relatively easy to clog because the attainment of efficient cleaning is difficult. Curved filter type thickeners are used in the pulp and paper industry when minor thickening and low pulp capacities are involved.
The above-described conventional pulp thickening apparatus or "thickeners" are characterized in that the thickening is carried out using very small pressure differences in more or less open equipment and only part of the filtering surface is utilized.
The small pressure difference and the only partial use of the filtering surface result in a poor ability to discharge liquid. The open construction and operational principles result in the possible inclusion of air in the pulp and filtrate. Air in the pulp decisively weakens, as is known, the infiltration qualities of the pulp.
In other heretofore known and earlier-used arrangements techniques, different types of vacuum filters are most common. The consistency of pulp in these filters is caused to increase through the removal of water from the pulp through a filter surface such, for example, as through a wire cloth covered by a thick fiber mat. In thickening pulp it is possible, by means of the suction effect on the pulp, to use a maximum pressure difference of about 0.5 bar because a stronger vacuum would, undesirably, cause the filtrate to boil.
The pressure difference required for filtering in vacuum and disk thickeners is achieved by a suction leg. Such thickeners differ from gravity deckers in that a pulp layer is formed therein. Thus, subsequent to thickening the consistency of the pulp is 8 to 14%; the capacity of a vacuum or disk thickener is accordingly about the same as that of a gravity decker. The difference between them is that the pulp web, in a vacuum or disk thickener, is formed by suction on the filtering surface through the pulp suspension when that surface is underwater. The filtrate is removed from the web formed on that part of the drum, when the same has risen above the surface of the suspension, so as to achieve the above-noted discharge consistency of 8 to 14%. It is clear that when forming a fiber mat on the filtering surface, the discharge of liquid through the pulp layer substantially slows due to the appreciable flow resistance of the filter web.
It is not advantageous to use this type of thickener for the purpose of prethickening, although it may be employed when the required discharge consistency is relatively high. The specific thickening capacity varies in accordance with the quality of the pulp and the volumetric flow conditions, e.g. in the range of 50 to 300 l/m2 /min. When employing the above-described apparatus two vacuum filters of that size would be necessary if seeking to achieve a thickened consistency of 10%. The advantage of utilizing a disk filter, rather than a vacuum drum filter, is that more filtering surface can be provided in the same device volume.
A pressure filter differs from a vacuum drum filter in that, in the former, the filtering pressure difference is generated by pressure rather than the suction or vacuum effect of the latter.
The problem with these and many other types of prior art thickeners is their tendency to clog. Where, for example, the pressurized suspension to be thickened is fed to a thickener, the pressure difference is in principle unlimited; in laboratory tests of such an arrangement this type of thickener became clogged by sulfate pulp in ten seconds, after which it had to be cleaned.
Several methods are known to prevent such clogging of or to loosen the web from the filter. For example, in the disclosures of Finnish Patent No. 41712 and U.S. Pat. No. 3,455,821 it is intended to clean the filter surface by vibration. However, the damping ability of the gaseous and fibrous paper pulp prevents the vibrations from having the intended cleaning effect.
Another cleaning method is shown in Finnish Patent No. 68005, according to which cleaning of the disk filter is carried out using compressed air. At a certain stage of the disk sector circulation, compressed air is directed to the inside of the disk sector whereby the air blast loosens the filtered pulp from outside of the sector.
The object of the present invention is to avoid or minimize the drawbacks and deficiencies of the above-mentioned prior art solutions and to create a new method and apparatus for the continuous thickening of 0.5 to 20% consistency pulp, without having to remove liquid through a thick fiber mat format uncontrollably on the filter surface due to a pressure difference and, therefore, also to remove fine impurities in the liquid. The filter plates are theoretically able to remove considerably greater amounts of liquid than in practice because the thickened pulp which collects on the surface of the filter plate effectively prevents the discharge of greater amounts of liquid. Thus, it is possible to considerably increase the filtering and separating capacity if the formation of a thick fiber mat on the surface of the filter plate can be controlled.
A method and apparatus for solving this problem by enabling substantially total fluidization of the pulp flow to be thickened is disclosed in Finnish Patent Application No. 781789 (Gullichsen). The apparatus provides a cylindrical conduit having a perforated wall disposed about a centrally-located rotor. The rotating rotor fluidizes the suspension whereby the fibers of the suspension are separated in the suspension and water can be filtered through the filter surface. As the suspension is totally fluidized a fiber mat is unable to form or collect on the filter surface and thereby plug the openings of the filter surface.
However, a tremendous amount of energy is required in the method and apparatus of this Finnish application of Gullichsen needed to fluidize the pulp flowing through the conduit during the time necessary to separate the liquid. The amount of energy needed thus required can be compared as follows to the energy needed when using the apparatus of the present invention. We may for this purpose assume a situation in which pulp of 10% consistency is dewatered to a consistency of 20%. Gullichsen must fluidize all of the suspension within the filtering chamber, whereby the required energy is E20 kW/mass ton and the rotational speed of the rotor is n20 rpm. E20 is the energy necessary to fluidize pulp at a consistency of 20%; n20 is the rotational speed of the rotor necessary to create shear stresses of sufficient magnitude to fluidize pulp at a 20% consistency.
We have, however, found that is not necessary to fluidize the total mass pulp flow to be able to remove liquid and fine impurities from the suspension as efficiently as in Gullichsen. It need only be insured that a thick fiber mat will not form on the filtering surfaces and that the changes in consistency, measured as a function of distance from the filtering surface, are minimized. Based on these principles, the dewatering of pulp in accordance with the present invention is operationally divided into three basic stages:
1. Mixing of the pulp in the mixing zone;
2. Controlling the thickness of the fiber mat on the filter surface and loosening and removal of the extra fiber material from that surface in the thickening zone; and
3. Removing the liquid through a filtering plate with openings small enough to prevent fibers from passing therethrough but large enough to allow liquid and fine scale particles smaller than said openings to pass through the filter surface.
First, the energy needed for mixing the pulp in the filtering chamber so as to achieve a uniform pulp with respect to inlet consistency is Em=0.03 . . . 0.15 * E20 and the rotational speed of the rotor is n=0.4 . . . 0.7 * n20. Second, the energy used for controlling, loosening and removing the fiber mat from the filter surface is El=0.5 . . . 0.8 * E20. It should also be noted that the energy mentioned above is subjected to the filter surface and not to the whole filter chamber. Finally, the average energy used by the method and apparatus in accordance with the present invention is E=0.15 . . . 0.5 * E20.
In addition, the present invention solves yet another problem. As earlier stated, the consistency of the pulp in the filtering chamber tends to increase toward the filtering surface and the present invention is able to prevent this by continuously mixing the pulp. However, the consistency of the pulp also increases toward the discharge end of the filtering apparatus in situations in which the flow of pulp to be thickened is axial. This phenomenon creates difficulties in controlling the operation of the filtering apparatus; at one end of the apparatus the fiber mat forms on the filtering surface at a certain pressure, while at the other end of the apparatus more pressure could advantageously be employed for removing liquid through the filtering surface.
The purpose or object of the present invention is to create an apparatus in which a continuous flow of pulp to be thickened is introduced onto the filter surface, which pulp does not permanently or uncontrollably attach to or collect on the filter surface but, rather, flows along the surface toward the discharge opening in such a way that no thick unbroken, uncontrolled fiber mat is generated and the pulp thickens in a continuous fashion. This operation may be facilitated by using known filter drums, the diameter of the perforations or the width of the slots of which is even less than 0.3 mm, whereby the pulp fibers do not pass through the perforated plate. Significant to apparatus applying this variation of the inventive method according to the invention is the requirement that the size of the pores, slots or perforations be sufficiently small for this purpose; it has been noted in tests that for most wood fibers a perforation size of 0.2 to 0.3 mm is sufficiently small. When such a small perforation size is used liquid can be removed, and yet the filtrate does not include or contain or carry disturbingly many fibers. In one performed test in which the consistency of the pulp was raised from 10% to 15%, the fiber consistency of the filtrate was less than 0.1%. However, tests have also shown that small particles may pass through and are separated from the fibers with the filtrate. In addition, the fibers found in the filtrate are mostly fines, which means smaller fiber fractions.
A further significant feature of the invention resides in the mixing of pulp in the thickening chamber by a moving member so as to continuously equalize its consistency and so that, even relatively close to the filter surfaces, the pulp consistency does appreciably differ from the average consistency. The operational advantages of the method and apparatus of the present invention, in both increased consistency and the uniformity of the consistency of the thickened pulp, far surpass and outnumber the effects of previously-known methods and apparatus.
