公开(公告)号：JP2014208548A

公开(公告)日：2014-11-06

申请号：JP2014122257

申请日：2014-06-13

Applicant: ケロッグ カンパニー ,  Kellogg Company ,  ケロッグ カンパニー

Inventor： DAVID OURS ,  SHARON JUNTUNEN

IPC: B65B1/02 ,  B65B11/02 ,  B65B43/00 ,  B65D19/44

CPC classification number: B65D71/0096 ,  B65B1/02 ,  B65B1/36 ,  B65B11/025 ,  B65B11/045 ,  B65B53/02 ,  B65D19/44 ,  B65D71/08 ,  B65D2571/00018 ,  B65D2571/00024 ,  B65D2571/0003 ,  B65D2571/00055

Abstract: 【課題】流動性ばら積み品のための運搬可能容器およびそれを作り出す方法を提供する。【解決手段】流動性ばら積み品のための運搬可能容器20は、底部支持体72からスリップフレーム形成装置24を垂直方向に間隔を空けて配置することによって形成される。ばら積み品を運搬可能容器20に加える前に運搬可能容器20を最初に形成するために、外側ラップ40,58が底部支持体72および少なくとも1つの形成装置壁56の一部の周りに配置される。スリップフレーム形成装置24および底部支持体72のうちの少なくとも一方は、ばら積み品の充填レベルに応じて他方に対して垂直方向に動く。運搬可能容器20において充填レベルが上昇すると、外側ラップ40の以前に配置された部分がスリップフレーム形成装置24から外される。【選択図】図1

Abstract translation: 要解决的问题：提供一种可流动散装货物的可运输容器及其制造方法。解决方案：用于可流动散装货物的可移动容器20通过将滑动架构架24与底部支撑件72垂直间隔而形成。外包装 40,58围绕底部支撑件72和至少一个前壁56的一部分设置，以便在将散装货物添加到可移动容器20之前初始地形成可运输容器20.至少一个滑动框架架24 并且底部支撑件72响应于散装货物的填充水平相对于另一个垂直移动。 当可运输容器20中的填充水平增加时，外包装40的预先设置的部分与滑动框架成形器24脱离接合。

公开(公告)号：JP2014061952A

公开(公告)日：2014-04-10

申请号：JP2014002406

申请日：2014-01-09

Applicant: Kellogg Company ,  ケロッグ カンパニー

Inventor： OURS DAVE ,  SHARON JUNTUNEN ,  STANLEY DAVIS ,  KREIDER CLARK

IPC: B65B39/12 ,  B65B1/06 ,  B65B37/20 ,  B65B39/00

CPC classification number: B65B39/08 ,  B65B1/36 ,  B65B11/045

Abstract: PROBLEM TO BE SOLVED: To provide a method of forming a transportable container of bulk goods.SOLUTION: The method begins by placing the distributing end of a hopper 40 over the open top of a bunched bag 42. Bulk goods are dispensed from the distributing end of the hopper 40 through the open top of the bag 42 to establish a level of bulk goods in the bag. The hopper 40 moves vertically relative to the closed base 58 of the bag 42 during the dispensing of bulk goods from the distributing end of the hopper to maintain vertical spacing between the distributing end of the hopper and the level of bulk goods in the bag 42. A hopper fill level is maintained in the hopper during the dispensing of bulk goods from the hopper. An outer wrap 52 is spirally wrapped around the bag 42 while filling the bag to form the transportable container 24. The outer wrap 52 is maintained near the level of bulk goods in the bag.

Abstract translation: 要解决的问题：提供一种形成散装货物的运输容器的方法。解决方案：该方法开始于将料斗40的分配端放置在聚束袋42的敞开的顶部上。散装货物从分配端分配 通过袋42的敞开的顶部设置料斗40，以在袋中建立一定量的散装货物。 在从料斗的分配端分配散装货物期间，料斗40相对于袋42的封闭基部58垂直移动，以保持料斗的分配端与袋42中的散装货物的水平面之间的垂直间隔。 在从料斗分配散装货物期间，料斗的料斗保持在料斗中。 外包装52在填充袋以形成可运输容器24的同时螺旋地卷绕在袋42周围。外包装52保持在袋中散装货物的附近。