In one variation of the method according of the present invention, the suspension to be thickened is introduced into the thickening apparatus in a pressurized state. A substantially thin layer of pulp is brought into communication with the filtering surface, this layer being mixed continuously such that the consistency of the suspension is maintained substantially constant throughout the layer, the fiber mat is prevented from uncontrollably forming on the filtering surface, and the thickness of the fiber mat is controlled by regulating the pressure difference across the filtering surface.
A preferred feature of the method of the invention is that the pulp to be thickened is introduced into the filtering chamber substantially along the full axial length of the chamber. In addition, the suspension is caused to rotate in the chamber, the liquid being removed from the suspension and the suspension being discharged from the filtering chamber along substantially the full length of the chamber whereby the suspension consistency is maintained substantially uniform throughout the filtering chamber.
The apparatus for thickening fiber suspensions in accordance with the present invention includes at least one of the cooperating surfaces--preferably the filtering surface and its counter-surface--being provided with means for non-mechanically limiting the thickness of a fiber mat formed on the filtering surface, thereby preventing uncontrolled formation of a fiber mat on the filtering surface.
In a preferred embodiment of the inventive apparatus, a substantially cylindrical member is disposed within the apparatus interior and includes a substantially axial slot through which the suspension to be thickened flows between the cylindrical member and the filtering surface.
Another preferred embodiment of the inventive apparatus includes an apparatus housing provided with a conduit for gas to be fed into the apparatus for backflushing the openings of the filtering surface and for creating a gas bubble centrally within the apparatus for controlling the total thickness of the pulp layer to be thickened.
The advantages achieved in accordance with the invention include, among others, acceleration of the thickening operation and an increase in the ability to discharge liquid from the thickener, since no thick fiber mat layer--which would prevent liquid from flowing from the center of the pulp stream to the filter surface--is permitted to uncontrollably form from the pulp to be thickened. Additional advantages of the closed arrangement to be herein disclosed are, by way of example, that inconvenient odors are not generated in the thickening process and that the apparatus may be pressurized or subjected to a partial vacuum.
A still further and important advantage over some prior art methods and apparatus is the considerably lower energy consumption of the present invention as compared to prior art devices and processes.
The invention is described below in detail, by way of example, with reference to the enclosed drawings, in which:
FIG. 1 is a schematic elevational illustration of a first embodiment of an apparatus for carrying out a method in accordance with the present invention;
FIG. 2 is a schematic elevational illustration of a second embodiment of an apparatus for carrying out a method in accordance with the present invention;
FIG. 3 illustrates four embodiments of recesses provided on the rotor surface;
FIG. 4 schematically depicts an arrangement of test equipment used in testing a method and apparatus in accordance with the invention;
FIGS. 5 and 6 are schematic illustrations of processes utilizing the method and apparatus of the invention;
FIGS. 7 and 8 are an elevational and a plan view, respectively, of a third embodiment of an apparatus in accordance with the invention;
FIGS. 9 and 10 are an elevational and a plan view, respectively, of a fourth embodiment of an apparatus in accordance with the invention;
FIG. 11 is a plan view of a fifth embodiment of an apparatus in accordance with the invention;
FIG. 12 is an elevational view of a sixth embodiment of an apparatus in accordance with the invention; and
FIGS. 13 (13A, 13B and 13C) and 14 (14A and 14B) depict first and second embodiments, respectively, of filter plates effective for increasing turbulence at the filter plate surface so as to improve the separation of fine particles.
Illustrated in FIG. 1 is a first embodiment of a pulp thickening apparatus constructed in accordance with the invention. As there shown, the thickening apparatus includes a cylindrical outer casing 1 with an inlet connection 2 for pulp to be thickened, an outlet connection 3 for the thickened pulp and an outlet connection 4 for the filtrate, a top cover 5 and a frame structure 6 including a base plate and a drive means 7. Disposed within the casing 1 is a drum 8 for operation as a filter surface and radially outwardly bounding an annular space 9 for the filtrate. Interiorly of the drum 8 is a rotor 10 arranged for rotation in predeterminately close proximity to the filter surface 8. By so arranging the form of the rotor 10 that it accelerates the pulp to a sufficient circumferential speed, it is possible to thereby carry out suitably efficient mixing of pulp. An alternative is to arrange the thickening drum as a rotor, whereby the purpose of the counter-part--i.e. the stator--is to operatively keep the pulp stationary or, rather, to permit it to flow axially downward between the rotating drum and the stator. On the surface of the rotor 10 are provided members 12 for loosening the fibrous layer. Equipment or devices for discharging light impurities, such as plastics or like, may also be attached to the apparatus.
The pulp to be thickened is introduced into the apparatus through an inlet connection 2 from which the pulp flows onto the rotor 10 and further into the ring-shaped thickening chamber 11 between the rotor and the filtering surface 8. The rotor, and especially its members 12, is effective to rotate the pulp so that a fiber mat is not able to freely form on the filter surface. Due to the rotor rotation the pulp being thickened is continuously mixed so that its consistency is uniformly increased throughout the pulp layer in the filtering chamber. It is clear, however, that the consistency of the pulp in the filtering chamber is increased as it passes or flows downward in the chamber. The liquid being filtered through the openings of the filtering surface is discharged through outlet connection 4 from the filtrate chamber 9 and the thickened pulp is discharged through outlet connection 3 from the lower part of the apparatus.
A second embodiment of the invention is illustrated in FIG. 2 and includes a thickening apparatus formed primarily of substantially the same or like components as the FIG. 1 apparatus hereinabove described. The primary difference between the two is that the apparatus of FIG. 2 is provided with two filter surfaces or drums 13, 14 between which a rotatable rotor 15 is arranged. The operation of the FIG. 2 apparatus is substantially the same as that shown in FIG. 1 with the exception that, in the former, the filtrate is discharged through the two outlet connections 16.
FIG. 3 illustrates several different types or configurations of members (identified by the reference numeral 12 in FIG. 1) for mixing the suspension and for controlling the thickness of the fiber mat on the filter surface, the filter surface being subjected to reciprocating or alternating pressure or suction pulses which loosen fibers stuck in the filter surface openings or fibers that have partly penetrated the openings, and by virtue of which the flow of filtrate through the filter surface is facilitated. With specific reference to FIG. 3, the pulsating member 20 is formed as a hemispherical protrusion arranged on the surface of the rotor or on the blade of the rotor. A bulge member 21, on the other hand, has a steeply inclined or stepped upstream edge and a relatively gently inclined or ramped or sloped downstream edge. Another alternate member 22 is a variation of the member 21 and comprises a rib that extends close to the surface of the filter plate, the upstream edge being relatively steeply inclined or stepped and the downstream edge being more gently or gradually inclined or sloped along and throughout the length of the rib. Still another member 23 is illustrated as a variation of the member 22 and includes a rib designed to consume as little power as possible--that is, it has a wing-like or aerodynamically-contoured form.
It is also advantageous to group the rotor and the pulsating members in the rotor and design them in such a way that the inflowing pulp is distributed equally throughout the thickening zone.
The method and apparatus of the invention have been tested in the laboratory in accordance with and utilizing the testing arrangement schematically shown in FIG. 4. Reference numeral 30 denotes a circulation tower from which pulp is pumped by a feed pump 31 to the test, i.e. filter, apparatus 32 through a feed valve. The pulp may, if required, be fed directly back to the circulation tower 30 past the filter apparatus 32 through a valve 34. A sample of unthickened pulp was taken from the extracting member 35 and a sample of thickened pulp from the member 38 downstream of filter valve 39. The desired pressure condition in the filter apparatus 32 may be adjusted by way of the valves 37 and 39. The dimensions of the filter apparatus utilized in the test were:
______________________________________Surface area if the filter cylinder 0.4 m2in the testing apparatusSize of perforations in the filter 0.2 mmcylinder of the testing apparatus______________________________________ pine birchResults: sulfate sulfate______________________________________inlet consistency 0.5% 0.5%in the apparatusconsistency of 1.5% 1.5%thickened pulpconsistency of filtrate 0.02% 0.04%capacity to 4500-5500 1/m2 /mindischarge liquidpressure difference 20-40 kPain the test run______________________________________ Pulsating members of the rotor in the testing apparatus were as shown in FIG. 3
The tests performed demonstrate that it is possible to attain multiplied efficiency with the pressurized thickening method and apparatus of the invention compared with conventional thickeners. The apparatus is, moreover, unusually compact in construction. Due to the pressurized operational principle both the filtrate and the thickened pulp are overpressurized, thereby providing great liberty and the ability to save space in positioning the apparatus to suit mill conditions. Additionally, inflow of air into the pulp in the thickening process is not possible.
When analyzing the filtrate it was found that although its consistency varied between 0.02 and 0.04% it contained very few actual fibers. Rather, the filtrate contained fines, fiber fractions, fillers, extractives and other small impurities. It is thus apparent that the apparatus may be used to separate all kinds of small particles that flow along with the liquid phase. Such particles may be found in great amounts when processing secondary fibers and broke at paper machines. In the processing of mechanical fibers the amount of damaged fibers and small extractives containing fibers is great and one may therefore also expect a greater quantity of particles in the filtrate when dewatering mechanical fibers. This separation of small particles may be used to improve mill operation. For example, by removing extractives and fines before bleaching, a reduction in the consumption of bleaching chemicals will be noted. This reduction is due to the fact that extractives and fines consume a substantial amount bleaching chemicals although bleaching these particles contributes little to overall brightness. Another example of improved mill operation is the removal of small dirt particles from the fiber suspension by permitting the small particles to pass through the filter surface openings and be thereby separated from the suspension. In this manner cleanliness can be improved while thickening the suspension.
The apparatus used in tests conducted in accordance with FIGS. 5 and 6 is, in principle, similar to that of FIG. 7--that is, it comprises a housing 1, a cover 5, a base 6, and drive means 7. The housing has an inlet conduit 2 for the pulp, a discharge conduit 4 for the filtrate and a discharge conduit 77 for the thickened pulp. A discharge conduit for possible reject may be additionally provided in or on the housing. Within the housing is arranged a stationary filter surface 78 and, positionally proximate thereto, a movable surface 79 which may, for example, comprise a rotatable rotor 79 of the type shown in FIG. 3 or of any other suitable type. The embodiment of FIGS. 7 and 8 differs from the earlier herein-disclosed arrangements in that the filter surface is not a uniform cylinder but, rather, has a discharge opening 80 in communication with the discharge conduit 77, the conduit 77 being located not in the lower part of the thickener, as in the apparatus of FIGS. 1 and 2, but on the side of the thickening apparatus.
A variety of advantages are achieved by this arrangement. For example, the opening 80 of the filter surface 78, irrespective of whether it comprises an opening as high as the entire filter surface or lower, generates additional turbulence which cleans the filter surface and the rotor. On the other hand, the thickened pulp does not have to flow between the rotor and the filter surface throughout the entire apparatus down to its lower or bottom part but is, instead, discharged at an earlier stage. It should also be noted that the mutual and relative positions and operation of the filter surface and rotor need not be as described hereinabove; rather, the stationary, not quite uniform cylindrical part may be a member having a surface alternative in accordance with FIG. 3 and the rotational part may be a filter surface, whereby the filtrate is discharged through the rotational member. The illustrated vertically-oriented apparatus may also be arranged horizontally or, if desired, at an inclined or angled orientation.
A further development of the embodiment of the apparatus depicted in FIGS. 7 and 8 is shown in FIGS. 9 and 10, in which the pulp is brought axially into the apparatus through a conduit 82. A filtering chamber 83 is separated by a stationary cylinder 84 from the central portion 85 of the apparatus, from which central portion the pulp may flow out through only one substantially axial slot 86 in the cylindrical inner wall 84 into the chamber 83 defined between the cylindrical surface 84 and the filter surface 87. Disposed within the chamber 83 is a rotatable rotor or blade member 88, the purpose of which is to operatively keep the pulp in motion, to mix it and to control the thickness of the fiber mat on the filter surface 87. The rotor or blade member 88 is preferably mounted on a shaft 89 by means of an arm 90 arranged in substantially the central portion of the apparatus and extending through a slot 91 in the cylindrical wall 84. Pulp is discharged from the apparatus shown in FIG. 7 through an opening 92 positioned at the same height as the apparatus on the filter surface 87, through which opening the pulp can flow into the discharge conduit 93. By providing a throttle means in the discharge conduit 93 it is possible to control the total time that the pulp circulates in the apparatus before flowing into the discharge conduit 93. The openings 86, 92 of the cylinder and of the filter surface, respectively, are preferably so located relative to each other that the blade member 88, commencing the circulation of the pulp flowing in from the opening 86 of the cylinder, enters from the direction of the opening 92 of the filter surface, whereby the pulp is caused to circulate about at least almost the entire inner circumference or periphery of the thickener before its first possibility of exiting the apparatus through the discharge conduit 93.
One advantage of the apparatus of FIGS. 7, 8, 9 and 10, as compared to the arrangements shown in FIGS. 1 and 2 and in accordance with the results of tests, is that the operation of the former is relatively easy to adjust. The pressure above the filter surface remains the same along the height or length of the filter surface and does not, as in some prior art arrangements, vary.
The further modified apparatus shown in FIG. 11 is quite similar to that depicted in FIG. 1. The apparatus is seen as viewed from above and comprises a housing 1, conduits 95, 96 and 97 for the intake of pulp to be dewatered, for the discharge of filtrate and for the discharge of thickened pulp, respectively, a filter surface 98, and a rotor 99 provided interiorly of the filter surface. The pulp is fed into the chamber outwardly of the filter surface 98--i.e. between the housing 1 and the filter surface 98--whereby discharge of the filtrate is effected in the direction opposite to that of the other embodiments; in other words, the filtrate flows inwardly through the filter surface 98. In this embodiment it is sometimes advantageous to make the filter surface rotatable and the surface inside it stationary, whereby the stationary surface subjects the filter surface to pulses for removing filtrate through the filter surface and for loosening or removing the fiber mat.
In one preferred embodiment the stationary surface includes recesses which are effective to generate suction through the filter surface. These recesses may be open--i.e. have their open ends--toward or at that part ascending to the same level as the rest of the surface so as to generate a pulse directed opposite to the filter surface for loosening the fiber mat formed on the filter surface, or the recesses may be open toward the opening through which the liquid filtered through the filter surface is directed to the inside of the surface and further led for discharge from the apparatus. The advantages of an apparatus constructed in accordance with this embodiment include, first, the ability to create an intensive suction effect on the inside surface of the filter surface, whereby the thickening effect is rendered unusually efficient. Second, when operating as a rotor the surface need not cause the entire pulp flow entering the apparatus to undergo rotational movement, so that a savings in energy consumption is achieved. Third, energy is also saved by predeterminately configuring or shaping the surface 98 so as to minimize the amount of energy consumed, irrespective of whether the surface operates as a rotor or as a stationary, pulse generating surface. This is a particular object, for example, for the last-described embodiment in which recesses are provided on the stationary surface. In this embodiment the pulse members may, in fact differ somewhat from that shown in FIG. 3 because their most important function is to subject the filter surface to a long suction that is as even as possible and as a result of which filtrate is removed, through the filter surface, from the pulp. As should be apparent, the intensity of the suction effect determines the length of the suction stage. If the suction is very intensive, the pulp tends to thicken quickly on the filter surface whereby the length of the suction pulse may not be so great that the pressure pulse is no longer able to loosen the fiber mat on the filter surface. By adjusting the speed difference between the filter surface and the surface generating pulses, on the other hand, the desired thickening speed may be varied so as to optimize the relation of the filtrate discharge to the amount of fiber mat.
A sixth embodiment of a thickening apparatus in accordance with the invention is shown in FIG. 12; this last embodiment is quite different from those hereinabove shown and described. The apparatus 101 of FIG. 12 is intended for most advantageous use in a horizontal position. It comprises a cylindrical housing 102 having two conduits 103 and 104 for the gas and for the filtrate, respectively. The inlet conduit 105 for pulp to be thickened is located at one end of the apparatus and a discharge conduit 106 for the dewatered pulp is provided at the opposite end of the apparatus. In one form or version of this embodiment a filtering drum 107 disposed axially within the housing 102 is stationary and a rotor 108 located inside the drum and for maintaining the motion in the pulp is operatively rotatable. Air or other gas is fed from behind the filter surface 107, through the conduit 103, and into a chamber 109 that surrounds the filtering drum. The air may be fed either as a pulsating or continuous flow and, most importantly, the air replaces the water which is radially removed from pulp layer and discharged from the apparatus through the conduit 104. The thickened pulp is directed out of the apparatus from the opposite end with respect to the feed end at the same pressure as the infed pulp. The pressure difference prevailing between the filtrate and the infed pulp is 20-100 kPa, depending on the particular case.