公开(公告)号：MY113946A

公开(公告)日：2002-06-29

申请号：MYPI19970212

申请日：1997-01-21

Applicant: THE M W KELLOGG COMPANY

Inventor： MICHAEL G HUNTER ,  KENNETH W GOEBEL

IPC: C07C1/00 ,  B01J8/04 ,  C10G65/04 ,  C10G51/06 ,  C10G65/10 ,  C10G65/12 ,  C10G65/14 ,  C10G65/16 ,  C10G65/18

Abstract: HYDROCARBON FEEDSTOCKS ARE HYDROPROCESSED IN PARALLEL REACTORS, WHILE HYDROGEN FLOWS IN SERIES BETWEEN THE REACTORS. A FIRST HYDROCARBON FEEDSTOCK AND A HYDROGEN-RICH RECYCLE GAS STREAM ARE INTRODUCED TO A FIRST REACTOR, WHERE A FIRST REACTOR EFFLUENT STREAM IS PRODUCED AND FED TO A FIRST SEPARATOR, WHICH SEPARATES THE FIRST REACTOR EFFLUENT STREAM INTO A FIRST HYDROGEN-RICH GAS STREAM AND A FIRST HYDROPROCESSED PRODUCT STREAM. THE FIRST HYDROGEN-RICH GAS STREAM AND A SECOND HYDROCARBON FEEDSTOCK ARE FED TO A SECOND REACTOR, WHERE A SECOND REACTOR EFFLUENT STREAM IS PRODUCED AND FED TO A SECOND SEPARATOR, WHICH SEPARATES THE SECOND REACTOR EFFLUENT STREAM INTO A SECOND HYDROGEN-RICH GAS STREAM AND A SECOND HYDROPROCESSED PRODUCT STREAM. A MAKE-UP HYDROGEN STREAM IS ADDED TO THE SECOND HYDROGEN-RICH GAS TO FORM THE HYDROGEN-RICH RECYCLE GAS STREAM THAT IS COMPRESSED AND FED TO THE FIRST REACTOR. FIGURE 3

公开(公告)号：MY103165A

公开(公告)日：1993-04-30

申请号：MYPI19880495

申请日：1988-05-11

Applicant: THE M W KELLOGG COMPANY

Inventor： DUFFER BROKS CRAWFORD ,  T MICHEAL O'CANNOR ,  RAMANATHAN R TARAKAD

IPC: F25J3/00 ,  C07C1/00 ,  C07C7/09 ,  C07C67/00 ,  C10G7/12 ,  C10G53/02 ,  F25J3/02

Abstract: HEAVY COMPONENTS OF HYDROCARBON GAS MIXTURES ARE RECOVERED THROUGH PARTIAL CONDENSATION OF A FIRST PORTION OF THE STARTING GAS BY INDIRECT HEAT EXCHANGE WITH A REFRIGERANT WHEREIN THE CONDENSATE FORMED IS ENTRAINED IN THE GAS STREAM. THE CONDENSATE IS SEPARATED FROM THE RESULTING PARTIALLY CONDENSED, TWO-PHASE MIXTURE AND THE SEPARATED CONDENSATE IS THEN THERMALLY STRIPPED OF LIGHT COMPONENTS BY HEAT EXCHANGE WITH A SECOND PORTION OF THE STARTING GAS WHICH IS THEREBY ALSO PARTIALLY CONDENSED. HEAVY COMPONENTS FROM THE STARTING GAS MIXTURE ARE RECOVERED AS STRIPPED HYDROCARBON CONDENSATE. (FIG. 4)

公开(公告)号：ES2017667B3

公开(公告)日：1991-03-01

申请号：ES87106867

申请日：1987-05-12

Applicant: THE M W KELLOGG COMPANY

Inventor： HACKEMESSER LARRY G ,  LANKFORD BRADLEY L

IPC: C10G9/14 ,  C10G9/36

公开(公告)号：MY100798A

公开(公告)日：1991-02-28

申请号：MYPI19871131

申请日：1987-07-27

Applicant: THE M W KELLOGG COMPANY

Inventor： DUFFER BROOKS CRAWFORD ,  RAMANATHAN R TARAKAD

IPC: B01D19/00

Abstract: MERCURY IS REMOVED FROM NATURAL GAS BY CONTACTING THE GAS WITH A RELATIVELY MERCURY-FREE LIQUID STATE HYDROCARBON AND RECOVERING A MERCURY-LEAN METHANE-RICH GAS AND A MERCURY-ENRICHED HYROCARBON LIQUID. THE MERCURY-FREE HYDROCARBON LIQUID MAY BE OBTAINED BY SEPARATION OF MERCURY FROM THE MERCURY-ENRICHED HYDROCARBON LIQUID OR ITS DERIVATIVE STREAMS. (FIG. 1)