In another version of this embodiment the thickening drum rotates and compressed air is blown or directed onto any sector or sectors of the drum. The air stream may be continuous so as to ensure that the filter surface remains clean.
The flow of air into the thickener may in some cases be utilized so that an air bubble is permitted to grow at the center of the thickening apparatus whereby the air bubble is effective to control the thickness of the fibrous layer moving close to the filtering surface. In this arrangement the rotor generates a sufficient shear force field in the pulp layer to mix the pulp and to successfully effect thickening. When required--as where a pressurized thickener is involved--the air bubble may be replaced by a central member between which member and the filter surface the rotor operatively rotates. It should be noted that when utilizing a gas bubble interiorly of the filtering surface the rotor may be formed of several foil-type blades, since the gas bubble controls the thickness of the pulp layer to be thickened and the blades only mix the pulp and control the thickness of the pulp mat on the filter surface.
A feature that is essential or important to each of the above-described arrangements is that a relatively thin pulp layer is somehow arranged or disposed or maintained close to the filter surface. At the same time, each arrangement is effective to insure that the entire volume of pulp which flows into the apparatus comes into contact with the filter surface, thereby enabling small particles to be separated, and that a substantially uniform consistency of the pulp inside the filtering chamber is maintained without regard to distance from the filter surface.
Test runs have shown that the higher the pulp consistency, the larger the filter plate opening that may be used. This occurs because the fiber network is at that moment stronger and a single fiber is not loosened from it with any reasonable degree of ease. As a consequence, filter plates having openings of one or more sizes may be employed. It is known that a larger opening provides greater penetration and, in addition, the apparatus is less costly to manufacture. The most practical arrangement is one in which, for example, the perforations are smallest at their inlet ends, are slightly larger in the middle and are largest at their thickened pulp discharge ends.
FIGS. 13A, 13B and 13C, on the one hand, and FIGS. 14A and 14B, on the other, depict filter plates having uneven surfaces. In FIGS. 13A, 13B and 13C, the filter plate 110 is formed by machining or otherwise forming grooves 112 in the surface of a smooth plate 114. The openings--in the form of small holes 116 or slots or the like--may be machined or formed in the plate 114 either before or after the grooving. The filter plate illustrated in FIGS. 14A, 14B is fabricated by attaching ridges or bars 118 on a smooth plate 120. In the form of the plate there shown, the openings 122 have been machined or otherwise formed in the plate prior to attachment of the bars 118 thereto. The openings may alternatively, of course, be defined in the plate after attachment of the bars 118 in which case they will also extend through the bars. The uneven surface of the filter plate--for both the FIG. 13 and FIG. 14 embodiments--is disposed so as to face the fiber suspension to be dewatered. In this manner, additional turbulence is created in the fiber suspension flowing over the filtering surface. This additional turbulence provides certain advantages with respect to the removal of fines. For example, the additional turbulence breaks up fiber agglomerates at the surface of the filter plate and enables the fine particles to reach the filter plate more easily and thereby be separated. The additional turbulence also loosens, from the fiber, dirt particles attached thereto and thereby facilitates the separation of such particles together with the filtrate.
As should by now be apparent from the foregoing description, a new type of pulp thickening method and apparatus has been developed, by virtue of which it is possible to minimize or eliminate the drawbacks and deficiencies of prior art apparatus and techniques without creating new or additional problems. Although only a relatively few advantageous apparatus alternatives and points of application have been expressly described in this disclosure, they are by no means intended to restrict the scope of the invention from that which is defined in the appended claims. Thus, by way of example, both the filter surface and the surface movable relative to the filter surface may be of a form other than cylindrical, these members being characterized only in that they are substantially rotationally symmetrical--be it cylindrical, conical, spherical, a combination thereof, or otherwise shaped or constructed for that purpose.
|Cited Patent
|Filing date
|Publication date
|Feb 24, 1927
|Jul 12, 1932
|Allen Pickard Joseph
|Apparatus for purifying used lubricating oil and the like
|Nov 10, 1955
|Aug 25, 1959
|Sanborn Neuhart David
|Liner for cargo spacer
|Sep 24, 1958
|Apr 17, 1962
|Bird Machine Co
|Screening device
|Jan 17, 1961
|Mar 23, 1965
|Lamort E & M
|Apparatus for cleaning liquids containing in suspension solid particles and particularly cellulosic pulps
|Apr 29, 1964
|Jan 16, 1968
|Bird Machine Co
|Screening apparatus with rotary pulsing member
|Jan 25, 1965
|Jul 15, 1969
|Ahlstroem Oy
|Apparatus for treating slurries or gases with screen or filter surfaces under pressure
|Jan 9, 1970
|Jun 1, 1971
|Improved Machinery Inc
|Screening apparatus
|Apr 16, 1968
|Jun 22, 1971
|Ingersoll Rand Canada
|Screening apparatus
|Mar 23, 1970
|Aug 1, 1972
|Bird Machine Co
|Aug 20, 1971
|Jun 4, 1974
|Centrifugal And Mechanical Ind
|Method for centrifugally removing liquid from a mixture
|Sep 12, 1972
|Nov 19, 1974
|Black Clawson Co
|Method and apparatus for screening paper fiber stock
|Mar 16, 1978
|Feb 12, 1980
|Hermann Finckh Maschinenfabrik
|Screening apparatus for fiber suspensions
|Jun 19, 1980
|Jun 30, 1981
|The Black Clawson Company
|Apparatus for screening paper fiber stock
|Jul 24, 1980
|Sep 28, 1982
|J. M. Voith Gmbh
|Separator for cleaning suspensions
|Dec 8, 1982
|Jan 1, 1985
|Westvaco Corporation
|Method for washing a fibrous particle mat with wash liquor having an impact energy sufficient to disrupt and rearrange the interstitial pore matrix
|Aug 27, 1986
|Jun 7, 1988
|Ingersoll-Rand Company
|Screening apparatus
|Jun 20, 1985
|Aug 8, 1989
|Beloit Corporation
|High consistency pressure screen and method of separating accepts and rejects
|Nov 21, 1988
|Jun 12, 1990
|Schneider-Shiley (U.S.A.) Inc.
|Hemostasis valve
|Jun 10, 1988
|Sep 4, 1990
|Beloit Corporation
|Wave screen plate
|Jul 8, 1988
|Dec 4, 1990
|A. Ahlstrom Corporation
|Method and apparatus for thickening fiber suspension
|May 31, 1979
|Jun 9, 1981
|Johan E. Gullichsen
|Method and an apparatus for treating fibre suspensions
|Title not available
|Title not available
|Title not available
|Title not available
|Title not available
|Title not available
|Title not available
|Title not available
|Title not available
|Title not available
|Title not available
|Title not available
|Title not available
|Title not available
|Title not available
|Title not available
|Chemical Abstracts, vol. 103, No. 8, Aug. 26, 1985, p. 90, Columbus, Ohio.
|Chemical Abstracts, vol. 95, No. 8, Aug. 24, 1981, p. 99, Columbus, Ohio.
|Citing Patent
|Filing date
|Publication date
|Feb 28, 1995
|Jun 18, 1996
|J.M. Voith Gmbh
|Device and method for choking a stock suspension flow in a paper machine
|Jun 30, 1994
|Oct 15, 1996
|J. M. Voith Gmbh
|Device and method for choking a stock suspension flow in a paper machine
|Aug 9, 1995
|Jul 8, 1997
|E & M Lamort
|Rotor-equipped cylindrical screens
|Aug 8, 1997
|Apr 25, 2000
|Inland Paperboard And Packaging, Inc.
|Reducing wax content and enhancing quality of recycled pulp from OCC and waste paper
|May 25, 2000
|Sep 3, 2002
|Voith Sulzer Papiertechnik Patent Gmbh
|Fittings and process for producing fittings for the mechanical processing of aqueous paper stock
|U.S. Classification
|210/785, 210/383, 162/56, 210/414, 210/791, 210/411, 162/380, 210/396, 210/415
|International Classification
|Cooperative Classification
|European Classification
|Oct 1, 1990
Owner name: A. AHLSTROM CORPORATION, SF-29600 NOORMARKKU, FINL
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNORS:HENRICSON, KAJ;MAKELA, MIKA;NISKANEN, TOIVO;AND OTHERS;REEL/FRAME:005468/0887
Effective date: 19900911
|Mar 13, 1996
|Fee payment
Year of fee payment: 4
|Mar 20, 2000
|Fee payment
Year of fee payment: 8
|May 31, 2000
Owner name: AHLSTROM MACHINERY OY, FINLAND
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:A. AHLSTROM CORPORATION;REEL/FRAME:010822/0820
Effective date: 20000530
|May 5, 2004
|Maintenance fee reminder mailed
|Oct 20, 2004
|Lapse for failure to pay maintenance fees
|Dec 14, 2004
|Expired due to failure to pay maintenance fee
Effective date: 20041020


text:
We found 2 providers named 'Young Huh' nationally.
Specializes in Adult Gastroenterology
2222 53rd Avenue
Bettendorf, IA
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Dr. Young Huh is a gastroenterologist. He takes Medicare insurance. Dr. Huh attended medical school at SUNY, University at Buffalo School of Medicine & Biomedical Sciences.
Specializes in Social Work
605 W Olympic Boulevard; Suite 600
Los Angeles, CA
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Ms. Younga Huh's area of specialization is social work. She is an in-network provider for L.A. Care Health Plan insurance.
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subset: commoncrawl


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television news anchor & reporter KPIX CBS 5
@AMartinCBSSF — 733 followers, 622 tweets
@TomMcGowan777 I always say 'I'm never coming back to this store'... yet I do because there are few options - which are all much more expensive
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RT @ExtraFoodDotOrg: Brief video by @AMartinCBSSF & Jen Mistrot of @CBSSF on our partnership w/@CollegeofMarin http://sanfrancisco.cbslocal.com/ …/…


text:
Xtreme Racing BX5-T Xtreme Blue Brake Disks (2)
Xtreme Racing
This item is discontinued and no longer available for purchase. You may want to search our site for a similar item.
|Low Price:
Discontinued Online
This is a set of optional Xtreme Racing Carbon Fiber Brake Disks, and are intended for use with the Mugen MBX5-T 1/8 truck.
This product was added to our catalog on May 25, 2007.


text:
Helpful (1)
I applied through a recruiter. I interviewed at Booz Allen Hamilton (Charleston, SC) in March 2017.
This was one of the longest, strangest interview processes I've experienced. I interviewed three times over the phone/Skype and then went into the onsite portion. Each interview came with a sense of urgency, I was left with the feeling that I should prepare to leave my current position and relocate as soon as possible. However then came more waiting in between each interview to the point where I felt I was out of the running, before I heard from them again weeks later. This cycle went on over the course of nearly three months, by the time I received their final decision I had thankfully long moved on. The one plus was that the recruiters are friendly and try to keep in touch, but I couldn't help but feel that the company either didn't have it all together for this position, or I was the absolute last choice. One of the follow-up emails I received wasn't even for the position I was applying for. The onsite interview was nice in the fact that everyone was welcoming and excited to answer questions, however it was labeled as a job shadowing with lunch when in reality was just background information about the merger and a short tour. I understand these things take time but if you want to attract talent and keep them excited about the opportunity, especially if asking to take time away from their current job, then have a little more transparency and be upfront (and professional) about the process.
Interview Questions
I applied online. The process took 2+ months. I interviewed at Booz Allen Hamilton (Charleston, SC) in February 2017.
The interview process was very smooth. First was a short phone interview followed by an on site interview. They got back to me within a few weeks and seemed extremely excited about having me as a part of their team for the summer.
Interview Questions
I applied through a recruiter. The process took 1+ week. I interviewed at Booz Allen Hamilton (Charleston, SC) in February 2015.
I met with hiring manager via Skype and then met with next three levels of management in person. They asked challenging questions and wanted to know more about my background and level of technical experience. I was not able to obtain much of any information from the BAH team about the position itself because the project is gov't-related and classified.
Interview Questions
Helpful (1)
I applied online. The process took 4+ weeks. I interviewed at Booz Allen Hamilton (Charleston, SC) in July 2014.
Applied for the position through their website, was contacted through HR about a week later and we set up an interview for the following week. Went in for a panel interview where we discussed my resume and relevant experience, as well as some behavioral type questions which were easy to answer. After the interview I then toured the facilities and got a look at what it would be like to work there. Overall easy interview but despite that there were more qualified candidates so I was not extended an offer.
Interview Questions
I applied online. The process took a week. I interviewed at Booz Allen Hamilton (Charleston, SC).
Applied on-line and was contacted by hiring manager in the DC area. Basic phone interview/pre-screening, then set up for a hiring event locally. Received an email prior to event with additional details. At the hiring events, candidates were introduced to multiple Booz Allen associates (one at a time) for informal discussion and interview questions.
Interview Questions
I applied through an employee referral. The process took a week. I interviewed at Booz Allen Hamilton (Charleston, SC) in November 2009.
I first had an interview over the phone which asked general questions about my skill set, how much I knew about the position to which I was applying, and general salary requirements. I was also asked why I was looking to change jobs from my current employer. Next, I received an appointment for a face-to-face and was prompted to complete an online new employee-type questionnaire to be used for a background screening. Finally, I was scheduled for the face-to-face interview and proceeded to it. I was interviewed by a total of three people, one at a time. There were a lot of questions about my abilities to perform as a team member as well as leadership abilities/aspirations. There were questions about process improvement, initiative, etc. There wasn't much in the way of job specifics which I found somewhat refreshing. They were more concerned with character and I saw this as a positive; quality people makes all the difference.
I'm rating the interview as easy due to the fact they were more interested in me as a person than any specific job skill. It wasn't a test to determine if I knew something...it was an evaluation of me and my alignment with BAH values.
Interview Questions
Helpful (1)
The process took 1 day. I interviewed at Booz Allen Hamilton (Charleston, SC) in May 2009.
I thought the interview was more about can you fit into the Booz team. The job I applied for expressed teamwork in workplace. They ask questions about my capabilities, leadership, and personality. I knew I had the capabilities for the job with my military background, so I focused more on the personality piece. It paid off.
Interview Questions
Would you like us to review something? Please describe the problem with this {0} and we will look into it.
Your feedback has been sent to the team and we'll look into it.
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text:
Does Blackheart Lingerie offer free returns? What's their exchange policy?
What's Blackheart Lingerie returns and exchanges policy? Can you return in-store? How many days do you have to return items to Blackheart Lingerie for a full refund? Do I need a receipt to return my item to Blackheart Lingerie? Do items need to be in new condition?
Blackheart Lingerie's returns & exchanges policies are rated:
4.0 - 1 rating
1 answer
Add answer and rate this store
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This user rated Blackheart Lingerie's returns & exchanges policies:
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Blackheart Lingerie's shipping costs are rated:
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Blackheart Lingerie's military discount policies are rated:
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text:
PC Games
This page contains Cheats for Dark Realm: Guardian Of Flames organized by sections for PC. This game has "Puzzle Hidden Object" as genre, made by Mad Head Games, released on Jul 8, 2017. If you can't find a hint or secret in our list, then please check this page periodically for the latest updates.
Boxshot & Details
- Developer: Mad Head Games
- Publisher: Big Fish Games
- Genre: Puzzle Hidden Object
- Release: Jul 8, 2017
- ESRB: Not Set
Game Walkthroughs
Added: 07-11-2017
Added: 07-15-2017
Submit Cheats
If you know cheat codes, secrets, hints, glitches or other level guides for this game that can help others leveling up, then please Submit your Cheats and share your insights and experience with other gamers.
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text:
Princess Baby Shower Invitations Pinterest
The appealing Princess Baby Shower Invitations Pinterest digital imagery below, is other parts of Princess Baby Shower Invitations content which is classified within Baby Shower Invitations and posted at October 2, 2016.
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|Princess Baby Shower Invitations Pinterest
|Published Date
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|Latest Updated Date
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Google Chrome 8 becomes official1/2
Google has launched the stable release of Chrome 8, adding a couple of nice new features as well as numerous security and bug fixes for the speedy browser.
Version 8.0.552.215, to give it its full moniker, comes with a new PDF viewer that brings the security of Chrome's sandbox. What this means is that the browser isolates a page showing a PDF file and even if the file is riddled with malicious code, set up by the web-baddies, Chrome would contain the threat and the file wouldn't be able to harm your system or modify its information.