公开(公告)号：ES214981Y

公开(公告)日：1976-12-01

申请号：ES214981

申请日：1975-09-08

Applicant: KELLOGG COMPANY

IPC: B65D20060101 ,  B65D

公开(公告)号：MY114664A

公开(公告)日：2002-12-31

申请号：MYPI19950188

申请日：1995-01-26

Applicant: THE M W KELLOGG COMPANY

Inventor： KENNETH WILLIAM GOEBEL ,  MICHAEL GLENN HUNTER

IPC: C10G7/00 ,  B01D3/14 ,  C10G49/22 ,  F02B3/06

Abstract: AN INTEGRATED THREE-COLUMN PROCESS FOR RECOVERING HYDROCARBON DISTILLATE PRODUCTS FROM A HYDROPROCESSING OR HYDROCRACKING REACTOR EFFLUENT STREAM AND A HYDROCARBON DISTILLATE PRODUCT RECOVERY TRAIN ARE DISCLOSED. ACCORDING TO THE PRESENT RECOVERY PROCESS, AN EFFLUENT STREAM FROM THE CRACKING REACTOR IS COOLED AND SEPARATED INTO LIGHT AND HEAVY PHASE STREAMS. THE HEAVY PHASE STREAM IS DEPRESSURIZED AND STRIPPED OF LIGHT END COMPONENTS IN A STEAM STRIPPING COLUMN. THE LIGHT PHASE STREAM IS FURTHER COOLED TO SEPARATE A LIQUID STREAM WHICH IS COMBINED WITH THE LIGHT ENDS FROM THE STRIPPER ANDFED TO A DEBUTANIZER. A C4-RICH LIGHT END STREAM TAKEN OVERHEAD FROM THE DEBUTANIZER IS CONDENSED TO PRODUCE PLG PRODUCT STREAM(S). A C4-LEAN HEAVY END STREAM REMOVED FROM THE BOTTOMS OF THE DEBUTANIZER IS COMBINED WITH A HEAVY END BOTTOMS STREAM FROM THE STRIPPER AND FED TO A FRACTIONATOR FOR FRACTIONATION INTO PRODUCT DISTILLATE STREAMS SUCH AS LIGHT AND HEAVY NAPHTHA, JET FUEL, DIESEL OIL, AND THE LIKE. A HEAVY OIL BOTTOMS STREAM RECOVERED FROM THE FRACTIONATOR IS RECYCLED BACK TO THE CRACKING REACTOR. FIGURE 1

公开(公告)号：RO109934B1

公开(公告)日：1995-07-28

申请号：RO14731191

申请日：1991-04-10

Applicant: MW KELLOGG COMPANY

Inventor： LEBLANC JOSEPH R

IPC: C01C1/04

公开(公告)号：YU55091A

公开(公告)日：1994-01-20

申请号：YU55091

申请日：1991-03-28

Applicant: M W KELLOGG COMPANY HUSTON

Inventor： LE BLANC J R

Abstract: AUTOTERMALNI REFORMING POSTUPAK PAROM, amonijačni sintezni gas se proizvodi reakcijom pare, oksidujućeg sredstva, i glavnog dela svežeg ugljovodoničnog napajanja u egzotermnoj katalitičkoj reforming zoni u prvi reformirani gas koji ima vrlo nizak sadržaj metana. Ostatak svežeg napajanja reaguje sa parom u endotermnoj katlitičkoj reforming zoni u drugi reformirani gas koji ima nizak sadržaj metana. Prvi i drugi reformirani gasovi se spoje i prelaze u indirektnu toplotnu izmenu sa reaktantima u endotermnoj reforming zoni da se dobije sva toplota potrebna u njemu i potom se izdvajaju kao sirovi amonijačni sintezni gas.