Chrome 8 also supports the, yet-to-be-released, Chrome Web Store - although you'll see no mention of this in the official release notes.
What the official notes do state, however, is over 800 bug fixes and stability improvements. You can see a full list of these at the Chromium security page.
Chrome 8 is also supposed to be much quicker than Chrome 7, with some reports even claiming that it is twice as fast.
Chrome 8 is available to download now, give it a spin and let us know what you think.
- Best Buy's Black Friday in July: All the best deals in one place
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- CityMapper is launching a night bus service in London this August
- Here's what is different in the Google app's new feed experience
- Snapchat: How to multi-snap record and change the colour of any object


text:
|Operation D.C Purge
|September 7th, 2012 - September 16th, 2012
Late In Battle
|United Nazi War
|United Nation Victory...
|D.C Purge
Operation D.C Purge also known as The D.C Purge Was a Nazi Offensive against the United States capital of Washington D.C, in hopes of seizing the United States military from interfering with there search for Kate Bush. It was also known to be an revenge operation for the United States interfering with Kate Bush escaping a second time during The Battle of Premium, 13 days back.
Operation D.C Purge would be the last Nazi Operation outside New England.
Discovery of New Nijmegan Bridge Edit
- Main article: New Nijmegen Bridge
Invasion of PennsylvaniaEdit
Invasion Of Knox TownEdit
- Main article: Fall of Knox Town
Fall of New HarlemEdit
Battle of the BoarderEdit
- Main article: Battle of The Pennsylvania/Maryland Boarder
Invasion of Maryland Edit
The Rojas GapEdit
- Main article: Battle Of Rojas Pass
Morus TownEdit
Operation NirmanEdit
- Main article: Operation Nirman
Invasion of Washington D.C Edit
- Main article: Nazi Invasion Of Washington D.C
Battle Of the SuburbsEdit
The Downtown AreaEdit
Battle Of the Grand MallEdit
- Main article: Battle of The Grand Mall
Defense Of the Capital BuildingsEdit
Reinforcements ArriveEdit
Battle of Roland SquareEdit
- Main article: Battle Of Roland Square
German WithdrawEdit
Liberation of New HarlemEdit
- Main article: Second Battle of New Harlem


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Hi there thought I might join in. I'm on the Aug/Sep thread already as my tww should end in August, if everything goes well. I'm here because my tubes are blocked due to endo and had a laparoscopy last year to discover the damage. Got my EPU sometime next week, find out Mon after my scan and bloods.
This is my first cycle so learning it all as I go but it certainly helps reading posts on here. Good luck everyone x
+ Reply to Thread
Results 61 to 70 of 946
21-07-2013 15:54 #61
21-07-2013 16:02 #62Member
- Join Date
- Jun 2013
- Posts
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- 36
- Thanked
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- 0
Hi Ladies,
Im new to this thread, ive been in the june/july one but nothing was really happening for me and Ive been waiting for a july/aug one.
Started my puregon injections 3 days ago so... hubby is away for work and will be away for most of the important times which sux but im dealing with it!
I am looking forward to hearing about all of your progression!
21-07-2013 19:01 #63Junior Member
- Join Date
- Jul 2013
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Hello ladies,
im feeling quite nervous, I go for my BT and scan tomorrow. Been taking my Gonal F and Orgalutran but haven't been having any symptoms, what if I haven't grown any extra follicles eek!
21-07-2013 19:39 #64
Welcome 7liha and lotsofthoughts
Sharon Im sure there are plenty of follicles await your scan and BT tomorrow! What day on your cycle are you up to?
AFM ET tomorrow!! Im so very nervous that they'll cancel due to my embies not surviving or my OHSS. But trying to keep positive, this will work!
The Following 2 Users Say Thank You to Wishnhope For This Useful Post:
7liha (23-07-2013),MGC Bertie (21-07-2013)
21-07-2013 20:26 #65Member
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Hi Sharon69. I'm sure you'll be fine. This cycle I didn't get any symptoms till yesterday and that's day 12. I'm predicted 10-14 follies with surgery tomorrow morning. Last time in only got 3 and had horrible moody systems. Fingers crossed for u
21-07-2013 20:53 #66
Mind if I join?
I'm 2dp3dt. I'm a little nervous and incredibly tired! I'm on the pessaries morning and night.
Wishing everyone good luck.
Sent from my iPhone using The Bub Hub mobile app
21-07-2013 21:16 #67
Hi ladies might join in on this thread. I'm on the Aug/Sept thread but on currently on CD4 of a FET cycle. I'm on my 2nd day of jabbing puregon. Due to have my next blood test and scan on Fri.
GL and FX to everyone!
The Following User Says Thank You to Nezz79 For This Useful Post:
Allymumtobe (22-07-2013)
21-07-2013 21:32 #68Senior Member
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Hi everyone Mind if I join? Emski - sounds like we're on the same kind of protocol. I start Tues - Synarel, Menapur, Human Growth Hormon, Melatonin, Thyroxin, and DH on Doryx. This is my 6th full cycle, DH has dodgy swimmers and I'm all good fertility wise except it turns out I'm a very poor responder to ivf - only ever made it egg retrieval twice, total of 4 mature eggs, only one beautiful embryo (Grade A!) - resulted in a fimbrial ectopic that they thought was a 'miscarriage' ... bloody painful 6 week miscarriage . If this doesn't work, that's my last hope for my biological child, we'll go to Greece for egg donation. Which is kinda crap given I've got lots of lovely eggs there - they just can't get 'em out. So no pressure for this cycle at all ... as if being pre-menstrual isn't bad enough, this added significance means I find myself holding back tears watching a woolwash commercial! So lots of good wishes for all of us! It must be our turn soon!
22-07-2013 07:29 #69
Good morning,
I just wanted to wish you all well for any injections, BT's, scans and ET's today.
The Following 2 Users Say Thank You to freakedout44 For This Useful Post:
Allymumtobe (22-07-2013),sootyswife (22-07-2013)
22-07-2013 11:39 #70
and welcome Freakedout44 ,KLM, EM,7liha and lotsofthoughts ,jodes, nezz, vixjc
Wishnhope How did your et go today?
Ally Any sign of af yet?
Sharon how many follicles? hopefully heaps
And hiya to everyone else and I hope everyone is well
The Following User Says Thank You to crimson74 For This Useful Post:
7liha (23-07-2013)
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Poke Man is back at it again! This time, hes got a special mission. He is trying to catch all of the Pokehoes he can so they can be trained to be the best in the nation. He gets his trainer gear on and hits the park. After just under an hour, Poke Man was able to capture a Pikahoe, a Gigglymuff, and a Cuntizard. When he releases them back at the house, those Pokehoes were a little scared. He calmed them quickly, and explained all they had to do was please their Poke Master. These Pokehoes were destined for this task. First they all take turns sucking Poke Mans great rod, which he thoroughly enjoyed. Then they all took turns fucking it too.
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My grandaughter lives in a snowy climate and needed a warm jacket. This is definitely it and has a zip out fleece so two jackets in one. I found the price at $** quite high for a 4 year old considering I could buy similar in an adult size for same pricing.Read More
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Chelsea Handler … In 10 Steps Find yourself getting sexually attracted to a great girl? Use these ten steps on how to get a girl to have sex with you to arouse her and seduce her. Getting to have sex with a girl you desire is a dream come true. You may want to date … Read More
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text:
[OP-ED]: Will New (Interim) Philly DA End Ineffective Expensive Practices?
The career accomplishments of Kelley Hodge situate her well for the vital mission she volunteered to undertake over the next five-plus months.
The career accomplishments of Kelley Hodge situate her well for the vital mission she volunteered to undertake over the next five-plus months.
Immigration is a major league policy challenge. But Congress, having recently passed a pair of bills that will accomplish nothing, is stuck playing in the minors.
Kelley B. Hodge fue designada la semana pasada Fiscal de Distrito de Filadelfia de forma provisional.
Thank you, thank you, thank you, President Trump.
I offer my gratitude because after years of being the last of my immigrant family members to undertake the naturalization process, my mother just took the oath to become a U.S. citizen.
Hundreds of members of the opposition turned out in cities throughout Venezuela on Wednesday to block streets and roads in rejection of the constitutional assembly convened by President Nicolas Maduro, the third action of this kind in the past week.
Si usted siente que después de las elecciones pasadas son los pacientes los que dirigen el manicomio, créame, no es el único. El lunático número uno es, sin duda, el mismo presidente, quien la semana pasada en Miami demostró una vez más que su concepto (o su comprensión) de la realidad no pasa de los "reality shows".
If you feel that after the last election the inmates are running the asylum, you are not alone. The main lunatic seems to be the president himself, who last week in Miami showed once again that his concept (or his grasp) of reality does not go beyond, well, very bad "reality shows."
Former Panamanian President Ricardo Martinelli faces numerous charges in Panama in a case involving alleged spying on more than 200 opposition figures.
La prohibición de las ciudades santuario no se hará efectiva sin una lucha de por medio. Esta vez el campo de batalla es Dallas (Texas).
El veto de Texas a las "ciudades santuario" ha despertado crispación en varias ciudades del estado.


text:
Our values express the expectations we have of each other and ourselves, and identify how we conduct business with our clients.
Demonstrates eagerness to acquire necessary technical knowledge, skills, and judgment to accomplish a result or to serve a customer's needs effectively. Has desire and drive to acquire knowledge and skills necessary to perform job more effectively.
Creates an atmosphere in which timely and high-quality information flows smoothly up and down, inside and outside of the University; encourages open expression of ideas and opinions.
Develops cooperation and teamwork while participating in a group, working toward solutions which generally benefit all involved parties.
Understands agendas and perspectives of others, recognizing and effectively balancing the interests and needs of one's own group with those of the broader organization.
Demonstrates a high level of dependability in all aspects of the job.
Promotes and generates cooperation among one's peers in leadership to achieve a collective outcome; fosters the development of a common vision and fully participates in creating a unified leadership team that get results.


text:
Zaza Pachulia injured Kawhi Leonard during Game 1 – Was it dirty? | SPEAK FOR YOURSELF
Chris Broussard and Jim Jackson joined Jason Whitlock and Colin Cowherd to discuss if Zaza Pachulia's close out on Kawhi Leonard was a dirty play.
- Golden State Warriors
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text:
Screenshot instructions:
Red Hat Linux
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Right-click on ad, choose "Copy Link", then paste here →
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You seem to have CSS turned off.
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Here is a wild idea. Why don't we pronounce it:
new-ell-pee-are as in the new lpr that we are working on.
> On Mon, Nov 20, 2000 at 05:02:32PM -0800, Roland Dreier wrote:
> > The push to Samba 2.2 and gnulpr 1.0 continues. (BTW how do you
> > pronounce gnulpr?)
> I believe we're pronouncing it like: guh-NEW L P R
> (actually say the letters {l,p,r}, don't sound them out)
> If you like buzzwords, you could say that the name implies a synergy between
> the gnu philosophy and the bsd software from which it is based.
> --Mark
> --
> If we were meant to get up early, God would have created us with alarm clocks.
> Mark James Fasheh <mfasheh@...>
> VA Linux Systems Professional Services
> http://www.exothermic.org
begin Ben Woodard quotation:
> Here is a wild idea. Why don't we pronounce it:
> new-ell-pee-are as in the new lpr that we are working on.
Nick Moffitt, Professional Services
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Misc Christmas ornaments/crafts.
Misc Christmas ornaments/crafts. Nice variety of wooden, crochet items. I especially like the elf with broom and the wooden coo coo clock. There are a couple of plastic frames for you to hang your artwork or photos in. Aprox 18 items, shipping is 3.00 if in the USA.
Items Similar To "Misc Christmas ornaments/crafts."
TCAC Mall, Inc.
Walkerton, Indiana
Dealer accepts: Check, Money Order, Cash, PayPal
Shipping: Negotiated with Seller


text:
ALL >> General >> View Article
What Do Men Wear For A Traditional Indian Wedding
Total Articles: 1
Indian traditional clothes vary on the basis of climate and natural fibers grown in a region. Few of the most common Indian traditional clothes for men are Sherwanis, Kurtas & Jodhpuris.
Today Designer Sherwani for men is one much demanded attire that has successfully grabbed eyeballs of many and is one of the most worn indian outfit for men. These Sherwanis represent the traditional attire of men and have a twist in them in the sense of designs and creativity. They are a perfect symbol of conventional attire with a contemporary touch. In India, it is primarily worn on the occasion of traditional family functions. Sherwanis can be of various types – the Peshawri and the Baloochi, and are usually embellished with embroidery and zardozi work. During Indian weddings the Sherwani is worn with matching turbans, stoles and mojaris or juttis. For wedding reception men also wear designer mens suit with embroidery. During smaller events like Mehendi ceremonies men prefer wearing Indian Kurtas.
As the changing times these days Sherwanis are coming up in a variety of styles, patterns and designs. Today, you can find versatile types of sherwani made out of different fabrics in the market. Silk, zari fabric and brocade fabric are some of the widely used fabrics for a Sherwani. This men's attire is usually worn in combination with a pair of jutis and a matching stole. Superb cuttings and elegant designs of this men's outfit have attracted thousands of people from all over the world. Some of the exotic work used to adorn a designer sherwani includes pearls, kundans, crystals and stones. You can easily wear this outfit with a churidhar, shalwar and khara pajama.Unlike the bygone times, today, men wear Sherwani only on the formal occasions such as wedding or some family cultural function. These Sherwanis are especially designed to be worn on auspicious occasions and festivals like Diwali and weddings. But today men also like the idea of having a semi-casual sherwani for events like the sangeet and cocktail parties too.
The heavily designed Indian kurtas paired with a matching churidar, a stole or a dupatta, and traditional mojaris are also among the favourites in mens traditional Indian clothing. These Kurtas tend to deliver a very royal look that is not only impressive but is also very charming and conventional. Some of the most popular color combinations of Indian traditional clothes have always been cream and gold, maroon and gold, black and gold, and cream and silver, besides the other color combinations that people choose based on their choices and preferences. The mature adults are the ones who opt for the neutral and evergreen shades like cream, maroon and gold, and so on. Kids' Sherwanis too are gaining popularity as these are available in delightful colors and reflect the innocence and purity that kids possess.
General Articles1. Considerations For Choosing The Best Mobile App Development Platform
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Author: Emily Smith


text:
Donate to the Fish Release Cause!
Special Angels (link to below emailable form)
Guardian Angel $1,000 donation (largest logo recognition available with link)
Herald Angel $500 donation (second largest logo recognition available with link)
White Angel $200 donation
Pink Angel $100 donation
Sea Angel $50 donation
Who should donate ?
Fishing Clubs & Tournaments
Clubs - Other (Women or mixed)
Conservation Organizations
All donations will be applied to costs to help underwrite the Fish Release initiative. We thank you for supporting this grass-roots conservation initiative! Every effort counts!
Name to be credited on website: _____________
Email to


text:
BRISTOW, Virginia VA 20136-1273
$505,000 Price
Est. Monthly Payment: $2,168.76 See Details
4 Bedrooms
3 Full Baths
4 Total Baths
1 Partial Baths
3,054 Square Feet
0.252 Acres
PW9945396 Listing ID
Schedule Showing Virtual Tour
Status Pending
County PRINCE WILLIAM
Year Built 2004
Property Type Residential
Property Sub Type Detached
{"zipcode": "20136", "price": "505000"}
Down Payment
Credit Score
Loan Amount
Loan Type
Ashley Leigh
Email: firstname.lastname@example.com
Total Square Footage
Living Area: 4534
Primary Features
Amenities: Attached Master Bathroom, Automatic Garage Door Opener, Bathroom(s) - Ceramic Tile, Crown Molding, Vanities - Double, Fireplace Gas Insert, Fireplace Glass Doors, Fireplace Mantel(s), Countertop(s) - Granite, Master Bathroom - Separate Shower, Master Bathroom - Separate Tub, Master Bedroom - Full Bathroom, Closet - Master Bedroom Walk-in, Vanities - Separate, Sump Pump, Tub - 2 or More Person, Tub - Soaking, Wall to Wall Carpeting, Closet(s) - Walk-in, Wood Floors
Auction: no
Cooling: Ceiling Fan(s), Central Air Conditioning
County: PRINCE WILLIAM
Elementary School: VICTORY
Exterior Features: Fenced-Fully, Fenced-Rear, Porch-front
Foreclosure: no
Garage Type: Attached, Front Loading Garage
High School: STONEWALL JACKSON
Interior Features: Floor Plan-Open
Middle School: MARSTELLER
New Construction: no
Pool: No
Potential Short Sale: no
Property Condition: Shows Well
Property Type: Residential
Style: Colonial
Subdivision: PEMBROOKE
Year Built: 2004
Location Information
City: 10000033151
Historic: no
Property Against Water: no
Water Access: no
Waterfront: no
Water View: no
Interior Features
Appliances: Cooktop, Dishwasher, Disposal, Dryer, Exhaust Fan, Icemaker, Microwave, Refrigerator
Attic: Yes
Basement: yes
Basement Area Finished: 1500
Basement Entrance: Connect Stair, Outside Entrance
Basement Type: Fully Finished
Half Baths: 1
Cooling Fuel: Electric
Den Level: Lower 1
Dining Room Level: Main
Dining/Kitchen Description: Fam Rm Off Kit, Kit-Island, Kit-Table Space, Sep Dining Rm
Family Room Level: Main
Fireplaces: 1
Fourth Bedroom Level: Upper 1
Foyer Level: Main
Handicap: None
Heating: Forced Air
Heating Fuel: Natural Gas Available
Hot Water: Natural Gas
Kitchen Level: Main
Library Level: Main
Living Room Level: Main
Lower Floor Baths: 1
Main Entrance: Foyer, Hall, Two Story Foyer
Main Floor Half Baths: 1
Master Bedroom Level: Upper 1
Other Room Level: Lower 1
Other Rooms: Living Room,Den/Stdy/Lib,Storage Room,Bedroom-Fourth,Kitchen,Utility Room,Recreation Rm,Bedroom-Master,Bedroom-Third,MBR w/Sit Rm,Other Room 1,Foyer,Game/Exer Rm,2nd Stry Fam Rm,Den,Family Rm,Library,Dining Room,Bedroom-Second
Rec Room Level: Lower 1
Room List: Living Room, Dining Room, Bedroom-Master, Bedroom-Second, Bedroom-Third, Bedroom-Fourth, Kitchen, Recreation Rm, Family Rm, Den, Other Room 1, Library, Foyer, 2nd Stry Fam Rm, Den/Stdy/Lib, Game/Exer Rm, MBR w/Sit Rm, Storage Room, Utility Room
Second Bedroom Level: Upper 1
Third Bedroom Level: Upper 1
Upper Floor Baths: 2
Upper Floor Bedrooms: 4
Walls Ceilings: 2 Story Ceilings, 9'+ Ceilings
External Features
Community Amenities: Basketball Courts, Bike Trail, Common Grounds, Jogging / Walking Path, Party Room, Pool - Outdoor, Tennis - Courts, Tot Lots / Playground
Exterior: Siding - Vinyl
Garage: 2
Lot Description: Backs to Trees, Landscaping
Roof: Shingle - Asphalt
Sewer Septic: Public Sewer
Stories: 3
Structure List: Above Grade, Below Grade
Above Grade Area Finished: 3034
Builder Name: BEAZER
Farm: no
Federal Flood Zone: no
Lot Number: 80
Model Name: FARNHAM
Other Structures: Above Grade,Below Grade
Pets Allowed: no
Physical Dock Slip Conveys: no
Property Sub Type: Detached
Riparian Rights Convey Y/N: no
Vacation Home: no
VRP: no
Water: Public
Zoning Code: R4
Financial Details
Agricultural Tax Due: no
Contingency List: Other
Distressed Listing: no
Federal Flood Insurance: no
For Sale=Yes, For Rent=No: yes
Listing Prior Price: 499900
Parking: Garage, Paved Driveway
Parking Included In List Price: no
Legal Subdivision: PEMBROOKE
Total Assessment Payment Freq: Annually
Transaction Type: Standard
Zoning Info
Listing courtesy of Linton Hall Realtors
© 2017 Metropolitan Regional Information Systems. All rights reserved. Information Deemed Reliable, but Not Guaranteed. Listing information is from various brokers who participate in IDX and not all listings may be visible on the site. The property information being provided is for consumers personal, non-commercial use and may not be used for any purpose other than to identify prospective properties consumers may be interested in purchasing. Data last updated on Sunday, July 23rd, 2017 06:16:58 PM.
Request More Information - Listing ID PW9945396
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text:
CiberPart of HTC Global Services
Base Salary
CiberPart of HTC Global Services
Base Salary
Total Compensation
Cash Bonus, Stock Bonus, Profit Sharing, Commission Sharing, Tips have not been reported for this role.
Base Salary
Total Compensation
Be the first community member to contribute total compensation for this company
How much does a Web Developer at Ciber make in Van Buren Township, MI? The typical salary for a Ciber Van Buren Township Web Developer ranges from $70,459-$82,566, with an average salary of $75,303. Salary estimates based on 5 salary report(s) submitted anonymously to Glassdoor by Ciber Web Developer employees in Van Buren Township, MI or estimated based upon statistical methods.
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Your task is simple: just answer a few questions about your horse and his diet
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Can you get a hay feeder or even hang a hay net, to keep the hay off the sand? I give all my horses Probios and psyllium (sp?), but never have had a problem with them ingesting sand. They may do it, but we've had no problems.
It is never the horse's fault
SmartPak Equine™ is the premier online provider of horse supplies and equine supplements.
© Copyright by SmartPak Equine LLC. All Rights reserved.
Legal | Security & Privacy Policy


text: Traffic Alerts Carpenter StreetSpringdale St to W Salome AveStarts: July 10, 2017Ends: July 28, 2017No Access (Detour Posted) Kenmore Construction and the City of Akron will be closing Carpenter St. between Springdale St. and W. Salome Ave. on Monday, July 10 for sewer separation work. Included in this closure will be the full intersection of Carpenter St. and Springdale St. Traffic will be detoured using Garfield St., Lorenz Ave., Carpenter St., W. Dalton St., Carlysle St. and the reverse. This closure is expected to last until Friday, July 28. Emergency vehicles and local residents will have access at all times.Associated ProjectsCarpenter Sewer Separation CSO Rack 30


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This Book is in Good Condition. Clean Copy With Light Amount of Wear. 100% Guaranteed. Summary: Suitable for preaching purposes, and for use by people with vision problems. This work contains references, book introductions, chronologies, subject chain references, indexes and Oxford Bible Maps. Buchnummer des Verkäufers
Inhaltsangabe: Dr. C. I. Scofield's classic study system and 1917 notes form the core of this definitive resource. A crisp red- letter typeface enhances this Bible's usefulness. Large, 10-point print makes this edition particularly attractive for preacher and people with vision difficulties.
Features include book introductions, chronologies, concordance, subject-chain references, comprehensive and subject indexes and full-color Oxford Bible Maps, with index.
* Clear, readable 10-point typeface.
* 16 pages of full color.
* Complete Scofield® Study Bible features.
* Oxford Bible Maps, with index.
* Red letter text.
About the Author: Cyrus Ingerson Scofield (1843-1921) was an American lawyer, pastor, Bible teacher and author. A defender of dispensational premillennialism, he is best known for his Scofield Reference Bible. Founded the Central American Mission, and with L. S. Chafer the Philadelphia College of the Bible. He was D. L. Moody's pastor at Northfield during the final years of Moody's life.
Zustand: Used
Buchbeschreibung Oxford University Press, 2005. Bonded Leather. Buchzustand: Good. Large Print edition. Ships with Tracking Number! INTERNATIONAL WORLDWIDE Shipping available. May not contain Access Codes or Supplements. Buy with confidence, excellent customer service!. Buchnummer des Verkäufers 0195274865
Weitere Informationen zu diesem Verkäufer | Frage an den Anbieter


text:
(1) Registered users: Shopping bag products are removed by the system after 5 days.
(2) Non-registered users: Bag contents can only be retained for 12 hours.
(3) Registered users can click "Save for later" to retain shopping bag contents for up to 30 days.
Stylish White Deep V Neck Floral Women's Dress - White - M
Stylish Deep V Neck Bell Sleeve Floral Print Women's Straight Dress - White - One Size(fit Size Xs To M)
Stylish Deep V Neck 3/4 Sleeve Front Twist Women's White Blouse - White - Xl
Stylish Deep V Neck Bell Sleeve Women's Chiffon Crop Top - White - S
Stylish Deep V Neck Sleeveless Open Back Chevron Stripes Asymmetrical Women's Maxi Dress - White And Black - L
Stylish Spaghetti Strap Hollow Out Solid Color One Piece Women's Swimwear - White - M
Stylish Cami Lace Spliced Women's Bikini Set - White - Xl
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you can check it in your Account .
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